Document nkkKD073neQ776J1obo333J5G

Cconoco) Interoffice Communication To J R. Holcomb From W, D. Stutesman Date March 19, 1974 subject Process Design for the Rail Car Vent Recovery System Attached is the process design for the rail car vent recovery system, A preliminary process design was issued to plant personnel on March 11, 1974 for review. Their comments and suggestions were incorporated, where appropriate, into the final design. Please proceed with a definitive estimate for the project. Planning and estimate work must be completed and the package sent to CED by April 11, 1974. Quotations are already being obtained on the heat exchangers, the package refrigeration unit/and the control valves. These will be made available to you as they are received. The cost of the project is expected to exceed $100,000. Therefore, copies of this design are being sent to R. 5. Matthews for review by PED. A copy is also being sent to R. R. Prescott for familiarization purposes to expedite the CED review. W, D, Statesman Chemical Engineer bs cc: RDG~RHG**[}EM"JRH(4)-GGD(5)-CEG-JSR JCL-DCS-RSM (2)--RRP REVIEWED BY: 'MHO, APPROVED BY: X H e/C*.*<?>/ CUH 000012397 TABLE OF CONTENTS RAIL CAR VENT RECOVERY SYSTEM LAKE CHARLES, LOUISIANA Purpose of Design Basis of Design Process Description Heat and Material Balances Table 1 Equipment Heat and Material Balance (Summer Conditions) Table 2 Equipment Heat and Material Balance (Winter Conditions) Table 3 Component Material Balance (Summer Conditions) ^ Table 4 Component Material Balance (Winter Conditions) Table 5 Utility Summary Equipment Specifications Equipment List NH-1 Refrigerated Vent Condenser NH-2 Vent and Recovered VCM Heater NP-1 Refrigerated VCM Return Pump NPK-1 Package Refrigeration Unit NST-1 Vent Stack NT-1 Refrigerated VCM Receiver NT-2 Vent Stack Knockout Pot Piping and Instrument Specifications Piping Schedule Instrument List Instrument Specifications Work List Description Operating Guidelines Drawings Process Flow Drawing Piping and Instrument Diagram - 1 of 2 Piping and Instrument Diagram - 2 of 2 CUH 00001 CUH 000012399 PURPOSE, BASS; PROCESS oesc*| % PURPOSE OF DESIGN RAIL CAR VENT RECOVERY SYSTEM LAKE CHARLES VCM PLANT The loading of VCM rail cars results in the venting of vinyl chloride vapors and inert gases. A portion of these rail cars enter the plant containing only nitrogen while many other cars must be purged with nitrogen prior to VCM loading to reduce the residual oxygen content below 100 ppm. An existing vent recovery system was installed.by the plant in 1970. This system was de signed to recover VCM from the vent of rail cars in dedicated VCM service (dedicated rail cars contain VCM vapors and do not normally require nitrogen purging). Loading of non-dedicated cars results in little VCM recovery because of the high nitrogen content of the vent gases. The loading of these non-dedicated cars results then, in the venting to the atmosphere of a considerable quantity of vinyl chloride. This is undesirable from environmental, safety and economic standpoints. The proposed vent recovery system will recover VCM from the vent of non-dedicated rail cars. This system will reduce the vent rate to a maximum of 50 Ib/hr, of VCM. The rail car vent recovery system is part of the VCM Plant's hydrocarbon compliance plan as sub mitted to the Louisiana Air Control Commission. The installation of this system will re duce the plant's vent from this source to a level compatible with our interpretation of the Commission's regulations concerning vents of reactive hydrocarbons. CUN 000012400 BASIS OF DESIGN RAIL CAR VENT RECOVERY ' SYSTEM LAKE CHARLES VCM PLANT The proposed system Is designed to recover the VCM from the vents of two nitrogen purged rail cars being loaded with VCM at a maximum total rate of 240 gpm, A maximum VCM vent loss of 50 Ibs/hr. is the basis of the design. The fl^w rate of 120 gpm per car is the maximum loading rate when all available rail car loading spots (10) are in use. This is the VCM flow rate basis for the system. Practical operating considerations require the flexibility to load nitrogen purged rail cars at any of the ten loading spots. A new vent header and VCM loading header will be required to tie this refrigerated recovery system into all ten loading spots. As nitrogen purged and dedicated cars (rail cars containing no nitrogen) are loaded simultaneously by the same pumps, a new loading header and flow control system will be required to limit the loading rate to the nitrogen purged car(s) to 240 gpm. Plant data indicates the temperature of the VCM in the storage spheres varies be tween 100 F in the summer to 30 F in the winter. The proposed system will meet the required performance criteria at both winter and summer conditions. The amount of nitrogen in equilibrium with the VCM in the vent stream leaving the rail car varies with the pressure in the rail car and the temperature of the VCM. By maintaining the pressure in the rail car slightly above the vapor pressure of the VCM at the loading temperature, it is possible to recover the required amount of VCM at a higher condensing temperature than would be possible at a higher pres sure. Therefore, by varying the system pressure as the VCM temperature changes from day to day, it is possible to greatly reduce the cost of the refrigeration system. The condensing temperature of -40 F is determined by the winter design condition of 30 F VCM in the storage spheres. Under winter loading conditions the concen tration of VCM in the rail car vent is low, and cooling of the rail car vent to -40 F is required to limit the final vent loss to 50 Ibs/hr. The feasibility of compressing the rail car vent and then condensing the VCM at a higher temperature was investigated. It is possible to compress the rail car vent to 225 psig and then condense at a higher temperature with only a slight increase in duty. Although this type of system would result in a lower refrigeration unit cost, it would not reduce the total investment and would result in a substantially greater system complexity and substantially lower system operating reliability. In addition the wide range of inlet temperatures, pressures and compositions would increase the compressor design and operating difficulties. Based on the above information a CWH 000012401 Basis of Design Rail Car Vent Recovery System Lake Charles VCM Plant Page 2 a pressure controlled refrigeration system was adopted over a compression-refrigeration system as the basis of this design. The possibility of using the existing compressor BL-409, for a compression-refrigeration'fype system was also investigated. However, calculations indicate this com pressor is far too large for the rai 1 car loading service. It would be necessary to operate BL-409 at about one-half the minimum recommended operating rate. This type of system then is not a practical solution. f CWH 0000.1240 PROCESS DESCRIPTION RAIL CAR VENT RECOVERY SYSTEM LAKE CHARLES VCM PLANT The rail car vent recovery system will reduce the vinyl chloride vented to the atmosphere to 50 lbs/hr. or less. The removal of the VCM from the rail car vent will be effected by cooling the vent stream to -40 F and collecting the VCM condensate. The recovered condensate will be returned to the VCM storage spheres. > Several new equipment items will be required for the new rail car vent recovery system. These are: NH-1 Refrigerated Vent Condenser NH-2 NP-1 Vent and Recovered VCM Heater Refrigerated VCM Return Pump NPK-1 NST-1 NT-1 Package Refrigeration Unit Vent Stack Refrigerated VCM Receiver NT-2 Vent Stack Knockout Pot The following is a description of the vent recovery process. A process flow drawing and piping and instrument diagrams are included in Section IX. The material and energy balances for summer and winter operating conditions are shown on Tables 1 to 4 in Section IV. Prior to loading of the VCM rail cars the dedicated cars are connected to the existing loading header and existing rail car vent line. Non-dedicated rail cars are isolated from the existing loading header and connected to the new rail car loading line. The vent from the non-dedicated cars is connected to the new rail car vent line. All rail cars are then prepared for loading in the usual manner. The liquid VCM from storage flows to vinyl chloride rail car loading area. VCM flowsInto the dedicated cars via the existing loading header system. VCM to the non-dedicated rail cars flows through NFIC-1 at 240 gpm (maximum) and then into the rail car(s). The total loading rate to the non-dedicated cars is controlled at 240 gpm or less by NFIC-1. The vent vapor from the non-dedicated car(s) exits through the new rail car vent line and flows to NH-1, the refrigerated vent condenser. NH-1 cools the vent from ambient temperature (30 F winter design conditions, 100 F summer design conditions) to -40 F, thereby condensing most of the VCM in the vent gases. Cooling for the refrigerated vent condenser is supplied by NPK-1, the package refrigera tion unit. NPK-1 consists of a two stage compression system using R-502 refrigerant. The refrigerant liquid flows on level control to NH-1. R-502 boils at -49 F and the boiling action cools the vent gases in the tubes of NH-1 to -40 F. The refrigerant vapors exit NH-1 and return to the package refrigeration unit. The refrigeration level is controlled on NH-1 by NLC-1 on the shell side of the exchanger. CWH 000012403 Process Descripti on Rail Car Vent Recovery System Lake Charles VCM Plant Page 2 The cooled vent gas and condensate flow from-NH-T to NT-1, the refrigerated VCM receiver. Here the VCM condensate separates from the gases and is accumulated during the loading operation. The gases exit NT-1 and flow to NH-2, the vent and recovered VCM heater, where they are heated to ambient temperature by low pressure steam on temperature control from NTC-1. The ga'ses then flow through NPC-1, the back pressure control valve for the system, and then to NT-2, the vent stack knockout pot, where any entrained liquid is separated. 