Document qaoexmnzz4xyr52nqdKKnj51G

(csnoco) Interoffice Communication To M. L. Ashby From S. W. Sommer Dare May 22, 1984 Subject R-101 TEMPERATURE CONTROL DESIGN NO. 202-100-584-SWS REVIEW ISSUE - Return Comments By June 8, 1984 Qld? MS --- YMF * sws -38R Attached is a class "A" design for the installation of a cooling water recirculation pump, a temperature controller and valve, and associated piping to control the temperature at the top of Direct Chlorination Reactor R-101 at 55C. Following the March, 1984, turnaround the temperature at the top of R-101 was 44C, due to the installation of a new, clean H-101 tube bundle. However, at this low temperature over 2500 ppm of 1,1,2-trichloroethane are produced in R-101, six times the maximum desired concentration. The new cooling water recirculation and control system will allow the temperature to be maintained at 55C, where the concentration of 1,1,2-trichloroethane will be 400 ppm or less. The temperature in R-101 is presently controlled by cutting the flow of cooling water to H-101 until the desired temperature in R-101 is achieved. Although the 1,1,2-trichloroethane concentration is reduced, the velocity of cooling water through H-101 is also reduced. At the lower cooling water velocities, the tubes in H-101 are more susceptible to severe fouling, pitting, and corrosion on the cooling water side than if the full flow of cooling water is maintained. It has been necessary to completely retube H-101 every three years at a total cost of $214,000. By recirculating a portion of the warm cooling water return, the temperature in R-101 can be maintained without reducing the flow of cooling water to H-101. By maintaining the maximum cooling water velocity in H-101, the shell side H-101 would foul and corrode less severely, thereby prolonging its life. This re circulation system potentially could extend the life of H-101 from three to four years, thus saving $17,500/yr. in average annual maintenance costs. Severe fouling in the past has limited the cooling capacity of H-101 to the point where full rates could not be maintained during the hot summer months. This project will help reduce the fouling in H-101, thereby helping to maintain the maximum possible cooling capacity of H-101 during the summer months. A portion of the H-101 cooling water return will be recirculated to the H-101 cooling water supply by H-101 Cooling Water Recirculation Pump, P-1. If not all of the recirculated water is necessary to maintain 55C in R-101, some of the P-1 discharge will be routed through R-101 Temperature Control Valve TCV-1 back to the H-101 cooling water return. J. C I ".It ^ K t$ t r 3 '/ u / -4 ' ,'a ^ $1 J r > \ V s~/ a w. 6^/y/ t ~( ? r t ,, J f rlc 7JC ;^ 2 V * ' 1 A. L U sH // T& I * ^ f si? y ^'1 i * / CWM 000008860 By copy of this design to 3. R. Holcomb, a cost estimate for budget purposes is requested. Tie-ins should be made during the First Quarter 1985 turnaround. If there are any questions, please call me at 5058. cc: RAC-JWW-RB-JRH(4)-MLA(4)-MCM-CRH(3)-SRA-PLF-DLD-JGC-PE I/.) i U c J'V' V e ; V4---fvw ? Xo C CWH 000008861 DESIGN BASIS In February, 1984, Direct Chlorination Reactor Cooler H-101 developed a tube leak, caused by severe pitting and corrosion of the tubes on the cooling water side. The tubes were also badly fouled. Because other cooling water exchangers had not experienced such severe damage, the problem in H-101 could be attributable to very low cooling water velocities through the exchanger. The design flow velocity through H-101 is only 0.628 ft/sec. at 7,700 gpm, whereas good exchanger design would have called for 3 ft./sec. (minimum). H-101 was retubed in February, 1984. Following retubing, the efficiency of H-101 increased and the' EDC temperature in R--101 decreased. The temperature in the top of R-101 was only 44C following the startup after the March, 1984, turnaround. At this temperature, the production, of 1,1,2-trichloroethane in R-101 increased by 2100 ppm, from 400 ppm to over 2500 ppm. (See Figure 1). The temperature in R-101 was increased slowly by approximately lC/day until the 1,1,2-tri- chloroethane concentration decreased. The 1,1,2-trichloroethane concentration did decrease back to 400 ppm, at an R-101 top temperature of approximately 55C (see Figure 2). Therefore, to avoid EDC product losses, R-101 must be run in the vicinity of 55C. At the 45C operation, 333 lbs./hr. of EDC production was lost due to conversion to 1,1,2-trichloroethane, based on an EDC production rate of 158.6M lbs./hr. (1.218MMM lbs./yr.). Operation of R-101 at higher -temperatures (greater than 55-58C) will moderately increase the amount of EDC vented from Crude EDC Tank T-101 to the incinerator (increase from 37.5 to about 45 lbs./hr.) while causing only a slight reduction in 1,1,2-trichloroethane concentration in R-101 (decrease from 400 to approximately 375 ppm) based on