Document o97eJab5Dvbe7pGLXEq0Omd9o

(conoco) Interoffice Communication to M. L. Ashby From P. D. Despres Date October 18, 1983 subject VCM-LCCP Low Pressure Steam Transfer Design No. 192-500-1083-PDD Review Design Return Comments by October 20, 1983 The attached review design specifies the installation of a line to transfer excess 250 psig and 150 psig steam from the VCM Plant to the LCCP 25 psig steam header. A 6" line will connect to the VCM Plant's 250 psig and 150 psig vent manifold and to the LCCP 25 psig (LP) steam header at the VCMLCCP fence line. A flow meter and local chart recorder, will be provided to account for the low pressure (LP) steam transferred to LCCP from VCM. The ability to transfer LP steam from VCM to LCCP will increase the over all energy efficiency of the Lake Charles Chemical Complex; the VCM Plant's efficiency will not be affected, but LCCP will benefit from the transfer. Certain methods of operation at LCCP create a need for LP steam, which is obtained by breaking down 650 psig steam directly from the steam plant. An alternative method of obtaining the LP steam will save LCCP the direct cost of producing that amount of 650 psig steam. The VCM Plant can supply a certain amount of the needed LP steam through the transfer of 250 or 150 psig steam that would normally be vented to the atmosphere. An approximate 36.60MM Lbs./Yr. of steam or 56,287MM BTU/Yr. can be saved by this project, based on a 10,000 Lbs./Hr. transfer for 3,660 Hrs./Yr. An estimate of the construction costs of this project will allow the economics to be completed. It is proposed that this project be completed on unallocated funds for 1983. By copy of this design to J. R. Holcomb, a preliminary cost estimate is re quested for the basis of the economic evaluation. A definitive estimate will be requested upon issue of the final design for the AFE preparation. Please bring or return all comments to me by the review meeting at 12:30, October - 20, 1983 (Ext. 5049). Paul D. Despres 1 Process Engineer kf cc: RAC-JWW-JRH(4)-JMT-MLA(4)-MCM RB-PLF-DLD-SRA-MWC-PE RJF-JAD-RHG-PDC-GLF-SAR-KC APPROVED Sr. Process Engineer OCR 000016978 Process Description This design will connect the VCM Plant's and LCCP's steam systems and allow excess steam from VCM to be consumed usefully by LCCP, A 6" line will tie into the VCM 250 and 150 psig steam vent manifolds and route normally vented steam into the 25 psig (LP) steam header at LCCP. The connection of the two systems will be made at the Plants' boundary line. There will be no changes in any steam system operations at the VCM Plant; the steam vent valves will be discharging into the LP steam header instead of to the atmosphere. There will be no loss of performance for the PIC-574B (250 psig vent valve), but a decrease in the maximum flow for PIC-575B (150 psig vent valve) from 40,000 Lbs./Hr. to 28,000 Lbs./Hr. will result. The LP steam transfer line will float on LCCP's pressure controller (normal setting is 25 psig) and excess pressure in the system will be vented through LCCP's vent control valve. Emergency overpressure in the VCM Plant's 250 psig and 150 psig steam systems will still be handled by RV's-507 and -508, respectively. A vortex flow meter (high rangeability, low differential pressure) and cir cular chart recorder will be installed in the 6" line to measure the quantity of steam transferred to LCCP. A similar flow meter and recorder is in stalled at LCCP on the LP vent. The VCM Plant will receive a 650 psig credit for the net use of the transferred steam (quantity transferred-quanti ty vented = amount of credit). LCCP will maintain the meter charts and account for the steam credits. However, the VCM Plant will maintain the equipment. 