Document M4Xd9x8LvkGjzxBBzM2BVQgkL

conoco Interoffice Communication To Distribution From W. R. Finch Date July 11, 1980 Subject Budget Designs--PVC Plants Attached are three designs prepared for the Oklahoma City and Aberdeen Plant 1981 budgets. They are: 1. Reactor Level Alarms. 2. Reactor Relief Containment--Blowdown Drum. 3. Reactor Relief Containment-Memo Item. These designs were preissued in rough draft form to allow for estimating. Walter R. Finch Senior Process Engineer Chemicals Division Process Engineering Department ke Enc CC: ^ JHM: REB: RDM: tyfi, 3 ): JPW ( 3 ) JF: CLM: AWS: CRM: DJR PVC Group File P-47.1 P-47.2 .1 .T. n .!+ -.1 T . . ||L u V.rt t -Ti|- VAB.0001099986 u. i-i REACTOR LEVEL VAB.0001099987 Interoffice Communication To R. E. Barker From W. R. Finch Oato July 3, 1980 Subjoct Budget Estimate for Reactor Level Alarms--Oklahoma City and Aberdeen PVC Plants Attached is a budget design by Mike Hurtz for installation of level alarms on the PVC reactors at Oklahoma City and Aberdeen. The design involves addition of high and low level alarms at Oklahoma City and addition of low level alarms at Aberdeen. Would you please prepare a budget-type estimate for both plants. Walter R. Finch Senior Process Engineer Chemicals Division Process Engineering Department lkm Enc CC: JHM: REB: RDM: JPW: RAF File A-20.1 File A-21.1 VAB.0001099988 | 'V + -M* BUDGET DESIGN REACTOR LEVEL ALARMS OKLAHOMA CITY AND ABERDEEN PVC PLANTS July 3, 1980 Work by: Michael J. Hurtz / Process Engineer Chemicals Division Process Engineering Department .-CaM. inr \ `I 1 | p--h -r 1 I | - If - v 1 >-*rnl|-- r " ? ' JV'"' . -I"'! .. .................................................... ' VAB.0001099989 * PROCESS DESCRIPTION REACTOR LEVEL ALARMS OKLAHOMA CITY AND ABERDEEN PVC PLANTS The purpose of this design is to provide reactor level alarms to reduce the probability of liquid full reactors, thereby reducing the potential for atmospheric VCM release. This design requires the installation of high level and low level alarms on all Oklahoma City reactors and instal lation of low level alarms on all Aberdeen reactors. The level detectors recommended are radiofrequency probes, A budget class design is requested for both plants. MJH-lkm 7/3/80 VAB.0001099990 lita* nh J, i INSTRUMENT LIST REACTOR LEVEL ALARMS OKLAHOMA CITY AND ABERDEEN PVC PLANTS Item No. LAH-1 LAH-2 LAH-3 LAH-4 LAH-5 LAH-6 LAL-1 LAL-2 LAL-3 LAL-4 LAL-5 LAL-6 LAL-7 LAL-8 LAL-9 LAL-10 LAL-11 LAL-12 LAL-13 LAL-14 LAL-15 LAL-16 Description Reactor High Level Alarm Reactor High Level Alarm Reactor High Level Alarm Reactor High Level Alarm Reactor High Level Alarm Reactor High Level Alarm Reactor Low Level Alarm Reactor