actual operating data taken during April and May, 1984. Therefore, to minimize total EDC losses, R-101 will be operated at about 55-58C. Presently, the temperature in R-101 is controlled by regulating the cooling water flow rate. An 18" butterfly valve on the H-101 cooling water supply is used to throttle the cooling water flow. For example, with a clean exchanger and 75F ambient temperatures, (cooling water temperature approximately 82F) only 75% of the design cooling water flow rate is needed. This only compounds the velocity problem through H-101. Operating for long periods of time with the ^___ cooljjiQ water-j^alve^tLlnched back is believed to have been the cause for the r latest;H-101 corrosion problems) and tube failure. Adequate temperatures in J R-101 plus maintaining the maximum cooling water flow rate through H-101 is it necessary to insure the maximum life of the tube bundle. > vp , ejj, s',A^y This design will provide for an H-101 Cooling Water Recirculation Pump to recycle up to 3500 gpm of the H-101 cooling water back through the exchanger. Mixing this warmer cooling water return with fresh cooling water will give a warmer cooling water supply to H-101. The warmer cooling water supply will cause a decrease in the heat transfered in H-101, resulting in a higher temperature in R-101, as desired, without reducing the velocity through H-101. If all 3500 gpm of cooling water need not be recycled to maintain 55C in the top of R-101, R-101 Temperature Control Valve will open to allow some of the cooling water to be routed back to the cooling water return line. During the hottest CUM 00000886 summer months when maximum cooling is required, it may be possible to shut the H-101 Cooling Water Circulation Pump off to save energy. A heat and material balance for the recycle system is shown in Table I. Installing this recirculation system could extend the life of H-101 from three to four (or more) years. Increasing the life of H-101 by one year will save an average of $17,500/yr. in maintenance costs, based on a cost of $214,000 to retube H-101 once. CUH OOC,0<>as6 O' wawmwMMlimniiwmi j* EEi-_ .ai ',aSH `"T" Ja k J 1 !v"j H H LO 0-4 5 IB 0-4,!JJ T. u . a: f-j Li .i 13 i ii I 4 s 9 CSS i^lTi css cm ess CSS CSS i^Ti css 1~*v*! ess >3!' r-" TT i--i i"i~i LfS 0-4 Ij'i -JU cm Si -a--} a i LfS T1 "? i i in -w--i a i Li 0-4 KS KS 0-4 0-4 0-4 -5--a t--a -:--a Udd 113 H W H JL 3OaO"1HJI dl-S " I " X C14H 000008864 I OlL \I\ !-- <C UL LU LL. LS_ i__i I-- I CN LU LkL __ * ii*:i i--i Ll. 'J H3Q dW3 dOl 10 T --a 00 ooo TABLE I. H-101 Cooling Water Recirculation Heat and Material Balance Recirculation Rate, 6PM (1) 0 500 1000 1500 2000 2500 3000 3500 CW Supply Temp., F (2) 82 83 84 85 86 87 88 89 Total Flow, GPM (3) 7705 7705 7705 7705 7705 7705 7705 7705 Heat Transfer MMBTU/Hr. (4) 57.9 54.1 50.2 46.3 42.5 38.6 34.7 30.9 Notes 1) Recirculation rate is controlled by R-101 Temperature Control Valve, TCV-1. 2) The cooling water supply is made up of fresh cooling water and recirculation cooling water. 3) Based on the full design flow rate. 4) Based on a fresh cooling water temperature of 82F, a constant heat transfer coefficient of 65.5 BTU/hr-Ft2-F, and a heat exchange area of 22,633 Ft2, and a constant recirculation temperature of 97F. 000003866 CUH PROCESS DESCRIPTION Cooling water will be circulated through Direct Chlorination Reactor Cooler H-101 at a rate of 7700 gpm. Of this rate, 3500 gpm will be recirculated by H-101 Cooling Water Recirculation Pump P-1. Warm cooling water return will be diverted to the P-1 suction line 10"-WH-1. The discharge of P-1 will be at a pressure of 75 psig. The recirculation water will then re-enter the H-101 cooling water supply line through line 8"-WH-3. Some of the P-1 discharge will be routed through line 8"-WH-2 back into the H-101 cooling water return line. The flow rate through line 8"-WH-2 will be regulated by R-101 Temperature Control Valve, TCV-1. TCV-1 will receive its control signal from Provox controller TIC-1, which will be set at 55C. Control will be based on the temperature at the top of R-101 (see Figure 2). 0000088^7 CV1H Energy Impact Statement This project will have very little effect on the total energy consumption of the VCM Plant. H-101 Cooling Water Circulation Pump P-1 will consume 0.2863MM KWH/yr. (2,863MM BTU/yr), or an increase of 0.083% in total plant energy consumption on the CMA basis. The Process Design Energy Checklist was completed and is included with this design. Environmental Impact Statement This project will have no effect on the environment. Safety & Health Impact Statement This project will have little effect on plant safety and health. Because of the large size of H-101 and the magnitude of the task to remove the exchanger, re placing H-101 less frequently will have a positive impact on safety. The Process Design Safety Checklist was completed and is included with this design. 