000016979 CCR Design Basis The success of the Low Pressure Steam Transfer Project depends primarily on the quantity and reliability of the steam transfers from the VCM Plant to LCCP, LCCP's need for LP steam and the VCM Plant's ability to supply it. The occurrence of a substantial VCM steam vent and the reasons for it are briefly explained in the following paragraph. The projects that will create an excess of LP steam in the VCM Plant are also listed. If no excess LP steam is expected to be produced in the VCM Plant during normal operation, these new designs will be evaluated along with this transfer line project in determining the final project justifications. Excess steam has been available at the VCM Plant for the majority of the time since the completion of the Oxy Modernization (average vent = 14,000 Lbs./Hr., July-Sept. 1983). However, much of that availability was due to inefficiencies in the cooling systems throughout the plant. This type of operation was not advantageous to the process and has since been corrected; However, it is expected that summertime cooling loads at maximum production rates will re sult in steam venting. There are several available designs that can increase the availability of excess steam that can be transferred from the VCM Plant to LCCP. They are: 1. Condensate System Revisions, 2030 Lbs./Hr., 15.56MM Lbs./Yr. 2. Heavy Ends Column Overhead/EDC Recycle Interchanger, 3,500 Lbs./Hr., 26.9MM Lbs./Yr. 3. Steam Generation from Oxy Effluent, 2,800 Lbs./Hr., 21.51MM Lbs./Yr. These designs will be evaluated for consideration in the final economics for this project. A need for approximately 10,000 Lbs./Hr. of LP steam is created at LCCP when the Clark air compressor in theAlcohol Plant Is shut down at low produc tion rates. The compressor is a turbine driven unit and breaks down 350 psig steam to 25 psig. This need for LP steam is also created by using a steam turbine driven BFW pump at the Steam Plant for a spare and running an electric motor driven pump in its place. One turbine driven BFW pump will always be in operation at the steam plant to provide safe operation in the event of a power failure. Overall steam savings are expected to provide a sufficient project payout in addition to offsetting the incremental electrical energy usage. The review design has been based on a transfer rate of 10,000 Lbs./Hr. A six inch line will require an 8 psi pressure drop at the design flow rate. A block valve has been provided at the VCM Plant-LCCP boundary limits to isolate the two steam systems. Therefore, the new six inch line in the VCM Plant has been specified for a 300# flange rating in case it is pressured up by the 250 psig steam system. However, the design flowing pressure of the CCR 00016980 new line is 33 psig based on an LCCP steam header pressure of 25 psig. A six inch transfer line is necessary to provide an acceptable pressure drop at a maximum expected flow rate of approximately 20,000 Lbs./Hr. A four inch line would restrict the vent rate and possibly cause the steam system at the VCM Plant to overpressure. The design steam temperature has been caluclated to be 360F based on equal flows of 150 psig and 250 psig steam vented into the transfer line. Approximately 80F of superheat will be provided in the LP steam. CCR 000016981 Environmental Impact Statement This project will have no effect on the environment. Energy Impact Statement This project will reduce the Lake Charles Chemical Complex energy con sumption by an approximate 56,287MM BTU/Yr. by transfer of excess low pressure steam from the VCM Plant to LCCP and reducing the steam boiler natural gas consumption by 65,442 MSCF/Yr. and increasing electricity consumption by 1,177 MKWH/Yr. The project will reduce the VCM Plant energy consumption by 60,573MM BTU/Yr. based on the 36,600M Lbs./Yr. of 650 psig steam savings. The Process Design Energy Checklist has been completed and is attached. Safety and Health Impact Statement This project will have no effect on plant safety. The Process Design Safety Checklist has been completed and is attached. CC$ 00J69ae VCM PLANT PROCESS DESIGN ENERGY CHECK LIST DESIGN NO: RL-SVO- t0&3~P>~b ~^C Item verified and action taken Item verified but no action required Item verified but not economically feasible no action necessary I. INSULATION The economical insulation thickness was calculated and specified for the following