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189-045
Pages NOT Scanned in this Well History File XHVZE This page identifies those items that were not scanned during the initial scanning project. They are available in the original file and viewable by direct inspection. /~'~-'~~' File Number of Well History File PAGES TO DELETE RESCAN [] Color items - Pages: [] Grayscale, halftones, pictures, graphs, charts- Pages: [] Poor Quality Original - Pages: [] Other- Pages: DIGITAL DATA [] Diskettes, No. [] Other, No/Type OVERS~.O.- ....... Logs of various kinds [] Other Complete COMMENTS: Scanned by: Bevedy Bren ~ Nathan Lowell [] TO RE-SCAN Notes: Re-Scanned by: Bevedy Bran Vincent Nathan Lowell Date: ·/s/ NOTScanned.wpd ~ ~~~~~ ~~ ALAS v~4io' QIL ANA? GAS G()NSERVATtOW C~A11A~iSSlON BOf'1= "t•est Report Subrrrrt to: Contractor: Nabors Rig No.: 3S DATE: 10/6/2008 Rig Rep.: J. Greco I R.Bjorh~ Rig Phone: 659-4487 Rig Fax: 659-4486 Operator. Bp Op. Phone: 659-4485 Op. Fax: 659628 Rep.: B. Burson! R. Mabeus Field/Unit & Well No.: NIP G-04 PTD # 't89-0L15 Operation: Drlg: Workover: x Explor.: Test: Initial: x Weekly: Bi-Weekly Test Pressure: Rams: 250/3500 Annular: 250/3500 Valves: 250/3500 TEST DATA MISC. INSP'ECTFONS: Test Result Test Resutt Location Gen.: P Wetl Sic, P Housekeeping: P Drl. Rig P PTD On Location P i-Lazard Sec, P Standing Order Posted P BOR STACK: Quantity Size Test. Result Annular Preventer 1 13 5/8 5000 I' Pipe Rams 1 2 7/$ X 5 P Lower Pipe Rams 0 NA Blind Rams 1 Blirxt P Choke Ln. Valves 1 3 1/8" 5000 P HCR Valves 2 31/8" 5000 FP Kill Line Valves 1 2 4/16" 5000 P Check Valve 0 NA MUD SYSTEM: V~.sual Test Alarm Test Trip Tank P P Pit Level Indicators P P Flow Indicator P P Meth Gas Detector P P H2S Gas Detector P P Test Reswtts FLOOR SAFETY VALVES: Quantity Test Result Upper Kelly 0 NA Lower Kelly 0 NA Bak Type 1 P Inside BOP 1 P CHOKE MANIFOLD: Quantity Test R lVo. Valves 13 P Manual Chokes 1 P Hydraukc Chokes 1 P ACCUMtlLATOR SYSTEM: Time/Pressure Test Result System Pressure 3100 P Pressure Auer Closure 1900 P 200 psi Attained 32sec P Full Pressure Attained 153 sec P Blind Switch Covers; All stations P Nitgn. Bottles (avg}: i 900 Number of Failures: 9 Test Time: 4=5 Hours Cornconents tested ALL Repair or replacement of ec~ment w~ be made ~ days. Notify the North Slope Inspector 659-3607, fo~OVV with written confirmation to Supervises at: Remarks: Tested with 2 7/8" test ioint against Two way check / KiN HGR leaked greased and retest -tested Good. 24 HOUR NOTICE GIVEN YES X NO Date 10/03/08 Time 1630 hrs Test start 0200 hrs Finish By Jeff Jones !M1/itness BOP Test (for rigs} l Y BFL 11 /14/07 Nabors 3s BOP Test MP G-04 10-06-2008.x1s STATE OF ALASKA ~ ALASKA OIL AND GAS CONSERVATION COMMISSION REPORT OF SUNDRY WELL OPERATIONS 1. Operations performed: r'l Operation Shutdown r'l Stimulate [] Plugging [] Perforate [] Pull Tubing [] Alter Casing [] Repair Well [] Other Change Out ESP 2. Name of Operator 5. Type of well: 6. Datum Elevation (DF or KB) BP Exploration (Alaska) Inc. [] Development KBE = 59.27' [] Exploratory 7. Unit or Property Name 3. Address [] Stratigraphic Milne Point Unit P.O. Box 196612, Anchorage, Alaska 99519-6612 [] Service 4. Location of w~ll at surface ' 8. Well Number 3466' SNL, 3370' WEL, SEC. 27, T13N, R10E, UM x = 557235, Y = 6014250 MPG-e4 At top of productive interval 9. Permit Number / Approval No. 189-045 1963' SNL, 3279' WEL, SEC. 27, T13N, R10E, UM x = ss?3~, y 10. APl Number At effective depth 50-029-21941-00 1834' SNL, 3279' WEL, SEC. 27, T13N, R10E, UM 'x=ss?3o~,¥=so~a~2 11. Field and Pool At total depth Milne Point Unit / Schrader Bluff 1799' SNL, 3280' WEL, SEC. 27, T13N, R10E, UM x= ss?30s. Y=60~sg~7 12. Present well condition summary Total depth: measured 4950 feet Plugs (measured) true vertical 4584 feet Effective depth: measured 4849 feet Junk (measured) true vertical 4490 feet Casing Length Size Cemented MD TVD Structural Conductor 75' 13-3/8" Arctic Set to Surface 110' 110' Surface 2639' 9-5/8" 189 Bbls Permafrost 'E', 112 Bbls 'G' 2674' 2513' Intermediate Production 4894' 7" 51 Bbls PRRM Cmt, 19 Bbls Arctic Set 4929' 4565' Liner Perforation depth: measured 4312' - 4320', 4362' - 4366', 4372' - 4378', 4394' - 4430', 4445' - 4456', 4480' - 4514', 4554' - 4570' 4572' - 4576' true vertical 3988' - 3995', 4034' - 4038', 4043' - 4049', 4064' - 4097', 4111' - 4122', 4144' - 4176', 4213', 4228' 4230' - 4234' Tubing (size, grade, and measured depth) 2-7/8", 6.5#, L-80 to 4118' Packers and SSSV (type and measured depth) 4586'Gravel Pack Assembly: BakerSC'lLpa~e~l_~. ia~rM°del'D'packerat 13. Stimulation or cement squeeze summary Intervals treated (measured) ~/~,N 2 7 2.005 Treatment description including volumes used and final pressure ~a$~(a 0il & Gas Cons. C01¥~mission Anchorage 14. Reoresentative Daily Averaoe Production or Injection OiI-Bbl Gas-Mcr Water. Bbl Casing Pressure Tubing Pressure Prior to well operation: Subsequent to operation: 15. Attachments 16. Status of well classifications as: [] Copies of Logs and Surveys run [] Oil [] Gas [] Suspended Service [] Daily Report of Well Operations .......... ,.- r 17. I hereby cert~rrect to the best of my knowledge ~{~AI~II~II:.I.~ r Si,qned So~dra Stewm Title Technical Assistant ., Date ~ ~ Prepared By Name/Numbec $ondra Stewman, $64.4780 Submit In Duplicate Legal Well Name: MPG-04 Common Well Name: MPG-04 Spud Date: 9/5/1989 Event Name: WORKOVER Start: 12/20/2002 I~nd: Contractor Name: NABORS ALASKA DRILLING I Rig Release: 12/22/2002 Rig Name: NABORS 4ES · Rig Number: 12/18/2002 00:00 - 06:00 6.00 MOB P DECOMP RIG DOWN AND BEGIN TO MOVE RIG AND EQUIPMENT FROM MPS-PAD TO MPG-04 06:00 - 08:00 2.00 MOB P DECOMP CREW CHANGE. PJSM. CONTINUE MOVING RIG AND EQUIPMENT TO MPG-04 WELL. 08:00 - 10:30 2.50 RIGU P DECOMP SPOT RIG SUB BASE, PITS, AND PIPE SHED. 10:30 - 12:00 1.50 RIGU P DECOMP RAISE AND SCOPE DERRICK. TAKE ON 10.7 LB/GAL BRINE IN PITS. ACCEPTED RIG AT 12:00 HRS...LMH. 12:00 - 13:30 1.50 RIGU P DECOMP SPOT TIGER TANK, RU AND TEST 3500 PSI, LINES TO TREE AND TIGER TANK. 13:30- 14:30 1.00 RIGU P DECOMP PU LUB AND PULL BPV- CIRCULATE 120 DEG SEAWATER TO CLEAN WELL 14:30 - 19:30 5.00 KILL P DECOMP CREW CHANGE, PJSM-KILL WELL WITH 10.7 PPG BRINE AT 4 BPM / 600 PSI-MONITOR WELL. WELL DEAD 19:30-20:30 1:00 KILL P DECOMP RD LINE FROM TREE, INSTALLAND TESTTWC 20:30 - 22:00 1.50 WHSUR P DECOMP ND TREE, PREP TUBING SPOOL 22:00 - 00:00 2.00 BOPSUF:P DECOMP NU BOPE 12/19/2002 00:00 - 01:00 1.00 BOPSUF:P DECOMP FINISH NU BOPE. 01:00 - 04:00 3.00 BOPSUF:P DECOMP TEST BOPE PER BP/AOGCC REQUIREMENTS AT 250~2500 PSI. GOOD TEST. STATE'S RIGHT TO WITNESS TEST WAIVED BY J. SPAULDING. 04:00- 04:30 0.50 BOPSUF:P DECOMP RD TEST EQUIPMENT. 04:30 - 06:00 1.50 BOPSUF:P DECOMP RIG UP LUBRICATOR. PULL TWC. RIG DOWN LUBRICATOR. 06:00 - 08:00 2.00 PULL P DECOMP CREW CHANGE. PJSM. PICK-UP LANDING JT. AND XO. BOLDS. PULL HANGER TO FLOOR (40K). LD LANDING JT. 08:00 - 09:00 1.00 PULL !P DECOMP FINISH RIGGING UP EQUIPMENT TO PULL ESP AND HEAT TRACED COMPLETION. 09:00 - 13:30 4.50 PULL P DECOMP TOH WITH 2 7/8 TBG & SPOOLING ~2265' OF HEAT TRACE. CLEAR FLOOR OF SPOOLING EQUIP. 13:30 - 15:00 1.50 PULL P DECOMP CONT TOH WITH TBG / ESP CABLE 15:00 - 17:00 2.00 PULL P DECOMP LD PUMP/MOTOR 17:00 - 19:00 2.00 PULL P DECOMP RD ESP PULLING EQUIP AND CLEAR FLOOR. RU TO RUN DC & DP. 19:00-20:30 1.50 PULL P DECOMP MU & RIH WlTH10 -4 3/4" DC & 20 JTS 31/2" DP 20:30 - 21:30 1.00 PULL P DECOMP MU & SET 7"RTTS WITH SSCV AT 57'. TEST RTTS TO 1000 PSI. 21:30 - 00:00 2.50 PULL .P DECOMP DRAIN STACK, CHANGE LDS PACKING.PU 7" CSG PACKOFF RETRIEVING TOOL & LATCH INTO PACKOFF MANDREL. BACK OUT CSG SPOOL LDS, PU 16K, PULL ' PACKOFF MANDREL TO SURFACE. SET SCREWS ON LOWER SECTION OF MANDREL SLEAVE SHEARED AND WAS LEFT IN CSG SPOOL. 12/20/2002 00:00- 02:00 2.00 WHSUB N SFAL DECOMP PJSM, ND BOP STACK. 02:00- 06:00 4.00 WHSUB N SFAL DECOMP REMOVE TBG SPOOL. ATTEMPTTO.REMOVE REMAINING PACK-OFF RINGS AND SEALS. 06:00- 07:00 1.00 WHSUB N SFAL DECOMP FABRICATE A"PULLING PLATE" AND SPACERS TO USE WITH A PORT-A-POWER. 07:00- 08:30 1.50 WHSUB N SFAL DECOMP PJSM...PERFORM GAS CHECK_FILL OUT HOT WORK PERMIT. WELD ON PULLING PLATE. CONTINUE TO PULL REMAINING PLATES AND PACKING. COMPLETE RECOVERY. PREP HEAD FOR NEW PACKING. 08:30- 09:00 0.50 WHSUB N SFAL DECOMP INSTALL NEW PACKING. RILDS. LD RUNNING TOOL. 09:00- 10:30 1.50 WHSUB N SFAL DECOMP INSTALL TUBING SPOOL. TORQUE, TESTTO 3,000 PSI. Printed: 12126/2002 10:19:02 AM Legal Well Name: MPG-04 Common Well Name: MPG-04 Spud Date: 9/5/1989 Event Name: WORKOVER Start: 12/20/2002 ¢:nd: Contractor Name: NABORS ALASKA DRILLING I Rig Release: 12/22/2002 Rig Nam, e: NABORS4ES , Rig Number: 12/20/2002 09:00-10:30 1.50 WHSUB N SFAL DECOMP GOOD. 10:30- 13:00 2.50 WHSUB N SFAL DECOMP NU BOP STACK. 13:00- 13:30 0.50 WHSUR N SFAL DECOMP SAFETY MEETING-PINCH POINTS-COMMUNICATIONS 13:30 - 14:30 1.00 WHSUR N SFAL DECOMP 'BODY TEST BOP 250 / 2500-GOOD TEST-RD TEST EQUIP.-DRAIN BOP STACK 14:30 - 15:00 0.50 WHSUR P DECOMP RUN RTTS RETRIEVING TOOL AND RETRIEVE RTTS FROM 57' 15:00-17:00 2.00 WHSUR P DECOMP LD 20 JTS 31/2 DP &10 4 3/4 DC - CLEAR / CLEAN RIG FLOOR : 17:00 - 19:00 2.00 RUNCO~ ~ COMP PJSM- PU & SERVICE ESP 19:00 - 19:30 0.50 RUNCOI~ ~ COMP PLUG IN CABLE, SECURE AND TEST 19:30 - 20:30 1.00 RUNCOI~ ~ COMP MU XN NIPPLE, 4 JTS 2 7/8 TBG,GLM WITH DUMMY VALVE,18 JTS 2 7/8 TBG. 20:30 - 22:00 1.50 RUNCOI~ ~ COMP RU HEAT TRACE RUNNING EQUIP AND PULL HEAT TRACE CABLE OVER SHEAVE. 22:00 - 00:00 2.00 RUNCO~ ~ COMP RIH WITH ESP COMPLEATION ASSY BANDING HEAT TRACE TO TBG WITH FLAT GUARDS 12/21/2002 00:00 - 06:00 6.00 RUNCOI~ ~ COMP RIH WITH ESP COMPLETION ASSY WITH CENTRILIFTHEAT TRACE 06:00 - 13:30 7.50 RUNCOI~ ~ COMP CONT RIH WITH ESP COMPLETION AND HEAT TRACE. 13:30 - 14:00 0.50 RUNCO~ ~ COMP PU LANDING JT AND NEW WKM HGR. INSTALL PENETRATORS 14:00 - 18:00 4.00 ' RUNCOI~ ~ COMP MAKE EFT AND HEAT TRACE SPLICE. 18:00 - 20:00 2.00 RUNCO~ ~ COMP SAFETY MEETING WITH NIGHT NAD CREW,BAKER,BP DISCUSS TODAYS FATALITY IN THE FIELD, NON STANDARD TASKS AND RIG MOVE. COMPLETE EFT AND HEAT TRACE SPLICE. ATTACH TO PIN AND TEST, SECURE TO TBG. 20:00-23:30 3.50 RUNCO~ ~ COMP LAND HGR WITH PHD AT 4118' AND HEAT TRACE AT 3450'. RILDS AND TORQUE, LD LANDING JT. ND BOP 23:30 - 00:00 0.50 RUNCO~ ~ COMP PREP HGR, INSTALL NEW TBG ADAPTER FLG, NU TREE 12/22/2002 00:00 - 02:00 2.00 WHSUR P COMP FINISHED NU ADAPTOR FLANGE AND PROD TREE. TEST SAME TO 5,000 PSI...GOOD. 02:00 - 03:00 1.00 WHSUR P COMP PU LUBRICATOR AND PULL TWC. INSTALL BPV. 03:00- 05:00 2.00 WHSUR P DECOMP RIG UP FESCO. TEST LINES. FREEZE PROTECT. CLEAN PITS. BLOW DOWN LINES. BEGIN PREPARING TO RIG DOWN NAD 4ES. 05:00 - 06:00 1.00 WHSUR P DECOMP FINISH FP WELL TO 2,100-FT. RD AND SECURE CELLAR. RELEASE RIG. RD FESCO. ,(,ANN ,:.D FEB 3 1 Printed: 12/26/2002 10:19:02 AM MEMORANDUM TO: Dan Seamount ~..~ Commissioner THRU: Blair Wondzell' P.I. Supervisor FROM: John CriSp'~ Petroleum Inspector State of Alasl~a Alaska Oil and Gas Conservation Commission DATE: October 1,2000 SUBJECT: Mechanical Integrity Tests BPX F & G Pads F-83i, G-01 i,03i,05i,07i Milne Point Unit Milne Point Field NON- CONFIDENTIAL -Packer Depth . Pretest Initial 15 Min. 30 Min. We,I F-83iITypelnj'I S I T.V.D. I 6425 '1 Tubing I=~00 I~00i"==oo I=~oo l,nterva,I I. ".P.T.D.I 2001030 iTyPetestI P ITestpsil 1606 I Casingl 1900I 2680. ! 2660 I 2650 I PIE I'P_ Notes: · ve"t P.T.D.I 1890290 IT.yPe'testl P ITestpsil923 ;I Ca'singl ' 0 '1 1725 I 1725 I 1725 I P/F I P_- Notes: '"we,IG-03i I Type,nj.i s I T.V.D. 13791 }Tubing I 17'~0 11720 I 1720 I 1720 l intervai'l '4 P.T.O.I 1890280' lType testI 'P ITestpsil. 948 .ICasingl 950 .I 2190 I 2180 I 2175 I P/FI'P__'- Notes: ' w~,l G-OSi I Ty,e,.j.I S I T.v.D.I ~'l~u~,.,I oo'1 .oo i~oo i.oo I,nte~.,l 4 P.T.D.I 1890460 ITypet.estl P ITestpsil' 982' I Casingl 0 I 1,775.1 17501 17301 P/F I_P' Notes: . ,, ~-~< _ ~_~_~- ~:~ . . . ' , ' ,, , we, i' ~ I Type In]. PiT. D.I~90450 ITypetestl P, ITestpsi'l e~ I.c~in, I. ~20 ! ~'s00 I.,2~s6 1'2~s0 I' ~ .I ~P' Notes: Type INJ~Fluid Codes F = FRESH WATER INJ. G = GAS INJ. S = SALT WATER INJ. N = NOT INJECTING Type Test M= Annulus Monitoring P= Standard Pressure Test R= Internal Radioactive Tracer Survey A= Temperature Anomaly Survey D= Differential Temperature Test I witnessed 5 successful. MIT's ~ BP's MPU. Test's Details Interval I= Initial Test 4= Four Year Cycle V= Required by Variance W= Test during Workover O= Other (describe in notes) .i.T.'s performed: 5_ Attachments: Number of Failures: 0 Total Time during tests: 2 hrs. cc: MIT report form 5/12/00 L.G. MIT MPU F & G Pads 10-01-00jc.xls 10/3/00 THE MATERIAL UNDER THIS COVER HAS BEEN MICROFILMED ON OR BEFORE OC.TOBER 24, 2000 P M C:LORILMFILM.DOC E E L E W A T E R IA L U N D E TH IS M A.R K ER R STATE OF ALASKA ALAS~.)IL AND GAS CONSERVATION CO~. ~SION REPORT OF SUNDRY WELL OPERATIOI~S 1. Operations performed: [] Operation Shutdown [] Stimulate [] Plugging [] Perforate [] Pull Tubing [] Alter Casing [] Repair Well [] Other Change Out ESP 2. Name of'~p~i~r ..................... 5. mype"'~)f well: ......... 6. Datum Elevati0'r~'(DF o'r'"l~B)'" BP Exploration (Alaska) Inc. [] Development KBE = 59.27' [] Exploratory 7. Unit or Property Name 3. Address [] Stratigraphic Milne Point Unit P.O. Box 196612, Anchorage, Alaska 99519-6612 [] Service 4. Location of well at surface 8. well NUmber MPG-04 3466' SNL, 3370' WEL, SEC. 27, T13N, R10E, UM At top of productive interval 9. Permit Number / Approval No. 189-045 1963' SNL, 3279' WEL, SEC. 27, T13N, R10E, UM 10. APi"~mber ....................... At effective depth 50- 029-21941-00 1834' SNL, 3279' WEL, SEC. 27, T13N, R10E, UM 11. Field and Pool At total depth Milne Point Unit / Schrader Bluff 1799' SNL, 3280' WEL, SEC. 27, T13N, R10E, UM r~~_. ~. 12. Present well condition summary I ~,l,,~,,~l.'.i'~" Total depth: measured 4950 feet Plugs (measured) true vertical 4584 feet MAR 2; 4 Effective depth: measured 4849 feet Junk (measured) ,~0JJ &Ga~ ,., ..... true vertical 4490 feet ~lch0rage Casing Length Size Cemented MD TVD Structural Conductor 75' 13-3/8" Arctic Set to Surface 110' 110' Surface 2639' 9'5/8" 189 Bbls Permafrost 'E', 112 Bbls 'G' 2674' 2513' Intermediate Production 4894' 7" 51 Bbls PRRM Cmt, 19 Bbls Arctic Set 4929' 4565' Liner Perforation depth: measured 4312' - 4320', 4362' - 4366', 4372' - 4378', 4394' - 4430', 4445' - 4456', 4480' - 4514', 4554' - 4570', 4572' - 4576' truevertical 3988'-3995', 4034'-4038', 4043'-4049', 4064'-4097', 4111'-4122', 4144'-4176', 4213'-4228', 4230' - 4234' Tubing (size, grade, and measured depth) 2-7/8", 6.5#, L-80 to 4123' Packers and SSSV (type and measured depth) Gravel Pack Assembly: Baker SC-1L packer at 4178' and Baker Model 'D' packer at 4586' 13. Stimulation or cement squeeze summary Intervals treated (measured) Treatment description including volumes used and final pressure 14. Representative Daily Average ProductiOn or Injection Data Oil-Bbl Gas-Mcr Water-Bbl Casing Pressure Tubing Pressure Prior to well operation: Subsequent to operation: 15. Attachments .............. i6. Status of we'ii'"c'l'~ssificati0ns a's'i ............................................ [] CoPies of Logs and Surveys run [] Oil [] Gas [] Suspended Service [] Daily Report of Well Operations 17, I hereby certify that the foregoing is true and correct to the best of my knowledge Signed TerrieHubble~'~~ ~ Title Technical Assistant,ll Date 0~'~' i ~ i: : : ProparodByNamo/Numbor: TorrloHubblo, 564-4628 Submit In Duplica ~ Form 10-404 Rev. 06/15/88 Facility Date/Time 11 Mar00 12 Mar 00 Progress Report M Pt G Pad Well MPG-04 Page 1 Rig Nabors 4ES Date 20 March 00 22:00-06:00 22:00-06:00 06:00 06:00-08:00 06:00-08:00 08:00 08:00-10:00 08:00-10:00 10:00 10:00-12:30 10:00-12:30 12:30 12:30-15:00 12:30-13:30 13:30 13:30-15:00 15:00 15:00-17:30 15:00-17:30 17:30 17:30-20:30 17:30-20:30 20:30 20:30-23:00 20:30-23:00 23:00 23:00-06:00 23:00-00:30 Duration 8hr 8 hr 2 hr 2hr 2 hr 2hr 2-1/2 hr 2-1/2 hr 2-1/2 hr lhr 1-1/2 hr 2-1/2 hr 2-1/2 hr 3 hr 3 hr 2-1/2 hr 2-1/2 hr 7hr 1-1/2 hr Activity Move rig Rig moved 100.00 % move rig from MPE-06 to MPG-04 & rig up & safe out equipment. At well location - Slot Wellhead work . Removed Hanger plug rig tiger tank & rig lubricator & pull bpv Equipment work completed Fluid system Fill pits with Brine Take on brine & rig hard lines to tree Completed operations Well control Circulated closed in well at 4100.0 ft circ. well bore with 9.9 ppg. brine & monitor. Influx Out of hole Wellhead work Installed Hanger plug Equipment work completed Retrieved Xmas tree Equipment work completed Nipple up BOP stack Installed BOP stack Equipment work completed Test well control equipment Tested BOP stack Pressure test completed successfully - 3000.000 psi Wellhead work Retrieved Hanger plug remove hanger plug & pull hanger to floor & lay dn same. Equipment work completed Pull Single completion, 2-7/8in O.D. Pulled Tubing in stands to 3753.0 ft 13 Mar 00 00:30 00:30-02:30 2 hr 02:30 02:30-06:00 06:00 3-1/2 hr pull 4-stds. & notice gas breaking out of fluid Stopped · To circulate Circulated at 3753.0 ft circ & clean fluids of influx & add sodium bromide for 1-tenth. wt. Hole displaced with Brine - 150.00 % displaced Pulled Tubing in stands to 80.0 ft Stopped · To hold safety meeting 06:00-07:30 06:00-07:30 07:30 07:30-08:30 07:30-08:30 08:30 08:30-01:30 08:30-10:30 10:30 10:30-23:00 1-1/2 hr 1-1/2 hr 1 hr lhr 17hr 2hr 12-1/2 hr Pull Single completion, 2-7/8in O.D. (cont...) Rigged down sub-surface equipment - ESP rig dn esp assy all bands accounted for & guards. Equipment work completed Derrick management Rigged up Completion string handling equipment Equipment work completed Run Single completion, 2-7/8in O.D. Rigged up sub-surface equipment - ESP Equipment work completed Ran Tubing in stands to 4121.0 ft ....... '-'"--- & : .... ""~=' -~ ~'~-' trace/ Facility Date/Time 14 Mar 00 Progress Report M Pt G Pad Well MPG-04 Page 2 Rig Nabors 4ES Date 20 March 00 Duration Activity 23:00 23:00-01:30 01:30 01:30-02:30 01:30-02:30 02:30 02:30-06:00 02:30-03:30 03:30 03:30-06:00 06:00 2-1/2 hr lhr lhr 3-1/2 hr liar 2-1/2 hr On bottom Installed Tubing hanger mu hanger & install heat trace & esp cable. & land hanger Tie-down bolts energised Nipple down BOP stack Rigged down BOP stack install twc & test to 2500 psi. before rig dn bop Equipment work completed Wellhead work Installed Xmas tree Equipment work completed Tested Xmas tree test adapter fig. & tree to 5000 psi. & i pull twc & install bpv Pressure test completed successfully - 5000.000 psi MEMORANDUM State of Alaska TO: Alaska Oil and Gas Conservation Commission THRU: David Jo~ Chairma~ DATE: March 12, 1997 Blair Wondzell, .~~ P. i. Supervisor FROM: Bobby Fos.~//~ SUBJECT: Petroleum Inspector FILE NO: A5LICLEE.doc BOPE Test - Rig 56 UNOCAL - TBU Monopod Platform. PTD# 89-0045 Wednesday,. March 12, 199.7: ! traveled this date to UNOCAL's TBU Monopod platform and witnessed the BOPE test. · As the attached AOGCC BOPE test report shows, all items passed. ! did not witness the testing of the upper and lower kelly valves or the blind rams due to being involved in doing SVS test also. The gas detection system was not tested since it was installed only last week but it will be tested when rig is skidded over the next well. Summary: i witnessed the BOPE test on UNOCAL's rig 56 - test time 3 hours - no failures. Attachment: A5LICLEE.XLS Unclassified Confidential (Unclassified if doc. removed ) STATE OF ALASKA OIL AND GAS CONSERVATION COMMISSION BOPE Test Report OPERATION: Dflg: X VVorkover: DATE: 3/f2_,/97 Drlg Contractor: ..... POOL - ' Rig No. 56 PTD # . 89-0045, Rig Ph.# g07-776-6676' "- : Operator: ............. UNOCAL ....... Rep.: DON BURNE .................... Welt Name: A-08 Rig Rep.: PAUL BARR casing Size: "'g. 625)~7" .......... set ~ 7340, ~ Location: Sec.' ~(" T. ~N R. f3W Meridian- ' - S ....... Test:. Initial ~' ~ Weekly "'~ .... off'er , .i . ,,, Test MISC. INSPECTIONS: Location Gen.: OK Well Sign OK Housekeeping: .."OK .. (Gen) Drl. Rig OK PTD On Location TLS Hazard Sec. YES - Standing Order Posted YES ' FLOOR SAFETY VALVES: Upper Kelly / IBOP Lower Kelly / IBOP Bali Type Inside BOP Quan. 1 I Pressure P/F i 50O/5,000__ 500/5,000 "500/5,'000.. I.P BOP STACK: Annular Preventer Pipe Rams Lower Pipe Rams Blind Rams Choke Ln. Valves HCR Valves Kill Line Valves Check Valve Ouan. Test Press. P/F 3 p. 500/5,000 P .500/5,~ "'P 2.. 500/ ,000. p. ..... I N,/.A ,, i . MUD SYSTEM: V'=uai Alarm Tdp Tank OK OK Pit Level Indicators OK OK Flow Indicator OK OK Meth Gas Detector OK ' 0/~"' - H2S Gas Detector ..... OK' ' oK ' CHOKE MANIFOLD: No. Valves ,17 I No. Flanges 48 I Manual Chokes ~//f Hydraulic Chokes Test Pressure P/F 500/5,000 I P 5o0/5,0oo '~ P ' Functioned I P Functioned _ P ' ACCUMULATOR SYSTEM: System Pressure Pressure After Closure .. 200 psi Attained After Closure System Pressure Attained 2 Blind Switch Covers: Master: Nitgn. Btl's: ~ 4 ~. 2700 .. ,, ~400 ....l, P, minutes 22 sec. ~ minutes '~7"sec. YES Remote: YES Psig. Number of Failures: 0 ,Test Time:..,3,p Hours. Number of valves tested 24 Repair or Replacement of Failed Equipment will be made Will'in" days. Notify the Inspector and follow with Wr~ten or Faxed verification to the AOGCC Commission Office at: Fax No. 276-7542 Inspector North Slope Pager No. 659-3607 or 3687 If your call is not returned by the inspector within 12 hours please contact the P. I. Supervisor at 279-1433 .... I Illl IlI I I. I I Il IIllll Il_Il I Ill II I II II I I IIII I Il I I I I IlI Ill I Il I IlI I Il , I I II I Il I I REMARKS: I.cr~i· not, .. witness.,., ~ . ,the. . testin~l of,the blind rams, or the upper an~, ,,,Iower kelly,,valves due to being on SVS test. Also the gs detection .~. ui ment was not tested- system installed last week and tested- will be retested when rig moves over :: - . ' I III , . Il 11 11 I ~ , I I Ill III 11 I I I II. I .I I. I I I. I I I[ I I I next well. Distribution: or[I-Well File c - Oper./Rig c - Database c - Trip Rpt File c - Inspector :STATE WITNEss' REQUIRED?" YES X NO 24 HOUR NOTICE GIVEN YES X NO , . . I I I , . II I_ I .1 I I11 I IJI . III [ , _1 . I _ I , . L.III I I I III Waived By: Witnessed By: BOBBY D. FOS TLR FI-021L (Rev. 12/94) A5LICLEE.XLS Alaska Oil Gas Conservation Commission 380i Porcupine Drive Anchorage, Alasf<a §g501-3192 907-279-1433 Permit # The following data is hereby acknowledged as being received: / ~~/~~ Dated: RECEIVED JAN 1 9 199~ jAlaska Oil & Gas Cons. Commission No Anchorage '?~"~ STATE OF ALASKA ~"~' A~~ OIL AND GAS CONSERVATION COMMI~ON REPORT OF SUNDRY WELL OPERTIONS ORIGINAL 1. ~Ype of Request: Operation shutdown Stimulate Alter casing m Repair well ~ Pull Tubing m Alter casing Repair well Other X Perforate 2. 6. Datum elevation (DF or KB) Name of Operator Conoco Inc. Address 3201 C Street, Suite 200 Anchorage, AK 99503 5. Type of Well: Development Exploratory Stratigraphic Service Location of well at surface 3466' FNL, 3370' FEL, Sec.27, T13N, R10E, U.M. NSB AK At top of productive interval 2028' FNL, 3283' FEL, Sec. 27, T13N, R10E, U.M. NSB AK At effective depth 1838' FNL, 3282' FEL, Sec. 27, T13N, R10E, U.M. NSB AK At total depth 1799' FNL, 3282; FEL, Sec.27, T13N, R10E, U.M. NSB AK Present well condition summary Total depth: measured true vertical 4950' feet Plugs (measured) 4584' feet Effective depth: measured 4850' feet Junk (measured) true vertical 4491' feet Casing Length Size Structural Conductor 75' 13-3/8" Surface 2639' 9-5/8" Intermediate Production 4894' 7" Uner Perforation Depth: KB 59.3' (MSL) Unit or Property name Milne Point Unit 8. Well number G-4 9. Permit number 89-45/92-239 10. APl number 50-029-21941 11. Reid/Pool Kuparuk River/Schrader Cemented Measured depth True vertical depth Surface 110' 110' Surface 2674' 2513' feet 51 bbls. Premium 4929' 4565' measured 4312-4320'; 4362'-4366'; 4372'-4378'; 4394'-4430'; 4445'-4456'; 4480'-4514'; 4554'-4570';4572'-4576' true vertical 3988'-3995'; 4034'-4038'; 4043'-4049'; 4064'-4097'; 4111'-4122'; 4144'-4176'; 4213'-4228';4230'-4234' Tubing (size, grade, and measured depth) 2-7/8" 6.5~/ft, 8rd EuE, 4046' MD Packers and SSSV (type and measured depth) Baker SC-IL Packer @ 4178' MD, Baker Model "D" Packer @ 4586' MD 12. 13. Stimulation or cement squeeze summary See attached "Completion Sketch" for treatment descriptions (item No. 8). Intervals treated (measured) Treatment description including volumes used and final pressure 14. Prior to well operation Subsequent to operation RECEIVED Representative Daily Averacje Production or Injection Data OiI-Bbl Gas-Mcf Water-Bbl Casing Pressure Tubing Pressure 307 113 3 252 264 136 ~''' 0 61 180 171 Service Date t'L-~.,[-~ SUBMIT IN DUPLICATE 15. Attachments 16. Status of well classification as: Copies of Logs and Surveys run Daily Report of Well Operations X Oil X Gas Suspended. Signed ~lt~ ~ ~ Title~~l~, ~:J~ Form l~ev ~/15/~ 0 [ Milne Point Unit G-04 API No.: 50-029-21941 Location: Milne Point Field - G-04 Complete 'N' Sands & Gravel Pack Current Operations: Released Rig to E-7. 10/31/92: Finish rig move from H-2 to G-4. Total down time due to bad weather was 6 hours. R/U on tree and kill well. N/D tree and N/U BOPE. Test BOPE. 11/01/92: P/U hanger, cut ESP cable, L/D hanger and band ESP cable to tubing. P/U singles and TIH to 4672' - did not tag fill. POOH with ESP assembly. R/U HLS E/L unit and make GR/CCL & 6" gauge ring/junk basket run 4558' - unable to get below perfs. Log out of hole and make 5.8" gauge ring run to 4620'. P/U sump packer and TIH to 4586'. Attempt to set packer - failed. POOH with sump packer. R/U E/L perforating guns and begin perforation operation. 11/02/92: Perforate with E/L from 4455' to 4312' - 100% fire. R/D E/L unit. Change rams to 4" and test BOP's. Fill hole, hole taking ±24 BPM. M/U TCP assembly and TIH on 4" drill pipe. R/U E/L unit and RIH with GR/CCL to correlate TCP guns. 11/03/92: Correlate TCP guns with E/L to space-out top shot at 4312' MD. POOH & R/D E/L. Set packer, M/U and test surface lines to 2500 psi. Displace tubing with 45 bbls diesel to achieve a 325 psi underbalance. Close annular and Function 'Fast Fil' valve with 1000 psi on annulus. Open TIW valve on drill pipe and pressure up to 2000 psi on annulus to fire guns (fired at 1350 psi). Open well for flow for 1 hour - no measurable flow. Function APRM-2 valve with 3500 psi on annulus and reverse circulate 190 bbls. Unseat packer and POOH with TCP assembly (100% fired). M/U 7" casing scraper and TIH to 4639' MD. POOH & L/D scraper. R/U E/L and M/U 7" EZSV. RIH and set same at 4469' MD (between 'N' & 'O' sands). POOH & R/D E/L. Change rams from 4" to 2- 7/8". 11/04/92: Test BOPE. TIH with EZSV stinger and sting into EZSV at 4469'. R/~ and test surface equipment. Perform sand pre-pack on 'O' sands (ISIP 200 psi). Unsting, POOH to 4276' and circulate. Perform sand pre-pack on 'N' sands. Sand out at 4000 psi. Monitor well and CBU (10 minute SIP at 1200 psi). POOH and L/D stinger. Change to 4" rams and test BOP rams to 300/3000 psi. P/U bulldog bailer and TIH on 4" DP. 11/05/92: Finish TIH with bailer and tag fill at 4169'. Bail 15.5' and bailer stopped functioning. POOH and found rubber in pump component. TIH and bail 30' when bailer stopped functioning. POOH and check bailer - OK. Rearrange assembly and TIH and tag fill at 4198'. Bail sand to EZ Drill at 4461'. POOH 6 stands and wait 1 hour. TIH and tag EZ Drill at 4461'. POOH and L/D bailer. 11/06/92: Clean sand from drill pipe & floor. M/U bit and 2 junk baskets and TIH and tag fill at 4452' (9' of sand fill), hook up power swivel and drill sand to EZ Drill at 4461'. Drill EZ Drill. TIH with no weight and tag up at 4643'. POOH with bit and junk basket assembly. R/U HLS and run 5.8" gauge ring/junk basket to 4620'. 11/07/92: RU wireline and change rams to 2 7/8". Make GR and junk basket run to 4613' RIH and set sump packer at 4586' RD wireline Pull wear bushing, run test plug, test BOPs and choke manifold to 300/3000#, change to 4" rams, test rams, pull test plug, run wear ring. LD-DC, TIH with 40 PTS DP. POOH LD DP. Repair backup on tongs. RIH with 13 STNDS DP, POOH with 3 JTS, Pipe full of oil. Hook up and circulate 48 BBLS. Circ out 20 bbls oil. RIH with 23 stnds, circ 10 bbls, LD DP. Fill hole with 10 bbls. Change rams to 2 7/8, pull wire bushings, set test plug, test 2 7/8" rams to 300/3000#, run wear bushing. 11/08/92: Hold safety meeting. PU & RIH w/305' screen/67' blank pipe, RIH w/wash pipe , pkr, tbing, RU & circ down to sump pkr, Space out. RU manifold on floor and hole prejob safety meeting. Pressure test eqpt. Set pkr at 4178 with 2600 psi. Pressure up on circ sub several times 4000# to 5000# wouldn't shear. RD manifold and pump lines. POOH wet. LD Dowell equipment. POOH to circ sub. Change out circ sub. Clean oil off rig floor. RIH with circ. sub and 1 STD, pressure to 1800 shear circ. sub. RIH sting into pkr. RU Halliburton and hold safety meeting. Test lines & Establish rates at various positions. 11/09/92: Pump total 43 bbls and 4100# sand, flush with 36 bbls didn't sandout, PU to reverse position, reverse 36 bbls of sand. Filter fluid in pits. Pump total 20 bbls slurry and 2000* sand, flush with 12 bbls. Sanded out to 1904#, PU to rev. pos. Reverse out 1300# sand, rev 90 bbls. Repressure pack to 750# at 1/2 bpd - shield sleeve, test to 2600#, RD Halliburton and Baker Equipment. Mix safe clean (50 bbls). Reverse safe clean and brine (209 bbls). POOH LD 3 bad jts, GP tool and wash pipe, Pull wear bushing. Run ESP equipment. 11/10/92: Finish pigtail splice. Test penetrator and land hanger. Install two check valve. Note pump located at 4124'. Nipple down BOP & choke line. Test Hanger to 5000psi. Clean pits. Nipple up tree and test same to 5000psi. Pull two way check valve & install BPV. Check ESP readings. Freeze protect with 25 BBLS down annulus and 5 BBLS down tubing. Finish Rig Down. RECEIVED DEC; 9 Alaska Oil & Gas Cons. Commission Anchorage WELL No. G-4 COMPf,ETION SKETCH MILNE POINT UNIT APl No.: 50-029-21941 PERMIT No.: 89-45 COMPLETED: 11/22/90 LAST WORKOVER: 11/9/92 ~ WKM 2 7/8' TUBING HANGER W/ 'H" PROFILE BPV NOTES: 1. ALL DEPTHS MEASURED RKB = ~2' 2 7/8' 6.5# L-80 8rd EUE PUP (1.60') TOP OF TUBING (33.6') 2. MAX. ANGLE = 29'44' {J 2300' .3. K.O.P. = 600' 4. SLANT HOLE: YES o , TREE TYPE..' WKM 2 9/16" 5000# W/ 2 7/8" 8rd TREETOP CONNECTION MIN. i.D. = 2.062" JJ 4585' COMPLETION FLUID: 8.6 PPG NoCl STIMULATION: FRAC (4480'-4514') PUMPED 20098~ OF 16/20 MESH CARBO-LITE FRAC (4554'-4576') PUMPED 21736i~ OF 16/20 MESH CARBO-UTE FRAC (4480'-4576') PUMPED 16,000# OF 20/40 MESH GRAVEL PACK SAND. (11/3/92) FRAC (4312'-4456') PUMPED 15,000# OF 20/40 MESH GRAVEL PACK SAND. (11/3/92) ESP ASSEMBLY: CENTR1LIFT FC-650 PUMP, 184 STAGES, 65 HP, 1250V/30A MOTOR, FPINT INTAKE (HP-2), GSB-T SEAL SECTION, PHD UNIT N SAND PERFORATION DATA DEPTH: 4312'-4520' 5988'-3995' 4562'-4366' 44334'-4038' 4372'-4378' 4043'-4049' 4394'-4430' 4064'-4097' 4445'-4456' 4111'-4122' DENSITY: 24 SPF, 22.7 GM 0 SAND PERFORATION DATA M___QD TVD DEPTH: 4480'-4514' 4144'-4176' 4554'-4570' 4213'-4228' 4572'-4576' 4230'-4234' DENSITY: 16 SPF, 25 GM &: 56 GM 123 JTS. 2' 7/8" 6.5# L-80 8rd EUE TUBING ESP CABLE - No. 2 CL-350 3935' 2 7/8" 6.5t¢ L-80 8rd EUE PUP (6.15') 3941' SIDE POCKET MANDREL l"x 2 7/8' (6.45'1 3947' 2 7/8' 6.5# L-80 8rd EUE PUP (3.68') 2 JTS, 2 7/8' 6.5# L-80 8rd EUE TBG (63.33') 4014' CHECK VALVE (0.40') 2 JTS. 2 7/8" 6.5# L-80 8rd EUE TBG (63.15') 4078' 2 7/8" 6.5# L-80 8rd EUE PUP (8.10') 4086' TOP (~F ESP 4125' BOTTOM OF ESP 4178' BAKER SC-IL PACKER (4.00" I.D.) ~ 4212' BAKER 3 1/2' BLANK PIPE (67') -~-4279' BAKERWELD &: HOWARD SMITH 3 :" 12ga SCREEN (305') ~ GRAVEL PACK (O,lg, l SANDS) 20/40 MESH GRAVEL 4585' BAKER SNAP LATCH SEAL ASSEMBLY (2.062" I.D.) 4586' BAKER MODEL "D" PACKER (3.25" I.D.) 4596' WlRELINE RE-ENTRY BOTTOM GUIDE (3.03' I.D.) 4850' PBTD 7" CASING iJ 4929' CONOCO INC. ANCHORAGE DIVISION JAPPROVED BY: BGA DRAFTED BY: CFP DATE: 11/12/92 CAD FILE: WCOG4 Conoco Inc. 3201 C Street, Suite 200 Anchorage. AK 99503-3999 (907) 564-7600 September 28, 1992 Mr. David Johnston Commissioner Alaska Oil and Gas Conservation Commission 3001 Porcupine Drive Anchorage, Alaska 99501 RE: APPLICATIONS FOR SUNDRY APPROVAL Dear Mr. Johnston, Attached are Applications for Sundry Approval, Form 10-403, for perforating Milne Point Unit Well G-4 and for pulling tubing in Milne Point unit Well H-2. Please direct any questions regarding these applications to me at 564-7660. L .~~J~ Tom Yeager "-J SHEAR Specialist Attachments cc: Chevron Occidental H-2 Well File G-4 Well File RECEIVI D S E P ~} 0 1992 Alaska 0il & Gas Cons, C0.mmissi0[~ Anchorage "il STATE OF ALASKA ALASKA OIL AND GAS CONSERVATION COMM~)SION APPLICATION FOR SUNDRY APPROVALS Type of Request: Abandon __ Suspend Operation shutdown Re-enter suspended well Alter casing Repair well m Plugging_ Time extention Change approved program __ Pull tubing . Variance __ Perforate X Name of Operator Conoco Inc. Address 3201 C Street, Suite 200 Anchorage, AK 99503 Location of well at surface 346E FNL, 3370' FEL, Sec. 27, T13N, R10E, U.M. At top of productive interval 2719' FNL, 3308' FEL, Sec. 27, T13N, R10E, U.M. At effective depth 1838' FNL, 3282' FEL, Sec. 27, T13N, R10E, U.M. At total depth 1799' FNL, 3282' FEL, Sec. 27, T13N, R10E, U.M. 5. Type of Well: Development X Exploratory Stratigraphic Service NSB AK NSB AK NSB AK NSB AK Stimulate ~ Other __ 6. Datum elevation (DF or KB) KB 59.3' (MSL) 7. Unit or Property name Milne Point Unit feet 8. Well number G-4 9. Permit number 89-45 10. APl number 50-029-21941 11. Field/Pool Kuparuk River/Schrader Bluff 12. Present well condition summary Total depth: measured 4950 feet Plugs (measured) true vertical 4584 feet None Effective depth: measured 4850' feet Junk (measured) true vertical 4491 feet Casing Length Size Structural Conductor 75' 13-3/8" Surface 2639' 9-5/8" Intermediate Production 4894' 7.' Uner Perforation Depth: measured 4480'-4514', 4554'-4570', 4572'-457~ Cemented Surface Surface 51 bbls. Premium true vertical 4143'-4176', 4213'-4233', 4231'-4234' Tubing (size, grade, and measured depth) 2-7/8", 6.5#, L-80, 8rd EuE, 4437' MD Packers and SSSV (type and measured depth) None Measured depth 110' 2674' 4929' True vertical depth 110' 2513' 4565' SEP 3 0 1992 Alaska Oil & Gas Cons, Ancti0rag~ 13. Attachments Description summary of proposal. X Detailed operations program __ BOP sketch 14. Estimated date for commencing operation November 15, 1992 16. If proposal was verbally apprOved Oil X Gas Name of approver Date approved Service 17.1 hereby certify that the~is true and correct to the best of my knowledge. Signed ~z,.~.~ B.G. Augustine Title Sr. Production Engineer FOR COMMISSION USE ONLY 15. Status of well classification as: Suspended , Date September 22, 1992 ,,.~proval No. - ? Conditions of approval: Notify commission so representative may witness Plug integrity BOP Test Location clearance Mechanical Integrity Test Subsequent form required 10- Original signed By Approved by order of the commission David V~, Johfls'toFI commissioner Form 10-403 Rev 06/15/88 SUBMIT IN TRIPLICATE MILNE POINT UNIT G-4 --~ COMPLETE 'N' SANDS AND GR~VEL P/~CK WELL SUMI~¥ PROCEDURE · · MIRU EWS #4 rig. Kill well with 8.6 ppg NaCl with 12% methanol· ND production tree. NU BOPE and test. · · POOH with tubing, ESP, and ESP cable. LD ESP and cable. RIH with bailer on drill pipe and tag fill. 5. Bail out fill to PBTD, as necessary. · · POOH with drill pipe and bailer. LD bailer. RU electric line unit. Make GR/JB run. Set sump packer at ± 4500'. RD electric line unit. · · RIH with tubing. prepack. RU treating company. Pump 'O' sands gravel Sand back well to ± 4470'· RD treating company. POOH with tubing. 10. RU electric line unit. RIH with perforating guns and perforate the following intervals with 12 SPF: 4312'-4320' 4362'-4366' 4372'-4378' 4394'-4420' 4445'-4456' RD electric line unit. 11. RIH with perforating guns on tubing and reperforate the above intervals with 12 SPF. Flow well. POOH with perforating guns. 12. RIH with tubing. RU treating company. Pump 'N' sands gravel prepack. 13. Reverse out sand to sump packer. Break glass disk below sump packer. POOH with tubing. 14. RIH with gravel pack assembly and locate on depth. 15. RU treating company. Pump gravel pack. RD treating company. POOH with workstring. 16. PU new ESP assembly and cable. RIH with ESP and tubing. bottom of pump at ± 4200'. 17. ND BOPE. NU production tree and test. 18. RDMO EWS ~4 rig. 19. Return well to production. Set RECEIVED S EP 0 1992 Alaska Oil & Gas Cons. Anchorage Conoco Inc. 3201 C Street, Suite 200 Anchorage, AK 99503-3999 (9O7) 564-760O October 8, 1991 Mr. David Johnston Commissioner, Alaska Oil and Gas Conservation Commission 3001 Porcupine Drive Anchorage, AK 99501 RE: Report of Sundry Well Operations; Reservoir Pressure Report Dear Mr. Johnston: Attached please find a Report of Sundry Well Operations for Well G-4 and a Reservoir Pressure Report for Well E-7. These wells are located on the Milne Point Unit. If you have any questions or require additional information please contact me at 564-7617. Yours very truly, Bob Soptei Environmental Coordinator RJS/bgs attachments CC Occidental Petroleum Chevron Inc. E-7 Well File G-4 Well File C:\DATA\WP51 \RJ S\AOGCC\AOGCC 19 STATE OF ALASKA0 AI. ASKA OIL AND GAS CONSERVATION COMMISSION REPORT OF SUNDRY WELL OPERATIONS RI 61 AL 1. Operations pedormed: 2. Name of Operator Operation shutdown ~ Pull tubing __ Alter casing __ CONOCO INC. 3Address 3201C St , Sulte 200, Stimulate __ Plugging __ Perforate __ Repair well __ Other ~X I5. Type of Well: Development X__. Exploratory __ Stratigraphic __ Service __ 4. Location of well at surface Anchorage, AK 9950~ 3466'FNL, 3370' FEL, SEC 27, ~topofproductiveinterval 2719'FNL, 3308' FEL, SEC 27, ~eflectivede~h T13N, RiOE, U.M. T13N, R10E, U.M. 1838'FNL, 3282' FEL, SEC 27, At total depth 1799'FNL, 3282' FEL, SEC 27, 4950' 4584' 12. Present well condition summary Total depth: measured true vertical T13N, R10E, U.M. T13N, R10E, U.M. feet Plugs (measured) feet Effective depth: measured 4849 ' true vertical 4491 ' feet Junk (measured) feet 6. Datum elevation (DF or KB) (KB) 59.3' MSL feet 7. Unit or Property name Milne Point Unit 8, Well number G-4 9. Permitnumberlapprovalnumber 89-45 10. APInumber 50-- 029-21941 11. Field/Pool Kupa~uk River/Schrader Blur Casing Structural Conductor Surface Intermediate Production Liner Perforation depth: Length Size 110' 2674' 13 3/8" 9 5/8" 4929' 7" measured 4480' 4554' truevertical 4143' 4213' Tubing (size, grade, and measured depth) 2-7/7", 6.5f~, L-80, (4433 ft), Packers and SSSV (type and measured depth) No Packers & no SCSSV. - 4514' - 4570' - 4176' - 4228' Cemented ESP Set @ Measured depth Arctic Set to Surface 189 bbls Permf "E" 112 bbls Class "G" 51 bbls PRRM 19 bbls Arctic Set 4572' - 4576' True vertical depth 110' 110' 2674' 2513' 4230' - 4233' 4473' RKB. 13. Stimulation or cement squeeze summary N/A Intervals treated (measured) N/A Treatment description including volumes used and final pressure 4929' 4565' 14. B,e. presentative Daily Average Production or Injection Data OiI-Bbl Gas-Md Water-Bbl Casing Pressure Tubing Pressure Prior to well operation 229 129 3 275 275 Subsequent to operation 332 19.5 7 288 288 15. Attachments Copies of Logs and Surveys run Daily Report of Well Operations 16. Status of well classification as: Oil __X Gas_ Suspended __ Service 17. I hereby certify that the foregoing is true and correct to the best of my knowledge. ISigned.._ ,,~~ ~f~q~ Title Senior Production Foreman Form 10-404 Rev 06/15/88 f) Date SUBMIT IN DUPLICATE DAILY REPORT OF WELL OPERATIONS SCHRADER BLUFF WELL G-4 CONOCO INC. DATE 1991 OPERATION 8/15 MIRU EWS WORKOVER RIG. KILL WELL W/ 8.5 PPG BRINE. 8/16 N/D TREE, N/U BOP, PULL BPV & INSTALL 2-WAY CK. BOPE (24 HOUR ADVANCE NOTIFICATION TO AOGCC). POOH W/ 2-7/8" TUBING & ESP CABLE. TEST BEGIN 8/17 FINISH PULLING ELECTRIC SUBMERSIBLE PUMP. RIH W/ 20 STANDS OF 2-7/8" TUBING TO 1210'md, PUMP 20 BBLS DIESEL FZ PROTECTION, SHUT IN PIPE RAMS, AND INSTALL TIW VALVE. RIG REPAIRS -- PULLING UNIT ENGINE HAND LEAKY GASKET ALLOWING COOLING FLUID TO ENTER OIL CASE. 8/18 THRU 8/26 RIG REPAIRS. 8/27 FINISH RIG REPAIR. DISPLACE 20 BBLS OF DIESEL W/ 8.5 PPG BRINE. POOH W/ 20 STANDS OF 2-7/8" TUBING AND TEST BOPE (24 HOUR ADVANCE NOTIFICATION TO AOGCC). RIH W/ SAND BAILER ON 4" DRILL PIPE. BAIL F/4504'-4849' (PBTD). 8/28 POOH TO 4400', LET SAND SETTLE, AND RIH TO 4849' (NO FILL). POOH L/D 4" DP & BULL DOG BAILER. P/U OTIS 'PLS' RETRIEVABLE PACKER, RIH ON 2-7/8" TUBING, AND SET AT 4455'. PERFORM CASING WASH. 8/29 RELEASE PACKER, POOH W/ OTIS 'PLS' RETRIEVABLE PACKER. M/U ESP AND RIH ON 2-7/8" TUBING. SET PUMP AT 4473'. LAND HANGER, SET BPV,.N/D BOPE, N/U TREE, PULL BPV & INSTALL 2-WAY CK, TEST ll"X5M FLANGE AND TREE TO 5000 PSIG. PULL 2-WAY CK, FZ PROT 2-7/8" X 7" ANNULUS, INSTALL BPV, AND FZ PROT TUBING. R/D MOVE OUT WORKOVER RIG. END OF REPORT J.D. POLYA DRILLING FOREMAN CONOCO INC. STATE OF ALASKA ALASKA OIL AND GAS CONSERVATION COMMISSION APPLICATION FOR SUNDRY APPROVALS ORl61 1. Type of Request: Abandon ~ Suspend Operation shutdown __ Re-enter suspended well __ Nter casing. Repair well __ Plugging m Time extention , Stimulate Change approved program __ Pull tubing Variance Perforate ,L Other ,.,,.X Name of Operator Conoco Inc. Address 3201 C Street, Suite 200 Anchorage, AK 99503 5. Type of Well: Development Exploratory Stratigraphio Service Location of well at surface 3466' FNL, 3370' FEL, Sec. 27, T13N, R10E, Umiat Meridian At top of productive interval 2719' FNL, 3308' FEL, Sec. 27, T13N, R10E, Umiat Meridian At effective depth 1838' FNL, 3282' FEL, Sec. 27, T13N, R10E, Umiat Meridian At total depth 1799' FNL, 3282' FEL, Sec. 27, T13N, R10E, Umiat Meridian 6. Datum elevation (DF or KB) (KB) 59.3' 7. Unit or Property name Milne Point Unit 8. Well number G-4 9. Permit number 10. APl number 50-029-21941 11. Field/Pool Kuperuk River/S~hrader Bluff feet 12. Present well condition summary Total depth: measured 4950' feet true vertical 4584' feet Plugs (measured) None Effective depth: measured 4849' feet true vertical 4491' feet Junk (measured) None Casing Structural Conductor Surface Intermediate Production Uner Perforation Depth: Length Size 110' 13-3/8" 2674' 9-5/8" 4929' 7" measured 4480'- 4514' 4554'- 4570' true vertical 4143'- 417E 4213'- 4228' Tubing (size, grade, and measured depth) 2-7/8", 6.5#, L-80, 4447 with ESP Packers and SSSV (type and measured depth) None Cemented Arctic Set to Surface 189 bbls Perm F "E" 112 bbls Class "G" 51 bbls PRRM 19 bbls Arctic Set 4572'- 4576' 4230'- 4233' Measured depth 110' 2674' 4929' True vertical depth 110' 2513' 4565' RECEIVE JUL l 1 1991 Alaska 0il & Gas Cons. Corm Anchorage 13. Attachments Description summaryof proposal X Detailed operations program BOP sketch __ 14. Estimated date for commencing operation July 30, 1991 16. If proposal was verbally approved 15. Status of well classification as: Oil X Gas__ Suspended. 