000003868 CUB VCM PLANT PRQCES5 DESIGN ENERGY CHECK LIST DESIGN NO: 2Q2.-IOO-SS4--^sLOSi c Legend Item verified and action taken UJfC Item verified Out no action recuirec Item verified Out not economically feasible No action necessary I. INSULATION The economical insulation thickness was calculated and specified for the following equipment: A. Permanent Insulation iItem No./Thicknessfinches' B. Reusable Insulation 1. Tank 2. Vessel 3. Heat Exchangers 4. Piping* / / / s-u>u / o / / f / / / / / 1. Tank 2, Vessel 3. Heat Exchangers 4. Piping* In-LdtV O t / / // 5. Control Valves // 5. Control Valves 6. Process Valves ' / f / 7. Pioina to and from / ! ! Steam Traps. 6. Process Valves 7. Piping to and from Steam Traps. Item No . /Thickness^inches) / // / // / // /// / // /// / // / // /// Listed is only one 1ine of a set of piping that have the same diameter and contain the same fluid at an identical temperature. TURBINES AND ELECTRIC MOTORS cThe design considered the following provisions when specifying the type of drive for the listed equipment. Agitators/ Equipment Item Pumos Ccmoressors Mixers Blowers Fans >) High efficiency electric motors o) Variable speed and/or variable horsepower motors or turoines in order to provide flexibility Curing operations at low rates. :) Design specifies optimal motor phase and voltage (normal is 3 phase, 440V motors) y d) Space or coil heaters for motors are in cluded only wnen necessary. e) Steam or gas turbine (instead of an electric motor). |0P 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. c CUH 000006869 DESIGN NO: 2-0"Z" ( OO -SS*4 " III. ROTATING EQUIPMENT The cesicn consicered the following provisions when specifying the listed equipment. A. Pu'TOS Item No. B. Compressors 1) Use of a 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 comoarison of the turndown vs. minimum flow requirements. 4) Efficiency at the normal flow rate_ 5) Efficiency at the minimum expected rate * 0. y y .si Jo_ 1) Minimum/Maximum flow comoatible with varying production rates. 2) Parallel but different sizes econ omically feasible to provice flexioi1ity. 3) Efficiency at the normal flow rate* A) Efficiency at the minimum expected rate = 5) Comparison of single versus multi stage. C. Hixers/Aoitators Item ho. 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 consicered in the design of heat transfer equipment. A. General Considerations for ATI Types of Heat Transfer Ecuipnent c 1) Control instrumentation is included 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 HTR[ design methods can be used in the calculation. 4) Variation of the overall heat transfer coefficient versus turndown. 5) A sufficient allowance for fouling. 6) Using another process stream as a heating or cooling medium (interchanging). _______________ Item No. B. Reboilers and Steam Heaters Item ho. 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 h'o. 3) Economic comparison of a cooling water exchanger versus an air cooled 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 Refrac?ory(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. c CWH 00000S870 DESIGN NO: uy2. \ OO - "SslOS. c STEAM TRIPS Refer to Conoco Engineering Standard A-l5 for design specifications. !tsn No. 1) Trap sized for proper flowrate and safety factor 2) Condensate is to be returned to the return system when economically feasible. 3) PSI 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. VI. MONITORING INSTRUMENTATION The following items are necessary in order to monitor the energy usage of the designated item. A. Heat Exchanoer Number __________ 8. Pump Number 1) Shell and tube side inlet and outlet temperatures. 1) Suction and discharge pressure gauges. 2) Steam side pressure. 2) Outlet flow meter 3) Steam flow meter. =i C. Compressor Number D. Turbine Number 1) Inlet pressure and temperature gauges for eacn stage. 1) Inlet pressure and temperature gauges, 2) Discharge pressure and temperature gauges. ____________ 2) Outlet pressure and temperature gauges. 3) Inlet flow meters for each stage c 4) Discharge flow meter. 5) Recycle flow meter. ____________ ____________ MAINTENANCE CONSIDERATIONS A. Equipment Preparation for Maintenance Work Procedures are included for the most efficient method of emptying, clearing, purging, and/or regenerating process 'equipment included in the design. B. Maintenance _A11 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. fae6ftT\vJ impact. C CWH 0000887l DESIGN WQ: ZOZMOQ-SS^ ~SlOS ENERGY IVQ&CT STATEuiNT 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 = Q Ps*9 2) From the plant steam balance the equivalent 6CO pstg steam savings (usage) 3) CMA Energy factor for steam. 4) Total CMA Energy for steam saved (used). B. Electricity 1) The electricity saved (used) by the project. V\r./Hc. h'M Lbs/Yr f*"i km Lbs/Yr. x 1655 BTU/Lb. Q MM 8TU ----------------- tr. 0 3a) mm KWH/Yr. 2) CMA Energy factor for electricity. 