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178-073
STATE OF ALASKA AL ,CA OIL AND GAS CONSERVATION COM, _SION REPORT OF SUNDRY WELL OPERATIONS 11.Operations Abandon ❑ Plug Perforations ❑ Fracture Stimulate 0 Pull Tubing 0 Operations shutdown ❑ Performed: Suspend ❑ Perforate ❑s Other Stimulate ❑ Alter Casing❑ Change Approved Program ❑ Plug for Redrill ❑ Perforate New Pool❑ Repair Well ❑ Re-enter Susp Well❑ Other: Jet Puma Completion 0 2.Operator 4.Well Class Before Work: 5.Permit to Drill Number: Name: Hilcorp Alaska,LLC Development 0 Exploratory❑ 178-073 3.Address: 3800 Centerpoint Drive,Suite 1400 Stratigraphic❑ Service❑ 6.API Number: Anchorage,AK 99503 50-733-20322-00 RECEIVED 7.Property Designation(Lease Number): 8.Well Name and Number: �+ ADL0018742 Granite Pt St 18742 30 MAY 2 2 2 fl 1 c1 9.Logs(List logs and submit electronic and printed data per 20AAC25.071): 10.Field/Pool(s): N/A Granite Point Field/Middle Kenai Oil Pool AOG CC 11.Present Well Condition Summary: Total Depth measured 9,931 feet Plugs measured N/A feet true vertical 9,467 feet Junk measured 9,810 feet Effective Depth measured 9,810 feet Packer measured N/A feet true vertical 9,348 feet true vertical N/A feet Casing Length Size MD ND Burst Collapse Structural Conductor Surface 596' 20" 596' 595' Intermediate 4,516' 13-3/8" 4,516' 4,507' 2,730 psi 1,130 psi Production 9,927' 9-5/8" 9,927' 9,463' 5,750 psi 3,090 psi Liner Perforation depth Measured depth See Schematic feet True Vertical depth See Schematic feet Tubing(size,grade,measured and true vertical depth) 2-7/8" 6.5#/L-80 9,503'(MD) 9,049'(ND) 2-7/8" 6.5#/L-80 9,470'(MD) 9,018'(ND) Packers and SSSV(type,measured and true vertical depth) N/A&N/A 12.Stimulation or cement squeeze summary: Intervals treated(measured): N/A Treatment descriptions including volumes used and final pressure: N/A 13. Representative Daily Average Production or Injection Data Oil-Bbl Gas-Mcf Water-Bbl Casing Pressure Tubing Pressure Prior to well operation: 75 0 16 105 72 Subsequent to operation: 21 0 128 54 70 14.Attachments(required per 20 AAC 25.070.25 071,&25.283) 15.Well Class after work: Daily Report of Well Operations 0 Exploratory❑ Development[] Service ❑ Stratigraphic ❑ Copies of Logs and Surveys Run ❑ 16.Well Status after work: Oil 0 Gas ❑ WDSPL❑ Printed and Electronic Fracture Stimulation Data ❑ GSTOR ❑ WINJ ❑ WAG ❑ GINJ❑ SUSP❑ SPLUG❑ 17.I hereby certify that the foregoing is true and correct to the best of my knowledge. Sundry Number or N/A if C.O.Exempt: 315-136 Contact Ted Kramer Email tkramertc7i.hilcorD.com Printed Name Ted Kramer Title Sr.Operations Engineer Signature ,,.. z, Phone (907)777-8420 Date 5/21/2015 RBDMSA4 MAY 2 9 2015 Form 10-404 Revised 5/2015 Ar 172-6%J' -�--( Submit Original Only l Bruce Platform II SCHEMATIC Well No. BR 30-42 Hileorp Alaska,LLC Completed: 04/23/15 API#50-733-20322-00 CASING DETAIL RKB to TBG Head =42.2' Size WT Grade Conn ID Top Btm 1 " / 20" 94# - 19.124" Surface 596' 13-3/8" 54.5,61,68 K-55,N-80& Buttress 12.347" Surface 4,516' &72 S-80 9-5/8" 40&47 N-80&S-95 Buttress 8.681" Surface 9,927' TUBING DETAIL Long String 2-7/8" 6.5# L-80 EUE 2.441" Surf 9,503' Short String L L 2-7/8" 6.58 L-80 EUE 2.441" Surf 9,470' JEWELRY DETAIL No Depth ID OD Item Long String 1 42.2' Tubing Hanger,CIW,11",5M,Split Hanger 2 9,463' 2.441 2.875 2-7/8"6.58 EUE Tbg Pup 3 9,473' 2.313 2.875 Kobe 4 9,477' 2.441 2.875 Tail Pipe 2-7/8"6.5#EUE Short String A 9,470' 2.441 2.875 X-over,2-7/8"EUE x 2-3/8"Sprmx B 9,472' 1.990 2.375 X-over,2-3/8"Sprmx x 1.25 LP PERFORATION DETAIL Zone Top(MD) Btm(MD) Top(TVD) Btm(TVD) Amt spf Comments Date 2-1/8"Slimkone C-2 8,524' 8,562' 8,192' 8,223' 38' 4 Hollow Carrier 02/04/1979 C-3 8,638' 8,730' 8,285' 8,359' 92' 8 2-1/8"Silver Jet 04/14/1994 C-5 8,916' 8,984' 8,511' 8,569' 68' 8 2-1/8"Silver Jet 04/14/1994 C-6 8,994' 9,014' 8,578' 8,596' 20' 5 4.625" TCP 04/19/2015 C-6 9,210' 9,222' 8,772' 8,784' 12' 5 4.625" TCP 04/19/2015 A C-7 9,317' 9,341' 8,872' 8,895' 24' 5 4.625" TCP 04/19/2015 C-7 9,380' 9,406' 8,932' 8,956' 26' 5 4.625" TCP 04/19/2015 C-7 9,470' 9,508' 9,018' 9,054' 38' 5 4.625" TCP 04/19/2015 B C-7 9,518' 9,552' 9,064' 9,097' 34' 5 4.625" TCP 04/19/2015 2 C-7 9,590' 9,600' 9,133' 9,143' 10' 5 4.625" TCP 04/19/2015 C-7 9,604' 9,610' 9,147' 9,153' 6' 5 4.625" TCP 04/19/2015 C-8 9,684' 9,716' 9,225' 9,256' 32' 5 4.625" TCP 04/19/2015 0 2-1/8"Slimkone I II C-8 9,758' 9,820' 9,297' 9,358' 62' 4 Hollow Carrier 02/02/1979 3 II • 0 0 4 0 0 11/12/2012-Coil hard Tag during cleanout @ 9810'CTM 00 0 Of PBTD=9,880' MD (9,416'ND) M TOF @ 9810' • TD=9,931' MD(9,467'TVD) /' = 'r • Revised By JLL 05/21/15 • IIHilcorp Alaska, LLC Well Operations Summary Well Name API Number Well Permit Number Start Date End Date Granite Pt St 18742 #30 50-733-20322-00 178-073 4/3/15 4/23/15 Daily Operations: 04/03/15 - Friday SET BPV IN LONG AND SHORT STRINGS.TUBINGS ON SLIGHT VACCUM. N/D TREE WHILE ANNULUS IS OPEN TO GAS BUSTER. N/U DSA, RISER AND BOPS WITH CHOKE & KILL LINE VALVES. 04/04/15 -Saturday INSTALL HYDRIL&TORQUE ALL CONNECTIONS DOWN SAME. INSTALL STAIRWAYS AROUND RIG. FULLY SCOPE DERRICK & SECURE CROWN CABLES. INSTALL RIG FLOOR & HAND RAILS WITH WIND WALLS. CONTINUE R/U RIG FLOOR WITH HANDRAILS AND WINDWALLS. RUN HYDRAULIC HOSES FOR BOP, SWACO CONTROL PANEL. PRESSURE UP ON KOOMEY UNIT. R/U UMBILICAL CORD TO BOP REMOTE, COILFLEX HOSES TO CHOKE AND KILL SIDE OF MUD CROSS. R/U TEST PUMP AND RUN HOSE TO RIG FLOOR. SPOT AIR COMPRESSOR AND POWER PACK FOR TONGS. R/U TONGS, INSTALL X- OVER TO DRILL WATER TO FILL TANKS FOR TESTING. WELDER MAKING LONGER DRYROD TO SET AND PULL BPV. PULL CHECK VALVE IN BOTH LONG AND SHORT STRING AND SET 2-WAY CHECKS IN BOTH. TIGHTEN TIW, IBOP TO 3-1/2 TEST JOINT WHILE R/U MUD PUMP AND TANK. 04/05/15-Sunday PERFORM GENERAL HOUSEKEEPING WHILE WAITING ON WEATHER TO CLEAR FOR AOGCC REPRESENTATIVE MATT HERRERA TO FLY OUT& WITNESS BOPE TEST. WITNESS WAIVED BY MATT HERRERA @ 1000 HRS &GIVEN THE O.K. TO PROCEED WITH TESTING. LOST POWER FROM MAGTEC GENERATOR. EXHAUST SENSOR SHOWING HIGH TEMP. ATTEMPT TO TROUBLESHOOT WITH PLATFORM MECHANIC. UNABLE TO REPAIR,TRANSPORT ELECTRICIAN FROM KING SALMON TO BRUCE. REWIRE RIG BANG BOX TO PLATFORM POWER, WIRE UP 200 AMP PLUG & POWER UP BANG BOX SAME. TEST BOPE WITH 3-1/2" & 2-7/8" TUBING TO 250 LOW& 3000 HIGH PER SUNDRY. WITNESS WAIVED BY MATT HERERRA @ 1000 HRS. FINISH TESTING BOPS. L/O TEST JOINTS AND PULL 2-WAY CHECKS VALVE ON LONG/SHORT STRING. M/U 3- 1/2" 8RD INTO SHORT STRING TO SURFACE. R/U E/LINE LUBICATOR. 04/06/15- Monday SERVICE RIG & EQUIPMENT. RIH WITH 2.5"JET CUTTER.TAG 2-3/8" X-O SUB @ 8,470'. CUT TUBING @ 8,463' & POOH SAME. BACK OUT HOLD DOWN PINS. P/U ON TUBING HANGER& HANGER COME FREE @ 12K OVER STRING WT. L/D HANGER & R/D POLLARD E-LINE. POOH LAYING DOWN 3-1/2" 9.2# BTC TUBING & SLM ON DECK. TOTAL OF 105 JOINTS LAYED DOWN @ 1600 HRS. DEPTH = 5,182'. CONTINUE POOH W/3-1/2" 9.2# BTC TUBING. LAY OUT CUT JOINT= 258 JOINTS+ 1 CUT JOINT= 8,413' DPM. SHUT DOWN DUE TO HIGH WINDS 50+ MPH. MIX 120 DRILL WATER 3%KCL= 165 BBLS 3%KCL IN PITS. M/U 3-1/2" 8RD INTO L/S SIDE. PULL HANGER TO SURFACE. L/D HANGER AND CONTINUE POOH W/ 2-7/8" 6.4# BUTTRESS TUBING. FILL METAL DISPLACEMENT WHILE POOH. TOTAL OF 75 BBLS OF 3% KCL PUT INTO WELL FOR DISPLACEMENT. Hilcorp Alaska, LLC Well Operations Summary Well Name API Number Well Permit Number Start Date End Date Granite Pt St 18742 #30 50-733-20322-00 178-073 4/3/15 4/23/15 Daily Operations: 04/07/15 -Tuesday SERVICE RIG & EQUIPMENT. CONTINUE L/D 2-7/8" 6.4# L-80 BUTTRESS TUBING. SLM ON DECK.TOTAL OF 3,348' ON DECK. SERVICE RIG AND EQUIPMENT. CONTINUE L/D 2-7/8" L-80 BUTTRESS TUBING. POOH SLOWLY DUE TO HANGING UP ON EVERY CASING COLLAR TO 7,020' TOTAL OF =216 JOINTS AND 42 PUP JOINTS. 40 BBLS OF 3% KCL ADDED TO WELL BORE LAST 24 HRS.TOTAL OF 110 BBLS. DEPTH @ 0600 HRS = 1,594'. 04/08/15 -Wednesday SERVICE RIG & EQUIPMENT. CONTINUE POOH. L/D 2-7/8" BUTTRESS TUBING. TOTAL OF 260 JOINTS LAYED DOWN WITH KOBE BHA.TOTAL LENGH OF 8,471.90' RECOVERED 25 LBS OF SCALE FROM AROUND KOBE ASSEMBLY. CLEAN RIG FLOOR & EQUIPMENT. P/U 3-1/2" HANDLING EQUIPMENT& PREPARE TO P/U 9-5/8" CLEANOUT ASSEMBLY. P/U 8.5" MILL TOOTH BIT, 9-5/8" 40-47#CSG SCRAPER WITH X-O SUBS BACK TO 3-1/2" PH-6 TUBING. TIH MEASURING & PICKING UP 3.5" 12.95# PH-6 TUBING FROM DECK.TOTAL OF 52 JTS P/U @ 1600 HRS DEPTH = 1,638'. SERVICE RIG AND EQUIPMENT. CONTINUE TIH WITH 3-1/2" PH-6 WORKSTRING, TALLYING AND DRIFTING OFF THE DECK. TAG 8,475' 12' IN ON JOINT 273. CALL FOR POWER SWIVEL ON GRANITE POINT. ADD 85 BBLS OF DRILL WATER AND 12 SKS OF KCL.TOTAL 205 BBLS 3% KCL. OFFLOAD POWER SWIVEL AND R/U SAME. PUMPING .5 BPM @ 0 PSI, 2000 FT/#TORQUE. SETTING 4K ON BRIDGE. 84K P/U WEIGHT, 78K S/O WEIGHT. MILLED DOWN TO 8,553' @ 6AM TORQUING UP TO 5000 FT/# UNABLE TO MAKE HOLE. DECIDED TO POOH RACKING IN DERRICK. CALL KNIGHT OIL TOOLS & EXPEDITE DRILL COLLARS,JARS, & MILL ASSEMBLY TO DOCK FOR 09:00 LOAD OUT. TOTAL OF 43 BBLS OF 3% KCL ADDED TO HOLE LAST 24 HRS. 04/09/15 -Thursday SERVICE RIG & EQUIPMENT. L/D POWER SWIVEL& PREPARE TO POOH WITH 3-1/2" 12.95#TUBING. POOH WITH 3-1/2" 12.95# TUBING FROM 8,500' TO SURFACE. L/D SCRAPER ASSEMBLY&8.5" MILL TOOTH BIT. ATTEMPT WAS MADE TO LOAD OUT KNIGHT OIL TOOLS EQUIPMENT AT 0900 HRS FROM OSK DOCK. UNABLE TO KEEP BOAT NEXT TO DOCK DUE TO WEATHER CONDITIONS. PERFORM GENERAL MAINTENANCE & HOUSEKEEPING WHILE WAITING ON KNIGHT OIL TOOLS EQUIPMENT. NEXT ATTEMPT FOR BOAT CALLOUT TO BE AT 21:00 HRS PER ONSHORE EXPEDITOR. SERVICE RIG & EQUIPMENT. PERFORM GENERAL MAINTENANCE & HOUSEKEEPING WHILE WAITING ON KNIGHT OIL TOOLS EQUIPMENT. OFFLOAD KNIGHT OIL TOOLS EQUIPMENT. M/U BHA#2 8.5 OD TAPERED MILL, X-OVER, PONY COLLAR, 8.5 OD STRING MILL, X-OVER, BOOT BASKET, BOOT BASKET, X-OVER, OIL JAR, 6-4-3/4" DRILL COLLARS, ACC JARS, X-OVER TOTAL LENGTH= 252.92. M/U 3-1/2" 12.95 P-110 PH-6 WORK STRING AND TIH, DEPTH @ 0600 HRS = 5,977'. 17 BBLS 3 % KCL LOST TO FORMATION IN LAST 24 HOURS. Hilcorp Alaska, LLC Well Operations Summary Well Name API Number Well Permit Number Start Date End Date Granite Pt St 18742 #30 50-733-20322-00 178-073 4/3/15 4/23/15 Daily Operations: 04/10/15 - Friday SERVICE RIG & EQUIPMENT. CONTINUE TIH WITH 3-1/2" 12.95#TUBING FROM 5,977' TO 8,541.40', TAG SAME. P/U POWER SWIVEL& PREPARE TO BEGIN MILLING. MILL ON SCALE F/8,541'TO 8,563', PUMPING .5 BPM OF 3% KCL DOWN TUBING, 85 RPM WITH 3-5K FT/LBS OF TORQUE, 2K WOB. UNABLE TO MILL PAST 8,563'. MILL IN PLACE FOR 1.5 HRS, CHANGING PARAMETERS TO GAIN PENETRATION WITH NO SUCCESS. DECISION MADE TO POOH & P/U BULL DOG PUMP BAILER WITH MILL CONNECTION. L/D POWER SWIVEL& PREPARE TO POOH. POOH WITH 3-1/2" PH-6 TUBING TO SURFACE. OOH WITH BHA#2 MINIMAL WEAR ON TAPER MILL. HAD 4 LBS OF SCALE IN BOOT BASKETS.TAPERED MILL HAD 8" OF PACKED OFF SCALE INSIDE WATER COARSES ON MILL. M/U BHA#3 8-5/16" OD PACKER MILL HEAD, X-OVER, BAILER FLAPPER VALVE, BAILER FLAPPER VALVE, X-OVER, X-OVER, 4-5/8 OD BULL DOG BAILER, X-OVER, DRAIN SUB, X- OVER.TOTAL LENGTH= 49.40. TIW WITH 3-1/2" P-110 12.95# PH-6 WORKSTRING TO 8,543.09'. R/U SWIVEL 81K P/U WEIGHT, 75K S/O WEIGHT. 1000 FT/# FREE TORQUE, TAG @ 8,563'. SET TORQUE @ 3000 FT/# . SET WEIGHT 500#ON BRIDGE WHILE ROTATING, MADE 6" IN 3 HRS. STILL HAD BAILER ACTION, UNABLE TO OBTAIN PENETRATION, DECISION MADE TO POOH & P/U PIRAHNA MILL. L/D POWER SWIVEL& PREPARE TO POOH, TOTAL OF 160 BBLS OF 3% KCL ADDED TO WELL BORE LAST 24 HRS. 04/11/15-Saturday SERVICE RIG & EQUIPMENT. POOH WITH 3-1/2" 12.95#TUBING FROM 8,500' TO SURFACE. BREAK DOWN BULL DOG PUMP BAILER. RECOVERED 1LB OF FINE SCALE BETWEEN UPPER DRAIN SUB& BAILER. SPOT CUTTING BOX NEXT TO RIG FLOOR. R/U MUD BUCKET. POOH WITH PUMP CAVITY (5 STDS OF 3-1/2" TUBING), DRAINING OIL& FLUIDS INTO CUTTING BOX. BREAK DOWN FLAPPER VALVES HAD NO SOLIDS. PACKER MILL HEAD HAD 1/4" GROOVES CUT ON OUTSIDE EDGE OF MILL. SEND PICTURES TO ENGINEER & DISCUSS OPTIONS. ORDER OUT 5-1/2" MILLS & 6" STRING MILLS. CLEAN BOPE STACK& RIG FLOOR. L/D MUD BUCKET. REPLACE DRILL LINE ON DRUM WHILE WAITING ON KNIGHT MILLS. MILLS ARRIVED TO BRUCE AT 15:30 HRS. MEASURE & CALIPER SAME. P/U 5-5/8"PIRANHA MILL, BIT SUB, 13.79' PONY COLLAR, 6" OD STRING MILL,JARS, &4-4-3/4" DRILL COLLARS. TOTAL BHA LENGH OF 171.28'. TIH WITH 3-1/2" 12.95#TUBING FROM DERRICK TO 8,526'. R/U POWER SWIVEL& HALLS HEAD RUBBER. TAG @ 8,563' KB MEASUREMENT. BEGIN ROTATING @ 40 RPM, 2500 FT/LBS TORQUE, 2-4K WOB, PUMPING 1.5 BPM (NO RETURNS). MILL F/8,563' TO 8,572', BROKE THRU. CONTINUE WASHING DOWN. DEPTH @ 0600 HRS= 8,651'. Hilcorp Alaska, LLC Well Operations Summary Well Name API Number Well Permit Number Start Date End Date Granite Pt St 18742 #30 50-733-20322-00 178-073 4/3/15 4/23/15 Daily Operations: 04/12/15 -Sunday BEGAN GETTING RETURNS ON ANNULUS. BEGIN MIXING & PUMPING 3% KCL DOWN TUBING AT .5 BPM,TAKING GAS& OIL RETURNS THRU GAS BUSTER. 0 PSI PUMP PRESSURE. PUMP TOTAL OF 180 BBLS OF 3% KCL. RETURNS STOPPED. WASH F/8,651'TO 8,806', PUMPING 1.5 BPM DOWN TUBING, 0-2 WOB. BEGAN GETTING OIL& GAS RETURNS UP ANNULUS AT 8,806'. MIX& PUMP 3% KCL DOWN TUBING TAKING RETURNS UP ANNULUS THRU THE GAS BUSTER SENDING OIL RETURNS TO PRODUCTION. PUMPING 1.5 BPM AT 50 PSI TUBING PRESSURE. SEND 60 BBLS OF OIL OUT OF ACTIVE PIT TO PRODUCTION. CLEAN ACTIVE TANK & BUILD 200 BBLS OF 3% KCL. CHANGE OUT RIG PUMP DUE TO BAD ALTERNATOR& ELECTRONIC ISSUES. CONTINUE DISPLACING WELL, PUMPING 3% KCL DOWN TUBING @ 1.5 BPM & 50 PSI TAKING RETURNS THRU GAS BUSTER. AFTER DISPLACING A TOTAL OF 520 BBLS OF 3% KCL FLUID, OIL RETURNS STOPPED. MONITOR WELL. SEND OIL INSIDE SHAKER TANK TO PRODUCTION. RINSE SHAKER TANK SAME. BREAK CIRCULATION IN REVERSE PUMPING 2 BPM @ 130 PSI, FULL RETURNS, ROTATING 80 RPM WITH 2-4K FT/LBS TORQUE, 0- 2 WOB. WASH & REAM F/8,806'TO 9,759'.TAG FILL SAME. BUILD 125 BBLS OF 3% KCL FLUID IN ACTIVE PIT. MILL F/9,759'TO 9,774', REVERSE CIRCULATING 2 BPM @ 160 PSI, ROTATING 80 RPM WITH 4K FT/LBS OF TORQUE, 2K WOB. FULL RETURNS. BECAME PACKED OFF IN TUBING, ATTEMPT TO BLOW OUT WITH NO SUCCESS. PLAN TO L/D POWER SWIVEL& POOH TO TEST BOPE. 04/13/15 - Monday SERVICE RIG & EQUIPMENT. L/D POWER SWIVEL. P/U MUD BUCKET. CHANGE OUT 11" HALLS HEAD SPOOL TO 13-5/8" SPOOL. PREPARE TO POOH. POOH W/3.5" 12.95#TUBING (WET STRING). LAYED DOWN TOTAL OF 52 JOINTS. POOH WITH 3.5" 12.95#TUBING (WET STRING) RACKING PIPE IN DERRICK. BREAK DOWN BHA. FOUND 1 STAND OF DRILL COLLARS PLUGGED WITH COARSE SCALE. L/D SAME. PIRANHA MILL 25%WORN. CLEAN RIG FLOOR. P/U 8.25" PIRANHA MILL, BIT SUB, 12' PONY COLLAR, 8.5" STRING MILL,JARS, & (4) 4-3/4" DRILL COLLARS. TIH SAME. TIH WITH 3-1/2" PH-6 TUBING FROM DERRICK TO 8,550'. R/U POWER SWIVEL& 11" HALLS HEAD FLANGE WITH RUBBER. ATTEMPT TO BREAK CIRCULATION PUMPING DOWN ANNULUS WITH NO SUCCESS. PUMP TOTAL OF 100BBLS. UNABLE TO CATCH UP TO FLUID. TAG @ 8,561'. PUMP DOWN TUBING @ 1 BPM &0 PSI, 80 RPM WITH 3-5K FT/LBS OF TORQUE, 2K WOB. MILL F/8,561'TO 8,562'. OBTAIN CIRCULATION AFTER A TOTAL OF 120 BBLS PUMPED. LINE UP & PUMP DOWN ANNULUS CATCHING RETURNS UP TUBING. BUILDING 3% KCL FLUID VOLUME @ 0600 HRS. EXTENSION GRANTED TO TEST BOP ON THURSDAY, 4/16/15 BY MR.JIM REGG, AOGCC. 04/14/15 -Tuesday L/D POWER SWIVEL. POOH F/8,562'TO 8,501'. BUILD 3% KCL VOLUME & 60 BBLS OF NW-50 LCM PILL(80 FUNNEL VIS). PUMP &SPOT PILL. SERVICE RIG & EQUIPMENT. TIH TO 8,550'. P/U POWER SWIVEL& BREAK CIRCULATION IN REVERSE. REVERSE CIRCULATE 1 TUBING VOLUME AT 1.5 BPM & 150 PSI. CONTINUE MILLING F/8,562'TO 8,566' REVERSE CIRCULATING 2.5 BPM @ 200 PSI, ROTATING 60 RPM @ 4500-6000 FT/LBS, 2-6K WOB. LOSSES TO FORMATION = 14 BPH. BROKE THRU BRIDGE AT 8,566' WITH 8.25" PIRANHA MILL. REVERSE CIRCULATE 2 TBG VOLUMES& BUILD 110 BBLS OF 3% KCL. WASH DOWN TO 8,577' &TAG BRIDGE WITH 8.5" UPPER STRING MILL. REAM F/8,577'TO 8,579', REVERSE CIRCULATING AT 2.5 BPM & 250 PSI, ROTATING 65 RPM WITH 4500-6500 FT/LBS TORQUE, 1-2 WOB. LOSSES AT 2 BPH. TOTAL OF 105 BBLS LOST LAST 24 HRS TO FORMATION. Hilcorp Alaska, LLC Well Operations Summary Well Name API Number Well Permit Number Start Date End Date Granite Pt St 18742 #30 50-733-20322-00 178-073 4/3/15 4/23/15 Daily Operations: 04/15/15-Wednesday CONTINUE MILLING, REAMING, &WASHING F/8,579'T/8,931', REVERSE CIRCULATING 2.5 BPM @ 225 PSI, 65 RPM WITH 4500-5500 FT/LBS TORQUE, 2-3K WOB. FULL RETURNS. GETTING FINE SCALE CUTTINGS OVER SHAKER. L/D POWER SWIVEL. CHANGE 11" HALLS HEAD FLANGE TO 13-5/8" FLANGE. POOH TO 8,500'. MIX, PUMP &SPOT 40 BBLS OF NW-50 HIGH VIS LOSS CIRCULATION PILL (80 FUNNEL VIS). POOH WITH 3-1/2" 12.95#TUBING FROM 8,500'TO BHA. RACK BACK DRILL COLLARS. LID JARS & PONY COLLAR, GAUGE STRING MILL& LEAD MILL. PIRANHA MILL 95%WORN (ONE PAD MISSING FROM MILL), STRING MILL 25%WORN. CLEAN RIG FLOOR & DECK AREA. PREPARE TO P/U TEST ASSEMBLY TO TEST BOPE WITH STATE WITNESS BOB NOBLE. 04/16/15-Thursday INSTALL 3.5" TEST ASSEMBLY& PRETEST BOPE WHILE WAITING ON WEATHER TO CLEAR FOR AOGCC INSPECTOR BOB NOBLE TO ARRIVE. TEST WITNESS WAIVED BY BOB NOBLE @ 11:24 HRS BY PHONE. RECEIVED E-MAIL CONFIRMATION FROM JIM REGG @ 12:49 THAT BOPE WITNESS HAD BEEN WAIVED AND REQUEST TO GET COPIES OF CHARTS WITH BOPE TEST RESULTS. TEST BOPE WITH 3.5" TUBING TO 250 PSI LOW & 3000 PSI HIGH PER SUNDRY. PERFORM KOOMEY DRAW DOWN TEST. BOPE WERE TESTED FROM REMOTE & MAIN WAS FUNCTION TESTED. L/D TEST ASSEMBLY, MEASURE & CALIPER BHA#5 PREPARING TO P/U 8.25" MILL&8.5" STRING MILL. P/U &TIH W/ BHA#5, 8.25" BLADED MILL, PONY COLLAR, 8.5" STRING MILL,JARS, (4) 4-3/4" DRILL COLLARS. TIH W/3-1/2" 12.95#WORK STRING FROM DERRICK TO 8,900'. R/D 13-5/8" SPOOL& R/U 11" HALLS HEAD SPOOL. P/U POWER SWIVEL& PREPARE TO START WASHING. ESTABLISH CIRCULATION IN REVERSE PUMPING 2.5 BPM @ 220 PSI, 60 RPM W/4-6K TORQUE. WASH, REAM & MILL F/8,931'TO 9,029'.TAG BRIDGE SAME. MILL F/9,029' TO 9,032', BROKE THRU. WASH & REAM F/9,032'TO 9,424'. LOSSES TO FORMATION LAST 24 HRS = 60 BBLS. 04/17/15- Friday MILL, WASH & REAM F/9,424' TO 9,743' REVERSE CIRCULATING 2.5 BPM @ 300 PSI, 40-60 RPM WITH 3000-6000 FT/LBS TORQUE, 0-3 WOB. TAG BRIDGE AT 9,743'. CONTINUE MILLING F/9,743' TO 9,788', GETTING FINE SCALE ACROSS SHAKER ON RETURNS. MILLING ON JUNK F/9,788' TO 9,789', PACKING OFF WITH METAL AT SURFACE. REVERSE CIRCULATING 2-3 BPM @ 400-800 PSI ATTEMPTING TO CIRCULATE METAL TO SURFACE. DECISION MADE TO POOH & P/U TEST PACKER TO TEST 9-5/8" CASING.TOTAL LOSSES TO FORMATION LAST 24 HRS= 90 BBLS. Hilcorp Alaska, LLC Well Operations Summary Well Name API Number Well Permit Number Start Date End Date Granite Pt St 18742 #30 50-733-20322-00 178-073 4/3/15 4/23/15 Daily Operations: 04/18/15-Saturday L/D POWER SWIVEL. ROLL UP HYDRAULIC LINES &SECURE UNIT TO OFFLOAD. N/D 11" HALLS HEAD FLANGE & N/U 13- 5/8" FLANGE. POOH WITH 3-1/2" 12.95#TUBING FROM 9,780'TO BHA. BREAK& L/D JARS, 4-3/4" DRILL COLLARS, X-O SUBS & MILLS. LOAD INTO BASKETS SAME. RECOVERED 14 LBS OF METAL OUT OF MILL. CLEAN & CLEAR RIG FLOOR. PREPARE TO P/U 9-5/8" 40-47#TEST PACKER. P/U 9-5/8" 40-47#TEST PACKER. TIH WITH 3-1/2" 12.95#TUBING &SET PACKER AT 8,001' KB MEASUREMENTS WITH 24K COMPRESSION. R/U TEST RECORDER. TEST 9-5/8" CASING TO 2000 PSI ON CHART FOR 30 MINUTES, HELD SAME WITH 0 PSI BLEED OFF. BLEED OFF CASING, R/D RECORDER. POOH WITH 3-1/2" 12.95#TUBING F/8,000' TO SURFACE. L/D TEST PACKER. SERVICE RIG &CLEAN RIG FLOOR. DAYLIGHT CREW HOLDING SAFETY MEETING WITH HALLIBURTON TCP TEAM ON P/U GUNS. 55 BBLS OF KCL LOST TO FORMATION LAST 24 HRS. 04/19/15-Sunday P/U &TIH WITH HALLIBURTON 4.625" TCP ASSEMBLY. TOTAL BHA LENGH = 897.02' WITH 202' OF LIVE SHOT 60 DEGREE PHASING, 5 SPF. TIH WITH TCP ASSEMBLY ON 3-1/2" 12.95#TUBING AT 1 MINUTE PER STAND, DRIFTING TUBING FROM DERRICK TO 8,860' KB MEASUREMENTS. SPACE OUT& R/U E-LINE. RIH WITH GAMMA & COLLAR LOCATOR, LOG ON DEPTH & CORELATE BACK TO OPEN HOLE LOG. GUNS 20' SHALLOW. POOH & L/D E-LINE. LOWER STRING 20' IN HOLE SETTING TOP SHOT AT 8,994' & BOTTOM SHOT @ 9,716'. R/U & DROP BAR, GUNS FIRED AFTER 4 MINUTES PERFORATING C-6, C-7, & UPPER C-8. WELL WENT ON VACUUM AFTER GUNS FIRED, MONITOR WELL FOR 15 MINUTES & PREPARE TO POOH. POOH WITH 3-1/2" 12.95#TUBING RACKING PIPE IN DERRICK. L/D SPENT 4-5/8" TCP GUNS. ALL SHOTS FIRED. 110 BBLS OF KCL LOST TO FORMATION LAST 24 HRS. 04/20/15 - Monday SERVICE RIG & EQUIPMENT. TIH W/365 JOINTS OF 3-1/2" 12.95#TUBING FROM DERRICK. POOH LAYING DOWN 3-1/2" 12.95#TUBING. TOTAL OF 365 JOINTS LAID DOWN. BOPE WITNESS WAIVED BY JIM REGG ON 4/20/15 @ 10:04 HRS. REMOVE SUBS, ELEVATORS& EQUIPMENT F/ RIG FLOOR. R/D MCCOY TONGS. OPEN PIPE RAMS & INSTALL DUAL 2-7/8" RAM BLOCKS. P/U DUAL TEST ASSEMBLY&TEST 2-7/8" DUAL RAMS TO 250 PSI LOW & 3000 PSI HIGH ON CHART. HELD SAME. L/D TEST ASSEMBLY. OFFLOAD 3-1/2" WORK STRING, SPENT TCP GUNS, POLLARD E-LINE UNIT. OFF LOAD & LAY OUT 2-7/8" 6.5# EUE PRODUCTION STRING, WEATHERFORD DUAL HANDLING PACKAGE. R/U WEATHERFORD TO RUN DUAL COMPLETION STRING. 04/21/15 -Tuesday R/U WEATHERFORD DUAL HANDLING EQUIPMENT. R/U STABBING BOARD INSIDE DERRICK& FUNCTION TEST EQUIPMENT. HOLD PRE JOB MEETING WITH WEATHERFORD & MONCLA. P/U KOBE ASSEMBLY W/2-7/8" 6.5# EUE TAILPIPE & RE ENTRY GUIDE. M/U X-O SUBS&TIH SAME. TIH P/U 2-7/8" 6.5# EUE PRODUCTION DUAL STRING TUBING WITH WEATHERFORD.TOTAL OF 220 JOINTS. P/U ON EACH SHORT& LONG STRING. DEPTH @ 0600 HRS = 6,912'. Hilcorp Alaska, LLC Well Operations Summary Well Name API Number Well Permit Number Start Date End Date Granite Pt St 18742 #30 50-733-20322-00 178-073 4/3/15 4/23/15 Daily Operations: 04/22/15 -Wednesday CONTINUE P/U &TIH WITH 2-7/8" 6.5# EUE DUAL STRING TUBING. RUN TOTAL OF 300 JOINTS ON LONG & SHORT STRING WITH KOBE ASSEMBLY & 1 JOINT OF 2-7/8" 6.5# EUE TUBING AS TAILPIPE. INSTALL DUAL SPLIT HANGER. P/U WT= 92K, S/O WT. = 72K. LAND OUT TUBING WITH 72K ON HANGER. END OF TAILPIPE @ 9,502.86' ORIGINAL KB. RUN IN HOLD DOWN PINS. INSTALL BACK PRESSURE VALVES ON LONG & SHORT STRINGS. R/D WEATHERFORD DUAL HANDLING EQUIPMENT, STABBING BOARD, & LOAD OUT SAME. CLEAR RIG FLOOR, REMOVE WIND WALLS, HANDRAILS& R/D RIG FLOOR. SCOPE IN & LAY OVER DERRICK, ISOLATE KOOMEY BOTTLES& BLEED BOPE LINES DOWN. ROLL UP KOOMEY LINES & N/D BOPE & RISER. N/U ADAPTOR, CIW DUAL 11" 5M X 3-1/8" 5M 5 BOLT TOP. TEST VOID TO 5K, HELD SAME, CONNECT SHORT STRING TO PRODUCTION & PREP TO R/U SLICKLINE. 04/23/15 -Thursday SPOT& R/U SLICK LINE. P/U &TEST LUBRICATOR TO 1000 PSI. RIH WITH 2.13" BLIND BOX TO 9,780'. FLUID @ 6,170'. POOH. P/U STANDING VALVE & RIH TO 9,482' WLM, SET VALVE. POOH. P/U 2.13" BLIND BOX, RIH & BEAT DOWN ON STANDING VALVE 5 TIMES @ 9,482'. POOH. P/U 2-7/8" X 5' PUMP & RIH. UNABLE TO PASS 1,300' WITH JET PUMP. POOH & R/D SLICKLINE @ 1330 HRS. PRODUCTION PUMPED JET PUMP DOWN HOLE & BROUGHT WELL ONLINE @ 1500 HRS. MEMORANDUM State of Alaska Alaska Oil and Gas Conservation Commission J TO: Jim Regg �Q�� X11 IC DATE: 5/2/15 P. I. Supervisor FROM: Bob Noble SUBJECT: No Flow Test Petroleum Inspector Granite Pt State 18742 #30 Bruce Platform jC>����® Mp( 2 2 X015' Hilcorp PTD 1780730 5/2/15: I arrived at the Bruce platform and went over the no-flow procedure and rig up with Hilcorp representative Aaron Douget. I left the well shut in for 3 hours as there was no pressure building up. After 3 hours of shut in time I opened it up to the flow meter and I could just see a bobble on the gauges needle. Not a measureable amount. The well was bleeding through a 1" hose and I could barely feel a whisper of gas coming out of the hose. The following table shows test details: Time Pressures' Flow Rate Remarks (psi) Gas - scf/hr Liquid - gal/hr 8:30 0/0/140 0 0 Shut well in to build pressure 9:30 0/0/140 0 0 Well shut in 10.30 0/0/140 0 0 Well shut in 11:30 0/0/140 <1 0 Opened well up 12:00 0/0/140 <1 0 Turned well back over to them 1 Pressures are T/IA/OA Summary: I witnessed a successful no flow test of Granite Pt Bruce #30. - Attachments: none 2015-0502_No-Flow_GranitePt State_18742_Bruce-30 bn.docx Page 1 of 1 OF 7•y_ ?4, THE STATE Alaska Oil and Gas i ! - ofALAS Conservation Commission _= 333 West Seventh Avenue *h„ ji GOVERNOR BILL WALKER Anchorage, Alaska 99501-3572 Main: 907.279 1433 OFALAS" Fax. 907.276.7542 www,aogcc.alaska gov May 5, 2015 Mr. Stan Golis Operations Manager—CI Offshore Hilcorp Alaska, LLC P.O. Box 244027 Anchorage, AK 99524-4027 RE: No-Flow Verification Granite Pt State 18742 #30 SCANNED RAY 0 5 2015 PTD 1780730 Dear Mr. Golis: On May 2, 2015 an Alaska Oil and Gas Conservation Commission (AOGCC) Petroleum Inspector witnessed a no-flow test of Granite Point State 18742 #30 located on the Bruce Platform in Cook Inlet. The well is operated by Hilcorp Alaska, LLC (Hilcorp). The AOGCC Inspector confirmed that the proper test equipment — as outlined in AOGCC Industry Guidance Bulletin 10-004 — was rigged up on Granite Point State 18742 #30 prior to the test. The well performance was monitored for three hours with resulting flow rates (oil and gas) below the regulatory limits, passing the no-flow test. A subsurface safety valve is not required to be installed in this well based on the no-flow test result. A fail-safe automatic surface safety valve system capable of preventing uncontrolled flow must be maintained in proper working condition in this well as required in 20 AAC 25.265. The subsurface safety valve must be returned to service if Granite Point State 18742 #30 demonstrates an ability to flow unassisted to surface. Any cleanout, perforating or other stimulation work in this well will necessitate a subsequent no flow test. Please retain a copy of this letter on the Bruce Platform. Sincerely, James B. Regg Petroleum Inspection Supervisor cc: P. Brooks AOGCC Inspectors 11$.ol 3 c. STATE OF ALASKA OIL AND GAS CONSERVATION COMMISSION ,rim 1 BOPE Test Report '6k Submit to: iim.reqqalaska.qov AOGCC.Inspectors analaska.gov phoebe.brooks@alaska.gov Contractor Moncla Rig No.: 404 DATE: 4/16/15 Rig Rep.: Steven Solis Rig Phone. 907-776-6660 Operator Hilcorp Alaska Op. Phone: 907-776-6660 Rep.: Bobby Harrington E-Mail bharrington@hilcorp.com Well Name: GRANITE PT 18742 30 - PTD# 1780730 - Sundry# 315-136 - Operation: Drilling: Workover: X Explor.: Test: Initial. Weekly: X Bi-Weekly. Test Pressure(psi): Rams: 250/3000 - Annular: 250/3000 Valves: 250/3000 MASP: 722 MISC.INSPECTIONS: TEST DATA FLOOR SAFETY VALVES: Test Result Test Result Quantity Test Result Location Gen. P Well Sign P - Upper Kelly 0 NA Housekeeping P - Rig P Lower Kelly 0 NA PTD On Location P - Hazard Sec. NA Ball Type 2 P - Standing Order Posted P Misc NA Inside BOP 1 P ' FSV Misc 0 NA BOP STACK: Quantity Size/Type Test Result MUD SYSTEM: Visual Alarm Stripper 0 NA Trip Tank NA NA Annular Preventer 1 13-5/8"5M P Pit Level Indicators P P - #1 Rams 1 2-7/8"-5"vbr P - Flow Indicator NA NA #2 Rams 1 Blinds P - Meth Gas Detector P P • #3 Rams 0 NA H2S Gas Detector P P ` #4 Rams 0 NA MS Misc 0 NA #5 Rams 0 NA #6 Rams 0 NA Quantity Test Result Choke Ln Valves 2 2-1/16" P . Inside Reel valves 0 NA HCR Valves 1 3-1/16" FP Kill Line Valves 2 2-1/16" - P - Check Valve 0 NA ACCUMULATOR SYSTEM: BOP Misc 0 NA Time/Pressure Test Result System Pressure(psi) 3000 - P - CHOKE MANIFOLD: Pressure After Closure(psi) 1700 P Quantity Test Result 200 psi Attained(see) 40 . P ' No Valves 10 P Full Pressure Attained (see) 155 - P ' Manual Chokes 1 P • Blind Switch Covers: All stations Yes Hydraulic Chokes 1 P . Nitgn. Bottles Avg (#and psi): 6@2200 P CH Misc 0 NA ACC Misc 0 NA Test Results Number of Failures: 1 ' Test Time. 4.0 Hours Repair or replacement of equipment will be made within 0 days. Notify the AOGCC of repairs with written confirmation to.AOGCC.Inspectors@alaska gov Remarks: Initial low test on test#2 bleed off on test pump leaking, tighten valve&retest, Test#5 her valve stem leaking, pack off with high pressure grease&retest. AOGCC Inspection 24 hr Notice Yes Date/Time 13 45 4/12/15 Waived By Bob Noble Test Start Date/Time: 4/16/2015 11:30 (date) (time) Witness Test Finish Date/Time: 4/16/2015 15.30 1"440•14.4... -- , '-W4—c lrC NES [�1u•' 4 ''01b 7 d,prrcect ��_ 5ils SCAN Form 10-424(Revised 06/2014) BOPE Form 04-16-2015 xlsx �- -_ �P� - �L��c 404 / � F i -7.4z___ grac�30 /lam 30 _ 41/(0/6-- i _ r?-b 45U') __ `4000, — ..__.__ .. _ --: .__, . / ..." ! ,..," .. . 1 ,.. , //://' -3500 ___ i l // 1 .i)U0 --- -." '',... -.- - i �" .fit 0 __ - ���,`. �\ / ///' '////' ''.,,'..' - . . ' 2,004- - ----•• ___/ -' -' • O . 151 U .\� \ Sr d \ \ \pp a a e . /..../. �0 as -- 0 ./ o - ,� `asap a ,pp • \\°- - --\C- \\\r.\ !pD �Dp . \ \ / // r .71 , / / ti// "''' o441 117; oo ,f Dp 1 ' \ \ \ 1 t7 � � / 'aavwia1 ,./. ,,c-3,; 47 . ,.... cta \ \ I � I 1 1 t.-4; ind f HVHO . i.71"�W ' r- ✓ !, - 1 i 11-- - -\I- \-12: • v Hl-it_OOOS--dW OW 'ON I , 11ijj , � , ; �F 1.�b��f . q / 1 \ \ \ \ \ \ o i/ ' \ \Nil,' _O\ \ //////,,,,,c) 8 Off. i 04 / / / , 0 0 r? " / q ....„ \ _ —0 __,c, , ,-,... \ r S� I 4 _ 0,, © ,/ / / - // / 7 .0 o� as \ / ( ', / / ci o� \\ \ I \ , , ,, „,/, / / . • \\ • • r / ! f f� fr UGS4r'r ` N..,,,,,, .- I 009 REfE—A.tatclet_40 f , ......_____ ------ . .- 60/ t'F 1'674z-mice 3 ,... 0 4//tops ,- ,.. ...7•...--- -_r - - 4500i 3, : 4000- , .. ., .,.,. d- : . ..---350G • 7.-P...--r...u. n . N s:N.' ,,,,Ve7" -. ' 7 000 _ - , N \ / / / / ,, .1__„------:::......,-, 25O0• , Zi1 ------ ( --200°- , , „.,- .. \\ 75\ , . „ \ .... . . .. , •6*-' 1 er 0 /. , ,, ..._,, , ••„60 \ 5\--\\ \ .\\ "5 o / 9 / / / / ., \ , 0 „ •,\00,,,,,A \ \ / / / ------ , / 7 7/ 07 / i i 1 1 /8----/, CHART NO. MC MP 5000 IHR \ . MI •"'"` i 1 -+-.,,,, ....± 1 1 1 'T.- ......;, . , , ,\(MART P:r 1 i ):7N \•••.....--'• I AKEN .11 kr- n m • , i i I) \ , \\(.\ 3°"4C) ....", e , - 40 ? 1 i--- (..,) ..... 1 I I i /- i I C4 **).1 (.,C2 lb . I I *\144 ...s472''.7' M I/1:1/ I \ \ 1 l , \\ \ \\,, RE MARK;; „, \)<\.,(00 N. . 7 I , 0 ) ' / 1 - ;rt ' -' if / i ,,i)s,, r) / , .. ,,,, ,/, Ni/ 0 0 rb 07 ..t,..::.. ''' ' ,/ / . 9 ' /' 0 4,n . ei-.6 cp occ";: // , ..,. „. •-•- 4 1 _ _.. \ .. -, . ,..„ ......1•0 , ",} I C'N .. ). 0 Cv 7 l 64 11 \c___ _.• 0 0\2 4) \\\N --N, ,,,, .2 ,... ---- ---__ __,,--' ,-• ---- ..._ 7 / / NN N. '',. N., •., ---.... -----__ ... __ .._- .-- -- $ --.,..,, --...„.,_ _,,..-- ___-• ,,,,,,,y NN'''/-*"--, ----- ---------- ---- - - .000V• - ' ---'''' .-'---- --- ,..... -...„___ _ ---____ - 0 ... . — _ ov, —-•-•-—_ . • 02 i golt - L 404 ____--- u 60/„ _______,,..........„,..„..: GPF I 674z- grzkce- 3° 4// /,5- ._. ----__--.--- --- ___ ,___ _---4500, _„.„- _,.-------- ___ _..- -• ..----- ..---_------- .-----4000• --. _ - --- )/N ,- ,,,--- --• ____...„...___... ______ _ ! N, • „. ..____ , / /7" ,..--• ----" ,,--- ----- / / • ' ,,---- ,„--- ,--- „----- - „...--•--- __„--• -3000 _. ! . '- /// Z ./"-' ,' ,----'!-- --- . ./ !!!' .., ..-- //// ,- -,, \ _2500- ---- / / ,--- ---- .--- - _-•- -- - . .,200 , a /V i' „--- • 0 ;•,, \ I 7 / 1 . I \ \s 0-.-Iv!'"C -7:-500 0111-1 R-'!! 1 I Li) Mr.If f4 I 11 I 11 ........,..t. 1 i \, "---7-:„- 1 i / I l1 1 / ) • \ - ... - 1 AI 0 . 0 ,-- Z • ---------..,_ : / / / -,, --•. 7 v / ._, V / /// \ \ ----- ''''' •--____ .---- -- ,--”. ,...--7- ./'''---...._ ,---7 --- ---, „,-".- ------.--- -—, . _---------- _ _.--- _.„...- - ——— - ----"''' --- ----' ''''''''-'"---..„ ''''------- ------ ---- ---" --O '----------'--."-'—' ,..------ ----- ---„ ---—-- —_ -.---------- ..., ,_„,------ --,---„,„ .,-- ------- ,_ ----- _ -- 'V (131 5- 02 . , II • BOP EQUIPMENT TESTS a ri�ixiiun Rig: MONCLA 404 - Operator: HILCORP Location: BRUCE Date:4/16/2015 Lease No: COOK INLET Well No.:GRANITE POINT 18742 30 . Previous Test Date 4/5/2015 Test Station Used: REMOTE BOP EQUIPMENT PERIODICAL TESTS TEST LOW TEST HIGH TEST REMARKS NO. Pressure Time Pressure Time Record all items tested, failed test and repairs 1 250 6 MIN 3150 6 MIN ANNULAR,M1,M2,M10,K3&IBOP 2 BLEED OFF VALVE NOT CLOSED ALL THE WAY. 250 5 MIN • 3150 6 MiN PIPE RAMS,TIW,K2,M3,M4,M9 3 250 6 MIN 3150 6 MIN K1,M5,M6 4 1200 MANUAL AND SUPER CHOKE 5 HCR VALVE LEAK GREASED 5A 250 6 MIN . 3000 7 MIN - HCR VALVE C2 6 250 6 MIN 3100 6 MIN C1 7 DRAW DOWN TEST 8 250 5 MIN 3200 6 MIN BLINDS FLUID USED: 3% KCL CHECKLIST ACCUMULATOR TEST Does all equipment hold pressure without excessive pumping? INITIAL PRESSURE 3000 PSI Yes® No❑ Is ACCUMULATOR VOLUME—GALLONS Yes®mNoto❑r void clean and reservoir filled to proper level? Item Closing Ending Volume To Is maximum allowable casing pressure posted on the rig floor? Time Pressure Close Open Yes® No❑ Annular Are accumulator and remote station tagged as to their function? Yes® No 0 2-7/8 X 5 Rams BLIND Rams Is there a spare annular packing element on board? Annular packing element Yes® No❑ Rams N/A N/A At least one set of ram inserts Yes® No❑ Rams N/A N/A Bonnet seals Yes® No❑ CHOKE HCR Drill crews instructed to function pipe and blind rams each trip? Yes 5:1 No El FP. t 6 ri,,cce 30 1 Moncla 404 BOPE Test Procedure 1. Fill stack w/ FIW through kill line with all It, C and NI valves open except 2. Close C when choke manifold is full- shutdown pump when stack is full- close !