17. I hereby certify that the foregoing is true and correct to the best of my knowledge. Signed '~J-~B. G. Augustine Title Senior Production Engineer FOR COMMISSION USE ONLY Date Conditions of approval: Notify Commission so representative may witness Plug integrity BOP Test Location clearance Mechanical Integrity Test __ Su"~bsequent form required 10-'~q.. Approved C.opy ORIGINAL SIGNED BY ,..Returnqa. Approved by order of the Commission LONNIE C. SMITH r'///~7/"//~Commlssioner IlLI I / Form 10-403 Rev 06/15/88 ,., IApproval No. SUBMIT/IN TRIPUCATE ~ I~IILNE PO~'NT UNIT ~-4 S UI, fl~,RY PROCEDURE 1. MIRU EWS #4 rig. 2. Kill well with 8.6 ppg NaCl. ND production tree. NU BOPE and test. 3. PU tubing joints and RIH to tag fill. 4. POOH with tubing, ESP, and ESP cable. LD ESP and cable. 5. RIH with bailer on 2-7/8" tubing and tag fill. Bail fill to 4650'. 6. POOH with tubing and bailer. LD bailer. 7. PU new ESP, motor, and cable. RIH with ESP assembly and tubing. Set bottom of pump at 4440'. 8. ND BOPE and NU production tree. RDMO rig. 9. Return well to production. - " ALASKA OIL AND GAS CONSERVATION COMMISSION WELL COMPLETION OR RECOMPLETION REPORT AND LOG , ,. 1. Status of Well Classification of Service Well OIL ~ GAS [] SusPENDED [] ABANDONED [] SERVICE [] 3'Au~f~045 PRUDHOE BaY, 2a.K 99734 s'~(~'-'2~fl, 94'1 · , 4. L~a4~iw~%rfa~370, FEL. SECTION 27, T13N. RlC~ 9. ~2~se~T UNIT At~T~uc~%~va~308' FEL, SECTION 27 pAT~ / VE~R~ ~0.~Wumber At1799~thFNL, 3282': FEL, SEC~ZON 27 ~~- ~, S.H~ 'k~~°~ZVER FZELD '- SCH~DER BLUFF POOL 5. E,~,o~i~ [e~ jin~at~; ~F,~ .~ 6.k~g~n and Serial No. 12' ~~~ ~ 13' D~,?i'~d 14' D~~'/~s~', °r Aband. I15. Wa~/~pth' "feetOffshoreMSL ]16' No. of Completions 17"T~l~t~(~T~) 18'PI~~7~(~D)19'Directi'°na'SurveYYES ~ X' "NO~ ] 20. Depth where SSSV set ~ 21.Thickness0fPermafrostN/~ feetMO ~1800' 22'. T~lect~o~Other Lo~s Run ,, 23. CASING, LINER AND CEMENTING RECORD SETTING DEPTH MD C~IN~WT. PE~FT. GRADE TOP BOTTOM HOLE SIZE CEMENTING RECORD AMOUNT PULLED . , . 24. Perforations o~en to Production (MD+TV~ of Top and Bottom and 25. TUBING flECk'fiD ,, interval, size and number) SIZE DEPTH SET (MD) PACKER SET (MD) , , OA S~DS 4480' (4143) - 4514' (4176) Z 7/8" 4447 N/A OB S~DS 4554~ (4213) - 4576, (4233) 26, AC~D, FRACTURE, CEMENTS~UEEZE, ETC. 12JSPF FIRST PERF RUN DEPTH ~NTERVAL (MD) AMOUNT& ~NDOF MATER~ALUSED 4JSPF FIRST PERF RUN 44~0 - 45~,I' 4la ~L Gelle~ wa~er . 20,098 LBS. Carb. Propp 4554 - 457 ~' 38'7 ~L Gelled Water . . 2~,736 LBS. Carb. Propp 27. PRODUCTION TEST Date First Production ' ~ Method of Operation (Flowing, gas lift, etc.) DSTIS 08/12/90-05/09/]0 Electrical Submersible P~p ..... Date of Test Hours Tested PRODUCTION FOR OIL-BSa' GAS-MCF WATER-BBL CHOKE SI~'E { GAS-OIL RATIO 05/09/90 24 TESTPERIOD ~ 390 120 5 34/64~ 308 ....... Flow Tubing Casing Pressure CALCULATED OIL-BBL ~ GAS-MCF WATER-BBL OIL GRAVITY-APl (corr) Press. 140 135 [24-HOUR RATE ~ 39~ 12~ 5~ 18.9 ~ US. CORE D~TA ' Brief description of lithology, porosity, fractures, apparent di~ and presence of oil, gas or ware r. Submit core chios. , [nt ant Form 10-407 Submit in duplicate o,,, -~_~_~n CONTINUED ON REVERSE SIDE 29. 3O. GEOLOGIC MARINERS NAME MEAS. DEPTH Top Upper Ugn L~ 3781 Top Lower Ugn~ 4047 Top West Sak 4480 TRUE VERT. DEPTH RKB 3507 3756 4145 31 LIS.T _OF A_TTA. Cl;IME, N. TS i~alIy AO~lVl~y Reports and Gyro Log FORMATION TESTS Include interval tested, pressure data, all fluids recovered and gravity, GOR, and time of each phase. os/o9/9o 32. I hereby certify that the ;oregoi,~g is true and correct to the best of my knowledge Signed~--~'~ , ~'~"~ ~ Title~'~l~, P~/~, ~~, Date /~ .Z/~(~.~/5' INSTRUCTIONS General' This form is de,,;igned for submitting a complete and correct well completion report and log on all types of lands and leases in Alaska. Item 1' Classification of Service Wells' Gas injection, water injection, steam injection, air injection, salt water disposal, water supply for injection, observation, injection for in-situ combustion. Item 5' Indicate which elevation is used as reference (where not otherwise shown) for depth measurements given in other spaces o:~ this form and in any attachments. Item 16 and 24' If this well is completed for separate production from more than one interval (multiple completion), so state in item 16, and in item 24 show the producing intervals for only the interval reported in item 27. Submit a separate form for each additional interval to be separately produced, showing the data pertinent to such interval. Item 21' Indicate whether from ground level (GL) or other elevation (DF, KB, etc.). Item 23: Attached supplemer~tal records for this well should show the details of any multiple stage cement- ing and the location of the cementing tool. Item 27: Method of Operation: Flowing, Gas Lift, Rod Pump, Hydraulic Pump, Submersible, Water in- jection, Gas Injection, Shut-in, Other-explain. Item 28' If no cores ti, ken, ir~dicate "none". Form 10-407 APPENDIX 4.2 Iq]LNE POTNT NELL G-4 DST 1, IA, AND ].B FLOI/ DATA SUHHARY MILNE POINT WELL G-4 DSTS 1, lA, AND lB TEST INTERVAL: 4480' TO 4514', AND 4554' TO 4576' MD SHALLOW OIL SANDS: OA AND OB SANDS 4.1 RESULTS SUMMARY Initial Completion Zone Perforations Perforating Guns Perforating Underbal ance Shallow Oil Sands OA and OB Sands 4480' to 4514' MD: OA Sand 4554~ to 4570~ MD: OB Sand 4572~ to 4576' MD: OB Sand Vann 4-5/8" TCP Guns, 12 SPF, 30° phasing, 25 gram RDX charges 250 psi 4.1.1 DST 1 Initial Flow/Buildup Periods Duration of Initial Flow 7.5 minutes Duration of Initial Buildup 2.9 hours Extrapolated Pressure, P* at 1838 psia 4130' TVDSS Datum Final Flow Period Duration Final Flow Rate Recovery FFWHP FFBHP Choke Size Flowing BHT 18.9 hours 73 STB/D of 21.3°API oil 0 Bbls/D of water 53 STB of 21.3°API oil O'Bbls of water 34 psig 1569 psia at 4130~ TVDSS 32/64 inch 84°F Final Buildup Period Duration of Buildup 28.7 hours Pressure Transient Analysis Results- kh/p (md-ft/cp) Permeability to Oil (md) Radius of Investigation (ft) P* (psia at 4130' TVDSS) Darcy Skin 377 180 65' 1832 +4.4 (4.1) Milne Point Well G-4 G-Pad Test Pro~ram Report 4.1.2 DST lA Electric Submersible Pump Test With Downhole Shutin Duration Final Flow Rate Recovery FFWHP FFBHP Choke Size 90.8 hours 33 STB/D of oil 5 Bbls/D of water 54 STB of oil 139 Bbls of water 13 psig 1370 psia at 4130~ TVDSS Datum 32/64 inch DST lA Buildup Period Duration of Buildup 50.8 hours Pressure Transient Analysis Results: kh/p (md- ft/cp) 4]9 Permeability to Oil (md) 173 Radius of Investigation (ft) 80' P* (psia at 4130' TVDSS) 1829 Darcy Skin +21 4.1.3 DST lB Post-Fracture Treatment Electric Submersible Pump Test With Packer~ First Flow Period Duration Final F1 ow Rate Recovery FFWHP FFBHP Choke Si ze 48.3 hours 237 STB/D of oil 71MSCF/D of gas 17 Bbls/D of water 320 STB of oil 204 Bbls of water 132 psig 1414 psia at 4130~ TVDSS Datum 20/64 inch Post-Fracture Treatment Electric Submersible Pump Test With Packer Unseated, Second Flow Period Duration Final F1 ow Rate Recovery FFWHP FFBHP Choke Size 53.3 hours 400 STB/D of oil ]45 MSCF/D of gas 3 Bbls/D of water 701STB of oil 134 Bbls of water 66 psig 1076 psia at 4130~ TVDSS Datum 34/64 inch (4.2) Milne Point Well G-4 G-Pad Test Program Report DST lB Buildup Period Duration of Buildup 33 hours Pressure Transient Analysis Results: kh/p (md-ft/cp) 410 Permeability to Oil (md) 196 Radius of Investigation (ft) 60 P* (psia at 4130~ TVDSS) 1855 Total Pseudo-Radial Skin -2 Fracture Half-Length (ft) 40 Fcd 2 4.1.4 WELL G-4 RESERVOIR AND FLUID DATA Reservoir Parameters- Net Thickness 58~ Porosity 24% Water Saturation . 32% Fm. Compressibil ity 7.0E-O5/psi Oil Properties at Initial Reservoir Conditions' API Gravity Solution Gas Oil Ratio Formation Volume Factor Vi scosi ty 21.3° 180 SCF/STB 1.085 bbl/STB 27.7 cp (4.3) The rates provided in this summary for Well G-4, DSTs 1, lA, and lB, are averaged over the time intervals at which the rates are reported. Flow rates were monitored at the test separator during DST lB only. During DSTs 1 and lA the flowing wellhead pressures and rates were too low to use the separator. The field data used to generate this rate summary is in PTS report (Ref. 4.1). SUMMARY OF RATE MEASUREMENTS FOR DST 1 . , ~ Sep Sep Choke Oil Gas Water Date Time BHP(1) WHP WHT Press. Temp Size Rate Rate Rate BS&W ............ lpsia) Ipsiq) ~OF) ~psiq) ~°F) 164tbs) .~Bbls/D)~MSCF/D) IBbls/D) I%} Comments 3/14 0819 1794 250 - - - 0 0 - 0 Open well for 1025 1575 15 - - 6 40 - 0 100 final flow 1200 1648 42. 66 - - 9 57 - 0 100 BS&W is 100% 1400 1577 35 78 - - 12 30 - 0 100 diesel cushion 1600 1449 32 52 - - 14 95 - 0 100 2000 1539 34 29 - - 32 85 - 0 0 21.3°API oil at 2400 1554 34 41 - - 32 58 - 0 0 surface 3/15 0300 1535 34 40 - - 32 73 - 0 0315 1535 Shut in well downhole for DST 1 final buildup 0 Took oil samples (1) Bottom hole pressure is reported at gauge depth, 4432' MDRKB. SUMMARY OF RATE MEASUREMENTS FOR DST lA Sep Sep Choke Oi 1 Gas Water Date Time BHP(1) WHP WHT Press. Temp Size Rate Rate Rate BS&W ......... (psia) (l~siq) {°_F) (psiq) (°F) (64ths) ,(Bbl,s/D) (MSCF/D) (,B, bls/D) (%) Comments 3/19 0545 1804 Start ESP for DST lA flow test 0845 1695 90 - - - 9 0 - - - Fluid at surface 1100 1663 46 86 - - 10 0 - 170 100 BS&W is 9.2 ppg 1515 1636 38 110 - - 10 0 - 108 100 brine 1915 1618 60 25 - - 10 0 - 120 100 2315 I582 60 26 - - 10 0 - 120 100 3/20 0245 1530 160 29 - - 8 0 - 91 100 0310 1518 Downhole pump shut down 0400 1819 Restarted pump with reversed polarity 0815 1604 75 33 - - 6 0 1215 1590 62 35 - - 6 0 1615 1585 55 32 - - 6 0 1808 2330 .1769 Restarted ESP with reversed polarity 3/21 0200 1508 Liquid to surface 0400 1451 20 24 - - 20 1 0800 1421 90 22 - - 20 29 1200 1445 115 28 - - 20 23 1600 1445 118 42 - - 14 25 2000 1402 78 34 - - 14 32 2400 1367 45 31 - - 14 33 3/22 0400 1385 53 31 - - 14 44 0755 1388 41 32 - - 14 40 0915 1620 Pump down, 0755 to 0915 1200 1429 10 37 - - 32 27 1600 1324 10 36 - - 24 31 2000 1322 15 33 - - 24 33 2400 1347 13 32 - - 24 33 3/23 0035 1322 Well shut in at 0035 at OMNI valve. 1660 Stopped ESP, shut in well at the surface 10 100 38 100 32 100 135 100 23 15 2 5 7 8 5 45 Oil to surface 40 7 14 18 15 11 3 10 3 9 5 13 5 13 (1) Bottom hole pressure is at gauge depth, 4391' MDRKB. SUMMARY OF RATE MEASUREMENTS FOR DST lB Sep Sep Choke Oi 1 Gas Water Date Time BHP(1) WHP WHT Press. Temp Size Rate Rate Rate BS&W (psia) (psiq) (~F) (psiq) (°.F) (64ths) {Bbls/D)(MSCF/D) (Bbls/.D). (%) Comments 5/3 2100 2200 2230 2400 1818 Start pump for DST lB first flow period 1764 10 34 - - 8 91 1758 720 33 8 0 1700 230 24 12 0 0 100 100% Diesel 0 - Pump down 2150 213 100 to 2205 5/4 0300 1643 41 25 - - 18 5 0600 1611 20 26 - 24 14 0900 1570 14 26 - - 30 26 1200 1541 17 26 - - 36 92 1500 1518 12 30 - - 44 139 1800 1499 12 33 - - 48 156 2100 1488 15 29 - - 64 179 2400 1468 14 26 - - 64 207 252 98 263 95 271 91 184 67 138 49 102 40 60 25 43 17 5/5 0300 1431 22 26 - - 64 207 0600 1397 28 34 21 131 64 239 0900 1392 33 30 20 142 48 302 1200 1382 56 32 20 147 28 258 1500 1378 80 31 21 136 24 252 1800 1376 130 35 20 136 20 251 2100 1373 132 31 20 135 20 237 2115 1373 2126 1421 - 60 22 55 50 17 F1 ow to sep. 70 21 7 75 8 3 72 15 6 69 5 2 71 17 7 Shut in downhole pump Closed OMNI valve, end of DST lB first flow period, DST lB buildup conducted SUMMARY OF RATE MEASUREMENTS FOR DST lB (cont'd) Sep Sep Choke Oi 1 Gas Water Date Time BHP(1) WHP WHT Press. Temp Size Rate Rate Rate BS&W (Psia) (Psiq) (°F) (psiq) (°F) (64ths) (Bbls/D) (MSCF/D)(Bbls/D), (%) Comments 5/8 0050 1766 Start ESP for DST lB second flow period 0115' 1766 Tubing and tree frozen, turn pump off and thaw 0500 1754 Restart ESP 0600 1750 21 38 - - 16 0 0900 1574 81 29 - - 16 19 1200 1461 44 33 - - 32 139 1600 1397 26 33 - - 48 236 2000 1344 44 33 - - 32 250 2400 1263 52 32 - - 32 294 98 100 BS&W is 9.2 ppg 314 94 brine 204 59 79 25 83 25 98 25 5/9 0400 1222 64 33 22 - 34 371 105 0800 1187 60 35 22 140 34 373 116 1200 1160 64 42 22 140 34 400 118 1600 1129 61 42 23 124 34 400 134 2000 1114 66 38 23 110 34 390 130 2400 1090 65 35 23 114 34 394 136 5/10 0400 1061 1000 1037 1020 1035 66 35 25 113 34 394 141 66 39 25 113 34 400 145 Shut down ESP, end of DST lB second flow period 44 30 27 7 28 7 2 0.5 5 1 5 1 5 1 3 O.7 (1) Bottom hole pressure is at gauge depth, 4414~ MDRKB. ORIGINAL CONOCO, INC. 'WELL: G-4 FIELD: MILNE POINT SIDEWALL CORE ANALYSIS OCTOBER 1989 FILE 13;299 RECEIVED OCT 2 ~ 1~9 "~,laska OJJ & Gas Cons. CommissiQO /Inchorage 12051 RIVERA RD. * SANTA FE SPRINGS, CA 90670-2289 TELEPHONE (213) 698-0081 * PANAFAX (213) 693-0947 October 4, 1989 Mr. Michael Zotzky Conoco, Inc. 3201 C Street, Suite 200 Anchorage, AK 99 § 03 Dear Mr. Zotzky: Re: Core Analysis File No.: 13299 EnclOsed is a final core analysis report for sidewall core analysis test performed on material from Point Milne G-4 well, north slope Alaska. Laboratory procedures have been included for your reference. We appreciate this opportunity to be of service and trust these data prove beneficial to the development of this reservoir. Sincerely, Petroleum Testing Service, Inc. Peter T. Schuyler President PTS:rdl Encl. Client: Conoco, Inc. Well: G-4 Field: Milne Point File: 13299 Date: Oct. 4, 1989 SIDEWALL CORE ANALYSIS 1. Trim sample to right cylinder. 2. Package with pre-weighed aluminum, teflon tape, and fit with 200 mesh stainless steel end screens. 3. Seat package to sample in a Hassler-type sleeve using 275 psi as confining stress. 4. Extract water and hydrocarbons from sample using Dean-Stark toluene method. Record produced water volumes. 5. Vacuum dry at 150°F until stable and weigh to 0.01g. . Cool sample'in dessicator to room temperature and measure sand grain volume using a Boyle's Law helium porosimeter. Calculate sand grain density. 7. Mount sample in Hassler-Type sleeve using a confining stress of 275 psi. 8. Measure pore volume using a Boyle's Law helium porosimeter, determine porosity and fluid saturations. 9. Measure permeability with nitrgen gas using a calibrated flow tube-type permeameter. COMpANy CONOCO, INC. CORE TYPE SIDEWALL S/U4PLES IqUD TYPE WATER BASE flEL ! UIq A I R Ol L WATER TOTAL DEPTH POROS I TY PERHEAB I L I TY O/g SATN SATN SATN ft . PERCENT md. RAT IO XPV ~PV XPV 4315.9 34.6 289. O.&5 27.8 61.9 89.7 4345.9 29.8 17. 0.01 0.8 97.2 98.0 4356.0 25.6 1.2 0.00 0.0 98.7 98.7 4375.0 INSUFFICIENT IMTERIAL 4376.1 36.8 1020. 0.53 31.8 60.3 92.1 4398.8 37.3 178. 0.2T 17.9 65.3 83.2 448Z.0 25.1 13. 0.03 2.T 85.6 88.3 4493.0 33.5 56. 0.35 22.0 63.3 85.3 4504.0 35.9 87. 0.20 14.1 69.2 83.3 4505.9 38.6 137. 0.18 11.4 61.9 73.3 4506.9 INSUFFICIENT HATERIAL 4507.9 36.8 71 . 0.15 11.2 74.2 4557.9 36.5 52. 0.34 21.3 6~.8 4560.0 35.4 61 . 0.25 17.3 68.2 4567.7 INSUFFICIENT HATERIAL 4568.2 INSUFFICIENT NATERIAL PETROLEUM TESTING SERVICE, INC. SIDEWALL CORE ANALYSIS APPARENT SAND GRAIN DENSITY gm/cc 2.61 2.69 WELL G-4 FIELD NILNE POINT C(XJNTY STATE ALASKA Page No. Fite No. Date 1 7OO68 Octet 4, 1989 2.62 RECOVERED INCHES LITHOLOGY Sat; bm, fg, fr odor, dk arm, dt g[~ fluor Sst; grysh tN'n, vfg, airy, fnt odor, mstn, dt Bid fluor Sst; gr¥, vfg, stt¥, n odor, n stn, n fluor 2.6~ 2.6]' 2.66 2.65 2.65 Sst; bm, f-mB, fr odor, dk stn, d[ Bid fluor 85.4 2.6]' 84.1 2.69 85.5 2.69 Sat; Qry~h bm, fg, fr odor, dk atn, dt Bid ftuor Sat; Qry1h brn, vfg, arty, fnt odor, matn, dt Bid fluor Sst; grysh bm, vfg, fr odor, dk atn, dt Bid fluor Sat; grysh bm, vfg, arty, fr odor, ctk atn, dt Bid ftuor Sst; grysh bm, vfg, arty, fnt odor, dk atn, dt Bid ftuor Sat; grlmh bm, vfg, airy, fnt odor, dk atn, dt Bid fluor Sat; grysh bm, vfg, miry, fr odor, dk stn, di Bid fluor Sat; grysh bm, vfg, arty, fr odor, dk atn, di Bid fluor PETROLEUM TESTING SEf~VICE, INC. COHPANY CONOCO, INC. NELL G-4 CORE TYPE SIDEWALL SAMPLES FIELD MILNE POINT HUD TYPE WATER BASE COUNTY STATE ALASKA Page No. 2 Fire No. 7006~. Date October 12, 1989 SIDEWALL CORE ANALYSIS APPARENT HELIUM AIR OIL WATER TOTAL SAND GRAIN DEPTH POROSITY PERMEABILITY O/W SATN SATN SATN DENSITY ft. PERCENT md. RATIO ~PV ~&PV ~PV gm/cc .....o. ...oo... ..o...o..... ....o .... ..... ... ........ .... RECOVERED INCHES LITHOLOGY TYPE OF EXTRACTION - DEAN STARK TOLUENE EXTRACTION CONFINING PRESSURE ON THE PERMEAMETER = 275 pSi OIL GRAVITY SUPPLIED BY CUSTOHER = 16 A.P.Io These results must be used ~ith caution. Side~a[[ samples are obtained by impact coring. This method can fracture hard formations, thereby possibly increasing the porosity and permeability. In soft formations, impact coring can compact the samples, resutting in decreased porosity and permeability. Drilling mud may penetrate fractures and soft formations, thereby affecting the porosity, permeability, ftuid saturation, grain density and cation exchange capacity results. DRILLIN~ HISTORY Kuparuk River - SOS - North Slope Borough, Alaska W. I. 1.000000% Milne Point G No. 4 (SOS REW) Confidential AFE 10-61-1206 Location: 3466' FNL, 3370'FEL, Sec. 27, T13N, R10E, Umiat Meridian Location: Bottomhole, 1681' FNL, 3310' FEL, SEC. 27, T13N, R10E Objective: 4,915' MD- Shallow Oil Sand 09-05-89: MI rig. NU divertor and function test. PU BHA. Drld f/ 100' to 225'. Accepted rig @ 1130 hrs. 9/5/89. Mud wt. 8.7 Viscosity 110 Cum. Mud Cost: $3044 Parker 141 (0-1-0) Drilling Foreman: Brady 09-06-89: Drilled from 225' to 1113'. MWD failure, POOH, change MWD, RIH. Drilled from 1113' to 1571'. MWD SURVEY DEPTH Angle 532' 1.8 806' 5.7 1200' 13.8 1506' 25.2 Mud wt. 9.1 Viscosity 71 Parker 141 (0-2-0) DIRECTION N76.2E N21.6E N9.4E N1.4E Cum. Mud Cost: $6639 Drilling Foreman: Fox 09-07-89: Drld 1571' to 2007'. Short trip 10 stands. Drld 2007' to 2700'. CirC bottoms up. Wiper trip to 270'. Circ and condition hole. POOH and LD BHA. RU and run 47 jts and 9 5/8" 47# L-80 btrc and 20 jts of 9 5/8" 36# K-55 btrc casing. Shoe at 2674' and float Collar @ 2591'. Now circ casing MWD SURVEY DEPTH. Angle 1910' 28.7 2536' 27.6 2635' 27.7 Mud wt. 9.6 Viscosity 64 Parker 141 (0-3-0) DIRECTION N0.7E N0.9E N0.6E Cum. Mud Cost: $8060 Drillinq Foreman: Fox 09-08-89: Circ csg. Pump 38 bbls. of 10 ppg Sepiolite spacer followed by 189 bbls of 12.3 ppg Permafrost "E" w/ 5#/sk gilsonite and 112 bbls 15.8 ppg Class "G" w/ 1% gel, 0.2% CFR-3 and 3% salt. Bumped plug to 1750 psig. ND divertor, NU BOP, now testing BOP. Mud wt. 8.6 Viscosity 29 Cum. Mud Cost: $10,955 Parker 141 (0-4-0) Drilling Foreman: Fox 09-09-89: Completed testing BOP's. PU BHAand RIH. Tagged cement @ 2580'. Tested csg to 1500 psig. Drilled cement and performed 11.0 ppg leakoff test. Drld from 2710' to 4159'. DEPTH ANGLE DIRECTION 2920 26.0 N1.9E 3362 26.6 N1.0E 3834 27.2 N0.4E 3929 26.6 N0.0E 4o24 25 3 NO 6W 4119 24.6 NO21E DRILLING HISTORY Kuparuk River - SOS - North Slope Borough, Alaska W. I. 1.000000% Milne Point G No. 4 (SOS REW) Confidential AFE 10-61-1206 Location: 3466' FNL, 3370'FEL, Sec. 27, T13N, R10E, Umiat Meridian Location: Bottomhole, 1681' FNL, 3310' FEL, SEC. 27, T13N, R10E Objective: 4,915' MD- Shallow Oil Sand Mud wt. 8.9 Viscosity 33 Parker 141 (0-5-0) AUTHORIZED COST: $935,000 Cum. Mud Cost: $17,767 Drilling Foreman: Fox COST TO DATE: $399,247 09-10-89: Drld 4159' to 4191'. Circ, POOH, change BHA, RIH to 4014'. Ream 4014' to 4191' for logs. Drld 4191' to 4950'. Circ. and condition hole. POOH to 9 5/8" shoe. Cut drlg line. DEPTH ANGLE 4327 22.0 4453 21.1 4839 20.3 Mud wt. 9.1 Viscosity 37 Parker 141 (0-6-0) AUTHORIZED COST: $935,000 DIRECTION N0.3E N1.5W N2.9W Cum. Mud Cost: $23,906 Drilling Foreman: Fox COST TO DATE: $448,284 09-11-89: RIH to 4950'. No fill. Circ and condition hole. POOH LD directional and logging tools. RU loggers, log DTTE, DTD, -CNTH & AMS from 4947' to 1500'. -Log BGT from 4948' to 2672'. WO sidewall core guns. RIH and shoot 24 SWC'S. Recovered 20 cores. RD wireline. MU BHA. Mud wt. 9.2 Viscosity 35 Cum. Mud Cost: $27,293 Parker 141 (0-7-0) Drilling Foreman: Fox AUTHORIZED COST: $935,000 COST TO DATE: $527,248 09-10-89: Drld 4159' to 4191'. Circ, POOH, change BHA, RIH to 4014'. Ream 4014' to 4191' for logs. Drld 4191' to 4950'. Circ. and condition hole. POOH to 9 5/8" shoe. Cut drlg line. DEPTH ANGLE 4327 22.0 4453 21.1 4839 20.3 Mud wt. 9.1 Viscosity 37 Parker 141 (0-6-0) AUTHORIZED COST: $935,000 DIRECTION N0.3E N1.5W N2.9W Cum. Mud Cost: $23,906 Drilling Foreman: Fox COST TO DATE: $448,284 09-12-89: TIH, circulate and condition hole, short trip 10 stds., circ. and condition hole, POOH, lay down HWDP & DP. RIH w/126 jts. 29#/ft. 7" L-80 BTRC csg. Float shoe at 4928', float collar at 4849'. Pump 40 BBL 10.0 ppg Dual spacer, 51 BBLs. 15.6 ppg premium cement w/0.2% CFR 3, 0.4% Halad 344, & 0.01% Dicel-LWL. Displace w/150 BBLs 9.6 ppg NaC1 brine and 20 BBLs diesel. Bumped plug w/1500 psi. Brine wt. 9.6 Cum. Mud Cost: $27,293 Parker 141 (0-8-0) Drilling Foreman: Fox AUTHORIZED COST: $935,000 COST TO DATE: $614,275 DRILLING HISTORY Kuparuk River - SOS - North Slope Borough, Alaska W. I. 1.000000% Milne Point G No. 4 (SOS REW) Confidential AFE 10-61-1206 Location: 3466' FNL, 3370'FEL, Sec. 27, T13N, R10E, Umiat Meridian Location: Bottomhole, 1681' FNL, 3310' FEL, SEC. 27, T13N, R10E Objective: 4,915' MD- Shallow Oil Sand 09-13-89: Hold pressure 30 mins., floats holding. N/D BOPE preparing for release of Rig. Parker 141 (0-9-0) Drilling Foreman: Brady AUTHORIZED COST: $935,000 COST TO DATE: $731,129 09-14-89: Complete work for rig release. Rig Released at 0300 Hrs. Parker 141 (0-10-0) Drilling Foreman: Brady AUTHORIZED COST: $935,000 COST TO DATE: $724,396 09-15-89: Drop from Daily Drilling Report. DST ! Shallow 0il Sands OA and OB Sands 4480' to 4576' ND March ]3~ ]990 0315 Commence picking up TCP guns. 0830 BHA made up, RIH with 2-7/8" tubing. RIH. Fill tubing with diesel as I415 Pressure test after running 40 stands of tubing to 2000 psig. 1845 Pressure test after running 60 stands of tubing to 2000 psig. lgO0 Rig up wireline with (~R/CCL for correlation run. 2130 Correlated to open hole logs, POOH with wireline and space out. 2230 Set packer, RIH with (~R/CCL to confirm set on depth. March 14, 1990 0030 (~uns are on depth, attempt to pressure up on annulus to open LPR-N test valve. Problems with the pump. 0330 Pressure up on annulus to open LPR-N, RIH with GR/CCL to confirm ball valve open. POOH. 0430 Make up flow line to flow I~ead, pressure test to ]000 psig. 0500 Pressure tubing to 125 psig to create a 200 psi underbalance at the sandface for perforating. 0509 Drop bar to fire guns. 0512 (~uns fire, positive indication at surface. Start initial flow period. 05]4 Open at choke manifold on 6/64" adjustable choke. 0516 Increase choke to 10/64" adjustable. 05]g Close LPR-N valve to shut in well for initial buildup. Strap of tank indicates 0.8 bbls influx during initial flow period. 0815 Commence cycling OMNI valve into position 7 to start final flow period. 084] Open well at choke manifold to start the final flow period on a 6/64" adjustable choke. Well is flowing diesel. Rates monitored at tanks. 1630 Oil and diesel mixture reaches surface. Well is slugging oil and gas. 2000 API gravity of oil is 20.1 at 60 deg. F. 2100 Bypassed heater, continued flowing well to tanks. March 15~ 1990 0049 Actuated downhole annul ar samplers. 0150 Took ! bbl and 2 jerry can samples of dead oil. 0205 Cycled OMNI to position 9. 0315 Shut in well downhole for buildup, cycle OMNI to reversing position. 0330 Commence reversing out tubing to tanks. Maintain low pressure on annulus to minimize disturbance to buildup. March 16~ 1990 0815 Final buildup terminated. POOH with test tools. All shots on the TCP guns fired and were centered in the scallops. Three of the four HMR gauges functioned throughout the test. The fourth gauge stopped when the guns fired. All tools clean and functioning properly. After the DST tools were poulled out of the hole, Hallibu.~ton ran a GR/CCL log which tagged bottom at 4843~ RKB. This indicated that no sand fill took place during the DST. After unsetting the packer, the hole started taking fluid at the rate of about 9 bbls/hr. END OF DST 1 DST IA Shallow 0il Sands OA and OB Sands 4480' to 4576' MD March I7, ]990 Commence picking up the BHA for the electric submersible pump (ESP) test, DST lA. RIH with test string. March 18, 1990 Continue RIH with DST lA test string. March 19, 1990 0300 Nipple up wellhead. 0530 Start ESP at 30 Hz. Observe well behavior. 0544 Shut off pump and reverse polarity. 0548 Restart pump at 25 Hz. 0730 BHP is about ]670 psig, but no wellhead pressure. Steamed the wellhead. Apparently the tree iced up when the brine level reached it. Pressure increased at the choke manifold immediately when the wellhead was steamed and the ice plug melted. 0845 Flow reaches surface, ]O0%.brine. 1315 Traces of oil in production stream. 2315 Well still producing 100% brine. March 20, 1990 0310 The ESP shut down in underload. 0400 Restarted the ESP with reversed polarity. 0630 Start rigging up flow lines from wing valve on wellhead. 0700 Changed to 6/64" positive choke ]800 Well continuing to produce ]00%0 brine. 1808 Shut down ESP, connected flowline to wing valve to allow for rig move. Commenced rigging up to run HP gauge on electric line. 2100 RIH with CCL/HP/Temp gauge to 4100' MD (3794' TVD) to compare with PHD on pump at 4376.5' MD (4047' TVD). 2200 Pressure at HP gauge hung at 4]00' MD : 1655 psia Pressure at PHD on pump at 4376.5' MD = ]760 psia Assuming a 9.1 ppg gradient (density of produced brine), the static gradient correction is 120 psi between the HP gauge and the PHD. The HP pressure corrected to PHD depth = 1774 psia. The PHD was adjusted to match this pressure. 2230 POOH with HP gauge. Rig down E-line and lubricator. 2300 Pressure test flowline to 3000 psig against wing valve. 2330 Re-start ESP. March 21, 1990 0200 Liquids to surface. 0330 Producing brine with about 1% oil 0530 Water cut is 20%, oil gravity is 20 degrees API. 2000 BS&W decreasing to 10 to 15%. March 22~ 1990 0755 Generator for submersible pump unit shut down due to low oil pressure. Generator was low on oil. 0915 Restart generator, restart pump. Bring well on as slowly as possible. 1400 Set pump for 1350 psi flowi, ng bottomhole pressure. 2330 Line up to pump to annulus to function test tools. March 23, 1990 0020 Pressure up to 3000 psig on annulus to actuate annular samplers. Bleed annulus pressure down to 0 psig. Pressure up to 1500 psig on annulus and bleed off to 0 psig 5 times to cycle OMNI valve into the blank position. 0035 OMNI valve goes into blank position, start of DST lA buildup. Continue pressuring up annulus to 1500 psig and bleeding off pressure to 0 psig to cycle OMNI valve into reversing position. 0100 Reverse tubing contents out to the strap tanks. Total of 30 bbls reversed. Returns were clean brine at the end of the re-verse out. Maintain minimal annulus pressures while reversing. 0145 Blow down flow lines with air. March 24~ 1990 Continue DST lA buildup. DST lB (Post-Frac Treatment Test} Shallow Oil Sands OA and OB Sands 4480' to 4576' MD May 2, 1990 Commence picking up DST lB test string. May 3, 1990 0300 Land tubing in wellhead. nipple. Rig up slickline and set plug in 'X' 0700 Set packer and test to 1700 psi. Tubing hanger leaking. 0930 RIH with slickline and retrieve plug. Rig down slickline. ]100 Cycle Omni valve to closed position, install back-pressure valve. ]130 Nipple down BOPs. 1530 Replace tubing hanger seals, nipple up tree and pressure test to 5000 ps i g. 1800 Cycle Omni valve to test position, line up ESP and test flowlines. 2030 Start ESP at 40 Hz. 2150 Shut down pump, reversed ro. tation. 2205 Re-started pump, tubing pressure increases immediately. 2330 Well flowing 100% brine and diesel. May 4, 1990 1400 Continuing to flow test well, BS&W is down to 50%. May 5, 1990 1500 Continuing to flow test well, BS&W is down to 8%. 2115 Stopped ESP. 21~7 Pressured up on annulus to take downhole samples. 2126 Shut in well downhole at the OMNI valve. DST lB buildup underway. 2127 Commence reverse out, reverse 35 bbls. May 6, 1990 Continue DST lB buildup. March 25, 1990 0320 End of DST lA buildup. Reverse out test string, unset packer, and POOH with test tools. All three of the HMR gauges functioned throughout the test. All tools functioned properly and were clean when recovered. The annular samplers recovered water. After the test string was pulled out of the hole, tubing was run in the hole to tag bottom. The tubing tagged bottom at about 4850t MD, indicating that no sand entered the wellbore during the test. END OF DST lA May 11, 1990 0100 Start trying to kill well. 1730 Well dead, set back-pressure valve and nipple down tree. 1800 Nipple up BOPs., commence POOH with test string. When tools were laid down, both annular samplers were found to be full. After a bubble point check, both samples were transferred to cylinders for shipment to RFL in Houston. Two gauges recorded data throughout the test. END OF DST lB 2200 Nipple down tree. 2230 Nipple up BOPs. May 7,1990 0130 Pull back-pressure valve. 0200 Test BOPs to 200 and 500 psig. 0500 Pull 2-way check valve. 0530 End DST lB buildup, cycle OMNI valve to test position. Well flowing. Cycle OMNI to reverse position, fill tubing and casing with brine, cycle OMNI to test position. Well dead. 0930 Pick up to unseat packer, RIH and lock down tubing hanger, set back- pressure valve. 1100 Nipple down BOPs. 1330 Nipple up tree, pull 2-way check valve. 2000 Release rig. Work on generator for ESP. May 8, 1990 0050 Start ESP. 0115 No flow, tubing and tree frozen. Shut down pump. 0200 Pump hot diesel down annulus to thaw tubing. Thaw tree with Tioga heater. 0500 Restart pump. 0600 Brine reaches surface. 1300 BS&W: 25%. May 9, 1990 0100 Flow well to test separator. 1300 BS&W = 2.5%. May 10~ 1990 1020 Shut down ESP. 1200 Blew down lines, dumped separator to tanks. 1300 Move in rig, rig accepted at 2200 hours. rodUcti-:-:.~-- .... .,? :..-.::-mo -nTe-s.,--:. '-::"-.-:,~$'eting:...:: rVi-''ces CONOCO, INC. 3201 "C" STREET, SUITE 200 ANCHORAGE, ALASKA 99503 WELL G - 4 MILNE POIN? NORTH SLOPE RECEIVED JAN 1 9 199,~ AJaaka 011 & Gas Cons. Comm~n Anchorage 3200 SEWARD HIGHWAY ANCHORAGE, ALASKA 99503 907-258-2022 roductionTesting Se .rVices TEST SUMMARY COMPANY · WELL NO. TEST NO. : G-4 : I LOCATION :MILNE POINT, PRUDHO~ BAY; ALASKA ZONE NO. : 0 SAND TUBING : PACKER TYPE : TOTAL DEPTH : TOTAL FLOW TIME : AVERAGE Q GAS : AVERAGE Q OIL : ., TOTAL PROD. OIL : OIL GRAVITY : 2 7/8 CASING SIZE : PACKER DEPTH : CUSHION COMP. : TUBING CUSHION FT. : PERF INTERVAl: · AVERAGE H20 : AVERAGE WELLHEAD PSI : AVERAGE GOR : INITIAL WELLHEAD PSI : AVERAGE GLR : SHUT-IN WELLHEAD PSI : TOTAL PROD. GAS : TOTAL PROD. H20 : GAS GRAVITY : CHLORIDE : TOTAL PROD. LIQ. : FLOw RATE FROM: 0830 (3/14) TOTAL TIME ~G AVERAGE F~.P. AVERAGE F;I'.T. r VERAGE O o,, l ~'vERAGE O GAS AVERAGE O H20 AVERAGE GOR AVERAGE GLR AVERAGE BS&W OIL GRAVITY GAS GRAVITY CHLORIDE RH. % H2S % CO2 RESlTIVITY PRODUCED Q GAS PRODUCED Q OIL PRODUCED Q H20 TOTAL PROD. LIQ. : 19 ~1~.c: : .47 P,qI. : 48°P :. 67_ gBPl') : 20_4 APT : - : -- : : : : : : 53. 347BBL : : 53. 347BBL FLOW RATE ' 2 / ~ FROM: 0800 (3/19) , TO: 7~ (3/22) TOTAL TIME ~G : 79 AVERAGE Ei'.P. : 60.6 PSI AVERAGE F.T.T. : 3:3 o]2 AVERAGE O OIL : - AVERAGE Q GAS : AVERAGE Q H20 : AVERAGE GOR : - AVERAGE GLR : · - AVERAGE BS&W : 100% OIL GRAVITY : - OIL GRAVITY : -- CHLORIDE : P.H. : % H2S : -- % CO2 : RESITIVITY : PRODUCED Q GAS : PRODUCED Q OIL : . 189.7BBL PRODUCED Q H20 . TOTAL PROD. LIQ. : 189 _ 7RRT, COMMENTS: ~,T, CT.WAN U~ ~ STATIC BHP READINGS Naska 011 & Gas Cons. Commission roductionTesting Services TEST SUMMARY COMPANY · WELL NO. : C~ - 4 TEST NO. : 1 TUBING PACKER TYPE TOTAL DEPTH TOTAL FLOW TIME AVERAGE Q GAS AVERAGE Q OIL TOTAL PROD. OIL OIL GRAVITY : 2 7/8 FLOW RATE I FROM:2100 (5/3) TO:~ZI00 (5/5) TOTAL TIME AVERAGE F.T.P. AVERAGE F.T.T. %VERAGE Q OIL ERAGE O GAS. ERAGE Q H20 AVERAGE GOR AVERAGE GLR AVERAGE BS&W OIL GRAVITY GAS GRAVITY CHLORIDE RH. % H2S % CO2 RESITIVITY PRODUCED Q GAS PRODUCED Q OIL PRODUCED Q H20 TOTAL PROD. LIQ. : 47 HRS : 46 PSI : 27°F : 163.4. : 69_ 3 MC~"D : 104.2 BPD : .1 52- 9 : 254.1 : 39% : 19.9 API : 0.766 : 59,000 PPM : 7 : 0 · 1 500 PPM - : 48.9 MCF : 319.9 BBL : 203.9 BBL : 523.8 BBL LOCATION ZONENO. . O SAND CASING SIZE : CUSHION COMR : PERF INTERVAI~ : AVERAGE H20 : AVERAGE GOR : AVERAGE GLR : TOTAL PROD. GAS : GAS GRAVITY : TOTAL PROD. LIQ. : COMMENTS: MIIATE POINT, PRUDHOE BAY, AI2L%qfA : PACKER DEPTH : TUBING CUSHION FT. : AVERAGE WELLHEAD PSI INITIAL WELLHEAD PSI : SHUT-IN WELLHEAD PSI : TOTAL PROD. H20 CHLORIDE : FLOW RATE FROM: 0600 (5/8) TO: 1000 ¢5/10) TOTAL TIME : 52, AVERAGE FJ*.P. : 62 PSI AVERAGE FTET. : AVERAGE O OIL : 343.4 Bt:,D AVERAGE O GAS : AVERAGE Q H20 : 62.1 RPD AVERAGE GOR : 338, 6 AVERAGE GLR : · 320.5 AVERAGE BS&W : 1 OIL GRAVITY : 1 9.0 API GAS GRAVITY :, 0.97 CHLORIDE : 53,000 pPM P.H. : - % H2S : 0 ~co2 : 1400PPM RESlTIVITY : - PRODUCED O GAS : 1 79 MC-~ PRODUCED O OIL PRODUCED Q H20 TOTAL PROD. LIQ. : 701.4 BBL : 134.5 BBL : 835.9 BBL jar{ ,I 9 1,99"5- Alaska 0il 8, Gas Cons. ¢o o¢o oductionTesting Services FIELD READINGS DATE 3-14-90 - ~ ~ 1 WEI.LNEAD HEATER OIL OR CONDENSATE IIETERII~ H,0 METERING OIL TEMP CHANGE OIL CUMULATN[ CHANGE WATER CUMULATIVE ..... ~' -- 4 CLOCK CASING CHOKE TEMP PRESS CHOKE TEMP H~S CO; ~ALINII'Y PH VESSEL OIL OIL MEAS. OIL GRAVITY SHRINK,IGECORR IN OIL FLOW TOTAL H;O IN H~O FLOW TOTAL TIM~ PRESS SIZE SIZE TEMF COUNTER GRAVITY TEMP BS & W ~ 60 -c FN3DR FACTOR COUNTER RATE 0Il. B8: COUNTER COUNTER RATE WATER BBL ]:JVFI'T ~ I~'IT~ ~ c.~ T.~ P~ C. Th T~ Oo C~ ~o eSW C,o~O sr,~ ~ oo ~o o. ~ Comments la, ion: 0 S and PSIG IN %¢ PSIG ~N ~F PPM ~ Bet APl 'F % APl % ~RAC 98L STB/D 88L SS,. 88L'D BBC ~ Et.al 0515 125PRES UP TUBING TO DROP BAR TO PERF. ~. METCALF 0509 _ DROP BAR . M. Joiner -, D. 0512GUNS FIRED 0514 6/640PEN WELL TO TANK mcemenl 9.2 FOR INITIAL FLOW ~CL 0516 10/6~iNCREASE CHOKE )rated Iht: tt 0518 lC)/~z 60 IR.: 0519 10/6Z. 50. 834 BLEED OFF ANNULAS .gSize: 3--~-8~i 0815 16 START C¥iCLR ~HNT %'AT,V~ ~ PRESS TO CLOSE OMNI i,,,,08!9! OPEN DOWN HOL~E TE~<T VA],VE VALVE vol.: 25 bb~ 0830i 230 ~ - ~ Eel:. 0840 ;250 0841 . ;250 OPEN CHOKE Ot~ 6/6z ..i ,?%: It 0845 188 INCREASE ¢~OZ<E 8/(4 .ill ~: ' i 025pLUG IN LINE-CLEAN OU~. leter1I1 ASS; UNIT BASIC FLOWING GAS SUPER. GASt t GAS CUMULATIVE SEP SEP OIL TOTAL LIQUID GAS WATER ' CLOCK PRESS ORs~E ORIFICE GAS MEAS. SEP CONY. ORIFICE TEMR GRAVITY COMPR EXPANS PRESS. FLOW TOTAL GAS. OIL GAS IN GAS- OIL GAS LIQUID OIL TIME 01F£ GRAVITY TEMP. PRESS. FACTOR FACTOR FAC~R FACTOR FACTOR FACTOR EXTENS. RATE GAS RATIO SOLUTION RATIO RATIO RATIO RATIO leter , , , }e: Pseo d t~ T(~ iPseoa Fu Fb FL/ R3 Fey Y ! '" ' .-hwPseoa' ' G~ GOR1 GOR2 GORT TGLR TLGR WOR PSIG IN ~NH,0 , , eF ' ~IA ODIM O01M ODIM ' O01M OD1M ODIM~ ' OD1M" MSCF/D , MMCF , SCI~/$TB SCF/STB SCF/STR 'SCF/BBL BBL/MMCF BBL/STB aete~ ,, & 3" Ru§_ 0 6 8 ..... i ,, .. '. ~ :Press , ' e Tank ~'~ ~leter -- [ , , ~fesS ...... Zon, Lease: Custo~ Shot/Ft: Rang ~e:_ ::tiff. ~tatic IBb'in: Tanks: ;tandard~itions GAS FLOW RATE CALCULATION LIQUID FLOW RATE CALCULATIONS F = Meter K =Voiume Corr. Fac'[or ReDuction FacIO~ ~c 1 4.73 PSIA PRESS BASE FACT TEMP BASE FACT [14.73'~ 460 + T~'~ ' '--~Oo ...~Oo (ASTM Des,gna, ton ~ 0¢ F PR -- 14.73 F T~ -- 460._+ OF Og = Fu Fb Fir Fg Fpv Y~/hw P sepa FU = .024 x \~1 x 520 ' / METEF11~Qo t. _:. F (1 - BSW)(1 - Shr 60) 1440 TANK · OD - K (1 - BSW~ 1440 O~L C~: i__i CO~O CO ~ ~ C . DductionTestin ervices FIELD READINGS DATE 3-14-90 .... ~ TEMP CHANGE ~L C~U~T~ CHANGE ~R CUMU~T~ ~ -- 4 CL~ ~ING C~E TEMP PRESS CH~E TEMP H~ CO~ ~LINI~ PH vE~EL ~L ~L ~E~. ~L GRaViTY SHRINKER C~R IN OIL FL~ ~JL H~O iN H~O FL~ ~AL TI~ P~SS ~E S~ TEMP COUNTER G~WTY TEMP BS & W _ ~;~T~ ~~ ~ C~ T~ ~ Ch Th ...... ~0 ~ ~ ~ __.: e~ ~ S~ K ~ ~ O. ~ Comments ~ Et.al 051S 125PR~S UP TUBING TO ..... DROP BAR TO PERF. ~. ~ 0509DROP BAR . ; ,: M. Joiner -,, D. 0512GUNS FIRED 0514 6/64 ~: , OPEN WELL TO TANK ~a~m 9.2 ~, FOR INITIAL FLOW ~: ~cT. 051 6 1 0/6~ INCREASE CHOKE omt~ Iht: ff , m.: 0518 10/6~ 60 ~ D~: .... in , 0519 1Q/6~ 50 ,, .834 BLEED OFF ANNULAS i~Size: 9 5/8~ 0815 16 START CYCLE CHNT ~'ALVE ~ , PRESS TO CLOSE OMNI 'D. RSize: 2.875i, 0819 OPEN DOWN HOIE TE~ T VA],VE VALVE ' ' ~,: 25 ~u 0830J 230 - - ~R¢: "0840 250 ' ' ' . , , OPEN cHoKE ON 6/6z ~.,~,: .0841 250 i ..j~) 0845 188 ~ iNCREASE, CHO~E 8/(4 ~,~ - , ~ '" ,, 5 B~RRE~ GAIN IN SEPA]:ATOR ~,~4 ~' 1 025 ........j ,m~~',, ~O-~q ,6-~,51 PLUG IN LINE-CLEAN OUQ ...... ~er 1" ' '~ ...... ~S. UN~ ~lC FLYING ~ SUER, G~ G~ CUMU~TIVE ~P SEP OIL T~AL LIQUID G~ WATER " CL~K PRE~ ~IFICE ORIFICE G~ ME~. SEP ~N~ ORIFICE ~MP GRA~ C~PR. EXPANS PRE~. FL~ ~AL ~-OIL G~ IN GAS- ~L G~ LIQUID OIL TIME SI~ O~F. G~VI~ TEMP. PRESS. F~R F~R FA~ F~ F~ F~ E~ENS. RA~ G~ RA~ SOLUTION RATIO RAT~ RATIO ~TIO ~eter ,, , ~ ,,, ~ d ~ ~ ~ Fu Fb ~ ~ F~ Y ] , -~oa ~ G~I GOR2 GORT ~LR TLGR WON ' PSIG IN ~N H~ , , · ~IA ODIM ODIM M~eg,, & 3" ~" ' ' ~ , , , .... Met~ ~, , · ; , , "R"~- 068 ' '~' " ' , , Pres~ aa ~ ~ " ~: - 50 ...... - .:~ ~ Pr~s .... ' ~ .... ,, ,, ~e: ........ 50,0 ,,, e Ta~ ~eter ' ' ,., RLL.L._ ,.p~ dAN 1 ) 1~ ~ .... Q 8 0 0 ~ ,, i ,, a~: B B~, ~ ...... -~ '- S: ~ ..... -- ~ ~~ ........................ T Fie Con, Meter Diff. Rang 3a ~le~er ~e:,., )iff. Pre~ IBUin: Tanks: tandard, s GAS FLOW RATE CALCULATION LIQUID FLOW RATE CALCULATIONS F = Meter K = Volume ~ . ( Corr. FacTor ReOuct~on Facto, sc 1 4 73 PSIA PRESS BASE FACT TEMP BASE FACT /14.73'~ 460 + T:;'~ AQo AQo 14.73 F~o a60 + OF Og = Fu Fb Ftf Fg Fpv y~/hw p sepa FU = .024 x \~../x (ASTM Des,gnat,on 60 0¢ Fp.-- .... -- .520 ' t METEF Qo ~. ~:~ F (1 - BSW)(1 - Shr 60) 1440 TANK 'Q,~ - . K (1 - BSW1 1440 O~L ..... :)ductionTesting Services { "~,GE 2 of 9 ~ATE 3-14-90 0~e,:_CONOCn TNC FIELD READINGS WELLHEAD HEATER OIL Off CONDENSATE METERING ~ H~) METERING · OiL TEM~ CHANG[ 0iL ~.UMUL&Te,/~ CIq&NGE WATER CUMULATIVE 4 CLOC~ c.C.~SING C~D~(E TEI~IP aRE[SS CHOKE TEMP M~.K CO.- ~ALINITY PH dESSEL OIL OIL ~;EAS J OIL GRAVITY S"~"~"(a'G[ CO~I:; ;N OIL I:LOW 'C".A. -:C .,~ I,.I.~ g'LOIN -"'"' TIME PRESS S~ZE SIZE TEMP COUNTER GRAVITY' TEMP ! BS & W ~, 50 I: =a~.~r. 3~. a..S. c~../'70~= COuNTEr= RATE COUN'rE~ RATE ::- :[~ :[::~::[~ ~ c,~ ~,~ ~,~ ch Th . Tse~ Oo Go ~o , BSW Go60 S~: , ~- =c 'a. 3, Comments ' 1025 R/Ra q~ n~ ~ 40.03 6.251 e*ETAL SW¼ ~ - I ·" ~. ~.. METCAT.P 1030 6/64 ~ np~ I CHANGR TO 200 PSI GAUC~. ,.. M. JO~ ........ _1032 ~/~a 100 OPEN · _. .. , j 0_40 _1 o41 8/~;a OPEN . INCREASE CHOKE TO 8/64 ~ated IRt: tl .... st.: :%045! 8/64 48 84 OPEN ti" 160,22 7,922 ,. ........ Dm: .....1100 8/64 52 60 OPENt~, 79.68 8.752 ~mze:9 5/8 i. , i!~ ..... , ,, , , ,,, ,, , , _ ~.eS~e:2~ 1115 8/64 69 64 OPEN 7q. RR 9.58 i ,~ ...... v~.: , 25 ..... ,,, ,, , ,,, ,,, , ,, ,, ~R~: ... = 11 3Q 8/64 70 74 OPEN ........ . 20.16 9.79 ROCK CHOKE-NOT PTZiC~ ~,0eFh: ..... " ' ..................... · , 1145 8/64 72 84 OPEN ...... 9.79 ........ ROCK CHOKE OK - NOT i................. ~ PT ~ ]C4~TNC. 1146 9 / 64, DPFN I ....... INCREASE CHOKE ........ , ,, CAS ~ETER~G ,, ; , , RAT"~ , eter 1" ,as UNIT BASIC FLOWING GAS SUPER GAS [ PRESS. CaAS CUMULATIVE S~P SEP OIL TCrr&. LIOUIQ GAS WATE, ... ...... CLOCK PRESS ORIFICE ORIFICE GAS MEAS. SEP CONV ORIFICE TEMP GRAVITY COMPR t[XPANS FLOW TOTAL GAS. OIL GAS IN GAS- OiL GAS LIQUID OIL TIME SIZE DIFF GRAWTY TEMP PRESS FAC'IOR FACTOR FACTOR FACTOR FACTOR .:ACTOR . EXTENS RArE GAS RATIO SOLUTION RATIO RATIO RATIO RAT<~ ~I~ ,, ., ,.., .. ,,, , . , I~IG ,, ,',,,IN ~N H~O o!= PSIA ....... ~DIM OOlM OOIM' O01M .... ODIM ' ODIU. i' ODI~ MSCFID M,MCr SCF/STB SCC.'$TB S~ S'R SCI~.aBL a~.:MMC~ ~eter 1" & 3" ~ , ............. i ~er , ,' ......... i .................... e:_ ..... ~ter . , i ,,,, ,,, ,, , , ,,, ,,, ,,,, ~reSS _ e: 0 - ,,50 ;:'~ 0 - 500 ......... ' ......... , ,, ,,, , ,,, ,,, , leter .... Run . ........ ..... ~1:__ , ,,, , ......... Press . .... ...... ~ ,,, I Jin: xlafflC4mditio~ GAS FLOW RATE CALCULATION LIOUID FLOW RATE CALCULATIONS Cor' F 3c :',3r ....... ~ PSIA PRESS~SEFA~ TEMPLE F~ [14.73~ (460 + Tsc~ ~0o F (1 - BSWI(I - Shr 60) 1440 TANK ' Oo: ~0o K [1 - BSW) 1440 O~L ~ASTM De~.gna,,on -- '"~ F -- ~ ' ~¢ Qg = Fu Fb Ftf Fg Fpv Y~/hw P sepa FU = .024 x ~/ x ' 520 / METER~: Qo = ~t mm ~-~,~ .............. D12~ Pe, .o,eum .... oductionTestin§ Services (: ( °' ~o~r: FIELDREADINGjS .... DATE 3-14-90 WELLHEAD NEJ,TER OIL OR CO#OENS~TE NETERING ..... H~) METERING OIL S,",~ d',~( ,~C~E ."EMP CHANGE OIL C.L~UULATIYE Cl.I A I%fl"/.~E WATER CUMULATIVE ~--4 CLOCK CA~tNG CHOKE TEMP PRESS CHO~E TEMP H2S COt SALINITY p~ vESSEL OIL OIL ~EAS. OIL GRAVtTY CORI~ iN OIL FLO~/ "~k. ~".,0 ,N ,4.-0 ¢'LO~, TUTAL " TIME PRESS SiZE Si/F TEMP COUNTER GRAvtTY rEM~ BS& W = 60 F ;~-"~ =AC'OR COuNTE~ RATE -'.'. "~8, COU%TE~ C~-,UN "E~ RATE ,~E= 88. 1200 9/64 66 ~2 OP]~ 20.1~ ~0.00 .~.r MS-TC. ALF 1215 9/64 69 42 OPEN 0 10.00 ROCK CHOKE, NOP PLUGGED · M. JOINER ·" 12~ 9/64 64 42 OPEN 40_ n~ 1 0- 417 .R_OCK CHOKE-NOT PLUGGR~ ). STRICKLANI ~wt:. , 1245 9/64 66 40 OPIC] 40.01 10,834 [.I~tCL9'2 1250 9/64 43 m.: ............... ~ ~51 1 ?./~14 OpFlxl INCRE~E ,CI-IOKE~ TURN 11.454 D.P. Size: 2.875 i, 13151 12/64 30 OPEN 206 ......,~ ~0.0 12.287 ' ~1 ~0 06 1:2-.496 1345 12/64 28 o?EN 206 ....... ~,,, . . ABS uNrr BASIC FLOWING GAS SUPER GAS . GA.~ CUMULATIVE SEP SEP OiL ~I~I'&L LIQUI~ GAS WATER I~et~t' 1 tl,. CLOCK PRESS ORIFICE ORIFICE GAS MEAS $EP CONV ORIFICE 1'EMP GRAVITY COMPR EX~ANS ' PRESS F:LOW 'R:)I'AL GAS-OIL GASIN GAS-OiL GAS LIQUID OIL TIME SIZE DIFF GRAVITY TEMP PRESS. FACTOR F~L"TOR F~.,CTOR FACTOR FACTOR I:ACTO~ EXI'EN$ RATE GAS RATIO SOLUTtON RATIO RATIO RATIO RATIO , , P~,IG " ' I~1 ,NH,~~ ' P~I~ ' , OD;M ODIM .... OOIM OOiM ' :,OOIM .... ,,.ODtM' ! ODIM ..... MSCF,'D MMCr: SCI:/STB SCC'S!'B , SCC!$'rR' SCF'/BBL BB~'MMC-' Ikleter ..... Press ........ ! ' ......... e 1'Ink _: ..... ..... ',Press ........ $ 2 ............ el .. · to~a~,, BL/in: ran~ m~damCo~ditions GAS FLOW RATE CALCULATION LIQUID FLOW RATE CALCULATIONS F -- Met~.,, Co~, ~:ac!'3~ ReCluCT,~,¢, F,)cto, ;C 14.73 PSIA PRESS BASE'ACT TEMP BASE FACT (14.73'~ (46~;0Tlc. '"Qo F ,, - BSW),t - Shr 60)1440 TANK'Qo= .AQo K (1 - BSVV)1440 OIL ',ASTM 60 o~ F.. - ~,7~ F~ -- 460. 0¢ Qg = Fu Fb Fzf Fg Fpv Y¥~hw P sepa FU = .024 x %,---~-~ / x METER · Qo -- At m,n .~! m,n ................ D1250 ,C oc ~- ~ WATEP ( oductionTesting Services { o, 9 INC. FIELD READINGS DATE 3-14-90 WELLHEAD HEATER O~L O~ CONDENSATE METERINCI H,O METERING OIL TEMP CHANGE OIL Cbl4~.AT~ ~".ANGE WATER CUMULATIV~ .~-G-4 CLOCK ~,~ING CHOKE TEMP PRESS CHOKE TEMP H2S CO.- SALINITY pM VESSEL OIL OIL MEAS OIL GRAVITY S~R'~,~.~ECORF3 IN Oil. FLOW '~'A. ":C~ .1~ ,~:~ FL0~' I'OTAL TIME PRESS SIZE SIZE TEMP COUNTER ,.GRAVITY ;EMP 85 & W c 60 c ~4~.-"0~' ¢ACTOR COUNTEla RATE ~:. SS. '.~0UN'ER COuN'rE~= RATE WA'ER BI). .~. c.~ T,~ ~.~ Ch ;~ Z~ Q~ G~ ~0 BSW [, Go~C S~ . . - Oc =o 5. 3. Comments PSIG ..... ~.N 3~ ~S~G, IN ~c P~ ~= BBc ~' r ~. ~p. := =aAC Bet. ~riNo 8B~ aB; BBL-D ~: ~ 1400 12/64 78 35 OP]~ 208 ¢ 12.496 .... O::X'~. ~ ~r.T. 't~-]RU :M- JO~ 1418 1"4/64 ~, ~E ~O~ SIZE ., D. :~T~.Z_~ 4/64 ~: , [1430 I 84 ~.. 74 OP~ 208 00:80 13.546 ~ 92 .......... ~: ~ ' 1445 14/64 64 68 OP~ 206 39.55 13.958 ..... , .. ~.: 1500 14/64 60 72 OP~ 208 .60-32 15.628 ...... , , ., 3-~Si~.~875 ~" 1530 14/64 '~0 60 OP~ 208 20.16 17.508 ~h: ~ , ..... ~-, ......... . ,~ 16!5 , 1.4/64 52 32 206 .~ 20.02.~ 21.675 ABS UN~ ~ FLYING ~ ~R G~ G~ CUMU~TIVE ~P SE~ O~L ~Ag g~ G~ WATER !I C~K PRE~ ORIF~E ~IF~E G~ M~. SEP CONV ORIF~E TE~ G~ C~ EXPANS PRESS FL~ ~AL ~.