3) Total CMA Energy for electricity saved (used). x 10,000 BTU/KWH ( ZyftfeSVl BTU C. Natural Gas 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). 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). 4) Additional ECC saved (lost). 5) Energy factor for EOC (obtain from energy coordinator). 6) Energy saved (lost) due to EEC savings (losses). 7) Additional HC1 saved (lost). 8) Energy factor for HC1. 9) Energy saved (lost) due to HC1 savings (lasses). 10) Total energy saved (lost) due to product recovery (loss). XL O MM Lbs/Yr. BTU/Lb. VCM MM BTU/Yr. _MM Lbs/Yr. _BTU/U>. EEC MM BTU/Yr. XL 2681.1 O _MM Ibs./Yr. BTU/Lb. HC1 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 EOC 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. Q MM SCF/Yr. X 1.040 BTU/SCf Q FM BTU Yr. Q 11 MM BTU ir. MM BTU/Yr, * 3,434,621 Wi BTU/Yr. x lOOt C-Q2S) ooooos07'3 cuv* VU, PLANT PROCESS DESIGN SAFETY CHECK LIST DESIGN NO: 2X>2-- lOO-Sft4-Su2S I. OVERPRESSURE PROTECTION A. Overpressure Design Basis Equipment was checked for conditions listed below. Overpressure protection designed for the condition indicated by a check. Pressure Vessels Item No. Exchangers Item No. 1 . Blocked Valve 2. Cooling Water Failure 3. Instrument Failure 4. External Fire 5. Other (Specify) Protection by RV-No. Alternate Protection Noted Below Rotating Equipment Item No. 1. Blocked Valve - Cold Fluid Vaporization 2. Blocked 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 Piping Line No. Blocked Discharge Valve Positive Disp. Pump Positive Disp. Compressor Steam Turbine Protection by RV-No. Blocked in Line Vaporization Thermal Expansion Protection by RV-No. PSvM\-Z- 8. Relief Valves Relief valves and inlet and outlet piping specifications were checked for the following conditions Relief Valve Number Psd-no. 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 OVL II. VESSEL CLEARING CWH 000008873 A. Clearing Connections Clearing of equipment containing toxic or regulated vapors and liquids is provided for as follows: Vessels Exchangers _____ Equipment Item Contents ________ ________ _______ _____ ________ _______ Wuo Pumps 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 Clearing/Draining/Purging ________ ________ ________ ________ ________ ________ ________ _________ ________ ________ ________ ________ ________ ________ ________ _________ ________ ________ ________ _____ _____ ________ ________ _____ _____ ________ ________ _____ ________ ________________________ ______ ________ ________ ________ ______ _________ ________ ________ _____ ________ ________ ________ ________ ________ ________ ________ I \/ Page 1 of 4 Others REV.l - 3/81 DESIGN NO; *2-02-1 CO~Sft4-.SlPS 8. Prevention of Backflow Nitrogen connections for clearing equipment Items and lines are protected against backflow as follows: Vessels___________________ Exchangers ________ Pumps____________ ________ Others Equipment Item 1. Check Valve in Permanent Ng Line 2. Hose Connection with ChecxValve 3. System Pressure <40 psig, Hoses to be Disconnected After Purge III. MECHANICAL & MAINTENANCE CONSIDERATIONS A. Plant Design Standards are more restrictive than company standards in several areas. Notes have been included as required in the following areas: 1. Gaskets Gasket Per Plant Standard J ______ ______ ______ Garlock 900 Round Flexitallic Spiral Wound TFE Envelope - Ring Gasket TFE Envelope - Full Face Piping Description CS, SS, Nickel, Monel Piping Steam & Condensate Service Lined Piping FRP & Furan Applicable Piping Specifications A2-1 , A2-7, A10-1, A13-4, A20-1, A21-1, B2-1 , B2-12, 813-1 , B13-3 A2-3, B2-6, D2--5 X25-2, X26-2, X27-1 R37-1, R37-3 2. Materials of Construction--Design notes have been included for: Electric driven equipment specifying no 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 and the required specifications and notes have been included: Equipment No. P-l Minimum Flow Requirements Shaft Seals--Type S Required Lubr./Flush y/ C. Tie-in Points to existing piping or equipment have been located, verified, and denoted if they are turnaround items. D. Preventive Maintenance o-. Notes have been Included on any new equipment that requires special PM to ensure safe operation. CWH 0 0 0 0 0 (3 8 Page 2 of 4 REV.1 - 3/81 DESIGN NQ. 2-67.- fop - S'gH-StOS IV. PERSONNEL EXPOSURE & PROTECTION A. Employee Exposure ______ Design has been checked from a personnel exposure standpoint to ensure that during normal operations, clearing for maintenance, or maintenance activity employee exposure Is within regulations. B. 