(m, and annular 3. Fill test jt w/ test pump till fluid comes out IBOP- close IBOP. Test#1 With Annular, Ml, M2, M10, K3 & IBOP closed- pressure up to 250#s- hold f/ 5 mins. Pressure up to 2500#s and hold for 5 mins. Release pressure. Test#2 Close pipe rams and open .nnulc , close Safety Valve- open , close .12- open , close M3 & M4- open close M9- open M2. Test low & high f/ 5 mins. Release pressure. Test#3 Close Ki- open K2, close ;A5 & M6- open M3 & M4. Test low & high f/ 5 mins. Release pressure. Test#4 Close manual & super choke- open M5 & M6. Pressure up to 1200#s & bleed down 200- 300#s w/ each. Release pressure. Test#5 Close C2 (HCR)- open manual & super choke. Test low & high f/ 5 mins. Release pressure. Test#6 Close C open (HCR). Test low & high f/ 5 mins. Release pressure. Test#7 Perform accumulator drawdown test: 1) Turn off electric & air pumps 2) Record accumulator pressure (+- 3000 P5I) 3) Close annular, pipe rams & HCR- open pipe rams to simulate blinds 4) While pressure is stabilizing check pressures in nitrogen bottles & record 5) Record accumulator pressure 6) Turn on electric pump & time seconds to pressure up 200 psi- turn on air pumps & time till unit pressures up to 3000 psi & shuts off (time will start from time electric pump starts till all pumps shut off). Test#8 Pull test jt and close Move test line to M10- close M7 & M8- open . Test low & u h f/ 5 mins. Release pressure. Test additional pipe sizes and safety valves as needed Schwartz, Guy L (DOA) From: Schwartz, Guy L(DOA) Sent: Thursday,April 09, 2015 10:00 AM To: 'Daniel Taylor' Cc: Juanita Lovett; Bettis, Patricia K(DOA) Subject: RE: Br 42-30, PTD: 178-073, Sundry:315-136 Dan, You have approval to re-perf the proposed intervals as shown below . No additional zones are approved. This email will be sufficient documentation for the change to the sundry program and will be placed in our well file. Guy Schwartz Senior Petroleum Engineer AOGCC 907-301-4533 cellCpNNED s Lu 1` 907-793-1226 office CONFIDENTIALITY NOTICE:This e-mail message,including any attachments,contains information from the Alaska Oil and Gas Conservation Commission (AOGCC),State of Alaska and is for the sole use of the intended recipient(s). It may contain confidential and/or privileged information.The unauthorized review,use or disclosure of such information may violate state or federal law.If you are an unintended recipient of this e-mail,please delete it,without first saving or forwarding it,and,so that the AOGCC is aware of the mistake in sending it to you,contact Guy Schwartz at (907-793-1226) or(Guy.schwartz@alaska.gov). From: Daniel Taylor [mailto:dtaylor@hilcorp.com] Sent:Thursday, April 09, 2015 9:27 AM To: Schwartz, Guy L(DOA) Cc: Juanita Lovett Subject: Br 42-30, PTD: 178-073, Sundry: 315-136 Guy, We are currently experiencing some trouble getting through a scale bridge at 8,553ft on Br 42-30. Our plan forward is to pick up a mill and try to clean it out. Our concern is that the scale that we break up is going to end up in the perforations and we will loose our connectivity. The bottom hole pressure being so low we can not get returns when circulating. We would like to re-perforate in the exact same zones once we are finished with our clean out run. Can we get your permission to re-perforate these zones? I have listed our proposed procedure for this below. If you would like to call to discuss I will be on my cell sir. Thank you. Daniel Taylor Operations Engineer CIO—Cook Inlet Offshore Asset Team Cell:907-947-8051 1. Identify and record fluid level. 2. Hold pre job safety meeting. 3. Prepare well for a-line perforating. a. Check well head pressure. b. Ensure crown and wing valves are closed. c. Bleed pressure from well head. d. Ensure there is no trapped pressure. e. Ensure there is proper lighting for operations. f. Keep excess personnel away from operations. 1 g. Ensure perforating unit is yrounded. 4. Rig up lubricator and wire line: a. Test lubricator to+/-1,500psi. 5. Run in hole with 4-5/8in Dummy Gun to tag. 6. Run in hole with perforating gun, GR and CCL and perforate the below intervals. Zone Tc.pMD 9trnMD TopTVD 9tmTVD Amt SPF C-2 8,524 8,582 8,192 8,223 38 5 C-3 8,638 8,730 8,285 8,359 82 5 C-5 8,916 8,884 8.511 8,569 68 5 C-6 8,894 9,014 8,578 8,596 20 5 C-8 9,210 9,222 8,772 8.784 12 5 Q C-7 9,317 9,341 8,872 8,896 24 5 2,( C-7 9,380 9,435 8,932 8,956 26 5 it- C-7 9,470 8,508 8,018 9.054 38 5 C-7 9,518 9,552 9,064 9,097 34 5 C-7 9,590 0.600 0.133 0,143 10 5 C-7 9,804 9,610 9,147 9,153 6 5 C-8 9,684 9,716 9225 9,256 32 5 C.8 9,758 9,820 9,297 9,358 62 5 7. Pull out of hole with perforating guns. 8. Rig down lubricator. 9. If perforating on wireline is not an option we will pursue Tubing Conveyed Perforating. a. Pick up TCP assembly and trip in hole covering the gross interval between 8,524ft and 9,820ft. b. Drop bar and perforate. c. Pick up above perforations making sure well is dead. d. Pull out of hole with TCP assembly laying down guns. 10. Continue on with well work as per Sundry 315-136. 2 OF T� Alaska Oil and Gas („<"--4 OFjsTHE STATE;,-s�� �, ofALASKA Conservation Commission x=__ 333 West Seventh Avenue ' + GOVERNOR BILL WALKER Anchorage, Alaska 99501-3572 OF r h Main: 907.279.1433 Lw914Fax: 907.276.7542 S���SCD �,��r` JE"S www.aogcc.alaska.gov Dan Taylor �� D Operations Engineer I 73 Hilcorp Alaska, LLC 3800 Centerpoint Drive, Suite 1400 Anchorage, AK 99503 Re: Granite Point Field, Middle Kenai Oil Pool, Granite Pt St 18742 30 Sundry Number: 315-136 Dear Mr. Taylor: Enclosed is the approved application for sundry approval relating to the above referenced well. Please note the conditions of approval set out in the enclosed form. As provided in AS 31.05.080, within 20 days after written notice of this decision, or such further time as the AOGCC grants for good cause shown, a person affected by it may file with the AOGCC an application for reconsideration. A request for reconsideration is considered timely if it is received by 4:30 PM on the 23rd day following the date of this letter, or the next working day if the 23rd day falls on a holiday or weekend. Sincerely, Cathy P. Foerster Chair DATED this 3 day of March, 2015 Encl. • 'RECEIVED STATE OF ALASKA MAR 1 1 2015 ALASKA OIL AND GAS CONSERVATION COMMISSION APPLICATION FOR SUNDRY APPROVALS AOGCC 20 AAC 25.280 1.Type of Request: Abandon❑ Plug for Redrill❑ Perforate New Pod❑ Repair Well❑ Change Approved Program 0 Suspend El Plug Perforations 0 Perforate❑ Pull Tubing[=] • Time Extension❑ Operations Shutdown❑ Re-enter Susp.Well❑ Stimulate❑ Alter Casing❑ Other. Complete v`'fi G , 2.Operator Name' 4.Current Well Class: 5.Permit to Drill Number: Hilcorp Alaska,LLC Exploratory ❑ Development 0 ' 178-073 3.Address. 3800 Centerpoint Drive,Suite 1400Stratigraphic ❑ Service El6.API Number. Anchorage,AK 99503 50-733-20322-00 7.If perforating: 8.Well Name and Number. What Regulation or Conservation Order governs well spacing in this pool? N/A Will planned perforations require a spacing exception? Yes ❑ No ❑ Granite Pt St 18742 30 9.Property Designation(Lease Number): 10.Field/Pool(s): ADL0018742 - Granite Pt Field/Middle Kenai Oil Pool . 11. PRESENT WELL CONDITION SUMMARY Total Depth MD(ft): Total Depth TVD(ft): Effective Depth MD(ft): Effective Depth ND(ft): Plugs(measured): Junk(measured). I 9,931 - 9,467 - 9,810' - 9,348' ' N/A 9,810' Casing Length Size MD TVD Burst Collapse Structural Conductor Surface 596' 20" 596' 595' Intermediate 4,516' 13-3/8" 4,516' 4,507' 2,730 psi 1,130 psi Production 9,927' 9-5/8" 9,927' 9,463' 5,750 psi 3,090 psi Liner Perforation Depth MD(ft): Perforation Depth ND(ft): Tubing Size: Tubing Grade: Tubing MD(ft): See Schematic d See Schematic 2-7/8"&3-1/2"dual 6.34#/L-80&9.2#/N-80 8,486'&8,470' Packers and SSSV Type: Packers and SSSV MD(ft)and ND(ft): N/A and N/A N/A and N/A 12.Attachments: Description Summary of Proposal 0 13.Well Class after proposed work: Detailed Operations Program ❑ BOP Sketch 0 Exploratory ❑ Stratigraphic❑ Development1=1 - Service ❑ 14.Estimated Date for 15.Well Status after proposed work. Commencing Operations. 4/1/2015 Oil 0 - Gas ❑ WDSPL ❑ Suspended ❑ 16.Verbal Approval: Date: WINJ ❑ GINJ ❑ WAG ❑ Abandoned ❑ Commission Representative: GSTOR ❑ SPLUG ❑ 17.I hereby certify that the foregoing is true and correct to the best of my knowledge. Contact Dan Taylor Email dtaylor@hilcorp.com Printed Name Dan Ta for Title Operations Engineer Signatures Phone Phone (907)777-8319 Date �fU�J� 3/10/2015 COMMISSION USE ONLY Conditions of approval: Notify Commission so that a representative may witness Sundry Number: �/ 3/6436,Plug Integrity ❑ BOP Test Lld' /� Mechanical Integrity Test ❑ ,,,, Location Clearanccee7❑ Other: f 3OOD re S,, see s/ r ( A 4 P /ZZ.-", ) .3( Wo Flow t 4—e4re 3 (,..4.,e,Q. Spacing Exception Required? Yes ❑ No IA/ Subsequent Form Required: /41— Y Oil APPROVED BY Approved by: 1_ COMMISSIONER THE COMMISSION Date: 3-/3 -/s 1 ZC J) Otey�.{ ' + 1N AI la Submit Fo and tForm 10-403 Revised 10/2012 AO12 months from the date of approval. Attachments in D plicate PYA. 3-/3.•/S RSDMS - MAR 1 6 2015 11 Well Prognosis Well: Br 30-42 Hilcorp Alaska,LL Date:03/10/15 Well Name: GRANITE PT ST 18742#30 API Number: 50-733-20322-00 Current Status: Oil Producer Leg: 3 Estimated Start Date: April 1,2015 Rig: Moncla 404 Reg.Approval Reqd? N/A Date Reg.Approval Rec: Regulatory Contact: Juanita Lovett 777-8332 Permit to Drill Number: 178-073 First Call Engineer: Dan Taylor (907)777-8319(0) (907)947-8051 (M) Second Call Engineer: Reid Edwards (907)777-8421 (0) AFE Number: Current Bottom Hole Pressure: - 1,600 psi at 8,775ft ND Based on slick line fluid level tag at 4,291ft TVD on 3/11/13. Maximum Expected BHP: - 1,600 psi at 8,775ft TVD Based on slick line fluid level tag at 4,291ft TVD on 3/11/13. Max.Allowable Surface Pressure: - 722 psi Based on 0.1 psi/ft gradient to 8,775ft ND Brief Well Summary This well was drilled and completed as a dual string Jet Pump lifted oil well in the Tyonek C2 though C8 intervals. Br 30-42 is currently on-line producing+/-120bopd. The plan forward involves unseating the hanger, pull to floor and break down, pick up additional 2-7/8in tubing and run in hole lowering the cavity. Procedure 1. Reverse out Jet Pump 2. Bleed well off(casing/tubing). 3. Shoot fluid levels on back side(s-line fluid level found at 4,320ft MD on 3/11/13 after 12hr shut-in). 4. Circulate FIW down long string taking returns up short string until clean. a. Work over fluid 3% KCL. 5. Rig up slick line on long string and run in hole and remove standing valve. 6. Run in hole with 2in bailer to tag and pull sample. 7. Ensure well is dead. — FL-ea, 8. Set BPV. 9. Nipple down tree/Nipple up BOPE. a. Function test BOPE(notify AOGCC of test 48hrs prior to expected test). 10. Test BOPE: 60, 3 a. Test BOPE 250psi low and 3,000psi high and chart. 11. Pick up long and short string to floor and set in slips. 12. Pick up and run in hole with cross overs and 2-7/8in EUE tubing to put BHA on depth at+/-9,600ft. 13. Land hanger. A 1: l poitt- c7 14. Set BPV and test. I� 15. Nipple down BOP, nipple up tree and test. 16. Turn well over to production. 17. Complete'No Flow'test in accordance with AOGCC regulations(20 AAC 25.265.Well safety valve systems, section.h). Attachments: 1. As-built Well Schematic 2. Proposed Well Schematic 3. Current/Proposed Wellhead Diagram(same) 4. BOP Stack Bruce Platform SCHEMATIC Well No. BR 30-42 Ililcori)Alaska,LLC Actual Completion 2/28/94 CASING DETAIL API#50-733-20322-00 Size WT Grade Conn ID Top Btm RKB to TBG Head=42.2' ( 20" 94# - 19.124" Surface 596' 13-3/8" 54.5,61, K-55,N-80 Buttress 12.347" Surface 4,516' a 68&72 &5-80 9-5/8" 40&47 N-80&S- !.-.. Buttress 8.681" Surface 9,927' Y. TUBING DETAIL 1. Long String i,. 2-7/8" 6.4# L-80 Buttress 2.441" 43' 8,486' L Short V String 3-1/2" 9.2# L-80 Buttress 2.992" 43' 8,470' a 16/ JEWELRY DETAIL No Depth ID OD Item M 1^)8 Long String /- 42.2' Tubing Hanger,CIW,11",5M,Split Hanger 1 43' 2.441 3.5 X-over,2-7/8"BTC x 3-1/2"BTC(only 0.38'long) 1' 2 8,486' 2.441 3.06 X-over,2-7/8"EUE x 2-7/8"BTC(only 1.1'long) i 3 8,487' 2.25 5.625 Kobe,2-1/2" Dbl.'B'cavity SN 94-2-18(20'long) $' 4 8,507' 2.441 3.06 X-over,2-7/8"BTC x 2-7/8"EUE(1'long) L 5 8,508' 2.441 2.875 1 Joint,2-7/8",6.4#,L-80,BTC tubing 6 8,539' 2.441 4.25 Re-Entry Guide-Bottom @ 8,540' I Short String A A 8,470' 1.995 3.5 X-over,2-3/8"BTC x 3-1/2"BTC(2'long) B B 8,472' 1.995 2.375 Pup,2-3/8",4.6#,N-80,Buttress x 5.4'long 2 C C 8,477' 1.375 2.375 X-over,1-1/4"10 rd EUE x 2-3/8"BTC(2'long) 3 itl isOTE:Long String measurement is 7.7'longer than the short string!! 4 I--- PERFORATION DETAIL Zone Top(MD) Btm(MD) Top(TVD) Btm(TVD) Amt spf Comments Date 5 2-1/8"Slimkone C-2 8,524' 8,562' 8,192' 8,223' 38' 4 Hollow Carrier 2/4/1979 6 Cr C-3 8,638' 8,730' 8,285' 8,359' 92' 8 2-1/8"Silver Jet 4/14/1994 C-5 8,916' 8,984' 8,511' 8,569' 68' 8 2-1/8"Silver Jet 4/14/1994 0 C-6 8,994' 9,014' 8,578' 8,596' 20' 8 2-1/8"Silver Jet 4/14/1994 C-6 9,210' 9,222' 8,772' 8,784' 12' 4 2-1/8"Silver Jet 4/14/1994 C-7 9,317' 9,341' 8,872' 8,895' 24' 8 2-1/8"Silver Jet 4/14/1994 C-7 9,380' 9,406' 8,932' 8,956' 26' 8 2-1/8"Silver Jet 4/14/1994 C-7 9,470' 9,508' 9,018' 9,054' 38' 8 2-1/8"Silver Jet 4/14/1994 C-7 9,518' 9,552' 9,064' 9,097' 34' 8 2-1/8"Silver Jet 4/14/1994 C-7 9,590' 9,600' 9,133' 9,143' 10' 8 2-1/8"Silver Jet 4/14/1994 1* C-7 9,604' 9,610' 9,147' 9,153' 6' 8 2-1/8"Silver Jet 4/14/1994 r` C-8 9,684' 9,716' 9,225' 9,256' 32' 8 2-1/8"Silver Jet 4/14/1994 2-1/8"Slimkone ef C-8 9,758' 9,820' 9,297' 9,358' 62' 4 Hollow Carrier 2/2/1979 0 0 11/12/2012-Coil hard Tag during cleanout @ 9810'CTM • TOF @ 9810' PBTD=9,880' MD (9,416'ND) y • •k-AW "4*It'' TD=9,931' MD(9,467'ND) Revised By TDF 12/7/2012 Bruce Platform • li Proposed Well No. BR 30-42 Hilcorp Alaska,LLC CASING DETAIL API#50-733-20322-00 Size WT Grade Conn ID Top Btm RKB to TBG Head =42.2' - 20" 948 - 19.124" Surface 596' 1 \ / 13-3/8" 54.5,61,68 K-55,N-80& Buttress 12.347" Surface 4,516' &72 S-80 9-5/8" 40&47 N-80&S-95 Buttress 8.681" Surface 9,927' TUBING DETAIL i Long String kb ref 2-7/8" 6.48 L-80 BX tre s 2.441" 43' 9600 N V Short String L , 3-1/2" 9.28 L-80 BX EUE 2.992" 43' 9548 A 2 JEWELRY DETAIL No Depth ID OD Item Long String 42.2' Tubing Hanger,CIW,11",5M,Split Hanger \fly 1 43' 2.441 3.5 X-over,2-7/8"EUE x 3-1/2"BTC(only 0.38'long) 2 ±1061 2.441 3.5 X-over,2-7/8"EUE x 2-7/8"BTC BXP 3 ±9547 2.441 3.06 X-over,2-7/8"EUE x 2-7/8"BTC(only 1.1'long) 4 ±9548 2.25 5.625 Kobe,2-1/2" Dbl.'B'cavity SN 94-2-18(20'long) Z , 5 ±9568 2.441 3.06 X-over,2-7/8"BTC x 2-7/8"EUE(1'long) 6 ±9569 2.441 2.875 1 Joint,2-7/8",6.4#,L-80,BTC tubing 7 ±9600 2.441 4.25 Re-Entry Guide-Bottom @ 8,540' Short String A ±1061 2.441 3.5 X-over,2-7/8"EUE x 3-1/2"BTC BXP B ±9531 1.995 3.5 X-over,2-3/8"BTC x 3-1/2"BTC(2'long) C ±9538 1.375 2.375 X-over,1-1/4"10 rd EUE x 2-3/8"BTC(2'long) i 7# NOTE:Long String measurement is 7.7'longer than the short string!! B PERFORATION DETAIL C Zone Top(MD) Btm(MD) Top(TVD) Btm(TVD) Amt spf Comments Date 2-1/8"Slimkone 3 --- C-2 , 8,524' 8,562' 8,192' 8,223' 38' 4 Hollow Carrier 2/4/1979 II 0 C-3 8,638' 8,730' 8,285' 8,359' 92' 8 2-1/8"Silver Jet 4/14/1994 C-5 8,916' 8,984 8,511' 8,569' 68' 8 2-1/8"Silver Jet 4/14/1994 4 C-6 8,994' 9,014' 8,578' 8,596' 20' 8 2-1/8"Silver Jet 4/14/1994 C-6 9,210' 9,222' 8,772' 8,784' 12' 4 2-1/8"Silver Jet 4/14/1994 C-7 9,317' 9,341' 8,872' 8,895' 24' 8 2-1/8"Silver Jet 4/14/1994 5 C-7 , 9,380' 9,406' 8,932' 8,956' 26' 8 2-1/8"Silver Jet 4/14/1994 C-7 9,470' 9,508' 9,018' 9,054' _ 38' 8 2-1/8"Silver Jet 4/14/1994 6 C-7 9,518' 9,552' 9,064' 9,097 34' 8 2-1/8"Silver Jet 4/14/1994 C-7 9,590' 9,600' 9,133' 9,143' 10' 8 2-1/8"Silver Jet 4/14/1994 C-7 9,604' 9,610' 9,147' 9,153' 6' 8 2-1/8"Silver Jet 4/14/1994 7 / t, C-8 9,684' 9,716' 9,225' 9,256' 32' 8 2-1/8"Silver Jet 4/14/1994 2-1/8"Slimkone C-8 9,758' 9,820' 9,297' 9,358' 62' 4 Hollow Carrier 2/2/1979 eelt 11/12/2012-Coil hard Tag during cleanout @ 9810'CTM y TOF @ 9810' PBTD=9,880'MD (9,416'ND) ;T..„.N.z �,R, TD=9,931' MD(9,467'ND) Revised By DRT 3/10/15 Bruce Platform BR-18742-30 04/04/2014 Hdrurp tla+ka.lit BR 18742-30 Tubing hanger,Dual,CIW-DCB, 20X133/8X95/8X 11X3''AEUElift X3''ABTC susp, 3''A X 2 7/8 w/3"type H BPV profile,5 3/64 centers Valve,Master,CIW-F, 3 1/8 5M 5 bolt,FE,HWO Qty 2 roo ' 1 4_440> 4'0 Adapter,CIW-dual,11 5M stdd X - Vial A.:9_, 3 1/8 5M 5 bolt top,prepped f/3" nom CIW hanger necks Tubing head,CIW-DCB, -- __ 5 3/64 centers 13 5/8 3M X 11 5M,w/2- 2 1/16 5M SSO,X-bottom _.:1 N' IS Ili■= prep — _ III Iii Valve,CIW-F,2 1/16 5M FE, C f� t tIuii. _ 0 HWO Qty 2 J Ili III UP Casing spool,CIW-WF,21'/4 2M ill11_. X 13 5/8 3M,w/2-2 1/16 5MIS IL EFO,X bottom prep Iii Valve,CIW-F,2 1/16 5M FE, 10:7*, - ® HWO MI 711[illetrl CI I lam- . - - III 0 III Casing head,CIW-WF,21'/a 2M X . /1 H SOW,w/2-2 1/16 2M EFO I Valve,CIW-F, 1/16 2M FE, 111 1 ,2 2 Bruce Platform BOP Stack Moncla 02/25/2015 Hifurp tIark.u.11.1 Bruce Platform 2015 Workovers BOP Drawing Moncla in 4.54' • Hyd ' q GK 13 5/8-50' j 00 IiI IiI Iillillil 1/I IF III III III - CU 2 7/8-5 variables or Cameron 4.67' — e$ I. _ — dual flex rams — Blinds I11 I11 I11 III lit Kill Side •- . 111 In•urul III, • 1,.� 110 Choke side 2.00 31/85Mw/HCR ; �' rw,,} l ,z • 31/8SMw/HCR Iii Ili IiI IiI lit- r 1.00'to 2.00' ,!t 11,,t1 ,1 I11 Drill deck 11.00' Riser 13 5/8 5M FE X 13 5/8 5M FE fit III IiI lIt IiI III 111111 III 111 2.00 Spacer spool 13 5/8 5M FE X 13 5/8 5M FE IiI IiI IiI IiI lit Moncla Rig 404 BOP Test Procedure Hilcorp Alaska,LLCAttachment#1 Attachment #1 Hilcorp Alaska, LLC - BOP Test Procedure: Moncla Rig 404, Grayling WO Program — Oil Producers, Water Injectors Pre Rig Move 1) Blow down well, bleed gas to Well Clean Tank that is vented thru flare to atmosphere 2) Load well with FIW to kill well. • Note: Fluid level will fall to a depth that balances with reservoir pressure. 3) Shoot fluid level at least 24 hours before moving on well. 4) Shoot fluid level again, right before ND/NU. Confirm that well is static. Initial Test(i.e.Tubing Hanger is in the Wellhead) If BPV profile is good 1) Set BPV. ND Tree. NU BOP. 2) MU landing joint. Pull BPV. Set 2-way check in hanger. 3) Space out test joint so end of tubing (EOT) is just above the blind rams. 4) Set slips, mark same. Test BOPE per standard test procedure. If the tubing hanger won't pressure test due to either a penetrator leak or the BPV profile is eroded and/or corroded and BPV cannot be set with tree on. Profile and/or landing threads must be prepped while tree is off. Worst Case: BPV profile and landing threads are bad. 1) Attempt to set BPV through tree. If unsuccessful, shoot fluid level. 2) If fluid level is static from previous fluid level shots, notify Hilcorp Anchorage office that the well is static and the tree must be removed with no BPV. As approved in the sundry, proceed as follows: a) ND tree with no BPV b) Inspect and prepare BPV profile to accept a 2-way valve, or prepare lift-threads to accept landing joint to hold pressure. If well is a producer and the culprit is scale, attempt to clean profile with Muriatic acid and a wire brush or wheel. c) Set 2-way check valve by hand, or MU landing (test)joint to lift-threads d) For ESP wells- Ensure that cap is on cable penetrator e) NU BOP. Test BOPE per standard procedure. 3) If both set of threads appear to be bad and unable to hold a pressure test and/or a penetrator leaks, notify Operations Engineer(Hilcorp), Mr. Guy Schwartz (AOGCC) and Mr.Jim Regg (AOGCC)via email explaining the wellhead situation prior to performing the rolling test. AOGCC may elect to send an inspector to witness. As outlined and approved in the sundry, proceed as follows: a) Nipple Up BOPE b) With stack out of the test path, test choke manifold per standard procedure 111 Moncla Rig 404 BOP Test Procedure Hilcmp:llaska, Attachment#1 c) Conduct a rolling test: Test the rams and annular with the pump continuing to pump, (monitor the surface equipment for leaks to ensure that the fluid is going down-hole and not leaking anywhere at surface.) d) Hold a constant pressure on the equipment and monitor the fluid/pump rate into the well. Record the pumping rate and pressure. e) Once the BOP ram and annular tests are completed,test the remainder of the system following the normal test procedure (floor valves,gas detection, etc.) f) Record and report this test with notes in the remarks column that the tubing hanger/BPV profile /penetrator wouldn't hold pressure and rolling test was performed on BOP Equipment and list items, pressures and rates. 4) Pull hanger to surface. (Requires tubing cuts as necessary to free tubing). CBU to displace annulus and tubing with kill weight fluid. 5) If a rolling test was conducted, remove the old hanger, MU new hanger or test plug to the completion tubing. Re-land hanger(or test plug) in tubing head. Test BOPE per standard procedure. Subsequent Tests(i.e.Test Plug can be set in the Tubing-head) 1) Remove Wear bushing. a) Use inverted test plug to pull wear busing. MU to 1 jt. of tubing. b) Thread into wear bushing c) Back out hold down pins d) Pull and retrieve wear bushing. 2) Break off test plug and invert same, and RIH on 1 joint of tubing. Install a closed TIW or lower Kelly valve in top of test joint. 3) Break joint off test plug and pull up to space the bottom of tool joint above blind rams. 4) Test BOPE per standard procedure. STANDARD BOPE TEST PROCEDURE(after 2-way check or test plug is set) 1) Fill stack with rig pump and install chart recorder on the stack side of the pump manifold. 2) Note: When testing, pressure up with pump to desired pressure, close valve on pump manifold to trap pressure and read same with chart recorder. 3) Referencing the attached schematics test rams and valves as follows. a) Close C-1 (inside gate valve on choke side of mud cross) and close the annular preventer. Pressure test to 200 psi for 5 minutes and 1,500 psi high for 5 minutes. If passes after 5 minutes on each, bleed off back to tank and open annular. b) Close Pipe Rams. Test to 200 psi for 5 minutes and 3,000 psi high for 5 minutes. If passes after 5 minutes on each, bleed off back to tank and open pipe rams. c) Test Dual Rams. If the well has dual tubing, and dual rams are installed in the stack,test the dual rams by picking up two test joints with dual elevators and lowering them into stack and position them properly in the dual rams. Close rams. Test to 200 psi for 5 minutes and 3,000 psi for 5 minutes. If passes after 5 minutes on each, bleed off back to tank and open rams. Moncla Rig 404 BOP Test Procedure Hileorp.Alaska.LL( Attachment#1 d) Open C-1. Flow through the choke manifold and purge air. Test the choke manifold starting with the outer most valves,to 250 psi low and 3,000 psi high,for 5 minutes each, as follows: (Valve numbers are in reference to Diagram B) i) Valves 1, 2, 10. After test,open same. ii) Valves, 3,4,9. After test, open valves 3 &4. Leave 9 closed. iii) Valves 5, 6, 9. After test,open valves 5 & 6, leave 9 closed. iv) Valves, 7, 8,9. After test, open all valves. e) Close C-2. This is the HCR(the hydraulic controlled remote)valve just outside C-1 on choke side of mud cross. Test to 250 psi low and 3,000 psi high. After test, open HCR, close C-1. f) Blind Rams. Make sure test joint is above the blind rams. Close blind rams. Test to 200 psi Low for 5 minutes and 3,000 psi High for 5 minutes. Bleed down pressure. g) Bleed off all pressure. Line up pumps to pump down tubing. h) Test K-1, K-2, and K-3 on the kill (pump-in) side by pressuring up on tubing.Test to 200 psi Low for 5 minutes and 3,000 psi High for 5 minutes. i) Test floor valves TIW(or Lower Kelly Valve) and IBOP. STANDARD TEST PROCEDURE OF CLOSING UNIT(ACCUMULATOR) 1) This is a test of stored energy. Shut off all power to electric and pneumatic pumps. 2) Record "Accumulator Pressure". It should be+/-3,000 psi. 3) Close Annular Preventer,the Pipe Rams, and HCR. Close 2"d set of pipe rams if installed (e.g. dual pipe rams). Open the lower pipe rams to simulate the closing volume on the blinds. 4) Allow pressures to stabilize. 5) While stabilizing: Record pressure values of each Nitrogen bottle and average over the number of bottles. (i.e. Report might read "10 bottles at 2,150 psi"). 6) After accumulator has stabilized, record accumulator pressure again. This represents the pressure and volume remaining after all preventers are closed. (The stabilized pressure must be at least 200 psi above the pre-charge pressure of 1,000 psi). 7) Turn on the pump and record the amount of time it takes to build an additional 200 psi on the accumulator gauge. This is usually+/-30 seconds. 8) Once 200 psi pressure build is reached,turn on the pneumatic pumps and record the time it takes for the pumps to automatically shut-off after the pressure to builds back to original pressure (+/-3,000 psi). Note: Make sure the electric pump is turned to "Auto", not "Manual" so the pumps will kick-off automatically. 9) Open all rams and annular and close HCR to place BOPE back into operating position for well work. 10) Fill out AOGCC report. FINAL STEP, FINAL CHECK 1) Test Gas Alarms 2) Double check all rams and valves,for correct operating position 3) Fill out the AOGCC BOPE Test Form (10-424) in Excel Format and e-mail to AOGCC and Juanita Lovett. Document both the rolling test and the follow up tests. Schwartz, Guy L (DOA) n(6 -0-13 From: Schwartz, Guy L (DOA) Sent: Monday, March 02, 2015 9:57 AM To: 'Juanita Lovett'; Daniel Taylor;Ted Kramer Cc: samantha.carlisle@alaska.gov Subject: RE:Withdraw Sundry# 314-198 - Granite Pt St (Bruce) 18742-30 - PTD 178-073 Juanita, AOGCC will withdraw sundry#314-198 as per your request below. Scope of proposed work was to pull dual string completion and run an expandable liner. (There is also a Frac sundry approved for this well. #314-219) Regards, Guy Schwartz Senior Petroleum Engineer S,CANED MAR 0 4 2015 AOGCC 907-301-4533 cell 907-793-1226 office CONFIDENTIALITY NOTICE:This e-mail message,including any attachments,contains information from the Alaska Oil and Gas Conservation Commission(AOGCC),State of Alaska and is for the sole use of the intended recipient(s).It may contain confidential and/or privileged information.The unauthorized review,use or disclosure of such information may violate state or federal law.If you are an unintended recipient of this e-mail,please delete it,without first saving or forwarding it,and,so that the AOGCC is aware of the mistake in sending it to you,contact Guy Schwartz at(907-793-1226) or(Guy.schwarfz@alaska.gov). From: Juanita Lovett [mailto:jlovett@hilcorp.com] Sent: Monday, March 02, 2015 9:49 AM To: Schwartz, Guy L (DOA); Daniel Taylor; Ted Kramer Subject: Withdraw Sundry # 314-198 - Granite Pt St (Bruce) 18742-30 - PTD 178-073 Guy, Please withdraw the above mentioned sundry. Thank you, Juanita Lovett Operations/Regulatory Tech Hilcorp Alaska, LLC 3800 Centerpoint Drive Suite 1400 Anchorage,AK 99503 Office: (907)777-8332 Email: ilovettPhilcorp.com 1 Schwartz, Guy L From: Schwartz, Guy L (DOA) Sent: Monday, January 26, 2015 9:19 AM To: 'Juanita Lovett' Cc: Daniel Taylor; samantha.cariisle@alaska.gov Subject: RE: Withdraw Sundry: Granite Pt St (Bruce) 18742 30 - Sundry # 314-219 Juanita, AOGCC will withdraw sundry 314-219 as requested. SCA NtiED JAN 2 7 2013 Guy Schwartz Senior Petroleum Engineer AOGCC 907-301-4533 cell 907-793-1226 office 013 CONFIDENTIALITY NOTICE: This e-mail message, including any attachments, contains information from the Alaska Oil and Gas Conservation Commission (AOGCC), State of Alaska and is for the sole use of the intended recipient(s). It may contain confidential and/or privileged information. The unauthorized review, use or disclosure of such information may violate state or federal law. If you are an unintended recipient of this e-mail, please delete it, without first saving or forwarding it, and, so that the AOGCC is aware of the mistake in sending it to you, contact Guy Schwartz at (907-793-1226 ) or (Guy.schwartz@alaska.aov). From: Juanita Lovett [mailto:jlovett@hilcorp.com] Sent: Monday, January 26, 2015 8:59 AM To: Schwartz, Guy L (DOA) Cc: Daniel Taylor Subject: Withdraw Sundry: Granite Pt St (Bruce) 18742 30 - Sundry # 314-219 Guy, Please withdraw the above mentioned sundry. Thank you, Juanita Lovett Operations/Regulatory Tech Hilcorp Alaska, LLC 3800 Centerpoint Drive Suite 1400 Anchorage, AK 99503 Office: (907) 777-8332 Email: ilovett@hilcorp.com THE STATE Alaska Oil and Gas °fALASKA Conservation Commission GOVERNOR BILL WALKER 333 West Seventh Avenue Anchorage, Alaska 99501-3572 Main: 907.279.1433 Fax: 907.276.7542 December 5, 2014 Mr. Stan Golis Operations Manager — CI Offshore Hilcorp Alaska, LLC P.O. Box 244027 Anchorage, AK 99524-4027 RE: No -Flow Verification Granite Point State 18742 Well 430 PTD 1780730 Dear Mr. Golis: On July 19, 2014 an Alaska Oil and Gas Conservation Commission (AOGCC) Petroleum Inspector witnessed a no -flow test of Granite Point State 18742 Well #30 located on the Bruce Platform in Cook Inlet. The well is operated by Hilcorp Alaska, LLC (Hilcorp). A subsurface safety valve is not required to be installed in this well based on the no -flow test result. A fail- safe automatic surface safety valve system capable of preventing uncontrolled flow must be maintained in proper working condition in this well as required in 20 AAC 25.265. The AOGCC Inspector confirmed that the proper test equipment — as outlined in AOGCC Industry Guidance Bulletin 10-004 — was rigged up to Granite Point State 18472 Well #30. The well performance was monitored for three hours with resulting flow rates (oil and gas) below the regulatory limits, passing the no -flow test. The subsurface safety valve must be returned to service if Granite Point State 18742 Well #30 demonstrates an ability to flow unassisted to surface. Any cleanout, perforating or other stimulation work in this well will necessitate a subsequent no flow test. Please retain a copy of this letter on the Bruce Platform. cc: P. Brooks AOGCC Inspectors Sincerely, 14(_- vtt . Fky?James B. Regg Petroleum Inspection Supervisor fif ANNFO DEC 0 $ 2014 MEMORANDUM State of Alaska Alaska Oil and Gas Conservation Commission TO Jim Regg i �Z�4ItQ DATE: 7/19/2014 l P. I. Supervisor FROM: Johnnie Hill SUBJECT: No -Flow Test Petroleum Inspector Hilcorp Alaska, Bruce Platform Granite Point State 18742 #30 PTD # 1780730 7/19/14: 1 witnessed the No -Flow test on Hilcorp's Bruce Platform, well# 30 in the Granite Point Field. After the flight to the Bruce Platform I was greeted by the Production Operator Stuart. We reviewed the well condition and their planned no -flow test procedure for Granite Point State Well 18742 Well #30. The well had been shut-in the previous day and depressured with the tubing and inner annulus open to communication and the flow line isolated from production. Test equipment was plumbed from the top of the tree cap through a 2" outlet reduced to a 3/" x %" tee with a 0-30psi calibrated gauge and out to a %" ball valve just upstream of the flow meter. A 1" air/water hose was used to route produced fluids after measurement to an open top barrel that was set near -by. The flow meter was an ERDCO Armor -Flow model 3451-03TO-13 scaled 0-1800 standard cubic feet per hour (SCFH). After gathering initial readings (4 SCFH; 0.2 psi flowing pressure; 130 psi tubing -casing annulus) the tubing was left open upstream of the meter for the first hour followed by a shut in period to allow for pressure build up. The table below summarizes the well's performance during the no -flow test se uence: Time PSI (T&IA/OA/OOA)' Meter (SCFH) Liquid (GPH) Comments 20:25 Initial 0.2/130/65 4.0 0.0 Tubing open to vent 20:50 'h hr 0.2/130/65 4.0 0.0 Tubing left open u/s of meter 21:20 1 hr 0.2/130/65 4.0 0.0 Tubing left open u/s of meter 21:50 '/2 hr 0.4/130/65 0.0 0.0 Tubing closed to vent 22:20 2 hr 1.0/130/65 1800 0.0 Open tubing; 4 SCFH and 0.2 psi after 10 min 22:50 '/2 hr 0.2/130/65 4.0 0.0 Open tubing 23:20 3 hr 0.2/130/65 4.0 0.0 Open tubing During the final flow monitoring period, Bruce 30 gas production decreased from an initial rate1800 to 4 SCFH. No liquid was seen during the test. The sustained flow rate of 4 SCFH was below the maximum allowed. This well is within limits for no flow status. Attachments: Photos (3) SCANNED DEC 3 12 014,' 1 Well is a packerless completion; tubing and tubing -casing annulus are rigged up in communication for the test 2014-0719_No-Flow_GranitePt_State_ 18742_30,j h. docx Page 1 of 2 No -Flow Test — Granite Pt State 18742 Bruce #30 Photos by AOGCC Inspector J. Hill 7/19/2014 No -Flow Test piping arrangement coming off production tree cap Test pressure gauge and flow meter No -Flow meter 2014-0719_No-Flow_GranitePt_State_18742_30 jh.docx Page 2 of 2 Regg, James B (DOA) From: Sent: To: Subject: Attachments: Follow Up Flag: Due By: Flag Status: (qf' S- ,,,re..- 146_14--z- —'i (-' P -i -I'S )760'73c, Larry Greenstein <Igreenstein@hilcorp.com>( I Friday, November 21, 2014 4:10 PM ' -11 I(l2 Regg, James B (DOA) RE: Bruce No Flows Br -30 no -flow pressures.xlsx; Br -08 no -flow pressures.xlsx Follow Up Saturday, November 22, 2014 9:35 AM Flagged ,cttite� +x, o Te_s- -7(111(A You bet, Jim. We have the TIO plot that shows the IA drop during the no -flow and the OA stability throughout the no -flow tests on 7/19/14. Hope this data will work for you. Larry From: Regg, James B (DOA) [mailto:jim.regg@alaska.gov] Sent: Friday, November 21, 2014 3:40 PM To: Larry Greenstein Subject: Bruce No Flows Thanks for checking. Could I bother you for an email of the pressures for IA and OA during the no flow tests? Not picking on format – scanned datasheet or listing of pressures in email. Whatever you can provide would be appreciated so I have correct info for our report. Jim Regg Supervisor, Inspections AOGCC 333 W. 7th Ave, Suite 100 Anchorage, AK 99501 907-793-1236 CONFIDENTIALITY NOTICE: This e-mail message, including any attachments, contains information from the Alaska Oil and Gas Conservation Commission (AOGCC), State of Alaska and is for the sole use of the intended recipient(s). It may contain confidential and/or privileged information. The unauthorized review, use or disclosure of such information may violate state or federal law. If you are an unintended recipient of this e-mail, please delete it, without first saving or forwarding it, and, so that the AOGCC is aware of the mistake in sending it to you, contact Jim Regg at 907- 793-1236 or iim.re�s alaska.gov. •MVJ 200 100 I 0 GPF Bruce 030 AOL 18742 - [50.0585.0045] 07/13/2014 07/20/2014 —95/8 13 3/8 20 Well: BR 30-42 Desc: Hydraulic Pump Permit to drill: 1780730 Admin Approval: N/A API: 50-733-20322-00-00 Date Range: 07/13/2014 - 07/26/2014 Date 95/8 133/8 20 7/26/2014 108 137 67 7/25/2014 78 137 67 7/24/2014 81 140 67 7/23/2014 84 140 67 7/22/2014 86 140 67 7/21/2014 79 140 67 7/20/2014 75 135 65 w 7/19/2014 0 135 65 7/18/2014 1 135 65 7/17/2014 63 137 65 7/16/2014 224 135 68 7/15/2014 111 137 68 7/14/2014 111 137 70 7/13/2014 113 137 70 o A 00br 200 150 100 50 Imac. ect Well History File Cover e XHVZE This page identifies those items that were not scanned during the initial production scanning phase. They are available in the original file, may be scanned during a special rescan activity or are viewable by direct inspection of the file. 71 _ o7 _ Organizing RESCAN [] Color items: [] Grayscale items: [] Poor Quality Originals: [] Other: NOTES: DIGITAL DATA OVERSIZED (Scannable) Diskettes. No. [] Maps: [] Other, No/Type [] Other items scannable by large scanner OVERSIZED (Non-Scannable) Logs of various kinds BY: BEVERLY ROBIN VINCENT SHERYL~INDY [] Other Project Proofing BY; Scanning Preparation BEVERLY ROBIN VINCENT SHERYL ~'NDY DATE; 14 I~11 ~'~/~/ ~ I x 30 = 3 0 + = u-5'-" BY: Production Scanning Stage 1 PAGE COUNT FROM SCANNED FILE: ',,~,~ PAGE COUNT MATCHES NUMBER IN SCANNING PREPARATION: YES NO Stage 2 IF NO IN STAGE 1, PAGE(S) DISCREPANCIES WERE FOUND: YES NO V~ARIA DATE'/;-/~SI J~ BY: BEVERLY ROBIN WINDY ~..