~L G~tN G~-O~g ~ L~UID OIL T~E ~ OIFF G~VI~ TEMP PRE~ F~ F~ ~ F~R F~R ~, E~ENS ~ G~ ~ ~OLuTION RATIC RAT~ RAT IO .......... j , ,,, , ...... ~er ............. ' , ,, .,. , .... r~.068 ............ t ..... .............. ~eter ~ ........ jA~ ~ 9 I~35 ........ ....... ~ , ..... anda~:lCond;,tionl OAS FLOW RATE CALCULATION LIOUID FLOW RATE CALCULATIONS F = Me,~, K = Vo,um" Cot, ~8C~'3r Re(JuC~,~,n F3cIo, ~.z~l~ wa PSIA PRESS ~.SE FACT TEMP~EFA~ / %/14.73//[460 + TN:~/ AGo F (1 - BSW)(1 - Shr 60) 1440 TANK ' Go = ago K (1 - BSa'V) 1440 O,t ~ ~c ~o ~473 F,o ~. 0¢ Q9 = Fu Fb Ftf Fg Fpv YN/hw P sepa FU = .024 x ~ P,c / x 5~- / METER · Qo - ~t m,n &t m~n W.~TEP ~(ASTMT..~ .... ~ De,,gnat,on (: .... tionTes.ting Services ( ...... (: °' INC. '~ FIELD READINGS DATE 3-1 4-90 WELLHEAO HEATER OIL OR CONOENsATE aE'"~?G H~ METERING G- 4 OIL TEMP CHANGE OIL C L,~ LF. AT f~ CHANGE WATER CUMUL.ATlVE ..... CLOCK C.,JLSINGCHOK~ TEMP PRESS CHOKE TEMP H~ CO: SALINII~ PH VESSel OIL OIL MEAS OIL GRAVITY S"='*'~ CORa IN OIL FLOW .-~-&. ~.-O IN H.~ i:LOW I~TAL TIME PRESS SIZE SIZE TEMP COUNTER GRAVITY TEMP BS & W ~ 60 'F r~..-'~,:~- ¢:~TOR COUNTER RATE 3'~..==.. COUNTER COUN'rER RATE WATER BE,. ..... Pt~ Cw~ Twfl ~ Ch Th TSeD O0 Ce TO,~ esw . ce60 S~,; K oc eo o." :~ Comments liOn O S,~I'D PSlG IN fl: PSIG IN ~: PPM ~' SBL APl F ,~ % APl :,: ,,, cRa. C; BBL STB-'O eel eel eBL~'o eRL 1630 14/64 58 36 206 80.01( 22.509 OIL SURFACE ,,,, ,,,,, -- , ,e, 1645 14/64 58 32 208 120.024 23.259 ~. JOI~ 1 648 ' 32 80.01 ~ 24. 093 ~ ~ .... 1649 18/64 IN~E C~OYJ~: ~eme~ 9 2 KCL · 1700 18/64 59 68 2Q6 ~_ 79-96~ 24. 926 aled Iht:__ 11 '" ' ....... :,: 1715 18/64 62 60 2.08 . . ..... 68.01~ , 25,635 ~ia in - , ..... as~ze: 9 5/8 in 1720 32/64 .... _ ........ INCRr~SE ._ ........ 160~ 03; "26.343 " e Size: ~ 1730 32'/.64 70 18 206 .:.. , ---- , , , ,, , ~e~: ...... 1745 32/64 62 24 208 , , 11 20.02~ 28.010 ' --i .... , · , Depth: . I1 ........ ,~' ...... 79'96~ 28.761 SWITCH TO TANK #1 ~: .. , 1800 32/64 64 40 208 .~ ..... ,, ,, ........ ,~ ,,, ,to, i815 32/64 42 42 206 .................... 80.01( 29,594 . .............. CAS ~_ESEmNG ............ RAtio ..... ABS UNCr BASIC FLOWING GAS SUPER G~,i GAS CUlaULAT~VE S~P SEP O~L TC~A',. LIOU~O GAS WATE~ CLOCK PRESS ORIFICE ORtl:ICE GAS ~EAS SEP CONY ORIFICE TEMP GRAVlTY COMPR EXP~;S PRESS FLOW TOTAL GAS - OIL GAS ~N GAS. OIL GAS LIQUID OIL TIME SIZE OIFF GRAVITY TEMP PRESS FACTOR FACTOR PACTOR CAC~OR FAC1OR FACI~R EX'TENS RATE GAS RATIO SOLUTION RATIO RATIO RATIO RATIO ~e~ ...... ~. esee e' Y~. T9 ~seOa f:u F~'" F~ r~ Fay Y .. ~.Pseoa G~ GOR~ GOR2' GOaT ~LR T LGR W0R , ~,~,1G .... m ~,,O ....... ' , e~ ,,P~iA OO~M ' 001'~ ' O0~ ' ' C~IM , OC~la 0{~,:i OC~I~ ~SCF~ UMCr, ' 5CrSTB.....SCr,ST6 SCF,S:e SCF.,'BSL ,,ee'~.uc~ am.s~e ,, ie~e~1 . & 3" ........... ,, ,, , i ........... , .......... ;et~ , , , ........... _ , , ..... iete~ ~T k'Tr.q SR ...... : ......... R""3.06_8 ........... ~ ............... _ ............. ::. 0 - 50 ............ ,, - ~e~ _ 500 . ' ............... )- ........ , .......... , ................ ~ Tank , Icier --' ......... ................. __ RUn ....................... '1 ......... ...... I'~S ,_ -- I Press , , , --.-,-- r ..... ~' ' ., Toni< ...... , -- .... ', 1 ._6.7_ _ ....... ~ 2 ...... .... .... ~, , , ,, FormaliOn Lease Re¢ Rep PTS Rep: Fluid: Shotq:L: ShotOia 'Cas~m Tub/QP De~t~ Ref: at De Oi! Meter Size: Oil Meter Rang Size: H~ Rang Gas Mete~ Type: Meter Run Size: 0i11. Pres Slat~ Rang Gas M Type: Size. StaPC Pn Ra~ ,ct: 8BU,n 5tan~ardCon(:litions GAS FLOW RATE CALCULATION LIQUID FLOW RATE CALCULATIONS F = Me,~,, K ,-- v,.,u ..... T,,c 60 oc Fpe _ 1473 FTB -- ,~60 - or Og = Fu Fb Ftf Fg Fpv Y\r~ww r, sepa FU = .024 x~ P,c / x> /---~-'~ ME'¥ER · Qo = "~'[';'~i;"~ F (1 - 8SW)(1 - Shr 601 1440 TANK · Oo --' , (' ( onTesting Services ( ..... · - (~AGE 6 of 9 ~e,:* ~ INC, FIELD READINGS ' 3-14-90 WELLHEAD"' N~AT~R 0#. O~ CONDE~TE ~E~: ......... H~ 6-4 o,~ ~ c,-~E ~ID ~[~ ~,,GE .,E. . CL~K ~ CH~E TEMP PRESS CH~E TEMP Hz5 CO: ~LINITM p H VES~L ~L ~L NE~ ~L GRAVITY S"='~E C~ IN OIL FL~ ~A. l.[~ ~~ ~ ~ c~ , ~ ~ c~ T~ T~o ~ ~ ~o" e~ ~ S~,. - Oc ~ ~ ~ Comments ~IG IN ~ P~IG ~N .~ ~ .... P~ ~ ~L APl C ~, AP~ c: cR~ 8BL ~T~0 8BL 8~. BBbO ~n: ~ 1830 32764 54 38 OP~ 208 79.968 30.428 ~. ~ 1845. R~/~a ~ ~0 OP~ 208 '" ' ~0.032 31.261 ., ~.,, ~O~ 1900 32/64: 52 35 0~ 208 ~0.032 31.678 ' D. ~T~.~I ~:~ ]915 32/64 38 oP~, 206 . 79.968 32.095 ~t 9.2 .............. 80.016 32.928 ~: K~ .~930 32/64 35 38 O~ 208 ..... ,,, ,,, · t.: 1945 32/64 28 33 O~ 204 79.968 33.761 ~a: ......... in . E ~ , ..' 2000 32/64 29 34 O~ 208 '~1/76o 20.1 80.016 34.595 ~e:_ 9. ~/~ ......... , , ,, ,, , , , j , 3.,~:2.~75 m-20~5.~ 3~"/6q 32 3~ oP~ 204 .. ~ ~ 7~.968 35.428 ,, , "', ......... , ,, ...... i , , h~: ....... 2030 .. 32/64 32 36 OP~ 208 ...... ~ 40.032 35.845 i ......... ~: ~ .......... ~ ....... ' .~o.a;.';h* 36 262 '~ ........ :,: ,20~5 ~2.[6q31 34 oP~ 2o0 ~....... 2100 32[64 30 32 OPm 200 _ '" 2i'~2 [. 20.3 40.'0'3~ ~6'.fi7~ ...... [ , , , ,, ,,,, .................. ~ ~0 ........ ' dm .... , ~' 1I1 ..... ASS UNIT ~IC gLUING ~ ~PER G~ ' ~ CUMU~TI~ ~P SEP OIL ~AL L~ID G~ WATER . ....... CL~K ~E~ ORIF~E ORIFICE ~ ME~ ~P C~V ~IF~E ~MP GRAVI~ C~ EXPOS ~ESS FL~ ~AL ~- ~L G~ IN G~. OIL ~ L~UID OIL TIME SI~ ~FF G~VI~ TEMP PRESS F~R ;~OR F~ F~ F~R ~p E~ENS ~ G~ ~T~ S~UT~ RATIO RATIO RATIO ~[ , ,, ,,,,, ........ , ..... ,, ,, , , ' , .................... ..... ~ ~al GOR2 GORT ~LR T~,; . ,, P~ .... ~, ,~ ~ ~; , ,, "s~*,, oo~ oo~ , 0D~G ~ ~ ,, o~ ,~0~ ~F~ ~'c~ .... ~;~ sc;,s=e sc;.s~ S?eec' eeu~; eeL. S~e ...... aae;l" & 3" .,, , ................. ; ............ ~ , .... ~ , , , , , ,,,,, , ~ , .... , , ........ ~: .... . ............. ] ' ., ~ ...... ~ter ~T~ ~ ................. ~ ....................~ .... .... mu, 3.068 . .... ~ , , , ~ , , ~ , ,,,, , , .... , ,, , ~ 0 ...... e:. . ,.50 .. ~ .... :~ ............... , ............ ~ ... ..... . ........ 0 500 e: r , , ,, ................ ~, . , t ,,., ..... 4eter ........... , ,. ....... ~: .... ~ ~ -- . . .. , ...... ~ ,, ,. A~u~ 0tl ~ Gas C~s. cc nmission .... - ~ho[a~ ............... w- . ................. ........ ~: 800 ..~ , ,, ~ ,, ~ ~' , ,,, ~: 4.67 ..... ~ ,, ~ ~,, ,, , , ,, ,, .... ,,, , ,,, , , = aMe L tL/in: anda~Cenditiom GAS FLOW RATE CALCULATION LIQUID FLOW RATE CALCULATIONS F = ~e,e, K = vo,u .... : (t~;C)) Co,, I:: ac ~ ...:, ,' Reaucl .... Fac,o, : , 14.73 PSIA PRESS~EFA~ TEMP~EFACT [14.73~ 46 Tsc ~Oo ~Oo iASTM Oeo,gnat,on 60 ...... 0~ F~.- ,,;3 F~.- ~.0.: Qg= Fu Fb Ftf Fg Fpv Yv~Psepa FU= .024 x ~ Pst /x METER · Qo ....... &t m,n F (1 - BSW)(1 -- Shr 60~ 1440 TANK 'Qo = &t mm K (~ - BSW) 1440 O~L ~' ~ ~ W~TEP ....... Mea~ ( C oductionTest;ing Services (r. : o. 9 omen. ~ :~C. -' FIELD READINCS OATE 3-1 4-90 I OIL ?EMP CHANGE O~L CUM;jLAT.~ CHANGE ~T~R CUMULATIVE G--4 , CLOCK C.A~ING CHOKE TEMP PRESS CHOKE TEMp H2S CO7 SALINITY PH VESSEL OIL OIL M'-_AS OIL GRAv:TY c~"~:~"~ ~Ec. ORR ~N OIL FLOW ~-~' T,.E PRI:SS S,ZE SIZE TEMP COUNTER GRAV, TY T~MP , BS.W .. = =~---ua =~CTOR COUNTE~ RATE __ PO~ ~h' c.~ ~,~ ~,~. ca T~ T~-~ Qo' Go ' ~o I esw Goeo ~.~. ~ oc =o ~ ~. Comments -IL2: 115 32/64 29 35 206 .~ 40.032 37. 096 ~e,'. ME-SF_ALF 2130 32/64 30 38 208 .... 40.032 37.513 M. JOINER 2145 32/64 31 34 208 40.032 37.930 D. " 2200 32264 33 33 208 " 20.1 120. 3 .180 " , . ,. ,, , ~ .... ~, , ,,. ~ 9'2 2215 32~t64 36 33 208 7~.89 40.012 " .,, ,,,, , ,, ., ,,, R.: .... 2230 32/64 ,40 30 20~ ......... ~, 80.04 40.846 I" 87rlTOt 2'0 ½ HOUR READING.~ ..~ ,,. ...... ,,,,, , ,,, , , .,,,, ,, ,,,, , ,,,,, ~.~.s~: ~ ~300 32/64 4~,, 36 208 , .......... ~.: 25 ~: ...2315 .... 32/64 40 32 296 .. ~ . . - -- , ..... ,~: . ...... , ~330 32/64 40 31 208 40.02 42.513 ' "' q .... ~ ....................... ,., .,,,, , ,, , ,, , ,,,., ,,, ,,.,, ,, , ,,, mr 1" .Bs UNff ~lC FLYING ~ ~R G~ ~ ~ CUMU~TIVE ~P SEP ~L ~&L L~UIO G~ WATER ....................... CL~K PRESS ORIFICE ORIFICE GAS ME~ ~P C~V ORIF~E ~MP GRA~ ~ EXPANS ' PRE~ F~ ~AL ~- ~L G~ IN G~- OIL G~ L~UID O~L T~E S~ DIFF G~VI~ TEMP PRESS. F~R F~R ~ F~ ~ F~R E~ENS ~ GAS RAT~ SOLUTION RATIO ~T~ RATIO ~T~O ~er .................... ~; ' ~0 ~ ~ ~Oa Fu Fb F~ ~ F~ v ~nw~a ~ ~1 ~ GOR2 ~ ..... , ........ ~ , , ............. , ..... SR ............. '~0 501~ '" ~, ...... ~ .... , , ........... , .......... ~ 0 ............ ~ ,,,, .......... t~er Run .................... ...... , ...... ..... ~- ,,, ,, .......... ,,, Pr~ ..................... ,, ,, ,,. ,, ,, ....... ~ ~. 800 ,,, , ........... ,,,,, , ,,,, ,. , ,., ....... t sing ~e: eter BL/in. rare: mm:la~lCom:litiom GAS FLOW RATE CALCULATION LIQUID FLOW RATE CALCULATIONS F (%0) ~ 1 4.73 PSIA PRESS ~E FAC TEMP ~SE FAC /34.7~/ T,¢ ¢0¢ AOo ~ASTM -- - .... _ ___ = y ~ ' FU = .024 x % P,c / x METER - Qo= ' F (1 - 8SW)(1 - Shr 60) 1440 TANK ' Qo - K (1 - BSWi 1440 OIL 60 0¢ F.~ = ~'~; F,e -- 460 . 0F Qg Fu Fb Ftf Fg Fpv %.hw P sepa . At m,n ~t [r :::)duct;ionmes:in9 Services °' ueomer: , FIELD READINGS DATE 3-14 X 1% - 9O OIL TEMP CHANGE O~L C,~M~ _4["yE CHANGE wATER CUMULAT~V~ ~4 CL~K ~NG C~E TEMP PRESS C~E TEMP H~ CO: ~LINI~ PH ~SSEL ~L ~L ME~ ~L GRAVI~ S~'k{~ CORR IN OIL CL~ T~- -;0 iN ~:C rL~ TiME a~SS SI~ SI~ TEMP C~TEa G~V~TV TEMP . BS & W ~ ~ c :~ tA~ C~UNTER RATE : - ~. C~"TEa COU~'ER RATE ~ATE : ~TT~ ~ ~ c~ ~. ~ , c. ~- T~ ~ ~ ~ e~ o~ ~' ' ~ ~ ~ ~ ~mments . ,,,, 2400 32/64~ 41 34 O~ 206 , B0.004: 44.180 ~. ~.~ 2415 32/64 42 32 OP~ 208 ,, ~. JO~ 2430 32/6~ 41 33 OP~ 208 :" 80.004~ 45.847 D. 2445 32/6~ 44 34 OP~ 208 ~ 9.2 '" '~ : g~ 0100 32/6~ 41 36 OP~ 208 80.004 , ,,,, ..... ,, ,, ~t.: 01 ~ 5 32/6~ 42 34 OP~ 206 " ..... ~: m ~ ..................... '"~t~ 0130 32/6~ 206 6":bo4 ~s~,: ~ ~ 2 - 5 , ~ ] ...... .,u ,, ,, ms~:.~2.875 ~ 0145 3216~ 42 ~0 OP~ 2~0 ........ : 1 - 55 ~1,1~ DR~ ,, , ,,,, , ,, , , , ,,, ~m~: ... 0200 32/6~ ...... 41 ' '38 ' OP~ 208 80.004.... 50.848 .... ~r ~h:. ~~' 0215 23/6~ 42 34 OP~ 208 ~: ,, , ~ ........................ ....... 0 ' '" ~2' ' ~2 O~ ,,i ,~] , , i ,,.,, , ~ ,,,, , , ,, , ~ 230 23/6~ 208 40.00 51 682 , ~ , , , , , , , , ,,, , , , , ~ 1 tl ~S UNff ~ FL~I~ ~ ~R ! ~ : ~ CUMU~TIVE ~P SEP 0'~ ~A~ L~ID G~ WATER ~ PRE~ ~IF~E ORIF~E G~ M~ SEP CO~ ~IFICE TEMP GRAVI~ ~PR EXPAN$ PRESS FL~ ~AL ~- ~L G~ tN G~- OIL ~ L~UID T~E S~E DIFF G~VI~ ~E~ PRE~ : F~ F~ F~ F~ F~I ~a: E~ENS ~ G~ ~T~ SOLutiON RAT~O RATIO RATIO ~e:~ter ~ ........ d hw ~ ~ 'F~ ' ,, , F~ , ~ ~ F~ y ~oa , ~ ~R' ' ,," GO~2 GO~T ~LR TLGP ~rl" & 3" ,, lemr ............................ e: ~r ........ ~~.q ~ ........... · ~n ....... ,,, , , ,, .,. . , , ...... "~ - 50 ~: ........... ' , , , , ,,e~~ 500 "' ' ..... ........ e:.,,,,,, ...... ~Ta~ , ~ ,,, .,. _ j . . ~_ .. Run ...... ..... ~' ,i , ,, , P~ ,, . .... , , ,, . ... , ,, ,, , , ....... -. , , luid: ;hot/Ft.: :)il Meter :rang ~e:, ~ang ~/~e: ~tatic Pre: ~er Run )~. P~ ~ Pm )BUm ;taf',dard Conditior~ GAS FLOW RATE CALCULATION LIQUID FLOW RATE CALCULATION: F = Me~_, K = vD o ..... ~: 14.73 PS'A PRESS~EFAC TEMPB~EFA~ (14.73~ ( 460 * T~ AGo AQo Co,' Fac~'3, Reduc, ..... Fac,o, ,~ 60 '--0¢ F~e __ ."~'3 FTB __ 4~.~- 0¢ Qg = Fu FD Ftf Fg Fpv YN/hw P sepa FU: .024 x ~ ~/ x ' 520 / METER · Qo ~ ~t m~n F (1 - BSW)(1 - Shr 60) 1440 TANK ' Qe ......... ~t m,n K (t - BSW~. 1440 W~TEpOIL ......... MedsDllASTM2~tdt~,~s)Pe~r°teumDe%'gna~'°n ( ::)ductionTest:ing Services ( .... tr' °' Cushier: ~... INC. FIELD READINGS DATE 3 - 1 5- 90 WELLHEAD H[ATE. R" OIL OR CONDENSATE METER1T ~ ME TERIN~ OIL TEMP CHANGE OIL CL~ULA-r't~ CHANGE WATER CUMULATIVE CLOCK CA~IflG CHOKE TEMP PRESS CHO~E TEMP H~S CO: SALtNITY PH VESSEL OIL OIL MEAS OIL GIa~VIT'~ S'= "'r'a~E CORR It~ OtL FLOW ~. '" .~' IlY H..O FLOW TOTAL TIME PRESS SiZE SIZE TEMP COUNTER GRAVIT~ iEMP BS & W ;: ~ F r&.--~.~. F&CTOR COuNTEI=I RATE ?..~=_. COU'~'En COUNTER RATE I. ~.4~.~~ P~, C-, T,~ P,., C, T, Tse~ Oo Go ~o ._ esw G~o S--. ~. oc ~ o,, ~, Comments PSIG IN o~: PSIG IN eF PPM q: 68L APl F o.. APt :: cRAC , . BBL ST~,T) BBC BBL BBL*~ ,a, io.' _O_SAi'ID__ 0300 32/'64, 40.00 43.347 . · ....... ~'~S. METC. g~ 0330 CI. DS[ ~ IN ~ : ~0.00 ' 53. ]47 ...... ~ · M. JOIRER ., Do , b-WRI~ ,,. ..... ~: ~ , , I~:e~m 9.2 ...... [ .... ......... ......... - , L ,, ~ ......... tFt.: ..'! ......... [:)ia,. ~m ......... ~s~ze: 9 -5/8!." ....... ~ - .... , ............. ,, ....... ,, .... '7 in ).P Size: ~- · ~ ~ _ ..........., voL: .... ~, , ,, _ , h Ref: ......................... ;er Depth: ........ 11 ........ / ................... '~, ..... Depth:_ ti .... · ................ ...... , , , . ...... , , . ..... , , ~ , ........... IretOr . , ........................... ................... ~s ~'~TE~!,~ ,,, ·leter 1 ' ~es. UNIT BASIC FLOWING GAS SUPER GAS GAS CUMULATIVE S~P SEP OIL TOT&L LIOUIO GAS CLOCK PRESS ORIFICE ORIF:~E GAS MEAS SEP CONV ORIFICE TEMP GRAVITY COMPR E X PAN.'S PRESS FLOW TOTAL GAS-OIL GAS~N GAS-O~L GAS LIOUID flUE SIZE OIF~: GI~VI TY TEMP PRE SS FACTOR FACTOR FACTOR FACTO~ FAC~ F~'TCI[I E XI'E NS RATE G ~ R ATto SOLU T ION R ATIO RATIO R AT ID aA' ~C leler .............. i,,, , ...................... '"' ............ h ' ..... ~etel" 3" ~eter ......................................... ~" ..... ~ , .................. , ........... Meter : i~~ Sa: , , l ................. ' .... ,~un 3 068 ..................... ~ ..... · o , ,,, : _ ;: ,, , , ,, Press ~: ..... 0 - 50 ...... , ................... ~ , ............... C P~ess ............. ~' , ....... i ..................... ~,: __0 - 500 ' " ~ ..................... , .... i ......... . ......... ~ Trunk · , , ,,,, : ........ i , , .... , ....... Meter · % ~ , ....... ~ ~Un .......................... ~ ...................... ,. , .... ~ ....... ~ ~!, , , . ...... Pm~ c Pm~ ......... ', ........ · ,. , ,,, , .... ,~ ~ i ............. k Tank .... ~ ................. ,, __I__.67 __ ' ............. ] KS 2 ' ' ......... ............ ~, , , ~, .............. Fmeld. Lease Custome FTS Rep: MudWt: 0isp Fluid: Shot/Ft.: Shol Dia. Casi~ Pil Scl 0il Meter Size: __ 0~t Ram S~ze: H~ Gas Ty~e: Meter R Size: Diff. Pr Ran< Stal~ Ran( Gas Meter Size: Dill., Rang Static P~ BBUm ~Tanks Stand.~lCond~lion~ OAS FLOW RATE CALCULATION LIQUID FLOW RATE CALCULATIONS F -- M~.,.~-, K = Vo,u ..... ~c ..... 14.~3PSIA PRESS BASE CAC,' TEMPB~EFACT ().~2,~ ¢'160 +T ~ ]Go F(1 BSW)(I- Sh, 60)1440 TANK'Go JOo K (1- ~S%%')1440 Olt. , ...........x x ~'-"/ ............. ..... ~ 60 or F~s_ ~4:3 FT. 460-'r Og=FuYhF~fFr~FpvY¥~Psepa FU=.O24x p.~/x ~FI~ER'Q": &~m,n &~m,n .... ~"- '.. ~ ~ .... ' W,~ oductionTesl:ing Services I ot 41 DATE 3-19-90 FIELD READINGS .~[vgT~ OIL TEl, IF CHANGE OIL. CUMULATIV~ CHANGE ~-_ ~R CUMU~T~ -4 CL~K ~ C~E ~MP PRESS C~E TEMP H~S CO~ ~INI~ PH ~S~L ~L ~L ~E~ ~ ~L GRAVIT~ ~E ~ ~N OIL ~ P~ S~E ~ TEMP ~TER G~ ~MP BS& w ~ ~ r r~ F~ COuNtER ~TE ~:L ' , ........ ~ C~ ~ ~ C~ Tn ~ ~ ~ ~ ,j B~ G~ S~: ~ ~ · ,, ~m: 0532 6/64 O~ O~ ~ ., ,,, ..... ~ 0609 6/64 55 O~ . R_ ~AT.~ _., M. ~. :0615 8/64 100 OP~ ,, ~T~A~ ........... ~ ...... ~ .0620 8/64 75 O~ ,, ,,, , , , ~ ~ 0630 8/64 114 O~ ]~ ~ S~PA~ ................ ,.,, ~.: ,, 0643 16/6~ ~ ~ ~~ ..... , ~: .... in .................... 0645 22/64 82 0~ ................ ~: __ , ~ i. ~...... o o0 o ..................... ............. ~.: .... 25 hR~: 0715 22/64 ' 0 ............... ......................... ~ ....... , ............. , 0745 22/64 0 ~S. ~G ...... ' ........ 1'656 ...... ~ , , , ,~,, ~ ,,, , ............... ~,~ , ..... ~ , ~11 A8S. UN~ ~IC FLYING ~ SUPER G~ ~ CUMU~TI~ ~P SEP OIL ~A~ L~ID G~ WATER ..... ~ p~ ~IF~E ~IF~ ~ ME~. SEP C~V ORIFICE ~MP G~ ~R EXPANS,' PRESS FL~ ~ ~-~L G~tN G~ .OIL ~ L~UIO OIL ~E SI~ ~P G~VI~ TE~ PRE~. F~ F~R F~ F~ ~ ~R [~E~ ~ G~ ~T~ SOLUTI~ RATIO RAT~ RATIO ~TlO ~r , ,~ ........ ~: ..... ~O, , d ~ ~ ~ Pu Pb Pti ~ F~ Y , ~ ~ , , , ~ Ih' ,NM~ , ~ ' ,,pS~ "hDIM, ' .... , , 0DIM ,,, ',',',ODIM "' ,, ~M' ' ,,'., ~M .... ~PlM ..... 0~M' U~Fe 'MMCr ~F~TB ~F}ST6 ~, , ,$~,Pj'ST~ ..... ~6L ~eb'M~r~ ' , aBL,~TB .... ~1" .......... , ........... , ,,,. ........ ,, ~ ............ ,,, , , , ,, . ~ .... ~: .......... ........... ~r ,- D~I~. ~, ................... ,, .... , rR~3. 068 ............. { ...... ......... _ ,,, ] ~ ,, , .... ~ro~0 50 :~- 500 ............... e: .............. . ............ , ,,, , , , ,, ........ , ,, ~ ~ ~ , ...... . ..... "'jA -I 9 ...... .......... , , ":~ ~ ~a UIi ~" ...... ' ' ....... ' ....... ,.._~r~: 800 -' ~: I . 667 - ' ....... _ ~: 2 : ' ~ '~ ...... , , , ,,,, , ,,, _ ~ ~ .... , ,,, ~1~2 ,, Tan,s: ;tandardCo~ition~ .. OAS FLOW RATE CALCULATION LIQUID FLOW RATE CALCULA"~IONS F = Me~e, K ~ Co~' Fac~.~ Reduct,~ F~fo, ~ ~ PSIA PRESS ~E FACT TEMP~EF~ [14.73~ 460 + T~ &Qo F (1 - BSW)(1 - Shr 60) 1440 TANK ' Oo - ~Qo K fl - BSW) 1440 OIL ,ASTM De~,gna,,on ~n ¢ ~._ 1473 ~.o_~-0¢ Og=FuFbFtfFgFpvYv/h~psepa FU="024x~/x 520 / f4ETER'Q°= ~'m,n ~lmin ............ · PAGE 2 of 41 co oo (' ction lesting Services ( FIELD READINGS - G-4 E~&L TEMP CHANGE OIL CUM U .AT.'VE ~A~ ~TER CUMU~TNE CL~ ~ C~E ~UP PRE~ CH~E ~MP H~ C~ ~INI~ PH ~L ~ ~L ME~ GR~ S~E C~ IN OIL FL~ T~ H~ IN .~ FL~ ,. ~ ~ S;~ ~ ~MP C~TER G~ ~MP W ~ ~ :C r~ ~ COUNTER RA~ ~'. ~5. COUNTER COuN~R RATE 080O 'i 14 ...... e: ...... .... 0820 ~ ~ T~ ~ ~t: 0830 9/64 12240.32 .420 1648 .... ~ ,, 0915 ~0/6~ 78 ,, ~ 235.2 7.03 ~625 ~r 1 ~ A8S UN~ ~ FL~G ~ ~R ~ ~ ~ CUMU~T~VE ~P SEPAL ~AL u~O G~ w~E~ _ P~IG IN ~N H~ ~ ,, , PSI'X ..... ODIM ' 'Q~IM OO~M ..... ~M ~M OOl,~/. ,' O~M M~F~, MMC~ ' ~F~TB SCFiSTB SCF~STR SCaB,Bt 8Bb~ "' ~B~S~ ~er .... , ..... ,-- ,. Mud Wt:. SI~R.: Casing Tub/D.P < H~) Ideter GasMe~ Diff. Pr Rang ,~abc Pn Gas Met~ Type: Diff. Static'P~ Sta~l.I, ~ GAS FLOW RATE CALCULATION LIQUID FLOW RATE CALCULATIONS F: Me.~, K - v,._. ....... 14 60 --' --' .... _ ...... [3t' - ,gnat _............... Fpe - ,,:3~e FTs - ~-,5~--' o¢ Q9 = Fu Fb Ftf F'9 Fpv Y%/hw P sepa FU = .024 x ~/x ~ MET:];R, ' Q'): &l m,n ' ~t msn WA ~ E P M .... T~' Tsc m roductionTesting, Services o, FIELD READINGS 3-19-90 Rang Gasl~ Type: ~:_ DifI. P. Stale BBUm: ~T~nks S~ncl~aCo~dioe., GAS FLOW RATE CALCULATION LIQUID FLOW RATE CALCULATIONS F = 4.73 PSlA PRE~EFA~ TEMP~EF~ /)4.7Q~ 460 * I,~ JO~ AGo (ASIM _ ,,7~ Y~. -- 4~ - ~F Qg = Fu Fb Ftf Fg Fpv Y%/hw P sepa FU = .024 x ~ Psc/ x -~20 / f4ETEit Q,~ ': ........ F (1 .- BSW)(1 . Shr 60) 1440 TANK - Qo = - K (1 - BSW) 1440 O~L I' O~L TEUP CHANGE OIL CL~U~CNE C~ANGE vd~TER C~T~E ;~- 4 ~T~ ~ C~KEs~ TEMP P~ C~E~ TEMP M~ C~ ~Nl~ pM ~L[E~ C~TER~ ~Ty~ ~TEMP B~Lw GRAVITY ~:~ ~ Ih "~' ~G ~ ~ P~ '~ ~c ~" 'S % a~: ....... n~R 10/64 70 O~ ~ 126.0: 10~83 1620 l: ~. ~ 1000 10/64 69 O~ ' m .... ' ..... 46 3: 11'25" 1620 ,,,, , ...... M. JO~ 1015 10/64 62 O~160.02 12.92 1622 D ..... ~~ m ......... , !.0/64 46 O~ 16~ 240.0[ 15'"'.42 1615 1030 M: , , .... ~~O. 1045 i0/64 ~8 O~~ ..... ~)~ ~ U~ _ ~ ~ ~~ L J m 160.3: 1?.09 1604 9.2 ........ ,,,, r~ I~:____~ ........... n.: 1100 10/64 36 46 OP~ 160 ...........[~.~, , ...... 159.5C 18~75" eo5 ~: in ....... ~-~- 1115 10/64 48 O~ 1' 200.6 20.84 1605 ~.: 7 · .... ~ ~ ....... ~.~a~: 2...7/Rm 1130 ..... ' 10/64 ' ' 40 O2~ 160 .......... ~?' .............. 39.5~ 21.25 1593 9.2 , ..... .~-~ . ~.: 25 ...... ~ ¢~, .. .,,, ,,.. ,, . . . ,.. ., ..... . ,~: _ 114S 10/64 46 OP~ ) 40'2( 21 67 1592 .............. ~ ........ ~'i %~ /6~ 94 38 OP~ 164 ......... !'? ........... 1 200 1 0 ~ 119.9 22.92 1592 _ ~ , ............ ,, ........... ,, ,, ,,,, ~ ~ ", .............. ~ ............... ~ ................ -~, ~- , , m ..... ~ ............. ~ ~i~ .... ~ ~: m ...... ~ ........... ~S UNIT ~C FL~I~ ~ ~ER ~ ' ~ ~ CUMU~Ti~ ~P SEP ~L ~&~ L~ G~ W~TER ~ C~K ~ ~IF~E ~¢~ ~ uE~ ~ C~V ~;~E TEUP ~TY ~en EXPANS :' PRESS FL~ frae S~E ~FF G~VITY TE~ P~ F~ F~R F~ F~ F~R F~ ; E~ENS R~ G~ ~ S~UT~ RAT~ RAT~ RATIO ~T~ ~ , ,,, , ~~ , , , , .......... ~: ......... ' ......................... ~], ' ..... r ............................ ......... , ........... ~Z~, SR. . ....... ~.~ .. . .... 3.068 ........ ',? .... , ,,, ~e. 0 - 50 ........................ ~ ' ............ ~; ....... .................... ..... ~ ....... ,,, , ,,, , .... L~0 - 500 ........... . - , ~ 'j t ,,,, , .... ,, , ..... , -, ~ . ,,, ,, ,, ~, ,~ ..... ~ , , ...... , , ,,~ ~ ............... . ,,,, ,i ,, l, ,,, ,,, .~. .,,, ~ '., .,. ., ~. ~ _ 66~ .............. ,....... ~ 2 ..... ~ ........... ....... , i i .i, ........ i .Z .... i ..... ca. co (' ( oduc ionTes ing SePv. ices (' ..... s °' :.s~,er: FIELD READINGS ..... ....~TE 3/19/90 'J.']~:~ ~ WELLH~AO HEJ.TER O4L OR C(:N, BOFJM~ATE .~ETERING '" .~.~m~ '' ~L TEMP C~A~E ~L C~AT~ ~ANGE wATE~ CUMU~TIVE ~ ~--4 CL~K ~ C~E TEMP PRESS CH~E TE~ ~S CO: ~INI~ PH ~S~L ~L ~L ME~ ~L GRAvIT~ ~R.N~ CO~ IN~L FL~ ~L ~:O ~a':O FL~ ~ TIME ~ 5~E SI~ TEMP C~TER G~TV ~MP BS & W .a ~ F F~ F~ COUNTER RATE ~. ~ COUNTEa C~NTER RATE wATER ~- ,,,, "~' 1445 16"/6,[ 110 44 OP~ 200160.0 37.12 1575 45 ...... ,. ~, ~T,~ 1500 10/64 57 OP~ . 1578 45 M. JO~ 1515 10/64 38 OP~39.94 37.95 ~1576 45 D. ~I~ ... m: * 1530 10/64 20 OP~ ~ 1565 45 ,, ,, ~' K~ 1545 10/64 106 42 OP~ 8 . ~ 60.13 41 . 29 1562 45 9.0 ~a~ im:~ ~ .... R,: 1600. 10~64 OP~ ~ 1560 45 Dm: __ in ~ ..... 1 61 5 10/64 110 63 OP~ 1 74 ~ 1 59.3~ 44.61 1 560 45 in ~S~ze: ,, . 7/8 ,n 1630 10/64 32 63 OP~ 166 ' ~,~ " 1559 45 ).P Size: ~.: 25 ob~ ....... .~" --'-- nae~: 1645 .10/64 26 50 OP~ 164 "~; ..... 80.1~ 46.28 1558 _44.9' ' ' , ~ , , , ~ ' , ~ I1,~ ii iii i i i i i i 1700 10/64 34 63 OP~ 190 ~.' 1554 44.9 ~: ........... ? .... 1 ' - r 1715 10/64 28 45 OP~ 184 .... [ 160 3: 49.62 1554 ,, ,, , n , ~ , * ~ ...... A~ UNIT ~IC FLYING ~ ~R G~ G~ CUMU~TtVE SEP SEP O~L ~AL L~UiO GAS WATER .... CL~K ~ ~IFCE ~IF~ G~ ME~ ~P C~V ~IFICE TEMP GRAVITY ~PR EXPANS ~ PRESS FL~ ~AL ~- ~ G~ IN G~- OiL G~ c~UIO OIL TIME Sl~ OIFF G~vITY TE~ P~SS F~ F~R F~R F~R F~R F~TOR ~; E~/NS ~TE G~ ~T~ ~UTION RAT~ RAT~ RATIO ~TIO le~r ~ , ~:~._ , ~o, e ~ ~ ~e~ F. Fo , , ~. ~ '" r~ ,,,, '"9 ~', -~-~e=a,,, ~ " ~m , GO~ GOaT ,. t~"h ~ wO~ .... e~a .... ~. ,..4 ,, oF eS'~ ....... I oma OO,U oo~ ~;b' ~ ,,. ~ O~ ~CF~O ~uC~ ~a '~,sre ScF;s~ s~,eec esu~ ............. ............... ~f ....... ..... ....... I, . ....... ~te' ~ , : D~ , ..... [~n.. 3. 068' ..... ., , ,,, ,,,,,,, , ,, . ~._: , , , ........ P~e~ 0 - 50 ~:, , , ..... ~ .......... C Pre~ , ~: 0 - 500 "' ' ........ i , , .... ~ TI~ , , , ...... ,, ,,, ~ter . ,, , _..~- ,, , , ~r Run ..... .. , ..... Pre~ cPr~ ., .... T. nk ?o., _ 800 ~, 1.667 ....... , , ~ .... ~ , ,, Rep: Mud Wt Fluid: Sr.'Ft.: Sba C~sing ~ ~e~ S~ze:... Ra~: Meier Ra~ Gu a~r R~ Diff. Pres R~ S~ ~lan~ Slanda.:lC. ondit~n~ OAS FLOW RATE CALCULATION LIOUID FLOW RATE CALCULATIONS F = ,',I¢,¢, K - vo ....... ,.. 6o ............. 0F F PB -- 1473n~ FTB ---- 460~_7.. OF Off. = Fu Fb Fit Fg Fpv YX~ P sepa FU = .024 x % P~c / xk /520 METE:R(, O,: .......... At m,n : (1 -- BSW)(1 - Sh~ 60) 1440 TANK ' O,, = ~t ....... nlln K (1 BSW~ ....... 1440 wOILz T / // )duction lesti g Services .omc: DATE 3-19-90 '* . - ! ~, TEMP CHANGE OIL CUMU',.,~TN~ CHANGE WATER CUMULATn,'E 3.-.4 ~_ CL~K C~ CHOKE TEMP PRESS CH~E TEMP H~ CO: ~LINI~ PM VESSEL ~l OIL ME~~ S~ GRAVITY :~ COUN~E~ '~~,~ ~ _~ TIME P~SS SiZE Sl~ TEMP COUNTER G~V~T~ TEMP .{ B W .~ ~ ¢ ~AC~ C0dNTE~oo RATE 3:; B~, COuNTER~ at,n: 2245 10/64 28 64 OP~ 186 :' 80.16 74.66 1530 47.3 ~-' , ~- ,, ~ ~r.~ 2300 10/64 26 62 OP~ 1741533 446 , , ~. GO~ 2315 10/64 26 60 OP~ 170 } 15~ 36 77.~8 1538 44 6 M:~ ~ 2330 10/64 27 60 OP~ 188 . . ,~' 1535 44.5 _ , , , , t, , , , , ,,, , , , ,, , n.: 2400 10/6q 2a 88 OP~ ~ 72..... ~'. 1 S34 44.5 ~a: in ,~ ...... oo s i0/64 27 80. 6 8 .32 ~Si~: 7 ..m.~ ' ~"' " ,.~S~,:~~O030 1'0/64 26 64 OP~ 190 ' ~ ..... 1526 ~4.5 , .... , ...... ~.: 25.. ~ ,~: ;004'5 10/64 28 67 OP~ 182 ? 80.16 82.99 1512 44.5 ,, ,~ , ,, ,,, 0100 10/64 26 56 OP~ 1661512 44.5 ~:, ~ ...... i ....... 0115 10/64 26 58 OP~ 158. . ~ .~ ...... 160.32 86.32 1505 44.5 ..... . ~ut~ ....~ ................. ~,~ ........ ~1" A.. UNff ~ FL~G ~ ~PER G~ ~ ~ CUMU~TIVE ~P SEP OIL ~AL L~ID G~ WATER , , ~K ~E~ ~ ~tF~E G~ M~ ~P C~v ~IF~E ~ ~VI~ ~ EXPA~ ' PRESS FL~ ~ ~- ~L G~ IN G~- OIL ~ L~UIO OIL ~E ~ ~FF G~I~ TEMP PRE~ F~ F~ F~ F~ F~ ;~, E~E~ ~ G~ ~T~ SOLUTION RATIO RAT~ RATIO ~T,O , ~IG ' tN INH~ ~ ' PSlA ~IM ODIM ~1~, ,, '~IM , ~,M ' OOlM ~ ~M" , M~F~ MMCr ~;~Ts' scnsTs ~;,st~ ~sBL sscU~r , ,seLsTe, "' ~r 1" ~ter .. ~ ........ 8~ ..... , ~~. ~. . ~ .. . 3.068 ,,, ..... 'r~ 0 - 50 ~2 ...... ~0 - 500 . . ,,. _ leter ~ . . .) ....... ~' I ~7 , ~ 2 .... ,,,.,, ,, ~'dConditio~ GAS FLOW RATE CALCULATION LIQUID FLOW RATE CALCULATIONS F Col' Facl'3f Iqe(:luc1.,,,'~ F.~clo, 14.73 P$1A PRESS BASE FAC~ TEMP BASE FACT ''(14.73~t'(460 + Tsc)k .30o F (1 - 3SW)(1 - Sh, 60) 1440 TANK 'Qo = .3Qo K (1 - BSW) 1440 O~t 60 0¢ F..-'";~ ..... F,.-- 460 - oF Og = Fu Fb Ftf Fg Fpv Y~,"hw P sepa FU = .024 x ~ P,c / x- 520 / METER - Qo ..~! m,n %-t'-~-m--~ De,,gna~,on C I S CPAGE 9 3_20_90 of 41 z tc, uct, ion esting er'vices ~r:, FIELD READINGS DATE · C~L ?E&~ C't'tANGE Otu C~U...~",,'E C~A,%'GE WATER CUMULA?~'E ~----:~4 CL~ ~1~ CH~E TEMP ~ESS C~E TEMP H~ C~ ~LINI~ p H ~L ~L ~ M~ ~L GRAV~ S~E CO~ IN OIL FL~ ~a_ H~G f~ ~ ~ rL~ TI~ P~ St~ S~ TE~ CO~TER G~V~ ~MP BS & W r~ COU~TER · ~ C~ ~ ~ C~ Tn T~ ~ ~ ~ B~ ~ ~ ~ ~ ~ ~ , , ~ ~.p 0130 10/64 28 59 ~p~ ~ ~ _ 1492 44.5 .., ~. ~O~ C~ C ~ 3 3 8/6~ (~ ~:~:~ ~] ~ D~??]~) 0145 8/64 26 110 OP~ 188 _ 80.16; 87.99 1494 44.5 0200 8/64 30 142 OP~ 1791492 44.5 . : ..... ~ ~. 0215 8/64 30 168 O~ 160 80.16 89,66 149~ , ,,, , , - ~L:, "°230 8/6a 30 180 0~ 190 ~~ ~0~ ~~ ~(~ ~0 ~ 1~97 ~4.5 ~:" ~ 0245 8/64 29 160 O~ 186 80,1'"~ 91.33 1486 44,5 ~: ~ __ i~ ,, ,I ............ .,,. ,. ,, ........ ,,,I , , , ,. ~.~s~: ~ ?/8 ~ ~300 8/64 28 159 O~ 1721484 44.5 , , ....... , , ,,,, ,, , ~ o3~5 8/6a 28 50 0~ 180 ;~ ' ' 80,16 93,00 1680 10,3 , , , ~ ~- ,,,, ~: ~ , . . ~ ~ HOT.~ ~T~ ~,~ ,:~ ............ 0330 8/64 28 ~2 O~ 198 ~ 1760 10, ~: fl ........... ~ ....... "~~ ,, , , , ,, ,~ i , , , ~ , ..... ~-- , .... "' , , ~s.~ ~:~ ,' ,' ' ~ " ~ 1 Il ,, ~ PRE~ ~F~ ~IF~E G~ ~. S~. C~V ~IF~E ~MP GRA~ ~. EXPAN~ ~ ~ESS ~ ~At. ~-~L G~IN G~.OIL G~ L~ID ~L , A~ ~ ~C FL~I~ ~ ~R G~ ' ~ CUMU~TIVE ~P SEP ~L ~AL L~ G~ WATER ~ME S~E ~FF G~VI~ TEMP PRE~ F~ F~ F~R F~ F~ F~ ,': E~ENS ~ G~ ~T~ SOLUT~N RATIO R~ RATIO ~TIO ~e ....... ~: ~o a ~ ~ ~oa Fu F~ F~ ~ Fm Y ~ /~ ~ , I ~I GOR2 G~T ~LR TLGa , , i , , , , .~ ,. , ,ae~r 1" ,, .............. [ ....... , . ~ ,, , .~ , , , t , ~:_ ~ ............ · ~_~.~_;, .......... ,, , , ~Run 3.068 ...... ~ ........ ~ ~ i ,, ,,, ,, , , ~--~ ,,,,, , , , , , Pm~ 0 50 ~:,., -- _L , ,,, [~ 0 - 500 ' ' ........ e~ '~ .... ....... Mae.~ , VL~ , , , , .... t - rRu. d~,H ! ~ ~ -- si0n ~-'~ ..... ~cho~ .age :P~ .... _ ......... ,, ~- , , , ~' 'ar ~ --~, '" "' ~ 1.667 ......... ~ - ............ ~ 2 ....... .... -~ , , ,,, a . ,,~ ~Dia: C~sincj 't" Gas Met, StSc Pre Standa~dCondit~m GAS FLOW RATE CALCULATION ' LIQUID FLOW RATE CALCULATIONS F: M,r .... I.,, v,~,~,, .... ( ~ PSIA PRESS ~E ~A~ TEMP ~E FA~' (14.73~ 460 --~4..-7~ ..... FU: ,02~ x x .... x; ...... F (1 - BSW)(1 Shr 60) 1440 TANK ' Oo .......... K (1 BSWI 1440 OIL _ :~73 FTE= 4~,.:~ Qg: FuFbFtf FgFpvY~"rhwPsePa Pst / ~2~- METLR onTesting Services ( .... ,,0 o, //2 ~' FIELD READINGS DATE 3-20-90 OIL ,~E 1,4~ CHANGE O~L CUMULATfV~ CHANGE WATER CUMULATIVE · ~-- CLOCK CASING CHOKE TEMP PRESS CHOKE TEMP H~S CO: SALINITY PH VESSEL OIL O~L MEAS OIL GRAVITY SHOlI~KAGECO;qP IN OIL FLO~ T~T~,/[.. H~O II,~ ~.-0 FLOW TOT&. TIME PRESS SIZE SIZE TEMP COUNTER GRAVITY TEMP BS & W ~ ~ 'F I:k,.,'"'~'O~ ~'AC'"OI:; COUNTER RATE 0:. S=-. COUNTER COUN'E~ RATE _ PSI~ IN el: PSI~ IN a~' PPI~I ~F BBL APl :F % AP* ~: caA~ BBL STB/C BEL 88~ BI)Lq; at,n: 0400 8/64 22 14 OI:,t~1 180 RESTt~I~ ]I.I~ 0,[00 1560 25,7 S. MK'PC_AT.r 041 5 8/64 22 32 OP:E~] 188 ' 0 94.67 1442 30 M. JOINER ..... 0430 8/64 32 180 OPI~I 1801471 30 m: ~ 0445 8/64 31 146 OPI~ 1 ~240.00 ~5.50 1456 30 ' 9# g_c3_. 0500 8/64 28 134 OPI~I 185 .... Ft.: 0515 8/64 28 130 OPEN 16480.16 97. 0530 8/64 28 125 OPEN 160 ~ Size: 7 in - _ (0540 RESET HERTZ ,TO 25 RESET .~___Q~.~ ~ TO 6 I64) ...... ~,P. Size: 27/t:1 i, 0545 6/64 26 113 OPI~I 178 80.16 98.84 1557 25 ~-- GAS METERING ABS UNIT BASIC FLOW~NG GAS SUPER. GAS , C-,-,-,-,-,-,-,-,-,~S CUMULATiVE SEP 5EP OiL TOTAL LIQUID GAS WATER - CLOCK PRESS ORIFICE ORIFICE GA~ MEA5. SEP CONV. OR,ICE TEMP GRAVITY COMPR. EXPANS. t PRESS FLO~ I'OTAL GAS.OIL GASIN GAS.OIL GAS LIQUID O~t. e~et, _ TIME SIZE DIFF GRAVITY TEMP' PRESS FACTOR FACTOR FACTOR FACTOR FAC1OR FACTOP.< EXTENS RATE GAS RATIO SOLUTION RATIO RATIO RATIO RA"r ~O ~e: ...... i:~'~' ¢ ~w ...., E T~ PseOa 'l:u ' OD~U'Fb' ODI~F'*f R3 ODIMFov , Y 'i-~ ' ..'~l~Da , C~ ' GORI GOR2 GORT TGLR ...... ,, TLGR ~'O~ __ P~IG IN iN H~0 [ ~F PSIA OOlM OOIM ODild, ODIM MSC~O MMC¢ SCF~STe SCFISTB SCF~STR SCF/BBL 88L'U~ICF Ileter _ ~eter - ' ............ , Run 'Run _ Press _ UudW I=luicl: I~,' H~0 Meter Size:_ Meter Fi Diff. P~ Gas Meb l~eter R~ Dill: ~r /Tan~ Standa~dCon~io~ OAS FLOW RATE CALCULATION LIQUID FLOW RATE CALCULATION: F 14.73 PSIA PRESS ~E ~A~ TEMP ~E FACT r14.73~ ~460 ' T. ~ JO9 JOo C .... 6Q...... ~ Fps-- -~-~:~ .... FTB= 4~_,g__oF Og = Fu FbFtf FgFpv YgZhw P sepa FU= .024x ~/x~ ]--~26-~ %gETE R - O,)' .........At m,n F (1 - BSW)(1 . Shr 60i 1440 TANK ' Oo .... ~ m,n K {1 BSW) 1440 O~.. oduction esti ervices FIELD READINGS ' DATE 3-20-90 OIL TEM~ CHANGE OIL CUtaU:J~TI%~ CHANGE ~ CUMU~T~E ' ~ ~: .... .0600 6/64 22 130 OP~ 186 _ 1561 25,1 , ~. ~ .,.0615 6/64 22 158 OP~ 184 8 1612 25.1 M. JO~ -' , ~. _0630 6/64 22 185 OP~ 200 ~_ , 1634 25.0 ..... ,, ~ ~ ~ 0645 6/64 22 158 OP~ 2101599 25.1 ,, , ~9~ K~ 0700 6/64 24 120 OP~ 209 * ~3 ~ POSI~E ~C~E * (6/64) 1614 25.1 ~ Iht: . , ,,, ~t.: 0715 6/64 24 105 OP~ 208 81594 24.9 ~: in .......... 7 m -0730 6/64 32 88 OP~ 1579 24.9 ,,, ~Sia: ......... , , , , ,, .... ~,,,., ~ ' , , , . ,, ).ES~:~2. 7/8 i, :0745 6/64 34 80 OP~ ,~ ,.. 1579 24.9 ,.. ~.: L , ,, ,,, , ,, ,~ , , ~: .... ~0800 6/64 ~6 75 0~ 210 8 ...... '~ 100~ 1572 ~.9 ~: ~, , ....... ,, K~. , ,, , ~ - ,,, 0815 6/64 33 75 ~ 1571 2~. 9 ~: ~ ...... ~ ~ , ,, -- ~,~,;,, , , ,, , ,,,,, ,, ~ , , ,,~ ~ ,, ,, , ~ ,, ~ , ..... , '~ ...... ~ ....... ~TEm~ ' ' ' ,J ~ ..... , , ,, ,,,, , , ,, ~' 1" ' ,,, UN~ ~ CL~NG ~ ~PER ~ ~ CUMU~TIVE SEP SEP ~L ~AL L~ G~ WATER .~ ~K ~ O~E ~F~E G~ ~ SEP C~V ~F~E ~ G~ ~PR EXPAN.~ PRE~ FL~ ~AL ~- ~L G~ IN G~- OIL ~ L~uID 0~L .... p~lG tN ~N H~ .F ..... ~SiA ' 0'DIM ODiM ODIM,,, ~M ' , ~ ~ ODI~ M~ ' MMCr' ~F~Te ~CF/STB SCF~STR ~ ~8L 88L:M~c ~6~ ~'~ ,,, ~ter ................. .......... .... , ...... ,~ , ,, ~er .......................... ~: ...... ............. ,.,, _ ,,,, r Ru, 3. 068 ................. ' i i , , , , ,, ,,, ~: ........ , ~ ~ . .~ ....... = . . :, ~:~ 0 - 500 .............. · ...... ...... ,, ......... . ...... rR~ , ,, ,,, ,, ~: .... - ...... : P~ ......... - ~:.. i , -,. ,~ ,,, Tank T~ 800 ~: 1 .667 - ' ...... . ,, , ~' :~ '' ,~ ,,,, ,,,, ,, , ..... ~. - _ ,,., , ,, Cu~ Ret I%~: $~t/R.: Casing Tub'D.R Oil ~ Size:_ Rang Size: H~ Me*,er R~ Diff. ~g Static t% GasM~ ~/~e: Static P, ~an~' Stan<:lamCondition~ OAS FLOW RATE CALCULATION LIOUID FLOW RATE CALCULATIONS ~c 14 73 PSIA ~ESS~EFA~ TEMP~E~ACT (14.?3~ (460'T..) AQo F(1 -BSWt(1 Shr60) 1440 TANK %: 60 ...........oF F Ce = ~:2,e F~ -- .... 4~5.3~_.- oF Og = Fu Fb F~f Fg Fpv Yx'~. P sepa FU = .024 x .~,~. x .... ~-6--~- fl~ET~R... O,,, ~t m,n C (' ::)ductionTesting Services °' ;ustome,: (/)N(X:D INC. FIELD READINGS DATE 3-20-90 j '~EMP CHANGE OIL CUMU;...A"V~ CHANGE WATER CUMULATIVE c.-4 CLO~. C.4~ING CHOKE TEMP PRESS CHOKE TEMP H~S CO.- SAUNITY PH VESSEL OiL OIL ',4EAS OIL GR~O~L~?YS.n~,(AGE CORR ~N O~L FLOW '~'A. ~:C ~, H:O FLOW TIME PRESS SIZE SIZE TEMP COUNTEP GRAVITY ,"EMP BS & w .; ~.~ c ~"~.4~ =ACTO~ COUNTER RATE $'. S~. COuNTER COUNTER RATE ,~TER BBL a,o.: 1 571 24.9 0830 6/64 34 75 OPIC1 200 ~e, 6/64 32 74 OPIC1 1569 24.9 __ N..TOTN]~ 0900 6/64 32 74 OPIC1 196 8 100% ~ 1 569 24.9 9. D. ~STRI~ 1 567 24.9 m:_ , 0915 6/64 32 73 OP~q _ ,, ~ KCL 0930 6/64 32 73 OP]~] 196 1565 24.9 rt: 0945 6/64 32 72 OPEN 1 562 24.9 . ,,, Dm: , in ,-- ' 1000 6/64 32 72 OPEN 192 8 100% 1562 24.9 9. xj Size: 7 i, KCr, ,,, ).P. S~e: .2_7_,L~ 1015 6/64 32 71 OPEN 1560 24.9 v~.: 25, ~ , hnef: 1030 '6/64 32 70 OPEN '210 ............ 1559 ~4.9 ",ep~h: ...... .,% ' "' ' ' 1 560 24.9 - .~h: , 1045 6./64 32 68 ...'OPEN . ~' , ,, ~I ' ' , '' ' I~tOr ' ' c~s ~.i~.m~ ......... , ~o , , i ,, ' ' ' ' ' ' GAS CUMULA'rlVE SEP SE P Oil. 1OTAL LIOUIO GAS WATER , ASS UNrr SAS~C ~LOW,NG CAS SUPER GAS PRESS FLOW ~rAL C..AS. O~L GAS ~N GAS- O.. GAS UOU~D O~L I~ I II CLTIMOCEK PRESS ORIFICE ORIFICE GAS MEAS SEP CONV ORIFICE TEMP GRAVITY COMPR. EXPAN$ ....... SIZE DIFF GRAVITY TEMP PRESS. FACTOR FACTOR FACTOR FACTOR FACTOR ~ACTOR' EXTENS RATE GAS RATIO SOLUTION RATIO RATIO RATIO RATIO I~ef ~ ,, , GOR2 GORI' TGLR TLGI:I WOR ' i~iG .... 'IN IN H,~' , ,, ~ PSIA OOtM ,,OOIM ODeM , 00tM, , , OI~,M ODIM ODIM , MSCF~ MMCF SCF/~TB SCF/STe SCr;STR SC~'BBL ,,88LJMMCc , BBi-,'STB..... ~eter 1. , ......... ' , ~ter , , , ' ' ~e:, i. ~I]~ S~. , ' " ' .__ ~R~ 3.068 " ,, i , ,, p,~ss0 ; . ,, ,: ..... - 50 " e Taf~k , . rRun ....... ..~ 'Press ,. ge Total: .: 1 .667 ': :~ _2 l, t · quid: ~he~ Dia: t: '7an~s GAS FLOW RATE CALCULATION LIQUID FLOW RATE CALCULATIONS F =.Me,~, K = vo,u .... , Co,' lCac~-.)~ ReOuc:,,.,,~ F~C~O, [~,, v./h~, p ~0~> FU = .024 x -- x cnn / ~ETER · Oo ~Oo~.~ F (t 8SW)(1 - Shr 60) 1440 TANK 'Qo - .~,, m,r~ D12~ Petroleum PAGE 13 of 41 ( :)Ouction lesting Services FIELD READINGS OIL TEMP CHANGE OIL Ct~U,.A'r N~ CHANGE WATER CUMULATIVE C-~-4 CLOCK CASING CHOKE TEMP PRESS CNOKE TEMP H~S CO: SALINITY PH VESSEL OIL OIL UEAS ' OiL GRAVITY S~"%<~£ CORR IN OiL FLOW T'-. "':$ IN H:O cLOY% TIME PRESS S;ZE SIZE TEMP COUNTER GRAVITY .-EMP OS & W '& 60 'i:-'a~'~J~= CO~;-~" E; ;ACTOR COUNTER RATE ~. _=5. COUNTEi= RATE WATEn ation: ....... 1100 6/64 32 66 c~p~-'~ I q4 8 100% .. 11560 24.9 9. ?. METCAT_,P 1115 6/64 32 66 OP]~I 1560 24.9 1130 6/64 32 64 OPIC1 'i .... 1561 24.9 D. STRI~ .... : .......... 1145 6/64 32 64 OPIlq 1561 24.9 , , ~-'e~ K'CI", 1200 6/64 33 63 OPEN 8 ~100% 1562 24 9 rated Int:~ ti: i~CL , , . ,, Ft.: 1215 6/64 35 62 ..... .OPEN ~ . . 1553 24, ~: in' i ............. ,gSize: 7 in: 1230 6/64 33 61 OP'F~ . .... 1552 24.9 ..... :i- ,, ,.p. Size.. 2 7/8 m1245 6/64 32 60 OPEN ....... 1553 24.9 ..... ~.:, , , , . ,, , ,,, , ,,, , , ,, , ,, ~R~: _ 1300 6/64 32 60 OPI~I (~ ,. 100% ....... 1552 24.9. ~ 0~:~ , , ~c~. , .... -~t,:__.___~, 1315 6/64 212 60 OPl~l ........ti .. 1552 ~ 24.9 , ,, , , , , , ,~ , ~,, ,~ , ,,,,,,, ,q ,,,, , ,,,, , , ~s i~rtRm~ ' ! eter 1" .............. ~" ............... ^as. UN. .AS~: ~Ow~ ~ SU~. 0*S i; C.*S CU~ULAT,VE S~. SE. 0,~ ~A~ ~OJe ~ WA~ER .... CLOCK PRESS ORIFICE ORIFICE GAS MEAS. SEP, CONV. ORIFICE TEMP GRAVITY COMPR EXPAN~ PRESS FLOW 1OTAL GAS. Off. GAS IN GAS- OIL GAS LIQUID OIL TIME SIZE DIFF GRAVITY . TEMt~ PRESS. FACTOR FACTOR Fa~'rOR FACTOR FACTOR FACTOR ~ EXTENS RATE GAS :RATIO SOLUTION RATIC RATIO RATIO RATIO ~e:., ..o ¢ A. , ~ ' ~.o. .... r,.,, Fe .... ~, ' n~ "'~., ~ ..........~,,~..,a ..... C~ GOre C. OR~ OC~T ...... ~.R '" T~G,,,. ,P.~IG , IN , 'NH,~) ..... ?, , PSIA ,, ODIM., ODIM ODIM '"O0~'M ..... :O0tM ODIM !, ODIM ,,MSCFtD. "'.MCI: SCF~TB $CF'$TEt S,Ci::,$T~ SC,CreeL .eS,_..~.'l~BSL.,S""B .... 'leter 1" ./~ i .... .................... 'r Ileter ............ ~ .... ,, e: ,4etef .......................... DANTe, Fro. ,, ~ .... ~ ,, ~ ., ,,,. :. ,,.,~..s ......................... '~ .... t r ....... e: 0- 50 , :Press .... e:. 0 - 500 ....... , ........ t ...... ' .... 'i ...... , ......................... , t , ,.. , ,, ........ , ....... ,~ , .... . ..... ....... , i , .. , Ru~ ........... ~. , , I, ~ .... -- ...... ~i , , .... , ~ ........ , ...... ,,,,,, ,,,,, , , ,, ~r~ ....... , , ...... ,, + "' ,, ~ ,,, }'om~ ..~0~~~ ......... ~: 1.667 ..................... ..... , ............. ~ ,, , , · ~ , h. ., , ..... ,, ,,,,, ,, , StanClard Condfho~ Dsc 60 oductionTesting ervices ( ..... °' ~ FIELD READINGS DATE 3-20-90 .. TIM~ PRES~ SIZE SIXF TEMP COUNTER GRAVITY TEMP BS & W c~/_..~. COI~ ,N OIL ;LOW "~T. 4. -;C, ;N H,O ~'LO9~ '~j",rA. iiii ,,.,at~: ,. 1330' 6/64 32 60 oP]~l 196 -., i 1552 24'.9 smmer ' " 189 1552 24.9 IIIII II 1400 32 58 180 8 100% 1552 24.9 9.0 M~: , ...... 1552 24.9 ~.: 1445 34 57 1931551 2~ 9 ..... ~: m , ,, ,,, , .............. - 1500 34 57 ..... 190 8 100~ 1549 24 9 9.0 1545 32 55 ~' ' ' ~ ................. ~:1550 24.9 ........... ~.~: , ~6oo .... ~2 55 19o 8 ~~oo~ ~... ~s49 24 9 9.0 ' ~ ~" , ....... A~S. UN~ ~tC FLYING ~ ~R ~ G~ CUMU~TIVE ~P SEP Oil ~L LIOUID ~ WATER ~: ............. ~K ~E~ ~I~E ~E ~ ME~ SEP C~V ~IF~E ~ G~I~ C~PR EXPANS ~ PRESS FL~ ~AL ~-~L G~{N ~ L~UtD OIL ~E SI~ ~FF G~VI~ TEMP PRESS. F~ F~ F~ F~R F~R F~R { E~ENS RA~ G~ RAT~ EOLuTtON G~-RATioO~L ~T~ RATIO ~T~ , , ,~> ............ ,,,, ,, O~ ............... ,, , ...... ..... ~ .................. ~ ......... , ,, ............ . ~ ........ ~Run , , ...... ,,, ~ ,,,,, ,, ,,, ..... ...... ~CULATION LIQUID FLOW RATE CALCULATIONS F = Me,-., K = vo,u ..... PSIA PRESS BASE FACT. TEMP BASE FACT [14.73~ 460 * T~c~ JOo F (1 - BSW)(1 - Shr 60) 1440 rANK ' Go = 30o K (1 - BSW) t440 O,L :ASTM De,,gna,.on ~ ._ 1473 ~ _ 4~ - 0r Oq = Fu Fb Ftf Fa For Y~/hw P sepa FU = .024 x k~l x 520 i METER - Qo = ( oduction lesting ervices °' ~°"~T #2 FIELD READINGS DATE 3-20-90 ,, WEU.~r. AD HEATER OIL 01t CONOENS~TE LIETERING N~ METERING .~ OIL 'rE Idl::' CMANGE OIL CUMU~.ATN~ CHANGE WATEla ~UMUL.,ATIVE '- k~'-4 CLOCK CASING CIqOKE TE~,iLo PRESS CHOKE TEMP ~r.~ CO.' SALINITY PH VESSEL OIL OIL ME,AS OIL GRAviTY S'G'~"'"Jk'~ CORR IN OIL FLOW '%~' ~'. "tC' ~N ~.'~ I:'LOV¥ TIME PI:qESS SIZE SIZE TEMP COUNTER GRAVITY TEMP BS & W 'Z 6C I:':k."--~P =AC'TOP CCUNTE~. RATE '~:. '--'~.. COu'~TE~ COuNTCa RAT~ ~'a'rEr~ :' I: ~ PO~ ~ c.,,. ~ ~ cf, Th Zseo Oo C,o To aSW ~ S~,. " m ~ C,,, P'S~G "' h~. ~ PSIG ~N ~ PPM q: BBL AP~ r ~. AP, ~ =aAC B~L STB~O 88~. 88:. ee',.'-~ a5~. ~ ~"~ ~at~: 1630 6/64 32 55 OP:]~ 2101545 24.9 ,ease: ,, ~0~r, ~ 1645 6/64 28 55 OP'E~ TAK~ IH~T']:ON ¢~rr rT3~ T.T]~;: 'T~ T~J-~ rea ~ ;'TROT T na~ ~'~_"rr~ OT~_r'~,:~ ~, 1545 24.9 JOINER ,,,, ~- 1700 6/64 26 59 O:P]~ 2101550 24.9 171'5 6/64 22 63" OPI~I 1551 24.~ ~ , ..... ~'mid: ~ KCL 1730 6/64 24 63 OP]~T 2121612 24.9 ,,,,,,, , ,, mouR.: 1745 .. .... Oia: ,n ...... 1800 :asi~ Size: . 7 in .... I ..... , ,,, , ).P. Skze: 27/8 m 1808 CID.q1: WELT. TN 'TY'J RTe. TT~ R-T.T~TW.. q'~ ~~ 1LT-TP r"T-T~,~1C,'. ~ rTr, T-m~ wj'/'~ , , i , , , ,,,, , ,,,, , , , ,, , , · )qq::*h Ref: ............. ,-0epm: tt .................. It ......... , , . , ........ icl , , , , ,~'qll:~ ,, ~ ~ ~ ,,, , , , ,, ,, , , ,, , , , , , , , ,, , , , ~ ~ .......... GAS~aONG ....... i ' ' ' ' ~Ut,O ' ' , , , , ,, , ,, , , ,,, ,,, , , , , ,,,, , ,, ~r 1" ABS uNrr~ BASIC R.OWING GAS SUlaER GAS ! GAS CU~uCATf¥E SEP SE~ OIC tOtAc C~Jfl) ~AS WATE~ I'~E ~ 6PAv~TY I'E~a' ~ES$. ~ACTOR ~'m::m ~,,CtOe ~ACTO~ ~*C'IOR r-AcTo~ ! EX'TENS PATE 6AS PATIO SOcuT,Cm IqAnO ~A'nO RA?,C) RATIO ' Jeter ,,s,~ ,~ ~..o .... o?~ " ,~^ o~,. oo,. ". oo,~ ooT,~ oc,, ' oo,..' . oo,." .sc~,o ..c~ sca,st8 sc~,s?e ' . S¢~ST~" SC~e~ ".ee~.'."..-C~ .88..'S."e' . .......... ileler ~e:~ 1" , , , ,, 4, aete ........ ::~JJJ~e: ...... " ' rJ;)~e; · , , , ,,, , , ,, , ,,, ~Run 3068 .......... ....... ~ .. , , m. Pre~ 0-50 '" qlll(J~: ...... , ......... ~,ess0 - 500 ' ' ....... ....... ~ , , m, je Tank ..... ~ pleter ' '~ ' ' ype: .... ,, ,, *ess ...... t .... Jarl{ ~:_ - I ....... ~,~-aoo___' ' " ,, ,,, , eL/in: ~. ~ 667 ...... Ta,~s: 2 -_ '' , , ,, ,,,, , , ,landarclCo~itiora GAS FLOW RATE CALCULATION LIQUID FLOW RATE CALCULATIONS F -- Me~,, K: Vo,u sc 14 73 PSIA PRESS BASE ~AC'r TEMP BASE FACT [~4.73'~~ 460 ~ Tsc~ ~Qo F (1 - BSWt{1 Shr 60i 1440 TANK'Go - ~C)o K (1 - BSW! 1440 O~L (ASTM ~n .. I:' __ -- ~4:3 I:' __ -- 460 . or Og = Fu Fb Ftf Fg Fi3v Y~./HW P sepa FU = .024 x \~-.. / x 520 / METER - Qo '-- A-T;.n,-'~ - A1 rain 01250 oductionTesting ervices ( ( .... °' ~ ::]~Co ~ ~r: FIELD READINGS DATE 3-21-90 ~4 CL~K TE~ CHANGE ~L ~UMUgAT~ ~ANGE WATER CUMU~T~ mat~: 2330 ST~~ ;~. aO~ 2335 !523 21.7 D. 0030 4 1611 21 6 0045 2 1650 21 . 6 0100 2 1665 21 . 6 ~~ K~ 0115 I 1615 25.2 , ,,, ,, ~.: 0125 ~ )~ ,,~ ~ ~ 8/64 ........ 140 4~ 1420 28.9 7 230 B~,~S ~~ .... 2 7/8 ~9 ~ ,,, ~()~ 2{~/64 ..... .... TIME S~ OlFF G~ TE~ P~SS F~ F~ F~ F~ F~ F~R E~ENS ~: ~ ......... ~er .............. ~ ...... ~ Run .... , ..... q h~R ........... ~: 0 - 50 ............ ............... ........ ,, Run .......... d ,, , ....... e: .... [ .... , ,,, ,luid: r~: 3iff. Pre ~age ~.BUin: itandardl GAS FLOW RATE CALCULATION LIQUID FLOW RATE CALCULATIONS F = Me,el %c 1 4.73 PSIA PRESS~E fAO TEMP ~E F~ /14.73~ 460 · T~c ~Oo F ( 1 - 8SW)( 1 - Shr 60) 1440 TANK ' Oo = AOo K ( 1 - 8SW) 1440 OIL q ASTM ~ .. ~ ~a73 ~-- : a~ :.°¢ Qg = Fu Fb Ftf Fg Fpv Y~hw P seDa FU = .024 x %~/~ ' 5~0 METER . Oo: ~t m,n ~t rain D12~ (- oductionTestincj Services o, ~I~C. ~,s~omer: FIELD REAOINGS DATE ~-~1-90 '" O~L TEMP CHANGE CUMU.&T'V~ CHANGE wATER CUMULATIVE · ~4 ~, ~1~ :~KE TEMP PRESS C~E TEMP H~ COt ~LINI~ PH ~L ~L ~L ME~ ~L GRAviTY S'a'%~E COfl~ ~N OIL FL~ ~_ ":~ 'h H:0 ¢L~ T~ P~ S~ S~ TEMP C~TER ~Vl~ TEMP BS & W : ~ ; r~ ;~T~ COUNTER RATE 5~. COUNTE~ COUNTE~ RAT~ ~T~ 8BL ,, , ,,, , ,, ~m: 0230 20/64 30 14 OP~ .._ ~.4 116.34 1431 31 e: ...... ~ ~T.P ,,0~45 ~0/~4 28 15 O~ 1440 31 N.~O~ ..... 0300 20/64 26 42 O~ 40.3' 1 17.18 1466 31 0315 20/64 24 90 OP~ ~ H7;S1490 31 ~__ ~ .., ~t ......... :: 9~ K~ "~330 ~0/64 22 30 OP~ ._ 99% 204. 122.18 1409 31 .... ,, ..... , ~,.: '"0345 ~0/64 24 40 OP~1399 30.9 9.0 ~: in ......... 0400 ~0/64 24 53 OP~ ~ ~'~Z [~ ~ ) 30 99% ¢ 122.1 8 1 331 31 ~Sm: 7 ... ~ .......... ,, ,, .... . , ).RSize: 2 7/8 in '~41'5 ~0/64 22 34 0P~1410 30 ~.: 25 ..... ,,,, ,,, , ,, , ,, .... ~: %430 ....... ~0/64 24 50 OP~ 40.1 123.01 1404 30 .................. .. , j,, 99% . , , · --~mh: ~ ~ ............. 0445 ~0/64 24 75 ~1440 30.1 ~-,~-~: fl~ ,,~ , · ' ........ ' 90% ...... ~ 40.1 123.85 ' 1440 30.1 <'" '~500 ~0/64 23 84 0~ , , , ~ ,, , ,, , , , , , ,, , ~ , ,,,,, ,, , , ~ ,, ~,~, . , , ) ....... ~*~ , ~e 1" ABS. UN~ ~IC FL~I~ ~ ~PER G~ ~ CUMU~TI~ ~P SEP OIL ~AL L~UIO G~ WATER : _ CL~K PRE~ ~IF~E ~IF~E G~ ME~. SEP CONV ~IF~E TEMP GRA~ ~ EXPANS" PRE~ FL~ ~AL ~. ~L G~ IN G~- OIL G~ L~UID OIL TIME SIZE DIFF G~Vt~ TE~ PRE~. F~ F~R F~R F~ ~ F~R . E~ENS RA~ G~ ~T~ ~OLUTION RATIO RAT~ RATtO ~T~O ~er ..... ; ~ ...... ~: ...... ~e' ~ ~ Tg ~ Cu F~ ~ ~' Fm v /n~eoa ~ ~I GOR2 GOR~ ~LR T~Ga WOR ....... p~ , IN tN ~ .... e¢ PSIA O~M '" Q~M O~M ~IM ~M O0~M ,';' , ,O~M M~F~ M~ ~F~TB ~¢~ST~ SC='STR ' , ,SCF~6L ~L'M~~ ~B~'STB ........... ~er 1" ...... , , ,. ~ ................ ,'~ . . L ,, :¢, r R~ , ~ ,, , ,, ,, , · , e:_ 0 - 50 ...... ~ .... :~0 - 500 ' '. '" e:~ , . . ....... i . ~ . , ........ ~ . 'Run ~ ,, _ ~: , , . ~ ..... ,,, , ....... ~: ~! . 667 I . . ......... . , ,, ,, , , ,, tatic Pre BUin: ran~s: mnda~Conditio~ GAS FLOW RATE CALCULATION i LIQUID FLOW RATE CALCULATIONS F Me,,er K-- , Cot, ac~ '.~, Reduct,~.~ P acco, ~ 14.73 PSlA PRESS BASE ;ACT TEMP SASE FACT [14.73~I 460 + Tsc~ AGo F (1 - BSW)(1 - Shr 60) 1440 TANK ' Oo - ~Oo K (1 - BSW) 1440 :2 c _ ~473 C _ 4~-~¢ Qa=FuFbFtfFoFo, Y~/hwPseoa FU='024x%~/x 520 / METER 'Q°= ..