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 has been specified for hot lines (?150F) where necessary. D. Accessibility of Valves ft Instruments ' Notes have been included to ensure that valves, instruments, motors, etc. are accessible from grade or platform to permit operation and maintenance. E. Hoi se Liini ts y Specifications of equipment have been checked or noted to ensure meeting noise limits as set by Standards H-7 (control valves) A X-5 (general). F. Spill Containment A 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 has been checked for the proposed location and provisions for any required new lighting have been included. H. Connnunicotions System ______ Provisions for additional communications system lines have been included as necessary. Page 3 of 4 s> REV.1 - 3/81 DESIQN NQ? 'ZQ`2.- 1 cq-Sb4-SuOS V. PREVENTION OF POTENTIAL HAZARDS A. Emergency Shutdown Requirements Design specifications, considerations, and notes have been made as necessary for the following items: J 1. c2. ______ 3. ______ 4. Control valve failure position in event of air and/or electrical loss has been noted on spec, sheet and P&I. Spare equipment has been provided as needed and verified with Operations. Required alarms and their set points have been confirmed with Operations. 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. 2. 3. 4. System flammability (both process streams and materials of construction) under normal and upset conditions. Provision for inert or nonflammable atmosphere such as nitrogen blanketing or purging. Need for flame arrestors to prevent flashbacks. Need for additional fire protection systems such as sprinklers, types of extinguishers,etc. C. Electrical Grounding/Bonding of vessels, pumps, and piping has been included as required to dissipate build-up of static charge. D. Locked or Chained Valves ______ Notes have been included on the P&I for valves that must be locked or chained opened or closed for safety reasons. E. Chemistry of Mixing Streams has been checked to ensure that chemical reactions will not create a potentially hazardous situation. F. Minimum Clearances of new equipment from existing equipment and structures have been checked with Standard X-3 and design notes included where required. oo oo Page 4 of 4 CO 03 NJ Legend \/ OK ~ '_____ Item verified as stated and specified action taken. Item verified but no action required. Item not applicable. No action taken. REV.1 - 3/81 CWH WORK LIST Refer to Drawing No. VCM-202-1. 1) Pour a foundation for H-101 Cooling Water Circulation Pump P-1 in the area just northwest of Direct Chlorination Reactor R-101. See Drawing No. VCM-202-3. 2) Install H-101 Cooling Water Circulation Pump P-1 on the new foundation. 3) Install an 18" globe valve in the H-101 cooling water return line (18"-WH-5-N-A2-l) downstream of the existing 18" globe valve in line 18"-WH-5. Locate the new 18" valve in an accessible location west of R-101. 4) Run line 10"-WH-1-N-A2-1 from the H-101 cooling water return line (18"-WH-5-N-A2-l) downstream of the existing 18" globe valve and upstream of the new 18" globe valve to the suction of P-1. Install a 10" gate valve, a 2" bleed valve, and a pressure gauge on line 10"-WH-1. 5) Run line 8"-WH-2-N-A2-l from the discharge of P-1 to the H-101 cooling water return line downstream of the new 18" globe valve on line 18"-WH-5. Install H-101 Cooling Water Temperature control valve TCV-1 in line 8"-WH-2. Install two 8" gate valves, an 8" check valve, two 2" bleed valves, and a pressure gauge in line 8"-WH-2. 6) Run line 8"-WH-3-N-A2-l from line 8"-WH-2-N-A2-l downstream of the 8" gate valve and upstream of TCV-1. Install an 8" gate valve in line 8"-WH-3. 7) Install R-101 Temperature Controller TIC-1 (Provox) in the rack room. TIC-1 will be located in cabinet 1-1, DC #1 (Device 6), File #3, and Slot #7. Jumper the voltage inputs from Temperature Transmitter TT-104-1 (Mux #1 (Device 21), File #2, Slot #5, Terminals 5 and 6) to analog input #1 of TIC-1 (Terminals 1 and 2). Refer to Drawing No. VCM-202-2. Configure TIC-1 and download the configuration. CWH 000003877 TIE-IN LIST Refer to Drawing No. VCM-202-1. All tie-ins below require a cooling water system shutdown and are, therefore, turnaround items. 1) Tie-in line 10'1-WH-1-N-A2-1 to the H-101 cooling water return line (18"-WH-5-N-A2-l) downstream of the 18" globe valve and upstream of the new 18" globe valve. 2) Tie-in line 8"-WH-2-N-A2-l to the H-101 cooling water return line (18"-WH-5-N-A2-l) downstream of the new 18" globe valve. 3) Tie-in line 8"-WH-3-N-A2-l to the H-101 cooling water supply line (l8,,-WC-4-N-A2-l) upstream of the 18" butterfly valve. CUH 000008878 (conoco) Engineering Center Ponca City, Oklahoma Control Valves SPECIFICATION DATA SHEET PROJECT NO- -'SS4<-ScOta A.F.E. NO REQ. NO DATE S/io/frA APP'D BY MADE BY SlOS GENERAL PR O C ESS D A T A A N D SIZIN G 1 TAG NO. 2 SERVICE 3 MOOEL NO. 4 LINE NO. 5 LINE SIZE/SCHEO. NO. 6 FLUIO Tc\}-\ CCt JTK-Of- IbOO AL-ASS 2% "-tOA.- 1 - rJ-AI-l P" S^H.4o mftu- 7 TEMP. NORMAL 8 PRESS. NORMAL 9 APMIN.RATE | MAX. MAX. NOR. RATE | MAX. HATE as so *3 15 no 85 15 1 10 MAX. SHUTOFF P 11 RATE MIN. 12 RATE NOR. ^ QtA 13 RATE MAX. 14 VALVE CV MAX. 15 SP. GR. 60`F 16 OPER. VISC. 17 % SUPERHEAT ' CV CV CV AP (ALLOW) MOL. WT. % FLASH A SOLIO 13 o 4440 eieo ,-- 1 fk 1 ST 1A 18 VAPOR PRESS. F.T.f**/^ CRIT. PHESS. PSIA %19 WEIGHT VAPOR IN 1 OUT 20 PRED. SNO. LEV.