Document vVOq28wpKNxLqvNQrN433ookw

ABDOO185001 PROCESS DESIGN EMISSION RECOVERY SYSTEM ABERDEEN PVC PLANT \ (PROCESS DESIGN NO. D-28) * WORK BY: APPROVED BY: &7WLGU R. "McCrimori ProcessEngineer M. "C._ Jeynigan Process Engineer )ougl^s Michels Chief Process Engineer ABDOO185002 EMISSION RECOVERY SYSTEM ABERDEEN PVC PLANT TABLE OF CONTENTS I. PURPOSE OF DESIGN II.BASIS OF DESIGN FLOW RATE BASIS III. PROCESS DESCRIPTION IV.EQUIPMENT SPECIFICATIONS EQUIPMENT LIST EQUIPMENT SPECIFICATIONS V. INSTRUMENT SPECIFICATIONS INSTRUMENT LIST INSTRUMENT SPECIFICATIONS VI. PROCESS PIPING SCHEDULE VII. WORK LIST VIII. DRAWINGS PLOT LAYOUT DRAWING PROCESS FLOW DRAWING VACUUM RECOVERY SYSTEM - 1 of 2 ABDOO185003 V EMISSION RECOVERY SYSTEM ABERDEEN PVC PLANT PURPOSE OF DESIGN Various waste water and vapor vent streams in the PVC process are con taminated with concentrations of vinyl chloride. Proposed EPA regulations will insist that these streams be treated to minimize their VCM con tent. Currently most of the process waters which contain VCM are being collected and batch stripped in the existing blowdown tank. The existing large reactor recovery system is now employed for this purpose. Most of the minor vapor vent streams are not now being collected. These include: Vents from railcar vapor and liquid hoses Vents from reactor sampling Vents from monomer sampling Vents from tandem seals on process pumps and tank farm pumps Vents from Corken compressors Vents from tank farm sphere and bullets Vents from other process vessels In addition to the above, vents originating from the Capacity Replacement Project will also have to be collected and treated. The project will provide the treating of these streams. A collection header system will be provided as part of a soon to be issued design for collecting these emission sources and routing them to a common treating system. A two stage vacuum-compression system will be provided to compress the vapor streams so that as much VCM as possible can be condensed and thus contained. This system will also pressurize these contaminated streams thus facilitating the eventual final treatment via carbon adsorption or incineration. The system described in this project will also free the existing large reactor recovery system from the task of blowdown tank stripping. This stripping will be handled by the Emission Recovery System described in this design. ABDOO185004 EMISSION RECOVERY SYSTEM ABERDEEN PVC PLANT BASIS OF DESIGN Flow Rate Basis The various emission sources which will be contained with this system were estimated. Details are discussed below. Blowdown Tank - This vessel will periodically be pressured to 10 psig as a result of the receiver draining process. The vessel will subsequently be evacuated with the Emission Recovery System. This procedure will result in total flow of 275 pounds of VCM. Estimated duration of this evacuation is 10 minutes. Rail Area - The estimated, normal continuous load from the railcar area is 16 liters per minute at atmospheric pressure. This minimal vapor flow rate is about' 1 CFM at vacuum pump suction conditions. VCM Receiver - The evacuation of one of the receivers will require the recovery of 690 lbs. of VCM. This will take about 60 minutes with the proposed recovery system. VCM Sampling - Sampling of VCM will require the collection of about 100 CF of vapor. This will take 30 seconds with the proposed system. This system will be used to collect many other sources than those indicated above. ABDOO185005 Ccp^joco mo. ^iD-AiC -IZIZ EMISSION RECOVERY SYSTEM ABERDEEN PVC PLANT ^ III. PROCESS DESCRIPTION This process design consists of a Vacuum Recovery System and is composed of a Vacuum Pump-Compressor System. This system will provide a source of vacuum for the various emission sources. The vapors from these sources will be compressed to 80 psig and the vinyl chloride will subsequently be condensed and collected. i ' Vapors will enter the Vacuum Recovery System from several sources. Fugitive emissions, vessel vents and railcar area sources will flow directly into T-701, the Inlet Knockout Drum. Vapors resulting from large reactor recovery operation, reactor sampling, liquid VCM sampling, receiver draining and filter pack clearing will first flow to the existing Blowdown Tank. They will exit the tank through CV-601 and then flow to T-701. The Blow down Tank and T-701 will normally be equalized via CV-601. When the blowdown tank is being pumped out CV-601 will automatically close to isolate the tank. An open-close switch for CV-601 will be located in the control room. The board operator will use this switch in the procedure for draining the recovered VCM receivers. The pressure in T-701 will be maintained at 20 in. Hg. Vac. via a bleed back vapor stream from the Recovered Monomer Receivers. This system will be controlled by PIC-701 located on a local explosion proof control panel which will be adjacent to the Emission Recovery System. The system is designed to maintain a 20 in. Hg. Vac. pressure in T-701. If the pressure in T-701 exceeds 15 psig, PA-701 will indicate on the local panel and PS-701 will shutdown the vacuum pump and compressor. A shutdown alarm in the large reactor control room will alert operating personnel when this occurs. The Inlet Knockout Drum is equipped with a level well which will sense the liquid level at three locations. LS-701B will sense a high liquid level and will open CV-701. This will drain liquid by gravity into the Blowdown Tank until LS-701Ais activated and closes CV-701. In the event LS-701A/B malfunctions and T-701 fills with liquid LS-701C will be activated and will shutdown the vacuum pump and compressor and also activate the control room shutdown alarm. A level alarm located on the local control panel, LA-701, will also be energized. t / /'s T-701 is an existing vessel in an existing location (Conoco No. 45026). Nozzle modifications will be required for its new service. ABDOO185006 A III. PROCESS DESCRIPTION - CONTINUED Vapors will exit T-701 and flow to the suction of P-704, the Vacuum Pump. The Vacuum Pump is existing equipment (Conoco No. 72-716) which ^ will be relocated from V-12. The pump is rated at5200 CFM at 20 in. Hg.C Vac. The vacuum pump is equipped with a double mechanical seal per --s AFE No. 9525 and 9495 which were approved in December of 1975. The seals will require high pressure service water which will be supplied from the header via rotameters FIC-704A, 704B, 704C, 704D. The vacuum pump is the rotating liquid ring type. Water to the ririg will be supplied by the seal water system via FIC-704. The vapors will be pressurized to about 0 psig at the outlet of the vacuum pump and will flow to T-702, the Vacuum Compressor Seal Water Separator. T-702 is an existing vessel (Conoco No. 45308) now located in V-12. this vessel will be relocated to the northwest area of the first floor of the V-ll building. The tank is to be mounted approximately five feet above grade and equipped with necessary access platforms and ladders. The stream from the vacuum pump will be separated into liquid and vapor. The liquid,which is essentially water, will flow to P-707 or P-708 for circulation or will be drained to T-701 via CV-702. The drain mechanism and shutdown system for level control for T-702 is identical to the system for T-701. T-702 will be equipped with a temperature alarm, TA-702 and pressure alarm, PA-702 which will be on the local panel board. High temperature or pressure in T-702 will also activate the system shutdown previously described. Water from T-702 will be circulated to the liquid rings of the vacuum pump and compressor via the Seal- Water Pump, P-707 or P-70S. This water will flow to FT-709 the Seal Water Filter and then to EA-709A, EA-709B, and EA-709C, the Seal Water Cooler. Cooling water flow to EA-709A, EA-709B, and EA-709C will be controlled by TIC-709 which will be mounted on the local control panel and will maintain a 90F set point. The seal water will exit the cooler and then flow to the liquid ring in the vacuum pump or compressor. Flow to the vacuum pump will be controlled by riC-705 or FIC-704- The three Seal Water Coolers, EA-709A, EA-709B, and EA-709C are existing equipment (Conoco No. 55002, 55004, and 55511). Item No. 55002 will have to be relocated from the adjacent V-ll recovery system while item No. 55004 is now in place. Item No. 55511 will be relocated from V-12. The vapors from T-702 will flow to the suction of the compressor, C-705 or C-706. Only one of these compressors will be operating. In the event of a vacuum pump failure, vapor flow will be direct from T-701 to the