~tm,n ~tmtn (' ductionTestinq Services °' INC. ' ~ 3-21-90 FIELD READINGS DATE , OIL TEMP =H&NGE CL~IUL&T~v~ CHANGE WATER CUMULA?r~~_ : ~L CLOCK CASING ~.,-,O~.E TEMP PRESS CHOKE TEMP H2S CO:- SALINITY l~H '~SSEL OIL OIL MEAS · OIL GRAVITY $-a~,~(~GE CORa ,'v OIL ._"~..a. '~-0 ~N "-O CLO~ TI~ ~ ~E ~ TEMP CO~,E~ G~V~TY ~EMP BS&W b ~ r =~ ~O~ :~J~TE~ RATE ~ ~' COu~Ea COUN~E~ a~ZE ~"' ~'515 20/64 24 80 OP~ ~ 1452 30.1 ~ 3530 20/64 ~4 96 OP~ ~ 40 1 124 69 1458 30. ~m , , ~ .... .......... ~ . . .... ~ I !t ~8S UN~ ~IC ~1~ ~ SUPER ~ '. G~ CUMU~TIVE ~P SE~ OIL ~Ag LIQUID G~ : ........... ~K ~E~ ~F~E ~IF~ G~ ME~ SEP C~V ~IFICE ~UP GR~ ~ EXPANS ~ PRESS FL~ ~ ~. ~L G~ IN G~- OIL ~ LIQUID O~L ~E ~ZE DIFF G~Vf~ TEMP PRE~ F~ F~ ~ F~ F~R F~R '~ E~ENS RA~ , G~ RAT~ ~OLUTi~ RATIO ~T~ RATIO ~et .................. mm mm mm m m m , mm mm mm m mm m m,. , m m~ .mm ,mmm m I mm mm m. ml, m mm rRun 3. 068 .......~ ........ ~ '~ ............... ~ ,, ,,,. I s ~1: )U~: anda~Co~t~'tm GAS FLOW RATE CALCULATION LIQUID FLOW RATE CALCULATIONS F = MET-., K ': Vo ....... c ~14.~ PS1A PRESS~EFA~ TEMP~EF~ 1 73 ~460 - T~ JOo AGo K (1 - BSW) t440 OIL ~ASTMDe,,gnai,on C '=-~ ~ 4~ - 0~ Go = Fu Fh Fir Fo For Yx../hw P seo8 FU = 024 x -- x ~ 570 / METE~ ' Oo - .3i m,n F (1 - 8SW)(1 - Shr 60) 1440 TANKm Oo = ~t ml~ D~ 2~ P~' ~O*eUm .. (' uctionTestin§ Services (' °' ,sm,mr: FIELD READINGS DATE 3-2'1-90 ""~i.~1--4 OIL ?EMP CHANGE ~ C'iJMU ~'AT'VE CHANGE l~e,TE R CUMULAI'NE ~,~""-- CLOCK C,*~ING ~HCKE TEMP PRESS CHOKE TEMP H~.S CO; .SALINF'r'YPH VESSEL OIL OIL MEAS O4L GRAVITY S'~'K&GE CO~ IN OIL ~'~.&. ~:C !.~ M;O PLOW TIME gl:lESS S~ZE SIZE TEMP COUNTER GRAVITY TEMP BS& W a 60 I:' :A'"'"J~ =ACTOI= COuI~!'ER RATE r.~ ~a~,.. cou%'E~ COuN'rEI:;RATE .,~,'AT'E~ i a~: ... 0515 20/64 24 801452. 30.1 ,. ,,, ..... ~r 0530 20/64 24 96 20% 20 40 I 12469 1458 30 $..M~'nY'~T.~ . ' · - M. ,.TO~ .... '~Z~ 0545 20/64 24 53 141R 36) , , Nt:. ~ 06IX) 20/~ 24 114 , 20% 20.1 125.11 1464 30 , i ,, , ~ KC~ 0630 :20/64 24 82 .. . 59.98 126.36 1483 30.5 ~c~. mmcllnt:., tt 0 , ..... i:t.: 0645 20/64 22 861442 30.5 Dia: m ...... : , , 0700 20/64 20 90 ,40% 200.02 130.53 1444 30.5 ~gsize: .~ 7 in . " ,, , i, ,, ,, , ..... ms~ze:. 2 ?/8!~ 0715 20/64 20 .86 ......... 1435 30.4 ~.: 25 ' , , , ,, ~: .... OT30 '20/64 20 89 i 1 9.8( 1 30 94 1 435 3(1.4 ................ t .... s .... ~ , , ,, , , ,! i, ,, , , ,, ,,,, , ,,, GAS Mt~,~mNG J' , ~AT~O " , ,, , , , ~ ,, , , ,,, , ,, ,, ,, ,, , _ e~ 1" ,'.85. UNIT BASIC FLOWING GAS SUPER GAS ('" GAS CUMULATIVE SEP SEP OIL TOTAL LIQUID GAS wATER ......... CLOCK PRESS ORIFICE ORIFICE GAS MEA$. SEP CONY ORIFICE TEMP GRAVITY COMPR EXPANS ! PRESS FLOW TOTAL GAS-OIL GASIN GAS-OIL GAS LIQUID OIL TIME SIZE Dill: GRAVITY TEMP PRESS FAC1OR FACTOR FAClOR FACTOR FACTOR FACTOR .~[ EX'TENS RATE GAS RATIO ~OLUTION RATIO RATIO RATIO RATIO e~ , ,, , r: , " ,,, P~IG IN ' Illume0 ~¢ PSIA ODIM .... OO~U ODIU Ioo~1~I 'O(~M ODtU ODIUm MSCFtD MUCc SCF,'STB SCF STe SC~'St~ SC~BBL BBuUIv~CK im i= i= 1,1= ii i ii ii .... i i F, ] ii i= ii m m (eler ......... i~i ..... e: ......... ~ .......... ~'lj~T ~..~ S~ ......... Ii i ............ ~ ~Un 3.068 ....... /i i ......... - ,, ~ i i i i i , i ~ ....... '~ 0 - 50 ~ .... ~ .... ~ m m m ?o- soo iii. ii ........ , ....... ~ ' ~', , , , -- lq ", _ ,,~ Run,, .i L ..... ,,,, ,: J..667 ' ' ~ ......... ; 2 .... ' .............. ._ .... I ....... Pres 4a~c Pm~ taridan::l Coew3it~'l~ GAS FLOW RATE CALCULATION I LIOUID FLOW RATE CALCULATIONS F = 1 4.73 P$iA PRESSBASE FACT TEMPBASE FACT 14.73'~ 460 + Ts~./ .30 -~Oo ~AST~ SC FU = 024 x --'P~c ! x METE ' Qo- o F (1 - BSW)(1 - Shr 60) 1440 TANK -C)o = '~-~--i'~-r~ K (1 - BSW) t440 OIL . 60 0~ F.e -- 14."3 FTB = 460 - *______F Og = Fu Fb Ftf Fg Fpv Yx,/hw P sepa 520 / ~,t m,n .............. D1250 p-t,roteum ,~.o c'~ ,. ...... ( roductionTesting Services ( tr' °' T~-T' #2 ~ FIELD READINGS ~ DATE 3-21-90 S..,ar%<~G~: TEMP CHANGE ~ SUMU~ATIV~ CHANGE WATEFi CUMULA~E OIL CASING CHOKE TEMP PRESS CHOKE TEMP H~ CO: SALINITY PH VES,~L OIL OIL MEAS OIL GRAVITY - CORR IN OILrr..,,.,w T,'~rA, ;.-0 c ff~ H-O ~LOW' TIME PRESS SIZE SIZE TEMP COUNTER GRAVITY.' TEMP RS & W ~, 60 F t,L.."-.'.'.'.'.'.'.'.~; FACTOi:a COuNTE¢~ RATE O.. ES. ~,.,~' .;4T-r, . COUNTEt= RATE ....... , Pt~ C~ T~. Pyro Ch T~ Tseo Oo G~ ~o SSW Go60 S.",' ~ ~:: ac O,, a,,. PSIG IN cF' PSI~ IN ~ PPN! eF ~L AP~ :F __~ e,t ' ' APl :-: FRAC BBL. ST~/D BBL BBL BB'-' '~ ation: 0800 20/64 22 90 CE~ _ 4r~ (1 130.94 1428 30.5 ~ ]3Y'- ;: AD.T * 0810 ]['~:~,c~r') tIER 7~ rD 3' .0 )met , 5. M,.=n~Z~T.; 0815 20/64 23 70 ~ 1393 31.0 M. JO]2qER ' ' 0830 20/64 23 77 ~ 20~ 10.0 131,15 1383 31,0 13845 20/64 23 87 13815 31 . 0 , ,:t.: 0915 20/64 24 '106 I~B 31.0 , , !, 0930 20/64 24 60 206 ' 80.04 133.03 1368 31 . 0 ~ 'II-I:U ~j $iz.: 7 i. ....... ~.p. Size: 2 7/8 i. 0945 20/64 23 45 .... 1343 31.0 ~Ref: 1000 ,20/64 22 40 194 ,, 35~ 39.84 133.86 !3~ 3%.0 ..... ... ' .' . ca,~.~,~ ' .. . . ' ~A,~ '" ABS. UNIT BASIC FLOWING ~ SUPER GA~I GAS CUMULATIVE ~EP SEP OIL TOTA. LIQUIO GA~ WATER , , C~OCK PRESS ORIFICE ORIFICE GAS MEAS. SEP CONV ORIFICE TEMI~ GRAVITY COMPR EXPAN$~ PRESS FLOW TOTAL ~- OIL GAS IN GAS- OIL GAS LIOUID OIL TIME SIZE DIFF GRAVITY TEMP PRESS. FACTOR FACTOR F4CIOR FACTOR FACTOR R~Oai EX~ENS RATE GAS RATIO SOLU?ION RATIO RATIO RATIO le: 'l~eo d '~ T~ '" Pseoa" ~u' F~ "~tt F~ Fi~ ' y' i -hwPseoa " C~ ........ GOR~ GOR2' GORT TGLR TuGR "~0a ,,, , , ,, ,, , ~,, , ,, : P~IG IN IN H;O , *F PSIA ODIM OOlM OOIM O0!M , OOtM ODIM I O01M~ MSCF/D MMCi:: SCF/STB SCI::/ST8 S~:'STF. SCR'BBL BBu, MMCC aeter 1" .............. ....... --' ' ..... I aeter , , le; .... , , , rRun 3. 068 ' "" -- ' ' " '"' 'i ' "" ' , , ,,, ....... ~ress 0 - 50 e: :~r~O - 500 - , .... . .................... , ...... ,, e?ank ,, ,,, , ,, " _ , ,,, :Press .. Na=~o 3!! & Gas Cons: Oo~_~ g ~- 1.667~~ ' ' Mud Wt: ~id: ~t~! Dia: OilMetef Type: Biff. Pn Slaic Pre Size:_ Diff. Pre Sta~c Pr Standan:lConditiom GAS FLOW RATE CALCULATION LIQUID FLOW RATE CALCULATIONS Ps: 14,. 73 ps~A PRESS BASE FACT TEMP BASE FACT \[14'73"'iPsc /,,f 460 Ts: _ .60__ ~ FpE =. FTB.... _ 460~5;.T. =¢ Og = Fu FD F'~f Fg Fpv Y\'?hw P sepa FU .024x x --~':~)'-'") ..S't. ....... m,n F ,'1 - BSW)(1 Sh, 60) 1440 TANK Oo - _-~.~ rTn.;;~ K ('1 B.c,W) t440 ( roductionTesting Services ( (: .... °' ~s~omer:DATE ~-~ ~ ~ FIELD READINGS -, -~.z..,~ W .FJ;t. HE.4~) H'E~TER OIL ~ C~T~ M~EmNG ..... ... ': OIL T~ CHA~E ~ ~LA'"~ ~A~ WA~R CUMU~T~ T~ ~ SiZE SI~ TE~ C~TER G~V~TY TEMP BS & W = ~ c =~ F~R ~N'E~ RATE ~. ~. COUN'~ COUNTER ~ATE M. ~O~ ...... '~ 1115 ~/~ ~ ~ ~ 1~ ~ .0 ~ , 11~ ~/~. 26 1~ ~ 1~ ~ ~.74 135.53 1~ ~.0 _ ~: 9~ ~ 11~ ~/~ .~. 1~ ~1415 ~.0 1~ ~/~ ~ 115 ~ ' ' ~ 18.4 ~ 74° ~ ~.4 1~.~ 1413 ~.0 Et.: ,,, O~: ..... in 17.6 ~ ~o E ,, , , ,, 1~5 ~/~ ~ 116 1413 ~,0 ~ S~e: - ~.P.S~:~ 1~ ~/~ ~' 114 ~ 1~ I ~ ,,, ~.: 25 ~ ' ,, .... m .... ;, , , , ...... ~r~h: fl _ .... '~' ,, , , (': ,,,, , ',%1 ..... , ', l',~x , ,,,,. , ~ ,, , ~ ~. .......... m~t~ ~ ',,' " ' ,,. '~,~ .... ABS. UN;~ ~C ¢L~ING ~ ~R G~ PRESS G~ C~u~T~VE ~ SEP O~L ~L L~U~O G~ WATER ........ ~ ~K ~E~ ~F~E ORIF~E G~ ME~ ~P C~V ~IFICE TE~ GRAVI~ C~PR EXPANS :~ FL~ ~A[ ~- ~[ G~ IN G~- OIL ~ g~UIO OIL ~E S~ DIFF G~VI~ TE~ PRESS ~ ~R F~ F~ F~R F~R E~ENS ~ G~ RAT~ SOLUTI~ RATIO ~r ...... ~IG IN IN H~ oF , , P,SI~ ~IM ODIM ' ODIM ,' ~M O~M O0lM , ~M M~FID , ,, ~MC¢ ~F~TB , j SCF~ST6 SC¢~STR ~BBL " ,,,~'M~r ~6L'~B , , , ~ter 1" ........... ~ ,, ,,,, ,,, ~er ' ' ' ~T~.~ ~. , ......... , , ] , , ~_~/ "' _ i , ~r~ 0 - ~0 :~ 0 - 500 ....... .... ~ e ~k , ., ,, ,,, ~, ~ , , A~er '" ........... 'Run ......... , , , ~ ....... 8: ~ .......... P~ ......... i ~a~: ~- ' .... " ~: 1.667 ~.... ~ .......... ~ 2 ' ' .......... ~ ~ , ~ ~ , ,, , el{ asing eF Ze: ~Uin: ~r<l~:lC0f~lttio~ GAS FLOW RATE CALCULATION LIQUID FLOW RATE CALCULATIONS F : 14.73 PSIA PRESS BASE FACT TEMP BASE FACT 14.7311 460 + T~ -~O_____9_o F (1 - BSW)(1 - Shr 601 t440 TANK 'Oo - }t rain D1250 P., o~eum '~'Oo K (I -- BSW) t440 Olc ,'ASTM De,,gnat,on .n 0. F,.-- 1473 .... F-=-- 4~ . oF Og = Fu Fb Ftf Fg Fpv Y%/hw P sepa FU = .024 x ~1 x 520 / METE~ · Qo': ~t m,n roductionTesting Services . ( .... °' us~)me,: ~ ItC. FIELD READINGS DATE 3-21-90 ' CHOKE SALINITY VESSEL OIL OK ' MEAS' t OIL S"n~h~G£ TEMP CHANGE ~ CUMULA? ~E -3~ -.. ":3 CHANGE ~TER CUMU~TNE ~ ~1~ c~E TEMP PRESS TEMP ~ CO: PH~ ~L GRAV:~ COR~ IN OIL FL~ ,h H.C FL~' T~ P~SS S;ZE S~ ~MP C~R G~v:T~ TEMP ~W ~ ~ r :~ ~A~ ~OUNTER RATE - 1~ 14/~ ~ 1~ ~ 1~ ~ 15.3 1~.19 ~:. ,, , ~ g~ 1415 14.~ ~ 114 ~ 1~ 1~ 31.0 i~ 14/~ ~ 1~ ~ ~0 15,4 ~.~ 1~.02 1'418 31.0 ~t.: 0ia:. ~ [ '" 1~ 14/~ ~ 1~ ~ ~8 1~ 31.0 ~ze: ~ 7 in , ~.e~e: 2 7/8 m 1~ ' 14/~ 37 1~ ~ ~0 ~.11 1~.~ 1~1 31.0 ~.: 25 ~: 1515 14/~ 4~ 1~ ~ , .... ~ " ~: ,, ~ ......... ,, , ,, ,,, , , , , , ~ 1tl ABS UNIT ~iC FLYING ~' ~R G~ ), ~ CUMU~TIVE ~P SEP OIL ~&L L~ID G~ WATER CL~ PRE~ ~IF~E OR.ICE G~ ME~ ~ CONV ~E ~MP GRA~ ~PR EXPANS '~ PRESS FL~ ~L ~- ~L G~ IN G~- OIL ~ LIQUID OIL " .... ~E SIZE DIFF. G~VI~ TE~ P~ F~R F~R F~ F~ ~ F~R E~ENS RA~ G~ RATIO ~OLUTION RATIO RAT~ RATIO ~TIO I~er~ ,, , ~O 0 ~ T~ ~ ~u Fb ~ ~ m , ~ V ' ~hw~oa ~ ~1 G~2 GORT ~LR TLGR WO~ ~: P~IG 1N (NH~ ~ PSIA ODJM ODiM O01M ~IM ~M O01M ,~ mODIM M~F~ MMC~ ~F~T~ .... m ,,, ,, ,,,,,,, , , ,,, , , , m mm m, m ~ef t. ...... ,, ~,~~ I ~ , ~ .... ~ 3.068 .... " ~ .... .......... 0,- 50 , ,, :~0 - 500 ' ........... , , , ~: 800 .... ............ , , i , , n: I 667 m S ~ '[ " m m mm m m m mmmm m 'ir ~ize: .... ar t~a.c BIJin: ran~: tandan:lCo~ditionl GAS FLOW RATE CALCU .ATION LIQUID FLOW RATE CALCULATIONS F = Mei'e, K: ¥o .... '~ Cot, Facl,jr Reduct,on Facto, ~ 14.73PSIA PRESS BASE FACT TEMP BASE FACT /14.73~ [ 460 + T,~ -~Oo JO,, ,AST~ ~n 0. Foo 1473 F.o 4~ ,F Og: Fu Fb Ftf Fg Fpv Y~,/hw P sepa FU = .024 x k~/ xt 520 / '~ETE:R~ - Qo - F (1 - BSW)(I - Shr 601 1440 TANK · Oo: K (I - BSW) 1440 O~L ............ De,,gnat,on · PAGE 23 of 41 Servi ;ustomer: (' ( roduction lesting ces TEST #2 FIELD READINGS O~L TEMP CHANGE ~ CUMULATIVE CHANGE WATER CUMULATIVE C-I--4 CLOCK CASING CHOKE TEMF PRESS CHOKE TEMP H~S CO.- SALINITY PH VESSEL OIL OIL MEAS OIL GRAV:TY $--"NKA~'_CORR IN OIL FLOW I~T/~. HzO IN H.-,O FLOW ~A, T1ME PRESS SIZ~ SIZE TEMP COUNTER GRAVITY -'EMP BS & W ~ 60. ~ =~.'"'--O~FACTOR COUNTER RA-'E $,..~. COUNTER COUNTER RATE ~ PSIG IN el:. PSIG IN e¢ PPM aC BSL APl =F % Am ;': ¢:RAC BBL STE/~ BB. BBL BBL~ BB. miorl: ' 1545 14/64 44 OPIC] 1440 31.1 ~: ADJ 1 25 * RO( 3fED C~ DKE (~ 1 5; 3( * S. MEq~AT,P 1600 14/64 42 118 CP]~ 190 6% 59.96 141.69 1419 31.1 M. JOINER - 1615 14/64 40 104 ~ 1399 31.1 D. 1630 14/64 39 98 ~ 200 39.99 142.52 1390 31.1 Nt: m ,. ~emem 9 # ~T, 1645 14/64 39 91 (:PEN ~ 1392 31.1 , - rated Int:_______~~ ,, FI.: 1700 14/64 40 85 ~ 200 19.2 17.:2 60.14 143.77 1382 31.1 in 100© F~ i , , 1715 14/64 40 86 ~ 1382 31.1 ~g Size: '7 in ' ' 7/8 i, 1730 14/64 40 81 ~ 186 i.P. size: 20.15 144.19 1384 31.1 ~Ref: 1745 14/64 40 82 ~ ~. 1383 _31.1 er Depth: tt .... 1800 14/64 40 83 ~ 206 ' 19.99 144.61 1386 "" 31.1 , 1815 14/64 42 90 ~ 206 ......... 1385 31.6 , G~S METERING " , RATIO ~r 1" .... i .... ABS UNIT BASIC FLOWING GA~ SUPER. GAS GA~ CUMULATIVE SEP SEP OIL TOTAL LIQUID GAS WATER ........ CLOCK PRESS ORIFICE ORIFICE GAS MEAS SEP. CONV ORIFICE TEMP. GRAVITY COMPR. EXPANS PRESS FLOW TOTAL GAS - OIL GAS IN GAS- OIL GA~ LIQUID OIL TIME SIZE DIFF GRAVITY TEMP PRESS FAC/OR FACTOR FACTOR FAC1OR FACTOR FACTOR EXTENS RATE GAS RATIO SOLUTION RATIO RATIO RATIO RATIO ete~ ,, , , i , le: ' P~o ~ ~, ~ '~e=. ..... ~.. ...... F= r~ ~ ~v " ~ ' ~,~se~ ~ ' , GOre GO'R~ GORT "' TGLR TLGR ' ' WOR I~IG IN IN H~ , , ~F PSIA ' ' ODIM 'ODIM O~1M .... OOIM ODIM OOlM ,: '~DIM MSCF/O MMC¢' ,~F/STB $C¢.'$T1~ $C¢:,STR sgr-iBBL BBuMM(:;r B8~.'STB , ~leter 1" ~ , ......... .. ~eter ....... le: ..... ' r Run .~,.,.. 068' ' ..... " ....... r III I I I II i I ~'essn ~ ,~: :,., - 50 .... ~ :Pres~ _ 500 ' " . ..... ~e: .... ,, , rRufl ....... _ , ....... '.Press ~ ..I _ .... ,, 800 667 :iuid: ~ol/FL: Static Pm ~an~ ~tandl~dCet~ittom GAS FLOW RATE CALC[ LATION LIQUID FLOW RATE CALCULATIONS : PSIA PRESS ~E ~A~ TEMP ~E FA~ /(460,~.20 ......... 1473 rs: 60 o¢ FpB- F-- FU='O24x~ P~c Jx ............. ----~'~'- TB- 52~- ~ ductionTesting Services (' (: .... o, C~omer: (" ( FIELD READINGS . DATE 3-21-90 TEMP CHANGE ~ CUMU~.TN[ CHANGE W4TER CUMULATIVE G-4 CLOCK CASING CHOKE TEMP PRESS CHOKE TEMP H2S CO- ,~INI'rY PH VESSEL OIL OIL MEAS OIL GRCA['LITY S'"~i"~ CORR IN OIL FLOVV '~&. H:O IN H~O CLOW T{~TAL TIME PRESS SIZE SIZE ' TEMP COUNTER GR.Ia~ ,TY TEMP BS & W ~ 60 ~F ;4k.'"'~Og ~-Ac'ro~ COUNTER RAT~ ~..,. 8=.. COUNTER COUNYEP RATE PI~ C~vf~ Twn Pwfl Ch Tn ~ Qo Go To BSW Go60 Sn~, ~< .0~ oo O~ dtJ0rl: PsiG IN eF PSIG ~N ~¢ PPM ~ BSL AP: -"F ,,, ~ APl % CRAC BBL STB/D 8B_ BBL BBtJO 8BL ~ 1830 14/64 42 96 ~ 197 .., 10% 16.7 19.87 145.02 1399 31.7 ~: 1845 14/64 40 82 ,, ~ 190 , 1397 31.6 ~ ~ 1900 14/64 40 78 ~ 184 ~.17 1~_;r7 1'~c~ H. JO~. 1915 14/64 ~ 70 ~ 1~ ,, _ 1387 31.6 1930 14/64 34 75 ~ 203 _ '~ '~A_R ~n '~R '~A~ '~'~ 1380 31.6 ~AI~ 1945 14/64 34 74 ~ 202 . -- 1.378 m:--_____3* 2000 14/64 34 78 ~ 196 16% 16.7 39.86 ~7:~ l~U ..... 2015 , 14/64 34 82 (P~N lS9 ,,, 13~ 31 9# KCL 2030 14/64 34 83 C~N 182 10% 16,.8 40.03 148.77 ~_%~. ~:__ " 2045 14/64 34 83 c]~ 194 ~ . .. 1385 31,5 ~.: 2100 14/64 34 8~ ~ 203 FI~DING 9,IGHT &INDIN] 10% 17.1 20.2 149.19 1393 31-6 D~:, ~, 2115 14/64 34 76 (:PSN 1~ F~JnST~ .,. 1395 31.5 2130 14/64 33 66 ~ 191 ..i8% 16.6 80.01 150.86 138S 31.5 ~ Size: 7 in 2145 . 14/64 32 60 (P~ 183. 1376 31 ).P.s~ze: 2 7/8 ~, 2200. 14/64. 32 52 (/~ 185 .. 20% 16.8 40.03 151.69 1~9 ~.:___3_5__~ 22~5 14/64 32 50 C~N 207 ' 1367 3t. 5 ~R~: ....... 2230 14/64 32 52 CP]~ 202 N::)~ SI(N CF . 16% 18.6 20.06 1~.11 1369 -.31.5 or~:... " 2245 14/64 31 49 ~ ~.193. ..]~3TS]:C~ .. _ 1367 ,~ 31.4 ~' , 2300 14/64 31 48 C~N 185 ,, ,;, '2O% .17.8 , 39.91 152.94 1361 31.4 2315 14/64 31 46 :(~ 179 , , i , , , · , ,, , ....__~, , , , , , ~ n30 !4/64 31 ~ ~N, ~8~,720% 19.6 40.08 153.77 1359 31.4 , , , , ,, · , ..... GaS I~ ~.1~ ........t I~10 ,~1 · , ~ _ 'lIME S~ZE OIFF GRAVITY TEMP PRESS FACTOR FACTOR FACTOR FACIOR FAC1OR FN~r0R EXTENS ~ GAS RATIO SOLuTiON RATIO R4TIO R~,T~O RATIO " ' ' ' C~ " - ' le; ,, I~,eo cl t~ ?~ Pseoa Fu Fb FI~ R3 , ,r.t~v Y ~ ..'hwPseoa GOR1 GOR2 GORT TGLR TLGR WOR ,PS, IG Ih ~N ~ oF PSi.~ ODtM ODIM ODIM O01M O0tM ODIM ! ' ODiM MSCF/D MMC~ SC¢/~TB SCF/ST8 SCF;STR SCF./BBL ~I~,,.zMMCF BBL.'S'r8 ~ter ........... ..... , , , , .... , ,, , , , , , la%, ,, .... ,, , I, ~ ", i , rRun 3.068 ,, T .... _ i , , i ,,,, ' '~. i , , , ~:~ss 0 - 50 , :Press 0 - 500 ........ . ....... . , , , , ,, , ,,, i ..... ,, , r Run -- _ ., !e:_ , , ~ :Press _ · , ,, , , , · ... 1.667 ' ,, ~ : ~ 2 ~ "' " ..... Lea~e: Mud Wt Sh<X Dm: ~:_ ~.Pr~ ~ Pr ~Tan~ Smnd~Condifion~ GAS FLOW RATE CALCULATION LIQUID FLOW RATE CALCULATIONS F: Me,~.; K; v~ ........ ~ ~!A~2.~ ,s,A P,ESS~,~¢ TE~P~E¢*C~ (14.73~ 460- T,~ 3Qo 3Qo ts: ............... 60 ....... 0, F p~ - ,,7~e FT~ ---- 460. t.~.... ~¢ Qg: Fu Fb Ftf Fg Fpv Yy/hw P sepa FU = .024 x ~/x 520 / ~ETtER. ' Qo ........ At m,n F (1 - BSW)(1 .. Sh, 60) 1440 TANK ' Qo = &~ ....... mmn K (1 - BSW) 1440 wO~ ( roductionTesting Services (] °' OC~O00 ZNC. ~ DATE ~-~ ~:' FIELD READINGS OIL TEMP C-HNGE ~ CUau: ~N~ CHHNGE WATER CUMULATIVE ~ .... ~L~I"-- 4 CLOCK C_~NG cHOKE TEMP PRESS CHOKE TEMP H2S CO.- S&LINITY pH VESSEL OIL OIL f'EA~ O~L GRAVITY 5'4='N~< aGE CORR N OIL~-t.u~ ~-CT.&. ~:C ,1~ .z~, ~'LOV~ TIME P~SS 5~E ~ ~MP COUNTER G~TY ' EMp BS & W ~ ~ F =~ ~TOR CO~'ER RA~ ~'. 55. COuN'EP COUN~E~ RATE ~IG ~ ~ PSIG ~ ~ PPM ~ 8BL AP~ F ~ AP~ :. cR~ 5BL ~T~ BBc BBL 8BL'D in Dia: RAT~ ~S UNff ~lC FL~I~ ~ ~R G~ ~ , CUMU~T~VE ~P SEP OIL ~AL L~D G~ WATER ~ 1 I~ CL~K PRE~ ~IF~E ORatE G~ ME~. SEP C~V ORtF~E ~MP G~ C~PR EXPkNS ~ESS FL~ ~AL ~- ~L G~ IN G~' OiL ~ L~uID ' TIME S~ ~FF G~VI~ ~ PRE~ ~ F~R F~ F~ F~ ~R ~ E~ENS ~ G~ ~ SOLUTION RATIO RAT~ RATIO ~ter .... ~ .... ~ ............... ~R~ 3.068 ...... ~ " ........ 're~ 0 - 50 .......... P~ ~1: hot Dia: 3Uin: anda~lConditiom GAS FLOW RATE CALCULATION LIQUID FLOW RATE CALCULATIONS PSIA PRESS ~.SE FA~ TEMP ~E FA~ _ 1~4.73 ~ _ FU: .024 x /14.73~ x F (1 - BSW)(1 - Shr 60) ~440 TANK · Qo- K - ":~ F,. 4~. 0¢ Og: Fu FD Ftf Fg Fpv Y%,%w P sepa ~/ METER,' ('~'~ ( ~roduction lesting ~ervices (~ ( :^~' ~ °' ~ ~,r: ~ ZNC. FIELD READINGS ' DATE 3-22-90 ] ~...~'J.' ~t,~ ' WELLHEAD HEATER Olt. OR COe~3F.N~a,T~ llETERIICu " H.0 METERING ., OIL TEMP CHANGE ~ I C..A~b.&T'VE CHANGE WATER CUMULATIVE "~'-- 4 CLOCK C,A, SING cHOKE TEMP PRESS CHOKE TEMP H~ CO:- SALINITY PH VESSEL OIL OIL MEAS OIL GRA',/iTvS.R"NK/I,~ECORR IN OIL FLO¥/ ~'"~&_ '":O 'N .;,~.. CL~ TOTA. TIM~ PI:~S.~ ¢~,ZE SIZ~ TEMP COUNTER GI~VITY TEMP 8S & h .,~ ¢3C c ='~ ¢&~?OR COUNTER RATEJ _=~. - . . RATE - I~ Cwn Twe, P~I1 Cl~ Th TSeD ii ........ e: _ ,, ~15 ,,14/~ ~ ~ ~ ~ , 1~ ~ .1 i II ii iii iii i s. ~~T.~ ,~ 14/~ ~ ~ ~ ~ ~ 18.5 ~.~6 ~.~ ~ ~.~ ~ 14/~ ~ ~ ~ 1~ 1~ ~ .2 ~. JO~,,.~ 1~/~ ~ ~ ~ 193~ ~s.o ~.~s ...... ~.~ ~ ~.0 ~. . ..... .~. ~~ ~15 1~/~ ~ m ~ ~ ....... ~ ~.0 ,. ~ 14/~ ~ ~ ~ ~0 1~ 17.3 1~.03 ' 1~.~ 1~9 ~-0 ~:_ ~__... ~: ~ .~ ~ ...... ~ 14/~ ~ 59 ~ 1~ 1~ 17.6 ~.~ 169.74 1~ ~.0 ...... ~ ...... " ~s 14/~ ~ ~. ~ 1~ ...... 1~ ~,0 ~.: O~ 14/~ ~ ~ ~ ~ ~ ~ 17.~ ~,~ 170.16 1~ ~ .0 Oia: in ~ 14/~ ~ ~ ~ ~ .. :- 1~ ~.0 . ...... ~. 1~ 17.2 ~.~ ~ ~. ] ~T~'C 0810 ~ 170.57 1~ ~ .0 ~ S~: 7 in: ' " ' -..~5 , ~4/~ ~ 18 ~ ~ ~[~ 0803 ..... >.~: ..... 2 7/a~:~ 14/~ ~ 10 ~ 1~ ~ ~r~ ~c.~ 170.57 0 ¢ ... h~: ~ ~/~ ~ 4 ~ ~ , ~m ~O~ * .... ¢ 170.~. ¢ ¢ ,, _ . ..~: ,~.~5 ~/~ ~ 4 ~ 1~ ~ ~..... * ~ ~,,~~, 0915 ,r. .. .. . . ,,, ,, 1~ '~ m.7 ,; ~ ~/~ ~ 3 ~ 1~ .... ' 1~ 17.5 19.~ .. ~ 1~-~ 1~ ~.7 ,, , ,, ,' u,, , , , ~ . , ...... ~ ~t~t~ '"~ ~ ..... I .......... kBS UNIT ~ FLYING ~ ~PER G~ : G~ CUMU~TIVE SEP SEP O4L ~AL LIQUID G~ WATER ..........__ __ OlFF, G~VI~ TE~ ~ESS FAiR F~R F~R F~R F~R F~R~ E~ENS ~ G~ RATe ~CU?~ON RA?~C RATIO RATZO ~O ~ter ...... ~ , ~ O ~ ,,T~ .... ~ FU FO ,, ~: .... [ ~tG ~ ,N~ .. o¢ pS~A ~M .... OO~ . oo~ ~lM 0~' ' .'~u. ~ .... ~ M~.~ ~C¢. . . ~T8 'SC~:S?8 SC~'S?~ ' ~ae~ 8S~ ' 88~'S~8 ........ .... .... ~ I i i i , .......... i i ii p i ......... ~A~ .q ~ ..................... : .... "~ 3.068 .......... ~ , II I L III ~ II ~ I ..... e: 0 - ~0 .......... '~ ,, ,, ~ 0 - 500 " ' ' ....... ~ ......... e:,,, .... i i ii ii ..... ~er ,4 ,, , , 'R~ . .. _1 ~ .... .......... ~a~:_ 800 ..... ~: 1.667 ........ ' ...... ~ 2 ....... '' ~, ,, ,, , ,,,, ,,, ~ .... tandardConditions GAS FLOW RATE CALCULATION LIQUID FLOW RATE CALCULATIONS F ':- SC 14.73 PStA PRESS BASE FACT TEMP BASE FACT /14.73~I (460 + T,~.~ .3Qo .3Qo Co,, Fact.J, Ren,c~ .....Facto, ~ FU = .024 x ~,---~-.. t x METER ' Qo= -- F (1 - BSW)(1 - Shr 60) 1440 TANK ' 0o - K (1 - BSW) 1440 .... I~ . -- 14.73 ~' _ 4~,0 - 0¢ Qg = Fu Fb Ftf Fg Fpv Y~.'hw P sepa 520 ! ~1' m~n ..~! m~n D1250 P~,oteum ( (' :tionmesting Services ( (.'GE 27 ot 41 ~ ~ 1-NC. FIELD REAOINGS DATE 3-22-90 ~ ~2 W~..Lt~AD HEATER O(L O~ CONDEN~AI'E ~ H~ ~ O~L TE~ CHANGE ~ ~MUcAT'~ C~E WATER CUMU~T~ ~ CL~K ~tNG CHOKE ~MP ~ESS CH~E TEMP H~S CO: ~klNi~ PM ~E[ ~L ~L ME~ ~l GRAVITY ~'k~ CO~ IN OIL FL~ ~. ":O "N ~:O CL~ ~" Ti~ PRE~ SiZE ~ TEMP CO~TER G~TY TEMP 8S & W a ~ = ;~ ;~C~ COUNTER RATE ~,. ~. COUNTER COUN-E~ ~ATE ~: 1000 ~/~ ~ ~ ~ ~ 1~ 17-2 ~) 1015 ~/~ ~ ~ ~ ~ 17.? 1~.~ 2~.3 ~. ~O~ 11~ ~/~ ~ 3 ~ 1~ 1~ lV.G ~ lV0.~ 1~ ~.2 D. 11~ ~/~ ~ 1~ ~ ~ 1~ 18.3 ~ . lV0.~ 1~ ~.~ 11~ ~/~ ~ 12 ~ 1~ (1155 ~E~G ~ ~~~;) . 1~2~ 2%0 ~ q~ ~- 1~ ~/~ 37 10 ~ ~ 1~ 18.2 11~.?B 1~.~ 1~0 ~.5 ~: ~ 1~5 ~/~ ~ 3 ~ 1~ (1235 ~~'~} ~~ ~ 2~/B~ ) 1~ 24.1 Ft: 1~ 24/~ ~1 3 ~ 1~ 1~ 18.1 ~ 1~.4g ~: ,n 12~ 2~/~ ~1 3 ~ 1~1~ ~.9 ~Size: ~ ? in , ).~s~:~ ~/8~n 1~ 2~/~ ~ 10 ~ 1~ 1~ 18.5 5D.~ 17~.?~ ~: 1~ 2~/~ 3~ 18 ~ ~1 (~ ~ ~) . 1~ 18.1 5~.78 .. ~.~ ,,~: , 1415 24/~ ~ 15 ~ ~7 ..... 13~ ~' ~.5 ' - 1~ 24/~ ~ 10 ~ ~ ,.,. 1~ ~,~ 176,~ 1~ ~,3 14~ 24/~ 35 19 24.0 . ' , , ' ~s~,~ , , ~ .... , ,,, G~ CUMU~TIVE ~P SEP OIL T~AL L~IO G~ WATE~ ~ 1 I I ASS UN~ ~IC FLYING ~ SUeR G~ PRESS FL~ ~AL ~- ~L G~ IN G~- OIL ~ L~UID OIL CL~ PRE~ ~IFICE ~IFICE G~ ~. SEP ~NV ~IF~E TEMP GRA~ C~PR EXPANS ~ E~ENS ~OLUTION RATIO RAT~ RATIO TIME SIZE DIFF G~VI~ ?E~ PRESS F~R r~R F~ F~ r~ F~R ] ~ G~ ~ IN ~N H~ e¢ PSIA ODI~ O~M ~ O~M ODtM ~ ODIM M~F~ MMCF ~F~TB SCF,ST8 5C~;STR SC~SBL BB~'M~ ,, ........... ~er ' ~: ................ .... :, ~ , , rR~ 3. 068 ,, ~ , ~ ' ~: ....... 0 - 50 .~ , , '", ' T- ' ' 500 ~: .... ~ .... eT~ ' . Run , ' , ,, n: ~ .667 ' .... : , , ..................... ~ ~.. ,. p: ~. $ :~rag tL/in: inks: lndardCondition~ GAS FLOW RATE CALCULATION ! LIQUID FLOW RATE CALCULATIONS F = Me:c-, K,: Vo ....... Cot, Fac:,~ Recluc~,~" Fac'J' (14.73'~ (460' T~,<; : 1 4.73 PSIA PRESS BASE F'ACT TEMP BASE FACT FU = .024 x ~,--~¢. / x --520 / ',4ETER, ' Qo F (1 - BSWi(1 Shr 60) 1440 TANK · Qo K (1 - 8SW) 1440 OiL ¢:;~ ,c ~'.,,, _ ~473 ~.o _ 460- - 0¢ Qg = Fu Fb Ftf Fg Fpv Y,v/hw P sepa o ooo c. ( oduction sting ,ervices ( TEST#2 FIELD READINGS ' -- WELLHEAD HEATER O1~ O~ CONOF. N~kTE METERING NlO ~ OIL TEMP CHANG~ 'F?~ ~'r') CUMu.&T,q/~. CHANGE WATER CUMULATIVE G-4 CLOCKTiME~INGpRESSCHOKEsIZE TEMP PRESS CHOKEsizE TEMP H~,S CO.- SALINITY PH VESS~LTEMP COUNTEROILGRAwTyOIL MEAS1EMP OIL GRAVITY S~R!¥K~GEc.t.. ,.'q"O~ CORl:i ~N OIL"'--"~ %~w&. COiJ;'4TEcH'C .~1H20 ;LOW RS & W. ~c 60 ~ rA.?OR COUNTER RATE .C. ~. COUNTER R~I'E I~IG IN ~: PSIG IN, eF PP'M ~c BBL AP: 'F __ ~.. APl ~ CRA: BSL $TB/D 88. BBL ' BSL:D a~,: 1500 247(~4 35 8 OP:Elq 1 98 14~ 17.7 40.3~ ' 177.99 1371 31.8 ~e~. ~ 1515 24/64 35 10 OP:E~I 1335 32.0 __, ~ .... M- JOIN]~ 1530 24/64 36 10 OP:l~q 184 39.82 178.82 1329 :23.7 D. 1545 24/64 35 14 OPEN w~: ,!_-'u.~_ :;5.6 ,,, 1600 24/64 36 10 OP:i~I 204 8~ 17.3 ~.16 ~aed Int: It ,,, ~=t,: .... 1615 24/64 36 10 OP:I~ 1344 2_6 Dia: ...... in l .. 1.630 24/64, 35 14 OI:'EN 198 ....... 19.68 180.90 1360 31.9 7 ~g Size: ,,, ...... 7/8 in 1645 24 35 14 O1:):]~ ........ 13~ 30.4 ).P. Size: va.:.... 25 bm h~: 1 700 24/64 35 15 OPEN 1 84 10~ 17.5 60.0 182.15 1.'~3 -~.1 ,,, er Del~h: tt ' "~,,.. qepm:.. It 1715 ... 24/64 35. 15 OPEN .................... ' 1'~39 31.9 .... ,'"~,~! .... i ,,, , , :, , , , , , , ,, ,, , , , , , , i , , , ,,,,, ~..~.._ , ,, GAS METERINCa , 1 RA130 ,, , , , ,,,, , la[el. 1 ii Ass UNIT BASIC FLOWING GA~ SUPER GAS GA~ CUMULATIVE SEP SEP OIL TOTAL UQUIO GAS WATER ..... CLOCK PRES~ O~IFICE ORIFICE GAS MEA$. SEP CONV ORIFICE TEMP GRAVITY COMPR EXPANS PRESS FLOW 'IOI'AL GAS. OIL GA~ IN C-A~- OIL GA5 LIQUID OIL T,ME S~ 0,¢~ ~v,TY TE.P PRESS ;AC~ ;AC'mR ~ACroR ;ACTOR ;AC~ ;^CrO~ EXT~NS RATE ~AS ~T~O SOLUT,O. .AT,O R^T~ R^T,O ~TIO leter . ~: ........ Pse~ '~3" t~, Ti Pseoa F:u FO Ft~ R3 F~ v ' ." hwPseo, C~ C.-(~ 1 GOR? GOR? 3GLR 'TLGR 'WOR ' P~IG ,IN ~, ~NH:,0 ,, oF PSIA ODIM.... ODI~ ODIN ,, 00tM 'O01M OD,Id ',! OOlU ' MSCFIO MMCr SCI::/STB ' ~-,F;STB SCC:'STR'' ' SC¢¥BBL ,BBL,'MMCF Meter ,1" · ,,, , , ,,, , ,,,, Meter ....... '~ .... , , .', , , Meteff ,.. ..... . .. . :,Ru, 3.068 ' ,: ..... · , ...... i , , , ~:. , ,, Press 0 50 ~e: ...... ~ , , ...... cPressn - 500 ......... ' ...... ~;)e: ........ v .... .... ,,~ ....... ,, ,, , Meter ,: .............. ~r Run .,, ,, · Press ~e:_ cPress ,, , , . -- ~. Total ~ .... ~ 3. ~7 t .... J .... i ..... , ~ 2 .......... ,,, . ._ ..--~-- ............. ~ _ , [ ..... Ruicl: ShoWy $~o~ Dia: Casing Tub/DR Packer Sh~:,,, ¢ H~ 1~: Ran~ 1~: Sb~ndardConditmr~ GAS FLOW RATE CALCULATION ! LIQUID FLOW RATE CALCULATIONS ~ _ ..................... 14 73 PSIA PRESS~EFA~ TEMPBASEFA~ 14.73~ 460 * T. ~ _ .... ]Oo F (1 - BSWt(1 Sh~ 60) t440 TANK ' O,, - AO~,. K {1 BSW) 1440 %: _ 60 ._ 0¢ - 4pB73 FTE: 460.__E~F- ...... ~¢ Og = Fu Fb Fir Fg Fpv yNrhw P sepa FU = .024 x --~/ x ~-~ METE~ · O,~ At m,n At m,,~ ~ PAGE 29of 41 uction lestin§ ervices FIELD READINGS '..L-~-''~- IY'Z. W .EI~LNEAD HEATER OIL OR CONOENSATE METERIN;' !%0 METEmNG C3'~4 OIL TEMP CHANGE ~ CbMI.;,~."VE CHANGE WATER CUMUL,ATIVE CLOCK CASING CHOKE TEMP PRESS CHOKE TEMP H>S CO: SALINITY PH VESSEL OIL O~L MEAS OIL GRAVITY S"~'~'¢'AGE CORR IN OIL ~'LOW ~'"C',t. ~20 tN H.,O FLOW .TrTT.,A. TIME PRESS SiZF SIZE TEMP COUNTER GRAVITY TEMP RS & W ~ 60 'C cA,..'t'.'.'.'.'.'.'."~ r,~,,.,.TOR COUNTER RATE 0,. =__=. COUNTER COUNYER RATE ¢~SIG IN ~ PS~G IN er PPM e¢ 8BL APi :r % AP~ % CRAC BB'.. ST8/O BB. 88,. BSL.,'D 69;. a/J011: ,, 1730 24/64 34 10 ~ 204 60.00 182.15 1336 27.3 ADT ~. ~ 1745 24/64 34 12 ~ 1322 24.8 ~. JOINER 1800 24/64 34 8 ~ 196 12~ 17_5 1K2_1c, lq~o, /7.9 Ira: ', 1815 24/64 33 13 C[:'SN 1340 26.9 · ~,, 9// KCL 1830 24/64 34 ' 10 ~ 180 ~ .40.18 182.99 1370 26.1 , , rt.: 1845 24/64 34 13 CPEN ,, 1340 27.2 Dm:... itl, 14% 17.7 39.86 183.82 1350 31.7 1900. 24/64 34 13 ~ 206 7 in ).R Size: _2_//_~ 19i'5'" 24/64 34 13 (]:EN ..... 1349 22.2 "' .... , , Vol.:. 2.5 ,, , , ~ I:lel: 1930 24/64 34 13 ~ 190 ........ 40.03 184.65 1320 , .,28.1 ~ Depm: ...... tt' . ........ ~p~h: ~: ~ r, , ..... I, , , ,t ....................................... ~ter 1 II kBS. UNIT BASIC FLOWING GAS SUPER GAS GAS CUMULATIVE ~EP SEP OIL TOTAL LIQUID GAS WATER '" ~ PRESS ORIFICE ORIClC, E GAS MEAS. SEP CONV ORIFICE TEMP GRAVITY COMPR. EXPAN,6. PRESS Pf,,O~ TOTAL GAS. OIL GAS IN GAS- OIL GAS LIQUID OiL TIME S~ZE OI¢'F GRAVIT~ TEMP PRESS FACTOR FACTOR FACTOR FACt'OR FACTOR FACTOi~ ~ : EX'TENS RATE GAS RATIO SOLUTION RATIQ RATIO RATIO RATIO '' P~IG IN IN-~,~) " ~ PS'iA ODIM.... 0D~ OO~ ~ ..... OOl~ OD~ :: , r ' O~M M~ MMCI: SCF'~TB' SCF"$~B SCF,'S'rR SC'I~/BBL BBL,'MM~F · , ,, , , , , , , , , ...... ~leter ' ............. , ........ , ......... liteter ...... , ......... i .... }e: Meter ...... ! ............ ~A~T'RT._q ._q'R ........ i ,, tR.. 3.068 ! ..... · -- i J i , , ' , ' , Press ~e:, 0 - 50 .................... :Press_ .:--- o - 500 ....... ' ' el'ink ' ,,, , .... J ....... r Run ,, ~ .... , , : ,, , HI:, , ' .......... ~ ' .......... : Press ......... · .... , te: j / "l"t~ ,,,,, I ~ [ .... To a, 800 ....... ............. ~s2 , i,, ~ """' ' ~--q '" i ,, "' MudWt: Rua: Shol/Ft.: SholDi Casi~ Del Packm'l $~:_ Gas Mea Meter Size:_ Diff. Static ~ranKs Standan:lConditmt= GAS FLOW RATE CALCULATION LIQUID FLOW RATE CALCULATIONS 1473 ' PSIA PRESS ~kSE FACT, TEMP BAS~ FACT / ~ / \ ~c ~s: 60 .¢ F ¢.= .]!72. FT8 : ~520 ag = Fu rb Ftf Fg Fpv Y%'~w P sepa FtJ = .024 x ~_ x. --5~' "~ METieR · Q,,' ~t m,n ' ~t m,n CONO00 NC. ( oductionTestincj Services ( ( .... :~:. DATE ~-~ ~ ~2 FIELD READINGS a..,~...a~,.a.. ~'l '~' WELLHEAD HEATER OIL OR CON~NSATE METERING I~OMETERI~ I OIL :EMP CHANGE ~ CLJM~LATIV~ CHANGE WATER CUuUt.AT'~VE ~r~ ~ 4 ,. CLOCK CASING C~OKI::j TEMPPRESS CHOKE TEMP HzS 00: ~I, LINITYa~4 VESSEL OIL OIL MEAS OIL GRAVITY S~'-* ~,. a,T.,[ C~:~:~ 'N OIL FLOW '03A. ~:O ~N ~zO FLO~ TIME PI:lESS S:~ SIZE TEMP COuNTI::R GRAViTy *EMP ILS & W ".t.."~c C0U~TER ,- ,, ~at~)n: .,, ~000 24/64 33 15 (2[~ 206 16% 17_ 2 4D_ q? 72 , :S. METCALP 2030 24/64 33 13 CP[N 208 41.8 186.36 1330 31.7 ~M. JOINER ;' ...... ' 2045 24/64 32 13 ~ 1361 31.2 ,.. wt:~ ' 2100 24/64 32 14 ~ 184 ,. .... 18~ 17.5 20.05 186.78 1360 27.2 lacement , , , ~:~ 9// ,KC~ 2115 24/64 32 14 ~ 1360 27.2 ,, ~rated Iht: It L, ,..L ~=t.: 2130 24/64 32 10 ~ 208 ~ . 59.9 188.03 1~_'~ ~.8 Dia: in - · , 2145 24/64 32 16 ~ 1355 27.0 7 i. ,, ---¢-- ng Size: , ~.P. size:_~ ' ~ 24/64, 32 12 CPJ~ 195 , ~ 14~ 17.6 39.9 ,,, 188.86 1351 27 Vol.: ,,25 bt~ , ,~ Rei: 2215 , 2.4/64 31 15 ~ i 1350 ~r Depth: tt ...... i ' ~ ,,, [: , ,l: 39.98 189.69 1320 27.1 ~,.~h: It .2230 2_4/64 32 10 Clq~] 1R2 ,~..: , ~t~ , L , , , GAS MEIERING RATIO k~e* 1" ..................... ABS. UNIT BASt~ FLOWING GAS SUPER GAS 'i' GA~ CUMULAT!VE SEP SEP OIL TOTAL LIOUID GAS WA'ER :,,, CLOCK PRES.5 ORIFICE ORIFICE GAS ME,IS. SEP CC)NV ORIFICE TEMP GRAVITY COMPR EXPANS PRESS FLOW TOTAL C~S. OIL GAS IN GAS-O~L GAS klQU~O O,L TIME SIZE DIFF GRAVITY TEMP PRESS. FACTOR FACTOR FACTOR FACTOR RACTOR FACTOR EX'TENS RATE GAS RATIO SOLUTION RATIO RATIO RATIO R~', ~0 ~e~elr 1 Il P~IG Ih ~N ~..0 ~ PS~A 90~M OD~M ODN~. OOIM OOt1~'~ OD~M I~ ODlU U~CF/D M~C~ SCF~STe SC¢~STB ,SCI~ S~R $CFYSBL aCc.'UMW; Be;- ,~un 3.068 ......... . ,, , ~: ,0,,- 50 ~, , ~P~0 - 500 ' " · ..... ~e: ~ , , , ,, deter I FEtlVLU :, ' r Run ,,1 .... dAN 1 9 ~99,~ ,, e: " ~.,.,,~le~ .~-!~ ~ Press 'Nask a 0il & Gas Gm ~s. ,.,...., ............. ,~-. , ..... ,, ~ , , ~ , . ~---,ota~: 800 n: 1.667 .... - ' ..... ' , ,. . o~ ~ ,,,. .., ~tandardCondifions GAS FLOW RATE CALCULATION LIOUID FLOW RATE CALCULATIONS F ~5C ~ PSIA PRESS BASE FACT TEMPBASEFAC~ [14.73~t ('460 + Tsc~ -%0 AQo __ ~473 FTB ~ 520 ] Al m~n ' ~t m~n ............. D12~ Pelroleum '.- 60 0¢ F.. _ 4~. 0F Og = Fu Fb Ftf Fg Fpv Y%;r,w Psepa FU = .024 x ~/ x ',~ETER - Qo: o F (1 - BSW~(1 - Shr 60) 1440 TANK · Oo = K ~1 - BSWi 1440 O~L ~ASTM ( .... (,' roduct::;ion%st;ing Services (' .... 3, 0, INC. FIELD READINGS DATE 3-22-90 & 3-23-90 ..4 CLOC. CASING cHOKE TEMP PRESS CHOKE TEMP H2S CO: SALINITY PH VESSEL OIL OIL MEAS CAL OIL TEMP CHANGE OIL CUMULATN~ CHANGE WATER CUMULATIVE GRAVITY SHRIt',K~E CORR IN OIL FLO~ ~rt&. ~:~' ff~l H ,0 CLOw TOTAL TIME PRESS SIZE SIZE TEMP COUNTER GRAVITY TEMP 85 & W ~,~'T0~ COu;~"=..~ ' ~:)r~'F~'FTI .: 60. F i:&C"rO~ COUN'"ER RATE ~'- ~. COuNTE~ RATE -: ' :7245 24/64 ,,, 32 10 ~ __ 1350 30.9 , ,,,~ 2300 24/64 32 20 ~ 180 1~ 17.6 1330 27.2 , JO~ 2315 24/64 33 ~3 ~ '1337 71,5 2~ 24/64 32 "'15 ~ 200 " _ --. ~# KCL 2345 24/64 32 '12 2400 ,24/64 32 13 O:~ 185 '17.'1 ,,,, ,, , , ~.: 2 7/8 ,. 0015 24/64 32 13 ~ I 1354 31.7 ,¢: _ 0030 24/64 32 ~ 206 ~ ,, ,, i,, , i,, ,, , i,,, ,, i , ,,,. ~d~TIO .......... ¢aA~ CUMULATIVE S~P ~P OIL TOTAL LIOUIO GAS WATER ABS UNFf BASIC FLC~/ING GAS SUPER GAS PRESS FLC~ ~I~TAL CaRS. O~J. GAS iN GAS- OIL GAS LK~UID OIL CLOCK pRESS ORIFICE ORIFICE GAS MEAS. · SEP CC)NV ORIFICE TEMP GRAVITY COMPR EXPAN$ ': ....... TIME SIZE OIFF. GRAVITY TEMP pRES~ FAC1OR FACTOR FACTOR FACTOR FACTOR FACTO~4 : EXTENS RATE GAS RATIO ~.OLuTION RATIO RATIO RATIO RATIO ,, / ,, ,, ,. ........ , , , ? ' , ,, ,,, ,,, , , ,,, ,,, ,,,, ] , , ,, ~ 0 - 50 ..... ................ ~0- 500 "' ' ..... ,,, ~,~ , ,, ~ ' ,, ........ , ,, $ ~__..~_6_6 7 ..... ' .... I GAS FLOW RATE CALCULATION LIQUID FLOW RATE CALCULATIONS F = Me~e, K :- ~ PSIA PRESS~EFA~ TEMP~EFACT /14.73~ 46 T~c ~Oo F (l - BSW)(1 -. Shr 60) t440 TANK ' Oo = o K (1 -. BSW) 1440 OiL [ASTM ~ 0c ~, _ ~473 ~ _ 4~ - ¢¢ Og = Fu Fb Fzf Fg Fpv Y%-fhw P sepa FU = .024 x t.~/x METIER . Q~, = Af m,n A~ m,n mt ' S PAGE 32 of 41 ( (,-- uction sting ervices ( O^ E Customer: FIELD READINGS Oh. TEMP CHANGE OIL CUMU~A'n,~ CHANGE WATER CUM:J'..~Tn/E ~ CL~ ~ CH~E TE~ ~ESS CH~E TEMP H~ CO* ~INI~ PH ~SSEL ~L ~L ~ ~L GRAVIT~ S-~,~K~E CORR ~ OIL FL~ ~. -~O IN '=C r~ TI~ ~ SIZE SI~ TEMP CO~TER ~ TEMP BSSW ~ ~ F ~ ~TOR COUNTER RATE 0,.5~. COONTE~ COuN~E~ RATE W~'~= ~IG IN ~ P~G IN ~ PPM ~ BBL ~ 'F ~ AP~ % CRAC BBc ~ BB~ BB~ BB~D at~: , e: , _ M. 30~ ~ 1410 i · t.: ~ ~: , ,, ~ Size: 7 , ie ~ ,,, , , ).~Size:2 7/8 m ~9 /~ , ,, ~.: 25 ~ . " ~ Ref: ..... ~1 , , , ,, , ,m , ,, ~r~: .... ~ , ~" i~: ~ ~ ...... /~/U il i , , ,I , ~ ' , ~r1 - ABS UNIT ~IC FL~ING ~ ~R G~ ~ CUMU~TIVE ~P SEP OIL ~AL LI~ID G~ ~' ~K ~ O~FICE ~ICE G~ ME~. SEP CONV ORIFICE TEMP G~VI~ ~: ~, PRESS. FL~ ~AL ~. ~ ~ IN G~- OIL ~ LIQUID O~L ' -'E~ENS RA~ G~ ~T~ ~OLUTION RATIO RA~ RATIO ~ ~ DIFF G~VI~ TE~ PRESS. F~R F~ F~ ~R F~ , ~er , , ,, , ,, P~I,G IN ~NH,~ ~ oF , PSIA ~Di~ OD{~ ODIM ~IM O~M ~1~,,, ~ OOIM" ' M~F~ MMCr ' ~F~e ~CF~ST8 , SCF~STP SC~BSL ~8~'M~F Maer 1" ~ ~ ~: ...... , .... i "; , , ~ , , ,, , , ~{, ~ , , , ,, ',:' , ,, i i , ~ ' P~ 1510 ~: 0 - 50 ~: - 500 0103 ,, ,, , , , , , , a~r 01 ~ 15~ ~ .... "- P~ , , ,, ~: ...... miD 15~ ~:,, , , · ~ 0'i13 T~ ! 600 ,,,, ,, , ~,, 1_6R7 ~15 .. 1570 _ ~ , . t~ 2... .. ,, , , Cus Rep Shot/Ft.: Shol Dm: Casing Tub/D.P. {)ill Size:_ H~ Rang~ Type: I:~. Static GasM, Type: $~ze: _ Diff. Ra~ .e,- .,~' ~anKs S~andardCondtt~ OAS FLOW RATE CALCULATION LIQUID FLOW RATE CALCULATIONS F = MET.,, K - vD, ...... 14.73 ~Qo ~Qo .................... ,,:s F,B 4~. ~¢ Og: Fu Fb Fir Fg Fpv Yx~'hw P sepa FU: .024 x · x tSET[~R . Q.,- ......... F (t - BSW)(1 Shr 60! 1440 TANK Oo ...... K Il BSW'~ 1440 ................ ' W - omoo0 ( ( .... oduction I .stino- -- .- -- o -- ." ecvices * FIELD REAOINGS ( ~ DATE 3-23-~ Customer. OIL ~E~ CHANGE OIL ~UMuLAT~ ~ANGE WA~R CUMU~T~E ~4 CL~K ~ C~E TEMP PRESS CH~E ~MP H~ C~ ~LINI~ PH ~EL ~L ~L TI~ ~ SI~ S~ . ~Mp ~TER G~VI~ TEUP BS & W ~ C~ ~ ~ On Tn " ~ ~ ~ ~o e~ G~ S~, - o: a~ ~' ~ ~ Comments aten: m~ IN ~ ~IG IN ~ P~ ~ BBL APl :c ~ ' Ap, ;: cR~ BB. ST~' BB: BBL B8~'~ S~. - 0118 ~: 1 S. ~~.P Ol 771590 M_ .~~ D. nl ~ - 1600 ~T~~ 0129 m: ~ _ 1610 ...... 0q32 , 1620 mt~ Int: ...... ~,.: 0134 "' 1630 3mc in, , 0139 ~ aze: 7 i" 1640 mSize:2 7/R ~, 0143 ~ ~ " ' ' .' 1650 ~.: ,25 ~ ~ Ref: 0148~ ' " 1 660 .......... ~ - . . ~r ~h: ..... ~ ~ 01 56 ......... ~h:, ~ 16~t0 0238 ~ ~ ' ' ...... ABS UNff ~lC FL~ ~ SUPER. G~ ) G~ CUMU~TIVE ~P SEF ~L ~AL L~ID G~ WATER .............. ~ ~E~ ~IF~E~ ~F G~ ME~TE~ PREs~SEP F~RC~V ~EF~R F~MP G~F~ C~PRF~ EXPANSr~ ' E~NsPRESS FL~ · ~AL ~ - ~L G~ IN G~- OIL ~ L~D OIL ~ ~ G~ ~T~ ~OLUTION RATIO ~T~ RAT~ ~T~O ~ IN . IN H~ ~eter 1" ~ ..... ,,~, ..... t~er .... ,,,~ e: ....... , , i .... ,, ,,, 3.068 ........ ~0 - 50 ~ ' ~ '" ~ ,, }, ,, ,. ~ _ 500 .......... ,, ~ ....... ,., , ,, .... ~: ..... ,,, , , .... ,, ,, P~ T~ ~ ' ' !_. 667 " ' '" ~ ~ ~ , ........ , .... affi ~ _ _ _ ,,,, .. Cus~ Rep: FrS PTS Rel Mud Wt: Fluid: Shot/R.: Sba Dia: Oil Meter Oil Meier H~0 Meter Type: Meier R~ Size:., . Diff. Pi~ Rang Gas Ty~e: MmerR Diff. Pn Static Pr VTanks Slam:lard GAS FLOW RATE CALCULATION LIQUID FLOW RATE CALCULATIONS F ~c 14.73 PSIA PRESS BASE FACT TEMPBASE ['AC'~cc,,, ~ac' :~ Reduc~ .... ~:ac~o, ..................... ('14.73~ (460 ? T~ .30o -- _ 460 .oF Og: Fu FbF~f FgFpv Y~.."hw Psepa FU= .024x \ Pst /X . ~s: 60 o~ Fp~ "~ F~- --~- -' 52~" / METER . Q,,~ ........ F (1 - BSW)(1 - Shr 60~ 1440 TAr'~K Qo : ....... K ~1 BSWI 1440 :)ductionTesting Services °' Customer: ~_;3--4 O1~ TEI~ C-ANGE OIL C;J~i.,. ~.T",!~ ~,0 ~A~E WASA CUUU~TNE __ ~ ~ CH~E ~MP PRESS C~E TEMP H~ CO: ~INI~ P H ~L ~L ~L M~ ~L GRAV:TY S"~K~E CORR =% OIL FL~ ~ - ~N ~O ¢_~- ~A~ ~ ~~ TIE ~ ~E S~ TEMP ~TER G~VI~ ~MP BS&W ~*F ¢~ ~AC~ COUNTER RA~ ~.~E. COuNTE~ COUNTER R~ 02~ ~ D240 C~ C31S t'~~ ~(~~ ~ _ ~680 ): 16t;0 ~ ~690 ~. JO~ .... e .... ~T~~ ,,, ~9~ K~~ , ,, , ...... Dm: ~n~ m ............ ~ m 0255 1680 ~ Size: , ? in ~ ..... ', ,,, ).P. si-:~)~ 0303 ..... ~ .... : 1690 mm ~ L m ,,mm~ m mm m h Re~: 03151.700 --? o9o ~ 1700,~ . . "' , , , ,,, ,, ,,,,, , ~ ,, , , , ~ w 0345 ' ~,~ ~ ..... 1700 ' " ..... ~s.,~ ""~ ,I .......... "~ ......... 1" .................... ' " ' ASS UN~ ~IC FLYING ~ ~R G~ ~ CUMU~TI~ ~P $EP Olu ~AL L~ G~ WATER CL~K ~E~ ORIF~ ORIFICE G~ ME~ SEP C~V ~IFICE TEMP G~ ~ EX~N~ PRESS F~ ~AL ~- ~L G~ IN G~- OIL ~ ~UlO O~L ~ SI~ DIF; G~VI~ TE~ PRESS F~ F~R ~ F~ ~ ~F: E~ENS RA~ G~ RA~ $~UTI~ RAT~ RAT~ RATIO ~; ~ d .w ~ 'F; Fb ;U ~ F~ - ~oa ~ ~1 GOR2 ~RT ~LR T LGR W~ ~e, 1" 0400 1710 , .... .............. ~, m m , m: 0415 ........... f ...... 1710 · --- -..-- --, m m ......... ,,,,, , , ,,,, ,Run 3.068 0430 ;;' 1710 , .......... ~ ......... ~ ...... , ,,. - ,,, 0 - 50 04 5 ......... ..... ~ 1710 :~ 0 - 500 ,, , ,,, ,, ,,~ ,, ~ , ,.'- ,: 0500 . ~ 1700 ......... · ~,, , , ,, , , ,, ,.. ~er 0515 ~~ 1700 .. ....... r Run ...... 0530 .......... ~ 1700 ,,, :p~ 0545 1700 .... , ..... k~ 0600 1700 ... ~ = ~67 061 5 ~ 700 ~ ~ ........... ,,,,m,, ' ' "' ' "" ' "' m, ,, Well: _ Ruid: Sh0l/Ft: SNXDm: P~ H~ Rang Rang Static Pn Gas Met, T~pe: Size: Oift. P~ Static Pn S~"~ '1 ~ran~s Star~ta~ C,o~d~t.~m OAS FLOW RATE CALCULATION LIOUID FLOW RATE CALCULATIONS F = M,.? K - ~o ....... 14.73 PSIA PRESS ~E FA~ TEMP ~[ FA~ ~ F ~l BSW)(~ - Snr 60) 3440 TANK ---- ~ .......... _ . . .... lsc 60 oF FPG - ~473 F_ 460 - oK Qg: Fu Fb Fff Fg For Y¥'~w P sepa FU: 024 x N~s~/x~ hqET[~R · O,> il m,n co. oco ( (" I oduct;ionTesting Sepvices ,,~ 35 o. 41 ~er: .. FIELD READINGS (' _ .~TE 3-23-90 , Ol,.. TEMP C~ANGE OIL CL/~ULA*%~ CHANGE WATER CUMULATIVE "I~"'"'4 CLOCK CASING CHOKE TEMP PRESS CHOKE TEMP M25 COt SALINITY PM v~SSEL OIL OIL MEA~ OIL GRAVITY SI'~IINKAG~. COR~ ~N OIL FLO~V ~T~,A_ M20 IN ~20 FLO~, ,'PO'rAL TIME PRES~ SIZE SIZE TEMP COUNTER GRAVITY TEM¢ BS& W .E 60 !: ~:J~-'"lOl= cACTO~ COuNTEP RATE '~'~ 5.._ COUNTER COUNTER RATE WATER PSIG IN e¢ PSIG IN aF PPM ~ BBL APl :F _ ~ AP, ~ CR~ 6BL STB.~ BB... BBL BB;_'D tiOn: , 0630 1720 · , ~ ~ 0645 ... 1720 ~ .'Tn~Z'~ 07001720 ,, ~ ,,, ~t: ..... ~ 0715 , ¢ 1720 , _ ~emm 9// KCL _ 0730 1720 .... ,, =t: 0745 +. ~ 1720 ,,, )ia: in , ,.,,, ~uS~e: 7 i, 0800 i 1720 , , . , , ,.P.S~e: 2 7/8'" 0815 " ' ~ '.... 1720 ...... t ,, , ...... , , ~ , , !, , i , ~ ,Re,: ,, u8 0 ':i 1720 ,,, , , , . ..... ~l:>o~: , ........ i ......... ~ .,.. .... , 0845 ........ , [ ... 1720 ...... ' ' , .... 'i , ..... 0900 ' ' ' ms~,~"i' ' ' ' ~o ' ' 1720 ~- , , , , ,, , ASS UNIT I~SIC FLOWING GAS SUPER GaS GAS CUMULATIVE SEP SEP O~L TOTAL LIQUID GAS WATER 1 tl ............... CLOCK PRESS ORIFICE ORIFICE GAS MEA~. SEP CONV ORIFICE TEMP GRAVITY COMPR EXP/.N$ PRESS FLOV¥ TOTAL GA~ -O~L GASIN GAS.OIL GAS LK~IO OIL TIME SIZE DII:~' GRAVITY TEMP PRES.S FACTOR FACTOR FACTOR FACTOR FACTOR FACIOR EXTEN$ RATE GAS RATIO SOLUTION RATIO RATIO RATIO RATIO ~!' , , , ,,,,, , ,,,,,, ~e: ....... Pseo ¢ .,~" T~ Psel~ Fu "" F~ ~ Ftf R3E For V '.,.hwPseoa ' C~ " GOR1 GOR2 GORT TGLR T.G~' 'W OR 'P~;IG ', " IN ~N H,=,0 oF PSIA C)DIM ' ODI~ O~IM ' OOIM ' C~DtM O~!M .... iI: '" ODIM MSCF,".~. MMCC SC¢:~"'TB SC¢',"BTB SCP,'STR SCF/BBL BBL.,,MMCI: ,,, i '"'"'" "' 1 '" ' ' ' " ~leter 1" 0915 I 1720 ,, , , ,, ~ ..... , ...... ,, ,,,, ~ .... i . .. . ': ..... 0930 i 1720 ~- ....... ,i ' D.~'r_~-c: SrF'_.. - ......... ;t ,, , ,,,,, rRu~ 3.068 0945 ~ ... 1720 _ ~ ..... ' ' ' '" ' -i ~ '" ' ' ~ , ~ 0 - 50 El000 !j 1720 ~; ,,, ; '" :~ss0 _ 500 . .. t .......... ,: ..... 101 5 .. =17~0 ...... , , ,, ,, ~ ...... , .... ~'u" 1030 ..... 1730 .... ¢ i ,, , , "Run , ,, ; ,,, , ........... :- 1045 ....... ; ....... t 730 e: ,, I .... .. p~ss 1100 .... ,, 1 730 , ,, · 1115 1730 ,. - ~.. 800 , ~ ;:-~ , ,~ . ~'?..667 1130 i ~ ......... 1730 __ . . ~ , .~ , , · ,,, ,, , ,,, datdCo~it~n~ OAS FLOW RATE CALCULATION LIOUID FLOW RATE CALCULATIONS F -- Me~.., K :- v<,,u ..... 1'~ ~ PSIA PRESS~EFA~ TEMP~EFACT (14.73~ (460-T.~ ~. ~Oo .... ~--_L ~ ..... FU = .024 x x ~ ~ _ ,,7~ F 4~ 0~ Q9 Fu Fb Fit Fg Fpv Yx'~w P sepa k p~c /~ /~- ME' ER Oo F (1 - BSW~{1 Sh, 60~ 1440 TANK · O~, - ...... K 11 BSW) 1440 O~L oductionTestin§ Services o, ~er: ~ ZNC. FIELD READINGS DATE 3-23-90 OIL TEMP CHANGE OIL 2.U~ U~.ATIV~ C~.IANGE WATER CUMU~T~E ~ ~ CL~K ~1~ C~KE TEMP PRESS C~E TEMP H~S CO: ~LINl~ PH VES~L ~L ~L ME~ ~L GRAVI~ S-~'NK~E C~ ~N OI/ rL~' ~A. "-~ ~ -~ rL~ at~: 1145 1730 ~r 1730 S. ~AT.P 1200 ~ 30~ 121 5 1 730 D. 1230 1730 ~m9~ K~ 12451730 ~ Iht: ~ .... 1300 1 ?3O R.: ~a: in ,~, 1 31 5 ! ?30 ~ Size: ? in ' ' , ~.~: 2 7/8 in ~ 330q 730 ~.: 25 ~ ,, ,,, i ~h: ~ ...... , 14001730 , , . ~, :i ,, .,, . C ..... .... ........... ~ 14151 . ?, . 1730' . .. ' ' '" " ' G~ ' .... ~, 1,i ABs UNIT ~ FLYING ~ SUPER G~ CUMU~TI~ ~P SEP OiL T~AL LIQUID G~ WA~E~ ~K PRE~ ORIFICE ~IFI~ G~ ME~ SEP CONV ORIF~E TEMP G~ ~PR EXPANd. { PRESS FL~ ~AL ~- ~L G~ IN G~- OIL G~ LtOUIO , . ~E SI~ DIFF. G~VI~ TEMP PRE~. F~ F~R F~ F~ F~ F~R ~ E~ENS ~ G~ ~T~ $OLUTI~ RATIO RATIO RATIO ~er , , ~ i ~ GOR2 GORT ~LR ~L~ WO~ ...... ~ 1" !430 ,, 1730 , ~~ ~, , , ......... ~R~ 3.068 1500 ~ 17~u ,, , , 're~ 0 - 50 ~ 51 5 ' , ,1730 .... e: .... , , =P~ 0 - 500 , . e: ...... 1 530 , 17~ , ...... ~k , , ,, , , , ,,. .......... 'Ru~ 1' 600 1730 p~ 1615 ~. 1720 . ~ IIII 1630 1720 ,, ,, ,, ~: ~ :667 1645 .... ,' ,~720 2 , [ ......... iZe: 0~,. ~g IL/in: mdaftlCo~itions GAS FLOW RATE CALCULATION LIOUID FLOW RATE CALCULATIONS F = Co,~ Fact,j, ReOuc1,.,.~ Facto, ~n .c J~'~. = .]_~7_3_ ~__ = 460 . of: Og = Fu Fb Ftf Fg Fpv Y\/hTM P sepa FU = .024 x~, .p.. l x~ 520 / METEB - C)o = .~t m,n F (t - BSW)(1 - Shr 601 t440 TANK ' Oo - \ .... ............. ( ,on lestincj ervices ( ( °' ~ ' DATE 3--2.3--90 TEST //2 FIELD READINGS OIL TEMP CHANGE OIL CUMULATIVE CHANGE WATER CUMULATIVE V" G-"4 CLOCK C~SING CHOKE TEMP PRESS CHOKE TEMP H~S ~ SALINITY PH VESSEL OIL OIL dF. AS OIL GRAVITY $.~,Nv,/~ CORR IN OIL FLOW ~3tk H~O IN ,~) FLOW TOTAL TIME PRES~ SIZE SiZE TEMP COUNTER GI~N1TY rEMP BS & W ~ 60 :F F~."TOR FACTOR COUNTER RA]~ 01~ BB. COUNTER COUNTER RATE WATER BSL !~ ~t~ c,~ x~ ~,~ c~ Th ~s~ Oo ~ ~o eSW ~ SM ~ O~ ~ O. a. H"]~ Comments ~ IN ~ PSIG IN el: PPM ~: ~ AP! fl: % APt ~ ~'RA~ BSL STB/D BBL Formam: 1700 1720 Lease: cu..er 1715 1720 M.JOINER 1730 1720 D. 1745 ~ 1720 ,, , Sma-i: 1815 17'20 ,,, ¢~: 7 m ~ ' ' 'i'' ' ~m~11~.S~ 2 7/8 m 1845 : " 1720 , ~ ~,, , i ,, ,,, IN~ ~P,~: 1900 ,, ', ,, 1720 - 1915 -~-~. ~-.'~ I:. :i .. 1720 ' '' t , i .......... , , , -- , ........... 1 93O ',L , ,, 1720 ~'i '~r ...... ~~ ,,!, ,I -~ ' "" Oilla~' 1" ........ ~ t " ............. CLOCK PRES8 ~ ORIFIC[ GAS MEAS. ~ CON~ ORIFICE TEMP. GIR,~TY COMIC. n,~. ,~,~F~X"~'"'~! PRESS. FU3W TOTAl. GA~ - ~ GAS IN C_.~e~- OIL GAS UQUI0 OIL TIME S~ZE DIFF. GRAVITY TEMP. PRES,& FACTOR ~ FACIOR FACTOR ~ EXTEN$. ~ ' GAS ~ ~:)LUTION RATIO ~ RATIO RATIO OilMe~ .... i ..... P§l(~ '" IN , IN l.~0 '' , ' eF , P~IA ,, O01M ~ O01U 'O01M ' 0DIM 0OlU{ .... OOlU I~ ' MMCF ,~"TS SCF, STB' SCF,STB scr-~6L eSL/MMCF ~'~ 1" 1945 1720 , · ~ ~ ............. ~, , ..... , , s~, ~m, 3 068 ' I ~.~.~'~'~': ~. ........ I I I I I II Ill I Ii ' ' ' ~' 0- sa 2o30 ~ .-,~.-??..-:~ ..... ~. ..t ~720 ' .-:~ C': :!-: ..~:, ~' '" ' ....... 0 ,, 500 :2045 I i~, '-..~i'. il 1720 · . 1~: ......... : .... 1720 t~'~ ,, , ,~:- 2115 ..... . '1720 s~c~ 2130 ,, 1T20 P~q~ll:, _ ~( " '~t:. 800 " ~ I, 667 2200 ...... i ........ ,, ~ ~ , , ,, ,, , $tanda~d~ OAS FLOW RATE CALCULATION LIOUID FLOW RATE CALCULATIONS F = Me~e, K = vo,~m" Co~, ~ t4.73 ~SIA P~£SS SASE FACT TE.PB~SE~ACT /14.73N [~0 + T~ .~a~_ ~ I: - BSW)(~ - S~ S01 ~440 TANK 'Qo - %- 60 °~ FP~B -- ~473~c F TE -- 460-~ Qg = Fu FD Ftf Fg Fpv YN/hw P sepa FU = '024 x \ P~c / x \ 520 / M£TE8 ' Q°=i Aim,r, ( uctionTesting ,ervices (' °' INC. 'bATE 3-23-90 & 3-24-90 FIELD READINGS ' ' WELLHEAD HEATER OIL 011CONI)EN,~TE IdETEf';ING ' ' H,O III[TEllING OiL TEMP CHANGI[ OIL C.:JMU~ATIV[ CI'~&NGI[ WATER CUMULATIVE .,-4 CLOCK CASING CHOKI[ TEMP PRI[SS CHOKE ?EMP -.,S CO: .~I-L ;NI ~'Tv PH VESSEL OIL OIL MI[Ac ~-FCi i,~ TIMI[ PRESS StZE. SIZE TEMP COUNTER GRAV~TY TEMF , ""~ 9/t KCL 2315 ~ '"' 1720 , .... ... , ,, , 1 '.S~e: 2 ,,,,,7/8 i.: 2400 i 1729 I~'~: ~! ............. ~' ,, 0030 1720 A88 UNIT ~AS~C FLOVflNG GAS SUPER G~S ·I GAS CUNIULAT~VE SEP SEP OIL TOTA:. UOU~D GAS WATER I l! ...........CLOCK PRES~ ORIFICE ORIFICE GAS MEAS. SEP CONV ORIFICE TEMP GRAVITY COMPR EXPANS :: PRESS FLOW TOTAL GAS. OIL GAS IN GAS- OIL GAS LIOUtD OiL TIME SIZE DIFF' GRAVITY TEMP PRESS FACTOR FACTOR FACTOR FACTOR FACTOR FAC'OR EX'TENS RATE GAS RATIO ":.OLUTION RATIO RATIO RATtO RATIO ............ ' ,0~0 MSC~ MUCr SCF~?B SC~,S~B .... SC.~;ST~' ' scr~BsC 86~..~C~ 1" ~ ' 1'720 ' .............. , , 3.068 ,, 0115 ......... ' .......... i ' 1720 '' ,, ' ,, 0 - 50 0'130 ..... 0 - 500 ..... "'' ~ ' ..................... ..... ...... , .... O230 1720 ,~,,, 0300 ,, .~ ,, , '1720 ,, , ~lCondilions GAS FLOW RATE CALCULATION LIQUID FLOW RATE CALCULATIONS F = Me,er K 14.73 PS~A PRESS~SEFA~ TEMP~EFAC7 /14.73~ 46 Tsc ~ ~Oo JOo (ASTM .n o¢ F~. -- ~73._ FTR = 4~.~- oF Qg = Fu Fb F(f Fg Fpv YN/hw P sepa FU = .024 x ~/ x , METER · , °= AT mm F (1 - BSW'(1 - Shr 60~ 1440 TANK ' Oo: &t m~n K (1 - BSW) 1440 OIL ('* duct. ionTesl:ing Services ( ~' PAGE, 39 ~! 