(I) RATE o a 21 MAX. ALLOW. SNO.(I) 2i RATE 23 MFR 24 TYPE OF BODY "25 BODY SIZE | MODEL GUIDING ftSKeja. 1 nboo ?LA*& 2. PiSttTfttl 26 PORT SIZE 27 ENO CONN & ANSI CLASS 26 BODY MATERIAL 29 PACKING MATERIAL 30 BONNET TYPE 31 TRIM FORM 32 CV FULL OPEN 33 LUBRICATOR | ISO. VAL 34 TRAVEL INDICATOR NO. OF PORTS Full J_ Zoo**- JZ.f. O-S. -Tf= StCs ca. peacEiO-r 2440 iOo ! fOo 35 % VALVE OPENING AT MIN./MAX. CV 36 TRIM MATERIAL SEAT/VH 37 STEM/SHAFT MTL 38 REQUIRED SEAT TIGHTNESSI2) 39 {ZcmAmoki frrr t-vfc*. FuxO 40 MFR MODEL 41 TYPE 42 CLOSE AT SIZE OPEN AT 43 FLOW ACTION TO OPEN/CLOSE 44 FAIL POSITION 45 HANDWHEEL (SIDE/TOP) 46 MFR. MODEL NO. 47 INPUT SIGNAL OUTPUT SIGNAL 48 AIR SUPPLY PRESS. MAX. \0* /`To* C.Sgr.s,____________ AO> CJ-AS'b & 13P bjAP4t2A4(4 \S_PSJ6l_ 3_psiccup^e __ - _______ Or? ^-IS PSIfr 'i-lno PSJ6. 49 FILTER REGULATOR 50 GAGES 51 | BYPASS Uo ___ 52 53 54 55 356 1. SOUND LEVEL IN OBA MEASURED FT. FROM CONNECTED PIPING. 57 2. ANSI 816.104 (CURRENT ISSUED) LEAKAGE SPECIFICATIONS. 58 1 1 1 1 1 11 1 1 1 w 1 1 OOOGOSF 79 BODY ACTUATOR QUOTATION WILL NOT BE CONSIDERED IF MANUFACTURER DOES NOT COMPLETE FORM 0Y FURNISHING INFORMATION FOR BLANK SPACES. SPEC NO. SHEET_ REV. _Q_ OF-S- 4-82 4-435*S 1NOTES 1OPTIONS 1 POSITIONER [Conoco) Engineering Center ponca Citv> Ok|ahoma Indicators, Recorders, Controllers (Receiver Instruments) specification data sheet project NO. -Za-z.-toa~s-s-f-sus A.F.E. NO. OCn TMtf^M/^4 iPPnnv pi ant , MCK ,, 'P'^AtOT" projfct P'-'Ot WAOF RV CoJn^i . GENERAL 1 j ITEM NO. 2 I SERVICE 31 4 manufacturer 5 MODEL NO. 6 | INSTRUMENT FUNCTION 7 | INSTRUMENT MOUNTING 8 | ELECTRICAL CLASSIFICATION 9 | POWER SUPPLY 10 | INPUT SIGNAL 11 | ACCURACY 12 | REPEATABILITY -Tic-4_______________ 1 -i i -*rr temp. <*(3fJTT2oi . Fr4,He=7Z- >(2. &ulO. CLIOOIXI-AI 'TE?ap. r.nro-ne-oi ?o\Jcr*. (4 -zo ^ >> 1 1 l 1 1 D E S IG N D E T A ILS 1N D IC A T O R -R E C O R O E R C O N TR O LLE R J2J 14 | 15 i 1 6 | NO. OF PENS OR POINTERS 1 7 | SCALE RANGE 1 8 | CHART SIZE AND TYPE 19 | CHART RANGE 20 | CHART NUMBER 21 jCHART FACTOR f _______ o-zoo c 1 1 i 1 22 1 CHART DRIVE 23 | 24 1 25 1 CONTROL MOOE (SEE LINE 26 1 CONTROLLER ACTION ________p.V/.PiO/'x______________ 1 i 27 | SCALE RANGE 28 I SET POINT AOJ.: MAN,--REMOTE 29 | AUTO --MAN. SWITCH AND ADJ. 30 | OUTPUT SIGNAL 31 j O-Zoo C. _________ 4-zoma 32 i 33 | ALARM FUNCTION 34 QUANTITY ANO FORM 35 | CONTACT RATING 36 | DEsDl fmoj ___ % PF~ 37 l 38 39 40 41 42 43 44 | CONTROL MOOES: P - PROPORTIONAL IGAINI, 1 INTEGRAL (RESET), D - DERIVATIVE (RATE). BIAS. GAP, RATIO. BATCH 45 | RECORDER IN< SUPPLY: CAPILLARY WITH 6 MONTHS MIN. SUPPLY. 46 'Cr> PEoOCWL . LoC/VTl OrJ ikA (Zj^-<LiC I2omA Tn TP^=". 471 'RM rcosTsuPeitoKiia. 43 ^rOPa^-m ^LApPUieO FiZoM TT-toM-l (rCi.^tioA 49 | -r*STr=-j2_M - 50 1 51 1 52 1 CUH 000003880______ A C C E S S O R IE S A L A R M S NOTES OUOTATlONWni NTtT RF C/-wiCllNFOFn IF MANUFACTURER DOES NOT COMPLETE FORM 8Y FURNISHING INFORMATION FOR Rl AN* <SOire^ SPEC NO. ^HFFT REV. O fic ^ 4439-S 7*82 PRoVOX V. ) CONFIGURABLE CONTROLLER CONFIGURATION CUSTOMER PLANT \)cLT-\ 'PC^JT' P.0. NUMBER Cassia J. fOo . 7-OZ- 1 CONTROLLER SPECIFICATION MODEL NO: CL3_ Q. .Q 1 -A_l ..-B -C -D CONTROLLER SPEC SHEET NO. OPERATOR STATION SPEC SHEET NO. PROCESS DESCRIPTION CL W(3RKSHEFT# _^ nf ^ DOCU MENT NUMBER /ft4DATE f=7j/l4 ENGir4EEH DATE REVISIONS ENG. COMMENTS CUH 000008881 POINT TAG NAME <~T \ 1 IC. FUNCTION DATE ,jl_l i i i i ENGINEERING UNITS (ELJi i PiTi<a i iCLi i CONTROL IMPLEMENTATION CHECK-OUT STATUS ENG. COMMENTS FUNCTION DATE ENG. COMMENTS' DOCUMENTATION REVISION CONFIG T^NE DATA ENTRY TUNER CONSOLE DATA CHECK j/)K STORAGE CARD ID NO. DISKETTE NO. DOWNLOAD / TUNER CONSOLE X TUNER CONFIGURED / \ CONFIGURATION PARAMETERS TUNING PA^METERS STEP# ''PARAMETER 1 P<XST 2 FF ENX CR? VALUE VALID RANGE 1 12 NO YES STEP# 1 2 PARAMETER EU 0% (EU) EU 100%~~{EU) Cf(? VALUE / ^------ VALID RANGE -99999 99999 -99999 99999 3 FF FIL? \ 2Y NO YES 3 GAIN (k) X 0 128 4 FF SORT? ^ nY NO YES 5 RESET (R/M) X 5 PV FIL? \ NO YES 6 RATE (min)/' 6 PV SORT? 7 SPT MAN? \ NO _x NO YES YES 7 RAMP TJjtf (min) 8 PV FptVI (min) 8 SPT DDC? \ NO YES 9 REDACT? 