compressor. ABDOO185007 A III. PROCESS DESCRIPTION - CONTINUED Each of the compressors will be equipped with double mechanical seals. This mechanical modification is part of this project. The seals will use high pressure service water which will be controlled by FIC-705A, B, C, D or FIC-706 A, B, C, D. The compressor is a rotating liquid ring type and seal water to the liquid ring is supplied via FIC-705 and FIC-706. *175 CFM at 90 psig"^ It will compress the The compressor is rated at vapors to 80 psig and the "apors will then flow to T-703, the Compressor Seal Water Separator. T-703 is existing equipment (Conoco No. 45301). Nozzle modifications will be required. It will be relocated to be adjacent to the proposed location for T-702. T-703 will be equipped with a pressure alarm-shutdown, temperature alarmshutdown and level alarm shutdown identical to T-702. Liquid will drain from T-703 to T-702 via the same level switch system as will be employed on T-701 and T-702. The vapors will exit T-703 and flow to an existing connection at the inlet to the existing large reactor recovery condensers. Here the monomer will be condensed. Subsequent processing of this stream will be coincident with the normal recovered monomer from the polymerization process. For the prevention of polymerization in the seal water system hydroquinone will be injected into the seal water pump suction. This hydroquinone will be obtained from the existing metering pump system. ABDOO185008 EMISSION RECOVERY SYSTEM ABERDEEN PVC PLANT IV. EQUIPMENT SPECIFICATIONS EQUIPMENT LIST Item Description Current Conoco No T-701 - T-702 - T-703 - Inlet Knockout Drum Inlet Knockout Drum Level Well Vacuum Compressor: 'Seal Water Separator Vacuum Seal Separator Level Well Compressor Seal Water Separator Compressor Seal Separator Level Well 45026 Not Existing 45308 Not Existing 45301 Not Existing P-704 P-705 P-706 Vacuum Pump Compressor No. 1 Compressor No. 2 72716 72752 72714 EA-709A EA-709B EA-709C Seal Water Cooler Seal Water Cooler Seal Water Cooler 55002 55004 55311 P-707 P-708 Seal Water Pump Seal Water Pump New New FT-709 Seal Water Filter 64-002 A . NOZZLE SCHEDULE ABP0Q185009 UJ J~ D V- V> uoj v/i vUoJ V W > tr iu to CaLi X 1 vC vc 2 vhO- c VA :*) >< ill UJ UJ a>- u.!I u. wM <v) CO Uj o a '5 - ] J b! u: i- vC ij UJ ui J 5> 11- V) u vo rV/\ Q j i r* _ r v . > 2 eC <<-L \r: 2 VI >: i *> UJ Vc A C. yi ".> UJ vl-'J uJ/ a i. ai J nJ > LU J 1 - >7) , -j UJ UJ _j ) '[ J lL c" _l. uJ _) UJ > .Cl %f J -v' r 5i m u.i yj ai *~i ` I VS 'C'i X X2 \L` I. ioj 2! <n!` C\> c\i ro| <N>|. N I UJ cc h: . oro <2 CD vj i oi /' UJ u. vj! nrj h "3 _ c-l -.1 2" D y u- 0i ID > Ul tCD O UJ pa H v/j '2. vi **' oO vO "nZ> D iU--D- %~ O CO UJ l-- o z vn uJ \*c0>nL V; h ',o O 2 VHI - oJ rh S 'i 'd- M s <JV r/ VO'S 'U sP - -vnC N0-J CLM-\ il h '7 O "k sq II - H 2. S: 5 v JLO cu.` vSj_; "2 O <, OU !| <aKj u. w\ a. oo 2 'JD- LU. O CO ID *CCt U0j. a15: y<-- L0 CO UJ a S a UJ => Q LU Uj a: o y~ a. a. to .. O uJ uj x o cr: o H 2 O UJ 3 o( o a z H>V- < < CO |o uj jo CO Oo _J X a:;. { ft mi CL yto uj g*5s ,, o _i _ y- uj <2 zUJ O CO o o < uj < ABDOO185011 > \ j \ \ ...... ARD.00185.012. ^. 38 vn l o JUJ uj t t~ tc CM 8 a 8.1 lii =; Om o -J cO 2 5f i3 2* 2 UaJ) i i_l Wu h it ot ui vi* s' vf 'O IU O ,-J CL \3 Q. J .. u. t/1 Q VP 5 i i/i o m -j _i v> o 03 </) Q * ** 01 O2 y" *-- ^ \o sj 8y <r ^ A o32 r-r-t ka ??* Ut o X -jj- 3 < uo OJ --1 T < H "1 w o 1----- x~ ^ UJ, >. o Z 7. __ u. Og ar. O3 o2 < u ----'1 ^s LlJ r- Ul 5 -" O \T) r- r --I vl O l_LJ ^ m c<- O< L1 m|| 1 I ............. . l 1 V' >/! UaJ a y (M (N + \t >~--------------------------- L-- Jffl 11 S-* ------------ --.-vfr--. i/I * j* l*- ul o vi v O * oin 5irt 3 uj to-- G -oez-v ABD00185013 cc -i c o -J-- UJ OOJ o!5 o o o or o -J _J UJ ___ >UJ 1<---cOo o o z G- < <o A ABD00185014 EMISSION RECOVERY SYSTEM ABERDEEN PVC PLANT Vacuum Pump Specification (Existing - See Note 1) Item No. Service Type Manufacturer Specification Conditions Of Flow Flow Rate - Operating Rated Rated Temperature- Operating - Rated Pressure - Operating Minimum Rated Outlet TemperaturePressure Seal Water To Rotating Liquid Ring Flow Temperature Motor (See Note 2) Horsepower RPM Enclosure Mechanical Shaft Seals (See Note 3) Type Flush Water Pressure Flush Water Temperature Materials Case Rotor Cones P-704 (Existing 72-751) Recovery Vacuum Pump Rotating Liquid Ring Nash Engineering Co. H-5 Vacuum Pump 200 CFM 130 CFM At 26 in Hg. Vac 200 CFM At 20 in Hg. Vac 120F 20 in Hg. Vac. 26 in Hg. Vac. 26 in Hg. Vac. 130 F 0 psig 6 GPM 90F 15 1150 Explosion Proof Double, Unbalanced 200 psig 60F Cast Iron Stainless Steel ABD00185015 Vacuum Pump Specification (Existing - See Note 1) Notes: 1. Vacuum pump is to be existing Conoco equipment. Item is now located in V-12 and is to be relocated to the Emission Recovery System. Item is Conoco No. 72-751. 2. Motor is to be existing Conoco equipment. The current motor now located in V-12 is suitable. Item is Conoco No. 70-300. 3. Double mechanical seals are to be installed on the selected vacuum pump. Funds have previously been provided for this project on AFE Nos. 9525 and 9495. 4. Required spare parts for this equipment should be obtained from other existing H-5 vacuum pumps now located at Aberdeen. 5. Vacuum pump and motor are to be completely overhauled prior to use in this service. A Jl.'LY 1, 1970 subject to chonfj" ~iihout notice; Supersedes oil previous pertotmtince dotes. Prtn'td in U...A. ABD00185016 ft* ? pumps * *l+S -- i V' i ' Hi ! . .. * *r r* . ' W 70 typo-H JS PUMPS--SIZES H5, HG 'i .imp vacuum * h t.OttUAL SCAL OPU 5 10 IS 20 26 t.C JO 10 6.0 K> PERFORMANCE OF 55t* 20055*0 30"BAA. AGE SEAL "TATCR K5 VACUUM PUMP EN 51* S63 e 20 VACUUM - INCHES OF MERCURY , s*jt n.U> u . pa jc B-4 i 9 July i, 1970 tubjcct lo change without notice; Kipcrtcdet oil previoul di<nrniionj o:id imloliotion doto. Printed in U.S.A, ABD00185017 pumps types L*H ( V. /' Drawing 14-1851 1 Kotor *C OOP 1c FC D EF H0 K H--! M N P Q K5 256T I 284T 284TS 3| 286T <A 286TS jj 284U i, 286U 324T 324T5 jj 324$ Sj 3241) 3 326U 3 326S 4 36CU :) 364US 57 5/8 58 5/8 57 1/8 60 1/8 58 5/3 58 7/S 60 3/8 CO 1/4 59 5/8 59 1/8 61 5/8 63 1/8 60 5/8 63 1/2 61 5/8 59 5/8 61 7/6 60 3/8 64 1/8 61 7/8 62 1/8 63 5/8 64 63 3/8 62 7/8 65 1/8 66 5/8 64 3/8 67 3/4 66 1/8 13 3/8 14 1/4 12 7/6 15 13 5/8 14 1/2 15 1/4 15 7/8 14 3/8 13 7/8 16 1/4 17 14 5/8 13 15 3/8 1 in. 1/8 1 in. 1/8 1 in. 10 7/8 3 12 3/8 4 1/4 13 3/8 7 1/4 14 1/2 16 1/4 4 3/16 - 46 1/4 48 23 46 43 10 1/8 20 1/4 22 1/4 4 5/16 29 66 60 7/8 1 in. 4 3/4 6 `Length when coupling specified by Nash Engineering Ccmpany, with gap as shown. * NOTES: 1. Items listed below are furnished only if specifically erderec. See Engineering Data Sheet. No. Item 1 Pump Vacuum with Companion Flanges 2 Kotor 3 Coupling 4 Guard 5 Base 6 Cock 7 Valve Control 8 Valve Solenoid 9 Strainer 10 Gland lantern 11 Valve Check 12 Gage Vacuum 13 Valve Relief 2. Piping, valves, and fittings shown in single lines are furnished by Nash Eng. Co. only if ordered. 3. Foundation bolts are not furnished. 4. Do not use this drawing for installation unless certified correct for your order. 5. Dimensions are in inches. 6. Piping connection dimensions are approximate. 7. Pipe threads are American Standard. U. For installation and operation sec Instruction. Bulletins. - ji K U.V. A- J.*.*-C.*wwitt pumps .. types L-H ABD00185018 PUMPS--SIZES L3 THRU L3, H4 THRU H9 JULY 1. 1970 subject lo chonqe without notice; supersedes till previous cron sections. Printed in II S.A. FS \J I __, 1=\------ r----------\T\\ < 1i \ IL \\J i>j1 \ .. i 4 !/ i t / D Cut B-27 inf T77 3 : il *. i Part i No. 101 i 102 j 104 105 :! 108 1 109 110 i 111 : J 112 'X 114* 3.JS 115 116 Part Name Body Head Cone-Drive End Cone-Idle End Bracket-Drive End Bracket-Idle End Rotor Shaft Gland Shaft Sleeve Bearing Cap-Outer-Drive End Bearing Cap-Inner-Drive End Part No. Part Name 117 116 119 120 125** 126 127 128 131 131A 132 134 Bearing Cap-Outcr-Idle End Bearing Cap-Inner-Idle End Bearing-Drive End Bearing-Idle End Shaft Nut-Drive End Shaft Nut-Idle End Rotor Key Packing Water Slincer-Drive End Water Slinoer-ldle End Gasket 8ody Gasket-Bearing Cao-Drive End Part No. Part Name 135 Gasket-Bearing Cap-Idle End 141 0iler For Bearing 142 Shaft Seal-Drive End 142A Shaft Seal-Idle End 153* lock Screw-Shaft Sleeve 154** Lockwasher-Shaft Nut-Drive End 155 Lockwasher-Shaft Nut-Idle End 164 Set Of Shims 170 Bearing Spacer (L3-H9 only) 178 Vent Cap Not required for sizes 14, HS and oelow. Not required for sizes 13 and H4. JT> rJ 1 liW.: 55OC06 TM u> *' -`J-?'