1 NPC-1 controls the pressure of the rail car vent recovery system at the optimum point for maximum VCM recovery. The set point for this control will be set by NTC-2 based on the temperature of the liquid VCM at the discharge of the VCM loading pumps (P-411A, B, C), This cascade control will be set so the NPC-1 set point. In psig, eqqals the tem perature, in F, of the VCM being' loaded. V The gases containing primarily nitrogen and a maximum of 50 Jbs/hr. of VCM exit NT-2 and flow to NST-1, the vent stack, where they are vented to the atmosphere 148 feet above ground level. A continuous nitrogen purge is provided for NST-1 to prevent the . . possibility of explosive VCM-air mixtures. The existing vent line from T-490 is tied into the line to NH-1 to permit recovery of any VCM vapors vented through the existing dedicated rail car system. 44" Upon completion of the loading operation,NH-2, the vent and recovered VCM heater, is isolated from the vent system and connected to the pumpout system. The recovered VCM from NT-1 is pumped by NP-1, the refrigerated VCM return pump through NH-2, NH-2 heats the VCM to -15 F via low pressure steam on temperature control from NTC-1. The VCM then flows into the existing return line to the storage spheres. CUH 000012404 00001240'3 CUH TABLE ! EQUIPMENT HEAT AND MATERIAL BALANCE (Summer Conditions) RAIL CAR VENT RECOVERY SYSTEM LAKE CHARLES VCM PLANT M.W. Tank Car In VCM from Spheres Out Vent Vapor to NH-1 62.50 52.36 NH-1 Refrigerated Vent Condenser In Vent Vapor to NH-1 Out Vapor-Liquid to NT-1 Refrigeration Duty by NPK-1 Total 52.36 52.36 NT-1 Refrigerated VCM Receiver In Vapor-Liquid to NT-1 Out Vapor to NH-2 Condensed VCM Total 52.36 29.25 62.50 Rate (1) Lb/Hr. GPM (ScFh) Temp F 105918 1924 240.0 (13928) 100 100 1924 1924 1924 ' (13928) . 100 -40 1924 327 1597 1924 -40 -40 -40 Press/psig 100 100 .100 100 100 - Enthalpy^ BTU/Lb Heat Flew M BTU/Hr -42.0 95.4 -4448.6 183.5 95.4 -56.3 183.5 -108.3 291.8183.5" -56.3 102.1 -88.7 . -108.3 33.4 -141.7 -108.3 CWH 0 0 0 0 1 2 4 0 6 CUH 0 0 0 0 1 2 4 0 7 M.W. NH-2 Vent and Recovered VCM Heater ^ m Vapor to NH-2 Duty from L. P. Steam Total Out Vent Gas to NT-2 29.25 29.25 NH-2 Vent and Recovered VCM Heater in Condensed VCM Duty from L. P. Steam Total Out Recovered VCM to Spheres 62.50 ' 62.50 TABLE I (Continued) Rote <'> Lb,/Hr. GPM (scfh) Temp F 327 (4245) 327 (4245) 327 . (4245) -40 100 25000 25000 25000 50 -40 50 50 -15 Press/pslg Enthalpy^ . BTU/Lb Heat Flow M BTU/Hr 100 102.1 100 137.9 33.4 11.7 45.1 45.1 -88.7 -2217.5 162.5 -2055.0 - -82.2 -2055.0 Notes: ^ Assumed VCM loading rate to non-dedicated cars of 240 gpm (2) Enthalpy basis is 0 for nitrogen ga$(aj^_0oR and Opsla and for saturated liquid VCM at 100 C, Rate of liquid accumulation in NT-1. PumpdTnf rate is 50 gpm, ' ' NH-2 duty to heat vent gases to ambient temperature, NH-2 duty to heat recovered VCM to -15 F, TABLE 2 EQUIPMENT HEAT AND MATERIAL BALANCE (Winter Conditions) RAIL CAR VENT RECOVERY SYSTEM LAKE CHARLES VCM" PLANT M.W. Rate <'> Lb/Hr. GPM (scfh) Temp F Press/psig Enthalpy ^ BTU/Lb Heat Flow M BTU/Hr. Tank Car in VCM From Spheres Out Vent Vapor to NH-1 62.50 46.22 NH-1 Refrigerated Vent Condenser In Vent Vapor to NH-1 Out Vapor-Liquid to NT-1 Refrigeration Duty to NPK-1 Total 46.22 46.22 NT-1 Refrigerated VCM Receiver in Vapor-Liquid to NT-1 Out Vapor to NH-2 Condensed VCM Total 46.22 31.20 62.50 112995 756 240.0 (6200) 30 30 756 756 ------ 753" (6200) - 30 -40 756 266 490 756 - (3229) 7.8W - -40 -40 -40 - -66.0 30 87.7 30 . 87.7 -23.1 - -23.1 30 97.9 - -88.7 -7457.7 66.3 66.3 -17.5 83.8 66.3 -17,5 26.0 -43.5 '-[775 oo o CWH 0 0 0 0 1 2 4 0 ? TABLE 2 (Continued) M.W, Rate ^ . Lb/Hr. GPKT^FK) Temp F Press/psig Enthalpy^ BTU/Lb. NH-2 Vent and Recovered VCM Heater W In Vapor to NH-2 Duty to L. P. Steam Total Out Vent Gas to NT-2 31.20 31.20 266 266 266 (3229) (3229) (3229) -40 30 30 97.9 30 115.0 ' NH-2 Vent and Recovered VCM Heater In Condensed VCM 62.50 Duty from L. P. Steam Total Out Recovered VCM to Spheres 25000 25000 25000 50 -40 56 50 ` -15 . . - -88.7 -82.2 Notes: 0) Assumed VCM loading rate to non-dedicated cars of 240 gpm. (2) Enthalpy basis is 0 ^*^/lb. for nitrogen gas at 0 R and 0 psia and for saturated liquid VCM at 100 C. (3) Rate of liquid accumulation in NT-1. Pumpout rate is 50 gpm. (4) NH-2 duty to heat vent gases to ambient temperatures. (5) NH-2 duty to heat recovered VCM to -15 F. Heat Flow M. BTU/Hr. 26.0 4.6 30.6 30.6 -2217.5 162.5 -2055.0 -2055,0 TABLE 3 COMPONENT MATERIAL BALANCE (Summer Conditions) RAIL CAR VENT RECOVERY SYSTEM LAKE CHARLES VCM PANT Stream No, (2) itream Name a) VCM trom Spheres (2) Railcar Vent Vapor to NH-1 (3) Condensed VCM "omponent M.W. Lb/Hr Lb-M/Hr Mol % Lb/Hr Lb-M/Hr Mol %' Lb/Hr Lb-M/Hr Mol % 'inyl Chi. 62.50 105918 Jltrogen 28.02 1694.69 100.0 1622 302 25.96 10.79 70.64 29.36 1597 25.55 100.0 otal 105918 1694.69 100.0 192? 36.75 100.00 1597 25.55 100.0 o C'3 b oo 5 U . (4) Vent Vapors to Atmosphere Lb/Hr Lb-M/Hr Mol % , 25 302 327 0.41 10.79 11.20 , 3.62 96.38 ... 100.0 emp, 0 F ress, psig )ensity, /ft, low Rate, GPM (SCFH) 100 55.0 240 0) 100 100 (13928) -40 6l:l o) -40 100 (4245) : 4otes: Assumed total VCM loading rate to non-dedicated rail cars, is 24o 6?*^ ^ Stream locations are shown on process flaw drawing. Rate of condensate accumulation in separator. Pumpout rate Is 50 gpm. *! TABLE 4 COM PONENT MATERIAL BALANCE (W int er Conditions) RAIL CAR VENT RECOVERY SYSTEM- LAKE CHARLES VC M PLANT Rate o f condensate accum ulation in separator. Pumpout rate is 50 gpm CJ ro -- > tcs 3 ao. o Q s Q. 5! CO o 33 T-3t S' oO(9 3 O3 QI _ (9 Q. Q a. oo* 3* (a <9 a. SJ 4*. o -CoQ 3 n 5 <9 3 00 _ c**i* sv* "Q Q Q ^ "O X O-o r:> S> Oi o4*. *CO __ *sl COO r3(9 Ozr Sg S3 33 zz 3 * (9 *ro 5ro ro -SOo3i 'O 'OOi X COoO CO o-vl ci r 5 roo >ro0 cor NO>' O CO CO oo o O' -- NJ O CO c3 4I^ o oo r--o (4j*\. O' o cr X a <n \ O' 'vj 00 cr 3 co "sj O' O' ro 4*. <d Q *D ro XO --t cn o ro ZI oro Oco 'O o -o-No X n o k'Vl a* 3 ClJ co M C4*D. cp 3i* CO (9 Q. < O O 2 o CO ro r<oj ,1 i CO oo Jr X CD vj o vj CO ci r ro o 5 oo o O "O ___ -o ro___ , o'- < (39 i* a o o >\ i" o -3zr (9 -f1t CUH 000012411 TABLE 5 UTILITY SUMMARY RAIL CAR VENT RECOVERY SYSTEM LAKE CHARLES VCM PLANT Steam, 50psig, 297 F Supply Conditions Item No. Description NH-2 Vent and Recovered VCM Heater Nitrogen, 200 psig, Ambient Supply Conditions Max continuous purge to NT-2 and NST-1 Electrical Power ^ Item No. Description NP-1 NPK-1 Refrigerated VCM Return Pump Package Refrigeration Unit Total Instrument Air 10 Users at 1 SCFH each - 10 SCFH Max Lb/Hr. 196 10 SCFH Installed Electrical H.P. 7.0 190.0 197.0 V (1) installation of switchgear equipment will be required for the listed items. (2) Includes electrical power requirements for compressors,- air-cooled exchanger motor, oil return pump, and electric oil heater. \ 000C->.Ui o' A T CUH OOQoj EQUIPMENT SPECIFICATIONS RAIL CAR VENT RECOVERY SYSTEM LAKE CHARLES VCM PLANT Equipment List NH-1 NH-2' Refrigerated Vent Condenser Vent and Recovered VCM Heater NP-1 Refrigerated VCM Return Pump* NPK-1 Package Refrigeration Unit NST-1 Vent Stack NT-1 Refrigerated VCM Receiver NT-2 Vent Stack Knockout Pot . CUH 00001 > CS7IT33 * r vm vrrr. 'ju lcpj c \ PONCA CITY. OKLAHOMA CMPM A TIIRP FYrMANfttaS r'Vf^ZX c Upy_- , AFFMn oatf3/.-5`/7V MADF BY Fv5 APT'n RY B U MO W. O. NO. 1NO NO . REO. NO. P 0. NO. PL ANT i^K cmrls, vcm pla*JT PRO IFPT fj.4/- - CrAP \SIFAf~r FF OO'/rFY S YS7'/FSS1 1 ITEM NO-& TAG fju--l if-". Open-. C-c;ton-.. . 2 SHELL SIOE 3 NdllUt *o Stic TINS ft ACIN 4 lLtT 5 oyri.iT ! a /f*L8 r-L'- FF. G t<?LB FLC- ff.F t 6 VC NT 1 ( tretp rLr-> p.,f~ 7 0*4'N V ( tfOLB PCS ff.F. B CON 'X i /sotF Ft.'b 9 CO* ^ f i a l'/a ISOLK F.F. 10 CHlM a \J2 !''<->La me. p.r. 2 11 RELIEF- / 2 t*0 LB *F? f 12 SUP-ON NOZZLE FLANGES ALLOWED (YES TUBE SIDE Hf TIMO ft PAClhO 3 ten LB Ft-i F.F. ?