Low Level Alarm Reactor Low Level Alarm Reactor Low Level Alarm Reactor Low Level Alarm Reactor Low Level Alarm Reactor Low Level Alarm Reactor Low Level Alarm Reactor Low Level Alarm Reactor Low Level Alarm Reactor Low Level Alarm Reactor Low Level Alarm Reactor Low Level Alarm Reactor Low Level Alarm Reactor Low Level Alarm Reactor Low Level Alarm Plant Oklahoma City Oklahoma City Oklahoma City Oklahoma City Oklahoma City Oklahoma City Oklahoma City Oklahoma City Oklahoma City Oklahoma City Oklahoma City Oklahoma City Aberdeen Aberdeen Aberdeen Aberdeen Aberdeen Aberdeen Aberdeen Aberdeen Aberdeen Aberdeen MJH-lkm 7/3/80 VAB.0001099991 PLANT kC /fift ENGINEERING CENTER PONCA CITY, OKLAHOMA SPECIFICATION SHEET LIQUID LEVEL INSTRUMENTS A.F.fc. NO DATE -/ MADE BY MThl W O. NO INQ. NO.. APP' D BY. REQ. NO. B.M.NOP. O NO., TAG NO. SERVICE INSTRUMENT, TYPE LOCATION ELEMENT, TYPE LOCATION RANGE, INCHES *U-I - Jl Ag&ftCTO* plt frrt lgt/^tJE=ACT^A. LqnaJ Hl(SH t4TUgL ALAtftVli t=siwj Leo ec Jk&AN BoARD (z) goAftp fc) toe fJ^PfKA^EJfty r<?p Qp ffertcroft. . u borrow of- fce ACTQ %% INTERFACE UPPER OENSITY, LB./CU. FT. n LOWER OENSITY, LB./CU. FT. TEMPERATURE F 13 PRESSURE PSIG 14 VALVE TYPE ftL-7Tttftw6H - /fe ft to Rmmlw Lou-> Lc.vjL> ftt-flfefti Boar# RAPioPKCtftteMCy RR TAToMm a F feflCTJ 16 LOCATION 17 MATERIAL BODY SIZE PORT SIZE PLUG FORM AF | MIN | NOR. | MAX. 21 CALC. Cv VALVE Cv AIR TO OPEN OR CLOSE MAXIMUM SHUTOFF AP FLUID TEMPERATURE F PRESSURE PSIG API <M.W.) SP. GR. AT STD. COND. SP. GH. ATP.ftT WEIGHT % VAPOR IN-OUT VISCOSITY AT P. ft T RATE, NORMAL RATE MAX. MIN NOTES: 0) F&a Oklahoma City Plf\mt (Six ouiHet>J (7-) All $,6rUA<-S To T&o##D A** e L&c T \<L.. (3.) PftofiC To ? P<?fcXLt?ftoc>K 5"ofe-/oo - ftAPioFR.CVautf'MCy \ %o *R. PlPpR.O\)6* ^tauiMALf MT. Pfto6r To X MTR |*)S iCALCy Z&F&. ^u-crRapi iCS AoiaSiWO explosion rfloOF. rn&eTM&G CLASS X t PnJisift*) x, Gr&0*p t> SpFC! figAT IO+IS t-emenX to 0, sr.s. t/ Li i To 0 0 v>1 > Di ^ tr Tl? ______fc "SOO ?ib *>- S - C-A l\}(sr * ^ewsiroiS trLf'mffjT r i SVrus i fuG- e'*o crirJ-r ro C*re *>rttet 0 T CoTEr to FoR. A BeRDSff *0 Rt-AfUT C T^nJ R^<au.iReDJ. (7.) Al-ARwi TO sow #00 buRH0 6 poi.'(M1li*ATiart AwD CMAR6 CYCLES c?WL/ ftOTi*^Trt(?Le f im^ D^LAy . 73li v PftTD (&) Al To S DUR1W6-e'uAc.uATioft? cycL^ orv>Ly. g'ncH neficroti to hpi^ ijoar0 iriouWTeo LmJHt ro jNDtcflrg' LUl/$q \~eoet conoitioiO. SHEET 7/3/80 WORK LIST REACTOR LEVEL ALARMS OKLAHOMA CITY AND ABERDEEN PVC PLANTS 1. Oklahoma City - Install low level alarms to D-305 and D-306 through existing spare nozzles. D-301, D-302, D-303, and D-304 require field installation of new six--inch, pad-mounted, 300-pound nozzles. The nozzles are to be electropolished 316 stainless steel. Aberdeen - D-300 requires field installation of a new six-inch, pad-mounted, 300-pound nozzle. The nozzle is to be electropolished 316 stainless steel. Install low level alarms through existing spare pad-mounted nozzles on the other nine reactors. 