41 ;us~omer: ~ :L~C. DATE 3-24-90 '2DS'2 //2. FIELD READINGS Oh. *EM~ CHANGE OIL SUMU.A'rV~. C'dANGE wATER CUMULAT,'VE C----4 CLOCK CASING CHOKE TEMP PRESS CHOKE ,"EMP H~S CO- SAUNtry PH VESSEL OIL OIL ~IEAS OIL GaAV:TY S~'~,'~A3ECOal= ~N OIL FLOW ~'~'.-'_ w,.,C =f~ H.C' cLOw TIME PRESS 5~ZE SIZE TEMP COUNTER GRAvIT~' "EMP 8S & W .; 6,~ : ~:~"L2-' =a, CTC,~COUNTER RATE .%..-..5. :OUt, TEn COUNYEa a~rE 0~5 ~r D. ~ , i ,, ,, ,, , ,, ~ ' " . ' . ........ ~S~E~ ..... ..... ,, . ' . ~,~ ' G~ CUMU~TIVE ~P SE~ OiL ~AL LtOUtO ~ W4TE~ ARS UNIT ~IC FLYING ~ SUPER G~ ~ PRESS FL~ ~AL ~-~L G~ IN GAS. OIL G~ ~UIO OiL ~ 1, Il ~K ~E~ ~IFICE ORIF~ G~ ME~ SEP CONV ~IF~E TEMP GRAVI~ C~PR EXPANS ~ E~NS T~E S~ OWF G~Vl~ TE~ PRESS FA~ F~ F~ F~R F~ ~P ~., RA~ G~ ~T~ SOLUTION RATIO RAT~ RATIO ~: p,~tG , ' ' ~N ~N ~,~ , '" oF ' PSIA ODIM ODIM ODiM, , ~M ~ ODIM" ~. .... O~M M~F~D ,MMCF '~F~TB ~FiS~S S~F'S~R SCF~BL 86L. M~= 88~'S~B ,, , ~' .... rR.. 3. 068 ..... , , , ..... ,,, Tank ,,, , ..... ,, 07~ ~_ , ..... ..... ~: 800 .ease: ~:8/R.: ~e: , ~ag BUin: ~n~' tandardCondit[ons GAS FLOW RATE CALCULATION !, LIQUID FLOW RATE CALCULATIONS F = ~ ,- (..~ ,~ ( Cot' ~:sc,',r ~e,'uC, .... ~: ~CTO, 5C -------.1~.~7~ PSIA PRESS BASE FACT TEMP BASE FACT 1 73 460 +Tsc'~ -~Qo --~Qo ~ASTM .~ nc ~-~.__ !~73 I~'__._ 460-0F Og: FuFbFtf FqFDvY,,;hwPseoa FU='024x -- x c-~'c; · VlETERi: Q~,= ,' .... F (1 - BSW)(1 -Shr60) 1440 TAt'~K'Q~-- ~- ..... K (1 - B.c;W~ 144¢) O~ (' :)ductionTesting Services ( ~2~ ~r:, DATF ~T fl2 FIELD READINGS ~.... ~4 CL~K ~NG C~KE TEMP PRESS C~E TEMP ~ COt ~LINI~ PH vESSEL ~L OIL ME~ ~L GRAVITY C~ =NOIL Ft~' T~. ":0 t, -:0 FL~ e: M. JO~ ~9~ K~ ~ [ ~: in ), , 1015 Size: ~ ~n ' ' ,[',,~, ~ m , );~si~: 2 7/8i. 10~ :: . 1 ~: 1~ ~] 1~' ,, ~,, ~r~: " ......... ~ .... ~ 1115 11:22 ~~mR ;~ ~m - ~~F m : , , , J ~ I Il A8S UN~ ~lC FL~I~ ~ SUPER G~ ; ~ CUMU~T~VE ~P SE. O~L ~Ac U~ G~ .............. ~ PRE~ ~IF~E ~IF~E G~ ME~ SEP C~V ~IFICE TEMP GRAVI~ ~PR EXPANS ~ ~ESS FL~ ~AL ~- ~L G~ tN G~, OIL ~ LIOUID O~L TIME SI~ OlFF G~VI~ ~MP PRESS F~R F~R P~R F~R F~R ~ ~ E~ENS RA~ G~ RAT~ SOLUTION RATIO RAT~ RATIO , ,,, , , ' ' ' P~tG IN iN ~ ~ PSIA ODIM ODIM ODI~ ~IM ~IM ......OD~M ~M"" M~F~ MMCK ~F~B SCF,STB SCK'SYR ~R~BL BGL'M~F iii ii i ii ii i i i ii i jl i ........ i ~11 i i i u i) i lU 1" ~1~ .... , ....... .,. ~r m [ , , ,, , ,, , ): rRun 3. 068 ~ ..... ,: ........ ........ ~ i i ,, i ~r~O - 50 ~5 ' ~: .... ,,, :P~ 0 - 500 ,, ~m ,,,, m m, , ~r__ ~ 2~ ~ 'Run m ~:, 800 mm ~: ~ ~7 ~5 ,,m ,, ~ , ,, ,,, IL:in: inKS' tr~m~lC0od:ilions GAS FLOW RATE CALCULATION ' LIQUID FLOW RATE CALCULATIONS F = PSiA Co~' Fac~ .~, Reduct;~,'~ Facto, .... PRESS SASE FACT TEMP BASE FACT / ~k(14.7~)/{460 + Ts;)~ JOo F (~ - BSW)(1 -- Shr 60) 1440 TANK 'Oo AOo ~*ST~ 60 0¢ F~o- 1473 F.~_ 4~-*F Og: Fu FbFtfFgFpvY~/hwPsepa FU='024xk~txk 520 / METE~ 'Qo Xtra,, - , .... K(1 - BSW)1440 OiL ............ ~ .............. ( ( oductionTesting Services ("E41 ~! 41 ~ m ~ INC. DATE R-24-90 'l~..~'r '#~- FIELD READINGS .... - WELLI'4EA0 HEATER O~L O~ CO(~tOENS&TE Ilm~i~.~G -- H~) METERING . OIL 'E~ CHANGE Olt C~MuLAT~f~ ~ -C C~ANGE ~TER CUMu~T~E ~ CL~K ~ING cH~E TEMP PRESS CH~E ~MP H~S CO: ~LINIh PH VE~L ~L ~L ~ ~L GRAVITY S"R~%~E CORR ~N OiL CL~ ~A. · TIME p~ ~ SI~ TEMP ~TER G~ TEMP ~['& W ~ ~ c :~ ¢~ COU~TER RA~E ~'.B~ ~OuNTE~ on: ~ 1400 .., , , ,, 1415 S_ ~T~ - D. ~ T~ A~ .... ~ 9~ K~ 1~ , 1515 ,., . a: in m 15~ Size: _, 7 i~ .... ~ ..... mm ,, m m , m . .m .,, .... ~m m mae m ~ Size~ ~ 1~ m~ ' ~l ..... 4.: 25 ~ , ,, -~ L , ,, ~ _ 1~ .......... ~:, ,, 1615 )~ ' , ~ .......... (, ,, ...... ~su~i~ , ~ ..... ~ . .. er1II ASS UNIT ~IC FL~I~ ~ SUeR G~[ ~ CUraTIVE ~P SEP OIL ~AL LIOU~ GAS WATER CL~K PRE~ ORIFICE ORIF~E G~ ME~ SEP C~V ORIF~E TEMP G~ ~ EXPAN3 . PRESS FL~ ~AL ~- ~L G~ IN G~- OIL ~ L~UID OiL ..... TIME SIZE DIFF G~VITV TEMP PRESS. F~ F~R P~ F~R F~R ~R ~ E~ENS RA~ G~ RATIO SOLUTION RATIO RAT~ ~ : , ' ~lO IN )N ~ ,,, ' ~, , PSIA .... OOIM O01M , ,, DDtM '~M ~M ~tM, ':~' , ,'O~Mm ,, M~F~O MMCc , ~F~T8 SCF~S~B ' SCF:STR ~ 1~'" ~e 1,,, 1~ .......... ~ ........ .... ~-q ~ ........ ~ , , ~ ....... 1~5 ....... ~un 3.068 ~ ............. ,,,, ,, , ~ 0 - 50 ~ ...... ' , , , ,, , ' [ , ~ 0- 500 ~7~ ...... I ' ~ .... , ~ ..... ,,, ,~ ..... ~ ,,, "" 1~5 " , ~ ...... '1~ , ,,, ~'~a(~~ 1~ .......... ...... , ,,, ~667 1~ ..... ..... ,, , , ,, rdComNtio~ GAS FLOW RATE CALCULATION LIQUID FLOW RATE CALCULATIONS F = M¢~, K = ¥o.~ ..... Cot, Factor Re(~uci,,,~ Faclo~ 1 4.73 PS~ PRESS ~E FA~ TEUP B~E FACT / x/14.73)/[460 + TscIx AOo F (1 - BSW)(1 - Shr 60) 1440 TANK 'Oo = ~0o K ~1 - BSW) 1440 OIL ~n o, F.~= ~473 FTB -- ~ ' oF Og = Fu Fb Ftf Fg Fpv YvXhw P sepa FU = .024 x ~/ x. 520 / M:ETi~R . ()o= Al m,n A~'-~,~ ................... ~ASTMDi2~ Pet,oleum ad u ction Te Ssting ervices (''GE 1 FIELD READINGS DATE W .EI~4EAD HEATER OIL OR CO~40£NS&TE METERII~G H~O ~ OIL TEMP CHANGE OIL CUUULATNE CHANGE WATER CUMULATIVE G -- 4 CLOCK CASING CHOKE TEMP PRESS CHOKE T£MP BH~ HT~7, SALINITY PH VESSEl. OiL Oil. blEAS OiL GRAVITY S~R~N'~,tG£ CORP ,N OIL =LOW ,u'rOT..: H.-,O !N H;C FLOW TIME PRESS SIZE SIZE · TEMP COUNTER GRAVITY TEMP BS & W =AC:r3'r~ ' .: COUNTER d: MII.~TE POINT ~: so ~ ~ACm~ CCUNTE.a ~ATE, _ .. 3'~ se. cou,~£~ R~E ,~TEa · . . Pbn Cwn T., Pwfl Ch T~ Tseo Oo Go To ,, esw c~o s~,= ~ oo :~ o, ~* Comments PSIG IN ~ PSIG IN ~.~ I:,PM %c . ~BL APl F % APl % I:RAC '3~L ST ~-'D 9EL SCL Bat./O na~n: 1 950 TOTkL TDST2Z) LINES TO 1 200 PSI ~e: DIAL SW¼ 2031 80 0 (1~ 176 1800 ~0.0 OIL F~ ~ I~TE CUM. H20 MLUID .~.rM~JOy 2039 8/64 80 200 C[~ 176 1800 ~0.0 .. ~ ~ B20 ~ :~k't'P[m]',,T~ 200 PSI SITP; 2100 46 8/64 51 122, (1~ 176 1752 ~0.1 0 0 ON 8/64 CHOK~ D. C~S~ 2130 58 8/64 39 1~5 ~ 178 1739 ~0.1 ROCF,~Z CHO~: ._~. 1.3 1.3 62.4 1.3 B S & W · M. OOIN2~R 2200 73 8/64 3~ 10 (1~ 180 1760 N/~ 21 50 ~ U~ SI ROT DO ~N 100 rf~ ,c~T. 2.5 2.5 120.0 3.8 % ~OIL % H20 % SOLID~ 2205 40.1 RL~ 2I) PL~ T,P 980 I~M: ~acemem 2210 35.0 DDC~ SDD [] ~RT~, ..... ~: . 2230 89 8/64 33 720 (1~. 177 1762 3~.9 ROCKI~ G CHO] ~ 0 0 3.8 0~ate~m: ~ ~ 2235 10/64 INC, ( HOKE ' .~ 1 0/ ;~ ..... ~Ft.:. 2300 116 10/64 26 300 (1~ 176 1681 3~.9 ROC~ CHOt~', ~ 1.6 ~.1 196.8 5,~ 2.5 7.9 ~0 59.4 .6 PIPE DOP~ tole: in 2330 165 10/64 24 240 (/::]]N 176 1674 34.9 INC. C HOKE ' ~Q 12/ i4 : 0.5 4.6 220.8 5.9 6.6 4.1 12.5 10 89.8 .2 PTPE DOPE 2400 214 12/64 24 230 ~ 178 1666 34.9~ 0.1 4.6 220.8 6.0 11.1 4.5 17.1 1 98.9 .1 PIPE DOP*F i,xjS~ze: ~" 0030 250 12/64 24 230 ~., 170 1667 34.9 INC. £HOKE ",~D 14/.~4; B]',FD CASfNG TC 98 0 5.0 240.0 6.0 16.1 5.0 22.1 0 100 TRACE , D.P. Size: in 0100 144 14/64 23 90 ~ 174 1646 34.9 ~ ..! 0 5.4 259.2 6.0 21.5 5.4 27.5 0 100 TRACR ,~.: ~ bU 0130 180 14/64 25 109 (/::5N 175 1647 34.9 INC. CHOKE '..'O 16/' i4 . 0 4.6 220.8 .6.0 26.1 4.6 32.1 0 100 - TRACR, m~ef: .... ~0200 220 16/64 25 86 ~ 169 1637 34-9 ~ CASING TO 10~); GAS TO SIRFAC~ @ 022) 0 5.0 240.0 6.0 31.1 5.0 37.1 I~, 100. TRACE... ~erOepth: " 0230 130 16/64 . 25 155 CEN 178 1626 34.9 INC. £ HOKE '. ~ 1 8/' ~4 i . . 0.3 5.8 278.4 '6.3 36.6 5.5 42.9 5 95 TRACE. --apth: " .0300 155 . 18/64 25 41 (/::'EN 174 1619 34.9 i!~.. 0,3 6.3 302.4 6.6 42.6 6.0 49.2 5 95 TRACE, . 0330 180 18/64 25 44 ~ 171 1622 34.9 INC. C HOKE. , 'O 20/' i4 . . ...... 0.4 7.5 . 360.0 7.0 49.7 7.1 56.7 5 95 TRACE. 'i/..~ LNG M0~ ~ ; 1 0.2 3.8 182.4 7.2 53.3 3.6 60.5 5 95 TRACE. ~,or 0400 220 20/64 26 31 ~ 177 1620 34.9 50K PI: M/8.7 H';O W' ."./PH 7 ;~},~:~,: ~T',.*UC. ~ nn , , ......... ,, , . ! T)TAL DIESEL PRODUCED ~etef 1 Il ARS UNIT BASIC FLOWING GAS SUPER. GAS ! GAS CUMULATIVE SEP SEP OIL TOTAL LIQUID GAS WATER '.' CLOCK PRESS ORIFICE ORIFICE GAS MEAS, SEP. CONV. ORIFICE TEMP GRAVITY COMPR EXPANS'i PRESS FLOW TOTAL GAS-OIL GASIN GAS.O~L GAS LIOUIO OIL 6 BARRELS AS OF 0200 TIME SIZE DIFF. GRAVITY TEMP PRESS. FACTOR FACTOR FACTOR FACTOR FACTOR FACTOla [' EXT, ENS, RATE GAS RATIO SOLUTION RATIO RATIO RATIO RAT)O ~e~er ' OIL STARTING TO SURFACE ge: ...... ~seo d ~. Tc~ Pseoa Fu , , Fb I Fff Fc~ For ¥ 'i .- hwPseoa C~ GOR1 GOR2 CORm TGLR TLGR WOR P$1G IN IN H~0 oF PSlA ODIM OOlM OOtM O01M ODtM ODIM ~i ODIM MSCF/D ;~,',C= SCF,$TB SCF/ST8 SC~:/STR SCFtaBL ,,88L~,MCF t38b'ST8 Meter. 1" 't 'I TOTALS PRODUCED Meter / DIESEL OI~ H20 ,, ge: ,, 6.0RR]',~c: 1.2RRT~q 53.3] Meter DANI]~_,S ,. ,,, , , !rRun 3.068 Press 0 - 50 ", i ~e: ............... ,, ' ! ......... I t , , , , , , , , , , , , · i I : Press . ~:,, " 'i t ~,~ rotat: 800BBL n: 1.667 ,,I .... Ruid: Casi~ Tub/D.P. P~ Ra~ Size:. Rang Type: Size: ,, Diff. Slam $~ ?y~e: Meter R~ Size: Static BBUin: ~anks: Standard Conditions GAS FLOW RATE CALCULATION LIQUID FLOW RATE CALCULATIONS F = Meter K = Volume Corr. Factor Reduct,on Factor Psc __ !4.73 PSIA PRESS BASE FACT TEMP BASE FACT ('14.73~t 460 + T~ct AOo F (t - BSW)(1 - Shr 60) !440 TANK * Oo - -~Oo K (1 - BSW) 1440 O~L (ASTM Des,gnat,on T.,~. ¢;n °~ F.e -- 14.73oo FTS -- 46o..~- OF Qg = Fu Fb Ftf Fg Fpv Yx/'hw P sepa FU = .024 x %,~/x 520 '/ METER. * Qo - At rain At rain f)~-)¢.~ p .... , .... (f (¢ ::)ductionTesting Services (-- o, s C~o~r:, CC]NCX/), INC. 54 90 FIELD READINGS DATE WEL,=LHEAD HEATER O~L OR CONDENSATE METERIN~ .~0 METERING ~-~'[ ~ G - 4 o,t OIL CHANGE Cb,OL,;~ ~ CH,NGE WATER CU,U~T~E ~ P~ SIZE SI~ TEMP C~TER G~VITY TEMP BS & W :a~ ' - z MI~ ~I~ ~ ~o ~ ~ "*~ ;"~' ~ OIL H20 ~ Cwn T~ ~h C. Th T~O ~ Go T~ 8SW Gc60 Sh,I ~ O~ on -;~ ~ ~ 1~ ~/~ ~ 31 ~ 1~ 1~ ~.9 ~C. ~ 22/64 0.3 5.8 ~.4 7.5 ~.8 5.5 ~.3 5 ~ ~. ~T,T~ ~ 1~ ~/~ ~ ~ ~ 1~ 15~ ~.9 0.3 6.2 ~.6 7.8 ~.7~ 5.9 ~.5 5 95 ~. ~T,T~ l~r D. ~JOY ~ 1~ ~/~ ~ ~ ~ 1~ 15~ ~.9 ~C. ~O~ ~ 24~64 ... 0.3 5.5 ~.0 8.1 69.9 5.2 ~,0 5 95 ~ 1~ 24/~ ~ ~ ~ 1~ 1~ ~.9 0.3 5.8 ~.4 8.4 ~.4 5.5 ~,8 5 95 ~. SOLI~ .D. ~~ ~ 1~ 24/~ ~ ~ ~ 1~ 1~ ~.9 ~C. ~O~ ~ 26~64 I .16 5.8 ~.4 9.6 ~.0 4.6 ~.6 ~ ~ ~. SOLT~ . M. JO~ 0~ 170 ~/~ ~ ~ ~ 1~ 1~ ~.9 ~ 0.3 5.8 ~.4 9.9 ~.5 5.5 ~.4 5 95 . 1 ~LT~ m: ~ 0~ 1~ 26/~ ~ 18 ~ 1~ 1~4 ~,9 ~C, ~0~ ~ 28~64 0.3 6.3 ~.4 10.2 ~.5 6.0 101,7 5 95 . 1 SOL!~ ~ 1~ ~/~ 26 16 ~ 1~ 1~5 ~.9 0.3 5.0 2~.0 10.5 ~.2 4.7 1~.7 5 95 . 1 SOT,!~ ~ace~nt ~: ~ 1~ ~/~ ~ 18 ~ 1~ 1~ ~.9 INC. ~O~ ~ 30 ~64 0.4 7.5 ~.0 10.9 103.3 7.1 114.2 5 ~a,~m,: " 0~ ~ ~/~ 26 14 ~ 1~ 1~ ~.9 0.7 6.7 3~.6 11.6 1~.3 6.0 1~.9 10 ~ . 1 ~T.!DS ~R.: ~ ~ ~/~ 26 14 ~ 1~ 1~1 ~.9 INC. ~O~ ~ 32~64 0.7 6.6 316.8 12.3 115.2 5.9 1~.5 10 ~ .2 SOLIDS :Dia: in 1~ ~ ~./~' 26 15 ~ ~ 1~ ~,9 1.4 5.4 ~9.2 13.7 119.2 4.0 1~.9 ~ 75 . 1 ~LIDS ~,gS~z,: ~n~ ~0~ ~ 32/~ 26 16 ~ ~ 1~ ~.9 INC. ~O~ ~. 34 /64 .... 1.4 4.6 ~.8 15.1 1~.4 3.2 137,5 ~ 70 . 1 SOLIDS ' 11~ ~ ~/~ 26 13 ~ 76 1535 ~.9 ............. 2.3 5.8 ~.4 17.4 1~.9 3.5 143,3 ~ ~ . 1 SOLIDS ~.~Size: ~ .11~ ~. ~/~ 26 17 ~ 70 1~ ~.9 INC, :~O~ ~ 36 /64 .... ~ 3.0 6.7 3~.6 ~.~ 1~.6 3.7 1~.0 ~ 55 .1 SOLT~ .~L: .bb~. 1~ ~ ~/~ ~ 17 ~ ~ 15~ ~.9 .... 2.7 5.4 ~9.2 ~.1 132~3 2.7 155.4 ~ ~ -,1 SQL/DS ~ef: 1~ ~ ~/~ ~ 17 ~ .... ~ 1518 ~.9 ~C. ~O~ ~ 38 ~64 ..,. 2.~ 5.9 ~.2 ~.0 135.~ 2.~ 161.3 ~ ~ . 1 SOLT~ ,r~h: " 1~ ~ ~/~ 26 17 ~ ~ 1512 ~.9 ~ 2.~. .5,0 2~..0 ~.55 137.7 2-~. 1~,3 51 49 . ! SOI,T~ ~.,~h: ~ 13~ ~ ~/~ ~ 17 ~ 1~ 1510 ~.9 INC. ~O~, ~ 41 ~64 . . 3.4 6.7 ~.,6 31 ,~ 141.0 3.3 1~.0 51 49 . 1 SOT,TDS .. 1~ ~ 41/~ ~ 14 ~ 1~ 1~ ~.9 2.~ . 5.4 ~9.2 ~.6 143.8 2.6 178.4 51 .49 11 ~T,T~ i~i~ 1~ ~ 41/~ ~ 14 ~ 151 1~1 ~.9 INC. ~O~ ~ 44~64 ' . .3.1 6.2 ~7.6 ~.7 .146.9 3.1 . 1~.6 ~ ~ . 1 SOT,TDS ..... ~S METERING . . ~T~ ..... ~ 1 ~ AgS. UNK ~IC FLYING ~ SUPER GAS ~ GAS CUMU~T~VE SEP SEP O~L T~aL ~ LtO~;D GAS WATER : C~K PRESS ~IF~E ORIFICE G~ ME~. SER ~NV ORIFICE TE~ GRAVI~ C~PR EXPANS ~: PRESS. FL~ T~AL G~-OIL S~IN S~-OIL GAS UOU~D OiL TIME SIZE DIFF. G~VI~ TEMP PRESS. F~R FAiR F~R F~R FAVOR F~ ~ E~ENS RA~ GAS RATIO SOLUTION RATIO~ RATIO RATIO ~TIO leter ~e~ ~ .w Pseoa Fu '~ ,, Fb ~ F~ ;~ ~ ~, ~nw~e~a ~ GO~ GO~2 GORT ~L~ TLG~ WOR ~2 ~tG', I~ .... IN ~,~ :T~ ,' PSIA ODIM ODIM ODIM ~IM O~M ' 0Dt~ ' ODIM MSCF/D M~F , SC~8 ' SCF~ST8 5CF'~B SCF/BBL BBL,~ 88USTB , . ~er I" · .. . .. .~ ~er , ... M~er · ~A~JT~.q ....... ~ ,,. :~R~. 3. 068 " - '' . .............. ~: 0 - 50 ,, .' : Pre~ i ..... ~ .. ~e:, 0 - 500 t I [ i,,, , I ~ ~ ...... 800BBB ~.. Jtai: ~: 1.667 s: 2 ,, , , , , , , Lease: Cus Fluid: Casing oel Sm: 1~: Rang S~ T~: ~ter ~n~: BBUin: StandacdConditions GAS FLOW RATE CALCULATION LIQUID FLOW RATE CALCULATIONS F: Meter K = Volume Corr. Factor Reduct,or~ Factor Pst 1 4.73 PSIA PRESS BASE FAC7 TEMP BASE FACT ('14.73'~ 460 + T~c'~ AQo F (1 - BSW)(1 - Shr 60) 1440 TANK · Qo - 2Qo K (t - BSW) 1440 O~L (ASTM De.,,gnat,on rsc ............... 60__ OF Fpe - 14.73~ FT8 -- 460~n ? OF Qg = Fu Fb Ftf Fg Fpv Yx/hw P sepa FU = .024 x ~ Psc / x 520 / METER ..: Qo- At rain Au rain 01250 P~,~o'~.. .... . ( .... oductionTesting Services (] (' °' s Customer:_ FIELD READINGS DATE ,, WELLHE&D HEATER OIL OR CONDENSATE METERIN 3 H~] METERING · C~OCK CASING CHOKE TEMP PRESS CHOKE TEMP SALINITY VESSEL OIL OIL MEASI OIL GRAVITY ;.. Cj?0F. CObNTERI RATE · MILNE POIN/. ~ :.~. T.~ ~,, c~ T~. ~o oo ~ '~ .~ ~s*,, ~ ~.~,~ ~ o~. :° '~' ~'i OIL H20 PSIG ,~ '~' PSIG ~N 3F ~'PM -"F ~BSL APl c ..... ! ~; AP' o-. =~AC '38L STB:D {)BI. 58~. Bla~ a~: 1500 200 44/64 30 12 ~ 155 1502 34.9 BLED lzI~ING~TO 80~ P.$I .... 2.8 5.4 259.2 40.5 149.5 2.6 ! 190.0 51 49 .1 SOT,TDS F:r['AL 1530 44/64 13 152 1500 34.9 ! 3.8 6.3 302.4 44,,3 1~52.0 2.5 1~)~,~ 60 40 .1 SOT.Tr')s ~. M(/,'NTJOY 1600 80 44/64 30 13 (PB~ 150 1489 34.9 INC. 1-1~ ID_ 4R/64' . 3.2 5.4 259.2 47.5 154.2 2.2 201.7 60 40 .1 SOT,TT')S 1700 70 48/64 32 13 (PEN 157 1489 34.9 6.3 10.5 252.0 53.8 158.4 4.2 212.2 60 40 . 1 SOLIDS D. CASSO - 1800 60 48/64 33 12 ~ 15~ 1AR1 34_9 INC. ~.--'qOKE_TO 54~ 64 . 6.0 10.0 240.0 59.8 162.4 4.0 222.2 60 40 . 1 SOLIDS M. JOINER 1900 50 54/64 31 14 fPEN 155 1472 34.9 INC. :~OS'R ~ 59~ 64_ _21.4 84 20.0 6.5 10.8 259.2 66.3 166.7 4.3 233.0 60 40 . 1 SOLIDS wt ~ 2000 40 59/64 30 1,,5 (PFN 152 1477 ?,4_9 ~ INC. (/HOKE [~) 64'/64 6.9 10.4 249.6 73.2 170.2 3.5 243.4 66 33.9 .1 SOLIDS 2100 20 64/64 29 15 ~ 150 1481 34.9 INC. {ERTZ TO 36. 5 21.6 81 20.4 6.1 8.7 208.8 79.3. 172.8 2.6 252.1 70 30 TR. SOLIDS acement - 2200 20 64/64 27 14 ~ 150 1483 36.5 INC. [ERTZ TO 38 7.6 10.1 242,4 86.9 175,3 2,5 262.2 75 25 TR. SOLIDS ,~ed~r,: "~ 2300 15 64/64 26 15 ~ 151 1467 38.0 INC. tERTZ TO 40 21.5 82 20.2 7.0 10.0 240.0 93.9 178.3 3.0 272.2 70 30 TR. SOLIDS ~=L:_ 2400 15 64/64 26 14 ~ 153 1459 40.0 61K[5:M INC. HEP, T: TO 41.~ 7.8 11.2 268.8 101.7 181.7 3.4 283.4 70 30 TR. SOLIDS Dm:_ in 0100 15 64/64 26 15 fPSN 149 1437 43.0 INC. I{53:~Z TO 45 ...... 7.6 10.8 259.2 109.3 184.9. 3.2 294.2 70 30 TR. SOLIDS 0200 30 64/64 26 22 (PSN 148 1434 45.0 INC. ] {ERTZ TO 4 7 20.8 88 1 9.2 8.1 11 . 3 271 . 2 117.4 188.1 3.2 305.5 72 28 TR. SOLIDS ~g Size: in.. 1 ~ 0300 i 40 64/64 26 22 (p8~ 150 1413 47.0 INC. ]{ERTZ TO 48 .. 10.2 11.3 271.2 127.6 189.2 1.1 31~,~ 90 10 TR. SOLIDS ).P. Size: !9 0400 60 64/64 27 19 ~ 149 1408 48.0 59KP[:M 21.8 88 20.2 8.6 10.8 259,2 136,2 191,4 2.2 327,6 .... 80 20 TR. SOLIDS ~ Ref: ~r Depth: ~ tt ......... _:,epth:_ . ft , I ~ ..... ~ , , , ,,, , , , , , irlltOr , ' ...... c~s a~.,~ ,, ', ~t~i ' , R~T~O , , , eter 1 ' ~es. uNrr s~s~c ~LOWING G~ SUPER G~S I ~ CU~U~T~vE SEP SEP O~ TO~ CtoU~O ~S W^TER CLOCK PRESS ORIFIC~ ORIFICE GAS MEAS. SE~ CONV ORIFICE TEME GRAVITY COMPR EXPANS,~ PRESS FLOW TOTAL GAS -OIL GAS IN GAS. OIL GAS LtoU~[~ OIL ~ ' TIME $~E DIFF. GRAVITY TEMR PRESS. FACTOR FACTOR FACTOR FACTOR FACTOR FAO'OR , ~' EX'rE NS RATE GaS RATtO SO[.L:~ON I:IAT~O ~A?~O RATIO i , , , le: P$1G IN' iN H~0 OF PSIA ' 'ODIM ODIM ODIM OOIM OD~M ODI~ i OD~M MSCF~D M~C~ SCF,'STB ' SCF. STB SCF~STR $C~'SBL 88UMMC , ,, , , , ,,,, ,, .~ , , ,, , , , ,,, ~le~er 1" ~ , ,, ,,, ~ ,,,, ,, , .'!~' , , ...... , rRu, 3 068 '~' I ' ...... .. , !: ,1 t 50 i soo ' "' i I t e: ....... ,l "' ~ I ~ ' ' . Press t -r I " -~ ....... Cu~ Rep: PTS Rep: ! FrS Rep: Dq Fluid: Shot/Ft.: Sho{ Dm: Casing Tub/D P~ ¢ Size: ~ Size: H~ GasMe~ T,~: Size: Rang Rang Type: Diff. Rare,e: BBL/in: #Tanks: Standard Conditions GAS FLOW RATE CALCULATION LIQUID FLOW RATE CALCULATIONS F = Meter K. = Votume Co~r Fac:or Reduction FacTor P~c 1 4.73 PS1A PRESS BASE FACT TEMP BASE FACT /14.73~ 460 + T~ ~ ~Qo F (1 - BSW)(I - Shr 60) 1440 TANK 'Qo - AGo K (1 - BSW) 1440 O,L (ASTM De.~,gnat,on Tsc ....60 oF FpB-- ~,73¢~ FTB -- 460~?n- oF Qg = Fu Fb Ftf Fg Fpv YV'hw P sepa FU = .024 x %, Psc / x 520 / METER :: Qo- ..%t min -%t min D1250 Petroleum ( o, ( ..... ( .... 'oduct;ionmesting Ser, vices OgNOCO, [NC. DATE 5-5-90 Cu.~o~r:_ FIELD READINGS ,, ~ WELLHEAD HEATER OIL OR ~.3~iDEI~-~TE ME'I'ERING., H~ METERING · 'P~M ' I OiL TEMP I'~or'~j~T...s OiL C~aL~t',E ~ANGE WATER CUMU~TNE ~ -- 4 CL~ ~ CHOKE TEMP PRESS CH~E TEMP H~S CO- ~LINI~ PH vESSEL ~L OIL MEAS OIL GRAV;TYj S-~'N~E COR~ =L~ ~:. '-3 ~'-O CL~ T~E ~SS S~:E SI~ ' TEMF CO~TER GRAVITY 'EM~ BS & W ~ ~ = F~ =~C:OR ~ ~TE 2. ~_ COu~TE= CC?~YER ~ATE ~TEn B6L ~20 ~ · ~ ~ ~ 70 ~/~ ~ ~ ~ 1~ .... 12,5 10.5 ~.0 1~_7 2.0 ~_0 J 193=4 ~: ~ ~ ~/~ ~ ~ ~ 1~ 131 ~~ ~ Tt~: gl 12.9 10.8 ~9.2 157.5 2,1 ~.4 J 1~.5 16.0 3~.0 , '~[ ~OOY 07~ ~ ~/~ ~ 32 ~ 1~ 0 ~ 1~ 15.0 13.8 ~.2. 1~.3 1.2 ~.8 1~.7 8.0 ~.0 ~ ~ ~/~ m 32 ~ 176 1~ ~~ ~O~ ~ 4(J/64 12.5 11.1 ~.4 1~.4 1.4 ~.6 1~.1 11.0 ~.5 .1 D. ~~ ~ ~ ~/~ ~ 33 ~ 1~ 1~ ~~ ~ ~ 4( /64 12.9 12.8 ~7.2 1~.2 0.1 2,4 1~,2 0.5 393.4 .1 SO~ZDS N. ~O~ 1~ ~ ~/~ ~ 37 ~ 181 ~ ~ ~O] ~ ~ ~0/64 1~ ~,0 110 19.9 10.8 10.6 ~.4 ~.8 0.2 4.8 1~.4 1_4 4~_2 ,1 ~T,T~ 11~ ~ ~/~ ~ ~ ~ 1~ 151 11.7 11.1 ~.4 ~6.9 0.6 14.4 1~,0 5.0 415.9 ~: .. ~ 10.8 10.5 ~.0 ~7.4 0.3 7.2 1~.3 3.0 426.7 ~. SO~ZDS a.mnl ,1~ ~ ~/~ ~ ~ ~ 1~ 147 ~~ ~o~ ~ 2~ /~4 · 1~ ~ ~/~ 31 55 ~ 1~ 1~ ~~ ~O~ ~ 2.~/64 11.3 10.8 ~9,2 ~.2 0.5 12.0 1~_~ 4.0 4~.0 ~,~: , 1~ ~ 24/~ ~ 82 ~ 157 0 1~ 139 10.8 10.3 247.2 2~.5 0.5 12.0 ~.3 5.0 ~.8 1~ ~. 24/~ ~ ~ ~ 1~ 1~ ~~ ~O~ ~ 2.~/64 11.3 10.4 2~.6 ~.9 0.9 ~,6 ~1.2 8,0 4~.1 'Ft.: 10.4 10.3 247.2 ~9.2 0.1 2.4 ~1.3 1.0 470.5 ~. SO~Z~ Dia: ,_ in 1~ ~ ~/~ ~ 1~ ~ 1~ 1~ ~ ,4 1~ 19,1 ........... 10.4 10.2 2~.8 ~.4 0.2 4.8 ~1.5 2.0 ~.5 1~ ~ ~/~ ~ 1~ ~ 157 132 ., . . ~s~: ~" !~ ~ ~/~ ~ 1~. ~ 1~ 1~ .~ 11.2 10.9 ~1.6 .~-3 ~ 0.3 7,2 ~0,8 3,0 492,1 ~, SO~[DS msize: in 1~ ~ ~/~ ~ 1~ ~ 1~ 1~ 21.8 92 11.3 10.6 ~,9 ~,9 0.7 16.8 ~2.5 6.0 ~3.4 ~. SO~ZDS v~.: bb~ ~ ~ ~/~ ~ 131 ~ 1~ 135 10.0 9.4 ~.6 310.3 0.6 14.4 ~3.1 6.0 513.~ ~- ~~ ~ ,, , , , , ~ ~A ~/~ ~ 13~ ~ 1~ ~ 135 ~ 10.4 9.6 ~.6 319.9 0.8 19.2 ~3.9.. 8.0 5~.8 ~, ~DS "~:~ ' " ~'~15 J ' S~ ~ [~-~C~T,~ ~m ~ 8.0 .1 SURDS er ~th: ff ~ ' ' ' ' ~26 ... S~ ~ ~~ (B~ ~4 HOT,~ RI]IT.r-Ira1 ........ ...... I , , ' , ......... ,intor ~ F~I~;~ ~ ~I]~ ~ ~,T, . j .... '" ~S M~ ~ ~Ni~ ,, ~T~O ..... ~ ,, ,, , , , , , ,, , , ( ,, , , , ~ I Il ABS. UNff ~IC FLYING ~ SUPER G~ ~ G~ CUMU~TIVE SEP SEP OIL T~AL LIOUID GAS WATER ' CL~K ~ ORtF~E OR1F~E GAS ME~ SEP C~V. ~IFICE TEMP G~VITY COMPR. EXPANS PRESS FL~ T~AL ~- OIL GAS IN GAS- O~L GAS MOULD OIL TIME St~ DIFF, fi~VITY TEMP PRE~. F~ FAiR F~R FAiR FAiR FA~0~ ~ E~ENS. RATE GAS RATIO SOLUTION RATIO RATIO RAT{O ~T~O taer ' " ~ ~Pse~a _~' GOR1 GOR2 GORT TG~ R TLG R WOR le: , ~ ~ .. T~ ~a ~ ~ ~b ~" ~ ~ ~ ~ .... ' ~ ~Z ~IG IN IN ~ =F PSIA 'ODIM ODIM ,0DIM ~IM O~M ~O~M OOlM MSCF/D MMCF SC~TB SC¢~ST9 SC[;STR 'SCr, BBL BBUM~F 6Bb$~, , ~er 1" 0~ ~ .~ 9 ..~4 70 ~.~ .~4 113-5~ .~ 1.137 i 1.~3 1.~2 1.7.~ . ~.5 2.~ ~6.1 1~ ~.9' 0.19 1~ ~-0.. ..... aete ~ ~ .~ 9.5 ..W4 ~ 35,7~ .024 113.5~ .~9 1.137 1.~3 1.~~ 18.~4 ~ 55.6 4.59 214.5 1~ ~1,9 .. 0,19 1~ ~: ....... 0~ ~ .~ 11.5 .~ 101 35.7~ .~4 113.5~ .~ 1..~ 1.~3 1.~ ~.~1 .... ~.7 7.~ 1~.2 163 ~.2 0.~ 1~ . ~.0 ~ter ..... . D~~q . ~ ~. .7~ ~ .~ 103 35.~ .024 1-13.5~ .%1 1,~ 1,~3 1.~ 26.732 W.4. 10.~ ~.5 ~. ~1.9 0.13. 1~ ~,0 ~ ~ .~ 19 .~ 118 ~.~ .024 113.5~ .~ 1.~ 1.~3 1.~ .~.~ 73,4 13,4 ~.9 ~ 41~.3 0.~ 1~ . ~.1 rRun 3.068 1~ ~ ~.7~ ~ .~ 1~ ~.~ .024 113.5~ .~ 1.~ 1.~3 1.~ 26.355 75.1 16.5 ~.2 ~ 3~7.5 0.02 1~ ~.0 .... 0 - 50 11~ ~ .7~ ~ .~ 124 ~.7~ .024 .!13.5~ ,~ 1,~ .1,~3 1-~ ... Press 26.3~ 74.9 19.6 ~1.~ 35%,7 0.05 47,9 ~: .......... ~ 1.~ 26.355 75.1 ~.7 ~.0 ~ ~ 3355.5 0.03 1~ ~.0 :Press0 - 500 1~ ~ .7~, ~ .~ 1~ ~.7~ .02~ 11]'5~ .~ 1.~I 1.~3 ~ .,, ~:_ 1~ ~ ~.7~ 19.5 .7~ 115 ~,.~ .024 113.~ .%1 .... !.143 ~1.~2 1.~ 26.024 ~.5 ~.9 ~.0 J ~ 3~.5 0.~ ....1374 ~.1 . ~Ta.k 1~ ~ .7~ ,, 15 ,7~ 1~ ~.~ .024 113.5~, .~9 1.143J 1.~3 1.~)3 ~.~4 ~.6 ~.8 2~.5 ~ 2.65 ~3.5 i 0.~ 1~2 47.9 [ " ~t~, 1~ ~ , .7~ 15 l .7~ 1~ 35.~ .024 113.5~ .~7 1.1~ t 1.m3 1.~13 ..~.151' 69.4 31.5 ~.0 j ] J35 .51 1~3 ' 47.8 .......... i rRun 1~ ~ ].7~ 15 .7~ 1~ ~.~ .024 113.5~ .~9 1.143 1.~3 1.~3 ~.~4 ~.5 .,~.4 2~.1 ~ 274 ~.8 0,~1 1~ ~.1 .. 17~ ~ ~.7~ '~ 15 , .7~ 1~ ~.~ .024 113.5~ .~ 1.1~ 1.~3 1.~3 ~.~4 ~,6 ~.3 ~.2 . ~5 3~.5 ~ 0.02 1~2 ~.1 ,es, ' '0.0 ~: ...... '1 ~ ~ ........ :Press 1~ ~ .7~ 16 .7~ 1~ ~.~ .024 113.5~ .9~ 1.1~ 1 .~3 1.~,3. ~.5~ 70.6 ~.0 2~.0 2~ ~! .0~ 0.07 1~ ~.0 ?... ~ ~ ~.7~ 16 .7~ 112 ~.~ .024 113.5~ .~ 1.1~ 1.~2 1'~ ~.5~ 70.4 ~.9 312,1,I ~$ ~.0 Q,~ 1~0 47,9 , ,, , , ~'-k ~ ~ ~ .7~ 16.75 .7~ 112 ~.7~ .024 113.5~ ' .953 1.143 1.~2 . .1.~ 24.119 72.0 ~.9 313.6 ~ ~,0 0.~ 1372 47.9 , k ~,~. 800BBL .......... ,, i ,, , ' ' '"' "t ~ " ~ ....... ~ ~ ... Rep: Mud Wt: D~spli Fluid: ShoqFt.: ShotDia: Casi~ Tub/D.P. Oel Packer De 4 OiiMeter ,Size: R~ng Su~J Mete: Difl, BBL,'in: ~tandard Conditions GAS FLOW RATE CALCULATION LIQUID FLOW RATE CALCULATIONS F = Meier K = Volume Corr. Facto~ Reduction Factor ~c 14.73 PS~^ PRESS BASE FACT__ ~4.73 TEMP BASE FACT_ _ sepa [14.73'~ (460520 +'~¢'~! \t'~Q° F (1 - BSW)(1 - Shr 60) t440 TANK 'Qo - -~Qo K (1 - BSW) 1440 O~L /ASTM --I~'pB ~. --F-""'TR 460_~. oF Qg = Fu Fb Ftf Fg Fpv YyZhw P FU = .024 x \~/x METER '.: Oo - m;~ ' ~ .... 60 O~ C (' oducr_,ionTestincj Services (" s C~o~er:CC~CX:~ INC. FIELD READINGS DATE 5-5--90 WELLHEAD HEATER OIL OR CONi~NSATE M£iE~NG H~ METERING ~ -- ~ CL~K ~ING TEMF PRESS TEMP CO. ~LINI~ PH ~L ME~ ~L GRAVITY CORP ;NOIL FL~ ~=. ~-C '%':0 =L~' ~AL TIME PRESS ~ ~ ~ ~ COUNTER ~ TEMP SS&W a ~ F :~= FAVOR COUNTE= "ATEJ 3:.5~. CgU~TE~ C~t?~= =ATEj ~: ~ ~ ~16 l~0) ~% l~ ~ 1~ ~ I ~18 1~ ~ 1~ ~0 D. ~ ,,~ ~19 1~ ~59 1~ ~15 ~ 1~ ~2 1~ ~ 15~ ace~nl · . .... ~ 1~ ~3 15~ ~ 1~ ~a~ ~n,: " D 24 1~ ~ 1~ 2~ 1 ~ ~ ... ~Ft.: ~ 1~ ~ 1~ ~15 1~ , Dia: in ~ ~ 1~ ~ 15~ ~ 1~ ~, ,. ~ 1470 ~7 15~ ,,, ~, 1570 , ~Siz~: I ,., ~.~ Size: _ i. ~ ~ 1~ ~ 15~ 0115 1570 ~,~ .... ~.: ~u ~ 14~ ~0 15~ 01~ . 1~ /.~ ........... _ ~ ~ ~ 31 1 ~ ~ 1 1 ~ 01 ~ 1610 erich: fl ~ i m1~ ~2 1~ 0~ 1~ ...... m ~ 1~ ~3 1~ 0~5 1~ ' ~h: fl ..... - " D~ 1~ ~4 1~ 0~ 16~ , , , ~Or ~35 1~ ~5 1~ , 0245 16~ ~ 1" UNIT FLYING ~ I GAS ~ G~ CU.U~TiVE SEP T~AL GAS WATE~ ORIFICE G~ UE~, CONV TEUP GRAVITY EXPANS FL~ T~AL G~- OC G~- OIL cIOu(D OIL , CL~KTtME PRESS ~ DIFF G~VITY TEMP. ?~ ~ T~~ ~ RA~ GAS RATm T~ RATIO B~ FAiR FAVOR FAVOR F~OR ~eter le: ~eo C ~ , , T~ ~eDa ~ Pb F:f ~ F~ Y ~, ~ nw~eoa G~ GOR' GOR2 GO~ TGL~ TLGP WOR ~IG tNm IN ~=0 m OF PSIA ODIM O~IM ODIU ~M O~M ' Oq)M ~' ODIM MSCF!D , , MMCF ~F/~8' SCF/~T5 SCF!STR m SCFFBBLm BB~;M~F ~e 1" ~ 1~ ~6 1~ 0~ , 1~ 11~ 1~0 . ', , , ~' ,, ........ ~ter ~37 1~ ~7 1~ 0315 '~ 1~ 11~ m , , ie: ~ 1510 ~8 1~ ,0~ 1~ 1~ ~ete~~S ~ 1510 ~1~ 1~ 0~ ~::~ 1~ 1~ ~m , '' i~ ' ' 3re~ 0- 50 ~ 1510 ~ ) 15~ ~ ~: 16~ ~ 14~ ~ 1~ I re: .... , .... ,, , ~ 1~ ~ ~ 14~ :Press 0 - 500 ~43 1510 ~ ~ 15~ ., ~5 :' , . 1~ i 'r~s ~ 49 1 ~ O~ "~ 1 ~ 1 ~ 1 ~ Pr~ C~ Rep: Oispl~ Fluid: Shot/Ft.: Sho~ Casing Pi~ Rang, Size: H~M~ Rang, Gas Mete Typo: Diff. Pn Ran§ Rang Su~ Ty~: Meter Run Size:.,, Diff. Rang, $~ic Stol DEL/in: .¢l"anks: Standan:lConditions GAS FLOW RATE CALCULA¥1ON LIQUID FLOW RATE :ALCULATIONS F = MeTer K = Volume Psc uu14.73PSIAoF _PRESS BASE FACT _TEMP BASE FACT_ __ FU = .024 x [14.73~ x (460 + T ),( i% -%00 F ' - -%t'%O0min Col, Fact,.), fAsTMReduct'°n Factor 460 ,- OF Qg = Fu Fb Ftf Fg Fpv Y%/hw P sepa ~,'-~c / (1 - BSW)(1 *- Shr 60) 1440 TANK Oo ~A FpD 14.73 FTe 520 METER~' Qo -%t rain . K (1 -- BSW) 1440 O)L -- -- D1250 Petroleum Cusa~m~: CO~OODt INC. , DATE 5-8-90 FIELD READINGS WFN LHEAO HEATER OIL 0~1CONOENSATE YETERING H~ ~ I E~ II ~ -- 4 OIL CHA~E ~L CUMULAT~ CHA~ ~R CUMu~T~E CL~ ~ING c~E TE~ ~ESS. C~E TEMP H~ CO= ~LINI~ PH vE~EL ~L OIL ME~ ~L GRAVITY S,a,~E ~~ ~NOIL rL~ ~. ~:O ~H~ rL~ ~L ~ ~ ~ S~ TEMP COUNTER G~V'TY TEMP BS&W ~ ~ F c~ (~~1 COUNTER RATE 0'L~ COUNTER COUNTER RA~ ~TE~ PS~ IN ~ ~ IN ~ ~M ~ BBL APl F ~ AP~ :: c~C BBL STUD BBL ae~ 86UD ~5~ ~t~: , , t~r D. ~JOY ~15 ~C/~ ~OZE ~ ~ O~ ~ 16/~ ~ ~ ~ 1~ P~ 5~ D~~ D~ ~~ & ~ P~ ~ ,:D. ~ 16/~ ~ ~ ~ 170 A. PHILIP: ~ 16/~ ~ ~ ~ 170 ~~G ~~ ~ '4.1 4.1 98.0 4,1 1~ 4,1 ~:_ , ~ 16/~ ~ 24 ~ 1~ 2.5 2_5 I~_R 6_6 1~ 6.6 0~ ~ 16/~ ~ ~ ~ 1~ 7.9 7.9 3~.0 ' 14.5 1~ 14.5 ~nt 0~ ~ 16/~ ~ 61 ~ 1~ 7.1 7,1 ~1.0 ~.6 1~ ~,6 ~m: " ~ ~ 16/~ ~ ~ ~ 1~ ~ 6.7 6.7 3~.0 ~-~ ~t.: ~ ~ 16/~ ~ ~ ~ 1~ ~ . ~ 6.7 6.7 ~,0 ~,0 1~ ~,0 IOia: in ~ ~ 16/~ ~ 81 ~ 1~ INC. C~O~ ~ 20/ ~4; I~C- ~'z~ 5~-~ 8.3 0.4 19.2 0,4 7,9 3~.0 ~.9 ~ ~.~ ~ ~ ~/~ ~ 1~ ~ 1~ INC. C~O~ ~ 24/ ~4: S~T,T, A ~ ~F ~ 7,5 0.7 ~.6 1.1 6_R _q26_~ 49_7 i~S~e: in 8.8 0.9 ~.0 2.0 7.9 ~.0 57.6 ~ 59.6 ..... 1~ ~ 24/~ ~ 1~ ~ 1~ TNC. C~O~ ~ ~R / ;~ 9.RSize: i9 10~ ~ ~/~ 31 ~ ~ 1~ ~ 7.5 3.75 1~.0 5.~ 3.75 1~.0 61.~ ~ ~.1 ~. SOT,T~ ~.:. ~' 11~ 1~ ~/~ 31 114 ~ 1~ INC. C~O~ ~ 32/ ~4 ..... ~. 7.0 3.5 1~.0 9.~ 3.5 1~,0 ..~.~ ~ 74.1 .1% ~LIDS roRer: 1~ ~ ~/~ ~ ~ ~ !~ ~ I . 12.1 8.5 ~.0 ..... 17.75 3.6 ~.,0.. ~,~ ~ ~,2- ~. ~LIDS ke,~mh:. " 1~ 1~ ~/~. ~ .~ ~ 1~ INC. CRO~ ~ ~/ ~4 ;~ 12.5 9.4 "~.6 .... ~5_ 3-1. 74.4, ~_55 ~ ~ ~.~ , 1~ ~ '~/~ ~ ~ ~ 1~ INC. CHO~ ~ 42/ ~4 j ... 13.7 10.3 247.0.. 37~.~ .... 3.4 ~.0 74.~ ~ 112.4.. .1% ~T,T~ ~h: .. . ....... 1~ ~. ~/~ 33 ~ ~ 169 6~ TNP_ ~~! . ~.6 92...[~ 19.7. 13'0 9.7 ~3.0 . 47.15 3.3 ~.0 ~.~ ~ 1~.4 .05 ~T,IDS ..... ~SaE~R~NG , , ~,, , ~O ~r I i~ a~. UN~ ~C FLYING ~ SUPER. G~ G~ CU~TiVE SE~ SEP O~L ~AL UOU~D G~ WmER CL~K ~E~ ORIF~E OmF~E G~ M~. ~P C~V ~iRCE ~Mp GRAV~ COMPR. EXPANS ~ PRESS FL~ T~AL ~- O~L GaS ~N SAS- 0~L S~ L~U~D O~L E~ENS TIME SIZE DIFK G~VIIY TE~ PRESS. F~R F~R FA~ F~R FA~ F~R , RA~ G~ RATIO SOLUTION RATIO RATIO RATIO ~r - , ~ , .......... ~ID ~: ~ ~0 d ~w T~ ~eoa Fu Fb Ftf ~ F~ Y ~, ~w~ ~ ~Rt GOR2 GC~T TGL~ TLGR WO~ , ~IG IN ~N fi~ .... '.~F. PSIA ODIM ODIM . ODIn... ~IM OOlM ODIM 4 ODIM'" M~F/D MMCF SCF~T8 SCF STB SCF;STB SC~BL BeU'M~" aSu'S,e ~ 1" ~ ~ 17~ ..... . ...... , "' ...... " ,~,, 3 068 ~ ~" 1810 ~ i , , ..... ~ ~.0 P~ess 0 50 ~ ~: -- , ,, ~: .......... - 500 0~t~ " ~.0 ~ rank ~ I ~ J ~. 0 15~ 3~ , , , , t ~- ' Run ~ ~ ~. 0 1 ~ 3~ '" ~ .. ' ~.0 1517 3~ Pr~ 1~ ~.0 14~ 42~ ~e: .... ' ..... ,,. Pre~ 10~ it ~. 0 1 ~ 3~ ~: 11~ J [ ~,0 1470 3~ I %~a~: .. 800BBL 1~ ~ ~. 0 1433 3~ ~s: 2 1~ .......~ ] ~.0 . 13~ 312 Raid: Shot Casing Tub Size: , Diff. Rant Rang Su~ Type: Meter R~ Size:., Diff. Rang Rar~ BBl./in: #'ranks: Standard Conditions GAS FLOW RATE CALCULATION LIQUID FLOW RATE CALCULATIONS F = Meter K = Volume P$c __ I z~ 7~ PSIA PRESS BASE FACT TEMP BASE FACT [14.73~ t/460 + T~c~ i Co-. Factor Redact,on FacTor TSC 6CI ..... OF FpB _ 14.73 ETS ---- __460 - °F Qg = Fu Fb Ftf Fg Fpv Y¥/hw P sepa FU = .024 x ~,--~c / x~, 520 / .METEfl, ' eo At~Q°mtn F (1 - BSW)(1 - Shr 60) 1440 TANK ' Qo - At~'Q°min K (1 - BSW) 1440 OIL (ASTMD1250 Pe~roleumDe'~'gnat'°n -- - - PB 520 WATER~ Meas. Tables) conoco, ( uctionTesting Services (' °' c, us~.~: FIELD READINGS DATE 5-8-90 OIL ~::7'~,~. CHANGE OIL CUMULA~NE CHANGE WATER CUMULATIVE (~ -- 4 CLOC-.K CASING CHOKE TEMP PRESS CHOKE TEMP H2S CO: SALINITY PH VESSEL OiL OIL MEAS O~L GRAVITY Sh~d~(.~._.~ IN OIL FLOW ..~,~.,~,. H.-,O .N -~0 FLOW 'tOTAL :]~[W ~ POiN~ 1 TIME PRESS SIZE SIZE TEMP COUNTER GRAVITY TEMP BS & ,N ,~ 60 ; =~)R { ~]ANG~ COUNTER RATE 0~L ~SL COuNTEt= ~,~uNTER RATE ,NATER 8BL PSIG IN ~ PS!G IN 3~' PPM aF BSL APl F :.. AP, ~ FRAC SBL s'rB/D BBL 8BL BBIJD BBL U~C) RRT..q a~: 1600 58 48/64 33 26 ~ 164 TNC. ~,~.:k,~z 1"O 52.0 ~.8 92 19.9 13.3 10.0 240,0 57.15 3.3 79.0 81.55 ~ 138,7 ,05 SOT,TDS :: :ET.~ ,..S~¼ 17(X:) 69 48/64 33 28' ~ 169 6(~ ]~C. H~':~I'~ rD) 54.0 12.9 9,7 Z~,.8 6~.8~ 3.2 7~.~ P-/4_'7~ ~ 151.~ _(::}~ .qC)T,TI'~q 30 1754 13.0 9.75 234.0 76.60 3.25 78.0 8 .0 164.6 TR. so n:)s ~r_,'vK:xJt~30¥ 1800 8~ 28/64 33 42 ~ 170 D:]~. C~OKE ~ 28/64 TO BC)T.D _~"~V~':~q _TNC. :--_--~- TO-~ 1900 99 32/64 33 44 ~ 170 INC. t~.:k'TZ ['O 58.0 ~_R 95 19.8 15.0 11.25 270.0 87.85 3.7~ 90.0 91.75 25%' 179.6 'i"R. SOT.InS D. CASSO 2[](]0 99 32/64 33 44 ~ 170 INC. II~:k"I'Z ['O 60. D 21,8 95 19.8 14.59 10.94 262.6 98.79 3.65 87.6 95.4 25% 194.2 TR, SOLIDS A. Pt{!T.T.TPS 2100 110 32/64 33 48 ~ 170 INC. ~:NTZ [XD 62. D 21.2 78 20.1 15.4 11.6 279.0 110.39 3.8~ 92.4 99.25 25% 209.6 TR. SOLTI"~ P900 115 32/64 R2 50 ~ 166 21.2 78 20.1 16,25 12,19 292.5 122.58 4.06 97.5 103_]1 ~ 725.89 "FR. SOL']'DS Nt:__ 23(X) 115 32/64 32 50 CP]~ 166 ~ TO TA~K I~2; 'IN'C. r',ZRTZ ['0.64 21,2 78 20.1 17.92 13.44 322.56 136.02 4.48 107.5 107.79 25% 243.8 TR. SOLIDS acement , 2400 120 32/64 32 52 fPJ~m 165 20_7 79 19.6 15.8 11.85 284.4 147.87 3.96 95.0 111.75 25% 259,6 TR, SOT.TDS ~ed~m:. " 0100 122 32/64 32 54 fPSN 166 TURN~D WIm'.T INTO SEPAR~ ~.TOR 20,7 79 19.6 17.08 14.52 348,5 .162.39 2.56 61.5 113.32 15% 275.7 TR. SOT,TDS FL: 0200 139 32/64 33 62 ~ 170 20.7 79 .. 19.6 16.25 14.95 358.8 177.34 1.] _%1_2 114_62 ,q% 291_9 'IR_ SOT,TrXC] D~a:__ in 0300 143 32/64 33 64 ~ 168 BACK TO TA~K #1; INC. i]~:k'TZ ['O 66 21.0 87 19.4 17.9 15.2 365.2 192.54 2.68 64.5 117.3 15% 309.8 TR. SOLI~P~ 0400 134 34/64 33 64 flq~N 170 0315 CHOKE TO 341 64 21.0 87 19.4 17.08 15.37 368.9. 207.92 1.7 50.0 119.0 10% 326.9 TR. SOT._TDS ~ Size: in ,, , i l~P. Size: _ l/ct.: bbl , , , ,, ~ Ret .... · ,~rl~p~h: ~ It ......... ~ i , , .... ' ' ' ' I , .... , , , , i ' GAS METERING ........ ~?~O "' ....... i . FLUID ~el' I I! I ASS. UNI'r BASIC FLOWING GAS SUPER GAS ? GAS CUMULATIVE S~P SEP OIL TOTAL UOUlD GAS WATER CLOCK PRESS ORIFICE ORIFICE GAS MEAS. SEE CONV ORIFICE TEMP GRAVITY ¢O~PR. EXPANS PRESS PLOW TO'rat. GAS- OIL GAS IN GAS- OIL GAS LIQUID OIL RATE '' TIME SIZE DIFF. GRAVITY TEMP. PRESS. FACTOR FACTOR FACTOR FACTOR FACTOR FACTOR! EX'TENS. RATE GAS RATtO SOLUTION RATIO RATIO RATIO RATIO , , , ,, ,,, ~.,, r 6-606PM ' p,,,o ,~ ~ T~ ,:,~, % ,:,: ~,, ~ ~ ¥ ~, .,~,,,P,~,~ c~ GOR~ GOR~ ~o,? T~LR TL~R WO" HERTZ B.H.P. BPD · ,, , , ,,, ,, , .... p~lG iN IN H~0 ' .F P$1A ODIM OOlM ODIM OO1~ ODIM 0DiM i' . 0DIM MSCF/D MMCF SCF/STe SCFIST8 ~C,F,'STB SCF/BBL , 8BL/MMCF BSLJSTB,, ~eterl", , 1600 ,,, ,i 't 50 1380 319.0 ~r 1700 I i52 1369 309.6 6-606~Zv~ , , , ,, ,, , , , ,,, e: , ,, '1800 INC. CHOKE TO,,3; /64 @ 1 800 EI~. ' ,,It 54 1358, 312.0 ~ebANIELS 1900 ~' 56 1339 360.0 , , , 'Run 3.068 2000 .j 58 1321 350.2 ............ 2100 "~ 60 1308 371.4 , ,,, , ?0 - 50 220062 12 5 390.0 e:, , ~ CHANGE TO '.:'ANK /~2 ~ I 62 1267 430.0 ~P~0 - 500 e:... 2400 . . ! t ~ 1244 :~ 0100 ! 64 1236 410.0 , , ~et~, 0200 23 0.75 24 0.650 82 37.730 0.024 113.530 0,979 1,240 1.002 1.004: 30.092 100.3 4.18 64 1725 390.0 ........ 'Run 0300 24 0.75 24 .0.650 95 38,730 0,024 113,558 0,968 1,240 1,002 1.004 31.733 104.5 8.53 287 283 4109,6~ 0.18 _ 64 1217 429.6 - 0400 22 0.75 31 0.650 103 36.730 0.024 113.558 0.964 1.240 1.002 1.005 33.744 110.5 13.13 299 295 3925.82 0.18 66 1204 418.9 -- ~tesS ~, ......... · 'al: 800BBL ,, t:~ ,,1,, 667 Mud Wt: Ruid: Shot/R; Sh0t Dia: 0il Me~er Rang Size: I~Meter Meter Run ~: ...... Diff. Pres~ Rang Type: SiZe:_ Diff. Press Static Pres S' Standard Conditions GAS FLOW RATE CALCULATION LIQUID FLOW RATE CALCULATIONS F = Meter K. = Volume Corr. Faclt3~ Reduct,on Factor ~ 14.73 PSIA PRESS BASE FACT TEMP BASE FACT /14.73~ /460 + T~c~ -%00 -%00 (ASTM De.~,gna,,on __ 460 - oF Qg = Fu Fb Ftf Fg Fpv Y¥~hw P sepa FU = .024 x %,--~c / x%, METER' Qo - F (1 - BSW)(1 - Shr 60) 1440 TANK ' Go - K (] - BSW) 1440 O~L Tsc 60 0F Fps - ~4.73 ETs _ __ 520 / .. -%t mir ' -%t mir 01250 Pe,roleum PB 520 WATER .... Mea$. Tables) C.o~e,: C(~OCO, INC. C'~ C :)ductionTestinlJ Services (' f"=' °' - FIELD READIN(~.S DATE 5-10--90 ~ -- ~ CL~ ~1~ CHOKE TEMP PRESS CH~E TEMP H~ COt ~LINI~ Pti ~SSEL ~L ~[ ME~ ; ~L GRAVITY INOIL FL~ .~. ~;~ 'N~O rL~' ~AL T~ P~ SIZE SI~ TEMP COUNTER G~VITY TEMP ~ 9S & W ~ ~ 'F r~= (~~ COUNTER RATE ?. ~. COUN~E: COUNTER RATE WATER BBL ~~ ~ _,~ % ~D ~: "~ ~ 1~ N/~ ~ ~ ~ 1~ 114 ~.3 ~ ~ 19.3 16.~ 16.1 ~.0 ~1.9 ~_16 ~:~ ~ ' ~.9 1~.1 1.~ ~.9 ~~ S~ 0~ 1~ ~/~ ~ ~ ~ 1~ 113 ~,~ ~ ~ 18.8 16.7 16.6 3~.4 ~.6 0.1 2.0 1~.2 0,~ 7~.6 : ~. ~S 0~ 1~ ~/~ ~ ~ ~ 1~ ' 113 ~,4 ~ 18.8 17.1 16.8 ~.2 ~.4 0.3 6.2 1~.5 1.~ 717.7 ~~ S~ ~' 1~ ~/~ ~ ~ ~ 1~ ~~{ ~ ~ ~1 11~ ~.4 ~ ~ 18.8 16.~ 16.0 ~.2 ~.~ 0.24 5.9 1~.7 1.~ ~,0 ~~ S~ D. ~ ~ 1~ N/~ ~ ~ ~ 1~ 113 ~.0 ~ 'i, 18.9 16.~ 16.0 ~.2 617.4 0.24 5.9 1~.9 1.~ 7~,2 ~~ S~ : A. ~NI~I~ ~ 1~ N/~ % ~ ~ 1~ 113 ~.0 79 ~, 18.9 15.~ 15.2 ~.9 ~.6 0.15 3_? 1Z~.1 1.~ ,, ~: , ~ 1~ N/~ ~ ~ ~ 1~ 112 19.2 74 ;~ 18.~ 18.7 18.6 ~.0 ~1.~ 0.1 2_o 1~_2 0.~ · ~,~ ~ 1~ N/~ % ~ ~ 1~ ~ ~ 112 ~.2 .~ :.~ 18.6 16.7 16.6 ~.0 ~,8 0.1 2.0 1~.3 ~,~ ~,1 ~,~ i: ~ 1~ ~/~ ~ ~ ~ 1~ 0 1~ 113 19.9 ~ ~ 18.8 17.1 17.0 ~.0 ~_~ 0.1 2.0 13~_4 0_~ ~8.2 ~~ ~T,z ,,~d~m: , 1~ 1~ N/~ ~ ~ ~ 1~ 11~ 19,8 ~ ~ 18.5 16.7 16.6 ~.0 7~.~ 0.1 2,0 1~,5 0,~ ~.9 ~~ ~T.~ ~t: 10~ ~ ~,0~; ~ ~ ~ .... j~. ~a: in ,, ).R Size: m ~ ' ~.: ~.: bbl , .... ., .. .... ....... ..... ; .... i'~ . '. ...... ........... I ...... -- , , ~ ~E~ :, , ,,, ~XT~O " ~r 1" ' ~ - ~E $1ZE OIFF G~VI~ ~MR ~RESS. F~R FAiR F~R ¢~R ~ E~ENS. RA~ G~ ~ ~OLuT~ON RATIO RATIO RATIO ~TIO ~ 6-606~N ....... ~0 I~' hw ~oa Fu Fb Ri ~ F~ Y ' ~ ~ G~I G0~' I I GOnT WOR ~: I ,,~A)G IN IN H~0 o~ PSIA ODIM 0DIM ODIM ~tM ~IM ODtU~ O~v m' M~FtD MMCF ...... SCF~8 SCF~ST6 SCr'ST8 SCF/BBL, ,mBb'a~F 88UST~ ~TZ B.H. ~. B. ~. D. ,, e~r 1".. . ,...,,.01~. ~ 1,~ 15.0 0,~ N 37.7~ .024 ~3.~1 0.%9 1,~7 1,~2 ... 1'~3 ~.~ 1~,6 124.3 ~ 7 ~ ~ ~ ; 0,~ 74,0 1~ ~,0 ~r 6-606~ 0~ ~ 1.~ 15,5 0,~ N 3~,~ .024 .~3,~1 0,%9 1,,~, 1,~2 1,~3 24,1~ 1~,9 1~,1 ~ 7 357 , ~ 3~ 0.~ , 74,0 1~ ~1.0 ": 0~ ~ 1 .~ 16,0 0.~ .93 39.~ . .024. .~3.~1 0.%9 1 .~ 1.~3 1 ~3 ~.~3 !~.8. 1~.4 .~9 7 3~ ~ 353 0.02 74.0 1~ ~.7 M~er ~~ ~ ~ 1 .~ 16.0 0.~ ~ 39.7~ .024 ~3.~1 0.~9 1.~ 1 .~3 1,~3[ ~,~3 1~.8 1~2~7 3~ 7 I ~ 2691 371 0.02 74_0 1~2 3~.0 rRun3.068 ~ ~ 1.~ 16.0 0.~ ~ 39.~ .024 ~3.~1 0.%9 1.~7 1.~3 .1'~3}. ..~.~3 1~.8 1~.7 3~ 7 ~ ~ 26~ 3~ 0.02 74,0 1~1 3~,0 ..~ ~ 1.~ 16.0 0.~ 92 39.~ .024 ~3.~1 0.~9 1.~7 1.~3. 1.~3 ~.213 1~.1 1~.8 ~ 7 4~ 25~ 393 0.01 74.0 1031 369.6 ~:~0 - 50 07~ 26 1.~ 15.5 0.~ 91 40.7~ .024 ~3.~1 0.9~ 1,~3 1.~3 , 1.~3 ~ ~.126 145.3 1~.8 ~ 7 333. 3~ 324 0.01 74.3 10~ ~ 26 1.~~ 15.5 0.~ 91 ~.~ ..024 ~3.~1 0.9~ 1.~3 1..~3 . 1.~3 ~. ~.126 1~.3 1~.8 .~ 7 3~ 27~ 3~ 0.01 74.3 10~ 401.0 ~re~0 - 500 ~ ~ 1.~ 16.0 0.~ 92 39.7~ .024 ~3.~1 0.9~ 1.~3 1.~3 1.~3 ~.~3 1~.7 1~.9 ~ 7 ~ ~ ~14 ~R5 O_Ol 7J_~ 1018 410_0 ~"~ ,~ ~ 1.~i 16.0 0.~ ~ 39.~ .024 ~3.~1 0.9~ 1.~3 1.~3 1.~3 ~.~3 1~.7 179.0 ~ 7 ( 3~ ~ 357 0.01 74.3 , , 1014 ~.0 ~,r 10~ S~ P~ 0~; ~ ~z, ~ , , .~ ,~ 'Run .~ I !tess ~ 'a~: 800~ , , , , , Custo Rep: Ruid: Shot/Ft.: ShaOia: C~i~ P~ Pacer ?, 0ilar Rang Size: .... Diff. Rang E)Bt. F~anks: ~tandard Conditions GAS FLOW RATE CALCULATION i LIQUID FLOW RATE CALCULATIONS F = Meter K = Volume Corr. FaCtOr Reduction Faclo~ ~sc 14.73 PSIA PRESS BASE FACT TEMP BASE FACT {'14.73~ /'460 + T~c~ :~ -~Qo F (t -- BSW)(1 - Shr 60) 1440 TANK ' Oo - -lOo K (1 - BSW) 1440 Oil (ASTM Des,gnat,on ~C 60 OF FpB -- 14.73 Fm-- 460 - °F Qg = Fu Fb Ftf Fg Fpv Y%/hw P sepa FU = .024 x k-~c / x k, 520 / METER Qo - -~t mtn .lt rain Dt250 Petroleum PB 52o : WATER___~ Meas Tables) 3 4 co oco, n sting ,ervices FIEI.D READINGS E 5-9-90 WELLHEAD HEATER OiL OR CONOENSATE Mt: i tHING I~Q MI: i ~ OIL $.I:i,I',,<AGE ril(::~'~L"l CHANGE OIL CUUUL,*,:'4 CHANGE WATER CU,,,u~T~E BS&W TOTAL ~ CLOCK CASING CHOKE TEMP PRESS CHOKE TEMP H~ CO: ~ALINIT~ PH vESSEL OIL OIL MEAS OIL GRAVITY '.N OIL FLOW ,'r~T~,~,~ H.-.O :N H..C FLOW T'OTAL TIME PRESS SIZE SIZE TEMP COUNTER GRAVITY TEMP BS & W ~ 6C F ~'~ (~(,-,~. COUNTER R~,TE 3~L 5F... COUNTER COuN"'ER RATE ~,'ATE~ BI:iL ~ MTT.N-R POTI~ , o. ,,. I'I~O P'ah Cw~ Twn Pwfl Ch Th Tseo Oo Go To BSW .~o6C* Snr, ,( Oo ~o PRIG IN ~: PRIG IH "F i=PM ~c BBl. APl F 2.,, ,:,P~ ;r "~Ae.. BBL ST~/D BBL a.E:. RBL,'D BBL ~n: 0500 133 34/64 34 60 ~ 171 140 19.9 80 1.0 18.7 15.4 13.9 333 221.8 1.5 36 120.5 10% 342.3 TR. SOLIDS :: ETAL SW¼ 0600 133 34/64 34 60 ~ 168 140 lq_q 80-. 18.7 16.7 16,4 394 238.2 0.3 8 120.8 '20% 359.0 TR. SOT,TDS ~.r MOUNTJO¥ 0700 134 34/64 34 61 ~ 172 SWITCmZr, TC mANK //2 140 18.8 17.1 410 255.3 1.7 41 122.5 9% 377.8 TR. SOT,TDS ~- ~ 0800 135 34/64 35 60 ~ lC;(t 140 ~ R 96 18.7 17.5 16.5 396 271.8 1.0 24 123.5 6% 395.3 TR. SOT.TDS D. CASSO 0900 134 34/64 36 61 ~ 166 140 20.6 98 ' 18.4 18,3 17.:2 413 289.0 1.1 ~6 124.~ 6% 413.6 mR. SOnTDS A. Ptm',T,'rPS 1000 133 34/64 38 61 ~ 171 INC. ~rFRT[ TO 68,10 140 20.8 94 18.8 16.7 15.9 381 304.9 0,8 15) 12~,4 5% 430,3 'IR, SOT,TDS 1100 136 34/64 39 62 (~ 170 INC. [4RRTZ TO 70.0 140 ~_4 106 18.9 17.5 16.1 386 321.0 1,4 34 126.8 8% 447.8 TR, SOT.TT')S M:__ ~mem 1200 139 34/64 42 64 ~ 170 140 20.6 102 18.2 18,8 17.4 41~ 338.4 1.4 ~ 1~_2 6.5% 466.6 'PR. SO'I',TT~q 1300 135 34/64 43 63 (PEN 169 143 _~0.6 104 18.1 17.9 17.5 420 355.9 0.4 10 128.6 2.5% 484.5 TR. SOLIDS raedint: " 1400 134 34/64 41 62 (PEN 146 137 _~),8 104 17.9 17.5 420 373.4 0.4 10 129.0 2.5% 502.4 TRA.CE 1500 133 34/64 43 62 (]::'5N 147 Pi:M 130 20.4 94 16.3 16.1 386 389.5 0.2 5 129.2 1.3% 518.7 TRACE Ft.: [:)ia:__ in 1600 135 34/64 42 61 (/::EN 134 Cp[qv~ 1,700 5~'~ 124 20.4 ...94...~ 18.5 16.6 15.6 374 405.1 1,0 24 130.2 6% 535.3 TRACE 1700 135 34/64 41 62 (I::EN 121 119 20.6 93 18.7 16.7 16.4 394 421.5 0.3 7 130.5 2% 552,0 TRACE ,:jSize: in 1800 138 34/64 40 63 CPEN 117 110 20.4 881 18..8 16.7 16.4 394 437.9 0.3 7 130.8 2% 568.7 TRACE ~.P. Size: in 1900 140 34/64 39 64 ~ 117 108 20.4 88I< 18.8 16.7 16.6 398.4 454.5 0.1 2 130.9 0.5% - 585.4 ~'oL: bb~ 2000 145 34/64 38 66 (PEN 125 110 20.4 88 i 18.8 15,8 1..5,(; ~75.4 470.1 0.2 4.8 131.1 1.0% 601.2 ,Ref: 2100 140 34/64 37 66 ~ 130 INC. 4RRTZ TO 72. 0 113 19.8 75 ~1 t8.9 16.7 16.4 394 486.5 0.3 7 1~1 _4 ~;~ 61'/29 =rDepth: t~ .2200 140 [.34/64 36. 64 ~ 126 . 11~ 19.8 75 ~,!~ 18.9 16.25 16.1 396.4 502.6 0.2 4.8 131.6 1.0% -,634.2 TRACE , , , ,, .... ~r ' ' ~s,~,,.G I RAT,O .. ABS. UNIT BASLE FLOWING GAS SUPER GAS I, GAS CUMULATIVE SEP SEP OtL TOTAL ~~D ~ ' WATER ....... CLOCK PRESS ORIFICE ORIFICE GAS MEAS. REP. CONV ORIFICE TEMP GRAVITY COMPR. EXPANS : PRESS ~=LOW TO'rA~. GAS- 0,. GAS,, r=AS.O,L OIL EERTZ B. H P. FLIED ' TIME SIZE DIFF. GRAVITY TEME PRESS. FACTOR FACTOR FACTOR FACTOR FACTOR FACTOR EXTENS RATE GAS RATIO SOLUTION RATIO TO ~T,O ' ere, 6-606PM .... P~e~ ~:~I ,' hwPsel~a C.~ GOAl .... GOR2 GOAT TGLR TLGR W0R RATE ~:. p~o ~ .. T~ F~ ~. r~ F~ v , i ' ..... BPD ~e~er 1" 0500 22 0.750 33 0.650 102 36.730 -024 '1i3.558 0.962 1.240 1.002 1.006: 34.815 114.1 17.88 343 1400 343 309 3237 .11 66 1194 370 .... ...... 0600 ~ 0.750 33 0.650 108 36.730 .024 113.558 0.957 1.240 1.002 1,006 34,81.5 113,,,5 22.61 288 ~ 288 282 3558 .02 66 1185 401 ,,, .... rRun 3.068 0900 ?-?. 0.750 37 0,;736 114 36,730 ,024 113,558 0.952 1.166 1.002 1.00'~ 36.865.. 112,5 t 37,08 272 '-=S 272 256 3920 .06 66 1157 439 ' ' 1000 21 0.750 40.5 0.736 116 35.730 .024 113.558 0.950 1.166 1.002 1.0G 38.040 116.0I 41.91 304 ..c~ 304 290 3448 .05 66 1153 401 " ' ' ' ' ' ' '' - ~s$ 0 - 50 1100 22 0.750 43 0.736 117 36.730 .024 113.558 0.949 1.166 1.002 1.002 39.742 121. I 46.96 317 17 334 288 34711.09 68 1146 420 . ',Press 0 - 500 1200 ~3_ 1.000 14 0.736 118 36.730 .024 203.541 0.949 1.166 1.002 1,00.~ 22,676 12.~,1 . 52.09 295 17 312 272 3675 .0R 70 1134 451 e: 1300 25 1.000 15 0.736 120 39.730 .024 203.541 0.947 1.166 1.003 1.00~ 24.412 132.3 57.60 315 17 i 332 308 3258 .02 ...... 70 1121 430 ,Ta~k 1400 24 1.000 16 0.736 118 38.730 .024 203,541 0.949 1.166 1.002 1.0(~- 24.893 135.1 63,23 322 7 I 329 314 ~'i~,~ [ ,02 70 1107 430 ,~e~er 1500 23 1.000 16 10.736 112 37.730 ,024 203,541 0.953 1.166 1.003 1.003 24.570 134.1 i 68.82 347 7 t354 343 2918.1 .01 70 1109 391 'Run 1600 21 1.000 15 i0.708 108 37.730. .024 203.541 0,9~7 1.188 1.002 1.00~" 23.790 132.8 74.35 355 7 i 362 334.. 3Q15 i .06 70 1092 398 .... 1700 22 1.000 15 0'708 104 36.730 ,024 203.541 0.960 1.188 1.002 1.003 23.472 131.5 79.83 334 7 ' 341 328 3049i .02 70 1092 401 'tess 1800 22 1.000 14.5 0.686 99 36.730 .024 203.541 0.964 1.207 1.002 1...00_~ 23.078 131.9 85..33 335 7 342 329 3040 .02 70 1091 401 Press 1900 23 1.000 13 0.686 88 37.730 .024 203.541 0.974 1.207 1.003 1.00~ 22.147 127.9 90.66 319 7 326 319 3154 .01 ....70 1083 400.4 e: 2000 23 1.000 13 0.686 88 37,730 ,024 203.541 0.974 1.207 1.003 1.0()2 22.147 127.9 95.99 319 7 326 ~1~t ~1.~>4I ,01 7Q. 10~6 379,2 -a,k 2100 21 1.000 15 0.686 91 35.730 .024 203.541 0.971 1.207 1.002 1.0(')3 21.151 133.3 lol _4 339 7 i 346 332 3005 ,02 70 1079 401 ~ -~m~: 800BBL ?300 23 1.000 15 0.686 92 37.730 .024 203.541 0.971 1.207 1.002 1.003 23.790 136.9 107.1 354 7 361 348 2857 .01 72 1074 393.2 ~:_ ... I. 667 ~ 23 1.000 15 0.686 92 37.730 .024 203.541 0.971 1.207 1.002 1,0()3 23.790 136.9 112.8 354 7 361 348 ~R57 , _01 ~ 1067 393.2 s: 2 2400 23 1.000 15 0.686 93 37.730 .024 203.541 0.970 1.207 1.002 1.0('),.3 23.790 136.8 11~_._5 333 7 340 334 3022I .01 72 1073 410 ~ ,. Cust Rep: __ Fluid: Shol/Ft.: Shol Dia: Cas~ P~ ~ ~t~ Standan:lConditio~ GAS FLOW RATE CALCULATION LIQUID FLOW RATE CALCULATIONS F = Mete. K = Volume Corr F,BCTOf Reduce,on F~ctor ~c 1 4.73 ~s~^ ~RESSS~SE~C'r TEUP BASE FACT /14.73'~ [ 460 + T~'~ -%00 F (t -- BSW)(I - Shr 60) 1440 TANK ' Go - AGo K (t - BSW) t440 O~L (ASTM De.~.gr, a~,on Tsc 60 0[ Fps -- 14.73pB FTB -- 460520- oF Qg = Fu Fb Ftf Fg Fpv Y~/hw P sepa FU = .024 x ~,---P~c / x~, 520 / METEF~ Qo -%t rain -~t min WATER.____ Meas.O1250Tables)Pmr°teum NO. t~-50.O: ,:..: .~ Y ':/':"' ~ 6 AM ! - i / / ;,AN M 3HART NO. M-500 METER PUT ON '"~.._....-" TAKEN OFF ~) SINGER AMERICANMETER DIVISION · Wd 9 6 AM ~.. %CAN r"~. CHART NO. M-500 ', .' ~'~ SINGER AMERICAN METER; ' 9 ~ 6 Ah~ AN AR]' NO. E~'~R ~ SINGER 6 AM 7 . ~ AN'M, O~ 0cx2 (~) stNGER AMEiRtCA, H METER WJ 9 / .. S~6 AM [CAN ~_~. &-~/ CHART NO. M-500 ~ETER~ .,, [~/ TAKEN S~6 AM ICAN -~HART NO. M-500 __ ON ~ TAKEN OFF ~.OCA'rfoN__~, (~ SINGER AMERICAN METER DIVISION ,6 AM Co~O CHART NO. M-500 ~R, ~, - ~'~ CHA~ PUT ON TAKEN OFF REMARKS , (~ SINGER ,,,,.,mc^. MET'=R D,ws,o. Wd 9 6 AM CHART NO. M-500 . -. ~. (~) SINGER AMERIGAN METER Wd 9 ./ 6 AM CAN CHART NO. M-500 .~..~;.~,. TAKEN OFF REMARKS __ (~ SINGER AMERICAN METER OlV ~roduction ~est;il'~g Sel-vices SPECIALIST IN OIL & GAS WELL TESTING - DUAL DISPOSAL OIL BURNERS LIQUID SAMPLE FIELD ANALYSIS RECORD PAGE CUSTOMER O0N~ ESP TEST WELL G - 4 TEST AFTER FRAC DATE 1 2 3 4 5 6 7 8 9 . 10 TIME SAMPLE SHAKE OUT API° CF WATER T SAMPLED POINT @ (ppm) RES (J~L m) pH o OIL WATER, BS&W 60OF (F) TiME .. 0630 .... 20 ,, 8 ........... , , · .. 0700 5 95 0.1 0730 5 95 0.1 .. 0800 ., 5 95 O. 1 ~, 0830 5 95 0.1 0900 10 90 0.1 ......... 0930 10 90 0.2 1000 ,, 25 ....... 75 ,·, 0.. 1 ....... 1030 30 70 O. 1 ..... , ..... , ., , 11 O0 40 60 0.1 1130 45 55 0.1 . 1200 50 50 0.1 , . 1 230 5O 50 0.1 1300 51 49 0.1 ....... ., 1330 51 49 0.1 . . 1400 , 51 49 O. 1 1.500,'... ....... 51 49 . 0.1 1 530 60 40 0 o 1 · , _ , , 1600 6;0 40 O. 1 _ . , . . _ _ , _ .... 1 700 . .,. I roduction lesting ervices (YJSTOMER CONOCO INC W~. G-4 Test #1 FIELD MILNE POINT PAGE# 1 STOCK TANK AND PRODUCTION REPORT I ?ANK'I" 'TANK 2 TANK 3 TANK' 4 ................ BBLS ..... °F .... B~l'~q °,,F .......... RR,I,S ,~,F, ....... BBLS, ,, °F ..... ,RDG., ,,, PRODU~,,, ' ......... , ,, ........... i .... , .... , i '"!1.~ I1 ~' i ,1~.~o~ '.,~ o7~. I ', . ",.5 1.~ I..i:~.~o:~ ¢ .. ~ ........ ', ..................... , ............... , ...... _~_o~i", ~"~'I'1"';'~' .......... ....... -,.'~ .,.~.',,,..~, .,'", ..... ... ' . ' . ....... .. ,.~, ~.o~ ~.. ~ ..1.~.~'" ~ '" ~.~s ~.~ I'~.