> 150 LS FUG R,F. i Vix /S'OLS.F/a R.F, 3 /OO L. Fl5. R.F. (NO SERVICE OF Wf pstf?pSc*EPA rcO vr..tT MANUFACTURER SIZE TYPE^wyoA P.KU <HORia CONNECTED IN EFF. SURF. PER UNIT. ( ) PARALLEL sq It ( 1 SERIES SHELLS PER UNIT } SHELL DIAM EFF. SURF. PER SHELL, so It NO. TUBES PER SHELL LENGTH IN. IN. UNITS REQ'D. DELIVERY. WEEKS / PRICE. PER UNIT EST. FREIGHT COST 13 SLIP-ON 6NO FLANGES ALLOWED (YES) (NO) - TOTAL PRICE 14 GASKETS: SHELL 15 CHANNEL 16 FLOATING-HEAD COVER DOLLARS PER SQUARE FOOT MATERIALS: (MARK SR AND PERCENT XR) ITEM MAT'L. DEG F SPECIFICATION 17 18 TEST RING REQ'JIR :/>$) est) 19 SPARE GASKE TS REQUIRED (YES1 (NO) 20 STACKING HIGH 21 INSULATION THICKNESS IN. 22 NO. TUBES OO^/y IN.: MIN. THK. .3 IN. 23 LENGTH 24 SHELL DIAM FT;PITCH IN. o o. / IN cS)'C233f) VAX ft SIAM 4 UCOW IN. 25 TRANSVERSE BAFFLE TYPE SPACING IN. TUBES SHELL SHELL COVER (REM) (INTEG) CHANNEL CHANNEL COVER (REM1 (INTEG) FLOATiNG-HEAD COVER TUBE SHEETS BAFFLES AND SUPPORT PLATES BOLTING: SHELLCOVER c.s- - C^__- *errr.3F A F/F> 3 s r^ A/J A- ^ r L A; Tf-^. //Air- rJ T-/-A " i A (- 26 PERCENT CUT IVERT.) IHORIZ.I (45 DEG1 CHANNEL 27 LONG BAFFLE TYPE 28 TEMA CLASS R ye c-, 29 30 IMPINGEMENT BAFFLE (YES) (NO) FLOATING HEAD ASME CODE REO'D VE.S CHANNEL COVER PERFORMANCE OF ONE UNIT SHELL SIOE ) \ TUBE SIDE 31 FLUIOCIRCULATED 32 TOTAL FLUID ENTERING. Ib/hr R rrmn.rF F.jrr 301 f'SF.B A/OTL- l 1 r.F-LO=>`Di,2H AAF-'S'FS 33 34 VAPOR. 35 LIQUID. 36 STEAM. Ib/hr Ib/hr Ib/hr IN -- .5 ZO t -- OUT 7 20 / ----- -- -- IN /(2 2 OUT / T9 7 37 WATER. Ib/hr ---- -- --. ------ -- 38 NONCONDENSABLES. ib/hr -- -- F-OO 29 GRAVITY:-^rr?S9SBf: SG 40 MOL. WT: VAPOR 41 MOL. WT: NONCONDENSABLES TFMP -- ___ -- 1//.69 -- -- 52, 2S OQ. O 2 }- o 29. 2,r Ip.oo 42 VISCOSITY: LIQUIO. CP 43 HEAT; LATENT *.> SP ...vx. liq .2Y @ `SCs F WPzJ/? @ 8(3 L T. HT. -FO. 2 F IOO F :.-a .if ip - >yo f 'AA '.r-=. .1- 0' :CO`f- t/a . - -rJ "= urr j ' 1 44 THERM. CQND: ...i':/*.... VAP. LIO. > F QF @ fOO F t.A-1 .C'.y - VO F : 45 TEMPERATURE 46 OPERATING PRESSURE F osig - V9 -V9 mo ioo -9 0 47 VELOCITY 48 NO. PASSES FPS in / H 49 PRESSURE DROP 50 FOULING RESISTANCE |MIN.) psi ALLOY/ < UP CALC OPl ALLOW 3.>{max) CALC .00 2 c-3 -H 51 PRESSURE. osj 52 DESIGN TEMPERATURE, DEG. F DESIGN Zl-RO TEST 1 D 5" t - sro DESIGN K.O 1-50 TEST o o 53 CORROSION ALlCWANCE: IN. 1/r " 54 MTO (WTO) (CORRI F HEAT EXCHANGED. BTU/HR 2 71.BOO i 55 TRANSFER RATE: SERVICE 56 WEIGHTS PER SHELL: SHIPPING CLEAN ib: FULL OF WATER lb: BUNDLE u lb; 57 NOTES THE CALCULATED SERVICE HEAT TRANSFER RATE OUTSIDE TUBE AREA OR EXTENDED AREA) IS TO OE DECREASEO BY t O PERCENT FOR ALL 50 DESIGN CALCULATIONS. 59 SUPPLY H TO COMPLETE FORM BY F UHNISHING INF ORMATION FOR flt ANK `.PACFS 1 . S.HT-- OF 3 REV. . ... - 4-421 PLANT LAKE ENGINEERING CENTER PONCA CITY. OKLAHOMA SPECIFICATION SHEET A.F.6. NO___________ DATE 3/,/7cf MADE BY W P>A. APP'D BY________ W. 0. NO. INO. NO. REQ. NO. SHELL & TUBE EXCHANGERS. B. M. NO_________ P. 0. NO. CtiAKLES VC-At PLAA/T___________ PROIPOT RA/L CAR VWT RE OOVFPV SYS -rFr/fi 4 -4 2 I-: r< { in 1 item no. & tag r/H-t (\MiMTE_n: Operz.. ; SERVICE OF UNp zPPlC->EPATFh Vps/T C F''/Z " P 2 SHELL SIOE TUBE SIDE 3 MOtiVM N0 | A * T INO f tCIM^ 1 NO. mr IaTIHA ft PACINO 4 INicT / H \ixoisrtz r.f. 5 OUTl 1 T / 6 r> G C3.gr 6 vcf / / FLG ft.R 7 QftAIM '~t / iisolp.f-lG P.r. 8 > M^Vg 3 / R Fi-a fi.F. 1 i9 C OwH* Ui`l2. 'Ad. '/roiB flu *.r. 3 ISO tf Fit1 R, P p /S'* LP. PIG R.F. ' 10 i:i:H ' o . 7. ''tr/)LP FLC, P X. 2. 11 ^kuepA _]_ _ 2 /rr>i.F. Fi`-. P. .F i ! 7s >5~0 l & PIG ft. P. 2. tSOiF FIG F..F, 12 SLIP-ON NOZZLE FLANGES ALLCWEO IYES) INOI MANUFACTURER SIZE CONNECTED IN TYPFa*L/,b 8*0 ( ) PARALLEL EFF. SURF. PER UNIT. so ft SHELLS PER UNIT / SHELL DIAM EFF, SURF. PER SHELL, sq ft NO. TUBES PER SHELL LENGTH UNITS REO'D. / DELIVERY. WEEKS PRICE. PER UNIT EST. FREIGHT COST <fiORl) iT23*l i } SERIES IN. IN. 13 SLIP-ON END FLANGES ALLOWED {YES) (NO) TOTAL PRICE 14 GASKETS: SHELL 15 CHANNEL DOLLARS PER SQUARE FOOT MATERIALS: (MARK SR AND PERCENT XR) 1 1 16 FLOATING-HEAD COVER 17 18 TEST RING REQUIRED (Y/S> KQ 19 SPARE C-ASKETS REQUIRED (YES) (NO) ITEM TUBES SHELL SHELL COVER IRE.VI (INTEGI mat'l.Ideg. f SPECIFICATION C, 5," 70re,`l? A 32* r-ft / C,S.I - rcr. us 20 STACKING 21 INSULATION THICKNESS 22 NO.TUBES 0DsA*y IN.iMIN.THK. .083 23 LENGTH FT;PITCH IN. 24 SHELL DIAM IN. ao d,V- HIGH IN. IN- paXg) IN. CHANNEL CHANNEL COVER (REM) IINTEG) FLOATING-HEAD COVER TUBE SHEETS BAFFLES AND SUPPORT PLATES 5S IS A r/ AC. -fs-=> sr AL TfET- /A A lT"A 25 TRANSVERSE BAFFLE TYPE SPACING IN. BOLTING: SHELL COVER 26 PERCENT CUT (VERT.) (HORIZ.) (45 DEG) CHANNEL 27 LONG BAFFLE TYPE IMPINGEMENT BAFFLE IYESI 'NO) FLOATING HEAD 28 TEMA CLASS R YE S 29 ASM6 CODE REO'D YES CHANNEL COVER PERFORMANCE OF ONE UNIT 30 SHELL SIDE TUDE SIDE 31 FLUID CIRCULATED 32 TOTAL FLUID ENTERING. 33 Ib/hr RFFRIG^P F//T PO 2 V/A/VL- CML/'";r>= ____ (SE AJQTZ l') ________________ _______ _______ _______ 7^"<3 IN ; OUT IN VAP7PS OUT 34 VAPOR. 35 LIQUID. 36 STEAM. Ib/hr Ib/hr Ib/hr -- __ 5 VO -- -- prn v7n 37 WATER, 38 NONCONDENSABLES, 39 gravity.- L^r:igaui 40 MOL.WT: VAPOR 41 MOL.WT: NONCONDENSABLES temp Ib/hr Ib/hr -- ---- -- -- -- --///. <s y __ -- 2 /< 22 _ 2/<o /, o 3/. 7 0 2?. 42 VISCOSITY: LIQUID. CP 43 HEAT; LATENT SP. 44 THERM. COND: .. :.*,,, VAP. LIQ. u/l .JV tr. NT. -- ED. ? e> P f *Ap.o/ar^> F L-i? . r S' C3 " u O F VAH SP .LI 2 o-F wq = . 2 y y i5> @F i/o - yo F 4b TEMPERATURE F - V9 - V9 E.O - VO 46 OPERATING PRESSURE pjiq - V 30 47 VELOCITY 48 NO. PASSES 49 PRESSURE DROP FPS psi ALLOW 4. /. O CALC ALLOV/a.sfAM*-) CALC T~i <r*.ri iH 50 FOULING RESISTANCE (MIN.) , not - 2C90 S 51 PRESSURE. cIq 52 DESIGN TEMPERATURE, DEG. F OESIGN 2SO TEST /?r 4 - SO --D--E-S-I-G/-N-2--r7---<--0------rr-s->-T-E-S-T------------ oO 53 CORROSION ALLOWANCE: IN. 54 MTD (>V TO) (COR R) F 'Aft | HEAT EXCHANGED. BTU/HR pa, 55 TRANSFER RATE. SERVICE CLEAN J 56 WEIGHTSPER SHELL: SHIPPING lb; FULL OF WATER ib; BUNDLE lb' b/ NOTES. THE CALCULATED SERVICE HEAT TRANSFER RATE I0UTS10E TUBE AREA OR EXTENOE 0 AREA* IS TO BE DECREASED BY JO PERCENT FOR ALL by DESIGN CALCULATIONS 59 SUPPLIER TO COMPLETE FORM BY FURNISHING INFORMATION FOR BLANK SPACES 2.SMFPT OF PPV SHELL AND TUBE EXCHANGER SPECIFICATIONS RAIL CAR VENT RECOVERY SYSTEM LAKE CHARLES VCM PLANT Item No. NH-1 ' Service Refrigerated Vent Condenser Notes: 1. Summer operating conditions are shown on Sheet 1 of 3. Winter operating conditions are shown on Sheet 2 of 3. 2. Exchanger tube size, length, and pitch may be adjusted for optimum exchanger design. 3. Vent Gas Composition - Summer Conditions Vent Gas In Vent Gas Out VCM Nitrogen 70.64 Mol %; 1622 IbsAr. 29.36 Mol %; 302 Ibs/hr. 3,62 Mol %; 25 Ibs/hr. 96,38 Mol %; 302 !bs/hr, 4, Vent Gas Composition - Winter Conditions Vent Gas In Vent Gas Out VCM Nitrogen 52.80 Mol %; 540 Ibs/hr. 47.20 Mol %; 216 lbs/br. 9.28 Mol %; 50 IbsAr. 90.72 Mol %; 216 Ibs/hr. Date: 3/15/74 CWI-I 000012417 Sheet 3 of 3 Instrument List Rail Car Vent Recovery System ;Lake Charles VCM Plant Page 2 jlnst. No. TypeH , ^IRV-l r-j j Relief Valve / . , . |NRV-2 ^'i^rr Relief Valve !\l' jNRV-3 k Relief Valve A\L- 1 ' MRV-4 Relief Valve L L`b ^IRV-5 Relief Valve \|RV-6 r:V- **"71; Relief Valve / *' ` - u/\Tt ^IRV-7^--4-yi1 Relief Valve ^JRV-8 Relief Valve ' 1 ' /- LfiTk MRV-9 HtJ---T-rrRe^e^ Valve / Location "'Line VCA-1 Line VCA-7 NH-1 NH-1 NT-1 Line VCA-8 NH-2 NH-2 Line VCA-9 Type Element Location ^ Spring Spri ng Spri ng Spring Spring' Spring Spring Spring Spring Line VCA-1 Line VCA-7 NH-1 NH-1 NT-1 Line VCA-8 NH-2 NH-2 Line VCA-9 Remarks Thermal Relief Thermal Relief Shell Side Tube Side Thermal Relief Shell Side Tube Side Thermal Relief "I 1-11=1 (;. V> 'iT\Er-vlvrl-: i-l ru '' H '.! n sr oo o E-.J -fc, CO SHELL AND TUBE EXCHANGER SPECIFICATIONS RAIL CAR VENT RECOVERY SYSTEM LAKE CHARLES VCM PLANT Item No, NH-2 ^ Service Vent and Recovered VCM Heater Notes: 1. Summer operating conditions are shown on Sheet 1 of 4 and winter conditions on Sheet 2 of 4. Heating require ments for VCM pumpout are shown on Sheet 3 of 4, Ex changer must perform satisfactorily at all conditions.^ 2, Exchanger is to be provided with a shell side expansion Joint. 3. Exchanger tube size, length, and pitch may be adjusted for optimum exchanger design, 4, Vent Gas Compositions Summer Conditions Winter Conditions VCM Nitrogen 3.62 Mo! %; 25 Ibs/hr. 96,38 Mol %; 302 Ibs/hr. 9.28 Mol %; 50 lbs/hr. 90.72 Mol %; 216 Ibs/hr. 5. Exchanger may be Brown Fintube or Type BEM or AEL, Date: 3/15/74 oooo i4V? CUH Sheet 4 of 4 i V?!*r3TT PLANT L*hE ^HAPiFS ENGINEERING CENTER PONCA CITY, OKLAHOMA SPECIFICATION SHEET SHELL & TUDE EXCHANGERS. yc/v? PLAA/T project R*n- OAK A.F.E. NO_____________ DATE MADE BY WZ> 5 APP'DBY_____________ B. M.NO----------------------- ^vr recovery W. O. NO. INQ. NO. REQ. NO. P. O. NO. ITEM NO, & TAG AJt4-2 (SlJMM ' SERVICE OF UNIT^^y J/Vi) P r~C O'zCrz? h ZC,`A /^~A-rF~' SHELL SIDE TUBE SIDE MANUFACTURER 3 hOHLII 4 l"ltT 5 eun.tr 6 VINT 7 OIMR 8 CTCO*hMM. N9 UK DillNO * PiClMO MO. / 7 -'B.'a R.F. I a. ?!