~ ~.,~..~/~,~......~~ ReScanned (individua! page [special at~e¢~fi~] ~catming completed) RESCANNED BY; BEVERLY ROBIN VINCENT SHERYL MARIA WINDY DATE; General Notes or Comments about this file: Is~ Quality Checked 12110/02Rev3NOTScanned.wpd 4�� I// THE STATE Alaska C S y / 0 ' — 333 vilest Seventh Avenue GOVERNOR SEAN PARNELI, Anchorage, Alaska 99501-3572 *:, � � Maya, 907 279 1433 Dan Taylor u,ANHE° AUG 0 8 214 Operations Engineer f g�' 3 Hilcorp Alaska, LLC 3800 Centerpoint Drive, Suite 1400 Anchorage, AK 99503 Re: Granite Pt Field, Middle Kenai Oil Pool, Granite Pt St(Bruce) 18742 30 Sundry Number: 314-219 Dear Mr. Taylor: Enclosed is the approved application for sundry approval relating to the above referenced well. Please note the conditions of approval set out in the enclosed form. As provided in AS 31.05.080, within 20 days after written notice of this decision, or such further time as the AOGCC grants for good cause shown, a person affected by it may file with the AOGCC an application for reconsideration. A request for reconsideration is considered timely if it is received by 4:30 PM on the 23rd day following the date of this letter, or the next working day if the 23rd day falls on a holiday or weekend. Sincerely, 7724te,a4,' Cathy P. oerster Chair DATED this 2^Litof April, 2014. Encl. RECEIVED STATE OF ALASKA APR 0 4 2014 ALASKA OIL AND GAS CONSERVATION COMMISSION 4.1 Z-11 I T- APPLICATION FOR SUNDRY APPROVALS /kOGCC 20 MC 25.280 1.Type of Request: Abandon❑ Plug for Redrill❑ Perforate New Pool 0 a, Repair Well❑ Change Approved Program 0 Suspend 0 Plug Perforations 0 Perforate Lids Pull Tubing❑ Time Extension❑ Operations Shutdown❑ Re-enter Susp.Well 0 Stimulate (Frac)14CAIJ Atter Casing❑ Other: Install ESP Q 2.Operator Name: 4.Current Well Class: 5.Permit to Drill Number: Hilcorp Alaska,LLC Exploratory 0 Development Q• 178-073 = 3.Address: 3800 Centerpoint Drive,Suite 1400Stratigraphic 0 Service 0 6.API Number: Anchorage,AK 99503 50-733-20322-00 - 7.If perforating: 8.Well Name and Number: What Regulation or Conservation Order governs well spacing in this pool? N/A ✓ Will planned perforations require a spacing exception? Yes El No IZl14° Granite Pt St(Bruce)18742 36). _ 9.Property Designation(Lease Number): 10.Field/Pool(s): ADL0018742 Granite Pt Field/Middle Kenai Oil Pool• 11. PRESENT WELL CONDITION SUMMARY Total Depth MD(ft): Total Depth TVD(ft): Effective Depth MD(ft): Effective Depth TVD(ft): Plugs(measured): Junk(measured): 9,931 , 9,467 ` 8,513' ' N/A 8,513'(fill) Casing Length Size MD TVD Burst Collapse Structural Conductor Surface 596' 20" 596' 595' Intermediate 4,516' 13-3/8" 4,516' 4,507' 2,730 psi 1,130 psi Production 9,927' 9-5/8" 9,927' 9,463' 5,750 psi 3,090 psi Liner Perforation Depth MD(ft): Perforation Depth TVD(ft): Tubing Size: Tubing Grade: Tubing MD(ft): See Schematic See Schematic 2-7/8"&3-1/2"dual 6.4#/L-80&9.2#/N-80 8,486'&8,470' Packers and SSSV Type: Packers and SSSV MD(ft)and TVD(ft): ' N/A and N/A N/A and N/A 12.Attat'hments: Description Summary of Proposal ❑ % 13.Well Class after proposed work: r Detailed Operations Program 0 BOP Sketch 9 • Exploratory❑ Stratigraphic❑ Development El• Service 0 14.Estimated Date for 15.Well Status after proposed work: 4/15/2014 Commencing Operations: Oil 9 • Gas ❑ WDSPL 0 Suspended ❑ 16.Verbal Approval: Date: WINJ ❑ GINJ ❑ WAG ❑ Abandoned ❑ Commission Representative: GSTOR ❑ SPLUG ❑ 17. I hereby certify that the foregoing is true and correct to the best of my knowledge. Contact Dan Taylor Email dtaylor@hilcorp.com Printed Name Dan Taylor //�� i Title Operations Engineer 9 4�i' /4"-I,.._. -4,7. �1i� Si nature ��Phone (907)777-8319 Date 4/4/2014 COMMISSION USE ONLY Conditions of approval: Notify Commission so that a representative may witness Sundry Number: 3ki-1- 2\cl Plug Integrity ❑ BOP Test Mechanical Integrity Test ❑ Location Clearance❑ Other: ..t. 300 rs� gaP fiT:sk RBDM MAY 08 2014 eE io Ft 0 w -f-a s 4- le l ...L.L.4-e n Spacing Exception Required? Yes ❑ No Subsequent Form Required: Chem(cal AAT jou tt-e, -fa cacra,US 0 APPROVED BY Approved by: ,,j64.7 1,- COMMISSIONER THE COMMISSION Date: 4 vi /c/ /� Submit Form and Form 10-403(Revised 10/2012) Appr v Ri c/'gym2 r i r months from the date of approval. Attachmentss in Duplicate 4170y II Well Prognosis Well: Br 30-42 IIileorn Alaska.LLQ Date: 04/04/14 Well Name: GRANITE PT ST 18742#30 API Number: 50-733-203-22 Current Status: Oil Producer Leg: 3 Estimated Start Date: April 15, 2014 Rig: Moncla 301 Reg.Approval Reqd? N/A Date Reg.Approval Rec: Regulatory Contact: Juanita Lovett 777-8332 Permit to Drill Number: 178-073 First Call Engineer: Dan Taylor (907) 777-8319 (0) (907)947-8051 (M) Second Call Engineer: Reid Edwards (907) 777-8421 (0) AFE Number: Current Bottom Hole Pressure: — 1,600 psi at 8,775ft TVD Based on slick line fluid level tag at 4,291ft TVD on 3/11/13. Maximum Expected BHP: 1,600 psi at 8,775ft TVD Based on slick line fluid level tag at 4,291 ft TVD on 3/11/13. Max.Allowable Surface Pressure: — 0 psi Based on 2/3 gas filled and 1/3 fluid filled well with 0.1 psi/ft gas and 0.35psi/ft diesel to 8,775ft TVD Brief Well Summary This well was drilled and completed as a dual string Jet Pump lifted oil well in the Tyonek C2 though C8 intervals. Br 30-42 is currently on-line producing +/-80bpd. The following Hydraulic Fracture procedure directly follows the earlier application for Sundry approval requesting to pull the dual string completion. That procedure covered the nippling down of the well head and the nippling up of BOP equipment and subsequent test. The well has been cleaned out and the expandable liner has been set across the perforations. The plan forward is to shoot perforations and hydraulically fracture the C-7 and C-8 sands./ L_____,), su jtt- 1 711A7 7.S2 Procedure: Regulation Response • See below table for casing sizes and specifications. Section a)6. • A cement bond log will be run prior to hyd frac in order to Detailed casing and cementing information. establish top of cement and cement quality in 9-5/8in casing. Date Size WT Grade Collapse Internal Body Con. ID Drift Cement bbl/ft Total Top BTM Installed (in) (lbs/ft) (psi) Min Yield Yield (in) (in) Top (bbls) (MD,ft) (MD,ft) (psi) (1000Ibs) (MD) 10/30/1978 20 94 - - - - - 19.124 18.936 - - - - - 11/12/1978 13 3/8 54.5 K-55 1,130 2,730 850 BUTC 12.615 12.459 Surf - - - - 11/12/1978 13 3/8 61 N-80 1,540 3,090 962 BUTC 12.515 12.359 Surf _ - - 11/12/1978 13 3/8 68 1,950 3,450 1,069 BUTC 12.415 12.259 Surf -- 11/12/1978 13 3/8 72 S-80 2,670 5,380 1,661 BUTC 12.347 12.191 Surf 4,516 1/20/1979 9 5/8 40 N-80 3,090 5,750 916 BUTC 8.835 8.679 Log 0.0758 - - - 1/20/1979 9 5/8 47 S-95 7,100 8,150 1,289 BUTC 8.681 8.525 Log 0.0732 748 294 9,927 . Well Prognosis Well: Br 30-42 IIilcor')Alaska,LL' Date:04/04/14 Regulation Response Section a)7. An assessment of each casing and cementing operation performed to construct or repair the well with sufficient • Please see table in Section a)6.for casing sizes and supporting information, including cement evaluation logs and specifications. other evaluation logs approved by the commission, to • A cement bond log will be run prior to hyd frac in order to demonstrate that casing is cemented below the base of the establish current cement quality in 9-5/8in casing. lowermost freshwater aquifer and according to 20 AAC • No fresh water aquifers are present. 25.030 and that all hydrocarbon zones penetrated by the well are isolated; Section a) 8. • A casing integrity test will be performed within the 9- Pressure test information if available and plans to pressure 5/8in casing prior to hydraulic fracture. test the casings and tubing installed in the well; • Please see the below figure for historical pressure data. 100 50 9-5/8in 400- .300 73-3/8in 1) '5 200- a'100- _ v 300 200- 20in 1001 Oct 2013 Nov 2013 Dec 2013 Jan 2014 Feb 2014 Mar 2014 Date Section a)9. • See 'Section a)6.'for accurate pressure ratings on the Accurate pressure ratings and schematics for the wellbore, casing. wellhead, BOPE, and treating head: • Please see attached schematic of well bore,well head, BOPE, and treating head. • Miocene Middle Tyonek Group--C-7C/D& C-8B/C Sands. • Interbedded, upward fining very course to fine grained sandstone, conglomeritic sandstone, and conglomerate intervals with interbedded siltstone that locally grades to Section a) 10. muddy coal. • Data for the fracturing zone and confining zones including MD-TVD of objectives: lithologic description, geological name, measured depth (MD) C 7C/D: 9470'-9583' MD; 9017-9126'TVD and true vertical depth (TVD), measured and true vertical C 8B/C: 9685'-9829' MD; 9225-9367'TVD thickness, and estimated fracture pressures for the fracturing • MD TVD thickness of target sands zone and confining zones; C-7C:45ft MD 33ft TVD C-7D: 37ft MD-25ft TVD C-8B: 32ft MD- 14ft TVD C-8C: 67ft MD-45ft TVD • Fracture pressure estimated to be 0.85 psi/ft. This value • is based data gathered during a previous attempt to fracture stimulate these same zones in this well. Section a) 11. The geologic name and depth (MD and TVD)to the bottom • None of all freshwater aquifers within the one-mile radius of the proposed wellbore trajectory. Mite. 01J Well Prognosis Well: Br 30-42 Hilcorp Alaska,LL Date:04/04/14 Regulation I Response Section a)12. The location,orientation,and a report on the mechanical condition of each well that may transect the confining zones and information sufficient to support a determination that such wells will not interfere with containment of the hydraulic fracturing fluid within the one-half mile radius of the proposed wellbore trajectory; WELL PTD Location Relative Description Mechanical Condition to BR-08-86 BR-86-03LT2 193-127 2018'W-NW Current producer inMidTyonekGroup N/A BR-86-03LT2PB 167-006 2234'W-NW P&A N/A BR-86-03LT1 193-127 2291 W-NW Current producer in Mid Tyonek Group No known AnnCom Issues BR-86-03LT1PB 167-006 1771W-NW P&A N/A BR-86-03 167-006 1374'W-NW P&A No known AnnCom Issues TYST86-01 166-036 1576'W P&A N/A B R-42-20R D 2538'N Current producer in Mid Tyonek Group No known A nnCo m Issues Shut in,completed in shallower interval above proposed frac BR42-16 167-077 2248'SW interval N/A BR-86-03RD 193-127 1887'W-NW Current producer in Mid Tyonek Group No known AnnCom Issues BR-86-08 180-084 1657'SW Current producer in Mid Tyonek Group No known AnnCom Issues BR-42-31 178-096 2304'SE P&A N/A Shut in Mid Tyonek Water producer;casing damage above BR-42-18 168-012 1393'E-NE frack interval No known AnnCom Issues BR-42-12RD 178-059 2283'NE Shut in M id Tyonek Water Inj No known AnnCom Issues TYST42-02 163-006 518'E P&A N/A BR42-10 167-042 1344'S P&A N/A BR86-05 168-046 1928'NW P&A N/A BR86-05RD 179-005 1659'NW Shut in Mid Tyonek Water lnj No known A nnCo m Issues B R-42-06 167-019 1459'N Shut in Mid Tyonek Water Inj No known AnnCom Issues Section A)13. The location,orientation,and geological data of known or suspected faults and fractures that may transect the confining zones,and information sufficient to support a determination that any such faults No faults are mapped within a%mile radius. and fractures will not interfere with containment of the hydraulic fracturing fluid within the one-half mile radius of the proposed wellbore _ trajectory; Section A)14. A detailed copy of the proposed hydraulic fracturing program including, Please see the attached fracturing program and the applicable but not limited to,the pumping procedure by stage where applicable, MSDS. with a chemical disclosure based on the total amounts and volumes per well including; Component Stage Total Section A)14.a) Frac Fluid(weathered oil) C7 38.4 kgal The estimated total volumes planned; Proppant C7 70.9 klbs Frac Fluid(weathered oil) C8 39.7 kgal Proppant C8 58.5 klbs Trade Name Generic Name Concentration Section A)14.b) GBO-5L Special:Gel Breaker 1 gpt The trade name,generic name,and purpose of all base fluid(s)and GO 64 Special:Oil Gelling Agent 12 gpt additives to be used.The estimated or maximum rate or concentration CarboLite Proppant 129 klbs of each additive shall be provided in appropriate measurement units; NE-110W Special: Non-Emulsifier 1 gpt XLO-5 Special:Cross-Linking 12t Agent gpt Well Prognosis Well: Br 30-42 llilcora Alaska,LI) Date:04/04/14 Regulation _ Response Section A)14.c) The chemical ingredient name and the Chemical Abstracts Service (CAS)Registry number,as published by the Chemical Abstracts Service(a division of the American Chemical Society,see www.cas.org),for each base fluid and each additive used.The actual or maximum concentration of each chemical ingredient in each base Please see attached MSDS sheets. fluid and additive used shall be provided in percent by mass. In addition,the actual or maximum concentration of each chemical ingredient in the hydraulic fracturing fluid shall be provided in percent by mass.Freeze-protect fluids pumped before and/or after hydraulic fracturing should not be included; Section A)14.d) Component Stage Total The estimated weight or volume of inert substances, including Proppant C7 70.9 klbs proppants and other substances injected; Proppant C8 58.5 klbs Section A)14.e) The maximum anticipated treating pressure and information sufficient to support a determination that the well is appropriately constructed for the proposed hydraulic fracturing program; See Figure 3: Fracture String Annulus Fluid Density= 6.8 ppg Max Treating Density= 11.34 ppg' Applied Anular Pressure= 1,000 Max Treating Pressure= 8,000 Recent Fluid Level= - Maximum Differential Pressure at Depth(psi) Below Formation Premium Premium Premium Item Depth(TVD) String Annulus Friction AP Pipe Packer (0.435psi/ft) AP Pkr Tubing % X 90% % X 80% Surface Surface - - - - - - - 15,638 51% 14,074 57% 12,510 64% SurfaceTOH Surface 8,000 1,000 - 7,000 - - - 15,638 45% 14,074 50% 12,510 56% 5in X 3.5in XO 8,089 12,770 3,860.27 1,086 7,824 - - - _ 15,638 50% 14,074 56% 12,510 63% Top ofPKR 8,170 12,818 3,888.91 1,211 7,718 - - - _ 21,429 36% 19,286 40% 17,143 45% Btm of PKR 8,170 - - 1,211 - 12,818 3,554 8,053 8,150 99% 7,335 110% 6,520 124% • Across Packer set at: 8,470 ft Below Above Friction AP Pkr 100% 12,995 psi 3,995 psi 1,211 psi 7,789 psi 9,000 psi_ 87% Heig Leng MD TVD Section A)14.f) Sand ht th (ft) (ft)) The designed height and length of the proposed fracture(s), (ft) (ft) including the calculated MD and TVD of the top of the C7 57 495 9,52 9,07 fracture(s)accompanied by a description of the methods and 5 0 assumptions used to determine designed fracture height and 9,74 9,28 length; C8 72 617 0 0 Please see attached Stimplan Model used for simulation. Plan Description Shut in Master Valve. Section A)15. Sut in TIW Valve. A detailed description of the plan for post fracture wellbore Bleed off frac lines to clean up tank. cleanup and fluid recovery through to production operations. Bleed off tubing and stored frac pressure from pump in sub below TIW valve to Opsi and monitor(route fluid to clean up tank). Ensure returns are broke by adding chemical if needed and route to production. Section B) When hydraulic fracturing through production casing or through intermediate casing,the casing must be tested to 110%of the maximum anticipated pressure differential to Refer to Section c) which the casing may be subjected. If the casing fails the pressure test it must be repaired or the operator must use a temporary casing string(fracturing string). Well Prognosis Well: Br 30-42 Hilcorp Alaska,LI) Date:04/04/14 Regulation Response Section C) When hydraulic fracturing through a fracturing string,the fracturing string must be stung into a liner or run on a Frac string will be tested to 110%of the maximum packer set not less than 100 ft MD below the cement top anticipated pressure differential of 7,122psi. of the production or intermediate casing and tested to 7,122psi X 1.10=—8,000psi not less than 110%of the maximum anticipated pressure differential to which the fracturing string may be subjected. Section D) A single nitrogen pop off valve will be placed between A pressure relief valve(s) must be installed on the the pumps and"wellhead" (fracture head)and set and treating lines between pumps and wellhead to limit the , tested before the start of frac operations. line pressure to the test pressure determined in (a)14(E) of this section;the well must be equipped with a 5000 Pi Please see the attached`Frac Iron Configuration:Tri- remotely controlled shut-in device unless the operator plex Pump to Well'. requests and obtains a waiver from the commission. Section E) The placement of all hydraulic fracturing fluids shall be Only approved formations will receive fracturing fluids. confined to the approved formations during hydraulic fracturing. Section F) If the surface casing annulus is not open to atmospheric pressure,then the surface casing pressures shall be monitored with a gauge and pressure relief device while Surface casing annulus will be open to atmospheric hydraulic fracturing operations are in progress;the annular space between the fracturing string and the pressure. intermediate or production casing must be continuously Surface casing pressure will be continuously monitored. monitored;the pressure in such annular space may not exceed the pressure rating of the lowest rated component that would be exposed to pressure should the fracturing string fail. Procedure 1. Swap well over to diesel. g0 €} 2. Rig up and run in hole with perforating guns and perforate across the interval+/-9,700ft to+/-9.780ft. 3. Pick up and run in hole with 9-5/8in 9kpsi retrievable packer and set at+/-8,470ft. a. Surface to 8,470ft, 5in 19.5lbs/ft S-135 i. Total theoretical weight:—170klbs(Moncla 301 max pull: 336kIbs). b. Ensure work string is rattled and clean. 4. Pressure test packer to+/-2,500psi and chart 30min. 5. Pressure test work string: a. Rig up slick line and run in hole with 20kpsi PRR test plug and set in RN nipple. i. Run in hole and set prong. b. Pressure test work string to—8,000psi (+1-110%of max STP) and chart. c. Rig up slick line and run in hole to remove prong and PRR test plug. 6. Install 15kpsi TIW valve and pump in sub. 7. Prepare rig and platform for fracture treatment. a. Install and inspect surface connections. b. Hold pre-job safety stand down to identify all hazards. i. Walk all escape routes for all personnel. c. Review attached MSDS sheets. d. Shut in BOP. i. Continuously man closed choke. ii. Production and frac crew to monitor back side pressure. iii. Set inner annulus pop off valve. ---i 2 5 o tori, e. Rig up fra-61 re rea n equipmen . i. Rig up pressure relief valve(s)on treating line(s)between pumps and wellhead. ii. Review the set pressure of the nitrogen pop off valve. f. See the attached calculations based on the anticipated maximum surface treating pressure of 7,615psi. Well Prognosis Well: Br 30-42 Hiicorp Alaska,LL) Date:04/04/14 g. Set nitrogen pop off valve to+/-10,500psi. 1. Set all pump Rick out pressures. 8. Begin fracture treatment of C-8 sand as per Baker Hughes hydraulic fracture procedures. a. Monitor and record all annular pressures. i. ***All annular pressures need to have recordable data turned into the state. 9. Upon shutting off frac pumps bleed back well to clean up tank. a. Inspect all fluid before sending to production. 10. Shut in master valve/Shut in TIW valve. a. Monitor frac string surface pressure through side entry sub pressure gauge. b. Bleed off all pressure to clean up tank and ensure well is dead. i. Monitor well for 1/2hr. 11. If possible(no screen out and gel is broke)rig up and run in hole with slick line to tag and record sand fill level. 12. Pump sand plug over uncovered C-8 perforations making sand plug to+/-9.600ft. SA-v 1) I) • 13. Pick up and run in hole with perforating guns and perforate interval +/-9,500ft to+/-9,550ft within the C7 sand. 14. Install 15kpsi TIW valve and pump in sub. 57) 15. Prepare rig and platform for fracture treatment. a. Install and inspect surface connections. b. Hold pre-job safety stand down to identify all hazards. c. Review attached MSDS sheets. d. Shut in BOP. i. Continuously man closed choke. ii. Production and frac crew to monitor back side pressure. Set inner annulus pop off valve. e. Rig up fracture treatment equipment. i. Rig up pressure relief valve(s)on treating line(s) between pumps and wellhead. ii. Review the set pressure of the nitrogen pop off valve. f. See the attached calculations based on the anticipated maximum surface treating pressure of+/-6,764psi. g. Set nitrogen pop off valve to+/-10,500psi. 1. Set all pump kick out pressures. 16. Begin fracture treatment of C-7 sand as per Baker Hughes hydraulic fracture procedures. a. Monitor and record all annular pressures. i. ***AII annular pressures need to have recordable data turned into the state. 17. Upon shutting off frac pumps bleed back well to clean up tank. a. Inspect all fluid before sending to production. 18. Shut in master valve/Shut in TIW valve. a. Monitor frac string surface pressure through side entry sub pressure gauge. b. Bleed off all pressure to clean up tank and ensure well is dead. 19. Pull out of hole with frac string and packer. 20. Pick up and run in hole with bailer assembly. a. Bail sand off packer. b. 12bbls sand/-2,000ft capture chamber 21. Pick up brush and clean out to bottom. 22. Pick up and run in hole with completion to+/-8,426ft: G 5 b(1 a. ESP/Cable b. 1/4in Chemical lnj Line c. 2-7/8in EUE tubing C►om p�. d. 2-7/8in EUE X No.2 CBL+ 1/4in bare cap string Cannon Clamps 23. Land hanger a. Pressure test across seals 1,500psi. 24. Nipple down BOP and Nipple up tree. 25. Turn well over to platform production. << k• "1-Z-51" /07 t-t-24.0 Attachments: 1. As-built Well Schematic. 2. Proposed Well Schematic. 3. BOP Schematic. 4. Well Head Schematic(s). 5. Surface connections. 6. MSDS Sheets. Bruce Platform n- SCHEMATIC Well No. BR 30-42 Ililcorp Alaska,LLC Actual Completion 2/28/94 CASING DETAIL API#50-733-20322-00 Size WT Grade Conn _ ID Top Btm RKB to TBG Head=42.2' - 20" 94# - 19.124" Surface 596' 13-3/8" 54.5,61, K-55,N-80 Buttress 12.347" Surface 4,516' 68&72 &5-80 9-5/8" 40&47 N-800&S- Buttress 8.681" Surface 9,927' TUBING DETAIL Long String 2-7/8" 6.4# L-80 Buttress 2.441" 43' 8,486' L r L Short String 3-1/2" 9.2# L-80 Buttress 2.992" 43' 8,470' ('' JEWELRY DETAIL No Depth ID OD Item Long String 42.2' Tubing Hanger,CIW,11",5M,Split Hanger 1 43' 2.441 3.5 X-over,2-7/8"BTC x 3-1/2"BTC(only 0.38'long) j 2 8,486' 2.441 3.06 X-over,2-7/8"EUE x 2-7/8"BTC(only 1.1'long) 3 8,487' 2.25 5.625 Kobe,2-1/2" Dbl.'B'cavity SN 94-2-18(20'long) 4 8,507 2.441 3.06 X-over,2-7/8"BTC x 2-7/8"EUE(1'long) Z. 5 8,508' 2.441 2.875 1 Joint,2-7/8",6.4#,L-80,BTC tubing 6 8,539' 2.441 4.25 Re-Entry Guide-Bottom @ 8,540' Short String A A 8,470' 1.995 3.5 X-over,2-3/8"BTC x 3-1/2"BTC(2'long) B B 8,472' 1.995 2.375 Pup,2-3/8",4.6#,N-80,Buttress x 5.4'long 2 C C 8,477' 1.375 2.375 X-over,1-1/4"10 rd EUE x 2-3/8"BTC(2'long) 3 NOTE:Long String measurement is 7.7'longer than the short string!! - I 4 PERFORATION DETAIL Zone Top(MD) Btm(MD) Top(TVD) Btm(TVD) Amt spf Comments Date 5 2-1/8"Slimkone C-2 8,524' 8,562' 8,192' 8,223' 38' 4 Hollow Carrier 2/4/1979 6 ce C-3 8,638' 8,730' 8,285' 8,359' 92' 8 2-1/8"Silver Jet 4/14/1994 TOF @ 8,513' C-5 8,916' _ 8,984' 8,511' 8,569' 68' 8 2-1/8"Silver Jet 4/14/1994 > C-6 8,994' _ 9,014' 8,578' 8,596' 20' 8 2-1/8"Silver Jet 4/14/1994 C-6 9,210' 9,222' 8,772' 8,784' 12' 4 2-1/8"Silver Jet 4/14/1994 • C-7 9,317' 9,341' 8,872' 8,895' 24' 8 2-1/8"Silver Jet 4/14/1994 C-7 9,380' 9,406' 8,932' 8,956' 26' 8 2-1/8"Silver Jet 4/14/1994 C-7 9,470' 9,508' 9,018' 9,054' 38' 8 2-1/8"Silver Jet 4/14/1994 C-7 9,518' 9,552' 9,064' 9,097' 34' 8 2-1/8"Silver Jet 4/14/1994 C-7 9,590' 9,600' 9,133' 9,143' 10' 8 2-1/8"Silver Jet 4/14/1994 C-7 9,604' 9,610' 9,147' 9,153' 6' 8 2-1/8"Silver Jet 4/14/1994 C-8 9,684' 9,716' 9,225' 9,256' 32' 8 2-1/8"Silver Jet 4/14/1994 2-1/8"Slimkone C-8 9,758' 9,820' 9,297' 9,358' 62' 4 Hollow Carrier 2/2/1979 5/26/2012-Tag fill @ 8,513'with 1-3/4"Dump Bailer I PBTD=9,880' MD (9,416'ND) ,•� TD=9,931' MD(9,467 TVD) Revised By TDF 12/7/2012 Bruce Platform PROPOSED Well No. BR 30-42 Hilcorp Alaska,LLC Completion: Future API#50-733-20322-00 RKB to TBG Head=42.2' CASING DETAIL Size WT Grade Conn ID Top Btm 20" 94# - 19.124" Surface 596' 13-3/8" 54.5,61, K-55,N-80 Buttress 12.347" Surface 4,516' 68&72 &S-80 9-5/8" 40&47 N 895 S Buttress 8.681" Surface 9,927' 7-5/8" - EX80 - 7.712" 8,500 9,850' 4 J Jewelry MD ND Description OD ID - - Hanger - _ - 8,490' 8,080' Sliding Sleeve - - 8,426' 8,100' ESP - G PERFORATION DETAIL Top Btm Top Btm Zone (MD) (MD) (ND) (TVD) Amt spf Comments Date 2-1/8"Slimkone C-2 8,524' 8,562' 8,192' 8,223' 38' 4 Hollow Carrier 2/4/1979 C-3 8,638' 8,730' 8,285' _ 8,359' 92' 8 2-1/8"Silver Jet 4/14/1994 C-5 8,916' 8,984' 8,511' 8,569' 68' 8 2-1/8"Silver Jet 4/14/1994 . ;„_ C-6 8,994' 9,014' 8,578' 8,596' 20' 8 2-1/8"Silver Jet 4/14/1994 C 6 9,210' 9,222' 8,772' 8,784' 12' 4 2-1/8"Silver Jet 4/14/1994 C-7 9,317' 9,341' 8,872' 8,895' 24' 8 2-1/8"Silver Jet 4/14/1994 / C-7 9,380' 9,406' 8,932' 8,956' 26' 8 2-1/8"Silver Jet 4/14/1994 C-7 9,470' 9,508' 9,018' 9,054' 38' 8 2-1/8"Silver Jet 4/14/1994 Exp Liner C-7 9,518' 9,552' 9,064' 9,097' 34' 8 2-1/8"Silver Jet 4/14/1994 ±9,150'-±9,850' C-7 9,500' 9,550' 9,046' 9,094' 48' 15 4-1/2" TBD C-7 9,590' 9,600' 9,133' 9,143' 10' 8 2-1/8"Silver Jet 4/14/1994 C-7 9,604' 9,610' 9,147' 9,153' 6' 8 2-1/8"Silver Jet 4/14/1994 C-8 9,684' 9,716' 9,225' 9,256' 32' 8 2-1/8"Silver Jet _ 4/14/1994 C-8 9,700' 9,780' 9,240' 9,319 79' 15 4-1/2" TBD 2-1/8"Slimkone C-8 9,758' 9,820' 9,297' 9,358' 62' 4 Hollow Carrier 2/2/1979 i PBTD=9,880' MD (9,416'ND) TD=9,931' MD(9,467'ND) Updated by: DT 04/04/14 Bruce Platform II BR-18742-30 04/04/2014 BR 18742-30 Tubing hanger,Dual,CIW-DCB, 20X133/8X95/8X 11X3''/2EUEliftX3'BTCsusp, 3'/2 X 2 7/8 w/3"type H BPV profile,5 3/64 centers Valve,Master,CIW-F, 3 1/8 5M 5 bolt,FE,HWO Qty 2 •iii.0 1 pli� ' O M; 'a4 Adapter,CIW-dual,11 5M stdd X Q0�r 3 1/8 5M 5 bolt top,prepped f/3" inom CIW hanger necks Tubing head,CIW-DCB, } ' 5 3/64 centers 135/83MX115M,w/2- p, , 2 1/16 5M SSO,X-bottom 21111 I 4E. prep 111 111 Valve,CIW-F,2 1/16 5M FE, A' 1 1 - HWO-®- ' ' � C> A, Qty /', orII j , it I■ oo -1- i11 , 111 I Casing spool,CIW-WF,21''A 2M X 13 5/8 3M,w/2-2 1/16 5MIn EFO,X bottom prep III 1 Ill Valve,CIW-F,2 1/16 5M FE, O HWO � '` tN .- Casing head,CIW-WF,21'''4 2M X SOW,w/2-2 1/16 2M EFOValve,CIW F,2 1/16 2M FE, I n 11 HWO ,h1 101-1. 1 : t _, _ .I� Bruce Platform BR-18742-30 Proposed 04/04/2014 Har irp Alltaia,1.1A, BR 18742-30 Tubing hanger,CIW-DCB-ESP, 20X133/8X95/8X 11 X 31A EUE lift and susp,w/ 2 7/8 3"type H BPV profile,5'/.EN, 2-3/8 continuous control line ports,prepped for BIW penetrator BHTA,Bowen,31/8 5M FE X 3"Bowen union nu Valve,swab,WKM-M, '•' 3 1/8 5M FE,HWO, ®o, T-24 /O 0®,A'. Valve,WKM-M,3 1/8 5M FE,w/ ,.,011.111111 . MA-16 operator Valve,wing,WKM M, = , 2 1/16 5M FE,HWO, it (:. )4lj III ' ° I T-24 Aim"ra. p7� Valve,lower master,WKM-M, 3 1/8 5M FE,HWO,T-24 in •Wav,1.1 1BI Adapter,CIW-Toadstool,11 5M 1i' Stdd X 3 1/8 5M FE,prepped for ' 5'''A ESP neck,2-%npt continuous ( ` control line ports Tubing head,CIW-DCB, l iir 13 5/8 3M X 11 5M,w/2- _ 2 1/16 5M SSO,X-bottom Lir prep UPIfti 1J Valve,CIW-F,21/16 5M -k II ' ■ I � i � opi-IF/ FE,HWO,AA, ' M � Qty 2 III I Casing spool,CIW-WF,21''/<2M '� X 13 5/8 3M,w/2-2 1/16 5M til 111 Valve,ClW-F,21/165MFE, EFO,X bottom prep i - = AlHWO 1111 .1111110111(1e41)111.1-I—; 011 . III . I f i - - a Casing head,CIW-WF,21''A 2M X ir SOW,w/2-2 1/16 2M EFO Valve,CIW-F,2 1/16 2M FE, nr ' HWO 11 Bruce Platform BOP Stack Moncla 03/10/2014 nitraxp Aiht•kr,r.iA; 1.,tit 111 t!1 lel 4.54' Hyddl GK 13;/8.6000 U1 iii lii III lis I!I 111 111 111 911 CIW-u.:... - 2 3/8-3 h Dual Flex rams 4 67 w --mum lir 13 5/8-5000 -- Blind a '1I lil i11,�}, 1T Ill In Ill III ! 1 ' 2 00 l 3 31/8 SM Choke and Kill " ° Ut4 tt valves 111 I11 Ill Ilt III - - 111 111111111 111 yw. 2.83' "-- 23/8-314 Cameron Flex rams Iii 115 111 1/!II I Mir .83' t(I ill 11111 Drill deck 10.00' 1 1 Ai .1 1 1 1 1 i l l ;1;I t l :t I 1 1 2.83' i lit Ili IlsiGlll k-11-0-73 Wallace, Chris D (DOA) From: Daniel Taylor [dtaylor@hilcorp.com] Sent: Monday, April 14, 2014 12:14 PM To: Wallace, Chris D (DOA) Cc: Ferguson, Victoria L (DOA) Subject: RE: GP State (Bruce) 18742 30 PTD 1780730 Sundry 314-219 Chris, I apologize for taking a bit to get back to you sir. The frac fluid is weathered crude oil coming directly from Granite Point field and is not associated in any way with the below listed CAS numbers. The StimPlan model has generated a maximum anticipated surface treating pressure for both the C-8 and C-7 sands. The C-8 MSTP is 7,121psi and the C-7 is 6,763 (pg 52 & 65 of Sundry application). I apologize for what I see as a typo. The—8,000psi was generated from rounding up. The pop off was stated to be set at 10,500psi because of the complications associated with popping off prior to the flush. If it is observed that we are climbing over the previously modeled STP then we will need to re-evaluate our frac procedure, stage design, and contact AOGCC. For the same reason all surface connections are rated to 15kpsi. The IA pop off valve will be set at 2,500psi. Thank you sir. Regards, Dan Taylor Operations Engineer Hilcorp Alaska, LLC. O: 907-777-8319 C: 907-947-8051 From: Wallace, Chris D (DOA)[ma iIto: chris.wallace@alaska.gov] Sent: Wednesday, April 09, 2014 2:29 PM To: Daniel Taylor Cc: Ferguson, Victoria L (DOA) Subject: GP State (Bruce) 18742 30 PTD 1780730 Sundry 314-219 Da n, We are processing the Sundry application for hydraulic fracturing and I have a few questions for your clarification. 1. The frac fluid appears to state weathered oil but no MSDS is received for the fluid. Please clarify that this is not diesel and does not contain Chemical Abstract Numbers (CASRNs) 68334-30-5, 68476-34-6, 68476-30-2, 68476-31-3, 8008-20-6, or 68410-00-4, and is not referred to as "diesel fuel" in its primary name or common synonyms. 2. Section A)14.e) shows an anticipated maximum treating pressure of 8000 psi (surface pressure). Section D) calls for a pressure relief valve that must be installed on surface lines to limit pressure to (a)14 (E). The frac simulation provided has a maximum surface pressure stated of 6763 psi. Whereas in the provided procedure at 7. f. it states the max surface treating pressure of 7,615 and at procedure 7. g. and 15. g. the surface line nitrogen pop off is to be set at 10,500 psi? Please clarify why the pop off is not set at the 8000 psi level or lower? 3. At procedure 7. d. iii. and 15. d. iii. It states you are to set inner annulus pop off valve — what is the set point on this? From previous emails on other wells I have a statement from Reid Edwards relating to using platform crude oil that I copy here for our well records "The use of lease oil as a base fluid for hydraulic fracture treatment in the oil bearing Tyonek interval in well Granite Point 18742 24RD is based on reservoir impairment concerns. The introduction of water to this reservoir has been shown through both production and core data to drastically decrease its permeability. This phenomenon is due to extreme water wetness of the rock and has been shown to reduce permeability by a factor 10. Previous fracture stimulations completed in this reservoir used water based fluids and showed no increase in production. It is expected that the water based fluid used for fracturing caused damage during the treatment. The use of an oil based fluid is expected to yield positive results as the oil is both native to the reservoir and is a non -damaging fluid based on relative permeability tests." Thanks and Regards, Chris Wallace Sr. Petroleum Engineer Alaska Oil and Gas Conservation Commission 333 West 7 t Avenue Anchorage, AK 99501 (907) 793-1250 (phone) (907) 276-7542 (fax) chris.wallace@alaska.gov CARBO CARBOBONDTM LITE,EP&HP,all sizes MSDS NO.21 CERAMICS REVISION DATE:01 May 2010 MATERIAL SAFETY DATA SHEET Page 1 of 1. PRODUCT AND COMPANY IDENTIFICATION TRADE NAME: CARBOBONDTM LITE, CARBOBONDTM EP&CARBOBONDTM HP, all sizes SYNONYM(S): Resin-coated ceramic proppant;semi-crystalline aluminosilicate CHEMICAL FAMILY: Aluminosilicate MANUFACTURER: CARBO Ceramics, Inc. 4810 Industrial Drive New Iberia, Louisiana 70560 Phone: 1-337-367-6151 EMERGENCY PHONE: 1-800-551-3247(U.S.A.) 2. COMPOSITION/INFORMATION ON INGREDIENTS INGREDIENTS CAS NUMBER CONCENTRATION CLASSIFICATION R-PHRASES Silicon Dioxide,amorphous as glass 7631-86-9 5-35% Not classified Not assigned Mullite 1302-93-8 60-85% Not classified Not assigned Silica Crystalline-Cristobalite 14464-46-1 0-20% Not classified R-45 Phenol Formaldehyde Resin 9003-35-4 0-5% Not classified R-36/38 R-43 Note—Analytical results do not indicate concentrations of free formaldehyde or phenol above 0.0001%. 