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Home My WebLink AboutCO 644 • • Image Project Order File Cover Page 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. ci: o ip ( 4 Order File Identifier Organizing (done) ❑ Two -sided II I I III Hi ❑ Rescan Needed 1 11111 III I RE AN DIGITAL DATA OVERSIZED (Scannable) C r Items: El Diskettes, No. El Maps: Grey Items: ❑Other, No/Type: ❑ Other Items Scannable by a Large Scanner ❑ Poor Quality Originals: OVERSIZED (Non - Scannable) ❑ Other: ❑ Logs of various kinds: NOTES: p� ❑ Other:: M BY: aria Date: (c) v ' /s/ Project Proofing I 1 1111 BY: NM Date: p 0 1 /s/ Y Scanning Preparation x 30 = + = TOTAL PAGES /c- / (Count does not include cover sheet) BY: Maria Date: In ' �' /s/ Production Scanning I 1E11 I Stage 1 Page Count from Scanned File: 1a (Count does include cov heet) Page Count Matches Number in Scanning Preparation: YES NO BY: Date: (Q/IQ I /s/ VVIp Stage 1 If NO in stage 1, page(s) discrepancies were found: YES NO BY: Maria Date: /s/ Scanning is complete at this point unless rescanning is required. I 11111111 ReScanned I HUM BY: Maria Date: /s/ Comments about this file: Quality Checked , I 111111 E 10/6/2005 Orders File Cover Page.doc INDEX CONSERVATION ORDER NO. 644 Docket Number: CO-11-12 West McArthur River Field Redoubt Shoal Field Kenai Peninsula Borough, Alaska 1. March 3, 2011 Cook Inlet Energy (CIE)'s request to commingling West McArthur River oil with Redoubt Shoal oil 2. March 7, 2011 Notice of Public Hearing, Affidavit of Publication, email distribution, and mailings 3. March 30, 2011 DNR's request to store Trading Bay oil and McArthur River Oil at the Kustatan Production Facility and request to commingle West McArthur River oil and Redoubt Shoal oil 4. April 14, 2011 Transcript 5. April 18, 2011 Public records request from Justin Black with Chevron 6. April 20, 2011 Chevron's response to AOGCC's questions 7. April 20, 2011 CIE's response to AOGCC's questions 8. July 29, 2011 Email re: Commingling WMR and Redoubt Production 9. March 9, 2015 Notice of Violation — Missing Reports (OTH-14-027) INDEX CONSERVATION ORDER NO. 644 • • STATE OF ALASKA ALASKA OIL AND GAS CONSERVATION COMMISSION 333 West 7 Avenue, Suite 100 Anchorage, Alaska 99501 Re: THE APPLICATION OF Cook Inlet Energy for an ) Docket Number: CO -11 -12 Order authorizing the commingling of West ) Conservation Order No. 644 McArthur River oil with Redoubt Shoal oil, in ) conformance with 20 AAC 25.215. ) West McArthur River Field ) Redoubt Shoal Field ) Kenai Peninsula Borough, Alaska ) May 6, 2011 NOTICE CLOSING DOCKET BY THE COMMISSION: The Commission has the closed the Docket in the above captioned matter. ENTERED AND EFFECTIVE at Anchorage, Alaska and this 6th day of May, 2011. BY DIRECTION OF THE COMMISSION Ilk At. A , k, _ tre, Jod, . Co ombie Sp. al Assistant to the Commission • STATE OF ALASKA ALASKA OIL AND GAS CONSERVATION COMMISSION 333 West 7 Avenue, Suite 100 Anchorage, Alaska 99501 Re: THE APPLICATION OF Cook Inlet ) Docket Number: CO -11 -12 Energy for an Order authorizing the ) Conservation Order No. 644 commingling of West McArthur River oil ) with Redoubt Shoal oil, in conformance ) West McArthur River Field with 20 AAC 25.215. Redoubt Shoal Field ) Kenai Peninsula Borough, Alaska ) ) May 6, 2011 IT APPEARING THAT: 1. By application dated March 3, 2011 Cook Inlet Energy (CIE) applied to the Alaska Oil and Gas Conservation Commission (Commission) for an order authorizing the commingling of West McArthur River oil with Redoubt Shoal oil, Kenai Peninsula Borough, Alaska. CIE also requests approval of a Micro Motion Coriolis meter for determining the proper allocation of Redoubt Shoal oil. 2. On March 10, 2011 pursuant to 20 AAC 25.540, the Commission published in the Peninsula Clarion notice of opportunity for public hearing on April 14, 2011. 3. The Commission held a public hearing on April 14, 2011 at 333 West 7 Avenue, Suite 100, Anchorage, Alaska 99501. Testimony was presented by CIE and Union Oil Company of California (Union). 4. No protests to the application were received. 5. The hearing record was held open until April 22, 2011 so that CIE and Union could provide written responses to Commission inquiry. FINDINGS: 1. Prior to March 23, 2009 Union stored oil from the McArthur River and Trading Bay Fields at the Drift River terminal. Mount Redoubt volcanic eruptions beginning on that date have prevented subsequent oil storage at the terminal. Terminal piping has been reconfigured to allow oil to be pumped directly onto a tanker. 2. Union currently stores McArthur River oil and Trading Bay oil at its Trading Bay Production Facility (TBPF). Trading Bay tank capacity is equivalent to about 18 days of production. Routine tank maintenance and repair reduce available storage capacity, and as the storage limit is reached, McArthur River and Trading Bay wells must be shut in to accommodate tanker scheduling. Conservation Order 644 • • Page 2 West McArthur River, Redoubt Shoal May 6, 2011 3. Eleven Union wells completed with electric submersible pumps (ESP) account for 26% of producing wells and 60% of oil produced from the McArthur River and Trading Bay Fields. Shutting in ESP wells exposes Union to significant risk of ESP failure requiring a rig workover. 4. To provide temporary substitute storage capacity through its regularly scheduled tank maintenance period, Union wishes to utilize two of CIE's Kustatan Production Facility (KPF) storage tanks, which would eliminate the need to shut in Union's eleven ESP wells. 5. In order to free the tank storage required to store Union's oil, CIE must commingle its West McArthur River oil and Redoubt Shoal oil in a KPF storage tank. 6. In order to comply with Commission regulations, CIE Redoubt Shoal oil must be metered prior to commingling with CIE West McArthur River oil to determine the quantities produced from each. CIE proposes to allocate Redoubt Shoal oil using a Micro Motion Coriolis meter with a stated accuracy of ±0.05% of rate, which would be more accurate than the current field custody sales meters. 7. CIE proposes monthly third party meter calibration, which will provide verification and will identify changes, damage or degradation in meter measurement performance. Monthly meter calibration will be done by Industrial Instruments Service Company (IISCO), an experienced company known to provide reliable meter calibrations. CONCLUSIONS: 1. The Drift River terminal configuration and Cook Inlet oil tanker scheduling will require Union to shut in McArthur River and Trading Bay wells which use ESPs, absent an alternate production storage means. 2. Frequent well shut in renders ESPs susceptible to failure, and replacing ESPs requires rig workover. 3. Freeing CIE KPF oil storage capacity for temporary use by Union will allow Union to avoid production upsets that would likely follow the shut in of Union's McArthur River and Trading Bay wells. 4. Commingling CIE West McArthur River oil with Redoubt Shoal oil at KPF is necessary to free KPF tankage for Union's temporary use. 5. Commission regulation 20 AAC 25.228(j) allows for the approval of a variance from production measurement equipment used for custody transfer if the variance will result in equal or improved accuracy in measuring hydrocarbons served from the property or unit. 6. West McArthur River and Redoubt Shoal oil volumes can be accurately determined utilizing Micro Motion Coriolis meters, and calibrating the meters monthly. e3 Conservation Order 644 Pa • g West McArthur River, Redoubt Shoal May 6, 2011 7. Commingling of CIE's West McArthur River and Redoubt Shoal oil will not promote waste, affect correlative rights, or result in harm to human health or the environment. NOW, THEREFORE, IT IS ORDERED THAT the following rules, in addition to statewide requirements under 20 AAC 25, apply to the temporary commingling of West McArthur River oil with Redoubt Shoal oil: Rule 1: Commingling of CIE West McArthur River oil with Redoubt Shoal oil at KPF is approved. Rule 2: Use of Coriolis meters is authorized for temporary measurement of oil served from Redoubt Shoal Field. Rule 3: CIE Redoubt Shoal Coriolis meters must be third party calibrated monthly, not to exceed 30 days between calibrations. Commission must be provided forty -eight (48) hours notice for opportunity to witness Coriolis meter calibrations. Rule 4: Analysis of meter calibration results, including raw calibration data, must be provided to the Commission within 7 days of completing a meter calibration. Rule 5: CIE shall provide the Commission with 48 hour notice and opportunity to witness Redoubt Shoal allocation meter calibration. Note that this Order does not authorize Union to store oil at CIE's Kustatan Production Facility. Conservation Order No. 646 governs Union's temporary oil storage at KPF. DONE at Anchorage, Alaska, and dated May 6, 20 1. " n �� orman, Pommissio er la a I it an • as Conservat : • C • •. - 'ssion • ` 4 "4", . N 4 1 Now '91 r Cathy P Foer: er, Commissioner Alaska Oil and Gas Conservation Commission • • Conservation Order 644 Page 4 West McArthur River, Redoubt Shoal May 6, 2011 RECONSIDERATION AND APPEAL NOTICE As provided in AS 31.05.080(a), within 20 days after written notice of the entry of this order or decision, or such further time as the Commission grants for good cause shown, a person affected by it may file with the Commission an application for reconsideration of the matter determined by it. If the notice was mailed, then the period of time shall be 23 days. An application for reconsideration must set out the respect in which the order or decision is believed to be erroneous. The Commission shall grant or refuse the application for reconsideration in whole or in part within 10 days after it is filed. Failure to act on it within 10 -days is a denial of reconsideration. If the Commission denies reconsideration, upon denial, this order or decision and the denial of reconsideration are FINAL and may be appealed to superior court. The appeal MUST be filed within 33 days after the date on which the Commission mails, OR 30 days if the Commission otherwise distributes, the order or decision denying reconsideration, UNLESS the denial is by inaction, in which case the appeal MUST be filed within 40 days after the date on which the application for reconsideration was filed. If the Commission grants an application for reconsideration, this order or decision does not become final. Rather, the order or decision on reconsideration will be the FINAL order or decision of the Commission, and it may be appealed to superior court. That appeal MUST be filed within 33 days after the date on which the Commission mails, OR 30 days if the Commission otherwise distributes, the order or decision on reconsideration. As provided in AS 31.05.080(b), "[t]he questions reviewed on appeal are limited to the questions presented to the Commission by the application for reconsideration." In computing a period of time above, the date of the event or default after which the designated period begins to run is not included in the period; the last day of the period is included, unless it falls on a weekend or state holiday, in which event the period runs until 5:00 p.m. on the next day that does not fall on a weekend or state holiday. • • Colombie, Jody J (DOA) From: Colombie, Jody J (DOA) Sent: Friday, May 06, 2011 1:38 PM To: 'Aaron Gluzman'; Ben Greene; Bettis, Patricia K (DNR); Bruno, Jeff J (PCO); caunderwood @marathonoil.com; 'Dale Hoffman'; David Lenig; 'Donna Vukich'; 'Elizabeth Bluemink'; 'Gary Orr'; Heusser, Heather A (DNR); 'Jason Bergerson'; 'Joe Longo'; 'Lara Coates'; Lois Epstein; Marc Kuck; 'Mary Aschoff; 'Matt Gill'; Maurizio Grandi; Ostrovsky, Larry Z (DNR); Richard Garrard; 'Ryan Daniel'; 'Sandra Lemke'; Steele, Marie C (DNR); Talib Syed; 'Wayne Wooster'; 'William Van Dyke'; Woolf, Wendy C (DNR); '( michael .j.nelson @conocophillips.com)'; '(Von.L .Hutchins @conocophillips.com)'; 'AKDCWeIIIntegrityCoordinator'; 'Alan Dennis'; 'alaska @petrocalc.com; 'Anna Raff; 'Barbara F Fullmer'; 'bbritch'; 'Becky Bohrer'; 'Bill Penrose'; 'Bill Walker'; 'Bowen Roberts'; 'Brady, Jerry L'; 'Brandon Gagnon'; 'Brandow, Cande (ASRC Energy Services)'; 'Brian Havelock'; 'Bruce Webb'; 'caunderwood'; 'Chris Gay'; 'Cliff Posey'; 'Crandall, Krissell'; 'D Lawrence'; 'dapa'; 'Daryl J. Kleppin'; 'Dave Matthews'; 'David Boelens'; 'David House'; 'David Scott'; 'David Steingreaber'; 'ddonkel @cfl.rr.com'; 'Dennis Steffy'; 'Elowe, Kristin'; 'Erika Denman'; 'eyancy'; 'Francis S. Sommer'; 'Fred Steece'; 'Garland Robinson'; 'Gary Laughlin'; 'Gary Schultz (gary.schultz @alaska.gov)'; 'ghammons'; 'Gordon Pospisil'; 'Gorney, David L.'; 'Greg Duggin'; 'Gregg Nady'; 'gspfoff; 'Harry Engel'; 'Jdarlington (jarlington @gmail.com)'; 'Jeanne McPherren'; 'Jeff Jones'; 'Jeffery B. Jones (jeff.jones @alaska.gov)'; 'Jerry McCutcheon'; 'Jill Womack'; 'Jim White'; 'Jim Winegarner; 'Joe Nicks'; 'John Garing'; 'John Katz (john.katz @alaska.gov)'; 'John S. Haworth'; 'John Spain'; 'John Tower'; 'Jon Goltz'; 'Judy Stanek'; 'Julie Houle'; 'Kari Moriarty'; 'Kaynell Zeman'; 'Keith Wiles'; 'Kelly Sperback'; 'Kim Cunningham'; 'Larry Ostrovsky'; 'Laura Silliphant (laura.gregersen @alaska.gov)'; 'Marilyn Crockett; 'Mark Dalton'; 'Mark Hanley (mark.hanley @anadarko.com)'; 'Mark Kovac'; 'Mark P. Worcester'; 'Marguerite kremer (meg.kremer @alaska.gov)'; 'Michael Dammeyer'; 'Michael Jacobs'; 'Mike Bill'; 'Mike Mason'; 'Mikel Schultz'; 'Mindy Lewis'; 'MJ Loveland'; 'mjnelson'; 'mkm7200'; 'nelson'; 'Nick W. Glover'; 'NSK Problem Well Supv'; 'Patty Alfaro'; 'Paul Decker (paul.decker @alaska.gov)'; 'Paul Figel'; 'PORHOLA, STAN T'; 'Randall Kanady'; 'Randy L. Skillern'; 'Rena Delbridge; 'Renan Yanish'; ' rob.g.dragnich @exxonmobil.com'; 'Robert Brelsford'; 'Robert Campbell'; 'Rudy Brueggeman'; 'Ryan Tunseth'; 'Scott Cranswick'; 'Scott Griffith'; 'Shannon Donnelly'; 'Sharmaine Copeland'; Shellenbaum, Diane P (DNR); Slemons, Jonne D (DNR); 'Sondra Stewman'; 'Steve Lambert'; 'Steve Moothart (steve.moothart@alaska.gov)'; 'Steven R. Rossberg'; 'Suzanne Gibson'; 'tablerk'; 'Tamera Sheffield'; Taylor, Cammy 0 (DNR); 'Temple Davidson'; 'Teresa Imm'; 'Terrie Hubble'; 'Thor Cutler; 'Tina Grovier'; 'Todd Durkee'; Tony Hopfinger; trmjrl ; Vicki Irwin; Walter Featherly; Will Chinn; Williamson, Mary J (DNR); Yereth Rosen; Aubert, Winton G (DOA); Ballantine, Tab A (LAW); Brooks, Phoebe; Colombie, Jody J (DOA); Crisp, John H (DOA); Davies, Stephen F (DOA); Fisher, Samantha J (DOA); Foerster, Catherine P (DOA); Grimaldi, Louis R (DOA); Herrera, Matt F (DOA); Johnson, Elaine M (DOA); Jones, Jeffery B (DOA); Laasch, Linda K (DOA); Matt Herrera; Maunder, Thomas E (DOA); McIver, Bren (DOA); McMains, Stephen E (DOA); Mumm, Joseph (DOA sponsored); Noble, Robert C (DOA); Norman, John K (DOA); Okland, Howard D (DOA); Paladijczuk, Tracie L (DOA); Pasqual, Maria (DOA); Regg, James B (DOA); Roby, David S (DOA); Saltmarsh, Arthur C (DOA); Scheve, Charles M (DOA); Schwartz, Guy L (DOA); Seamount, Dan T (DOA); Shartzer, Christine R (DOA) Subject: CO 644 and CO 646 (Cook Inlet) Attachments: co644.pdf; co646.pdf Jody J. Colombie Special Assistant Alaska Oil and Gas Conservation Commission 333 West 7th Avenue, Suite 100 Anchorage, AK 99501 (90 7)793 - 1221 (phone) (90 7)276 -7542 (far) 1 Mary Jones David McCaleb XTO Energy, Inc. IHS Energy Group George Vaught, Jr. Cartography GEPS P.O. Box 13557 810 Houston Street, Ste 200 5333 Westheimer, Suite 100 Denver, CO 80201 -3557 Ft. Worth, TX 76102 -6298 Houston, TX 77056 Jerry Hodgden Richard Neahring Mark Wedman Hodgden Oil Company NRG Associates Halliburton President 408 18 Street 6900 Arctic Blvd. Golden, CO 80401 -2433 P.O. Box 1655 Anchorage, AK 99502 Colorado Springs, CO 80901 Bernie Karl CIRI Baker Oil Tools K &K Recycling Inc. Land Department 795 E. 94 Ct. P.O. Box 58055 P.O. Box 93330 Anchorage, AK 99515 -4295 Fairbanks, AK 99711 Anchorage, AK 99503 North Slope Borough Richard Wagner Gordon Severson Planning Department P.O. Box 60868 3201 Westmar Circle P.O. Box 69 Fairbanks, AK 99706 Anchorage, AK 99508 -4336 Barrow, AK 99723 Jack Hakkila Darwin Waldsmith James Gibbs P.O. Box 190083 P.O. Box 39309 P.O. Box 1597 Anchorage, AK 99519 Ninilchick, AK 99639 Soldotna, AK 99669 Kenai National Wildlife Refuge Penny Vadla Cliff Burglin Refuge Manager 399 West Riverview Avenue 319 Charles Street P.O. Box 2139 Soldotna, AK 99669 -7714 Fairbanks, AK 99701 Soldotna, AK 99669 -2139 ..- ) 1 I `\ C V IP THE STATE 01ALAA SKA GOVERNOR BILL WALKER March 9, 2015 Mr. David Hall CEO Cook Inlet Energy 601 W. 51h Ave., Suite 310 Anchorage, AK 99501 Re: Docket Number: OTH-14-027 Closeout - Notice of Violation Conservation Order 644 Missing Reports Alaska Oil and Gas 333 West Seventh Avenue Anchorage, Alaska 99501-3572 Main- 907 279 1433 Fax 907 276 7542 www aogcc alaska gov The Alaska Oil and Gas Conservation Commission (AOGCC) issued a notice of violation to Cook Inlet Energy dated December 5, 2014 failing to comply with the requirements of Conservation Order 644. Cook Inlet Energy responded on December 18, 2014 with the required calibration reports and corrective actions to improve the quality of its compliance program. The AOGCC does not intend to pursue any further enforcement action regarding the Conservation Order 644 violations. Sincerely, Cathy P. F erster Chair, Commissioner cc: Mr. David Kumar (CIE) Cook Inlet Energy_ December 18, 2014 Ms. Cathy P. Foerster Chair, Commissioner Alaska Oil and Gas Conservation Commission 333 West 7th Ave., Suite 100 Anchorage, Alaska 99501 Re: Docket Number: OTH-14-027-errata Notice of Violation: Missing Reports Conservation Order 644 Dear Commissioner Foerster, RECEIVED DEC 18 2014 ACGCC In response to your letter dated December 5, 2014 related to Conservation Order 644 (CO 644) issued on May 6, 2011, Cook Inlet Energy (CIE) conducted an internal investigation and provides the following information. According to our internal records, CIE was commingling Redoubt Shoal oil processed at Kustatan Production Facility (KPF) and oil from West McArthur River Unit Facility (WMRU), via the 4-inch pipeline in two of the five tanks at KPF. The commingling occurred between June 2011 to November 2011 under guidelines established by CO 644. The micro motion meters in question that required calibration under CO 644 were flow meters installed on the oil leg of the separators that handled processing of all fluids from the Osprey platform (Redoubt Shoal). During the months of June, July and August 2011, there were two separators A & B simultaneously handling production from Redoubt Shoal. CIE later switched over to a single separator, A on September 9, 2011 for the remainder of the period till November 2011. CIE properly calibrated the meters and also kept tank strap records during this period. 601 W. 5'h Avenue, Suite 310, Anchorage, AK 99501 (907) 334-6745 main (907) 334-6735 fax CIE attaches all necessary documentation involving calibration reports for the above mentioned time periods. CIE regretfully did not offer the Commission for an opportunity to witness the calibration event due to failure in communication and follow-up by key personnel. We have internal documentation that upon receiving CO 644, instructions were given to certain personnel to not only calibrate the flow meters as per the regulations but also to provide an opportunity for the Commission to witness the process. Unfortunately even though the calibrations were done properly, the personnel in question responsible for submitting reports and notifying the Commission ahead of time did not follow through. The personnel in question are no longer employed by CIE so it was unable to ascertain exactly what went wrong in our internal procedures and communications with the Commission. However, CIE assures the Commission that we now have in place personnel and procedures to prevent such problems in the future. CIE has been in compliance with other required meter calibration protocols for the last three years. CIE informs the Commission of a typographical error in your letter dated December 5, 2014. Your letter references an email dated July 29, 2014 inquiring about the missing calibration reports; Review of the Commission files for CO 644 reveals that the email is actually dated July 29, 2011.The email enquires whether the meters were calibrated in June and July 2011, and if they were, CIE was to provide the results. CIE assures the Commission that calibration for the above meters were done and are attached to this letter. It should be noted that CIE no longer commingles production from both these fields. An analysis matrix is presented to the Commission to indicate the sequence of events that occurred. Also included are preventative measures to ensure that such incidents do not happen again in the future. CIE is sincerely striving to improve the quality of its compliance program. CIE is also in the process of implementing a rigorous training program with the help of a third party consultant experienced with AOGCC regulations. A new chain of command has also been implemented which will allow for greater oversight and multiple levels of control when it comes to 601 W. 5'h Avenue, Suite 310, Anchorage, AK 99501 (907) 334-6745 main (907) 334-6735 fax compliance. More personnel are being added to the chain of command and being trained to improve the effectiveness and efficiency of the regulatory compliance process. CIE respectfully requests the Commission include notification to the following personnel: David Hall (david.hallgcookinlet.net), David Kumar (david.kumarAcookinlet.neo and Robert Royce (robert.royce(ao,cookinlet.net) any electronic communication concerning Production Practices and related regulations. CIE, on its part, will dutifully inform the Commission of the receipt of the email and the immediate actions taking place in order to keep an open line of communication. CIE thanks the Commission for the opportunity to address this issue. Please do not hesitate to contact me at (907) 433-3804 if the Commission needs anything further. Sincerely, David Hall CEO Cook Inlet Energy Attachments - Analysis Matrix and Preventative Action - Chain of Command - Calibration Reports 601 W. 51h Avenue, Suite 310, Anchorage, AK 99501 (907) 334-6745 main (907) 334-6735 fax Analysis Matrix and Preventive Actions Redoubt Volcanic Eruptions (2009) Sequence prevent oil storage at Drift River of Events terminal Union loses storage capacity due to tank repair and maintainance CIE stores Redoubt Shoal and West McArthur River Oil in two of the five KPF storage tanks CIE asks Commission for commingling approval Commingling occurs from June 2011 to Nov 2011 • Oil storage capacity reduced • Cook Inlet producers advised to directly load into tankers Union asks CIE for storage capacity at KPF facility to prevent shut down of its 11 ESP wells • Commission grants CIE approval and issues CO 644 • Commission requires calibration reports and opportunity to witness calibration • CIE calibrates meters • CIE straps tanks • CIE offers Commission site visit of storage tanks prior to transfer Instruction given to Personnel fail provide personnel as per CO 644 to , Commission with reports provide Commission with and notification for calibration reports and opportunity to witness I witness � i Preventive Steps I Multiple personnel should have been involved in Communication and follow through procedure should have been thoroughly process .executed Integrated chain of command -Chain of command-� Corrective CIE provides Commission implemented for regulatory and training will ensure that with all calibration reports compliance follow through and Actions for the time period CO was . Multiple personnel and communication between utilized training involved in process personnel will be more smooth I and effective Chain of Command Operator Lead Production Operator Foreman i Production Engineer Chief ! Production Operating Manager Officer i AOGCC rRegulatory Manager Cook Inlet Energy Test date: 6/18/11 Tested by: Sig Chester, PCE Pacific, Inc (an Emerson Business Partner) FT-15 Seperator A Oil Flow Sensor Model Number CMF400M436NKBUEAZZ Sensor Serial Number 405625 Meter Verification Summary: Transmitter sensors found to be within 1% - no calibration required at this time. Transmitter Characterization correct. Transmitter Zero Calibration within manufacturer's specifications. Transmitter density calibration within desired specifications. Transmitter diagnostics did not reveal any hidden or intermittent problems. Transmitter meets manufacturer specifications based on testing. kl#f Transmitter Characterization Characteriation Summary The meter factors were verified to match the sensor nameplate values. The slight variations below are a result of coversion between decimal and binary in the transmitter. Nameplate Transmitter Config Model CMF40OM436NKBUEAZZ Serial Number 405625 Flow Cal 4260.43.89 Dens Cal 6206073414 D1 0 0 D2 1 1 TC 4.37 4.37 K1 6206.408 6206.39990 K2 7340.606 7340.60986 FD 608 608 Zero Calibration Zero Calibration Summary The zero was fine, re -zeroing did not produce any appreciable change. No additional zero calibrations were performed, transmitter performance verified to be satisfactory. Mass Low Flow Cutoff currently set to 1.5 kg/min Micro Motion tech support suggests a setting of 9 kg/min - far more than the final sensor zero. 1st Zero 2nd Zero 3rd Zero 4th Zero Mass Flow -0.03 -0.06 n/a n/a (kg/min) For reference only: For CMF400 sensors, mass flow accuracy is +/- 0.1% at 680 kg/min or more flow Zero stability is rated at .68 kg/min For flows below 680 kg/min, accuracy = zero stability/flow rate Density Density Summary Density is the most important secondary value in measuring the flow in this type of sensor. This was verified to be within the required limits. Reference Sample at 60 degF 7.407 pounds/gallon = 0.887554 grams/cubic centimeter Adjusted from chart for 106 degF = .887554 - .016129 = .8714 grams/cubic Centimeter Measured by sensor averaged all valyues when within 0.5 degF over 10 minutes 0.8632 grams / cc Accuracy = measured/known sample = 0.8632/0.8714 = 99.06% W. 9 IN 310 E F. TE PIERAIURIE _ #C 0 Z'6 I M t FLA Inh ItA ■ W. - r- V. lR A I %F E\ E - • '1 :3.1 x .05 = .016129 1owe i (Iensity at 106 deck F Note: Using graphic editor, box was made to same dimension as 1 square on graph. This box was scaled up/down to get desired width For Example, 50 degF scaled to 12% of size to get 6 degF 0.8636 0.8634 0.8632 0.863 8628 ,8626 0.8624 0.8622 0,862 8.5 8,45 8.4 8.35 c .W 8.3 C 8.25 8,2 0.8618 1 ' 8.15 12:02:53 PM 12:04:19 PM 12:05;46 PM 12:07:12 PM 12:08:38 PM 12:10:05 PM 12:11:31 PM 12:12:58 PM 12:14:24 PM 12:15:50 PM —Density(grame/cubic centimeter) —Drive 1200 1000 800 600 - 0 F 400 200 0 12:02 -200 3 PM 12:04:19 PM 12:05.46 PM 12:07:12 PM 12:08:38 PM 12:10:05 PM 12:11:31 PM 12:12:58 PM 12:14:24 PM 12:15: --Mass Flow Rate(kilograms/minute) Density(grams/cubic centimeter) 0.8636 0.8634 0.8632 0.863 0.8624 0.8622 3�.t, 0.8618 0.8636 1 1 108 0.8634 0.8632 0.863 8628 .N c a� 0 8626 0.8624 0.8622 0.862 107.5 107 a� .r T a`) E m H 106.5 106 0.8618 + 1 T 1 T I I I -I ' 105.5 12:02:53 PM 12:04:19 PM 12:05:46 PM 12:07:12 PM 12:08:38 PM 12:10:05 PM 12:11:31 PM 12:12:58 PM 12:14:24 PM 12:15:50 PM Density(grams/cubic centimeter) Temperature(Fahrenheit) 0.4484 0.4483 0.4482 0.4481 a 0.448 0.4479 0.4478 0.4477 0.4476 0.46825 0.4682 0.46815 0.4681 O a 0.46805 0.468 0,46795 0.4679 0.46785 12:02:53 PM 12:04:19 PM 12:05:46 PM 12:07:12 PM 12:08:38 PM 12:10:05 PM 12:11:31 PM 12:12:58 PM 12:14:24 PM 12:15:50 PM 8.5 8.45 8.4 8.35 m �L 8.3 8.25 8.2 8.15 0.4484 0.4483 0.4482 0.4481 0.448 as J 0.4479 0.4478 0.4477 0.4476 12:02:53 PM 12:04:19 PM 12:05:46 PM 12:07:12 PM 12:08:38 PM 12:10:05 PM 12:11:31 PM 12:12:58 PM 12:14:24 PM 12:15:50 PM Drive Gain(%) Left Pickoff Voltage(Volts) 0 a� N N J 350 300 250 200 150 100 50 O.f -50 Live Zero verse Density (scatter graph) ■ ■ ■ ■ r ■ ■ IPi ■ i ■ ■ 18 0.862 m .8628 0.863 01. 8632 0.8634 0.8 Density M 0 a� N CD J 350 300 250 200 150 100 50 -50 Live Zero verse Drive (scatter graph) 20 40 60 80 10 Drive Status -Alarms posted (Each occurrence marked - examine column N in Data worksheet for details) A 12:02:53 PM 12:04:19 PM 12:05:46 PM 12:07:12 PM 12:08:38 PM 12:10:05 PM 12:11:31 PM 12:12:58 PM 12:14:24 PM 12:15:50 PM 12:02: -0.01 U N y g.015 E -0.02 -0.025 -0.03 -0.035 Flow Signal Offset At Zero Flow (Captured values from performing a meter zero) 3 PM 12:04:19 PM 12:05:46 PM 12:07:12 PM 12:08:38 PM 12:10:05 PM 12:11:31 PM 12:12:58 PM 12:14:24 PM 12:15: 50 PM C=�� ffmPCE Pacific,, inc. June 12, 2011 David Hall Cook Inlet Energy 601 West 5th Avenue, Suite 310 Anchorage, AK Dear David, Per your request, this provides a letter of qualification for Sig Chester relative to Micro Motion validation. Sig Chester has had training and industrial experience during the last year on Micro Motion meters so has practical field experience. His report for Cook Inlet Energy was checked by Micro Motion subject matter experts and myself to ensure accuracy. I attest he is qualified to validate the proper operation of Micro Motion Coriolis meters within the constraints as specified in Micro Motion documentation. Regards, Mel Olson Director Business Development PCE Pacific, Inc. Alaska Washington Utah 3700 Woodland Dr- #750 2525 223R0 Street, S.E. 475 W Parkland Dave Anchorage, AK 99517 Bothell, WA 98021 Sandy, UT 84070 (907) 243-3833 FAX (907) 248-0298 (425) 487-9600 FAX (425) 487-1114 (801) 565-4723 FAX (801) 565-3747 Cook Inlet Energy Test date: 6/27/11 Tested by: Sig Chester, PCE Pacific, Inc (an Emerson Business Partner) FT-15 Seperator B Oil Flow Sensor Model Number CMF400M436NKBUEAZZ Sensor Serial Number 406712 Meter Verification Summary: Transmitter was found set for external temp and pressure compensation - since no source, there was no compensation (constant) - this was corrected, now uses internal temperature sensor. Decreased low flow cutoff from 378 to 150 g/sec to improve accuracy. Transmitter sensors found to be within 1% - no calibration required at this time. Transmitter Characterization correct. Transmitter Zero Calibration within manufacturer's specifications. Transmitter density calibration within desired specifications. Transmitter diagnostics did not reveal any hidden or intermittent problems. Transmitter meets manufacturer specifications based on testing. k44 Transmitter Characterization Characteriation Summary The meter factors were verified to match the sensor nameplate values. The slight variations below are a result of coversion between decimal and binary in the transmitter. Nameplate Transmitter Config Model CMF40OM436NKBUEAZZ Serial Number 406712 Flow Cal 4345.13.89 Dens Cal 6127072494 D1 0 0 D2 1 1 TC 4.37 4.37 K1 6127.146 6127.14990 K2 7248.73 7248.72998 FD 608 608 Transmitter Model 170OR13ABUEZZZ Serial Number 2247420 Zero Calibration Zero Calibration Summary The sensor was re -zeroed. Mass Low Flow Cutoff currently set to 378 g/sec Micro Motion tech support suggests a setting of 9 kg/min (150 g/sec)- far more than the final sensor zero. as found 1st Zero 2nd Zero Mass Flow -121 36.5 4.87 (g/sec) For reference only: For CMF400 sensors, mass flow accuracy is +/- 0.1% at 680 kg/min (11,333 g/sec) or more flow Zero stability is rated at .68 kg/min (1,133 g/sec) For flows below 680 kg/min, accuracy = zero stability/flow rate Note: On the trends the zero at 1st appears to be roaming a lot, but this is because of the custom units. Density Density Summary Density is the most important secondary value in measuring the flow in this type of sensor. This was verified to be within the required limits. Reference Sample at 60 degF 7.506 pounds/gallon = 0.899417 grams/cubic centimeter Adjusted from chart for 90 degF = .899417 - .00909 = .890327 grams/cubic Centimeter Measured by sensor averaged all values 89.3062 degF, 0.897118 grams / cc Accuracy = measured/known sample = 0.897118/0.890327 = 100.76% TEPPERA uRE - oC SE TI KiJ 11 550OX 7 OF 90F TEmPERATURE ., * F 100% / 550% x .05 = .00909 g/cu-cm lower density Note: Using graphic editor, box was made to same dimension as 1 square on graph. This box was scaled up/down to get desired width For Example, 50 degF scaled to 12% of size to get 6 degF 0.89975 0.8997 0.89965 M.8996 0,89955 0.8995 0.89945 7.64 7.62 7.6 e c 7.58 C 7.56 7.54 7.52 11:42:43 AM 11:44:10 AM 11:45:36 AM 11:47:02 AM 11:48:29 AM 11:49:55 AM 11:51:22 AM 11:52:48 AM —Density(grams/cubic centimeter) —Drive Gain(°�) 0.9 0.8 0.7 0.6 0 0.5 0.4 0.3 0.2 0.1 0 0.89975 0.8997 0.89965 0.89 c m 0 0.89955 0.8995 0.89945 11:42:43 AM 11:44:10 AM 11:45:36 AM 11:47:02 AM 11:48:29 AM 11:49:55 AM 11:51:22 AM 11:52:48 AM --T--Mass Flow Rate(NONE) Density(grams/cubic centimeter) 0.89975 89.75 0.8997 0.89965 R8996 0.89955 0.8995 0.89945 11:42:43 AM 11:44:10 AM 11:45:36 AM 11:47:02 AM 11:48:29 AM 11:49:55 AM 11:51:22 AM rDensity(grams/cubic centimeter) Temperature(Fahrenheit) 89.7 89.65 89.6 m cu a5 U-) 89.55 89.5 89.45 89.4 11:52:48 AM 0.4592 - ---T 0.4726 0.45915 0.4591 0.45905 a 0.459 0.45895 0.4589 0,45885 0.47255 0.4725 0.47245 O a 0.4724 0.47235 0.4723 0.4588 1 1 1 1 1 1 ' 0.47225 11:42:43 AM 11:44:10 AM 11:45:36 AM 11:47:02 AM 11:48:29 AM 11:49:55 AM 11:51:22 AM 11:52:48 AM 7.64 0.4592 7.62 7.6 m 7.58 7.56 7.54 7.52 -I-- 11:42:43 AM 11:44:10 AM 11:45:36 AM 11:47:02 AM 11:48:29 AM 11:49:55 AM 11:51:22 AM Drive Gain(%) Left Pickoff Voltage(Volts) 0.45915 0.4591 0.45905 0.459 n0 J 0.45895 0.4589 0.45885 --� 0.4588 11:52:48 AM 30 25 20 15 10 Live Zero verse Density (scatter graph) i ■ EL E ■MjP 0 MOM M-1 0 ■ M wom M ■ ■ 945 Cd995 ■ ■ 0.8995". ■ ■ ■T.W396 ■ ■ 5 ■ 0.8997 0.8 M IL Density 975 Live Zero verse Drive (scatter graph) 30 25 -5 4O '1b Status - Alarms posted (Each occurrence marked - examine column N in Data worksheet for details) N 11:42:43 AM 11:44:10 AM 11:45:36 AM 11:47:02 AM 11:48:29 AM 11:49:55 AM 11:51:22 AM 11:52:48 AM Flow Signal Offset At Zero Flow (Captured values from performing a meter zero) 0.16 0.14 0.12 �cU cn 0 U E 11: 1 1. 