2. Oklahoma City - Install high level alarms to the existing spare sixinch nozzles. Aberdeen - None required. MJH-lkm 7/3/80 VAB.0001099993 |" T*| * " * Sr v^ 0001099994 t 0 '! 4- ' ir ?l H- '' ' - f! i-- I I' " .:. V *r > ir r4^ V'-m. ***, **** VAB.0001099996 1|"Z Interoffice Communication To R. E. Barker From W. R. Finch Oat* July 11, 1980 Subjact Budget Estimate for Reactor Relief Containment--Memo Item-- Oklahoma City PVC Plant Attached is a preliminary design by Mike Hurtz for a reactor relief blow down system for the Oklahoma City PVC Plant. The design involves instal lation of a pressure vessel, centrifugal pump, turbine-type agitators, and associated piping as outlined in the design. Please prepare an estimate to be used for the upcoming budget. Walter R. Finch Senior Process Engineer Chemicals Division Process Engineering Department lkm Enc CC: JHM:REB:RDM:JPW VAB.0001099997 PRELIMINARY PROCESS DESIGN REACTOR RELIEF CONTAINMENT--MEMO ITEM OKLAHOMA CITY PVC PLANT July 11, 1980 %AJ Work by: Michael J. Hurtz Proc Engineer Chemicals Division Process Engineering Department VAB.0001099998 PROCESS DESCRIPTION REACTOR RELIEF CONTAINMENT--MEMO ITEM OKLAHOMA CITY PVC PLANT The purpose of this design is to provide a partial reactor relief contain ment system for the Oklahoma City PVC reactors. This is a very preliminary design requiring an order-of-magnitude estimate to be used for a budget memo item. The des ign calls for addition of one rupture disc/relief valve assembly on each reactor, one* on-off valve on each reactor to he used as a manual vent, one blowdown lank sized al 100,000 gallons, and a blowdown lank slurry pump. The manuaJ vent and relief valve assembly will be piped to the blow down tank. The existing reactor relief valves will remain vented to the atmosphere. Manual venting at 160 psig and relief valve/rupture disc set point of 175 psig are recommended. The slurry blown to the blowdown tank will be mixed with AMS. Once blowdown is complete, the slurry will be pumped back to a reactor for VCM recovery. The proposed system is sized for relief from one reactor. Very preliminary calculations indicate the system will provide an additional ten minutes more than the existing system for AMS injection into the reactors in the event of an emergency AMS injection failure before an atmospheric VCM release will occur. Without manual venting, approximately five minutes additional time will be realized. MJH:1km 7/11/80 j F '| -T" ` i h -ifi VI- - 1 VAB.0001099999 BASIS REACTOR RELIEF CONTAINMENT--MEMO ITEM OKLAHOMA CITY PVC PLANT 1. A reactor charge of 51,000 pounds of VCM and a water-to-monomer ratio of 1.2 are assumed. 