3. HEALTH HAZARD INFORMATION INHALATION: Inhalation of dusts may cause respiratory tract irritation. Repeated or prolonged breathing of particles of respirable size may cause severe respiratory disease. However,this product contains few particles of respirable size. Repeated industrial hygiene monitoring and testing conducted throughout the production and shipping process at CARBO Ceramics, Inc.shows that the final product produces levels of respirable silica(in the form of crystalline crystobalite)below laboratory detection limits and applicable exposure limits(see section 8). The amount of dust due to breakdown during shipment and intended use and handling is not expected to exceed applicable exposure limits(see section 8). Analyses for crystalline forms of silica at CARBO Ceramics, Inc.facilities were performed by X-ray diffraction based upon OSHA ID 142 guidelines. Formaldehyde gas is possible if heated but elevated concentrations are not anticipated during normal use. EYE CONTACT: Airborne dust may cause irritation to eyes. SKIN CONTACT: Prolonged contact with a skin may cause irritation or sensitization. HMIS RATING: HEALTH 1 (slight) FLAMMABILITY 1 (slight) REACTIVITY 0(minimal) SPECIAL PROTECTION: See section 8. 4. FIRST AID MEASURES INHALATION: Remove affected person from source of exposure. Get medical attention if irritation occurs. INGESTION: Seek medical attention if large quantities are ingested. EYE CONTACT: Immediately flush eyes with large amounts of water, lifting the lower and upper lids occasionally. If irritation is present after washing,get medical attention. SKIN CONTACT: Wash the affected area with soap and water. Get medical attention if irritation occurs. 5. FIRE-FIGHTING MEASURES ESTIMATED EXPLOSIVE LIMITS(%by volume in air): LEL:N/A UEL: N/A FLASH POINT: N/A SPECIAL FIRE FIGHTING PROCEDURES: This material does not give a flash point by conventional test methods. Use extinguishing agent suitable for type of surrounding fire. UNUSUAL HAZARDS: Avoid generating dust,fine dust dispersed in the air in sufficient concentrations,and in the presence of an ignition source is a potential explosion hazard. 6. SPILL OR LEAK PROCEDURES STEPS TO BE TAKEN IN CASE MATERIAL IS RELEASED OR SPILLED: No special procedures are required for clean-up of spills or leaks of this material. Caution should be exercised regarding personal safety and exposure to the spilled material,the material's nature could cause reduced traction. Persons should take care so as not to slip. CARBO CARBOBONDTM LITE,EP&HP,all sizes MSDS NO.21 CERAMICS REVISION DATE:01 May 2010 MATERIAL SAFETY DATA SHEET Page2of3 7. HANDLING AND STORAGE HANDLING: Minimize dust generation and accumulation. Use personal protective equipment. Refer to section 8 for suggested personal protective equipment. Pneumatic transports should be discharged at the minimum pressure to ensure a steady stream of flow into the receiving storage bin. The discharge pressure will be no greater than 5-8 psi for standard field delivery. Following this instruction will minimize the generation of potentially explosive resin dust and maintain the performance of the product. Take precautionary measures,such as capturing dust at generation points,practicing good housekeeping, controlling sources of ignition(including static electricity),and grounding equipment,to minimize dust accumulation, airborne dust,and static discharge during mechanical handling,transfer and/or conveyance. STORAGE: Store dry in a cool dry place to prevent blocking in sacks or bulk bags. Keep away from heat and open flames. Do Not store in direct sunlight as ultraviolet radiation will deteriorate the performance of the product. 8. EXPOSURE CONTROLS/PROTECTION DURING USE EXPOSURE LIMITS: INGREDIENTS OSHA PEL-TWA ACGIH-TWA TLV Silicon Dioxide, 80 mg/m3/%Si02(total) - amorphous,as glass Mullite 15 mg/m3(total) 10 mg/m3(total) 5 mg/m3(respirable) 3 mg/m3(respirable) Silica, Crystalline, 15 mg/m3/(%Si02+2)(total) 0.025 mg/m3(respirable) Cristobalite 5 mg/m3/(%Si02+2)(respirable) ENGINEERING CONTROL Exposure to this material may be controlled in a number of ways. The measures appropriate for MEASURES: a particular worksite depend on how the material is used and the potential for exposure. Use of the basic principles of industrial hygiene will enable safe handling of the material. RESPIRATORY: An applicable NIOSH approved respirator should be worn where airborne exposures may exceed OSHA/ACGIH permissible air concentrations. EYE PROTECTION: Wear safety glasses or chemical goggles to prevent eye contact. Do not wear contact lenses when working with this substance unless protected under full coverage goggles. CLOTHING/GLOVES: Gloves are optional to reduce abrasion or sensitization. WORK HYGIENE PRACTICES: Handle in accordance with good personal hygiene and safety practices. VENTILATION: Ensure that dust-handling systems(such as ducts,dust collectors,vessels and processing equipment)are designed in a manner to prevent the escape of dust into the work area,i.e.,there is no leakage from the equipment. 9. PHYSICAL AND CHEMICAL PROPERTIES BOILING POINT: N/A °F SPECIFIC GRAVITY: 2.66 (H20=1) pH: N/A MELTING POINT: 4000°F (estimated) BULK DENSITY: 98 pound/foot3 ODOR:mild VAPOR PRESSURE: N/A mm Hg VOLATILE%by weight: N/A VAPOR DENSITY: N/A (Air=1) EVAPORATION RATE: N/A(butyl acetate=1) APPEARANCE: pale green to pale yellow spheres SOLUBILITY in water: Insoluble VOLATILE ORGANIC COMPOUNDS(VOC): 0 pound/gallon(EPA Reference Methods 24) COMBUSTIBILITY: Combustibility data not available. Not considered a significant combustible dust hazard during normally anticipated use conditions due to low organic content. 10. STABILITY AND REACTIVITY REACTIVITY: Minimal STABILITY: Stable INCOMPATIBLE MATERIALS: Chlorine triflouride and strong oxidizers DECOMPOSITION PRODUCTS: Decomposition products may include carbon monoxide,carbon dioxide,oxides of nitrogen, ammonia,aldehydes, or other materials. 11. TOXICOLOGICAL INFORMATION ACUTE EFFECTS: Coughing and throat irritation are early symptoms of excessive exposure. May be irritating to the respiratory system, lungs and skin. May also cause irritation to eyes. May cause sensitization of skin. CARBO CARBOBONDTM LITE, EP&HP,at sizes MSDS NO:21 CERAMICS REVISION DATE:01 May 2010 MATERIAL SAFETY DATA SHEET Page3of3 Inhalation of formaldehyde in excess of established human exposure limits is known to cause human CHRONIC EFFECTS: cancer. Chronic exposure in excess of established human exposure can cause severe respiratory disease. 12. ECOLOGICAL INFORMATION This product poses no significant environmental contamination impact during expected use, handling,and proper disposal. 13. DISPOSAL CONSIDERATIONS WASTE DISPOSAL: Disposal must be at an approved waste disposal facility and in accordance with applicable Federal, State and Local laws and regulations. Contact the district Director of the Environmental Protection Agency and/or state regulatory agency for appropriate requirements. 14. TRANSPORTATION INFORMATION UN NO. N/A ICAO/IATA Not restricted RID/ADR Not restricted DOT SHIPPING DESCRIPTION Not restricted CAN Not restricted IMO Not restricted 15. REGULATORY INFORMATION TOXIC SUBSTANCE CONTROL ACT(TSCA)STATUS:All chemicals in this SARA Section 302: None product are listed, automatically included, or are exempt from listing on the TSCA TITLE III: Section 312: None Inventory. Section 313: None CERCLA REPORTABLE QUANTITY: NA CLEAN AIR AMENDMENTS-HAZARDOUS AIR POLLUTANTS(HAPS): None CALIFORNIA STATE PROPOSITION 65: Silica,crystalline,airborne particles of respirable size 16. OTHER INFORMATION This material safety data sheet is provided as an information resource only. CARBO Ceramics believes the information contained herein is accurate and compiled from reliable sources. It is the responsibility of the user to verify its validity. The buyer assumes all responsibility of using and handling the product in accordance with federal,state and local regulations. Refer to NFPA 654, Standard for the Prevention of Fire and Dust Explosions from the Manufacturing, Processing and Handling of Combustible Particulate Solids,for safe handling. r/'- Material Safety Data Sheet BAKER HUGHES 1 . Product and company identification Product name : GBO-5L Supplier : Baker Hughes, Inc. 12645 W. Airport Blvd. Sugar Land, TX 77478 For Product Information/MSDSs Call: 281-351-8131 Material Uses : Special: Gel Breaker Code : 398195 Validation date : 6/17/2013. Print date : 6/17/2013. Version : 1 Responsible name : Global Regulatory Affairs -Telephone 281-276-5400 or 800-231-3606 In case of emergency : CHEMTREC 800-424-9300 (U.S. 24 hour) (001)281-276-5400 CANUTEC 613-996-6666 (Canada 24 hours)CHEMTREC Intl 01-703-527- 3887 (International 24 hour) 2 . Hazards identification Physical state : Liquid. [Suspension] Odor : Hydrocarbon. Color : Pink to Light tan. OSHA/HCS status : While this material is not considered hazardous by the OSHA Hazard Communication Standard (29 CFR 1910.1200),this MSDS contains valuable information critical to the safe handling and proper use of the product. This MSDS should be retained and available for employees and other users of this product. Emergency overview : MAY CAUSE RESPIRATORY TRACT, EYE AND SKIN IRRITATION. Avoid breathing vapor or mist. Avoid contact with eyes. Avoid prolonged or repeated contact with skin. Use only with adequate ventilation. Keep container tightly closed and sealed until ready for use. Wash thoroughly after handling. Routes of entry : Dermal contact. Inhalation. Potential acute health effects Inhalation : Slightly irritating to the respiratory system. Ingestion : Ingestion may cause gastrointestinal irritation and diarrhea. Skin : Slightly irritating to the skin. Eyes : Slightly irritating to the eyes. Potential chronic health effects Target organs : Contains material which may cause damage to the following organs: lungs, upper respiratory tract, skin, eyes. Over-exposure signs/symptoms Inhalation : respiratory tract irritation, coughing Ingestion : None known. Skin : irritation, redness Eyes : irritation, watering, redness See toxicological information (Section 11) 6/17/2013. 398195 1/7 LBO-5L 3 . Composition/information on ingredients Name CAS number Magnesium oxide 1309-48-4 60- 100 Petroleum distillates 64742-47-8 10-30 Paraffinic petroleum distillate 64742-55-8 10-30 White mineral oil 8042-47-5 10-30 4 . First aid measures Eye contact : Get medical attention immediately. Immediately flush eyes with plenty of water for at least 15 minutes, occasionally lifting the upper and lower eyelids. Skin contact : In case of contact, immediately flush skin with plenty of water for at least 15 minutes while removing contaminated clothing and shoes. Wash clothing before reuse. Clean shoes thoroughly before reuse. Get medical attention immediately. Inhalation : Move exposed person to fresh air. If not breathing, if breathing is irregular or if respiratory arrest occurs, provide artificial respiration or oxygen by trained personnel. Loosen tight clothing such as a collar, tie, belt or waistband. Get medical attention immediately. Ingestion : Wash out mouth with water. Do not induce vomiting unless directed to do so by medical personnel. Never give anything by mouth to an unconscious person. Get medical attention immediately. Protection of first-aiders : No action shall be taken involving any personal risk or without suitable training. It may be dangerous to the person providing aid to give mouth-to-mouth resuscitation. 5 . Fire-fighting measures Flammability of the product : In a fire or if heated, a pressure increase will occur and the container may burst. Extinguishing media Suitable : Use an extinguishing agent suitable for the surrounding fire. Not suitable : None known. Special exposure hazards : Promptly isolate the scene by removing all persons from the vicinity of the incident if there is a fire. No action shall be taken involving any personal risk or without suitable training. Hazardous thermal : carbon dioxide,carbon monoxide,metal oxide/oxides decomposition products Special protective : Fire-fighters should wear appropriate protective equipment and self-contained breathing equipment for fire-fighters apparatus (SCBA) with a full face-piece operated in positive pressure mode. 6 . Accidental release measures Personal precautions : No action shall be taken involving any personal risk or without suitable training. Evacuate surrounding areas. Keep unnecessary and unprotected personnel from entering. Do not touch or walk through spilled material. Avoid breathing vapor or mist. Provide adequate ventilation. Wear appropriate respirator when ventilation is inadequate. Put on appropriate personal protective equipment (see Section 8). Environmental precautions : Avoid dispersal of spilled material and runoff and contact with soil, waterways, drains and sewers. Methods for cleaning up Small spill : Stop leak if without risk. Move containers from spill area. Absorb with an inert material. Dispose of via a licensed waste disposal contractor. Large spill : Stop leak if without risk. Move containers from spill area. Approach release from upwind. Dike spill area and do not allow product to reach sewage system or surface or ground water. Notify any reportable spill to authorities. (See section 12 for environmental risks and 13 for disposal information.) Contain and collect spillage with non- combustible, absorbent material e.g. sand, earth, vermiculite or diatomaceous earth and place in container for disposal according to local regulations (see section 13). Dispose of via a licensed waste disposal contractor. Contaminated absorbent material may pose the same hazard as the spilled product. Note:see section 1 for emergency contact information and section 13 for waste disposal. 6/17/2013. 398195 2/7 GBO-5L 6 . Accidental release measures If RQ(Reportable Quantity) is exceeded, report to National Spill Response Office at 1-800-424-8802. 7 . Handling and storage Handling : Put on appropriate personal protective equipment(see Section 8). Eating, drinking and smoking should be prohibited in areas where this material is handled, stored and processed. Workers should wash hands and face before eating, drinking and smoking. Do not ingest. Avoid contact with eyes, skin and clothing. Avoid breathing vapor or mist. Use only with adequate ventilation. Empty containers retain product residue and can be hazardous. Do not reuse container. Storage : Store in accordance with local regulations. Store in a dry, cool and well-ventilated area, away from incompatible materials (see Section 10). Keep container tightly closed and sealed until ready for use. Containers that have been opened must be carefully resealed and kept upright to prevent leakage. Do not store in unlabeled containers. Use appropriate containment to avoid environmental contamination. 8 . Exposure controls/personal protection Occupational exposure limits TWA(8 hours) STEL(15 mins) Ceiling Ingredients: List name ppm mg/m3 Other ppm mg/m3 Other ppm mg/m3 Other Notations White mineral oil US ACGIH - 5 - - - - - - - [a] OSHA PEL - 5 - - - - - - - Paraffinic petroleum distillate US ACGIH - 5 - - - - - - - [a] OSHA PEL - 5 - - - - - - - Petroleum distillates US ACGIH - 200 - - - - - - [1] Magnesium oxide US ACGIH - 10 - - - - - - - [a] OSHA PEL - 15 - - - - - - - [b] OSHA PEL 1989 - 10 - - - - - - - [b] [1]Absorbed through skin. Form: [a]Inhalable fraction [b]Total particulates Consult local authorities for acceptable exposure'limits. Only components of this product with established exposure limits appear in the box above. If OSHA permissible exposure levels are shown above they are the OSHA 1989 levels or are from subsequent OSHA regulatory actions.Although the 1989 levels have been vacated the 11th Circuit Court of Appeals, Baker Hughes recommends that these lower exposure levels be observed as reasonable worker protection. Recommended monitoring : If this product contains ingredients with exposure limits, personal,workplace atmosphere procedures or biological monitoring may be required to determine the effectiveness of the ventilation or other control measures and/or the necessity to use respiratory protective equipment. Engineering measures : Use only with adequate ventilation. If user operations generate dust, fumes, gas, vapor or mist, use process enclosures, local exhaust ventilation or other engineering controls to keep worker exposure to airborne contaminants below any recommended or statutory limits. Hygiene measures : Wash hands, forearms and face thoroughly after handling chemical products, before eating, smoking and using the lavatory and at the end of the working period. Ensure that eyewash stations and safety showers are close to the workstation location. Take off contaminated clothing and wash before reuse. Personal protection Respiratory : If a risk assessment indicates it is necessary, use a properly fitted, air purifying or supplied air respirator complying with an approved standard. Respirator selection must be based on known or anticipated exposure levels,the hazards of the product and the safe working limits of the selected respirator. Hands : Chemical-resistant gloves. Eyes : Wear chemical safety goggles. When transferring material wear face-shield in addition to chemical safety goggles. Skin : Wear long sleeves and other protective clothing to prevent repeated or prolonged skin contact. 6/17/2013. 398195 3/7 GBO-5L 9 . Physical and chemical properties Physical state : Liquid. [Suspension] Flash point : Closed cup: 100°C (212°F) Auto-ignition temperature : Not available. Flammable limits : Not available. Color : Pink to Light tan. Odor : Hydrocarbon. pH : Not available. Boiling/condensation point : Not available. Initial Boiling Point : Not available. Melting/freezing point : Not available. Relative density : 1.776 (23.88°C) Density : 14.81 (lbs/gal) Vapor density : Not available. Odor threshold : Not available. Evaporation rate : Not available. VOC : Not available. Viscosity : Dynamic: <100 cP Solubility(Water) : Slight Vapor pressure : 0 kPa(0 mm Hg) Pour Point : Not available. Partition coefficient : Not available. (LogKow) 10 . Stability and Reactivity Chemical stability : The product is stable. Possibility of, lazardous : Under normal conditions of storage and use .hazardous reactions will not occur. reactions ` Hazardous polymerization : Under normal conditions of storage and use, hazardous polymerization will not occur. Conditions to avoid : No specific data. Materials to avoid : Reactive or incompatible with the following materials:acids and moisture. Chlorine , Phosphorus pentachloride , Trifluoride Hazardous decomposition : Under normal conditions of storage and use, hazardous decomposition products should products not be produced. Conditions of reactivity : Slightly flammable in the presence of the following materials or conditions:open flames, sparks and static discharge and heat. 11 . Toxicological information Acute toxicity Product/ingredient name Result Species Dose Exposure White mineral oil LD50 Oral Rat >5000 mg/kg Paraffinic petroleum distillate LC50 Inhalation Rat 3900 mg/m3 4 hours Vapor Carcinogenicity Classification Product/ingredient name ACGIH IARC EPA NIOSH NTP OSHA Magnesium oxide A4 - - Paraffinic petroleum distillate A4 - - White mineral oil A4 - - Chronic toxicity Remarks 6/17/2013. 398195 4/7 GBO-5L 11 . Toxicological information 1) Magnesium oxide Not available. 2) Petroleum distillates Not available. 3) Paraffinic petroleum distillate Not available. 4) White mineral oil Not available. 12 . Ecological information Aquatic ecotoxicitv Product/ingredient name Result Species Exposure Petroleum distillates Acute LC50 2200 ug/L Fresh Fish - Bluegill - Lepomis 4 days water macrochirus-35 to 75 mm Conclusion/Summary : Not available. Biodegradability Conclusion/Summary : Not available. 13. Disposal considerations Waste disposal : The generation of waste should be avoided or minimized wherever possible. Empty containers or liners may retain some product residues. This material and its container i must be disposed of in a safe way. Dispose of surplus and non-recyclable products via a licensed waste disposal contractor. Disposal of this product, solutions and any by- products should at all times comply with the requirements of environmental protection and waste disposal legislation and any regional local authority requirements. Avoid • dispersal of spilled material and runoff and contact with soil, waterways, drains and sewers. Disposal should be in accordance with applicable regional, national and local laws and regulations. Refer to Section 7: HANDLING AND STORAGE and Section 8: EXPOSURE CONTROLS/PERSONAL PROTECTION for additional handling information and protection of employees. 14 . Transport information Regulatory UN number Proper shipping Classes PG* Label Additional information name information DOT Classification Not - - - - regulated. TDG Classification Not - - - - regulated. IMDG Class Not - - - - regulated. IATA-DGR Class Not - - - - regulated. PG" : Packing group DOT Reportable Not applicable. Quantity 6/17/2013. 398195 5/7 GBO-5L 14 . Transport information Marine pollutant Not applicable. North-America NAERG : Not available. 15 . Regulatory information HCS Classification : Not regulated. U.S. Federal regulations : United States inventory(TSCA 8b): All components are listed or exempted. SARA 302/304/311/312 extremely hazardous substances: No products were found. SARA 302/304 emergency planning and notification: No products were found. SARA 302/304/311/312 hazardous chemicals: magnesium oxide; Distillates (petroleum), hydrotreated light SARA 311/312 MSDS distribution - chemical inventory- hazard identification: GBO-5L: Immediate (acute) health hazard CERCLA: Hazardous substances.: Methanol: 5000 lbs. (2270 kg); Clean Water Act(CWA)307: No products were found. Clean Water Act(CWA) 311: No products were found. Clean Air Act (CAA) 112 regulated flammable substances: No products were found. Clean Air Act (CAA) 112 regulated toxic substances: No products were found. Clean Air Act Section 112(b) Hazardous Air Pollutants(HAPs) : Not listed United States inventory : All components are listed or exempted. (TSCA 8b) Canada WHMIS(Canada) : Class D-2A: Material causing other toxic effects (Very toxic). Canada(CEPA DSL): : All components are listed or exempted. 16 . Other information Label requirements : MAY CAUSE RESPIRATORY TRACT, EYE AND SKIN IRRITATION. Hazardous Material Information System (U.S.A.) Faith 1 Flammability 1 Physical hazards 0 Personal protection b Caution: HMIS®ratings are based on a 0-4 rating scale, with 0 representing minimal hazards or risks,and 4 representing significant hazards or risks Although HMIS®ratings are not required on MSDSs under 29 CFR 1910.1200, the preparer may choose to provide them. HMIS®ratings are to be used with a fully implemented HMIS®program. HMIS®is a registered mark of the National Paint & Coatings Association (NPCA). HMIS® materials may be purchased exclusively from J. J. Keller(800) 327-6868. The customer is responsible for determining the PPE code for this material. National Fire Protection Association (U.S.A.) Flammability Health 0 Instability Special Date of printing : 6/17/2013. V Indicates information that has changed from previously issued version. Notice to reader 6/17/2013. 398195 6/7 GBO-5L 16 . Other information NOTE: The information on this MSDS is based on data which is considered to be accurate. Baker Hughes, however, makes no guarantees or warranty, either expressed or implied of the accuracy or completeness of this information. The conditions or methods of handling, storage, use and disposal of the product are beyond our control and may be beyond our knowledge. For this and other reasons,we do not assume responsibility and expressly disclaim liability for loss, damage or expense arising out of or in any way connected with the handling, storage, use or disposal of this product. This MSDS was prepared and is to be used for this product. If the product is used as a component in another product,this MSDS information may not be applicable. 6/17/2013. 398195 7/7 F1"- Material Safety Data Sheet BAKER HUGHES 1 . Product and company identification Product name : GO-64 Supplier : Baker Hughes, Inc. 12645 W. Airport Blvd. Sugar Land, TX 77478 For Product Information/MSDSs Call: 281-351-8131 Material Uses : Special: Oil gelling agent Code : 488159 Validation date : 1/27/2012. Print date : 1/27/2012. Version : 1 Responsible name : Global Regulatory Affairs -Telephone 281-276-5400 or 800-231-3606 In case of emergency : CHEMTREC 800-424-9300 (U.S. 24 hour) (001)281-276-5400 CANUTEC 613-996-6666 (Canada 24 hours)CHEMTREC Int'l 01-703-527- 3887 (International 24 hour) . Hazards identification Physical state : Liquid. Odor : Musty. [Slight] Color : Water-white./Light yellow OSHA/HCS status : This material is considered hazardous by the OSHA Hazard Communication Standard (29 CFR 1910.1200). Emergency overview : DANGER! CAUSES EYE AND SKIN BURNS. MAY CAUSE ALLERGIC SKIN REACTION. Do not breathe vapor or mist. Do not get in eyes or on skin or clothing. Use only with adequate ventilation. Keep container tightly closed and sealed until ready for use. Wash thoroughly after handling. Routes of entry : Dermal contact. Eye contact. Ingestion. Potential acute health effects Inhalation : May give off gas, vapor or dust that is very irritating or corrosive to the respiratory system. Ingestion : May cause burns to mouth, throat and stomach. Skin : Corrosive to the skin. Causes burns. May cause sensitization by skin contact. Eyes : Corrosive to eyes. Causes burns. Potential chronic health effects Chronic effects : Once sensitized, a severe allergic reaction may occur when subsequently exposed to very low levels. Over-exposure signs/svmptoms Inhalation : None known. Ingestion : stomach pains Skin : pain or irritation, redness, blistering may occur Eyes : pain,watering, redness Medical conditions : Pre-existing skin disorders may be aggravated by over-exposure to this product. aggravated by over- exposure See toxicological information (Section 11) 1/27/2012. 488159 1/6 GO-64 3 . Composition/information on ingredients Name CAS number Phosphate ester Trade secret. 60 - 100 4 . First aid measures Eye contact : Get medical attention immediately. Immediately flush the eye(s) continuously with lukewarm, gently flowing water for at least 20-60 minutes while holding the eyelid(s) open. Skin contact : Wash affected area with soap and mild detergent for at least 20 - 60 minutes. Wash clothing before reuse. Clean shoes thoroughly before reuse. Get medical attention immediately. Inhalation : Move exposed person to fresh air. If not breathing, if breathing is irregular or if respiratory arrest occurs, provide artificial respiration or oxygen by trained personnel. Loosen tight clothing such as a collar, tie, belt or waistband. Get medical attention immediately. Ingestion : Wash out mouth with water. Do not induce vomiting unless directed to do so by medical personnel. Never give anything by mouth to an unconscious person. Get medical attention immediately. Protection of first-aiders : No action shall be taken involving any personal risk or without suitable training. If it is suspected that fumes are still present, the rescuer should wear an appropriate mask or self-contained breathing apparatus. It may be dangerous to the person providing aid to give mouth-to-mouth resuscitation. Wear suitable protective clothing and gloves. Remove contaminated clothing and shoes. 5 . Fire-fighting measures Flammability of the product : In a fire or if heated, a pressure increase will occur and the container may burst. Extinguishing media Suitable : Use an extinguishing agent suitable for the surrounding fire. Not suitable : None known. Special exposure hazards : Promptly isolate the scene by removing all persons from the vicinity of the incident if there is a fire. No action shall be taken involving any personal risk or without suitable training. Hazardous thermal : carbon dioxide,carbon monoxide,phosphorus oxides decomposition products Special protective : Fire-fighters should wear appropriate protective equipment and self-contained breathing equipment for fire-fighters apparatus (SCBA)with a full face-piece operated in positive pressure mode. 6 . Accidental release measures Personal precautions : No action shall be taken involving any personal risk or without suitable training. Evacuate surrounding areas. Keep unnecessary and unprotected personnel from entering. Do not touch or walk through spilled material. Do not breathe vapor or mist. Provide adequate ventilation. Wear appropriate respirator when ventilation is inadequate. Put on appropriate personal protective equipment(see Section 8). Environmental precautions : Avoid dispersal of spilled material and runoff and contact with soil,waterways, drains and sewers. Methods for cleaning up Small spill : Stop leak if without risk. Move containers from spill area. Absorb with an inert material. Dispose of via a licensed waste disposal contractor. Large spill : Stop leak if without risk. Move containers from spill area. Approach release from upwind. Dike spill area and do not allow product to reach sewage system or surface or ground water. Notify any reportable spill to authorities. (See section 12 for environmental risks and 13 for disposal information.) Contain and collect spillage with non- combustible, absorbent material e.g. sand, earth, vermiculite or diatomaceous earth and place in container for disposal according to local regulations (see section 13). Dispose of via a licensed waste disposal contractor. Contaminated absorbent material may pose 1/27/2012. 488159 2/6 GO-64 6 . Accidental release measures the same hazard as the spilled product. Note:see section 1 for emergency contact information and section 13 for waste disposal. 7 . Handling and storage Handling : Put on appropriate personal protective equipment (see Section 8). Eating, drinking and smoking should be prohibited in areas where this material is handled, stored and processed. Workers should wash hands and face before eating, drinking and smoking. Persons with a history of skin sensitization problems should not be employed in any process in which this product is used. Do not get in eyes or on skin or clothing. Do not breathe vapor or mist. Do not ingest. Use only with adequate ventilation. Empty containers retain product residue and can be hazardous. Do not reuse container. Storage : Store in accordance with local regulations. Store in a dry, cool and well-ventilated area, away from incompatible materials (see Section 10). Keep container tightly closed and sealed until ready for use. Containers that have been opened must be carefully resealed and kept upright to prevent leakage. Do not store in unlabeled containers. Use appropriate containment to avoid environmental contamination. . Exposure controls/personal protection Occupational exposure limits TWA(8 hours) STEL(15 mins) Ceiling Ingredients: List name ppm mg/m3 ther ppm g/m3 Other ppm mg/m3 Other Notations No exposure limit value known. If OSHA permissible exposure levels are shown above they are the OSHA 1989 levels or are from subsequent OSHA regulatory actions. Although the 1989 levels have been vacated the 11th Circuit Court of Appeals, Baker Hughes recommends that these lower exposure levels be observed as reasonable worker protection. Recommended monitoring : If this product contains ingredients with exposure limits, personal, workplace atmosphere procedures or biological monitoring may be required to determine the effectiveness of the ventilation or other control measures and/or the necessity to use respiratory protective equipment. Engineering measures : If user operations generate dust,fumes, gas, vapor or mist, use process enclosures, local exhaust ventilation or other engineering controls to keep worker exposure to airborne contaminants below any recommended or statutory limits. Hygiene measures : Wash hands, forearms and face thoroughly after handling chemical products, before eating, smoking and using the lavatory and at the end of the working period. Ensure that eyewash stations and safety showers are close to the workstation location. Take off contaminated clothing and wash before reuse. Personal protection Respiratory : If a risk assessment indicates it is necessary, use a properly fitted, air purifying or supplied air respirator complying with an approved standard. Respirator selection must be based on known or anticipated exposure levels, the hazards of the product and the safe working limits of the selected respirator. Hands : Chemical-resistant gloves. Eyes : Wear chemical safety goggles. When transferring material wear face-shield in addition to chemical safety goggles. Skin : Wear long sleeves and chemical resistant apron to prevent repeated or prolonged skin contact. 9 . Physical and chemical properties Physical state : Liquid. Flash point : Closed cup: 165.56°C (330°F) Auto-ignition temperature : Not available. Flammable limits : Not available. Color : Water-white./Light yellow Odor : Musty. [Slight] 1/27/2012. 488159 3/6 GO-64 9 . Physical and chemical properties pH : 2.4 : 1%Aqueous Solution Boiling/condensation point : Not available. Initial Boiling Point : Not available. Melting/freezing point : <4°C (<39.2°F) Relative density : 1.04 Density : 8.66 (lbs/gal) Vapor density : Not available. Odor threshold : Not available. Evaporation rate : Not available. VOC : Not available. Viscosity : Not available. Solubility(Water) : Insoluble Vapor pressure : <0.017 kPa (<0.13 mm Hg) at 25°C Pour Point : Not available. Partition coefficient : Not available. (LogKow) 10 . Stability and Reactivity Chemical stability : The product is stable. Possibility of hazardous : Under normal conditions of storage and use, hazardous reactions will not occur. reactions Hazardous polymerization : Under normal conditions of storage and use, hazardous polymerization will not occur. Conditions to avoid : No specific data. Materials to avoid : Reactive or incompatible with the following materials: oxidizing materials. Hazardous decomposition. : Under normal conditions of storage and use, hazardous decomposition products should products not be produced. Conditions of reactivity : Slightly flammable in the presence of the following materials or conditions:open flames, sparks and static discharge and heat. 11 . Toxicological information No additional information. Chronic toxicity Remarks 1) Phosphate ester Not available. 