0.04 0.02 11:42:43 AM 11:44:10 AM 11:45:36 AM 11:47:02 AM 11:48:29 AM 11:49:55 AM 11:51:22 AM 11:52:48 AM ;: 0 C 4 =�� PCE Pacific, Inc. June 12, 2011 David Hall Cook Inlet Energy 601 West 5th Avenue, Suite 310 Anchorage, AK Dear David, Per your request, this provides a letter of qualification for Sig Chester relative to Micro Motion validation. Sig Chester has had training and industrial experience during the last year on Micro Motion meters so has practical field experience. His report for Cook Inlet Energy was checked by Micro Motion subject matter experts and myself to ensure accuracy. I attest he is qualified to validate the proper operation of Micro Motion Coriolis meters within the constraints as specified in Micro Motion documentation. Regards, Mel Olson Director Business Development PCE Pacific, Inc. Alaska Washington Utah 3700 Woodland Dr *750 2525 223RD Street. S.E. 475 W Parkland Drive Anchorage, AK 99517 Bothell. WA 98021 Sandy, UT 84070 (907) 243-3833 FAX (907) 248-0298 (425) 487-9600 FAX (425) 487-1114 (801) 565-4723 FAX (801) 565-3747 Cook Inlet Energy Test date: 7/16/2011 Tested by: Sig Chester, PCE Pacific, Inc (an Emerson Business Partner) Seperator A Oil Flow Sensor Model Number CMF400M436NKBUEAZZ Sensor Serial Number 405625 Meter Verification Summary: The transmitter was swapped with Seperator B to aid troubleshooting of an intermittent fault. All relevant settings were transferred and the transmitter re -zeroed. Transmitter Zero Calibration is within manufacturer's specifications. Transmitter density calibration is within desired specifications. Transmitter diagnostics did not reveal any hidden or intermittent problems. Transmitter meets manufacturer specifications based on testing. k1#4 9( Transmitter Characterization Characteriation Summary The meter factors were verified to match the sensor nameplate values. The slight variations below are a result of coversion between decimal and binary in the transmitter. Nameplate Transmitter Config Model CMF40OM436NKBUEAZZ Serial Number 405625 Flow Cal 4260.43.89 Dens Cal 6206073414 D1 0 0 D2 1 1 TC 4.37 4.37 K1 6206.408 6206.39990 K2 7340.606 7340.60986 FD 608 608 Transmitter Model 170OR13ABUEZZZ Serial Number 2247420 Zero Calibration Zero Calibration Summary The transmitted was swapped with Seperator B for troubleshooting and the sensor was re -zeroed. Mass Low Flow Cutoff currently set to 1.5 kg/min Micro Motion tech support suggests a setting of 9 kg/min - far more than the final sensor zero. After Re -zeroing Mass Flow 2.11 (kg/min) For reference only: For CMF400 sensors, mass flow accuracy is +/- 0.1% at 680 kg/min or more flow Zero stability is rated at .68 kg/min For flows below 680 kg/min, accuracy = zero stability/flow rate Density Density Summary Density is the most important secondary value in measuring the flow in this type of sensor. This was verified to be within the required limits. Reference Sample at 60 degF 7.407 pounds/gallon = 0.887554 grams/cubic centimeter Measured by sensor averaged all values at 73 degF 0.87985 grams / cc Accuracy = measured/known sample = 0.87554/0.87985 = 99.5% 0.87994 0.87992 0.8799 0.87988 7986 7984 0.87982 0.8798 0,87978 0.87976 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM —Density(grems/cubic centimeter) —Drive Gain(%) 8.41 8.4 8.39 8.38 8.37 c .W C9 8.36 O 8.35 8.34 8.33 8.32 12:00:00 AM 8.41 8.4 8.39 8.38 8.37 G 8.36 8.35 8.34 8.33 8.32 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM Drive Gain(%) Left Pickoff Voltage(Volts) 12:00:00 AM 0.44855 0.4485 0.44845 0.448 J 0.44835 0.4483 I 0.44825 12:00:00 AM 2.5 2 1.5 0.5 Live Zero verse Density (scatter graph) ■ ■N09P P m am ■ ■ ■ ■ ■■ �■ ■� j■■ ■ ■ ■ ■WA WA MIN NJ ■■■ 0.87976 0.87978 0.8798 0.87982 0.87984 Density 0.87986 0.87988 0.8799 0,87992 0.87994 0 a) N 2.5 1.5 0.5 Live Zero verse Drive (scatter graph) 20 40 60 80 100 Drive Status -Alarms posted (Each occurrence marked - examine column N in Data worksheet for details) 5] 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM 0 12:00 -0.005 -0.01 -0.015 U 0 0.02 0 U E MIXiYIM -0.03 -0.035 0 "i13 -0.045 -0.05 Flow Signal Offset At Zero Flow (Captured values from performing a meter zero) 0 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00: 0 AM 0.44855 _ 0.4485 0.44845 R-00i .4484 0.44835 - 0.4483 0.44825 1-- 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM 0.469 0.46895 0.4689 0.46885 O n. 0.4688 0.46875 0.4687 -! 0,46865 12:00:00 AM �'I ��II� II I�I.Il.ili j� II��IIiII�I�I I0,8798 Mass Flow Rate(kilograms/minute) Density(grams/cubic centimeter) 0.87994 73.08 0.87992 0.8799 0.87988 7986 a c a� 7984 0.87982 0.8798 0.87978 0.87976 ! 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM Density(grams/cubic centimeter) Temperature(Fahrenheit) 73.06 73.04 73.02 73 a� 72.98 a`") D- E 72.96 WPAOZI! 72.92 72.9 --! 72.88 12:00:00 AM PCE Pacific, Inc. June 12, 2011 David Hall Cook Inlet Energy 601 West 5th Avenue, Suite 310 Anchorage, AK Dear David, Per your request, this provides a letter of qualification for Sig Chester relative to Micro Motion validation. Sig Chester has had training and industrial experience during the last year on Micro Motion meters so has practical field experience. His report for Cook Inlet Energy was checked by Micro Motion subject matter experts and myself to ensure accuracy. I attest he is qualified to validate the proper operation of Micro Motion Coriolis meters within the constraints as specified in Micro Motion documentation. Regards, Mel Olson Director Business Development PCE Pacific, Inc. Alaska Washington XT7 3700 Woodland Dr #750 2525 223RD Street, S.E. 475 W. Parkland Drive Anchorage. AK 99517 Bothell, VA 98021 Sandy, UT 84070 (907) 243-3833 FAX (907) 248-0298 (425) 487-9600 FAX (425) 487-1114 (801) 565-0723 FAX (801) 565-3747 Cook Inlet Energy Test date: 7/16/2011 Tested by: Sig Chester, PCE Pacific, Inc (an Emerson Business Partner) FT-15 Seperator B Oil Flow Sensor Model Number CMF400M436NKBUEAZZ Sensor Serial Number 406712 Meter Verification Summary: The transmitter was swapped with Seperator A to aid troubleshooting of an intermittent fault. All relevant settings were transferred and the transmitter re -zeroed. Transmitter Zero Calibration is within manufacturer's specifications. Transmitter density calibration is within desired specifications. Transmitter diagnostics did not reveal any hidden or intermittent problems. Transmitter meets manufacturer specifications based on testing. k1#4 #/ Transmitter Characterization Characteriation Summary The meter factors were verified to match the sensor nameplate values. The slight variations below are a result of coversion between decimal and binary in the transmitter. Nameplate Transmitter Config Model CMF40OM436NKBUEAZZ Serial Number 406712 Flow Cal 4345.13.89 Dens Cal 6127072494 D1 0 0 D2 1 1 TC 4.37 4.37 K1 6127.146 6127.14990 K2 7248.73 7248.72998 FD 608 608 Zero Calibration Zero Calibration Summary The transmitted was swapped with Seperator A for troubleshooting and the sensor was re -zeroed. Micro Motion tech support suggests a setting of 9 kg/min - far more than the final sensor zero. After Re -zeroing Mass Flow 0.27 (kg/min) For reference only: For CMF400 sensors, mass flow accuracy is +/- 0.1% at 680 kg/min or more flow Zero stability is rated at .68 kg/min For flows below 680 kg/min, accuracy = zero stability/flow rate Density Density Summary Density is the most important secondary value in measuring the flow in this type of sensor. This was verified to be within the required limits. Reference Sample at 60 degF 7.407 pounds/gallon = 0.887554 grams/cubic centimeter Adjusted from chart for 90 degF = .887554 - .00909 = .87845 grams/cubic Centimeter Measured by sensor averaged all values 99.4 degF, 0.870631 grams / cc Accuracy = measured/known sample = 0.87845/0.870531=100.9% 0.8707 0.87065 0.8706 — 7055 .y c .8705 0.87045 0.8704 0.87035 12:00:00 AM 12:00;00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM —Density(grems/cubic centimeter)—DhveGeinN 7.51 7.5 7.49 7.48 7.47 7.46 7.45 G 7.44 7.43 7.42 7.41 7A 12:00:00 AM 0.9 0.8 0.7 0.6 0 0.5 LL 0.4 0.3 0.2 0.1 0 0.8707 0.87065 0.8706 0.87055 N C N 0.8705 0.87045 0.8704 0.87035 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM ---Mass Flow Rate(kilograms/minute) Density(grams/cubic centimeter) 0.8707 0.87065 0.8706 0.87055 N 0.8705 0.87045 0.8704 0.87035 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM Density(grams/cubic centimeter) Temperature(Fahrenheit) 99.7 99.6 99.5 99.4 cu a) a E 99.3 ' Uzi 99.2 99.1 99 12:00:00 AM 0.4605 -r-- 0.47405 0.46045 0.4604 0.46035 a J 0.4603 0.46025 0.4602 0.474 0.47395 0.473� IL 0.47385 0.4738 0.46015 1 1 1 1 1 0.47375 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM 7.51 7.5 7.49 7.48 7.47 7.46 d c 7.45 7.44 7.43 7.42 7.41 7.4 V I� 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM Drive Gain(%) Left Pickoff Voltage(Volts) 0.4605 0.46045 0.4604 0.46035 0 a 0.4603 0.46025 0.4602 0.46015 12:00:00 AM 12:00:00 AM 0 a) N N :J 0.5 0.4 0.3 0.2 0.1 0 4- 0.87035 Live Zero verse Density (scatter graph) Owmm on ■ ■ ■ ■ ■. ■ ■ . ■ .. ■- ME ■ . E16 .. ■ ■ ■: ■ ■ ■ i ■ ■ ■ ■ � r ■ ■ ■ ■ ' ■ IP^ ME■ ■ ON ■ ■■ ■ a ■ ■ ■ 0.8704 0.87045 0.8705 0.87055 0.8706 0.87065 0.8707 Density 0 am N N J 0.6 0.5 ' ■ ■ 0.4 0.3 0.2 0.1 ■ ■ Live Zero verse Drive (scatter graph) 20 40 60 80 100 Drive Status - Alarms posted (Each occurrence marked - examine column N in Data worksheet for details) 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM Flow Signal Offset At Zero Flow (Captured values from performing a meter zero) 0.16 0.14 0.12 to 03 0 U E Ili I li 0.04 0.02 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM PCE Pacific, Inc. June 12, 2011 David Hall Cook Inlet Energy 601 West 5th Avenue, Suite 310 Anchorage, AK Dear David, Per your request, this provides a letter of qualification for Sig Chester relative to Micro Motion validation. Sig Chester has had training and industrial experience during the last year on Micro Motion meters so has practical field experience. His report for Cook Inlet Energy was checked by Micro Motion subject matter experts and myself to ensure accuracy. I attest he is qualified to validate the proper operation of Micro Motion Coriolis meters within the constraints as specified in Micro Motion documentation. Regards, Mel Olson Director Business Development PCE Pacific, Inc. Alaska Washington 1177 3700 Woodland Dr #750 2525 223RD Street, S.E. 475 W Parkland Drive Anchorage, AK 99517 Bothell, WA 98021 Sandy, UT 84070 (907) 243-3833 FAX (907) 248-0298 (425) 487-9600 FAX (425) 487-1114 (801) 565.4723 FAX (801) 565-3747 Cook Inlet Energy Test date: 8/15/2011 Tested by: Sig Chester, PCE Pacific, Inc (an Emerson Business Partner) FT-2005-15 Seperator A Oil Flow Sensor Model Number CMF400M436NKBUEAZZ Sensor Serial Number 405625 Meter Verification Summary: Transmitter Zero Calibration is within manufacturer's specifications. Transmitter density calibration is within desired specifications. Transmitter diagnostics did not reveal any hidden or intermittent problems. Transmitter meets manufacturer specifications based on testing. k1#4 Transmitter Characterization Characteriation Summary The meter factors were verified to match the sensor nameplate values. The slight variations below are a result of coversion between decimal and binary in the transmitter. Nameplate Transmitter Config Model CMF40OM436NKBUEAZZ Serial Number 405625 Flow Cal 4260.43.89 Dens Cal 6206073414 D1 0 0 D2 1 1 TC 4.37 4.37 K1 6206.408 6206.39990 K2 7340.606 7340.60986 FD 608 .608 Transmitter Model 170OR13ABUEZZZ Serial Number 2247420 Zero Calibration Zero Calibration Summary Transmitter re -zeroed. New and old zero offset well within manufacturer's recommended low flow cutoff. Mass Low Flow Cutoff currently set to 1.5 kg/min Micro Motion tech support suggests a setting of 9 kg/min - far more than the final sensor zero. Wound 1st Zero Mass Flow -6.17 1.09 (kg/min) For reference only: For CMF400 sensors, mass flow accuracy is +/- 0.1% at 680 kg/min or more flow Zero stability is rated at .68 kg/min For flows below 680 kg/min, accuracy = zero stability/flow rate Density Density Summary A lab sample was taken of the process fluid used in this test. Density is the most important secondary value in measuring the flow in this type of sensor. This was verified to be within the required limits. Reference Sample at 60 degF 0.87865 grams/cubic centimeter At 92.51 degF density should be 0.86559 grams/cubic centimeter Measured by sensor averaged all values at 92.51 degF 0.86877 grams / cc Accuracy = measured/known sample = 0.86877/0.86559=100.37% 0.8698 0.8696 0.8694 0,8692 0.869 8688 0.8686 0,8684 0.8682 0,868 8.46 8,44 8.42 8.4 8.38 e c 8.36 'C 8.34 8.32 8.3 8.28 0.8678 i— 1 8.26 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM —Density(grams/cubic centimeter)—DriveGeln(°�) 1000 EKE 0 400 200 0 12:00 -200 0 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM AM 12:00:00 AM 12:00: Mass Flow Rate(kilograms/minute) Density(grams/cubic centimeter) 0.8698 0.8696 0.8694 0.8692 0.869 0.86 c m 0 0.8686 0.8684 0.8682 30 AM - 0.868 - 0.8678 0.8698 0.8696 0.8694 0.8692 — 0.869 M8688 0.8686 0.8684 0.8682 0.868 0.8678 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM Density(grams/cubic centimeter) Temperature(Fahrenheit) 93.4 93.2 93 92.8 92.6 m Cu 92.4 `m a E m 92.2 WYN 91.8 91.6 ' 91.4 12:00:00 AM 12:00:00 AM 0.4485 0.4484 0.4483 0.4482 na 0.4481 0.448 0.4479 0.4478 0.46865 [11U.T. [IM,1:1;311 O a 0.46845 0.4684 0.46835 0.4683 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM 8.46 8.44 8.42 8.4 8.38 m L 8.36 0 8.34 8.32 8.3 8.28 8.26 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM Drive Gain(%) Left Pickoff Voltage(Volts) 0.4485 0.4484 0.4483 0.4482 O IL J 0.4481 0.448 0.4479 0.4478 12:00:00 AM 12:00:00 AM 12:00:00 AM Live Zero verse Density (scatter graph) 700 500 400 300 200 100 0.8678 0.868 0.8682 0.8684 0.8686 0.8688 Density 0.869 0.8692 0.8694 0.8696 0.8698 a) N J 700 - 500 400 300 200 100 Live Zero verse Drive (scatter graph) 1 i 20 40 60 80 100 Drive Status - Alarms posted (Each occurrence marked - examine column N in Data worksheet for details) 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00 -0.01 -0.02 ra M y O U U E -0.04 -0.05 -0.07 M Flow Signal Offset At Zero Flow (Captured values from performing a meter zero) 0 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00:00 AM 12:00: 10 AM PCE Pacific, Inc. June 12, 2011 David Hall Cook Inlet Energy 601 West 5th Avenue, Suite 310 Anchorage, AK Dear David, Per your request, this provides a letter of qualification for Sig Chester relative to Micro Motion validation. Sig Chester has had training and industrial experience during the last year on Micro Motion meters so has practical field experience. His report for Cook Inlet Energy was checked by Micro Motion subject matter experts and myself to ensure accuracy. I attest he is qualified to validate the proper operation of Micro Motion Coriolis meters within the constraints as specified in Micro Motion documentation. Regards, Mel Olson Director Business Development PCE Pacific, Inc. Alaska VMashington 1iT7 3700 Woodland Dr. #750 2525 223RD Street. S.E 475 W Parldand Drive .Anchorage. AK 99517 Bothell, WA 98021 Sandy, UT 84070 (907) 243-3833 FAX (907) 248-0298 (425) 487-9600 FAX (425) 487-1114 (801) 565A723 FAX (801) 565-3747 Cook Inlet Energy Test date: 8/15/2011 Tested by: Sig Chester, PCE Pacific, Inc (an Emerson Business Partner) FT-2006-15 Seperator B Oil Flow Sensor Model Number CMF400M436NKBUEAZZ Sensor Serial Number 406712 Meter Verification Summary: Transmitter Zero Calibration is within manufacturer's specifications. Transmitter density calibration is within desired specifications. Transmitter diagnostics did not reveal any hidden or intermittent problems. Transmitter meets manufacturer specifications based on testing. k1#4 91 Transmitter Characterization Characteriation Summary The meter factors were verified to match the sensor nameplate values. The slight variations below are a result of coversion between decimal and binary in the transmitter. Nameplate Transmitter Config Model CMF40OM436NKBUEAZZ Serial Number 406712 Flow Cal 4345.13.89 Dens Cal 6127072494 D1 0 0 D2 1 1 TC 4.37 4.37 K1 6127.146 6127.14990 K2 7248.73 7248.72998 FD 608 608 Zero Calibration Zero Calibration Summary Re -zeroed. Micro Motion tech support suggests a setting of 9 kg/min - far more than the final sensor zero. As found 1st re -zero Mass Flow -2.139 -0.21 (kg/min) For reference only: For CMF400 sensors, mass flow accuracy is +/- 0.1% at 680 kg/min or more flow Zero stability is rated at .68 kg/min For flows below 680 kg/min, accuracy = zero stability/flow rate Density Density Summary A sample was taken to a lab to measure the density of the process fluid used in this test. Density is the most important secondary value in measuring the flow in this type of sensor. This was verified to be within the required limits. Reference Sample at 60 degF 0.88140 grams/cubic centimeter Adjusted from worksheet for 107.47 degF = .86253 grams/cubic Centimeter Measured by sensor averaged all values 107.47 degF, .86610 grams / cc Accuracy = measured/known sample = 0.86610/0.86253=100.4% 0.868 0.8675 0.867 0.8665 M.866 aci G .8655 0.865 0.8645 0.864 0.8635 12:34:34 PM 12:37:26 PM 12:40:19 PM 12:43:12 PM 12:46:05 PM 12:48:58 PM 12:51:50 PM —Density(grams/cubic centimeter) —Drive Gain(°�) 7.5 7.48 7.46 7.44 a c 7.42 6 t9 m 7.4 7.38 7.36 7.34 12:54:43 PM 12:57:36 PM 1 0.9 0.8 0.7 0.6 6 0.5 LL 0.4 0.3 0.2 0.1 0 12:34:34 PM 12:37:26 PM 12:40:19 PM 12:43:12 PM 12:46:05 PM 12:48:58 PM 12:51:50 PM 12:54:43 PM Mass Flow Rate(kilograms/minute) Density(grams/cubic centimeter) 0.8675 0.867 0.8665 0.866 .N c 0 0.865 0.865 0.8645 0.864 1 0.8635 12:57:36 PM 0.868 111 0.8675 0.867 0.8665 .866 T cn C N C) 8655 0.865 0.8645 0.864 110 109 108 2 f9 U-) 107 KT 105 0.8635 1 1 1 1 r 104 12:34:34 PM 12:37:26 PM 12:40:19 PM 12:43:12 PM 12:46:05 PM 12:48:58 PM 12:51:50 PM 12:54:43 PM 12:57:36 PM Density(grams/cubic centimeter) Temperature(Fahrenheit) 0.4607 0.4606 0.4605 m 0 .4603 0.4602 0.4601 0.46 0.4599 0.47395 0.4739 0.47385 0.4738 0.47375 0.4730- 7 0.47365 0.4736 0.47355 0.4735 0.47345 12:34:34 PM 12:37:26 PM 12:40:19 PM 12:43:12 PM 12:46:05 PM 12:48:58 PM 12:51:50 PM 12:54:43 PM 12:57:36 PM 7.5 7.48 7.46 7.44 m 7.42 7.4 7.38 7.36 7.34 0.4607 0.4606 0.4605 0.4604 0.460'n�. J 0.4602 0.4601 0.46 0.4599 12:34:34 PM 12:37:26 PM 12:40:19 PM 12:43:12 PM 12:46:05 PM 12:48:58 PM 12:51:50 PM 12:54:43 PM 12:57:36 PM Drive Gain(%) Left Pickoff Voltage(Volts) 0 a� N N J 10 - 0.E -2 Live Zero verse Density (scatter graph) ■ ■ ■ ■ ■ ■ 35 %jF .8645 0.865 0.8655 6 0.8665 5 0. Density m 10 - -2 Live Zero verse Drive (scatter graph) ■ ■ ■ ■ ■ ---------------- 20 40 60 80 10 Drive Status -Alarms posted (Each occurrence marked - examine column N in Data worksheet for details) 12:34:34 PM 12:37:26 PM 12:40:19 PM 12:43:12 PM 12:46:05 PM 12:48:58 PM 12:51:50 PM 12:54:43 PM 12:57:36 PM Flow Signal Offset At Zero Flow (Captured values from performing a meter zero) 0.16 0.14 0.12 '. cn 0 U_ E 1 1: 11• 0.04 0.02 12:34:34 PM 12:37:26 PM 12:40:19 PM 12:43:12 PM 12:46:05 PM 12:48:58 PM 12:51:50 PM 12:54:43 PM 12:57:36 PM ;DC4 PCE Pacific, Inc. June 12, 2011 David Hall Cook Inlet Energy 601 West 5th Avenue, Suite 310 Anchorage, AK Dear David, Per your request, this provides a letter of qualification for Sig Chester relative to Micro Motion validation. Sig Chester has had training and industrial experience during the last year on Micro Motion meters so has practical field experience. His report for Cook Inlet Energy was checked by Micro Motion subject matter experts and myself to ensure accuracy. I attest he is qualified to validate the proper operation of Micro Motion Coriolis meters within the constraints as specified in Micro Motion documentation. Regards, Mel Olson Director Business Development PCE Pacific, Inc. Alaska Washington Utah 3700 VWbodland Dr. #750 2525 223RD Street, S.E. 475 W ParWand Drive Anchorage, AK 99517 Bothell, WA 98021 Sandy, UT 84070 (907) 243-3833 FAX (907) 248-0298 (425) 487-9600 FAX (425) 487-1114 (801) 565-4723 FAX (801) 565-3747 Cook Inlet Energy Test date: Sept 9, 2011 Tested by: Sig Chester, PCE Pacific, Inc (an Emerson Business Partner) FT-2005-15 Seperator A Oil Flow Sensor Model Number CMF400M436NKBUEAZZ Sensor Serial Number 405625 Meter Verification Summary: Transmitter Zero Calibration is within manufacturer's specifications. Transmitter density calibration is within desired specifications. Transmitter diagnostics did not reveal any hidden or intermittent problems. Transmitter meets manufacturer specifications based on testing. k1#9 #'I Transmitter Characterization Characteriation Summary The meter factors were verified to match the sensor nameplate values. The slight variations below are a result of coversion between decimal and binary in the transmitter. Nameplate Transmitter Config Model CMF40OM436NKBUEAZZ Serial Number 405625 Flow Cal 4260.43.89 Dens Cal 6206073414 D1 0 0 D2 1 1 TC 4.37 4.37 K1 6206.408 6206.39990 K2 7340.606 7340.60986 FD 608 608 Transmitter Model 170OR13ABUEZZZ Serial Number 2247420 Zero Calibration Zero Calibration Summary No need to re -zero transmitter Mass Low Flow Cutoff currently set to 1.5 kg/min Micro Motion tech support suggests a setting of 9 kg/min - far more than the final sensor zero. Wound Mass Flow 0.362 (kg/min) For reference only: For CMF400 sensors, mass flow accuracy is +/- 0.1% at 680 kg/min or more flow Zero stability is rated at .68 kg/min For flows below 680 kg/min, accuracy = zero stability/flow rate Density Density Summary A lab sample was taken of the process fluid used in this test. Density is the most important secondary value in measuring the flow in this type of sensor. This was verified to be within the required limits. Reference Sample at 60 degF 0.87865 grams/cubic centimeter At 101.5 degF density should be 0.86206 grams/cubic centimeter Measured by sensor averaged all values at 101.5 degF 0.8651 grams / cc Accuracy = measured/known sample = 0.8651/0.86206=100.4% 8.39 8.38 8.37 8.36 8.35 8.34 m L f� 8.33 8.32 8.31 8.3 8.29 0.4481 0.44805 0.448 0.44795 0.4479 O a J 0.44785 0.4478 0.44775 0.4477 8.28 ! 1 1 1 1 1 1 1 ' 0.44765 12:25:55 PM 12:27:22 PM 12:28:48 PM 12:30:14 PM 12:31:41 PM 12:33:07 PM 12:34:34 PM 12:36:00 PM 12:37:26 PM 12:38:53 PM Drive Gain(%) Left Pickoff Voltage(Volts) .11 500 MIA 300 200 100 Live Zero verse Density (scatter graph) ■ ■ ■ ■ ■ ■ ■ ■ 0.864 0.8642 0.8644 0.8646 0.8648 Density 0.865 0.8652 0.8654 0.8656 0.8658 .11 500 400 300 200 100 ■ ■ ■ ■ ■ ■ ■ ■ ■ Live Zero verse Drive (scatter graph) 20 40 60 80 100 Drive Status -Alarms posted (Each occurrence marked - examine column N in Data worksheet for details) 181 12:25:55 PM 12:27:22 PM 12:28:48 PM 12:30:14 PM 12:31:41 PM 12:33:07 PM 12:34:34 PM 12:36:00 PM 12:37:26 PM 12:38:53 PM 12:25: -0.01 -0.02 C y O V E -0.04 -0.05 -0.07 Flow Signal Offset At Zero Flow (Captured values from performing a meter zero) 5 PM 12:27:22 PM 12:28:48 PM 12:30:14 PM 12:31:41 PM 12:33:07 PM 12:34:34 PM 12:36:00 PM 12:37:26 PM 12:38: 53 PM 0.4481 , 1 0.4684 0.44805 0.448 0.44795 0.4479 Ma J 0.44785 0.4478 0.44775 0.4477 0.46835 0.4683 0.46825 0.4682 0 a w 0.46815 0.4681 0.46805 0.468 0.44765 1 1 1 1 1 1 1 1 ' 0.46795 12:25:55 PM 12:27:22 PM 12:28:48 PM 12:30:14 PM 12:31:41 PM 12:33:07 PM 12:34:34 PM 12:36:00 PM 12:37:26 PM 12:38:53 PM 1000 - :II .ON MLL 400 200 12:25 -200 ft A.A%X�"k Al JV/ 5 PM 12:2742 PM 12:28:48 PM 12:30:14 PM 12:31:41 PM 12:33:07 PM 12:34:34 PM 12:36:00 PM 12:37:26 PM 12:38: Mass Flow Rate(kilograms/minute) Density(grams/cubic centimeter) 0.8658 0.8656 0.8654 0.8652 0.865 T c a� 0.864.N 0.8646 0.8644 i30P8642 0.864 0.8658 0.8656 0.8654 0.8652 0.8646 0.8644 0.8642 102.4 102.2 102 101.8 a� L F+ 101.6 aco") CL CD 101.4 101.2 101 0.864 1 1 1 1 1 1 ' 100.8 12:25:55 PM 12:27:22 PM 12:28:48 PM 12:30:14 PM 12:31:41 PM 12:33:07 PM 12:34:34 PM 12:36:00 PM 12:37:26 PM 12:38:53 PM Density(grams/cubic centimeter) Temperature(Fahrenheit) 0.8658 0.8656 0.8654 0.8652 " .865 .8848 0.8646 0.8644 0.8642 8.39 8.38 8.37 8.36 8.35 8.34 c C9 8.33 O 8.32 8.31 8.3 8.29 0.864 1 1 8.28 12:25:55 PM 12:27:22 PM 12:28:48 PM 12:30:14 PM 12:31:41 PM 12:33:07 PM 12:34:34 PM 12:36:00 PM 12:37:26 PM 12:38:53 PM —Density(grams/cubic centimeter) —Drive Gain(%) ; 4 = d�� PCE Pacific, Inc. June 12, 2011 David Hall Cook Inlet Energy 601 West 5th Avenue, Suite 310 Anchorage, AK Dear David, Per your request, this provides a letter of qualification for Sig Chester relative to Micro Motion validation. Sig Chester has had training and industrial experience during the last year on Micro Motion meters so has practical field experience. His report for Cook Inlet Energy was checked by Micro Motion subject matter experts and myself to ensure accuracy. I attest he is qualified to validate the proper operation of Micro Motion Coriolis meters within the constraints as specified in Micro Motion documentation. Regards, Mel Olson Director Business Development PCE Pacific, Inc. Alaska Washington Utah 3700 Vlbodland Dr. #750 2525 223RD Street, S.E. 475 W Paridand Drive Anchorage, AK 99517 Bothell, WA 98021 Sandy, UT 84070 (907) 243-3833 FAX (907) 248-0298 (425) 487-9600 FAX (425) 487-1114 (801) 565-4723 FAX (801) 565-3747 Cook Inlet Energy Test date: Sept 9, 2011 Tested by: Sig Chester, PCE Pacific, Inc (an Emerson Business Partner) FT-2006-15 Seperator B Oil Flow Sensor Model Number CMF40OM436NKBUEAZZ Sensor Serial Number 406712 Meter Verification Summary: Transmitter Zero Calibration is within manufacturer's specifications. Transmitter density calibration is within desired specifications. Transmitter diagnostics did not reveal any hidden or intermittent problems. Transmitter meets manufacturer specifications based on testing. k1#9 Transmitter Characterization Characteriation Summary The meter factors were verified to match the sensor nameplate values. The slight variations below are a result of coversion between decimal and binary in the transmitter. Nameplate Transmitter Config Model CMF40OM436NKBUEAZZ Serial Number 406712 Flow Cal 4345.13.89 Dens Cal 6127072494 D1 0 0 D2 1 1 TC 4.37 4.37 Kl 6127.146 6127.14990 K2 7248.73 7248.72998 FD 608 608 Zero Calibration Zero Calibration Summary Zero was accurate - I did not rezero. Micro Motion tech support suggests a setting of 9 kg/min - far more than the final sensor zero. Wound Mass Flow 0.23 (kg/min) For reference only: For CMF400 sensors, mass flow accuracy is +/- 0.1% at 680 kg/min or more flow Zero stability is rated at .68 kg/min For flows below 680 kg/min, accuracy = zero stability/flow rate Density Density Summary Density is the most important secondary value in measuring the flow in this type of sensor. This was verified to be within the required limits. Reference Sample at 60 degF 0.88140 grams/cubic centimeter Adjusted from worksheet for 102.7 degF = .8644 grams/cubic Centimeter Measured by sensor averaged all values 102.7 degF, .8672 grams / cc Accuracy = measured/known sample = 0.8672/0.8644=100.3% 7.54 T 0.4604 7.52 7.5 7.48 > 7.46 0 7.42 7.4 0.46035 0.4603 0.46025 0.46022 J 0.46015 0.4601 0.46005 7.38 I 1 1 1 1 1 1 ' 0.46 11:06:43 AM 11:08:10 AM 11:09:36 AM 11:11:02 AM 11:12:29 AM 11:13:55 AM 11:15:22 AM 11:16:48 AM 11:18:14 AM Drive Gain(%) Left Pickoff Voltage(Volts) 0 a� N N J 1.6 1.4 1.2 1 0.8 0.6 0.4 0.2 0 0.8E -0.2 - -0.4 -0.6 Live Zero verse Density (scatter graph) ■ MEN mm ■ ■ ■ ■ 705 00.867 J � .86715 ■ 1686 ■ ■ O.8673 0.86735 0.8674 0.8 ■ ■■ m NBC ■ Density �745 0 m N N J 1.6 1.4 1.2 1 0.8 0.6 0.4 0.2 0 -0.2 -0.4 -0.6 Live Zero verse Drive (scatter graph) ■ ■ ■ ■ ■ 20 40 60 80 10 Drive Status -Alarms posted (Each occurrence marked - examine column N in Data worksheet for details) 11:06:43 AM 11:08:10 AM 11:09:36 AM 11:11:02 AM 11:12:29 AM 11:13:55 AM 11:15:22 AM 11:16:48 AM 11:18:14 AM Flow Signal Offset At Zero Flow (Captured values from performing a meter zero) 1 0.14 0.12 701 cn 0 U_ E 1 1: 1 1. 0.04 0.02 11:06:43 AM 11:08:10 AM 11:09:36 AM 11:11:02 AM 11:12:29 AM 11:13:55 AM 11:15:22 AM 11:16:48 AM 11:18:14 AM 0.4604 - 0.46035 t 0.4603 0.46025 a.4602 -- I 0.46015 I, 0.4601 — 0.46005 0.4741 0.47405 0.474 0.47395 O a 0.4739 0.47385 0.4738 0.46 1 1 1 1 1 1 1- ' 0.47375 11:06:43 AM 11:08:10 AM 11:09:36 AM 11:11:02 AM 11:12:29 AM 1113:55 AM 11:15:22 AM 11:16:48 AM 1118:14 AM 1 0.9 0.8 0.7 0.6 0 0.5 u_ 0.4 0.3 0.2 0.1 0.86745 0.8674 0.86735 0.8673 0.86 m 0 0.8672 0.86715 0.8671 0 1 -T 1 ' 0.86705 11:06:43 AM 11:08:10 AM 11:09:36 AM 11:11:02 AM 11:12:29 AM 11:13:55 AM 11:15:22 AM 11:16:48 AM 11:18:14 AM Mass Flow Rate(kilograms/minute) Density(grams/cubic centimeter) 0.86745 103.2 0.8674 0.86735 0.8673 M6725 0.8672 0.86715 0.8671 0.86705 ! 11:06:43 AM 11:08:10 AM 11:09:36 AM 11:11:02 AM 11:12:29 AM 11:13:55 AM 11:15:22 AM Density(grams/cubic centimeter) Temperature(Fahrenheit) 103.1 103 102.9 102.8 (D 102.7 aCo") E m F- 102.6 102.5 102.4 102.3 -- I 102.2 11:16:48 AM 11:18:14 AM 0.86745 0.8674 0.86735 0.8673 6725 0.8672 0,86715 0.8671 7.54 7.52 7.5 7.48 e c_ 7.46 m O 7.44 7.42 7.4 0.86705 1 I 7.38 11:06:43 AM 11:08:10 AM 11:09:36 AM 11:11:02 AM 11:12:29 AM 11:13:55 AM 11:15:22 AM 11:16:48 AM 11:18:14 AM —Density(grams/cubic centimeter) —Drive Gain(%) PCE Pacific, Inc. June 12, 2011 David Hall Cook Inlet Energy 601 West 5th Avenue, Suite 310 Anchorage, AK Dear David, Per your request, this provides a letter of qualification for Sig Chester relative to Micro Motion va iodation. Sig Chester has had training and industrial experience during the last year on Micro Motion meters so has practical field experience. His report for Cook Inlet Energy was checked by Micro Motion subject matter experts and myself to ensure accuracy. I attest he is qualified to validate the proper operation of Micro Motion Coriolis meters within the constraints as specified in Micro Motion documentation Regards, Mel Olson Director Business Development PCE Pacific, Inc. Alaska Washington Utah 3700 Vkbod4and Dr. #750 2525 223RD Street, S.E. 475 W Parkland Drive Anchorage, AK 99517 Bothell, WA 98021 Sandy, UT E4070 (907) 243-3833 FAX (907) 248-0298 (425) 487-9600 FAX (425) 487-1114 (801) 565-4723 FAX l801) 565-3747 Cook Inlet Energy Test date: October 8, 2011 Tested by: Sig Chester, PCE Pacific, Inc (an Emerson Business Partner) FT-2005-15 Seperator A Oil Flow Sensor Model Number CMF40OM436NKBUEAZZ Sensor Serial Number 405625 Meter Verification Summary: Transmitter Zero Calibration is within manufacturer's specifications. Transmitter density calibration is within desired specifications. Transmitter diagnostics did not reveal any hidden or intermittent problems. Transmitter meets manufacturer specifications based on testing. Transmitter Characterization Characteriation Summary The meter factors were verified to match the sensor nameplate values. The slight variations below are a result of coversion between decimal and binary in the transmitter. Nameplate Transmitter Config Model CMF40OM436NKBUEAZZ Serial Number 405625 Flow Cal 4260.43.89 Dens Cal 6206073414 D1 0 0 D2 1 1 TC 4.37 4.37 K1 6206.408 6206.39990 K2 7340.606 7340.60986 FD 608 608 Transmitter Model 170OR13ABUEZZZ Serial Number 2247420 Zero Calibration Zero Calibration Summary Transmitter re -zeroed Mass Low Flow Cutoff currently set to 1.5 kg/min Micro Motion tech support suggests a setting of 9 kg/min - far more than the final sensor zero. Wound istZero Mass Flow -2.25 0.41 (kg/min) For reference only: For CMF400 sensors, mass flow accuracy is +/- 0.1% at 680 kg/min or more flow Zero stability is rated at .68 kg/min For flows below 680 kg/min, accuracy = zero stability/flow rate Density Density Summary A lab sample was taken of the process fluid used in this test. Density is the most important secondary value in measuring the flow in this type of sensor. This was verified to be within the required limits. Reference Sample at 60 degF 0.87865 grams/cubic centimeter At 111.9 degF density should be 0.8583 grams/cubic centimeter Measured by sensor averaged all values at 111.9 degF 0.8632 grams / cc Accuracy = measured/known sample = 0.8583/0.8632 = 99.4% 0.865 0.8645 0.864 c .8635 0.863 0.8625 8.48 8.46 8.44 8.42 8.4 8.38 c 8.36 •c 0 8.34 8.32 8.3 8.28 0.862 1 T T 1 8.26 1115:22 AM 11:16:48 AM 11:18:14 AM 11:19:41 AM 11:21:07 AM 11:22:34 AM 11:24:00 AM 11:25:26 AM 11:26:53 AM 11:28:19 AM 11:29:46 AM —Density(grams/cubic centimeter) —Drive Gain(%) 1200 1000 800 600 n 400 200 0 11:1: -200 Mass Flow Rate(kilograms/minute)—Dens ity(grams/cubic centimeter) ).8645 ).864 86 c m 0.863 0.8625 AM 0.862 0.865 0.8645 0.864 M8635 0.863 0.8625 0.862 113.5 113 112.5 112 a� cu cu 111.5 CL aD 111 110.5 110 109.5 11:15:22 AM 11:16:48 AM 11:18:14 AM 11:19:41 AM 11:21:07 AM 11:22:34 AM 11:24:00 AM 11:25:26 AM 11:26:53 AM 11:28:19 AM 11:29:46 AM Density(grams/cubic centimeter) Temperature(Fahrenheit) 0.4495 0.449 0.4485 ME 0.448 0.4475 0.447 0.4684 0.4682 0.468 0.4678 0.467E 0.4674 [II[P:11&j 0.467 0.4668 11:15:22 AM 11:16:48 AM 11:18:14 AM 11:19:41 AM 11:21:07 AM 11:22:34 AM 11:24:00 AM 11:25:26 AM 11:26:53 AM 11:28:19 AM 11:29:46 AM 8.48 8.46 8.44 8.42 8.4 8.38 m L 0 8.36 8.34 8.32 8.3 8.28 0.4495 0.449 0.4485 O n. J 0.448 0.4475 8.26 I 1 1 1 1 1 1 1 1 1 ' 0.447 11:15:22 AM 11:16:48 AM 11:18:14 AM 11:19:41 AM 11:21:07 AM 11:22:34 AM 11:24:00 AM 11:25:26 AM 11:26:53 AM 11:28:19 AM 11:29:46 AM Drive Gain(%) Left Pickoff Voltage(Volts) 0 m N N J 800 700 600 500 400 300 200 100 0 C -100 Live Zero verse Density (scatter graph) ■ N ■ ■ ■ ■ ■ ti N ■ ■if ■ ■ ■ Am ■ ■ ■ 62 0.8625 0.863 0.8635 0.864 0.8645 0. Density 65 0 a`) N N J 800 700 600 500 400 300 200 100 0 -100 Live Zero verse Drive (scatter graph) ■ 20 40 60 80 10 Drive Status -Alarms posted (Each occurrence marked - examine column N in Data worksheet for details) 11:15:22 AM11:16:48 AM11:18:14 AM11:19:41 AM11:21:07 AM11:22:34 AM11:24:00 AM11:25:26 AM11:26:53 AM11:28:19 AM11:29:46 AM Flow Signal Offset At Zero Flow (Captured values from performing a meter zero) 0 11:15 -0.01 -0.02 -0.03 V4 1 -0.07 -0.08 -0.09 AM ; 4 = 0�� PCE Pacific, Inc. June 12, 2011 David Hall Cook Inlet Energy 601 West 5th Avenue, Suite 310 Anchorage, AK Dear David, Per your request, this provides a letter of qualification for Sig Chester relative to Micro Motion validation. Sig Chester has had training and industrial experience during the last year on Micro Motion meters so has practical field experience. His report for Cook Inlet Energy was checked by Micro Motion subject matter experts and myself to ensure accuracv. I attest he is qualified to validate the proper operation of Micro Motion Coriolis meters within the constraints as specified in Micro Motion documentation. Regards, Mel Olson Director Business Development PCE Pacific, Inc. Alaska Washington Utah 3700 Woodland Dr #750 2525 223R' Street, S.E 475 W Parkland Drive Anchorage, AK 99517 Bothell, WA. 98021 Sandy, UT 84070 (907) 243-3833 FAX (907) 248-0298 (425)487-9600 F.AX (425) 487-1114 (801) 565-4723 FAX (801) 565-3747 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 CERTIFIED MAIL — RETURN RECEIPT REQUESTED 7014 2120 0004 7782 3491 David Hall CEO Cook Inlet Energy 601 W. 51" Ave., Suite 310 Anchorage, AK 99501 Re: Docket Number: OTH-14-027 - errata Notice of Violation: Missing Reports Conservation Order 644 The Alaska Oil and Gas Conservation Commission's (AOGCC) granted temporary approval to Cook Inlet Energy (CIE) to commingle oil produced from the West McArthur River and Redoubt Shoal Fields. Conservation Order 644 dated May 6, 2011 included temporary authorization to use a Micro Motion coriolis meter to determine the proper allocation of Redoubt Shoal oil. Motivation for this temporary approval was the need for storage of oil produced from Trading Bay and McArthur River Fields at the Kustatan Production Facility (operated by CIE) while the storage tanks at the Trading Bay Production Facility (operated by Union Oil Company of California) experienced routine maintenance and repair beginning in June 2011. The approval for commingling of Redoubt Shoal and West McArthur River oil at the Kustatan Production Facility included two rules under Conservation Order 644 addressing the use of a Coriolis meter: - CIE Redoubt Shoal coriolis meters must be third party calibrated monthly, not to exceed 30 days between calibrations. AOGCC must be provided forty-eight (48) hours notice for opportunity to witness coriolis meter calibrations. - Analysis of meter calibration results, including raw calibration data, must be provided to the AOGCC within 7 days of completing a meter calibration. AOGCC never received a notice of the opportunity to witness any coriolis calibrations. AOGCC also never received any analyses of the results of the coriolis calibrations. On July 29, 2014, AOGCC requested confirmation of the third party calibrations of the coriolis meters and copies of the results. CIE neither responded nor provided documentation that would substantiate compliance with the requirements of the CO 644 rules. Failure to comply with the rules of Conservation Order 644 is a violation of AOGCC regulations. Failure to provide the information Docket Number: OTH-14-027 - —ata Notice of Violation December 5, 2014 Page 2 of 2 requested on July 29, 2014 by AOGCC is a separate violation of AOGCC regulations. No later than December 18, 2014 CIE is required to provide the documents required by Conservation Order 644. This request is made pursuant to 20 AAC 25.300. Failure to comply with this second request will be an additional violation. The AOGCC reserves the right to pursue an enforcement action in this matter according to 20 AAC 25.535. Should you have any questions about the information request, please contact Jim Regg at (907) 793-1236. Sincerely, Cathy P. F erster Chair, Commissioner cc: P. Brooks AOGCC Inspectors RECONSIDERATION AND APPEAL NOTICE As provided in AS 31.05 080(a), within 20 days after written notice of the entry of this order or 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 of the matter determined by it. If the notice was mailed, then the period of time shall be 23 days An application for reconsideration must set out the respect in which the order or decision is believed to be erroneous. The AOGCC shall grant or refuse the application for reconsideration in whole or in part within 10 days after it is filed. Failure to act on it within 10-days is a denial of reconsideration. If the AOGCC denies reconsideration, upon denial, this order or decision and the denial of reconsideration are FINAL and may be appealed to superior court. The appeal MUST be filed within 33 days after the date on which the AOGCC mails, OR 30 days if the AOGCC otherwise distributes, the order or decision denying reconsideration, UNLESS the denial is by inaction, in which case the appeal MUST be filed within 40 days after the date on which the application for reconsideration was filed If the AOGCC grants an application for reconsideration, this order or decision does not become final. Rather, the order or decision on reconsideration will be the FINAL order or decision of the AOGCC, and it may be appealed to superior court That appeal MUST be filed within 33 days after the date on which the AOGCC mails, OR 30 days if the AOGCC otherwise distributes, the order or decision on reconsideration. In computing a period of time above, the date of the event or default after which the designated period begins to run is not included in the period; the last day of the period is included, unless it falls on a weekend or state holiday, in which event the period runs until 5:00 p.m. on the next day that does not fall on a weekend or state holiday. Postal CERTIFIED MAIL@ RECEIPT Er Domestic = For delivery information, visit our website at wwwusps.coma. nut co 17� Postage $ 17- Certified Fee Postmark C3 Return Receipt Fee Here E3 (Endorsement Required) C3 Restricted Delivery Fee C3 (Endorsement Required) nj r-R Total Postage & Fees fti David Hall r sent to CEO O StreetBApt.fVo., Cook Inlet Energy r� or PO Box No. ---------------------• 601 W. 5th Ave., Ste. 310 City. State, ZIP+4 PS Form :r0 July 2014 Anchorage, AK 99501 ■ Complete items 1, 2, and 3. Also complete item 4 if Restricted Delivery is desired. ■ Print your name and address on the reverse so that we can return the card to you. ■ Attach this card to the back of the mailpiece, or on the front if space permits. 