~~,~.' I .~.~= ~e,e.. ~l~S' 1 ~1.~ }~.~ 9.~~ 1.~ ]!6.~,~ .............. 4.~ ~,~. -~i ~ ~.~..~!.~ .. 9.~.~ .~6.~ ¢ .... I ~-~ ~"~. -~i. ~ .~.~ .~.~ ..... ~0..0 ~.~ ~6.¢ .~0 ..... _ !~5! 1 1 .~ 1.~ 10.0 -1245~ 1 1.~ ~,~ 10,~1 1.~ 17,~ .417 .... 5.~ .¢.m _ 1~.~ ~ ~.~. 1.~ 10.~ 1.~ ~7.~2 ,~ . 6,~ 9.~ _~5~ ~ 1.~ 1.~ 11.~ 1.~ 18.~ .~ 7.~ ~.0 --- '1..... ' ..... _ 1~5~ 1 1,~ 1.~ _ 11.~ 1.~ .... 18.~ _~ _, 7.4~ .... ~.~ - 1~ ~ 1.~ 1.~ 11.~ 1 ,, ,, ~ '" i, , , - I ..... . ....... i , ,, ., , , ~ ...... ..... roductionmesting Services PAGE # CONOCO INC. G-4 TEST #1 i~-- ~-~'~ MILNE POINT 2 DATE 3-1 4-90 · . STOCK TANK AND PRODUO2ION REPORT ...... BBLS ,.F ................ BR~.~..*F .... RRb.c: ~F . . BBI~ ~G. PRODUO~. ,.34!5. J, a ,, , 1,.~ 1,,.~,,, ,,. 11,.~ ,1,~ 18.~ ¢' ' ..... 8.~ l~.m __ ,,!4~ ,,1,, .......... ~ 1,~ 1,~ 11.~5 1.~ 19.~ 1.05 ......... ,,,, 8.~ ~.~ 1~5 i 1 1.~ 1.~ 12.1~ 1.~i ~.~ .412~ ............ ' ........ ~ .................... ~0.~,, 1~.~ 1~1~. 1 i 1,~ 1.~ , 14.!~ 1.~ ~.~ 1.¢", ........ ' ' ' ..... 12.~ ~.16 15~ 1 ! 1.~ 1.~ 14,~l 1.~ ~.76 -~0 ,, ' ........... .... , ..... ,~ 1, ,} ,1',~,,l ~.~ i .......... )4,.~ 1.~ n.76 ¢ ' ' " 32.~ 1615, 1 ... 1.~ ,lt~ ....... ~ 14.~ 1.~ ~.76 . ¢ . .. . , 12.~ .¢ ~6~ ~ ~.~ ~.~ ,, . 74.~ 1.~ .m.76 ¢ . 12.~ n~5~...~ 1.~ n..~ 14.~ ~.~ .~.76 ¢ ,, ,. u.~ 17~- ~ 1.~ 1.~ 14.~ 1.~ ~.76 ¢ ,, 12.~ 1715;' 1 1.~ 1.,,~ ,. 14.~ 1.~ ~.76 "' ~ " " 12.~ ¢' _ _ I ............... "' . 1745~ .... 7 ........ 1.~ 1.~ ......., 14.~ ~.~ ~.76 .9 ~as{ ,,,~~.~ ~.~ ........... , ,,. ~ ~ ~.~ ~.~ .... ~ ...... .. _ ~ ............. .,. i .......... ..~, ,, , ~ .......... ~ ~ ............ , , ,, , roductionTesting Services DATE 3-14-90 STOCK TANK AND PRO[TJC'i~ON 9]3PORT CUSTOMER . CONOCO INC. W~,T, G-4 TEST #1 DST PAGE # ..... 3 TIME INCHES FACTOR BBLS GAIN TEMP [NCHE~ FACTOR BBLS GAIN TS~E~ INCHES FACTOR :BBLS GAIN ~ iNCHES 'FACIY)R BBLS GAIN ~ SURGE TANK TOTAL .RATE BPD BBT-q °F BBT~ °F BBLS ~F ' ' BBLS *F RDG. PRODOCED ....._i, · , , .1800 8..,0 .! ,667 ,,,1.,.3.33611 .669 ........... 14.250 !.667 ,23,76 ................. ,1815,, 8,5 .., 1.66~/.., ,,!,4.1,70 ,0.834 ........................................... _1830 9.0 ..... 1..6~....1.5.C~. 3 ... 0.833 ............................... .1~5. 9..,25 !..667 .15..4~. 0.41.7 ........... I .................... - .1900 9,5 1.667 .15.837 0.417 ......... i ........... . _!915 1Q,O ,1.667 16.670 0,833 ........ ' ..... - 1930 10.5... ,1,667 !7.50~ .... 0,834...t ........... "t ... .... - ..19~5 11,0 !.,667 .!8.337 O.K~'~ ........... ~ ..... . -...~ 2000 11.5 ~.. 1,.667 19.171 0,834, .... 2015 12.0 1,667 20.00~ 0,833 ............ . ' - 2030 12.25 1,667 ,,20.421 0,417 ....... -" -- ~ 12.5 1.667 20.838 0.417 ,,, ,, , -- . _21FD 12.75 1.667 21.255 0.417 .... -- 2115 13.0 1.667 21.672 0.417 ...... -- 2130 13.25 1,667 22.089 0.417 ............. -- ,,, ..... · __ , ........ __ , __ , , ..... ~ .......... __ .......... ............................. ................ DATE 3-1 9-90 ----..-.----..._.__ TANK1 TIME INCHES 0845. 1030 ~~oduot;ionmest:in'§ ' Se~v., oes C~S~ PAGE # CONOCO INC. G-4 TEST #2 MILNE POINT 1 TANK2 12.45 i 14 T~3 j BEGI] TANK4 PRODUCED RATE BPD ,52 239.04 42 ~ O~ ~ 17 119.93 _ o'ductionTestin§ Services DATE 3-1 9-90 CUSTOMER CONOCO INC. WRr,T. G-4 TEST #2 FI~ MILNE POINT PAGE# 2 STOCK TANK AND PRODUCTION REPORT TIME IINCHESI FACTOR BBLS GAIN Tt~4P INCHES FACTOR BBLS GAIN T~4P INCHES FACTOR: BBLS GAIN ~ INCHES FACTOR BBLS I GAIN T~MP HRLY, TOTAL RATE BPD BBLS *F " ' i 'I AVG. ~_~r_.~ OF PRODUCED t ..... ' .... ,~!~1' ~$ ..... .°,k. .............. ',, ',' °F ............. 1230 '! 1 3 ' 21.67 18.25 30.42 .mX ' ' "" '1 .... 90. ..25..00 .... 79..69_._~ i2~s i ! ......... ' "i~.~o .... *2.so 21';; "' .2,.o~ ~.. ~.m ~ ! "~ i ............ ~ , '~oo '~s'.oo ~.~,' I,,' ' , .................. ~.~o t,,, ~o.~. ~s I...", .....................22.25 ~7..0~ 2,0~t ............................. ~.~0 I. ................... , ............ . ..... , ....... .,~ l, , i .... I .,. t 25.,s ,42.s~ 3.a~.......... 37,U ,~.00_ ~s~s., ! ,,, ! ..... ! .... i 26'0 ~,.~ .a~. ........................ 37.~s '~.~_ 1~4~ i I i ........ : ' i' ~ ...... ~,,0, ~,~ ~o34 ............... ~1,2~ .~i...~, . .. t ...... ~ i'~-' ~. .....'~"~ -"~~,, ~.~ ' ' .... ' "" ..... . ~'~.~... ,~.~-~'~- _~Td~ ~ ........ ~,, ~q.~a a_~ ........................ 51,.2S ~.1~ ~mql .................... 35 58.35 1~67 ............. ~.06 m.16 ~i ,.,~ ..... ~.o~ ~.~ ...... ~,~ .~o'.~ _ 1915! ......... ~ 63.~ 3o33 ........................... _~;'7_ ~ - !~51 40 , ~.68 ~.34 r' , , .,., ., .... ~ _~ ~_-~._. 2msl .... ~j .... a~.~s ~.~ .................. ~., _ 0_o7. ,, ' ! ........... ,,,, , .......... , ,, ,, ,,, I ........... . . ro'd uctio n Testi n.g "Se rvi ces O3STOMER CONOCO INC. WELL G-4 TEST #2 FIELD MILNE POINT PAGE# 3 DATE 3-1 9-90 TIME 'INCHES! FACTOR BBLS GAIN TSZ~P INCHES FACTOR BBLS GAIN ~ INCHES FACTOR BBLS GAIN ~ INCHES FACTOR BBLS I GAIN T~4P SURGE TANK TOTAL RATE BPDi .[ l~2T.q ,.°,.F RRT.c: °F ........... BBT;q, °F .... ' ' ' · ....m BBLS °F RDG.,, pRODUCED , ,. ' ~ 64.64 80.16 .2045 .... i ..... 42 ..... 70.01 1.67 .................... -' 1 ............... l .............................. ~5,,,I ...... I ,4~ ,, ~.~ 1.~v,I ......... 7~.~ , ~.~- ~ i .... i ........................... ., ~ ~ !, ! ..... ~o ~ ! ~.~ 3.~, !~" ,. , ........ ~-~ ~--~ - 23~_5 ; I ........ $1 I,, 18s.02 1.67~ ~ , ' 79.6s eo.~6 _ 00151 ' ~. ...81.32 ,,, ! ~ ..,52, 86.691 1.67'~ ................... ~ ~5 I i ~ .... 53 8s.~i 1.~i ' ' , I ..... ,, ~-_99 ',. 0~5! I ss 9~.~1 3,33i i ..... 8~.3~ ,~e.03 _ ................ ~, , , ,,, ,,~sl ..... .m m.m~1.~! .... I '1 .,, ~.~ m-~ _ ~si ..... ~ 95.02] 1.¢z~ j .......... !m.66. ~0.~6 _ o2,~s~ ......... 58 96,691 1.67i i cp_-~-~ m_~ _ ~ ....... t .... 60 100.02i 1.67 .94,67 ED,16 _ n'~5,,! .......... _oa~si ......... 6o . .. 1~,02.. ~, , ," .. '94.67 ..~. _ · ~! ........... 6o.5 loo.~: .~; ............. ~s.so ~o.,oo _ _t~ ~ 61.5 102.52! 1.6'/ 97.17 ID.16 _ ,! ............. -- I , , ~.. ! -- .... I ..... . .... i ,, , ......... , ...... -- ,., I .... ro'ductionTestin, g Services DATE 3-20-90 CUSTOMER CONOCO INC. WF/~, G-4 TEST #2 FIELD MILNE POINT PAGE# 4 STOCK TANK AND PROU3CI~ON REPORT ·[ BBLS °F ...... RRr~, , *F , BBLS ~F . ' 'I BBLS ...... ~F RDG. PRODUCtD 't ..... 6~.5 ~m.52 ~.~ I 1 i 9~.~ ~0.~ °s~5 i ......... ! ........................................................... I ...... 0~5 1 ..... i .......... (~.5 10~.19 1.67., ........................... I 98.84 ! 80.16_ ,o~!5 I ~ ''' t ~.5 105.1~ 1.~ I_'"' . .................. I lOO.51, i ..... i .......... i 63.75 ..... II~;,Z'/ .4111 1 ........... I* "~W .q'T~l~Pm ~I .!00.92 I 19o74 ~715 .j. i ~ t t 63-75 1~_97' ~ i i* c~ N~ ~O PC ~ITIVE CHOKE , (6/64i 100.92 07~51' , '' ........ 63.75 106.27 ,' -i .............................. 100.~ ~ .......... ! ' i .....................81 " ................. ' ' ~01q ; I i ] (~. 10~.36 1.25' } 103.01 i ......... , ................. ~ ....... i ............... ' ..... 1015i ......... I.. 66.0 110.02 .412 . [ ............. 104.67 ~5 ~ ..... I. 6~,2s 1110.44 .419 . i ................... 1~.~ ~n_~n ! ........ ; 106.76 lg-'~ ~51 . 67..25!. 112.11 ,416 ~ ..... 1215i .... 67.75 112,94 ,829 . ~ ......... 107.59 ~.~_ , 1245 i 68.0 113.36 ,416 " . .'. !08,01 19.~__ ~ ,, , .............. : 1~i,~ 68.251 113.78 .428 .. , ....... 108.43 ~.%6_ _1~5 ~ , ..,,,,,,69.0 115.02 . 1.24 ., I. - ......... 109.67 59.7 ~ ......................t "' · ............... ,,, ! , ..... ....... , ..... r od u-Cti o n .Te sti..ng' ServiCes CUSTOMER CONOCO INC. ~' ~-- 4 ...... PAGE # ....... 5 TE,$,T , # 2,, , MILNE POINT DATE 3-20-90 · . STOCK TANK AED PRODUCi~ON REPORT TIME tINCHES[ FACTOR BBLS GAIN TtSMP IN(/-IES FAC1Y)R BBLS GAIN ~ INCHES FACTORi BBLS GAIN I]~4P INCHES FACIOR ~ GAIN TJ~4P SURGE TANK TOTAL RATE BPD{ I [ BBf.S oF R~T.c: oF .......... BBT~ °F. .. ' i .... BBLS OF . .RDG. PROE~JC~ i i 69.5 ....... 110.51 40.32 1415[ I ........ 11S-86 .a40 ................. 1515i .... ~ .................. , . , ,1.11.76 19.84. " ',"' i ............. 69.75 ... 116.2'/ ,413 ................. '" 112.1.7. 20.16_ 1545i I .. 70..0 ..... 116.69 420 ......... ' ' 1.!.3.00 40.00 _ , , ]6!5! [ ......... 70.5Q.. 117.52 ....834 ....... 1.13,42. . .20.17_ , , 1645 ! I .......... .70,75 ...... 117.94 ..420 ' 113,84 20,01_ ' : " 'i .... I ........ 7!.00 ... 118.36 .417 "' ' 1715 .. , .. , ....... 114.67 1745~ [ i 71.5 ... .119.19 .830 .... ' . lmS l ......... ' ' ' 1915~ .1945 ~ .............. ' ' " 20'~5; "' - ,,,'2115! .......... ~ .... -- I t " " " 2245 ,. ...................... I . . DATE 3-20-90 & 3- 21- 90 uctionTesti.n.§ services CUSTOMER CONOCO INC. W~Z, G 4 TEST #2 FIELD MILNE POINT PAGE # 6 STOCK TANK AND PRODU~ON REPORT TIME INCHES1 FACTOR BBLS GAIN TS~P INCHES 'FACTOR BBLS GAIN iT~V~ INCHES FACTOR BBLS GAIN ~ INCHES FACTOR BBLS GAIN T~4P SURGE TANK TOTAL RATE BPD ............ BRL~ °F BBLS °F BBLS °F "' ' R~L.~ °F RDG. PRODUCED . I ......... 71.5. . 119.19. .830 ....... I ........... 11.4.67. . 39,84 ............1 '' ' ..... ' ' .... , .......... , ,.: .............. 0300 ...../"',i ~3. I .~ ~2~.69 ..e4~ ... 1.~?,34 ~0.3~ i .............. !, , , , ............ ,, , o330 I.. F .... 76. 126,69 .560 ........... 122.181 r~NY) i .... i ! 76 [126.69 I~ ...... 122.181 t ,, ..... . . . , ........... os~i.t ' w½ .. ~m.l~. .~ ,, ~-4.69 ~o.1 ~3f13q i ..... 77,751 129.61 .419 125.11 m_11 { ....... ~nn,,I ,, 81.0 135.031 4.1'7 I' 1'~_~'~ mn_n~ :~800 ~ m.~5 135.~ ~ ....I "' ,r ..... . ..... ;)8.301 81.~ 135.65 .ZI 131.15 10.0 ~x'x3 I . , 81 ,,5. 135.86 ~21 , ~ .. 131.36 . ,, 10.10 =. , ,,. _ I ............... I .....~., I ........ .... , ........ I~roduction "lestincj ervices DATE ___ R-21-90 STOCK TANK AND PRODUCTION REPORT O3S~ CONOCO INC. WR~z. G-4 TEST #2 FIELD MILNE POINT PAGE# 7 du ctionTes'tin, g s;'e'rvi"Ces, DATE 3 21-90 STOCK TANK AND PRODUCTION REPORT CUSTOMER CONOCO INC. WEre, G-4 TEST #2 FIELD MILNE POINT PAGE# 8 TIME~BBLS i BBLsGAIN Tt~P ~ FAiR ~OF GAIN TEMP INCHES~_~_ BBLS GAIN 15~4P INCHES FACTOR BBLS ~ T~4P ~GE T~ TOTAL 'RATE BPD ..... BBLS OF OF RDG. PRODUCSD . ,, 89.~ ~.2 .4~7 .... ~.~ ~9.~ _1820! ' , , 89.95 1~.61 .413 .... 1~5.02 19.8~~-- , , , .... , ...... I ,,, , , , , , ' ..... .!9oo J i ~o.~ .~ ~n_P~ 1.~-~ ............. ~.Z7 ~3.17 ,, _1930 i I 91~ ,.351.7 . .837 ............. 147.11 , ~.18 ..- ~' .... ' ,, .... , ,, , , , ~030i I 92.0 ~53.36 m34 ....... .. 14~.77 _2~i I " 93,75 ~s6.28 .e34 -- 94. 1~.7 .,418 152.11 :3:).06 ' 153.77 5.08 . 2400~ 95.5 159.19 '~ 154.6 ~ ~ __ ~ 161.:28 .41__2 " " '156.69 19.79 ___q ------ -- ........... ~_~ ~.~____Z_~ rOduction sting ervices DATE 3-22-90 CU~ CONOCO INC. WE[ff., G-4 TEST #2 FI~ MILNE POINT PAGE# 9 STOCK TANK AND PROI:~ REPORT ....... TANK 1 " TANK 2 ..... TANK''3 .... TANK 4 .......... TIME INCHES FACTOR BBLS GAIN TEMP INCHS~ !FACTOR BBLS GAIN ~ INCHES FACTOR BBLS GAIN ~ INCHES!FACTOR BBLS I GAIN T]~P SURGE TANK TOTAL RATE BPD , - ,, BR~'.~ oF , , B~T~ °F ..... RRT-~ OF ' 'I R~',-~, ,OF , ,, RDG. PRODUCk'D , ,, _0200 .l ..... 97.75. .162.95, 1.669 .............. 161,36 . .80.12__ 023o [, ! 'i 9~.~ ~62.9s ¢~ ,,, , ....... 16~.36 ~ ,,, ' ' .................' ' 0400 i .... ~,75 ~.62 .836 .... '163.08 _0500 · ~..-i ........ ~.75,. ,I ' , 1~:____I:~ .~ 164.74 ~ i 102.25 170.45 2.50 168.91 lm.O~ .0700 !, 102.75 171-__'28 .__R38 , ,, 169.74 ~_n4 _JTr'~ ! 103.0, 171.70 .421 .... 170.16 · OB(X) ~ 103.25 172.12 .418 l~-m m.r~' ncc. m J 103.25 172.12 I~ * 081 5 PUM.., SI-i[rT OF:[' ~ 170_57 ~i' ' __O9~_ : 103.25 17')_'~:; ~ 170.57 ..~)30_ i 103..5 172.54 r.415 : * 091 ~ PUM:,~ RE: ',TART * 17t3_c~ 1~0(O I 103.5 172.54 ~ , 1713_qq ! , _ .... i ! ~ ,, , ,, -- [ ' , , .... I i ,, .... 'rOd S¸ . u'ction'mesting ervices CUSTOMER CONOCO INC. WEr,~; G-4 TEST #2 FIELD MILNE POINT PAGE# 10 DATE 3-22- 90 S'I~CSK TANK AND PRODUCI~ON REPORT .......... ~,,, BBLS °r ........ BBI'~ °r BBI.~5 ~,F,, ' .......I BBLS ,o~, RDG... PRODUC'ED ..... : ~oo . t ~o3.s I ~.r~ H~.~ ..¢ ......... ... ~o.~ ~ ..... ~o3.,s ,!,, H'z2.54 ...................... ~'~o.99 ,, ,1200 !,, I ....... 105.0 i . i175,,04 2.5 I ., , ......... i ..... 173.49 120.0_ 12301 'I ...... ,,,105.0 [ 1'1,75.54 ¢~ , ,, '"',"1 ' I 173.49 ¢ _ 1300j, I .... !05.0 I ' 1!75.54 ¢ ~0! !'.,,,' ':, ,' ............. ~0~.~,. I~.~ ~...0 ...... i "' ~, ~.4~ ~.o i~ t ........ ~.0 ~. 1~0.04 .~ .... I ... ~=-'~ . 1600! ............ - ~630~ ~09.0 i 181.70 . .410 ~79.65 , ~9.68, !,~1 ....... ,0.50 ~4.2 1.25 ,,, ~--lS · !800 1 .... 110.5 18~.2 ltl ~i. .. m.o I~.04 .~'. ~ ~,~ . ~0.18 1930 !I 112.0 ~.? .8~. .......... l~.e~ ~0.03 .,. ,,. rOductionmesting Services DATE 3- 22- 90 ~ TANK AND PRO~3CTION REPORT CUSTC~4ER CONOCO INC. W~z, G-4 TEST #2 FIELD MILNE POINT PAGE# 11 ...... TAN~ 1 ..................................... TANK 2 .................. ,_rANk' '3 .............. TANK 4 ............................. i t ....... 1930 I i ..... 112,0 i ,11~.7,, .8~ I ..................... i184.65 40.03 ~i ! ~:.' i'.i'j'i.'.'. ......... ~..~.'i I~.s ~.~ I ..... ~ ~.,~ ~ ~-~ t ~ . ~ ............ !13,.. ~ I1~.~ -.~ I ....... I 1~-~ ~1.8 I ..... ~1~.~ .418 1~.78 ~.~ ~ ~. .I.. . ,. .. ~4.,; ,, I~.~ ~'~ i ., ....... ~ ...... i~.~ ~-~-. ~ ! .... l ............... 114.~, ~ !1~.~ -m2 I .... 1~.~ ~-g ................ ,,, , 116. I i~_~ .~ ...... I .,, ~m-~ · ~ 1 , ~ [ ' , ~.~.~[ ..... ~1~.~ ..1~ I 1~.~. ~.~ I ' "' ' ' ' ~ ........... ' ...... ~ ........... ~1~.~ 1.249 ~ ........................ ......................I '~' ........................ ............. i .......................... . ~ ................ ~ .... I. '~ ~ . ,, "' ,, ,~ :',,,' ............ .... } ....... ,,, ,-, .... } ~ .... ~ ~ ..l , ~ .i ' ..... i ...... I ............ ~ ........ ~ ! I ............. ~' ~ , , , .......... I .... i ~ ~ ....... ~ t ~ I ............. ". .... "i ..... :lUCtionTesting Services · ~'~CIAI.~ST ~f~ O~L. & '~"~'~, WE~,,L TEST~I'~G -- DU,~I, D~$POSAL. Oil.. 8Uf~NERS STOCK TANK AND PRODUCTION REPORT 5-3-90 03~ CONOCO WRr,?. G - 4 FIm~D ........ MIU~-E POINT PAGE # 1 TEST #2 T ]INCHES FACTOR BBLS GAIN TEMP INCHES FACTOR BBLS GAiN TEMP INCHES FACTOR BBLS GAiN TEMP INCHES FACTOR BBLS GAIN TEMP SURGE TANK TOTAL PRODUCED RATZ' ~D ~ ,, BBL,S ,,,°F....... BBLS "F ,,, BBLS °F BBLS ~F RDG. , .. _0400 1.25 1.667 2.1 2.00 1.667 3.3 INITIkL READi[NGS _ · __2100 2.00 1,667 3.3 ..... ' .................. 2130 ....... 2.75 1. ,6~7,,` 4.6 1.3............................... · .... 1.3 ~ - · : 2200 4.25 1.667 7.1 2.5 3.8 120.0 ,, , ........ , ......... , ,, , ,, , ............. , , ,, _ __~2230 ~ , , 4.25 ~.667 7.~ ~ 3.8 ,, , , .... , , , ,, ~ 2300 6.75 1.667 11.2 4.1 7.9 196.8 ,, ,, ...... .,,, 2330 9.50 1.667 15.8 4.6 12.5 220.8 ....... _ __2400 12.25 1.667 20.4 4.6 17.1 220.8 ............. ·_oo3o ......... ~5.2s ~..667,, 2s.4 $.0 .......... n..~ 0~00 ~8.so 1.667 3o.8 s.4 27.5 .... , _0130 21.25 1.667 35.4 4.6 32.1 220.8' , ,, 0200 24.25 1.667 40.4 5.0 37.1 240.0 .. _ 0230 27.75 1.667 46.2 5.8 42.9 27~.4 ._ 0300, 31.50 1.667 52.5 6.3 '~ 49.2 3~2.4 ! 0350 36.00 1.667 ~60.0 7.5 56.7 3~).0 ,,, 0400 38.25 1.667 63.8 3.8 ,, .-. 60.5 182.4 _ 0430 41.75 1.667 69.6 5.8 ...... ..... 66.3 278.4 0500 45.50 1.667 75.8 6.2 72.5 ~c7.6 ...... 'oduction"l'esting Services ~E~C:IAI_I~T IN OIL & ~'~ wELL TESTING -- DUAl,, DISPOSAL OIL Bt.)RN£RS · STOCK TANK AND PRODUCTION REPORT 5-4-90 CUSTOMER ~ WELL G - 4 TEST #2 FIEIZ) MIIATE POINT PAGE # 2 TIME INCHES FACTOR BBLS gAIN TEMP INCHES FACTOR BBLS GAIN TEMP INCHES FACTOR BBLS GAIN :TEMP FEET FACTOR BBLS GAIN TEMP SURGE TANK TOTAL PRODUCED RATE BPD .................. BBLS *F ..... BBLS "F BBLS °F . BBLS ,,°F, ,, ' RDG ..................... 0530 48.75 1.667 81.3 5.5, 78.0 264.0 · . ~ 0600 ................ I .... 52.25 1.667 .87,1. 5.8 . ....... . ......... 83._8. 2?8.4 oeo I ', 55.75 ~.9.i 5.8 ,~'? 75" .~.6~.4 0~® ........ ~.~ ~.7 5.~ .......... 4'11.~'t .......... ~.~ 278.4 0730 63.00 105.0 6.3 5'3.0" 101.7 302.4 0800 66.00 I10.0 5.0 5'6.0" 106.7 240.0 0830 70.5 117.5 7.5. 5'10.50'I 114.2 360.0 0900 74.50 124.2 6.7' 6'2.50" 120.9 321.6 0930 78.50 130.8 6.6 6'6.50" 1~7.5 316.' ..... 1000 ,, 81.75 , , 136.2 ,5.4,, 6'9.75" 132.9 259.2 , 1030 ...... 84.50 140.8 4.6 7'0.50" ....... 137.5 220.8 _1100 88.00 146.6 5.8 7'4.0" 143.3 '278.4 1130 92.00 153.3 6-7 7'8.0" 150.0 ..321.6 1200 95.25 158.7 5.4 [" 7'11.25'! 155.4 259.2 1230 ........ 98.75 164.6 , 5.9 8'2.75'' ,,,,.. , 161.3 283.2 ,1300 1~ .75 169.6 5.0 , ,,, 8'5.75" 166.3 240.0 __ 1330 ...... 105.7~, 176.3 ,, 6.7 8'9.75" 173.0 .... 321.6 1400 109.0 .... 1~.7 5.4, 9'1.75" ,., 178.4 259.2 'odUctionTesting Services ~I~I~CIAL. IST tH OIL, & ~,'~ WI~L.~. TESTINQ -- DU~L OISI~)$AL OIL BURNERS STOCK TANK AND PR0~UCTION REPORT 5-4-90 CUSTOMER CONOCO WELL G, 4 TEST #2 FIELD MIIA1E POINT PAGE # 3 TIME INCHES FACTOR BBLS GAIN TEMP INCHES FACTOR BBLS GAIN TEMP INCHES FACTOR'BBLS GAIN TEMP FEET i FACTOR BBLS GAIN TEMP SURGE TANK TOTAL PRODUCED RATE BPD :. BBLS °F ,,, BBLS °F BBLS ,,,F, ,, BBLS ,,°F l~C,o ................ _1430 .............. 112.75 18'7.9 ..6,2 ....................... 9'4.75" ...... 184.6 .... 297.6. · ~_ 1500 ........... 116,00 193.3 5.4 9"8.0" ......... 190,0 ..... 259,2 !530 ........ 119,75. 199.6 6.3 9'11.75' .. !96,3 ... 302.4 .... 1600 123.00 1205.0 5.4 10'3.0" "' 201,7 259,2 _1700 .... ,129.25 .. ;215.5 10.5 1019-25'' ..... 212,2... 2r.3~0.. _1800 ...... 1135.25 225.5 10.0 11'3.25" . . 27)~2 .. 240,0 1900 . . 141.75 236.3 1'0.8 .......... I1 '9.75'r .. 2q~q,0 259.2 2000 .... 148.00 246.7 10.4 12'4.0" 243,4 249.6 2100 153.20 255.4 8.7 . . 12'9.25" . . . 2200 .... 157.25 265.5 10.1 .. 13'3.25" i 262.2 242.4 2300 165.25 275.5 10.0 13'9.25" .. 272.2 240.0 · 2400 172.00 286t7' 11.2 14'4.0" .... 2Rt.4 ..268.8 0100 178.50 297.5 10.8 14'10.50' 294.2 259.2 0200 185.25 308.8 11.3 15'5.25" 305.5 271.2 0300 192.00 32)0.1 11.3 16'0" 316,8 271,2 0400 198.50 330.9 ,.1,.0,.8 )6'6.5" 327.6 259.2 __0500 206.00 343.41 12.5 17'2.0" 340,1 300.0 0600 213.75 356.3 12.9 17'9.75" ~/~.0 309.6 .......... I~r°duction]esting_ ~ervices .. ~r~,~, , ............ ~-4 ~s~ #2 fd:~CIALI$'T IN OIL & ~'5 WELL TESTINO -- DU~L DISPOSAL OIL BURNERS ~ ~Z~ ~. PA~ ~ 4 STOCK T~ ~D PR0~UCTION ~PORT ~ TIMEI INCHES FACTOR BBLS GAIN TEMP INCHES FACTOR BBLS GAIN TEMP INCHES FACTORIBBLS GAIN TEMP FEET FACTOR BBLS GAIN TEMP SURGE TANK TOTAL PRODUCED RAI! BPD BBLS *F BBLS *F ........... · BBLS *F ............ BBLS *F RDG., , 0700 10.25 1.667 17.115.0 - , ............... ,,,,' ..... lO.~" ....... :~.o ,, ,:~.0, 0800 17.75 29.612.5 i 1'~ 75"' -' ' .... , ....... ' ...... i ......... 380.5 3'.'0.0 0900 25.50 42.5 12.9 ...... I ,, i 2'1.50" 393.4 359.6 1000 32.00 53.3 10.8 ...... i 2'8.0" 404.2 259.2 t 1100 39.00 ,65'0 ,1,!,'7 ....... i 3'3.0" 415.9 22-0.8 1200 , 45,.50 ..... 75.8 10.8 . . I 3'9.50" 426.7 259.2 1300 52.25 .... 87-1 11.3 ............ ! 4'4.25" 438.0 2~1.2 , , 1400 58.75 97.9 10.8 , , { 4'10.75 ' 448.8 ~.2 1500 65.50 109.2 11.3 5'5.50"! 460.1 1600 71.75 119.6 10.4 ! 5'11-~' 470.5 1700 78.00 130.0 10.4 .... I 6'6.0" 480.9 2-5).6 1800 84.75 141.2 11.2! 7'0.75" 492.1 P~R.8 . i 1900 91.50 152.5 11.3 ! 7'7.50" 503.4 271.2 2100 103.75 172.9 10.4 [ ~.8 249.6 ! 2105 105.25 175o! ' ' 1 __ 2145 126.25 210..' ! RE~JRNED 5.0 BB],S R~ERSI~rG O~ AND BiDWING ~ ~ ~ m , , Milne Point G No. 4 COMPLETION HISTORY Kuparuk River Field - North Slope Borough, Alaska W.I. 1.0 Milne Point G No. 4 CONFIDENTIAL AFE 10-61-1311 Location: 3466' FNL, 3370' FEL, Sec 27, T13N, R10E U.M. NSB AK Location: Bottom Hole 1790' FNL, 3314' FEL, Sec 27, T13N, R10E, U.M. 11-20-90: R/D from G-2. Start R/U on G-4, call AOGCC for BOP test @ 1500 hr. Start N/D Tree & N/U BOP's. Off load 300 bbls of 9.0 NaCl brine & heat to 80°. Mud wt. 9.2 ppg Viscosity: N/A Cum. Cost: $ 18,950 EWS Rig 4 (0-0-1) Drilling Foreman: HAUSER 11-21-90: N/U BOP. Remove BPV, install TWC. (Call AOGCC for BOP test @ 1200). Remove TWC, install lifting JT. POOH & L/D TBG HGR. P/U one JT of 2-7/8" TBG. RIH to aprx 8' over RBP @ 4395'. Reverse circulate the following cleaning Pill: Lead pad 25 bbls of 3.5# HEC/bbl of brine, Chemical pad 50 bbls of brine 9.0 + one drum of surfactant/dispersant (dirt magnet), Tail pad 25 bbls of 3.5#s HEC/bbl of brine. Circulate w/ 9.0 filtered brine (10 micron). Circulate hole clean. RIH & retrieve Baker 7" RBP @ 4395'. POOH & L/D RBP. R/U to run ESP. RIH w/ ESP & power cable attaching two cable bands per joint w/ additional bands above & below each cable splice. Also install AVA sleeve two JTS above pump. Mud wt. 9.0 ppg Viscosity: N/A Cum. Cost: $ 35,285 EWS Rig 4 (0-0-2) Drilling Foreman: HAUSER 11-22-90: Continue RIH w/ 2-7/8" TBG and ESP. MU TBG HGR. Land HGR. Set BPV and ND BOPE. NUtree. Retreive BPV and set 2-way check. Test tree to 5000 psi. Retrieve 2-way check. Set BPV. Pump 70 bbls diesel down annulus for freeze protection. RDMO to D-2A. Operations suspended pending test. Mud wt. 9.0 ppg . Viscosity: N/A Cum. Cost: $ 58,950 EWS Rig 4 (0-0-3) Drilling Foreman: HAUSER/STEVENS CONOCO INC. G-4 MILNE POINT ALASKA COMPUTATION DATE: SPERRY-SUN DRILLING SERVICES ANCHORAGE ALASKA 9/19/89 TRUE SUB-SEA COURS MEASD VERTICAL VERTICAL INCLN DEPTH DEPTH DEPTH DG MN ,' 0 .00 -59.27 100 100.00 40.73 200 199.99 140.72 300 299.97 240.70 400 399.95 340.68 500 499.92 440.65 600 599.85 540.58 700 699.60 640.33 800 799.13 739.86 900 898.48 839.21 1000 997.42 1100 1095.61 1200 1193.01 1300 1289.47 1350 1337.00 1400 1383.68 1500 1475.22 1600 1566.13 1700 1657.15 1800 1747.27 1900 1835.82 2000 1923.45 2100 2010.80 2200 2097.88 2300 2184.75 2400 2271.34 2500 2358.88 2600 2447.48 2700 2536.25 2800 2625.68 2900 2715.54 3000 2806.11 3100 2897.15 3200 2987.21 3300 3076.50 DATE OF SURVEY: 9-17-89 BOSS GYROSCOPIC SURVEY JOB NUMBER: AK-BO-90101 KELLY BUSHING ELEV. = 59.27 FT. OPERATOR: D. HARGER 0 0 0 3O 0 52 1 9 1 28 COURSE DLS TOTAL DIRECTION RECTANGULAR COORDINATES DEGREES DG/100 NORTH/SOUTH EAST/WEST N .00 E .00 .00 .00 S 85.70 E .50 .03S .44E S 85.50 E .37 .12S 1.63E S 78.60 E .31 .38S 3.38E S 79.00 E .32 .83S 5.64E VERT. SECT. .00 -.01 -.04 -.20 -.53 1 19 2 46 4 58 6 1 7 2 N 89.70 E .31 1.07S 8.06E N 42.60 E 2.10 .71N 10.86E N 26.40 E 2.44 6.37N 14.42E N 20.70 E 1.19 15.17N 18.20E N 18.10 E 1.05 25.90N 21.97E -.64 1.30 7.14 16.12 27.05 938.15 1036.34 1133.74 1230.20 1277.73 9 29 12 16 13 51 16 42 19 25 N 16.10 E 2.47 39.65N 26.16E N 13.40 E 2.84 57.92N 30.91E N 10.40 E 1.71 80.04N 35.53E N 6.70 E 3.02 106.09N 39.37E N 4.60 E 5.59 121.52N 40.88E 41.00 59.50 81.83 108.06 123.55 1324 1415 1506 1597 1688 .41 .95 .86 .88 .00 22 33 24 51 24 22 24 32 26 46 N 2.70 E 6.41 139.40N 42.00E N 1.50 E 2.34 179.56N 43.45E N 1.70 E .48 221.20N 44.61E N 1.80 E .17 262.59N 45.88E N 1.50 E 2.22 305.87N 47.12E 141.46 181.64 223.28 264.68 307.96 1776.55 28 35 1864.18 29 0 1951.53 29 15 2038.61 29 38 2125.48 29 44 N 1.70 E 1.82 352.30N 48.42E N 1.50 E .43 400.46N 49.76E N 1.80 E .28 449.12N 51.16E N 1.70 E .40 498.26N 52.67E N 3.20 E .75 547.75N 54.78E 354.39 402.55 451.22 500.37 549.90 2212 2299 2388 2476 2566 .07 30 16 .61 27 32 .21 27 43 .98 27 5 .41 26 4 N 3.50 E .55 597.67N 57.71E N 1.30 E 2.93 645.95N 59.77E N .70 E .33 692.32N 60.58E N 1.50 E .73 738.33N 61.46E N 2.40 E 1.09 783.06N 62.98E 599.91 648.23 694.57 740.57 785.31 2656 2746 2837 2927 3017 .27 .84 .88 .94 .23 25 57 24 12 24 40 26 48 26 43 N 3.10 E .33 826.87N 65.08E N 4.10 E 1.80 869.16N 67.73E N 3.10 E .63 910.44N 70.32E N 2.80 E 2.14 953.80N 72.55E N 2.60 E .13 998.79N 74.67E 829.17 871.54 912.91 956.33 1001.36 ' ~PERRY-SUN DRILLING SERVICES ANCHORAGE ALASKA PAGE 2 CONOCO INC. G-4 MILNE POINT ALASKA COMPUTATION DATE: 9/19/89 DATE OF SURVEY: 9-17-89 BOSS GYROSCOPIC SURVEY JOB NUMBER: AK-BO-90101 KELLY BUSHING ELEV. = 59.27 FT. OPERATOR: D. HARGER TRUE SUB-SEA COURS COURSE DLS TOTAL MEASD VERTICAL VERTICAL INCLN DIRECTION RECTANGULAR COORDINATES VERT. DEPTH DEPTH DEPTH DGMN DEGREES DG/100 NORTH/SOUTH EAST/WEST SECT. ,' 3400 3166.18 3106.91 25 47 N 3.00 E .94 1042.98N 76.83E 1045.60 3500 3256.37 3197.10 25 21 N 2.70 E .46 1086.10N 78.98E 1088.78 3600 3346.29 3287.02 26 31 N 2.10 E 1.20 1129.81N 80.81E 1132.52 3700 3435.35 3376.08 27 34 N .50 E 1.27 1175.27N 81.83E 1177.97 3800 3524.13 3464.86 27 13 N 1.10 E .44 1221.28N 82.47E 1223.95 3900 3613.19 3553.92 26 52 N .70 E .39 4000 3702.92 3643.65 25 28 N .90 E 1.41 4100 3793.58 3734.31 24 26 N .90 E 1.03 4200 3884.76 3825.49 24 4 N 1.80 E .52 4300 3976.57 3917.30 22 36 N 2.30 E 1.47 1266.76N 1310.87N 1353.05N 1394.12N 1433.71N 83.18E 1269.40 83.80E 1313.48 84.46E 1355.63 85.43E 1396.69 86.84E 1436.30 4400 4069.34 4010.07 21 11 N 1.00 E 1.50 4500 4162.69 4103.42 20 51 N .30 E .42 4600 4256.21 4196.94 20 37 N .20 E .23 4700 4349.86 4290.59 20 25 N .70 W .37 4800 4443.61 4384.34 20 17 N 1.00 W .17 1470.98N 1506.85N 1542.26N 1577.32N 1612.10N 87.93E 1473.58 88.33E 1509.42 88.49E 1544.78 88.34E 1579.78 87.82E 1614.49 4839 4480.19 4420.92 20 17 N 1.10 W .09 1625.63N 87.57E 1627.99 THE CALCULATION PROCEDURES ARE BASED ON THE USE OF THREE-DIMENSIONRADIUS OF CURVATURE METHOD. HORIZONTAL DISPLACEMENT = 1627.99 FEET AT NORTH 3 DEG. 5 MIN. EAST AT MD = 4839 VERTICAL SECTION RELATIVE TO WELL HEAD VERTICAL SECTION COMPUTED ALONG 3.08 DEG. SPERRY-SUN DRILLING SERVICES ANCHORAGE ALASKA PAGE 3 CONOCO INC. G-4 MILNE POINT ALASKA COMPUTATION DATE: 9/19/89 DATE OF SURVEY: 9-17-89 JOB NUMBER: AK-BO-90101 KELLY BUSHING ELEV. = 59.27 FT. OPERATOR: D. HARGER INTERPOLATED VALUES FOR EVEN 1000 FEET OF MEASURED DEPTH TRUE SUB-SEA TOTAL MEASD VERTICAL'VERTICAL RECTANGULAR COORDINATES MD-TVD VERTICAL DEPTH DEPTH DEPTH NORTH/SOUTH EAST/WEST DIFFERENCE CORRECTION 0 .00 -59.27 1000 997.42 938.15 2000 1923.45 1864.18 3000 2806.11 2746.84 4000 3702.92 3643.65 .00 .00 .00 39.65 N 26.16 E 2.58 2.58 400.46 N 49.76 E 76.55 73.97 869.16 N 67.73 E 193.89 117.34 '1310.87 N 83.80 E 297.08 103.19 4839 4480.19 4420.92 1625.63 N 87.57 E 358.81 61.73 THE CALCULATION PROCEDURES ARE BASED ON THE USE OF THREE-DIMENSION RADIUS OF CURVATURE METHOD. ~uPERRY-SUN DRILLING SERVICES ANCHORAGE ALASKA PAGE 4 CONOCO INC. G-4 MILNE POINT ALASKA COMPUTATION DATE: 9/19/89 DATE OF SURVEY: 9-17-89 JOB NUMBER: AK-BO-90101 KELLY BUSHING ELEV. = 59.27 FT. OPERATOR: D. HARGER INTERPOLATED VALUES FOR EVEN 100 FEET OF SUB-SEA DEPTH TRUE SUB-SEA MEASD VERTICAHVERTICAL DEPTH DEPTH DEPTH TOTAL RECTANGULAR COORDINATES MD-TVD VERTICAL NORTH/SOUTH EAST/WEST DIFFERENCE CORRECTION 0 .00 -59.27 59 59.27 .00 159 159.27 100.00 259 259.27 200.00 359 359.27 300.00 .00 .00 .00 .01 S .08 E .00 .00 .08 S 1.01 E .00 .00 .22 S 2.57 E .02 .01 .63 S 4.61 E .04 .02 459 459.27 400.00 559 559.27 500.00 659 659.27 600°00 759 759.27 700.00 860 859.27 800.00 1.07 S 7.12 E .07 .03 .72 S 9.53 E .11 .04 3.24 N 12.86 E .25 .14 11.23 N 16.72 E .64 .39 21.30 N 20.46 E 1.22 .58 961 959.27 900.00 1062 1059.27 1000.00 1165 1159.27 1100.00 1268 1259.27 1200.00 1373 1359.27 1300.00 33.52 N 24.39 E 2.05 .83 50.58 N 29.10 E 3.61 1.56 71.85 N 34.03 E 5.98 2.37 97.38 N 38.26 E 9.28 3.30 129.73 N 41.45 E 14.47 5.20 1482 1459.27 1400.00 1592 1559.27 1500.00 1702 1659.27 1600.00 1813 1759.27 1700.00 1926 1859.27 1800.00 172.18 N 43.26 E 23.15 8.68 218.09 N 44.52 E 33.20 10.04 263.56 N 45.91 E 43.06 9.86 311.92 N 47.28 E 54.17 11.11 365.08 N 48.80 E 67.44 13.27 2040 1959.27 1900.00 2155 2059.27 2000.00 2270 2159.27 2100.00 2386 2259.27 2200.00 2500 2359.27 2300.00 420.32 N 50.28 E 81.69 14.25 476.31 N 52.01 E 96.31 14.62 533.22 N 53.97 E 111.39 15.08 590.64 N 57.28 E 126.75 15.36 646.15 N 59.78 E 141.17 14.42 2613 2459.27 2400.00 2725 2559.27 2500.00 2837 2659.27 2600.00 2948 2759.27 2700.00 3058 2859.27 2800.00 698.51 N 60.65 E 154.05 12.88 750.10 N 61.77 E 166.58 12.53 799.49 N 63.67 E 178.13 11.55 847.97 N 66.25 E 189.30 11.16 893.08 N 69.38 E 199.05 9.75 3168 2959.27 2900.00 3280 3059.27 3000.00 3392 3159.27 3100.00 3503 3259.27 3200.00 3614 3359.27 3300.00 939.70 N 71.86 E 209.42 10.38 990.12 N 74.28 E 221.44 12.02 1039.64 N 76.66 E 233.06 11.62 1087.47 N 79.05 E 243.94 10.88 1136.29 N 81.05 E 255.24 11.30 SERRY-SUN DRILLING SERVICE& ANCHORAGE ALASKA PAGE 5 CONOCO INC. G-4 MILNE POINT ALASKA COMPUTATION DATE: 9/19/89 DATE OF SURVEY: 9-17-89 JOB NUMBER: AK-BO-90101 KELLY BUSHING ELEV. = 59.27 FT. OPERATOR: D. HARGER INTERPOLATED VALUES FOR EVEN 100 FEET OF SUB-SEA DEPTH TRUE SUB-SEA MEASD VERTICAL' VERTICAL DEPTH DEPTH DEPTH 3726 3459.27 3400.00 3839 3559.27 3500.00 3951 3659.27 3600.00 4062 3759.27 3700.00 4172 3859.27 3800.00 TOTAL RECTANGULAR COORDINATES MD-TVD VERTICAL NORTH/SOUTH EAST/WEST DIFFERENCE CORRECTION 1187.76 N 81.94 E 267.72 12.48 1239.36 N 82.82 E 280.25 12.53 1289.96 N 83.48 E 292.33 12.08 1337.46 N 84.22 E 303.04 10.71 1382.74 N 85.07 E 312.82 9.78 4281 3959.27 3900.00 4389 4059.27 4000.00 4496 4159.27 4100.00 4603 4259.27 4200.00 4710 4359.27 4300.00 1426.51 N 86.55 E 321.99 9.18 1467.08 N 87.86 E 329.93 7.93 1505.55 N 88.33 E 337.07 7.15 1543.41 N 88.49 E 344.00 6.93 1580.82 N 88.29 E 350.77 6.77 4816 4459.27 4400.00 4839 4480.19 4420.92 1617.89 N 87.72 E 357.42 6.65 1625.63 N 87.57 E 358.81 1.39 THE CALCULATION PROCEDURES USE A LINEAR INTERPOLATION BETWEEN THE NEAREST 20 FOOT MD (FROMRADIUS OF CURVATURE) POINTS SPERR ~v-~-, SUN HORIZON 7AL ¢-4 ~4ILNE POINT ALASKA 9-17--89 DLRG. ~VCS. START TVD = 0 FINISH TVD = 4480.19 SCALE IS 500 FEET/IN 3000 I..L..J 2500 2000, 1500 1000 SO0 O, 4.839 56o ,oho DEPARTURE ~obo 25bo soho · ~ ~t~ILNE POINT ALASKA 9-17-89 LEI 1000 4OO0 SO00 0000 ?000 4! VERTICAL I.~1%Lin, %.t~ e qu~ V ~.P'%,.~ · PROJECTION START TVD = 0 FINISH TVD = 4480. 19 SCALE IS 1000 FEET/IN · 1627.99 (~ 10~)0 "~ .oo oob .bo so~)o ~o~)o VERTICAL SECTION DIRECTION = O. O0 NOTES: ~,'IILNE POb~JT UNIT I. ,STATE PLANE COORDINATES ARE ZONE 4 08'05'42' ~.~,,, 2. ALL GEODETIC POSITIONS ARE BASED ON ^cc~ .¢'~ ..... ._";" ~. ~,~,o~ ~O^D'-"--'~' N.~.D. 1927 ~,.~ /, 3. OFFSETS TO SECTION LINES ARE COMPUTED BASED ON PROTRACTED VALUES OF THE ,SECTION CORNER POSTIONS ,I MILNE PT. VICINITY MAP z ~ . 3o' ---~''~ 4-- ' . ~ LOCATION ~N ,~ ,SEC, 27, T13N, RICE, UMIAT MERIDIAN .-'-i:~l~- WELL ,ROM NORTH UNE .ROM ~ __ . o ~ , ~-~ ~' ~o' ~ G-7 3288' 3393' I ~ o- ~1 ,~ ~ WELL NORTH (V) EAST ' dI ~ ~ '! G:: ~ I ~ G-5 6,014,308 91' 557.~.7~' ~ · ~: ~ G-6 ,6.014.368.30' 557. 218.~8' I ~ o j ~_ ~ ~ G-7 6.014.427.70' 557.209.84' J G-8 6.014. 487.10' 557,201.39' ~EODETIC POSITION8 NAD 1927 W~L NO~ LAT~DE WEST ~ PAD ~-~ G-5 70' 26' 5g.022' ~4g* 31' 5g.222' ~ 10' G-6 70'26'59.607' 149'31'59.453' ~ 9' ~ 15'~ 15'~ 290' 2 ~ ...................................... ~ :'..:..2':).'::~::..'.::T:..'~;:"::.':>}~ M? :,::':'::.':5'):)F.) :.'?}??:.'.};::!::'?:.. TYPICAL gECTION o PROPOSED N~ WELL NO SCALE · EXISTING WELL CONDUCTOR (LOCATION A~-BUIL T) i ,, ~:~-' ('. F. gober[ ~ & NEW WELL LOCATIONS ~ ~ ~ ~ JO9 NO. 90059 ,SCALE 1':2OO' COMPLETION DATE I Y I._~ ~) CO, CONTACT ~1 i iii ii iiiii check off or list data as' it i~" ~eceiv~'~l.~list received da;i~ for'4'O?, if ~o_t ry,~i'red Ii'~t a~ ~R 407 !'* ~'/~/~1 i ~ril,,ling hist.~ !'~ s'~weyl i ! we~l,tcsts .... ~core descripU~d~~ cored inte~ais ?,re analysis [, ~ d~,ditch ~ntcwals digital data ', ~ ~ ~ ,,_~ ~ ,, , ~ .... ' .... ¢=~ ~- ~ ", ~, ,, ,, ,, , , , ,,, ~ ,,, ,, ~ , ~ ~, H ~ ~ ~ , -,, , ,, 1 ...... LO~ ,'rY,~E ........ I .... ~l)l',t ...... I~TER~ALS ' SCALE ................. NO., , [to t.h.c qC..~rc~.t foot) [inch/100'] , , Il I II - Ii ' I I I I1 I I iii ii i i i iii r iii i i , ..... Noven~ber 29~ ~990 Conoco Inc. Milne Point Operations Center Pouch 340045 Prudhoe Bay, AK 99734 (907) 659-6300 Mr. Lonnie C. Smith Commissioner Alaska 0il & Gas Conservation Commission Subject= Milne Point Unit, Well No. G-4 Dear Mr. Smith= Please find enclosed an application for Sundry Approvals in triplicate for the above referenced well. Sr. Production Engineer RECEIVED NOV ~. 9 1990 Alaska Oil & Gas Cons. Commission Anchorage ~ . STATE OF ALASKA ' 0 !~ i ALASKA OIL AND GAS CONSERVATION COMMISSION " APPLICATION FOR SUNDRY APPROVALS 1. Type of Request: Abandon __ Suspend __ Operation shutdown __ Re-enter suspended well Alter casing __ Repair well __ Plugging __ Time extension __ Stimulate Change approved program __ Pull tubing __ Variance ~ Pedorate 2.CO"CCC T:N Name-°J O°eratQr-O. 5. Type of Well: 6. Datum elevation (DF or KB) Development ~ KB- 59 · 3 g MB 1', feet Exploratory ~ Stratigraphic __ 7. Unit ~f~,C~ty 0pa~NT UNTT 3. A~d~ .~. 8'i'· sO'rTE 200 · ANCHO:RAG Ii: · &[ Service ~ 4. Location of well at surface 8. Well number 3466~ FNT,· 3370~ ~E'r.· BE~'ro~ 27· T13M· R10E· OM At top of productive interval 9. Permit number 2719~ FNT.· 3308~ ~ET.· 8EOTTOM 2'7· T13N· R10E· OM 89-45 At effective depth 10. APl number 1799g FNT.· 3282~ FET.· 8E~TTOM 27· T13N· R10E· UM 50--029-21941 At total depth 11. Field/Pool , UPPER CRET-W BAK ~2. ~resent well condition summary Total depth: measured 4950' feet: :: ;i. ·Plugs!measured) true vertical 4584 ~ feet ....... ~ "" : .... :.. .... .,. ' N OV 2. 9 1990 Effective depth: measured 4849 ~ feet Junk(measured) true vertical 4491 ~ feet ". :, . Alask 011 & Gas Cons, 6ommts¢o Casing Length Size cemented Measured depth AllCll0~vertical depth Structural Conductor 80 g 13-3/8" 48#/FT 60 BBLB ARC BET 110 ~ RKB 110~ RKB Sudace 2643 ' 9-5/8" 47'#/FT 189 BBLS PERF E 2674 ' RKB 2454 g RKB Intermediate 4901~ 7' 29126#/FT 125 BBLS CLASS G 4929~ RKB 4565~ RKB Production Liner 4480 ~ - 4514 g Perforation depth: measured 4555 ~ - 4576 ~ 4143" - 4176 ~ true vertical' 4213 ~ - 4223 g 2-7/8', 16.4#/FT. L-80, EVE, 4395~ RKB Tubing (size, grade, and measured depth) · BAKER' RETRIEVABLE BRIDGE PLUG SET @4395' RKB Packers and SSSV (type and measured depth) 13, Attachments Description summary of proposal Detailed operations program -X-- BOP sketch 14. Estimated date for commencing operation 15. Status of well classification as: 16. If proposal was verbally approved Oi Gas][~ Suspended __ LONNIE SMITH 11/14/90 Name of approver Date approved Service 17. I hereby ce~_ify that the foregoing is true and correct to the best of my knowledge. Signed ~,,~ ~ t1~'/~) Title SR. PRODUCTION ENGINEERDate 11/19/90 FOR COMMISSION USE ONLY Conditions of approval: Notify Commission so representative may witness I Approval Plug integrity __ BOP Test __ Location clearance __I y"r~ '- MeChanical Integrity Test __ Subsequent form required 10- z-/° ~7 ORIGINAL SIGt, IED LONNIE C. SI~ITR Approved Copy : Returne& , [..~ Approved by order of the Commission, ,., , IO~(~[~, Commissioner Date ,6~O Form 10-403 Rev 06/15/88 SUBMITIIN '~'RIPLICATE MPU G-4 WELL Milne Point Unit PRO'POSED ESP RUNNING PROCEDURE AFE No. 10-61-1311 11/16/90 - CVL Objective- Clean up fluids; Retrieve bridge plug; run ESP and postpone start-up until surface equipment hook-up is completed. Surface Location- 3466' FNL & 3370' FEL of Sec. 27, T13N, RIOE Depths' All depths are measured from original RKB (59.3') and open hole logs dated 9/11/89. Casinq- Surface: 9-5/8", 47 #/ft, L-80, btrs. set @ 2674' Production: 7", 29 #/ft, L-80, btrs. set @ 4929'. Capacity: 0.0371 bbl/ft Drift ID : 6.184" Burst Pressure : 8160 psi Tubinc//workstr' 2-7/8", 6.5 #/ft, L-80, EUE 8rd Capacity = 0.00579 bbl/ft tubing; 0.0291 bbl/ft annulus ID = 2.441"; Drift ID-- 2.347" Burst Pressure = 10,570 psi Torque (ft-lb): Min : 1730; Optimum: 2300; Max : 2880 Misc- Retrievable bridge plug (RBP) @ 4395'(Baker Model "G") PBTD = 4857'(driller)/4832'(CCL 4-25-90) TD: 4950' Pore pressure = 8.54 ppg equivalent (1833 psi) Fluid in well = 9.2 ppg NaCl(possibly topped off w/ diesel) Proposed completion fluid = 9.2 ppg NaC1 (10 deg F TCT) Max Angle : 30 deg; Angle through pay = 21 deg Perforations- OA; 4480'-4514' OB; 4554'-4570' 4572'-4576' RECEIVED NOV 2 9 1990 Alask~ Oil & Gas Cons. Oomm~ssion ;Anchorage Proposed RU, Cleanup, and Bridge Plug Retrieving Procedure: NOTE: Hold frequent on site safety meetings prior to all potentially hazardous tasks-. i · Skid rig to the G-4 well and RU on well. Install pump-through BPV in tubing hanger profile. ND tree and tubing hanger. NU BOP's. Install pipe rams for 2-7/8" tubing. Test rams to 250/4000 psi and test Hydril to 350/3500 psi. Record tests on AOGCC and Conoco daily reports. Pull BPV. NOTE: Insure that well is dead. Freeze protection may have induced an underbalance on fOrmation if bridge plug is leaking. It may be necessary to kill well by circulating 9.2 ppg brine throughout wel 1 bore. · Back out hold-down pins on hanger and PU tubing to remove tubing hanger. GIH to 4390' (5' above RBP @ 4395'). Reverse circulate the following cleansing pill at maximum pump rates. Be Ce Lead pad - 25 bbls of 3.5 #'s HEC/bbl of brine Chemical pad - 50 bbl s of brine + 1 drum of surfactant/dispersant(Safe-Kleen, Dirt Magnet, etc..) Tail pad - 25 bbls of 3.5 #'s HEC/bbl of brine Post flush - circulate with filtered brine (10 microns) at maximum rates until less than 50 NTU NOTE: 1. Safety and environmental precautions must be taken when handling brine and chemicals. Review MSDS sheets prior to handling. 2. Chemicals must be mixed and maintained above 70 deg F. e · Monitor brine clarity every 50 bbls during post flush with a Turbidity Meter. Submit results to engineering. GIH and latch RBP @ 4395'. POOH and rack back tubing. running/pul 1 lng tool. L/D RBP and REEEIVED NOV 2 9 1990 Alaska Oil & Gas Cons. Commission Anchorage Proposed ESP and Tubinq Runninq Procedure' 1. MU ESP assembly on 2-7/8" tubing as follows- a. g. h. i. Centrilift PHD (BHP device) unit Centrilift 65 hp 562 Series motor w/ centralizer (7", 29 #/ft casing) Centrilift 513 GSB seal section Centrilift FRSX Gas Separator Centrilift FC-650 400 Series pump w/ 184 stages X-over to 2-7/8" EUE 8rd 2 jts 2-7/8" EUE 8rd 2-7/8" AVA ported nipple {w/o sleeve or check valve} 2-7/8" EUE 8rd to surface . RIH w/ ESP assembly no faster than 30' per minute. Attach two cable bands per joint. Attach additional bands above and below each cable splice. . Locate bottom of ESP assembly at + 4440'. perforation @ 4480'. Maintain 30'-50' above top NOTE: Do not space out with pup joints at surface. Spot the assembly with a full joint connection at the wellhead for ease in NU tree. . Pump sufficient diesel down annulus allowing it to U-tube back through the kelly hose into tubing to allow 1800'-2000' of freeze protection. . ND BOP's. NU tree. RD and move to next well. Await surface facilities connection for production. Prepared by: ~----~, ~l,~x/[~/~ ~ C. Van Li nebei~j~r Reviewed bY'~'A.~ Marc Shannon Supervising Prod. Engr. NOV 2 9 1990 Approved by' lD'] E. Howell Production Supt. Alaska Oil & Gas Cons. CommiSsion Anchorage cc' DEH, PMS, MPU Sr. Fm. (2), CVL, Original to File' G-4 Well File ~"'~~ R ! L! FT EQ U l PM E I~"(r-'~OTAT I O N A ~3Ker Hughes company 200 W. Stuart Roosa Dr, · Claremore, Oklahoma 74017 · (918) 341-9600 DATE 8- 02 - 90 O U-O-TATI O I~ NO. Dz2f3-u6'"22~3fBJ ~RE~ENTI~D ElY - 'S. Hesl:et' CAPACITY TOTAL IflEAD FREQUENCY CONOCO ~psC Office Bo~ 3&00~5 Prudhoe Bay, AK., 997}4 _ ii - , · i i i ii ii . _ i -- . mi iii il - ii ii · _ '~JEL L NAME: (~'4 FIELD NA~tE; Mil'ne PO~n£ ' I~OCATION: ' Pru~oe ~ay,- ~K SP, GR. El.ti.T, G.D,R. NET LIFT FREQUENCY MOTOR H.P. 65 RATING PUMP STAGES PUMP INTAKE PUMP DSCHRG. GAS SEPARATOR SEAL SECTION POWER CABLE FLAT CABLE FLAT GUARDS CABLE SADDLES ElANDS CABLE BANDS SWAGED NIPPLE CHECK VALVE DRAIN VALVE EQUIPMENT COATING: MOTOR CONTROLLER ACCESSORIES INCLUDE: P£RFS P.RI MARY VOLTAGE CASING O.D. SURFACE PSi ~-00 WEIGHT ~ 60 H E RTZ VOLTAGE 12.~0 AMPERAGE 30 SERIES 562 MODEL ~ LENGTH TYPE ~ HaG. NO. ~ SERIES ~00 MODEL F~L1 LENGTH SERIES MODEL LENGTH S~:RIES MODEL LENGTH SERIES MODEL LENGTH SERIES 513 MODEL GS]~ LENGTH AWG TYPE. LE,~GTH SE~,E$ TYPE LEN~T,~ TYPE MODEL OVERLOAD ~ AUTO RESTART VARIABLE FREQUENCY CONTROLLER: TRANSFORMERS SIZE PRIMARY TAPS VARIABLE FREQUENCY TRANSFORMER JUNCTION BOX (VENTED-$AFETYi TUBING HEAD PY,.D PHD (Surface TnducCor ?acka e) Ada 400 x 513 CONOCO Mods for ICS Dr~ve ' SETTING DEPTH REg. SURFACE VOLTAGE TUBING SIZE FRICTION LOSS L3 $0 HERTZ NO, PCS NO. PCS. 1 6.3 CONN. ARMO~ ARMOR LENGTH SIZE VOLTAGE UNDERCURRENTS. D. ~ RECORDING AMMETER LT. LIGHTING ARRESTER ~ OTHER KVA TYPE SECONDARY TAPS KVA MulCt Tap Wet, GUIDE CABLE REEL NO. REEL SUPPORT SHIPPING CASE QTY, SIZ~ DiSCou~ , SIIIPPING CASE QTY SHIPPING CASE QTY, SIZE SHIPPING CASE QTY. SIZE NOTE: SERVICING EQUIPMENT MAY ~)E RETURNED FOR ~00~ CREOIT WITHIN 6 MO.. SUBJECT EQUAL TO 25% OF THE LIST PRICE. A REPAIR REQUIRED KVA TH R EAO ' T.-~.N." EEEIVED NOV 2. 9 1990 & Gas Cons. L;ummissio~ Rnohorage CONOCO MILNE POINT VSC System Performance VSC 66 kVA 1OeO hp 200 i~00 400 ~00 600 700 800 900 1000 1100 PUHP 18~ stage FC&50 HOTOR (60 H= rating) I~62 sert~ 65 hp 12~0 volt 30 amp EPERRY-SUN DRILLING SEI~.-C~ -- ANCHORAGE ALASKA PAGE CONOCO INC. G-4 MILNE POINT ALASKA COMPUTATION DATE: 9/19/89 TRUE SUB-SEA COURS MEASD VERTICAL VERTICAL INCLN DEPTH DEPTH DEPTH DG MN 0 .00 100 100.00 200 199.99 300 299.97 400 399.95 -59. 40. 140. 240. 340. 27 0 0 73 0 30 72 0 52 70 1 9 68 i 28 DATE OF SURVEY: 9-17-89 BOSS GYROSCOPIC SURVEY JOB NUMBER: AK-BO-90101 KELLY BUSHING ELEV. = OPERATOR: D. HARGER 59.27 FT. COURSE DLS TOTAL DIRECTION RECTANGULAR COORDINATES DEGREES DG/100 NORTH/SOUTH EAST/WEST N .00 E .00 .00 .00 S 85.70 E .50 .03S .44E S 85.50 E .37 .12S 1.63E S 78.60 E .31 .38S 3.38E S 79.00 E .32 .83S 5.64E VERT. SECT. .00 -.01 -.04 -.20 -.53 500 499.92 600 599.85 700 699.60 800 799.13 900 898.48 440. 540. 640. 739. 839. 65 58 33 86 21 1 19 2 46 4 58 6 1 7 2 N 89.70 E .31 1.07S 8.06E N 42.60 E 2.10 .71N 10.86E N 26.40 E 2.44 6.37N 14.42E N 20.70 E 1.19 15.17N 18.20E N 18.10 E 1.05 25.90N 21.97E -.64 1.30 7.14 16.12 27.05 1000 997.42 1100 1095.61 1200 1193.01 1300 1289.47 1350 1337.00 938. 1036. 1133. 1230. 1277. 15 34 74 2O 73 9 29 12 16 13 51 · 16 42 19 25 N 16.10 E 2.47 39.65N 26.16E N 13.40 E 2.84 57.92N 30.91E N 10.40 E 1.71 80.04N 35.53E N 6.70 E 3.02 106.09N 39.37E N 4.60 E 5.59 121.52N 40.88E 41.00 59.50 81.83 108.06 123.55 1400 1383.68 1500 1475.22 1600 1566.13 1700 1657.15 1800 1747.27 1324.41 1415.95 1506.86 1597.88 1688.00 22 24 24 24 26 33 51 22 32 46 N 2.70 E 6.41 139.40N 42.00E N 1.50 E 2.34 179.56N 43.45E N 1.70 E .48 221.20N 44.61E N 1.80 E .17 262.59N 45.88E N 1.50 E 2.22 305.87N 47.12E 141.46 181.64 223.28 264.68 307.96 1900 1835.82 1776. 2000 1923.45 1864. 2100 2010.80 1951. 2200 2097.88 2038. 2300 2184.75 2125. 55 18 53 61 48 28 29 29 29 29 35 0 15 38 44 N 1.70 E 1.82 352.30N 48.42E N 1.50 E .43 400.46N 49.76E N 1.80 E .28 449.12N 51.16E N 1.70 E .40 498.26N 52.67E N 3.20 E .75 547.75N 54.78E 354.39 402.55 451.22 500.37 549.90 2400 2271.34 2212. 2500 2358.88 2299. 2600 2447.48 2388. 2700 2536.25 2476. 2800 2625.68 2566. 07 30 16 61 27 32 21 27 43 98 27 5 41 26 4 N 3.50 E .55 597.67N 57.71E N 1.30 E 2.93 645.95N 59.77E N .70 E .33 692.32N 60.58E N 1.50 E .73 738.33N 61.46E N 2.40 E 1.09 783.06N 62.98E 599.91 648.23 694.57 740.57 785.31 2900 2715.54 2656. 3000 2806.11 2746. 3100 2897.15 2837. 3200 2987.21 2927. 3300 3076.50 3017. 