2. The blowdown system is sized for one reactor vent only. 3. The system will provide an additional ten minutes for emergency AMS inj ection. 4. The manual vent will begin relieving at 160 psig. The rupture disc/ relief valve assembly relieves at 175 psig. The relief valve has a T orifice. Atmospheric VCM release occurs at 195 psig. 5. A worst case situation of 5 percent conversion is assumed. MJH:1km 7/11/80 r 'I -m- . ,|. . I -mt' * |t < - -[. ^ .< . TV' T ,L _ I -ki .................................... - -7 T Hi -i | VAB.0001100000 .'I ' EQUIPMENT LIST REACTOR RELIEF CONTAINMENT--MEMO ITEM OKLAHOMA CITY PVC PLANT Item No. NA-100 NA-101 NF-100 NF-101 NG-100 Service Blowdown Slurry Agitator Blowdown Slurry Agitator Blowdown Drum AMS Injection Pot Blowdown Slurry Pump MJH:1km 7/11/80 I' L -Jl ' -I : II . ^ I 1 , L |: . If: r - : -1 VAB.0001100001 n ' I -V TV EQUIPMENT SUMMARY REACTOR RELIEF CONTAINMENT--MEMO ITEM OKLAHOMA CITY PVC PLANT NA-100 and NA-101 Blowdown Slurry Agitators (Two Required) Use T.ightnin Model 8r>S20 (or Conoco Approved Equivalent) 20 Horsepower Motor Approximate Cost = $30,000 Each NF-100 Blowdown Drum Design Conditions Pressure, psig Maximum Temp, F 0-200 180 Diameter, Feet Length (T-T), Feet 20 40 Material of Construction Carbon Steel with Baked Phenolic Internal Lining NF-101 AMS Injection Pot Design Conditions Pressure, psig Maximum Temp, F Diameter, Feet Length, Feet 0-400 750 2 3 Material of Construction 304 SS NG-100 Blowdown Slurry Pump Type GPM Centrifugal with Open Impeller 150 AP 30 psi MJH:lktn 7/11/80 : v:. ' 'i'I-T 11 i.-j --.................; -0 .1 f i....... t 'i i.- l I, i > .I VAB.0001100002 -ri ' r U it& o VAB.0001100003 VAB.0001100004 I- ^T|I4W conoco : .1 -HS Interoffice Communication To From Doto Subjoct R. E. Barker W. R. Finch July 11, 1980 Budget Estimate for Reactor Relief Containment--Blowdown Drum Oklahoma City and Aberdeen PVC Plants Attached is a budget design by Mike Hurtz for a blowdown drum installation at Oklahoma City. The design involves three alternates: Alternate 1 - Use a blowdown drum size of 18,000 gallons. Alternate 2 - Use a blowdown drum size of 30,000 gallons. Alternate 3 - This design will also be used for budgeting an installation at Aberdeen. Use two 30,000-gallon blowdown drums, one for each module. Please include the appropriate difference in labor cost and pipe cost. If any. Would you please prepare a budget-type estimate for