equipment: Permanent Insulation 1. Tank 2. Vessel 3. Heat Exchangers 4. Piping* Item No./Thfcknessh'nches) f/ ff // f 5. Control Valves 6. Process Valves 7. Piping to and from Steam Traps. // // // // M-///.C* CK-Z* / f f / t / / / 8. Reusable Insulation 1. Tank 2. Vessel 3. Heat Exchangers 4. Piping* 6. Process Valves 7. Piping to and from Steam Traps. Item No./Th1ckness(inchesl f // f f/ f r/ f f/ f // / // 3" f / / / / / / 'listed Is only one line of a set of piping that have the same diameter and contain the same fluid at an identical temperature. `.J. TURBINES AND ELECTRIC MOTORS The design considered the following provisions when specifying the type of drive for the listed equipment. .... Equipment Item Pumps a) High efficiency electric motors b) Variable speed and/or variable horsepower motors or turbines In order to provide flexibility during operations at low rates. c) Design specifies optimal motor phase and voltage (normal is 3 phase, 440V motors) _______ _______ _____ ___ d) Space or coil heaters for motors are ineluded only when necessary. _______ _____ e) Steam or gas turbine (instead of an electric motor). _____ _____ __ Items to be considered when specifying a turbine 1. Compatibility with current and projected plant steam balance. 2. Use of exhaust gas or steam in other areas. Compressors Agitators/ Mixers _______ _____ ____ _____ "1 Blowers ____ Fans CCR 000016983 DESIGN NO:ffl -^00- Q35'PITfr III. ROTATING EQUIPMENT The design considered the following provisions when specifying the listed equipment. A. Pumps Item No. B. Compressors Item No. 1) Use of e pressure system as a viable alternative. 2) System pressure drop optimized by comparing cost of energy to the cost of the system (piping and equipment). . 3) A comparison of the turndown vs. minimum flow requirements. 4) Efficiency at the normal flow rate j 5) Efficiency at the minimum expected rate ^_____ C. Mixers/Aqitators Item No. 1) Minimum/Maximum flow compatible with varying production rates. 2} Parallel but different sizes economically feasible to provide flexibility. 3) Efficiency at the normal flow rate* 4) Efficiency at the minimum expected rate 5) Comparison of single versus multi stage. 1) High efficiency blades and use of baffles for better mixing. ________ 2) Economic comparison of a larger size _________ ______ versus multiple mixers. 3) Use of variable speed mixers IV. HEAT TRANSFER EQUIPMENT The following provisions were considered in the design of heat transfer equipment. A. General Considerations for All Types of Heat Transfer Equipment Item No.1 1) Control instrumentation is incluoed to prevent over-heating or over-cooling. _____ 2) Economics of an in-line spare if an onstream cleaning can not be performed. _________ _____ 3) Calculating an accurate overall heat transfer coefficient. The HTRI design methods can be used in the calculation. _____ _____ 4) Variation of the overall heat transfer coefficient versus turndown. . ______ _____ 5) A sufficient allowance for fouling. G) Using another process stream as a heating or cooling medium (interchanging). _____ _____ B. Reboilers and Steam Heaters Item No._______ C. Coolers and Condensers Item No. 1) Compatibility with steam balance 2) Condensate returned to a header 3) Allowances in the design for use of different pressure steam. __ __ _________ __ D. Fired Heaters Item No. 1) Economic comparison of a cooling water exchanger versus an aircooled exchanger. 2) Provide the necessary connections to perform an onstream back wash of the cooling water side of the exchanger. E. Interchangers _ " " Item No. 1) Insulating Refractory(Consult with MED) ___^_ 2) Multi-fuel burners _____ 3) Preheat of combustion air 4) Stack gas heat recovery _____ 5) Stack gas analyzer and/or excess oxygen controller __________ 1) Steam savings must be compatible with the plant's steam balance. i iQOO'ic<* DESIGN NO: ~ ^0Q-/O83-fJ>'b V. STEAM TRAPS Refer to Conoco Engineering Standard MS for design specifications. 1) Trap sized for proper flowrate and safety factor 2) Condensate is to be returned to the return system when economically feasible. 