12 . Ecological information Aquatic ecotoxicity Conclusion/Summary : Not available. Biodegradability Conclusion/Summary : Not available. 1/27/2012. 488159 4/6 GO-64 13. Disposal considerations Waste disposal : The generation of waste should be avoided or minimized wherever possible. Empty containers or liners may retain some product residues. This material and its container must be disposed of in a safe way. Dispose of surplus and non-recyclable products via a licensed waste disposal contractor. Disposal of this product, solutions and any by- products should at all times comply with the requirements of environmental protection and waste disposal legislation and any regional local authority requirements. Avoid dispersal of spilled material and runoff and contact with soil, waterways, drains and sewers. Disposal should be in accordance with applicable regional, national and local laws and regulations. Refer to Section 7: HANDLING AND STORAGE and Section 8: EXPOSURE CONTROLS/PERSONAL PROTECTION for additional handling information and protection of employees. 14 . Transport information Regulatory UN number Proper shipping Classes PG* Label Additional information name information DOT Classification UN3265 CORROSIVE LIQUID, 8 III Ak - ACIDIC, ORGANIC, N.O.S. (Contains: CO CO Phosphate ester) 8 TDG Classification UN3265 CORROSIVE LIQUID, 8 III - ACIDIC, ORGANIC, N.O.S. (Contains: Alkyl ortho phosphate ester) IMDG Class UN3265 CORROSIVE LIQUID, 8 III - ACIDIC, ORGANIC, N.O.S. (Contains: Phosphate ester) IATA-DGR Class UN3265 CORROSIVE LIQUID, 8 III - ACIDIC, ORGANIC, N.O.S. (Contains: Phosphate ester) PG* : Packing group DOT Reportable Not applicable. Quantity Marine pollutant Not applicable. North-America NAERG : 153 15 . Regulatory information HCS Classification : Corrosive material Sensitizing material U.S. Federal regulations : United States inventory(TSCA 8b):All components are listed or exempted. SARA 302/304/311/312 extremely hazardous substances: No products were found. SARA 302/304 emergency planning and notification: No products were found. SARA 302/304/311/312 hazardous chemicals: No products were found. SARA 311/312 MSDS distribution-chemical inventory- hazard identification: GO- 64: Immediate (acute) health hazard CERCLA: Hazardous substances.: No products were found. Clean Water Act(CWA)307: No products were found. Clean Water Act(CWA)311: No products were found. Clean Air Act(CAA) 112 regulated flammable substances: No products were found. 1/27/2012. 488159 5/6 GO-64 15 . Regulatory information Clean Air Act(CAA) 112 regulated toxic substances: No products were found. Clean Air Act Section 112(b) Hazardous Air Pollutants (HAPs) : Not listed United States inventory : All components are listed or exempted. (TSCA 8b) Canada WHMIS(Canada) : Class E: Corrosive material Canada(CEPA DSL): : Not determined. 16 . Other information Label requirements : CAUSES EYE AND SKIN BURNS. MAY CAUSE ALLERGIC SKIN REACTION. Hazardous Material • Information System (U.S.A.) ealth 2 Flammability 1 Physical hazards 0 Personal protection d Caution: HMIS®ratings are based on a 0-4 rating scale, with 0 representing minimal hazards or risks,and 4 representing significant hazards or risks Although HMIS®ratings are not required on MSDSs under 29 CFR 1910.1200, the preparer may choose to provide them. HMIS®ratings are to be used with a fully implemented HMIS®program. HMIS®is a registered mark of the National Paint & Coatings Association (NPCA). HMIS® materials may be purchased exclusively from J. J. Keller(800) 327-6868. The customer is responsible for determining the PPE code for this material. National Fire Protection • Association (U.S.A.) Flammability Health ; O Instability ♦ Special Date of printing : 1/27/2012. 17 Indicates information that has changed from previously issued version. Notice to reader NOTE: The information on this MSDS is based on data which is considered to be accurate. Baker Hughes, however, makes no guarantees or warranty, either expressed or implied of the accuracy or completeness of this information. The conditions or methods of handling, storage, use and disposal of the product are beyond our control and may be beyond our knowledge. For this and other reasons,we do not assume responsibility and expressly disclaim liability for loss, damage or expense arising out of or in any way connected with the handling, storage, use or disposal of this product. This MSDS was prepared and is to be used for this product. If the product is used as a component in another product,this MSDS information may not be applicable. 1/27/2012. 488159 6/6 CARBO CARBO LITE'(All Mesh Sizes) MSDS NO:02 CERAMICS REVISION DATE:February 26,2007 MATERIAL SAFETY DATA SHEET PAGE 1 OF 3 1. PRODUCT AND COMPANY IDENTIFICATION TRADE NAME: CARBOLITE®(All Mesh Sizes) SYNONYM(S): Ceramic Proppant;Semi-Crystalline Alumina Silicate CHEMICAL FAMILY: Aluminosilicate MANUFACTURER: CARBO Ceramics 4810 Industrial Drive New Iberia,Louisiana 70560 Phone: 1-337-367-6151 EMERGENCY PHONE: 1-800-551-3247(U.S.A.) 2. COMPOSITION/INFORMATION ON INGREDIENTS INGREDIENTS CAS NUMBER CONCENTRATION CLASSIFICATION R-PHRASES Silicon Dioxide, (amorphous 7631-86-9 5-35% Not Classified Not assigned as glass) Mullite 1302-93-8 60-85% Not Classified Not assigned Silica Crystalline-Cristobalite 14464-46-1 0-20% Not Classified Not assigned 3. HEALTH HAZARD INFORMATION INHALATION: Inhalation of dusts may cause respiratory tract irritation. Repeated or prolonged breathing of particles of respirable size may cause severe respiratory disease. However, this product contains few particles of respirable size. Repeated indoor air quality monitoring and testing conducted throughout the production and shipping process at CARBO Ceramics, Inc.shows that the final product produces levels of respirable silica(in the form of crystalline crystobalite)below laboratory detection limits and applicable exposure limits(see section 8). The amount of dust due to breakdown during shipment and intended use and handling is not expected to exceed applicable exposure limits(see section 8). Analyses for crystalline forms of silica at CARBO Ceramics,Inc.facilities were performed by X-ray diffraction based upon OSHA ID 142 guidelines. EYE CONTACT: Airborne dust may cause irritation to eyes. SKIN CONTACT: Prolonged contact with a skin may cause irritation. HMIS RATING: HEALTH 1 (slight) FLAMMABILITY 0(minimal) REACTIVITY 0(minimal) SPECIAL PROTECTION: (See section 8) 4. FIRST AID MEASURES INHALATION: Remove affected person from source of exposure. Get medical attention if irritation occurs. INGESTION: Seek medical attention if large quantities are ingested. EYE CONTACT: Immediately flush eyes with large amounts of water, lifting the lower and upper lids occasionally. If irritation is present after washing,get medical attention. SKIN CONTACT: Wash the affected area with soap and water. Get medical attention if irritation occurs. 5. FIRE-FIGHTING MEASURES ESTIMATED EXPLOSIVE LIMITS(%By volume in air): LEL: N/A UEL: N/A FLASH POINT: N/A SPECIAL FIRE FIGHTING PROCEDURES: This material does not give a flash point by conventional test methods.Use extinguishing agent suitable for type of surrounding fire. UNUSUAL HAZARDS: N/A 6. SPILL OR LEAK PROCEDURES STEPS TO BE TAKEN IN CASE MATERIAL IS RELEASED OR SPILLED: No Special procedures are required for clean-up of spills or leaks of this material. Caution should be exercised regarding personal safety and exposure to the spilled material,the material's nature could cause reduced traction. Persons should take care so as not to slip. CARBO CARBOLITE°(All Mesh Sizes) MSDS NO:02 CERAMICS REVISION DATE:February 26,2007 MATERIAL SAFETY DATA SHEET PAGE2OF3 nuvrurII 7. HANDLING AND STORAGE HANDLING: Do not create dust. Use personal protective equipment. Refer to section 8 for suggested personal protective equipment. STORAGE: Store dry in closed container to reduce dust. 8. EXPOSURE CONTROLS/PROTECTION DURING USE EXPOSURE LIMITS: INGREDIENTS OSHA PEL-TWA ACGIH-TWA TLV Silicon Dioxide,amorphous as 80 mg/m3/%Si02(total) - glass Mullite 15 mg/m3(total) 10 mg/m3(total) 5 mg/m3(respirable) 3 mg/m3(resp) Silica Crystalline Cristobalite 15 mg/m3/(%Si02+2)(total) 0.05 mg/m3 5 mg/m3/(%SiO2+2) (respirable) (respirable) ENGINEERING CONTROL Exposure to this material may be controlled in a number of ways. The measures MEASURES: appropriate fora particular worksite depend on how the material is used and the potential for exposure.Use of the basic principles of industrial hygiene will enable safe handling of the material. RESPIRATORY: An applicable NIOSH/MSHA or equivalent approved respirator should be worn where airborne exposures may exceed OSHA/ACGIH permissible air concentrations. EYE PROTECTION: Wear safety glasses or chemical goggles to prevent eye contact. Do not wear contact lenses when working with this substance unless protected under full coverage goggles. CLOTHING/GLOVES: Gloves are optional to reduce abrasion. WORK HYGIENE PRACTICES: Handle in accordance with good personal hygiene and safety practices. n VENTILATION: Provide sufficient(general and/or local exhaust)ventilation to maintain exposure below permissible air concentrations. 9. PHYSICAL AND CHEMICAL PROPERTIES BOILING POINT: N/A °F SPECIFIC GRAVITY: 2.7 (H2O=1) pH:N/A MELTING POINT: 4000 °F (estimated) BULK DENSITY: 98 lb/cu.ft. VAPOR PRESSURE: N/A mm Hg %VOLATILE BY N/A WEIGHT: VAPOR DENSITY: N/A (Air= 1) EVAPORATION RATE: N/A(Butyl Acetate=1) APPEARANCE/ODOR: Odorless cream to light—gray spheres SOLUBILITY IN WATER: Insoluble VOLATILE ORGANIC COMPOUNDS (VOC): 0 lbs/gal(EPA Reference Methods 24) 10. STABILITY AND REACTIVITY REACTIVITY: Minimal STABILITY: Stable INCOMPATIBLE MATERIALS: Chlorine Triflouride. 11. TOXICOLOGICAL INFORMATION ACUTE EFFECTS Coughing and throat irritation are early symptoms of excessive exposure. Acute pneumoconiosis from excessive exposure to silica dust has occurred. May be irritating to the respiratory system,lungs and skin. May also cause irritation to eyes. CHRONIC EFFECTS: Inhalation of respirable crystalline-crystobalite in excess of established human exposure limits is known to cause human cancer. Chronic exposure can cause severe respiratory disease. CARBO CARBOLITE®(All Mesh Sizes) MSDS NO:02 CERAMICS REVISION DATE:February 26,2007 MATERIAL SAFETY DATA SHEET PAGE3OF3 12. ECOLOGICAL INFORMATION This product poses no significant environmental contamination impact during expected use,handling,and proper disposal. 13. DISPOSAL CONSIDERATIONS WASTE DISPOSAL: Disposal must be at an approved waste disposal facility and in accordance with applicable Federal,State and Local laws and regulations. Contact the district Director of the Environmental Protection Agency and/or state regulatory agency for appropriate requirements. 14. TRANSPORTATION INFORMATION UN NO. N/A ICAO/IATA Not Restricted RID/ADR Not Restricted DOT SHIPPING DESCRIPTION Not Restricted CAN Not Restricted IMO Not Restricted 15. REGULATORY INFORMATION TOXIC SUBSTANCE CONTROL ACT(TSCA)STATUS:All chemicals in this product are SARA TITLE III: Section 302: None listed,automatically included,or are exempt from listing on the TSCA Inventory. Section 312: None Section 313: None CERCLA REPORTABLE QUANTITY: None CLEAN AIR AMENDMENTS-HAZARDOUS AIR POLLUTANTS(HAPS): None CALIFORNIA STATE PROPOSITION 65: Silica,crystalline(airborne particles of respirable size) 16. OTHER INFORMATION //r Material Safety Data Sheet BAKER HUGHES 1 . Product and company identification Product name : NE-110W Supplier : Baker Hughes, Inc. 12645 W. Airport Blvd. Sugar Land, TX 77478 For Product Information/MSDSs Call: 281-351-8131 Material Uses : Special: Non-emulsifier. Code : 499690 Validation date : 7/27/2012. Print date : 7/27/2012. Version : 1.01 Responsible name : Global Regulatory Affairs-Telephone 281-276-5400 or 800-231-3606 In case of emergency : CHEMTREC 800-424-9300 (U.S. 24 hour) (001)281-276-5400 CANUTEC 613-996-6666 (Canada 24 hours)CHEMTREC Intl 01-703-527- 3887(International 24 hour) 2 . Hazards identification Physical state : Liquid. [Clear.] Odor : Aromatic hydrocarbon. Color : Amber. OSHA/HCS status : This material is considered hazardous by the OSHA Hazard Communication Standard (29 CFR 1910.1200). Emergency overview : WARNING! COMBUSTIBLE LIQUID AND VAPOR. INHALATION CAUSES HEADACHES, DIZZINESS, DROWSINESS AND NAUSEA AND MAY LEAD TO UNCONSCIOUSNESS. CAUSES RESPIRATORY TRACT AND EYE IRRITATION. MAY CAUSE SKIN IRRITATION. PROLONGED OR REPEATED CONTACT MAY DRY SKIN AND CAUSE IRRITATION. HARMFUL OR FATAL IF SWALLOWED. CAN ENTER LUNGS AND CAUSE DAMAGE. CONTAINS MATERIAL THAT MAY CAUSE TARGET ORGAN DAMAGE, BASED ON ANIMAL DATA. SUSPECT CANCER HAZARD -CONTAINS MATERIAL WHICH MAY CAUSE CANCER. ASPIRATION HAZARD. At elevated temperatures, vapors can form an ignitable or explosive mixture with air. Can form explosive mixtures at temperatures at or above the flash point. Static discharges can cause ignition or explosion when container is not bonded. Keep away from heat, sparks and flame. Do not breathe vapor or mist. Do not ingest. Avoid contact with eyes, skin and clothing. Use only with adequate ventilation. Keep container tightly closed and sealed until ready for use. Wash thoroughly after handling. Vapors can travel to a source of ignition and flashback. To avoid fire or explosion, dissipate static electricity during transfer by grounding and bonding containers and equipment before transferring material. Routes of entry : Dermal contact. Eye contact. Inhalation. Potential acute health effects Inhalation : Can cause central nervous system (CNS) depression. Irritating to respiratory system. Ingestion : Harmful if swallowed. Can cause central nervous system (CNS) depression. Aspiration hazard if swallowed. Can enter lungs and cause damage. Skin : Moderately irritating to the skin. Eyes : Irritating to eyes. Potential chronic health effects 7/27/2012. 499690 1/9 NE-110W 2 . Hazards identification Chronic effects material that may cause target organ damage, based on animal data. Prolonged or repeated contact can defat the skin and lead to irritation, cracking and/or dermatitis. Carcinogenicity : Contains material which may cause cancer. Risk of cancer depends on duration and level of exposure. Target organs : Contains material which may cause damage to the following organs: blood, kidneys, the nervous system, liver, upper respiratory tract, skin, central nervous system (CNS), eye, lens or cornea. Over-exposure skins/symptoms Inhalation : respiratory tract irritation, nausea or vomiting, coughing, headache, drowsiness/fatigue, dizziness/vertigo, unconsciousness Ingestion : nausea or vomiting Skin : irritation, redness, dryness, cracking Eyes : pain or irritation, watering, redness Medical conditions : Pre-existing disorders involving any target organs mentioned in this MSDS as being at aggravated by over- risk may be aggravated by over-exposure to this product. exposure See toxicological information (Section 11) 3 . Composition/information on ingredients Name CAS number Heavy aromatic naphtha 64742-94-5 30 - 60 Alkylaryl sulfonates Trade secret. 5 - 10 Methyl amyl alcohol 108-11-2 5 - 10 Diisopropylnaphthalene 38640-62-9 5- 10 Naphthalene 91-20-3 5- 10 Alkyl aryl amine sulfonate Trade secret. 1 -5 1,2,4-Trimethylbenzene 95-63-6 1 -5 Light aromatic naphtha l ,64742-95-6 1 -5 Additional information This product is a mixture. Chemical family : Petroleum distillate. 4 . First aid measures Eye contact : Get medical attention immediately. Immediately flush eyes with plenty of water for at least 15 minutes, occasionally lifting the upper and lower eyelids. Skin contact : In case of contact, immediately flush skin with plenty of water for at least 15 minutes while removing contaminated clothing and shoes. Wash clothing before reuse. Clean shoes thoroughly before reuse. Get medical attention immediately. Inhalation : Move exposed person to fresh air. If not breathing, if breathing is irregular or if respiratory arrest occurs, provide artificial respiration or oxygen by trained personnel. Loosen tight clothing such as a collar, tie, belt or waistband. Get medical attention immediately. Ingestion : Wash out mouth with water. Do not induce vomiting unless directed to do so by medical personnel. Never give anything by mouth to an unconscious person. Get medical attention immediately. Protection of first-aiders : No action shall be taken involving any personal risk or without suitable training. If it is suspected that fumes are still present,the rescuer should wear an appropriate mask or self-contained breathing apparatus. It may be dangerous to the person providing aid to give mouth-to-mouth resuscitation. Wear suitable protective clothing and gloves. Remove contaminated clothing and shoes. Additional information If product is ingested and vomiting occurs naturally, have person lean forward to reduce the risk of aspiration into the lungs. 7/27/2012. 499690 2/9 NE-110W 5 . Fire-fighting measures Flammability of the product : Combustible liquid. In a fire or if heated, a pressure increase will occur and the container may burst, with the risk of a subsequent explosion. The vapor/gas is heavier than air and will spread along the ground. Vapors may accumulate in low or confined areas or travel a considerable distance to a source of ignition and flash back. Extinguishing media Suitable : Use dry chemical, CO2, water spray(fog) or foam. Not suitable : Do not use water jet. Special exposure hazards : Promptly isolate the scene by removing all persons from the vicinity of the incident if there is a fire. No action shall be taken involving any personal risk or without suitable training. Move containers from fire area if this can be done without risk. Use water spray to keep fire-exposed containers cool. Fire water contaminated with this material must be contained and prevented from being discharged to any waterway, sewer or drain. Hazardous thermal : carbon dioxide,carbon monoxide,nitrogen oxides,sulfur oxides decomposition products Special protective : Fire-fighters should wear appropriate protective equipment and self-contained breathing equipment for fire-fighters apparatus (SCBA)with a full face-piece operated in positive pressure mode. 6 . Accidental release measures Personal precautions : No action shall be taken involving any personal risk or without suitable training. Evacuate surrounding areas. Keep unnecessary and unprotected personnel from entering. Do not touch or walk through spilled material. Shut off all ignition sources. No flares, smoking or flames in hazard area. Do not breathe vapor or mist. Provide adequate ventilation. Wear appropriate respirator when ventilation is inadequate. Put on appropriate personal protective equipment (see Section 8). Environmental precautions : Avoid dispersal of spilled material and runoff and contact with soil, waterways, drains and sewers. Water polluting material. May be harmful to the environment if released in large quantities. Methods for cleaning up Small spill : Stop leak if without risk. Move containers from spill area. Absorb with an inert material. Use spark-proof tools and explosion-proof equipment. Dispose of via a licensed waste disposal contractor. Large spill : Stop leak if without risk. Move containers from spill area. Approach release from upwind. Dike spill area and do not allow product to reach sewage system or surface or ground water. Notify any reportable spill to authorities. (See section 12 for environmental risks and 13 for disposal information.) Contain and collect spillage with non- combustible, absorbent material e.g. sand, earth, vermiculite or diatomaceous earth and place in container for disposal according to local regulations (see section 13). Use spark-proof tools and explosion-proof equipment. Dispose of via a licensed waste disposal contractor. Contaminated absorbent material may pose the same hazard as the spilled product. Note: see section 1 for emergency contact information and section 13 for waste disposal. If RQ(Reportable Quantity) is exceeded, report to National Spill Response Office at 1-800-424-8802. 7 . Handling and storage Handling : Put on appropriate personal protective equipment(see Section 8). Eating, drinking and smoking should be prohibited in areas where this material is handled, stored and processed. Workers should wash hands and face before eating, drinking and smoking. Do not get in eyes or on skin or clothing. Do not breathe vapor or mist. Do not ingest. Avoid release to the environment. Use only with adequate ventilation. Store and use away from heat, sparks, open flame or any other ignition source. Use explosion-proof electrical (ventilating, lighting and material handling) equipment. Use non-sparking tools. Take precautionary measures against electrostatic discharges. To avoid fire or explosion, dissipate static electricity during transfer by grounding and bonding containers and equipment before transferring material. Empty containers retain product residue and can be hazardous. Do not reuse container. 7/27/2012. 499690 3/9 NE-110W 7 . Handling and storage Storage : Store in accordance with local regulations. Store in a segregated and approved area. Store in a dry, cool and well-ventilated area, away from incompatible materials (see Section 10). Eliminate all ignition sources. Separate from oxidizing materials. Keep container tightly closed and sealed until ready for use. Containers that have been opened must be carefully resealed and kept upright to prevent leakage. Do not store in unlabeled containers. Use appropriate containment to avoid environmental contamination. 8 . Exposure controls/personal protection Occupational exposure limits TWA(8 hours) STEL(15 mins) Ceiling Ingredients: List name ppm mg/m3 Other ppm mg/m3 Other ppm mg/m3 Other Notations Methyl amyl alcohol US ACGIH 25 104 - 40 167 - - - - [1] OSHA PEL 25 100 - - - - - - - [1] OSHA PEL 1989 25 100 - 40 165 - - - - [1] Naphthalene US ACGIH 10 52 - 15 79 - - - - OSHA PEL 10 50 - - - - - - OSHA PEL 1989 10 50 - 15 75 - - - - 1,2,4-Trimethylbenzene US ACGIH 25 123 - - - - - - OSHA PEL 1989 25 125 - - - - - - - [1]Absorbed through skin. Consult local authorities for acceptable exposure'limits. Only components of this product with established exposure limits appear in the box above. If OSHA permissible exposure levels are shown above they are the OSHA 1989 levels or are from subsequent OSHA regulatory actions.Although the 1989 levels have been vacated the 11th Circuit Court of Appeals, Baker Hughes recommends that these lower exposure levels be observed as reasonable worker protection. Recommended monitoring : If this product contains ingredients with exposure limits, personal, workplace atmosphere procedures or biological monitoring may be required to determine the effectiveness of the ventilation or other control measures and/or the necessity to use respiratory protective equipment. Engineering measures : Use only with adequate ventilation. Use process enclosures, local exhaust ventilation or other engineering controls to keep worker exposure to airborne contaminants below any recommended or statutory limits. Use explosion-proof ventilation equipment. Hygiene measures : Wash hands, forearms and face thoroughly after handling chemical products, before eating, smoking and using the lavatory and at the end of the working period. Ensure that eyewash stations and safety showers are close to the workstation location. Take off contaminated clothing and wash before reuse. Personal protection Respiratory : If a risk assessment indicates it is necessary, use a properly fitted, air purifying or supplied air respirator complying with an approved standard. Respirator selection must be based on known or anticipated exposure levels, the hazards of the product and the safe working limits of the selected respirator. Hands : Chemical-resistant gloves: Nitrile or Neoprene gloves. 4H gloves. Eyes : Wear chemical safety goggles. When transferring material wear face-shield in addition to chemical safety goggles. Skin : Wear long sleeves and other protective clothing to prevent repeated or prolonged skin contact. 9 . Physical and chemical properties Physical state : Liquid. [Clear.] Flash point : Closed cup:50°C (122°F) [SFCC] Auto-ignition temperature : Not available. Flammable limits : Not available. Color : Amber. Odor : Aromatic hydrocarbon. pH : 2 to 3 : 5%of product in 75%isopropanol/25%water solution 7/27/2012. 499690 4/9 NE-110W 9 . Physical and chemical properties Boiling/condensation point : Not available. Initial Boiling Point : Not available. Melting/freezing point : Not available. Relative density : 0.95 (25°C) Density : 7.91 (lbs/gal) Vapor density : >1 [Air= 1] Odor threshold : Not available. Evaporation rate : Not available. VOC : Not available. Viscosity : Not available. Solubility(Water) : Dispersible Vapor pressure : 0.25 kPa (1.9 mm Hg) at 21.1°C (Calculated Value for all Components.) Pour Point : Not available. Partition coefficient : Not available. (LogKow) 10 . Stability and Reactivity Chemical stability : The product is stable. Possibility of hazardous : Under normal conditions of storage and use, hazardous reactions will not occur. reactions Hazardous polymerization : Under normal conditions of storage and use, hazardous polymerization will not occur. Conditions to avoid : Avoid all possible sources of ignition (spark or flame). Do not pressurize, cut, weld, braze, solder, drill, grind or expose containers to heat or sources of ignition. Do not allow vapor to accumulate in low or confined areas. Materials to avoid : Reactive or incompatible with the following materials: oxidizing materials. Hazardous decomposition : Under normal conditions of storage and use, hazardous decomposition products should products not be produced. Conditions of reactivity : Flammable in the presence of the following materials or conditions: open flames, sparks and static discharge and heat. 11 . Toxicological information Acute toxicity Product/ingredient name Result Species Dose Exposure Heavy aromatic naphtha LD50 Dermal Rabbit >2 mL/kg - LD50 Oral Rat 3200 mg/kg - LD50 Oral Rat >2000 mg/kg - LC50 Inhalation Rat >11.4 mg/L 6 hours Vapor LC50 Inhalation Rat >590 mg/m3 4 hours Vapor Methyl amyl alcohol LD50 Dermal Rabbit 3560 uUkg - LD50 Oral Rat 2590 mg/kg - Alkylaryl sulfonates LD50 Oral Rat >1400 mg/kg - Naphthalene LD50 Dermal Rabbit >20 g/kg - LD50 Dermal Rat >2500 mg/kg - LD50 Oral Rat 490 mg/kg - 1,2,4-Trimethylbenzene LD50 Oral Rat 5 g/kg - LC50 Inhalation Rat 18000 mg/m3 4 hours Vapor Light aromatic naphtha LD50 Oral Rat 8400 mg/kg - LD50 Oral Rat 2900 mg/kg - Carcinogenicity Classification Product/ingredient name ACGIH IARC EPA NIOSH NTP OSHA 7/27/2012. 499690 5/9 NE-110W 11 . Toxicological information Naphthalene A4 2B - - Possible - Chronic toxicity Remarks 1) Heavy aromatic naphtha Not available. 2) Alkylaryl sulfonates Not available. 3) Methyl amyl alcohol Male rats exposed to 3753 mg/m3 (900 ppm) methyl isobutyl carbinol for 6 hours/day, 5 days/week for 6 weeks showed an increase in kidney weights. These effects were not seen in male rats exposed to lower concentrations or in female rats at even the highest level of exposure. 4) Diisopropylnaphthalene Not available. 5) Naphthalene This product contains naphthalene. A National Toxicology Program (NTP) report concluded there is clear evidence to support carcinogenicity of naphthalene in male and female rats. These observations were based on 2-year inhalation studies in which the test animals were exposed to 10, 30, and 60 ppm naphthalene. In male and female rats, exposure to naphthalene caused significant increases in the incidence of nonneoplastic lesions of the nose (NTP TR-500). The relevance of the rodent findings to humans is questionable. Naphthalene has caused hemolytic anemia,jaundice, cataracts (Shopp et al, 1984), allergic reactions (Tsyrkunov& Yakovleva, 1985), possible neurotoxicity(Riala et al, 1984), and aplastic anemia(Harden & Baetjer, 1978) in humans. Increased lung aveolar adenomas were seen in mice exposed to 30 ppm naphthalene for 6hrs/day for 6 months (ACGIH, 1992). Naphthalene crosses the placenta leading to methemoglobinemia(decreased ability for the blood to carry oxygen), and/or hemolytic anemia, conditions considered especially dangerous to the unborn (Reprotext). Liver and kidney damage has also been seen with exposure to naphthalene (Reprotext). Peripheral lens opacities occurred in 8 of 21 workers exposed to high levels of naphthalene fumes or vapors for 5 years, but cataracts have not been reported in other occupational studies. (Hathaway et al, 1991). The International Agency for Research on Cancer(IARC) evaluated naphthalene and concluded that there was sufficient evidence for carcinogenicity in experimental animals, but inadequate evidence that it causes cancer in exposed humans. Accordingly, IARC classified naphthalene as a possible human carcinogen (Group 2B). 6) Alkyl aryl amine sulfonate Not available. 7) 1,2,4-Trimethylbenzene 1,2,4-Trimethylbenzene, also know as pseudocumene, is a component of this product. Chronic pseudocumene exposure may provoke bronchospasm with cough and wheezing (Plunkett, 1976; ACGIH, 1991; Battig et al, 1956). Respiratory distress was noted in experimental animals following sub acute inhalation exposure (Gage, 1970). Nervousness and anxiety were noted with chronic occupational exposure (Battig et al, 1956; ACGIH, 1991). At the time of this review, no studies were found on the potential adverse reproductive effects of pseudocumene in humans, but trimethylbenzenes (including pseudocumene) can cross the placental barrier(Clayton &Clayton, 1994; Doroty et al, 1976). In an experimental animal study, offspring born to pregnant rats exposed to pseudocumene were healthy at birth and grew normally(Cameron et al, 1938). Blood effects such as anemia and delayed clotting time have been noticed in workers chronically exposed to a solvent containing trimethylbenzene. The blood effects, however, may have been due to a contaminant in the solvent such as benzene (a known blood toxin). 7/27/2012. 499690 6/9 NE-110W 11 . Toxicological information 8) Light aromatic naphtha Solvent naphtha (petroleum), light aromatic is a component of this product. Solvent naphtha (petroleum), light aromatic may cause damage to the peripheral nerves, resulting in numbness or tingling of the extremities with chronic (long term) exposure to high concentrations. (Micromedex) Rats exposed for 4 months to 1700 ppm of a solvent similar to this product showed evidence of mild damage to the liver, lungs and kidneys. These effects were not seen in rats exposed for one year to 350 ppm of another similar solvent. Rats exposed to vapors of a similar solvent during pregnancy showed embryo/fetotoxicity at concentrations producing maternal toxicity. In response to a TSCA test rule, several studies of a solvent similar to this product were completed. Mutagenicity studies and a rat inhalation neurotoxicity study were negative. In a mouse developmental effects study, reduced fetal body weight was seen but no teratogenicity. A rat reproductive effects study demonstrated toxicity but little effect on reproductive parameters. (Vendor MSDS) Ingestion has produced Central Nervous System effects in laboratory animals. (EPA/OTS 87-8214199 and 88-920000348) 12 . Ecological information Aquatic ecotoxicitV Product/ingredient name Result Species Exposure Naphthalene Acute EC50 1.96 mg/L Fresh Daphnia-Water flea- Daphnia 48 hours water magna-<24 hours Acute LC50 2350 ug/L Marine Crustaceans - Daggerblade grass 48 hours water shrimp- Palaemonetes pugio Acute LC50 213 ug/L Fresh water Fish - Crimson-spotted rainbowfish 96 hours - Melanotaenia fluviatilis - LARVAE - 1 days Chronic NOEC 600 ug/L Fresh Daphnia-Water flea- Daphnia 48 hours +, water magna- <=24 hours 1,2,4-Trimethylbenzene Acute LC50 17000 ug/L Marine Crustaceans - Dungeness or 48 hours water edible crab-Cancer magister- Zoea Acute LC50 7720 to 8280 ug/L Fish - Fathead minnow- 96 hours Fresh water Pimephales promelas -34 days Conclusion/Summary : Not available. Biodegradability Conclusion/Summary : Not available. 13. Disposal considerations Waste disposal : The generation of waste should be avoided or minimized wherever possible. Empty containers or liners may retain some product residues. This material and its container must be disposed of in a safe way. Dispose of surplus and non-recyclable products via a licensed waste disposal contractor. Disposal of this product, solutions and any by- products should at all times comply with the requirements of environmental protection and waste disposal legislation and any regional local authority requirements. Avoid dispersal of spilled material and runoff and contact with soil, waterways, drains and sewers. Disposal should be in accordance with applicable regional, national and local laws and regulations. Refer to Section 7: HANDLING AND STORAGE and Section 8: EXPOSURE CONTROLS/PERSONAL PROTECTION for additional handling information and protection of employees. 7/27/2012. 