these three alternates. a( ) W. R. Finch Senior Process Engineer Chemicals Division Process Engineering Department lkm Enc CC: JHM: REB: RDM: JPW: RAF -*t hi- j- 11 ' ,ji - <-; i- Jtfe if * -p "c-mapr -m VAB.0001100005 BUDGET DESIGN REACTOR RELIEF CONTAINMENT--BLOWDOWN DRUM OKLAHOMA CITY AND ABERDEEN PVC PLANTS July 11, 1980 Work by: Michael J. Hurtz Process Engineer Chemicals Division Process Engineering Department | , TT-7-H- 1^'* '-`T: ' '' ft ' r +* fc| I'-i' r- i IP m VAB.0001100006 - TABLE OF CONTENTS BUDGET DESIGN REACTOR RELIEF CONTAINMENT--BLOWDOWN DRUM OKLAHOMA CITY AND ABERDEEN PVC PLANTS PROCESS DESCRIPTION . . . EQUIPMENT LIST ................... EQUIPMENT SPECIFICATIONS INSTRUMENT LIST ................... INSTRUMENT SPECIFICATIONS PIPING SCHEDULE ................... WORK LIST .................................. DRAWINGS No. ] 3 7 9 24 nr'-i r- V`U VAB.0001100007 .. >4.4 -I-..I -U` 1 ! I'WWT-I'- 'L r- j -|-7 f *,^'Tr ' --WT.-4TM .1-. . --.h 4-- PROCESS DESCRIPTION REACTOR RELIEF CONTAINMENT--BLOWDOWN DRUM OKLAHOMA CITY AND ABERDEEN PVC PLANTS Pu ge I The purpose of this design is to provide a partial containment system that will eliminate VCM release if a reactor becomes liquid full. The design requires installation of a blowdown drum (pressure vessel). The blowdown drum will be connected to the existing reactor charge water header to allow dumping of the reactors into the blowdown drum. The slurry will be pumped from the blowdown drum back into one of the reactors through the existing dump header for steam stripping. The blowdown drum is to be a carbon steel vessel lined with a baked phenolic resin. This design is based on the Oklahoma City PVC Plant. Two alternates are considered for Oklahoma City. Alternate A assumes a blowdown drum size of 18,000 gallons. Alternate B assumes a blowdown drum size of 30,000 gallons. This design will also be used for budget estimating at the Aberdeen PVC Plant. Aberdeen requires two 30,000-gallon blowdown drums (one for each module). MJH:1km 7/11/80 EQUIPMENT LIST REACTOR RELIEF CONTAINMENT--BLOWDOWN DRUM OKLAHOMA CITY PVC PLANT Item No. NF-1 NF-2 NA-1 and NA-2 NG-1 Service Blowdown Drum AMS Injec tion Pol Blowdown Drum Agitators Blowdown Drum Slurry Pump Blowdown Drum Spray Nozzle MJH:LKM 7/11/80 VAB.0001100009 I,*4. NOZZLE SCHEDULE >. * * 1* 1 . l*o rw til 1 <s _\A \J^ w > I tH **+ cj t^' > B *| & 4-^J 4 V ^ 1 <*n *1 'M .hM ' v> I ID O iDDni KM * va fc 2A IaI *C* 0/ ,9/ rr' >-- * -- *1 0 / t? --/ ^ Hi f// juom) n- t m 4 b * u, vu T; 14 dg Si$f L, , ><j Ssc 5{ a v* V *" i ^S J-^* i<5 $fc ?* ^ ^ i?fe w HNi - iN* ^ vj 5* V N< tj ifS* S ^ ^L^ ^ JNl- t - *0 W ; w \ la W ^ ^ j a* ^e^s5is^ ^^v *w*a 3-Jf W!