3) PM notes for discharge piping into the top of the return header. ' 4) A three way test valve is to be installed downstream of traps discharging to a return header. 57W KiF A/ F Item No. 57-Z- 5 T-3 NF NF hf F NF HP NF VI. MONITORING INSTRUMENTATION The following items are necessary in order to monitor the energy usage of the designated item. A. Heat Exchanger Number _____ _____ B. Pump Number 1) Shell and tube side inlet and outlet temperatures. 1) Suction and discharge pressure gauges. 2) Steam side pressure. 3) Steam flow meter. 2) Outlet flow meter C. Compressor Number . D. Turbine Number 1} Inlet pressure and temperature gauges for each stage. 2) Discharge pressure and temperature gauges. 1) Inlet pressure and temperature gauges. 2} Outlet pressure and temperature gauges. 3) Inlet flow meters for each stage 4) Discharge f'ow meter. 5) Recycle flow meter. VII. MAINTENANCE CONSIDERATIONS A. Equipment Preparation for Maintenance Work OkC Procedures are included for the most efficient method of emptying, clearing, purging, and/or regenerating process equipment included in the design. B. Maintenance 0 All preventive maintenance items that contribute toward maintaining the maximum efficiency of the process equipment are noted. VIII. GENERAL The following items should be considered for all designs. A. Operating Procedures Normal operating procedures are included that note in detail those items which must be followed in order to achieve maximum energy efficiency. Supplemental operating procedures are included for maximum energy efficiency for operations at below normal rates or - any other special conditions such as startups, shutdowns or abnormal operations. B. Relief Valves Discharge of relief valves are returned to process or a collection vessel for product recovery. C. Impact Installation of the project Impacts energy consumption of existing plant equipment. i OCR 000016985 4 DESIGN NO: tfZ'SOQ -/&?- ENERGY IMPACT STATEMENT The following is a procedure for calculating the energy savings or usage of the project on the CMA Basis. A. Steam 1) The amount of steam that is saved (used) by the project and its pressure = MM Lbs/Yr - kOD psig 2) From the plant steam balance the equivalent 600 psig steam savings (usage) ^6'- (&0 MM Lbs/Yr. 3) CMA Energy factor for steam. 4) Total CMA Energy for steam saved (used). 8. Electricity a x 1655 BTU/Lb. stu 0) ------ TrU 1) The electricity saved (used) by the project. 2) CMA Energy factor for electricity. 3) Total CMA Energy for electricity saved (used). C. Natural Gas MM KWH/Yr. X 10,000 BTU/KWH HH BTU ---------------- Yr. 1) The natural gas saved (used) by the project. 2) CMA Energy factor for natural gas. 3) Total CMA Energy for natural gas saved (used). MM SCF/Yr. x 1.040 BTU/SCF W BTU ---------------- rr. 0. Product Recovery and Loss 1) Additional VCM saved (lost) 2) Energy factor for VCM (obtain from energy coordinator) 3) Energy saved (lost) due to.'VCM savings (losses). MM Lbs/Yr. xBTU/Lb. VCM MM BTU/Yr. 4) Additional E0C saved (lost). 5) Energy factor for EDC (obtain from energy coordinator). 6) Energy saved (lost) due to E0C savings (losses). MM Lbs/Yr. xBTU/Lb. EDC W BTU/Yr. 7) Additional HC1 saved (lost). 8) Energy factor for HC1. 9) Energy saved (lost) due to HC1 savings (losses). ___________ m Lbs./Yr. 2681.1 BTU/Lb. HC1 10) Total energy saved (lost) due to product recovery (loss). E. Summary 1) Total net savings (usage). Sum of lines A-4, B-3, C-3, and D-10. 2) Equivalent 1972 CMA energy usage based upon production of 670MM Lbs. VCM/Yr, no incremental EDC and no HC1 sales. 3) Fractional decrease (increase) In energy consumption on the CMA Basis. 4} Percent decrease (increase) in energy consumption on the CMA Basis. MM BTU "TFT hOS=}3 m BTU/Yr. 3.434.621 m BTU/Yr. x 100X A 7^ * NOTES: 1. Actual Chemical Complex savings are 56,287MM BTU/Yr. based on savings of 65,442 MSCF/Yr. of natural gas and increased electricity consumption of 1,177 MKWH/Yr. at the Steam Plant. 