27 84 88 94 23 25 57 24 12 24 40 26 48 26 43 N 3.10 E .33 826.87N 65.08E N 4.10 E 1.80 869.16N 67.73E N 3.10 E .63 910.44N 70.32E N 2.80 E 2.14 953.80N 72.55E N 2.60 E .13 998.79N 74.67E 829.17 871.54 912.91 956.33 1001.36 Cons, ~SPERRY-SUN DRILLING SE. ANCHORAGE ALASKA CONOCO INC. G-4 MILNE POINT ALASKA COMPUTATION DATE: TRUE MEASD VERTICAL DEPTH DEPTH · 3400 3166.18 3500 3256.37 3600 3346.29 3700 3435.35 3800 3524.13 PAGE 9/19/89 DATE'OF SURVEY: 9-17-89 BOSS GYROSCOPIC SURVEY JOB NUMBER: AK-BO-90101 KELLY BUSHING ELEV. = 59.27 FT. OPERATOR: D. HARGER SUB-SEA COURS COURSE DLS TOTAL VERTICAL INCLN DIRECTION RECTANGULAR COORDINATES VERT. DEPTH DG MN DEGREES DG/100 NORTH/SOUTH EAST/WEST SECT. 3106.91 25 47 N 3.00 E .94 1042.98N 76.83E 1045.60 3197.10 25 21 N 2.70 E .46 1086.10N 78.98E 1088.78 3287.02 26 31 N 2.10 E 1.20 1129.81N 80.81E 1132.52 3376.08 27 34 N .50 E 1.27 1175.27N 81.83E 1177.97 3464.86 27 13 N 1.10 E .44 1221.28N 82.47E 1223.95 3900 3613.19 4000 3702.92 4100 3793.58 4200 3884.76 4300 3976.57 3553.92 26 52 N .70 E .39 1266.76N 83.18E 1269.40 3643.65 25 28 N .90 E 1.41 1310.87N 83.80E 1313.48 3734.31 24 26 N .90'E 1.03 1353.05N 84.46E 1355.63 3825.49 24 4 N 1.80 E .52 1394.12N 85.43E 1396.69 3917.30 22 36 N 2.-30 E 1.47 1433.71N 86.84E 1436.30 4400 4069.34 4010.07 21 11 N 1.00 E 1.50 1470.98N 87.93E 1473.58 4500 4162.69 4103.42 20 51 N .30-E .42 1506.85N 88.33E 1509.42 4600 4256.21 4196.94 20 37 N .20 E .23 1542.26N 88.49E 1544.78 4700 4349.86 4290.59 20 25 N .70 W .37 1577.32N 88.34E 1579.78 4800 4443.61 4384.34 20 17 N 1.00 W .17 1612.10N 87.82E 1614.49 4839 4480.19 4420.92 20 17 N 1.10 W .09 1625.63N 87.57E 1627.99 THE CALCULATION PROCEDURES ARE BASED ON THE USE OF THREE-DIMENSION RADIUS OF CURVATURE METHOD. HORIZONTAL DISPLACEMENT = 1627.99 FEET AT NORTH 3 DEG. 5 MIN. EAST AT MD = 4839 VERTICAL SECTION RELATIVE TO WELL HEAD VERTICAL SECTION COMPUTED ALONG 3.08 DEG. REi EIVED NOV 2 9 1990 ~l~sl~ Oil & Gas Cons. comm'~ss~on ~mchorage SPERRY-SUN DRILLING SEk ANCHORAGE ALASKA PAGE 3 CONOCO INC. G-4 MILNE POINT ALASKA COMPUTATION DATE: 9/19/89 DATE OF SURVEY: 9-17-89 JOB NUMBER: AK-BO-90101 KELLY BUSHING ELEV. = 59.27 FT. OPERATOR: D. HARGER INTERPOLATED VALUES FOR EVEN 1000 FEET OF MEASURED DEPTH TRUE SUB-SEA TOTAL MEASD VERTICAL'VERTICAL RECTANGULAR COORDINATES MD-TVD VERTICAL DEPTH DEPTH DEPTH NORTH/SOUTH EAST/WEST DIFFERENCE CORRECTION 0 .00 -59.27 1000 997.42 938.15 2000 1923.45 1864.18 3000 2806.11 2746.84 4000 3702.92 3643.65 .00 .00 .00 39.65 N 26.16 E 2.58 2.58 400.46 N 49.76 E 76.55 73.97 869.16 N 67.73 E 193.89 117.34 1310.87 N 83.80 E 297.08 103.19 4839 4480.19 4420.92 1625.63 N 87.57 E 358.81 THE CALCULATION PROCEDURES ARE BASED ON THE USE OF THREE-DIMENSION RADIUS OF CURVATURE METHOD. 61.73 R.i 'EEIVED NOV 2 9 :Oil & Gas Cons. ~n(~horage SPERRY-SUN DRILLING SER,~CA- ANCHORAGE ALASKA PAGE CONOCO INC. G-4 MILNE POINT ALASKA COMPUTATION DATE: 9/19/8.9 DATE OF SURVEY: 9-17-89 JOB NUMBER: AK-BO-90101 KELLY BUSHING ELEV. = 59.27 FT. OPERATOR: D. HARGER INTERPOLATED VALUES FOR EVEN 100 FEET OF SUB-SEA DEPTH TRUE SUB-SEA MEASDVERTICAL'VERTICAL DEPTH DEPTH DEPTH 0 .00 -59.27 59 59.27 .00 159 159.27 100.00 259 259.27 200.00 359 359.27 300.00 TOTAL RECTANGULAR COORDINATES NORTH/SOUTH EAST/WEST .00 .00 .01 S .08 E .08 S 1.01 E .22 S 2.57 E .63 S 4.61 E MD-TVD VERTICAL DIFFERENCE CORRECTION .0O .0O .00 .00 .00 · 02 .01 · 04 .02 459 459.27 400.00 559 559.27 500.00 659 659.27 600.00 759 759.27 700.00 860 859.27 800.00 961 959.27 900.00 1062 1059.27 1000.00 -1165 1159.27 1100.00 1268 1259.27 1200.00 1373 1359.27 1300.00 1.07 S 7.12 E .72 S 9.53 E 3.24 N 12.86 E 11.23 N 16.72 E 21.30 N 20.46 E 33.52 N 24.39 E 50.58 N 29.10 E 71.85 N 34.03 E 97.38 N 38.26 E 129.73 N 41.45 E .07 .03 · 11 .04 · 25 .14 .64 .39 1.22 .58 2.05 .83 3.61 1.56 5.98 2.37 9.28 3.30 14.47 5.20 1482 1459.27 1400.00 1592 1559.27 1500.00 1702 1659.27 1600.00 1813 1759.27 1700.00 1926 1859.27 1800.00 2040 1959.27 1900.00 2155 2059.27 2000.00 2270 2159.27 2100.00 2386 2259.27 2200.00 2500 2359.27 .2300.00 172.18 N 43.26 E 23.15 8.68 218.09 N 44.52 E 33.20 10.04 263.56 N 45.91 E 43.06 9.86 311.92 N 47.28 E 54.17 11.11 365.08 N 48.80 E 67.44 13.27 420.32 N 50.28 E 81.69 14.25 476.31 N 52.01 E 96.31 14.62 533.22 N 53.97 E 111.39 15.08 590.64 N 57.28 E 126.75 15.36 646.15 N 59.78 E 141.17 14.42 2613 2459.27 2400.00 2725 2559.27 2500.00 2837 2659.27 2600.00 2948 2759.27 2700.00 3058 2859.27 2800.00 3168 2959.27 2900.00 3280 3059.27 3000.00 3392 3159.27 3100.00 3503 3259.27 3200.00 3614 3359.27 3300.00 698.51 N 60.65 E 154.05 12.88 750.10 N 61.77 E 166.58 12.53 799.49 N 63.67 E 178.13 11.55 847.97 N 66.25 E 189.30 11.16 893.08 N 69.38 E 199.05 9.75 939.70 N 71.86 E 990.12 N 74.28 E 1039.64 N 76.66 E 1087.47 N 79.05 E 1136.29 N 81.05 E 209.42 10.38 221.44 12.02 233.06 11.62 243.94 10.88 ~55 24 11.30 REEEIVED NOV 2-9 1990 .Oil.& Gas Cons. commission chorage SPERRY-SUN DRILLING ANCHORAGE ALASKA PAGE 5 CONOCO INC. G-4 MILNE POINT ALASKA COMPUTATION DATE: 9/19/89 DATE OF SURVEY: 9-17-89 JOB NUMBER: AK-BO-90101 KELLY BUSHING ELEV. = 59.27 FT. OPERATOR: D. HARGER INTERPOLATED VALUES FOR EVEN 100 FEET OF SUB-SEA DEPTH TRUE SUB-SEA MEASD VERTICA~VERTICAL DEPTH DEPTH DEPTH 3726 3459.27 3400.00 3839 3559.27 35'00.00 3951 3659.27 3600.00 4062 3759.27 3700.00 4172 3859.27 3800.00 TOTAL RECTANGULAR COORDINATES MD-TVD VERTICAL NORTH/SOUTH EAST/WEST DIFFERENCE CORRECTION 1187.76 N 81.94 E 267.72 12.48 1239.36 N 82.82 E 280.25 12.53 1289.96 N 83.48 E 292.33 12.08 1337.46 N 84.22 E 303.04 10.71 1382.74 N 85.07 E 312.82 9.78 4281 3959.27 3900.00 4389 4059.27 4000.00 4496 4159.27 4100.00 4603 4259.27 4200.00 4710 4359.27 4300.00 1426.51 N 86.55 E 321.99 9.18 1467.08 N 87.86 E 329.93 7.93 1505.55 N 88.33 E 337.07 7.15 1543.41 N 88.49 E 344.00 6.93 1580.82 N 88.29 E 350.77 ' 6.77 4816 4459.27 4400.00 4839 4480.19 4420.92 1617.89 N 87.72 E 357.42 6.65 1625.63 N 87.57 E 358.81 1.39 THE CALCULATION PROCEDURES USE A LINEAR INTERPOLATION BETWEEN THE NEAREST 20 FOOT MD (FROM RADIUS OF CURVATURE) POINTS 1 RE .EIVED NOV ? 9 1990 Alaska 0il & Gas Cons. CommiSS'~on Anchorage STATE OF ALASKA ALASK^ OIL AND GAS CONSERVATION COMMISSION REPORT OF SUNDRY WELL OPERATIONS 1. Operations performed: Operation shutdown X stimulate ~ Plugging Pull tubing __ Alter casing Repair well __ 2. Name of Operator CONOCO THC. PRUDHOE BAY, ALASKA 99734, Perforate X Other X 0 RIG i 5. Type of Well: Development .__X Exploratory __ Stratigraphic __ Service __ 3. Address BOX 340045 feet 4. Location of well at surface 3466' FNL, 3370' FEL, Section 27, T13N, RIOE, UH At top of productive interval 2719' FNL, 3308' FEL, Section 27, T13N, RIOE, UN i At effective depth 1799' FNL, 3282' FEL, Section 27, T13N, RIOE, UN At total depth measured 4950 ' feet Plugs (measured) N/A true vertical 4584 ' feet 12. Present well condition sUmmary Total depth: Effective depth: measured 4849 ' feet Junk (measured) N/A true vertical 4491 ' feet 6. Datum elevation (DF or KB) KB-59.3' NSL 7. Unit or Property name Nilne Point Unit 8. Well number G-4 9. Permit number/approval number 10. APl num [;er 4 50- 029-2194:1 11, Field/Pool Upper Cretac. - 14 Sak Cemented Measured depth True vertical depth 60 bbls Arc Set 110'RKB 110'RKB 189 I~1~t~ Permf E 2674' RKB 2454'RKB 112 Class G 125 BBLS CLASS G 4924'RKB 4565'RKB Casing Length Size Structural N/A Conductor 80' 13-3/8"48#/Ft Surface 2643' 9-5/8"47#/Ft Intermediate N/A Production 4901' 7" 29&26#/Ft Liner N/A Perforation depth: measured 4480' -4514' - 4555' -4576' true vertical 4143'-4176'- 4213'-4223' Tubing (size, grade, and measured depth) 2-7/8", 6.4#/FT, L-80, EUE, RECEIVED Productj on Foremar~ ISigned _.~~)~(~;--~ Title Senior Form 10-404 Rev 06/15/88 SUBMIT IN DUPLICATE Subsequent to operation 390 .... 5 15. Attachments } 16. Status of well classification as: Copies of Logs and Surveys run __ Daily Report of Well Operations ~ Oil X_ Gas __ Suspended __ 17. I hereby certify that the foregoing is true and correct to the best of my knowledge. Prior to well operation N/A 143 PSIG 65 PSTG Service 13. Stimulation or cement squeeze summary SAND FRACTURE ON OA&OB SANDS SEPERATELY. Intervalstreated(measured) OA SAND 4480'-45:14' & OB SAND 4555'-4576' Treatment description including volumes used and final pressure OA SAND--PUHPED 20.098 LBS. SAND (FTD=4223 PSZG)OB SAND--PUHPED 21,736 LB~:' OF SAND (FTP--3995 PS]G) 14, Representative Daily Average Production or Injection Data OiI-Bbl Gas-Md Water-Bbl Casing Pressure Tubing Pressure Date Packers and SSSV (type and measured depth)A BAKER RETR]:EVABLE PACKER SET g4395' RKB. ,' ,/'~ska.Oil.& Gas Cons. Commission 4395 ' RKBr.Anch0rage Conoco Inc. Milne Point Operations Center Pouch 340045 Prudhoe Bay, AK 99734 (907) 659-6300 MR. LONNIE SMITH STATE OF ALASKA OIL AND GAS COMMISSION 3001 PORCUPINE DRIVE ANCHORAGE, AK 99501 DEAR MR. SMITH, FOLLOWING IS THE DAILY REPORT OF WELL OPERATIONS FOR THE G-4 COMPLETION: l)i:tTE OPERATION 03/07/90- 03/10/90 03/12/90- 03/14/90 03/15/90- 03/16/90 03/17/90 03/18/90- 03/24/90 03/25/90 03/27/90 04/24/90 04/25/90- 05/01/90 05/02/90 05/03/90- 05/06/90 05/07/90 05/08/90- 05/10/90 05/11/90 05/12/90 MI RU WORKOVER RIG. N/D TREE, N/U BOP's AND PRESSURE TEST -- OK. PERFORATE 0 SANDS. DST 0 SANDS. RIH W/ ELECTRIC SUBMERSIBLE PUMP. WELL TEST AND PRESSURE BUILD UP SURVEY. END PRESSURE BUILD UP SURVEY AND POOH W/ ELECTRIC SUBMERSIBLE PUMP. SET HALLIBURTON RTTS RETRIEVABLE PACKER @ 4387', FREEZE PROTECT WELL, N/D STACK, N/U & TEST TREE TO 5000 PSIS -- OK. INSTALL BPV AND MOVE RIG OFF WELL. MIRU WORKOVER RIG, N/D TREE, N/U BOP's AND PRESSURE TEST -- OK. PERFORATE AND SAND FRAC 0 SANDS -- POST FRAC CLEAN OUT. RIH W/ ELECTRIC SUBMERSIBLE PUMP. WELL TEST AND PRESSURE BUILD UP SURVEY SEQUENCE. N/D BOP's, N/U AND TEST TREE TO 5000 PSIS -- OK, INSTALL BPV AND MOVE RIG OFF WELL. TEST WELL. MIRU WORKOVER RIG, N/D TREE, N/U BOP'S AND PRESSURE TEST -- OK. POOH W/ ELECTRIC SUBMERSIBLE PUMP, RIH AND SET BAKER RETRIEVABLE PACKER AT 4395' RKB. FREEZE PROTECT WELL, N/D BOP's, N/U AND TEST TREE TO 5000 PSIS -- OK. MOVE RIG OFF WELL. EOR RESPECTFULLY, DR ILL I NS FOREMAN APPLICATION FOR SUNDRY APPROVALS 1. Type of Request: Abandon __ Suspend __ Alter casing __ Repair well Change approved program ~ 0 R I G IN IC)k. 2. Name of Operator CONOCO INC. 3. Address 4. 'Location of well at surface 3466' FNL, 3370' FEL, Sect, ion 27, At top of productive interval i 27:19' FNL, 3308' FEL~, Sect, ion 27, At effective depth ' :1799' FHL, 3282' FEL, Section 27, At total depth Operation shutdown -X- Re-enter suspended well __ Plugging __ Time extension ~ Stimulate ~ Pull tubing ~ Variance __ Pedorate ~ Other 5. Type of Well: Development --X Exploratory __ Stratigraphic __ Service __ 1,2. Present well condition summary Total depth: measured true vertical Effective depth: measured true vertical Casing Length Structural Conductor 80' Surface 2643 ' Intermediate T13N, RIOE, UH T:13N, RIOE, UH. T13N, RIOE, UH 6. Datum elevation (DF or KB) KB-27.95' HSL 7. Unit or Property name ~!LHE P0!.qT 'J.".!T 8. Well number G-4 9. Permit number 89-45 10. APl number 5o- n~q-~1Q41 11. Field/Pool Upper Cret-l~ Sak 4950' feet Plugs (measured) N/A 4584' feet 4849, feet Junk (measured) N/A 4491' feet Size Cemented Measured depth True vertical depth 13-3/8"48#/Ft 60~bbls Arc Set 9- 5/8"47#/?~218o9o11~b~ alPs~rmaf E 110'RKB 110'RKB 2674'RKB 2454' RKB feet Production 4901' 7" 29&26#/FT 125 BBLS CLASS G 4929'RKB ~, 4565'RKB Liner ,...11,, N~'Ci~/k~ U Perforation depth: measured 14480' -45:14' 4555'-4576' true vertical 4:143'-4:176' "~/'~ O/7/V O 4 ]..qo 42:13'-4223' ' '.e 8e,~ Tubing (size, grade, and measured depth) 2-7/8", 6.4#/Ft, L-80, EUE, 4395' RKB ~/Zego~.?~.Co~' Packers and SSSV (type and measured depth) BAKER RETRZEVABLE BRZDGE PLUG SET e4395' RKB Description summary of proposalx._ Detailed operations program __ BOP sketchx_. 13. Attachments 14. Estimated date for commencing operation Date apprOved 16. If proposal was verbally approved Name of approver 15. Status of well classification as: Oil ~(._ Service Gas ~ Suspended__ knowledge. 17. I hereby certify that the foregoing is true and correct to the best of m, Title RR' PRODUCTION FORFMAN FOR COMMISSION USE ONLY Date i Approval No. ~JC) ,--- q.,.~ Plug integrity __ BOP Test'~._ Location clearance __ Mechanical Integrity Test_ Subsequent form required 10- Conditions of approval: Notify Commission so representative may witness ORIGINAL SIGNED BY LONNIE C. SMITH Approvea Cop~j Returned Commissioner Approved by order of the Commission SUBMIT IN TRIPLICATE Form 10-403 Rev 06/15/88 Conoco Inc. Milne Point Operations Center Pouch 340045 Prudhoe Bay, AK 99734 (907) 659-6300 MR. LONNIE SMITH STATE OF ALASKA OIL AND GAS COMMISSION 3001 PORCUPINE DRIVE ANCHORAGE, AK 99501 RE: LETTER OF APPLICATION DEAR MR. SMITH, I AM REQUESTING SHUTDOWN OF WELL OPERATIONS FOR THE G-4 WELL UNTIL THE CONTRACTED WORKOVER RIG CAN FINISH WITH COMPLETION OPERATIONS AND STIMULATION WORK ON THE KUPARUK WELLS. ALSO, WE WILL REQUIRE TIME TO CONSTRUCT THE PRODUCTION FACILITIES FOR THE G-PAD PRODUCTION. THE WELL WAS FREEZE PROTECTED, A RETRIEVABLE BRIDGE PLUG WAS SET IN THE WELL AT 4395', AND THE WELLHEAD TREE WAS FLANGED UP AND PRESSURE TESTED TO 5000 PSIG. CONOCO WILL SUBMIT THE APPLICATION FOR SUNDRY APPROVAL TO RE- ENTER THE SUSPENDED G-PAD WELLS UPON COMPLETION OF THE ABOVE OPERATIONS. RESPECTFULLY, J.D. POLYA DR ILL I NG FOREMAN '~ ' STATE OF ALASKA - ALASKA OIL AND GAS CONSERVATION COMMIS~ION 0 APPLICATION FOR SUNDRY APPROVALS 1. Type of Request: 2. Name of Operator CONOCO INC. 3. Address lC St 4. Location of well at surface 3466' FNL, 3370' At top of productive interval 2719' FNL, 3308" At effective depth 1799" FNL, 3282" At total depth Abandon __ Suspend __ Operation shutdown Alter Casing __ Repair well __ Plugging __ Change approved program ~ Pull tubing -.3r,. Variance __ 5. Type of Well: Development Exploratory Stratigraphic Anchorage 99503 Service __ Re-enter suspended well __ Time extension __ Stimulate X Perforate _][. Other 12. Present well condition summary FEL, Section 27, T13N, R10E, UM FEL, Section 27, T13N, R10E, OM FEL, Section 27, T13N, R10E, UM 6. Datumti~v..a~q~ !D~r.K~sL feet 7. Unit or Property name MILNE POINT UNIT 8. Well number G-4 9. Permit number 89-49 10. APl number 50-- 029-21941 11. Field/Pool Upper Cret-W Sak Total depth: meaS'ured true vertical Effective depth: measured true vertical 4950' feet 4584' feet 4849' feet 4491' feet PlUgs (measured) N/A Junk (measured) N/A Casing Length Structural Conductor 80 ' Surface 2 643 ' Intermediate Production 4901 ' Liner Size Cemented 13-3/8"48#/Ft 60 bbls 9-5/8"47#/Ft ~:~ ~}~ 7" 29&26#/PT 9.2#PPG Perforation depth: measured 4480'-4514' 4' SHOTS/FT 4555'-4576' 4' SHOTS/FT true vertical 4143 ' -4176 ' 4213'-4223' Measured depth Tubing (size, grade, and measured depth) 2-7/8", 6.4#/Ft, L-80, APR 1990 True~pth Arc Set 110, RKB 110 ' RKB 2674' RKB 2454'RKB NACL AND DIESEL COMPLETION S EUE, !4478' Packers and SSSV (type and measured depth) 7", 26#/PT RTTS RETRIEVABLE PACKER @ 4387' 13. Attachments Description summary of proposal ~ Detailed operations program __ BOP sketch __ 14. Estimated date for commencing operation 16. If proposal was verbally approved Name of approver ~~, ~ .~ ~ A Date approved Service 17. I hereby certify th~ the fjaregoing is true and correct to the best of my knowledge. Signed ~o~J- //%~~ ~ ~J%03,,~9' Title PRODUCTION FOREMAN FOR COMMISSION USE ONLY 15. Status of well classification as: Oil _~ Gas __ Suspended Date Conditions of approval: Notify Commission so representative may witness Plug integrity __ BOP Test __ Location clearance Mechanical Integrity Test __ Subsequent form required 1"~'- "~-c~ Approved by order of the Commission ORIGINAL SI6NED BY LONNIE C. SMITH [ Appr°v~% ..~u · ~ Date~%__¢~_r~, ~,~) Form 10-403 Rev 06/15/88 SUBMIT IN TRIPLICATE.. ,,~ oo~ STIMULATION PROCEDURE Reperf &Frac Well Milne Point Unit S=urface Location: 3,366' FNL, 3,370' F£L, Sec. 27, T13N, RIOE, UM ~: All depths are measured from KB datum. Cas~9.g: Surface - I3 3/8", 72#/ft, L-80 btrs., set at 2,630'. Production - 7", 26#/ft, L-80, btrs., set_ at 4,929' Capacity: 3.75 bbl/lO0' Burst Pressure: 7,240 psig Tubing; 2 7/8", 6.5#/ft, L-80, EUE e 4,477' Capacity: 0.579 bbl/lO0' Capacity of tubing/casing annulus: 3.02 bbl/lO0' Burst Pressure: 10,570 psig (no safety factor) Present Completion- SOS "OA" 4 480'-4,514' "OB" 4 554'-4 ~i70' 4 572'-4,576' ,, .._ · 1 ~ , Il , Y ~resent Status' Shut-in pending frac. Objectiv..e: Reperforate and fracture stimulate the "OA" & "OB" sands. Recgmmended Proq. edure: Hold a meeting with all contractors to discuss job requirements ~nd safety prior to the job. 2) Nipple down the wellhead and nipple up the BOPs. Release RTTS packer set at 4,387' and POOH with tubing. 3) Rig up electric line company and wireline pressure control equipment. Run a GR/CCL from 4,600'- 4,350'. Correlate with the attached CNL/LDI' log dated ' 9/11/89. Perforate the intervals from 4,480'-4,514' and 4,554'-4,576' with 4 SPF. Perf depths are based on. the attached log dated 9/11/89. POOH and rig down perforating company. PERFO.RATION DET~AIL I N~_TERVA~LL F EE_____~T S P___EF ~I.OTAL..SHOTS ?~HAS IN~ E H____QD EC~P 4,480'-4,514' 34 4 136 90 deg 0.46 10.88 4,554'-4,576' 22 4 88 90 deg 0.46 10.88 Perforate with 4" casing guns with four runs of 14' each. The minimum recommended specs for EHD and £CP are listed above. Dist. DLB, PMS, JDC, MPU Senior Foreman I Fracture MPU Well G-4 April 20, 1990 Page 2 4) Pick up RTTS packer, a ?", 26 #/ft bridge plug ~nd in-~tall an "X" nipple located one Joint above the packe~. RIH with tubing anti set; the plug at 4 620' pull up and set_the ~oacker at 4,535',., RIX wi~h $1tckline and set a ' Retri the plug in the nipple. (1)~esstire t~t-"t~he ~ubing to 6,000 psi_~ eve plug. 6) Spot two 500 bbl frac tanks on location approximately 150' from the wellhead, Elevate the rear of the tanks approximately 8". Visually inspect the interior of the tanks for cleanliness (do not climb into the tanks). Fill each tank with 500 bbls. of clean MPU injection water filtered to 10 microns. The water should be heated and maintained at 75-80 degrees F in order to insure proper hydration of the gelling agent. 7) Rig up service company pump lines {use no threaded cross-overs, swedges or valves). Install two shut-off valves on the wellhead. Use two in-line densitometers.~/~Set up backup pumps for crosslinker and diesel. Rig up annulus pump to inject clean 2% KCL brine ( filtered to 10 microns) into the "OA"sand during the "OB" frac job. 8) Batch mix 1,000 bbl. (42,000 gal.) gelling agent at 40 lbs/lO00 gal. and additives as prescribed in the Material Detail (Attached). The pre-pad consists of non-crosslinked gel. Particulate fluid loss additive should be in the pad and pre-pad only. Diesel and crosslinker activator are the only additives that should be mixed on the fly. Sand will be added in the prescribed stages through the blender. 9} Fill out the fluid report forms, Check all additives against the attached material detail. Continuously roll the tanks until the viscosity is within the recommended limits {30 to 35 at 300 rpm on Fan 35 viscometer). Check samples from the top and bottom of the tank, values should correspond within 3 cps. lO) Hold a safety meeting with all personal on location. 11) Pressure test the surface lines and frac head to(7,0OO~psig and insure that there are no leaks. Set the pump trips at approximately 6,200 psig. Prepare to begin annular injection at a rate of 1 BPM and a pressure not to exceed !,000 psig. 12) Prepare to pump the "OB" frac job as follows- A) Standby pumps (50%) are required. These pumps must be manned and primed to immediately come on line if needed. A standby blender must be hooked up and ready to come on line in the case of primary blender failure. 004 Fracture MPU Well G-4 April 20, 1990 Page 3 B) Tank bottoms are included in the volumes listed in step 6. Leave 50 bbls tank bottom. C) Use the in-line densitometers during the Job, Record rate and pressure on a strip chart. Send the charts to the Anchorage office. D) Take samples of the crossl inked gel during the job. Place them in a water bath at 80 deg. F. Observe the samples and note when the gel breaks. E) Pre-Pad is not crosslinked and does not contain diesel oil. F) DO NOT OVER DISPLACE. Frac Rate: 25 BPM Maximum Allowable Surface Pressure: 6,000 psig ~ 25 BPM Anticipated Surface Pressure: 2,500 - 3,000 psig Gel Diesel Cum Sand Cum Fluid Pump Time .(.qal ) ~(gal ) ~ ...lbs. (1 bs..~) (.gat ~.) ~ P-Pad 4,000 4,000 3.8 Pad 6,840 360 11,200 10.7 1 1,983 104 4.0 8,349 8,349 13,600 13.0 2 1,755 92 8.0 14,774 23,124 16,000 15.2 Flush 1,061 17,061 16.2 Totals 15,639 556 23,124 23,124 17,061 16.2 Cum fluid:gel+diesel+sand Pre-Pad and Pad should contain 50#/lO00gal. fluid loss additive. Surfactant and non-emulsifier should be batch mixed with all fluid except flush. 13) Shut down. Allow the pressure to bleed off into the Formation. Record the ISIP, 5minute, 10 minute and 15 minute pressures. Close all surface valves and leave the well shut-in. Have the service company monitor the break time of the last sample collected. 14) Rig up slickline. Run in the hole and tag fill. If Kill is present above 4,545', release packer, pull up and reset 4,450'. If fill is not above 4,545', release packer and circulate sand down the tubing to achieve the required fill depth. If it is necessary to circulate sand, the concentration should not exceed 2 ppg. When the required sand fill is in place, pull up and set packer at 4,450'. NOTE: Maintain 2000 psig pressure on the annulus during the "OA" frac job. 04×20×90 Fracture MPU Well G-4 April 20, 1990 Page e, 15) Prepare to pump the "OA" frac job as follows: Frac Rate: 25 BPli Maximum Allowable Surface Pressure: 6,000 psig g 25 BPM Anticipated Surface Pressure: 2,500 psig to 3,000 psig Gel Diesel Cum Sand Cum Fluid Pump Time Staqe ~ ~ ~ lbs_ . (lbs.) (aal.) . Min~utes P-Pad 4,000 4,000 3.8 Pad 7,980 420 12,400 11.8 ! 2,313 122 4.0 9,741 9,741 15,200 14.5 g 2,047 108 8.0 17,937 26,978 18,000 17.1 FLUSH 1,040 19,040 18.1 Totals 17,380 650 26,978 26,978 19,040 18.1 Cum fluid--gel+diesel+sand Pre-Pad and Pad should contain 50#?lO00gal. fluid loss additive. Surfactant and non-emulsif(er should be batch mixed with all fluid except flush. 16) Shut down. Allow the pressure to bleed off into the formation. Record the ISIP, 5 minute, 10 minute and 15 minute pressures. Close all surface valves and leave the well shut-in. Have the service company monitor the break time of the last sample collected. Rig down the service company. 17) Release packer and allow fluid level Lo stabilize. POOH with packer &nd tubing displacing out with diesel. RIH with hydrostatic .bailer and clean out sand to the bridge plug located at 4,6~20'. POOH. RIH and retrieve the bridge plug. 18) Pick up ESP complete with surface readout of the BHFP. RIH and set the pump so the bottom of the motor is located at 4,400'. (.Nipple down BOPs and ~ nipple up t~ne tree.~ Pressure test the tree to 5,000 psig. Connect the surface lines and pressure test to 3,000 pslg. 19) Bring the well on production at an initial choke setting of 8/64 and the ESP controller set at 40 hz. Slowly open the choke to 64/64 over a 24 hour period. Allow the well to produce at this choke setting until the rate and fluid cuts stabilize. Report production data to engineering on a daily basis. 006 Fracture MPU Well G-4 April 20, 1990 Page 5 HATERI.AL DETAIL Clean MPU injection water (Filtered to 10 microns) KCL (2%) Gelling Agent (40#/lO00gal Hydroxypropylguar) Noni°nic Surfactant (2 gal./I,000 gal) Non-Emulsifier (2 gal/lOOOgal) Cross Linker (3#/lO00gal) Anti-Foamer (Sgal/tank) Bio¢tde (500 ppm) 45,000 gal, 7,500 lbs. 1,680 lbs. 84 gal. 84 al. 126 ~bs 10 gal. 21 gal. 1,206 lbs. FLA (50#/]O00gal Pad and Pre-Pad only) Breaker (80 deg reservoir temperature) As recommended by Service Co. ' 1,180 gal. Diesel 50,100 lbs. 10-20 Carbo-Light Prop TREATMENT HYDRAULICS_ Maximum Rate: 25 BPM Average Anticipated Pressure: 3,000 ps~g Estimated Hydraulic Horsepower: 1,840 hhp (An additional SO% hp capacity is required on location) Backside pump capable of maintaining g,O00 psig static surface pressure is required. The following backup equipment is required: 1) 50% backup on primary injection pumps, 2) 100% blender backup. 3) 100%, backup on diesel and crosslinklng pumps. Prepared By: Steve Rossber.q Senior Production Engineer Approved By: Supervising Production Engineer Field Superintendent --- 7", Zct'~/~:v, L-"~oO ,TM 0'~-.~. Conoco Inc. · _ '~f:~T-tO/~ O~ C.~- x__~ CalCulation Sheet Job No. Fie~d St~t~ CONOCO. MIl. NE POINT UN[/-~ BOP STACK FOR 9-5/8" SURFACE CASING FILL-UP LIR[ FLOw LIN[ ANNULAR (l) o)%" APl ~oooe NAM lOP ~ ~ l~ NAM . _ ~ RAM loft IlDC OUTL[TS~I SPOOL )' APl ~000~, CSG ll:; .-. ..... . Threade~ ' . ' ' .. Connection . ~-~/8"c,s,.o .[ · .: I I!.. ~ - ~ ' · .' , . .' .. ' Ii o : ' · - .'.," ''' · '11 ~ ~ .. ' '. "'.'. -',..~11 '.. . I$ l/t · AFl ~000 lk ~ I1%" ,&FI ~0OOIt " ' APl $OOO SlOE OUTLI:TI · - I{I/I' APl (2) (~) · APl $0OOd · '11e APl $000 B.O.P. stock size ratinF meets APl RP 53 & spec 6A for class 511 with clamp & hub connectors all hydraulically operated. BOPE to be operated on each trip & pressure tested weekly. Hydraulic control system for BOPE to include (5) station control manifold located remote with 160 8ollon accumulator and reservoir unit and auxiliary enersy source for system activation. tSSio, s e t s GasC0ns'C°~mi ~ppropriate :~c, hO~ae~ rams. (5) Ram type BOP to include a minimum of one set of blind rams and tvo of pipe Choke and kill manifolds sho~n separately to meet APl R? 53 class 511 requirements. '90 5:30 STAI~ OF ~ ALASKA OIL AN]) GA~ CON~VATION CI31111S~ION DATE BOPE STACK: ' ' Test Pre~sure Petrol t: t Casing set 6;_C~,.ULATOR SYST~ Full charge pressure ~~0 Press after clo~uve P~GE. 00 ! psig psig Pump tncr clos press 200 psig pstg /'~'<:::) K_E. Ur,,Y ANO FLOOR ~FETY VALVI~ Upper Kelly Lower Kal ly Ball type l~s~de ~ C~oke manifold N~r valves Test pressure Test pressure ,~'~'~:7 Test pressure~'~ '~0_ Test pressure_~'~ '~~ Number flanges Ad~ustable choke~ / Hydraultcalty operated choke TEST R~ULTS t Faf t utes Test time/')//=~/~,, hfs Repair or replacame~c of failed e~uipment :O be a,~ede within ii i ....... , i m , ,,-* -- Distrlbu:~on: or~g - AC)GCC C.O0~ (rev 03117/89) Inspector: CONOCO MPU OPS CTF~ STATE OF ALASKA ALASKA OIL AND DATE Rig ~ Genera] housekeeptng Reserve p*~ _~/~ Trip %ask Pit gauge Fl~w~n~or Annul ar preYen~,er O~oke 1 i ne va 1 yes HC~ vel ye Ki'l! ]tne Yalve$ Cheek vel Ye V~sual Audio t/ __ ACCt~ULATOR SYSTE]~: f~ charge pressure Press after elo~ure _...KO0 0 Pump inet cTo$ pres, 200 pslg __~__mln Full charge pres~ attained Controls: Nest~ / R~ ~ Bt I nd sw~cch covet KE~Y ~D FL~ SAE~Y VALVe= L~r Koll~ ~ ~11 ~y~ ~ I nslde 5OF) ~ , .. psig , psig -- Number valve~ · Number flonges _. Adjustable chakes -- . __ HydrnuI~c.lly opere~ed choke Digit,button= otto - nOCCC ~ - Opera,or e - Supervisor Inspector; C.004 (rev 03/17/89) ' / STATE OF ALASKA ALASKA OIL AND GAS CONSERVATION COMMISSION APPLICATION FOR SUNDRY APPROVALS ORIGIN 1. Type of Request: Abandon __ Suspend__ Alter casing __ Repair well __ Change approved program __ 2. Name of Operator CONOCO INC. 3. Address 3201 C St $200. Anchoraae -- Operation shutdown __ · ,-P.= s.-.ter ?_,%_,'~_ .tied welL.-' /d.~c~' Plugging __ Time extension __ Stimulate __ Pull tubing __ Variance __ Perforate ~ Other ~ 5. Type of Well: 6. Datum elevation (DF or KB) Development ~ KB- 5 9 · 3 I MS L Exploratory __ Stratigraphic __ 7. Unit or Property name 99503 Service__ MILNE POINT UNIT 4. Location of well at surface 3466' FNL, 3370' FEL, Section 27, T13N, R10E, UM At top of productive interval 2719' FNL, 3308' FEL, Section 27, T13N, R10E, UM At effective depth 1799' FNL, 3282' FEL, Section 27, T13N, R10E, UM At total depth 12. Present well condition summary Total depth: measured true vertical 4950 ' feet Plugs (measured) N/A feet 4584' Effective depth: measured 4849 ' true vertical 4491 ' feet Junk (measured) N/A feet Casing Length Structural Conductor 80 ' Surface 2 643 ' Intermediate Production 4901' ?"29&26#/Ft Liner Perforation depth: measured 4480 ' -4514 ' 4554'-4576' feet 8. Well number G-4 9. Permit number 89-45 10. APl number 50-- 029-21941 11. Field/Pool Upper Cret-W Sak Size Cemented Measured depth 13-3/8"48#/Ft 60 bbls Arc Set true vertical 4143 ' -4176 ' 4213'-4223' True vertical depth Tubing (size, grade, and measured depth) 2-7/8", 110'RKB 110'RKB 2674'RKB 2454'RKB Blank 4570'-4572' 6.49/Ft, L-80, EUE, Packers and SSSV (type and measured depth)Retrievable @ +4150 ' RECEIVED FEB 2 6 1990 4 2 Rlaska..011 & Gas Cons. _Commi~ 0 ' ' ~ ~chora~ 13. Attachments Description summary of proposalX_ Detailed operations program __ BOP sketch:~r~_ 14. Estimated date for commencing operation f4ar~h 1. 1990 16. If proposal was verbally approved Name of approver Date approved 15. Status of well classification as: Oil ~ Gas __ Suspended Service 17. I hereby certify that the foregoing is true and correct to the best of my knowledge. ...... / ~ FOR COMMISSION USE ONLY Conditions of approval: Notify Commission so representative may witness Plug integrity __ BOP Test ~ Location clearance __ Mechanical Integrity Test ~ Subsequent form required 10- ~o+ Approved by order of the Commission :O~flGINAL SIGNED ElY LONNIE C. SMITH Commissioner Date I Approval No. ¢O --//8 Date Form 10-403 Rev 06/15/88 SUBMIT IN TRIPLICATE G-4 COMPLETION AND TEST SUMMARY · ~ ~ ~ · · · MIRU, NU BOP, test BOP. RIH w/ 2 7/8" tbg. w/Vann gun assembly to depth. Perforate "O" Sands ~ 8 shots/ft. 200 PSI underbalanced w/diesel at the following intervals: MD TVD 4480 - 4514 4143 - 4176 4554 - 4576 4213 - 4233 Run 24 hour flow test. POOH w/guns. RIH w/ESP and retrievable packer. Set pump ~ 420Q' MD. ND BOP, RD, NU well head, move to G-2. Test w/ESP for 7 - 10 days. POOH w/ESP. RECEIVED FEB 2 6 1990 ~laska .OJJ & Gas Cons. Commission ~,nchoraffa CONOCO. INC. U,LNE PO,NT BOP STACK FOR 9-5/8" SURFACE CASING · FILL-UP LIRE PLOW LIRE ANNULAR PREVENTER I' APl fOOO~l,,..,.. TIG SIDE OUTLETS U/ '~r""j SPOOL ~' APl ~OOO~__~~, CSO S,O[ OUTL£TS ~i~ ~ SPOO~ W 'U Threaded Connection 18" c~s~.o APl 50004 RAM lOP I$~/I" APl 5000 RAIl lOP I}%" APl 5OOOI{ " ," APl 5000 SIDE OUTLETS -~- 155/I" APl 50004 RAM BOP I$~/i' APl $000d' · '11' APl II' APl ~0OOd' (l) B.O.P. stack size rattnR meets AP! RP 53 & spec 6A for class 5M with clamp & hub connectors all hydraulically operated. (2) BOPE to be operated on each trip & pressure tested weekly. (3) Hydraulic control system for BOPE to include (5) station control manifold located remote with 160 gallon accumulator and reservoir unit and auxiliary energy source for system activation. (6) Ram type BOP to include a minimum of one set of blind rams and two sets of appropriate pipe rams. (5) Choke and kill manifolds shown separately to meet APl RP 53 class 5M requirements. ~, STATE OF ALASKA ' AI..~S~ OIL AND GAS CONSERVATION COMMISSION REPORT OF SUNDRY WELL OPERATIOI R IG IN 1. Operations performed: Operation shutdown .__X Stimulate __ Plugging __ Perforate __ Pull tubing __ Alter casing __ 2. Name of Operator ! 5. Type of Well: CONOCO 3'NC ' I Development ..._X Exploratory __ 3. Address Stratigraphic __ 3201 C ST #200, ANCHOPJ%GE, AK 9 503 Service_h Repair well __ Other __ 4. Location of well at sudace 3466' FNL, 3370' FEL, Section 27, T13N, R10E, OM At top of productive interval 2719' FNL, 3308' FEL, Section 27, T13N, R10E, UM At effective depth 1799' FNL, 3282' FEL, Section 27, T13N, R10E, UM At total depth 12. Present well condition summary Total depth: 6. Datum elevation (DF or KB) KB-59.3' MBL 7. Unit or Property name Milne Point Onit 8. Well number G-4 9. Permit number/approval number 89-45 10. APl number 50-- 029-23.941 11. Field/Pool upper cretao. - w measured 4950 · feet Plugs (measured) true vertical 4584 · feet N/A feet S~ ~k Effective depth: measured true vertical 4849 ' feet Junk (measured) 4491' feet N/A Casing Length Structural N/A Conductor 80 ' Surface 2643 ' Intermediate N/A Production 4901 ' Liner N/A Perforation depth: measured Size 13-3/8"48#/Ft 9-5/8"47#/Ft 7" 29&26#/Ft N/A true vertical N/A Tubing (size, grade, and measured depth) N/A Packers and SSSV (type and measured depth) N/A Cemented Measured depth True vertical depth 60 bbls Arc Set 189 bbls Permf E 112 bbls Class G 51 bbls Prem Cmt s Arc Set I 60 Diesel 110'RKB 2674' RKB 4929' RKB 110'RKB 2454' RKB 4565' RKB RECEIVED DEC ! 3 i989 A~ask~ 0il & Gas Cons. C0rr,~ Anchorage 13. Stimulation or cement squeeze summary Intervals treated (measured) N/A Treatment description including volumes used and final pressure 14. Representative Daily Average Production or Injection Data OiI-Bbl Gas-Mcf Water-Bbl Casing Pressure Tubing Pressure Prior to well operation N/A Subsequent to operation N/A 15. Attachments ~ 16. Status of well classification as: Copies of Logs and Surveys run __ I Daily Report of Well Operations __X Oil _X. Gas 17. I hereby certify that the foregoing is true and correct to the best of my knowledge. Form 10-40~, R~ev C(6/15/8~" Service Senior Production Foreman Date12/05/89 SUBMIT IN DUPLICATE Kuparuk River-(SOS) North Slope Borough, Alaska W.I. 1.0000000% Milne Point G No. 4 CONFIDENTIAL ( 4,915' TD ) AFE 10- 61-1206 API No. 50-029-21941 Ak. Permit No. 89-45 Elevation Location:3,370' FEL, 3,466'FNL, Sec 27, T13N, R10E Umiat Meridian September 5, 1989 Ready rig to dkid to G-4, skid to G-4. RD jacking equipment. Cut & weld bell nipple, wellhead is 8" too high (or pad is 8" too low). Function test diverter & inspect w/Harold Hawkins AOGCC. PU BHA & orient. Drlg. ACCEPT RIG 1130 HRS. Daily Mud Cost: $ Daily Cost: $ 3,044 Cumulative Mud Cost: $ 3,044 34,177 Cumulative Cost: $ 34,177 September 6, 1989 Continue drilling F/225' to 1113'. Directional MWD tool (turbine) failure. Trip out to replace. Drilling F/ll13' to 1571 _ MD DIRECTION ANGLE 532 N76.2E 1.8 806 N21.6E 5.7 1200 N09.4E 13.8 1506 N01.4E 25.2 Daily Mud Cost: $ Daily Cost: $ 3,595 Cumulative Mud Cost: $ 6,639 55,597 Cumulative Cost: $ 89,774 September 7, 1989 Continue drilling F/1571' to 2007'. Short trip 10 stands. Encountered bridge at 1982' RKB. Ream through bridge and 25' to bottom. Drilling F/2007' to 2700'. Circulate bottoms up. Wiper trip to 270'. Tight spot encountered at 1830' RKB. Circulate and condition the hole. POOH and eLM. L/D BHA. R/U to run casing. Run 47 joints of 9-5/8", 36#/Ft, K-55 Btrs. casing bottom of float shoe at 2674'. Top of float collar at 2591' RKB. No tight spots encountered. R/U Halliburton cementing head. Start circulation and conditioning of hole. R~CEIV MD DIRECTION 1910 28.7 2536 27.6 2635 27.7 ANGLE ! !989 NO. lasks. Oil & Gas Cons. N0.6E Anchorage Daily Mud Cost: Daily Cost: $ 1,421 $ 110,275 Cumulative Mud Cost: Cumulative Cost: $ 8,060 $ 200,049 September 8, 1989 Continue circulation and conditioning of hole at 7 to 8 BPM. Circulated 490 BBLS with full returns throughout. Continue pipe reciprication. Pump 38 BBLS of 10 PPG sepiolite followed by 189 BBLS 12.3 PPG permafrost Type E cement with 5 lbs sSK Gilsonite and 112 BBLS 15.8 PPG Class G cement with 1% gel, 0.2% CFR-3 and 3% salt (BWOW). Drop top plug and displace with 193 BBLS of 9.6 PPG mud. Lost returns suddenly with 120 BBLS displaced returns were cement contaminated (10.4 PPG). Bumped plug with 1725 PSI, bled off - float equip held. N/D diverter system R/D cementing equip run 90' of 1/2" pipe through 9-5/8 Hmg flute. Circulate 9 BBLS of permafrost C cement for top job. Cement returns seen after ± 4 BBLS. Break down diverter stack, clean and service all spools, valves and hydrill. Make up wellhead on 9-5/8 casing torque to llK FT-lbs. N/U BOPE. M/U test equipment pressure test upper and lower kelly valves, floor safety valve, top pipe rams, inside and outside. Kill lime valves to 5000 PSI. Test annular preventer to 3000 PSI. Test manual HCR valve to 5000 PSI - OK. Witnessing of BOP test was waived by Harold Hawkins verbally. Daily Mud Cost: Daily Cost: $ 2,895 Cumulative Mud Cost: $ 10,955 $ 106,135 Cumulative Cost: $ 338,538 September 9, 1989 Complete testing of BOPs. Install wear bushings. P/U all 12-1/4: stabilizers, break out sleeves and L/D. P/U BHA. Orient, calibrate RLL, install R/A sources. RIH with 2 STDS. Flowline plugged. Clean out same. Test Navidrill and MWD - OK. Continue RIH. Tag fill at 2580'. L/D excess DP. Circ 15 min. Pressure test casing to 1500 PSI - OK. Drill out cement, 9-5/8" float equipment and 10' of new formation. Perform leakoff test to 11.0 PPG - OK. Drilling F/2710' to 4159'. DEPTH ANGLE DIRECTION 2920 26o 3362 26~ 3834 27~ 3929 26~ 4024 25~ 4119 24~ Daily Mud Cost: $ Daily Cost: $ RECEIVED N1.0E .o. 1 :¢ 1989 NO. 0E NO. 9T~aSJf, a OJJ & GaS 0o~$. - Cumulative Mud Cost: $ 10,955 60,709 Cumulative Cost: $ 399,247 September 10, 1989 Continue drilling F/4159' to 4191'. Circ and cond hole. POOH for BHA change (install RLL MWD closer to the bit moving the directional MWD further up the string) . Remove R/A source, download RLL. Replace RLL internals, change BHA, calibrate RLL, install R/A source. Test tools - OK. RIH to 4014' RKB. Ream for logs F/4014' to 4191'. Drilling F/4191' to 4950'. Restricted to ROP of <200 FPH due to logging tool. Circ and cond hole. Pump pill and perform wiper trip to 9-5/8" shoe. Sup and cut 90' of drilling line. DEPTH ANGLE DIRECTION 4827 22.00 N0.3E 4453 21.10 N1.5W 4839 20.30 N2.9W Daily Mud Cost: $ Daily Cost: $ 6,139 Cumulative Mud Cost: $ 23,906 49,037 Cumulative Cost: $ 448,284 September 11, 1988 R/H to bottom - 0' of fill. Circulate and condition hole. Strap out of hole. Stand back NMDC, L/D MWD, X.O.S, 2 stab, RLL MWD, navi and bit. Download RLL MWD. Rig up Schlumberger wireline. Lot DTTE/DTD, CNTH and AMS F/4947' RKB to 2672'. W.O. sidewall core gums from Deadhorse. RIH and shoot 24 SWCs - recovered 20 cores. R/D Schlumberger wireline. Make up BHA. Daily Mud Cost: $ Daily Cost: $ 3,387 Cumulative Mud Cost: $ 27,293 78,964 Cumulative Cost: $ 527,248 September 12, 1989 RIH to bottom, tag 3' high. Circ & cond hole. Short trip 10 std & LD DP to 9 5/8" csg shoe. Break all connections on kelly & LD kelly hose. LD HWDP & DP. Repair LD machine. Continue LD HWDP & BHA. LD kelly. Pull wear bushing. Test variable rams to 3000 psi - o.k. RU to run csg. Run126 jts of 7", 29#/ft, L-80 btrs csg. Btm of float shoe = 4929' RKB. Top of float collar = 4849'. PU landing jnt & cmt head. Start reciprocation. Circ and cond hole w/500 psi @ 8 BPM. Pressure test lines to 3000 psi - o.k. Mix & pump 40 bbls 10 ppg dual spacer, 51 bbls 15.6 ppg premium cmt (w/.4% Halad 344, 0.% CFR-3, & 0.01% dicel LWL, followed by 150 bbls of 9.6 ppg brine and 20 bbls diesel. Stop reciprocation. Land csg, bump plug. Casing Tally No. of Size-Weight-Grade-Thread-Etc. Length ~ Pieces Depth 1 Hallib. 7" superseal float shoe 1.29 4928.76 2 jts 7", 29#/ft, L-80, Btrs csg 77.65 4927.47 1 Hallib. 7" superseal float collar 1.00 4849.82 10 jts 7", 29#/ft,L-80,Btrs csg-sand blstd 388.01 4848.82 114 jts 7", 29#/ft, L-80, Btrs csg 4422.20 4460.81 1 7" WKM csg hng 10.24 38.61 Kelly bushing to wellhead flg (top) 28.37 28.37 September 12, 1989 (cont'd.) Preflush - 40 bbls 10.0 ppg Halliburton dual spacer Cmt (Stage I)- 51 bbls 15.6 ppg premium cmt w/0.2% CFR-3, 0.4% Halad 344, & 0.01% Dicel - LWL. Disp. Fluid - 150 bbls 9.6 ppg NaCl brine, 5 bbls water, and 20 bbls diesel. Daily Mud Cost: Daily Cost: $ Cumulative Mud Cost: $ 27,293 $ 147,027 Cumulative Cost: $ 674,275 September 13, 1989 Displace & bump plug w/1500 psig. Hold for 30 min - floats held. Bleed off press. RD cmt lines, RD csg crew. Blow down choke manifold, open BOPs, clean & grease, rams & door seals, ND adapter spool. ND BOPs. NU wellhead, instlal packoff & test same. Inject mud from pits (3 bpm @ 700 psi). Total of 1182 bbls of mud injected. Injected 60 bbls of diesel into annulus. Clean mud pits & flush solids control equip. Daily Mud COst: $ Daily Cost: $ Cumulative Mud Cost: $ 38,909 Cumulative Cost: $ 713,129 September 14, 1989 Fill pits w/200 bbl H20 & flush hoppers, pumps, solids control equipment & all centrifugals. Pits clean. RIG RELEASED 0300 HRS. About 17" fuel on rig = 1513 gal About 11" fuel in camp = 979 gal Note: This is approximately the same amount of fuel which was on board at initial acceptance. Begin sucking liquids from reserve pit and injecting into G-2. Daily Mud Cost: $ Daily Cost: $ Cumulative Mud Cost: $ 11,267 Cumulative Cost: $ 724,396 RE,¢E'IV D Conoco Inc. Suite 200 3201 C Street Anchorage, AK 99503 (907) 564-7600 October 24, 1989 Mr. John Boyle Alaska Oil & Gas Conservation Commission 3001 Porcupine Drive Anchorage, Alaska 99501 Dear Mr. Boyle- Please find enclosed the routine analysis and gamma ray of the G-1 conventional core, analysis of G-1 sidewall cores, and analysis of G-4 sidewall cores. No conventional or sidewall cores were taken in the G-2 and G-3 wells. This data should be held CONFIDENTIAL. Sincerely, Michael R. Zotzky Senior Reservoir Engineer cc- G-1 Well File ~ Well File Conoco Inc. 32.01 C Street Suite 200 Anchorage, AK 99503 (907) 564-7600 October 6,' ]989 John Boyle Alaska Oil & Gas Conservation Commission 3001 Porcup.ine Drive Anchorage, Alaska 99501 Dear Mr. Boyle: Please find enclosed the gyroscopic surveys on the Milne Point G-l, G-2, G- 3 and G-4 wells. No LIS tape or floppy disk format directional data is available for these wells. Sincerely, Michael R. Zotzky Senior Reservoir Engineer cc-well files (4) [3 I~ I L..I-I N I~ SEF~JI r' E S TO: Mr. John Boyle Alaska Oil & Gas Conservation Commission 3001 Porcupine Drive Anchorage, Alaska 99501 DATE: TRANS.#: September 26, 1989 890919AK REFERENCE: CONOCO Milne Point G-4 The following technical data is being submitted herewith. Please acknowledge receipt by signing and returning a copy of this letter to this office, attention Mr. Erik A. Opstad. ENCLOSED INFORMATION SUMMARY Well G-4 MD: Digital: 1 Each Blueline; Total 3 1 Each Sepia; Total 3 1 Each Blueline; Total 1 1 Each Sepia; Total 1 1 LIS Tape 1 LIS Tape Verification Listing Received By: A.O.G.C.C. / Date 2_3 Alaska Oil & Cons. Commission Anchorage 8537 Corbin Drive (99507) · RO. Box 231649 · Anchorage, Alaska 99523 (907) 267-0200 · Fax (907) 522-3432 A Baroid Company CONOC0, Inc 3201 'C' Street, Suite 200 SCHLUMBERGER WELL SERVICES A DIVISION OF SCHLUMBERGER TECHNOLOGY CORPORATION HOUSTON, TEXAS ?7251-2175 PLEABE REPLY TO $£P 1 5 ~J89 SC, LUUBEROER WE'L Pouch 340069 Prudhoe Bay, AK 99734-0069 AT~q: Bernie/Shelley Anchorage, AX 99503 Attention: Rick ~neeler Gentlemen' Enclosed are orints of Company CONOCO, I~' Well l~lne Point Unit D IL ( PHASOE), CNL ( RAW ), CNL (PORO ), C ybe r look, GT 1/89 on' Field Ktlne Point Additional prints ore being sent to: _L-lg~prints CONOCO, ,Inc 3201 "C' Street, Suite 200 Anchorage, AX 99503 ATI~: Harc Shannon County North Slope State A1 a .nit. I BL prints, I RF Sepia Chevron; U:$:A: _ 5043 ATTN: Priscilla Hacl~rov I BL orints, I RF Sepia CONOCb, Inc 1000 South Pine -Ponca-City, OE .... ~603 ATTN: Log Library I BL prints CONOCO, Inc 600 North Dairy Ashford Houston, TX 77079 ATTN: Georze Lamb, Off 2018 PER , I RF Sepia Comm4 ~ion 3001Porcupina Anchorage. AK ~501 ! Br. prints, 1 RF Sepia OXY; P 0 Box 12011 .Bakersfield, CA 93389-2011 ATTN: ~im Conners prints PLEASE SIGN AND RETURN ONE COPY OF THIS TRANSHITT~. THANK YOU, The film is returned to Conoco_ .Anchorage We appreciate the privilege of serving you. Received by: Very truly yourAJaska 0il & Gas Cons. Commtssio SCHLUMBERGER WELL .David M. Saalwaechter DISTRICT MANAGER SW$-- 1327-F *CONOCO, CONOCO AK OIL ANCH, AK PONCA Ci~TY, OK F'- ~ GAS CONS. COMM, 3522 SCHLUMBERGER WELL SERVICES 500 w. INTERNATIONAL AIRPORT ROAD ANCHORAGE, ALASKA 99518 COMPANY · LOCATION · ATTENTION · AK OIL & ~AS CONSERVATION COMM. 3~01 PORCUPINE DRIVE JOHN BOYLE .. COMPUTING CENTER PRINT CENTER WELL NAME · M. ILNE PT. ~NiT G-4 SERVICES · 1 OH LIS TAPE NO. OF BOXES: ONE JOB NO. . 