>LR piQ fT.fr. / 1 v* C.P' A . / 1*0 LZ FL.G/LF i li7C VIMO 4 PACINO O. iso lr FrG * ft.F 7 /50 LR FLP- P.F. SIZE CONNECTED IN TYPEVva f IHORI# ( ) PARALLEL 1 ) SERIES EFF. SURF. PER UNIT. SQ ft SHELLS PER UNIT / SHELL DIAM IN. EFF. SURF. PER SHELL, sq ft NO. TUBES PER SHELL LENGTH IN. 9 Cd -- 11 10 11 RELIEF ;> r" / _? . IFF LB.FA *> Jf - / /J/? /COLflA'5 R.F. 7 /*i-o t-F. FLF K.F. 1? SLIP-ON NOZZLE FLANGES ALLOWED IVES (NO UNITS REQ'D. DELIVERY. WEEKS PRICE. PER UNIT EST. FREIGHT COST / 13 SLIP-ON END FLANGES ALLOWED (YES) (NOI TOTAL PRICE 14 GASKETS: SHELL DOLLARS PER SQUARE FOOT 15 CHANNEL MATERIALS: (MARK SR AND PERCENT XRI T 16 FLOATING-HEAD COVER ITEM MAT'L. DEG f SPECIFICATION 17 18 TEST RING REQUIRED (NO) 19 SPARE CASKETS REQUIRED (YES! (NO) 20 STACKING HIGH TUBES SHELL SHELL COVER (REM) (INTEG) CHANNEL 50-1CC A--y*M GF 1 rjt. A-5/0 FF ; C A SS 21 INSULATION THICKNESS IN. CHANNEL COVER (REM) (INTEGI ACC. A Ft L r 22 NO. TU8ES OQOD3/V IN.: MIN. THK. t 3 IN. FLOATING-HEAD COVER l~\ VA 7 23 LENGTH 24 SHELL DIAM FT;PITCH ; IN. IN. M AA UNOL* OIAM ALWDM TUBE SHEETS AAA-'' IN. BAFFLES AND SUPPORT PLATES 25 TRANSVERSE BAFFLE TYPE SPACING IN. BOLTING: SHELL COVER 26 PERCENT CUT (VERT.) (HOR1Z.) (45 OEGI CHANNEL 27 LONG BAFFLE TYPE IMPINGEMENT BAFFLE (YES) iNOI FLOATING HEAD 28 TEMA CLASS R y.cr c; 29 ASME CODE REQ D Vs S .. CHANNEL COVER PERFORMANCE OF ONE UNIT 30 SHELL SIDE TUBE SIDE 31 FLUID CIRCULATED 32 TOTAL FLUID ENTERING. 33 Ib/hr SO LB . STJTA./A 10.8 IN ; OUT YZ/ST 327 (SEE IN V A POP 8, )/ZCT-- / ________ OUT 34 VAPOR, Ib/hr --. -- 05 2ET 35 LIQUID. Ib/hr --- -- ------- 1 36 STEAM, Ib/hr 10.B -- -- 37 WAT E R. ib/hr 10.8. 38 NONCONOENSABLE5. Ib/hr --- 3,03. 300 39 GRAVITY: 3r : SG 0 eBI TS'/YlF .-- - 9P> 40 MOL. WT: VAPOR Iff. 03. 07. 2-5* 0.2.0 0 41 MOl.WT: NONCONDENSABLES 42 VISCOSITY: LIQUID, CP 43 HEAT; LATENT v SP ..`W. 44 THERM. COND. 45 TEMPERATURE -- ____ 2g.p2__________ 0 9.02 *ap .a/.r f ua . / 8 077 yap 5p = .^r,`-i`'7,` LT.//T.-4IZ. CC 71 7 tifl.*/,<> F!vap./s@ F VAP. r/A tOO F Mr sp=.:5<5>-9o *.- yip nrxz .-zrL^J')S'-P 7VAr .orzQ'X'7 F ji.AT.3a7 "Q?7 F YAP.0I2.& -90 F Ptf* !0O F F 297 0.97 - 90 too 46 OPERATING PRESSURE (ni so too 47 VELOCITY 48 NO.PASSES 49 PRESSURE DROP 50 FOULING RESISTANCE IM1N.) 51 PRESSURE, psiq FPS t ps /OALLOW CALC . oon *r ODESIGN /7 TEST ALLOW DESIGN / L/.O CALC 09/ 200 TEST r-i 7V,i 0 X 52 DESIGN TEMPERATURE, DEG. F a SO SS'O 0 53 CORROSION ALLOWANCE: IN. 54 MTD IWTD) tCORFi) F 55 TRANSFER RATE: SERVICE _ __ . vv. HEAT EXCHANGED, BTU/HR CLEAN It,700 3 L3 66 WEIGH TS PER SHELL SHIPPING lb FULL OF WATER <b; BUNDLE ib; /J57 NOT t S. THE CALCULATED SERVICE HEAT TRANSFER HATE OUTSIDE TUBE AREA OH EXTENDED AREA) IS TO BE DECRE ASCO BY PERCENT FOH ALL 58 OF SIGN CALCULATIONS. 52 SUPPLIES TQ.CQVm.If-.EQflM.ay StlF-FT _Q.e ENGINEERING CENTER PONCA CITY. OKLAHOMA SPECIFICATION SHEET SHELL & TUBE EXCHANGERS. PLANT.CffJftLSS VOM PLAA/T_________ A.F.lE. NO______________ DATE S/&/ m MADE BY WPS AfflD BY______________ 6.H.N0__________ CAP VF.'/T RFCOYFPV W. 0. NO. INQ. NO. REO. NO. P. 0. NO. SYSTFM 1 ITEM NO. & TAG S/A/-2 (Wi KTTTE.r., <Cr*=Lf1, wCKJCC,.) service of unit 'v'^4/7- /i/jp prr.nvr&*= r> vcm pfai-fr 2 3 onm 4 INII? 5 QVTLir 6 V(Mf 7 D44M ItWF 8 COMM 9 P#t| CONN 10 <H( M SHELL SIDE MO t 1 \t50L FIS. PJZ 1 a >sots.Ac-\ p.f. / 3/v G.'5'V7 L P. GPL''- ( ISO LS,Ftn, PF. -Q ! ( 11 REurrp / ^r^OLP, FLC-.P.F 12 SLIP-ON NOZZLE FLANGES ALLOWED IVES) TUBE SIDE U( ..T.0 . fC.~0 ? fSOLE. FiG\ RF. 2 tSrtLR. FLO. fl.ft ISOLB. FLC~. P.F 2. JS`OUB.FlC,a FLF. INO) MANUFACTURER SIZE CONNECTED IN TYPE c, . e A/0 7Z R CtDFT 1 2i IVT2CCJ | ) PARALLEL 1 ) SERIES EFF. SURF. PER UNJIT. sq ft SHELLS PER UNIT f SHELL DIAM EFF. SURF. PER SI-HELL, so ft NO. TUBES PER SHELL LENGTH >N. IN. UNITS REQ'D. DELIVERY. WEEKS / PRICE, PER UNIT EST. FREIGHT COST 13 SLIP-ON END FLANGES ALLOWED (YES) (NOI TOTAL PRICE 14 GASKETS: SHELL DOLLARS PER S0U:AR6 FOOT 15 CHANNEL MATERIALS: (MARK SR AND PERCENT XR) j 16 FLOATING-HEAD COVER 17 18 TEST RING REQUIRED (77^) 19 SPARE GASKETS REQUIRED (YES) (NO) 20 STACKING 21 INSULATION THICKNESS HIGH IN. 22 NO. TUBES 00 3/y IN,: MIN. THK. , QQ 3 IN. 23 LENGTH FT:PITCH IN- O) 24 SHELL CAM IN. IN. ITEM* TUBES SHELL SHELL COVER |RE?V.) (INTEG) CHANNEL CHANNEL COVER I REM) IINTEG) FLOATING-HEAD COVER TUBE SHEETS BAFFLES AND S'JPP-ORT PLATES MAT'L.I DEG. F SPECIFICATION I . -roT,,;Jo A.7,? V G>A / .S.-i ,oo AS'/O' A rr- A>.y i MA T- A,'J XJc: 25 TRANSVERSE BAFFLE TYPE SPACING IN. 2G PERCENT CUT (VERT.) IHORIZ.) (45 DEG) BOLTING: SHELL COVER CHANNEL 27 LONG BAFFLE TYPE 28 TEMA CLASS R YE 29 IMPINGEMENT BAFFLE (YES) (NO) ASMS CODE REQD yrg FLOATING HEAD CHANNEL COVETS PERFORMANCE OF ONE UNIT 30 SHELL SIDE TUBE SIDE 31 FLUID CIRCULATED 32 TOTAL FLUID ENTERING, Ib/hr S'O L3. S TF-AM S- O____________ i/EV/T VAP^^T, ?G>r0 (SZ /sn-T / > 33 IN OUT IN | OUT 34 VAPOR. 35 LIQUID. Ib/hr Ib/hr SO \ so 1 36 STEAM, 37 WATER, 38 NONCONDENSABLES. 30 GRAVITY: ...................... .. SG TF/4R Ib/hr Ib/hr Ib/hr S.O B-.O 2 !G 1 1/G 40 MOL.WT: VAPOR 41 MOL. WT: N0NC0NDENSA8LES 42 VISCOSITY- LIQUID. C? 43 HEAT; LATENT 'V SP. / 8.012. kT. #1, = v/ -- Lia 3/. 3.0 afi. 02 F 91,0.0 23.02 44 THERM. COND: A`V*_,. 45 TEMPERATURE 46 OPERATING PRESSURE 47 VELOCITY 48 NO. PASSES VAP. UO. 49 PRESSURE DROP 50 FOULING RESISTANCE (MIN.I 51 PRESSURE, ps.g 52 DESIGN TEMPERATURE, DEG. F 53 CORROSION ALLOWANCE; IN. F pv'q FPS wi vAP.CIfiQ 3.9 7" T SO F XIP .?*7 2<7 7' D.q-7 F --FO -ao 30 f i/io.-^iv^ A (0 \ =o ' ALLOW /O DESIGN /yr> 3 fro _______ -'/6 / CALC TEST ___________________________ / ALLOW A/,C> -/ DESIGN 300 35-^2 CALC TEST c-i "2, OC- 55 TRANSFER RATE: SERVICE CLEAN 56 WEIGHTS PER SHELL: SHIPPING FULL OF WATER !b; BUNDLE lb; 57 NOTES. THE CALCULATED SERVICE HEAT TRANSFE R RATE IOUT5I J TUBE ARE A OR EXT ENDED ARC AV IS TO BE DEC HE ASEO SY / O PE RCENT 58 OE5ICN CALCULATIONS O X -X 59 SUPPLIER TO COMPLETE FORM 8Y FUR Nl SUING INFORMATION FOR BLANK SPACES SHiFET. OF _^_R EV. 4 -4 2 I- VTTuOTT r:,rpjrr:.ci ENGINEERING CENTER PONCA CITY. OKLAHOMA SPECIFICATION SHEET SHELL U TUBE EXCHANGERS. A.F.E. NO___________ DATE 3/<p/77MADE BY WD 5 APP'D BY___________ 8.M. NO_____________ W. 0. NO. INO. NO. REQ. NO. P. 0. NO. . PLANT LAhS OHA-RLSS VCsH 71. AMT PRniFrj RAIL CAR. VJ?MT R COYEST _STS TE.M 1 &ITEM NO. TAG ////_-? -T?, 2 3 4 INLfT 5 OUTLCT 6 WNI 7 8 TCONMM* SHELL SIDE MO ill P4CIM0 / a i^nit FL^ P..F. f 7 irroi-F. Ft& rj*. iAU '<?con LB CPLC-* ( f /!TO L3 FUzr P.F MO. / TUBE SIDE 12 K *T*MO MCIN4 *7 WOLfi. FtrA PP. 'SOLS.FLC*. R.r. 9 10 CCONMCMM i' T7 fY'i rroLF.Ft'L p.p. 11 ZFLJFF 1 CL \tr+J.B FL<? PJ? a I52L3 FLt, ft-P.i 12 SLIP-ON NOZZLE FLANGES ALLOWED IYES) {NO) SERVICE OF UNIT vv^vr Ao/n f=fFCrn'E55n vc./v\ hfatPH MANUFACTURER SIZE CONNECTED IN TYPE c = r. WTe r-rROTHT) fV_JXa { ) PARALLEL ( I SERIES EFF. SURF. PER UNIT. sq ft /SHELLS PER UNIT SHELL DIAM IN. EFF. SURF. PER SHELL, vn ft NO. TUBES PER SHELL UNITS REQ'D. / LENGTH IN. DELIVERY. WEEKS PRICE. PER UNIT EST. FREIGHT COST 13 SLIP-ON END FLANGES ALLOWED (YES) (NO) TOTAL PRICE 14 GASKETS: SHELL 15 CHANNEL D0LLAR5PER SQUARE FOOT MATERIALS: (MARK SR AND PERCENT XRI 16 FLOATING HEAD COVER ITEM MAT'l.l DEG. F SPECIFICATION 17 18 TEST RING REQUIRED. ~{U6) 19 SPARE GASKETS REQUIRED (YES) (NO) 20 STACKING HIGH 21 INSULATION THICKNESS IN. 22 NO. TUBES op S/a/ in,: min, thk. ,c>83 IN. 23 LENGTH FT;PITCH \ IN. (@<^35 24 SHELL DIAM IN. IN. TUBES SHELL SHELL COVER (REM) (INTEGI CHANNEL CHANNEL COVER (REM) (INTEG) FLOATING-HEAD COVER TUBE SHEETS BAFFLES AND SUPPORT PLATES -sfto3cc _A~ f /g A-A/ A/. /tl j. + r. p A L JL 25 TRANSVERSE BAFFLE TYPE SPACING IN. | BOLTING: SHELL COVER 26 PERCENT CUT (VERT,} (HORIZ.) (45DEG1 CHANNEL 27 LONG BAFFLE TYPE 28 TEMA CLASS R Y_ES 29 30 IMPINGEMENT BAFFLE (YES} (NOI FLOATING HEAD ASME CODE REQ'D YES CHANNEL COVER PERFORMANCE OF ONE UNIT SHELL SIDE TUBE SIDE 31 FLUID CIRCULATED 32 TOTAL FLUID ENTERING, 33 Ib/hr SO LB. STS AM ITS !N OUT VCM UQ'JlD O.SOCO IN A-tn-rr- / ) OUT 34 VAPOR. Ib/hr -- ------- --- 35 LIOUID, 36 STEAM, 37 WATER, 38 NONCONDENSABLES, Ib/hr Ib/hr Ib/hr Ib/hr -------t7& -- --. ___ __ -- /7 ft 2 *TCOO --. --- -IM1 2 TOnC: . -- -- 39 gravity: 40 MOL.WT: VAPOR sg& css* T&S/l ft -- /P..OO. . 9e --- t* o /. O 41 MOL.WT: N0NC0NDENSA3LES ._ -- -- 42 VISCOSITY: LIQUID, CP 43 HEAT; LATENT *.v Sp 44 THERM. COND: 4b TEMPERATURE 46 OPERATING PRESSURE VAP. I_IQ. F p*j0 v*s> '2.7*7' F wo ./ 29 7 F US .15 -- VO ir, n r. a'hVr'Wi zif'F yap c-p^.vr tir> <tpW.0'^:C'>7'V=I'W:J SP= ,Ap .ohS @ 217 F w<j.S?7<?> H?"*? F VrO 297 50 297 -HO F LJQ " f 5~ F Lia. CP. F - rv-t'^ ~ / 47 VELOCITY FPS 48 NO. PASSES 49 PRESSURE DROP 50 FOULING RESISTANCE IM1N.) 51 PRESSURE, piiq 52 DESIGN TCMPERATURE, DEG. F 53 CORROSION ALLOWANCE. IN. 54 MT D (WTD) (COH R} F bb IHANSFtH HAlfc: SERVICE 1 psi ALLOW fO CALC t ALLOW 5~. O CALC ,, OO^S DESIGN /7 O TEST , OO 2 OESIGN SOO TEST _ x/% 3SO | HEAT EXCHANGED. BTU/HR IOD. SOO CLEAN Vi "7 o O -- 56 WEIGHTS MR SHELL: SHIPPING lb; FULL OF WATER !b; RONDLE lb 3 57 NOTES THC CALCULATED SERVICE HEAT TRANSFEH RATE IOUTSIOE TUBS AREA OR EXTENOCO ARE A US TO BE DECREASED BY / O PERCENT ^ OR AL ' 58 OESIGN CALCULATIONS. 7 V PLANT IflrATinN W^LE- VC-M ENGIKCEniMG CENTER PONCA CITY, OKLAHOMA SPECIFICATION SHEET *S=4x|_ - U&Se " CENTRIFUGAL PUMPS PRD.1FC.T PCKfor" --O-f^SZ^ A.F.C. NO. ^5 /44 DATE II- II - 7V MADE BY_ APP'O IIY _ B.M. NO___ J\ eco'i' W. O. NO. INQ. NO. . REO. NO. P. 0. NO. -Y i'rtSTe.l * APPLICABLE 70: ESTIMATE! ) PURCHASE ("s#) \TE.VA NO O. .