000016906 CCR 910000 O O 70 hD CS> VCM PLANT LEGEND I. OVERPRESSURE PROTECTION PROCESS DESIGN SAFETY CHECK LIST DESIGN NO :/?Z- S?)Q- tn&>3' PTjro Item verified as stated and specified action taken Item verified but no action required ____ No action taken A. Overpressure jteslgn Basis Overpressure protection was designed for the listed equipment for the conditlon(s) indicated below: Pressure Vessels Item No. Exchangers Item No. 1. Blacked Valve 2. Coaling Water failure 3. Instrument Failure 4. External fire 5. Other (Specify) Protection by RV-No. Alternate Protection Noted Below 1. Blocked Valve - Cold Fluid Vaporization 2. Slocked Valve - Cold Fluid Expansion 3. Tube Rupture 4. External Fire Protection by RV-No. (Tube Side) Protection by RV-No. (Shell Side) Alternate Protection Noted Below Rotating Equipment Blocked Discharge Valve Positive Disp. Pump Positive Disp. Compressor Steam Turbine Protection by RV-No. Item No. ' _____ _______ _______ _______ ____ ___ ___ ___ Piping Blocked in Line Vaporization Thermal Expansion Protection by RV-No. Line No. ZVTMrf __ C>tc ___ 8* Relief Valves Relief valves and inlet and outlet piping specifications were checked for the following conditions; Relief Valve Number 1. Liquid Flashing Effect on Valve Capacity Design Temperature 2. Discharge Back Pressure 3. Inlet Line Losses --Friction & Acceleration A p --Notes Included for Max. Length 4. Inlet & Outlet Piping-Free Draining or Drain Valve Included 5. Upstream Rupture Disc If In VOC Service II. VESSEL CLEARING A. Clearing Connections v The design includes the following provisions for the clearing of equipment containing toxic or regulated vapors and liquids. Equipment Item Contents Vessels____________________ Exchangers _________ Pumps______________ _________ Others Permanent Piping for: 1. Liquids to Closed Process Sewer 2. Vent to Direct Chlorination Header 3. Vent to Wet Vent Header 4. Vent to Relief Vent Header 5. Return to Process Connections for Temporary Hoses Isolation Capabilities for Clearing Bleeders for Clearlng/Drainlng/Purgtng Page 1 of 4 REY.l , 3/81 REV.2 - 3/82 DESIGN NO: ttZ' Z6G-h*& PFT> B. Prevention of Backflow Protection against backflow In nitrogen connections used for clearing equipment and process lines has been provided In the design and listed below: Vessels___________________ Exchangers______ ________ Pumps____________ ________ Others Equipment Item 1. Check Valve In Permanent N? Line 2. Hose Connection with Check valve 3. System Pressure <40 pslg, Hoses to be Disconnected After Purge in. mechanical A MAINTENANCE considerations A. Plant Design Standards are more restrictive than company standards In several areas. The design includes notes and specifications as required for The following Items: 1. Gaskets Gasket Per Plant Standard Piping Description Applicable Piping Specifications __ . Garlock 900 Round Flexltallic Spiral Wound _____ TFE Envelope - Ring Gasket ____ TFE Envelope - Full Face CS, SS, Nickel, Monel Piping Steam A Condensate Service Lined Piping FRP A Furan 2. Materials of Construct1on--Desiqn notes have been Included for: A2-1, A2-7, A10-1, A13-4, A20-1, A21-1, 82-1 , 82-12. B13-1, 813-3 A2-3, 82-6, D2-5, 02-6 X25-2, X26-2, X27-1 R37-1, R37-3 ________ Electric driven equipment specifying no bare aluminum parts. ________ Dry chlorine piping (B2-12 Spec.) specifying CS valves with Hastelloy C trim. ________ Minimizing copper or copper alloys in possible contact with acetylene. B. Rotating Equipment The following pumps, compressors, blowers, and agitators have been checked for the following requirements and the required specifications and notes have been Included In the design. Equipment No. n Minimum Flow Requirements o Shaft Seals--Type A Required Lubr./Flush 50 Seal Vent System to Incinerator If In VOC Service C. Tie-in Points Design Includes note(s), to specify which (If any) tie-lns(s) to existing equipment or piping are turnaround items. 0. Preventive Maintenance ________ Design Includes notes on any new equipment that requires special PM to ensure safe operation. 