> -* *^t 3bs ^< C\i r f'. 5t 3 <i^|Wi| m il |i Ua | 1, >? r-.'1 >* *f= ^ ' - 1 - t 1 * ^ 1*r- f'.fip- - *- .0001100010 p-M t! *I . -1 .................... H - H . -f -:|l 001100011 ......................* - -- r4n.1p4+**v .. *> T . ......................................... ! , 1 Pr < * : I .-f, ffs *+*! : r*f f-M I 0012 F-270-9A F-27O-0A i i" < .... e age 5 conoco C'.oMtinunial Oil Cumn.iny Engineering Comet Ponca City. Oklahoma Centrifugal Pumps PLANTClTY. - P VC PROJECT AgftCT Oft MM Cll H A I ION Mil I I 1*111) II (, I Nil ____ ____.............. . All NO DA I t L-- I NO NO MADE BY__ fAll XtL. he O( NO APP D BY_1 * p o NO LlF CowTftiri W'fJTm APPLICABLE TO: ESTIMATEJ>^r PURCHASE < ) ___M^-r SERVICE MOk O du*J I ;/k \Jc iAvr>. S Iv-rc y '.Ji.Wx MOTOR DRIVE t TURBINE ( OPERATING CONDITIONS LIQUID v/OYl U.S. gpm at PT, NOR. ) RATED PT F ^ DISCH PRESS., psig / 7Q SUCT PRESS.^psig^MAX & Q& _ RATED j*f SPGH.iiPT /,>> VAP PRESS, ill PT, psia VIS at PT, S*j {> rf'*? COHR/EHOS i:.iuw<l 1>V p \J DIEF PRESS , psi DIET HEAD, (1 NPSH AVAIL , ft 3.0 CONSTRUCTION CASING MOUNTING (CENTERLINE ^ (FOOT I (BRACKET ) (VERTICAL ) SPLIT TYPE ___(AXjAL^ J (RADI A L I (SINGLE VOLUTE ' ] (DOUBLE^/6 LUTE (DIFFUSER TAPPED OPENINGS (VENT V ) (DRAIN X > (GAGE CONNS. 20 NOZZLES LmfcSIZE ANSI RATING FACING POSITION 21 SUCTION /S & F 22 DISCHARGE f SO Rf 23 MATERIAL CODE-EXTERNAL CASING 24 l-CAST IRON INTERNALS CODE 25 B BRONZE IMPELLER 2fT S STEEL INNER CASE PARTS 27 C 111 3% Cr SLEEVE (PACKED) 28 ] A-ALLOY SLEEVE (SEAL) 29 j h HARDENED WEAR PARTS 30 f -FACED SHAFT INTERNAL PARTS X 1Bs C SPECIAL MTL. CODE 1 B s C .... . . A .... 1i sc . Cr Cr At At Ccc C 1 B Cr Cr s s sS .. 31 'Hj X 32 | MOTOR DRIVER BY \| /S <* <? f. ITEM NO. MTD BY TURBINE DRIVER BY ITEM NO. MTD BY HP HPM FRAME HP HPM MAT'L Ml R OR COMPANY APPV'D, EQUAL TYPE_'T l):. c. 1NSUL _ ENC " "TEMP RISE C 40 + D LTS/PHASE/CYCLES .. 4----------- BEARINGS LUBE MFF1 anil TYPE INLET STEAM, psiy EXHAUST ~ * ... TEMP F STEAM RATE, FL Ib/BHP'HR BEARINGS LUBE NOZZLES SIZE ANSI RATING FACING POSITION FULL LOAD AMPS INLET 43 EXHAUST REMARKS i---------- IaYO % CL. 3-sJr__ i j a c y\ V/YLpcU C'f C:z 4 Li, p<?Y X V e <s + Y vaj a \ <* i o t 2.2.0 ^ ^ )oof .pf M P r 3 > ^ - PUMP IS TO BE MANUFACTURED IN ACCORDANCE WITH THE FOLLOWING STANDARDS. * - 49 AP161Q 50 ( I INDICATES ITEM CHANGED ON LATEST REVISION i NOTE THE SOUND LEVELS GENERATED BY THE PUMP AND DRIVER SHALL BE WITHIN THE LIMITS OF THE ATTACHED SPECIFICATION. VENDOR MANUFACTURER SIZE AND TYPE STAGES RPM ROTATI ON F ACJ NG CPl.G t FF. HYD. H.P RATED B.H.P RATED HP DRIVER DIA. IMP. MAX DIA. IMPE LI f fl N.P.S.H. REC1D IN f I LL DID PUMPED MENS HEARING No RADIAL. THRUST ^ACKW.0R SEAL