^?r\ SERVICE ?sT\)a.^ PV)\-^ VENDOR MANUFACTURER SIZE AND TYPE STAGES MOTOn DRIVE TN ) TURBINE ( ) RPM ROTATION FACING CPLG. OPERATING CONDITIONS DESIGN EFF. l|QU1D\llKVta^ Gut nl?lDE U-S.SPmctPV.NOR. T=Sr7 DES DESIGN S.H.P. PT F DISCH PRESS.. p;ig SUCT PRESS.. p.igMAX A 11 SP GR at PT D1FF PHSSS., pii IQ: 12 VAP PRESS. at PT. psia /f jC, DIFFHEAD. ft DES MAX. B.H.P. HP DRIVER DESIGN DIA. IMP. MAX. 01 A. IMPELLER 13 VIS at PT/5S* O- ~ ~0 c. p NPSH AVAIL., ft 14 CORP./EROS caused by t'Q O fOSr_ Myd. H. :.CL 15 CONSTRUCTION CASlNG-M.OUNTiNG {CENTERLINE (FOOT > (BRACKET (VERTICAL SPLIT {AXIAL (RADIAL N.P.S.H. REQD. IN FT. FLUID PUMPED MFRS. BEARING No. RADIAL TYPE (SINGLE VOLUTE I DOUBLE VOLUTE (DIFFUSER TAPPED OPENINGS (VENT^ ) (DRAIN (GAGE CONNS. NOZZLES SIZE ^SA RATING FACING POSITION 21 SUCTION 3 SC 1?F~ THRUST PACKING OR SEAL FLUSHING. GP.M 22 DISCHARGE 23 MATER.A'. CODE--EXTERNAL CASING l-CAST IRON INTERNALS CODE B-BRONZE S-STEEL C--11 -13rj Cr. A-ALLOY h-HARDENED f-FACED IMPELLER INNER CASE PARTS SLEEVE (PACKED) SLEEVE (SEAL) WEAR PARTS SHAFT RE=m INTERNAL PARTS 1 B S| C X 1 B is) c or. )V3U 1 1 (s\ c /\3rA Gk.. 1 otlK-'SL Cr Cr Af Af i C C C C 1 ^t=>TSE. ^'Ef'-tA-f^lcS 1 i 6 Cr | Cr r-;tl_OW "> S S SS MATERIAL EXCEPTIONS BY VENDOR X- MOTOR DRIVER BY ITEM NO. MTD BY HP RPM FRAME MFR OR COMPANY APPV'D. EQUAL TYPE INSUL ENC T^F2 -r TEMP RISE C VOLT S-PHASE7CYCLES 440/3/ BEARINGS LUBE FULL LOAD AMPS REMARKS:|>/X,-S> f\K1 2. \<> TUR8INE DRIVEn BY ITEM NO. MTD BY HP RPM MAT'L MFR and TYPE INLET STEAM, psig TEMP F EXHAUST STEAM RATE, FL IWBHP/HR BEARINGS LUBE NOZZLES SIZE I ASA RATING FACING POSITION INLET [EXHAUST r-^TTS. . G^OTF- fxU-- IT'D . ,ekl-Less -rypg. omuy . PUMP IS TO BE MANUFACTURED IN ACCORDANCE WITH THE FOLLOWING STANDARDS. ( ) IND1CA1 ES ITEM CHANGED ON LATEST REVISION. ^ - Va \=. CHcM|^vli.. i< !NW`-.Ld-:s mix' ^ A ufC rv*) WATER COOLING BEARINGS STUFF. BOX PEDESTAL GLAND TOTAL C.VV. REQD. COUPLING, MFR. COUPLING, TYPE GUAR D MECH. SEAL, MFR. MECH. SEAL. TYFE PACKING DELIVERY, WEEKS PUMP PRICE DRIVER PRICE EST, FREIGHT TOTAL PRICE 0U01 ATION WILL NOT EE CONSIDERED IF SUPPLIER DOES NOT COMPLETE RIGHT HAND COLUMN. CWH 000012423 SHEET- L____ OF rev. V j PI ANT 1 nrATinN . \' " . ENGINEERING CENTER PONCA CITY, OKLAHOMA a.f.e.no. DATE ----- f /* z/7.V-- W.O. NO---------------------- SPECIFICATION SHEET MAOE BY--------- INQ.NO. AP'n ry RFflNO p CENTRIFUGAL PUMPS* b.m.no. p.o.no. --------------------- lf(ti PRn.lFCT Rail. C^fK VAur RztoOcAr ------------------------- 1 APPLICABLE TO: ESTIMATE (*--J PURCHASE ( ) VENDOR 2 irnn /\Jo 3 SERVICE N f--( i/drl k'^.ru^K) ftif-iA MANUFACTURER SIZE ANO TYPE 4 STAGES 5 MOTOR ORIVE I i-+ TURBINE ( 1 6 7 OPERATING CONDITIONS ' RPM ROTATION FACING CPLG. DESIGN EFF. 8 LIQUID \JIK} yt ('m-OniOi* U.S.gpmatPT, NOR. ^0 ' OES 9 OISCH PRESS., psiq / <f V 10 PT F ~~H0 SUCT PRESS.. psigMAX ) q^OES $*O DESIGN B.H.P. MAX. B.H.P. HP DRIVER 11 SPGRatPT i. 0 DIFF PRESS., psi 12 VAP PRESS, at PT, ps>a *y /s- OlFFHEAD.lt /OS' *f ^ DESIGN 01 A. IMP. MAX. DIA. IMPELLER 13 VIS at PT. E3 L'-Sb' c' P NPSH AVAIL., ft // N.P.S.H. REOD. IN 14 CORR/EROS caused by Nc ' FT. FLUID PUMPEO 16 CONSTRUCTION 16 CASING-MOUNTING (CENTERLINE 1 (FOOT ) (BRACKET ) (VERTICAL > MFRS. BEARING No. 17 SPLIT (AXIAL ) IRAOIAL ) RADIAL 18 TYPE (SINGLE VOLUTE ) (DOUBLE VOLUTE 1 (DIFFUSER > THRUST 19 TAPPED OPENINGS (VENT 1 (DRAIN vT" | (GAGE CONNS. 1 20 NOZZLES SIZE ASA RATING FACING | POSITION 21 SUCTION 3 /ST? /?. P. PACKING OR SEAL - FLUSHING. GPM 22 DISCHARGE [ ! / SZI . /' 23 MATERIAL CODE-EXTERNAL CASING INTERNAL PARTS MATERIAL EXCEPTIONS BY VENDOR 24 1--CAST IRON INTERNALS CODE i 8I S C| X 2S B-BRONZE 26 S-STEEL 27 C-l 1-13% Cr IMPELLER INNER CASE PARTS SLEEVE (PACKED} i B fs) C 1 /-l 33V b/zi eA _A-SlL i 5H Cl A 6-szt M -<"/(, Cr Cr At i Af 28 A-ALLOY 29 h-HARDENEO 30 f-FACED SLEEVE (SEAL) WEAR PARTS SHAFT C C c i c SS /.C A A/ 1 R Cr Cr A C.C. ZL ~"7" Af=/-_ S' S S S s A/ 7* .5- 31 X- 32 33 MOTOR DRIVER BY | AAA 1 --r~ TURBINE DRIVER BY U WATER COOLING 34 ITEM NO. MTD8Y ITEM NO. MTD BY BEARINGS 35 HP RPM FRAME HP RPM MAT'L STUCC 30X 36 MFR 37 OR COMPANY APPVD. EQUAL MFR and TYPF ! INLET STEAM, psig TEMP F PEOESTAl GLANO 38 TYPE >r/Zlc l*SUL 39 ENCfrfC TEMP RISE C 40 VOLTS/PHASE/CYCLES ii'iU/3/(1>U EXHAUST STEAM RATE. FL BEARINGS 1D/6HP/HR LUBE TOTAL C.W. flEQO COUPLING. MFR. COUPLING.TYPE 41 BEARINGS LuB'E i NOZZLES J SIZE 1 ASA RATING I FACING POSITION GUARD 42 FULL LOAD AMPS 43 ! INLET 1 1 Exhaust | 1 i ! 1 MECH. SEAL. MFR. MECH. SEAL, TYPE 44 REMARKS: I?, PACKING 45 np fs To /. *>ii i-i tR7O L<J r n-/ 46 C(?&>jr- f'-'r't- t'l &, r1t~ /4L- DELIVERY. WEEKS 47 PUMP PRICE 43 PUMP IS TO 8E MANUFACTURED IN ACCORDANCE WITH THE FOLLOWING STANOAROS. DRIVER PRICE 49 EST. FREIGHT 50 { ) INDICATES ITEM CHANGED ON LATEST REVISION. TOTAL PRICE Vr ' ' * " ** CUH 000012424 r UUUi A HU.* WILL NUI Bfc LUNblUtHtD II* SUPPLIER UUtS NUT CUMPLfc 11 RIGHT HAND COLUMN. SHEET ^ OF --l REV. EQUIPMENT SPECIFICATIONS RAIL CAR VENT RECOVERY SYSTEM LAKE CHARLES VCM PLANT Item No,:. NPK-1 Service: Package Refrigeration Unit Description: The package refrigeration unit is to supply refrigerant to a condenser at approximately -49 F. The.refrigerant will be used to cool and partially condense a vent gas stream to -40 F. The inlet vent gas temperature will vary from +100 F (summer) to +30 F (winter) de pending upon ambient temperature conditions. The system is to con sist of a two stage compression system utilizing R-502 refrigerant or equivalent. ** \ System Requirement:1 2 3 4 5 1. Duty Requirements: Winter duty = 7,0 tons (83,800 ^"j/hr) Summer duty = 24.3 tons (291,800 /hr) Design duty = 30.0 tons (360,000 ^ vhr) 2. , System is to be designed for intermittent service (approximately 8 hours/day) with fast simple startup and shutdown procedures. Provisions, such as a hot gas bypass loop, should be provided to permit system protection under zero load conditions. 3. As no cooling water is available, the system is to use air cooled exchanger(s) as required. Air cooled exchanger design conditions are: 93 F Dry Bulb 80 F Wet Bulb. . 4. A fully automatic oil return and regulation system must be in cluded in the design. Oil will be returned to the system via three 1-inch drawoff points located on the shell side of the condenser. Provisions to observe oil return flow, to separate oil and refrigerant, to heat oil, and to return oil to crankcase automatically as required are to be part of the package re frigeration unit. 5. System should provide for continuous heating in the oil reservoir and in the crankcase to maintain a constant oil viscosity during the shutdown periods. CWH 0000124 Equipment Specifications Rail Car Vent Recovery System Lake Charles VCM Plant Page 2 %-. 6, System should be so designed as to make liquid carryover to the compressor suctions impossible. Liquid knockout pots must be provided for all streams returning to compressor suction. ^ 7. Electric Power Available: 440 volt 3 phase 60 cycle 8. Totally enclosed fan cooled enclosures are to be provided for all motors, 9. This item is to be supplied as a skid-mounted unit ready for in stallation and operation. i' 10, Vendor should supply a recommended spare parts list (if any are recommended.) 11, Vendor may include a proposal on NH-1 as an addendum to this design. CWH 00001.2426 A V" SE a&TE / <-> /VO'Z'Z.LE SCPEPOCB rtARtr 0/0, A*?, S/2 T/rg / SERV/CjE. / / H fL Cr PROCESS lA/LBT 2 -I z/*f CPL& SAMPLE TAP 3 i / CPL& DPAIA/ A/otES l, Srxt* Ta SE VivUtiWPiPIL LtA/LESS LAPCBR P/AA1PrER requires &Y SrnuzruRAL OOa/s/DERA-T'/O'VS. a. Stack /5 8 y Gl'V to BE StARpoare.Q As Rouuir&p ujtftzs, 3. //= stack fS larc-ER TRajJ H/+>. frfid. A T/P C/V pptt-t- HE P.Ouu{E-D RoR Ve*jr Gas Pis PeasioR. . H. STACK OUTLET TO EE PROV/DEP W/TP PLAPRER STT\}A/G 5. ALTERNATE material OF CQSJSTROC-T/DAJ 'SS /S ACCSPTA&LE G. BOTTOM of stack to rave A sealep EPS? cr r VES/G/V DATA OPEPATiA/G TEMPER AT0RB} *P PES/QM TEMPERATCJRBj AtA-TERJA-P OR C.&A/STRUC.T/OA/ AtfgieAjr I O.OAiAA.y~PO A/a/ C--S. A-StL Or G.&'Ji'j, B ST-1 VEa/T stack C-UH 00001242? RA(l CAP VEa/T recover SYSTEM CoM&CO VCM RLAAJ-f /YOZZLB SCHEDULE. M/WK NO. 1 2 NO, JKEQ, { R 5/ZS /5 3/V FL& CPLG SERVfGE MANWAY W/COVER DAVIT LEVEL &AV&E ' 3 i f FtG VENT 9 t 3/V CPLG PRESSURE &AO&E r) a FLGr VAPOR OUTLET g / 3 PLG> PROCESS INLET 7/ 8/ 2 FLG> UTILITY CONNECTiO A/ ; CPL& TEMPERATURE GAUGE 9 / 3 FL& LIQUID outlet /d? / Vy CPLG PRESSURE CONTROLLER LEVEL ALARM^ DR A (A* 1 \" i (\> . NOTE'S 1. LOCATE LOW level ALARM /J.S CLOSE TO BOTTOM as Poss./&LE Lon l&vgl shot off snitch to be P*ovu>g[> to surroow/v MP-! -> CO DES/&A/ DATA OPERATING TEMPERATURE/F DESIGN TEMPERATURE <7= OPERATING pressure^ ps/& DESIGN PRESSUREj PS/G INSULAT/U At MATERIAL op construction CORROSION ALLOWANCE -VO lOOMA)Lj-50M)iN 100 (BO 5" cellular GLASS OR FAVNALBNT A-S/G -- -- Vs " C.S. SEE NOTE *j 2. BOTTOM LEVEL GAUGE 70 BE LOCATED AS *>LOSf 70 BOTTOM TANGENT LINE AS JS PRACTICAL 3. TWO OVERLAPPING LEVEL GAGES WILL BE REQUIRED V, alternate material ; 3oy-ss with +- V/<4>" COAROSfON ALLOWANCE. NT-1 REFR/GCRaTEU vcm receiver RAIL CAR VENT RECOVERY SYSTEM! CONOCO VCM PLANT LAPS CHARLES, LA. map h vr>. 