1. Article Addressed to: David Hall CEO Cook Inlet Energy 601 W. 5th Ave., Ste. 310 Anchorage, AK 99501 A. Signature X ❑ Agent awn!!Y�❑ Addressee Q. Received by (Printed Nam ) C. Date f De ery D. Is delivery address differe4k from item 1? LB Yep If YES, enter delivery address below: ❑ No 3, Service Type ❑ Certified Mail ❑ Express Mail ❑ Registered 13 Return Receipt for Merchandise ❑ Insured Mail ❑ C.O.D. 4. Restricted Delivery? (Extra Fee) ❑ Yes 2. Article Number 701,4 21,20 0004 7782 3491 (Transfer from service /abe( PS Form 3811, February 2004 Domestic Return Receipt 102595.02-M-1540 THE STATE Alaska Oil and Gas olALAS� Conservation Commission GOVERNOR BILL WALKER 333 West Seventh Avenue Anchorage, Alaska 99501-3572 Main: 907 279.1433 Fax 907.276.7542 December 4, 2014 CERTIFIED MAIL — RETURN RECEIPT REQUESTED 7014 2120 0004 7782 2234 David Hall CEO Cook Inlet Energy 601 W. 51h Ave., Suite 310 Anchorage, AK 99501 Re: Docket Number: OTH-14-027 Notice of Violation: Missing Reports Conservation Order 644 The Alaska Oil and Gas Conservation Commission's (AOGCC) granted temporary approval to Cook Inlet Energy (CIE) to commingle oil produced from the West McArthur River and Redoubt Shoal Fields. Conservation Order 644 dated May 6, 2011 included temporary authorization to use a Micro Motion coriolis meter to determine the proper allocation of Redoubt Shoal oil. Motivation for this temporary approval was the need for storage of oil produced from Trading Bay and McArthur River Fields at the Kustatan Production Facility (operated by CIE) while the storage tanks at the Trading Bay Production Facility (operated by Union Oil Company of California) experienced routine maintenance and repair beginning in June 2011. The approval for commingling of Redoubt Shoal and West McArthur River oil at the Kustatan Production Facility included two rules under Conservation Order 644 addressing the use of a Coriolis meter: - CIE Redoubt Shoal coriolis meters must be third party calibrated monthly, not to exceed 30 days between calibrations. AOGCC must be provided forty-eight (48) hours notice for opportunity to witness coriolis meter calibrations. - Analysis of meter calibration results, including raw calibration data, must be provided to the AOGCC within 7 days of completing a meter calibration. AOGCC never received a notice of the opportunity to witness any coriolis calibrations. AOGCC also never received any analyses of the results of the coriolis calibrations. On July 29, 2014, AOGCC requested confirmation of the third party calibrations of the coriolis meters and copies of the results. CIE neither responded nor provided documentation that would substantiate compliance with the requirements of the CO 644 rules. Failure to comply with the rules of Conservation Order 644 is a violation of AOGCC regulations. Failure to provide the information Docket Number: OTH-14-027 Notice of Violation December 4, 2014 Page 2 of 2 requested on July 29, 2014 by AOGCC is a separate violation of AOGCC regulations. No later than December 18, 2014 CIE is required to provide the documents required by Conservation Order 644. This request is made pursuant to 20 AAC 25.300. Failure to comply with this second request will be an additional violation. The AOGCC reserves the right to pursue an enforcement action in this matter according to 20 AAC 25.535. Should you have any questions about the information request, please contact Jim Regg at (907) 793-1236. Sincerely, Cathy P. oerster Chair, Commissioner cc: P. Brooks AOGCC Inspectors Postal CERTIFIED o RECEIPT �- Domestic m ti For delivery information, visit our website at wimmusps.como. CID r� Postage $ Certified Fee Postmark O Return Receipt Fee Here ❑ (Endorsement Required) ED Restricted Delivery Fee C3 (Endorsement Required) ru r-j Total Postage & Fees $ David Hall nJ Sent to CEO --- --------------- Cook Inlet Energy Street 8 Apt. No., or Po sox No. 601 W. 5th Ave., Ste. 310 city, State, ZIP+4 Anchorage, AK 99501 PS Form :00 July 2014 See Reverse for Instructions ■ Complete items 1, 2, and 3. Also complete item 4 if Restricted Delivery is desired. ■ Print your name and address on the reverse so that we can return the card to you. ■ Attach this card to the back of the mailpiece, or on the front if space permits. 1. Article Addressed to: David Hall CEO Cook Inlet Energy 601 W. 5th Ave., Ste. 310 Anchorage, AK 99501 A. Signature X ❑ Agent /�j)�(/�V`t�n n ^� n❑ Addressee S��IVI"I- fUt-ImerWr C. Date of Delivery ed Na) D. Is delivm 11 U Yes If YES, enter delivery address below: ❑ No 3. Service Type ❑ Certified Mail ❑ Express Mail ❑ Registered ❑ Return Receipt for Merchandise ❑ Insured Mail ❑ C.O.D. 4. Restricted Delivery?(Extra Fee) ❑ Yes 2. Article Number 7014 2120 0004 7782 2234 (Transfer from service label) PS Form 3811, February 2004 Domesticfleturn Receipt 102595-02-M-1540 Regg, James B (DOA) From: Regg, James B (DOA) Sent: Friday, July 29, 2011 10:51 AM To: David Hall Cc: DOA AOGCC Prudhoe Bay; Aubert, Winton G (DOA) Subject: Commingling WMR and Redoubt Production Attachments: co644. pdf Conservation Order 644 requires monthly calibration of coriolis meters being used for custody transfer measurement, 48hr notice for Commission witness, and analysis of coriolis meter calibrations within 7days of completing calibration. Copy of CO 644 attached. Production commenced from Redoubt 1 and 7 in June according to our records. Were coriolis meters calibrated in June and July; if so, please provide the results. Jim Regg AOGCC 333 W.7th Avenue, Suite 100 Anchorage, AK 99501 907-793-1236 STATE OF ALASKA ALASKA OIL AND GAS CONSERVATION COMMISSION 333 West 71h Avenue, Suite 100 Anchorage, Alaska 99501 Re: THE APPLICATION OF Cook Inlet Energy for an Order authorizing the commingling of West McArthur River oil with Redoubt Shoal oil, in conformance with 20 AAC 25.215. Docket Number: CO- I 1-12 Conservation Order No. 644 West McArthur River Field Redoubt Shoal Field Kenai Peninsula Borough, Alaska May 6, 2011 IT APPEARING THAT: 1. By application dated March 3, 2011 Cook Inlet Energy (CIE) applied to the Alaska Oil and Gas Conservation Commission (Commission) for an order authorizing the commingling of West McArthur River oil with Redoubt Shoal oil, Kenai Peninsula Borough, Alaska. CIE also requests approval of a Micro Motion Coriolis meter for determining the proper allocation of Redoubt Shoal oil. 2. On March 10, 2011 pursuant to 20 AAC 25.540, the Commission published in the Peninsula Clarion notice of opportunity for public hearing on April 14, 2011. 3, The Commission held a public hearing on April 14, 2011 at 333 West 7'j' Avenue, Suite 100, Anchorage, Alaska 99501. Testimony was presented by CIE and Union Oil Company of California (Union). 4. No protests to the application were received. 5. The hearing record was held open until April 22, 2011 so that CIE and Union could provide written responses to Commission inquiry. FINDINGS: Prior to March 23, 2009 Union stored oil from the McArthur River and Trading Bay Fields at the Drift River terminal. Mount Redoubt volcanic eruptions beginning on that date have prevented subsequent oil storage at the terminal. Terminal piping has been reconfigured to allow oil to be pumped directly onto a tanker. 2. Union currently stores McArthur River oil and Trading Bay oil at its Trading Bay Production Facility (TBPF). Trading Bay tank capacity is equivalent to about 18 days of production. Routine tank maintenance and repair reduce available storage capacity, and as the storage limit is reached, McArthur River and Trading Bay wells must be shut in to accommodate tanker scheduling. Conservation Order 644 West McArthur River, Redoubt Shoal May 6, 2011 Page 2 3. Eleven Union wells completed with electric submersible pumps (ESP) account for 26% of producing wells and 60% of oil produced from the McArthur River and Trading Bay Fields. Shutting in ESP wells exposes Union to significant risk of ESP failure requiring a rig workover. 4. To provide temporary substitute storage capacity through its regularly scheduled tank maintenance period, Union wishes to utilize two of CIE's Kustatan Production Facility (KPF) storage tanks, which would eliminate the need to shut in Union's eleven ESP wells. In order to free the tank storage required to store Union's oil, CIE must commingle its West McArthur River oil and Redoubt Shoal oil in a KPF storage tank. 6. In order to comply with Commission regulations, CIE Redoubt Shoal oil must be metered prior to commingling with CIE West McArthur River oil to determine the quantities produced from each. CIE proposes to allocate Redoubt Shoal oil using a Micro Motion Coriolis meter with a stated accuracy of ±0.05% of rate, which would be more accurate than the current field custody sales meters. 7. CIE proposes monthly third party meter calibration, which will provide verification and will identify changes, damage or degradation in meter measurement performance. Monthly meter calibration will be clone by Industrial Instruments Service Company (IISCO), an experienced company known to provide reliable meter calibrations. CONCLUSIONS: I The Drift River terminal configuration and Cook InIct oil tanker scheduling will require Union to shut in McArthur River and Trading Bay wells which use ESPs, absent an alternate production storage means. 1 Frequent well shut in renders ESPs susceptible to failure, and replacing ESPs requires rig workover. 3. Freeing CIE KPF oil storage capacity for temporary use by Union will allow Union to avoid production upsets that would likely follow the shut in of Union's McArthur River and Trading Bay wells. 4. Commingling CIE West McArthur River oil with Redoubt Shoal oil at KPF is necessary to free KPF tankage for Union's temporary use. 5. Commission regulation 20 AAC 25,2280) allows for the approval of a variance from production measurement equipment used for custody transfer if the variance will result in equal or improved accuracy in measuring hydrocarbons served from the property or unit. 6. West McArthur River and Redoubt Shoal oil volumes can be accurately determined utilizing Micro Motion Coriolis meters, and calibrating the meters monthly. Conservation Order 644 West McArthur River, Redoubt Shoat May 6. 2011 Page 3 7. Commingling of CIE's West McArthur River and Redoubt Shoal oil will not promote waste, affect correlative rights, or result in harm to human health or the environment. NOW, THEREFORE, IT is ORDERED THAT the following rules, in addition to statewide requirements under 20 AAC 25, apply to the temporary commingling of West McArthur River oil with Redoubt Shoal oil: Rule 1: Commingling of CIE West McArthur River oil with Redoubt Shoal oil at KPF is approved. Rule 2: Use of Coriolis meters is authorized for temporary measurement of oil served from Redoubt Shoal Field. Rule 3: CIE Redoubt Shoal Coriolis meters must be third party calibrated monthly, not to exceed 30 days between calibrations. Commission must be provided forty-eight (48) hours notice for opportunity to witness Coriolis meter calibrations. Rule 4: Analysis of meter calibration results, including raw calibration data, must be provided to the Commission within 7 days of completing a ineter calibration. Rule 5: CIE shall provide the Commission with 48 hour notice and opportunity to witness Redoubt Shoal allocation meter calibration. Note that this Order Production Facility. storage at KPF. does not authorize Union to store oil at CIE's Kustatan Conservation Order No. 646 governs Union's temporary oil DONE at Anchorage, Alaska, an, C� ffCathyAP Foer er, Commissioner Alaska Oil and Gas Conservation Commission Conservation Order 644 West McArthur River, Redoubt Shoal May 6, 2011 ION AND APPEAL Page 4 AN provided in AS 31.05,090(a), within 20 days after written notice of the entry of this order or decision, or such further lime as the Commission grants for good cause shown. a person afTwed by it may file with Cite Commission an application for reconsidenitimi of the matiet determined by it. if the notice was mailed, then the period of tinre ,hall be 23 days. An application flor reconsideration must set out the respect in which the order or decision is believed to he erroneous. The Commission shall grant or refuse the application for reconsideration in whole or in pan within 10 days after it is filed. Failure to act on it within 10-days is a denial of reconsideration, If the Commission denies reconsideration, upon clLoial, this order or decision and the denial ofi-cconsidLi-afion are FINAL and may be appealed to superior court. The appeal MUST he filed within 33 days after the date on which the Commission maits, OR 30 days if the Commission otherwise distributes, the order or decision denying n.vonsidetation, UNLESS the denial i,, by inaction, in which case the appeal MUST be riled within 40 days alter the date on which the application for reconsideration was riled, If the Commission grants an application for rLconsideration. this order or decision does not licconic final. Rather, the order or decision on reconsideration will be the FINAL order or decision or the Commission, and it may be appealed to superior court. That appeal MUST be Filed within 3.1 days after the date on which the Commission mails, OR 30 days if the Commission otherwise distributes, the order or decision on reconsideration, As provided in AS 31.05,080(b).-It1he questions reviewed on appeal are limited to the questions presented to the Commission by the application flor reconsideration - In computing it period of time above, the date of the event or default aftLi- which the designated period begins to run is not included in the period: the last day of the period is includW. unless it fills on a weekend or state holiday. in which event the period runs until 5:00 limi. on the next day that does not fall an a wcckciid or state holiday. CO Page 1 of 1 Regg, James B (DOA) b 4 From: Regg, James B (DOA) `�� fref� `( Sent: Friday, July 29, 2011 10:51 AM To: David Hall Cc: DOA AOGCC Prudhoe Bay; Aubert, Winton G (DOA) Subject: Commingling WMR and Redoubt Production Attachments: co644.pdf Conservation Order 644 requires monthly calibration of coriolis meters being used for custody transfer measurement, 48hr notice for Commission witness, and analysis of coriolis meter calibrations within 7days of completing calibration. Copy of CO 644 attached. Production commenced from Redoubt 1 and 7 in June according to our records. Were coriolis meters calibrated in June and July; if so, please provide the results. Jim Regg AOGCC 333 W.7th Avenue, Suite 100 Anchorage, AK 99501 907 - 793 -1236 7/29/2011 t, • • Cook Inlet Energy_ April 20, 2011 _ ri g _ 1 L) Mr. Dan Seamount, Chair Alaska Oil and Gas Conservation Commission 333 West 7 Ave., Suite 100 ' filo Anchorage, Alaska 99501 Afi Re: Additional Information Requested by Commission at Hearing on April 14, 2011 Regarding Commingling WMRU and RU Production and Related Metering Changes Dear Mr. Seamount, Cook Inlet Energy, LLC ( "CIE ") would like to provide additional information in support of its request to commingle West McArthur River ( "West Mac ") oil and Redoubt Shoal ( "Redoubt ") oil. Again, this application is necessary to support the Union Oil Company of California ( "UNOCAL ") application to store Trading Bay and McArthur River oil at CIE's Kustatan Production Facility ( "KPF "). The Commission requested additional information from CIE and UNOCAL at the hearing held on April 14, 2011 and held the docket open to allow CIE and UNOCAL opportunity to respond to questions raised at that hearing. Specifically, the Commissioners requested that CIE 1) provide additional information to show that its ORRI holders would not be harmed by the Commission's approval of this application, or that the ORRI holders had been notified of this proposed action and 2) provide additional information regarding the accuracy of the meters proposed for allocating the commingled production to West Mac and Redoubt and its plans to maintain and test the meters to ensure their continuing accuracy. As to the first question, ORRIs are not consistent across the West McArthur River Unit (WMRU) and Redoubt Unit (RU), and in fact are not consistent within the Redoubt Unit (they vary lease to lease). ORRIs range from .0125% to 1.25% of West Mac production and .0001% to .2302% of Redoubt production. CIE has not notified its ORRI holders at WMRU or RU about its application to commingle West Mac and Redoubt production. CIE analyzed the financial risk associated with the allocation issues associated with the approval of its application (Allocation Risk) and the transportation cost issues associated with UNOCAL storage issues if the application is denied (Price Risk) and determined that the potential damage to its ORRI holders, as with the State of Alaska, CIE and all other royalty owners on the West Side of Cook Inlet, is much greater from not applying for the commingling of West McArthur April 20, 2011 Additional Information ubmittal — April 14, 2011 Hearing Page 2 of 5 River and Redoubt Shoal production to support UNOCAL's application to store Trading Bay and McArthur River oil at KPF. That is the Price Risk far outweighs the Allocation Risk. CIE's analysis is based upon an assumed $70/bbl realized price (realized prices have ranged from $56.50 to $86.87 over the past 6 months, Oct `10 thru March `11) and West Mac production of 900 bbls /day and Redoubt production of 400 bbls /day. ORRI Interest Allocation Risk Price Risk (per bbl at $70 /bbl (per day for each $0.25 realized price) increase in transportation costs per bbl) West Mac Smallest 0.031250% $0.021875 $0.070313 Largest 1.250000% $0.875000 $2.812500 Redoubt Smallest 0.000100% $0.000070 $0.000100 Largest 0.230200% $0.161140 $0.230200 Price Risk results from either 1) reduced production from Trading Bay and/or McArthur River that would result in a higher CIPL tariff as a result of lower total throughput to the Christy Lee loading facility or 2) alternatively, if production is maintained at current levels and storage at the Trading Bay facility is taken off -line, more frequent tanker trips with each tanker carrying less oil than under current scheduling resulting in higher transportation charges per barrel for transport from the Christy Lee loading facility to the Tesoro refinery in Nikiski. A definitive estimate for the Price Risk is difficult as there are so many variables involved in determining tariffs for CIPL and Tesoro tankers. However, CIE is confident that UNOCAL reducing production by 20,000 bbls over each 12 to 14 day period (the tankage volume at KPF and the current tanker schedule) or Tesoro making tanker runs every 8 to 10 days versus 12 to 14 days (KPF tankage being able to store approximately 4 days of Trading Bay and McArthur River production) will result in significantly higher increases to transportation costs than the $0.25 used in the illustration above. Allocation Risk results from the possibility of commingled oil production being allocated to the wrong field (e.g. West Mac production being allocated to Redoubt). The cost for each misallocated barrel to ORRI holders is very straightforward. The only question is the actual Realized Price and the likelihood of production being misallocated. The above, along with the following information regarding the accuracy of the metering plan, should justify CIE's determination that Price Risk far outweighs Allocation Risk. • April 20, 2011 Additional Information ubmittal — April 14, 2011 Hearing Page 3 of 5 Regarding the second question, there has been some concern as to the accuracy of the proposed RU allocation meter (FT -15) that would be used to meter Redoubt oil prior to entering Tanks 142/135 where fluids would be comingled with West Mac oil. The manufacturer of meter FT -15 is Micro Motion, an Emerson company. The FT -15 is the ELITE Coriolis meter, which is the leading precision flow and density measurement solution. The Elite series meter offers the most accurate and repeatable measurement for liquids with an accuracy of +/- of .05% of rate as shown below. Accuracy and repeatability Electronics option Model 24008, Other MVO transmitter, eels. Dore processor std_ store processor Mass and Liquid Accuracy 20.05% of rate „1, .0.10% Of rata volume flow,” Repeatability 20.025% of fete .0.05% Of rata Gas Accuracy *0.35% of rate °, x0.36% of rate Repeatability 20.20% of rata *0.20% of rata Density L Iquld Accuracy .0.0002 g /cm' *0.0005 g /cm' (x0.2 k9 /m') ( *0.5 kg/m') Repeatability *0.0001 9/00 *0.0002 9 /cm (x0.1 kg /m') ( *0.2 kg/m.) Temperature Accuracy *1 °C * 0.5% of reeding *1 "C. 0.5% of reeding Repeatability *0.2 `C .0.2 `C Ns(twln 11.8/6 Zero stability CMFS010M 0.000075 0.002 CMF130101 -1, p 0.00015 0.004 CMF3015M 0.00037 0.01 CMFSOISH.0 0.00073 0.02 CMF010M. 14 0.000075 0.002 CMF01OP 0.00016 0.004 CMF025 0.001 0.027 CMF060 0.006 0.163 CMFIOO 0.025 0.650 CMF200 0.08 2.18 CMF300 0.25 5.60 CMF400 1.50 40.91 (1) ccurec t o m n d :;: t h y by e Rg et Model. pfOna, CM00rO CMFSOI er/on on S. sens g 42. ors with Made/ 22005 transmitter, and ng Mf am (2) When flow rata la leas than ram stability / 0.0005, racy = *((zero stability / now rate) . 100)% of rata, and repeatability = *(31(zero stability / flow rata) r 100 (3) *0* e< ordered ero Stability / 0.001, accuracy ` *f(eso sta/I option, now rate) a 100 % of rate 000 repeatability rate zero ere stabillty arability y / l ow When now 100% of rate. ° .(K(zero stb //!ty ,l rate) x (4) When now rate Is /sea than zero stability / 0.001, accuracy = *((zero stability / flow rate) . 100)% of rata and repeatability = *(X(zem stability / flow rate) . 100)% of rate. (5) * /bwtrate) a 1 00 )% lit / 0.0035, aecurecy equals *5(zem stability /no. rate) a 1001% of rate end repeatability equals (0) azz 16 o 30 pslg ( 0. 0002 b g/ m' (.0.2 kg/ it') density accuracy ere based on reference conditions of water at 08 to 140 °F (20 to 60 °C) 4 Micro Motion ELITE. Fiber and Density Meters Micro Motion Coriolis meters have no moving internal parts resulting in no wear and tear, no maintenance and an expectation that meter calibration will not drift over time. These characteristics, coupled with exceptional accuracy and the delivery of mass, volume, temperature and density measurements from a single device, have resulted in the widespread adoption of Micro Motion meters in processes around the world for over three decades. As a comparison, the AO -Smith PD rotary vane meter used as the RU & WMRU crude oil custody sales meters located at Mosquito Station has an accuracy of +/- .15% of rate, as shown below. In other words, the Micro motion ELITE (FT -15) is three time more accurate. • Additional Information mittal —April 14, April 2011 20 Hearing Page 4 of 5 �I C reChnQIogies Smith Mate PD Rotary Vane Mater 4" Ste®/ Model F4 Spocificatsons issue/Row 0A (4/10) 133311s161 6801012 The SnMth Allatersltudv/ Fe Masan is a 4 double-cave. etraipht- through rotary verve, paean,. displacement me- , f nu: AppliCatione isciants= CtersdrsR b ststrirsy, disper1slrry, , MEM inventory control. and custody aerator dolls, advents. _ chemicals. psbstr, Acts. and IWtlarera 7- Faxtturss -, ....:- • Sup.do. Acaawarcy -The Smith Meter Rotary Vane = ... Molar principle, combined with the meter's uniquely - _ - designed (e(rset) inlet and outlet . nmtzos pleasure dnoP nozzles 'dross the msaswhlp crwmbe f w►Mch ms educes lbw accuracy. meter clearance ( slippa(te ), maximize aouamcy INV 1 Low drop_ Orals- Streamlined flow path provides low P IN Poo UVe nand Acressrate R Modal /Y-et ddva 0.1brabr wOt. ant 5% High nt. Mtn /mean Flow Ram - 7) pica/ pw/a►r►asnos ensures accurate registration. Vtteoa4y (mow) 1161 Long Ser,lae Line - Law friction ball bearings, fixed Llnean/7 1 Untie 0J 1 6 • 20 100 400 cam- ty g, rugged construction give sus- tained accuracy and long service 111e. USOPM loo — _ 6o 25 6 - 1.25 0.30 40.16% L/018 376' _ 227 06 23 _4.75 1.14 10 USOPM 75 45 ' 15 4 1.00 0.26 402663 Urnn 204 170 65 15 800 0.05 • High Viscosity Meter Clearances - To °stand ' uscyPM 60 ao 12 3 - 0,60 0.133 operation at maximum (low rate from 400 mPa°s to 2,000 rr1Pa°s. 40 ' Lh111n _ 100 ' 114 _ 46 ' 11 _ 2.25 0.57 - High Tampsraturo Ctsaraneee - To extend born RopeaLblN[y Mfg temperatures bo 150 to 200 °F (65°C to 03 °C). M Ali iron Trim - For operating temperatures above 4:0.0296 200°F (93°C)- V/sooi /y M 1.-P13 - For low lubricity liquids such as LPG. Standa, S 400 mPa°s° (2,000 SU) maximum. • meet roqulr'arrtenfa of NACE S MR- '75. d 01 Optional 2 Pa.s (10,000 F.8117.1.) "'Olin""/ - specity'Hiyh V si cosil Meter Cle Over 2 Poor -specify "High Viscosity Meter Clearances^ Operating SpeciPcatfons and denote maximum now rate in direct proportion to viscosity over 2 Paa°s (e.g., at 4 Pa°s, derats Maximum Masfmaan Flow Rile Flow Rate to 50% of Normal Continuous Fisting - 300 USOPM IJmin US(3PM). Standard lthn 600 2.250 nddSterW.rd Temperature intermittent Rating. ard Meter Thf o With: Standard T p• - 720 2.725 Blma N/EPFVTe1bn: n: -2 -20°F b 750 (-26°C b 06 Vkon: 10°F b 150°F (-12°C b 06°C). Co Minuous Rating - Hih g Tsmperatunl Metsr Clssrencas ith: AM Iron or LPG Trim 450 1.700 9una ■a bgon: .4= b 200°, W (-Qg°C b 93'21. Vk on: 1 0°F b 204 ( - 12 °2 b 93 °C). f 4061n>irrO aacsar to 52530 en Cana., 10636 P'04UUab 620e,s eonri6Wa 3PM rbn to rnal 2421.2 ( 4-. OOdt /0/4510. 220 6"041, /'M Ar�66V o '"'" stb0/J 2 LNYVIy a w.mnu.. *0 ".,ar at ea0 u6oP"� ($zso L.nvn) un..s ernsr.wr 30220 3 asean ,smm26 orm L1sraPAl (1,678 t 1. 4 0,020 44 1,000A. f 63.5 7ha Mon 7)tuted N4,na In Measurement Even though FT -15 would not be tested for accuracy via a prover loop type system, CIE proposes to schedule monthly third party calibration of the FT -15. Again, with the FT -15 meter being a Micro Motion Coriolis type meter it has no moving parts subject to wear and tear as does the AO -Smith PD meter type, which warrants rigorous testing methods. The proposed third party meter testing will provide verification and will identify changes, damage or degradation in the measurement performance of the meter. As the mechanical stiffness, or rigidity, of Micro Motion Coriolis flow tubes are directly related to its flow calibration factor. CIE would like to raise one point in support of UNOCAL's application to store Trading Bay and McArthur River oil at KPF and have that oil metered at Mosquito Station as it enters CIPL. On the West Side most LACT meters are already located well off of the leased area as offshore production is transported to onshore processing facilities and then transported to CIPL for shipment. In almost every case, if not all cases, the LACT meter for production is at the receiving point at CIPL. CIE requests that the commission rule favorably on UNOCAL's application to store Trading Bay and McArthur River production at KPF, and approve CIE's application to commingle production streams from West Mac and Redoubt and CIE's metering plan to allocate production to the April 20, 2011 Additional Information Submittal — April 14, 2011 Hearing Page 5 of 5 appropriate fields. CIE firmly believes that these two applications are in the best interests of all parties. Respectfully, �J David Hall Enclosures: Product Data Sheet for Micro Motion ELITE Coriolis Flow and Density Meters Specification Sheet for Smith Meter PD Rotary Vane Meter Cc: Kevin R. Banks, Division of Oil and Gas Justin Black, UNOCAL II III Product Data Sheet PS- 00374, Rev. R March 2011 Micro Motion ELITE Coriolis Flow and Density Meters Micro Motion ELITE Coriolis meters are the leading precision flow and density measurement solutions. ELITE meters offer the most accurate and ELITE Peak performance repeatable measurement available for liquids, gases, or slurries. Coriolis meter . i, 1 , 1 . ' ELITE HC Peak performance or g high capacity ` ;c f meter d zy 4, F- Series High performance 1 compact drainable C �, Coriolis meter S itit 4 :- ve 7:' 2 elt 4 0 i _ I ,;. L ^rte' ,,, r ` r H- Series Hygienic compact drainable Coriolis meter Best precision flow and density measurement • Unique design delivers unparalleled measurement sensitivity and stability • Guarantees consistent, reliable performance over the widest flow range T - Serie Straight tube full - bore • Smart Meter Verification for quick, complete meter diagnosis without Coriolis meter process interruption. • 2 -wire loop- powered option for installation simplification R General purpose Superior performance in the most challenging applications fl - on l y Coriolis meter • Industry standard for custody transfer and critical process control • Best two -phase flow capability for batching, loading, and entrained air applications LF- Series Extreme low - flow Coriolis • Immune to fluid, process, or environmental effects for superb meter measurement confidence Alitz Micro M .. iori EMERSON. Process Martageotertt • • Micro Motion ELITE flow and density meters Micro Motion Coriolis meters meet a vast range of application needs, ranging from extreme low -flow up to high -flow, high- capacity lines. Cryogenic, hygienic, high - temperature, and high - pressure —Micro Motion meters can handle them all. Micro Motion meters are available with a variety of wetted parts to ensure the best material compatibility. Now with the industry's only 2 -wire Coriolis option, Micro Motion provides unsurpassed simplicity of installation and application flexibility. Coriolis meters. Coriolis meters offer dramatic ELITE Coriolis meters. Micro Motion ELITE meters benefits over traditional volumetric measurement are the leading meters for precision flow and density technologies. Coriolis meters: measurement. ELITE meters offer the most • Deliver accurate and repeatable process data accurate measurement available for virtually any over a wide range of flow rates and process process fluid, while exhibiting exceptionally low conditions. pressure drop. Every ELITE meter features standard secondary containment, and is available • Provide direct inline measurement of mass flow with stainless steel or nickel -alloy wetted parts and and density, and also measure volume flow and a wide variety of process connections to meet your temperature —all from a single device. every need. • Have no moving parts, so maintenance costs Now with Smart Meter Verification, ELITE delivers are minimal. the best in measurement and ease of use for critical • Have no requirements for flow conditioning or applications. ELITE meters offer the best straight pipe runs, so installation is simplified measurement performance for mass, density, and and less expensive. volume, regardless of process or environmental • Provide advanced diagnostic tools for both the conditions. ELITE meters provide measurement meter and the process. capability for two -phase flow, liquid, and gas custody transfer, and process conditions from -400 °F ( -240 °C) to 662 °F (350 °C). Contents Temperature limits 3 Environmental effects 10 Accuracy and repeatability 4 Hazardous area classifications 11 Liquid flow performance 5 Materials of construction 19 Gas flow performance 6 Weight 19 Density range (liquid only) 8 Dimensions 20 Vibration limits 8 Fitting options 31 Power consumption 8 Ordering information 42 Pressure ratings 9 2 Micro Motion ELITE Flow and Density Meters • 0 Temperature limits All models except high- 176 (80) 140 temperature models el) l2llsl c 140 (60) (60) 11 in u 104 (40) ; 113 (45) o — au m 2 --- 8V- 32(0) o •c E Mount transmitter ' -40 ( -40) remotely; use j -box El E a) 0 ac E m 2 — -112 (-80) '6 111111111111 aa) -148 ( -100) la 0 a CO ° N c 0 CO ° 0 0 v N CO a NII �I I M CD V V CO (D O a O 0) W r N M" V I N '7 S a Maximum process temperature in °F ( °C) High- temperature models 176 (80) o` $ 140 (60) in a) 104 (40) - 2 2E.%-. 