73470 *S ADD'LTAPES ' EE ABOVE WELL NAME · SERVICES · NO. OF BOXES: JOB NO. · ADD'L TAPES · WELL NAME · SERVICES · NO. OF BOXES' JOB NO. · ADD'L TAPES ' '-/2.33 WELL NAME ' SERVICES · NO. OF BOXES' JOB NO. · ADD'L TAPES · SCHLUMBERGER COURIER: WELL NAME ' SERVICES NO. OF BOXES' JOB NO. · ADD'L TAPES · WELL NAME SERVICES NO. OF BOXES: JOB NO. · ADD'L TAPES · DATE DELIVERED: Anchorage RECEIVED BY:x~;'I¢' )" M EMORAN D M State uf Alaska Ak~S~ OIL AND GAS CONSERVATION COMMISSION TO: Lonnie C. Smit Yf~;~ '. >~/ DATE: September 13, 1989 Commissione FILE NO: D. HRH. 0 61 THRU: TELEPHONE NO: Sr. Petroleum Engineer ~,Diverter Test Conoco MPU G-4 Permit No. 89-45 Kuparuk Rv Field FROM: Harold R. Hawkins Petroleum Inspector Tuesday, September 5, 1989, I left Anchorage at 7:10 am by Alaska ~ir~i~e~s' ~'6 Prddh0~' arriving at 8:40 am. I went to Conoco's G-4 well at Milne Point and checked out the diverter system visually and also by function testing control system and valves. The diverter was installed correctly and also function tested properly. There were no failures. In summary, the diverter performed satisfactorily on Parker Rig 141 well G-4 for Conoco Inc., Milne Point. 02-001A (Rev. 8~85) l' RECEIVED ALASKA OIL AND W ~)N)~RVATII)N ~01~II ' I, S EP 1 :L ]989: Alaska 0ii & Gas Cons. commission Loath(eD (~Jnmrol) ~- W~ll ~tgr, ~ -- - __ N Lowsr Killy Number velvet Number flmnpl AdJus~sbll SION COMM RES ENG I SE F_,NG SR ENG I .... ENG ASST I SR CEIL I CEIL ASSTI GEOL ASSTI ':s,"~, ,,"uH I tltnd lwltM~ sever,. Test pPIIowPI '~0° ~tltvrei ~_/1~/O/~ ~' _ Tei~ tlme ,5'.~_ hri - Ol~rlter - (rev May 5, 1989 Conoco Inc. Milne Point Operations Center Pouch 340045 Prudhoe Bay~ Al( 99734 (907) 659-6300 Mr. D. Johnston Alaska 0il an Gas Conservation Commission 3001 Porcupine Drive Anchorage, Alaska 99501 RE' Milne Point Unit; Wells G-l, G-2, G-3, and G-4 Dear Mr. Johnston: With reference to Bob Soptei's conversation with Mr. Bob Crandell on May 5, 1989 and the AOGCC mud logging and sampling requirements returned with the approved subject permits dated March 21 and April 21, please be advised that Conoco agrees to mud log Well G-1 and take mud samples on Wells G-]/2/3/4. No mud logs are planned on Wells G-2/3/4. Conoco regrets any confusion that may have occurred when we informed you we were planning to mud log all the subject wells. If you should have any questions please call Bob Soptei or Hal Stevens at (907) 659-6327. Yours very truly, D. F. Rainwater/E. L. Robinson Senior Production Foreman RJS cc Field Superintendent, Anchorage Safety & Compliance Coordinator Senior Production Specialist RECEIVED MAY _ .Oil.& . as Cons. April 21, 1989 Telecopy: (907)276-7542 T. R. Painter Division Manager ~noco inc. 3201 C Street, Suite 200 Anchorage, Alaska 99503 Mt!ne P°int UnXt .No. ~-4 Conoco Inc. Permit No. 89-45 Sur. Loc. Btmhole Loc. 3466'FNL, 3370'FEL, Sec. 27, T13N, R10E, UM. 1790'FNL, 3314'FEL, Sec. 27, T13N, R10E, UM. Dear Mr. Painter E~Closed is the approved application for permit to drill the .,'above referenced Well. · : The permit to drill does not exempt you from obtaining additional pem!ts required by law from other governmental agencies, and does not authorize con~cttng drilling operations until all other required permitting deteminations are made. To aid'us in scheduling field work,.please notify this office 24 hours prior to commencing instalia~ion of the blowout prevention equipment so that a representative of the Commission may be present to witness testing of the equipment before the surface casing shoe is drilled, ~ere a.~diverter system is required, please also notify this office 24 hours prior to commencing equipment instal!attonso that the Commission may witness testing before drilling below the shoe of the conductor pipe. Very tr~uly ~ours, Chat~n of < Alaska Oil' and Gas Conservation Commission BY O~ER OF THE COMMISSION dlf EnClosure cc~ Department of Fish & Game, Habitat Section w/o encl. ~Partment of Environmental Conservation w/o encl. Tom Painter Division Manager Conoco Inc. 3201 C Street Suite 200 Anchorage, AK 99503 April 12, 1989 Mr. C. V. Chatterton Chairman of the Commission Alaska Oil and Gas Conservation Commission 3001 Porcupine Drive Anchorage, Alaska 9950] Dear Mr. Chatterton: RE: PERMITS; MILNE POINT UNIT; WELLS G-l, G-2, G-3 AND G-4 Enclosed you will find ApplicatiOns for Sundry Approvals for Milne Point Unit Wells G-I and G-2 (original drilling permits approved by your office on March 6, 1989) and Permit to Drill Applications for Wells G-3 and G-4. A check for $200 is included for the Drilling Applications. If you should have any questions, please contact Bob Soptei or Hal Stevens at 659-6327. [~ivision Manager RJS/jah File 500.21.04 ?-"~ STATE OF ALASKA ALASKAti !AND GAS CONSERVATION C,.. ,,,: ISSION PERMIT TO DRILL 20 AAC 25.005 la. Type of work Drill [] Redrill lb. Type of well. Exploratory [] Stratigraphic Test [] Development Oil Re-Entry [] Deepen . Service [] Developement Gas [] Single Zone [] Multiple Zone 2. Name of Operator Conoco Thc. 3. Address 3201 C Street,Ste 200, Anchorage, AK 99503 4. Location of well at surface 3466' FNL, 3370' FEL, Sec. 27, T13N,R10E,UM At top of productive interval 1979' FNL, 3320' FEL, Sec. 27, T13N,R10E,UM At tota~ depth ~ 1790' FNL, 3314' FEL, Sec. 27, T13N,R10E,UM 12. Distance to nearest property line @ Target 1979 feet 13. Distance to nearest well 60 feet 16. To be completed for deviated wells Kickoff depth 600 feet Maximum hole angle 27° 18. Casing program size Hole Casing 30" 13-3/8" 12-1/4" 9-5/8" 8-1/2" 7" 5. Datum Elevation (DF or KB) KB 28 feet 6. Property Designation ADL 25906 7. Unit or property Name Milne Point Unit 8. Well nuqnber G-4 9. Approximate spUd date September 1989 10. Field and peel Kuparuk River Field 11. Type Bond (see 20 AAC 25.025) Blanket Number 8086-15-54 Amount $200,000 14. Number of acres in propert 2560 17. Anticipated pressure (see 20 AAC 25.035 (e)(2)) Maximum surface 2200 psig At total depth ~rVD) Setting Depth 15. Proposed depth (MD and TVD) 4914MD*/4545 TVD* feet 2300 psig Specifications Weight ! Grade ! Coupling I Length 48# l u-4o I Weld 36# 1~:-55 t]~TRs I'II 263080', 26# tL-80I BTRS ]4886' Top Bottom I °S'l 0s' 28' I ,28'12658'1 2500' 28' I 28' 14914'1 4545' I i I 19. To be completed for Redrill, Re-entry, and. Deepen Operations. P~'esent well condition summary Total depth: measured feet Plugs (measured) true vertical feet Quantity of cement (include stage data) ~485 SKS PermaFrost C ~486 SKS PermaFrost E ~515 SKS PermaFrost G +129 SKS P.ermaFrost E ~i38 SKS PermaFrost G ~409 SKS PermaFrost C ~60 Bbls. Arctic Pak Effective depth: measured feet Junk (measured) true vertical feet Casing Structural Conductor Surface Intermediate Production Liner Perforation depth: measured Length Size Cemented Measured depth True Vertical depth true vertical -. .... ,,,,,-,,~d.& G~i$ CONS.Cum~'JlS,SJ0;" 20. Attachments Filing fee ~ ~erty plat ~ BOP Sketch ~ Diverter Sketch"~ Driiling pr6~r~rage '. Drilling fluid program ~e~ de~th plot ~ Refraction analysis ~ Seabed report ~ 20 AAC 25.050 requirements 21.1 hereby ce~the~rego~~nd correct to the best of my knowledge Signed :/:~ (~'~4 . Title Division Manager Date / Commission Use Only Permit ~umber ~ APl number _ . ~ Approval date ~ See cover letter ~- ~ ! 50-- O ~- ~ / ~ ~/ J 0 4 / 2 1 / 8 9! for other requirements Conditions of approval Samples required ~ ' Yes ~o Mud log required ' Yes ~ No Hydrogen sulfide measures ~ Yes ~No' Direcffodal survey required ~Yes C N~ ' · Required working~ssure~for BO~ ~; ~ 3~ ~ 5M; C 10M; ~ 15M Other: ~~~ ~~~ ~g ordor o, Approved by L' L' f ' ~ '~~ Commissioner the commission Dat Fo~m 10 401 Rev.~5- ' ' ~ ' ~Hh~it in ~rinli~t~ SUPPLEMENTAL DATA SHEET APPLICATION FOR PERMIT TO DRILL CONOCO MILNE POINT UNIT G-4 Conoco Inc. 3201 C Street, suite 200 Anchorage, AK 99503 I · Casing and Cementing Program ae The 13-3/8" conductor will be set at 80' below the surface, then cemented to the surface with ±485 sacks of Permafrost Type "C". Be The 9-5/8" surface casing will be cemented with ±486 sacks of Permafrost ,'E" cement followed by ±515 sacks of Class "G" cement. A top job will be done if cement is not circulated to the surface. Ce The 7" production casing will be cemented in two stages. The first stage will consist of ±129 sacks of Permafrost "E" cement pumped around the casing shoe followed by ±138 sacks of Class "G" cement. The secondary cement job will consist of ±409 sacks of Permafrost "C" cement followed by ± 60 barrels of Arctic Pack pumped down the 7" x 9- 5/8"annulus. II. Drilling Fluid Program A· Be Ce 0-3545' 9.0 ppg freshwater spud mud. 3545'-3765' 9.2 ppg low solids non-dispersed. 3765' - TD 9.4 low solids non-dispersed. III. Drilling Program Conoco Inc. proposes drilling the subject well as a production well in the Kuparuk River field (Upper Cretaceous-West Sac). The mud system will be low solids, non-dispersed with a mud weight in surface hole of 9.0 ppg. Mud weight at TD will be 9.4 ppg. A 20", 2000 psi diverter will be installed on the 13-3/8" conductor for drilling surface hole. A 13-3/8", 5000 psi RSRRA BOPE stack will be used on the surface casing. Pressure test will be performed as per State Regulations. BOP's, choke manifold, upper and lower kelly will be tested to 500 psig and 5,000 psig, the Hydril to 350 psig and 3500 psig. Casing will be pressure tested to 1,500 psig. Maximum downhole pressure is based on initial reservoir pressure. Maximum surface pressure is based on an unexpanded gas bubble, temperature taken into account. The closest wellbore is G-3 with a closure of 60 feet at the surface. The well will not be completed or tested at this time. ae Drill a 30" conductor hole to +80' and set 13-3/8" conductor. Be Drill a 12-1/4" surface hole to +2500' TVD (2658' MD) and set 9-5/8" casing. Ce Drill a 8-1/2" production hole to 4914' MD and set 7" casing. TVD MD FORMATION BIT MUD WT YP PV VIS FL 0' 0' Gravel 1-1-4 9.0 32 20 90 15 2500' 2658' Sand/Clay 1-1-4 9.0 25 20 65 15 3545' 4028' "K" Sand 1-1-4 9.2 25 15 35 10 3765' 4289' "M" Sand 1-1-4 9.4 25 15 35 10 4025' 4574' "N" Sand 1-1-4 9.4 25 12 35 5 4195' 4755' "O" Sand 1-1-4 9.4 25 12 35 5 4545' 4914' TD 1-1-4 9.4 25 12 35 5 *The proposed depth is an estimate only. If the actual depth exceeds the permit depth by over 300 feet TVD, a Sundry Notice will be submitted. CONOCO, ! no. PAd G, Well No, 4 Revised Proposal HIIne Poln~ Un l4, North SI ope, Al asks 0 . RKB ELEVATION, 28' I 000 _ m 2000. 3000 _ 4000 5000 _ KOP TVD-600 TMDm600 DEP=O 9 BUILD 3 DEO 15 PER I00 FT 21 EOB 'TVD=1463 TPID=1495 DEP=206 PIAX I HUH ANGLE 26 DEG 51 HIN 9 5/8= CSG. PT TVD=2$O0 THD=2658 DEPm731 DROP 3 DEg PER IOOFT i 1000 VERTICAL SECTION K SNDS TVDm3545 THD=3829! DEP'1260 H SNDS TVD=;5765 THD=4076 DEP'13?2 BEGIN ANGLE DROP TVD'3816 THD'4132 DEP'1397 TARGET / N SNDS TVD'4025 THD'4361 DEP'I488 0 SNDS TVD'4195 THD-4542 DEP-1550 TD / 7' CSG PT -TVD-4545 THD-4914 DEP-167~ PERH[TTED DEPTH TvD-4845 THD~5233 DEP-I786 2000 ,,; TARGET ANGLE 20 DEG HORIZONTAL PROJECT ION SCALE 1 IN. I 1000 FEET PERMITTED DEPTH LOCATION, 1681' FNL. ,3,310' FEL SEC. 27. TIi3N. RIOE SURFACIE: LI:X~ATION ' 3~' FNL. 3370' FEL SEC. 27. TI3N. R!OE Z 0 :~000., 2000 _ 1 000 _ mm 1000 _ CONOCO, Ie°, ~ Ped O. Well Noe 4 Revleed Propo~el Hllne Point Unit. North Slope, Alaekm WEST~EAST 2000 1000 0 1 000 I , I , N 1 1488' DEO 56 MI N E (TO ' TAROET) 2000 I TD LC)CAT l ON s 1790' FNLo 3314' FEL SEC. 27. T13N. RIOE TAROET / N SNDS TVD=4025 TMD=4,361 DEP- 1488 NORTH 148? EAST 50 TAROET LOCATION s l gZg' FNL. 3320' FEL SEC. 27'. T 13N. R ! OE 3350 3400 3450 3500 3550 3600 3650 3700 3750 3500 - I 34~ 3400 3350 I I I 200 ~ 1100 I I ~' 1000 1 I 900 I 800 60O ~°~ 000 ~'"900 .¥o.oOO "9o-% o.oo ~0 3250 3200 ! i L 6OO 800 9oo 1 000 1100 *'1-200 33' 3500 3450 3400 3350 ,3300 3250 3200' _ 370' . 375~ 34C .345 I I [ .35O I . 355 I I .360 I I oo. I B/l- 3s5 DEVELOPMENT WELL WELL NAME: WELL G-4 02-Feb-89 CONDUCTOR SETTING DEPTH: SURFACE CASING SETTING DEPTH: INTERMEDIATE CASING SETTING DEPTH: PRODUCTION CASING SETTING DEPTH: DEPTH IOPERATION: · 0 A RIG MOVE: 0 B RIG-UP; SET CONDUCTOR:' (2,750) . C DRL/SURVEY SURFACE'HOLE: (2,750) D SURFACE HOLE LOGGING: (2,750) E CONDITIONING TRIP: {2,750) F RU/RUN SURFACE CASING: (2,750) G RU/CEMENT SURFACE CASING: {2,750) H CHNG BOPs; PU BHA; RIH: (2,850) I DRL OUT; TEST; TOOH; RIH: (5,130) J DRILL PRODUCTION HOLE: -' (5,130) K CORING OPERATIONS: (5,130) L LOGGING OPERATIONS: (5,130) M CONDITIONING TRIP: (5,130) N RU/RUN PRODUCTION CASING: (5,130) 0 RU/CEMENT PRODUCTION CASING: (5,130) ~iP ND BOPs; NU TREE: (5,130) Q ADDITIONAL RIG-TIME: (5,130) R RIG-DOWN; MOVE RIG: 8O 2,75O 0 5,130 .., HOUR DAYS 0 0.00 12 0.50 49 '12.02 0 0.00 3 0.11 9 0.39 6 0.25 9 0.36 9 0.38 53 2.20 0 0.00 18 0.75 9 0.38 14 O.6O 5 0.21 12 0.50 0 0.00 0 0.00 CUM DAYS 0.00 0.50 2.52 2.52 2.64 3.03 3.28 3.65 4.03 6.23 6.23 6.98 7.36 7.96 TRACT 14 DEVELOPMENT I 1000 0 0 WEI G-4 . . i · · ii i i 11 ii i 111, i 111 i · , i11 ! ! ................ ? ..................... ,,. .................... I I I : : : : : : . i i i e , I .!11111111111111111111 :,. · FG H:I: .............. ,;~ ..., .... I .. i i i . ~.~/ I ' ;~ ..':l = " a:~ ' l :=:? ~ · . . .. . . - . 2 · ~' 4:'?:~:: ' ,::/":."6 8 ?: 10 . . :~ , . . ~... · . .. . . . ' ,.'4~-~ - DRILLING RIG - :~' , :: - . DEPTH II I II I I I I I NOTES: 1. STATE PLANE COORDINATES ARE ZONE 4. 2. ALL GEODETIC POSITION8 ARE BA`SED ON ^ccc~ N.A.D. 1927 Z 3. OFI:SETS TO ,SECTION LINES ARE COMPUTED BA,SED ON PROTRACTED VALUES OF THE ,SECTION CORNER PO,STION$ MILNE PT. VICINITY MAP r ! 30' ---'"' "'-- o ' : ~'~,,~~ i--ii , LOCATION IN ~! '~b' SEC. 27, T13N, R1OE, UMIAT MERIDIAN ;~1 WELL FROM NORTH LINE FROM EAST LINE 30'-- '"" ; i;~L_~ ~F' G-1 3644' 3346' ~ ' ~ G-4 ... < ~. ,o, G-2 3,585' 33,54' VI O , ,., o ..... = > ... G-3 b' G-3 3.525' 3362' ;-, m= o (~ ~ ' ~"~ G-2 ':-iT O G-4 3466' 3370' 8J.~_~ ~ STATE PLANE COORDINATES-ZONE 4 ~ '~ V,~L NoRTH EAs'r G-1 6,O14,O71.302 ,557,260.513 ,~1 , ..____...~r ,:. .. .iL G-2 6,O14,130.704 557,252.065 G-3 6,O14,190.106 5,57,243.616 290' G-4 6,O14,249.,509 5.57,235.167 18'" , r~' GEODETIC POSITIONS NAD 1927 _ 60'_. _ 80' ~, i _ ,.,, ~ _~~ ...... "~- - F" WB.L NORTH LATITUDE WEST LONGITUDE .~ '~.- .... .L~ ~ "' G-1 70' 26'56.0828' 149' 31',58.2867 ~/~~::.;;'='~'-' ~, G-2 :70' 26'57.2677 149' 31',58.5214 G-3 70' 26'57.8,520 149' 31',58.7561 G-4 70' 26'58.4374 149' 31'58.9908 ( TYPICAL ,SECTION NO SCALE II III I I ! I II I I I! I III I I J C'~mCATE oF ~u~v~YOR: · , LICEN~ TO PRACTI~ LAND SURVEYING ~l THE STATE OF ~'~..~..-' ..... ~"~.']..~-'~ ~. ~obe~t-~ ~LA~ ~ THAT TH~ mAT ~~T. ALL D~ AND OT~ D~T~LS A~ CO~T. ~;...-~~--£-~,.~, ,,,,, , ,,,, , SURVEYED FOR: ~ ~ ~ ~m FII?,.D BOOK ~ ~ ~ ,SCALE 1'=2OO' JOB NO. 89009 ~ ~' R~ o J,41~[ j I~gl~ ~ I .,~11 23 Z4 A.1:)C-255 O'S 25~3 .~C JU~L-2$$~IS 2S44 AC 29 ii i T 13~ R 10E I T 13 N R 11 E MILNE POINT UNiT - ~ ~ .~.- .~ · .....! '"~ ~ ,,m!, ~, ,,~ "_-~ ' ~ /~ ~ ~ [AD~-31971~ 126S AC ~. ~L ,, ~ ....... , ........ _ ._..~-/.-: _-.. ,- , .... i , ,,, _ .. . 27 26 25 35 36 AGL-2$S 18 25~0 AC · I 30 29 31 32 ADL-28231 2555 AC III i EXHT~LT A. MILNE POINT UNTT AREA ~$1et 0 I 2 ~ ~? - ; Sc ~1~ o o ~'ILL,- U P LINE CONOCO, INC. MILNIr POINT UNIT BOP STACK FOR 9-5/8" SURFACE CASING · · 'PLOw LINE ANNULAR PREVENTER 13¥1' APl SO00 13%' APl 5000 RAM BOP I)%' APl ~000 SPOOL 'L A_ · RAM BOP L 2' APl 5000~ TBG JlDE OUTLETS LJ/ ~,J-j~sPooc · II' APl ~000~ }' APl ~0004 ~, CSG ' / I .* --S' - APl SO00 SIDE OUTLETI . -- 15S/II APl 50004 APl 5000d · '11' APl 5000 (1) B.O.P. stack size rating meets APl R? 53 & spec 6A for class 5~f v/th ,. clamp & hub connectors all hydraulically operated. (2) BOPE to be operated on each trip & pressure tested weekly. (3) Hydraulic control system for BOPE to include (5) scat/on control manifold located remote vith 160 gallon accumulator and reservoir unit and auxiliary energy source for system activation. (4) Ram type BOP to include a minimum 'of one set of blind rams and two sets of appropriate pipe rams. (5) Choke and kill manifolds sho~rn separately to meet AP1RP §3 class 5~ requirements. CONOCO, INC. MILNE POINT UNIT DIVERTER STACK FOR 13 318'.CONDUCTOR t,. FILL UP Lille ~ ' i FLOW LINE · L_ _ · , J M~e V&tVl~ O' IIELIEF YALV[ ~0' AP! ~C)OO I~li AFiNULJb. R I)R[V[N?[II OIVERT[R QhiICK CONNECT ASS[hilLY STARTINO t4[AO · CASING 1. The hydpaulic control syste~ will be in accordance with APl specifications and AOGCC requirements. 2. The HCR valve will open ~hen the preventer closes. A single tO# ~elief line wil! Fun off of the dpilling spool HCR valve and ~ill have a ta~§eted do~nstpea~ tee 'for' downwind diversion. Valves on both sides of the tee will be full opening and linked together to enable one to al~ays be open and the othep to be closed. UTIL PO~~., 'PLIIV~ PITS BAt. L VAt..V~ PiT BALL. VALVe_ ~ __ _ _ i ill i i : .. . 5O0O t,4ANUAL CHOKE .. . .. ,.-':"~',.'. ':- :.. ,':. ::".: :. i.'.,':r/.fi~.' .... ,. - - -. ~ ..,. . ';: ?. 4':': ~/. "- ....... CHECK LIST FOR NEW WELL PERMITS ITEM APPROVE DATE .oc (8) (3) Admin~____ f3_~2/q~ 9. (9 thru 10. (10 and 13) 12. 13. (14 thru 22) (23 thru 28) Company Is the permit fee attached .................................... , ..... Lease & Well No. YES NO T -- 2. Is well to be located in a defined pool ............................. j~ 3. Is we~] located proper distance from property line .................. ~ . . 4. Is w~,[located proper distance from other wells ................ ' ... ~ 5. Is su.z~icient undedicated acreage available in this pool ............ 6 Is well to be deviated and is wellbore plat included ................ 7. Is operator the only affected party ................................. ~__ ....... 8. Can permit be approved before fifteen-day wait ...................... R S" Does operator have a bond in force .................................. /~ Is a conservation order needed ...................................... ~ Is administrative approval needed ................................... Is the lease number appropriate ..................................... ~-- Does the well have a unique name and number ......................... 14. 15. 16. 17. 18. 19. 20. 21. 22. 23. 24. 25. 26. 27. 28. Is conductor string provided ........................................ Will surface casing protect all zones reasonably expected to serve as an underground source of drinking water ..................... Is enough cement used to circulate on conductor and surface ....... '. Will cement tie in surface and intermediate or production strings ... Will cement cover all known productive horizons ..................... Will all casing give adequate safety in collapse, tension and burst,. Is this well to be kicked off from an existing wellbore ............. Is old wellbore abandonment procedure included on 10-403 ............ Is adequate wellbore separation proposed ............................ Is a diverter system required ....................................... ~ Is the drilling fluid program schematic and list of equipment adequate ~. .L. Are necessary diagrams and descriptions of diverter and BOPE attached. ~ Does BOPE have sufficient pressure rating - Test to ~ psig .. ~ Does the choke manifold comply w/API RP-53 (May 84) .................. Is the presence of H2S gas probable ................................. (29 thru 31) (6) Add: ~~. Geolo ~y: Eng .ineering: DWJ ~"' LCS rev: 01/30/89 6.011 Fo r 29. 30. 31. 32. exploratory and Stratigraphic wells: Are data presented on potential overpressure zones? ................. Are seismic analysis data presented on shallow gas zones ............ If an offshore loc., are survey results of seabed conditions presented Additional requirements ............................................. INITIAL ' GEO"~ UNIT' ON / OFF POOL CLASS STATUS AREA NO. SHORE /-o,'/ ~0 Well History File APPENDIX Information of detailed nature that is not particularly germane to the Well Permitting Process but is part of the history file. To improve the readability of the Well History file and to simplify finding information, information, of this nature is accumulated at the end of the file under APPENDIXl .. No special 'effort has been made to chronologically organize this category of information. COMPUTING CENTER RECEIVED SEP XgLq~ ~asl~ Oil & GasCons..C, onnisSt~; Anohorage ~60~ ~ ~ZI~ D~ X~ ~OVTO0 ~ **** a3O~3X 3qi3. 00'~6)~-6~0=09~=D ~INfi ~NIOd 2NIIW~ lNIOd 2N~IN~ 'DNI ODONOD z : 3dY& OIA3~d I : # NOI~QNI&NOD OL~EL : 3WVN 8~/60/6~ : 3~VO $I03 : 3W~N 00-I)6~-6Z0-0S')-9 $INA $NIOd 3NqIW' SNIOd 3N~IW' 'DNI O~ONOD : : # NOI&VQNI~NO~ OL~£L : ' 3WVN blq~ : NI~I 0 8~/60/6~ : &Id3 : 3WVN LO:Or 686~'d3~-8T bUT3ST5 UoT3e~T;TJeA ede~ SIq ~'9 :~0~ ~I~ ~'8 :Nd L~ ~t&I~OD~IA ~'6 :X~I~N30 ~Lgg O& --.30 H~d3O ~3qql~G d Gq L~ .8/S 6 :~ DNI~qD 0'8~6t 0S6~ 2HO 68-d3g-~ :03DDO~ S'6~ E'6S :~ SNOI&VA3'I3 13DVd LO:O~ 686;-d3~-ST eou~AO.~d ~:o gNOD = 3dX2, VNWUO/NOa&~3N Q3&VgN3dWOD DgD' aD qOO& RB&3NO3D 3qOH3aOa &DB' &Da NO~3N Q3&Y~N3aWO~ &NDe H/Q/V- ND ~ZgN3O OH&I~ &Oq' &Oq qO0$ NOI;N3&X3 lOO& &33& 000~'- Xa3A3 Q3qdWVg V&~Q LO=Or 686;-d3g*8! X&IAI&~QONO~ ~O~VHd d33Q NOI~AQNI A~IAZ&gIg3~'~Og~Hd d~3O NOI&DQGNI ~noeue~uod~ ~IAt~s~sa~ mnSPaW-~I ' P~Be~a~euN ~&g ~D ~QX~ HdQ! t :3DVd LO:OT 686I-d3~-Bt ~a3uej ~uI%ndmoj e~selV ~eb~eqmntq~9 ** ft3~9-" 3.dt& &3~ ** c~ ;3DVd NOIgN3& 0~3~ uossue& NOI~N3& Q¥3H N3~H uo suo& TIeD I~V3 LO:OI 686I-d3g-8! zelueD buT~ndwO~ eXsel¥ ~eb~eqmn ISamc Verilicatio~ Listing mberger Alas utlng Cente 18-$EP-1989 10:07 PAGE: -.-,,---..------...-.----,,,-., ..-......-.. ID ORDE~ , ~O~ TYPE CLASS ~OD NUNB S~NP EBEN CODE (HEX) DEPT FT 549133 O0 000 00 0 1. I 4 SFLI, DTE 0... 549133 07 220 01 0 I I 4 ILM DTE O.~N 549133 07 120 44 0 I I 4 ILD DTE OHMM 549133 07 120 46 0 I I 4 SP DTE MV 549133 07 010 01 0 I I 4 I I 4 44 0 1 1 4 IDP DTE M~HO 549133 07 110 46 0 1 i 4 IIRD DT£ MMHO 549133 07 000 O0 0 ! I 4 ~x~ ~.~o.,~ o~ ooo oo o . ~ ~ ~,~.o ~,~ o, ooo oo o , ~ 68 0000000000 68 0000000000 68 0000000000 68 0000000000 68 0000000000 68 0000000000 68 0000000000 68 0000000000 68 0000000000 68 0000000000 68 0000000000 68 -0000000000 68 0000000000 68 00000:00000 68 0000000000 $c~81umberger Alaska ¢omput .. PAGE! bB 549133 MAES tNT OHMM 549133 MTE~ CNT DEGF 549i33 HTE~ CNT bB 549 C! BGT IN NaMF SERV UNIT SERVICE AP1 API APl AP! FILE NUMB NUMB SIZE REPR PROCESS ID ORDER # bOG TYPZ CLASS MOD NUMB SAMP EbEM CODE (HEX) ' ' ' ~I oooo~ooooo ~.~ cs~ ~us4~a~ o?~oOD o i ~ ~ 4 ~ oooo ooooo ~ cs. ~ s~. o? . l~° o~ ~ ~ ! 4 ~o oooooooooo ,oo~ o ~ ~ , ~ s~ oooooooooo ~s cs~ ~s ,,~ o s~ oooooooooo 33 O7 .?Er CSG LB 549 33 OT 0 000 O0 0 ODOD o t I I ~ ~) oooooooooo 0000000000 DATA DEPT CI T£ DEPT C D:RHO: LDT b8 LDT CN T 5O g. 41 2:1 ): 2 867 ~DTE 2 596 IbD DTE C~"N~ 000 8'FBU,DTE 867 ...... I:~'~ DTE ,943 3:0¸ NT RCNT NT: 2029: 59'6 I'LD "99:9: ,549 SO LIS Tape Verlttcation blstlnq Schlumberger Alaska ComputlnO Center 'CFT~? CI,SGT GR,CSG NTEM.CSG 583 154 2 082 -999 250 -999 250 -999 250 GR CNT MTEM CNT C2 BGT CAb! CSG NTEN CSG DEPT SP DTE CZDP DTE IIRM DTE MRES DTE DRHO bDT bS bDT 851 bDT S1RM,LDT G~ bDT H~EN.bDT N OR,CNT CFTC.~NT M~E8, NT CI,,BGT MTEM,CSG 4900 000 -35 000 281 ~00 250 50 2 082 0 001 253 000 187 500 ooo 597 ~74 2 82 -999 250 SFLU DTE IDPH DTE CIMP DTE GR DTE HTEN DTE PEF bDT LU DT SS2 ~DT bSRH bDT TENS bDT NPH~ NT RCNT,~NT GR CNT MTEM CNT HTEN CSG DEPT SP DTE 4800 000 SFbU -39250 iDPH "'999 HTEN TE TE DTE DTE 18-SEP-1989 10:07 100 688 88 25O -999 250 -999 250 -999 250 5 684 3 559 258 500 103 438 1.501 000 3 707 O0 000 39 0~3 1983 250 -999 :50 ;388 135 CAbZ,CNT HTEN,~NT TENS, GT TENS,CSG IbM DTE IMPH DTE IIRD DTE TENS DTE DPH! bDT OhS bDT bb ~DT bSHV bDT U RH. ~D? TE~ ~DT TN,PH RCFTHI NT HTEN, 3¸0 ~CFTC DTE !2t : :HTE.N: 0'03 PEF L:D~ 2 L'DT 92 CNT 592 733 bDT LDT CNT 92 5. ,: PAGEI -1 ~,719 TENS,CNT t790,000 .750 GR.BGT -999,250 -9 ~,250 NPHX.CSG '999.250 -99 ,250 MRES.CSG -999.250 3 730 XLD DTE 3 863 IFRE DTE 330 130 1231 2 88 -37 598 8 150i 625 XIXD 000 MTEM 93 02~ RHOBoss 250 LITH 000 SSHV ES 549 TNRA 810 CNT'C 750 TENS 000 GR DTE DTE bDT LDT bDT bDT bDT bDT ~CNT CNT GT 00 NP:H~, CSG 50 MRES.CSG 2~ 533 000 42 438 88 25O 2 470 0 005 60 563 1661-000 8,750 2,082 1902, 3304'000 . 69.563 ~999, DTE TENS CNT 00.0 MRES,CNT 2,121 MTEM CNT CI,BGT B,648 C2:BGT GR,CSG '999,]50 CALI,CSG MTEP,C$~ -999, 50 NTEN,CSG DEPT, SP,DTE CIDP,DTE fIRM DTE RES DTE LS LDT SSi. bDT S1RH bDT GR bDT HTEN LDT NPO~ CNT CFTC CNT MRES CNT C! 8GT 4600.000 -40688 259750 328 2~0 201250 2 75 74 ~?1 1336 2 ,$0 -999 SFLU DTE GR DTE HTEN DTE PEF bDT LU bDT SS2 bDT ~SRH bDT TENS bDT NPHI CNT RCNT CNT GR CNT BGT CALl CSG HTEN CSG DEP' ¢: 4500,000 SFLU DTE DTE DTE -999 'g9'9' SIRH, .::OR:.,: HT'£N, CFTC. 4400 20:3 ~:250 ::::SS:2 2~15'6 LSRH ~: :~50 '563 j944 GR 2,209 MTEM DTE 18-8EP-1989 10:07 87.0~0 HTEN,CNT 9,3 ! TENS,,BGT '999,250 TENS,CSG -999.250 3 ,934 3 ,848 262 750 000 500 28450 2 ~i4 2910000 38894 212674 2 886 000 ?$6 -99 ,,.99; ILM,DTE IM~H,DTE IIRD.OTE TEN$~DTE DPNI'LDT QLS,~DT LL,~DT bSHV, bDT LURH,~DT MTEN DT TNPH iNT RCFT NT CA~i .NT HTE'N,:~Ni TENS BGT ¢$G 7 211 'ILM DTE ~ENS i'4 IbM H,~E'-:N CNT 1341.000 2150.000 -999,250 GR,BGT NPHI,CSG MRES,CSG 3 729 3 224 2910 19 -0 174 1231 35 ?O9 -999 ILD DTE 803 IFRE DTE 875 IlXD 000 MTEN DTE 69] RH08 bDT 007 OSS bDT 375 LITH bDT 000 SSHV LDT 320 CAb! bDT O00 MRES bDT 834 TNRA" CNT 298 CNTC CNT ?g? ~£NS CN~ 000 000 NPH~,CS¢ 250 MR£S,CSG · 123 !t: 28I DTE ~,1402! 000 GR BG:T PA. GE) 100,87~ '999,25 '999,250 3 777 20000 29141 86000 325 1661,000 8 797 2,150 3288 255 029 910000 84 8 3 -999 "999 250 250,, 0 666" 000~ 686~£~gg 0~ £ 000 199I 8BI,LIT 8~0o0 £8T ~ 8L6'6~ O00'~g 60~' 0~Z;'666 ZHdN~::O0:O SLGI &N ? ¸18 666' OEE;C t~ 69 ggD DgD .1'.ND ,I,N ,ZHdN 000 000 D&N3 00~ V~N& 8§6 ~Oq AHgg 000 ~q H&lq iL( SOq ggo &Oq BOH~ 3&O N3&W 000 3&O OXlI 000 666' iT6T ~8 O- · ND HdN& ~Oq ~Oq'AHgq &oq~qq &oq'lHdO 350 gN3$ 350 QUII 3iQ HdWI DgD.'g3;tW OS~'~66' DgD"IHdN 000' 86T g SE;I: O0 DgD'N3&H W3&W ~D $SJU IHdN gN3& Hagq Egg 33d N3gH ~D HdO! flqjS 666- 0 g88,6EL 000'~g 65 ~is OiL fO0 000 00~ ~0~ 906 g~- 000 00~ O.Ha~ &d3O DSD &ND ~OdN &Oq'H~Tg &Gq OHiO 3&O g3dN 3&O 3&O dOl '&d3O 0gE;'666' DSD' VD Oil' 6 ' DgD'~D ,t, gg gN3& 6£9'8 ,I, DB' g69' ~,giil: i,D LO:OT 666I'd3S-gT 2e3ueD ~UT3ndaoD eNselV ~ab~eqanTq3g Schlum rger Alaska Compu nq Center G~.CSG -~9999.250 CALX.CSG MTE~,CSG ' ,250 HTEN.CSG 4000 000 -57 781 2 000 2 301 -0 0t3 444 250 19'/ 250 2 197 48 969 1419 000 41 573 65~ 6t2 "999 250 "999 250 SFLU DTE IDPH DTE CIMP DTE GR DTE HTEN DTE PEF LDT LU LDT SS2 ~DT LS~ ~DT TENS LDT NPNX CNT ~CNT,,CNT GR.,CNT ~T~ CNT C2 CA~Z~CSG HTEN CSG DFPT DTE DTE D T E DTE 3900 000 000 65 SFLU DTE IDPH DTE Ci'MP DTE 18-$EP-1989 10107 '999.250 TEN$,CSG '999.250 4 265 29~ 467 750 48 969 1419 000 2 469 40'8 250 295 500 2 146 2684 000 43 350 '999 2:0 -999 2~0 6 50 1418 ILM,DTE IMPH DTE IlRD DTE TENS DTE DPHI bDT QLS bDT Lb LDT LSHV~bDT LURH bDT TNPH RCrT CNT CALl CNT HTEN CNT TENS BGT TENS CSG ILM DTE DTE DTE -999,250 MRE$,CSG 3 346 2684 31 -0 240 1230 2 78 41 1419 ~805 999 ILD.DTE 355 IFRE DTE 625 IIXD:DTE 000 MTEM,DTE 276 RHOB,LDT 009 QSS,LDT 250 LIT'H,LDT 000 &SHY,bDT 152 CALI.LDT TNRA CNT 778 CNTC CNT 586 TENS CNT 000 GR 8GT 000 NPHI, CSG 250 MRES, CSG 6 852 ILD,DTE I'FRE ,DTE iiXD,DTE .D'TE .'LDT 12.3 PAGE= 11 "999.250 3 406 20 2 T~ 813 134 1660 000 8 586 2 301 3 515 2239 243 2694 000 55 438 -999 250 -999 250 6 996 Tape Vertitcatlon blsttnq chlumberqer AlasRa Comput/nq Center 18-SEP-1989 I0{07 -999,250 HTENoCSG -999,250 SFLU,DTE IDPH DTE CIMP DTE GR DTE HTEN DTE PEF bDT SS~ BDT LSRH LDT TENS LDT NPH! CNT ECNT CNT GR CNT MTEM CNT HTEN CSG DEPT. 3700,00 SP.DTE -39.53~ CIDP.DTE 85,12 MRES.DTE 2,383 DPHO.LDT - - 0,018 LS.LDT 467,250 SSi.bDT 195,750 S1RH,LDT 93 4O6 HTEN.LDT 1 000 NPOR.CNT 3~':978 CFTC,CNT 655~498 MRES,CNT 2,38 Ct.BGT 0 3600 00 --28 ,6 0 IDP~ DTE DTE CSG HTEN 84 063 49 406 1363 000 2 453 436 000 297 75O 13 40 ~ 2352 49 406 75 563 8 891 -999 250 -999 250 204: 83' 141,~ -999 25:0 ILM,DTE IMPH,DTE IIRD,DTE TENS,DTE DPHX,.LDT QLS,GDT Lb,bDT LSHV,LDT LURH,,bDT MTEM,,LDT TNPH'r~NT RCFT, NT CALX,CNT HTEN CNT TENS BGT TENS CSG IlbN DTE NPH DTE :DTE DTE ;14.3 250 11 102 ll 78 2500 33 -0 249 1230 PAGEI 12 2 75 40;,700 TNRR 649.730 CNTC 789 TENS 000 GR 000 NPHI. 250 MRES XLD,DTE 891 IFRE,DTE 750 IXXD,DTE 000 NTEM,DTE 0 4 015 RHOB.LDT QSS.LDT 375 LITH bDT O0 SSHV bDT 113 CAb! LDT 563 MRES LDT CNT CNT CNT BGT CSG 11. 500 20 000 6 48 75 ~63 2 ~05 0 O5 ~5 O0 165~ ~00 8 ]89 83 221~ 496 3?6 2500~000 55 813 99 25O 82.0 887 ,DTE T~ LI~ Tape Verification Listi q Sc lum~erger AlasEa Computt~O Center 18-SEP-1989 10107 PAGEI I3 DFPT SP:DTE C~DP,DTE I~RM,DTE M ES,DTE DRHO.LDT hS.SDT SS~,LDT S~RH,LDT GR bDT HTEN bDT NPOR CNT CFTC CNT MRES,CNT C1,BGT GR,CSG MTE~.¢SG DEPT. ClSP DT~ _DP DTE I~RN DTE MRES DTE LDT LDT bDT 'LDT DEPT' C MT 3400 000 -37 875 119 438 115 750 2 471 -0 0~3 462 750 198 000 2 180 48 375 14~6 000 38 492 693 3~9 2 47i -99 -250 -99 250 ~5 SrbU DTE IDPH DTE CINP DTE OR DTE HTEN DTE PEF bDT LU bDT 352 bDT LSRH bDT TENS bDT NPHI CNT RCNT CNT GR CNT MTEM CNT C2 BGT CALX ~TEN ¢SG 8FLU DTE ' DTE HTEN 32oo ooo .SFLU' ~DTE 8 430 8 119 48 1426 2 417 30~ 2424 37 2419 48 ~999 999 ILM DTE 367 IMPH DTE 188 IIRD DTE 375 000 TENS DPHX 4'39 OLS 750 Lb 000 LSH¥ 127 LURH TNPH 3 5 RCrT 3~5 CALX ~7~5 HTEN 8 TENS 20 TEN~ 250 DTE bDT bDT LOT bDT bDT bDT CNT CNT CNT CNT BGT 6 434 60 393 IbM DTE Il[RD 8 8 t09 0 t23~ 1426 152~ -99.9 1¸: DTE ~99:9 164 ILD DTE 383 XFRE DTE 188 IIXD DTE 00 NTEM DIE 33 RHOB LDT OSS bDT 000 $SHV LDT 13~ CRL! 375 MRES,LDT 085 TNRR,¢NT 565 CNT~,CNT ~25 T~N .CNT 000 OR.BOT 000 NPHI'CSG :250 MRES,CSG 6 2'38 ILD DTE :DTE 'DTE DTE LDT CSG 'DTE 8 125 000 ?~ 375 115 O, 008 150 375 2286,926 2424,000 55~53 -999 -999 250 6 402 9 836 2 250 chlumberger Alaska Comput/nq Center -18-8EP-1989 10=07 PAGE; 14 DFP?. SP IIRM DRHO L8 GR HTEM NPOR CFTC MRE$ C! GR D~PT II'RM DEPT, DTE DTE DTE DTE LDT LDT BDT BDT bDT LDT NT BGT SG DTE DTE DTE DT 3100 000 -4187488;5 80 313 2 516 o 361 198 125 2 264 6~ 750 142 000 ~72 6 2 8 555 , 50 -999 ~$0 -999 3000.000 ,813 08 SFLU DTE IDPH DTE CIMP DTE GR DTE HTEN DTE PEr bDT LU bDT -SS2 bDT BSRH bDT TENS bDT NPHI CNT MTEM CNT T~N CSG SFbU DTE ZDPH DTE CiMP DTE GR .DTE HTEN DTE BU BDT 2900 000 SFBU 10 875 Ii 367 8 000 69 750 1427 000 447 33~ 000 289 O0 2 ~62 224'4 000 34 242 2310 579 69 75O -999 14 5O0 13, 48* 1422 I0 I:64 44:¸ IbM DTE INPH DTE IIRD DTE TENS DTE DPHI bDT OhS BDT Lb bDT LSHV bDT LURH, LDT MTEM, bDT TNPH CNT RCFT, CNT CABI.,CNT HTKN~CNT TENS.,BGT 'TENS CSG IbM D'TE DT bD 11 789 ILD.DTE 11 625 IFRE,DTE 83 i88 IIXD.DTE 2244 000 HTEM,DTE 23 479 RHOB,LDT 195 LITH BDT 1231 000 SSHV 273 CAL! 71.000 MRE$ 34 499 TNRA 65; 366 CNTC O86 TENS 1427 000 GR 1385 000 NPH! -999 250 MRES.CSG bDT LDT LDT CNT CNT CNT BGT 2 6~ 0 1658 000 9 ~96 2 16 3 058 2244 ~9 ~25 -999 250 -999,25O 13 166 XLD DTE 49 IIXD DTE ~:~ IF:RE DIE D:T.E CSG 977 00 47 25 0 844 "::999 CSG 99 2::50: MR::E:S: ¢SG -99 bis Tape Verification hiSt!hq Schlumberger AlaSka Computlno Center DEPT, SP,DTE CIDP,DTE IIRM,DTE MRES.DTE DRHD,bDT S$t,LDT $1RH bDT OR bDT HTEN bDT NPOR CNT CFTC CNT MRES CNT C1 8GT GR $~ 2800 000 56 i13 59~ -0 009 820 000 213 ?50 1446 000 ~ 8 -999 50 SFbU DTE IDPH DTE CIMP DTE GR DTE HTEN DTE PEP bDT bU bDT SS2 bDT bSRH bDT TENS bDT NPH! CNT RCNT CNT GR CNT MTEM CNT C2 BGT CALl DEPT ES DTE DTE DE 2700 000 8) 50,0 '0 024 401 500 SFbU DTE DPH IMP H'TEN DTE DTE 18-8EP-1989 10=07 719 63 42 1446 2 751 347 210~ 6 6~ 9 -999 -999 656 000 000 ?$0 000 ILM,DTE IMPH,DTE IIRD,DTE TENS,DTE GLS ~DT bSH LUR~ bDT bDT NTEM bDT TN~H RCFT,¢NT CA~I CNT HTEN CNT TENS BGT 50 TENS ,CSG 50 IbM DTE ,DTE ,DTE ~!DTE 'bDT 00'0 15 867 IbD.DTE I5-781 IFRE,DTE 55 094 IIXD,DTE 21'00 000 MTEN DTE 51 256 RHOB LDT 0 014 QSS bDT 444 250 L~TH LDT 1230 000 SSHV LDT i 817 CAbI bDT 8 MRES bDT TNRA CNT 403 341 CNTC CNT 438 TENS CNT 1446 000 GR BGT 1270 000 NPH! CSG -999~ 250 MRES CSG I0 578 898 ~:0~ 9'38 5 ILD.DTE IF,RE DTE IIXD DTE D'E :~000 ~MR'ES PA'GEl 15 16,734 20,000 4,355 67.875 1 804 -0 002 360 250 1657 000 9 438 2 613 4 588 2100 40 906 -999 250 -999 250 10 969 2~ 0'00 332 IS Ta~e Verification L~stinq c~lum~er~e~ Alaska ¢omputIn~ Center lB-$EP-X989 ~0~07 PAGE~ t6 D~PT, SP,DTE CIDP.DTE I~RN DTE MRES DT£ DRHO LDT L$ ~D? SS 1 LDT S1RH LDT GR LDT HTEN LDT N~OR CNT CFTC CNT MRES CNT C1BGT GR. CSG MTEM CSO DEPT, ~SP,DTE CXDP,DTE X~RM,DTE MR'E~.DTE :DRHO LDT LS LDT D~PT 2500 000 -999 250 -999 250 -999 250 -999 250 -999 250 -999 250 -999 250 -999 250 -999 250 -999 250 -999 250 -999 250 -999 250 -999 250 5 92 2400.000 999,280 '9 99,-'250 -999'250 2':30 O' '9'99 '999 '9~99 SFLU, DTE IDPH. DTE CZNP DTE OR DTE HTEN DTE PEF bDT LU bDT SS2 LDT LSRH LDT TENS bDT GR CNT ~TEM CNT HTEN SFLU DTE XDPH DTE C'IMP DTE DTE 'HTEN DTE -999 250 -999 250 -999 250 -999 250 -999 250 -999 250 -999 250 -999 250 -999 250 ~999 250 '999 250 -999,250 -999.250 ILa DTE IHPH DTE IIRD DTE TENS DTE DPH! LDT GLS LDT LL LDT LSHV LDT LURH LDT MT,E~ LDT TNPH C~T CALl, HTEN CNT TENS .BGT TENS CSG :9'99 25:0 DTE ~999 DTE 999 DTE O'TE ~DT 5:0 :OLS LOT 50 ':L:~ LDT -999 -999 -999 -999 -999 -999 -999 250 ILD,DTE 250 IFRE,DTE 250 IZXD,DTE .~250 MTEM DTE 250 RNOB.LDT 250 OSS~LDT 250 LITH LDT 250 $SH¥ LDT 250 CAL! LDT -999,250 MRES LDT -999'250 TNRA CNT -999;250 CNTC CNT -999.250 TENS CNT -999,250 GR BGT -999.250 NPH! 1910,000 NRES,CSG -999 250 ILD DTE TE '999 -9'99 -999 250 -999 250 -999 25O -999 ~250 -999 250 -999 250 -999 250 -99 250 -99~ 250 -999 250 -999 250 -99~ 250 -99 250 -999 250 51 577 2 709 -999 250 -ggg '999 ~:ENS DTE -9 DTE~. ~,::865 00:' 0 ::,: NRES D'T'T =999: LIS Tape Yerlficstion Llstlno Schlumberqer AlasKe ¢omputln~ Center 18-SEP-t989 I0=07 PAGE: 17 DEPT. SP.DTE CTDP.DT£ IIRN.DTE MRE$.DTE DRHO,LDT SSI LDT SJRH bDT NPOR CNT CFTC CN? MRES CNT ¢] GR H?EH CSG DEPT DTE IXR:N DTE MRE$ DTE LDT LDT D~P? ¢ 2200 000 -999 250 -999 250 -999 250 -9~9 250 -999 25O -999 250 -999 250 -999 250 -999 '250 -999 250 -999 2'50 -999 250 '999 250 -999 250 27 828 62 7]9 2100 000 '9199 ':999r' 999 -9i9~ 99 SFLU DTE IDPH DTE CI~P DTE GR DTE HTEN DTE PEF LDT LU. GDT SS2~GDT ~SRH.~DT TENS. bDT NPHI CNT ~TEM.~CNT C2 BGT CA~I CSG HTEN CSG SFLU,DTE ~DPH,DTE CIMP,DTE 250 .GR;DTE 250 ~TEN.,DTE 250 250 2o00 O0o DTE -999 250 -999 250 -999 250 -999 250 -999 250 -999 -999, 50 -999,~50 -999~2~ '999~ '999.250 '999.250 $;16.4 1376,00'0 -99~ -9 9 ILM DTE IMPH DTE IIRD DTE TENS .DTE DPH! ~DT QLS ~DT LL ~DT LSHV ~DT LURH MTEM DT TNPH ~NT RCFT~.CNT CALI.CNT HTEN-CNT TEN$.B~T TENS~CSG 25o o DTE DTE DTE -999', -999~ -999: -999 -999 -999 -999 250 IGD.DTE 250 IPRE.DTE 250 IIXD,DT~ 250 250 RHOS,LDT OSS,LDT 250 SSHV,LDT 250 50 MRES,LDT TNRA,CNT :99'9 50 999 ~$0 CNTC,CNT TENS.CNT -999 2.50 .GR,BGT 'q99 2'50 NPHI.CSG 1810 000 -999 250 -999 250 -999 25O .2,0 '999 '~50 -999 50 -999 2~0 -999 250 -999 25O -999 250 ~999 250 -999 250 '999 250 49 2,795 -999 250 IGD ,DTE ,:DTE ,LDT -999 250 000:/ I~:RE:S:*CSG -9:99 25'0 ' I:~D DTF 1730 ,O00':-,:,~RES C,SG (: SLI$ Tale Verification bistinH chlUm erger Alaska ¢omputinc Center 18-$EP-1989 10107 PAGEI 18 D£PT. 8P,DTE ClDP.DTE IIR~,DTE SSl,bOT SJRHebDT GR bDT HTEN bDT NPOR CNT CFTC CNT MRES CNT Cl ~GT G~ CSG MTEM CSG D~PT, ~ISP,DTE C. DP,DTE IiIRM.,DTE: M~ES,D'TE . D~O bDT L$ ~DT 1900,000 -999. -999 250 -999 250 -999 ....°o -999 250 -999 25O -999 250 -999 250 -999 250- -999 250 -999 250 -999 250 23 656 60 750 SFbU DTE IDPH DTE CIMP DTE GR DTE HTEN DTE PEF bDT LU bDT 882 bDT LSRH bDT TENS bDT NPHt CNT RCNT CNT GR CNT MTEH CNT C2 BGT CRbI 1800 000 "999 250 -999 250 '999!50 °9:99 SFLU DTE DPH DTE IMP DTE HT~N PEF ~U CNT -999 250 -999 2~0 -999 2 ~ -99~ 250 -99 250 -99 250 -99 25O -999 250 -999 250 -99~ 250 250 -99 25 -999 250 '999 250 137~ 164 000 -999 250 099 -999 -999 -999 -999 -999 -99:9 ILM,,DTE I~P~ DT IIRD DT~ ENS DTE PHI bDT OLS bDT Lb bDT bSHV bDT bURH bDT MTEM bDT TNPH CNT C~! TENS BGT TENS CSG ILI~ DTE {,4PH DTE IED DTE DTE LDT -999 -9 --999 -999 -999 -999 -999 -999 -999 =999 -999 -999 -999 -999 ~?00 250 ILD,DTE 250 IFRE, DTE 250 IIXD DTE RXOB LDT 250 OSS bDT ~50 b~TH bDT 25O $8X¥ hOT 250 CALl LOT 250 MRESeLDT 250 TNRR~CNT 25~ CNTC.,CNT 25 TENS.CNT 250 GReBGT 250 NPHIeCSG 000 MRE$~CSG -999 250 -999 250 -999 250 -99 -99 -999 250 -999 250 -999 250 -99 250 -999 250 50 234 2 ~846 -999 250 ILD DTE -999 250 -999 50 999 DTE -~999 250 999 L. DT '-999 250 666' 0~.~'.666- 666-. ooo: 5g.666' gg_666' osz :6 6 0~ 666- 06~ 666- 66 0~ 666' 0~ 666' 0~ 666' 666' ~,N ;i, Oq ~(] IHdN 0~ D&N3 H&/q ~gO OGg OXI! 666' 6'66' 666' 666- 666' 666' 666- 666' 666' 666' 666' 666- 666- 666- 666- 666- 666-. 666' 666" LNg IqVD ~ND ~Gq ~O~ xan~ ~Oq AHgq 3&O Oall 3&O HdXZ 000 gOtI 0 ~ 666- O~ 666~ 666' OS~ 666' OG~ 666' Og~ 666' OG~ 666' Og~ 666- OG~ 666- t O~ 66' Og~ 666- 0~ 666~ 0~ 666- kO ~D' 666 3&O ~WID. O! 3&O Xdal 0 - 3&O ~3~ 000 OOG~ D~D'N3&H &Gq 33d 3&Q N3$H 3&O'UD 3&O'HdOI 0~ 9S 0~ 666- 05 666- OS~ 666- 0~[ 666- O~ 666- 666- OS~ 666- OG~ 666- 0~e666- Og~' Ogg,666' 666' 0G~'666' 0~'666' 000'009l Oq &ND g38N &ND aOdN ~Oq ~D &Oq ~q 3~0 *&d3O 6T LO;OI 686~-d39-8~ I O~ : ~60I : 3~Ig J3~ :0~00 : NOIg~3A ~00° &I~3 : 3N~N 81/60/65 z ~OfflO0 : NOI~3A 100' ~I03 I 3N~N LO:OI 686I'd3g-8~ bUT~ST~ UOT~eOTIT~eA eae~ ~o~j p~nsea~ ~oq B'~ && &rOd · eq~nN ~P~O ~T~e~ ..~~ a~eN $.zeeuTbu3 HVH~NZ~ 'g · Pn3Tbuo~ DNQ~ UOT~eN V aOuT~ozd ~o e~e~g V~V~V A~UnoD 3dO~g. H&BON N~OD · ~ug~ 30T dTUsU~O& NET NMO& UOT~e~o~ PTOT3 ~33,0LEE · ~N~ .99~ ~qsnN TeT~e~ ZdV O0-T~6T~-6~O-OG NIdV e~eN PTeT~ ®men ~uedmoD 'DIOd ~N 3N~I~ I330 O~VA ZN~& gNOD S 3dX& ~gV~ T~ ~3DVd LO~OT 666T'd3~-6T ~e~ueD bUT~ndmOD eNseTv ~eb~eqmnTq3~ bUT~STq UOT3e~TST~a~ ede& ~.I~ LIS Tu~ · Yeri~ic~tio, List!n~ 8e,hl ~er~er ~l~s~8 eo~utl~ Center 18-8EP-1989 10{07 PAGE: 23 ** SET TYPE - CHAN *~ MIME SERV UNIT SERVIC~ APl APl AP! ReI FILE NUMB NUMB SIZE REPR PROCESS ID ORDER # bOG TYPE CbRSS MOD NUMB SAMP EbEM ' CODE CHEX] PEF LDH 549~33 07 GLS LDH 5491~I OSS LDH 5491 bS bDH CPS 549,33 07 LU bOH CPS 549133 07 882 LDH CPS 5491)3 O? bSHV L:DH V 549,~3 O? SSHV LDH V 54913'3 O? ,/C3 !:549' )3 07 N 549113 O? 000 O0 0 2 {190 Ol 0 2 350 02 0 2 356 01 0 2 358 O! 0 2 354 O! ,0 2 354 O! 0 2 54 O! 0 2 54 O! 0 2 54 O1 0 54 O! 0 0 2 5'4 0 0 2 ~54 0 O0 0 2 3 0 0 1~0 02 O2 0 35'0 02 0 ,280 01 0 ! 1 4 68 0000000000 1 I 4 68 0000000000 i 1 4 68 0000000000 ! 1 4 68 0000000000 ! I 4 68 0000000000 I 1 4 G8 0000000000 1 ! 4 68 0000000000 1 i 4 68 0000000000 ! 1 4 68 0000000000 I 1 4 68 0000000000 I 4 68 0000000000 ! I 4 68 00000000'00 1 1 4 68 0000000000 1 , 4 68 0000000000 1 i 4 68 0000000000 i 4 68 00000000.00 4 68 0000000000 ~I~ .ma~e veri~¢atLon ~2st~ q chi tn ~erger AlasKa ComputinnO Center 18-SEP-1989 10{07 RCN?.~NH 2216,578 RCFT,CNH GR.CNH 73.625 CALI.CNH M?EM.CNH 85.625 HTEN,CNH 574.561 9.148 1151,000 CNTC,CNH TENS.CNH 212] 0012 CFTC.CNH 2944; O0 MRES,CHH DEP?, PEF.LDH LU ~DH TENS bDH NPH! CNH RCN? CNH OR CNH MTE¥ CNH 4700 000 3 O57 30 2903 250 5OO 2 342 29'70 000 44 0'/2 2216 578 '73.85 66~55 DPH! l,DH QLS bDH bi, l,DH bSHV bDH I,URH l,DH TNPH CNH HTEN CNH 17 -0 43 9 134S 768 051 000 33O 625 131 581 148 000 RHOB l,DH 0SS bDH bZTH l,DH $$HV l,DH CAb! bDH MRE$ bDH TNRA,¢NH CNTC. CNH TEN$,CNH 2 357 0 82 1660 9 2 3 2123 2970 DRHO LDH 012 b8 125 SSi 000 $1RH 148 GR 150 HTEN 600 NPOR 012 CFTC 000 MRES LDH bDH LDH bDH LDH CNH CNH CNH DEPT PEF l,$R! NPH] R. CNT M-?EM LDH LDH DH bDH CNH C NH eNH eNH' 4600 000 000 28~ '~50 29.~t 000309 89 DPHI.EDH GLS bi., bLSHV URH TNPH 500 HTEN {.,DH l,DH LDH CNH ,N H CNH 19 367 123~ 000 ~{383 OO.0 RHOB LDH bDH $&HV bDH CALl bDH DH C:NH 2.330 DRHO,bDH 166~-000 $1RH,LDH .719 GRiLDH LDH CNH ' ,'" LDH ~ R H · bDH EN~,bDH NPH:T, ,CNH RCN? , ~NH 450~,000 ;750 LSHV iCCNHNH 00:0: MR:ES: CNH T~N::$. HPH! CNH 4400 3025 2 i: 83 000 DPHI LDH 4'38 HTEH 31 57'6 ::':RHOB LDH 2 bDH ,:'.0: ~DH 143 '~:~'DH ti6:6~ ~000 LDH D~ 4300 L'DH 2 , LD'H 2 ' LDH 2:'800 "CNH :' . ~1,74 LURH bDH 000 :{qTE}q bi:iH 818 ~:TNPH CNH TN:RA ~ DH CN:H 3 ~26:8 .' N:POR PAGEI 24 597 850 2:150 0 014 313 000 20~ 375 285 73 625 1345 oeo 43 597 50 2 150 OO8 oo 2 186 -0 006 LIS Tape Verl£1catton blsttnq SchlumBeroer Alaska ¢omputlno Center 18-SEP-1989 10{07 RCNT,*¢NH 2313,800 RCFT,CNH 664,208 CNTC,CNH G".CN. 48.594 CAbI.CNH 9.266 TENS.CN. MTEM,CNH 823, 13 HTEN,CNH 1404,000 424~,800 ,141 46{,000 304,750 287~ 078 000 36 847 2i48 428 80 DPH OB~ BDH bb bDH LSHV bDH bURH bDH MT~N bDH ?NPH CNH RCrT CNH CAb! CNH HTEN CNH DEPT PEr LDN $S2 bDH bSRH bDH TEN8 LDH NPH! CNH RCN? CNH GR CNH MTE~ CNH 36 090 -0 276 1230 ~0 6~0 145~ RHOB EDH 004 085 EDH 250 bXTH bDH 000 $SHV EDH 078 :CAbl~ bOH 875 MRES bDH 733 CNTC 93 CNH 00~ TENS, 297.188 CFTC.CNH 800.000 MRES.CNH 2,055 DRHO,bDH -0,009 LS,LDH 1.79,000 861 bDH 1660.000 &IRH LDH 9 930 GR 2 281 H?EN bDH 3 269 NPOR CNH 2073 897 CfTC CNH 2870 000 MRE$ CNH PAGEI 25 69~,964 ,258 '0 024 508 750 194 375 2 176 66 375 1452 000 39 548 607 945 2 281 END OF DATA **** FI'bE TRAIbER **** F!LF NAME I EDIT ,002 ~ bO LIS Tape Verttlcatlon Ltstln~ Schlumberger Alaska ¢omputlno Center 18-SGP-1989 I0:0.7 DEF! · GR Gamma R~¥ TENS Tension MTEM MUD TEMPERATURE MRES MUD RESISTIVITY HTEN HEAD TENSION NPHT NEUTRON POROSITY TMPH THERMAL NEUTRON POROSXTY TNRA CALIBRATED THERMAL NEUTRON RATIO NPO~ NEUTRON POROSITY OUTPUT FROM AN APPLICATION PROGRAM ReNT RAW CORRECTED HEAR THERMAL COUNTS RCFT RAW CORRECTED FAR THERMAL COUNTS CNTC CORRECTED NEAR THERMAL COUNTS CFTC CORRECTED FAR THERMAL COUNTS GR Gamma Ray CAL! Ca1! er TENS Tens¥o~ MRES MUD RESXSTZVITY ~TEM MUD TEMPERATURE HTEM HE'A,D~TENSION PAGEI 22 DATA FORMAT:SP!ECZFICATXON RECORD ** 65 68 09'9 66 i 66 **** LIS READ **** (NOTE: MAXIMUM RECORD LENGTH- 8192 BYTES) ** REEL HEADER ** SERVICE NAME: SPERRY DATE: 89/09/21 oRIGIN OF DATA: MWD REEL NAME: CONOCO cONTINUATION %: 01 pREVIOUS REEL NAME: COMMENTS: PETROLEUM COMPUTING INC. REEL SEQUENCE % i - LIS FORMAT ** TAPE HEADER ** SERVICE NAME: RLL DATE: 89/09/21 ORIGIN OF DATA: G-4 TAPE NAME: MILNE PT cONTINUATION %: 01 PREVIOUS TAPE NAME: - LIS FORMAT coMMENTS: pETROLEUM coMPUTING INC. ********** END OF FILE ********** RECEIVED Alaska Oil & Gas Cons. Commission Anchorage S~DO~I8 NOIA~DI~ID~S ND~¥G (S~I~N~ ~O~ ON) ~O~NINH~ 99 I 0 NMOG 'NOI~DHHI~ D0q ~E 99 I 9 NOIA~IHDS~G AHAN~ ~GOD ~H ~ZIS ~X~ S~DfYI~ XR~N~ s9 z o ~ ~ o o o o ~9 z o ~ ~ o o o o 'n-a 89 I 0 ~ I 0 0 0 0 89 I 0 ~ I 0 0 0 0 89 I 0 ~ I 0 0 0 0 NI 89 I 0 ~ I 0 0 0 0 89 I 0 ~ I 0 0 0 0 89 I 0 ~ I 0 0 0 0 S~D 89 I 0 ~ i 0 0 0 0 89 I 0 ~ I 0 0 0 0 89 I 0 ~ I 0 0 0 0 ~D/D 89 I 0 ~ I 0 0 0 0 89 I 0 ~ I 0 0 0 0 H/~ 89 I 0 ~ I 0 0 0 0 89 I 0 ~ I 0 0 0 0 89 I 0 ~ I 0 0 0 0 89 I 0 ~ I 0 0 0 0 ~GOD ~A~ 'ON GON S~D ~ D0~ ~.~ 7~S DO~d .~ZS H~II.~ I~%f I~¥ I~%f I~¥ ,T, IND .WDIA~.WS .WDIA~.WS .WN~fN SHDOq8 NOI~¥DI~IDH~S (SHIHANH HHO~ ON) HO~NIk~HHA 99 I 0 NMOG 'NOI~D~HIG DO~ ~§E 99 I ,, ~ NOI~DI~ID~S ~AHO& ~ ~ I # HDNHflOHS H~I.~ ** HHO~HH H~II& ** A~ O0'O00g' ~kr~HO~ SI~ -'DNI DNIA~NOD I~/IH~OH~H6 :S~NH~540D :H~fN H~ ~XHN I0 :# NOI~I1NI~NOD 9-D :~G &O NIOIHO IE/60/68 :H&~G ~H :Hk~fN HDIAHHS OA 00'0g~E 89 I 0 9 89 I o ~ 89 I 0 9 89 I 0 ~ 89 I 0 ~ 89 I 0 ~ I 0 0 0 0 I 0 0 0 0 I 0 0 0 0 I 0 0 0 0 I 0 0 0 0 I 0 0 0 0