1 2 3 H r & 7 8 7 to u 12 /VOZZLB SCHEDULE A'O. nsQ -S >ZE XZFE. SERVICE ( /s FLG. MAA/WAY W/COVER DAVIT H CPUS LEVEL GAUGE t / PLS VEAfT / 3/v CPL& PRESSOPE &AO&E ) .. 2 pus VAPOR OUTLET 1 3 FLG PROCESS //VLET l 2 FLG> UTILITY COMMENTtO A! ! i GPLS TEMPERATURE GAUGE i 3 FLG LIQUID OUTLET / 3/y CPLG pressure comtR<?ll&R 2 .2 FLG level alarm / Z flg DR AIM n s: oo o o' jo to -G DES16AJ DATA GPEFATlMG TEMPERATURB/F DESfGAt 'TEMPSFtATORS^ F OPERATtA/G PRSSGUPEj Ps/G 0$/GAf PRESSOFEjPS/G I/vsulat/O a! mATZF/AL OR C0A/STRUC7Ioaj CORPOSiOM ALLOWANCE -VO too WAX-50MIA? too 160 S" CELLULAR &LASS OR &OUNAL&A/T A-S/G C.S. '/S " SEE MOTE y A/OTB'.S 1. LOCATE LOW Level ALARM AS CLOSE TO BOTTOM A* POSSIBLE Low LEVEL SMOr-CFP SmrCH TOSS Pfiov/OBO "** 5H*rt>6w* AJp-i2 3 2. BOTTOM LEVEL GAUGE 70 BE LcCATEO AS c'LOSE 70 BOTTOM TAM&EWr LIME AS IS PRACTICAL 3. TWO OVERLAFPlA/G LEVEL GAGES WILL BE REQUIRED V, Altera/atE material: 3oy ss with Vlo." CoAROSlOAl ALLOWANCE MT-\ r- m REFRiGCRaTEO VCM RECEIVER RAIL CAP VEA/T RECOVERY system CQaJOCO VC Alt PL AMT LAKE CHARLES, LA. . / * MARK NO, NO, RE<S 1\ 2i `3 1 V1 5" 1 62 SILL TYPE H FL& ( CPU* y FLO / CPU* 8 PL& vv CPLG SERVICE PROCESS OUTLET VENT PROCESS INLET DRAIN HA/vpP0L W /COVER LVEL GAUGE * NOTE.'- I- VESSEL NAY B FABRICATED FROM] IX IN, C.S. (A'V6) P/PE'.OR SS P/PE CL BOTTOM LEVEL GAUGE C ONNEC TfON TO BE LOCATED AS CLOSE TO BOTTOM TAHG.EA/T u*/E AS /S PRACTICAL 3. altera/ate material or cunstpuot/un *. ss /s accepta i DESIGN- DATA OPERATING TEMPERATURE ^ F DES/GH TEMPERATUREJ *F OPERATING pRESSuA E ,PS/G OES/GW PRESSURE} PstG> MATERIAL OF CONSTPOC.T/0N corrosion allowance Am&IE/JT JOOMAX^SO MiAj o 200 4-.576 C,, S. y&" CUH 000012430 * NT-3. VENT STACK K.O. PROM RA/L CAR VENT RECOVERY SYSTEM CONOCO VCM PLANT CUH 000012431 PROCESS PIPING SCHEDULE PROCESS ENGINEERING DEPARTMENT Date Z-2Z-7*V Hade By Project Cur? Ve^r rj7&rf Plant L*tz>-L Chapc&s Vert Pi.* r Line Designation *V - VCb - / 3- VlA-2 3- VCA-S Z - l/CA -Y H - l/CA-f V- UCA -6 3- l/CA-7 2.- l/CA -a 2 - VCA -? 3 - l/C-/0 V - v-C/i -// 3-VC4-/2 2- KX- / 6- /?*-?. / - P.K-? \ 1 - Rx-V Service Fran To Flow V Rate Normal 1 At T .and P Press J Drop L Lb/Hr Cnzir"mi3> oF Lb/CF Vise PsiG|(crrrrv Cp PSI/ Velocity 100* Ft/Sec Remarks VC MLoADi^cMtoO. (^A>CC 6 /or?/ff /oo -- ST./ 076 i.&) Ra/l CaR Nh/-/ V /92V loo IDO 1.0 0.0tz .04 Nri-l A/r-/ ft /?2V -Vo loo -- -- .03 Nr~t NH-Z y 327 -Vo no o.\ 0.0/0 23 /V//-2 Atr-z V 3 27 /OO 0.1 o.o/e -- A/r-2 NiT-f 1/ 327 /oo o.i 3,0/0 -- A/r-i NP-f L 2b"ooo -Vo -- 62.3 o,?r .?r A/P-/ AJ//-Z. L artfoo -Vo -- 62.3> 1.8?. Mhf-Z Ml6 Psct/tf. L zr<?c?0 -/r -- 62,3 a3T I. ez T-lHO PtV Luo. VCA-Z V -- -- -- -- -- A/RV~*r UAJc VC A - S' 1/ - ---- --. -- Lt/VB VC, A-S v\ - -- -- -- -- NfK-t MH-! L 1 T8o/ O'O -- 76./ 0.2V N //-/ MH-1 MH-t NPM V AffK-f (o.lPtauj) k NPH -/ (o, l 1 l\ rao/ kiSP -- -- -ST) -- o.V o.y/3 .06 I Ni-/-i u I-J2) | 1 1| ! 1! 1 1 i ___ 1| 0.0 to.1/ 2.r Ho-1 ------ 2.2 v.f y.e -- -- -- 0,? ZI.O C.S.ltv C. S. Lj ' A-ru C.S. ex JoYr.S. A-srice.i. ex Ja^s-S. A-&C c.S. *n $Wr& AAU C.S rt/? -T/C r.r. 3o4iS A<lc.e.s.on ?aVs^ /1-S7i (A-Onlc^SS A'RlC rA. On 4-s/c c.s.fi* 4-X/C, C-S rR -^OV^ A'WCfS. 0r?o4ss A-VtJ. On Riss A-rfoc.s. OftJoVjs \A-sucs. On ?0`lsi A-HIC  PROCESS PIPING SCHEDULE PROCESS ENGINEERING DEPARTMENT Date 3-27-741/ Made By Project Rail Caa \ffftUr~Pecoi/. Svs7&n Plant L*k/z C haacg.% \/tn Line Designation Service From TO Flow Press V Rate Normal At T tind P Drop L Lb/Hr Lb/CF Vise PSI/ Velocity F PS1G Cp 100' Ft/Sec Remarks 2 - Si2- U -1 l-N~l SO Lb< %ra*rr MR-X. V L RirtloC-CeJ Live VCA-r V ' n& 2?7 iD o.ii o-otr .or /7 8 JT7-3 0.1*1 -- l^.c H loo - ---- -- -- C. s. C. I, L,^e. * i " oooi,^ -- L________ ______ j _J___ 1l , H z lfl[p Sis r>^ VP J `i CUM 00001243-4 INSTRUMENT .LIST RAIL CAR VENT RECOVERY SYSTEM LAKE CHARLES VCM PLANT ist. No. Typo pFIC-1 Flow Indicating Controller ILC-1 Level Control IPC-l ; Pressure Control ITC-l T -rK Temperature Control ITC-2 1 |FM i ' Temperature Control Flow Indicator LA-1 LA-2 High Level Alarm-' Low Level Alarm TG-1 - TG-2 TG-3 !tg-4 TG-5 ' T G-6 1 LG-1 i LG-2 LG-3 ! LG-4 n c o o ;PG-1 IPG-2 iPG-3 l-* JO cn PG-4 Temperature Gauge Temperature Gauge Temperature Gauge Temperature Gauge Temperature Gauge Temperature Gauge Level Gauge Level Gauge Level Gauge Level Gauge Pressure Gauge Pressure Gauge Pressure Gauge Pressure Gauge Location "-Line VCA-1 Line RX-1 Line VCA-5 Line SL-1 Line VCA-1 Line N-l NT-1 NT-1 Line VCA-2 Line RX-1 Line RX-2 NT-1 Line VCA-5 V, Line VCA-1 NH-1 NT-1 NT-1 NT-2 Line RX-1 Line RX-2 NT-1 Line VCA-8 Type Element' Location Remarks Orifi ce Line VCA-1 4" C.V. Falls Closed Ext, Float NH-1 2n C.V, Bourdon Tube NT-1 2" C.V. Fails Open Filled Bulb Line VCA-5 2" C.V, Fails Closed Filled Bulb Line VCA-1. Resets NPC-1 Rotameter Line N-l -- Float F loat NT-V NT-1 Bimetallic Bimetal lie Bimetallic Bimetal lie Bimetallic Bimetal II c Line VCA-2 Line RX-1 Line RX-2 NT-1 Line VCA-5 Line VCA-1 Reflex Reflex Reflex Reflex ^ NT-1 NT-1 KIT1 _9 r.i-v -oo-mi a, V_.o_.FtjT Bourdon Tube Bourdon Tube Bourdon Tube Bourdon Tube Line RX-1 Line RX-2 NT-1 Line VCA-8 Local Alarm Sounds Local alarm sounds and shuts off NP-1 ) 31 -3\ > POF-T-Mf-OF. ) lOLCv-Z \Z - (<.)> W/ PLANT 1>AK ENGINEERING CENTER PONCA CITY. OKLAHOMA SPECIFICATION SHEET FLOW INSTRUMENTS PliAvr ' PROJECT Ran. &/?, A.F.E. NO.. DATE 2`2 8~*7*j V/.O. NO. MADE 8Y Pr1 _ 1NQ. NO. APP'DBY SEO.NO. . B.M.NOP. O. NO. l/&or Rcc.ooe.x.'t SvIran 1 TAG NO. 2 SERVICE NFtC- t VtiJTU Cw fct-7?/P F~\ C. - --2 " p-' )Vl N'\ "W 3 4 INSTRUMENT. TYPE 5 LOCATION 6 ELEMENT TYPE 7 LOCATION 8 LINE SIZE. IN. } SCHEDULE 9 BORE. IN. 10 RANGE. IN\ H^O 11 METER FACTOR L1 U M 1 D Luca l Haines. L>ut V'CA - I V V0 -:~iTTZJL4c.\*`i Ps Vr L_ KOJT \ C ; "T*. 11 o - zoo fui.L Pa 12 VALVE TYPE 13 14 LOCATION 15 MATERIAL 16 BODY SIZE | 17 PLUG FORM PORT SI2E ec a. 8u<?y u Fcrucor. Ltuc VC(\-\ $tc l. V *' 1 W 5/fl" . 18 AP | MIN | NOR | MAX 19 CALC Cy j VALVE C- | I0 /O 17^ 73 1 20 AIR TO OPEN OR CLOSE 21 MAX.SHUTOFF AP 22 FLUID 23 TEMPERATURE F (`iei0+' \ti f'AtL. 0 > p 11 4 1/iPuYt. CtfLurZusc Lit. hO 24 PRESSURE PSiG f 00 25 APl (M. W.l 26 SP. CR.ATSTO. CONO. k27 SP. GR. AT P. T. |28 CP/CV. AT T.&P. COMPRESSIBILITY &29 VISCOSITY AT P. T. iLZ-'fO) ' 0 .*12. * 0.^2 /.its " 0.10 cp. 1 30 RATE NORMAL )31 RATE| MAX MIN 2 *00.,,1. ________ ________ 1 1 I ( 1 ! I 1 ________ 1______ - uX? CUH 000012.43* SHEET. ( or__ L PEV. 4 PI ANT -1 i. > m:raa v ENGINEERING CENTER PONCA CITY. OKLAHOMA SPECIFICATION SHEET LIQUID LEVEL INSTRUMENTS l/C^7 FLa*jt project 1 A f*/? AFF. NO OATF 7-2.9 -*7V MAnF BY P^-^7 APP'O BY R M NO lNS*>r f?fOt>E#.Y vi n no INO. NO. RECT. NO. P. 0. NO. S^rsrEn i TAG NO. 2 SERVICE 3 4 INSTRUMENT. TYPE 5 LOCATION 6 ELEMENT. TYPE 7 LOCATION 8 RANGE. INCHES 9 INTERFACE 10 UPPER OENSI.TY. LB./CU. FT. 11 LOWER OENSlTY, L6./CU. FT. 12 TEMPERATURE F 13 PRESSURE PSIG 14 VALVE TYPE 15 16 LOCATION 17 MATERIAL 18 BOOY SIZE PORT SI26 19 PLUG FORM 20 AP 1 MiN. NOR. ) MAX. 21 CALC. C VALVE Cv 22 AIR TO OPEN OR CLOSE 23 MAXIMUM SHUTOFF AP 24 FLUID 2b TEMPERATURE F 26 PRESSURE PSIG 27 API IM.W.I 28 SP.GR.AT STO.COND. 29 SP. OR. AT P. & T. 30 WEIGHT % VAPOR IN-OUT 31 VISCOSITY AT P. & T. 32 RATE, NORMAL 33 RATE: 34 MAX. | MIN. 35 NOTES: 11 1. NLC-! ( Re?Ai(~Gfi4*JT ~r v.rno.Cj Ltfjiu E*r, Flu at NH-! 12 ,o. I/a pop / Lt ouio O.V 76 J -BO O* EC L tufa ft L,& tfX-i 2cW SS 2 V/4 1 fun. $/ 2<L Tair\ 0 -- I o.H 1 \Cr.ia>ir.oy., 1 ------------ -------1 Cl osd Ofj Ai/X Fan. S.'XO ?H<i R'TCiZ XermuzzAijr - S'O 0 TT7TO -- /. 2Z o - ioo , 2H tp. reo/ **</>/* |1 1 ------------1-------------i------------ - 1 L---------- 1 ------------ ------ 1 1 ---------- 1o 1 C- o*G<rftu>t 0+j *NH~i A'<S I ilV- Lb. f?.F,- 1 } 1 V1t4 JJU. . value s/2 to bt coaJf/bajet> ey 't/oaj system uea/eo^ CUIH 000012437 SHEET OF / REV V PI ANT (-&* C/+<LZ ENGINEERING CENTER PONCA CITY. OKLAHOMA PRESSURE INSTRUMENTS 1ICfl RjUJr PROJECT /& ft Ca4 r A F F NO nATF 2-28-7*/ w n no MAnF RY p rt APP'O BY INO NO RFO NO. P. 0. NO. f?C.o</e-SLr i TAG NO. 2 SERVICE NPt.-t ^IC-O^U vVai -a/, 1 Iapoa 3 4 INSTRUMENT, TYPE 5 LOCATION 6 RANGE, PSIG 7 ELEMENT P/ir<>Su/? Cuor. Local. 0 - / TO 8 TYPE | MATERIAL ffuvK.TuQil 1 10V Si 9 LOCATION \ NT- } 10 TEMPERATURE F 11 PRESSURE PSiG - HO lo O pn | 12 VALVE TYPE 'LL " ST 13 au-U. YtSOfOT, 14 LOCATION L it-jc. Vc.a- S" 15 MATERIAL 16 BODYSIZE | PORTSI2E 3oHss z \1 17 PLUG FORM A7/c/to " ra 18 & P j MlN. | NOR. | MAX. O 1Too Usd 19 CALC. Cv j VALVE Cv 20 AIR TO OPEN OR CLOSE 21 "'MAX. SHUTOFF ,P SO \?()P<ruVr> 0ft-O 0*J A HI fAIL. 2 SO psttj 22 Fluid N-> . v cn i/Apcm 23 TEMPE. ATURE F (0 0 24 PRESSURE PSIG i oo 25 AP| IM. V. l (30) 26 SP. OR. AT STD C0N0. 27 SP. GR. AT P. & T. (.03 28 WEIGHT * VAPOR IN--OUT 29 VISCOSITY ATP AT. loo -/OO . 0} 8 30 RATE. NORMAL 31 RATE | MAX. | MIN 327 28 700 0 32 NOTES 1 fc* f r=-' iv1!, *E'-* ' t=- ' / i-' - '.