8869X 00 Page 2 of 4 REV.l - 3/81 REV.2 - 3/82 .juSii_________ DESIGN NO. (9? Sm-fnt'S-f'Dh IV. PERSONNEL EXPOSURE & PROTECTION A. Employee Exposure Design includes provisions where required to ensure that during normal operations, clearing for maintenance, or maintenance activity employee exposure Is within regulations. 8. Handling of Hazardous Materials Design includes provisions for safety equipment (fire extinguishers, deluge systems, safety shower and eyewash stations, fresh air systems, etc.) where required.. C. Personnel Protection Insulation <0K, Design includes specifications for Insulation on hot lines (>150F) where personnel protection is necessary. D. Accessibility of Valves & Instruments ^ Notes have been included to ensure that valves. Instruments, motors, etc. are accessible from grade or platform to permit operation and maintenance where required. E. Noise Limits Specifications have been Included for equipment where required to ensure meeting noise limits as set by Standards H-7 (control valves) and X-5 (general) or 85 dB. F. Spill Containment & Control Design includes provisions where required for spill containment and control such as diked areas, piping to process* sewers, etc. G. Lighting for Night Operations Design includes provisions for adequate lighting for night operations where required. H. Communications System Design includes provisions for additional communications system lines as necessary. Page 3 of 4 REV.l - 3/81 REV.2 - 3/82 i CCR 0 0 0 0 1 6 9 8 9 DESIGN NO. V. PREVENTION OF POTENTIAL HAZARDS A. Emergency Shutdown Requirements Design specifications, considerations, and notes have been made as necessary for the following Items: _____ 1. Control valve failure position in event of air anctbr electrical loss has been noted on spec, sheet and P4I. _____ 2. Spare equipment has been provided as needed and verified with Operations. _____ 3. Required alarms and their set points have been confirmed with Operations. _____ 4. Consideration has been given to make the system failsafe, including automatic shutdown sequences and system interlocks where feasible. B. Fire Prevention and Protection The following items have been checked and specifications or notes Included as required: _____ 1. System flammability (both process streams and materials of construction) under normal and upset conditions. _____ 2. Provision for Inert or nonflammable atmosphere such as nitrogen blanketing or purging. _____ 3. Need for flame arrestors to prevent flashbacks. _____ 4. Need for additional fire protection systems such as sprinklers, types of extinguishers, etc. C. Electrical Grounding/Bonding _____ Design has been checked and specifications and/or notes included where necessary for the electrical grounding/bonding of vessels, pumps, and piping to dissipate build-up of static charge. D. Locked or Chained Valves _____ Notes have been included on the PM for valves that must be locked or chained opened or closed for safety reasons. E. Chemistry of Mixing Streams ^ _____ Design includes provisions, operating procedures, or notes as required to ensure that no chemical reactions which could create a potentially hazardous situation will occur as a result of mixing two or more process streams. F. Minimum Clearances _____ Design includes provisions or notes as required to ensure equipment and piping clearances meet with Standard X-3 or special plant requirements and that no pinch points exist where valves must be opened and closed. Page 4 of 4 REV.1-3/81 REV.2-3/82 r> o 'x o o 00J699Q V WORK LIST Refer to Drawing No. VCM-192-500-1083-PDD. 1. Tie in line 6"-$M-l-H-B2-6 to the 250 psig vent manifold between the vent control valve, PIC-574B and the vent stack. Refabricate the vent manifold and install a 6" gate valve and bleeder between the tiein and the vent stack. Insulate the lines. The line steam system must be blinded for this tie-in. 2. Tie-in line 6"-SM-l-H-B2-6 to the 150 psig vent manifold between the vent control valve, PIC-575B and the vent stack. Refabricate the vent manifold and install a 6" gate valve and bleeder between the tiein and the vent stack. Include a pressure gauge and bleeder and a temperature gauge and thermowell in the line. Include expansion loops as needed. Insulate the line. The live steam system must be blinded for this tie-in. 3. Tie-in line 6"-SM-l-H-B2-6 to the LCCP 6" low pressure vent header at the boundary limits. The pipe spec changes at this point from 300# (B2-6) to 150# (A2-3). Insulate the lines. 