9 VOT ENB? 10 VOT MAN? 9Y X YES NO 4 nYES 10 y6iC CLO? v ALM A (EU) 11 OVERIDE? NO Xs A ALM B (EU) 12 ALM BHI? NO YES\ <13 ALM C (EU) 13 ALM CHI? NO X4 ALM DBND (EU) 14 DO ALMB? NO yts 16\ SP LO Limit (EU) 15 WTCHDOG? NO , ' YES 17 Xs HI Limit (EU) 16Y 5Y 0 0 0 0 'NO NO 0 -16 -16 0 -13.97 -13.97 293 895 56 1.8 YES YES 136 136 136 136 113.97 113.97 16 TR RAMP? 17 MV1 SIG? 18 MV2 SIG? Np< /Uo NO YES YES YES 18 VOXp Limit (%) 19 VO HlXpit {%) 20 ARW LO l3hgt {%) -13.97 -13.97 -13.97 113.97 113.97 113.97 19 MV3 SIG? NO YES 21 ARW HI LimitX) -13.97 113.97 20 MV4 SIG? 21 HI SEL? / /22 RST LSP? 23 RST LMD? / 24 RST LVQT' 25 RST J/6l? 26 T&/&QRT? 9Y 27 /TK FIL? 9Y NO YES NO YES NO YES NO YES NO YES NO YES NO YES NO YES 22 FF GAIN (k) \ 2Y 23 FF REV? X 2Y 24 FFFTIM (min) XY 25 TKFTIM (min) 27^ 26 WTCHDOG TIMER (min) 15Y 27 BACKUP MODE (Code) 1 5Y 28 RESTART MODE (Code) 23N 29 RESTART VO (%) 24 N 30 RESTART SP (EU) 22N 01 NO YES 0 112 0 112 0 \ V-X 56 2 5 113.97 -13.9N J 13.97 31 RESTART BIAS (%) 25N -13.97 1X-97 Forni FM4.2:C16201 (WS) Cktob< 1981 Prints in U.S.A. PCA/STATION TYPE ENTRY CODES MANUAL AUTO/MAN AUTO/M AN/RSP AUTO/MAN/SUP AUTO/MAN/DDC MAN/DDC PCA DEFINITION CONT. QLD NO. SELECTION COMMENTS 1 ^OO 2o 3 4 4o e.u o z. SP. Rifen >F u-oco nr*rr 5 izeu DUA<mr>J 6 PO IP f-tPcP? 7 feSTAR-T LAST SP7 1 2 3 4 15 CONSOLEENTERED CODE MANUAL LOADER BIAS & GAIN SIGNAL SELECT PD/P PI/PI D/I 11 10 g 12 8 76 5 432 1 rUNERENTERE D CODE MODE ENTRY CODES (TUNER ENTERED) STATION MODE MANUAL AUTO REMOTE SET POINT (RSP) SUPERVISORY (SUP) DIRECT DIGITAL CONTROL |DDC) CODE 1 2 3 4 5 CONSOLE CONFIGURED T TD ArPPgQ^JAO OF X*g SUPv/ 8 9 IOS 10 11 4-.o 12 f-o 13 14 -=p Al^tO Ll^lT HlLh\ Lt m. rT i n J iz-Are 15 STATION DEFINITION STATION TYPE |TYPE NO. QLD NO. SELECTION COMMENTS 1 lOf^ top Hr<b.u Ui^rr 2 -S IMP LouJ Cli-MT 3 3 rx*>j. At_Ar-nz-iP 4 L-CcO AeAnLrn Q. 5 O At A-fS't-A R "FiLiP 6 His. 14 Art .A-^rA C 7 ^n A-i . A-i^r-A. <*. TTZ-VP 8 At_PrfL+A DDfVhRAKlr) 9 NiO AUrA R TD DO l7 10 iAc.oPeu/cLose. 11 rOo Ge^mer last wodp? 12 tM A>1 ej&'rrveT Kooe. 13 Po LAST \\3P? 14 IOO NP. 15 HWY NO. I 2. i (1 through 8) Reference Only 16 17 CIA NO. 0,L DEVICETYPE (1 through 30) DATACONC. 18 19 20 PSEUDO FST DEFINITION DEVICE NAME llSlC 1^ I lj QLD NO. SELECTION 1 fOO DATA CONC. PORT NO: I I I .Si (1 through 1 6) 2 3 cOO -- POINT TAG NO. rr. 11Ci-,i 4 fOo 5-- PCA DEFINITION 6 7 NFS PCA TYPE pi/piq/x PCA NO. 8 0-olS 9 rOo COMMENTS FF GtiOfVfeLF? PF lO Pula' Ff= lop. FiL-TCnL'TiMe. FF IcJPUT 50.(2.. FF > AcnJG fF (5iAria p\) irOPL/rr Fu.rrerL? i ro Purr p u ta PM iOPuht <>... F^kI? POINT I \ |Q,\ I ,n~.g:trAi Pi 1 DESCRIPTOR iC.i_Oir\Oti-T&ifoOi,Li i i i i i i POINT ADDRESS lO |Z.| - I___ L (Reference Only) i - i Of 1 i ENG.N EERING UNIT \V> (EU) DESCRIPTOR iC j___i 10 1 12 13 14 15 16 17 rOo fOo Oo fOo -- VAo OUTFucr "nLALLiLL,7 output -n^AtckL oOeyLv c^. eWPYeLE.? T^L lOPWT F(LTSe_? " TraALtLFierce TltA-e._______ -reprCLL LUr! OOOOO-Juo^ 4 OF c?".___________ _____________ 1 (conoco) Engineering Center Ponca City. Oklahoma SPECIFICATION DATA SHEET PROJECT ND ZOZ-- ICOA.F.E. No Centrifugal Pumps REQ. NO- DATE. sAo/t-A APP'D BY- PLANT- hJT MADE BY_ PPrilFCT .-VQl TgrMPg-fg.^VTVAge CO^JTUOL 1 APPLICABLE TO: ST ESTIMATE p- --1_ O PURCHASE O AS BUILT O ITEM NO. 2 BfsERYice 14-lci 0/v;i_iO6 rti.o < 3 # LOCATION BL-OC.U- X. * !0FP4L 12.-101 ^.MANUFACTURER tXi (ZC O <T(Z. HO.SC REQUIRED ^ < Ul 4 MOTOR DRIVE f> , ftfio j??r\ * O TURBINE 5LU PUMP IS TO BE MANUFACTURED IN ACCORDANCE WITH THE FOLLOWING STDS.: O API 610 XANSIB73.1 OANSIB73.2 6 PUMPStZE I OX.&- \UU TYPE TT -* NO. STAGES A 7 NOTE: O INDICATES INFORMATION TO BE COMPLETED BY PURCHASER BY MANUFACTURER 8 SfLiouio L^Prrea. 9 'gi PUMPING TEMPERATURE <"F): NORM. MAX. H Cl 10 SPECIFIC GRAVrTY @ PT V) z 11 VAPOR PRESSURE @PTi*m o 12 VISCOSITY @ PT: WO .v. ^ \\c fO.RlSOcp"^ O NPSH AVAILABLE (fl) (3.^ O CAPACITY @ PT (US gpm): NORM. SSOQ O DISCHARGE PRESSURE (psig)MA)C loU O SUCTION PRESSURE (psig): MAX. ft 5 RATED ZTlSd UAH-Ef} "}< RATED .. f *%> o 13 o 14 o 15 oz 16 < 17 X Ui 18 o 19 20 21 22 23 .24 u 25 < 26 c 27 28 UJ 29 30 31 32 33 34 35 36 37 38 39 40 z 41 o 42 o 43 c 44 {/) 45 o 46 47 48 49 50 51 52 53 54 55 56 54 SITE AMBIENT TEMPERATURE (*F): O UNUSUAL CONDITIONS MAX. )nf\ MIN. 5~ O CORROSION/EROSION CAUSED BY REMARKS: HPROPOSAL CURVE NO. MTT S4^\| SSPEEDfrpm) "7-5H.NPSH REQUIRED <WATER)m) a RATED bhp El MAXIMUM bhp WITH RATED IMPELLER 52. (>^MAXIMUM HEAD WITH RATED IMPELLER f,T REMARKS: S* * 4 * * *r>o Kicrr iT to nje^icso^ CASING MOUNT: Si CENTERLINE O NEAR CENTERLINE O FOOT O VERTICAL O IN UNE O BRACKET 0 VERTICAL BARREL 0 SUMP PUMP O OTHER CASING SPLIT: AXIAL 0 RADIAL CASING TYPE: VOLUTE SINGLE STAGGERED DIFFUSER O DOUBLE MAXIMUM ALLOWABLE PRESSURE: paig @ 60 F psig @ PT HYDROSTATIC TEST PRES5URE: paig IMPELLER DIAMETER (in.): H RATED ^MAXIMUM i(o`' RMINIMUM l2>'* IMPELLER MOUNT: BETWEEN BEARINGS OVERHUNG PACKING: MANUFACTURER TYPE SIZE/NO. OF RINGS MECHANICAL SEAL: 5*mfr. reAi-fe oe. F3uiiJ- MODEL I f-V, l MFR. CODE API CLASS CODE GLAND TYPE/MATERIAL REMARKS: O DIFFERENTIAL PRESSURE (pi) /fq ) ' AT 4 rjLPATTO O DIFFERENTIAL HEAD (II) 44AT DGStforJ (''APACtTS O HYDRAULIC hp iX\ .U A LOCATION: O INDOOR ^OUTDOOR O HEATED O WITH ROOF Idtn, AX?a . OCjJNHEATED ^WITHOUT ROOF I U~/f)l MINIMUM CONTINUOUS FLOW (US gpm): THERMAL STABLE ROTATION (VIEWED FROM COUPLING END) CW CCW SUCTION SPECIFIC SPEED (%)^EFFICIENCY (AT NORMAL CAP. AND RATED SUCT. PRESS.) 