FLUSHING. GPM J MATERIAL EXCEPTIONS BY VENDOR -I WATER COOL ING BEARINGS STUFF BOX PLDl SI AL GLAND TOTAL C.W. REQD coupling7mf R COUpCrNG, TYPE 'GUARD MECH. SEAL, MFR. MECH. SEAL, TYPE PACKING ou DELIVERY. WEEKS pump~prce DRIVER PRICE EST. FREIGHT TOTAL PRICE 01)01 AT ION WILL NO! HE CONSIDERED IF SUPPLIER DOES NOT COMPLETE Rll.H1 HAND COLUMN 1 76 SHE I 1 Ol 7/11/80 VAB.OOOl100014 A* F-270-9A INSTRUMENT LIST REACTOR RELIEF CONTAINMENT--BLOWDOWN DRUM OKLAHOMA CITY PVC PLANT Page 7 Item No. CV-1 CV-2 CV-3 CV-4 CV-5 CV-6 CV-7 FI-1 FI-2 and FI-3 FCV-2 and FCV-3 LG-4 LI-1 LAH-1 LAL-2 LS-4 PG-1 PG-2 PG-3 PG-4 PG-5 PG-6 PG-7 PG-8 PG-9 PG-10 PG-11 PI-1 PAL-5 PCV-1 PAL-6 and PAL-7 PSV-1 PSV-2 PSV-3 PSV-4 PSV-5 PSV-6 PSV-7 MJHilkm 7/11/80 Service Recovery/Steam Stripping Header Valve Recovery Valve Recovery Valve AMS Dump Valve Slurry Dump to Blowdown Drum Valve Hot Water Charge Valve Hot Water Charge Valve Slurry Pump Seal Flush Flow Agitator Seal Flush Supply Flow Agitator Seal Flush Return Flow AMS Injection Pot Level Gauge Blowdown Drum Level Indicator Blowdown Drum High Level Alan Blowdown Drum Low Level Alarm AMS Injection Pot Low Level Switch Slurry Pump Suction Pressure Slurry Pump Discharge Pressure Nitrogen Pressure to AMS Injection Pot Nitrogen Pressure of Nitrogen Bottle AMS Injection Pot Pressure Charge Water Header Slurry Dump Header Agitator Seal Water Supply Pressure Agitator Seal Water Return Agitator Seal Water Supply Pressure Agitator Seal Water Return Pressure Blowdown Drum Pressure Indicator AMS Injection Pot Low Level Alarm Nitrogen Pressure Regulator Low Agitator Seal Water Pressure Alarm Blowdown Drum Safety Valve Blowdown Drum Safety Valve Blowdown Drum Safety Valve Blowdown Drum Safety Valve Blowdown Drum Outlet Line Safety Valve Water Spray Line Safety Valve AMS Injection Pot Safety Valve VAB.0001100016 Instrument List Pace 2 Item No. RD-1 RD-2 RD-3 RD-4 RD-7 SW-4 SW-5A thru SW-5F Page 8 Blowdown Drum Rupture Disc Blowdown Drum Rupture Disc Blowdown Drum Rupture Disc Blowdown Drum Rupture Disc AMS Injection Pot Rupture Disc Reactor Blowdown Switch Reactor Blowdown Switch (1) All signals to the board are electric (4-20 ma). (2) All electric instrumentation is to be intrinsically safe. MJH-lkm 7/11/80 " HI -h. --f 1 |! i \ ' "v .......................... . ' - H'sfl If- -** T VAB.0001100017 PLANT conoco Continental Oil Company Engineering Center Ponca City, Oklahoma Control Valves CY\y . PHOJkCT iJm t Page 9 SPECIFICATION SHEET PROJECT NO _ Art NO . DATE INO NO MADE REO NO APPO hyALCSL--, PO NO T flfl fr OCNKHAL tllMNn A TAG `iPWVIC i: _C-l fa) co-3 Rec/4rni SrKimwg ftFr. /grrrt f-rliPflfnt- RecArm . jLl1_IQ LINL JjUL MANUFACTURER ?