-i'Pfl 11 1 I 1 ' 1 __________ 1__________ __ _____________1____________ ^l\ , i *+* CflCr'* {Coooib.) 1 1 ', 1 ! l A/Pt-I TO BE RESET BY A/TC-2 SO^H T&AT TP E SB T PRESSURE^ /A/ PS/BQoAi-Z Ttf B/-OU//A/G TA1Pt?A TVfj * OF ,TRE ltCMj /M ( ; ,V - .' * r *j ' ` ( CUH 000013433 LSHEET___ OP--/ _ REV PLANT. L V C*fAKLS ENGINEERING CENTER PONCA CITY. OKLAHOMA SPECIFICATION SHEET TEMPERATURE INSTRUMENTS VCH Fi-AiJT _ PROJECT KfiUL L*rt. A.F.E.NQ _______________________ OATE i- 2 3-7*/ W O NO MADE BY PS/n . INO. NO.. APPO BY REO. NO.. , Be..Mm..NnUor..yj.itpK. /o.. no. \htuir fecaus*,? 1 TAG NO. NTC-l (3; PTC -7L ? SERVICE 50 psm SrfAtn \/CM L/n<Jt> 3 4 INSTRUMENT TYPE b LOCATION 7'firtP. Co^T/?.dLiJ3e TTA/p CC </ T/?t'a j? L OOQL L-OCA L 6 RANGE F ~10 To iOO /vi ,jlo 7 ELEMENT, TYPE 8 LOCATION ftt.t.D HfAi-R la*}/? VCA - P F/t-i.Tn nrj/.n LiVc \JCA 9 TEMPERATURE f 10 PRESSURE1 PSIG n VALVE TYPE 12 13 LOCATION 14 MATERIAL 15 B00YSIZE. [ PORT SIZE 16 PLUG FORM -207i /0 0 mo B S ftoOT txU4L. ?C*JT. I, l+JiZ $ L- / C.Kft&OtJ if L 2 3/V P/xne podf1 70 ro . 10.0 /on .S BE A'OTE I \ 1 17 AP | MlN. | NOR f MAX. O i 5* 1 5*0 |j 11 18 CALC. Cv | VALVECv S.<6 1 H.2tO% | 19 AIR TO OpN OR CLOSE 20 MAX SHUTOFF A P CloSCIOa/ A\<ZpA(Lt SO 21 , FLUID 5V psii 5rg.\n 22 TEMPE RATURE F 23 " PRESSURE PSIG ^.47 SO 24 APl (M. W.l 25 SP. GR. AT ST0. CONO 26 SP. GR. AT P. & T, av.oz) . O. 6 2. 27 WEIGHT % VAPOR IN-QUT to o - m o 28 VISC05ITY AT P 4 T 29 RATE. NORMAL . o tS ns 30 RATE. 31 MAX 32 NOTES 1 | MIN 5"8 O i O _L --------------------1------------------ 1 1I J.. l, //TC-J. PBSETS Ajpc-/ S-dcH -THAT TPE SB T PPPSSCJPP W PS/& EGVAOJS l/CAt TBPlF'/r'RATVPEj /A/B \2) TcH--0&F5. N-VM'Eu :V5i "* a & -r - CUH 000012439 SHEET. OF. REV. yyggg^f V ENGINEERING CENTER PONCA CITY, OKLAHOMA SPECIFICATION SHEET LIQUID LEVEL INSTRUMENTS PLANT La< V^.n Pt-AtJT PROJECT' Rah- CaK A.F.E. NO.__________________________________ DATE t 2fl7V v/. O. NO. MADE 8Y INQ. NO. APP O BY REQ.NO. B. M. NOP- O. NCL, V-ecj1?f=s> vOC-flT $>YSnzs-r 1 TAG NO. 2 SERVICE 3 4 INSTRUMENT. TYPE 5 LOCATION 6 ELEMENT. TYPE 7 LOCATION 8 RANGE. INCHES 9 INTERFACE 10 UPPER DENSITY. LB./CU. FT. 11 LOWER DENSITY. L6./CU. FT. 12 TEMPERATURE F 13 PRESSURE PSIG 14 VALVE TYPE 15 16 LOCATION 17 MATERIAL 18 SOOY SIZE | PORT SIZE 19 PLUG FORM 20 |AP MIN. NOR. (MAX. 21 CALC. Cv j VALVE Cv 22 ' AIR TO OPEN OR CLOSE 23 MAXIMUMSHUTOFP AP 24 FLUID 2b TEMPERATURE t>F 26 PRESSURE PSIG 27 AP1 |M.W.) 28 SP.GR. ATSTO. COND. 29 SP. OH. AT P. & T. 30 WEIGHT ^ VAPOR IN-OUT 31 VISCOSITY AT P. & T. 32 RATE. NORMAL 33 RATE: 34 MAX. I 35 NOTES. { MIN. N LA-1 NLA-2 VitJHl. CtJLvAfPC Li an to UC Lt autcp t-Tr / Ot: LooJ Lftffii. Ai~A/7r1 i~ pcat-- Fc oa r A/ r-/ L ocA L. f~L OA T /\J T~ t 0*>- Oer- O J - O e e l/*Prrz/ L/C.t4iO \J*pon/Liauic> o, 1 o .1 62.3 -Vo 0 2.3 -VO to 0 tero No+j/Z \ \ \ /\ /\ /\ r/ ---/ \/ \ / \| | / \l / w A /\ *' \/ \l XT \/ \/ \J A /\ ------------ i--r_^i /\ /\ /\ /\ /\ /\ / \/ \ / \/ \ /\ 17 \ ra ! t 0) Tic^r To -es A-S-tC, 0.5. (TK lO^SS. i. --------- -- --1 P~J1---------- 1 (2) > Vessel. Go*j4Jct/cjs Aaa 2/v 1ST)' -Lb flc- !?.f*. (s) ji, - \` , Httr*4 A*ja Loom. * Gir*-{ ; ne O+j A^r- / 7V Jqmmc Qtvtaz May Mio .(Vj LOW LEVtTL ALARM TO 4G TWATE FtOMF A/R-/ SHUT~J>OvJjJ ,v Automatically & iT- CUl-i 0000i2^40 t 1FHrFT OF . P.c.v/ % PLANT . V/ ENGINEERING CENTER PONCA CITY. OKLAHOMA SPECIFICATION SHEET a.f.e.no. DATE 3/? /.?'/- W. 0. NO------------------------MADE BY.Wfl g---- 'NO. NO. TEMPERATURE GAUGES APP'D BY-------------- ^ req. no.------------------------ R M NO P.O. NO. CHARLES 1/041 PLAA/T PROJECT -RA / L C A P VF//T RFCO'/y-PY SYSTF/A 1 TAG 2 NO. 3 //TG-I 4 A/7 0>- 2 5 /j~rC-~ R. 6 1 /V7-& - F- 7 tJ Tr- ' Y7 8 A/TF a 9 SERVICE ye//?4*-/v/twoa// v/>ihor p-so: L/tv/s/o A". `"C2 w\ P'-'i r-? VO/A l-K2.V!-Y VC/A U6>wr'WM~ ** VC/a VAPC'A' ) Vr/y LJO/O'D INSTRUMENT RANGE. F 111 '2 ora 10.'O SO-r tOO io.o -ROv r> >0.0 2 0 /.rs ^ OPERATING { TEMP F 1 LOCATION A.',,&!} .`/T y-oo ~ v^-, ~ 1--, ,'O0 -uo--, tOO !-- !/JB VC A - ~ l)a/e py -/ L /// ~ F> X -- J?. // r -/ Li/;y- V Opt - cT A Mr / T L !,'/;= VC A -1___________________ 10 11 12 13 14 - 15 16 17 18 19 20 21 , 22 23 24 . 25 26 27 28 29 30 31 32 33 V 34 35 4 36 37 38 39 40 (1) ALL GAUGE ELEMENTS TO BE 81 METALLIC UNLESS OTHERWISE NOTED. 41 , 42 ' 43 44 45 46 47 48 49 50 51 52 53 54 55 5G ... . CUH 000012441._ SHEET ! OF f REV FLOW INDICATOR SPECIFICATION RAIL CAR VENT RECOVERY SYSTEM LAKE CHARLES VCM PLANT Tag No. Type NF1--1 Rotameter Location Line N-l Stream Material Stream Pressure, psig Stream Temperature, F Nitrogen 200 Ambient Indicator Type Material Visual Rotameter with Wheel Control as. Normal Flow SCFH Line Size Connection 0-10 1 in. T-5e-lb^Hg-^^ VtOFT & V/"'1' -xu-rsn:- ( t O'JT*--, Note: ^ Rotameter is to be Brooks Instrument Company Sho-Rate Rotameter with metering tube or equivalent. 3- -So CUH 000012442 Item No. Location Upper Fluid Lower Fluid Operating Temp,0 F Design Temp. F Max Min Operating Press. , psig Design Press. , psig Type Glass Length (Approx.) Material Connection \Jb lkl o 000012 s> LEVEL GAUGE SPECIFICATIONS RAIL CAR VENT RECOVERY SYSTEM LAKE CHARLES VCM PLANT \ '>\ (\.Bf^-: ri .i-c. r.. n;i ; \' \J NLG-1 NH-1 R-502 Vapor R-502 Liquid -50 100 -50 0,4 250 Reflex 32 in. SS 1 in. FLG NLG-2 NT-1 VCM, N2 Vapor VCM Liquid -40 100 -50 30 to 100 125 Reflex 47 in. SS 3/4 in. CP LG NLG-3 NT-1 /-oy., \.o. v_y,. v-.o. \crv NLG-4 NT-2 VCM, N2 Vapor VCM Liquid VCM, N2 Vapor VCM Liquid -40 Ambient 100 100 -50 -50 30 to 100 125 . 0 125 Reflex 47 in. SS Reflex 32 in. SS 3/4 in. CP LG 3/4 in. CP LG ^k V ENGINEERING CENTER VWV J PONCA CITY. OKLAHOMA \-f V SPECIFICATION SHEET PRFSSURF GAllfiFS a.f.c.no. DATE .3 SR/lVl W. 0. NO. MADE BY //D S INO. NO. . APP'D BY REQ.NO. R M NO PIANT^^^H CMAff'Le'5', VC/Vf PL/5 //T PRO.IFCT -.RA// n/Sf? \/rr//T ?cC07-P'/ P.O. NO. 1 TAG 2 NO. 3 N.F&r 1 4 upr>- r? 52 6 // p c, - tf 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 45 46 l. 47 48 49 50 51 52 53 54 55 5G SERVICE K-S'OS. P-.tr/.?2 VAPOR VC/A VA POP VC// L/O/V./O \ INSTRUMENT RANGE, PSIG o-- to 0-/0 n -/bo o-uoo 1 OPERATING i PRFSS. PSIG lo.V 'Pre / s,o--/oo OPERATING I TEMP.. F i LOCATION -- <ro --1P/OO \LI//U RX ~ !_____________ L\NB RX-ZL ` NT--I - 7/0 UAtP. VO A ~ P - , V /VO OFFP T/7 PE P?AV7/.'/*iE.O 777 T // ELEMEA/T MAY BE 0> V<*T/R - P'/P-.P' O 7.^r PPOT-- r'r/OV/ TO = /jp to ?.POPZ?Tr pi.iu onnm oaaa OUOTATION WILL NOT BE CONSIDERED If SUPPLIER OOES NOT COMPLETE RIGHT HAND COLUMN. SHEET / Of / REV EFCTK3 w\jr .A PLANT La k if/RfZLCS ENGINEERING CENTER, PONCA cur, OKLAHOMA SPECIFICATION SHEET RELIEF VALVES n Vt?7 fe.A4jr pro irr.T DA Kail. Car "r l A.F.E. NO__________________ DATE- W O. NO. MADE DY. APP-D DY. 1NO. NO-- REO. NO. B. M,. NNOO. .__` P. O NO-------------P---.---O------N---O----------- J K<LouR,r GENERAL. I ITEM NO a TAG . 2 RELIEVES EQUIPMENT NO. 3 MANUFACTURER NRtf-1 L/aja \ZCA-I t AtRxJ'T. L,jJC tfCA - 7 A AiV-i t\-Ti C.D NRV-H MH-! 4 MODEL NO. 5 SERVICE CONDITIONS 6 FLUID 7 STATE N 8 REOUIRED CAPACITY C]fi*J Vi- UL.oAtOtr. L> ! ttM / 0 Yf.rt L (QUID ' IS10 l*A/rZ 9 MOL. WT, SP. GR. IO VISCOSITY 11 COMPRESSIBILITY FACTOR C2S 0.V& O.IC /. /e 02,5_ A OO * 3-5- 12 DCSIGN PRE5S. OF EQUIPMENT -- 13 PRESS. OPERATING RELIEVING 14 TEMP. FLOWING RELIEVING 15 BACK PRESSURE 16 DIFFERENTIAL SET PRESSURE 17 ACCUMULATION 1 too / 00 s pt 1 /57) rui too -VO 5~~ p 5i ^ 2.00 piii 18 BLOW DOWN TV R-56Z Rcfzig, Vtrt.tJ; lf L ia* f0 -- n/.t, 1 /. 2^ UA f><rrz 21100:. ^A/rr 1 (*zs ?. if 0 .ZV -- o.Q(?_______________ /./________________ ZV 0 57) Fit * 1J 2S& 100 1 -VC i $ & a <*i________________ 2. 57>tg> s tJ*_____ 19 BASIS OF SELECTION 20 CODE REQUIREMENT 21 EXPOSED AREA 22 INSULATION THICKNESS 23 OTHER BASIS / Tu/?siac Re nap TutZnAt. Reuse X X 24 DESIGN DETAILS 25 DESIGN TYPE 26 SEAT TYPE FI **JO-D .S>*/aJA- Fla<jas0 Set At AO- FuAAJK-t-O <T PAIl)^ Sfrt/tJi' 27 BONNET [OPEN OR CLOSED) 28 INLET SIZE. RATiNG. FACING 29 OUTLET SIZE. RATING. FACING 30 CALCULATED AREA 31 ORIFICE LETTER | ACTUAL AREA MATERIALS 32 BODY | BONNET 33 SEAT ft DISK 34 GUJOE ft RING 35 SPRING 36 BELLOWS ACCESSORIES Opdfj 2* tr*Lhfi.r. -- v .no 1 c.s. 0. 5. f. 5. CA. 0 P6-/J r JiU 4*. (IP '2" V.r. X> .t/o SS U-J/6 eft eS A~'S/C er.R 5-S err SS SS ss 37 LIFTING LEVER IPLAIN OR PACKEO 30 GAG 39 CODE STAMP 40 CAP l SCREWED OR BOLTED) 41 OTHER Yes bolted Y&S BOLTED NOTES: MANUFACTURER SHALL VERIFY SELECTION OFCRIFICE SIZE AND MATERIALS. 326.VALVES SHALL MEET DIMENSION REQUIREMENTS OF API RP- VALVES SHALL MEET TEST REQUIREMENTS OF API HP 327. Or>Gt) 2" is~o in> ibt.fi 3"/?) 44 R-fifi V'Vyj u Rf. J 1 f.2?7 x. ! /.gjg~ A-fiess \A-&*:ss A'Sic*K$S A'HCerE. ss S5 ^*P4mi5 iA$7c**7f55 A-Wf* rtSS SS Si Ves BOLT D BOLTED CUtf 00001.3445 SUPPLIER TO COMPLETE FORM BY FURNISHING INFORMATION FOH ULANK SPACES SHEET. OF- , 4-43S-S i. ENGINEERING CENTER PONCA CITY, OKLAHOMA A.F.E. NO. SPECIFICATION SHEET RELIEF VALVES - Vv A'R VBA/-T RECOVERY TBtEto nro no : GENERAL 1 ITEM NO. 5 TAG . 