- ABD00185019 EMISSION RECOVERY SYSTEM ABERDEEN PVC PLANT Compressor Specifications (Existing - See Note 1) Item Nos. Service Type Manuafacturer Specification Conditions Of Flow Flow Rate - Operating Rated Rated Temperature- Operating Rated Pressure Operating Rated Outlet Temperature Pressure Seal Water To Rotating Liquid Ring Flow Temperature Motor (See Note 2) Horsepower RPM Enclosure Mechanical Shaft Seals Type Flush Water Pressure Flush Water Temperature Materials Case Rotor Cones C-705 $ C-706 (Two Required) Recovery Compressor Rotating Liquid Ring Nash Engineering Company Nash 1253 C 177 CFM 170 CFM At 105 psig 177 CFM At 60 psig 130F 65 psig 105 psig 125F 65 psig 16 GPM 90F 75 1770 Explosion Proof (See Note 3) Double, Unbalanced 200 psig 60F Cast Iron Stainless Steel ABDOO185020 Compressor Specifications (Existing - See Note 1) Notes: 1. Compressors are to be existing Conoco equipment. One compressor is now located in V-12 and will be relocated to the Emission Recovery System. The remaining 1253C Compressor is now located in the V-10 Stores Area. Conoco equipment numbers are 72-714 and 72-752. 2. Motors are to be existing Conoco equipment. Both motors are now located in V-12, Conoco equipment No. 70-298 and 70-299. 3. Double mechanical seals are to be installed on each of the compressors. Funds should be included in this project. 4. Required spare parts may be available from other existing equipment or from the warehouse. 5. Both compressors and motors are to be completely overhauled prior to use in this service. r ABDOO185021 JULY 1, 1970 subject to change without notice; supersedes alt previous performance data. compressors series 125& Printed in U.S.A. COMPRESSORS-SIZES 1251, 1253 ~> 100 75 c o a v> 50 X a d> 25 NASH ENGINEERING COMPANY SOUTH NORWALK. COHN..- U.S.A. page C-415 ABDOO185022 Ji'L'r 1, 197^ subject to thonge without notice; supersedes oM previous performoncc doto. Printed in U.S.A. ABDOO185023 ____ V[ compressors r'i&4i.& sr > series 1250 COMPRESSORS-SIZES 1251C, 1253C 9 rs 0 25 c PRCUUKt * POUNW PCh SQUARE INCH **. FEBRUARY 1, 1971 uibjccl lo chongc without notice; tupotedei oil previoui dimentions and nitalla'ion da'o. tinted in U S.A, ABDOO185024 C0MPRES50R3-SIZFS 1251, 1253 k-- J .J fTt v"""-r;--! [4]' A 1.L pumps .................... " scries 1250 r* tE t.L* or 1--\ pt JZmtr min Drawing 14-2614 Motor *C ODP TEKC D 324TS 63-1/2 64-3/4 14-3/8 324T 326TS 65 65 56 -- 66-1/4 15-7/8 15-1/8 326T 66-1/2 67-1/2 16-5/8 364TS 55-1/2 69-3/4 15-3/8 3641 67-5/3 72 17-1/2 36STS 66-1/2 70-3/4 15-7/8 365T 68-5/8 73 18 j 404TS 68-1/2 73 17-1/8 404T 71-1/2 76 20-1/8 E 1/8 Weights Pump 970 lbs. Separator 460 lbs. Base 280 lbs. Length when coupling specified by Nash Engineering Co., with gap as shown. NOTES: 1. Items listed below are furnished only if specifi cally ordered, (see Engineering Data Sheet.) 1 Compressor with Companion Flanges 2 Motor 3 Coupling 4 Guard Coupling 5 6ase 6 Separator with Float Valve 7 Glass Gage 8 Valve Relief 9 Elbow 10 Nipple 11 Funnel 12 Gage Pressure 13 bnicn Orifice 14 Val'-e Solenoid 15 Valve Check 16 Filter Inlet 17 S^lencer 18 Strainer 19 Valve Control 2C Arrester Snocfc 21 Anti Siphun 22 Silencer filter 2. Piping, valves and fittings shown in single ^ines are furnished by Nash Engineering Co., only if ordered. 3. Foundation bolts are not furnished. 4. For certification refer to Engineering Data Sheet. 5. Puttp flanges are A.S.A. STD. 125 lbs. Pipe tb-eads are American Standard. 6. Piping connection dimensions are approximate. 7. Dimension are in inches. 6. for installation ana operation see Instruction Bulletins. I n i/l 1 Y*-- i -i -V' por.e v O'? vst- FEBRUARY 1, 1971 lubject to chon^e without notice; supersedes oil pe*ious cron sections. Printed in U.S.A. ABDOO185025 compressors JVseries 125/3 COMPRESSORS-SIZES 1251C, 1253C 1* 4 J '3S '5 H Part ';;Vj No. 1 101 A i02 r| 103 a 104 Pi 108 -1 109 "l no *1 111 112 fart Name Body Head-Drive End head-idle End Cone bracket-drive End Bracket-Idle End Rotor Shaft Gland-Drive And Idle End Part No. 114 115 116 117 118 119 120 .126 127 Part' Name Shaft Sleeve-Drive And Idle End Bearing Cap-Outer Drive End Bearing Cap-Inner Drive End Bearing Cap-Outer Idle End Bearing Cap-Inner Idle End Bearing-Drive End Bearino-Idle End Shaft Nut Rotor Key Part No. 128 131 132 132A 134 135 153 155 164 169 Part Name Packing-Orive Ar.d Idle End SIinger-Drive And Idle End Gasket-Head-Drive End Gasket-Head-Idle End l Gasket-searing Cap-Idle End Lockscrew-Shaft Sleeve Lockwasher-Shaft Nut Set of Shims Lantern Gland-Cr^ve And Idle nd if. i1 kSvir.4*''^w--1 '' ' =' " :l a'jr ' i.v,\Ke*a*ic*bir&CA *- . 3 MtU: r~ ---------------------- --ABPOet&5'626r V\ // V a PLANT. n 6EK9EZH PVt ENGINEERING CENTER A.F.E.NO_________ ____ . PONCA CITY. OKLAHOMA OATP to -7--7/- W. 0. NO. SPF.CIPICATION SHEET made ry Q&rr INO NO APP'n RY REG. NO. SHfLL TUBE EXCHANGERS. R M NO PuA^r PROJECT --SsLUSt^'____ Setwe/ZY P. 0. NO. Sfi r.f7 EM no. ft TAG -70S A (Cu.jc<> No. SS'OOZ') SERVICE OP UNIT nTr? CL oo^- H/Z. --i 3^ MCIJK ft . xo kill humo ft r*ciKG NO. f?c ft* TING ft t ACIN9 4 1 NI.O { 3 hi) $o(ti= / 7- (SC 5 oyllfT 1 3 /si) Jo a? / 2-- /SI) <oR.i- 6 VCMT / Vh- icoo C-PlO* 7 O^ilH 1 fa 3000 C?L(r 8 1# MV .nosM 9 PMUI SIZE' TYPE ivoa CONNECT ED IN < ) PARALLEL ( > SERIES FFF.SURP.PFRUNIT. sq ft l~7Q SHELLSPER UNIT / SHELL DIAM. /C :i/*/ IN. El- F. SURF. PER SHELL, so f; /70 NO. TUBES PER SHELL "7 2.LENGTH / */V IN. UNITS RED'D. / 10. Cwt N "iT DELIVERY. WEEKS PRICE. PER UNIT 12 SLIP-ON NOZZLE FLANGES ALLOWED|fYES ) (NO) EST. FREIGHT COST 13 SLIP-ON END FLANGES ALLOWED (YES) (NO) TOTAL PRICE 14 GASKETS: SHELL DOLLARS PER SQUARE FOOT 15 CHANNEL MATERIALS: (MARK SR AND PERCENT XR) T(wp 16 FLOATING-HEAD COVER 17 18 TEST RING REOUIRED (YES) (NO) 19 SPARE GASKETS REOUiRED (YES) (NO) 20. STACKING HIGH TUBES ITEM SHELL SHELL COVER (REM) (INTEG) CHANNEL MAT'L. DEG. F SPECIFICATION /? -Z.H A-yjis a 2& r 21 INSULATION THICKNESS IN. CHANNEL COVER (REM) (INTEG) 22 NO. TUBES 73 OD 3/* IN.: MIN.THK. /& SU)C'r~ Vt. 23 LENGTH ,}'()" FT;PITCH tr//h IN. <&'/ Sr <&) 24 SHELL DIAM IN. tt S.V TLow IN. FLOATING-HEAD COVER TUBE SHEETS BAFFLES AND SUPPORT PLATES s /J-2fcS~-C. 25 TRANSVERSE BAFFLE TYPE SPACING IN. BOLTING: SHELL COVER 26 PERCENT CUT (VERT.) (HORIZ.) (45 DEG) CHANNEL 27 LONG BAFFLE TYPE 28 TEMA CLASS R IMPINGEMENT BAFFLE (YES) (NO) ASME CODE RED'D y,< FLOATING HEAD CHANNEL COVER 29 PERFORMANCE OF ONF. UNIT 30 31H 32 33 34 FLUID CIRCULATED ' TOTAL FLUID ENTERING. VAPOR. Ib/hr Ib/hr SHELL SIDE CLcouirJi*' 0tJ /* rp.,z In no a IN OUT -- --- TUBE SIDE 5 OAl. U)/\ri?tL / To o o IN OUT .-- -- 35 LIQUID, Ib/hr -- -- ____ -- 36 STEAM. Ib/hr -- ---- 37 WATER. 38 NONCONDENSABLES. Ib/hr Ib/hr 3 cre-mw 3 crtnrv -- / `iUxrO ______ -- 39 GRAVITY; 40 MOL. WT: VAPOR SG @ GO F /a -- LO /. () /a 41 MOL. WT; NONCONDENSABLES 42 VISCOSITY: LIQUID. CP 43 HEAT; '> SP. 44 THERM. COND: VAP. LIO. 4b TEMPERATURE 46 OPERATING PRESSURE 4/ VELOCITY --- V/lti S' "70 F UO G> F F Qo Ps>9 -CO- FPS --- ^ no /. o @ IOO -- _ f O/iV- e -70 /. O F e /3 b F f -- o.WQ nO /- o @ cf 0 f f 48 NO. PASSES 49 PRESSURE DROP 50 ' FOULING RESISTANCE (MIN.) hi PRESSURE, psiij 62 DESIGN TEMPERATURE. DEG F 63 CORROSION ALLOWANCE: IN. f psi ALLOW CALC Ci.Oc l DESIGN f<rn TEST *4 no 2 Z.ST t/t(o ALLOW DESIGN -4 CALC 0. Oof /S7j TEST 400 -2.2.JT l rlL. 65 Tvo (>7` 'wr l/.V 2&JL. TRANSFER RATE. SERVICE / 2 2_ _WEJ Gi 1TSPI_R_S 11 LI.: _ SNIiVING 1~30 6) *: FUl L CP WATER CLEAN lb; /6/ BUNDLT lb. KOI l b or sk>u TMH CAl.CUk. A1 cm i.'ji.a nor L-> jE HVICP /m iS *$ If AT AiJ THAI i `>.srii/E'VVdcR- A/Airt^CiCotwHi^tAsArior<pe>.r/ToJunc <^zu\rCa on extnolo'|a\"~uc-a-)--is--t-o---a-c.--o-c--c-r--l-a-s-c- o---b-y-------p--c-m-c--c-k--t--r-n-H---a-i--l r-iiriM i; n t o coN^Lf 'M iiY ruiiNi'jHmn nK-OKUMICK I-'.'II heam; 5.. ACIS I SMELT______ or_________ rev_________________ D & R ST`D UL VOG4 - U U H O F T 2 SURFACE ABD0Q185028 ENGINEERING CENTER A.r-.E. NO______________ WV PONCA CITY. OKLAHOMA . SPECIFICATION SHEET DATE 10- (a ~7(a _ MADE BYjZ/7___ __ APP'D BY______________ _ W. 0. NO._ INQ. NO. _ REQ. NO. _ SHELL a TUBE EXCHANGERS . B.M. NO. PLANT fiBE/?V*l.J?VL_'__&4Atr_ PROJECT JL?Ai7 lii/O/J tfeco _ P. 0. NO. _ Sjtsr^rt 3 1 ITEM NO. ft Tag EA-yOQS CCoujoCO No.'TSVOHI 2 SHELL SIDE TUBE SIDE 3 ML>7 Z L f t HO iZ l ATINQ FAC>6 HO. till PHtlS', * PACINO 4 IMLCT 1 o Vr *11 ( 7- KF-f0 5 CUH 1 T \ 3 (2\~ to ( ? IZ C VENT l -7.1700 C'7^ 7 ORAIN 8 71 MP 9 P*i CON * 1 'T.CVTJ C'PLir- 10 SERVICE OF UNIT MANUFACTURER SIZE .