5?^ LS* NOZZLES SUCTION DISCHARGE SIZE J5 IO S? 6 RATING JS. 1-T-r*fc LSD*** FACING EP * fc-p LOCATION BEARINGS (TYPE/NO.): RADIAL LUBRICATION TYPE: RING OIL FLOOD THRUST OIL MIST FUNGER PRESSURE -ut COUPLING: MANUFACTURER TYPE MOOEL DRIVER HALF-COUPUNG MANUFACTURED BY: BfPUMP MANUFACTURER O DRIVER MANUFACTURER O PURCHASER GLAND PLATE TAPS REOUIHED: O QUENCH O FLUSH REMARKS: O DRAIN O VENT WEIGHT OF PUMP AND BASEPLATE (lb*) WEIGHT OF MOTOR (lbs) WEIGHT OF TURBINE (tea) HUH 000008883'" 4-424-SI QUOTATION WttX NOT BE CONSIDERED IF MANUFACTURER DOES NOT COMPLETE FORM BY FURNISHING INFORMATION FOR BLANK SPACES 6-62 SPEC NO. SHEET _ REV. OF , 3- (conoco) Engineering Center Ponca City, Oklahoma SPECIFICATION DATA SHEET PROJECT Nft.to3- A.F.E. No. PI AMT ViCM ?L/VrJT Centrifugal Pumps PROJECT 12.-10 \ REQ. NO- DATF SAoJtA APP'D 8Y- MADE RY -Su3S cMpgg.^i2 CDtJTiiOU 1 C SEAL FLUSH PIPING PLAN MATL z 2 O AUXILIARY FLUSH PLAN MATL CL 3 SEAL FLUSH PIPING: O THREADED C SOCKET WELDED O FLANGED >- 4 O EXTERNAL SEAL FLUSH FLUID REQUIRED <5 US gpm O psig 6 REMAHKS: 7 8 O COOLING-WATER PIPING PLAN MATL TOTAL COOLING WATER REQUIRED (US Qpm) O SIGHT FLOW INDICATORS REQUIRED 0 PACKING COOLING INJECTION REQUIRED US gpm ps>g 9 O TABLE E-1 CLASS (PER API 610) ifi 10 Xbarrel/case C.S. < 11 >3 INNER CASE PARTS E UJ 12 IMPELLER S.S. 13 53 CASE/IMPELLER WEAR RINGS S 14 REMARKS: .S . .B'SHAFT/SLEEVE s.s. BASEPLATE (MATERIAL/TYPE) API STANDARD 610 STANOAHD BASEPLATE NO. ANSI B73.1 STANDARD BASEPLATE NO. 15 tn 16 TEST NONWITNESSED (A 17 PERFORMANCE O WITNESSED O OBSERVED O H 18 HYDROSTATIC O O O o 19 NPSH O OO < 20 O SHOP INSPECTION O MATERIAL CERTIFICATION Z o 21 O DISMANTLE AND INSPECT AFTER TEST p 22 O CASTING REPAIR PROCEDURE APPROVAL UJ 23 REMARKS: <n 24 O INSPECTION REQUIRED FOR NOZZLE WELDS: O MAGNETIC PARTICLE O DYE PENETRANT 0 INSPECTION REQUIRED FOR CASTINGS: O RADIOGRAPHIC O ULTRASONIC O INSPECTION REQUIREO FOR O MAGNETIC PARTICLE 0 DYE PENENETRANT O RADIOGRAPHIC O ULTRASONIC 25 26 O MOTOR DRIVER BY 27 O ITEM NO. O MTO BY 28 55. hp *70 ^rpm^oq frame 0 ITEM NO. HP RPM O TURBINE DRIVER BY O MTD BY MATL 29 < i<- Q 30 31 O MFR OR COMPANY APPVO. EQUAL O TYPE O INSUL OC 32 RENC O TEMP RISE C. /C.O> 33 5(VOLTS/PHASE/HERT2 AjfcjO/3 GC O 34 BEARINGS ' LUBE 35 FULL LOAD AMPS O TYPE O INLET STEAM, ps>g O TEMP F. O EXHAUST, ps>g STEAM RATE, FL to/BHP/HR BEARINGS LUBE NOZZLES SIZE ANSI RATING FACING POSITION INLET 36 37 REMARKS: t+l6*+ T=FuMer-arM hVotd^. GPOU 1 EXHAUST 38 _______________ LOiTU UOV^LUMI^LI^ Pft-gTS._______________________________________________________ 39 V) 40 2 41 O PIT OR SUMP DEPTH (in.) '-prXyfifi MINIMUM SUBMERGENCE REOUlfeED (in.) COLUMN PIPE O FLANGED (vKOfH FIXSl hfUrf . FLOAT AND ROO At- -- e0iTlL-%. r.cfl BON STEEL TfiflEADEO 0 FLOAT SWITCH O STAINLESS STEEL 0 BRONZE O NONE 0. 42 LINE SHAFT O OPEN ENCLOSED PUMP THRUST (fes): < 43 GUIDE BUSHINGS icU=cJ 44 45 > 46 BOWL GUIDE BUSHING LUBE REMARKS: UNE SHAFT WATER OIL GREASE AT MINIMUM FLOW AT RUNOUT: UP AT DESIGN FLOW DOWN 47 < 48 DELIVERY, WEEKS < 49 PUMP PRICE 50 0RIVER PRICE (/) o 51 EST. FREIGHT o 52 TOTAL PRICE 53 THE SOUND LEVELS GENERATED BY THE PUMP AND DRIVER SHALL BE WITHIN THE LIMITS OF THE ATTACHED SPECIFICATION. HUJ- 54 o 55 56 000008884 4-424-S2 QUOTATION WILL NOT BE CONSIDERED IF MANUFACTURER DOES NOT COMPLETE FORM BY FURNISHING INFORMATION FOR BLANK SPACES SPEC NO_____ SHEET ____ ie REV. O OF _3 6-62 fi fcrfm Mo 42 l?MI (conoco) Engineering Center Ponca City. Oklahoma Pressure Gages SPECIFICATION SHEET PROJECT NO. -Ott- APE. NO. _ PEQ NO DATF APPO0Y MAOE BY _____________________________ 1 TAG RANGE (.pyO OPER. TEMPERATURE 2 NO. REV. QUANT. TUBE OIAL PRESS. NORM. MAX. SERVICE .xetiaeniea. 3 P6'l Q 4 PA-2. o S 1 1 0-1150 O- ISO IS AS J to ClOOLIrJU 10/VTE32J - UrJe lo'-wiU-l 0-\50 n-iso ns es im f'nnu\k."X> tO/YrraZJ P>t-lrJRP -voO-7 NOTES 6 7 8 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 35 36 37 38 39 40 41 42 \ 43 ! 44 MOTES: 45 46 47 48 49 50 CUIH OOOOOSf 86---- 51 QUOTATION will not BE CONSIDERED If MANUFACTURER DOES NO! COMPlf fF FORM 0V FURNISHING INFORMATION FOR BLANK 5PACFS SPEC NO____ SSHEET REV. O OP 4-81 4-447-S t i ; . . ' . * f SHser `1 o F ^ (conoco) Engineering Center Ponca City. Oklahoma Specification Sheet PROCESS PIPING SCHEDULE SPECIFICATION SHEET PROJECT NO. LOO A.F.E, NO_ neo. no_ DATE g/i4/&4 APP D BY --ZzUS5> MADE BY _____________________________. Line Designation Service From To H-\ot <LvOfc_ P-\ r-\ 8" - tOvi-3- hi-A2- \ lime w-iot ooie. H-to\ ClOS Flow V fife L _ ??SPO L 3>si>o L_ 3x500 Press Normal At T and P Drop LB/CF Vise PSIG/ F PSIG (SP GR) CP 100* Vel ft/se c Fluid SS IS 65 "75 fcZ.l A7..1 "Z-3.S -ft* -in -8i% "MS l4.ZA* ZZ.34\ -ZZ.34\ COC>L\*y~> toATg. OOOL-i 06% xOfTyEPfc. )0otE -A TO I ^ <^A-ooc tr ^Oo (20 cUOfl > P '1/2- A' SPOL - vieiK n sr o o; o o CO CO N* . BOUNINS 40-514 57340 *3 ......> "'V !>**.vk t