2 RELIEVES EQUIPMENT NO. 3 MANUFACTURER 4 MODEL NO. /VRV ~ 5 a/ ~r --) ^A/R V-G LIA/E VC A - ft t '' -- - 7 I A/RY-V /V//-2L 5 SERVICE CONDITIONS 6 FLUID <*':>. VC/VI VAPOR 7 STATE \ VA pr>R 8 REOUIRED CAPACITY 0 MOL. WT. SP. GR. 29300 LS.Y/`P &2-/T 2_/S~ io VISCOSITY 11 CO M PR ESS 101L IT Y FACTOR VjPOR, 12 DESIGN PRESS. OF EQUIPMENT 13 PRESS OPERATING | RELIEVING 14 TEMP. FLOWING j RELIEVING . O/f7 l./ft /SOps/* /no -- CJ o 15 DACK PRESSURE S~ RS/cx' 16 DIFFERENTIAL SET PRESSURE JROpsftq 17 ACCUMULATION 18 BLOW DOWN T. Ltr>/It> l/CM LfO oin 15 70 02.E /,o o ' O. 35 1./& 0.50 -YO 5 ps /o 300 psi<* 50psfa 'b'fe.arY) VA POP -- /?.. 03 O.G2 , <P/5 -- /DO PSio, 5-0 0.7 7 L3 /OS/? i /DO RS/a 19 BASIS OF SELECTION 20 CODE REQUIREMENT 21 EXPOSED AREA 22 INSULATION THICKNESS 23 OTHER BASIS 24 DESIGN DETAILS XX THERMAL ZEutF 25 DESIGN TYPE 26 SEAT TYPE Flam geo RPR/A/E FLA/J&Eb SPRY/Cft FLA/JFrD SRPtA/fft -r-7 l A/RV-ft A/M - O voaa \/APr>n \/A PnR ?~S , 5 \ ft . /5 Os a/ ft /. /a 5.00 Z..RO - /F S~PZ/9 350 PS ! x FLAa/E'ET) 5 PR l A/(ft 27 BONNET IOPEN OR CLOSED) CPE A/ OPS// OPE// 28 INLET SIZE. RATING. FACING 29 OUTLET SIZE. RATING. FACING 30 CALCULATED AREA 3>"/5CLB. R.F. Y*'53tS. R.F. t" /TOLR. R.F. 1"/EOtR. R.f=. 3" / 30 LR. R.F 3,f /TO L R . R.F. 31 ORIFICE LETTER j ACTUAL AREA MATERIALS R___________ A 328 D . f/O J t`2Z>7 32 BODY | BONNET 33 6EAT & DISK 34 GUIDE 6 RING 35 SPRING 36 BELLOWS 4-57frt>A 3 j U-SVg-fH SO 4 *5'//S-#5-S.!4-S/G.o* S3. A-t/C. SS A-S-/C.0P SS A-S/r,,r,f>. 5S A -Jr/F op SS ss SS SS SS C.S, 1 C, 5. c.s. c.s. C.S. c.s. ACCESSORIES 37 LIFTING LEVER IPLAIN OR PACKED OPFi/J 2 ^/'TO'. ^ PF. 3/4 fS~0L3 FS.t. J f-Oft 7 '. *r//i U'SVAorr T>- 4`5/C. OP SS A-'tt/r. f>v ST. ZS ,cF 30 GAG 39 CODE STAMP 40 CAP l SCREWED OR BOLTED 1 41 OTHER YE 5 BOL TED YES BOLTED YES BoltPO YES roltf r> NOTES: MANUFACTURER SHALL VERIFY SELECTION OF ORIFICE SIZE AND MATERIALS. VALVES SHALL MEET DIMENSION REQUIREMENTS OF AP' RP-5Z6VALVES SHALL MEET TEST REQUIREMENTS OF API RP-5Z7. CUH 0000 j. 24 46 SUPPLIER TO COMPLETE FORM HY FURNISHING I currr 3 --4 3 6 --S i 'iT'r-l'-' ENGINEERING CENTER PONCA CITY, OKLAHOMA SPECIFICATION SHEET RELIEF VALVES PLANT LAhf= CHARLES VCM PLA/TT PPFTI Pr.T A.F.E. NO------------------------ /zoateJ-1/2 ? y.. MADE OY_^W1_____ V/ O. NO. INO. NO -- APP'D BY_ REO. NO. B. M. NO-- P. O NO.. CAR VBA/T RPCO'/EPV SYSTEM GENERAL 1 ITEM NO. ft TAG . 2 RELIEVES EOUIPMENT NO. 3 MANUFACTURER 4 MODEL NO. KV'- -fvr /V/? v-- P L1//E VCA-9 5 SERVICE CONDITIONS 6 FLUID 7 STATE 8 RCQUIREO CAPACITY 9 MOL. WT. SP. GR. VC//) L/OUID /'y-sn io VISCOSITY 11 COMPRESSIBILITY FACTOR ^ 12 DESIGN PRESS. OF EQUIPMENT 13 PRESS. OPERATING RELIEVING 14 TEMP FLOWING RELIEVING IS BACK PRESSURE 16 DIFFERENTIAL SET PRESSURE 17 ACCUMULATION 18 CLOW DOWN r. r. 19 1. i p> SOTO 1 -fS S" F>r, / ISO BASIS OF SELECTION 20 CODE REQUIREMENT 21 EXPOSED AREA 22 INSULATION THICKNESS 23 OTHER BASIS 24 DESIGN DETAILS 25 DESIGN TYPE 26 SEAT TYPE , THF-PMAl. RtZLlZF FLA/JGED SPRING 4 27 BONNET IOPEN OR CLOSED OPE A/ 28 INLET SIZE. RATING. FACING 29 OUTLET SIZE. RATING. FACING 30 CALCULATED AREA 31 ORIFICE LETTER ACTUAL AREA l"/ST0/.B P. F. P.F. b 1 \uo MATERIALS 32 CODY | BONNET 33 SEAT ft DISK 34 GUIOE ft RING C.S. | o.s. C.5, C. 5, 1 3S SPRING 36 BELLOWS 0.5, C,-S, ACCESSORIES 37 LIFTING LEVER (PLAIN OR PACKED 38 GAG 39 CODE STAMP 40 CAP (SCREWED OR BOLTEO 1 41 OTHER YES BOLTED NOTES: MANUFACTURER SHALL VERIFY SELECTION OF ORIFICE SIZE AND MATERIALS. VALVES SHALL MEET DIMENSION REQUIREMENTS OF API RP-5Z6VALVES SHALL MEET TEST REQUIREMENTS OF API RP- 527. SUPPLIER TO COMPLETE FORM EIY FURNISHING INFORMATION FOR BLANK 5PACES __________ t__________ 1 f CUIH 0000:12447 ? ? SHEET-________ OF_= REV.. 4 --4 3 5 --S Cui-I OOqqj ?4<? WORK LIST DESCRIPTION RAIL CAR VENT RECOVERY SYSTEM LAKE CHARLES VCM PLANT The following work list is provided as a guide for planning and estimating purposes only. Although it may be used for construction planning, it is not intended as a final work list for construction of this system. 1. 'Jnstall the new VCM loading header and flow control system (4-VCA-l, NFIC-1) and the ten new loading lines from the header to the rail car load ing spots. 2. Install the new rail car vent header (3-VCA-2) and the ten new connections to the existing vent header. Install the line and instrumentation to NH-1. 3. Install the new vent stack, NST-l. 4. Install the new vent stack knockout pot, NT-2, v' 5. Install piping between NT-2 and NST-l (4-VCA-6). 6. Install the new refrigerated VCM receiver, NT-1, and its associated instru mentation. 7. Install the new refrigerated VCM return pump, NP-1, and its associated in strumentation. 8. Install the new refrigerated vent condenser, NH-1 with its associated in strumentation. 9. Install piping between NH-1 and NT-1 and associated instrumentation (3-VCA-3). 10. Install the Vent and Recovered VCM heater, NH-2, and its instrumentation. 11. Install piping between NT-1 and NH-2 with instrumentation.. (2-VCA-4) ' 12. Install piping and instrumentation between NH-2 and NT-2. (4-VCA-5) 13. Install piping and instrumentation between NT-1 and NP-1. (3-VCA-7) 14. Install piping and instrumentation between NP-1 and NH-2. (2-VCA-8) 15. Install piping and instrumentation between NH-2 and P-490 discharge. (2-VCA-9) CWH ooooi 0449 Work List Description Rail Car Vent Recovery System Lake Charles.VCM Plant Page 2 16, Install piping and instrumentation between T-490 and line 3-VCA-2 (3-VCA-l 0). 17, Install the new package refrigeration unit, NPK-1. 18a Install all inter-connecting piping between NH-1 and NPK-l (2-RX-l, 6-RX-2, 1-RX-4, 1-RX-5) with all associated instrumentation. t. CUH 000012450 UH 00001 OPERATING GUIDELINES RAIL CAR VENT RECOVERY SYSTEM LAKE CHARLES VCM PLANT Tank Car Venting - Preliminary Actions 1. Package Refrigeration Unit should be started up at least one hour before start of VCM loading. 2. Check liquid levels in T-490 and NT-1. Levels should be near bottom. 3. Set NPC-1 on automatic so its pressure in PSIG is equal to the tempera ture in F of the VCM being loaded (NTC-'2). 4,. The pressure set point of PC on T-490 should be greater than NPC-1. This should be checked. ** 5. Set NTC-1 at the ambient air temperature. * 6. Check NFI-1 to see if a N2 flow of about 2 SCFH is being maintained. 7. Turn on H-490 fan. 8. Open 4" valve upstream of H-490. Open the two 3" valves downstream of H-490. 9. Open 3" valve upstream of NH-1. Open 3" valve between NH-1 and NT-1* These valves should remain open. 10. Open 2" valve between NT-1 and NH-2. 11. Openthree 2" valves between NH-2 and NT-2. (Controlvalvebypass closed.) 12. Open 2" valve between steam header and NH-2. 13. Insurethat NP-1 discharge is blocked in and that line from NH-2to P-490 discharge is blocked in. Tank Car Venting - Loading Procedure 1. Connect vent line swing arms to rail cars and VCM loading swing arms. 2. Open the 2" valves at the rail cars so the dedicated cars are tied into the existing vent header to H-490 and the nitrogen purged cars are tied into the new VCM loading header and loaded through NFIC-1 . NFIC-1 should be set at 240 gpm maximum. CW/-J OOOotq Operating Guidelines Rail Car Vent Recovery System Lake Charles VCM Plant Page 2 3, Turn on P-411 pumps and fill rail cars as per normal procedure. C, Recovery System Isolation 1. After completion of loading, close rail car vents. 2. Connect N2 to bleed line. Purge through the fine for approximately 5 seconds. 3. Close the bleed valve and the 2" valve below it. Remove the N2 line, then open the bleed and remove the vent swing arm after line is de pressurized. ^ 4. Disconnect VCM loading arms using normal procedure. 5. Raise set points on NPC-1 and PC on T-490 to 125 psig, 6. Close 4" valve upstream of H-490. Close two 3" valvesdownstream oF H-490. 7. Turn off H-490 fan and NPK-1. D, Refrigerated VCM Return 1. Sample the recovered VCM in T-490 and NT-1 and determine whether it can be returned to storage or needs to be reworked. 2. Pump out T-490 as per present operating procedure. - 3. Close the 3" valve upstream of NH-1. Close the 3" valve betweenNH-I and NT-1. Close the 2" valve between NT-1 and NH-2. Close the 2" valve at the outlet of NH-2 between NH-2 and NT-2. 4. Set NTC-1 at -15 F. 5. Open the two 2" valves between NH-2 and P-490 discharge. 6. Open first 2" valve upstream of NH-2 in line 2-VCA-8, 7. Open the 3" valve between NT-1 and NP-1. 000012453 CUH Operating Guidelines Rail Car Vent Recovery System Lake Charles VCM Plant Page 3 8. Crack 2" discharge valve on NP-1 and start pump. Open valve as pump begins to operate. 9, Pump NT-1 until empty. Turn off NP-1. ^ 10. Close 2" valve on discharge of NP-1 and 3M valve on suction of NP-1, 11, Closethe two 2" valves between NH-2 and dischargeof P-490. 12, Closethe first 2" valve upstream of NH-2 in line 2-VCA-8. 13. Open the 2" valve between NT-1 and NH-2. ^ 14, Pressure N2 through the valve downstream of NH-2 to force the condensed VCM from NH-2 to NT-1. 15. Turn off the N2 flow and open the 2" valve between NH-2 and NT-2. 16. . Reset NTC-1 at the ambient air temperature. CUH 000012454 SSfrSTOOOO Hf13 CONOCO YCM P LA A /T