0 • u- 32 (0) - 0 c - m m z E -40 (- 40) Mount transmitter m a' m /� remotely; use j -box E -112 ( -80) - aa) -148 ( -100) , , E u ° coo 4, v ° ( 0 0) CO �{ o r N (0 CO to N I M a (00 "- r N Maximum process temperature in °F ( °C) CO (1) Temperature limits may be further restricted by hazardous area approvals. See pages 11 -17. (2) The temperature graphs shown here are for use only as a general guide. (3) When ambient temperature is below -40 °F ( -40 ° C), a core processor or Model 2400S transmitter must be heated to bring its local ambient temperature to between -40 °F ( -40 °C) and +140 °F ( +60 ° C). Long -term storage of electronics at ambient temperatures below -40 °F ( -40 ° C) is not recommended. (4) The temperature limits shown apply only when the electronics are not covered (for example, by insulation). if the sensor case must be insulated, use extended mount electronics. Micro Motion ELITE Flow and Density Meters 3 • • Accuracy and repeatability Electronics option Model 2400S, Other MVD transmitter, enh. core processor std. core processor Mass and Liquid Accuracy ±0.05% of rate (2)(3) ±0.10% of rate volume flow' Repeatability ±0.025% of rate ±0.05% of rate Gas Accuracy ±0.35% of rate ±0.35% of rate Repeatability ±0.20% of rate #0.20% of rate Density" Liquid Accuracy ±0.0002 g /cm ±0.0005 g /cm ( ±0.2 kg /m (±0.5 kg /m Repeatability ±0.0001 g /cm ±0.0002 g /cm ( ±0.1 kg /m ( ±0.2 kg /m Temperature Accuracy ±1 °C ± 0.5% of reading ±1 °C ± 0.5% of reading Repeatability ±0.2 °C #0.2 °C lb/min kg /h Zero stability CMFS010M 0.000075 0.002 CMFS010H, P 0.00015 0.004 CMFS015M 0.00037 0.01 CMFS015H, P 0.00073 0.02 CMF010M, H 0.000075 0.002 CMF010P 0.00015 0.004 CMF025 0.001 0.027 CMF050 0.006 0.163 CMF100 0.025 0.680 CMF200 0.08 2.18 CMF300 0.25 6.80 CM F400 1.50 40.91 (1) Accuracy options vary by model. Models CMF010, CMFS010, CMFS015, sensors with Model 2200S transmitter, and all high - temperature models have fewer accuracy options. See Ordering information on page 42. (2) When flow rate is less than zero stability / 0.0005, accuracy = #((zero stability / flow rate) x 100J% of rate, and repeatability = ±[ %(zero stability / flow rate) x 100] %. (3) When ordered with the ±0.10% factory calibration option, accuracy on liquid = ±0.10% when flow rate _>. zero stability / 0.001. When flow rate < zero stability / 0.001, accuracy = ±((zero stability/ flow rate) x 100)% of rate and repeatability = #(%(zero stability / flow rate) x 100)% of rate. (4) When flow rate is less than zero stability / 0.001, accuracy = #((zero stability / flow rate) x 100)% of rate and repeatability = ±( %(zero stability / flow rate) x 1001% of rate. (5) When flow rate is less than zero stability / 0.0035, accuracy equals ±[(zero stability / flow rate) x 1001% of rate and repeatability equals ±f %(zero stability / flow rate) x 1001% of rate. (6) Specifications for ±0.0002 g /cm 40.2 kg /m density accuracy are based on reference conditions of water at 68 to 140 °F (20 to 60 °C) and 15 to 30 psig (1 to 2 bar). 4 Micro Motion ELITE Flow and Density Meters • MI Liquid flow performance Mass Volume ) lb/min kg /h gal /min I/h bbl /h m /h Maximum flow rate CMFS010 4 108 0.5 108 CMFS015 12 330 1.5 330 CMF010 4 108 0.5 108 CMF025 80 2180 10 2180 CMF050 250 6800 30 6800 CMF100 1000 27,200 120 27,200 CMF200 3200 87,100 385 87,100 550 87 CMF300 10,000 272,000 1200 272,000 1700 272 CMF400 20,000 545,000 2400 545,000 3400 545 Typical accuracy, turndown, and pressure drop with CMF100 and 2400S or enhanced core processor The graph below is an example of the relationship between accuracy, turndown, and pressure drop when measuring the flow of water with a Model CMF100 sensor and Model 2400S transmitter or enhanced core processor. Actual pressure drop is dependent on process conditions. To determine accuracy, turndown, and pressure drop with your process variables, use the Micro Motion product selector, available at www.micromotion.com. 2.5 -4— 100:1 1:1 -.— 2.0 --- 20:1 1.5 10:1 2:1 1.0 - A al 0.5 0 0 a - 0.5 -1.0 - -1.5 - 2.0 0 10 20 30 40 50 60 70 80 90 100 Flow rate, % of maximum Turndown from maximum flow rate 500:1 100:1 20:1 10:1 2:1 Accuracy ±% 1.25 0.25 0.05 0.05 0.05 Pressure drop psi -0 -0 0.2 0.7 13.5 bar -0 -0 0.01 0.05 0.93 (1) Specifications for volumetric flow rate are based on a process -fluid density of 1 g /cm (1000 kg/m For fluids with density other than 1 g /cm (1000 kg /m the volumetric flow rate equals the mass flow rate divided by the fluid's density. Micro Motion ELITE Flow and Density Meters 5 0 • Gas flow performance When selecting sensors for gas applications, measurement accuracy is a function of fluid mass flow rate independent of operating temperature, pressure, or composition. However, pressure drop through the sensor is dependent upon operating temperature, pressure, and fluid composition. Therefore, when selecting a sensor for any particular gas application, it is highly recommended that each sensor be sized using the Micro Motion product selector, available at www.micromotion.com. Mass Volume lb/min kg /h SCFM Nm /h Flow rates that produce CMFS010 0.3 8 4 6 approximately 10 psi (0.68 bar) CMFS015 1 24 12 18 pressure drop on aie2) CMF010M, H 0.30 8 4 6 CMF010P 0.2 6 3 5 CMF025 4 110 60 90 CMF050 10 300 145 230 CMF100 50 1300 640 1000 CMF200 150 4000 2000 3100 CMF300 490 13,300 6500 10,300 CMF400 1250 34,000 16,600 26,250 Flow rates that produce CMFS010 1 30 30 45 approximately 50 psi (3.4 bar) CMFS015 3 90 90 130 pressure drop on natural gas'3l CMF010M, H 1 30 30 45 CMF010P 0.9 25 20 35 CMF025 16 450 380 600 CMF050 40 1140 970 1530 CMF100 185 5000 4300 6700 CMF200 560 15,200 13,000 20,500 CMF300 1850 50,500 43,000 68,000 CMF400 4700 128,000 109,000 172,000 (1) Standard (SCFM) reference conditions are 14.7 psia and 68 F. Normal (Nm /h) reference conditions are 1.013 bar and 0 °C. (2) Air at 68 °F (20 °C) and 100 p sia (6.8 bar). (3) Natural gas with MW 16.675 at 68 °F (20 °C) and 500 psia (34.0 bar). 6 Micro Motion ELITE' Flow and Density Meters • . Gas flow performance continued Typical mass flow accuracy and pressure drop with CMF100 and transmitter with MVD technology Air at 68 °F (20 °C), static pressures as indicated on graph Inches psi bar H 1.5 0.9 0.8 m 100 psia 500 psia 1000 psia - 300 1° • 1.0 (7 bar) (35 bar) (70 bar) 10 0.7 6 0.6 ' o v 0 .5 - 200 1- V y 0.4 • u 0.5- 5 a O 0. 100 0.2 0.1 ' lb/min 0 0 20 40 60 80 100 120 140 160 0 - 0 kg /h 0 1000 2000 3000 4000 Flow rate Natural gas (MW 16.675) at 68 °F (20 °C), static pressure as indicated on graph Inches psi bar H 1.5 • 0.9 . 0.8 m - 300 2 • 1.0 - 100 psia 500 psia 1000 psia 10 0.7 c (7 bar) (35 bar) (70 bar) 0 6 . c e 'a ;b 0.5 -200 2 o N c� 0.4 m o 0.5 - 5 a` O 0.3 100 0.2 • 0.1 • 0 0 0 --0 lb/min 0 20 40 60 80 100 120 140 160 kg/h 0 1000 2000 3000 4000 FIow rate Standard or Normal Volumetric Capability Standard and normal volumes are "quasi mass" flow units for any fixed composition fluid. Standard and normal volumes do not vary with operating pressure, temperature, or density. With knowledge of density at standard or normal conditions (available from reference sources), a Micro Motion meter can be configured to output in standard or normal volume units without the need for pressure, temperature, or density compensation. Contact your local sales representative for more information. Micro Motion ELITE Flow and Density Meters 7 • Density range (liquid only) Range Up to 5 g /cm Up to 5000 kg /m Vibration limits Meets IEC 68.2.6, endurance sweep, 5 to 2000 Hz, 50 sweep cycles at 1.0 g Power consumption Meter with core processor 4 watts maximum Meter with Model 2400S transmitter 7 watts maximum Meter with Model 2200S transmitter Loop - powered, 0.8 watts maximum Meter with Model 1700/2700 transmitter Refer to transmitter documentation 8 Micro Motion ELITE Flow and Density Meters • • Pressure ratings 316L and 304L Sensor rating stainless steel Alloy C -22 High pressure psig bar psig bar psig bar CMFS010 1813 125 3263 225 6000 413 CMFS015 1813 125 3263 225 6000 413 CMF010 1813 125 3263 225 6000 413 CMF025 1500 103 2755 190 — — CMF050 1500 103 2683 185 — — CMF100 1450 100 2465 170 — — CMF200 1580 108 2755 190 — — CMF300 1730 119 2683 185 — — CMF400 1500 103 2855 197 2973 205 PED compliance Sensors comply with council directive 97/23/EC of 29 May 1997 on Pressure Equipment Dual seal compliance CSA sensors comply with ANSI /ISA 12.27.01 -2003 requirements for process sealing between electrical systems and flammable or combustible process fluids ASME B31.3 1 secondary containment rating (2) (3) Burst pressuree Housing rating (3) psig bar psig bar CMFS010 850 58 5169 356 CMFS015 850 58 5169 356 CMF010 425 29 3042 209 CMF025 850 58 5480 377 CMF050 850 58 5286 364 CMF100 625 43 3299 227 CMF200 550 37 2786 192 CMF300 275 18 1568 108 CMF400 250 17 1556 107 (1) Process connection rating may differ from sensor rating. Please choose process connections accordingly. (2) For operating temperatures above 300 °F (148 °C), pressure needs to be derated as follows. Linear interpolation may be used between values. Process connection derating may differ from sensor rating. Flow tubes Housing 316L sensors 304L sensors Alloy C -22 sensors 316L sensors 304L sensors up to 300 °F (up to 148 °C) None None None None None at 400 °F (at 204 °C) 7.2% derating 5.4% derating None 7.2% derating 5.4% derating at 500 °F (at 260 °C) 13.8% derating 11.4% derating 4.7% derating — — at 600 °F (at 316 °C) 19.2% derating 16.2% derating 9.7% derating — — at 650 °F (at 343 °C) 21.0% derating 18.0% derating 11.7% derating — — (3) The housing of high - temperature models is rated for neither secondary containment nor burst pressure. (4) Optional rupture disks for high - pressure CMF010P will burst if pressure inside sensor housing reaches 400 psig (27 bar). Micro Motion ELITE Flow and Density Meters 9 • • Environmental effects Process temperature effect Process temperature effect is defined as: • For mass flow measurement, the worst -case zero offset due to process fluid temperature change away from the zeroing temperature. • For density measurement, the maximum measurement offset due to process fluid temperature change away from the density calibration temperature. Process temperature effect % of maximum flow rate per °C density accuracy per °Co g /cm kg /m CMFS010, CMFS015, CMF010, CMF025, ±0.0002 ±0.000015 ±0.015 CMF050, and CMF100 CMF200 ±0.0005 ±0.000015 ±0.015 CMF300 ±0.0005 ±0.000015 ±0.015 CMF400 ±0.0007 ±0.000015 ±0.015 Pressure effect Pressure effect is defined as the change in sensor flow and density sensitivity due to process pressure change away from the calibration pressure. Pressure effect can be corrected. Pressure effect on flow accuracy % of rate per psi % of rate per bar liquid gas liquid gas CMFS010 None None None None CMFS015 None None None None CMF010 None None None None CMF025 None None None None CMF050 None None None None CMF100 —0.0002 None —0.003 None CMF200 — 0.0008 —0.0004 —0.012 —0.006 CMF300 — 0.0006 — 0.0003 —0.009 —0.0045 CMF400 —0.0015 —0.0015 — 0.022 —0.022 Pressure effect on density accuracy g /cm per psi kg /m per bar CMFS010 None None CMFS015 None None CMF010 None None CMF025 0.000004 0.058 CMF050 — 0.000002 —0.029 CMF100 — 0.000006 —0.087 CMF200 —0.000001 —0.0145 CMF300 —0.0000002 —0.0029 CMF400 —0.00001 —0.145 (1) For — 100 °C and above. 10 Micro Motion ELITE Flow and Density Meters • Hazardous area classifications UL' All models with core processor Ambient temperature: —40 to +104 °F (-40 to +40 °C) Class I, Div. 1, Groups C and D Class I, Div. 2, Groups A, B, C, and D Class II, Div.1, Groups E, F, and G All models with junction box Ambient temperature: +104 °F ( +40 °C) maximum Class I, Div. 1, Groups C and D Class I, Div. 2, Groups A, B, C, and D Class II, Div.1, Groups E, F, and G CSA and CSA C -US All models with Model 2400S transmitter Ambient temperature: —40 to +140 °F (-40 to +60 °C) Class I, Div. 2, Groups A, B, C and D Class II, Div. 2, Groups F and G Models CMFS010 and CMFS015 with Ambient temperature: —13 to +140 °F ( -25 to +60 °C) FMT transmitter Class I, Div. 2, Groups A, B, C and D Class II, Div. 2, Groups F and G All models with core processor Ambient temperature: —40 to +140 °F ( -40 to +60 °C) or Model 2200S transmitter Class I, Div. 1, Groups C and D Class I, Div. 2, Groups A, B, C, and D Class II, Div.1, Groups E, F, and G All models with junction box Ambient temperature: +140 °F ( +60 °C) maximum Class I, Div. 1, Groups C and D Class 1, Div. 2, Groups A, B, C, and D Class II, Div.1, Groups E, F, and G NEPSI All models with Model 2400S transmitter Ex nA II T1 —T5 Models CMF010, CMF025, CMF050, CMF100, Ex ib IIC T1 —Tm CMFS010, and CMFS015 with core processor or junction box Models CMF200, CMF300, and CMF400 Ex ib IIB /IIC T1 —To' with core processor or junction box (1) The following products are not available with UL approval: sensors with enhanced core processor, Model 2400S transmitter, or Model 2200S transmitter; high- temperature sensors; extreme high- temperature sensors. (2) The following products are available only with CSA C -US approval (i.e., not CSA): sensors with enhanced core processor or Model 2400S transmitter; high - temperature sensors; extreme high - temperature sensors. (3) For ambient and process temperature limits, refer to the temperature graphs on pages 13 -16. Micro Motion ELITE Flow and Density Meters 11 • • Hazardous area classifications continued ATEX All models with Model 2400S transmitter; C E Ex II 3G Ex nA IIC T1 —T5 Gc Models CMFS010 and CMFS015 with FMT transmitter II 3D Ex tc IIIC To °C Dc IP65 Models CMFS010, CMFS015, CMF010, CMF025, C E 0575 Ex II 2G Ex ib IIC T1 —T4 CMF050, and CMF100 with Model 2200S transmitter II 2D Ex ibD 21 To °C �E ix II 3G ExnAIIT1 —T4 II 3D Ex tD A22 IP65 To °C Models CMF200, CMF300, and CMF400 with ( E 0575 £x II 2G Ex ib IIB /IIC T1 —T4 Model 2200S transmitter II 2D Ex ibD 21 To °C E Ex II 3G Ex nA II T1 —T4 II 3D Ex tD A22 IP65 To °C Models CMFS010 and CMFS015 (E 0575 i:x 112G Ex ib IIC T1 —To with core processor or junction box II 2D Ex tD A21 IP65 To °C Models CMF010, CMF025, CMF050, and CMF100, (E 0575 Ex II 2G Ex ib IIC T1 —To Gb with core processor or junction box II 2D Ex ib IIIC To °C Db IP65 Models CMF200, CMF300, and CMF400 (E 0575 l:x II 2G Ex ib IIB /IIC T1 —To Gb with core processor or junction box II 2D Ex ib IIIC To °C Db IP65 IECEx All models with Model 2400S transmitter; Ex nA IIC T1 —T5 Gc Models CMFS010 and CMFS015 with FMT transmitter Models CMF010, CMF025, CMF050, CMF100, Ex ib IIC T1 —T°" Gb CMFS010, and CMFS015 with core processor or junction box Models CMF200, CMF300, and CMF400 Ex ib IIB /IIC T1—To Gb with core processor or junction box Models CMFS010, CMFS015, CMF010, CMF025, Ex ib IIC T1 —T4 CMF050, and CMF100 with Model 2200S transmitter Ex nA II T1 —T4 Model CMF200, CMF300, and CMF400 with Ex ib IIB /IIC T1 —T4 Model 2200S transmitter Ex nA II T1 —T4 (1) For ambient and process temperature limits, refer to the temperature graphs on pages 13 12 Micro Motion ELITE Flow and Density Meters • • Hazardous area classifications continued Model CMF010, CMF025, or CMF050 with junction box connected to MVD transmitter 90 - 80 - 70 - Sa 60 - 55 a1 40 a5 30 20 - E 10 - T6 T5 T4 T3 T1 -T2 m 0 - M -10 - 240 1 30 1 45 1 1 I 1145 1 1 -240 0 20 40 60 80 100 120 140 160 180 204 220 Sensor fluid temp ( °C) Use the above graph to determine the temperature class for a given fluid and ambient temperature. The maximum surface temperature for dust is as follows: T6:T 80 °C, T5:T 95 °C, T4:T 130 °C, T3:T 195 °C, T2 to T1:T 254 °C. The minimum ambient and process fluid temperature allowed for dust is —40 °C. The use of the sensor at an ambient temperature higher than +55 °C is possible, provided that the ambient temperature does not exceed the maximum temperature of the medium taking into account the temperature classification and the maximum operating temperature of the sensor. Ambient temperature range Ta —240 °C to +55 °C Model CMF100 with junction box connected to MVD transmitter 90 - 80 - _ 70 - U 60 — 55 . 50 45 g 40 30 a 20 - m 10 - T6 T5 T4 T3 T1 -T2 0 - 2 -10 - -60 1 1 30 1 45 I 1 1 1 145 I r 1 -60 0 20 40 60 80 100 120 140 160 180 204 220 Sensor fluid temp ( °C) Use the above graph to determine the temperature class for a given fluid and ambient temperature. The maximum surface temperature for dust is as follows: T6:T 80 °C, T5:T 95 °C, T4:T 130 °C, T3:T 195 °C, T2 to T1:T 254 °C. The minimum ambient and process fluid temperature allowed for dust is —40 °C. The use of the sensor at an ambient temperature higher than +55 °C is possible, provided that the ambient temperature does not exceed the maximum temperature of the medium taking into account the temperature classification and the maximum operating temperature of the sensor. Ambient temperature range Ta —60 °C to +55 °C Micro Motion ELITE Flow and Density Meters 13 • Hazardous area classifications continued Model CMF200 or CMF300 with junction box connected to MVD transmitterl' 90 - 80 - 70 - U 60 55 £ a 50 45 2 40 - 30 a 20 - 83 10 - T6 T5 T4 T3 T1 -T2 x m 0 - - 10 - - 55 1 1 30 1 45 1 I 1 1145 1 1 -55 0 20 40 60 80 100 120 140 160 180 204 220 Sensor fluid temp ( °C) i and ambient temperature. The maximum surface in the temperature class for given fluid p Use the above graph to determine p 9 temperature for dust is as follows: T6:T 80 °C, T5:T 95 °C, T4:T 130 °C, T3:T 195 °C, T2 to T1:T 254° C. The minimum ambient and process fluid temperature allowed for dust is -40 °C. The use of the sensor at an ambient temperature higher than +55 °C is possible, provided that the ambient temperature does not exceed the maximum temperature of the medium taking into account the temperature classification and the maximum operating temperature of the sensor. Ambient temperature range Ta -55 °C to +55 °C Model CMF400 with junction box connected to MVD transmitter 90 - 80 - 70 - o 60 50 E n 40 - d 30 - 20 T6 T5 T4 T3 T1 —T2 to - m o- co -10 -20 - - 30 - -40 - - 68 1 1 1 1 I I 1 1 1 16 1 -68 -40 -20 0 20 40 50 60 80 100 120 140 160 180 204 220 Sensor fluid temp ( °C) Use the above graph to determine the temperature class for a given fluid and ambient temperature. The maximum surface temperature for dust is as follows: T6:T 80 °C, T5:T 95 °C, T4:T 130 °C, T3:T 195 °C, T2: to TI :T 234 °C. The minimum ambient and process fluid temperature allowed for dust is -40 °C. The use of the sensor at an ambient temperature higher than +60 °C is possible, provided that the ambient temperature does not exceed the maximum temperature of the medium taking into account the temperature classification and the maximum operating temperature of the sensor. Ambient temperature range Ta -68 °C to +60 °C (1) Refer to page 15 for "T" rating graph for high temperature models with junction box. 14 Micro Motion ELITE Flow and Density Meters • Hazardous area classifications continued High- temperature models CMF200A, CMF200B, CMF300A, CMF300B, CMF400A, or CMF400B with junction box connected to MVD transmitter 90 - 80 - 70 - U 60g . 50- m 40 30 - y 20 - E 1 0 - T6 T5 T4 T3 T2 T1 to 0 - x -10- 2 -20- -30 -50 1 87 1 82 1 117 1 1 182 1 1 1 277 1 350 -50 -20 0 20 40 60 80 100 120 140 160 180 200 220 240 260 280 300 320 340 360 Sensor fluid temp ( °C) Use the above graph to determine the temperature class for a given fluid and ambient temperature. The maximum surface temperature for dust is as follows: T6:T 80 °C, T5:T 95 °C, T4:T 130 °C, T3:T 195 °C, T2:T 290 °C, T1:T 363 °C. The minimum ambient and process fluid temperature allowed for dust is -40 °C. The use of the sensor at an ambient temperature higher than +55 °C is possible, provided that the ambient temperature does not exceed the maximum temperature of the medium taking into account the temperature classification and the maximum operating temperature of the sensor. Ambient temperature range Ta -50 °C to +55 °C Models CMF010, CMF025, CMF050, CMF100, CMF200 or CMF300 with core processorl' 80 - 70 - 60 _ E 40 �� a) 30 - a) m 10 T5 T4 T3 T1 -T2 x m 0 - -10 - -40 1 1 1 45 53 1 1 I 1 145 1 -40 0 20 40 60 80 100 120 140 160 180 204 220 Sensor fluid temp ( °C) Use the above graph to determine the temperature class for a given fluid and ambient temperature. The maximum surface temperature for dust is as follows: T5:T 95 °C, T4:T 130 °C, T3:T 195 °C, T2 to T1:T 254 °C. Ambient temperature range Ta -40 °C to +60 °C (1) Refer to page 16 for "T" rating graph for high - temperature models with core processor. Micro Motion ELITE Flow and Density Meters 15 • Hazardous area classifications continued Model CMF400 with core processor 80 - 70 - 60 U 50 46 40 - 30 - 20 - m 10 _ T5 T4 T3 T1- T2 E 0- m x -10- -20 - -30 - 40 1 1 53 65 1 1 1 1 165 1 -40 -20 0 20 40 60 80 100 120 140 160 180 204 220 Sensor fluid temp ( Use the above graph to determine the temperature class for a given fluid and ambient temperature. The maximum surface temperature for dust is as follows: T5:T 95 °C, T4:T 130 °C, T3:T 195 °C, T2 to T1:T 234 °C. Ambient temperature range Ta -40 °C to +60 °C High- temperature models CMF200A, CMF200B, CMF300A, CMF300B, CMF400A, or CMF400B with core processor or Model 1700/2700 transmitter 90 - 80 - 70 - U 6051 a 50 - y 40 - • 30 - aa> 20- m O _ T5 T4 T3 T2 Ti as -10- • -20- -30 50 1 52 1 117 I 1 11182 1 1 1 2771 1 1 350 -50 -20 0 20 40 60 80 100 120 140 160 180 200 220 240 260 280 300 320 340 360 Sensor fluid temp ( °C) Use the above graph to determine the temperature class for a given fluid and ambient temperature. The maximum surface temperature for dust is as follows: T5:T 95 °C, T4:T 130 °C, T3:T 195 °C, T2: T 290 °C, T1 :T 363 °C. The minimum ambient and process fluid temperature allowed for dust is -40 °C. Since the electronics are mounted approx. 1 meter away from the sensor by means of a flexible stainless steel hose, the use of the sensor at an ambient temperature higher than +55 °C is possible, provided that the ambient temperature does not exceed the maximum temperature of the medium taking into account the temperature classification and the maximum operating temperature of the sensor. Ambient temperature range Ta -50 °C to +55 °C 16 Micro Motion ELITE Flow and Density Meters • • Hazardous area classifications continued Models CMFS010 or CMFS015 with core processor 90 - 80 - _ 70 - U 60 - 55 • 50 46 40 - w 30 - E 20 - m 10 - T5 T4 T3 -T2 -T 1 2 0 - -10 - -40 I 1 1 1 I 92 1 103 1 127 1 1 I 192 -40 0 20 40 60 80 100 120 140 160 180 204 220 Sensor fluid temp (°C) Use the above graph to determine the temperature class for a given fluid and ambient temperature. The maximum surface temperature for dust is as follows: T5:T 95 °C, T4 :T 130 °C, T3:T 195 °C, T2 to T1:T 207 °C. The minimum ambient and process fluid temperature allowed for dust is -40 °C. Ambient temperature range Ta -40 °C to +55 °C Models CMF010, CMF025, CMF050, and CMF100 with Model 2200S transmitter 80 - U 70 - n 60 E • 40 - a 30 - m 20 - m 10 - T4 T3 T1 -T2 • 0 - -10 - -40 I 1 1 g I 1 1 1145 1 I 1 -40 0 20 40 60 80 100 120 140 160 180 204 220 Sensor fluid temp ( °C) Use the above graph to determine the temperature class for a given fluid and ambient temperature. The maximum surface temperature for dust is as follows: T4:T 130 °C, T3:T 195 °C, T2 to T1:T 254 °C. Micro Motion ELITE Flow and Density Meters 17 • • Hazardous area classifications continued Models CMFS010 and CMFS015 with Model 2200S transmitter 80 — 70 — U 60 E 5046 a1 40 — c 30 - a1 :n 20 — m 10 _ T4 T3 - T1 —T2 m 0 — —10 — 40 1 1 1 53 I 1 1 12 7 1 ' 1 192 —40 0 20 40 60 80 100 120 140 160 180 204 220 Sensor fluid temp ( °C) Use the above graph to determine the temperature class for a given fluid and ambient temperature. The maximum surface temperature for dust is as follows: T4:T 130 °C, T3:T 195 °C, T2 to T1:T 207 °C. Models CMF400 with Model 2200S transmitter 80 — 70 — 60 50 46 0. 40 — E 4; 30 — 0 • 20 — £ ▪ to T4 T3 T1 — T2 as x 0 - m 3 -10 - 20 - - 30 - - 40 I I I I I I I I I t 65 I I —40 —20 0 20 40 60 80 100 120 140 160 180 204 220 Sensor fluid temp ( °C) Use the above graph to determine the temperature class for a given fluid and ambient temperature. The maximum surface temperature for dust is as follows: T4:T 130 °C, T3:T 195 °C, T2 to T1:T 234 °C 18 Micro Motion ELITE Flow and Density Meters • • Materials of construction Wetted parte' (2)13) 304L or 316L stainless steel; or alloy C -22 Housing 304L stainless steelo Junction box 300- series stainless steer' or polyurethane- painted aluminum; NEMA 4X (IP66) Core processor 300 - series stainless steel or polyurethane- painted aluminum; NEMA 4X (IP66) Model 2400S transmitter Polyurethane - painted aluminum or 316L stainless steel; NEMA 4X (IP66) Model 2200S transmitter Polyurethane- painted aluminum or 316L stainless steel; NEMA 4X (IP66/67) (1) General corrosion guides do not account for cyclical stress, and therefore should not be relied upon when choosing a wetted material for your Micro Motion sensor. Please refer to the Micro Motion corrosion guide for proper material compatibility information. (2) The outer flange ring on lap joint type flanges is non - wetted and is 304L stainless steel. Consult factory for other materials. (3) Models CMF010P, CMFS010P, CMFS015P, and CMF400P have nickel alloy tubes and stainless steel fittings. Material compatibility is never better than 316L stainless steel. Refer to the Micro Motion Corrosion Guide for the Micro Motion policy on fixed bi- metallic sensor capability. (4) 316L stainless steel is available. Weight Weights provided are the weight of the flowmeter with 150 Ib weld neck raised face flanges. With core processor, Model 2400S,or Model 2200S With junction box transmitterm With EMT transmitter Ib kg Ib kg Ib kg CMFS010 — — 9 4 12 5 CMFS015 — — 9 4 12 5 CMF010 14 7 19 9 — — CMF025 8 4 13 6 — — CMF050 12 6 17 8 — — CMF100 29 13 34 16 — — CMF200 63 29 68 31 — — CMF300 165 75 170 77 — — CMF400 441 200 446 202 — — (1) Weight stated for sensor with aluminum core processor. Add 4 lb (2 kg) for stainless steel core processor or stainless steel Model 2400S transmitter. Micro Motion ELITE Flow and Density Meters 19 0 • Dimensions Models CMFS010 and CMFS015 with Model 2200S, Model 2400S, or enhanced core processor Dimensions in l(mm) Flow ♦ � �� 2x29/16 _ �'�� 21/16 31/4 " ( - O � (52) (83) N. Model 2400S or r N t IBM core /� 131/2- processor: op i (342) 2 x 1/2 " -14 NPT female (.�� I1 \\ � or M20 . 1.5 female %\`. _ . O �„� 01 1/4 Model 2200S: '� /'� � �� e1 Optional 81/4" (32) 1 x 1/2 " -14 NPT female . 1 female purge Pplug (209) or M20 • 1.5 female \ IS� �:MIMI Mil Ln a. C2 -1 tthilil or 4,,m,s,,,,,,,,.„...z.„, .itrIIIIIIIIMMIWalkllamim OtlIAIII `4 Ir. 1t 1' (19) II ■■ r iiimmi• 4 7/16 ,,I'' 1111 (113) \ii.xy,II 111 J 2 3/16 2 118 (56) 8 5/8 (54) (219) 3 Dim. A (76) face -to -face t1 /8 (3) 7.20 Flange detail (183) I �, '� i Ion 1IIII� /1111 ��I Dim. e ♦ I 2 ■■i■ (51) THUM adapter detail Dim. A face -to -face 31/8 (3) * For dimensions A and B, see fittings options on pages 31 and 32. ** Electronics with painted aluminum housing shown. For stainless steel housing, add 0.40 inches (10 mm). No. of Flow tube ID Model flow tubes inches (mm) CMFS010 2 0.07 (1.8) CMFS015 2 0.11 (2.9) 20 Micro Motion ELITE Flow and Density Meters 1 Dimensions continued Models CMFS010 and CMFS015 with Filling Mass Transmitter Dimensions in inches (mm) 2 (50) 3/16 8 1/2 (5) (216) 1/4 1/4 (6) p �� (6) 3 x 1/2 (6) (13) M12 flush type um plug male k PROFIBUS -DP or Wank plug �', .I 75/8 1 (194) _ M12 flush type ' ∎M 5 3/8 ■11..WAV plug female !. ;- 4 11/16 (137) .II' J (119) A P (14 02) I 0 1�. I I 111ia1 I _ + 1011 11 }I L2x01(25) 4 7/16 (113) 2 1/8 (54) 11 1/2 ±1 /8 (292 ±3) * For dimensions A and B, see fittings options on page 29. No. of Flow tube ID Model flow tubes inches (mm) CMFS010 2 0.07 (1.8) CMFS015 2 0.11 (2.9) i II I Micro Motion ELITE Flow and Density Meters 21 1 • Dimensions continued Model CMF010 Dimensions in inches (mm) Flow y Side view with rupture disk 2 13/16 2 / (71) 2 x 1 9/16 4 Optional 2 x 1/2 " -14 female purge ` I (40) (112) 12) — plug fitting rii% /', i ll Il 35/16 / (110 4-----:-.J.. ,\ 0,•/� ± . a Optional IMO M. 2x rupture Num 113/16 disks (46) Dim. A face -to -face Flange detail + 1 t1 /8 (3) r Dim. A face -to -face we ,:,.111 law t1l8 (3) 400) 0 49/,6 1 f 1 2 x ) Dim. 0 B (116) (59 I Cr� �- _r4 1 thru cj (180) I21 rir 3 3/8 (86) 9 (229) * For dimensions A and B, see fittings options on pages 31 and 32. ** Dimensions for each electronics option are shown on page 26. No. of Flow tube ID Model flow tubes inches (mm) CMF010 1 0.11 (2.9) 22 Micro Motion ELITE Flow and Density Meters • • Dimensions continued Models CMF025, CMF050, and CMF100 Dimensions in ( Flow 2x Dim. J Dim. C Optional 2 x 1/2 " -14 female purge plug fitting CO aryl I Li ., it 7. Dim. H Pal :D Dim. D IPA11 40 - s• .74t. _ i Dim. E Dim. G Dim. A face - to-face Wafer detail }- t1/8 (3) I {mil Dim. 0 B i_re Tsi l =l+ Union detail Dim. A face - to-face r 3118 (3) 2 x 1 j I- 45 El 1 116 a .lii- *11 1/2"-14 female ' WI be all Mel I I Flange detail Dim. A III face - to-face 1 31/8 (3) ff Dim. 013 DM I l lj1 III ' l Tr lid No. of Ai Oa Dimensions in inches (mm) Model flow tubes Flow tube ID C D E G H J CMF025 2 0.21 2 13/16 8 1/4 10 1 5/8 3 5/16 2 1/4 (5.2) (72) (209) (255) (41) (85) (58) CMF050 2 0.35 5 11 1/16 14 5/16 2 4 3/8 2 1/2 (8.8) (126) (280) (364) (51) (111) (63) CMF100 2 0.65 5 15/16 15 15/16 21 1/2 3 9/16 5 3/8 3 5/16 (16) (150) (405) (546) (91) (136) (83) (1) For dimensions A and B, see fittings tables on pages 34-36. (2) Dimensions for each electronics option are shown on page 26. Micro Motion ELITE Flow and Density Meters 23 • Dimensions continued Models CMF200 and CMF300 Dimensions in inches (mm) Flow Dim. A face -to -face ±118 (3) itt Dim. 6 B - -� Dim. H Dim. D Optional 2 x 1/2 " -14 female purge plug fitting 1P 2 x Dim. J 4 Dim. G — , --- Dim. C - Dim. E 'r No. of Dimensions in inches (mm) Model flow tubes Flow tube ID C D E G H J CMF200 2 1.1 14 28 5/8 19 9/16 5 9/16 11 7/8 4 5/16 (27) (356) (727) (497) (142) (302) (110) CMF300 2 1.8 22 38 7/16 30 3/16 8 3/16 13 7/8 5 5/8 (45) (559) (977) (767) (209) (352) (143) (1) For dimensions A and B, see fittings tables on pages 37 -39. (2) Dimensions for each electronics option are shown on page 26. 24 Micro Motion ELITE Flow and Density Meters • • Dimensions continued Model CMF400 Dimensions in inches (mm) Flow Dim. A face - to-face ±1/8 (3) Dim. OB -I� lait i 12 3/8 (314) 17 3/8 (441) SN em 110 381/4 \ I / (971) Optional 2 • 1 " -11 1/2 female purge plug fitting 2x67/16 22 (163) 10 3/4 (559) -. (274) 32 3/4 (832) I I I B see fittings pages 31 and 32. s o tions on a For dimensions A and g p p g •* Dimensions for each electronics option are shown on page 26. No. of Flow tube ID Model flow tubes inches (mm) CMF400 2 2.9 (73) Micro Motion ELITE Flow and Density Meters 25 • • Dimensions continued Electronics detail for Models CMF010, CMF025, CMF050, CMF100, CMF200, CMF300, and CMF400 Enhanced core processor, Model 2400S, or Model 2200S with painted aluminum housing Flange center Dimensions in inches (mm) Model F M P S T 2 x i 1/2 " -14 NPT or CMF010 513/16 (147) 3 7/8 (98) 9 5/16 (236) 71/8 (180) 121/2 (318) M20x1.5 female ` F 1 C 77/16(188) 313/16(97) 95/16(236) 71/16(179) 121/2(318) ' O ^ O CMF050 101/16 (255) 41/16 (103) 9 7/16 (240) 75116 (185) 1211116 (322) © ® O � i i CMF100 141/8(360) 43/4(121) 101/8(257) 8(204) 133/8(340) / / 16 / � CMF200 6 7/8 (175) 5 7/8 (150) 11 1/4 (286) 91/8 (232) 141/2 (368) i 1 3/ M (29) i P 1 II CMF300 93/8 (238) 7 3/16 (183) 125/8 (320) 1012 (266) 15 7/8 (403) 1 1 3/16 (29) 1 3/16 (29) i CMF400 12318 (314) 8 7116 (215) 13 718 (352) 11 11116 (297) 171116 (434) s ---� i T — Enhanced core processor, Model 2400S, or Model 2200S Flange center with stainless steel housing Dimensions in inches (mm) 2 • I Model F M P S T 1/2 " -14 NPT or M20x1.5 1 CMF010 513/16 (147) 41/16 (103) 9 5/16 (236) 7 9/16 (192) 1213/16 (325) F CMF025 7 7/16 (188) 4 1/16 (103) 95/16(236) 79/16(192) 12 13/16 (325) p O I! il CMF050 101/16(255) 4(102) 93/16(234) 79/16(192) 123/4(324) / %�!� 13/16 r r CMF100 143/16(360) 47/8(124) 101/8(257) 83/8(213) 135/8(346) 1 M ( _�� p 1 CMF200 6 7/8 (175) 53/4 (147) 11 (280) 9 7/16 (239) 145/8 (372) I i 1 3/16 (29) 1 3116 (29) I CMF300 93/8 (238) 71/4 (183) 12 7/16 (316) 103/4 (273) 16 (406) I i CMF400 123/8 (314) 812 (216) 133/4 (349) 121/16 (306) 171/4 (439) S --•-i T Model 2200S with THUM adapter Flange center Dimensions in inches (mm) �I Model F P S CMF010 5 13/16 (147) 5 3/16 (132) 7 9/16 (192) 7.20 CMF025 7 7/16 (188) 5 3/16 (132) 7 9/16 (192) (183183 ) CMF050 10 1/16 (255) 51/8 (130) 7 9/16 (192) i F CMF100 14 3/16 (360) 6 (152) 8 3/8 (213) �\ �n ) 11� CMF200 6 718 (175) 6 718 (175) 9 7/16 (239) '� II CMF300 9 3/8 (238) 8 5/16 (212) 10 3/4 (273) *4 hr�� 1 � J1 " CMF400 12 3/8 (314) 9 5/8 (245) 12 1/16 (306) `� / i I (51) I 1 I I 1/2 " -14 NPT i female P i I S -..l 26 Micro Motion ELITE Flow and Density Meters • • Dimensions continued Electronics detail for Models CMF010, CMF025, CMF050, CMF100, CMF200 CMF300, and CMF400 Standard core processor Flange center Dimensions in Inches (mm) Model F M $ CMF010 8 7/16 (214) 2 7/8 (73) 4 9/16 (116) ..... t CMF025 10 1/16 (255) 2 15/16 (75) 4 11/16 (119) CMF050 12 11/16 (322) 3 1/16 (77) 4 3/4 (121) II po CMF100 16 13/16 (426) 3 13/16 (96) 5 1/2 (139) CMF200 9 1/2 (241) 4 13/16 (122) 6 1/2 (165) CMF300 11 15/16 (303) 6 1/8 (155) 7 13/16 (199) r i M CMF400 15 (380) 7 3/8 (188) 9 1/8 (231) i S --I 112 " -14 NPT or M20x1.5 female Junction box Flange center Dimensions in inches (mm) Model F M S CMF010 7 3/4 (197) 2 (50) 3 5/16 (84) -.5. t CMF025 9 11/16 (246) 2 1/16 (53) 3 7/16 (87) F CMF050 12 (305) 2 3/16 (55) 3 1/2 (89) !4li CMF100 16 1/8 (409) 2 15/16 (74) 4 1/4 (108) 1 CMF200 8 13/16 (223) 3 15/16 (100) 5 1/4 (134) �� I CMF300 11 1/4 (286) 5 1/4 (133) 6 9/16 (167) M CMF400 14 5/16 (363) 6 3/8 (162) 7 11/16 (195) 3/4 " -14 NPT S female Extended 9 -wire junction box Dimensions in inches (mm) CMF010 95/16 (236) 95116 (236) 12112 (318) 1213/16 (325) Az; CMF025 9 5/16 (236) 9 5/16 (236) 121/2 (318) 1213/16 (325) . p �' ii r r /`p� o o i i CMF050 9 7/16 (240) 93/16 (234) 1211/16 (322) 123/4 (324) l CMF100 10118 (257) 1018 (257) 13318 (340) 1358 (346) P -• P2 - I CMF200 11 1/4 (286) 11(280) 141/2 (368) 1458 (372) I I II CMF300 1258(320) 127/16(316) 157/8(403) 16(406) i I CMF400 13 78 (352) 133/4 (349) 171/16 (434) 171/4 (439) T1 -w' T2 ----. Micro Motion ELITE Flow and Density Meters 27 • 0 Dimensions continued High- temperature Models CMF200A, CMF200B, CMF300A, and CMF300B Dimensions in inches (mm) Transmitter, core processor, or junction box mounts on end of flexible 41/8 (105) =1 ri conduit. Dimensions for electronics t are shown on page 30. - IN e e Dim. I Dim. K Q C,>1 1 Dim. F hivit D im. H / / .,•..i. .,•..i. _ L u u 01 5/16 (33) U \ Flexible conduit 48 (1219) minimum bend radius 6 in (152 mm) 3 (76) IP 10 Refer to page 24 for additional sensor dimensions. I Dimensions in inches (mm) Model F H K Q CMF200A and 6 7/8 (175) 6 5/16 (160) 3 15/16 (100) 6 7/16 (163) CMF200B CMF300A and 9 3/8 (238) 9 1/4 (235) 5 1/4 (134) 7 3/4 (197) CMF300B • 28 Micro Motion ELITE Flow and Density Meters ! • Dimensions continued High- temperature Models CMF400A and CMF400B Dimensions in inches (mm) Transmitter, core processor, or junction box -1--- — I 1 1 mounts on end of flexible conduit. Dimensions for 4 1/8 (105) - -I 9 t electronics are shown on page 30. i . (229) 6 1/2 (166) Iv II I 0 1 11 i ":11 (1 99) � edAlk 7 17 8 - ' ► L _ ‘I I, '''--- 48 (1219) Flexible conduit minimum bend radius 6 in (152 mm) 3 (76) i ll Refer to page 25 for additional sensor dimensions. II I Micro Motion ELITE Flow and Density Meters 29 • • Dimensions continued Electronics mounted on high- temperature sensor flexible conduit Dimensions in inches (mm) Model 2400S, 1700, 2700, or enhanced core processor: o 2 • 1/2 " -14 NPT female � or M20 . 