499690 7/9 NE-110W 14 . Transport information Regulatory UN number Proper shipping Classes PG* Label Additional information name information DOT Classification UN1993 FLAMMABLE LIQUID, 3 III - N.O.S. (Contains: Methyl amyl alcohol) TDG Classification UN1993 FLAMMABLE LIQUID, 3 III - N.O.S. (Contains: Methyl amyl alcohol) IMDG Class UN1993 FLAMMABLE LIQUID, 3 III Emergency N.O.S. (Contains: schedules(EmS) Methyl amyl alcohol) F-E S-E IATA-DGR Class UN1993 FLAMMABLE LIQUID, 3 III - N.O.S (Contains: Methyl amyl alcohol) PG* : Packing group DOT Reportable Naphthalene, 236 gal of this product. Quantity Xylene, 5835 gal of this product. Marine pollutant Not applicable. North-America NAERG : 128 15 . Regulatory information HCc.",Classification : Combustible liquid Irritating material Carcinogen Target organ effects U.S. Federal regulations : United States inventory(TSCA 8b): All components are listed or exempted. SARA 302/304/311/312 extremely hazardous substances: No products were found. SARA 302/304 emergency planning and notification: No products were found. SARA 302/304/311/312 hazardous chemicals: Naphthalene; 1,2,4-trimethylbenzene; Light aromatic naphtha; Methyl amyl alcohol SARA 311/312 MSDS distribution -chemical inventory- hazard identification: NE- 110W: Fire hazard, Immediate (acute) health hazard, Delayed (chronic) health hazard CERCLA: Hazardous substances.: Naphthalene: 100 lbs. (45.4 kg); Potassium hydroxide: 1000 lbs. (454 kg); xylene: 100 lbs. (45.4 kg); Cumene: 5000 lbs. (2270 kg); Ethylbenzene: 1000 lbs. (454 kg); Clean Water Act (CWA) 307: Naphthalene; Ethylbenzene Clean Water Act (CWA) 311: Naphthalene; xylene; Potassium hydroxide; Ethylbenzene Clean Air Act (CAA) 112 regulated flammable substances: No products were found. Clean Air Act (CAA) 112 regulated toxic substances: No products were found. Clean Air Act Section 112(b) Hazardous Air Pollutants(HAPs) : Listed SARA 313 Product name CAS number Concentration Supplier notification : Naphthalene 91-20-3 5 - 10 1,2,4-Trimethylbenzene 95-63-6 1 - 5 United States inventory : All components are listed or exempted. (TSCA 8b) 7/27/2012. 499690 8/9 NE-110W 15 . Regulatory information Canada WHMIS(Canada) : Class B-3: Combustible liquid with a flash point between 37.8°C (100°F) and 93.3°C (200°F). Class D-2A: Material causing other toxic effects (Very toxic). Class D-2B: Material causing other toxic effects (Toxic). Canada(CEPA DSL): : All components are listed or exempted. 16 . Other information Label requirements : COMBUSTIBLE LIQUID AND VAPOR. INHALATION CAUSES HEADACHES, DIZZINESS, DROWSINESS AND NAUSEA AND MAY LEAD TO UNCONSCIOUSNESS. CAUSES RESPIRATORY TRACT AND EYE IRRITATION. MAY CAUSE SKIN IRRITATION. PROLONGED OR REPEATED CONTACT MAY DRY SKIN AND CAUSE IRRITATION. HARMFUL OR FATAL IF SWALLOWED. CAN ENTER LUNGS AND CAUSE DAMAGE. CONTAINS MATERIAL THAT MAY CAUSE TARGET ORGAN DAMAGE, BASED ON ANIMAL DATA. SUSPECT CANCER HAZARD - CONTAINS MATERIAL WHICH MAY CAUSE CANCER. ASPIRATION HAZARD. Hazardous Material • Information System (U.S.A.) Health 2 Flammability U Physical hazards <IlL 0 Personal protection Caution: HMIS®ratings are based on a 0-4 rating scale, with 0 representing minimal hazards or risks, and 4 representing significant hazards or risks Although HMIS®ratings are not required on MSDSs under 29 CFR 1910.1200,the preparer may choose to provide them. HMIS®ratings are to be used with a fully implemented HMIS®program. HMIS®is a registered mark of the National Paint &Coatings Association (NPCA). HMIS® materials may be purchased exclusively from J.J. Keller(800)327-6868. The customer is responsible for determining the PPE code for this material. National Fire Protection • Association (U.S.A.) Flammability Health4.0 Instability Special Date of printing : 7/27/2012. V Indicates information that has changed from previously issued version. Notice to reader NOTE:The information on this MSDS is based on data which is considered to be accurate. Baker Hughes, however, makes no guarantees or warranty,either expressed or implied of the accuracy or completeness of this information. The conditions or methods of handling, storage, use and disposal of the product are beyond our control and may be beyond our knowledge. For this and other reasons, we do not assume responsibility and expressly disclaim liability for loss, damage or expense arising out of or in any way connected with the handling, storage, use or disposal of this product. This MSDS was prepared and is to be used for this product. If the product is used as a component in another product,this MSDS information may not be applicable. 7/27/2012. 499690 9/9 FAr Material Safety Data Sheet BAKER HUGHES 1 . Product and company identification Product name : XLO-5 Supplier : Baker Hughes, Inc. 12645 W. Airport Blvd. Sugar Land, TX 77478 For Product Information/MSDSs Call: 281-351-8131 Material Uses : Special: Cross-linking agent. Code : 488160 Validation date : 12/16/2011. Print date : 12/16/2011. Version : 1 Responsible name : Global Regulatory Affairs-Telephone 281-276-5400 or 800-231-3606 In case of emergency : CHEMTREC 800-424-9300 (U.S. 24 hour) (001)281-276-5400 CANUTEC 613-996-6666 (Canada 24 hours)CHEMTREC Intl 01-703-527- 3887 (International 24 hour) 2 . Hazards identification Physical state : Liquid. Odor : Characteristic. [Slight] Color : Brown. [Light] OSHA/HCS status : This material is considered hazardous by the OSHA Hazard Communication Standard (29 CFR 1910.1200). Emergency overview : DANGER! CAUSES RESPIRATORY TRACT, EYE AND SKIN BURNS. MAY BE HARMFUL IF SWALLOWED. CONTAINS MATERIAL THAT MAY CAUSE TARGET ORGAN DAMAGE, BASED ON ANIMAL DATA. Do not breathe vapor or mist. Do not ingest. Do not get in eyes or on skin or clothing. Use only with adequate ventilation. Keep container tightly closed and sealed until ready for use. Wash thoroughly after handling. Routes of entry : Dermal contact. Eye contact. Inhalation. Ingestion. Potential acute health effects Inhalation : Corrosive to the respiratory system. Ingestion : Harmful if swallowed. May cause burns to mouth,throat and stomach. Skin : Corrosive to the skin. Causes burns. Eyes : Corrosive to eyes. Causes burns. Potential chronic health effects Chronic effects : Contains material that may cause target organ damage, based on animal data. Target organs : Contains material which may cause damage to the following organs: upper respiratory tract, skin, eyes. Over-exposure signs/symptoms Inhalation : respiratory tract irritation, coughing Ingestion : stomach pains Skin : pain or irritation, redness, blistering may occur Eyes : pain, watering, redness Medical conditions : Pre-existing disorders involving any target organs mentioned in this MSDS as being at aggravated by over- risk may be aggravated by over-exposure to this product. exposure 12/16/2011. 488160 1/7 XLO-5 2 . Hazards identification See toxicological information (Section 11) 3 . Composition/information on ingredients Name CAS number Ferric sulfate Trade secret. 30-60 2-Dibutylaminoethanol Trade secret. 10- 30 Ethoxylated oleyl amine Trade secret. 5- 10 4 . First aid measures Eye contact : Get medical attention immediately. Immediately flush the eye(s)continuously with lukewarm, gently flowing water for at least 20-60 minutes while holding the eyelid(s) open. Skin contact : Wash affected area with soap and mild detergent for at least 20-60 minutes. Wash clothing before reuse. Clean shoes thoroughly before reuse. Get medical attention immediately. Inhalation : Move exposed person to fresh air. If not breathing, if breathing is irregular or if respiratory arrest occurs, provide artificial respiration or oxygen by trained personnel. Loosen tight clothing such as a collar, tie, belt or waistband. Get medical attention immediately. Ingestion : Wash out mouth with water. Do not induce vomiting unless directed to do so by medical personnel. Never give anything by mouth to an unconscious person. Get medical attention immediately. Protection of first-aiders : No action shall be taken involving any personal risk or without suitable training. If it is suspected that fumes are still present, the rescuer should wear an appropriate mask or self-contained breathing apparatus. It may be dangerous to the person providing aid to give mouth-to-mouth resuscitation. Wear suitable protective clothing and gloves. Remove contaminated clothing and shoes. 5 . Fire-fighting measures Flammability of the product : In a fire or if heated, a pressure increase will occur and the container may burst. Extinguishing media Suitable : Use an extinguishing agent suitable for the surrounding fire. Not suitable : None known. Special exposure hazards : Promptly isolate the scene by removing all persons from the vicinity of the incident if there is a fire. No action shall be taken involving any personal risk or without suitable training. Hazardous thermal : carbon dioxide,carbon monoxide,nitrogen oxides,sulfur oxides,metal oxide/oxides decomposition products Special protective : Fire-fighters should wear appropriate protective equipment and self-contained breathing equipment for fire-fighters apparatus(SCBA)with a full face-piece operated in positive pressure mode. 6 . Accidental release measures Personal precautions : No action shall be taken involving any personal risk or without suitable training. Evacuate surrounding areas. Keep unnecessary and unprotected personnel from entering. Do not touch or walk through spilled material. Do not breathe vapor or mist. Provide adequate ventilation. Wear appropriate respirator when ventilation is inadequate. Put on appropriate personal protective equipment(see Section 8). Environmental precautions : Avoid dispersal of spilled material and runoff and contact with soil,waterways, drains and sewers. Methods for cleaning up Small spill : Stop leak if without risk. Move containers from spill area. Absorb with an inert material. Dispose of via a licensed waste disposal contractor. 12/16/2011. 488160 2/7 XLO-5 6 . Accidental release measures Large spill : Stop leak if without risk. Move containers from spill area. Approach release from upwind. Dike spill area and do not allow product to reach sewage system or surface or ground water. Notify any reportable spill to authorities. (See section 12 for environmental risks and 13 for disposal information.) Contain and collect spillage with non- combustible, absorbent material e.g. sand, earth, vermiculite or diatomaceous earth and place in container for disposal according to local regulations (see section 13). Dispose of via a licensed waste disposal contractor. Contaminated absorbent material may pose the same hazard as the spilled product. Note: see section 1 for emergency contact information and section 13 for waste disposal. If RQ(Reportable Quantity) is exceeded, report to National Spill Response Office at 1-800-424-8802. 7 . Handling and storage Handling : Put on appropriate personal protective equipment(see Section 8). Eating, drinking and smoking should be prohibited in areas where this material is handled, stored and processed. Workers should wash hands and face before eating, drinking and smoking. Do not get in eyes or on skin or clothing. Do not breathe vapor or mist. Do not ingest. Use only with adequate ventilation. Empty containers retain product residue and can be hazardous. Do not reuse container. Storage : Store in accordance with local regulations. Store in a dry, cool and well-ventilated area, away from incompatible materials (see Section 10). Keep container tightly closed and sealed until ready for use. Containers that have been opened must be carefully resealed and kept upright to prevent leakage. Do not store in unlabeled containers. Use appropriate containment to avoid environmental contamination. 8 . Exposure controls/personal protection Occupational exposure limits TWA(8 hours) STEL(II15 mins) Ceiling Ingredients: List name ppm mg/m' Other ppm ung/m3 Other ppm mg/m' Other Notations Ferric sultate,as Fe US ACGIH - 1 - OSHA PEL 1989 - 1 - - - - - - - [a] 2-Dibutylaminoethanol US ACGIH 0.5 3.5 - - - - - - - [1] OSHA PEL 1989 2 14 - - - - - - - [1]Absorbed through skin. Form: [a]Soluble Consult local authorities for acceptable exposure'limits. Only components of this product with established exposure limits appear in the box above. If OSHA permissible exposure levels are shown above they are the OSHA 1989 levels or are from subsequent OSHA regulatory actions.Although the 1989 levels have been vacated the 11th Circuit Court of Appeals, Baker Hughes recommends that these lower exposure levels be observed as reasonable worker protection. Recommended monitoring : If this product contains ingredients with exposure limits, personal, workplace atmosphere procedures or biological monitoring may be required to determine the effectiveness of the ventilation or other control measures and/or the necessity to use respiratory protective equipment. Engineering measures : Use only with adequate ventilation. If user operations generate dust, fumes,gas, vapor or mist, use process enclosures, local exhaust ventilation or other engineering controls to keep worker exposure to airborne contaminants below any recommended or statutory limits. Hygiene measures : Wash hands,forearms and face thoroughly after handling chemical products, before eating, smoking and using the lavatory and at the end of the working period. Ensure that eyewash stations and safety showers are close to the workstation location. Take off contaminated clothing and wash before reuse. Personal protection 12/16/2011. 488160 3/7 XL0-5 8 . Exposure controls/personal protection Respiratory : If a risk assessment indicates it is necessary, use a properly fitted, air purifying or supplied air respirator complying with an approved standard. Respirator selection must be based on known or anticipated exposure levels, the hazards of the product and the safe working limits of the selected respirator. Hands : Chemical-resistant gloves. Eyes : Wear chemical safety goggles. When transferring material wear face-shield in addition to chemical safety goggles. Skin : Wear long sleeves and chemical resistant apron to prevent repeated or prolonged skin contact. 9 . Physical and chemical properties Physical state : Liquid. Flash point : Closed cup: >93.33°C (>200°F) Auto-ignition temperature : Not available. Flammable limits : Not available. Color : Brown. [Light] Odor : Characteristic. [Slight] pH : Not available. Boiling/condensation point : Not available. Initial Boiling Point : Not available. Melting/freezing point : <4°C(<39.2°F) Relative density : 1.35 Density : 11.88 (lbs/gal) Vapor density : Not available. Odor threshold : Not available. Evaporation rate : Not available. VOC . Not available. Viscosity : Not available. Solubility(Water) : Dispersible Vapor pressure : <0.13 kPa (<1 mm Hg)at 25°C Pour Point : Not available. Partition coefficient : Not available. (LogKow) 10 . Stability and Reactivity Chemical stability : The product is stable. Possibility of hazardous : Under normal conditions of storage and use, hazardous reactions will not occur. reactions Hazardous polymerization : Under normal conditions of storage and use, hazardous polymerization will not occur. Conditions to avoid : No specific data. Materials to avoid : Reactive or incompatible with the following materials: oxidizing materials, metals and alkalis. Hazardous decomposition : Under normal conditions of storage and use, hazardous decomposition products should products not be produced. Conditions of reactivity : Slightly flammable in the presence of the following materials or conditions: open flames, sparks and static discharge and heat. 12/16/2011. 488160 4/7 XLO-5 11 . Toxicological information Acute toxicity Product/ingredient name Result Species Dose Exposure 2-Dibutylaminoethanol LD50 Dermal Rabbit 1680 uL/kg - LD50 Oral Rat 1070 mg/kg - Chronic toxicity Remarks 1) Ferric sulfate Not available. 2)2-Dibutylaminoethanol Not available. 3) Ethoxylated oleyl amine Not available. 12 . Ecological information Aquatic ecotoxicity Product/ingredient name Result Species Exposure Ferric sulfate Acute LC50 28 mg/L Fresh water Fish-Brown trout-Salmo trutta- 4 days Fingerling-30 g 2-Dibutylaminoethanol Acute EC50 73.7 mg/L Fresh Daphnia-Water flea- Daphnia 48 hours water magna-<24 hours Conclusion/Summary : Not available. Biodegradability Conclusion/Summary : Not available. 13. Disposal considerations Waste disposal : The generation of waste should be avoided or minimized wherever possible. Empty containers or liners may retain some product residues. This material and its container must be disposed of in a safe way. Dispose of surplus and non-recyclable products via a licensed waste disposal contractor. Disposal of this product, solutions and any by- products should at all times comply with the requirements of environmental protection and waste disposal legislation and any regional local authority requirements. Avoid dispersal of spilled material and runoff and contact with soil, waterways, drains and sewers. Disposal should be in accordance with applicable regional, national and local laws and regulations. Refer to Section 7: HANDLING AND STORAGE and Section 8: EXPOSURE CONTROLS/PERSONAL PROTECTION for additional handling information and protection of employees. 14 . Transport information Regulatory UN number Proper shipping Classes PG* Label Additional information name information DOT Classification UN2922 CORROSIVE LIQUID, 8 (6.1) III - TOXIC, N.O.S. Alts (Contains: Ferric sulfate, 2- Dibutylaminoethanol) fi 12/16/2011. 488160 5/7 XL O-5 14 . Transport information TDG Classification UN2922 CORROSIVE LIQUID, 8(6.1) III Ak - TOXIC, N.O.S. (Contains: Ferric a sulfate, 2- Dibutylaminoethanol) IMDG Class UN2922 CORROSIVE LIQUID, 8 (6.1) III Emergency TOXIC, N.O.S. Atkschedules(EmS1 (Contains: Ferric , F-A, S-B sulfate, 2- Dibutylaminoethanol) IATA-DGR Class UN2922 CORROSIVE LIQUID, 8(6.1) III - TOXIC, N.O.S. (Contains: Ferric sulfate, 2- Dibutylaminoethanol) PG* : Packing group DOT Reportable Ferric sulfate, 168 gal of this product. Quantity Marine pollutant Not applicable. North America NAERG : 154 :a 15 . Regulatory information HCS Classification : Corrosive material Target organ effects U.S. Federal regulations : United States inventory(TSCA 8b): All components are listed or exempted. SARA 302/304/311/312 extremely hazardous substances: No products were found. SARA 302/304 emergency planning and notification: No products were found. SARA 302/304/311/312 hazardous chemicals: 2-dibutylaminoethanol; diiron tris(sulphate) SARA 311/312 MSDS distribution -chemical inventory-hazard identification: XLO- 5: Immediate (acute) health hazard CERCLA: Hazardous substances.: diiron tris(sulphate): 1000 lbs. (454 kg); Clean Water Act(CWA)307: No products were found. Clean Water Act(CWA)311: diiron tris(sulphate) Clean Air Act(CAA) 112 regulated flammable substances: No products were found. Clean Air Act(CAA) 112 regulated toxic substances: No products were found. Clean Air Act Section 112(b) Hazardous Air Pollutants(HAPs) : Not listed United States inventory : All components are listed or exempted. (TSCA 8b) Canada WHMIS(Canada) : Class D-1 B: Material causing immediate and serious toxic effects (Toxic). Class E: Corrosive material 12/16/2011. 488160 6/7 XL0-5 15 . Regulatory information Canada (CEPA DSL): : All components are listed or exempted. 16 . Other information Label requirements : CAUSES RESPIRATORY TRACT, EYE AND SKIN BURNS. MAY BE HARMFUL IF SWALLOWED. CONTAINS MATERIAL THAT MAY CAUSE TARGET ORGAN DAMAGE, BASED ON ANIMAL DATA. Hazardous Material • Information System (U.S.A.) Health Flammability O Physical hazards 0 Personal protection d Caution: HMIS®ratings are based on a 0-4 rating scale, with 0 representing minimal hazards or risks, and 4 representing significant hazards or risks Although HMIS®ratings are not required on MSDSs under 29 CFR 1910.1200, the preparer may choose to provide them. HMIS®ratings are to be used with a fully implemented HMIS®program. HMIS®is a registered mark of the National Paint& Coatings Association (NPCA). HMIS® materials may be purchased exclusively from J. J. Keller(800) 327-6868. The customer is responsible for determining the PPE code for this material. National Fire Protection • Association (U.S.A.) Flammability Health ♦O Instability Special Date of printing : 12/16/2011. V Indicates information that has changed from previously issued version. Notice to reader NOTE: The information on this MSDS is based on data which is considered to be accurate. Baker Hughes, however, makes no guarantees or warranty, either expressed or implied of the accuracy or completeness of this information. The conditions or methods of handling, storage, use and disposal of the product are beyond our control and may be beyond our knowledge. For this and other reasons,we do not assume responsibility and expressly disclaim liability for loss, damage or expense arising out of or in any way connected with the handling, storage, use or disposal of this product. This MSDS was prepared and is to be used for this product. 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VZ-8,934 Bre . .\A.111/klAi ' orm R-86�03LT2= •— — — '� =-1-86-03LT2PB e ° BR-86-03RD = --42-12RD / -9,548 e B 86-03LT1 PB TYST86-t TYST42-02 €BR-86-03 a BR-42-18 -8,842 -9,457 • R-42-30 -9,095 BR-86-08 -9,184 / ot 2-40 •�� / BR-42-10 t-42 ' o / 9,179 BR-42-31 441. -9,599 BR-42-16 p -8,787 •. PB AN AN- o 1 000 FEET AN-11 PETRA 4/1/201411:14:19 AM \ 0.\Alaska\Appl\Petra\P ojects\GRANITE POI T\OVERLAY\GRANITE POINT.OVL Schwartz, Guy L (DOA) From: Wallace, Chris D(DOA) Sent Monday,April 14, 2014 1:08 PM To: Schwartz,Guy L(DOA) Subject: Fwd:GP State(Bruce) 18742 30 PTD 1780730 Sundry 314-219 Guy, This relates to the sundry you have in hand for Hilcorp and addresses my questions adequately. Regards, Chris Original message From: Daniel Taylor Date:04/14/2014 2:14 PM(GMT-07:00) To: "Wallace, Chris D (DOA)" Cc: "Ferguson,Victoria L (DOA)" Subject: RE: GP State(Bruce) 18742 30 PTD 1780730 Sundry 314-219 Chris, I apologize for taking a bit to get back to you sir. • The frac fluid is weathered crude oil coming directly from Granite Point field and is not associated in any way with the below listed CAS numbers. • The StimPlan model has generated a maximum anticipated surface treating pressure for both the C-8 and C-7 sands. The C-8 MSTP is 7,121psi and the C-7 is 6,763 (pg 52 &65 of Sundry application). I apologize for what I see as a typo. The'r8,000psi was generated from rounding up. The pop off was stated to be set at 10,500psi because of the complications associated with popping off prior to the flush. If it is observed that we are climbing over the previously modeled STP then we will need to re-evaluate our frac procedure, stage design, and contact AOGCC. For the same reason all surface connections are rated to 15kpsi. • The IA pop off valve will be set at 2,500psi. Thank you sir. Regards, Dan Taylor Operations Engineer Hilcorp Alaska, LLC. 0: 907-777-8319 C: 907-947-8051 From: Wallace, Chris D(DOA) (mailto:chris.wallace@alaska.gov) Sent: Wednesday,April 09, 2014 2:29 PM To: Daniel Taylor Cc: Ferguson, Victoria L(DOA) Subject: GP State(Bruce) 18742 30 PTD 1780730 Sundry 314-219 1 Dan, We are processing the Sundry application for hydraulic fracturing and I have a few questions for your clarification. 1. The frac fluid appears to state weathered oil but no MSDS is received for the fluid. Please clarify that this is not diesel and does not contain Chemical Abstract Numbers(CASRNs)68334-30-5, 68476-34-6,68476-30-2, 68476-31-3, 8008-20-6, or 68410-00-4, and is not referred to as "diesel fuel" in its primary name or common synonyms. 2. Section A)14.e)shows an anticipated maximum treating pressure of 8000 psi(surface pressure). Section D) calls for a pressure relief valve that must be installed on surface lines to limit pressure to(a)14(E). The frac simulation provided has a maximum surface pressure stated of 6763 psi. Whereas in the provided procedure at 7.f.it states the max surface treating pressure of 7,615 and at procedure 7.g.and 15.g.the surface line nitrogen pop off is to be set at 10,500 psi? Please clarify why the pop off is not set at the 8000 psi level or lower? 3. At procedure 7. d. iii. and 15.d. iii. It states you are to set inner annulus pop off valve—what is the set point on this? From previous emails on other wells I have a statement from Reid Edwards relating to using platform crude oil that I copy here for our well records "The use of lease oil as a base fluid for hydraulic fracture treatment in the oil bearing Tyonek interval in well Granite Point 18742 24RD is based on reservoir impairment concerns. The introduction of water to this reservoir has been shown through both production and core data to drastically decrease its permeability. This phenomenon is due to extreme water wetness of the rock and has been shown to reduce permeability by a factor 10. Previous fracture stimulations completed in this reservoir used water based fluids and showed no increase in production. It is expected that the water based fluid used for fracturing caused damage during the treatment. The use of an oil based fluid is expected to yield positive results as the oil is both native to the reservoir and is a non-damaging fluid based on relative permeability tests." Thanks and Regards, g , Chris Wallace Sr. Petroleum Engineer Alaska Oil and Gas Conservation Commission 333 West 7th Avenue Anchorage,AK 99501 (907)793-1250(phone) (907) 276-7542 (fax) chris.wallacePalaska.gov 2 Wallace, Chris D (DOA) From: Wallace, Chris D (DOA) Sent: WednesdaY, April 09, 2014 2:29 PM To: 'dtaylor@hilcorp.com' Cc: Ferguson,Victoria L(DOA) Subject: GP State(Bruce) 18742 30 PTD 1780730 Sundry 314-219 Dan, We are processing the Sundry application for hydraulic fracturing and I have a few questions for your clarification. 1. The frac fluid appears to state weathered oil but no MSDS is received for the fluid. Please clarify that this is not diesel and does not contain Chemical Abstract Numbers(CASRNs) 68334-30-5, 68476-34-6, 68476-30-2, 68476-31-3, 8008-20-6, or 68410-00-4,and is not referred to as "diesel fuel" in its primary name or common synonyms. 2. Section A)14.e)shows an anticipated maximum treating pressure of 8000 psi (surface pressure). Section D)calls for a pressure relief valve that must be installed on surface lines to limit pressure to(a)14(E). The frac simulation provided has a maximum surface pressure stated of 6763 psi. Whereas in the provided procedure at 7.f. it states the max surface treating pressure of 7,615 and at procedure 7.g. and 15.g.the surface line nitrogen pop off is to be set at 10,500 psi? Please clarify why the pop off is not set at the 8000 psi level or lower? 3. At procedure 7.d. iii.and 15. d. iii. It states you are to set inner annulus pop off valve—what is the set point on this? From previous emails on other wells I have a statement from Reid Edwards relating to using platform crude oil that I copy here for our well records "The use of lease oil as a base fluid for hydraulic fracture treatment in the oil bearing Tyonek interval in well Granite Point 18742 24RD is based on reservoir impairment concerns. The introduction of water to this reservoir has been shown through both production and core data to drastically decrease its permeability. This phenomenon is due to extreme water wetness of the rock and has been shown to reduce permeability by a factor 10. Previous fracture stimulations completed in this reservoir used water based fluids and showed no increase in production. It is expected that the water based fluid used for fracturing caused damage during the treatment. The use of an oil based fluid is expected to yield positive results as the oil is both native to the reservoir and is a non-damaging fluid based on relative permeability tests." Thanks and Regards, Chris Wallace Sr.Petroleum Engineer Alaska Oil and Gas Conservation Commission 333 West 7th Avenue Anchorage,AK 99501 (907)793-1250(phone) (907)276-7542(fax) chris.wallace@alaska.gov 1 ®F B ,, , \l/- .,,,,, THE STATE ' E1:>= "' `:i f H 7----,-,:: ;_ :_ 333 West Seventh Avenue ,', GovERNoR SEAN PARNELI. Anchorage Alaska99501 3572OWt F �nliX727° 1433As i;>: 9u .2,5.%x22 NEa A�G 0� 201 Dan Taylor SLp,N Operations Engineer Hilcorp Alaska, LLC ! 1 e4 --. ° V 3800 Centerpoint Drive, Suite 1400 Anchorage, AK 99503 Re: Granite Point Field, Middle Kenai Oil Pool, Granite Pt St(Bruce) 18742 30 Sundry Number: 314-198 Dear Mr. Taylor: Enclosed is the approved application for sundry approval relating to the above referenced well. Please note the conditions of approval set out in the enclosed form. As provided in AS 31.05.080, within 20 days after written notice of this decision, or such further time as the AOGCC grants for good cause shown, a person affected by it may file with the AOGCC an application for reconsideration. A request for reconsideration is considered timely if it is received by 4:30 PM on the 23rd day following the date of this letter, or the next working day if the 23rd day falls on a holiday or weekend. Sincerely, 1 Ft-74,- Cathy P. oerster Chair DATED this lb da of f April, 2014. Encl. , • RECEIVED • MAR 2 8 2014 STATE OF ALASKA ALASKA OIL AND GAS CONSERVATION COMMISSION AOGCC APPLICATION FOR SUNDRY APPROVALS l� • -----. 20 AAC 25.280 1.Type of Request: Abandon❑ Plug for Redrill❑ Perforate New Pool 0 Repair Well 0 Change Approved Program 0 Suspend 0 Plug Perforations 0 Perforate❑ Pull Tubing 0 I/A, Time Extension 0 Operations Shutdown 0 Re-enter Susp.Well 0 Stimulate❑ Alter Casing Ijp Other. Install Expandable Liner I] 2.Operator Name: 4.Current Well Class: 5.Permit to Drill Number. Hilcorp Alaska,LLC Exploratory 0 Development 0 • 178-073 • 3.Address: 3800 Centerpoint Drive,Suite 1400 Stratigraphic 0 Service ❑ 6.API Number Anchorage,AK 99503 50-733-20322-00. 7.If perforating: 8.Well Name and Number. What Regulation or Conservation Order governs well spacing in this pool? N/A Will planned perforations require a spacing exception? Yes 0 No 0 Granite Pt St(Bruce)18742 30 • 9.Property Designation(Lease Number): 10.Field/Pool(s): ADL0018742 ' Granite Pt Field/Middle Kenai Oil Pool • 11. PRESENT WELL CONDITION SUMMARY Total Depth MD(ft): Total Depth TVD(ft): Effective Depth MD(ft): Effective Depth TVD(ft): Plugs(measured): Junk(measured): 9,931 ' 9,467 8,513' N/A 8,513'(fill)• Casing Length Size MD TVD Burst Collapse Structural Conductor Surface 596' 20" 596' 595' • Intermediate 4,516' 13-3/8" 4,516' 4,507' 2,730 psi 1,130 psi • Production 9,927' 9-5/8" 9,927' 9,463' 5,750 psi 3,090 psi - Liner Perforation Depth MD(ft): Perforation Depth TVD(ft): Tubing Size: Tubing Grade: Tubing MD(ft): See Schematic• See Schematic 2-7/8"&3-1/2"dual 6.34#/L-80&9.2#/N-80 8,486'&8,470' Packers and SSSV Type: Packers and SSSV MD(ft)and TVD(ft): N/A and N/A N/A and N/A 12.Attachments: Description Summary of Proposal 9 13.Well Class after proposed work: Detailed Operations Program 0 BOP Sketch 0 Exploratory 0 Stratigraphic 0 Development 0 i Service 0 14.Estimated Date for 15.Well Status after proposed work: 4/15/2014 Commencing Operations: Oil 0• Gas 0 WDSPL 0 Suspended 0 16.Verbal Approval: Date: WINJ 0 GINJ 0 WAG 0 Abandoned 0 Commission Representative: GSTOR 0 SPLUG 0 17.I hereby certify that the foregoing is true and correct to the best of my knowledge. Contact Dan Taylor Email dtaylorahilcorp.com Printed Name Dan Taylor 4-7-#4:7Title Operations Engineer Signatur�" 4/i OSP e (907)777-8319 Date 3/28/2014 COMMISSION USE ONLY Conditions of approval: Notify Commission so that a representative may witness Sundry Number: _// •3V�— \C� Plug Integrity 0 BOP Test L7 Mechanical Integrity Test 0 Location Clearance 0 Other: * 3oOo pit See --., - - / RBDA4 MAY 1 0 2014 Spacing Exception Required? Yes 0 No 17( Subsequent Form Required: /Q —L/O I APPROVED BY Approved by: i ,---- COMMISSIONER THE COMMISSION Date: 4.-/ —( 11 �►I�,y . Y�•r'-( rVylwlic� A- Submit Form and Form 10-403(Revised 10/2012) Ap eRplIiCaf1/�1 a�pil o'12 months from the date of approval. Attachments in Duplicate 11 Well Prognosis Well: Br 30-42 Hi!corp Alaska,LI) Date:03/28/14 Well Name: GRANITE PT ST 18742#30 API Number: 50-733-203-22 Current Status: Oil Producer Leg: 3 Estimated Start Date: April 15,2014 Rig: Moncla 301 Reg.Approval Reqd? N/A Date Reg.Approval Rec: Regulatory Contact: Juanita Lovett 777-8332 Permit to Drill Number: 178-073 First Call Engineer: Dan Taylor (907) 777-8319(0) (907)947-8051 (M) Second Call Engineer: Reid Edwards (907)777-8421 (0) AFE Number: Current Bottom Hole Pressure: — 1,600 psi at 8,775ft TVD Based on slick line fluid level tag at 4,291ft TVD on 3/11/13. Maximum Expected BHP: — 1,600 psi at 8,775ft TVD Based on slick line fluid level tag at 4,291ft TVD on 3/11/13. Max.Allowable Surface Pressure: — 0 psi Based on 2/3 gas filled and 1/3 fluid filled well with 0.1psi/ft gas and 0.35psi/ft diesel to 8,775ft TVD Brief Well Summary This well was drilled and completed as a dual string Jet Pump lifted oil well in the Tyonek C2 though C8 intervals. Br 30-42 is - currently on-line producing+/-80bpd. The recompletion plan is to pull the current completion,clean out the well to TD utilizing 3%KCL as our work over fluid, insert a expandable liner over the C6—C8 zones(+/-700ft). An additional Sundry will be submitted in order to hydraulically frac the ---- C7 C7 and C8 zones and complete with a packerless ESP completion. Procedure 1. Reverse out Jet Pump 2. Bleed well off/shoot fluid levels on back side(s-line fluid level found at 4,320ft MD on 3/11/13 after 12hr shut-in). 3. Use 3% KCI to circulate dirty oil out of well bore down long string and up short string until clean. a. Total tubing volume+/-106bbls. 4. Rig up slick line and run in hole with standing valve pulling tool and remove standing valve. 5. Shut in short string, pump down long string and circulate out oil until clean returns. ' a. Total annular volume to Jet Pump BHA+/-452bbls. b. Total BHP with 3%KCL to surface+/-4,184psi. 6. Nipple up BOPE. a. Function test BOPE(notify AOGCC of test 48hrs prior to expected test). 7. Install back pressure valve. 8. Install 3-1/2in and 2-7/8in test joint. 