$ TYPE La )/7 ATTX CUr7ju&/Z 4 (fiORI/^ (VT3CT-) CONNECTED IN ( ) PARALLEL ( ) SERIES F.FF. SURF. PGR UNIT, sq ft )~lO SHELLS PER UNIT / SHELL DIAM / Q IN. F.FF. SURF. PER SHELL, ki ft / "7 0 NO. TUBES PER SHELL '711fNGTH / TnI UNITS REQ'D. DELIVERY. WEEKS / 11 12' SUP-ON N077LE FLANGES ALLOWCO IYESj3' (NO) 13 SLIP-ON END FLANGES ALLOWED (YESTlNG) PRICE, PER UNIT EST. FREIGHT COST TOTAL PRICE 14 GASKETS: SHELL 15 CHANNEL 16 FLOATING-HEAD COVER 17 18 TEST RING REQUIRED (YES) (NO) DOLLARS PER SQUARE FOOT MATERIALS: (MARK SR AND PERCENT XR) TfVP ITEM MAT'L. DEG. F SPECIFICATION TUBES A-2.1 f SHELL A-r3t? 19 SPARE GASKETS REQUIRED (YES) (NO) SHELL COVER (REM) (INTEG) _d -2.fc.r- 20 STACKING HIGH CHANNEL 21 INSULATION'THICKNESS IN. CHANNEL COVER (REM) (INTEG) 22 NO. TUBES 7 2_ OD 3/v IN.: MIN. THK. 23 LENGTH / ^ '(J '< FT;PlTCH in- 24 SHELL DIAM /,) J/.f IN. ,V '.VSw "W. D=Oj IN. FLOATING-HEAD COVER TUBE SHEETS BAFFLES AND SUPPORT PLATES 25 TRANSVERSE BAFFLE TYPE SPACING IN. 26 PERCENT CUT (VERT.) (HORIZ.) (45 DEG) 27 LONG BAFFLE TYPE IMPINGEMENT BAFFLE (YES) (NO) BOLTING: SHELL COVER CHANNEL FLOATING HEAD 28 TEMA CLASS R ASME CODE RED'D '/^ $ CHANNEL COVER 29 30 31 FLUID Cl RCULATED 32 TOTAL FLUID ENTERING. 33 34 VAPOR. 35 LIQUID, 36 STEAM. Ib/hr Ib/hr Ib/hr Ib/hr PERFORMANCE OF ONE UNIT SHELLSIDE ('i_ro t-/ "^crzszm IN LOt^jTzn OUT ---- .-- ---- TUBE SIDE . t. U)*-ne/!>. r>77Zr~C IN OUT 1 --' .-- 37 WATER, 38 NONCONDENSABLES, Ib/hr Ib/hr '3o-Cr~0-V -- -- ts'l'-v'O / S. ~Zrz~ti -- 39 40 41 42 43 44 45 46 47 48 49 50 51 52 Nt*L GRAVITY; LIO. DEG API; SG @ 60 F 1.0 t. 0 MOL. WT: VAPOR MOL. WT; NONCONDENSABLES -- *-- -- VISCOSITY: LIQUID. CP /),YV ~Id f no f1 0.9$ e *7 6- F1 HEAT; LATENT '.V SP. t, O 1:0 / U THERM.COND: . VAP. LIO. F F F TEMPERATURE OPERATING PRESSURE F So psig CO / (TO / 3 (J 1^ VELOCITY FPS NO. PASSES 1 PRESSURE DROP psi ALLOW CALC ALLOW CALC FOULING RESISTANCE (MIN.) PRESSURE, p*.g , era/ 2zrDESIGN />7> TEST .cn)} DESIGN / 07? test DESIGN TEMPERATURE, DEG. F ^CrO CORROSION ALLOWANCE: IN. MTD (\E3 (CORR) f TRANSFER RATE: SERVICE WEIGHTS PER SHELL: SHIPPING VlO *2,3. /2,, 2- (3try lb; FULL OF WATER HEAT EXCHANGED. 8TU/HR CLEAN lb; BUNDLE '//o ^(YfjVZrO /. (0 ` -- -- n6 f.6 <7 0 zzr lb. f F MOtl i, T HC CALCUt ATLO SCItVlCf: Ht' AT 1 HAUSUtt RAT E (OUT SIDE Ti.Hl!. ARC A OH CXTCNIlFO ARC A) lf TO RC IU-CREASED BY peucuxrso exc****t- PERCENT roH AM. SUN" II. R TO COI.'i'LPT f I ORM RY I UHNISHING INF (HIM AT I ON I OH BLANK SRACTS SHEET OF. .. nrv________________ 4 21 u *-\r 1 ^ D & R ST*D UL 4VO<b - \Z H n o FT2 SURFACE ABD90435O3fr ENGINEERING CENTER PONCA C/TV. OKLAHOMA SPECIFICATION SHEET SHELL & TUDE EXCHANGERS. PLANT {^QF-rt..0 g.gAZ P\/r. Pu AMr PROJECT A.F.E. NO_____________ DATE f V- 'IP~ 7k MADE BY L?b-rt APP'D DY_____________ B. M. NO W. 0. NO.. INQ. NO. . RQ. NO. P. 0. NO. A "p 2 3 4 5 6 7 6 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 47 48 49 50 51 52 53 54 55 5_7_ 'bp 59 &ITEM NO. T AG A-16$C(trx)OCO !\L .ST3J1 shell side 'TUBE SIDE *0171 t HQ Vi 7 1 PAllKG * rClNO NO. !l( MATING ft FACING i*H r t OUH.IT vr N T OP* IK It. v* / 3 ; >7; m-SQ / *5 /5?J Rfii<\ f 9/V ?<nrD CFOs- f 1 ( i-- is 7) 7- nv a Pk'CO s c't * SERVICE OE UNIT $/)(_ U)^rr/t Csrtn Sy? MANUFACTURER VoYie. AnO /Znrt4 ___i SIZE TYPE ^ThORIZV (TC2J) CONNECTED IN ( 1 PAR ALLCL ( ) SERIES (if F. SURF. PER UNIT. iq ft mo SHELLS PER UNIT / SHELL DIAM Vw IN. EFF. SURF. PER SHELL.sq ft i no 7NO. TUBES PER SHELL 2-ENGTH 1 V / UNITS REO'D. / IN. . DELIVERY. WEEKS )SLIP-ON NOZZLE FLANGES ALLOWEOtffES' (NO) SLIP-ON END f LANGES ALLOWED (YES) (NO) GASKETS: SHELL CHANNEL FLOATING-HEAD COVER TEST RING REQUIRED {VESI (NO) SPARE GASKETS REQUIRED (YES) (NO) STACKING HIGH INSULATION THICKNESS IN. NO. TUBES 7 2- OD LENGTH /2-' Cl*4 SHELL DIAM/0 ?/Y in. ?/u IN.: MIN. THK. I {JvU4c- -at FT;PITCH rr >i /ft. in. /q n=s$x) kf A K i OIAM * LSLO* IN. TRANSVERSE BAFFLE TYPE SPACING IN. PERCENT CUT (VERT.) (H0RI2.) (45 DEG) PRICE. PER UNIT . EST. FREIGHT COST TOTAL PRICE DOLLARS PER SQUARE FOOT MATERIALS: (MARK SR AND PERCENT XR) T f * ft ITEM MAT'L. DEG. F SPECIFICATION TUBES SHELL SHELL COVER (REM) (INTEG) zZJLH____ A nn A CHANNEL CHANNEL COVER (REM) (INTcG) FLOATING HEAD COVER TUBE SHEETS jr-Zbrc. BAFFLES AND SUPPORT PLATES BOLTING: SHELL COVER CHANNEL LONG BAFFLE TYPE TEMA CLASS R IMPINGEMENT 8AFFLE (YES) (NO) FLOATING HEAD A5ME CODE REO'D y^s CHANNEL COVER PERFORMANCE OF ONE UNIT SHELL SIDE TUBE SIDE FLUID Cl HCULATED TOTAL FLUID ENTERING. VAPOR. LIQUID, STEAM. WATER. NONCONDENSABLES. Ib/hr Ib/hr Ib/hr Ib/hr Ib/hr Ib/hr C, tJ-CS L Lc 3 irzrtro . ___ IN OUT -- -- -- 3 crzrCz> -- 3 crv~W -- nnrzm IN -- -- -- 1 \~LrzrO OUT -- -- lT7vrm GRAVITY; LIO. DEG API; SG @ 60 F MOL.WT: VAPOR MOL. WT: NONCONDENSABLES VISCOSITY: I.IOUIO.CP HEAT; ||'iTMJ " SP. ..va. THERM. COND: .. .V- U.. VAP. LIO. TEMPERATURE OPERATING PRESSURE VELOCITY F psig FPS /.0 -- -- fi# 7o /*6 VO Ca 0 F F / r() i.O 1.0 -- ---- 70 f .`yy'e 777 f .HF* no /* c @ F /' 0 & F / 0 @ / cm> -- i3Q ~nr _____ f F NO PASSES PRESSURE DROP FOULING RESISTANCE (MIN.) PRESSURE, t'sig ) psi ALLOW CALC , Crvi DESIGN IS 7) test ___________________ V ALLOW CALC ______ - o-Qi ___________ . . DESIGN /ST) TEST DESIGN TEMPERATURE, DEG. F CORROSION ALLOWANCE: IN. MTD IKSaLICORR) F TRANSFER RATE: SERVICE nLb.e rLZT' V.'FIGHTS PER SHELL: SHIPPING jl (fZ) Id. FULL OF WATER HEAT EXCHANGED. BTU/HR 1/g /,, fr?) flTTf) CLEAN BUNDLE toi _______ lb; N'Oir-S 1Mr CA1.CUl.ATL-D .SI!..nnVvICE HL AT 1 RANSFtn RATE (OUTSIPE TUBE ARf A (JltXXTE KJE'D AREA) IS 7 0 HE PC CREASED IIY Th ifDCSiGNCMCULAltON' $ /}-> G-Kl$77+Jb-^ X.Lt-OCA7lA ________________________ iS.\ `ctfAzLe**/** SDf'I'l ICS 1 O C.OV.f'Lt 7 L fO'iM BY I IJi'lMSiUNG HtT-ORMM ION TOR UL ANK SPACES sheet_______ _____ or________ ri.ncr.N7 rou au p.r.v ____ ABDft,ftl.a.5Q32 t-ott ENGINEERING CENTER a.fe.no. E*JIE33 .- DATE \SPECIFICATION SHEET MADE BV V APP'n RV pi ant i nrATinN) CENTRIFUGAL PUMPS b.m.no. ' pro.ifot MtSSJ0M^ P/fPOl/Pfl-V W.O. NO. INQ.NO. RFG NO p.o.no. SYJ A i APPLICABLE TO. EMlMATEl ) PURCHASE l 1 2 Tf). ajo. ~Tr^7&7~ir7'- 7(1* 3 SERVICE S^/)/ kJAT~/?tf P/J/^PS 4/ 5 MOTOR DRIVE \V\ TURBINE ( ) 6 7^ 8 UOUID y/)T. & 9 10 PT F J& OPERATING CONDITIONS U.S.gpmat PT. NOR. D1SCH PRESS., osig t/H SUCT PRESS., psig MAX DES DES O 11 SPGRjiPT <J?L DIFF PRESS., psi 7PT 12 VAP PRESS, at PT, ps-a ^.7, DIFFHEAD.fi I'JJP 13 VIS at PT, Sstfe , 0,5NPSH AVAIL.. U / 14 CORR/EROS caused by 15 CONSTRUCTION 1C CASING'MOUNTING (CENTERLINE 1 (FOOT t (8RACKET ) (VERTICAL ) 17 SPLIT (AXIAL ) (RAOIAL 1 18 TYPE (SINGLE VOLUTE I (DOUBLE VOLUTE ) (DIFFUSER ) 19 TAPPED OPENINGS (VENT )() (DRAIN )C ) (GAGE CONNS. 1 20 I 21 i NOZZLES SUCTION 1 | SIZE ' I 1 ASA RATING ; : FACING | j POSITION 22 j DISCHARGE i ' 23 1 24 * 25 2Cj 27j 28 ' 29 30 31 32 MATERIAL CODE-EXTERNAL CASING 1-CASTlRON j INTERNALS CODE B-BRONZE S-STEEL C -- 11-13% Cr | | | IMPELLER INNER CASE PARTS SLEEVE (PACKED) A-ALL0Y 1 SLEEVE iSEAL) h-HAROENED 1 f-FACED 1 WEAR PARTS SHAFT X- .1 f)7-nvc.r//. XtfD'J INTERNAL PARTS i 1 G1 S1 Ci II 3 . & C 1 1 i S c Cr ! Cr Af . At c 1 c c c: 1 i B Cr s isi s --------1--------1 1 Cr ` s \ 'i : 1 Q X 33 MOTOR DRIVER RY TURBINE DRIVER BY 34 ITEM NO. MTDBY \ ITEM NO. MTO BY 35 HP 36 MFR RPM FRAME 37 OR COMPANY APPV'D. EQUAL 1 HP RPM 1 MFR j'ltj TYPE ! INLET STEAM, ps.g MAT L TEMP F 38 TYPE 39 ENC 't?XP INSUL RISE C EXHAUST ! STEAM RATE. FL Ib-BHP HR 40 VOLTS PHASE-CYCLES /*/(.& BEARINGS LU3E 41 BEARINGS lGb NOZZLES (SIZE 1 ASA RATING 1 FACING < POSITION 42 FULL LOAD AMPS 43 INLET ,1 j[Exhaust i 1| 44 REMARKS; 451 46 __ s/tJ.okir ____aj/ t// svvja/ 47 4.8 49 50 1 PUMP IS TO BE MANUFACTURED IN ACCORDANCE WITH THE FOLLOWING STANDARDS. WVJ l ) INDICATES ITEM CHANGED ON LATEST REVISION. VENDOR MANUFACTURER SIZE AND TYPE STAGES RPM ROTATION FACING CPLG OESIGN EFF. DESIGN P. H.P. MAX B.H.P. HP DRIVER OESIGN DIA. JMP. MAX. DIA. IMPELLER N.P S.H. REQD. IN FT. FLUID PUMPED MFRS. BEARING No. RADIAL THRUST PACKING OR SEAL FLUSHING. GPM MATERIAL EXCEPTIONS BY VENDOR V WATER COOLING BEARINGS STUFF 30X pedestal GLAND TOTAL C IV REQD. COUPLING MFR COUPLING. TYPE GUARD MECH. SEAL. MFR MECH SEAL. TYPE PACKING DELIVERY. WEEKS pump price DRIVER PRICE EST. FREIGHT TOTAL PRICE quotation will not be considered if supplier does not complete RIGHT HAND COLUMN. SHEET------ OF REV jiBDaQ185031 y/)c pumP comp/usson. -I t.sxz x #= af .Hb /*'/*> If ,/ > SUCUON I>P. ESS UEE Origin P r e cur e pair* Static Dead psi Line Lnsr. A P psi u m p suer; o_m_p aa s s u r e _ pr. ia NET POSITIVE SUCTION HE/- G Static Head reel -Line Lose feet mn if / /4u . i . 2- LIQUID PULPING TEMP. F VISCOSITY ( }30J c VAPOR PRESS. F P r, i SPECIFIC CRAV.I' //GALL ON C/^2 G?M . < /btf'E GPM JL<l A?