1.5 female vi i) Standard core processor: '` ■ 1/2" —NPT female 1 - i' O • G � 11 / or M20 • 1.5 female t Dim. C i Junction box: 1 3/8 _ 3/4 " -14 NPT female (36) CIIIli =illL �Is� u �I� slim � 13/8 -- —_ (36) 4 x 03/8 (10) 1 3/8 13/8 (36) (36) 1 4 9/16 (116) �" Electronics interface option Dimension C in inches (mm) 0 Model 2400S transmitter, painted aluminum housing 8 7/8 (225) Model 2400S transmitter, stainless steel housing 9 1/4 (235) 2 Enhanced core processor, painted aluminum housing 8 7/8 (225) 3 Enhanced core processor, stainless steel housing 9 1/4 (235) Q Standard core processor, painted aluminum housing 6 5/16 (161) A Standard core processor, stainless steel housing 6 5/16 (161) C Model 1700/2700 transmitter 10 1/4 (261) R Junction box, painted aluminum housing 3 9/16 (91) S Junction box, stainless steel housing 3 9/16 (91) I 30 Micro Motion ELITE Flow and Density Meters 0 • Fitting options Dim. A Dim. B Fitting face -to -face outside diameter code" inches (mm) inches (mm) Models CMFS010 and CMFS015 316L stainless steel sensors 1/2 -inch ANSI CL150 weld neck raised face flange 313 12.64 (321) 3 1/2 (89) 1/2 -inch ANSI CL300 weld neck raised face flange 314 13.00 (330) 3 3/4 (95) 1/2 -inch ANSI CL600 weld neck raised face flange 315 13.50 (343) 3 3/4 (95) DN15 PN40 weld neck flange; DIN 2635 type C face 300 12.21 (310) 3 3/4 (95) DN15 PN40 weld neck flange; DIN 2635 type N grooved face 301 12.21 (310) 3 3/4 (95) DN15 PN40 weld neck flange; EN 1092 -1 Form B1 176 12.21 (310) 3 3/4 (95) DN15 PN40 weld neck flange; EN 1092 -1 Form D 310 12.21 (310) 3 3/4 (95) DN15 PN100 weld neck flange; DIN 2637 type E face 302 12.76 (324) 4 1/8 (105) DN15 PN100 weld neck flange; EN 1092 -1 Form B2 177 12.76 (324) 4 1/8 (105) DN15 PN100 weld neck flange; DIN 2637 type N grooved face 303 12.76 (324) 4 1/8 (105) DN15 PN100 weld neck flange; EN 1092 -1 Form D 178 12.76 (324) 4 1/8 (105) DN25 PN40 weld neck flange EN1092 -1 Form B1 172 12.37 (314) 4 1/2 (115) DN25 PN40 weld neck flange EN1092 -1 Form D 183 12.37 (314) 41/2 (115) JIS 15mm 10K weld neck raised face flange 304 11.98 (304) 3 3/4 (95) JIS 15mm 20K weld neck raised face flange 305 11.98 (304) 3 3/4 (95) 1/4 -inch NPT female Swagelok size 4 VCO fitting 323 12.16 (309) - Swagelok compatible size 4 VCO union fitting 334 12.16 (309) - 1/2 -inch NPT female Swagelok size 8 VCO fitting 319 11.52 (293) - Swagelok compatible size 8 VCO union fitting 335 11.52 (293) - 1/2-inch sanitary fitting (Tri -Clamp compatible) 321 11.52 (293) 1 (25) 1/4 -inch tube compression fitting 324 12.16 (309) - 6 mm tube compression fitting 325 12.16 (309) - EHEDG certified, 3 -A approved fittings 3/4 -inch sanitary fitting (Tri -Clamp compatible) 344 11.52 (293) 1.0 (25) ISO clamp DN10; ISO 2852 facing /ISO 1127 pipe 345 11.2 (284) 1.34 (34) ISO clamp DN15; ISO 2852 facing /DIN 11850 pipe 346 11.2 (284) 1.34 (34) Nickel alloy sensors 1/2 -inch ANSI CL150 lap joint flange 520 12.64 (321) 3 1/2 (89) 1/2 -inch ANSI CL300 lap joint flange 521 13.00 (330) 3 3/4 (95) JIS 15mm 10K lap joint flange 522 12.98 (330) 3 3/4 (95) DN15 PN40 lap joint flange; DIN 2656 type C face 523 13.22 (336) 3 3/4 (95) DN15 PN40 lap joint flange; EN 1092 -1 Form B1 524 13.22 (336) 3 3/4 (95) 1/4 -inch NPT female Swagelok size 4 VCO fitting 323 12.16 (309) - Swagelok compatible size 4 VCO union fitting 334 12.16 (309) - (1) Fittings listed here are standard options. Other types of fittings are available. The face to face dimensions for any custom fittings ordered using a 998 or 999 fitting code are not represented in this table. It is necessary to confirm face to face dimensions of these fittings at time of ordering. Contact your local Micro Motion representative. Micro Motion ELITE Flow and Density Meters 31 • • Fitting options continued Dim. A Dim. B Fitting face -to -face outside diameter code inches (mm) inches (mm) High - pressure models CMFS010P and CMFS015P Nickel alloy sensors with stainless steel fittings 1/4 -inch NPT female Swagelok size 4 VCO fitting 323 12.16 (309) — Swagelok compatible size 4 VCO union fitting 334 12.16 (309) — 1/2 -inch NPT female Swagelok size 8 VCO fitting 319 11.52 (293) — Swagelok compatible size 8 VCO union fitting 335 11.52 (293) — 1/4 -inch tube compression fitting 324 12.16 (309) — 6 mm tube compression fitting 325 12.16 (309) — 1/2 -inch ANSI CL900/1500 weld neck raised face flange 150 14.48 (368) 4.75 (121) 1/2 -inch ANSI CL2500 weld neck raised face flange 191 15.48 (393) 5.25 (133) High - pressure model CMF010P 316L stainless steel sensors 1/4 -inch NPT female Swagelok size 4 VCO fitting 323 6 7/16 (164) — Swagelok compatible size 4 VCO union fitting 334 6 7/16 (164) — 1/4 -inch tube compression fitting 324 6 7/16 (164) — 6 mm tube compression fitting 325 6 7/16 (164) — (1) Fittings listed here are standard options. Other types of fittings are available. The face to face dimensions for any custom fittings ordered using a 998 or 999 fitting code are not represented in this table. It is necessary to confirm face to face dimensions of these fittings at time of ordering. Contact your local Micro Motion representative. 32 Micro Motion ELITE Flow and Density Meters • 0 Fitting options continued Dim. A Dim. B Fitting face -to -face outside diameter code inches (mm) inches (mm) Model CMF010 316L stainless steel sensors 1/2 -inch ANSI CL150 weld neck raised face flange 313 7 7/8 (199) 3 1/2 (89) 1/2 -inch ANSI CL300 weld neck raised face flange 314 8 3/16 (209) 3 3/4 (95) 1/2 -inch ANSI CL600 weld neck raised face flange 315 8 11/16 (221) 3 3/4 (95) 1/2 -inch sanitary fitting (Tri -Clamp compatible) 321 6 15/16 (177) 1 (25) DN15 PN40 weld neck flange; DIN 2635 type C face 300 7 7/16 (189) 3 3/4 (95) DN15 PN40 weld neck flange; EN 1092 -1 Form B1 176 7 7/16 (189) 3 3/4 (95) DN15 PN40 weld neck flange; EN 1092 -1 Form D 310 7 7/16 (189) 3 3/4 (95) DN15 PN100 weld neck flange; DIN 2637 type E face 302 8 (203) 4 1/8 (105) DN15 PN100 weld neck flange; EN 1092 -1 Form B2 177 8 (203) 4 1/8 (105) DN15 PN100 weld neck flange; EN 1092 -1 Form D 178 8 (203) 4 1/8 (105) DN25 PN40 Weld Neck Flange; EN 1092 -1 Form B1 172 7 9/16 (193) 4 1/2 (115) DN25 PN40 Weld Neck Flange; EN 1092 -1 Form D 183 7 9/16 (193) 4 1/2 (115) JIS 15mm 10K weld neck raised face flange 304 7 3/16 (183) 3 3/4 (95) JIS 15mm 20K weld neck raised face flange 305 7 3/16 (183) 3 3/4 (95) 1/4 -inch NPT female Swagelok size 4 VCO fitting 323 6 7/16 (164) — Swagelok compatible size 4 VCO union fitting 334 6 7/16 (164) — 1/4-inch tube compression fitting 324 6 7/16 (164) — 6 mm tube compression fitting 325 6 7/16 (164) — 304L stainless steel sensors 1/2 -inch ANSI CL150 weld neck raised face flange 413 7 7/8 (199) 3 1/2 (89) 1/2 -inch ANSI CL300 weld neck raised face flange 414 8 3/16 (209) 3 3/4 (95) DN15 PN40 weld neck flange; DIN 2526 type C face 423 7 7/16 (189) 3 3/4 (95) DN15 PN40 weld neck flange; EN 1092 -1 Form B1 421 7 7/16 (189) 3 3/4 (95) Nickel alloy sensors 1/2 -inch ANSI CL150 lap joint flange 520 7 7/8 (199) 3 1/2 (89) 1/2 -inch ANSI CL300 lap joint flange 521 8 3/16 (209) 3 3/4 (95) DN15 PN40 lap joint flange; DIN 2656 type C face 523 9 7/16 (240) 3 3/4 (95) DN15 PN40 lap joint flange; EN 1092 -1 Form B1 524 9 7/16 (240) 3 3/4 (95) JIS 15mm 10K lap joint flange 522 8 3/16 (208) 3 3/4 (95) 1/4 -inch NPT female Swagelok size 4 VCO fitting 323 6 7/16 (164) — Swagelok compatible size 4 VCO union fitting 334 6 7/16 (164) — (1) Fittings listed here are standard options. Other types of fittings are available. The face to face dimensions for any custom fittings ordered using a 998 or 999 fitting code are not represented in this table. It is necessary to confirm face to face dimensions of these fittings at time of ordering. Contact your local Micro Motion representative. Micro Motion ELITE Flow and Density Meters 33 0 0 Fitting options continued Dim. A Dim. B Fitting face -to -face outside diameter code' inches (mm) inches (mm) Model CMF025 316L stainless steel sensors Wafer style; 1/2 -inch ANSI (150 Ib; 300 Ib; 600 Ib bolt kit) 009 2 3/8 (60) 1 13/16 (46) Wafer style, 15mm DIN 2526; type C face (PN40 bolt kit) 016 2 3/8 (60) 1 13/16 (46) Wafer style; 15mm DIN 2512; type N grooved face (PN40 bolt kit) 017 2 3/8 (60) 1 13/16 (46) Wafer style; 15mm DIN 2526; type E face (PN100 bolt kit) 018 2 3/8 (60) 1 13/16 (46) Wafer style; 15mm DIN 2512; type N grooved face (PN100 bolt kit) 019 2 3/8 (60) 1 13/16 (46) Wafer style; 15mm; standard JIS facing (10K; 20K bolt kit) 029 2 3/8 (60) 1 13/16 (46) 1/2 -inch ANSI CL150 weld neck raised face flange 313 6 3/4 (172) 3 1/2 (89) 1/2 -inch ANSI CL300 weld neck raised face flange 314 7 1/8 (181) 3 3/4 (95) 1/2 -inch ANSI CL600 weld neck raised face flange 315 7 5/8 (194) 3 3/4 (95) 1/2 -inch NPT female Swagelok size 8 VCO fitting 319 4 11/16 (119) — Swagelok compatible size 8 VCO union fitting 335 4 11/16 (119) — 1/2-inch sanitary fitting (Tri -Clamp compatible) 321 4 11/16 (119) 1 (25) DN15 PN40 weld neck flange; DIN 2635 type C face 300 6 5/16 (160) 3 3/4 (95) DN15 PN40 weld neck flange; EN 1092 -1 Form B1 176 6 5/16 (160) 3 3/4 (95) DN15 PN40 weld neck flange; DIN 2635 type N grooved face 301 6 5/16 (160) 3 3/4 (95) DN15 PN40 weld neck flange; EN 1092 -1 Form D 310 6 5/16 (160) 3 3/4 (95) DN15 PN100 weld neck flange; DIN 2637 type E face 302 6 15/16 (176) 4 1/8 (105) DN15 PN100 weld neck flange; EN 1092 -1 Form B2 177 6 15/16 (176) 4 1/8 (105) DN15 PN100 weld neck flange; DIN 2637 type N grooved face 303 6 15/16 (176) 4 1/8 (105) DN15 PN100 weld neck flange; EN 1092 -1 Form D 178 6 15/16 (176) 4 1/8 (105) DN25 PN40 Weld Neck Flange; EN 1092 -1 Form B1 172 6 7/16 (164) 4 1/2 (115) DN25 PN40 Weld Neck Flange; EN 1092 -1 Form D 183 6 7/16 (164) 4 1/2 (115) JIS 15mm 10K weld neck raised face flange 304 6 1/8 (156) 3 3/4 (95) JIS 15mm 20K weld neck raised face flange 305 6 1/8 (156) 3 3/4 (95) 304L stainless steel sensors 1/2 -inch ANSI CL150 weld neck raised face flange 413 6 3/4 (172) 3 1/2 (89) 1/2 -inch ANSI CL300 weld neck raised face flange 414 7 1/8 (181) 3 3/4 (95) DN15 PN40 weld neck flange; DIN 2526 type C face 423 6 5/16 (160) 3 3/4 (95) DN15 PN40 weld neck flange; EN 1092 -1 Form B1 421 6 5/16 (160) 3 3/4 (95) Nickel alloy sensors 1/2 -inch ANSI CL150 lap joint flange 520 6 3/4 (172) 3 1/2 (89) 1/2 -inch ANSI CL300 lap joint flange 521 7 1/8 (181) 3 3/4 (95) DN15 PN40 lap joint flange; DIN 2656 type C face 523 7 5/16 (186) 3 3/4 (95) DN15 PN40 lap joint flange; EN 1092 -1 Form B1 524 7 5/16 (186) 3 3/4 (95) JIS 15mm 10K lap joint flange 522 7 1/8 (181) 3 3/4 (95) (1) Fittings listed here are standard options. Other types of fittings are available. The face to face dimensions for any custom fittings ordered using a 998 or 999 fitting code are not represented in this table. It is necessary to confirm face to face dimensions of these fittings at time of ordering. Contact your local Micro Motion representative. 34 Micro Motion ELITE Flow and Density Meters • ! Fitting options continued Dim. A Dim. B Fitting face -to -face outside diameter code' inches (mm) inches (mm) Model CMF050 316L stainless steel sensors Wafer style; 1/2 -inch ANSI (150 Ib; 300 Ib; 600 Ib bolt kit) 009 3 1/2 (89) 1 13/16 (46) Wafer style; 15mm DIN 2526; type C face (PN40 bolt kit) 016 3 1/2 (89) 1 13/16 (46) Wafer style; 15mm DIN 2512; type N grooved face (PN40 bolt kit) 017 3 1/2 (89) 1 13/16 (46) Wafer style; 15mm DIN 2526; type E face (PN100 bolt kit) 018 3 1/2 (89) 1 13/16 (46) Wafer style; 15mm DIN 2512; type N grooved face (PN100 bolt kit) 019 3 1/2 (89) 1 13/16 (46) Wafer style; 15mm; standard JIS facing (10K; 20K bolt kit) 029 3 1/2 (89) 1 13/16 (46) 1/2 -inch ANSI CL150 weld neck raised face flange 313 7 15/16 (202) 3 1/2 (89) 1/2 -inch ANSI CL300 weld neck raised face flange 314 8 5/16 (211) 3 3/4 (95) 1/2 -inch ANSI CL600 weld neck raised face flange 315 8 13/16 (224) 3 3/4 (95) 3/4 -inch NPT female Swagelok size 12 VCO fitting 320 6 1/2 (165) — Swagelok compatible size 12 VCO union fitting 336 6 1/2 (165) — 3/4-inch sanitary fitting (Tri -Clamp compatible) 322 6 1/2 (165) 1 (25) DN15 PN40 weld neck flange; DIN 2635 type C face 300 7 1/2 (191) 3 3/4 (95) DN15 PN40 weld neck flange; EN 1092 -1 Form B1 176 7 1/2 (191) 3 3/4 (95) DN15 PN40 weld neck flange; DIN 2635 type N grooved face 301 7 1/2 (191) 3 3/4 (95) DN15 PN40 weld neck flange; EN 1092 -1 Form D 310 7 1/2 (191) 3 3/4 (95) DN15 PN100 weld neck flange; DIN 2637 type E face 302 8 1/16 (205) 4 1/8 (105) DN15 PN100 weld neck flange; EN 1092 -1 Form B2 177 8 1/16 (205) 4 1/8 (105) DN15 PN100 weld neck flange; DIN 2637 type N grooved face 303 8 1/16 (205) 4 1/8 (105) DN15 PN100 weld neck flange; EN 1092 -1 Form D 178 8 1/16 (205) 4 1/8 (105) DN25 PN40 Weld Neck Flange; EN 1092 -1 Form B1 172 7 11/16 (195) 4 1/2 (115) DN25 PN40 Weld Neck Flange; EN 1092 -1 Form D 183 7 11/16 (195) 4 1/2 (115) JIS 15mm 10K weld neck raised face flange 304 7 1/4 (184) 3 3/4 (95) JIS 15mm 20K weld neck raised face flange 305 7 1/4 (184) 3 3/4 (95) 304L stainless steel sensors 1/2 -inch ANSI CL150 weld neck raised face flange 413 7 15/16 (202) 3 1/2 (89) 1/2 -inch ANSI CL300 weld neck raised face flange 414 8 5/16 (211) 3 3/4 (95) DN15 PN40 weld neck flange; DIN 2526 type C face 423 7 1/2 (191) 3 3/4 (95) DN15 PN40 weld neck flange; EN 1092 -1 Form B1 421 7 1/2 (191) 3 3/4 (95) Nickel alloy sensors 1/2 -inch ANSI CL150 lap joint flange 520 7 15/16 (202) 3 1/2 (89) 1/2 -inch ANSI CL300 lap joint flange 521 8 5/16 (211) 3 3/4 (95) DN15 PN40 lap joint flange; DIN 2656 type C face 523 8 1/2 (216) 3 3/4 (95) DN15 PN40 lap joint flange; EN 1092 -1 Form B1 524 8 1/2 (216) 3 3/4 (95) JIS 15mm 10K lap joint flange 522 8 1/4 (210) 3 3/4 (95) Micro Motion ELITE Flow and Density Meters 35 • 0 Fitting options continued Dim. A Dim. B Fitting face -to -face outside diameter code' inches (mm) inches (mm) Model CMF100 316L stainless steel sensors Wafer style; 1 -inch ANSI (150 Ib bolt kit) 010 4 (102) 2 1/2 (64) Wafer style; 1 -inch ANSI (300 Ib; 600 Ib bolt kit) 011 4 (102) 2 1/2 (64) Wafer style; 25mm type C face (PN40 bolt kit) 020 4 (102) 2 1/2 (64) Wafer style; 25mm DIN 2512 type N grooved face (PN40 bolt kit) 021 4 (102) 2 1/2 (64) Wafer style; 25mm type E face (PN100 bolt kit) 022 4 (102) 2 1/2 (64) Wafer style; 25mm DIN 2512; type N grooved face (PN100 bolt kit) 023 4 (102) 2 1/2 (64) Wafer style; 25mm; standard JIS face (10K; 20K; 30K bolt kit) 030 4 (102) 2 1/2 (64) 1 -inch ANSI CL150 weld neck raised face flange 328 9 1/4 (235) 4 1/4 (108) 1 -inch ANSI CL300 weld neck raised face flange 329 9 3/4 (248) 4 7/8 (124) 1 -inch ANSI CL600 weld neck raised face flange 330 10 1/4 (260) 4 7/8 (124) 1 1/2 -inch ANSI CL600 weld neck raised face flange 331 10 7/8 (276) 6 1/8 (156) 1 -inch sanitary fitting (Tri -Clamp compatible) 339 8 3/8 (213) 2 (50) DN25 PN40 weld neck flange; DIN 2635 type C face 306 8 5/16 (211) 4 1/2 (115) DN25 PN40 weld neck flange; EN 1092 -1 Form B1 179 8 5/16 (211) 4 1/2 (115) DN25 PN40 weld neck flange; DIN 2635 type N grooved face 307 8 5/16 (211) 4 1/2 (115) DN25 PN40 weld neck flange; EN 1092 -1 Form D 311 8 5/16 (211) 4 1/2 (115) DN25 PN100 weld neck flange; DIN 2637 type E face 308 9 11/16 (246) 5 1/2 (140) DN25 PN100 weld neck flange; EN 1092 -1 Form B2 180 9 11/16 (246) 5 1/2 (140) DN25 PN100 weld neck flange; DIN 2637 type N grooved face 309 9 11/16 (246) 5 1/2 (140) DN25 PN100 weld neck flange; EN 1092 -1 Form D 181 9 11/16 (246) 5 1/2 (140) JIS 25mm 10K weld neck raised face flange 317 8 5/16 (211) 4 15/16 (125) JIS 25mm 20K weld neck raised face flange 318 8 5/16 (211) 4 15/16 (125) 304L stainless steel sensors 1 -inch ANSI CL150 weld neck raised face flange 415 9 1/4 (235) 4 1/4 (108) 1 -inch ANSI CL300 weld neck raised face flange 416 9 3/4 (248) 4 7/8 (124) DN25 PN40 weld neck flange; DIN 2526 type C face 424 8 9/16 (217) 4 1/2 (115) DN25 PN40 weld neck flange; EN 1092 -1 Form B1 422 8 9/16 (217) 4 1/2 (115) Nickel alloy sensors 1 -inch ANSI CL150 lap joint flange 530 9 1/4 (235) 4 1/4 (108) 1 -inch ANSI CL300 lap joint flange 531 9 3/4 (248) 4 7/8 (124) DN25 PN40 lap joint flange; DIN 2656 type C face 533 9 9/16 (243) 4 1/2 (115) DN25 PN40 lap joint flange; EN 1092 -1 Form B1 534 9 9/16 (243) 4 1/2 (115) JIS 25mm 10K lap joint flange 532 9 5/16 (237) 4 15/16 (125) (1) Fittings listed here are standard options. Other types of fittings are available. The face to face dimensions for any custom fittings ordered using a 998 or 999 fitting code are not represented in this table. It is necessary to confirm face to face dimensions of these fittings at time of ordering. Contact your local Micro Motion representative. 36 Micro Motion ELITE Flow and Density Meters • • Fitting options continued Dim. A Dim. B Fitting face -to -face outside diameter code inches (mm) inches (mm) Model CMF200 316L stainless steel sensors 1 1/2 -inch ANSI CL150 weld neck raised face flange 341 22 7/8 (581) 5 (127) 1 1/2 -inch ANSI CL300 weld neck raised face flange 342 23 3/8 (594) 6 1/8 (156) 1 1/2 -inch ANSI CL600 weld neck raised face flange 343 23 7/8 (606) 6 1/8 (156) 2 -inch ANSI CL150 weld neck raised face flange 418 22 7/8 (581) 6 (152) 2 -inch ANSI CL300 weld neck raised face flange 419 23 3/8 (594) 6 1/2 (165) 2 -inch ANSI CL600 weld neck raised face flange 420 23 5/8 (600) 6 1/2 (165) 1 1/2 -inch sanitary fitting (Tri -Clamp compatible? 351 21 3/8 (543) 2 (51) 2 -inch sanitary fitting (Tri -Clamp compatible? 352 21 3/8 (543) 2 1/2 (64) DN40 PN40 weld neck flange; DIN 2635 type C face 381 21 11/16 (551) 5 15/16 (150) DN40 PN40 weld neck flange; EN 1092 -1 Form B1 368 21 9/16 (547) 5 15/16 (150) DN40 PN40 weld neck flange; DIN 2635 type N grooved face 383 21 11/16 (551) 5 15/16 (150) DN40 PN40 weld neck flange; EN 1092 -1 Form D 312 21 9/16 (547) 5 15/16 (150) DN40 PN100 weld neck flange; DIN 2637 type E face 377 23 1/8 (587) 6 11/16 (170) DN40 PN100 weld neck flange; EN 1092 -1 Form B2 363 22 7/8 (580) 6 11/16 (170) DN40 PN100 weld neck flange; DIN 2637 type N grooved face 379 23 1/8 (587) 6 11/16 (170) DN40 PN100 weld neck flange; EN 1092 -1 Form D 366 22 7/8 (580) 6 11/16 (170) DN50 PN40 weld neck flange; DIN 2635 type C face 382 21 15/16 (557) 6 1/2 (165) DN50 PN40 weld neck flange; EN 1092 -1 Form B1 369 21 3/4 (553) 6 1/2 (165) DN50 PN40 weld neck flange; DIN 2635 type N grooved face 384 21 15/16 (557) 6 1/2 (165) DN50 PN40 weld neck flange; EN 1092 -1 Form D 316 21 3/4 (553) 6 1/2 (165) DN50 PN100 weld neck flange; DIN 2637 type E face 378 23 9/16 (598) 7 11/16 (195) DN50 PN100 weld neck flange; EN 1092 -1 Form B2 365 23 5/16 (593) 7 11/16 (195) DN50 PN100 weld neck flange; DIN 2637 type N grooved face 380 23 9/16 (598) 7 11/16 (195) DN50 PN100 weld neck flange; EN 1092 -1 Form D 367 23 5/16 (593) 7 11/16 (195) JIS 40mm 10K weld neck raised face flange 385 21 9/16 (548) 5 1/2 (140) JIS 40mm 20K weld neck raised face flange 387 21 9/16 (548) 5 1/2 (140) JIS 50mm 10K weld neck raised face flange 386 21 13/16 (554) 6 1/8 (156) JIS 50mm 20K weld neck raised face flange 388 21 13/16 (554) 6 1/8 (156) (1) Fittings listed here are standard options. Other types of fittings are available. The face to face dimensions for any custom fittings ordered using a 998 or 999 fitting code are not represented in this table. It is necessary to confirm face to face dimensions of these fittings at time of ordering. Contact your local Micro Motion representative. (2) Not available with high - temperature models CMF200A or CMF2008. Micro Motion ELITE Flow and Density Meters 37 • • Fitting options continued Dim. A Dim. B Fitting face -to -face outside diameter code' inches (mm) inches (mm) Model CMF200 304L stainless steel sensors 1 1/2 -inch ANSI CL150 weld neck raised face flange 441 22 7/8 (581) 5 (127) 1 1/2 -inch ANSI CL300 weld neck raised face flange 442 23 3/8 (594) 6 1/8 (156) 2 -inch ANSI CL150 weld neck raised face flange 518 22 7/8 (581) 6 (152) 2 -inch ANSI CL300 weld neck raised face flange 519 23 1/2 (597) 6 1/2 (165) DN40 PN40 weld neck flange; DIN 2526 type C face 481 21 11/16 (551) 5 15/16 (150) DN40 PN40 weld neck flange; EN 1092 -1 Form B1 457 21 9/16 (547) 5 15/16 (150) DN50 PN40 weld neck raised face flange; DIN 2526 type C face 482 21 15/16 (557) 6 1/2 (165) DN50 PN40 weld neck raised face flange; EN 1092 -1 Form B1 458 21 3/4 (553) 6 1/2 (165) Nickel alloy sensors 1 1/2 -inch ANSI CL150 lap joint flange 540 22 7/8 (581) 5 (127) 1 1/2 -inch ANSI CL300 lap joint flange 541 23 3/8 (594) 6 1/8 (156) 2 -inch ANSI CL150 lap joint flange 544 22 7/8 (581) 6 (152) 2 -inch ANSI CL300 lap joint flange 545 23 3/8 (594) 6 1/2 (165) DN40 PN40 lap joint flange; DIN 2656 type C face 543 21 11/16 (551) 5 15/16 (150) DN40 PN40 lap joint flange; EN 1092 -1 Form B1 548 21 11/16 (551) 5 15/16 (150) DN50 PN40 lap joint flange; DIN 2656 type C face 547 21 15/16 (557) 6 1/2 (165) DN50 PN40 lap joint flange; EN 1092 -1 Form B1 549 21 15/16 (557) 6 1/2 (165) JIS 40mm 10K lap joint flange 542 21 9/16 (548) 5 1/2 (140) JIS 50mm 10K lap joint flange 546 21 13/16 (554) 6 1/8 (155) (1) Fittings listed here are standard options. Other types of fittings are available. The face to face dimensions for any custom fittings ordered using a 998 or 999 fitting code are not represented in this table. It is necessary to confirm face to face dimensions of these fittings at time of ordering. Contact your local Micro Motion representative. I I 38 Micro Motion ELITE Flow and Density Meters 0 • Fitting options continued Dim. A Dim. B Fitting face -to -face outside diameter code' inches (mm) inches (mm) Model CMF300 316L stainless steel sensors 3 -inch ANSI CL150 weld neck raised face flange 355 33 11/16 (856) 7 1/2 (191) 3 -inch ANSI CL300 weld neck raised face flange 356 34 7/16 (875) 8 1/4 (210) 3 -inch ANSI CL600 weld neck raised face flange 357 35 3/16 (894) 8 1/4 (210) 4 -inch ANSI CL150 weld neck raised face flange 425 34 1/16 (865) 9 (229) 4 -inch ANSI CL300 weld neck raised face flange 426 35 (889) 10 (254) 4 -inch ANSI CL600 weld neck raised face flange 427 36 11/16 (932) 10 3/4 (273) 3 -inch sanitary fitting (Tri -Clamp compatible)? 361 32 (813) 3 9/16 (90) DN80 PN40 weld neck flange; DIN 2635 type C face 391 32 7/8 (835) 7 7/8 (200) DN80 PN40 weld neck flange; EN 1092 -1 Form B1 371 32 3/4 (832) 7 7/8 (200) DN80 PN40 weld neck flange; DIN 2635 type N grooved face 393 32 7/8 (835) 7 7/8 (200) DN80 PN40 weld neck flange; EN 1092 -1 Form D 326 32 3/4 (832) 7 7/8 (200) DN80 PN100 weld neck flange; DIN 2637 type E face 395 34 9/16 (878) 9 1/16 (230) DN80 PN100 weld neck flange; EN 1092 -1 Form B2 373 34 5/16 (872) 9 1/16 (230) DN80 PN100 weld neck flange; DIN 2637 type N grooved face 397 34 9/16 (878) 9 1/16 (230) DN80 PN100 weld neck flange; EN 1092 -1 Form D 375 34 5/16 (872) 9 1/16 (230) DN100 PN40 weld neck flange; DIN 2635 type C face 392 33 1/4 (845) 9 1/4 (235) DN100 PN40 weld neck flange; EN 1092 -1 Form B1 372 33 1/4 (845) 9 1/4 (235) DN100 PN40 weld neck flange; DIN 2635 type N grooved face 394 33 1/4 (845) 9 1/4 (235) DN100 PN40 weld neck flange; EN 1092 -1 Form D 333 33 1/4 (845) 9 1/4 (235) DN100 PN100 weld neck flange; DIN 2637 type E face 396 35 9/16 (903) 10 7/16 (265) DN100 PN100 weld neck flange; EN 1092 -1 Form B2 374 35 1/4 (896) 10 7/16 (265) DN100 PN100 weld neck flange; DIN 2637 type N grooved face 398 35 9/16 (903) 10 7/16 (265) DN100 PN100 weld neck flange; EN 1092 -1 Form D 359 35 1/4 (896) 10 7/16 (265) JIS 80mm 10K weld neck raised face flange 400 33 3/8 (848) 7 5/16 (186) JIS 80mm 20K weld neck raised face flange 402 33 3/8 (848) 7 7/8 (200) JIS 100mm 10K weld neck raised face flange 401 33 9/16 (853) 8 1/4 (210) JIS 100mm 20K weld neck raised face flange 403 33 9/16 (853) 8 7/8 (225) 304L stainless steel sensors 3 -inch ANSI CL150 weld neck raised face flange 455 33 11/16 (856) 7 1/2 (191) 3 -inch ANSI CL300 weld neck raised face flange 456 34 7/16 (875) 8 1/4 (210) DN80 PN40 weld neck flange; DIN 2526 type C face 491 32 7/8 (835) 7 7/8 (200) DN80 PN40 weld neck flange; EN 1092 -1 Form B1 459 32 3/4 (832) 7 7/8 (200) Nickel alloy sensors 3 -inch ANSI CL150 lap joint flange 550 33 11/16 (856) 7 1/2 (191) 3 -inch ANSI CL300 lap joint flange 551 34 7/16 (875) 81/4 (210) DN80 PN40 lap joint flange; DIN 2656 type C face 553 32 7/8 (835) 7 7/8 (200) DN80 PN40 lap joint flange; EN 1092 -1 Form B1 554 32 7/8 (835) 7 7/8 (200) JIS 80mm 10K lap joint flange 552 33 3/8 (848) 7 5/16 (185) (1) Fittings listed here are standard options. Other types of fittings are available. The face to face dimensions for any custom fittings ordered using a 998 or 999 fitting code are not represented in this table. It is necessary to confirm face to face dimensions of these fittings at time of ordering. Contact your local Micro Motion representative. (2) Not available with high - temperature models CMF300A or CMF3008. Micro Motion ELITE Flow and Density Meters 39 • 0 Fitting options continued Dim. A Dim. B Fitting face -to -face outside diameter code inches (mm) inches (mm) Model CMF400 316L stainless steel sensors 4 -inch ANSI CL150 weld neck raised face flange 435 40 3/16 (1021) 9 (229) 4 -inch ANSI CL300 weld neck raised face flange 436 41 (1041) 10 (254) 4 -inch ANSI CL600 weld neck raised face flange 437 42 11/16 (1084) 10 3/4 (273) 4 -inch ANSI CL900 weld neck raised face flange 438 43 11/16 (1110) 11 1/2 (292) 6 -inch ANSI CL150 weld neck raised face flange 451 40 5/16 (1024) 11 (279) 6 -inch ANSI CL300 weld neck raised face flange 452 41 5/16 (1049) 12 1/2 (318) 6 -inch ANSI CL600 weld neck raised face flange 453 43 1/2 (1105) 14 (356) DN100 PN40 weld neck flange; DIN 2635 type C face 460 39 5/16 (999) 9 1/4 (235) DN100 PN40 weld neck flange; EN 1092 -1 Form B1 443 39 5/16 (999) 9 1/4 (235) DN100 PN40 weld neck flange; DIN 2635 type N grooved face 462 39 5/16 (999) 9 1/4 (235) DN100 PN40 weld neck flange; EN 1092 -1 Form D 480 39 5/16 (999) 9 1/4 (235) DN100 PN100 weld neck flange; DIN 2637 type E face 464 41 5/16 (1049) 10 7/16 (265) DN100 PN100 weld neck flange; EN 1092 -1 Form B2 445 41 5/16 (1049) 10 7/16 (265) DN100 PN100 weld neck flange; DIN 2637 type N grooved face 466 41 5/16 (1049) 10 7/16 (265) DN100 PN100 weld neck flange; EN 1092 -1 Form D 447 41 5/16 (1049) 10 7/16 (265) DN150 PN40 weld neck flange; DIN 2635 type C face 461 39 5/8 (1006) 11 13/16 (300) DN150 PN40 weld neck flange; EN 1092 -1 Form B1 444 40 1/16 (1018) 11 13/16 (300) DN150 PN40 weld neck flange; DIN 2635 type N grooved face 463 39 5/8 (1006) 11 13/16 (300) DN150 PN40 weld neck flange; EN 1092 -1 Form D 478 40 1/16 (1018) 11 13/16 (300) DN150 PN100 weld neck flange; DIN 2637 type E face 465 41 15/16 (1065) 14 (355) DN150 PN100 weld neck flange; EN 1092 -1 Form B2 446 43 1/4 (1099) 14 (355) DN150 PN100 weld neck flange; DIN 2637 type N grooved face 467 41 15/16 (1065) 14 (355) DN150 PN100 weld neck flange; EN 1092 -1 Form D 448 43 1/4 (1099) 14 (355) JIS 100mm 10K weld neck raised face flange 470 39 5/16 (999) 8 1/4 (210) JIS 100mm 20K weld neck raised face flange 472 39 13/16 (1011) 8 7/8 (225) JIS 150mm 10K weld neck raised face flange 471 39 5/8 (1006) 11 (280) JIS 150mm 20K weld neck raised face flange 473 40 1/8 (1018) 12 (305) (1) Fittings listed here are standard options. Other types of fittings are available. The face to face dimensions for any custom fittings ordered using a 998 or 999 fitting code are not represented in this table. It is necessary to confirm face to face dimensions of these fittings at time of ordering. Contact your local Micro Motion representative. (2) Available only with high- temperature models CMF400A. 40 Micro Motion ELITE Flow and Density Meters • Fitting options continued Dim. A Dim. B Fitting face -to -face outside diameter code inches (mm) inches (mm) Model CMF400 Nickel alloy sensors 4 -inch ANSI CL150 lap joint 907 42 5/8 (1083) 9 (229) DN100 PN40 weld neck flange; EN 1092 -1 Form B1 906 39 1/4 (997) 9 1/4 (235) DN100 PN100 weld neck flange; EN 1092 -1 Form B2 908 41 1/4 (1048) 10 7/16 (265) DN100 PN160 weld neck flange; EN 1092 -1 Form B2 910 42 (1067) 10 7/16 (265) 4 -inch ANSI CL150 weld neck raised face flange 911 40 1/8 (1019) 9 (229) 4 -inch ANSI CL300 weld neck raised face flange 912 40 15/16 (1040) 10 (254) 4 -inch ANSI CL600 weld neck raised face flange 913 42 5/8 (1083) 10 3/4 (273) 4 -inch ANSI CL900 weld neck raised face flange 914 43 5/8 (1108) 11 1/2 (292) High - pressure model CMF400P 316L stainless steel sensors JIS 100mm 20K weld neck raised face flange 472 39 13/16 (1011) 8 7/8 (225) JIS 150mm 20K weld neck raised face flange 473 40 1/8 (1018) 12 (305) 4 -inch ANSI CL600 weld neck raised face flange 437 42 11/16 (1084) 10 3/4 (273) 4 -inch ANSI CL900 weld neck raised face flange 438 43 11/16 (1110) 11 1/2 (292) 4 -inch ANSI CL1500 weld neck raised face flange 439 44 7/16 (1129) 12 1/4 (311) 6 -inch ANSI CL600 weld neck raised face flange 453 43 1/2 (1105) 14 (356) 4 -inch ANSI CL600 carbon stee1/316L stainless steel lap joint flange 562 43 11/16 (1110) 10 3/4 (273) 4 -inch ANSI CL900 carbon steel /316L stainless steel lap joint flange 563 43 11/16 (1110) 11 1/2 (292) (1) Fittings listed here are standard options. Other types of fittings are available. The face to face dimensions for any custom fittings ordered using a 998 or 999 fitting code are not represented in this table. It is necessary to confirm face to face dimensions of these fittings at time of ordering. Contact your local Micro Motion representative. Micro Motion ELITE Flow and Density Meters 41 • • Ordering information Model Product description Standard models CMFS010M Micro Motion Coriolis ELITE sensor; 1/10 to 1/6 -inch (2 to 4 mm); 316L stainless steel CMFS010H Micro Motion Coriolis ELITE sensor; 1/10 to 1/6 -inch (2 to 4 mm); alloy C -22 CMFS015M Micro Motion Coriolis ELITE sensor; 1/6 to 1/4 -inch (4 to 6 mm); 316L stainless steel CMFS015H Micro Motion Coriolis ELITE sensor; 1/6 to 1/4 -inch (4 to 6 mm); alloy C -22 CMF010M Micro Motion Coriolis ELITE sensor; 1/10 to 1/6 -inch (2 to 4 mm); 316L stainless steel CMF010H Micro Motion Coriolis ELITE sensor; 1/10 to 1/6 -inch (2 to 4 mm); alloy C -22 CMF010L Micro Motion Coriolis ELITE sensor; 1/10 to 1/6 -inch (2 to 4 mm); 304L stainless steel CMF025M Micro Motion Coriolis ELITE sensor; 1/4 to 1/2 -inch (6 to 13 mm); 316L stainless steel CMF025H Micro Motion Coriolis ELITE sensor; 1/4 to 1/2 -inch (6 to 13 mm); alloy C -22 CMF025L Micro Motion Coriolis ELITE sensor; 1/4 to 1/2 -inch (6 to 13 mm); 304L stainless steel CMF050M Micro Motion Coriolis ELITE sensor; 1/2 to 1 -inch (13 to 25 mm); 316L stainless steel CMF050H Micro Motion Coriolis ELITE sensor; 1/2 to 1 -inch (13 to 25 mm); alloy C -22 CMF050L Micro Motion Coriolis ELITE sensor; 1/2 to 1 -inch (13 to 25 mm); 304L stainless steel CMF100M Micro Motion Coriolis ELITE sensor; 1 to 2 -inch (25 to 50 mm); 316L stainless steel CMF100H Micro Motion Coriolis ELITE sensor; 1 to 2 -inch (25 to 50 mm); alloy C -22 CMF100L Micro Motion Coriolis ELITE sensor; 1 to 2 -inch (25 to 50 mm); 304L stainless steel CMF200M Micro Motion Coriolis ELITE sensor; 2 to 3 -inch (50 to 75 mm); 316L stainless steel CMF200H Micro Motion Coriolis ELITE sensor; 2 to 3 -inch (50 to 75 mm); alloy C -22 CMF200L Micro Motion Coriolis ELITE sensor; 2 to 3 -inch (50 to 75 mm); 304L stainless steel CMF300M Micro Motion Coriolis ELITE sensor; 3 to 4 -inch (75 to 100 mm); 316L stainless steel CMF300H Micro Motion Coriolis ELITE sensor; 3 to 4 -inch (75 to 100 mm); alloy C -22 CMF300L Micro Motion Coriolis ELITE sensor; 3 to 4 -inch (75 to 100 mm); 304L stainless steel CMF400M Micro Motion Coriolis ELITE sensor; 4 to 6 -inch (100 to 150 mm); 316L stainless steel CMF400H Micro Motion Coriolis ELITE sensor; 4 to 6 -inch (100 to 150 mm); alloy C -22 High - pressure models CMFS010P Micro Motion Coriolis ELITE sensor; 1/10 to 1/6 -inch (2 to 4 mm); high pressure; nickel alloy with stainless steel fittings CMFS015P Micro Motion Coriolis ELITE sensor; 1/6 to 1/4 -inch (4 to 6 mm); high pressure; nickel alloy with stainless steel fittings CMF010P Micro Motion Coriolis ELITE sensor; 1/10 to 1/6 -inch (2 to 4 mm); high pressure; nickel alloy with stainless steel fittings CMF400P Micro Motion Coriolis ELITE sensor; 4 to 6 -inch (100 to 150 mm); high pressure; nickel alloy with stainless steel fittings High- temperature models CMF200A Micro Motion Coriolis ELITE sensor; 2 to 3 -inch (50 to 75 mm); high temperature; 316L stainless steel CMF200B Micro Motion Coriolis ELITE sensor; 2 to 3 -inch (50 to 75 mm); high temperature; alloy C -22 CMF300A Micro Motion Coriolis ELITE sensor; 3 to 4 -inch (75 to 100 mm); high temperature; 316L stainless steel CMF300B Micro Motion Coriolis ELITE sensor; 3 to 4 -inch (75 to 100 mm); high temperature; alloy C -22 CMF400A Micro Motion Coriolis ELITE sensor; 4 to 6 -inch (100 to 150 mm); high temperature; 316L stainless steel CMF400B Micro Motion Coriolis ELITE sensor; 4 to 6 -inch (100 to 150 mm); high temperature; alloy C -22 Code Process Connections ### See process fitting options on pages 31-41. Continued on next page 42 Micro Motion ELITE ® Flow and Density Meters • • Ordering information continued Code Case options For all models except CMFS010 and CMFS015 N Standard pressure containment P Purge fittings (see pages 22 -25) D Rupture disks (two 400 -psig [28 bar] disks) — Model CMF010P only For models CMFS010 and CMFS015 N Standard case (300- series stainless steel) J Standard case (300- series stainless steel) with mounting bracket M 316L stainless steel case C! 316L stainless steel case with mounting bracket Ho Hygienic; 32 Ra finish (0.81.1m); 316L stainless steel case To) Hygienic; 32 Ra finish (0.8 µm); 316L stainless steel case with mounting bracket P Purge fitting (see page 20); standard case U Purge fitting (see page 20); standard case with mounting bracket Code Electronics interface For all models except Model CMFS010, Model CMFS015, and high - temperature models 0 Model 2400S transmitter 1 Extended mount Model 2400S transmitter 2 4 -wire polyurethane - painted aluminum integral enhanced core processor for remote mount transmitters 3 4 -wire stainless steel integral enhanced core processor for remote mount transmitters 4 4 -wire polyurethane - painted aluminum integral extended mount enhanced core processor for remote mount transmitters 5 4 -wire extended mount stainless steel integral enhanced core processor for remote mount transmitters Q 4 -wire polyurethane - painted aluminum integral core processor for remote mount transmitters A 4 -wire stainless steel integral core processor for remote mount transmitters J (2) 2 -wire integrally mounted Model 2200S transmitter UP 2 -wire extended Model 2200S transmitter R 9 -wire polyurethane - painted aluminum junction box S 9 -wire 316L stainless steel junction box H 9 -wire extended mount polyurethane - painted aluminum junction box T 9 -wire extended mount stainless steel junction box For high- temperature models 0 Model 2400S transmitter 2 4 -wire polyurethane- painted aluminum integral enhanced core processor for remote mount transmitters 3 4 -wire stainless steel integral enhanced core processor for remote mount transmitters Q 4 -wire polyurethane - painted aluminum integral core processor for remote mount transmitters A 4 -wire stainless steel integral core processor for remote mount transmitters C Model 1700/2700 transmitter R 9 -wire polyurethane - painted aluminum junction box S 9 -wire 316L stainless steel junction box Continued on next page (1) Available only with process connection 321, 344, 345, or 346. (2) Available only with calibration option Z. Micro Motion ELITE Flow and Density Meters 43 • • Ordering information continued Code Electronics interface For Models CMFS010 and CMFS015 0 Model 2400S transmitter 1 Extended mount Model 2400S transmitter 2 4 -wire polyurethane - painted aluminum integral enhanced core processor for remote mount transmitters 3 4 -wire stainless steel integral enhanced core processor for remote mount transmitters 4 4 -wire polyurethane- painted aluminum integral extended mount enhanced core processor for remote mount transmitters 5 4 -wire extended mount stainless steel integral enhanced core processor for remote mount transmitters MI'> Integral FMT Filling Transmitter No Integral FMT Filling Transmitter with improved surface finish (64 Ra) j (2) 2 -wire integrally mounted Model 2200S transmitter U (2) 2 -wire extended Model 2200S transmitter Code Conduit connections For electronics interface codes 0, 1, K, J, U, and C A Not applicable For electronics interface codes 2, 3, 4, 5, H, T, Q, and A B 1/2 -inch NPT — no gland E M20 — no gland F Brass /nickel cable gland (cable diameter 0.335 to 0.394 inches [8.5 to 10 mm]) G Stainless steel cable gland (cable diameter 0.335 to 0.394 inches [8.5 to 10 mm]) For electronics interface codes R and S (9 -wire Junction box) A 3/4 -inch NPT — no gland H Brass /nickel cable gland J Stainless steel cable gland Code Approvals For electronics interface codes 0, 1, M, and N M Micro Motion Standard (no approval) N Micro Motion Standard / PED compliant 2 CSA C -US (U.S.A. and Canada) Class I, Div. 2 ✓ ATEX — Equipment Category 3 (Zone 2) / PED compliant 3 IECEx Zone 2 Continued on next page (1) Must be ordered with FMT Filling Transmitter. Transmitter is permanently attached to sensor case. (2) Available only with calibration option Z. 44 Micro Motion ELITE ® Flow and Density Meters • • Ordering information continued Code Approvals For electronics interface codes 2, 3, 4, and 5 M Micro Motion Standard (no approval) N Micro Motion Standard / PED compliant A CSA C -US (U.S.A. and Canada) Z ) ATEX – Equipment Category 2 (Zone 1) / PED compliant 6 (1) ATEX – Equipment Category 2 (Zone 1, IIC modified) / PED compliant; Models CMF200, CMF300, and CMF400 only j (1) IECEx Zone 1 7 (1) IECEx Zone 1, IIC modified; Models CMF200, CMF300, and CMF400 only p(l)(2) NEPSI 8(1)(2) NEPSI, IIC modified For electronics interface codes J and U M Micro Motion Standard (no approval) N Micro Motion Standard / PED compliant ✓ ATEX — Equipment Category 3 (Zone 2) / PED compliant 3 IECEx Zone 2 A CSA C -US (U.S.A. and Canada) Z ATEX – Equipment Category 2 (Zone 1) / PED compliant IECEx Zone 1 For electronics interface codes Q, A, C, R, S, H, and T M Micro Motion Standard (no approval) N Micro Motion Standard / PED compliant U UL — Not available with electronics interface code C C CSA (Canada only) — Not available with electronics interface code C A CSA C -US (U.S.A. and Canada) Z ) ATEX – Equipment Category 2 (Zone 1) / PED compliant 6 (1) ATEX – Equipment Category 2 (Zone 1, IIC modified) / PED compliant; Models CMF200, CMF300, and CMF400 only 1 (1) IECEx Zone 1 7 (1) IECEx Zone 1, IIC modified; Models CMF200, CMF300, and CMF400 only p )l)(2) NEPSI 8(1)(2) NEPSI, IIC modified Code Language A Danish CE requirements document and English installation manual D Dutch CE requirements document and English installation manual E English installation manual F French installation manual G German installation manual H Finnish CE requirements document and English installation manual Italian installation manual J Japanese installation manual M Chinese installation manual Continued on next page (1) Models CMF200, CMF300, and CMF400 are rated for Group 118 with standard ATEX approval code Z, IECEx approval code 1, or NEPSI approval code P. The /IC modification option (approval codes 6, 7, and 8) should be used only when necessary for the specific area classification. (2) Available only with language option M (Chinese). Micro Motion ELITE Flow and Density Meters 45 • Ordering information continued Code Language (continued) N Norwegian CE requirements document and English installation manual O Polish installation manual P Portuguese installation manual S Spanish installation manual W Swedish CE requirements document and English installation manual C Czech installation manual B Hungarian CE requirements document and English installation manual K Slovak CE requirements document and English installation manual T Estonian CE requirements document and English installation manual U Greek CE requirements document and English installation manual L Latvian CE requirements document and English installation manual ✓ Lithuanian CE requirements document and English installation manual Y Slovenian CE requirements document and English installation manual Code Calibration options For all models except CMFS010, CMFS015, CMF010, and high- temperature models Z (1) 0.10% mass flow and 0.0005 g /cm (0.5 kg /m density D (2) 0.10% mass flow and 0.0002 g /cm (0.2 kg /m density 2 (2) 0.05% mass flow and 0.0005 g /cm (0.5 kg /m density 3 (2) 0.05% mass flow and 0.0002 g /cm (0.2 kg /m density For models CMFS010 and CMFS015 C 0.10% mass flow and 0.002 g /cm (2.0 kg /m density K 0.10% mass flow and 0.0005 g /cm (0.5 kg /m density 2 0.05% mass flow and 0.0005 g /cm (0.5 kg /m density For model CMF010 ZI'> 0.10% mass flow and 0.0005 g /cm (0.5 kg /m density 2 0.05% mass flow and 0.0005 g /cm (0.5 kg /m density For high- temperature models Z 0.10% mass flow and 0.0005 g /cm (0.5 kg /m density Code Measurement application software Z No measurement application software Code Factory options Z Standard product X ETO product Typical model number: CMF050M 313 N 2 B A E Z Z Z (1) For gas applications, select calibration option Z. Mass flow accuracy on gas is ±0.35 %. (2) Requires electronics interface codes 0-5. (3) For gas applications, select calibration option C. Mass flow accuracy on gas is ±0.35 %. 