9. Fill stack with filtered inlet water and remove air throughout BOP. 10. Test BOPE (chart each test for 5min): a. Test BOPE 250psi low and 3,000psi high and chart. b. Remove 3-1/2in and 2-7/8in test joint. Install blanked and ported 2-7/8in test joint and test 250psi low, 3,000psi high. Install blanked and ported 3-1/2in test joint and test 250psi low, 3,000psi high. 11. Test annular preventer 250psi low,2,500psi high and chart. • 12. Perform blind ram test. ' 13. Perform accumulator unit test. 14. Remove test plug. 15. Pick up on short string (3-1/2in)side of hanger and pull to floor(Dry wt. 78klbs) 16. Rig up slick line and run in hole on short string (3-1/2in Buttress w/ID=2.992in)to+/-8,470ft to establish deepest possible cut. a. Pull out of hole with gauge ring and run in hole with e-line jet cutter. i. Cut 3-1/2in tubing at preferred depth of+/-8,470ft on top of 2-3/8in cross over. ii. Pull out of hole with wireline. 17. Pull out of hole with short string 3-1/2in tubing and lay down the same. Well Prognosis Well: Br 30-42 Hi'cora Alaska,LL Date:03/28/14 18. Pick up and pull out of hole with longs string hanger and long string 2-7/8in tubing and 2-1/2in Jet Pump bottom hole assembly and lay down the same(Dry wt.55klbs). 19. Rig up and run in hole with s-line bailer assembly. a. Tag and sample fill. 20. Pick up 9-5/8"471b/ft test packer and trip in hole to+/-8,000ft. Test casing to 2,000psi and chart 30min. 21. Pick up and run in hole with: a. 8.5in bladed mill. b. 2 X 9-5/8in 47lb/ft String Mills spaced out(split mill and string mills into two runs if drag dictates). c. Clean out fill to+/-9,850ft(+1-1,300ft of sand/fill). i. May have to spot time delayed LCM to maintain returns to surface. 22. Rig up wire line and run in hole with CCL/GR/Temp/CBL log and log from+/-9,850ft to top of cement. 23. Pick up and run in hole with 9-5/8in 47lb/ft Expandable liner and place from+/-9,150ft to+/-9,850ft(Total post expansion length of 700ft). 24. Additional application for Sundry approval will be submitted for Hydraulic Fracture and completion. / Attachments: 1. As-built Well Schematic 2. Proposed Well Schematic Bruce Platform • 14 SCHEMATIC Well No. BR 30-42 IlileorpAlaska.LLC Actual Completion 2/28/94 CASING DETAIL API #50-733-20322-00 Size WT Grade Conn ID Top Btm RKB to TBG Head =42.2' 1 20" 94# 19.124" Surface 596' ilmlir 13-3/8" 54.5,61, K-55,N-80 Buttress 12.347" Surface 4,516' 68&72 &5-80 N-80&S- 9-5/8" 40&4795 Buttress 8.681" Surface 9,927' TUBING DETAIL Long String 2-7/8" 6.4# L-80 Buttress 2.441" 43' 8,486' L L Short String 3-1/2" 9.2# L-80 Buttress 2.992" 43' 8,470' JEWELRY DETAIL No Depth ID OD Item Long String 42.2' Tubing Hanger,CIW,11",5M,Split Hanger 1 43' 1 2.441 3.5 X-over,2-7/8"BTC x 3-1/2"BTC(only 0.38'long) 2 8,486' 2.441 3.06 X-over,2-7/8"EUE x 2-7/8"BTC(only 1.1'long) 3 8,487' 2.25 5.625 Kobe,2-1/2" Dbl.'B'cavity SN 94-2-18(20'long) 4 8,507' 2.441 3.06 X-over,2-7/8"BTC x 2-7/8"EUE(1'long) G' 5 8,508' 2.441 2.875 1 Joint,2-7/8",6.4#,L-80,BTC tubing 6 8,539' 2.441 4.25 Re-Entry Guide-Bottom @ 8,540' Short String A A 8,470' 1.995 3.5 X-over,2-3/8"BTC x 3-1/2"BTC(2'long) B B 8,472' 1.995 . 2.375 Pup,2-3/8",4.6#,N-80,Buttress x 5.4'long 2 Er I C C 8,477' 1.375 2.375 X-over,1-1/4"10 rd EUE x 2-3/8"BTC(2'long) ` 3 NOTE:Long String measurement is 7.7'longer than the short string!I i. - I 4 PERFORATION DETAIL _Zone Top(MD) Btm(MD) Top(TVD) Btm(TVD) Amt spf Comments Date 5 2-1/8"Slimkone C-2 8,524' 8,562' 8,192' 8,223' 38' 4 Hollow Carrier 2/4/1979 - 6 y C-3 8,638' 8,730' 8,285' 8,359' 92' 8 2-1/8"Silver Jet 4/14/1994 TOF @ 8,513' __ C-5 8,916' 8,984' 8,511' 8,569' 68' 8 2-1/8"Silver Jet 4/14/1994 • C-6 8,994' 9,014' 8,578' 8,596' 20' 8 2-1/8"Silver Jet 4/14/1994 C-6 9,210' 9,222' 8,772' 8,784' 12' 4 2-1/8"Silver Jet 4/14/1994 C-7 9,317' 9,341' 8,872' 8,895' 24' 8 2-1/8"Silver Jet 4/14/1994 I. _C-7 _ 9,380' 9,406' 8,932' 8,956' 26' 8 2-1/8"Silver Jet 4/14/1994 * _ C-7 9,470' 9,508' 9,018' 9,054' 38' 8 2-1/8"Silver Jet 4/14/1994 C-7 9,518' 9,552' 9,064' 9,097' 34' _ 8 2-1/8"Silver Jet 4/14/1994 'N' C-7 9,590' 9,600' 9,133' 9,143' 10' 8 2-1/8"Silver Jet 4/14/1994 • C-7 9,604' 9,610' 9,147' 9,153' 6' 8 2-1/8"Silver Jet 4/14/1994 O C-8 9,684' 9,716' 9,225' 9,256' 32' 8 2-1/8"Silver Jet 4/14/1994 2-1/8"Slimkone • C-8 9,758' 9,820' 9,297' 9,358' 62' 4 Hollow Carrier 2/2/1979 0 5/26/2012-Tag fill @ 8,513'with 1-3/4"Dump Bailer M w • PBTD=9,880' MD (9,416'TVD) ,g, fir` Via. TD=9,931' MD(9,467'TVD) Revised By TDF 12/7/2012 Bruce Platform PROPOSED WeII No. BR 30-42 • IlilcorpAlaska.LLC Completion: Future API#50-733-20322-00 RKB to TBG Head =42.2' CASING DETAIL Size WT Grade Conn ID Top Btm 20" 94# - 19.124" Surface 596' 13-3/8" 54.5,61, K-55,N-80 Buttress 12.347" Surface 4,516' 68&72 &5-80 9-5/8" 40&47 N-80&S- Buttress 8.681" Surface 9,927' L L PERFORATION DETAIL Top Btm Top Btm Zone (MD) (MD) (TVD) (TVD) Amt spf Comments Date 2-1/8"Slimkone C-2 8,524' 8,562' 8,192' 8,223' 38' 4 Hollow Carrier 2/4/1979 C-3 8,638' 8,730' 8,285' 8,359' 92' 8 2-1/8"Silver Jet 4/14/1994 C-5 8,916' 8,984' 8,511' 8,569' 68' 8 2-1/8"Silver Jet 4/14/1994 _ C-6 8,994' 9,014' 8,578' 8,596' 20' 8 2-1/8"Silver Jet 4/14/1994 C-6 9,210' 9,222' 8,772' 8,784' 12' 4 2-1/8"Silver Jet 4/14/1994 _C-7 9,317' 9,341' 8,872' 8,895' 24' 8 2-1/8"Silver Jet 4/14/1994 C-7 9,380' 9,406' 8,932' 8,956' 26' 8 2-1/8"Silver Jet 4/14/1994 C-7 9,470' 9,508' 9,018' 9,054' 38' 8 2-1/8"Silver Jet 4/14/1994 Exp Liner C-7 9,518' _ 9,552' 9,064' 9,097' 34' 8 2-1/8"Silver Jet 4/14/1994 ±9,150'-±9,850' C-7 9,590' 9,600' 9,133' 9,143' 10' 8 2-1/8"Silver Jet 4/14/1994 NA C-7 9,604' 9,610' 9,147' 9,153' 6' 8 2-1/8"Silver Jet 4/14/1994 C-8 9,684' 9,716' 9,225' 9,256' 32' 8 2-1/8"Silver Jet 4/14/1994 2-1/8"Slimkone C-8 9,758' 9,820' 9,297' 9,358' 62' 4 Hollow Carrier 2/2/1979 PBTD=9,880' MD (9,416'TVD) TD=9,931' MD(9,467'TVD) Updated by: JLL 03/26/14 Bruce Platform BOP Stack Moneta n1k..T Al..kL 03/10/2014 0 111,1111111-11 fIl 411-1 asa' • r Hydril cr Hyde t Ili lil Ili 111111 1 ill 1111II III 181 I ' 2 7111 3/8-3%Dual Flex rams 4/114 _-' _I 5/8-5000 � 13� � ,. Blind i rttl rttirftl if1 2.00' Xtrt 111 �}l I�� _ �; { o � 3 1/8 5M valves and KIII A61i1.NIL111.111° I �'®' 1111II 11111 IS CIW-l) 283' al 135/8 SM 23/8-3;4 Cameron Flex rams `r(1rt7.1�111-1 rib rib .83' VU 4J1 Drill deck Riser 135/85M FEC 13 5/8 5M FE 10.00' 10.00' lit 1%1111 1111 III IV 111 111 1_11 Spacer spool 2.83' 13 5/8 5M FE 8115M FE 111 Ir>I di di 11i ,-.--. STATE OF ALASKA ~ ALASK/ IL AND GAS CONSERVATION CO. .,fiSSION REPORT OF SUNDRY WELL OPERATIONS 1. Operations performed: Operation shutdown __ Stimulate m Plugging m Perforate X__ Pull tubing Alter casing Repair well Pull tubing __ Other__ 2.UnocaIName of Operator 5. Type Development OfExp~orato~yWell: __X- 6. KB:Datum115'elevati°n (DF or KB) 3. Address Stmfigraphic ~ 7. Unit or Property name P.O. Box 196247 Anchorage, Alaska 99519-6247 Ser~ce Granite Point 4. Location of well at surface Leg #3, Conductor #8, Bruce platform 8. Well number 1951' FSL, 1976' FWL, Sec. 31, T11N, R11W, SM BR-30 At top of productive interval 0/~/~.~/$4L 9. Permit number/approval number 1061' FSL, 695' FWL, Sec. 31, T11 N, R11W, SM 78-73 At effective depth 10. APl number 50 -733-20322-00 At total depth 11. Field/Pool 615' FSL, 383' FWL, Sec. 31, T11 N, R11W, SM Granite Point/Middle Kenai feet 12. Present well condition summary Total depth: measured 9931 feet Plugs (measured) true vertical 9467 feet Effective depth: measured 9760 feet Junk (measured) true vertical 9299 feet Casing Length Size Cemented Measured depth Structural True vertical depth Conductor .. Surface 595' 20" To surface 595' 595' Intermediate 4469' 13-3/8" To surface 4516' 4500' Production 9882' 9-5/8" 1250 sx 9927' 9463' Liner Perforation depth: measured 8524-8562, 8638-8730, 8916-8984, 8994-9014,9210-9222, 9317-9341,9380-9406, 9470-9508, 9518-9552, 9590-9600, 9604-9610, 9684-9716, 9758-9820 13. true vertical 8192-8223, 8284-8358, 8513-8578, 8587-8604, 8772-8783, 8872-8895, 8931-8956, 9017-9054, 9063-9096, 9133-9143, 9147-9153, 9224-9256, 9297-9358 Tubing (size, grade, and measured depth) Long stdng: 2-7/8", 6.4#, L-80@ 8540' Short String: 3-1/2", 9.2#, N-80 @ 8499' Packers and SSSV (type and measured depth) Stimulation or cement squeeze summary Intervals treated (measured) Treatment description including volumes used and final pressure ~9~ Cas Cons. Commission Anchorage 14. Prior to well operation Representative Daily Average Production or Injection Data OiI-Bbl Gas-Mcf Water-Bbl Casing Pressure 129 56 22 65 Tubing Pressure 55 Subsequent to operation 200 105 92 NA NA 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. SignedC~ ~!~,~O~~~. -..- _ Title/~yl~'. '.j~[i/i~" Form 10-404 Rev 06/15/88 Date SUBMIT IN DUPLICATE Unocal North Americar~ Oil & Gas Division Unocal Corporation P.O. Box 190247 Anchorage, Alaska 99519-0247 Telephone (907) 276-7600 UNOCAL Alaska Region April 27, 1994 Mr. Steve McMains Statistical Technician Alaska Oil & Gas Conservation Commission 3001 Porcupine Drive Anchorage, Alaska 99501-3192 Dear Mr. McMains: This is to inform you that on April 14, 1994 well BR-30 on the Bruce platform (API# 50-733-20322-00) was perforated in the following intervals: BENCH TOP (MD) BOTTOM (MD) C3 8638 8730 C5 8916 8984 C6 8994 9014 C6 9210 9222 C7 9317 9341 C7 9380 9406 C7 9470 9508 C7 9518 9552 C7 9590 9600 C7 9604 9610 C8 9684 9716 Sincerelz Ralp P. Holman RECE]VED Anchorage .... STATE OF ALASKA --- t. ,SKA OIL AND GAS CONSERVATION CO~, _,ISSION APPLICATION FOR SUNDRY APPROVALS 1. Type of request: Abandon __ Suspend__ Operations shutdown __ Re-enter suspended well__ Alter casing ~ Repair well ~ Plugging __ Time extension~ Stimulate __ Change approved program ~ Pull tubing X_ Variance __ Perforate~ Other_ _ Type of Well: 6. Datum elevation (DF or KB) 2. Name of Operator 15. Development X_ UNION OIL COMPANY OF CALIFORNIA (UNOCAL) I F_.xp~oratory __ 3. Address Stratigraphio __ P.O. BOX 196247 ANCHORAGE, AK 99519 Senate ~ 115 KB 7. Unit or Property name GRANITE POINT , Location of well at surface 1951' FSL, 1976' FWL, Sec. 31, R11N, R11W, SM At top of productive interval 1061' FSL, 695' FWL, SEC. 31, T11 N, R11W, SM At effective depth PLATFORM BRUCE LEG #3, SLOT 8 At total depth 615' FSL, 383' FWL, Sec. 31, T11N, R11W, SM 8. Well number WELL #30 9. Permit number 10. APl number 50-133 -20322 11. Field/Pool GRANITE POINT feet 12. Present well condition summary Total depth: measured 9931' true vertical 9467' feet feet Plugs (measured) NONE Effective depth: measured 9760' true vertical feet Junk (measured) NONE feet Casing Length Size Structural Conductor Surface 549' 20" Intermediate 4469' 13-3/8" Production 9882' 9-5/8" Liner Perforation depth: measured Cemented Measured depth True vertical depth TO SURFACE 595' TO SURFACE 4516' TO 7748' W/1250 SX .9927' SEE A'FI'ACHED SCHEMATIC 595' 4500' 9463' R££I IV D true vertical FEB - 7 1994 Tubing (size, grade, and measured depth) DUAL 3-1/2", N-80, TO KOBE CAVITY AT 841~i~Sk~ 0il & (~aS ~,ons. C0mm~$$~011 TAIL PIPE RUN TO 8474' Anchorage Packers and SSSV (type and measured depth) N/A 13. Attachments Description summary of proposal_ _ Detailed operations programX_._ BOP sketch _ _ 14. Estimated date for commencing operation ~15. Status of well classification as: FEBRUARY 15, 1994 16. If proposal was verbally approved Oil X_ Gas __ Suspended ~ Name,of ap@rover ,~ Date approved Service 17. I/3here~ce t~__~~rue and correct to the best of my knowledge. 8 · Signed G. Russell Schmidt Title Drilling Manager Date FOR COMMISSION USE ONLY FEBRUARY 2, 1994 Conditions of approval: NoUfy Commission so representaUve may witness Plug Integrity __ BOP Test Location clearance Mechanical Integrity Test__ Subsequent form required 10- Original Signed By David W. Johnston Approved Copy Approved by the order of the Commission Form 10-403 Rev 06/15/88 Returned Commissioner Date SUBMIT IN TRIPLICATE TIME: BRUCE WELL #30 ADL 18742 PLAN OF PROCEDURE l · · · · · · · · 10. 11. 12. Kill the well with diesel taking returns to the production system. Install BPV's, remove tree. Install and test BOPE to 5000 psi with water. Establish that the pump cavity moves freely. Cut the short string just above the cavity. POOH with the short string. Visually inspect the tubing for possible re-use as the short string· POOH with the long string. Visually inspect the tubing for possible re-use as the short string. Pick up a new 2-1/2" TYPE "BB" Kobe cavity and RIH. Hydrotest and broach the long string (new 2-7/8") to 3500 psi, do not test the short string. Land the completion with the cavity at +/- 8500'. Land the short string with 20,000# added tension over the actual weight. Install the BPV's, remove the BOPE, Install and test the tree. Re-perforate with strip guns as directed by the asset group at a later date· 10 days RECEIVED FEB -? 1994 Alaska 0il & Gas Cons. Commission Anchorage P_erUnent Data: Spud Dat~: Surfooe Lo¢oUon: Subsurface Lo¢aUon: Devatlon: TD: PBO: Caring: PerforoUone: GRANITE POINT ADL 18742 WELL NO. 30 MIDDLE KENN SANDS PLATFORM BRUCE lCV2~/78 Le~ 3. Slot B. O.P. Platform Bruoe 1948' FSI.. 1975' ~ Sea. 31.1'11N. RllW. S.M. e15' ~ 383' FWL. Sea. 31. TllN. R11W. S.M. 115' KB-USL 0931' ~ 9487' 9880' ~ 9418' 20". 9~ B/H ~0 ~adng Nt at ~gS'. ~ent to lu~o~ 13 ~, 72, 68. 81 and ~.~. N-e0. K-~5 and g--BO ~lng g ~.. ~ and 47~, N-80 one S-9~ Caeing ~t at ~92~, ~t ~ ~' ~ 12~ ~ ~ C-2: 8~2~8582' ~-8: 068~716' 0-3; ~638-~7~' ~7~8-~820' C-5: 8~16-8684' C-6; 600~9014' C-7: 9317-9341' 9470-9~8' 6~18-9~2' Completion Record Long Stdng: 1. 0am~'~n Dual DCB Hangs" 2. 3 1/2" B~ttrele tubing 3. 3 1/2" Buttmae pup 4. 3 1~" B~ and But~ee XO ~. Ko~ 3" ~ 'B' c~ en--g84 6. 3 t~' Bursa and 8~ XO 7. 3 t~' Bu~e B. Mule eh~ Short Sb~ng: &. 3 1/2" Buttmea tubing b) 2 7/8 8RD emi 3 1/2" Buttrey. XO C. 2 7/~" 8RD pup (A~ run 817 BOPD. 88 BWPD. 418 MCI~ DIL 9914-..-4512', FIX:-OR 9921-6850' BHC--~Ia 0906--40t2' CSL--SIOH 9880-.7850' Oyro 9868-mJrfaoe Depth 43' 8385' 8302' 8303' 8411' 8412' 8473' 8474' 8383' a3a4, 8394' PBTDgB80' 1139931' [ 20". ~. CSA ~VS". 72. 68. 4518' 13524' 8562' 6638' ~7:~0' tl 8' 3984' 9994' 9014' 9317' 110° 0884' 9820' 47f CSA 9927' L. A. Darsow District Superintendent May 14, 1979 File: LAD-442-~F Mr. HoyleH. Hamilton, CcD1Aissioner Alaska Oil and Gas Conservation~ssion 3001 Porcupine Drive Anchorage, Alaska 99501 Amoco Production Company I ~ ."/~ ~,~^~'-~__.~ Post Office Box 779 Anchorage, Alaska 99510 Dear Mr. F~milton: Magnetic ~L0g. ging Tape Granite Point 18742 Well No. 30 Granite Point Field, Cook Inlet, Alaska Enclosed please find a copy of the magnetic logg~g tape of the subject well. For your information, the well was logged between 9934' and 4490' . Yours very truly, L. A. Darsc~ District Superintendent Attackm~nt AME:sls L. A. Darsow District Superintendent February 16, 1979. File: LAD-158-WF Mr. Hoyle H. Hamilton, Commissioner Alaska Oil & Gas ConserVation Commission 3001 Porcupine Drive' Anchorage,'Alaska 99501 Amoco Production Company j Post Office Box 779 Anchorage, Alaska 99510 907- 272-8471 FILE: Dear Mr. Hamilton: Completion RepOrt Granite Point '18742.Well No. 30' Platform Bruce~'Cook Inleti.Alaska Attached'please. findthe"State'Of Alaska'FormNo. P-7Well Completion or RecOmpletionReport and Log on.the Completion of'drillingGranite'Point 18742 Well No. 30'. Included'is a copy of.the ChrOnological history and directional survey'for theabove referenCed'well. The Open'hole logs have already.been'forwarded to'your office by Schlumberger'Offshore SerVices~ Yours very truly, L. A. Darsow District Superintendent Attachments MJN:sls Form ' SUBMIT IN DU'~.~CATE* STATE OF ALASKA (Seeother st ructions on reverse sideI OIL AND GAS CONSERVATION CO/iM~ITTEE WELL cOMPLETION OR RECOMPLETION REPORT AND LOG* b. TYPE OF COMPLETION: WELL OVER EN BACK RESVR. Other 2. NAME OF OPICRATOR Amoco Production Company ADDRESS OF OPERATOR P. 0. Box 779~ Anchorages'Alaska 99510 LOCATION OF WELL (Report location clearly and in accordance with apy State requirem6nts)* At~u~aceLeg 3, Slot 8, Granite Point Platform Bruce 1951' FSL, 1976' FWL, Sec, 31, TllN, RllW, S.M. At top prod. interval reported below 1060.8' FSL, 695.2' FWL, Sec. 31, TllN, RllW, S.M. At total dep~ 615' FSL, 383.2'.FWL, Sec. 31, TllN, RllW, S.M. 8524-8562' 8638-8730' 8916-8984' 8994-9014' 9317-9341' 13. DATE SPUDDED 10-28-78 ~. PRODUCING !N~VAL(S), OF ~IS COM~TIO~--~, BOSOM, N~E (D AND ~)* 8524' ~ - 8191"~D 9820' ~ - 9354' ~D. Middle Kenai Sand 24.'T~E E~CTRIC ~D OTH~ LOGS RUN . DIL~ FDC-GR, BHCjSon$C-Gr-Caliper ,, ~. CAS~G RE~ (Re~rt all strings set in well) '' C~shNG SIZE20" 1 'VEIGHT~B/FT' [ 944~/f ~ 54.5 · 9-5/8" ¢O&47#1ft. ' 26. LINER ~COD ~8. PErOrATiONS OP~ TO PRO~O~ ([ngerval size and number) 9380-9606 ~ 9684-9716 ~ Depths 9670-9508~ 9758'9820~ taken' from 9518-9552 ~ Son~c Log 0590-9600' 2-1/8" tbg 1/18/79 960~-9610~ gun .~ODUG~ION MEi:H&D (~lowh~g, ga~ lif~, pump~g~size an~ ~ype of pump) P~P~ng - Kobe 3" Type B DATZ OF T~ST, [~OUHS TES~ ]~tOXE SiZE ]PROD'N FOR OI~BBL. ~OW; WBING ICA~G PRBSU~ [CAL~~ OI~BBL. 110 817 I ~18 ' 31. D'ISPOSlTION O~ GAS (~old, U,ed for tuel, vented, etc.) 5. AP1 N~C. AL CODE 50-133-20322 LEASE DESIGNATION A/WD SERIAL NO. ADL 18742 7. IF INI)I~, ALLOTTEE OR TRIBE N.~dVIE 8.UNIT,FA/:UVI OR LEASE NAME Granite Point 18742 9. WELL NO. 3O 10. FIELD A,ND POOL, OR WILDCAT Granite Point-Middle Kena: 11. SEC., T., R., M., (BOTTOM I-IOT.I~, Sand OBJF. CTIVE) Sec. 31, TllN, RllW, S.M. 12. PERA-VIIT NO. 78-73 DATE FIRST PI~ODUCTION [%VELL STATUS (Producing or 2-5-79 [ ~,~u~-~n)Producing G2~S---1V~CF. WATEi~--BBL. ] GAS-OIL ~TIO 32. LI~T OF ATTACHMENTS Directional surveY.Report, Chronological. History Alaska Oil 3~. I hereb~ cert~ that th~oregoing and attached information is complete and correct as determined from SIGNED . ' % TITLE District Superintendent · DATE .February 16.~1979 s/.Z'o ! 5951' I 26" Cmt tO NS0,K5[ ~ 451,6' [17-1/2" Cmt ~o surface 580 [ [80,S9~ 992~.01~12.25" Cmt to 7748' w/1250 sx C ass G cmt 27. TUB~G ~C. OF~ SCR~ (MD) SIZE ~ DE~ SET (~D) [ PACI(ER SET (MD) I , 29. ACID, SHOT, F~CT~RE, C~IE:NT SQUw~E ~C. D~-i INT~v~ (MD) ~ AMOUN'C ;~D KIND OF M~?~AL US~ 1 ,[ 9931 ' 0 23. WAS DIRECTIONAL !SURVEY MADE Yes 14. DATE T.D. RE,AC~ 15: D'A'I'~' co'M,P- SUSr O~ ABANI). 16.' 1-17~79 ! 2-12-79 115 ' RKB-MSL INSTRUCTIONS General: This form is designed for submitting a complete arid correct well completion report end log on all types of lands and leases in Alaska. Item: 16: Indicate which elevation is used as reference (where not otherwise showr~) for depth measure- ments given in cther spaces on this form and in any attachmer'~ts Items 20, and 22:: If this well is completed for separatc, prcducti.on from more than one i,terval zone (multiple completion), so state ~n item 20, and in item 22 show the prcJuci~;g interval, or intervals, top(s), bottom(s) and name (S) (if any) for only the interv¢~l reported in item 30. Submit a separate report (page) on this form, adequately identified, for each additional interval to be seperately producert, show- ing the additional data pertinent to such interval. Item26: "Sacks Cement": Attached supplemental records for this well should show the details of any mul- tiple stage cementing and the location of the cementing tool. Item 28: Submit a separate completion report on this forrn for each interval to be separately produced. (See inslruction for items 20 and 22 above). 34. SUMMAH. Y OF FOi{MATION TESTS INCLUI)IN(; IN'I'EII{vAL TE,STED. PHE,'-~SI. JRE DATA AN'D ~COVE'RIES OF (,)IL. GAS, 35 G E]OI.,OG I C MARK~ WATEJI AND MUD _ NAIV~ MEAS. D~PTI{ r~:~U~ VI~T. A 6435 6290.5 B 6770 6710 C Unit 8305 8011 C-5 8770 8391 ., C-8 9645 9186 AN'a, lt~C~.l) ~tlOWS OF OIL. G~S O,R WA~I. . , , ........ ~f~'Pi~'~ T]b ~q--[R'E'POR'T F E BRU~CRY--I'3';I 979 ~-~-~q~-C'O'-PR0-D'O-CY-ibN-CO-,~PAi~Y .................................. PLA'TFOR'~'~RUCE -GP 18 7~2-30 .... ~YROS C'OD I C-'SURVEY ................................................................. 1 ~'50~GYM3-077 ..... ~DIIJS "OF'-~RV'~TURFMETHO'~-'OF ' COMPUTATTONS ................ K-~"~EV';--I ~'5-FT', ................ ~OMPUTED'-FOR 'SCi-ENTIFIC-DRILLING CONTROES-'BY F. M'-'~NDSEY AND 'ASSOCIATES' --'F~EA'S' ~ ..... D 2 IFT-VE~R T I CAi ........ S U B [~EP'TH' A ,,GEE- DEPTH ......... .SEA A-LC-CALCULATIONS PERFORMED--BY ..... I B --'T'~0 E DR IFl TOTAL COORDINATES ......... C l"-'0 S U R E DIREC .............................. DI STANCE 'DEG', 0 0-"----0- O-~-'0-0" -~ 105~'©0' N 0 ;0'0E 0 · O0 5 o ........ 0 .... 5 ....... 5'0-,-00 ........... ~54";~99 .... N 'o; O'O'E O. Oo zoo --o ....... 0 ............ ~dO';"o5 .......... .4'99 N O.O0'E ............... 0.00 ...... 1'5"0 .... O---b ....... i-5'0.0'0 .... ~5;0C N O.OOE ........... o.oo ...... ~ 6"5-~---~ ..... ~66'-;'56' ................ 9 ~" o o .... -~'--0 ;55 ~' ....... b-',- o o 25o~'6'-~6 .......24'9;-~'-9 ............. t~.~9 N- 8.5'5~ ..... 3 :o_ .... ......... ......... z_fA, .... -6-; 350 1 O 349,99 2~,99 N68.OOW 1,03 ~00 t 30 -' 399.97 ..... 294.97 N76.00W ..... 1.36 500 1 45 499,93 39g.93 NB3,50W 1,ES ......... 550 2__15 549,90 44a,q'O N85,50W 2,05 600 2 30 599,86 494.86 NU6.50w 2,1~ ..... 700 3_~.5 __5~9..7! ......... %9~;'71 .NSl.iOW 2.7~ 800 & 0 799.~8 69&o48 NT?.72N ~.OZ 9C0 4 0 899.23 794,23 NTT.35W 5,57 1CO0 .......... 1100 1200 1300 4 0 1298.23 I193.23 1400 ~ 4~- '-139~.00. 1293,00 .... ~¢0~ 3 45 ...... i497,79-- i392'79 1600 3 30 1597.58 ia92.58 ..... 1700 ? 15 _._1697.al 1592,41 1~-6~ .... 3 15 1797.25 1692,25 N7B.60W 11. N81,22~ 12, NSl,BSw 13, NS1,47W l~- NS2.08W ...... 1.5, _ s 7 3 ,.~ ....... ~ ~ · 4 0 998.99 893.99 N78, TOY,' 6.97 4 0 1098.75 ............. 993.75 N7 S-"~ ~'W .......... 8.48 ' , ................... --~ ..... ~ ..... ; .............. 7- ........... ,-,'- -, 15 1198.49 .0~3.49 NTT,gSw lv.08 54 6i 45 O~ S S 5 N ,,. UT'O-O'-W ............ 0-; 00 --'S 0'700"%7- ................. 0;50--5 ..... 6'"ob-W ......... 0-, oo..--w.. ........... 0,01 0,2.9 0,96 W ---i--.~-.W. 3,38 W 4,89 W 6,6~ W 8,69 W 14.11 w 20,75 w 27.57 W .. 34.39 ~8,21 _.. 55.25 61,91 68,38 74.63 _ _ 80.45 86,07 O,O0 S o-,'ou s ,j o 'o-~~ o..~o6 o.~ 6';-6'-5"--;S .... o '0' ....... U'-'~- ............ 'd';O00 ............... 0 '."c 0-, ~--i ...... ~ - 3 ~ 9 5-9 '--;~ ..... ~, o o 0 ............. ~;'o .-1 o.~ .... ~' 23 3¢'--~-0--~ ...... o;'~50 ............................. -o.2 DoG'-'-EEG s ........... SEVER I TY ..........SEC T I o ANGLE ........... D'EG/IOOFT .... D'I'STAN' D' ...... M ..... 0 0 ..... 0 w --0-';'0o0 .......... O 0 '~--'~' ........ 0 · C C 0 ...... -' ,' 1.41 N 42 57 12 W 0.500 2.42 N 55 34 7 W 1,OOO 3,77 N 63 Z+8 G7 W 0.500 1.5 5.24 N 68 57 19 ',N 0,214 2,5 6.94 N 72 49 2 W 1-OOO 3,7 8.97 N 75 50 10 w 0.500 5.2 14,38 N 78 50 ~8. W 1,250 9, 21.14 N 79 1 29 w 0,251 i3.~ 2~.ii-7~ ~8 39 ia'--W ........ 0-;o-2~ ......... i7.~ 35"6'~'-~ ..... 78 31 47"'i'~ .... %".09a ...... ~gJZ-'~'-~---~'-6 to D9 ~- .... o.z~o ............. ~o'~-~ ............................. 69.73 N 78 40 27 W O.Oal ~3.~ 76,05 N 78 55 20 W 0 ~50 ............ 81.9~ N 79 7 37 w 0.250 _ . 87.37 N 80 3 59 w ~.386 56.' A LL__CA L CU L AZI 0 N S .P ER F 0 RM ~0__BP_Y_:_I_~_ ~_. £ L E C _T_ LR_.iZB_I_C__.__C_.Q.~_'[~Jg !.. E R ................ ~'_ TRUE MEAS. DRIFT VERTICAL SUB DRIF;:f ........... ~;OTAE COORDINATES C L O 5 U R E S SEVERITY . DEPTH ANGLE D,_PTH SEA DIREC DISTANCE ANGLE DEG/10OFT DISTAN D H D,.G. 2100 3 45 2096.72 1991.72 S53.35W 6.06 N 2200 3 30 2196.52 2091.52 S53.75W 2.30 ......... ~..~ .... 33~....__22_~3.~ __2 !.9.1. ?33 .... S 57 · 1 ~_~_ ..........~ _~ ~ 5 ..... S 2500 3 30 2495.96 2390.95 S61.87W 7.4~ S 2600 3 30 2595.77 2490.77 S62.25w 10.30 S 101.38 W 101.56 N 86 3~ 35 '~ 0.250 7~.0 106.46 W t06.~9 N ~8 45 28 W 0.250 80.3 111.49 W lll,5.Q_..S 89.._24_..._.2~_w 0.205 .... _ ........... ~_6,~ 116.66 W 116.74 S 87 50 12 W 0.084 92.5 121.95 W 122.18 $ 86 30 29 W 0.206 98,5 127.35 w 127.76 S 85 22 30 W 0.023 I~.~ _2.~Op ..... A._30 ...... 2_7? 5.,.~,_. ...... 2690._42 2900 3 30 2895.2A 2790.2q. ...... 3000 ..... %_~p_ .... 2':)~5.?.0>~_X8_?o.o5 3100 3200 3300 3~+00 3500 3600 _3700 3~00 4000 41C:O '-,42 00 -/4~oo 4500 ~60,~. 4,700 3 30 3094.86 2989.86 3 45 3194.66 3089.66 3 45 3294.45 3189.45 3 30 3394.25 3289.25 S7~.52W 27.72 ._3 ~0. .3494.06 3389.06 S76.90W 29.22 ._ ...... 3_~5 ........ 3593.56 3488.86 580.2.~ ...... 30.47 A_. ~ 3693.63 3588.63 S77.63W 31.77 4 15 ...... 3793.37 .... 3588,37 578-2~ ....... 33,23 4 ~0 ._3893.08 3788.08 578.15W ........... 34.75 4 .30 3992.77 3887.77 S76.70W 36.45 5 0 4092.43 3987,43 S77-38W 3~,31 S 30 4291.5S 4186.59 S79.03W 42.21 5 45 43gi.ll 4286,I1 S78,77~ 44,09 5 45 4490.61 2385,61 S78,60W 46.06 ....... ........ 5 45 4590.10 4485,10 $BI-C2W 47.80 5 45 4689.60 4584,60 S75,23W 49.57 _ . 566.00W 15.48 $ 137.92 W 138.78 S 83 35 38 w 0.250 115.9 567.63W 17.88 S 143.53 W i4~.64 $ 82 53 45 W 0.100 121,7 S'6'~"~"02-~ ............. ~0,14 S 149,20 W 150,55 S 82 18 40 W 0,985 127,5 S70.38w 22.26 S ~54.93 W 155.52 S az "9 2. W 0.083 S73.'77W .... 2~.20 S i60-;'~9-~-~ 162.75 S aZ 25 47 W ...... 0;250 i39.2 ............................. S74.15~ 26.0t S 167.23 W 169.24 S 81 9 29 ~' 0-025 173.31 W 175.5j S 80 54 26 w 0.250 i50.% 179,23 W 181,60 S 80 44 17 w 0,145 i5o,~ 185.43 W 187.92 S 80 39 57 W 0,250 162,f 192,06 ~ 194,67 S 80 36 22 w 0.250 i67,~ 1Q9.?~%O_W.~ 201.86 S 80 31 24 W ......... 0,250 206,58 W 209,48 5 80 27 4 w 0,250 181,~ 214,24 W 217,32 S 80 20 31 w 0,!14 186.' ......... 222,31 W 225,58 S 80 13 15 W 0,5C0 231,02 ~ 234,51 S 80 6 33 W 0,250 203.~ .240,19 W 243e87 S ~0 1 57 W 0,251 2iI-~ 249,80 W 253,67 S 79 59 20 W 0.250 220.; 259,63 w 263,68 S 79 56 21 W 0,017 269,49 W 273,70 S 79 56 31 W 0,283 237,' ...... 279.35 W 283,72 S 79 56 15 W 0,320 .._ RECORD OF SURVEY ALL ..... ~"~ [.-~j-~-,~'¥ TRUE '-- '?.~-' ....................................... DOG __._M.[_A...S. DRIFT VERTICAL .......... SUB DRIFT. .............. ?OTAL C()ORD.IN.A. TES'- ...... C L 0 S U R E S SEVERITY ....... SECTiO DEPTH ANGLE DEPTH SEA DIREC DISTANCE AN~,L E DEG/!OOFT ..... DISTAN D ..... S ..................................... DEQ, D M S 4900 6 15 4888,50 4783,50 S82.93W 53.25 S 299,93 ........ 51OO 5_,.15 _50873.~.5 .... ~982.45 S61.22~ ........... 57.97 S ......... 3_19.70 5200 4 15 5187,11 5082,11 S45,93W 62,$7 S 326,~5 m~.~O0 6 ...... 1.5 ..... 5286,68 ......... 518!,$8 Slg,7~}~ .............. ~0.~9 .S ........ 5400 8 0 ~5385.91 5280,91 S18,40W :?~82.21 S 335,32 5500 9 15 5484,77 5379.77 519,05W 96,42 ._ 5600 10 0 -'5583o36 5478~36 S25.60W-' 111.88 5700 10 30 5681,77 5576,77 S27,20W 127,81 /~'58-00 lo .4_5 A.5760,05 5575,05 S33,22w ..... 143,74 5900. 11 15 5878,22 5773.22 .538.20W 159,23 6000 13 0 5975,9~ 5870. ~.~ S3°,95W 175,53 __~100 13 30 6073.32 5968,32 S43,45W ...... 192.64 _.. ~§200 1~ 3.0 a_6.170..,35 ...... 6065,35 S48,8p~ ................ 209.40 ..6300 16 30 ~ 6266,71 6161,71 S53,12W 226,22 6400. !8 0 6362.20 6257,20 552.57W _. 244,12 6500 . 6600 20 0 A6551,86 64a6,86 S41,55W 289,85 6700 21 3C 6645.37 6540,37 S42,42w 316.!~ 6800 22 ........ -~:~'0024 15 6829".~7 6724.87 S51.07W ......... 3'65.43 000 26 0A 6920,al 6815,al S58.3~ ...... 39~,15 7200 28 30 70~7.59 6992,59 S54,33W 445,49 .../~300 28 15 7185-58 .... 7080.58 549,55W 474,78 w7400 28 30 7273,57 7168,57 S50,22W 505.40 .................................... 7500 30 45 7360.49 7255,49 558,83W 534.06 ._ 9'7600 _ . _ 340,14 W 346,48 W 354,40 W . . 363,67 W 374~80-~W' 388 · 04 ~03 · 2'9 W 420,73 441.48 W 465,12 W _. 487,53 W 5O8,93 W ..... 532,63 559 -15 w 660.84 W ............................... 700.2~ W 737.65 774.00 ............ a~.21 861.06 w 304.62 S 79 55 55 W 0.25~ 315,28 S 79 59 37 W 0,251 324.92 S 79 43 17 ~ 0,767 332.35 S 79 5 39 W I,O0~+ 338,68 S 77 59 9 W 2,024 3~+5,25 S 76 13 23 W 1,750 353.54 S 74 i0 23 W 1.250 364,10 S 72 6 17 W 0,776 255,4 273,7 282.8 291.0 299.7 A3i :3,3 337.9 376,7~ S 70 lo 3 W 0,503 354,1 39t,05 S 68 25 59 W 0,326 ~371.5 407.22 S 66 58 56 W 0,535 3~9,9 425,90 S 65 39 34 W 1,752 4i0.5 446,94 S 64 27 59 w 0.535 469,96 $ 63 32 24 W 1.056 496,07 S 62 52 9 W 2.029 525,29 S 62 18 22 w 1,50i 555,05 S 61 26 ~i w 3,677 585.68 S 60 20 15 W 2,003 .. 019.~1 S 59 1~ 20 ~ 1.505 655.77 S 58 30 6 ~ 1~269 694,97"~-'57 59 6 m ........... 1.837 737,25-5 57 40 b2 W 1.859 782.63 S 57 36 20 W 2.195 829,94 S 57 32 '9 W 1.059 877.24 S 57 13 59 W 1,10O . _ 924.39 S 56 51 23 w 0,293 973,74 S 56 4~ 18 W 3.153 1026,46 S 57 1 13 W 3.22'~ .... ................................................................................... R ALL .._CALCULAT IONS _PERFORME ..... BY:._I _B .. M ELEC~.R,O.~N'I C__CC.,~PU TE R TRUE DEPTH._~,~m ~ DEPTH SEA D~REC DISTANCE ANG ..................... D __.M ................. DE G? .................................................................. 7900 37 ~5 7687.18 7582.18 .,.55_2,~_~0W-- .... 6.~5,_!9 S a¢00_...~0__30 .... 7764..15 ]~.59.75 _~.<1_00. 35 15 7g~3.65 7738.65 ~'~0 ..... 3-5 ....... 3-~"~--~'9-25. ~----~-20. 19 8305 35 23 90!0.68 7905.68 $50_._Q~]w ..... 6.74.40 S .... lP.~69_;9_2 ...... w ......1264..7_8 $ 57 46 S4_E..,..7..~_~__ 7.1 ~+,_.~3 ..S __.!.~.6--~.2_..._~ ............ !_325,5 3 S_ 57 23 S48.50W 752,69.. S ........ !.~..~.9~~],~ ......... .~.3,82.-.7_8 ..... S ..... 57._ 1 S42_,..3_9~ ....... 791.24 S ...... 12.0_~_~.0 .W ...!4a0.22 S_.56 40 S~7.75W 793.~8 S 1205.55 W 1~fi3.09 S 56 39 _~_~.500 34 30 8172.16 8067.16 S31,_8..~_.~ ........ 878.49 / .... S.7 op .... 3~.~_3_0_ %8_3~_~.,_.F.! ~.219.2 ~ ..... ~$.3 2 · 7 ~s.7.!. ~ o 8800 36 0 8414.85 8309.85 534,22W 1026.41 9100 25 0 8671.a~ 8566,4~ S23.85W 1161.74 ...... --~ Z'O 0 2-S ...... O-- S'7 S 2 · Z S .... ~-~ ~ ~. ~ ~ .... g S ~ ,b]W ...... ! ~ ~ 7. ~ S s .. 12.7~-~0 w ........ 1546.9.~ .... s 5_5 S 1304.37 ~ 1600.42 $ 54 S 1336.63 W 1655,.69 S 53 S 1369.27 W 1711,26 $ 53 S 1399,24 W 1763.92 S 52 S lZ+23.99 W 1811.55 $ 51 S la43.74 W 1853,11 S 51 S 1452.75 W 1890.51 $ 50 q30O 20 0 8g55.82 8750.82 534.70W 1227.2B __';_L~9~OO 18 .__0.__9_~50.37 ~845.37 __S_3.~..,.5~ ..... 1.254.75 95~0 16 o_ 9045.9? _~9.~0.~9 ...... 5~!_~g.~ ...... 1.277.50 OhO0 14 0 9142.58 9037.58 546.03W 1295,2~ 9645 13 13 9186.32 90~1o32 S49,65W 1303.33 ........................... 9700 12 15 9239.96 ~134.96 S54.08W 1310.52 9880 10 30 9416.35 9311.35 557.23W 1331.04 S 1584,99 ...... ~_~_?.3_!_!0 30 9.4.6.6..5.0 ~_16.I.,50 __55.Z__.~3'~ .... !336.07 S. !59__2.--_8_!_Zw 1482.87 W 1925.51 S 50 1501,82 W 1957.01 S 50 1520,17 W 19~5.68 S 49 1538.02 W 2011.40 S 1545.87 W 2021.98 S 1~55.~o w zo3~.09 s 2069.75 S ~9 2078.97 S 50 .......... _~E BRUAR.Y_I 3,19 Z 9_ ............ .......... DOG LEG "' --~'-- E S SEVERITY SECTIC L~ DEG/!OOFT DISTAN 9 23 35 49 29 49 I0 ~.i 21 7 57 52 51 52 55 . 58 0 21 W 3.856 m 1074.4 57 W 1.052 ~!131_,5 9 w 5 · 1 z 3 ....... !_9 W .......... 3 _._0 O0 iZ53,a 8 W 5.266 1315.2 29 ~ 0.116 26 W 4,296 143~-~ 23 ~ 4.306 i~57.C 48 W 2.149 ....... 15~0_.~ 21 W 1.805 ~1595,E 56 W 0.273 ~1652o~ 40 W 0.703 1709.[ . . _ 28 W 3.690 176Z.~ _. 7 ~.~ 2.426 .~ 12!0.~ "-~ 8--;'~ ............. ~-"'2-7 3 24 W 2.34~ 1893.~ 18 W 2.008 26 W 2.032 1985,( 33 W 2,020 20ii-~ 55 W 1.784 202.1.~ 38 ~' 1.801 203'+.( 4 z--w- ........ o. 75 3 ..... ~'-2o 38 w 1.251 2069.' 34 w O.CO0 ~2078.' AMD CO GP~3..0 ..... '_GYRO S_C_0.P_!_C~5 U...R..v_.E Y .... F..E~.RU. ARY ..... ,1~., lCj 7_~ TRUE CODE MEASURED VERTICAL TOTAL CO,.,Ru!.NATES C L 0 S U R E SUB NAi'4E DEPTH DEPTH D I S TA.f.'~ C.E ................... _ANGLE. .... _SEA D___ M ,S C-1 8905 8010'"68 ~93,18 S ~,~,,,5,55 W 1443,09 ..... S 55 39 26 v~ 7905 C-5 8770 8390,60 I012,00 S 1359,03 W 1694.43 S. 53 19 35 W. ~_2_85.60 _. C-7 9505 .......... 8860..,.52 .................. 122776~ ....... S ......... 1483.82 W 1927~,19 .......... S._,SQ 21 i w_ C-8 96fi5 ......... g!86,~2 ..... 1303,3~..__.S 15~5,B.Z._N ....... 202i,95 .... 5 ~9_ 51 55 '~ ..... ~D_81.32 .............. PB TD 9880 9~16,35 1331,0~ S 158~,99 W 2069,75 S ~9 58 3~ W ....... _~_}_.!_~,95 TD 9931 ...... ?~.66,.,.~0 ........... ~3~_,.0.~_..~ .......... 1592,81 W 2~?~.9~7 ......S..5_0 ..... O~ 9~ w 9351,~0_ __M, EASURED_DEPTH AND_0_THER DATA FOR EVERY EVEN 100 FEET OF SUB SEA .......................................... ~EBRUARY_13,1979 _ COORD[NATES ......................................... TRuE ..................... MEASURED ........... V.ER_T [ CAL SUG ..... MD-TVD ....... yERT ICAL ..................... DE.BT_H. DEPTH .SEA DIFFERENCE CORRECTION TOTAL . _ ............... 205. 305 ~O~ ............ 50.5 ................. 605 .................... _705 .................. 806 305. ._405. 505. __605. 705. 805. .......... 90 ......... I10 120 .................... 130 1~O 150 160 170 180 190 200 .. . 2108 220B 2309 . 2~09 2509 26Oa 27O9 281n 2910 3010 3110 3210 ..... 3311 3411 ....... 3511 3611 .............. 905. ............... IR05. i105. 1205. 1305. 1405. 1505. _ . 1605. 1705. 1805. 1905 2005 · 2105. 2205. 2305. 2405. 2505. 2605. 2705. 2805· 2905. 3005. 3105. 3205. 3305. _3405. 3505. 36C. 5. . - 100 O 200 O 300 ............. 0 ........................... 400 500 ........ 0 600 O 700 1 800 ........... 1 ........... 900 t000 1 1100 2 1200 2 1300 2 1400 2 . 1500 2 1600 3 1700 3 1800 2 1900 3 2000 3 2100 3 2200 4 2300 4 2400 4 2500 4 2600 4 2700 ............ 5 ................ 2800 5 . 2900 5 3000 5 . 3100 5 3200 6 3300.. 6 3400 5 0.00 N 0.70 N 1.40 N 1.90 N 2.21N ..... 2,83 N 4,ii N 5.62_.N '1.06 N 8.58 N I"' ~,19 N I1.6z~ N -- 12.80 N 13.76 N -_ la,67 N 15.50 N 14,89 N _ 12.78 N .................. 9. 9 r.,i .... .. 5.75 N ,,: · 01 N i.4~+ S _ 4.69 S 7.70 S 10.55 S 13,21 S 15.72 $ 18.12 S .. 2',-, · 36 S _ 22.46 S . 2~+. 39 5 26.20 S 27.90 $ ....... 29.38 S 30,, 6U L- O,CO 0.34 2.12 5.04 8.91 14,44 21.13 27.96 34.80 41,61 4B.6~ 55.72 62.36 68.83 75.05 80.89 86,49 91.76 96.73 101,~0 106.86 111.94 ii7,i2 122.~3 127.83 133.05 138.45 144,08 169.77 155.50 161.57 167.89 173o95 179.88 1~5.1~ ...... ~.~_ASURED Dg_~_~H AND OTHER DATA FOR EVERY EVEN 100 FEET._OF_._SUB SEA DEPTH" TRUE ..... V:EASU.~.~.D ........ .~ ER_T I CA~_._SUB . .H.D~.TVD .................. ~ER T I CAL ........ DEPTH ........................... DE~.~H ..... SEA DIFFERENCE .... CORREC T! O~. ............ TOTAL COORDINATES ............................................................ ................. 3812 ..................3805, ....... 3700 ........ 6 ............ 0 .................... 33,~.1 S _,_ 199,95 W ...... . ..................... . . ................................................. .......................... ~,_,~I,Z ..................... ~905 B800 7 1 ............................. 