<?J .0. | : 30 j .30 i + Vapor Pvcf?. Correction AVAIL/. RLE L/SH DISCHARGE PRESSURE fr e t -2. ;M e L J.3i* DIFFERENTIAL PRESSURE Delivery I'ni^/ar e poia 7*7 Discharge Prcsa.pcia = Y / Static Head pci S>*^ S u c t i o n Prcsr>.____p s i a = '~A A P Control V a 1 v c (5 } A P Exeban;er (s ) AP /R// 7T/2 A P Ori[icc(e] psi pci pa i psi 3.^ AT O TOTAL PUMP A P ( gt I / -> ` 7 ,~i GPM DESIGN = .Line Loss A P psi / BRAKE HORSEPOWER Other. 2 psi Min. Dyr osi PUMP DISCHARGE PR CSS. psi. MAX] M U M S U C T 10 N P R E S S U R E SS-rl BHP = J^^pm_>^7r?5U //. ? !;i 7 ; b ?; 0 , Hu mi) i _ Vessel S. V. Settinr- p y la l Of3 Static Head pci -5 PUMP CA or . * FT p;na Usr.i MAXIMUM DiSCHARCC MSS UR E PLANT Job No. Pump No. /AT Max. Suction Press. pci a. t(S,Z By: Checked: 5 Norm a I Purnn A R < pci IS Date .. T p s i a IHD'X. Sketch No. ir bubble point V-. p. corr. Or Xq , /3L.1 - vapor pr ABDQ0185Q3'1 PLANT. Ahtrcfte+J ENGINEERING CENTER PONCA CITY. OKLAHOMA SPECIFICATION SHEET A F E NO DATE___ MADE BY. APP'D BY. PfC* e M NO project F/ais^/oaH, #ece>e//?tty W 0 NO INO NO REO NO P 0 NO sy*rpm A _ i*4sosa &e*aw TTAM A/O AT- 70 9__________________ Ag'/Pl/tCX 3A/)L /aJATAA /=7jir^ locnr/oJ 0ischfipcz cf NP-ie747ax , ____ rys>_______________ P. A PL TTlI OCA - v57^^/m d/}>jaia FL U/O TCttP */? NORMAL CQcst ?// ) PdBSi. PsiC mn.rpL Ccxs{o^) ft&tOXATBJ cJtifiM*. A/OAmA/ f~atsi****) JPCC/P/C. GreVi'Jv 7~A*)& P ________ //s co6//y , Cp /?/ 7~/}sJ6 P______________ % |<K J g'rtL cJat-jf/% fC0-J<T0 fjoo) 7#-/0O f/S~d) 30 P CO ) 0.<M /Vc- Fes/*/ ____/Ul0tJ*#Le O/easJ AP>. FS'_______________ Pflpr* c/ /?/T*JT/b*J. ____ WAT'teP/O/ aA OcJ-sTeuc-T/aA A/a rvst Ar/e/>?e*J A 3 JCO c. s. Pt>/\jjo f~d/y u /SaJ? ____ A/.OTF \__ L/A sx/jr/A/c y.n &)AJ0C6 . A/O. 1 r Jen) e*J aj c/ OtJtA^ c///)fi6 ij7~P A/LTA/Z T6D&DBR P'/crsP. f,//er,4t 7yf ji/nsaj-j/^a -c/ra SHEET OF_________ t' ABDOO185035 EMISSION RECOVERY SYSTEM ABERDEEN PVC PLANT V. INSTRUMENT SPECIFICATIONS Instrument List Item FIC-701 FIC-704 FIC-705 FIC-706 FIC-704A FIC-704B FIC-704C FIC-704D FIC-705A FIC-705B FIC-705C FIC-705D FIC-706A FIC-706B FIC-707C FIC-706D Description / Rotameter \ 6PM (4- Rotameter") Rotameter / froCteL 11 G2 RotameterJ Rotameter Rotameter \ Rotameter zoo PS Rotameter Rotameter Rotameter Rotameter Rotameter l y 1 <ar/V\ 10 P Rotameter Rotameter Rotameter j Rotameter PG-701 PG-702 PG-703 PG-704 PG-709A PG-709B Pressure Gauge Pressure Gauge Pressure Gauge Pressure Gauge Pressure Gauge Pressure Gauge PIC-701 Pressure Indicating Controller PA-701 PA-702 PA-703 Pressure Alarm - High Pressure Alarm - High Pressure Alarm - High PS-701 PS-702 PS-703 Pressure Switch Pressure Switch Pressure Switch LG-701 LG-702 LG-703 LA-701 LA-702 LA-703 Level Gauge') Level Gauge JLevel Gauge Level Alarm Level Alarm Level Alarm Location Ins. Flush T-701 Line HM-739 Line RM-736 Line HM-733 Vac. Pump P-704 Vac. Pump P-704 Vac. Pump P-704 Vac. Pump P-704 Compres. C-705 Compres. C-705 Compres. C-705 Compres. C-705 Compres. C-706 Compres. C-706 Compres. C-706 Compres. C-706 T-701 T-702 T-703 P-704 P-709 FT-709 Line HM-701 --=^ T-701 T-702 T-703 T-701 T-702 T-703 T-701 T-702 T-703 T-701 T-702 T-703 A ABDOO185036 v. INSTRUMENT SPECIFICATIONS - CONTINUED Item Description .Location LS-701A LS-701B LS-701C LS-702A LS-702B LS-702C LS-703A LS-703B LS-703C Level Switch Level Switch Level Switch Level Switch Level Switch Level Switch Level Switch Level Switch Level Switch T-701 T-701 T-701 T-702 T-702 T-702 T-703 T-703 T-703 TG-701 TG-702 TG-703 TG-709 TG-709A TG-709B TG-709C Temperature Gauge Temperature Gauge Temperature Gauge Temperature Gauge Temperature Gauge Temperature Gauge Temperature Gauge T-701 T-702 T-703 Line HM-726 EA-709A EA-709B EA-709C TA-702 TA-703 Temperature Alarm Temperature Alarm T-702 T-703 TS-702 TS-703 Temperature Switch Temperature Switch T-702 T-703 TIC-709 Temperature Indicating Controller Line HM-726 - CV-701 CV-702 CV-703 CV-601 On-Off Valve On-Off Valve On-Off Valve On-Off Valve T-701 T-702 T-703 Blowdown Tank SV-701 SV-702 SV-703 SV-704 SV-705 SV-706 Relief Valve Relief Valve Relief Valve Relief Valve Relief Valve Relief Valve T-701 T-702 T-703 Line HM-707 Line HM-710 Line HM-712 RD-701 RD-702 RD-703 RD-704 RD-705 RD-706 Rupture Disc Rupture Disc Rupture Disc Rupture Disc Rupture Disc Rupture Disc T-701 T-702 T-703 Line HM-707 Line HM-710 Line HM-712 RO-704A R0-704B R0-70SA R0-705B R0-706A RO-706B Restriction Orifice Resti'iction Orifice Restriction Orifice Restriction Orifice Restriction Orifice Restriction Orifice Line HM-763 Line HM-764 Line HM-775 Line HM-774 Line HM-782 Line HM-781 A ABDOO185037 V. INSTRUMENT SPECIFICATIONS - CONTINUED Item Description Shutdown Description Local Panel Board Description Location ABD00t35O3fr- B 4 EMGi!\'!-`G CENIEsl . POWCA CITY. OKLAHOMA v Ef'!:C:rKV,710N ft*:CT FLOW INSTRUMENTS plant ABEEPftEN PVC PROJECT A.E.C. N0.___ ___________________ DATE I Oj\t I~\ U it T>. NO WADE by. JTO IN-O. NO. APPOHYREQ.NU. M. NO.__.P- 0. NO. ; *1 ] 7/.C.'. !0. : ? { rii;vt<x *1 :d1 E 51 ? <> i ) 71 e 0| : 5i ' ::>i ^ `.1 1 7V-7 U.-/.-G ! lO.V7:v-< Iff. } ro'.r.iN. LUf:' S. .v.-or, FIC-7QI_____________ ; HPSW FLUSH TO- LVA/-70\ . 1. ROTAMETER UM. _._J____________ J !i 1 i! ! ' \ Vi > .-VM* 1 f \f. \ I.GCAT/n ! 1! ! * U j . ^01 rr:.''vi;:-?. | \7 i rcvi:-'.- j , | O' ; | ';ox , ;/A>: r | -'ii-C r.r i .'Ai.i c- vo j i.r \ to o-r ; c- cvxe t 1 r-'.y. rKL-rv^;- r . i i v-> v-i i.t-* ! i [ j. I HPSVtf -70 P-0 o Tie'S \ t 23 i cm:v. at r f.. | rvv.vir.'VG' -i.: .V 1 j ;t, j v ;vv--.vv p. /, 1.0 1.0 I ITTqg J so: />/*? i .5* 2- T i." 1 L ; ! i i j : ! \ j \ ! i i ; !i j; [j <i ______________ '______ ii \ . ; 1 ! _____________ ______ 1_________________ i | i i i : j _ J ..... ! 1 ... Jr > J i ! i .--------------- :? ; ; !; i i i : ; : ; i :1 1 :1---------------; ; i ! 1 i J* j i ! -t | !- i t i i* > >: A. 4 f L >**v*wrtg;taHur #; 'fa-VfpyArj^. l i i t i i $> cr__________;-> ABDOO185039- bt\*/V;;*7*&. V *c* hvC* /v"- |I *i.vi; r i^ *\t ZC'>1** /Cu>'\!lTLr;r; t, PONC.X CITY. OKLAHOMA S?C4'I-T-ATION fM'CT FLor;iK$rnu^*fiNTs K.f E. NO._______________________ DATE \t\l\\HQ W. O. NO. ,, MADE DTjSSltt. INO.NO.. AT'P'ORYPEG. NO.. 8 M. NO.. P. 0. NO. p pi/int ApB2D-fcM P\/C rroFrrFAll^SiriMS eeecveisv systetw A i i,Ai-sDnn *;*. t :< | FIC-7C4 .. . i5AL WAT02. i PlC-lO.S iSALWftTCR . ! PIC~'7C>^ SEAU WATHR ! i : <1 i l>:* fn:_r*r.;<7. TY1-* t 5 ! U-; Lti 1 '''-r; ';v',; t | U\ = Ul. ! LCtf.' OUL*-' 1 /^/OUfTAjA Cetobitii F/c^TajO . Co*jr*//c(L /7bJ -Z*JO. fo'i'/r'o/tA 2-HA- 7? C 2-Vs* _ >7^3 i O-s/n- 7*9 rtCTA A7T/?/t. d7/yiie71^/1. ) S 2-*/'- 7J 2 \ VO \ X- t ^4) X VO \ 1 9 i ro.-.r.i.-/. ------- - __ i `. 10} :;. .h?o ; \ 'i } -i:*. :-r. 1 1? j w.:.'.e ivn: ' .... i }/* t i.ryvT/;,^ ir*| 16 1 re:.'- i -- - ,. <See AJer/?' j, rc'T o' ~ i :-- ; ___ 1 i ^uc. A/d>r^ / ; | :i -- <V<S Xor& / ; ________ i i ii ; ; ) i_ ! W|r;.ooK.-:o \ Vo 1 { MM, ; ; ;,:a>: r )<\ i w'"LC r.i ; VAi.v' C.- ; 20 \ A:n to o-- : O'. r/.7,:z t 2* ! r.Hwro- r- ,'j. e 22 j y-f-'j \ : Vi - ^ 1 n.- <i VO i J _J i LOA77Z& 90 70 _ i1 i! ...J_ _______i . i_____ ' r !: j .; * | i ua r/r# j fO ! 70 liiA-ne/t Gr> ; ! i i T^/i ^.f}!.AYi.AT. J j c'/*.:v a7 7 | c';v.vf<vr-i. 'l: t'Y j ;r0 i v :;. wv /-, r. /, i, j ; rv.Yi. vO-1-...-'. ! i-.'-'.rl :.y j S-jSiiiSiisJ /? /.& ! J.o. \ ! t.o / <9 1 i . 7t i i * Lo /. <o ! i: i /OOTb (/J use. F'SCHFf i foursfooeL //SZ. i , ! ______ !i j . : ': ! 1 i \ t i i ` Lawirrj^V!rri**^-wMMTMv'r MtrMrn<n'3urrc(^M.-n)r%u-oi^<.<..K:a.-.:knruMr<QM.''^;<' ! V-VtT_________ O nT\ ABLtlQfl1.aSQ4Q. ARDQni8SQ41 EM f*'l rv5'.;cr-,f /** (^i;l \< t ti\' I..1.I..I V < L. 1. . V, vX. '* PONCA CITY. OKLAHOMA C?^C4n-.''JkTION :DIZCT FLOW IK'STflUL'ENTS plant ASERDEEKI P.N/C .PROJECT IV: w1 orwTn/./;iso. >.riC-7P5 As IeSjSsb! `HPSVM FUUSK__jKPSuJ FLUSH A.F.E.NC. DATE 1P/H HADE [|Y*J] APP'D (JY 8 M. NO.. w. 0. r.O. INO. NO.. ____ RFC. NO. P. 0. NO. A :fic-"jo5c. ;fic- < HP^uJ FLUSH___uAPSlM FUlSil 4 >>v-' *W .r 4nivyA> I J * i ti SaL*T.... ........ C*1_____ Pf*'. J ABDOO185042 A P PLANT ABEgD&g 1 [ TAO NO. ? { f if;vice PVC_ CENTER PONCA CITY, OKLAHOMA CTECl^CATJON fMECT FLO?s IMSTHUWEN1S project emissions A.P.E.NO. DATE 4 WADE BYilR/fl" V/.O. NO._ INO. NO.,, APP'OflYRFC. NO. BM.noP.O.NO. Raccvew svsi-gm W~ .w K I M--m I ,IMIP) r * P> WM ' /,* ^1P FtCrtOfo A_____ I,_J_E__J_i_J_C__f_e__B__.________________ _ ____;__\JPELSCs-3TL^>6_J0Z_.. iMP^tOFuUg.U -MPg>u;> PUJgH i HPSuS FUU.SH HPS,u;-PLUSH___ : ii \L ' :C ! rc'O- -1 " ?. j v.^ j j "i`' f ox ; i.'.ax Q'^Qrx ~io o-: x c^c^ojj It 23 j -s-r- I WAT^T2. ! "70 o0 ______ L_Q0 |~?oJ cr.-cv AT 7_tp. | C'pp-x'OH,- v.:'i V | .._LUJPrIS2^ a>ATgP. _ _J_J3JC2__. ,,7g..... . ?