46 Micro Motion ELITE Flow and Density Meters • • I 1 Micro Motion ELITE Flow and Density Meters 47 . SI Micro Motion —The undisputed leader in flow and density measurement World- leading Micro Motion measurement solutions from Emerson Process Management deliver what you need most: 9 pr\ ,/ /;'� ; � Technology leadership �` �� Micro Motion introduced the first reliable Coriolis meter in 1977. Since ,, .� . ' that time, our ongoing product development has enabled us to . , ' ` ® �, provide the highest performing measurement devices available. .... '" Product breadth From compact, drainable process control to high flow rate fiscal transfer —look no further than Micro Motion for the widest range of \ measurement solutions. Unparalleled value Benefit from expert phone, field, and application service and support made possible by more than 600,000 meters installed worldwide and over 30 years of flow and density measurement experience. iJVW W.micromotion.com © 2011 Micro Motion, Inc. All rights reserved. The Emerson logo is a trademark and service mark of Emerson Electric Co. Micro Motion, ELITE, ProLink, MVD and MVD Direct Connect are marks of one of the Emerson Process Management family of companies. All other trademarks are property of their respective owners. Micro Motion supplies this publication for informational purposes only. While every effort has been made to ensure accuracy, this publication is not intended to make performance claims or process recommendations. Micro Motion does not warrant, guarantee, or assume any legal liability for the accuracy, completeness, timeliness, reliability, or usefulness of any information, product, or process described herein. We reserve the right to modify or improve the designs or specifications of our products at any time without notice. For actual product information and recommendations, please contact your local Micro Motion representative. 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Y* , i >t mi "rist tt €70. €a III 4111 �eS Smith Meter PD Rotary Vane Meter 'F IVIC Technologies 4" Steel Model F4 Specifications Issue/Rev. 0.9 (4/10) Bulletin SS01012 The Smith Meter®Mode! F4 Meter is a 4', double-case, straight- through rotary vane, positive displacement me- j ,. g ter. Applications indude: blending, batching, dispensing, inventory control, and custody transfer of oils, solvents, 11111111 L ': chemicals, paints, fats, and fertilizers. , Features • Superior Accuracy -The Smith Melee Rotary Vane = x Meter principle, combined with the meter's uniquely designed (offset) inlet and outlet nozzles, minimizes - pressure drop across the measuring chamber, which reduces flow through meter clearances (slippage), to maximize accuracy. • Low Pressure Drop - Streamlined flow path provides low pressure drop. Model F4 ■ Positive and Accurate Registration - High torque drive calibrator with adjustment in 0.05% increments Minimum Flow Rate -Typical Performance ensures accurate registration. Viscosity (mPa•s) • Long Service Life - Low friction ball bearings, fixed cam -type timing, and rugged construction give sus- Lirlearity , units 0.5 1 5 20 100 400 tained accuracy and long service life. USGPM 100' 60 25 6 1.25 0.30 10.15% Umin 375 227 95 23 4.75 1.14 Options USGPM 75 45 18 4 1.00 0.25 °° Umin 284 170 68 15 3.80 0.95 ■ High Viscosity Meter Clearances - To extend USGPM 50 30 12 3 0.60 0.15 operation at maximum flow rate from 400 mPa•s to 2,000 mPa•s. Umin 190 114 45 11 2.25 0.57 • High Temperature Clearances - To extend operat- R epeatability ing temperatures from 150 °F to 200 °F (65 °C to 93 °C). ■ All Iron Trim - For operating temperatures above t0A2% 200 °F (93 °C). Viscosity • LPG Trim - For low lubricity liquids such as LPG. Standard: 400 mPas (2,000 SSU) maximum. • NACE Construction - Special components available to meet requirements of NACE Standard MR -01 -75. Op 2 Pass Clearances! 0 SSU) maximum - specify "High Viscosity Meter Clearaances ° Over 2 Pass - specify "High Viscosity Meter Clearances" Operating Specifications and derate maximum flow rate in direct proportion to viscosity over 2 Pa's (e.g., at 4 Pa•s, derate Maximum Maximum Flow Rate Flow Rate to 50% of Normal Continuous Rating - 300 USGPM Umin USGPM). Continuous Rating - Temperature Standard Trim 600 2,250 Standard Meter Clearances With: Intermittent Rating' - Buna N /EPR/Teflon: -20°F to 150°F ( -29°C to 65°C). Standard Trim 720 2,725 Viton: 10 °F to 150 °F ( -12°C to 65 °C). Continuous/Intermittent Rating - High Temperature Meter Clearances With: All Iron or LPG Trim 450 1,700 Buna N/EPR/Teflon: -20°F to 200 °F ( -29°C to 93 °C). Viton: 10°F to 200 °F ( -12 °C to 93 °C). 1 lnfermIttent rating apples to service on dean, refined products where continuous operation its not required (e.g., truck loadng, nil loading, and other batd►hg applications). 2 Linearity based on a maximum How rate o1800 USGPM (Z250 Umhr) unless otherwise stated. 3 Unearfty based on a maximum of 500 USGPM (1,875 Umin). 4 1,000 mPa•s = 1,000 cP = 1 Pass. The Most Trusted Name In Measurement • • All Iron Trim With: Maximum Working Pressure Buna N: -20 °F to 225 °F ( -29 °C to 108 °C). Model Flange PSI kPa* EPR: -20 °F to 300 °F ( -29 °C to 149 °C). F4-S1 150 150 1,034 Teflon: -20 °F to 400 °F ( -29 °C to 205 °C). F4-S3 150 285 1,965 Viton: 10 °F to 400 °F ( -12 °C to 205 °C). F4-S5 300 300 2,068 F4-S6 300 740 5,102 Meter Gearing F4-S7 600 1,480 10,204 Five U.S. gallons or one dekalitre and one barrel or five F4-S8 900 2,220 15,306 dekalitres per revolution of meter calibrator output shaft. Flange Class per ANSI B16.5 Raised Face Flanges Materials of Construction Pressure Drop (AP) Trim Housing Internals Seals• Flow - Litres per Minute Standard Steel Iron, Steel, Stainless Buna N Viton 4.0 0 400 890 1,200 1,600 2 2,400 - Steel, Aluminum Teflon, or EPR Data based o 0.82 sp. gr., 25 LPG Steel Add Rulon and Nylon Buna N Viton 3.0 2 mPas product. A Teflon, or EPR A - Styaight- Thro Type 20 w► All Iron Steel Delete Aluminum Bea N', Viton AP zo - 1s AP Teflon, or EPR Psi kPa - -10 10- - 5 Installation P ill 0 0 120 ' ' 2 ' 0 r' 3 60 460 600 72 It is recommended that the meter be protected with a Flow - U.S. Gallons per Minute suitable mesh strainer. Catalog Code The following guide defines the correct PD meter for a given application and the respective catalog code. This code is part of the ordering information and should be included on the purchase order. 1 2 3 4 5 6 7 8 9 10 K F 4 S 1 G B S 0 0 Position 1: Code Position 6: Meter Gearing K — Catalog Code G — Gallons (5:1 - S1) B — Barrels (1:1 - S3 through S7) Positions 2 and 3: Model/Flange Size D — Dekaliters (1 :1 - S1) (5:1 - S3 through S7) F4 — 4" (F4) 1 — Imperial Gallons Position 4: Flow Path P — Pound S — Straight Position 7: Seals ✓ — Vertical B — Buna -N Position 5: Pressure Class and End Connections T — T ef V — T it on on Standard (Raised Face Flanges) 1 — Class 150, 150 psig/1,034 kPa Position 8: Trim 3 — Class 150, 275 psig/1,896 kPa S — Standard 5 — Class 300, 300 psig/2,068 kPa A — All Iron 6 — Class 300, 720 psig/4,964 kPa L — LPG 7 — Class 600, 1,480 psig/9,928 kPa 8 — Class 900, 2,220 psig/15,306 kPa Position 9: Temperature Compensation 0 PED (Raised Face Flanges) A — None A — ATC 1 — Class 150, Not Available B — ATG 3 — Class 150, 285 psig/1965 kPa 5 — Class 300, Not Available Position 10: Special Requirements 6 — Class 300, Consult Factory 0 — Standard 7 — Class 600, 1,480 psig/10,204 kPa P — PED Ati Flanges designed to ANSI B16.5, Pressure Ratings Maximum Working Pressure at 100°F 5 Maxhnum WP at 100°F (38°C). 6 All 53 through S8 motets sib Viton bin wit have Teflon packing gland sews. 7 Standard 8 See catalog code k r more options 9 Consult factory for Model number when selecting knperial or Pound Gearing. Page 2 • SS01012 Issue/Rev. 0.9 (4/10) • • Dimensions Inches (mm) Model F4-S1 through 87 D Drain Anchor Hole - A IMO �� Meter Anchor Bolt Holes _l_ _ sIl`�1 ; 3 - 0.8" (20) Bolt Holes on a 5.5' II�,� 13.5" (343) Diameter Bolt Circle (140) A 2.9' (74) Required to Open Printer Top 11.2' 4.8" (284) (117) 9.4" iI (239) 1 Emig 6 "" (152) C Ira.11 ote: Dimensions - krches to the nearest f tenth (milmetres to the nearest whole mm), f. each independently dimensioned from 111 _. • +�i k_ respective engineering drawings. 'includes cover. E Drain 3/4" NPT in Rear Model A B C D E F Weight - lb (kg) - F4-S1 20.0' (508) 9.3' (235) 23.4' (594) 17.8" (452) 1.3" (33) 5.4' (137) 295 (134) F4-S3 20.0' (508) 9.3" (235) 24.7" (627) 17.8" (447) 1.3" (33) 5.4" (137) 300 (136) F4-S5 21.1' (536) 9.3" (235) 24.7° (627) 17.6° (447) 1.3' (33) 5.4' (137) 340 (154) F4-S6 24.9' (632) 9.4" (239) 25.6' (650) 19.8° (503) 1.6' (41) 6.0" (152) 540 (245) F4-S7 26.6" (676) 9.8" (249) 27.8' (706) 21.0" (533) 1.7" (43) 6.3" (160) 830 (376) F4-S8 28.6' (726) 20.6' (523) 37.1" (942) 28.0' (711) 62' (157) 13.5" (342) 1885 (942) Ordering Information Accessories Application Hatching, Loading, Blending, Inventory Process Control, etc. Strainer Operating Liquid - Name, Specific Gravity or API Gravity, 4" steel, R.F. flanged, 4 mesh or finer screen. Conditions Flow Rangef Temperature Rarge Viscosity Range Maximum Working Pressure. Mechanical Preset Valves Seals Buna N' Won, Tenon, or EPR. 4" straight - through type, steel, flanged, 300 psi maxi- Units of Gallons, Litres, Pounds, Kilograms, mum working pressure. Registration Dekalitres, Barrels, Tons, etc. Direction Left to right (as viewed above) is standard Hydraulic Valves of Flow and will be supplied unless right to left 4" globe -type, steel, R.F. flanged, 300 psi maximum flow is s ed. working pressure. Style Straight through. Options and Air Eliminator Accessories As required. 4" steel, R.F. flanged, 300 psi maximum working pressure. 10 Speclly :mininumihonmavmaidmum. 11 Standard seals supplied unless optional material speciffed. Issue/Rev. 0.9 (4/10) SS01012 • Page 3 • • Counters Flow Rate Indicator 200 Series — Accumulative, 9- digit, non -reset type. Direct Mount Mechanical. 600 Series — 5 large digit reset, 8 small digit non -re- Remote Electronic. set. Remote Registration Printer Electro-Mechanical Counters. Seven -digit accumulative. Electronic Totalizers. Optional six -digit zero start. Automatic Temperature Compensation Preset Counter Model ATC — Factory-set for a given product. 300C Series — four -digit (five -digit optional) mechanical Model ATG — Field- adjustable for different products. pushbutton preset with valve linkage. Microswitch pack- age for hydraulic valve, pump control, or other interlock optional. Pulse Transmitters Type E — SPDT Mercury Wetted Switch. LNC Pulse Transmitter (adapts to 600 Series Coun- ters). Low - Resolution —1 to 10 pulses High - Resolution (HR) — 50 or 100 pulsest UPT — Quad - channel, infrared, security pulse transmit- ter in an explosion -proof housing (up to 1,000 pulses/ rev.). 12 Per rew,Iution of LNC Right -Hand Wheel. Revisions included in SSO1012 issue/Rev. 0.9 (4110): F4-S8 added throrgtout. Page 2 - F4-A3 removed from Maximum Working Pressure; F4-S8 added. Page 2 - Angle Type removed from Pressure Drop graph. Page 3 - Angle type style removed from Ordering Information. Page 4 - Model F4-A1 and F4-A3 removed from Dimensions. The specifications contained Herein are subject to change without notice and any user of said specifications should verily from the manufacturer that the specifications are curren in effect. Otherwise, the manufacturer mares no reeporstliily for the use of specification which may have been changed and are no longer n effect. Contact aformation is subject to change. For the most current contact inbrmation, visit our webate at vnvwfmcsechnologies.com/measurementsolufions and click on the *Contact Us ink in the teftahand column. 500 North Sam Houston Parkway West, Suite 100, Houston, TX 77067 USA, Phone: +1 (281) 260 2190, Fax: +1 (281) 260 2191 Gas MaseusmsntProducts: Liquid Measurement Products: Erie, PA USA +1 (814) 898 5000 Erie, PA USA +1(814) 898 5000 Beijing, China +86 (10) 8500 2251 Etlerbek, Germany +49 (4101) 3040 Los Angeles, CA USA +1 (310) 3281236 Singapore +65 6861 3011 Thetford, England +44 ( 1842) 822900 Ellerbek, Genmany+49 ( 4101) 3040 Chemed, India +91 (44) 450 4400 Kongsberg, Norway +47 (32) 28 67 00 Slough, Buenos Aires, Argentina +54 (1 England 1) 4312 4736 Barcelona, i (1753) 57151 4 Spain +34 (93) 201 09 9 Integrate Moasuroment Systems: Moscow, Russia +7 (495) 5648705 Corpus Christi, TX USA +1 (361) 289 3400 Melbourne, Australia +61 (3) 9807 2818 Kongsberg, Norway +47 (32) 28 67 00 San Juan, Puerto t8co +1 (787) 772 8100 United Arab Emirates, Dubai +971 (4) 883 0303 t0stt ow webstte at www.bnctochnologios.com/measuromentsolut ions Pr6ned in U.SA 0 4/10 RAC Tedsrdogies Measurement Solutions, Inc. All rights reserved. 6801012 Issue/Rev. 0.9 (4/10) C) _ I • • ALASKA OIL AND GAS CONSERVATION COMMISSION Before Commissioners: Daniel T. Seamount, Chairman John K. Norman Cathy Foerster Chevron's request to store Trading ) RECEIVED Bay oil and McArthur River oil at ) Cook Inlet Energy's facilities ) OTH -11 -12 and Cook Inlet Energy's request ) OTH -11 -13 to commingle West McArthur River ) auks & f ss Grans. Commission oil and Redoubt Shoal oil ) , U rge; ) Responses by Union Oil Company of California to Questions Posed by the Alaska Oil and Gas Conservation Commission At the hearing on this matter on April 14, 2011, the Commission posed certain questions to Union Oil's representative and requested that Union Oil respond to the questions by April 21, 2011. This document sets forth the background and responses to the questions. Pursuant to the Commission's suggestion at the April 14 hearing, Union Oil representatives met with Commission staff on April 19, 2011, to review a draft of this response. Introduction In 1965, drilling in Cook Inlet resulted in the discovery of the oil and gas accumulation known as the Trading Bay Field and McArthur River Field. Pursuant to approvals by the Department of Natural Resources including the Oil and Gas Conservation Committee, the McArthur River Field was unitized into the Trading Bay Unit. Production from both Trading Bay Field and Trading Bay Unit is directed onshore to the Trading Bay Production Facility (TBPF) where it is treated and shipped by the Cook Inlet Pipeline south to the Drift River Marine Terminal for export by tanker to refineries on the West Coast. A photograph of one of the first AOGCC OTH -11 -12 and OTH -11 -13 Page 1 Responses by Union Oil Company of California to Questions Posed by the Alaska Oil and Gas Conservation Commission • • tanker liftings at the Christie Lee Platform at Drift River is included in AOGCC: 50 Years of Service to Alaska (2008) at 26. The Cook Inlet pipeline was designed with a flow rate of 225,000 BOPD, traveling through 42 miles of 20 -inch pipe. The Drift River terminal has crude oil storage capacity in excess of 1 million barrels. Because the terminal at Drift River has ample storage, none of the west side oil fields were required to construct and maintain significant storage tankage. But the Drift River terminal was constructed in the shadow of Mount Redoubt, an active volcano which has erupted five times since 1900. The volcano erupted in December 1989 and continued to erupt for over six months. Sudden melting of snow and ice at the summit caused by pyroclastic flows and dome collapses caused lahars, or mudflows, which flowed down the north flank of the mountain. The mudflows coursed to Cook Inlet, about 22 miles from the volcano summit, along the Drift River and inundated the storage yard at the terminal. In January 2009, the Alaska Volcano Observatory issued a warning about a possible eruption of Mount Redoubt. On March 23, March 26, and April 4, three major lahars inundated the Drift River Valley and its downstream coastal fan. All of these reached the Cook Inlet and affected the Drift River terminal. The terminal ceased operations and filled several tanks with sea water in order to mitigate the risk of the lahars floating tanks off their foundations. In September 2009, Drift River terminal recommenced operations with a different configuration. Piping at the terminal was reconfigured to allow crude oil stored at Granite Point, West McArthur River and Trading Bay to bypass the storage tanks at Drift River and be pumped directly onto a tanker docked at the Christy Lee loading platform, a process called "tight- lining." Current operations do not involve the storage of any oil at Drift River to avoid the possibility that AOGCC OTH -11 -12 and OTH -11 -13 Page 2 Responses by Union Oil Company of California to Questions Posed by the Alaska Oil and Gas Conservation Commission • • a sudden eruption and subsequent lahars could cause damage to the tanks resulting in an oil spill. There are no present plans to change this method of operating. The absence of available storage at Drift River severely limits operations at Trading Bay. In an effort to ameliorate these limitations, a ±8,000 bbl tank was erected in 2010, bringing the total effective storage to ±82,000 bbl. At present, the tankage at Trading Bay allows storage for approximately 17 to 18 days of production. As storage capacity is reached, wells at Trading Bay Field and Trading Bay Unit must be shut in. Regular maintenance is also constrained by the tight - lining operation. Trading Bay Production Facility has two main large tanks for the storage of pipeline quality crude oil, Tanks 7 and 8, each of which holds ±37,000 bbl.' As noted below, good oilfield practice and agency regulations require routine maintenance and repair of active crude oil tanks. Whenever either Tank 7 or Tank 8 are taken out of service for maintenance, the total storage at Trading Bay is reduced to ±45,000 bbl or 9 -10 days of storage. Working with Tesoro, the buyer of all Cook Inlet crude oil, it is difficult to maintain a lifting schedule with a tanker arriving every 14 -16 days (or more frequently) at the Christie Lee. Tank 8 is due for regularly scheduled maintenance this summer. Tank 7 is due for such service next year. It is in this context that Union Oil and Cook Inlet Energy have negotiated a written agreement to allow Union Oil to use two of CIE's tanks at its Kustatan Production Facility with a working capacity of ±17,000 bbls. total for the temporary storage of crude oil while the work on Tank 8 progresses this summer. Union Oil hopes to enter into a similar 1 Tanks 7 and 8 have a rated capacity of 45,000 bbls with a working capacity of 37,000 bbls. Tank 10 has a rated capacity of 10,000 bbls with a working capacity of 8,000 bbls. Each of the tanks has a "high alarm" set at the working capacity and in order to mitigate the risk of over -flow, the tanks are never filled beyond their working capacity. AOGCC OTH -11 -12 and OTH -11 -13 Page 3 Responses by Union Oil Company of California to Questions Posed by the Alaska Oil and Gas Conservation Commission • • arrangement with CIE for next summer's work on Tank 7. No agreement between Union Oil and CIE will be executed unless and until the AOGCC approves CIE's application for comingling the streams of oil from Redoubt Shoal Unit and its West McArthur River production. Responses to Commission Questions Question 1: How long will Chevron produce under this configuration? Answer: Tank 8 at Trading Bay Production Facility (TBPF) is scheduled to come out of service for inspection and repair. This work is a regulatory requirement established by the Alaska Department of Environmental Conservation. 18 AAC 75.065 (adopting by reference API 653, Tank Inspection, Repair, Alteration and Reconstruction, Third Edition, December 2001, and Addendum 1, September 2003). The tank work is scheduled to begin in June and estimated to take +4 months. We will be utilizing the tanks at Kustatan for this time period. However, the agreement as drafted between Union Oil and CIE allows Union Oil to use the Kustatan tanks through 2011. Question 2: What are the maintenance plans for the tank that is down and the other tanks in the area? What are the conditions of the other tanks? What are the steps that will be taken? Answer: In accordance with 18 AAC 75.065, internal inspection of vessels are required within a 10 -year timeframe. Tank 8 was last internally inspected in 2002. During that inspection corrosion was noted on the internal surfaces of the roof and associated structural members. The project scope for the 2011 work includes replacement of the roof and rafters as well as the top most ring of wall plate. The new roof will be designed to increase the tank pressure rating. Tank 7 is Trading Bay's other 45,000 bbl pipeline quality crude oil tank. Tanks 7 was last inspected in 2002 and, accordingly, is scheduled for similar inspection and repair in the AOGCC OTH -11 -12 and OTH -11 -13 Page 4 Responses by Union Oil Company of California to Questions Posed by the Alaska Oil and Gas Conservation Commission • • summer of 2012. Corrosion appears less significant in Tank 7, so roof replacement may not be required. Over the last three years, three 10,000 bbl bolted skim tanks have been taken out of service and replaced with two 10,000 bbl welded tanks. Two other 10,000 bbl process vessels have also been constructed within the last five years to replace older bolted tanks taken out of service 10 or more years ago. With the exception of two firewater tanks, no bolted tanks remain at Trading Bay. Each of these new vessels has been internally coated and a rigorous cathodic protection program is in place to protect tank bottoms. All vessels are regularly inspected as specified by API 650. Question 3: What would the reservoir damage be if this is not approved and list affected wells? Answer: If the two fields (Trading Bay and McArthur River) had to be shut -in every 8 —10 days for a couple of days because of the vessel loading schedule, there would probably be very little reservoir damage. However, there are eleven wells in which electric submersible pumps (ESPs) have been installed. These wells are M -25, M -28, D -1, D -47, G -28RD, K -1RD2, K- 12RD2, K- 13RD2, K- 19, K -25, and K -30RD. These eleven wells make up 26% of the producing wells and 60% of the oil production from Trading Bay Field and Trading Bay Unit. Shutting in a well with an ESP requires turning off the ESP. In Union Oil's experience, every time an ESP is shut down, there is an unfortunately good chance that it will not turn back on. Shutting in such wells every 8 — 10 days to accommodate delayed liftings at the Drift River terminal substantially increases the risk of the ESP equipment not restarting. Il i AOGCC OTH -11 -12 and OTH -11 -13 Page 5 Responses by Union Oil Company of California to Questions Posed by the Alaska Oil and Gas Conservation Commission . • If an ESP fails in a well, the well is usually shut -in 3 — 6 months until the well can be worked over and returned to production. Because of the drilling program set for the Steelhead Platform for this summer season, if an ESP fails in a Steelhead well, it probably could not be worked over until sometime in the spring or summer of 2012. The typical work -over costs between $2,000,000 to $3,000,000 and, of course, production from the affected well is entirely lost until the workover is completed. Question 4: What motivated the timing of this request now versus last year? Answer: Tank 10 was installed in 2010. This tank provides ±8,000 bbls of additional capacity at TBPF. Combined with the capacity of Tanks 7 & 8, this gave TBPF an overall storage capacity of ±82,000 bbls. With Tank 8 being taken out of service this summer, TBPF will lose ±37,000 bbls. The two tanks at Kustatan provide an additional ±17,000 bbls. The ability and permission to use the two Kustatan tanks will provide close to ±62,000 bbls of total storage capacity. Our anticipated daily production rate this summer will be ±5,000 bbls. This includes the enhanced production anticipate from our workover of five ESPs which is in progress and should be completed by the end of June. At this daily rate of ±5,000 bbls, and with the Kustatan tanks, we will have only 12 days of storage capacity. Scheduling a vessel every 9 —11 days with Tesoro will be challenging but Union Oil believes this can be accomplished for the majority of the time Tank 8 is out of service. Without the use of the Kustatan tanks, the TBPF storage capacity would only be 45,000 bbls which would require a lifting every 7 — 8 days. Tesoro cannot meet such a tight schedule. * * * * AOGCC OTH -11 -12 and OTH -11 -13 Page 6 Responses by Union Oil Company of California to Questions Posed by the Alaska Oil and Gas Conservation Commission • For these reasons, Union Oil respectfully requests that the Commission approve the comingling request submitted by Cook Inlet Energy, allowing Union Oil and CIE to execute the agreement permitting Union Oil to use the CIE Kustatan tanks on a temporary basis which will allow the required maintenance work on TBPF's Tank 8 to proceed and mitigate the risk of shutting in wells at Trading Bay Field and Trading Bay Unit. Should the Commission have any additional questions, please do not hesitate to contact us. DATED at Anchorage, Alaska this 20th day of April, 2011. Marc Bo d Justin Black Senior Counsel Land Representative Union Oil Company of California Union Oil Company of California AOGCC OTH -11 -12 and OTH -11 -13 Page 7 Responses by Union Oil Company of California to Questions Posed by the Alaska Oil and Gas Conservation Commission , W. • • Colombie, Jody J (DOA) From: Colombie, Jody J (DOA) Sent: Monday, April 18, 2011 1:59 PM To: 'Black, Justin' Subject: RE: Transcript from 4/14/11 Hearing Attachments: Chevron 11 -12 and 11- 13.pdf See attached. From: Black, Justin [ mailto:JustinBlack @chevron.com] Sent: Thursday, April 14, 2011 2:00 PM To: Colombie, Jody) (DOA) Subject: Transcript from 4/14/11 Hearing Hi Jody, Per our telephone conversation, please email me a transcript from this morning's hearing once you receive it on Monday. Thanks, Justin R. Black Land Representative, MidContinent /Alaska Business Unit Land Department Chevron North America Exploration and Production Company (a Chevron U.S.A. Inc. division) 3800 Centerpoint Drive, Suite 100, Room 14140 Anchorage, AK 99503 Tel 907 263 7872 Mobile 907 250 5311 1ustinblack(aichevron.com CONFIDENTIALITY NOTICE: This message is confidential and may be privileged. If you believe that this email has been sent to you in error, please reply to the sender that you received the message; then please delete this email. 1 I I • • 1 ALASKA OIL AND GAS CONSERVATION COMMISSION 2 Before Commissioners: Daniel T. Seamount, Chairman John K. Norman 3 Cathy Foerster 4 Chevron's request to store Trading ) 5 Bay oil and McArthur River oil at ) Cook Inlet Energy's facilities ) OTH -11 -12 6 and Cook Inlet Energy's request ) OTH -11 -13 to commingle West McArthur River ) 7 oil and Redoubt Shoal oil 8 ALASKA OIL and GAS CONSERVATION COMMISSION 9 Anchorage, Alaska 10 April 14, 2011 9:00 o'clock a.m. 11 VOLUME I 12 PUBLIC HEARING 13 BEFORE: John K. Norman, Acting Chairman Cathy Foerster, Commissioner 14 15 16 17 18 19 20 21 22 23 24 25 R & R COURT REPORTERS 811 G STREET (907)277- 0572 /Fax 274 -8982 ANCHORAGE, ALASKA 99501 s 1 TABLE OF CONTENTS 2 Opening remarks by Acting Chairman John K. Norman 03 Testimony by Justin Black 05 3 Testimony by Pirtle Bates, Jr. 13 Testimony by Ray Chumley 16 4 Testimony by Alan Dennis 19 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 R & R C O U R T REPORTERS 811 G STREET (907)277- 0572 /Fax 274 -8982 ANCHORAGE, ALASKA 99501 • 1 P R O C E E D I N G S 2 (On record - 9:05 a.m.) 3 ACTING CHAIRMAN NORMAN: Good morning. I'll call this 4 hearing to order. This is a hearing being held before the 5 Alaska Oil and Gas Conservation Commission. The date is April 6 14th, 2011. The time is approximately 9:00 o'clock a.m. And 7 these proceedings are being conducted at the Commission's 8 offices at 333 West Seventh Avenue, Suite 100, Anchorage, 9 Alaska. 10 My name is John Norman and I am acting as temporary 11 chairman in the absence of Chairman Seamount who is traveling. 12 To my left is the Engineering Commissioner, Commissioner 13 Cathy Foerster. 14 Should anyone in this hearing have special needs that 15 require attention to allow you to participate in the hearing, 16 please see the Commission's special assistance Jody Columbie 17 who is seated in the rear of the room. 18 R & R Court Reporting will be recording these proceeding 19 and you may obtain a copy of a transcript after the 20 proceedings. And, again, if you'll see Ms. Columbie, she'll 21 facilitate that should you desire a copy of the transcript. 22 I want to remind all who are speaking to talk into the 23 microphones so that persons who are in the rear of the room 24 will be able to hear you and also so that the Court Reporter 25 may obtain a clear transcript. R & R C O U R T R E P O R T E R S 811 G STREET (907)277- 0572 /Fax 274 -8982 ANCHORAGE, ALASKA 99501 3 1 • 1 This matter comes before the Commission upon the 2 application of -- and I believe this is -- although it's 3 submitted on Chevron letterhead, this is a Union Oil 4 application. If I'm not correct on that when the applicant 5 comes forward you may -- you may correct me on that. 6 Notice of this hearing was published on March 10th, 2011 7 in the Peninsula Clarion, as well as in the State of Alaska 8 online notices and on the AOGCC website on March 10th, 2011. 9 This hearing is being conducted in accordance with 10 20 AAC 25.540 of the Alaska Administrative Code. The docket 11 numbers applicable here are Docket numbers OTH -11 -12 and 12 OTH- 11 -13. 13 The reasons that matters are being heard as a consolidated 14 matter is there is a companion request filed by Cook Inlet 15 Energy to be able to commingle some production at its Kustatan 16 facility in aid of the application of Chevron to be able to 17 allow storage of oil produced from the Trading Bay field and 18 McArthur River field to be maintain in storage tanks at the 19 Kustatan production facility. 20 Before we begin I want to ask Commissioner Foerster if she 21 has any opening comments or anything to add? 22 COMMISSIONER FOERSTER: Not with my mouth full. 23 ACTING CHAIRMAN NORMAN: Very well. Are there 24 representatives of the applicants present? Okay. Would you 25 come forward then, please, and take a seat. As you're coming R & R C O U R T R E P O R T E R S 811 G STREET (907)277- 0572 /Fax 274 -8982 ANCHORAGE, ALASKA 99501 4 • • 1 forward I'll remind all of you that even though many of you are 2 known to these Commissioners, we are also making a record here 3 and someone reading that record in the future may not know 4 this. 5 Additionally, even though we are aware of events over the 6 past several years at some of the facilities, someone reading 7 the record in the future may not know that and so it will be 8 necessary to have you go into some background as if you were 9 telling a story, so lay out why were here today and what it is 10 that you're seeking. 11 So I'll ask the representative of Unocal to first raise 12 your right hand, please. 13 (Oath Administered) 14 MR. BLACK: Yes. 15 ACTING CHAIRMAN NORMAN: If you, please, proceed to state 16 your name? 17 MR. BLACK: Justin Black. 18 JUSTIN BLACK 19 called as a witness on behalf of Chevron, testified as follows 20 on? 21 DIRECT EXAMINATION 22 ACTING CHAIRMAN NORMAN: And, Mr. Black, will you be 23 offering expert testimony or just general testimony? 24 MR. BLACK: Expert testimony. 