4,5,6. Tie-in lines 3/4"-CM-l,2,3-H-B2-6 to line 6"-SM-l approximately every 200 linear feet. Extend the lines to grade and install a 3/4" block valve, a 3/4" "Y"-strainer and a steam trap. The steam trap will dis charge to grade. Insulate the lines. 7. Install the flow meter and local flow recorder, FR-1 in the line up stream of the last block valve at the VCM Plant boundary. CCR 000016991 (conoco) PLANT fcikedmrlc* VCM Conoco Inc. Engineering Center Ponca City, Oklahoma Flow Instruments I Ltmj_______________ project VCMr.LCCP SPECIFICATION SHEET PROJECT NO. /7^-- -7Z7?-/rt<*3 - A.F.E. NO REO- NO. _ OATE ** /4(?J~$ APP D BY MADE BY ________________ ' St&am 77?w^ggg<g 1 Tag no. 2 SERVICE cc 3 lzl) 4 INSTRUMENT TYPE u a 5 LOCATION 6 7 f TYPE 8 1 LOCATION 9 | LINE SIZE. IN. | 10 | BORE. IN. SCHEDULE F& -/ 'Pf`y&Sur&/r&if-Fd Sd-e?)t+i -- Mrrrhe-* P/ertnri-ett.r~&) ---------- - -- /*> 40 .-- i ELEMENT 11 RANGE. IN. KjQ 12 METER FACTOR 13 MATERIAL 14 TRANSMITTER: PNEU OR ELECT. 15 16 1 TYPE 17 | -- n) S3\U>') S.S, bcil rc- do ** - - 1 VALVE- * A & T f l SERVICE CONDITIONS 18 | LOCATION K 19 MATERIAL: BODY UJ 20 S'ZE: BOOY 21 Nuwoen or ports -WWM PORT i^TT^T _ -- -- 22 PLUQ FORM 23 | iP: MIN. NORM MAX. -- <J.O | i1 24 | CALC. CV -- NORMAL FLOW MAX. FLOW -- --- 25 1 VALVE CV -- FULL OPEN -- 26 FAILURE POSITION -- 27 MAX. SHUTOFF AP. PSIG -- 28 DESIGN PRESSURE -- 29 30 FLUIO (NOTE UQ/VAP) 31 TEMP. -F NORM. | ^Or&1-\32 PRESSURE. PSIG MAX. M**. ' 3b0 33 433 z?o 1 33 API (MW) -- 34 SP GR AT STD. COND. 35 je^ftattap "Densth* , ft-/#* --- o.tf o 36 VAPOR PRESS- AT T. PS! ' 37 CP/CVAT TAP COMPRESSIBILITY 39 VISCOSITY AT TAP , />/>/-ft2* LuZ - A3 _ _ -- .32,1 y /-<* . 39 % UQ.. IN | 40 RATE: NORMAL , !i?i. j Hf~ 41 I RATE: /**./*, MAX. | OUT MIN _____ 0 -- o to, oco ZO.OOO 1 o "1 ,. 42! 0) MrTdr Sar'f&r aorret^rf^ *V/W ra+r. v&lue, t`s 43 1 -ddr dHrere*cr rrs 44 | /z.y C-boa<~' } i^r^/-trr7 -r CLO - 3Of ry Oi--A (4 . Vrradr* * tju*ri^r tws (ci<mt?snt. r fryvb^rn E 451 Et<,hire~ Msid&L 'K\/'?OOS~ 47 < yew///w Mrdt>J V x?-ff*r 48 1 - 49 1 , I NOTES 50 | 51 1 4-571-S (X) INOtCATES MANUFACTURER TO GIVE INFORMATION IN MIS QUOTATION. 2*61 CCR 000016992 Q.SPEC NO. / -- REV.__ SHEET -- - OF____ k. R E C E IV E R ENGINEERING CENTER PONCA CITY. OKLAHOMA SPECIFICATION SHEET INDICATORS, RECORDERS, CONTROLLERS Esi a kit / Ai^f^ f AAV//7/ f~^ \/CM ppn icrT sj rni no HI-SWA-/tin -P?rr> OATE. W. O. NO . MADE BY, (NO NO -- APPO BY, n m no (*ST\a/ "p&fit( r\P Nt-I ITEM NO. SERVICE INOICATOR OR RECORDER INPUT SIGNAL: PNEU. - ELEC. LOCATION: YARD PANEL MOUNTING: YOKE - FLUSH NO OF PENS OR POINTERS CHART- SIZE CIRCULAR . STRIP CHART RANGE CHART NUMBER CHART FACTOR CHART ORlVE: MECH. . ELEC. SCALE RANGE CALIBRATED ACCURACY SENSITIVITY REPEATABILITY F/Z -i fersT/rl* r Recorder Irifer-frrrrt / Yard Yo l Fj'rr.U-irif~ 0-/0 -iT zone ObsJhr Flerf-nca ( 6 -20.000 CONTROLLER LOCATION CONTROLLER ACTION PROP. BAND PER CENT K AUTOMATIC RESET U J DERIVATIVE J o CASCADE RESET BY e H Z REPEATABILITY 0 u SENSITIVITY ACCESSORIES INPUT OUTPUT - .----A ... v- K.V' MANUFACTURER MODEL NO PRICE Fox d erro {err 'C'tA.'h&tercf) 40 PR-fZPF.tA/a ^rAZ/AN - - '.y.:v- OENCRAL SPECIFICATIONS RECCRCER INK SUPPLY CAPILLARY WITH 6 MONTHS MIN. SUPPLY ALL CONTROL STATIONS SHALL HAVE A VALVE POSITION INDICATOR. AUTOMATlC-MANUAL SWITCH. AND OIRECT * REVERSE SWITCH. ELECTRONIC INSTRUMENTS SHALL HAVE A SOLID STATE SYSTEM ELECTRIC CHART ORlVE 115 VOLT 60 CYCLE SYNCHRONOUS MOTOR MECH CHART DRIVE 24 HOUR 5PRING WIND PROPORTIONAL BAND COMPLETELY ADJUSTABLE INSTR ELEC CLASSIFICATION IS CLASS 1 GROUP O. DIVISION 2 UNLESS OTHERWISE NOTEO SUPPLIER TO COMPLETE FORM BY FURNISHING