__-_0__D_ !.................................. SAtiLL_2. O* 4__iajy_______ a&S________..................... .... . C_LlL:1.0 j i t f \ \ \ \ ;i * t s > 1t I* ABDOO185043 ENGINEERING CENTER PONCA CITY. OKLAHOMA SPECIFICATION SHEET PRESSURE GAUGES PLANT_.ABEReEEWJ?VCproject OAlSSlCMS RE^VT2>/ Af E NO ______ oate icm/rib W 0 NO MADE INQ NO __ APP 0 BY REQ. NO _ B M NO SVSTEAA P 0 NO 1 TAG 2 NO. SERVICE 3 s/CA\ VAFDE. / WATER- 4 e6i -.1 at. VOV\ VAPOR/ WATER:. b VCM VAPO- / WATER. 6 PS --)<54 VCtV\ VAP A7 P&.-1CQ WATQ^ 8 P&'IC&R WATEe 9 10 1 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 3'-' 38 39 40 41 INSTRUMENT RANGE. PSIG ' 7 oVAifac-200 30'/% tfCt^JOO ^6- W O - .} /9/0 0- OPERATING PRESS, fgS 3c"/A Mr. O 0 fit/ C /oC> //>d OPERATING TEMP., OF /.r<? IZO /JO /JO /JO /JO LOCATION T-IOI T--7DZ T'-1D^ P-T64 PllCtfAOSe P--7D1 discharge PT--7C& DlSCHAQfifc 43! 44 | '451 46 J? 48 49 90 52 531 54] "55 56j________ _____________ QUOTATION WILL NOT R CONSIDERED IE SUl'Pl 11R DOES NG1 f.OMPU ^ E RIGHT HAND COLUMN SHEET________ 01 RU ABDOO185044 A v Ahe.re/trtrJ PLANT. ENGINEERING CENTER PONCA CITY. OKLAHOMA SPECIFICATION SHEET PRESSURE INSTRUMENTS fit/C. PROJECT. tr/y)/.',S/0*JS A.F.E. NO.. DATE ___ W. 0. NO. MADE BY. INQ. NO. APP'D BY_ REO. NO. 8. M. NO.. P. 0. NO. /tCet/A\/ <iv.cr/rt 1 TAG NO. 2 SERVICE p/C.1- 70 / i/cm f/etj 3 4 INSTRUMENT, TYPE 7b T. -7/0/ Preti.TAiA. <?aoT/. 5 LOCATION 6 RANGE. PSlG 7 1LEMfcNT 8 TYPE | MATERIAL 3 0/i/L C W/A Pftft. 77? SI*JS. filttpk 9 LOCATION 10 TEMPERATURE F 11 PRESSURE PS'C 12 VALVE TYPE T 7/3 i t*rn |________a p// ___________ 13 //if.. AtO 14 LOCATION P*ct/~ 70f - 76 t IS MATERIAL 16 BOOY SIZE | PORT SIZE C. s zrr 17 PLUG FORM 18 A P | MIN. | NOR. MAX. 1 74> 1 19 CALC <tef] VALVE Cv 776) r 20 AIR TOOP'EN OR CLOSE 21 MAX SHUTOFF . P 22 FLUID AT/) Zoo Uc/*i i/apofL 23 TEMPERATURE F 24 PRESSURE PSIG 25 API :M. W.) 70 Lft . 26 SP. CR. AT STD CONO. fi/St. 27 SP. GR. AT P. & 1. 2. / 7 28 WEIGHT % VAPOR IN-OUT &29 VISCOSITY AT P. T. 30 RATE. NORMAL /t//^ j |31 RATE MAX. M!N. j32 NOTES OIL / z oo __ 1 1 11 1 __ -- . 1 __________ L 1 1- 1 - 1 J__ _______. __________ 1__________ v c<- sr Iffi/itc. t4) ic. 7^> tavcJ/e rr/auS Li SHEET. OF. REV. ABDOO185045 A PLANT. E-E333 v ENGINEERING CENTER PONCA CITY. OKLAHOMA SPECIFICATION SHEET A.F.E. NO.. DATE ___ MADE BY_ PRESSURE INSTRUMENTS APP'D BY_ 0f?p Me B. M. NO. ^PROJECT:f*iss/d/J rfscM/g/tv W.O. NO. INQ. NO.. REQ. NO. P. 0. NO. sysr&/n 1 TAG NO pa - -- ~VA- 7AA 2 SERVICE 3 4 INSTRUMENT. TYPE 5 LOCATION 6 RANGE, PSlG 7 ELEMENT /Jr*A PsesS Jr-?*/ ALAPm RDP/L A o - no P/eM. ^SO/TcK //it, A PStS <, 'ST-yoZ* Pil PifiA popp o .0 - /OO PftiS S0~>i i-zX. 8 TYPE | MATERIAL Oiah S*+k 9 LOCATION 10 TEMPERATURE F 11 PRESSURE PSlG 12 TYPE S UP 13 T/)& . pJo. ~r~ io / JJ o LSL.____________ _________________ AT Ji.r.Mi C> 0A - ?/) t T~-7^ /v3 0 &S PT/*. c. A/-!' r_ - 70 2, 14 Uc&K>]3n 15 MATERIAL 16 s*ttDY$lZE 1 . PORT SIZE./ 17 PFORM 18 A p | MAX- 1 1 1 19 CALC. Cv >^'*N.VALV6 Cv ________ 1 1 20 .-iR^CC^OPEN OR Cf&SS^ 21 ,XTax SHUTOFF- 6P --PTT^TZT-- MS* A. Pse-J < "Vc yo* P)/S)/?S^ a dp/to c- Press SuJt+eA. Difiok JfM 7^ 7*3 /J 0 SCO S'^C.7V/C PS - P D ? , 1 1( .............. 1 1 1V 22 FLUID 23 TEMPERATURE 0F 24 PRESSURE PSlG 2b API (M W 1 26 SP. GR. AT STD. CONO. 27 SP. GR. AT P. & T. 28 WEIGHT S VAPOR IN-OUT 29 VISCOSITY AT P. & T. 30 RATE. NORMAL 31 RATE | MAX | MIN 32 NOTES: | _ ______J______ __________ ece________ ------------- E--------EE ------------------------------ (l) Pf> - 7<9// 702.j 70>_J 70 0c. /'<&//-j/q /r>`>/Pi'~ &/a s. efJ Uc/font./ ^2) PS-76/; )eit >_) t4> 6c. t4 isS /;jA S^s-Sc^ . SHEET. OF. REV. m9 ABDOO185046 PLANT ENGINEERING CENTER PONCA CITY. OKLAHOMA SPECIFICATION SHEET LIQUID LEVEL INSTRUMENTS _ project /r/v/ss/d'Js- AFt NO________________ _____ OATF_____________ W O NO MADE UY INO NO. APP'U BYHLO NO u0 mM.. iNOvj _________.P. 0. v/NO. . f}ECrt///?Ay sur&Ai 1 TAG NO 2 SERVICE 3 4 INST nUMCNl. TYPE 5 LOCATION 6 F.LEMf-NT. TYPF 7 LOCATION 8 RANGE, INCHES 9 INTGRrACE 10 UPPER DENSITY, Lfl./CU. FT, 1 LOWER DENSITY, LB./CU. FT. 12 TEMPERATURE l 13 ;M PRFSPURE PSlG VALVE TYPE IS 16 LOCATION 1? MATERIAL 13 19 20 j 21 | 22 SODYGlZi 1 PORTSIZS PLUG FORM j {&P l/i'N. NOR. | MAX. CALC. Cv | VALVe Cv AiR 1 0 OPEN OR CLOSE 23 MAXIMUM CHUTOM- A>' ?A FLUIO 2b TEWi'V RAT'JRf. F fi P) y 26 FREssufi:-: psic r\fi*X 27 API (M.W.I 2S SA GIL AT GTO. CONO. 23 f.P. GR. AT P. T. | 30 , 31 1 22 WEIGH! % VAPOR IN-OUT Uviycosn Y AT P T. RATE. NORMAL 33 RATE: 34 ''AX. | . MSN 35 NOTES- ) /rf- 70 / Lt\/r, . / /j 7^- /* / /cu/ot/ cCxu/rJt*tLTXAxJS AOA/'/C T- 70/ i/r vr* //oo /). SC - /. / /,/.} - Co. /Oo -/s-e) Do"/A 1 i/cr*i //Ax> 3 00 / TO 1 / C> - 702 /sue.//D 7^ 70*- L 6 - 70 z /sue/ /u 7~^7a /Lcutf (jpMt, /_n e. *) / TX/lu ( Aa/oto r T~- 7 O X- vr L-s uc/ C ucc sc. Loe At / T7L/)*JS 770 X vr yen /sa.0 Arr- // l/ts* //A. O Arr-/ / 6/. l-4;. /Oo - /Sro ______ LZ3/& . . . i | / 0 0 - / s~o t/O- /TO 1 1 i- 1 1 i/cn ///-o 3b o > ro J/c/* //fr-O /rzj r \ .1 1_________________ 1... i____________ l n i \ \ ~3 i l t | i r t 1 !i L "; i i " i --; i i f * i t t (i) use /tst,/ 6&ajts t/h/cs c/c<?n /fijcJ d?e/L /{<?*./ SHEET____________ ......................Nl.V__________ 1 ABDOO185047 W3 ENGINEERING CENTER PONCA CITY, OKLAHOMA SPECIFICATION SHEET LIQUID LEVEL INSTRUMENTS plant__ABERD.EEM Pv/c_______________ project -EJVU5SI OM<; AFE NO _______________ ____________ DATF LG/llll6 W 0 NO._____ MADE OY JRkA INO NO.______ APP'D BY RfcO NO B M. NO P. 0 NO RecedeRsj systema _I 1 1 AG NO. 2 SERVICE 3 L5-70/A (0 T-7D1 l LEVEL () LS-70LB____________(h LS-TOIC............ ^ r-TOi T~noi (z) LAOGJ_- - U16U ueveLT-TDI 1 (3) 4 INST HUME NT, TYPE 5 LOCATION 6 ELEMENT, TYPE 7 LOCATION 8 RANGE, INCHES UGUID Leva LOCAL FLOAT LV4-T0I l M&.U&V&L CC^Te. Ufe. L&Y6L. COWTR high level local LOCAL PAfcLL_ . J =U)AT FLOAT FLOAT \ UVJ--70I LVN - 701 i.V^rlP.1 ... ............ \ 9 INTERFACE 10 UPPER 0EN3ITY, L3./CU. FT, VC(V\ VAPftK.yWmB V/CMVAP6R. /wATEB. VCmVAPOTL/WATEIL VCM VAPcM2/WfltF.; 11 LOY.E ft DENSITY, Ltl./CU. FT. ! 12 TCMPfcRAlURfc F 13 PRESSURE PSIG 14 VALVE TYPE 1 15 16 LOCATION 17 MATERIAL 18 BODY SIZE PORTSIZE 19 . .PLUG FORM 20 &P 1 MIN. NOR. | MAX. 21 CALC. Cv VALVE Cv 22 AIR TO O'VtN OR CLOSE 1J 11 i i......... i r 1 1 1! ) f t ; 23 i.v.ximul; ; <UTO?-F P ? f 2b 26 71 2R [ 29 30 31 32] l-L'.HD TCV.f EftATUHF. F PRESSURE PS:C. IM.W ) SP. OR. AT STD. COMO. CP. Cirt. AT P t> T. W.'UGin N VAPOR IM--OUT VISCOSlT Y AT P. A T. RAT c. NORMAL LWAT&ft. J j (\&>_________ | ` } WfVTEEL _________ WATICR. ^ (i e>N vuArEJe "773x ; | 33 RATE: ;w MAX.35 NOTES' MSN. | 1 . (0 )MSTRU meMT TO B6 M0Ofc EL6CTE.IC UQUtO LGV EL CO^TROLLS^ MO0L 2.7-5- 4-15-M V/ITH ZVz 31GSS fcPiLL FLOAT tX.PLOSlOM PKCOP Heavy Duty mtci^ SWITCH . $ US-IOI A TO CL05S CV-701 AUD LS-701 B OPEMS Cv'-TOl- (3) US-TCHC TO SHUT DCWM SYSTEm UFObS HICK LEX/STL IMT-70| sheet Lor_____ RfV ABDOO185048 --o----J--IMHOHWfl|KJ kj PLANT_A@RC^SLhl ENGINEERING CENTER PONCA CITY. OKLAHOMA SPECIFICATION SHEET LIQUID LEVEL INSTRUMENTS pmcproject eiyussiomS recovers n `* AFE NOl_~__________________________________ DATF |U/36l W.o NO------------------------- MADE CY^iRN\_ INO NO. AJ'P'O BYRfcO NO B M. NO p 0 NO.} svste:iv\ t 1 TAG NO. ? r.i.' hvice 3. 4 instrument, type 5 LOCATION 6 ELEMENT.TYPE 7 LOCATION 8 RANGE, INCHES 9 INTERFACE 10 UPPEfT DcNG TY. L3./CU. FT. 11 LOWE A DEN jITY. lh./cu. ft, 1? YE MPfc RAT URb P 13 PRESSURE PS1G 14 VALVE TYPE 15 16 LOCATION 17 MATERIAL 18 CODY SIZE PORT SIZE 19 PLUG FORM 20 AP | MIN, NOR. | MAX. 21 CA'.C. Cv VALVE Cv 22 AIR TO CfEN OR CLCSE 23 i.L' xii.ui;:, IUTOr-r P 24 FLU-0 25 TENTfi-RATUNS: ' 1V rtr PRESSURE rs:C ***4 u.V.V 1 SP. GR. AT 3 0. COMO. CP. OR. AT P ft T. 30' W.MOM V VAPOR `N-OUT 31 VISCOSITY AT P. ft T. 32 HATE. NORMAL 33 RATE 34 MAX.' MIN. LS-70ZA GT (0 L5-TD1C T-"?na i-cs/vLKvet T-70? (&s T*1D7_ ( 3"> LIQ. ua/a. COMTEOJJcR. U&. L6V6L 0>WTR/*Jf i.ttTAt- UOCAU FLOAT 1 VA/ - 702 FU>AT LW-702. FU3AT UV/4-7Q2. (\S VtW\ VAPOR, yWATER; VCM VAPOR/WATER \/CMVftPc-ANATeR .1-A-J7Q& _ HIGH LB/P=I T-7C2 I c bT| ueyl.Alarm? RAwiet- 1 PtflAT ... _ 5 uw-jQZ... ............ i K _____________________ ._______________ > VCM Vl\PO&/u>ATCfc ? * i1 I 1 -1 1 i j 1! ! V 1 * l : i WATER. (t$C\ ( l (=$S nSs LJATPv? : "zips /-------------------------- *. ___________________1___________________ ___________________ i_______ __________________ l__________________ J_________; ^INSTRUMENT TD BE fflCOR-E ELECTRIC LIQUID LEVEL CONTROLLER mODEL. 27-S-4I5-N v/itR Zi-i 3i4> ss ball float ano Explosion Proof HOWy BUTV MICRO SW/rcK. j)LS-7C>2A TO CLOSE C.V-702 AMD LS-IOZB to OPEM CV-7&2 . l^LS-IOIC TO SHUT DoWM SVSTEM UPON rflSM LEVEL IM T-IOZ. Mf F 1 RfV ABDOO185049 PLAN t_ABEDI ENGINEERING CENTER AFE NO________________ ___________ PONCA CITY, OKLAHOMA SPECIFICATION SHEET LIQUID LEVEL INSTRUMENTS DATF MADE VY.O NO.