25 ACTING CHAIRMAN NORMAN: Very well. Then in order that we R & R COURT REPORT E R S 811 G STREET (907)277- 0572 /Fax 274 -8982 ANCHORAGE, ALASKA 99501 5 1 may properly qualify you as an expert witness I'll ask you to 2 describe your background, perhaps, beginning with educational 3 credentials, experience and so forth. 4 MR. BLACK: Yes. I graduated with a Bachelor's Degree in 5 Business Administration with a concentration in marketing in 6 2006 from California State University, Bakersfield. I have 7 been employed by Chevron /Union Oil Company of California for 8 five years and I have been in Alaska for the last 10 months. I 9 am a land representative with Chevron /Union Oil Company of 10 California. Yeah. 11 ACTING CHAIRMAN NORMAN: Very well. And to put a little 12 sharper point on the pencil, the particular area of expertise 13 that you will be addressing your remarks to is what? 14 MR. BLACK: I want to address Union Oil Company of 15 California's support of this project and the storage of the oil 16 at the Kustatan production facility. And also to reaffirm what 17 you stated earlier that it is Union Oil Company of California 18 which is a subsidiary of Chevron Corporation. 19 ACTING CHAIRMAN NORMAN: Very well. Commissioner 20 Foerster. 21 COMMISSIONER FOERSTER: What is your area of expertise? 22 You're asking to be recognized as an expert witness, in what 23 area of expertise? 24 MR. BLACK: Particularly the land matters and land 25 negotiations. R & R COURT REPORTERS 811 G STREET (907)277- 0572 /Fax 274 -8982 ANCHORAGE, ALASKA 99501 6 4 1 COMMISSIONER FOERSTER: Okay, thank you. 2 ACTING CHAIRMAN NORMAN: Very well. And, Mr. Black, 3 before you proceed I ought to also note for the record that we 4 have not had any opposition to either of the applications. We 5 have had a letter of support from the State of Alaska, Division 6 of Oil and Gas supporting what the applicants seek. 7 Would you please proceed to give us a brief description of 8 what you are seeking and as I mentioned to you, remember you're 9 for a record. 10 MR. BLACK: Thank you. Thank you for this opportunity to 11 speak to the Commissioners today. I want to express support 12 for the storage of the oil from Trading Bay field and McArthur 13 River field at Cook Inlet Energy's Kustatan production 14 facility. 15 Union Oil Company of California believes that this is the 16 most efficient way to continue production from our Cook Inlet 17 assets and it is beneficial to the state as to not diminish or 18 decrease production and prevent reservoir damage. 19 Finally, just to clarify that even though in many 20 instances the letterhead does state Chevron that it is Union 21 Oil Company of California which is requesting to store the 22 production from Trading Bay field and McArthur River field at 23 Cook Inlet Energy's Kustatan production facility. And Union 24 Oil Company of California is a direct subsidiary of Chevron 25 Corporation. Thank you. R & R C O U R T R E P O R T E R S 811 G STREET (907)277 -0572 /Fax 274 -8982 ANCHORAGE, ALASKA 99501 7 4 1 ACTING CHAIRMAN NORMAN: Very well. Commissioner 2 Foerster. 3 COMMISSIONER FOERSTER: I have no questions. 4 ACTING CHAIRMAN NORMAN: The matter that brings this 5 before the Commission at this particular time is it purely for 6 business or economic reasons that this request is being made? 7 MR. BLACK: It is for business and economic reasons, but 8 as I stated it will prevent potential damage to the reservoir 9 by maintaining these wells on production by not having to shut 10 them in. 11 COMMISSIONER FOERSTER: Commissioner Norman, I do have a 12 question. 13 ACTING CHAIRMAN NORMAN: Commissioner Foerster. 14 COMMISSIONER FOERSTER: How long do you intend to produce 15 under this configuration? 16 MR. BLACK: I'm sorry, I do not know. 17 COMMISSIONER FOERSTER: Well, is there someone within 18 Union of California who would know? 19 MR. BLACK: Yes. 20 COMMISSIONER FOERSTER: And so this is an answer that you 21 can get back to us with? 22 MR. BLACK: Yes, absolutely. 23 COMMISSIONER FOERSTER: Okay. 24 ACTING CHAIRMAN NORMAN: Anything further? 25 COMMISSIONER FOERSTER: No, that's it. R & R C O U R T R E P O R T E R S 811 G STREET (907)277- 0572 /Fax 274 -8982 ANCHORAGE, ALASKA 99501 8 i • 1 ACTING CHAIRMAN NORMAN: Before we turn to Cook Inlet 2 Energy I will read briefly from the letter received from the 3 landowner, the State of Alaska, Division of Oil and Gas. I 4 think there are some helpful comments in here by way of framing 5 the record and also so that any persons that have not received 6 a copy of the letter and desire it would have the benefit of 7 it. 8 There is a letter dated March 30, 2011. It is signed by 9 Director Kevin Banks of the State of Alaska, Department of 10 Natural Resources, Division of Oil and Gas. 11 It indicates that the Division of Oil and Gas supports the 12 applications of Cook Inlet Energy, Inc. and Chevron North 13 America Exploration and Production. And you've clarified, Mr. 14 Black that, that would be a Unocal application, to store oil 15 produced from the Trading Bay and McArthur River fields at Cook 16 Inlet Energy's Kustatan production facility and to commingle 17 production from the West McArthur River field and Redoubt Shoal 18 field in storage tank at Kustatan. 19 And I'm paraphrasing here just -- but continuing. 20 Allowing Chevron to store at Kustatan benefits the state as the 21 mineral owner by mitigating the risks of lower production and 22 decreased transportation costs. It allows Chevron to continue 23 uninterrupted production of the Trading Bay field and the 24 McArthur River field while storage tank maintenance operations 25 are conducted over the summer. R & R C O U R T R E P O R T E R S 811 G STREET (907)277- 0572 /Fax 274 -8982 ANCHORAGE, ALASKA 99501 9 1 4 1 This reduces the risk of damaging the reservoir due to 2 shutting in production and avoids increased transportation 3 costs by mitigating the need to add additional vessel calls on 4 the Drift River Terminal to compensate for less available 5 storage in Chevron's existing facilities. This reduces 6 environmental risks to Cook Inlet pipeline operations since 7 each vessel creates an incremental risk. 8 And then it goes on to comment upon having confidence in 9 the metering methodology proposed. And concludes by saying 10 given minute risks to the state and the potential risk of 11 losing production if wells are shut -in and the very real cost 12 considerations of adding more vessel calls, the Division 13 strongly supports approval of Chevron's and Cook Inlet Energy's 14 request to store and commingle at Kustatan, et cetera. 15 COMMISSIONER FOERSTER: I do have another question. 16 ACTING CHAIRMAN NORMAN: Pardon me? 17 COMMISSIONER FOERSTER: I do have another question when 18 you're done, okay? 19 ACTING CHAIRMAN NORMAN: Say again, please? 20 COMMISSIONER FOERSTER: I do have another question 21 whenever you're done. 22 ACTING CHAIRMAN NORMAN: Very well. And that would be of 23 this particular witness, Mr. Black, while we still here (ph)? 24 COMMISSIONER FOERSTER: Yeah. 25 ACTING CHAIRMAN NORMAN: Yes, please, Commissioner R & R C O U R T R E P O R T E R S 811 G STREET (907)277- 0572 /Fax 274 -8982 ANCHORAGE, ALASKA 99501 10 411 411 1 Foerster. 2 COMMISSIONER FOERSTER: Do you know or would you be able 3 to get me an answer to the maintenance plan for that -- for the 4 tank that is down and the condition and maintenance plans for 5 any other tanks that Union operates in that facility? 6 MR. BLACK: I do not have that answer at this time, but I 7 can get that information for you. 8 COMMISSIONER FOERSTER: Okay, thank you. 9 ACTING CHAIRMAN NORMAN: And that I assume would include 10 the duration 11 MR. BLACK: Correct. 12 ACTING CHAIRMAN NORMAN: of this? Yes, okay. 13 COMMISSIONER FOERSTER: But I want more than just the 14 duration. I want -- I want the 15 ACTING CHAIRMAN NORMAN: Yes. 16 COMMISSIONER GIARD: ....steps that are going to be 17 taken.... 18 ACTING CHAIRMAN NORMAN: Yeah. 19 COMMISSIONER FOERSTER: and I want the qual- -- the 20 condition of the other tanks and if there are any maintenance 21 plans or surveillance plans for the other tanks in the area. 22 MR. BLACK: Okay. 23 ACTING CHAIRMAN NORMAN: Anything more, Commissioner 24 Foerster? 25 COMMISSIONER FOERSTER: That's all. R & R C O U R T R E P O R T E R S 811 G STREET (907)277- 0572 /Fax 274 -8982 ANCHORAGE, ALASKA 99501 11 1 ACTING CHAIRMAN NORMAN: Very well. Mr. Black, do you 2 have anything more to offer? 3 MR. BLACK: No, thank you. 4 ACTING CHAIRMAN NORMAN: We would ask then that you remain 5 present just in case some additional questions might arise and 6 we have 7 MR. BLACK: Sure. 8 ACTING CHAIR NORMAN: ....the benefit of you here. If 9 there are any additional questions and we have to shift back to 10 you I would also ask you to remember that you would remain 11 under Oath, do you understand that? 12 MR. BLACK: Yes, sir. 13 ACTING CHAIRMAN NORMAN: Okay, very well. So let's go to 14 Cook Inlet Energy, Mr. Bates. 15 MR. BATES: Good morning, Commissioner Norman, 16 Commissioner Foerster. I am Pirtle Bates, Jr., the land 17 manager with Cook Inlet Energy. I am here to speak as -- make 18 general comments on the application from Cook Inlet Energy to 19 the Commission. Do you want me 20 ACTING CHAIRMAN NORMAN: Let's go ahead and we will swear 21 both of you at the same time and then we'll get into the 22 testimony, so would you both raise your right hands. 23 (Oath Administered) 24 MR. BATES: I do. 25 MR. CHUMLEY: I do. R & R C O U R T R E P O R T E R S 811 G STREET (907)277- 0572 /Fax 274 -8982 ANCHORAGE, ALASKA 99501 12 1 1 ACTING CHAIRMAN NORMAN: Very well. The record should 2 reflect that both witnesses stated in the affirmative. So who 3 would like to proceed first? 4 MR. BATES: I will go ahead and lead off with 5 ACTING CHAIRMAN NORMAN: All right. 6 MR. BATES: just a general description. 7 ACTING CHAIRMAN NORMAN: And, Mr. Bates, I assume that you 8 want to offer something based upon your expertise and 9 experience, so would you please give a bit about -- of your 10 background so 11 PIRTLE BATES, JR. 12 called as a witness on behalf of Cook Inlet Energy, testified 13 as follows on: 14 DIRECT EXAMINATION 15 MR. PIRTLE: Yes. I'm a certified professional landsmen 16 and hold the position of land manager for Cook Inlet Energy. I 17 have over 20 years experience doing land work in the State of 18 Alaska, a number of years with the Department of Natural 19 Resources and then as a private consultant and more recently 20 with Cook Inlet Energy for approximately a year at this point. 21 I am generally familiar with the assets on the west side 22 and -- but am here to more specifically to speak to the general 23 purposes of the application and the -- the business reasons and 24 commercial reasons for Cook Inlet Energy's interest in putting 25 forth this matter to the Commission. R & R C O U R T R E P O R T E R S 811 G STREET (907)277-0572/Fax 274 -8982 ANCHORAGE, ALASKA 99501 13 1 1 ACTING CHAIRMAN NORMAN: Very well. Commissioner 2 Foerster, questions? 3 COMMISSIONER FOERSTER: I have no questions, thank you. 4 ACTING CHAIRMAN NORMAN: All right. Well, we will accept 5 you certainly as a general witness and then as an expert 6 witness within the area of your particular expertise. Please 7 proceed. 8 MR. BATES: Well, I'll try to keep this fairly brief and 9 to the point. Cook Inlet Energy's application is solely in 10 support of the application -- or to make possible the 11 completion of the storage (indiscernible) of the Trading Bay 12 and McArthur River production for Unocal at our Kustatan 13 production facility. 14 The request to commingle and the metering considerations, 15 to which my associate here can speak to more specifically, are 16 needed and necessary to enable the storage of the Unocal 17 production and the ultimate shipment to market of that 18 production without interfering with Redoubt or West McArthur 19 River production from our own facilities or our own fields. 20 That is the general purpose of our application. 21 We have been in discussions with Unocal and have a -- are 22 pretty close to a final agreement on those terminally (ph) 23 agreement. And pretty well the only thing that's left is the 24 approval of these two applications with AOGCC to finalize those 25 and be able to put those plans into effect. R & R C O U R T R E P O R T E R S 811 G STREET (907)277- 0572 /Fax 274 -8982 ANCHORAGE, ALASKA 99501 14 410 410 1 As DNR's letter very clearly stated this -- these two 2 applications will be of very specific benefit to Unocal in 3 enabling them to protect their reservoir to continue their 4 production at their normal levels. 5 It provides some benefit to Cook Inlet Energy directly and 6 obviously we will be receiving fees for the use of our 7 facilities at KPF, but I think the more important thing is the 8 general benefits to all producers on the west side of Cook 9 Inlet and to all royalty owners for the west side in Cook Inlet 10 in that transportation charges will be kept at the lowest 11 possible levels by these -- by this process being allowed to go 12 forward which will increase everybody's royalty revenues. 13 And we have also spoken with our lessors for the rights - 14 of -way, the easements and have met with CIRI on that and 15 explained to them this process and they are fully aware and 16 they would receive benefit also as part of -- out of this, 17 also. 18 And I believe that pretty well summarizes the purpose of 19 the application and the benefits. 20 ACTING CHAIRMAN NORMAN: Very well. Commissioner 21 Foerster, questions? 22 COMMISSIONER FOERSTER: Nope. 23 ACTING CHAIRMAN NORMAN: Well, thank you, Mr. Bates. 24 MR. BATES: Um -hum. (Affirmative) 25 ACTING CHAIRMAN NORMAN: And so will there be further R & R C O U R T R E P O R T E R S 811 G STREET (907)277- 0572 /Fax 274 -8982 ANCHORAGE, ALASKA 99501 15 . . 1 testimony from Cook Inlet Energy? 2 MR. BATES: I would just state that Mr. Chumley is here 3 for questions if -- should there be any of a technical nature. 4 ACTING CHAIRMAN NORMAN: Mr. Chumley, why don't you put 5 yourself on the record stating your name and general background 6 and then we can determine if there's any further questions? 7 RAY CHUMLEY 8 called as a witness on behalf of Cook Inlet Energy, testified 9 as follows on: 10 DIRECT EXAMINATION 11 MR. CHUMLEY: Sure. Ray Chumley. I am an Alaskan 12 resident for 35 years. Been in the oil and gas production 13 industry for 15 years. I'm currently the production 14 superintendent for field operation in Cook Inlet for Cook Inlet 15 Energy. 16 I'm very familiar with all the assets that are currently 17 being discussed as far as storage for Unocal -- oil storage for 18 Unocal. And I'm just here to offer any clarification for 19 questions anybody may have as far as the facilities and our 20 assets. 21 ACTING CHAIRMAN NORMAN: Very well. Commissioner 22 Foerster, anything for 23 COMMISSIONER FOERSTER: I'm very familiar with the -- with 24 the way that you plan to conduct this hook -up so I don't have 25 any questions for you, but I do have another question for R & R C O U R T R E P O R T E R S 811 G STREET (907)277-0572/Fax 274-8982 ANCHORAGE, ALASKA 99501 16 1 Unocal whenever were done with Cook Inlet. 2 ACTING CHAIRMAN NORMAN: All right. We may then think of 3 a few other questions so as a reminder to you, Mr. Bates and 4 Mr. Chumley, I'd like you to remain and also remind you that 5 you would remain under Oath, do you understand that? 6 MR. BATES: Yes. 7 MR. CHUMLEY: Yes. 8 ACTING CHAIRMAN NORMAN: Commissioner Foerster. 9 COMMISSIONER FOERSTER: Okay. Mr. Black, 10 MR. BLACK: Yes. 11 COMMISSIONER FOERSTER: can you tell me or can you 12 find someone who can, you talk about reservoir damage, could 13 you quantify, you know, what wells, what the damage mechanisms 14 would be just for the record? 15 MR. BLACK: I would like to get with someone that knows 16 the well names and that information for you, so I will get back 17 to you on that. 18 COMMISSIONER FOERSTER: Okay. That's all I've got. 19 ACTING CHAIRMAN NORMAN: I have a question here for Cook 20 Inlet Energy. Insofar as Cook Inlet Energy is concerned your 21 application is submitted primarily out of the need to support 22 Unocal and we don't need to know any business terms, but I 23 believe you indicated that there's also some benefit to Cook 24 Inlet Energy in doing this and then you see some peripheral 25 benefit to, perhaps, others on the west side and royalty owners R & R C O U R T R E P O R T E R S 811 G STREET (907)277- 0572 /fax 274 -8982 ANCHORAGE, ALASKA 99501 17 410 410 1 and so forth, is that 2 MR. BATES: Yes, sir, that is correct. 3 ACTING CHAIRMAN NORMAN: Okay. And said differently, if 4 -- the flip side of this if -- if Union Oil had not submitted 5 this then you wouldn't be here today? 6 MR. BATES: That is correct. 7 ACTING CHAIRMAN NORMAN: Okay. And now a question for 8 you, Mr. Black. What dictated the timing of submitting this 9 application right now as opposed to last year or next year or 10 at some other time, what is it that has brought you here today? 11 MR. BLACK: I'm sorry, I do not know the specifics of the 12 timing of the application this year versus last year or any 13 other time. I can get back to you though. 14 ACTING CHAIRMAN NORMAN: Very well. 15 COMMISSIONER FOERSTER: Mr. Black, I think -- I think you 16 should take home to Unocal the importance of bringing adequate 17 representation 18 MR. BLACK: Yes. 19 COMMISSIONER FOERSTER: to a hearing such as this 20 one. 21 MR. BLACK: Thank you. 22 ACTING CHAIRMAN NORMAN: I think -- Commissioner Foerster, 23 do you have anything more at this time? 24 COMMISSIONER FOERSTER: No, I think that there were some 25 DNR people that wanted to testify R & R C O U R T R E P O R T E R S 811 G STREET (907)277- 0572 /Fax 274 -8982 ANCHORAGE, ALASKA 99501 18 410 410 1 ACTING CHAIRMAN NORMAN: Yes, uh - huh. 2 COMMISSIONER FOERSTER: as well. Okay. 3 ACTING CHAIRMAN NORMAN: So we now have on the list -- and 4 I'll take the personnel in order, but we have one, two, three 5 personnel from DNR so I will call first on -- perhaps, if you 6 wouldn't mind if you could remain, Mr. Black, but make room at 7 that particular table 8 MR. BLACK: Yeah. 9 ACTING CHAIRMAN NORMAN: and any of the DNR. We have i 10 Alan Dennis, Greg Hobbs and Wendy Woolf here. And you could 11 come forward. Would you raise your right hand, please. 12 (Oath Administered) 13 MR. DENNIS: I do. 14 ALAN DENNIS 15 called as a witness on behalf of DNR, testified as follows on: 16 DIRECT EXAMINATION 17 ACTING CHAIR NORMAN: Please state your name. 18 MR. DENNIS: Alan Dennis. I'm the business manager for 19 the Division of Oil and Gas. I've been in Alaska now for two 20 and a half years in that position. Been working oil and gas 21 issues in Alaska since 1981. 22 ACTING CHAIRMAN NORMAN: Very well. Any questions, 23 Commissioner Foerster? 24 COMMISSIONER FOERSTER: Can we take a 30 second recess so 25 I go R & R C O U R T R E P O R T E R S 811 G STREET (907)277- 0572 /Fax 274 -8982 ANCHORAGE, ALASKA 99501 19 411 410 1 ACTING CHAIRMAN NORMAN: Yes 2 COMMISSIONER FOERSTER: fight my allergies? 3 (Off record) 4 (On record) 5 ACTING CHAIRMAN NORMAN: Back on the record. We've been 6 off record for approximately one minute. 7 COMMISSIONER FOERSTER: I'm real familiar with Mr. Dennis. 8 I don't have any general questions about his 9 ACTING CHAIRMAN NORMAN: Very well. 10 COMMISSIONER FOERSTER: qualifications. 11 ACTING CHAIRMAN NORMAN: Mr. Dennis, do you have anything? 12 MR. DENNIS: I just wanted to -- all three of the DNR 13 representatives are here to support these applications. We 14 don't have anything -- any specific testimony. Were just here 15 to be available to answer questions. Greg Hobbs can speak to 16 whatever technical issues there may be and I can speak to the 17 policy issues. 18 ACTING CHAIRMAN NORMAN: Okay, thank you. Perhaps, I'll 19 throw out a general question and then either Mr. Hobbs or Ms. 20 Woolf can respond to it if you can't, but do you know of any 21 persons that would be adversely affected by the two 22 applications that were filed should the Commission grant them? 23 Would they have -- would this have an adverse affect on any 24 persons? 25 MR. DENNIS: We know of no one who would be adversely R & R C O U R T R E P O R T E R S 811 G STREET (907)277- 0572 /Fax 274 -8982 ANCHORAGE, ALASKA 99501 20 1 impacted and I think, in fact, all produces, all landlords, all 2 overriding royalty interest owners, in fact, would be 3 benefitted by an affirmative decision on these two 4 applications. 5 ACTING CHAIRMAN NORMAN: Very well. We have here Ms. 6 Wendy Woolf and Mr. Greg Hobbs, also. Do you all -- let me 7 just ask right now without even swearing you, do you have 8 anything -- I assume you're here also in support of this. 9 Commissioner Foerster, do you have any questions of Mr. 10 Hobbs or Ms Woolf so we could bring them forward and swear 11 them or 12 COMMISSIONER FOERSTER: No, I don't. 13 ACTING CHAIRMAN NORMAN: Okay, all right. Well, I think 14 the very helpful letter from the Division of Oil and Gas, 15 that's gone into the record and we do appreciate that, plus 16 your testimony and support, Mr. Dennis, would suffice. And 17 there being no opposition and us have heard none from anyone 18 else, then I don't think that we have to trouble Mr. Hobbs or 19 Ms. Woolf to come forward. 20 Are there any other persons present at this hearing that 21 wish to offer any testimony? I see no one has signed up and 22 the Chair sees no one in the room asking to be recognized to 23 testify. 24 I think what we will do with Commissioner Foerster's 25 consent, is take a five minute recess, see if we have any final R & R C O U R T R E P O R T E R S 811 G STREET (907)277 -0572 /Fax 274 -8982 ANCHORAGE, ALASKA 99501 21 1 wrap -up questions, come back on the record and then we should 2 be able to conclude very quickly. 3 COMMISSIONER FOERSTER: That sounds good. 4 ACTING CHAIRMAN NORMAN: We'll take a five minute recess. 5 (Off record) 6 (On record) 7 ACTING CHAIRMAN NORMAN: Call the hearing back to order. 8 The Commissioners have taken a brief break recess and were 9 back on the record now at approximately 9:50 a.m. 10 The Commission has several questions and I think an 11 underlying question is how long is this expected to continue, 12 but we have several questions because some of the request here 13 does deviate from the Commission's normal practices, statewide 14 regulations and so forth. 15 So I'll call on Commissioner Foerster and I, perhaps also, 16 will have a question. 17 COMMISSIONER FOERSTER: Before we can move forward on a 18 decision there are a number of questions that we've already 19 asked of Unocal that we do require an answer to and so that 20 none of those is forgotten or not addressed I'm going to 21 reiterate them. 22 First, we need to know how long you intend to produce in 23 this configuration. 24 Second, we need to understand the maintenance plan for 25 this and any other tanks in the area. R & R COURT REPORTERS 811 G STREET (907)277- 0572 /Fax 274 -8982 ANCHORAGE, ALASKA 99501 22 . . 1 We need, also, to have an explanation for the timing of 2 this request, what motivated this request. 3 We also need to know what the details are, quantify the 4 reservoir damage, quantify and explain the reservoir damage 5 mechanisms that you're trying to avoid. 6 I don't think I've left anything out, do you? Okay. 7 ACTING CHAIRMAN NORMAN: No. 8 COMMISSIONER FOERSTER: But, again, Mr. Black, we will not 9 be able to make a decision on this matter without the answers 10 to those questions. And for future reference Unocal should 11 send people to the hearings who can answer the questions that 12 are likely to be asked. 13 For Cook Inlet we have a series of questions on the 14 Coriolus meter and on the custody transfer point. Well, 15 actually custody transfer point really. Approving a custody 16 transfer point off the lease line is a deviation of -- from our 17 regulations and we don't want to set a precedent of approving 18 that sort of thing on a permanent basis. 19 However, should you be able to provide us enough 20 justification for reservoir damage and other causes that would 21 allow us to grant on a temporary basis and then you have to be 22 able to give us the information on what that temporary time 23 frame is, then we will be able to consider whether to deviate 24 from our regulations. 25 But for Cook Inlet Energy the other issue is the Coriolus R & R C O U R T R E P O R T E R S 811 G STREET (907)277-0572/Fax 274 -8982 ANCHORAGE, ALASKA 99501 23 411 110 1 meter which is not recognized under our regulations as an 2 accepted custody transfer meter and you guys tell us that it is 3 more accurate than meters that we normally use and it's more 4 accurate than the standard that we require. However, we need 5 you to prove that to us, so we need -- and we need you to be 6 able to prove that accuracy initially. 7 We also need you to be able to prove that it maintains 8 that accuracy over time. So what we need from you is how can 9 you prove to us the accuracy of the meter and how can you 10 ensure the maintenance of that accuracy over time and prove it 11 periodically to our inspectors as you would with any other 12 custody transfer meter. 13 And what we need from you guys is answers to all of these 14 essential questions and so that we can know how long to keep 15 the record open or what -- whether we need to continue the 16 hearing. When can you get back to us with answers to all of 17 these questions? 18 MR. BATES: I'm not 100 percent certain how long it will 19 take to get back. I would think we would be able to give you 20 at least some of the information, if not all of it, next week. 21 COMMISSIONER FOERSTER: Mr. Black? 22 MR. BLACK: I would say only a matter of days and we can 23 get you this information. 24 COMMISSIONER FOERSTER: Okay. And there's one more 25 question that we have that -- and I'm not sure who is the right R & R C O U R T R E P O R T E R S 811 G STREET (907)277-0572/Fax 274 -8982 ANCHORAGE, ALASKA 99501 24 • 1 person to give it to us, perhaps, it's DNR, but, you know, DNR 2 has said that they're fine with any inaccuracies that -- well, 3 I'm paraphrasing, but DNR is fine with this and doesn't see a 4 threat to the inaccuracies that may result if you're not able 5 to prove that it's equal or better, but, Mr. Dennis, there are 6 probably other people with smaller bank accounts than the State 7 of Alaska who might not agree with you. Can you give me -- can 8 you give us a complete listing of all affected parties and 9 assurances that they all agree that this is okay? 10 MR. DENNIS: I think maybe Mr. Bates could talk about -- I 11 mean, he's got, perhaps, hundreds of overriding royalty owners 12 so in 13 COMMISSIONER FOERSTER: Okay. So it's not for -- the 14 question is not for you. It's for Mr. Bates. 15 MR. BATES: No, it probably is move over there. 16 COMMISSIONER FOERSTER: Okay. So Mr. Bates, you 17 understand my question just because DNR is okay with small 18 inaccuracies, that doesn't mean that, you know, somebody for 19 whom $100 might be a huge windfall might see things 20 differently. 21 MR. BATES: Yes. 22 COMMISSIONER FOERSTER: Can you give us assurances that 23 everyone whose royalty interests you're representing is fine 24 with this? 25 MR. BATES: There have been no notice made to -- to R & R C O U R T R E P O R T E R S 811 G STREET (907)277- 0572 /Fax 274-8982 ANCHORAGE, ALASKA 99501 25 • 1 individual overriding royalty interest holders. 2 COMMISSIONER FOERSTER: So the answer is no? 3 MR. BATES: No. 4 COMMISSIONER FOERSTER: Okay. 5 ACTING CHAIRMAN NORMAN: Commissioner Foerster, if 6 I -- 7 COMMISSIONER FOERSTER: I'm done. 8 ACTING CHAIRMAN NORMAN: if I could inject. Mr. 9 Bates, perhaps, it might suffice if -- I appreciate the 10 difficulty in giving multiple notice and trying to get 11 responses back from parties, but it would be helpful to have a 12 representation from Cook Inlet Energy that you reviewed the 13 record and that there are no parties that would be 14 disadvantaged by virtue of differential overriding royalty 15 interests, et cetera that might -- in other words, that there 16 -- there's no potential disadvantage to anyone because this all 17 will cut evenly, am I -- am I confusing you with that question? 18 MR. BATES: No, I -- I understand the 19 ACTING CHAIRMAN NORMAN: You looked puzzled 20 MR. BATES: request, but 21 COMMISSIONER FOERSTER: I don't think he was saying that. 22 MR. BATES: until I review the record I -- yeah. 23 ACTING CHAIRMAN NORMAN: I'm not asking for an answer now, 24 but 25 MR BATES: Okay. i R & R C O U R T R E P O R T E R S 811 G STREET (907)277-0572/Fax 274 -8982 ANCHORAGE, ALASKA 99501 26 III • 1 ACTING CHAIRMAN NORMAN: the other alternative is to 2 just contact individual parties and say this has been 3 requested. 4 The Commission is supposed to be a gatekeeper and assure 5 people that there is accurate measurement and that when the 6 production is measured their royalty check is cut properly and 7 so that's the reason for this question. 8 MR. BATES: Okay. 9 ACTING CHAIRMAN NORMAN: And, I think, in lieu of asking 10 people if you could look at it and provide us with that 11 representation, that would suffice subject to what Commissioner 12 Foerster thinks as opposed to -- I'm guessing there are 13 multiple overriding royalty interests out there 14 MR. BATES: Um -hum. (Affirmative) 15 ACTING CHAIRMAN NORMAN: and as long as they are on 16 roughly equal footing, than there is no possibility of 17 disadvantaging someone, but if there are differential interests 18 than that possibility does exist. 19 MR. BATES: Okay. 20 COMMISSIONER FOERSTER: Well, Commissioner Norman, I think 21 we need to at a very minimum leave the record open, but there's 22 a possibility that the answers to these questions that we get 23 may lead to other questions and unfortunately the people to 24 answer the questions aren't here so that we can determine that 25 at this point, so I'm wondering if we should continue this R & R C O U R T R E P O R T E R S 811 G STREET (907)277-0572/Fax 274 -8982 ANCHORAGE, ALASKA 99501 27 III 0 1 hearing or -- you know, what's the proper way to ensure that we 2 eventually find 3 ACTING CHAIRMAN NORMAN: Yes. 4 COMMISSIONER FOERSTER: the right people and get the 5 right answers. 6 ACTING CHAIRMAN NORMAN: I would suggest, Commissioner 7 Foerster, that we leave the record open for one week which 8 would be until close of business on -- on the 21st of April. 9 As I've understood it now I think both Cook Inlet Energy and 10 Union Oil have indicated that they can could back with answers 11 to our questions at that time and then based upon what answers 12 we get, then the Commission may be in a position to either 13 enter an order or we may have to at that point reconvene the 14 hearing. 15 COMMISSIONER FOERSTER: Okay. I'm going to be out of town 16 all next week, but I'm reachable by phone and e -mail, so 17 ACTING CHAIRMAN NORMAN: Certainly. And so -- but this 18 would be on the 21st and then it would be analyzed and 19 then 20 COMMISSIONER FOERSTER: Okay. 21 ACTING CHAIRMAN NORMAN: I would anticipate the week 22 following. 23 COMMISSIONER FOERSTER: Okay. 24 ACTING CHAIRMAN NORMAN: One other point would relate to 25 you, Mr. Black and that is the requirement that the Commission R & R C O U R T R E P O R T E R S 811 G STREET (907)277 - 0572 /Fax 274 -8982 ANCHORAGE, ALASKA 99501 28 1 has that production must be measured in accordance with this 2 section before severance from the property or unit where 3 production is, et cetera. And we have in the past received 4 applications seeking a variance for that and generally we have 5 not granted that 'cause you begin to start down a slippery 6 slope once you get measurements taking place at remote 7 locations. 8 So that -- the reason I'm saying that is that underscores, 9 again, our need to know how long will this continue. Are you 10 asking for a permanent reconfiguration of the facilities here 11 in the measuring or is it temporary? 12 If it's temporary and there is a need to protect against 13 reservoir damage then I think that the Commission would be 14 responsive to that. 15 If you're asking for a permanent reconfiguration and under 16 Section 228 to be able to measure production off the property 17 then that's a whole different question. 18 MR. BLACK: That's understood, thanks. 19 COMMISSIONER FOERSTER: And that relates to the 20 maintenance plan for all the other tankage because 21 MR. BLACK: Yeah. 22 COMMISSIONER FOERSTER: if it's temporary for this 23 tank and then it's temporary for the next tank and then it's 24 temporary for the next tank, then it's time for the first tank 25 again, it becomes permanent. R & R C O U R T R E P O R T E R S 811 G STREET (907)277- 0572 /Fax 274 -8982 ANCHORAGE, ALASKA 99501 29 1 MR. BLACK: Um -hum. (Affirmative) 2 ACTING CHAIRMAN NORMAN: Very well. We previously asked 3 if there were any other persons present that wished to testify 4 and no one identified themselves, but I will ask again. Are 5 there any other persons present in this room who believe they 6 have relevant testimony that would like to speak? 7 I'm pausing and hearing none, I would add then finally 8 that the record will remain open until -- Commissioner Forester 9 reminded me she will be out next week, so we could leave the 10 record open until the close of business on Friday the 22nd 11 which might give you a little more time if you would prefer. 12 That's an extra 24 hours. 13 And if you have questions about what the Commission is 14 seeking then you're certainly welcome to interact with the 15 Commission Staff here and call if you need clarification. 16 Bearing in mind that even though some of the production volumes 17 are not great when the Commission enters an order invariably 18 years later someone else brings that order forward and says but 19 you did it here or you did it there so that's why we have to be 20 careful before we start down the proverbial slippery slope. 21 Do you, Mr. Black, have any final comments? 22 MR. BLACK: No. 23 ACTING CHAIRMAN NORMAN: Very well. And, Mr. Dennis, do 24 you have anything that you'd like to add? 25 MR. DENNIS: No, sir. R & R C O U R T R E P O R T E R S 811 G STREET (907)277- 0572 /Fax 274 -8982 ANCHORAGE, ALASKA 99501 30 411 410 1 ACTING CHAIRMAN NORMAN: And, Mr. Bates? 2 MR. BATES: No. 3 ACTING CHAIRMAN NORMAN: All right. Well, we thank you 4 all very much for your attendance. And to Ms. Woolf and Mr. 5 Hobbs I would remind you of John Milton's comment, they also 6 serve who only stand and wait or sit and wait or however that 7 went. 8 (Recessed - 10:00 a.m.) 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 R & R C O U R T R E P O R T E R S 811 G STREET (907)277- 0572 /Fax 274 -8982 ANCHORAGE, ALASKA 99501 31 M 1 C E R T I F I C A T E 2 UNITED STATES OF AMERICA ) )ss. 3 STATE OF ALASKA 4 I, Rebecca Nelms, Notary Public in and for the State of Alaska, residing at Anchorage, Alaska, and Reporter for R & R 5 Court Reporters, Inc., do hereby certify: 6 THAT the annexed and foregoing Public Hearing In the Chevron's request to store Trading Bay oil and McArthur River 7 oil at Cook Inlet Energy's facilities and Cook Inlet Energy's request to commingle West McArthur River oil and Redoubt Shoal 8 oil, was taken by Lynn Hall on the 14th day of April, 2011, commencing at the hour of 9:00 a.m., at the Alaska Oil and Gas 9 Conservation Commission, Anchorage, Alaska; 10 THAT this Hearing Transcript, as heretofore annexed, is a true and correct transcription of the proceedings taken by Lynn 11 Hall and transcribed by Suzan Olson; 12 IN WITNESS WHEREOF, I have hereunto set my hand and affixed my seal this 18th day of April, 2011. 