INFORMAT'ON FOR BLANK SPACES SHEET. CCR 000016993 .OF. 1 SERVICE | CONDITIONS TEMPERATURE GAUGE Cconoco) Engineering Center Ponca City, Oklahoma Temperature Gauges and Thermowells pi akit LAtt-- VCM PROJECT 1 ITEM NO. < cc 2 SERVICE UJ z3 O 4 MANUFACTURER 5 FLUID tvw 6 FLUID STATE 7 PRESSURE. PSIG 8 TEMPERATURE. *F 9 10 STEM LOCATION 11 STEM LENGTH 12 DIAL RANGE. "F 13 STEM MATERIAL 14 CASE MATERIAL OPER MAX OPER MAX Vaw 31 tin 3A0 -423_______ \j<e*S<3b(jL '{h'ru ________________CO_____________________ O-- boo 15 WINOOW MATERIAL 16 ACCESSORIES 17 18 19 MOOEL NO. 20 DIAL SIZE: S ' 21 ELEMENT: BI-METALLIC 22 THREADED CONNECTION: 1/2'MALE NPT 23 STEM OIA: .250 ' 24 ACCURACY: PLUS OR MINUS 1 PERCENT OF RANGE 25 EXTERNAL ADJUSTMENT 26 BLACK LETTERING ON WHITE DIAL 27 28 29 1 30 TYPE: THRU OR FLG'D 31 FLANGE SIZE AND RATING 32 FLANGE MATERIAL 33 WELL CONSTRUCTION 34 WELL 80RE 35 WELL MATERIAL 36 LENGTH BELOW THO. OR FIG. 37 LAGGING EXTENSION 38 CAP AND CHAIN 39 f % n - 'bOO3' . C^s. 3/*'' *>04-$.$. 11 r _____________ N_o THERMOWELL 40 41 42 MODEL NO. 43 GAUGE CONN.: 1/2 * FEMALE NPT 44 PROCESS CONN : 1 ' MALE NPT 45 46 47 NOTES 48 49 50 51 SPECIFICATION DATA SHEET PROJECT NO. /? 2-SV a -tfi S3 - 7>'b'b> A.F.E. NO__________________________________ REQ. NO. ______________________________ DATE _/Q /5 APP'P RV MADE BY. Law P&ZSazG. tAM ~T&)ASfrg R - - CCR 000016994 ------- 4-720-S QUOTATION WILL NOT BE CONSIDERED IF MANUFACTURER DOES NOT COMPLETE FORM BY FURNISHING INFORMATION FOR BLANK SPACES SPEC NO. SHEET 3. - REV. 3 OF O 4-62 (conoco) Engineering Center Ponca City. Oklahoma Pressure Gages SPECIFICATION SHEET PROJECT NO. Q&3 '"PtTb A.F E. NO REO. NO. nATF /0/4-/85 APPO0Y MADE BY t TAG 2 NO. 3 P& 'i 4 5 6 7 S 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 3S 36 37 38 39 40 41 42 43 44 NOTES: REV. QUANT. / RANGE TUBE I DIAL n- /tic 1 n-ico | OPER. PRESS. 33psI<? rJ 1 1 1 ! 1 TEMPERATURE NORM. 1 MAX. 5*0 433"P 1 1 /** SERVICE ACCESSORIES ' NOTES 4-447-S QUOTATION wilt NOT BE CONSIDERED If MANUFACTURER OOES NOT COMPll tf FORM er FlMtNISHlNG INFORMATION FOR BLANK SPACES 441 oooox 6995 _____ SPEC NO ____ REV SHEET------- 4l. OF (conoco) SESTcEr . PI AMT LAMze CHd&t-^ ITEM NO. t -r- SERVICE i Soecification Sheet m=n datf tcl4-/&3 APP'nnv VCM project MADE BY ,_pPLP _ rfr/rss((<3. St^am V?AHsree\ vcm-l.ccp n. $ /JVO* 6s - SA^- J - I4/ -- &2 ~ (& ^ervicje : 33 / s^^zH'irsfQfd o-haw ^; Mrtnti'/: $rty)S~/r<rytn Coy <z<3clW. ) ^ "71- Mfide.C ; 5^r?Vr 20// /)n~/icjL -. 1 Fi-oiZ- C01 nec.Tftnt.S : ('Fnread^d) hhtmh*r j&Awirrd t 3 ^ i/Jssrk-LMOi Fbosh^) Prrccu re : 33x5-/^ ksIflY fp7^22i~c4jZ? t Z.2TO: T^zisr J --------------------------- *------ a--------- -------------------------------------------------------^ 7^ ^---------------------------- "7'j / $sl_f:>.r.1~T.{. ( 7etu'zx^rdTu,-^ ' A/Crtlts/' 3A ^ ^ Mr) Y Z-^b0 &S>t~ Ma Y. tH Lfwa ; Afrrrw&( ^3Afi F UrlX 4^ May: Ji/ov-,w6Gz, ?)60*o A/otw&L Flow ; /-SZ> /s, /h\~, ^ /)rr^2>`50r~fOS- : V- - w 0,0 422" ^-er'&rnt&d 3<9<S.S, 7 6 /2Aiom : / j Nori^rii -ft Y'J -v^y- pCarm-ty e^dctteus f<jf i f e1 / M. L.ipt*rh*?rt`T ' yirt Fry 2 Agg>n stpcP^i 3~f 3bC A-- f f <***/Jjoc.t'tcn*~ /d a^tcC'-tt'tcict 12") ZuS'fau xM&w -frays g-ifA Zti6 0 CCR 000016996 SPEC NO. -4- SHEET -5" REV. -OOP & 4-61 4-441-S Line Designation V+-CM-Z-H %-r.M-3-ri-6Z'C> (COnOCO^ V WI lvv*u7 Engineering Center Ponca City, Oklahoma Specification Sheet PROCESS PIPING SCHEDULE SPECIFICATION SHEET PROJECT NO. 'r A.F.E. NO_________________________ __ REQ. NO. / s\/r~ /ft : PLANT PHniPrT V*?//- LCC.P LWF*?rZZl< (/ SfFAU Service From To \/CM \Ze*rf~S TtQlAsfcj,- lc t\ u LC-CV Mrlr> (jr^de. t Flow V Rate 6} Press Normal At T and P Drop L Lb/Hr LB/CF Vise PSIG/ (Hot BPSD) F PSIG (SP GR) CP 100' V /O.noo ZbO 33 L ZSO flL) z^o 33 L zso {t> 33 L zso (t> ZPiO 33 ,/z.o bZ(oZ feZ- *ois4 / -' -_ * Vel ft/sec Ub -- - Fluid s/tf $&&***. %3p%j'- Coi--<d, ti ft Aio~rE$\ O) /tUrt. w$u.(&t?'&ns x^i. 'tckft'ess : 3 " . &) K/^r^iap <yn /u , () Etmi'-jattccs Spiral <=i?*?k.erfs Cty A/s-tf -fetotp =4-33*F) max *= Z-=?0 000016997