______ INQ NO.______ APP'D BY RfcO NO 0 M. NO p 0 NO__________________ PVCprojecteiVMSSIOMS RECOVERY.............................. SYSTEM, A 1 TAG NO. 2 SERVICE 3 US-103 A m LS-103B T-ltiXinu LEVEL r 2.^ T--70.% f*i A) LS-IOBC T-703 fli LA -"I0.2>____________i Hl6H LEVEL T:_7 0^> 1 (& i 4 INSTRUMENT. TYPE Lift. LEVEL COW1R5L ua level cairn U&L *../V/EL CONTROL HlfiH LEVEL AiARm 1 5 LOCATION LOCAL. LCCAL LCCAL PANEL I 6 ELEMENT, TYPE FLOAT FLOAT FLOAT FLOAT J 7 LOCATION 8 RANG!'.. INO'fS l_VW- "763 LV4-*7 0^ LVJ--703 * * 9 INTERFACE 10 UPPF R DENSITY. L3./CU. FT. VCfA VAPOR, /wftim vcmvap^l/va/atbtl VCfi\ VAPOS./tf4AT7r12 VCmVAP 02./ L-yAT1=T> 1 --------------;--^_=---- ; 11 EOY/ER DENSITY, LH./CU. FT. 12 TEMPERATURE F 13 PRESSURE PSIG 14 VALVE TYPE 15 16 LOCATION 17 MATERIAL * 18 BODYSIZE j PORTSIZE i i L l ; j 1------------------- s. 19 . .PLUG FORM 20 &P | MIN. NOR. j MAX. 21 CALC. Cv VALVE Cv 22 AIR YC> Orai OR CLCSE 23 maximum :;muto;-`` jP 1- i 1 1! 11 i 1 24 2b TCMr'L'I.ATU HE OF wArrn WATER. nwateil WATEJL ri r^o PRESSURE F >:C. ll.I.W.I S?. (j R .Tfairo. COM3. EP. C.R. AT P. ft 1, nay TTfSS -- ' 30 VY.MC.lil ^ VAPOR IN-OUT 31 VISCOSITY AT P. 6 T, 32 RATE, NORMAL | j 33 RATE-: 34 MAX. | MIN. j 1 1 1 1----___ I________________ c (0 IMSTRUMEMT TO BE. MOORS. ELECTRIC LIQUID LEVEL CCMTR.OU.MODEL I 27-S-4I5-N WITH 3/j" 2>16 SS BALL FLOAT AMD E*PU>SioiU PROOF HEAVY DUTY MICRO SWITCH. ^ls-tosa to close, cv-t03 awd us-tosb to open cv-tos. (3) LS-103C TO SHUT DOWM SYSTEM UPON H-I6H LEVEL |L T-762>, SmFFT, of_____ ncv_____ ABDOO185050 i pi ant ^2; \j/ ENGINEERING CENTER P0NCACI1Y.0MAIIUMA SPECIFICATION SHEET 1a.f.e.no---------------------------------------------- 6DATE jO/.Il/'7 W. 0. NO------------------------ MADE BY_U.fe.hQ INO. NO. TEMPERATURE GAUGES APP'D CY R M NO REO.nO. P. 0. NO. ABRDEM PA/C project EhAtSSlDMS RECOVERS' SVSTn\ 1 TAG 2 NO. SERVICE 3 T^-*7DI WATER / VC1KA 4 -T6-.7g2.__. wAtcb.7 5 T6- in?* 6 T&--IO* 7 WATBvf.f WfV\ WATHE-i V/ATHR. &J gU P |J> 1 8 WATGJH. 9 Tfi-TO^C 10 WATER. 11 INS , RUMENT RA ,f 111 r, -\oo /i - .2. n O r\ -- -1.0 0 0-3.00 O -- 0-00 n ~ 0.0 0 to - OLOO ONE RAT ING TEMP. Of I IO t 36 / 3n / yn 90 90 LOCATION' v-~ro\ ____________________ T-noi L 7UTM'-r-lOh--J Z" A- no&i A A -7 CP> S EA -7CA C 12 13 14 15 16 17 18 19 * 20 21 22 23 24 25 26 ---------------------------------------------------------------------------j 27 23 29 30 31 32 33 34 1 35 36 37 38 39 4C (1) ALL GAUGE ELEMENTS TO BE SIMETALL'C UNLESS OTHERWISE NOTED. 41 42 43 ............." " 44 ....................................................................... ................ ' 45 46 47 481 49! _ .... 50 51 52| 53 j *'L 55 56 __________ ________ ................ " " ........... .. ............................................... - - ....... .......... QUOTATION WILL NOT (it CONSIDERED IF SUPPLIER DOES NOT COMPLETE RIGHT HAND C0LU',',,N _ SHEET OF PV ABDOO185051 iA PLANT_ yr-S^f BSIKEJ v\/y ENGINEERING CENTER PONCA CITY, OKLAHOMA spcciftcaticn smelt TEMPERATURE INSTRUMENTS project emissions A.PC. NO DATE lit* W. O.NO. WADE ItY ^I INO NO.. APP'O OY____ _ REQ.NO. 0. M NO ____ P.O. no. gBcsVEEW system l ! AG NO. ) sc nvict 3 TA -109. T-1Q1L TEfAP A 1 TVS 1 liUV.LNT TYPE ["> LOC A1 ION M HAMGK f ! ClEMC NT, TYPE. (UAfifi1 d) ROAE.D (/) O- Z&G ' -fe/^n SuttcJL. 8 LOCATION n -r a 7 9 Tf. [.'.PE NATURE r io pnf.s:.unc PSIG 11 eatsu: t ype lJ /isn 12 t /3VI& 13 J^**3*^ 70C..tiO. ~r<- 701. 14 MAT EHIAL IS \pODY SIZE POT SIZE 1 in ^^i.uG rohm 17 ^P | MAX i * II TA-TOB T-To^iemP ALAfi-f*' U\ ROA> m ^ - i7 6>` - '77 -7 ? /?r* P cO nULA TS- 70 3 11 --................................ i >i 18 C-ALC. VAI.VC Cv 19 Alf!i4<rpEN Or7^5 20 shutqpr Ap 21 PlUID f32 TEMPERATURE 23 PRESSURE t'SIG 24 capi iv v; i 23 SP GH AT S to CONO 2n SP CH. ATP 4 T 27 WEIGHT VAPOR IN' OUT 28 VISCOSITY AT P fi. T ?vc a vapc^Aa/atss r y o' -T . VCinvAPOG./vAjATB? Altf' ?/0 i i \ -t i 1 1 \ i i t 29 30 31 37 I HAT . NORMAL HATE MAX | noils I M.IN ............. - 1 i i | 1 i* ( /) 705 TV j3 -h'icj rviiAl-h-akf* to/'/i T^ss/ aoA. ^ L---o---c--^-- l f' to' *Jc ^ TS-70X j70$ To be - sXwf'c/dtA SHlEI cc_ ^v---------------\ I ABDOO185052 '8%%% \y V -ENGINEERING CENTER ponc:aCity Oklahoma SPECIFICATION SMELT TEMPERATURF INSTRUMFNTS PI ANT A^e^OEM pvc PROJECT fcJYUSSlOMS a.fe.no date \^[\Jp.(o. w 0.no. MADE RY^f2/VL_ INO. NO. app'd ry RPO NO n M NO R6COVERV P. 0 NO. SV'STETM 1 t AO NO. 2 sriu'ici :< TtC_--7 0^ tTR TfV\P j iNbl riuv.i NT T vpe TEmp. IMD.C&NTfc. A LOCATION Bn/XRo o HANOI. K _ y ELEWS NT. rvpi, rt- 2.60 H LOCATION 9" Tl.MPC FlATuf>6 r izo "o' PES0>JP.E VS'O 11 VAtvE TYPE 90 BUTTERFLY 1? TAfi hiO. 13 LCCAT ION TICV/-769 UM& 14 MATERIAL 1b OODY Si2b | PORT SIZE C.<^. 1 _______________ 1 1G PLUG FORM 17 4^1* j MIN. | NOR MAX. J_____ _ 3 18 CALC. Cv | VALVE Cv oTan 19 AIR TO OPEN OR CLOSE >$rc. 20 vax. shutoff /3 p 21 F-LUIO 2?' TEvr-lllAUiHE F 23. ` PPESbUril. ('SIC ?'. ' 2b "O* V. ' SP. OP. AT f.ro CCND 2G i-P 0P> AT PIT 27" i.E'G'll < VAPOR IN OUT / WATER /C/7 ____ Z0____________________ /y /. 0 ____ /_w<> 28 VISCOSITY AT p J> T ot r,f "29' "30H RATE. NORMAL KATE C//^ -Aq _ *"31 33 MAX notes! | MIN /?o~~l_______________ ____!_______ ^ Jo 5/Z.&& /** 11 ------------------- 1--------------------//m ^ /?& />r' U/M- forJ (2) Ci/ oJ~~ & O /sn 7C6 /Vh 1 1 i 1 i 1 1 [ } >tl f J J i i i 1 tr* V i shi n or nr v > ABM01&5O53 ENGINEERING CENTER DAI (I II, M NO. -A PONCA CITY, OKLAHOMA A. P. C. NO. V SPCCiriCATION SHEET CONTROL VALVES W. O. NO. _ REQ. NO.___________ MADE DY JRPA. ____ INO. NO. ____ I*. O. NO ACP D OY ___ PLANT .ABR.DEhL_V: PROJECT .eMISSlDJ^S-RECOvm^-SYSlEM GENERAL 1 ITEM NO. ft TAG 2 SERVICE a sizeline A (.1AI'.'U PAC TUltEK CV-'7.DJ___ tP2 _UfeL (J&UiL T-70'2. DftAlN DfcAlM 2" 2." CV- 703 - CV-d=Ol _M.Q3_UfcU.lfiL VC16 y.ftBOR . _RA|.M BLDWfcatfM iMikL 2" 3" U MODEL NO.' G TYPESERVICE CONDITIONS on /off ON /OFF OK/ /OFF IOK//0FF 7 FLUID 0 7I.MP t- NORMAL 9 PRESS . INLET,, NORMAL lO A P MIN. NORMAL 11 MOLECULAR WEIGHT MAX. MAX MAX. A.P.I. WATER A/CfA /So ' 20%hc- v1 WATER/\/CfV\ ALD LT water/ \/ClY\ /-o' I lOtoiO | va\ VAPOR__ 'jro 1______ jLO'Vk J_, r 12 SP. GR >< 60 F. 13 WEIGHT ? VAPOR IN M viscosity " i't. a r. F.T. OUT 10 16 RAIC MAX. L3 HH tSCFHl GPM iSL(* 17 NORMAL FLOW Cv .10 BODY 19 DODvyi/E PORT S17.E :-o 7 YI'C .ANGLE OU Ol.uQ C > "L MAI,,HAL END CONNECTIONS 3 UONNT.7 2* 1 .5 TO 2." i j ra o2.#/ 1 jra --u .3 i _Jt> . BALL C.S. _ __ BAU rC.S. Ball JCL.S 8AUL c.s. i ISO tb._ R-E.___ J.SO_lk_&___ J.5D lb R.F. " IS0Jb,g,R_ J Cv 20 LUBRICATOR 26 PACKING ISO VAL. 1 I 7 RAVEL INOlCA fOR 20 l TRIM 29 |TYPE INNER VAL NO OF PORTS 30 f. ITPLUG SEA! MA I RIAL ' 31 5,^ 31 SLEEVE. OR SEAT TFE. i 32 TYPE ACTUATOR 3 3 FAILURE POSH ION 32 Phf/J vnpsb'z* C/ds<lJ i TI6 .<=,. TF <4/e.HOt* ^./o sec/ i 31 /> .. TFB 1 3IA S.S. TF P/)t.K>U Aa/j'c- c/o$c<Z POSITIONER 35 INPUT SIGNAL OUTPUT SIGNAL 36 OYPASS GAUGES 37 MANUFACTURER 20 MODEL NO. [ ACCESSORIES 39 L$-7ci 4, b , (l) Tc Ao*t<- 1 Rttc! $-70z 4\ a C6*> T^e/ Pu/Jcf riJc/ /in#//novd'rcef of***J/c'***' ' .. A. . 435-: cv-Lot *> { i ik'piCMrs itrm ouNCti) on latlst ntvi&tON. ti :Nri'<r*irs m*nu'actucii to civt Ktouis'rj isfyomnoi in m-s ouc'ation. sheet /i 0aJ . or Rl.v -- ' .........- -------------- -----------------------------------ADDOQ185054----------------------------------------------------------------------------------------------------------------- --------------------------- V-sra-TT CflJEH*! V ENGINEERING CENTER PONCA CITY, OKLAHOMA SPECiriCMION SHEET DATE_L0/_fi/-3li w. o. no * MADC UY_U26A----------------- ' <>-----------------------------" PI AMT ABERDEEN PMC RELIEF VALVES APPDUY B. M NO. huq.no P O NO project EMlSS/0M5^ec^YCR^_S^STe'M___________________ g e n e: R A1. 1 ITEM NO. ft TAG 2 RELIEVES EQUIPMENT NO. 3 MANUFACTURER 4 MODEL NO. 5 SY-TOI T~ - 7/0 / SERVICE CONDITIONS C FLUID i/cm 7 STATE G REQUIRED CAPACITY 9 MOL WT. SI'. GR. 10 VISCOSITY 1 1 COMPRESSIBILITY FACTOR 12 DESIGN PRESS. OF EQUIPMENT 1 tT O 13 PRESS. OPERA! INC RELIEVING 14 TEMP FLOWING RELIEVING IS BACK PRESSURE 1C DIFFERENTIAL SET PRESSURE 17 ACCUMULATION `-i ' 10 BLOW DOWN C 19 /<TO / <ro AlT/vn s / CTO BASIS OF SELECTION 20 CODE REQUIREMENT 21 EaPOSF.Li AREA 22 INSULATION THICKNESS 23 OTHER BASIS 24 UhSIGN DETAILS 2 5 DESIGN TYPE 26 SEAT TYPE Co*o i/t>J ho CISC SV-702 -r - if)-a SV-70S 7"- 7 D^> 1fr m tfc n _/rv /CO /c~c /? r/*io s tco -- l b6 /j-O /) 7~/*i0 /CD Of.sc AnA/Cfih'&ufi} nnc 27 DONNET r OPEN OR CLOSED' d/oscdf f?/<os <cf 20 INLET SIZE. RATING. FACING 29 OUTLET SIZE. RATING. FACING y'/ro# /?F *"/<-!