13 14 �� ` C Notary Public in and for Alaska 15 My Commission Expires: 10/18/14 16 17 18 19 20 21 22 23 24 25 R & R C O U R T R E P O R T E R S 811 G STREET (907)277- 0572 /Fax 274 -8982 ANCHORAGE, ALASKA 99501 • • STATE OF ALASKA OIL AND GAS CONSERVATION COMMISSION OTHER 11 -12 and 11 -13 COMMINGLE WEST MCARTHUR RIVER oil and REDOUBT SHOAL oil April 14, 2011 at 2pm NAME AFFILIATION PHONE # TESTIFY (Yes or No) tii4 ( Ae . Phi;fin (ail 613ipmny tP 61.263 -7 67Z '%61.)LA z 3 3q - 6 z�15 - fjgs u �f DP 105 J o o Y Cc e_ () L cc no' CO L J L J �— - 1 / A f S EAN PARNELL, GOVERNOR DEPARTMENT OF NATURAL RESOURCES 14 550 WEST 7 "AVENUE, SUITE 1100 ANCHORAGE, ALASKA 99501 -3650 DIVISION OF OIL AND GAS PHONE: (907) 269 -8431 FAX: (907) 269 -8918 March 30, 2011 fr - . Cairn. Alaska Oil and Gas Conservation Commission '° + w , 0 ;71344 333 W. 7 Avenue, Suite 100 Anchorage, AK 99501 Re: Request to Store Trading Bay oil and McArthur River oil at the Kustatan Production Facility Request to Commingle West McArthur River oil and Redoubt Shoal oil Dear Commission: The Department of Natural Resources, Division of Oil and Gas (Division) supports the applications from Cook Inlet Energy LLC (CIE) and Chevron North America Exploration and Production (Chevron) to store oil produced from the Trading Bay Field and McArthur River Field at CIE's Kustatan Production Facility (Kustatan), and to commingle production from the West McArthur River Field and the Redoubt Shoal Field in a storage tank at Kustatan. CIE and Chevron have discussed their plans with the Division, Oil Flow Diagram enclosed. The Division has no objections and urges the Alaska Oil and Gas Conservation Commission (AOGCC) to approve the two applications. /Allowing Chevron to store oil at Kustatan benefits the State, as the mineral owner, by mitigating the risks of lower production and increased transportation costs. It allows Chevron to continue uninterrupted production from the Trading Bay Field and McArthur River Field while storage tank maintenance operations are conducted over the summer. This reduces the risk of damaging the reservoir due to shutting in production and avoids increased transportation costs by mitigating the need to add additional vessel calls on the Drift River Terminal to compensate for less available storage in Chevron's existing facilities. This reduces the environmental risks to Cook Inlet Pipe Line (CIPL) operations since each vessel call creates incremental risk. As the mineral owner, the risks associated with allowing CIE to commingle production from the West McArthur River Field and the Redoubt Shoal Field is de minimis to the State. The oil volumes from these two fields are relatively small. Division staff reviewed specifications for the existing meters, and is satisfied the proposed metering scheme protects the state's interests. The two meters which are proposed for tracking Redoubt oil production are Micro Motion ELITE Coriolis flow and density sensors. These sensors appear to be in line and would have a single phase going through them with only a heater treater between the meters. While the system does not "Develop, Conserve, and Enhance Natural Resources for Present and Future Alaskans." equest to Store Oil at Kustatan March 30, 2011 Page 2 of 2 contain a test loop for LACT testing, using these meters with a single phase fluid, and only a heater treater in between would be similar to the installation discussed in the Micro Motion White Paper by Ruben Moldes, Engineer with Total Austral, enclosed. In the example installation in Australia, the sensors are mounted in series and are used in an LPG custody transfer application. While there are issues with the use of these meters with LPG, the meters have proven accurate and required little maintenance. The white paper outlines Total Austral's experience showing a Coriolis meter to be more accurate and require lower maintenance in oil service over a six year period than the positive displacement LACT meters used in the Total Austral project where the Coriolis meter was tested. Given this data, CIE's current installation of two Coriolis meters prior to the storage tank for oil from the Redoubt Platform should provide accurate, redundant and a self checking system to determine Redoubt production volume. This volume would then be subtracted from the total stream shipped through the CIPL LACT meter to determine West McArthur River volume. Given the minute risks to the State, the potential risk of losing production if wells are shut -in, and the very real cost considerations of adding more vessel calls, the Division strongly supports AOGCC approving Chevron's and CIE's a request to store and commingle oil at Kustatan. The Division does not require a hearing; however, if a hearing is held, the Division reserves the right to provide additional testimony in support of the applications. We appreciate your consideration of our support. If AOGCC staff has questions, please contact Alan Dennis at 375 -8236, or via email at alan.dennis @alaska.gov. Sincerely, Kevin R. Banks Director Enclosures: Cook Inlet Energy Oil Flow Diagram Micro Motion White Paper: Coriolis Flowmeters in an LPG Custody Transfer Application Cc: Benee Braden, DO &G Kevin Tabler, Chevron David Hall, CIE 1 On the CIE Oil Flow Diagram, these meters are labeled FE -02 and FE015. RU/WMRU SAI FS 00 Al LOCATION d3316 DR CxCCBD The purpose of this document is to help provide a clear understanding the proposed method of measuring RU/VRARU soles of stored at KPF. Both oil streams ore measured through multiple meters in the flow pc — — — — — — — — before entering sales oil tank T -142. and /or T -135. MPD -OGA- 2000 -005 OSPREY PLATFORM RU Fluid Allocation FE- 2015 -09 -1 • RU Oil produced from RU Well p wll be metered at the wellhead 1 WELL HEAD through Mass Flow Meter FE- 2015 -09 -1 for well allocation. RU1 METER • If other RU wells were brought online, same would apply. PIG LAUNCHER • RU 00 produced from RU Well / 7 will be metered at the wellheag ' FE -03 il y_101 tri I - using Moss Flow Meter FE- 2015 -09 -7 for well allocation. METER J • Fluid from RU 1 and RU 7 will then be metered together using Le I MPD -OGA -2002 I Detection Meter FE -03 before leaving the Osprey Platform. MASS FLOW LEAK • RU fluid will travel to Kustatan Production Facility (KPF) via the F FE- 2015 -09 -7 DETECTION METER PC line. WELL HEAD METER • When entering KPF, RU fluid wll be metered using Leak Detection RU7 Meter FE -2013. • After the primary separation process RU Oil is then metered usini ultrasonic meter FE -15 downstream of V -113A and or V -1138 be — — — — — — — — entering V -115C. • RU oil is then metered using ultrasonic meter FE -02 prior to entering sales oil tank T -142 and /or T -135 where it will be • _ _ — — — — — — — — 1 corningled with WMRU oil. •OINT OF WMRU/RU COMINGLE CRUDE OIL TANK LAUNCHER FE- 1020 -733 FE -02 X -733 to METER - 1 T- 142/7 -135 METER HEATER " T -142 / U OIL �� TREATER VORTEX LEAK —� (10,000 Bbls) ULTRASONIC MASS / MPD -004 -2018 DETECTION METER FLOW METER MPD -KCA -2015 \ V -1150 MPD -KGA -2018 MPD -KCA -2010 ■ 4' ' PIPELINE WMRU PRODUCED (I — X -108 w. CRUDE `L I P -732 ....-- FE -7006 X -732 FE- 1015 -732 /// T -906 �' METER METER CRUDE re. (10,000 Bbls) ULTRASONIC LEAK VORTEX LEAK MPD- MCA -1015 DETECTION METER DETECTION METER P -440 MPD- MCA -1014 MPD -MGA -1014 I / . 1 TANK FLUID MEASUREMENT: I WEST McARTHUR RIVER UNIT (WMRU) — — 1. TANK LEVEL INDICATORS — — — 2. DAILY OPERATOR HAND STRAPS REFERENCE DRAWINGS REVISIONS REVISIONS DRANK NUMBER SHEET DESCRIPTION REV DATE BY CPR DESCRIPTION gg F"„8 WI REV DATE or aw DESCRIPTION 0 C MICRO MOTION WHITE PAPER BY RUBEN MOLDES, ENGINEER, TOTAL AUSTRAL Coriolis Flowmeters in an LPG Custody Transfer Application This paper discusses the use of Coriols mass flowmeters in a UAM2Calibracbnes del MedidorMasico Leased Automated Custody Transfer (LACT) application involv- ing Liquid Petroleum Gas (LPG). It contains a description of ror Total Austral's facilities, calibration strategy, proving results, "T"°SU"°"°` and application problems. Finally, this paper presents Total -- Austral's conclusions concerning the appropriateness of Coriolis technology for this application. 0999 4\( Previous experiences with Coriolis - 0999 At Total Austral, we first used Coriolis technology in 1991 to 07108/20p1 21091201 06111Q001 20/12/2001 031112120tre meter the liquid outlet of our test and production separators. Figure 2. Meter proving data Coriolis was a solution to maintenance problems because well test figures were very close to actual oil production. The avail- These experiences, in combination with Micro Motion's accu- ability of a density measurement allowed us to estimate Basic racy specifications, triggered interest in testing a flowmeter in Sediment and Water (BSW), and after some time separators a LACT unit. were moved from tri -phase to bi -phase operation. LPG LACT unit In 1997, a Micro Motion Coriolis meter was mounted down- In 1999 Total Austral signed a contract to deliver LPG to ENAP stream in series with the fiscal positive displacement (PD) (the Chilean National Oil Company). ENAP's previous experi- meters in a crude oil application. Typical flow in this applica- ence with Coriolis had been very good, so both ENAP and Total tion is around 50% of mass nominal range of the sensor. Austral considered Coriolis a suitable technology for the LACT During six years of uninterrupted operation, a number of PD unit. meters were replaced. However, the Coriolis meter never required maintenance, and its meter factors remained within Facility and design 0.1%, with no drift since startup. Total Austral and ENAP agreed to build a LACT unit with two Figure 1 shows the solid mounting of the meter; Figure 2 meters in series. The measurement objectives were to meter shows data from seven months of weekly proving. LPG quantities and split mass units, in propane and butane, to produce commercial - quality propane and butane as per GPA s . < � 2140, propane content approximately 60 %, typical density �` 0.535 g/cm3. P, I _ The LACT unit is located north of Tierra del Fuego Island, on i i „1-_4 t the Argentina -Chile border. This area experiences frequent k `` high winds (above 100 km/h), and the ambient temperature 1 varies from -20 °C in winter to +25 °C in summer. The installa- `, tion uses a 6" pipeline with centrifugal pumps, for an applica - tion flow of 700 -780 tons/day at a pressure of 70 bar. Fluid $ ° temperature is 20 -30 C. The site is supervised remote) '� ■ P P remotely via f . telemetry. ` ! The LACT unit contains two 3" ELITE sensors from Micro +1„.= - ' Motion, connected to RFT9739 transmitters. The sensors are Pk mounted in series. Fiscal figures are obtained by averaging the data from both meters. The transmitters send mass and densi- Figure 1. Mounting of Micro Motion meter ty data to the flow computer. The frequency pulse outputs are configured to send volume totals to the flow computer, which will use them for proving input for calibration. Micro Motion EMERSON. • • MICRO MOTION WHITE PAPER Page2of4 Other equipment on the LACT unit (see Figure 3) includes: ture data using the COSTALD method. This procedure is • Danalyzer 500 -2350 automatic sampler and on -line chro described later in this paper, in the section entitled "Density matograph Validation ". • Auxiliary transmitters for conventional volume proving Because the flowmeter density values and the calculated den- sity values were in perfect agreement, we felt confident about • Bi- directional volume prover of 570 liters (1140 liters per both the Coriolis density performance and the on -line chro- round trip) matograph and temperature transmitters. The LACT unit has several known design weaknesses: The meter factor for mass can be derived from the volume • The flowmeters are slightly oversized. This was intentional, meter factor and the density meter factor using the following to allow for future expansion and to minimize pressure drop. formula: The typical mass flow of this application is around 25% of MF,R - MF„ *MF, nominal range. • For simpler skid design, the sensor is mounted in an inverted Volume proving position. This carries the risk of spurious measurement dur- ing a stop, if fluid in the sensor is partially vaporized. To Volume proving is performed using the conventional method - overcome this, the meters are maintained under pressure ology of API MPMS Cap 4.8. The meter factor is the average of during stops, to avoid two -phase flow through the sensor. all valid runs. According to policy, any run that is more than three standard deviations from the average is discarded, but • Pipe fixing elements are not rigid enough for a high - pressure that did not happen during volume proving. application with severe stress during pump start. These weak points are reflected in higher zero shifts, com- In the first several procedures, twenty runs were performed. pared with our other fiscal application, and the meter factors However, due to the consistency of results, only ten runs were present a bigger spread, but accuracy is still well within API required for later procedures as long as random uncertainty remained below 0.027 %. suggested limits. Density self - calibration .� 4 ' ,r u r A ` ,, , r Density is read several times to minimize random effects of . repeatability, and both averages are used to obtain density 4 , meter factors with the following equations: D � _ Di 2 Ds MFD, - � MFD, D2 During the first two years, density data were collected with �, ,' F meters at operating pressure, operating temperature, and I • 1 . i" i zero flow. Approximately sixteen measurements for each flowmeter were averaged in the flow computer. This method Figure 3. Proving equipment allowed data collection with both meters in the same condi- Calibration strategy tion. However, a slight drift was observed between the two Because Total Austral places top priority on safety, the select- flowmeters, probably originating in a different cool -down of ed calibration strategy could not involve manipulation of dan meters due to ambient temperature. gerous liquids. To overcome the drift, density data were collected during the Considering manufacturer accuracy specs (0.12% at our typical entire day, with both meters at normal flow and pressure com flow) and the sensitivity of LPG density to pressure and tem- applied as per API MPMS Chap 11.2.2. perature (0.5 °C change in temperature means 0.15% change When this correction was applied, the average daily density in liquid density), it is difficult to improve uncertainty figures values reported by the two meters were within 0.01 % of each with a field prover. The LACT unit was implemented to obtain other. traceability to national standards, while at the same time guar Total Austral compared these results to the results predicted anteeing that no systematic errors would remain undetected. by manufacturer specifications. Micro Motion's specifications Reduction of measurement uncertainty was not the primary for density measurement are 0.0005 g/cm3 for accuracy and objective. 0.0002 g/cm3 for repeatability (assuming a 95% confidence Installation of a picnometer or a master densitometer was con- level). A density product of 0.53 g/cm3 corresponds to 0.1% sidered and discarded. Instead, density measurements from accuracy. The average of both meters should have an expand - the Coriolis meter were validated against a calculated density ed uncertainty around 0.07% (95 %). which we obtained from composition, pressure, and tempera - On the other hand, if both instruments are operating normally, II • • Coriolis Flowmeters in an LPG Custody Transfer Application Page 3 of 4 density spread should be within ''0.1 %. This is the expect- 0150 ed density meter factor (DMF) limit of each meter: •M••rn 0,00 0.9986 <_ DMF _< 1.0014 0 050 Proving results 0.00° . The Coriolis meters have been calibrated fifteen times since startup. Average meter factors for the two meters are 0.9988 -0 °50 and 0.9985, with a standard deviation of approximately 0.1 %. - 0100 Figure 4 shows data from thirteen procedures. One abnormal value was observed in one of the proving meters. This value -0 150 _ ._ — -- — — was assumed to be an outlier, and was discarded. CALIBRACIONES ULACT LPG 1.0050 M.a a °. Figure 6. Repeatability estimates — Lim,t, Infenor 95•<, Density validation 1.0030 1 f The correlation between the density values from the Coriolis 00,0 meters and the on -line chromatograph is used to confirm the 0 9990 • y accuracy of the flowmeter density measurements, the tem- y ` `� e perature transmitters, and the on -line chromatograph. 0.9970 f - ;� T Accordingly, this procedure was implemented very carefully. 0.9950 ` I The flow computer measures density and reads and calculates 8 O 2 average values for pressure and temperature. Every five min- a e = - a a - a utes (the approximate time between chromatograms), it cal- " culates meter density at standard conditions and compares Figure 4. Proving results these values with a calculated density obtained from composi- Measurement spread between meters tion and the COSTALD method. At typical operational flow, Micro Motion's specifications for Coriolis density values are transformed to standard conditions mass flow measurement are 0.12% for accuracy and 0.05% for using API MPMS Chap 11.2.2, pressure correction, and GPA TP repeatability. Gross differences in mass flow measurements 25 for temperature compensation. An iteration technique is between the two meters should be less than 0.16% (assuming required for maximum accuracy, with an estimated value at a 95% confidence level) with a rate of change of the gross dif standard conditions. Meter density is first corrected in pres ference value between one day and the next of approximately sure to calculate a value at fluid temperature and vapor pres 0.07%. sure, then TP 25 converts the value to 60 °F (there is no TP 25 for international units yet). This iteration is necessary if esti- Data on meter performance for calendar year 2002 are shown mated and calculated values are different. below. Figure 5 shows the difference between meters. Micro Motion's specifications are verified. Figure 6 shows an esti- Dilerencias Dlarias de Den3idad a Condition Estandar - Dia 231512003 mate of repeatability, using a 24 -hour time period. 0 5410 0.5400 Diferencias Brous en0e medidores masicos ano 20021 — rte 0.5390 • •.,,,. , 0 200 0.5380 - - - 0. 150 - - - 0.100 _ 0.5370 i 0.050 0 5360 — — - ..,v..Q,. -- ��• ? �--'— _ v_�r y__ 0.535° -- _ - -. - -- — _ - - --- - 0.000 \\` 0.5340 -0 050 ' 0.5330 - - - - - -- -0 .100 - .._. _ _ - 150 .0 20o e g 4 a t t M1 Figure 7. Density validation data from a typical day Using the 5 minute data, a report and graph are generated in Figure 5. Gross differences between mass flow meters, CY2002 the SCADA system. Figures 7 and 8 compare data from the two flowmeters and the chromatograph. Figure 7 shows data from a typical day; Figure 8 shows data from a day with some • • MICRO MOTION WHITE PAPER Page4of4 Coriolis Flowmeters in an LPG Custody Transfer Application process variation. The chromatograph data show a slight delay South West Research Institute (SWRI) and the National due to sample time. Both graphs demonstrate the high agree- Engineering Laboratory of Great Britain (NEL). ment of both density measurements. Daily differences are In conclusion, in Total Austral, Coriolis flowmeters are one of approximately 0.05 % to 0.1%. the preferred technologies for liquid hydrocarbon custody ` Diferencias Diaries de Densidad transfer. a Condicibn Estandar - Dia 22/5!2003 0.5410 0.5400 0.5390 I -- 0.5380 I i. - - —_ - 0.5370 +_ 0.5360 0.5350 0.5340 {- 0.5330+ - -- rn um 414, 4m 141x1 16. 1.111 xm 72119 Figure 8. Density validation from day with process variation Flowmeter operation problems On two occasions, a Micro Motion transmitter reported a sen- sor failure alarm. Both times, the alarm disappeared when the transmitter was reset. This was diagnosed as a defect in the transmitter software, which has since been corrected. In three years of operation, no other incidents have been observed. Conclusion Performance of the Coriolis technology in this application has been highly satisfactory, in terms of both reliability and low maintenance. Micro Motion's specifications have proved accu- rate. Total Austral has confirmed its experience against several reports from recognized independent institutions such as the WWW`micromotion.com The contents of this publication are presented for informational purposes only and, `` ° PlantWeti while every effort has been made to ensure their accuracy, they are not to be construed • i as warranties or guarantees, expressed or implied, regarding the products or services described herein or their use or applicability. We reserve the right to modify or improve Micro Motion supports PlantWeb field -based architecture, the designs or specifications of our products at any time without notice. a scalable way to use open and interoperable devices and systems to build process solutions of the future. Micro Motion, Inc. USA Micro Motion Europe Micro Motion Japan Micro Motion Asia Worldwide Headquarters Emerson Process Management Emerson Process Management Emerson Process Management 7070 Winchester Circle Wiltonstraat 30 Shinagawa NF Bldg. 5F 1 Pandan Crescent Boulder, Colorado 80301 3905 KW Veenendaal 1 -2 -5, Higashi Shinagawa Singapore 128461 T (303) 527 -5200 The Netherlands Shinagawa -ku Republic of Singapore (800) 522 -6277 T +31 (0) 318 549 549 Tokyo 140 -0002 Japan T (65) 6 777 -8211 F (303) 530 -8459 F +31 (0) 318 549 559 T (81) 3 5769 -6803 F (65) 6 770 -8003 www.micromotion.com F (81) 3 5769 -6843 aik Micro Motion EMERSON. WP -00695 ©2004. Micro Motion, Inc. All rights reserved. N STATE OF ALASKA NOTICE TO PUBLISHER ADVERTISING ORDER NO. ADVERTISING INVOIC T BE IN TRIPLICATE SHOWING ADVERTISING ORDER NO., TIFIED A O_2114029 AFFIDAVIT OF PUBLICATION (PART 2 OF THIS FORM) WITH ATTACHED COPY OF M ORDER ADVERTISEMENT MUST BE SUBMITTED WITH INVOICE. SEE BOTTOM FOR INVOICE ADDRESS F AOGCC AGENCY CONTACT DATE OF A.O. R 333 W 7 Avenue, Ste 100 Jody Colombie 3/7/11 ° Anchorage, AK 99501 PHONE PCN M (9071 793 -1221 DATES ADVERTISEMENT REQUIRED: o Peninsula Clarion 3/10/11 PO Box 3009 Kenai, AK 99611 THE MATERIAL BETWEEN THE DOUBLE LINES MUST BE PRINTED IN ITS ENTIRETY ON THE DATES SHOWN. SPECIAL INSTRUCTIONS: Type of Advertisement ® Legal ❑ Display ❑ Classified ['Other (Specify) SEE ATTACHED (commingle West McArthur River oil and Redoubt Shoal oil) SEND INVOICE IN TRIPLICATE AOGCC, 3001 Porcupine Drive PAGE 1 OF TOTAL OF TO Anchorage, AK 99501 2 PAGES ALL PAGES$ REF TYPE NUMBER AMOUNT DATE COMMENTS 1 VEN 2 ARD 02910 3 4 FIN AMOUNT SY CC PGM LC ACCT FY NMR DIST LID 1 11 02140100 73540 2 3 4 REQ ISITIONED BY: i ' DIVISION APPROVAL: 02 - 902 (Rev. 3/94) Publisher /Original Copies: Department Fiscal, Department, Receiving AO.FRM • • Notice of Public Hearing STATE OF ALASKA Alaska Oil and Gas Conservation Commission Re: Chevron's request to store Trading Bay oil and McArthur River oil at Cook Inlet Energy's facilities, and Cook Inlet Energy's request to commingle West McArthur River oil and Redoubt Shoal oil. Chevron North America Exploration and Production (Chevron) has requested to store oil produced from the Trading Bay Field and the McArthur River Field, in storage tanks at Cook Inlet Energy (CIE)'s Kustatan Production Facility. In order to free tankage required to store Chevron's oil, CIE has requested to commingle oil produced from the West McArthur River Field and the Redoubt Shoal Field, in a storage tank at CIE's Kustatan Production Facility. The Commission has tentatively scheduled a public hearing on this matter for April 14, 2011 at 9:00 am. To request that the hearing be held, a written request must be filed by 4:30 p.m. on April 11, 2011. If a request is not timely filed, the Commission may consider the issuance of an order without a hearing. To learn if the Commission will hold a hearing, call 907 - 793 -1221 after April 12, 2011. Written comments regarding the application may be submitted to the Commission, at 333 West 7 Avenue, Suite 100, Anchorage, Alaska 99501. Comments must be received no later than 4:30 p.m. on April 11, 2011, except that, if a hearing is held, comments must be received no later than the conclusion of the hearing. If, because of a disability, special accommodations may be needed to comment or attend the hearing, call 907 - 793 -1221 by April 11, 2011. Cathy V. Foerster Commissioner • • PUBLISHER'S AFFIDAVIT UNITED STATES OF AMERICA, } STATE OF ALASKA ss: r Notice of Public Hea ' STATE OF ALASKA Alaska Oil and Gas Conservation Commission Denise Reece being first duly I Re: Chevron's request to store Trading Bay oil and , McArthur River oil at Cook Inlet Energy's facilities, and sworn, on oath deposes and says: l ICook Inlet Energy's request to commingle West I McArthur River oil and Redoubt Shoal oil. That I am and was at all times here IChevron North America Exploration and Production I (Chevron) has requested to store oil produced from the, in this affidavit mentions, Supervisor of 'Trading Bay Field and the McArthur River Field,. in I storage tanks at Cook Inlet Energy (CIE)'s Kustatan Legals of the Peninsula Clarion, a news - li Production Facility. In order to free tankage required to store Chevron's oil, CIE has requested to commingle paper of general circulation and published !: oil produced from the West McArthur River Field and `I the Redoubt Shoal Field, in a storage tank at C1E's at Kenai, Alaska, that the 1 Kustatan Production Facility. . Public Hearin 1 The Commission has tentatively scheduled a pubic g hearing on this matter for April 14, 2011 at 9:00 am. To A0-2 1 14029 1 must be flied by 4:30 p.m. on April 11, 2011. request sl if a request is not timely filed, the Commission may a printed copy of which is hereto annexed was . consider the issuance of an order without a hearing. To learn if the Commission will hold a hearing, call 907 - published in said paper one each and 1 793 -1221 after April 12, 2011. 1 Written comments regarding the application may be every day f one successive and I submitted to the Commission, at 333 West 7th Avenue, i t Suite 100, Anchorage, Alaska 99501. Comments must consecutive day in the issues on the 1 be received no later than 4:30 p.m. on April It 2011, .I except that, if a hearing is held, comments must be following dates: I received no later than the conclusion of the hearing. March 10, 2011 IV, because of a disability, special accommodations I may be needed to comment or attend the hearing, call 1 907- 793 -1221 by April 11, 2011. 1 Daniel T. Seamount, Jr. �} • s (�/19.11_61-- I Chair X /? ..e4...1..- /19.11_61-- L I,LISH: 3110, 2011 l 621 /20ti SUBSCRIBED AND SWORN to me before ' this 10th day of March 2011 NOTARY PUBLIC in favor for the �� S•RUSA, ' State of Alaska. )OTAR y My Commission expires 26- Aug -12 ..._m. PUBLIC STATE OF ALASKA • NOTICE TO PUBLISHER ADVERTISING ORDER NO. ADVERTISING OE IN A SHOTSING RDE NO., TI /� AFFIDAVIT CAE/ OF PUBLICATION BE TRIPLIC (PART TE 2 OF THIS WING FORM) ADVERI WITH O ATTACR CER HED COPY OF FIED AO- 2114029 ORDER ADVERTISEMENT MUST BE SUBMITTED WITH INVOICE. SEE BOTTOM FOR INVOICE ADDRESS F AOGCC AGENCY CONTACT DATE OF A.O. R 333 W 7 Avenue_ Ste 100 Jody Colombie 3/7/11 ° Anchorage, AK 99501 PHONE M (9071 793 -1221 DATES ADVERTISEMENT REQUIRED: Peninsula Clarion 3/10/11 PO Box 3009 Kenai, AK 99611 THE MATERIAL BETWEEN THE DOUBLE LINES MUST BE PRINTED IN ITS ENTIRETY ON THE DATES SHOWN. SPECIAL INSTRUCTIONS: AFFIDAVIT OF PUBLICATION United states of America REMINDER State of ss INVOICE MUST BE IN TRIPLICATE AND MUST REFERENCE THE ADVERTISING ORDER NUMBER. division. A CERTIFIED COPY OF THIS AFFIDAVIT OF PUBLICATION MUST BE SUBMITTED WITH THE INVOICE. Before me, the undersigned, a notary public this day personally appeared ATTACH PROOF OF PUBLICATION HERE. who, being first duly sworn, according to law, says that he /she is the of Published at in said division and state of and that the advertisement, of which the annexed is a true copy, was published in said publication on the day of 19_, and thereafter for consecutive days, the last publication appearing on the day of , 19 , and that the rate charged thereon is not in excess of the rate charged private individuals. Subscribed and sworn to before me This day of 19_, Notary public for state of My commission expires 02 -901 (Rev. 3/94) AO.FRM Page 2 PUBLISH 0 0 Mary Jones David McCaleb XTO Energy, Inc. IHS Energy Group George Vaught, Jr. Cartography GEPS P.O. Box 13557 810 Houston Street, Ste 200 5333 Westheimer, Suite 100 Denver, CO 80201 -3557 Ft. Worth, TX 76102 -6298 Houston, TX 77056 Jerry Hodgden Richard Neahring Mark Wedman Hodgden Oil Company NRG Associates Halliburton 408 18 Street President 6900 Arctic Blvd. Golden, CO 80401 -2433 P.O. Box 1655 Anchorage, AK 99502 Colorado Springs, CO 80901 Bernie Karl CIRI Baker Oil Tools K &K Recycling Inc. Land Department 795 E. 94 Ct. P.O. Box 58055 P.O. Box 93330 Anchorage, AK 99515 -4295 Fairbanks, AK 99711 Anchorage, AK 99503 North Slope Borough Richard Wagner Gordon Severson Planning Department P.O. Box 60868 3201 Westmar Circle P.O. Box 69 Fairbanks, AK 99706 Anchorage, AK 99508 -4336 Barrow, AK 99723 Jack Hakkila Darwin Waldsmith James Gibbs P.O. Box 190083 P.O. Box 39309 P.O. Box 1597 Anchorage, AK 99519 Ninilchick, AK 99639 Soldotna, AK 99669 Kenai National Wildlife Refuge Penny Vadla Cliff Burglin Refuge Manager 399 West Riverview Avenue 319 Charles Street P.O. Box 2139 Soldotna, AK 99669 -7714 Fairbanks, AK 99701 Soldotna, AK 99669 -2139 I k l\ ' ). \/\\ I P 491 1 . • Fisher, Samantha J (DOA) From: Fisher, Samantha J (DOA) Sent: Monday, March 07, 2011 3:12 PM To: '(foms2 @mtaonline.net)'; '( michael .j.nelson @conocophillips.com)'; '(Von.L .Hutchins @conocophillips.com)'; 'AKDCWelllntegrityCoordinator; 'Alan Dennis'; 'alaska @petrocalc.com'; 'Anna Raff; 'Barbara F Fullmer'; 'bbritch'; 'Becky Bohrer'; 'Bill Penrose'; 'Bill Walker; 'Bowen Roberts'; 'Brady, Jerry L'; 'Brandow, Cande (ASRC Energy Services)'; 'Bruce Webb'; 'caunderwood'; 'Chris Gay'; 'Cliff Posey'; 'Crandall, Krissell'; 'D Lawrence'; 'dapa'; 'Daryl J. Kleppin'; 'Dave Matthews'; 'David Boelens'; 'David House'; 'David Steingreaber; 'ddonkel @cfl.rr.com'; Delbridge, Rena E (LAA); 'Dennis Steffy'; 'Elowe, Kristin'; 'Erika Denman'; 'eyancy'; 'Francis S. Sommer; 'Fred Steece'; 'Gary Laughlin'; 'Gary Rogers'; 'ghammons'; 'Gordon Pospisil'; 'Gorney, David L.'; 'Greg Duggin'; 'Gregg Nady'; 'gspfoff; 'Harry Engel'; 'Jdarlington (jarlington @gmail.com)'; 'Jeanne McPherren'; 'Jeff Jones'; 'Jerry McCutcheon'; 'Jill Womack'; 'Jim White'; 'Jim Winegarner; 'Joe Nicks'; 'John Garing'; 'John Katz'; 'John S. Haworth'; 'John Spain'; 'John Tower'; 'Jon Goltz'; 'Judy Stanek'; 'Kari Moriarty'; 'Kaynell Zeman'; 'Keith Wiles'; 'Kelly Sperback'; 'Kim Cunningham'; 'Larry Ostrovsky'; 'Marilyn Crockett'; 'Mark Dalton'; 'Mark Hanley (mark.hanley @anadarko.com)'; 'Mark Kovac'; 'Mark P. Worcester; 'Michael Dammeyer'; 'Michael Jacobs'; 'Mike Bill'; 'Mike Mason'; 'Mikel Schultz'; 'Mindy Lewis'; 'MJ Loveland'; 'mjnelson'; 'mkm7200'; 'nelson'; 'Nick W. Glover; 'NSK Problem Well Supv'; 'Patty Alfaro'; 'Paul Decker (paul.decker @alaska.gov)'; 'Paul Figel'; 'PORHOLA, STAN T'; 'Randall Kanady'; 'Randy L. Skillern'; ' rob.g.dragnich @exxonmobil.com'; 'Robert Brelsford'; 'Robert Campbell'; 'Ryan Daniel'; 'Ryan Tunseth'; 'Scott Cranswick'; 'Scott Griffith'; Scott, David (LAA); 'Shannon Donnelly'; 'Sharmaine Copeland'; Shellenbaum, Diane P (DNR); Slemons, Jonne D (DNR); 'Sondra Stewman'; 'Steve Lambert'; 'Steven R. Rossberg'; 'Suzanne Gibson'; 'tablerk'; 'Tamera Sheffield'; Taylor, Cammy 0 (DNR); 'Teresa Imm'; 'Terrie Hubble'; 'Thor Cutler; 'Tina Grovier; 'Todd Durkee'; 'Tony Hopfinger'; 'trmjrl'; 'Valenzuela, Mariam '; 'Vicki Irwin'; 'Walter Featherly'; 'Will Chinn'; Williamson, Mary J (DNR); 'Yereth Rosen'; 'Aaron Gluzman'; Bettis, Patricia K (DNR); caunderwood @marathonoil.com; 'Dale Hoffman'; 'David Lenig'; 'Gary Orr; 'Jason Bergerson'; 'Joe Longo'; 'Kevin Skiba'; 'Lara Coates'; 'Marc Kuck'; 'Mary Aschoff; 'Matt Gill'; 'Maurizio Grandi'; Ostrovsky, Larry Z (DNR); 'Richard Garrard'; 'Sandra Lemke'; 'Talib Syed'; 'Wayne Wooster'; 'William Van Dyke'; Woolf, Wendy C (DNR); Aubert, Winton G (DOA) (winton.aubert @alaska.gov); Ballantine, Tab A (LAW); Brooks, Phoebe L (DOA) (phoebe.brooks @alaska.gov); Colombie, Jody J (DOA) (jody.colombie @alaska.gov); Crisp, John H (DOA) (john.crisp @alaska.gov); Davies, Stephen F (DOA) (steve.davies @alaska.gov); Foerster, Catherine P (DOA) (cathy.foerster @ alaska.gov); Grimaldi, Louis R (DOA) (lou.grimaldi @alaska.gov); Herrera, Matt F (DOA); Johnson, Elaine M (DOA) (elaine.johnson @alaska.gov); Jones, Jeffery B (DOA) (jeff.jones @alaska.gov); Laasch, Linda K (DOA) (linda.laasch @alaska.gov); Maunder, Thomas E (DOA) (tom.maunder @alaska.gov); McIver, Bren (DOA) (bren.mciver @alaska.gov); McMains, Stephen E (DOA) (steve.mcmains @alaska.gov); Mumm, Joseph (DOA sponsored); Noble, Robert C (DOA) (bob.noble @alaska.gov); Norman, John K (DOA) (john.norman @alaska.gov); Okland, Howard D (DOA) (howard.okland @alaska.gov); Paladijczuk, Tracie L (DOA) (tracie.paladijczuk @alaska.gov); Pasqua!, Maria (DOA) (maria.pasqual @alaska.gov); Regg, James B (DOA) (jim.regg @alaska.gov); Roby, David S (DOA) (dave.roby @alaska.gov); Saltmarsh, Arthur C (DOA) (art.saltmarsh @alaska.gov); Scheve, Charles M (DOA) (chuck.scheve @alaska.gov); Schwartz, Guy L (DOA) (guy.schwartz @alaska.gov); Seamount, Dan T (DOA) (dan.seamount @alaska.gov); Shartzer, Christine R (DOA) Subject: Public Hearing Notice Trading Bay and McArthur River Attachments: Chevron and CIE Notice.pdf 5t4 a -uM,vi t. ,1u ' Fix A 7,as1c oat x414/ t( a4 Covt4n.,vva ti;ovv Co I naru3rsio w (907)793 -1223 (907)276 -7542 ('fay) 1 r • • Cook Inlet Energy_ RECEIVFD MAR 03 Alaska Oil & G, ,,ryN(1:ssior March 3, 2011 Mr. Winton Aubert Alaska Oil and Gas Conservation Commission 333 West 7 Ave., Suite 100 Anchorage, Alaska 99501 RE: Permission to comingle WMRU and RU oil at Kustatan Production Facility Dear Mr. Aubert: As per your request Cook Inlet Energy is requesting permission from AOGCC to be able to comingle WMRU and RU oil at the Kustatan Production Facility using tanks 142 and 135. The current Micro Motion meters in place on the Osprey Platform as well as the Kustatan Production Facility would be used for accurate allocation of RU oil. As you are aware these meters are capable of .1% accuracy and are a commonly used in this application in the oil and gas industry. Cook Inlet Energy has supplied you with all the specification data on these meters and would be happy answer any questions you might have regarding this matter. Please feel free to contact me directly at 907 -317 -8239. Sincerely, /Vj David Hall CEO 601 W. 5 Avenue, Suite 310, Anckorage, AK 99501 (907) 334 -6745 * (907) 334 -6735 Fax • • Cook Inlet Energy_ March 3, 2011 Mr. Winton Aubert Alaska Oil and Gas Conservation Commission 333 West 7 Ave., Suite 100 Anchorage, Alaska 99501 RE: Permission to comingle WMRU and RU oil at Kustatan Production Facility Dear Mr. Aubert: As per your request Cook Inlet Energy is requesting permission from AOGCC to be able to comingle WMRU and RU oil at the Kustatan Production Facility using tanks 142 and 135. The current Micro Motion meters in place on the Osprey Platform as well as the Kustatan Production Facility would be used for accurate allocation of RU oil. As you are aware these meters are capable of .1% accuracy and are a commonly used in this application in the oil and gas industry. Cook Inlet Energy has supplied you with all the specification data on these meters and would be happy answer any questions you might have regarding this matter. Please feel free to contact me directly at 907 -317 -8239. Sincerely, / David Hall CEO 601 W. 5 Avenue, Suite 310, Anchorage, AK 99501 (907) 334 -6745 * (907) 334 -6735 Fax