34., 9_~,,... $ ........ 207,50 w ............................................. .................. _.40_12 .................... ~005.. .... 3.900 ...........? ............. 0 ........................ 36,5_8. $ ....... 215,16 w ......................... ~ !.!_S_ ..................... ~.105, ........ 4000 ............... 7, .................. 0 ................................ _38 ,. 5 _6 __S ....... 223,38 ~,~ ........................... ................. ~_2,!~_ ........................ ..zf. 205, ......... 4.100 .............. ~ .......................... t ............................. ~0,.54_ S .............. 282,18 w ................... _~ ~_1~ ................. ._43_05 · . ....... 4200 ............. _~ ...................... 0 ........................... 42,4_5 _$ .......... 241. ~ 1 ............. ~ ~ !_~_ ................. ~_~ 05 · ~, 300 ............ ~ .................... 1 ....................... 4_Z+., s $ ._& ........... 251 · ! 7 a=l.~ .................... 4505, 4400 9 O 46 34 $ 261 00 ...................... .~_6_15 ........................ 4605, 4500 I0 ..... ~715 1,705 , z, 600 10 .............. ___~_8__~_6 ......................... _~_~ 05 · . ........ 4 700 ............ .11 ....................... ~7 ~o~. ~s. oo ~2 ~017 5005, ~900 12 5118 ~I05. 5000 5216. 5205. 5100 t2 - 5318 5305. 5200 13 6764 6grJ3 7no 5 720n 5~19 5405, 5300 14 .................. %~_!% ................ 55o~. _._ ~,so !_~ ...... 5622 5605. 5500 16 5724 5,~5. 5600 18 5~25 5805. 5700 20 5927 5905. 5800 22 6030 6005, 5900 24 6133 6105, 6000. 27 6236 6205, 6100 30 6340 6305. 620'0 34 ~45 ......... 6~05._ _ 6300 ......90 6550 6505. 6aC0 45 6~5.7 ............... 6605, ........ 6500 ............. ~1 .................... 6705. 6600 59 6B05, _6700 ...... 67 6905~ ......... 6800 77 7005. 6900 89 7105. 700(3 103 1 C 1 1 0 1 1 I 1 1 1 2 2 3 6 5 6 8 10 1'2 4~.04 S 270.97 49.88 $ 280,83 51.89 S 291o04 53,50 S 301,71 55.1.3 S 312,21 5B,77 S 321.07 63.89 S 327.29 72.40 S 331,92 6~,77 S 336,15 99,47 .5 341,22 115.34 S 348.12 13i,64 S 356.40 147,64 $ 366.27 163,46 S 378.12 160,73 5 392,34 198,20 S 408,62 ................ 215,44 S .......... -427,65 233,2i S 450.6~ 253.19 S 475.65 277.a3 S 497.77 ...................... 30~.72 S ...... 333.40 S 361,~ S .................... 389.85 S. 41~.26 S ..... ~47.74 $ 521,99 54-9.~4 580,:~5 616.94- 658.65 703.32 TRUE D[?.T._U ...... SEA DI_FE~BFNCE ........... CORRECTION .............. ~_OTAL ......_CO. DRDINATES · 76_7D_ ......... 750..5., 7400 ................. 7797 _.160_.~_- ..... 7500 ...................... 7_~22_ ................... !ZQ~. ....... 7aoo ........... 8Q~2__ .................. 78.Q5, 7700 ...................... ~lZ._5 ............ 77~5. ......... 7800 ......................... ~B ....... ~,5.. ....... 7900 ....... ~.At..~ ..... ~]05. 8000 ~540 8205, 866~ 8305, ~200 878R 9405, ~909 8505, 9025 8605, 9!B7 8705, . . 9246 8805. ___ 9352 8905, 9457 9005. 9561 9105, 9664 9205. 9766 9305, 9865 9AC5. 8300 8400 8500 8600 8700 88O0 8900 9000 9100 9200 9300 516,24 5.4'z.,..~ 7. 167 20 575.54 S 898.97 192 25 60~.~0 $ 967.04 '217 .......................... 25 .........................643..,.58._.S ...... 10~1,23 247 30 695.78 S 1094.S~ 270 23 743,46 S 1148,76 293 23 790.77 S 1202,26 313 20 841,01 S 12~7,90 335 22 89B,00 S 12B5,21 W 358 23 959 383 25 1020 z, 04 21 1078 420 16 11~1 432 12 1175 44I 9 1212 447 6 1242 452 5 1265 456 4 12B9 459 3 1306 461 2 1318 463 2 1329 .09 S 1324.74 ,74 S 1364,83 .14 $ 1401,61 · 14 S 1429o42 .74 S 1450,11 · 40 5 1~71.8~ · 57 S 1492,69 · 30 S 1512.20 .43 S 1531 · 1 1 .lO S 1549.15 ,82 $ 1566,55 .95 S i58B.0~ _ .:...._ A,'~O CO ..G P-.3_O ......... _~!.EASURED ................... DEO TH ..... TRUE .V._ER T I CAL DER.TH .................... 1000 ............... 2000 .............. 3000 ......................... 4000 ....... 5000 600n ................................... ,7.000 ................... 8000 ......................... 9000 I)96, 29_95 · .......... 3992 · 4987 · 5975, 6920, 7'/64, 8582. .GYROS¢OP_i.C_$URVEy ........................... 1000 FEET OF MEASURED DEPTH. SEA ..... TOTAL C-~O R D I N A-:F ~-'~- .............................. . 893. 7,04~ N 3~+.38 W .., 1891. 9.B3 N 96.3! W 2890, _ . 20.17 S _1~9..,19 W 3887.. ............ 36,~I S .... 2.1.4:22_.' ................ 4882. 54.92 S 310,46 W 5870. 175,(>7 S 387.88 W .. . 6815. 394.27 S 622.95 W 7659. 674.89 S 1069,61 W 8477, 1119~97 S 1423,68 FEBRUARY.... 13,1979 .~. AMOCO PRODUCTION COMPANY SCALE I"=1000' GYROSCOPIC SURVEY PLATFORM BRUCE GP 15742-30 JAN. 31, 1979 =, ,, ALL DEPTHS SHOWN ARE TVD 2400 4000 --'---7 / 5200 '-~ 6000,/' / 84oox/'/ '7 6 O0 ~..,..~ ~,..~ 8ooo.//~/~ ~\~- 8400X' 8800 . ~o0 ~,~'0~ TYD = 94153' TMD=9931' 400 800 1200 1600 2000 2400 2800 3200 360O 4000 44O0 4800 5200 560O 6000 6400 AMOCO PRODUCTION COMPANY GYROSCOPIC SURVEY SCALE I'-I000' PLATFORM BRUCE GP 18742-:30 JAN. :31~ 1979 ALL DEPTHS SHOWN ARE TVDo 6 7200 -~ 76O0 .~ ooo 9200 TVD = 946:3' TMD=9931' Granite Point 18742 Well No. 30 Chronological History October 28, 1978 TD: 256' Skid rig to Leg 3, Slot 8 and rig up over drive pipe. Drive pipe to 256'. October 29, 1978 October 30, 1978 to November'l, 1978 November 1-11, 1978 November 12, 1978 November 13-18, 1978 November 18, 1978 November 28-29, 1978 November 30, 1978 December 1, 1978 December 2-31, 1978 January 1-13, 1979 TD: 610 ' TD: 610' TD: 4520' TD: 4520' TD: 4520' TD: 4520' TD: 4520' TD: 4520' TD: 4520' TD: 8 41~5~'.~ TD: 9357' Dynadrill and survey 17-1/2" directional hole to 610'. Open 17-1/2" hole to 26", run 20" casing and cement casing. Drilling 12-1/4" hole and open hole to 17-1/2". Cementing 112 its. of 13-3/8" with 850 sx of Class~G cement Remedial cementing of 13-3/8" casing to ensure cement to surface Operations temporarily suspended on GP #30. Rig releaSed to GP 18742 #12 for completion. Recommence operations. Remedial cementing of 13-3/8" casing to ensure good pressure test Cleaning out 13-3/8" ~asing. Cleaning out 13-3/8" casing. Drill and survey 12-1/4" hole. Drill and survey 12-1/4" hole. G.P. 18742 Well No. 30 Chronological History Page 2 January 14, 1979 January 15-18, 1979 January 19, 1979 January 20, 1979 January 21-22, 1979 January 23, 1979 January 24-26, 1979 January 27-28, 1979 January 29, 1979 January 30, 1979 January 31, 1979 February 1, 1979 February 2-4, 1979 TD: 9370' TD: 9931' TD: 9931' TD: 9931' TD: 9931' PBTD: 9880' PBTD: 9880' PBTD: 9880' PBTD: 9880' PBTD: 9880' PBTD: 9880' PBTD: 9880' PBTD: :9880' Stuck with bit at 9340'. Pump Pipe-Lax and work pipe and free fish. Drill, survey and condition 12-1/4" hole. Logging. Run DIL 4516-TD, BHC- Sonic 4516-TD, GR-Density-Caliper 6850-TD. Run 9-5/8" casing. Run 9-5/8" casing (246 joints) and land at 9927'. Pump 550 sacks Class G cement. Clean out 9-5/8" casing to 9880'. Run SDC gyro survey 9880-4000'. Squeeze cement 9-5/8" casing. Pump 100 sacks Class G cement into perfs 9064-66', squeeze to 2800 psi. Pump 500 sacks Class G cement into perfs 8870-72', squeeze to 2200 psi. Clean out and test 9-5/8" casing to 2500 psi. Test good. Run Dresser CBL-CCL from 9880-7500'. Pick up 3-1/2" tubing. Run 3-1/2" completion assembly. Run dual tubing string and test. Rig released. Rig up flowlines, run Kobe pump and pump diesel from casing. Recover pump and perforate from Sonic Log dated 1-18-79 9758-9820', 9684-9716', 9604-9610', 9590-9600', 9518-9552', 9470-9508', 9380-9406', 9317-9341', 8994-9014', 8916-8984', 8638-8730', 8524-8562', at 4 JSPF with 2-1/8" Dresser Atlas Slim Kone Hollow Carrier tubing gun. February 5, 1979 PBTD: 9880' Run Kobe pump and place on production. L, A. Darsow District Superintendent February 12, 1979 File: LAD-144-W-F Amoco Production Company--,i : ,i,~~ Post Office Box 779 Mr. Hoyle H. Hamilton, Commissioner Alaska Oil and Gas Conservation Commission 3001 Porcupine Drive Anchorage, Alaska 99501 Dear Sir: Monthly Report of Drilling and Workover Operations Granite Point 18742 Well No. 30 Platform Bruce, Cook Inlet, Alaska Please find attached in duplicate State of Alaska Form 10-404 summarizing drilling operations on Granite Point 18742 Well No. 30. Very truly yours, L. A. Darsow District Superintendent Attachments MJS:klt F~rm No. 10.404 RF~V. 3-1-70 SUBMIT IN DUPLICATE STAT E 0 F A LAS KA OIL AND GAS CONSERVATION COMMITTEE MONTHLY REPORT OF DRILLING AND WORKOVER OPERATIONS 5. APl NUMERICAL CODE 50-133-20322 6. LEASE DESIGNATION AND SERIAL NO. ADL 18742 1. 7. IF 1NDIAN'ALOTTEE OR TRIBE NAME WELL WELL OTHER 2. NAME OF OPERATOR 8. UNIT FARM OR LEASE NAME Amoco Production Company Granite Point 18742 3. ADDRESS OF OPERATOR 9. WELL NO. P. O. Box 779, Anchorage, Alaska 99510 30 4, LOCATION OF WELL Leg 3, Slot 7, Granite Point Platform Bruce 1948' FSL, 1975' FWL, Sec. 31, TllN, RllW, S.M. 10. FIELD AND POOL, OR WIL~AT Granite Point - Middle Kenai 11. SEC. T. R. M. (BOTTOM HOLE OBJECTIVE) Sec. 31, TllN, RllW, S.M. 12. PERMIT NO. 13. REPORT TOTAL DEPTH AT END OF MONTH, CHANGES IN HOLE SIZE, CASING AND CEMENTING JOBS INCLUDING DEPTH SET AND VOLUMES USED, PERFORATIONS, TESTS AND RESULTS FISHING JOBS JUNK IN HOLE AND SIDE-TRACKED HOLE AND ANY OTHER SIGNIFICANT CHANGES IN HOLE CONDITIONS. Status as of December 31, 1978 TD: January 1-13, 1979 TD: January 14, 1979 TD: January 15-18, 1979 TD: January 19, 1979 TD: January 20, 1979 TD: January 21-22, 1979 TD: January 23, 1979 TD: January 24-26, 1979 TD: January 27-28, 1979 January 29, 1979 January 30, 1979 January 31, 1979 TD: TD: TD: TD: PBTD: 8415' 9357' 9370' 9931' 9931' 9931' 9931' 9931' 9931' 9931' 9931' 9931' 9931' 9880' Drill and survey 12-1/4" hole. Drill and survey 12-1/4" hole. Stuck with bit at 9340'. Pump Pipe-Lax and work pipe and free fish. Drill, survey and condition 12-1/4" hole. Logging. Run DIL 9914-4516', BHC-Sonic 9906-4516', GR-Density- Caliper 9921-6850'. Run 9-5/8" casing. Run 9-5/8" casing (246 joints) and land at 9927'. Pump 550 sacks Class G cement. Clean out 9-5/8" casing to 9880'. Run SDC gyro survey 9880-4000'. Squeeze cement 9-5/8" casing. Pump 100 sacks Class G cement into perfs 9064-66', squeeze to 2800 psi. Pump 100 sacks Class G cement into perfs 8870-72', squeeze to 2200 psi. Clean out and test 9-5/8" casing to 2500 psi. Test good. Run Dresser CBL-CCL from 9880-7500'. Pick up 3-1/2" tubing. Run 3-1/2" completion assem~~ Run dual tubing strings and'Y&s~.Et 'V~D 14. I hereby cer,~y, th~, t~a¥.~ol~~,d~.~..~ ue and correct SIGNED ~'-~ ~.~/ / TITLE District Superintendent DATE February 12, 1979 NOTE-Report on this' form is required for each calendar month, regardless of the status of operations, and must be filed in duplicate with the oil and gas conservation committee by the 15th of the succeeding month,unless otherwise directed. SCHLUMBERGER OFFSHORE SERVICES A Division of Schlumberger Limited HOUSTON. TEXAS 7700! PLEASE REPLY TO January 24, 1979 500 W. International Airport Road Anchorage, Alaska 99502 P.O. Box 779 Attention: Amoco Production Company Anchorage, Alaska 99510 Gentlemen: 1 RFolded Sepia Enclosed are 2 B~rints of the DIL, BHC/GR, FDC/CNL/GR Company Amoco ProduCtion Co ,Well Granite Point 18742 #30 Field. Granite Point , County ' Kenai State Alaska on: , 1 RFO~d~n~~ are being sent to: i BL.prints Amoco Production Company 1010 Security Life Building Denver, Colorado 80202 Attention: Mr. A.M. Roney 1 RFolded Sepia 1 BLprints ARCO OIL an GAS Company P.O. Box 360 Anchoraqe, Alaska 99510 Attention: Mr. D.W. Bose 1 RRolled Sepia 1 BLprints Chevron U.S.A., Inc. P.O. Box 7-839 Anchorage , Alaska Attention: Mr. C.F. Kirkvold 2 BLprints Getty Oil Company 1~60 Lincoln Street Denver, Colorado 80203 .A~tention: Mr. J.E. Hofman 2 BL prints Phillips Petroleum Company . . 1010 Security Life Building Denver, Colorado 80202 Attention: Mr. J.P. Denny 1 BL pri~s _ D~p~..of N~tu~al Resources 300~ Porcupine Dr~ve Anchorage ~ Alaska 995]0 1 RFolded Sepia 2_BL_prints Union Oil Company of California 909 W. 9~h Avenu~ AzLc/1Qr~e, Alaska 9950] Attention: Mr. Bob Warthen prints The film is. iReturned to Amoco (Anchorage) Please return one copy of this letter for' our files. Thank-you, '/2& ~[ ~ We appreciate the privilege of serving you. Received By: _ ~ ~ _ Very truly yours, Sales Engineer L. A. Darsow District Superintendent January 11, 1979 File: LAD-036-WF Amoco Production Post Office Box 779 Anchorage, Alaska 99510 907 - 272-8471 Mr. Hoyle H. Hamilton, Commissioner Alaska Oil and Gas Conservation Commission 3001 Porcupine Drive Anchorage, Alaska 99501 Dear Sir: Monthly Report of Drilling and Workover Operations Granite Point 18742 Well No. 30 Platform Bruce, Cook Inlet., Alaska Please find attached State of Alaska Form 10-404 summarizing drilling operations on Granite Point 18742 Well No. 30. Very truly yours, L. A. Darsow District Superintendent Attachment MJS: klt SUBMIT IN DUPLICATE Form No. 10404 REV. 3-1-70 STAT E O F A LAS KA OIL AND GAS CONSERVATION COMMITTEE MONTHLY REPORT OF DRILLING AND WORKOVER OPERATIONS 5. APl NUMERICAL CODE 50-133-20322 6. LEASE DESIGNATION AND SERIAL NO. ADL 18742 1. 7. IF IND1AN'ALOTTEE OR TRIBE NAME OiL GAS [] WELL WELL OTHER 2. NAME OF OPERATOR 8. UNIT FARM OR LEASE NAME cOmPany Granite Point 18742 Amoco Production 3. ADDRESS OF OPERATOR 9. WELL NO. P. O. Box 779, Anchorage, Alaska 99510 30 4. LOCATION OF WELL Leg 3, Slot 7, Granite Point Platform Bruce 1948' FSL, 1975' FWL, Sec. 31, TllN, RllW, S.M. 10. FIELD AND POOL, OR WIL~AT Granite Point - Middle Kenai 11. SEC. T. R. M. (BOTTOM HOLE OBJECTIVE) Sec. 31, TllN, RllW, S.M. 12. PERMIT NO. 13. REPORT TOTAL DEPTH AT END OF MONTH, CHANGES IN HOLE SIZE, CASING AND CEMENTING JOBS INCLUDING DEPTH SET AND VOLUMES USED, PERFORATIONS, TESTS AND RESULTS FISHING JOBS JUNK 1N HOLE AND SIDE-TRACKED HOLE AND ANY OTHER SIGNIFICANT CHANGES IN HOLE CONDITIONS. Status as of November 30, 1978 TD: December 1, 1978 TD: December 2-31, 1978 TD: 4520' 4520' 8415' Cleaning out 13-3/8" casing. Cleaning out 13-3/8" casing. Drill and survey 12-1/4" hole. 14. I hereby certifY~'t~t~ for~gofln~4s true and correct SIGNED.//"-~e. ~' ~~~/~ TITLE District Superintendent DATE January 11, 1979 NOTE-Report on this' form is required for each calendar month, regardless of the status of operations, and must be f/led in duplicate w/th the · oil and gas conservation committee by the 15th of the succeeding month,unless otherwise directed. AM.O0.~O~ L. A. Darsow D~slrict Superintendent Amoco Production Compar Fost Office BOx 779 Anchorage, Alaska 99510 907 - 272-8471 December 13, 1978 File: LAD-1167-WF Mr. Hoyle Hamilton, Director Division of Oil and GaS Conservation Department of Natural ResoUrces State of Alaska 3001 Porcupine Street Anchorage, Alaska 99501 Dear Sir: :' '~" Monthly Report of Drilling and Workover Operations Granite POint'I8742 Well No. 12 and Well No 30 and Middle Ground Shoal 17595 Well No. 7 Please find attached State of Alaska Form P-4 summarizing drilling operations on Granite Point 18742 Well No. 12, Well No. 30 and Middle Ground Shoal 17595 Well No.. 7. Very truly yours, L.A. Darsow District Superintendent Attachment MAM: sjr Form No. 10-404 REV. 3-1-~0 SUBMIT IN DUPLICATE ,. - STAT E O F A LAS KA OIL AND GAS CONSERVATION COMMITTEE MONTHLY REPORT OF DRILLING AND WORKOVER OPERATIONS 5. API NUMERICAL CODE 50-133-20322 6. LEASE DESIGNATION AND SERIAL NO. ADL 18742 OIL [~ GAS ~] WELL WELL OTIIER 2. NAME OF OPERATOR 8. UNIT FARM OR LEASE NAME Amoco ProduCtion Company Granite Point 18742 3. ADDRESS OF OPERATOR 9. WELL NO. P.O. Box 779, Anchorage, Alaska 99510 30 4. LOCATIONOFWELL Leg 3, Slot 7, Granite Point Platform Bruce 1948' FSL, 1975' FWL, Sec. 31, TllN, RllW, S.M. 7. IF INDIAN'ALOTTEE OR TRIBE NAME 10. FIELD AND POOL, OR WILDCAT Granite Point - Middle Kenai 11. SEC. T. R. M. (BOTTOM HOLE OBJECTIVE) Sec. 31, TllN, RllW, S.M. 12. PERMIT NO. 13. REPORT TOTAL DEPTH AT END OF MONTH, CHANGES IN HOLE SIZE, CASING AND CEMENTING JOBS INCLUDING DEPTH SET AND VOLUMES USED, PERFORATIONS, TESTS AND RESULTS FISHING JOBS JUNK IN HOLE AND SIDE-TRACKED HOLE AND ANY OTHER SIGNIFICANT CHANGES IN HOLE CONDITIONS. Status as of 10/31/78 November 1-11, 1978 November 12, 1978 November 13-18, 1978 November 18, 1978 November 28-30, 1978 TD: 610' TD: 4520' TD: 4520' TD: 4520' TD: 4520' TD: 4520' Drilling Drilling 12-1/4" hole and open hole to 17-1/2" Cementing 112 jts. of 13-3/8" with 850 sx of class G cement Remedial cementing of 13-3/8" casing to ensure cement to surface Operations temporarily suspended on GP #30. Rig released to GP 18742 #12 for completion Recommence operations. Remedial cementing of 13-3/8" casing to ensure good pressure test 14. I hereby cert'f~,."//\..,,,n-~'~'~t/h~jO~'~''~'fs-t?ue and correct SIGNED .d?~''. d"/,/'~)/'?['/'~~''''''''~ TITLE District Superintendent DATE December 14, 1978 NOTE-Report on this' {orm is required ~or each calendar month, regardless of the status of operations, and must be filed in duplicate with the oil and gas conservation committee by the 15th of the succeeding month,unless otherwise directed. I,orm bi(), 1040,1 RI'V. 3.1.7(I ,- " ~' STATE Or ALASKA Oi'L AND GAS CONSERVATION COMMITTEE MONTHLY REPORT OF DRILLING AND WORKOVER OPERATIONS APl N I IM I.'RI('A I ('()1)1: 50-133-20322 6. I.EASE I)I.'SIGNA'I'I()N ANI) SERIAl. NO. ADL 18742 I. 7.IF INDIAN'AI,OTTEE OR TRIBE NAME OIL (;AS WE, LL ~ OTiiEr WELL I--] :. nAME OF oPerATor s.UNrr FARM or I.EASF. name Amoco Production Company Granite Point 18742 3. ADDRESS OF OPERATOR 9.WEI.I. NO. P.O. BOx 779, AnchOrage, Alaska 99510 30 4. LOCATIONOFWE.LI. Leg 3, Slot 7, Granite Point Platform Bruce 1948' FSL, 1975' FWL, Sec. 31, TllN, RllW, S.M. 10. FII{I.I) AND POOl., OR wll. Ig~AT Granite Point - Middle Kenai 11. SEC. T. R. bi. (BOTTOM tiOLE OBJECTIVE) Sec. 31, Ti!N, RI1W, S.M. 12. PERMIT NO. 13. REPORT TOTAL DEPTH AT END OF biONTIt, CIIANGES IN IIOLE SIZE, CASING AND CEMENTING JOBS INCLUDING DEPTtt SET AND VOLUMES USED~ PERFORATIONS, TESTS AND RESULTS FISHING JOBS JUNK IN HOLE AND SIDE-TRACKED HOLE AND ANY OTHER SIGNIFICANT CHANGES ~IN HOLE CONDITIONS. Status as of 10/31/78 TD: 610' . . November 1'11, 1978 TD: 4520' November 12, 1978 November 13-18, 1978 November 18, 1978 November 28-30, 1978 TD: 4520' TD: 4520' TD: 4520' TD: 4520' Drilling Drilling 12-1/4" hole and open hole to 17-1/2" Cementing 112 jts. of 13-3/8" with 850 sx of class G cement Remedial cementing of 13-3/8" casing to ensure cement to surface Operations temporarily suspended on GP #30. Rig released to GP 18742 #12 for completion Recommence operations. Remedial cementing of 13-3/8" casing to ensure good pressure test 14. I hereby cc~f~l~r fs~j~]tr~nd corrcc! SIGNED I ti n ti ~C'.~1/~1 TITLE District Superintendent DATE December 14, 1978 NOTE--Report on this form is required for each calendar month, regardless of the status of operations, and must be filed in duplicate with the oil and gas conservation committee by the 15th of the succeeding month,unless otherwise directed. November22, 1978 Amoco Prod~c~ Attn: L.A. Darsc~ District Supe~/n~ P.O. Box 779 Anc/~rage, Al{ 99510 A pezn~t to drill the Granite Pt. 18742 }~. 30 well was issued by this office 10-6~78. ~is ~% app~ a sett~ d~ of 3500 ft. for the 13 3/8" surfa~ cas~. On 11-15-78, J~ Miller of ~ office w~ oontacted by Jeff Cuine. John %~s im~o~d that the 13 3/8" casing was set to 4516 ft. and c~m~nting probl~ brad dev~lmped. The problems and solutions mm. re discussed and v~rbally approved, with a ~t for a P-3 ~ttai describing the opera~~. ~ P-3 form was recei~ 11-17-78. ti tutes a wi~ violation of the a!~ program. ~my change of this nature requires .prior approval frcm ~ Oil and, c~as Ccn~erva~ ~ttee. ~ do not ~tic~ your rea~s for ~ating~. frcm the approved p .~rcgTam b%~ by notic~ of this le~ ~ deviatic~s from approved pz~]rams ~ust be ~s~ ~assed and a~ by cur office before imp~~~. ~j Chief Petroleum Eng~ L. A. Darsow District Superintendent November 16, 1978 File: LAD-iO91-WF Amoco Production Anchorage, Alaska 99510907 - 272-8471 ~.. Mr. Hoyle H. Hamilton, Director Division of Oil and Gas Conservation Department of Natural Resources State of Alaska 3001 Porcupine Drive Anchorage, Alaska 99501 Dear Mr. Hamilton: Casing Program Change G.P. 18742 Well No. 30 Attached please find our completed Form 10-403, a subsequent report of altering the 13-3/8" surface casing setting depth in Granite Point 18742 Well No. 30. During the drilling of G.P. 18742 Well No. 12 Redrill, gas sands were encountered between 4000-4500' that required utilization of a 9.5 ppg mud system. In addition, a water flow encountered in the C-3 zone of the Middle Kenai sands required an increase in mud weight to 10.8 ppg. These higher mud weights increased the possibility of lost circulation through the more depleted production intervals in the C-5 and C-7 / zones. In an effort to case off these gas sands and increase wellbore integrity, the 13-3/8" casing setting depth was changed from the previously approved 3500' to 4516'. A total of 111 joints of 13-3/8" 61-72# casing were run, and cemented as required. Yours very truly, L. A. Darsow District Superintendent Attachment Form 10-403 REV. 1-10-,73 Submit "Intentions" in Triplicate & "Subsequent Reports" in Duplicate STATE OF ALASKA OIL AND GAS CONSERVATION COMMITTEE SUNDRY NOTICES AND REPORTS ON WELLS (Do not use this form for proposals to drill or to deepen Use "APPLICATION FOR PERMIT--" for such proposals.) 1. [] GAS D ~,I~L,w~.~.L WE LL O THE R 2. NAME OF OPERATOR Amoco Production Company 3. ADDRESS OF OPERATOR P. O. Box 779, Anchorage, Alaska 99510 4. LOCATION OF WELL At surface Leg 3, Slot 8, Granite Point Platform Bruce 1951' FSL, 1976' ~rL, Sec. 31, Ti1N, RllW, S.M. 13. ELEVATIONS (Show whether DF, RT, GR, et~) 115' KB-MSL 14. Check Appropriate Box To Indicate Nature of Notice, Re 5. APl NUMERICAL CODE 50-133-20322 6. LEASE DESIGNATION AND SERIAL NO. ADL 18742 7. IF INDIAN, ALLOTTEE OR TRIBE NAME 8. UNIT, FARM OR LEASE NAME Granite Point 18742 9. WELL NO. 30 10. FIELD AND POOL, OR WILDCAT Granite Point - Middle Kenai ].1. SEC.,T., R., M., (BOTTOM HOLE OBJECTIVE) Sec. 31, TllN, RllW, S.M. 12. PERMIT NO. 78-73 ~ort, or Other Data NOTICE OF INTENTION TO: TEST WATER SHUT-OFF ~ PULL OR ALTER CASING FRACTURE TREAT SHOOT OR ACIDIZE REPAIR WELL (Other) MULTIPLE COMPLETE ABANDON* CHANGE PLANS SUBSEQUENT REPORT OF: FRACTURE TREATMENT ALTERING CASING SHOOTING OR ACIDIZING ABANDONMENT* (Other) (NOTE-' Report results of multiple completion on Well Coml31etion or Recompletion Report and Log form.) 15. DESCRIBE PROPOSED OR COMPLETED OPERATIONS (Clearly state all 13ertlnent details, and give pertinent dates, including estimated date of starting any proposed work. In an effort to case off potential shallow gas sands between 4000' and 4300', which were encountered while drilling Granite Point 18742 Well No. i2RD, and increase wellbore integrity, the 13-3/8" surface casing setting depth was changed from the.'previously approved 3500' to 4516'. A total of 111 joints of 13-3/8", 61#, 68#, and 72# S-80, N-80 and K-55 casing were run in 17-1/2" hole and cemented as required. Also, please note that the above surface location reflects a slight change from that originally permitted. Slot 8 in Leg 3 was selected over Slot 7 as it provided a clearer ~eparture path for the wellbore. ].6. I hereby certify that the fore, lOng is true and correct TITLE District Superintendent November 15, 1978 DATE (This space for State office use) APPROVED BY CONDITIONS OF APPROVAL, IF ANY: TITLE DATE See InStructions On Reverse Side ~6, 1978 ~zite Point 18742 ~ ~3~n Ca, any pezmit ~a). 78-73 District Super~ P. O. Box 779 Ancho~, .~~ 99510 ~losed ~ ~ approved application for permit to drill the above ~t' referenced v~ll at a loca ~ in secti~ 31, Towns~p llN, P~m~ge~ llW, S~. core chips, ~ a ~mud log ~ r~t ~~. A directional M~ny riva_rs in ~ and ~ draL~ sy~ have ~ classifi~ as i~t for the spawD3~g or migration of armdrc~ous fish. Operations in ~~ ~ ~ subj~ to ~ 16.50.870 ~ ~ reticulations propagated ~~ (Title 5, Ala~ ~ini~i~ ~). Prior to ~cing operations }~)u I~y ~ c~ bY ~ }~3bitat Coordinator's office, De~t of F~ ~ ~. Pollu~ic~ of any waters of ~ State ~ prohibited ~ ~ 46, C~ 03, Article 7 ~ ~h~ rec~ulaticns pr~gated ther~r~]~r (Title 18, Alaska Admj/~is~_rative ~, C~mapter'70) a~ by ~he ~ Water F~llution Control Act, as ~.. Prior to'~ing op~~~ ~ may be cc~utau~ by a representative of the De~t of ~virc~z~en~l Cc~servation. ~sum~nt to ~ 38.40, Local ~lire U~ State Leases, the AlasA~ De.~t of Labor ~ b~--ing notified of ~ is~ of ~s Fermit to ~&ill. To aid us in sc~dulLng fiel¢t work, ~ would appreciate your notifying.. office witkin 48 hours after ~ ~11 is ~. ~. would also like to be notified so that a rep_~esentative of the Division may be present to %~itness tes~ of blowout preventer eq. ui.~ ~fo~e ~fac~ casing s~hoe is drilled. L.A.~ -2- (~-~te ~. ~30 Oct~ 6, 1978 In tine event of mmpe~i~ ~r abamk~mmt please give ~s office adequate a~am~ ~ficaticm so ~hat ~ may ham a witness present. ~lo~are Department of Fish ~ ~, Habitat Secticm w/o encl. Separt~mt of ~mir~mm~ O~~~ w/o encl. Department of Labor, ~~visor, ~ Law ~~ Division w/o ertl. L. A. Darsow District Su penntendent November 2, 1978 File: LAD-1060-WF Mr. Hoyle Hamilton, Director Division of Oil and Gas Conservation Department of Natural Resources State of'Alaska 3001 Porcupine Drive Anchorage, Alaska 99501 Amoco Production ComF Post Office Box 779 Anchorage, Alaska 99510 907 - 272-8471 Dear Sir: Monthly Report of Drilling and Workover Ope!..a~s._~ Granite Point 18742 Wells No. 12 Redrill ~ No. 3~~ Platform Bruce~ Cook Inlet, Alaska Please find attached State of Alaska Forms 10-404 summarizing drilling operations on Granite Point 18742 Wells N~. 12 Redrill and No. 30 for the month of October 1978. Very truly yours, L. A. Darsow District Superintendent AttaChments MAM:klt .!~,[.. *... ~ 7// .. ,i~;..i~ · ,-'i 14/f.? !./., /"4':fi" Form No. 10404 REV. 3-1-70 SUBMIT IN DUPLICATE STATE OF ALASKA OIL AND GAS CONSERVATION COMMITTEE MONTHLY REPORT OF DRILLING AND WORKOVER OPERATIONS 5. API NUMERICAL CODE 50-133-20322 6. LEASE DESIGNATION AND SERIAL NO. ~L 18742 WELL WELL OTHER 2. NAME OF OPERATOR 8.UNIT FARM OR LEASE NAME Amoco Production Company Granite Point 18742 3. ADDRESSOFOPERATOR 9. WELLNO. P. O. Box 779, Anchorage, Alaska 99510 30 4. LOCATION OF WELL Leg 3, Slot 7, Granite Point Platform Bruce 1948' FSL, 1975' FWL, Sec. 31, TllN, RllW, S.M. 10. FIELDANDPOOL, ORWIL~AT Granite Point - Middle Kenai 11. SEC. T. R. M. (BOTTOM HOLE OBJECTIVE) Sec. 31, TllN, RllW, S.M. 12. PERMIT NO. 13. REPORT TOTAL DEPTH AT END OF MONTH, CHANGES IN HOLE SIZE, CASING AND CEMENTING JOBS INCLUDING DEPTH SET AND VOLUMES USED, PERFORATIONS, TESTS AND RESULTS F1SHING JOBS JUNK IN HOLE AND SIDE-TRACKED HOLE AND ANY OTHER SIGNIFICANT CHANGES IN HOLE CONDITIONS. 10-28-78 10-29-78 - TD-610' 10-31-78 Rig up and commence operations. Drill 26" hole to 610'. Run 20" casing and land at 595', cement casing with 1400 sx. Class G cement. _ 14. Ihereb~th~efo..~,ristrueandc~--'-'-~ District Superin~e~den~ DATE s~o~~- /'W '~/~-~-~;~; ~x~ November 2, 1978 ~OTE-Raport on this' form is required for ~ach calendar month, re~ardle~ of the status of op~rations, and mu~ ba iliad in duplicate with the oil and oas conservation committee by the ~Sth of the su~aedin~ month,unl~ otherwise directS. Conservat_icn October 4, 1978 ADMINISTRATIVE APPROVAL NO. 76.9 ~he pressure-maln.-:~~-~j~ct appr~ by Conservation Order No. 76. I.~. L. A. Darscw District Superinte~t / P. O. Box 779 Anchorage, Alaska 99510 On October 3, 1978 the referen~ applicatic~ was received. %7~ proposed w~ll would serve to recover tra[~ reserves from the northeast flank area of .the Granite Point structure. This well is the fourth to be' c(xapleted in edge southwest quarter of Secti(a% 31. The Oil and Gas Conservaticn Con~ittee ~y authorizes the drilling of the referenced well pursuant to Rule 7 of Conservation Order ~,b. 76. Very truly yours, t~%rry W. Kugler Amoco Production Company P.O. Box 779 Anchorage, Alaska 99510 L. A. Darsow Area Superintendent October 2,.1978. File: LAD-962-WF Mr. Hoyle H. Hamilton, Director Division of Oil and Gas Conservation Department of Natural Resources State of Alaska 3001 Porcupine Drive Anchorage, Alaska 99501 Dear Mr. Hamilton: Application for Permit to Drill G.P. 18742 Well No. 30 Attached is the completed State of Alaska Form 10-401, requesting a permit to drill Granite Point 18742 Well No. 30. Amoco proposes to drill this well from Leg 3, Slot 7, Granite Point Platform Bruce to a target location on top of the Middle Kenai C-8 zone at -9100' MSL as outlined on the attached form. Total depth, estimated at 9800', will be achieved following complete penetration of the C-8 zone. This will be the fourth well completed in the southwest quarter of Section 31 and is required to recover trapped reserves from the northeast flank area of the Granite Point structure. Also attached are BOP stack sketches, a plat of the proposed target location relative to Platform Baker, and a draft in the amount of $100 to cover the filing fee. Since this will be the fourth well completed in the SW 1/4. of Section 31, we hereby request administrative approval for the above location. Yours very truly, L. A. Darsow District Superintendent Attachments JBK:sls Form 10-401 ' REV. 1-1-71 STATE OF ALASKA OIL AND GAS CONSERVATION COMMITTEE PERMIT TO DRILL OR DEEPEN la. TYPE OF WORK DRILL [] DEEPEN r'-] b. TYPE OF WELL WELL [ I OTHER ZONE SUBMIT IN TRIPs- ~E (Other instructions dn 2. NAME OF OPERATOR ,a,~eo Product!on ~~y 3. ADDRESS OF OPERATOR P. O. ~ox 779, ~caora~e, 4.LOCATION OF WELL reverse side) Atsurface ~g ~, SlOt 7, Cranite Point Platform ~ruce tP/da'.rSL. 1975' ~e~, Sec. 31~ TI1N, F~IW, $.M. proposed prod, z~e MULTIPLE ZONE API No. 50-133-20322 6. LEASE DESIGNATION AND SERIAL NO. tool 18742 7. IF INDIAN, ALLOTTEE OR TRIBE NAME 8. UNIT FARM OR LEASE NAME Granite Point 187&2 9. WELL NO. 30 10. FIELD AND POOL, OR WILDCAT Granite Point - Hlddle Kenai 11. SEC., T., R., M., (BOTTOM HOLE OBJECTIVE) 700'FSi_. 500'FWL_. Sac. 31;TllN,nllW..M.M. To? of C-~ zoa_~ (-91~') 13. DISTANCE IN MILES AND DIR~ION FROM NEAREST TO~ OR ~ST OFFICE* 7-1/2 mile~ ~W of 'fyonek 14. BOND INFORMATION: 15. DISTANCE FROM PRO~SED ~ ~ m~ ~ ~ ~ ~_~16. No. OF ACRES IN LEASE 17. NO,ACRES ASSIGNED LOCATION TO NEAREST ~d ~s ~ g~O ~~&~ TO THIS WELL PROPERTY OR LEASE LINE, FT. / (Mso to newest dfig, u~t, ff any~t)[ ] 75fi6 tAPCO }-AnLI 8742 5060 40 18. DISTANCE FROM PRO~SED LOCATION 19. PRO~SED DE~H 20. ROTARY OR CABLE TOOLS to ~EAREST ~rr VRIrU~C,COUVrEtEV, ~0 * ~ Of OR APPLIED FOR, FT. 21. ELEVATIONS (Sh~w whether DF, RT, CR, etc.) 22. APPROX. DATE WORK ~LL START !!5' g~ - ?~L Wee~c of ~gobe: 23, 1978 23. PRO~SED CASING AND CEMENTING PROGRAM See. 31; TIiN_. RllW: S.M. 12. SIZE OF HOLE SIZE OF CASING WEIGHT PER FOOT GRADE SETTING DEPTH Quantity of cement 26 20 94# a--40 600 Co aurfac~ 17-1/1 i3-3/5 61~ a 66~ ~-55 3500 ~o Surfac~ ~OTg: C~sin~; deslg~ ~fe~y factors of'i.!;3, 1.0 ~d I.~: wLll'b~ ~ed fo~ co~a~ae, burse Operator proposes to drill subject ~1I from Leg 3, Slot 7, ~antte Point Platfo~a Bruce, co a target t.ocatlon oa top of tb~ }addle itali C-~ zone at 700' Y~L, 500' FWL, Sec. 31, Tll~, R~IW, at -9100' ~L. Total depth, estimated at 95(;0' TMD, will be achlev~ foll~t~ c~plete penetration of tho C-8 mo-me. After log eval~tioa$, zones of i~gerest will be perforated, stl~late~, if necessa~, and prod~. ~ere age no affect~ op~ator8. A loc~tion plat ~d BOP sketcI~a attached. IN ABOVE SPACE DESCRIBE PROPOSED PROGRAM: If proposal is to deepen give data on. present productive zone and proposed new productive zone. If prOposal is to drill or deepen directionally, give pertinent data on subsurface locations and measured and true vertical depths. Give blowout preventer progxam. 24, I hereby ce:~2£y- that4~he Foregoing is True and Correct DA~ October 2, 1978 ~TLE District auperintendent (This space for State office use) SAMPLES AND CORE CHIPS REQUIRED I MUD LOG [] YES'~NO I [] YES DIRECTIONAL SURVEY REQUIRED [] NO PERMIT NO. f t7 ~- ~ ~'~ ~ · APPOVED By' - CONDITIONS OF APPROVAL, IF ANY: OTHER REQUIREMENTS: A.P.I. NUMERICAL CODE M~snber TITLE DATE October 6, 1978 *See Instruction On Reverse Side 12,201 TMO ~ I0,502 TVD ~ 1 · ~ -8276 10,905 T M D'~ ~'~'~ 10,425 TVD 4(4-8) , \\\ II, [4- .- -aoa2 3 (4- 6/ .~ .' 3O ~., - d.. 7C.;3 I ! ~64 10,573 T · ~7926 .7980 I0'3-6) t c' ' e-'>"- 838~ 10,370 TMD 9818 TVD ~t6o %, ., I · PAN AM 12,33b TMD . 2 12,245 TVD ~,I,~- ~ "-9175 ) II,~,OO TMD ~O. I6B /~',~uk,, 8971 17587 AM ET AL HBP 18'142.. -~.-:~. , 10,480 TMD /2(2-/)~°'22¢ rvD -9035 TIIN -r~oN ~u.J~¢~'._ ,2.0 CR~TE' ?ol~T' BRUCE' / '.r 2 ' Z&R,'. # L.\ N?., % Z.O r AI~t~N FILLUP /tN,() Amoco Pro, ~uction Compar' ENGII',"" ERING CHART ANNUL~IR BOP ~ HAFFE-R ~_1 LVV5 I~ r:.!L[ ......................... APPN i 4 .. ~( .... NO Nom~rks fee attached ..................... '1 ":' _Ts well [.o be located 3 Is a reaister~ s~:ev plat attached ................ 4. Is well located pro~r dist~ce from property line 5. Is well located proper dis::~ce 6. Is sufficient undedica~ed acreage available in ~is 7. Is well to be deviated ....................... 9. C~n !~i ~ ~pproved ~ore ~en-d~y w~Sk ............. 10. D~e~ ~r~tor h~ve ~ bond 5n . ~.: a conse:ation order needed ............ ].2. Is a.c~n~s~rat~ve approval n~ded .......... !3. is conductor string provided ..................... ].4. Is enough count used to circulate on conduct;or and (3) Admin/t 11.5. t:i ]_] cc:-~ent tie in surface and hyhe~__~medi_a-he or pr(.Yiuction strings . _ ...... ~ (4) Casg. ,, Will c~nt cover all known pr~uctiv(>. Nori.:¢ons .......... ].7. Ni.].l surface casina, protect fresh water zones ........... ~ ] 8. ??ill all casing give adequate safety in collapse, tension & burs%. . 19. ll):::s BOPE have suf:icient pressure rating - Tes'h to _~..~.O__ psi.g ~ .................................................................................. ---(5) . '- ........................... ~ ................ Approval Recot::nd~"d .....................................