>b 2"/.&*#.* ? * ,<ro * rt-f* 30 CALCULATED AREA 3 1 ORIFICE LETTER f ACTUAL AREA MATERIALS 32 BODY j BONNET T /-rn c-5 1 r.5 rr 1 A *7 CS \ cs 33 SEAT ft DISK 34 j GUIDE ft RING 35 SPRING 36 BELLOWS ACCESSORIES 37 LIFTING LEVER 'PLAIN OR PACKED 30 GAG 39 CODE STAMP 40 cap . r-cHEwro or uoltedi .5 5 35 rc /J /o a1 a AJ 0 .5 CfleuFA 1 | 3J C <, A/0 Ai/'i A/n 41 j OTHER NOT f.G: manut aoturer shai i. verify select ion or orifice t,i zr. and materials VALVf S SH ALL Mi E. ? DfMI-.Ns.tON REQUIREMENTS OF API KP-526. VALM G SHALL MEET If ST HCOU'fECMENTS OF API RP- bZ7 buppi iiimo ccvt.-i rtr. form by furnishing 1*1* ft'-'VA'I tr>N IOII 1 `t ANK `.PAG I O HI V. 1-Asi-oL ' --M--------------------------- d /d Sir d 7"/ro* T 1 /-?P7 ! cs i rs 33 c <; AJh A/ O a/ n .{C/z &wrn i 1 % ___ ____ OF* ___ . REV _ ___________ V",r!iTr'7 K-rai-ia vy/ V pi ant ABD00185055 ENGINEERING CENTER PONCA CITY fll-UlliTUi ' SPECIFICATION SHEET KLllfcr VALVES n*-rr MADE OY.^J pvc pro ifct EIAlSSlOWS RECOVERY SYSTEM... 1 .2 3 A 0 6 7 Q 9 io 11 .1 13 14 IS 1G 17 10 19 20 - 25 22 23 24 25 26 GENUUAL ftITEM NO. TAG KGUilVES l.OUlPMl'.Ul NO. MANUKAC1URER MODEL NO. SV-704 SERVICE CONDITIONS FLUID STATE REOUIIIEO CAPACITY mol. v/r. sp. GIL VISCOSITY COMPREbSlOILlT Y FACTOR DESIGN PRESS. OF EQUIPMENT PRESS OPERATING RELIEVING TEMP FLOWING RELIEVING HACK PRESSURE Dll FERENTIAL SET PRLSSURE ACCUMULATION 7, LOW OOVVN N f/G- / yo /TO /yo }<T6 OASIS OF SELECTION CODE REOUIRLMENT EXPOSED AREA INSuLAT ION THICKNESS OTHER BASIS DESIGN DETAILS DESIGN T YPE SEAT TYPE Port /)/.S6 V . 'A SV-70S . 3`Hff\-770-A'7)X~ / i/cri /y<y /S7> /yo A 7Pm * /yo nri<- SV-7D6 1-//M -7U -aJ-Ai-) !/C^ !TO__ _ AZ>_ tJT6 /)T/*l6 < /yo A/S C- 27 UONNET iOPEN OR CLOSED 26 INLET SIZE. RATING. FACING 29 OUTLET SIZE. RATING FACING 30 CALCULATED AREA J3 1 ORIFICE LETTER ACTUAL AREA MATERIALS 32 BODY | UONNET 33 5CAT A.DISK 34 GUIDE a RING 35 SPRING 3G BELLOWS r/r\ I*A - "/re* A.y .0 " - /<Cc* A A *.c/ i&'-./.ro# A* } A -/S'O # />.A Pl/o A* - /-t>#A.y 0.101 /= 1 0. 367 \ O.J&7 C S 1 As S3 rc A)n cs 1 sy ss cS> AJ 0 C-S rs \ CJ SS s% f .3 aJ 6 ACCESSORIUS 37 LIFTING LEVER (PLAIN OR PACKED 30 GAG 39 CODE STAMP . AJfJ _ jJ r> <J0 aJ AlO a/0 I i 40 CAP ibCHLWl'.O Oil UOLIEOl 41 OTHER AcA^a/FA JC Aclo^n <cA/?ioyo . >~ NOT r s- MANUFAOfURER SHALL VERIFY SELECTION OF ORIFICE SJ7E AND MATERIAL S. VALVTs SHAl.u MI LT DIMENSION REQU 1 REMENTS OF API RP-526. VALVES SHALL MLFT IFST REOUlREMCNTS OF API RP- 527, | 1 % . SUIT'l'l K IO COM 1 'l i.T FORM 15 Y FURNISHING INF ('"'MAIN N IO>l 111 Af.K SPACES W'MM Hi V. 1 od s MEET_______ -- OF . ... REV . . A > i 1 ABDOO185056 f i , i-` tnrnmumia ADD00-1&5O5-7- ryr. 7 r , u--y PLANT. fiber Jff*J ENGINEERING CENTER PONCA CITN . OKLAHOMA SPtC!F`CATIOr SHEET Pf/ project SrA) J SS/ /} sJ S AFC NO______ DATE___________ W O NO__________ MAOE OY___________INO NO APP'D BY RCO NO A fi M NO P O NO fi/scd_itjr/i\/[/AFJlL- . WKSamw ../* /? lJ ft / OA,7 P/SC* PiP.OC/ A/ C/tT/tO^ ' :nrM a/o* \ / /)r a ~r/r) aJ Lftje !> A`J. /}/rit. Size //) . j?fi- 70V DischfiP- fi?o9 i ry^ Ab-7oy . SO- Pis CHfttCk' C-loT OiSCHtoteC-lni. _v& -- v) ^1 PASAS. PJ/c* 7~0mP CF /<ro iF~0 l a r/A/r, eMO/Pfi a/sf E 7Tr/>!/>, o/r SJ i Oise /*nrr?/t//)/ i p ?f ' f/ak*u^ piAr&s/ri/ . Z/jfcP Ou+Pt / /JO ... __._ r lrtQArt3*#3ATiSr* WkMAvk4 MHi|l .,'r,, < /ST5 /jga____ /^O /S~0 . X ] i t1 TO (3 0 !ZO { i< ss s s "it S CA /< ' ! a. sii t /S&*jp.r\ it t! ! ~ i | r>nCET_______ Of_ i ( i I . ' ABDOO185058 Banska ENGINEERING CENTER PONCA Cl IV. OP.'I AMOf.'i A SPHCiriCATlCN CHF.ET ORIFICE PLATES & FLANGES * INCLUDING DATA FOR LORE CALCULATION PLANT -6jre/<*LJStX^project A.F F. NO____ ______________________ OATF. I0/>SPU V.VO.NO MADE BYINO. NO. APP'O BYRLQ. NO _ e. m. no___________ p o. no. sysr^sh f.i NLiiAL ' i'l.Clf U'A i ION 'j omncii PLATE c 0 CHSFIC.E Fl ANGE5 3 MAKE STANDARD 4 I'lAH MATERIAL | '!) other OTHER 5$ 10 RATING A FACING 11 T YI'E WELO NECK > Ml .1 Mlf.'O MAl't A TYPE G pore m-uimum h/> if NEAREST 1/8" 12 1,`Al'l.; 13 ta^ si?e STCEL \r:" npt S I AMI' TO ISA Sr AND A P.D OTHER 14 FLANGESOY 15 1C IT TAG f.'O L1\'C NO Va Yd SERVICE CONDI I IONS ROvoyAte 76 3 yen R0-7d$/U& j- 775%-//*- 77^ /? O-7>CA40. - 7 fi &/- Z//7 - Itz. ?o 21 22 23 24 2A 7C> 27 2B Vo y-j '* Is FU;ir; Fl.GV. UNITS i.'/./imiiM r'.ov; NORMAL FLOW FLOW PRtSS'Jnc-f'SlC FI C-.V, Tf MCE RATCRF Op $ G G <*0:'F & |4.7 PSIA SCiSI'.T.i 1 Cf *5 PSIA SUPER COMP. FACTOR '> 0. P. GAPOft GAS MOL AT VISCOSITY. Cl' *> f . i`. Si 1 AV (HiA: iH sll.'.MS'/l'i'A'iAT up. apt\ ?..rs 1. o iP>o fOO 1.0 O.W -- _ n.uS -- DAT?71. (*P /*> 3 .> /. o ( to / oo /. o 0.4$ _ r_ 6.t.X -- DAT/r/L 7 .4? /. o /go / 00 7,0 O. <?<? -- 0. it -- ' OTHER 01: if ft OTHER ! | 1 A To / - j Mi i 37 ... ... I .... . J i10 j 42 MCASUHlNG STATION DATA i 43 ACtUAl ORlFiCr !. O.. INS i 44 ll.M F l Ai\C> 1. 0 . INS. 40 SLAU s c. G GCrtF ; 4(i MANOV.G TER TYPt TV Uirr. rAngc ins h;>o dry Lii ST ATlC RANGE. PSIA I 49 Chart On sca i E range loo CHART ML*l T IPLICR T i ^>2 33 vr 10 `Jo 07" 00 NOTES: 0-017. o.m-2 . ... i. _ ............... n .072, ./? , 7V7 _ ft . 0 71. /). -74/2, i 1 i i ......... _ . .... 1 i1 ii ! Pi _ i1 i! ii .i : i ... .... . ii; !;! ;< i III. i i________________ 1 ~" i i I'I ' INSTFPJMFNT bOClCTY OF AVCRICA * sciT f________ cr______nrv______ ABDOO185059 EMISSION RECOVERY SYSTEM ABERDEEN PVC PLANT V. INSTRUMENT SPECIFICATIONS Shutdown Description The Emission Recovery System is to include a shutdown system to stop operation in the event of a malfunction. The shutdown system will stop the motors on the following operating equipment: P-704 C-705 C-706 P-707 `P-708 Vacuum Pump Compressor Compressor Seal Water Pump Seal Water Pump The shutdown system will activate a single shutdown light and alarm on the existing Large Reactor Ronan Alarm Panel. The shutdown system will be activated by the following switches: Item Indication Set Point LS-701C LS-702C LS-703C TS-702 TS-703 PS-701 PS-702 PS-703 High Level In T-701 High Level In T-702 High Level in T-703 High Vac. Pump Dis. Temp. High Comp. Dis. Temp. High System Inlet Press. High Vac. Pump Dis. Press. High Comp. Dis. Press. _ - - 175F 175F 15 psig 25 psig 100 psig A i ABDOO185060 EMISSION RECOVERY SYSTEM ABERDEEN PVC PLANT INSTRUMENT SPECIFICATIONS Local Panel Board Description The local panel board is to be installed in a location adjacent to the Emission Recovery System. A location to the south of the compressors is suggested. The operator should read the panel while facing north. An explosion proof enclosure for the panel is required. The local panel board is to contain the following items: 1. One Ronan Alarm Consol. The following alarms (lights only) are to be designated on the consol. a. High Inlet Pressure b. High Intermediate Pressure c. High Discharge Pressure d. High Intermediate Temperature e. -High Discharge Temperature f. High Inlet Drum Level g. High Seal Water Drum Level h. High Discharge Drum Level 2. One Temperature Indicating Control for TIC-709. 3. - One Pressure Indicating Controller for PIC-701. 4. P-707 Start/Stop and Run Light 5. P-708 Start/Stop and Run Light 6. P-704 Start/Stop and Run Light 7. C-705 Start/Stop and Run Light 8. C-706 Start/Stop and Run Light 9. Provide approximately 40% spare room on panel for future instruments. Oi uu wo HcC <; dw a. O23 Q tO Z O hi Z hrxh UJ H-< z ft. CJ3; tCoO ZW w o to o to ffct.t UUJ o aa. r ' I * c tu-J '\Ti >- \0 <i s,, iV u* > x. c tv 0 TTOO? > a - > -;l jJ; < r 'l r lA .. j < a! ii o 4<TJOu O Or-1 i-T>O TO $H r-H a. to- to- sw w_J nwtoT* C_3 T<TOO.'. C co r n 2 ctf TO.TKOH. w>c --I CO CO w ' CTtoooOJj'. CcTucOOoOiJ TO- v x 1V u n& 51 s 'Oa a a a 2 \A A O ijJ Ui r~ V} vi rv a) ijfjr cci <0 o 4- 1 OJ +J r~i c n u oU <-"a< Cu a wr W. - H 35 oa wa CV3J Q u L^'~D< haC-Jj aa HH l-i a vwLU vi2u-ui: cj co OV aa uw o a a i ABDOO185066 EMISSION RECOVERY SYSTEM ABERDEEN PVC PLANT VII. WORK LIST 1. Tie in 2-UM-701-N-A2-1 to the north and south R-VCM Receiver. 2. Tie in 3-HM-704-N-A2-1 to the Large Reactor Blowdown Tank. . 3. Tie in 3-HM-715-S-A2-] to the Large Reactor Blowdown Tank. 4. Tie in 1-SL-751-H-A2-3 into the Process Steam System. 5. Tie in 1-WP-752-S-A2-3 into the High Pressure Service Water System. 6. Overhaul existing hydroquinone injection pump and tie in line I-HQ742-H-A2-1 to the hydroquinone injection system. 7. Tie in line 3-HM-702-N-A2-3 into the Large Reactor Recovery System at the VCM condenser inlet header. 8. Tie in electrical switch for CV-601 into the control system for the Blowdown Tank Discharge Pump. 9. Tie in lines 4-WH-747-N-M2-4 and 4-WC-743-N-M2-4 into the Large Reactor CTS and CTR System. A