> MODEL NO. 77 TuFLMVJg SERVICE CONDITIONS FL UID a TEMP F NORMAL MAX PRESS t INLET MAX l-OEF vicm vapor 9* (A TO MIN NORMAL MAX MOLtrULAH WEIGHT A PI yog SP OR '> *Q F. FT 1 3 WEIGHT ' VAPOR IN I 4 VI aIT Y -Vr F T. P OUT RATE NOR. L0 HR (SCFHi GPM R AT f* MAX L9 HR (SCFH * GPM l 7 NORMAL FLOW Cv le BODY .-O -21 22 2J 24 26 27 28 31 33 34 DOPY SIZE 7 YPC i ANGLE OR MATERIAL POUT SI END CONNECTIONS BONNET Cv LUBRICATOR ISO VAL PACKING TRAVEL INDICATOR Flft S/9F^ TRIM TYPE INNER VAL I NO OF PORTS PLUG A SLAT MATERIAL t\ T. ACTUATOR TYPE FAILURE POSITION PL \JL C-S* L0 K.F. pm, (7 BgTTlS POSITIONER 35 INPUT SIGNAL OUTPUT SIGNAL 36 BYPASS GAUGES 37 MANUFACTURER MODEL NO. ACCESSORIES NOTES: <9M "OFF 'j PllU^ PLUG ^ I (o 5 S . :Q: Harris TU^FH fVi G CA g>M-oF F STr A j v c w y a i?. o 2oe>0) n ofO -OFF /4ms/ 3oo I Z c? o i/ f U(aG* h S-S . 3oo* K.F LUG- g <: PLUG 3<2L3 W. flLOCWCD (S') Tk^TC-" t OC ti- a * il H z> I I INDICATES ITEM CHANQCO ON LATEST REVISION, I t M INDICATES MANUFACTUAIA TO Si VI RCOUKSTSO INFORMATION IN HIS OUOTATION. REV. 7 24 60 SHEET or 7/11/80 REV. 00018 -i ............. ` "h V* 4 ni' Page 10 NOTES XrJTfc'lltoai lyirrM CM-H , ( > INOICATCS ITEM CMANOCO ON L.ATSST RCVISION. iKilNOICATtS MANUFACTURE TO OlV* REQUESTED INFORMATION IN HIS QUOTATION hev.TjTSq SHEET OP 7/11/80 REV. 00019 i ' 11 * 4-435 NOTES FOR CONTROL VALVE SPECIFICATIONS (1) All Tufline on-off valves need a tap for the bleeder on the valve body. (2) 250F at 15 pslg. (3) 200 psig at 172F. (4) On instrument air failure, valve fails as is; and on electrical failure, the valve will close. (5) To be equipped with open-close switch with lights. (6) The solenoid valve is to be Asco Model No. 8344B5M0 or company--approved equal with explosion-proof case and operating voltage of 24-volt DC. (7) Deleted. (8) 250 psig at 100F. MJH-lkm 7/11/80 Sheet 3 of 3 VAB.0001100020 WTMHOmm lift vie* " | FX - f K)6 -f F,ef\t- Fl. u S l-t .... Page 12 SP Gfl AT P ft T ,?8 [ CJVCV A1 T ftP IcOMPRESSiatUTV 29 /*sc(fcr atp * r j(>, RATt NORMAL f -f - -- _ 3 1 AATt MAX | M*N J2 ] ^HTfcs m fl^r ^crr> ^TroowsTje-i FLO-Gft &c~ OjjTH 5-5"- 0c>rvJ$tj^cT/O^ /^/UP T'Hfl fl 0 0 CotO^C*T iO tic, Com PA toy ftPP&Oviep eSKJ I \J At G A)T~ '*! .' ^I -I-*' "*+ " * = s I* 1 ^-+ - (i J T I *. Ht- * ht: <:! a' CONOCO V ENGINEERING CENTER PONCA CITY. OKLAHOMA SPECIFICATION SHEET CotfTfittiSO PLAN T 0\LLf\ Ho## CiT C ITEM NO SERVICE FC \}~ Aw 0 CU - 3 erfcu tc e A<S I'TATofe__ Akr A F E NO. _____ DATE 6~ MADE BY llflJ APP'D BY A B M NO n c? W O NO INO NO REQ. NO P O NO. Page 13 ReriAAfl) T^~i i i i A Jiccorrrv c T". Cp <S? l?F6LftTof^ X1ml e-r PS IG . &\aTLg-T" . PS\<g> FLjvai Rflre, Gf W ^gr/F/c Ct ASK \J i Ty <X> X~ IaJ AT^/e ^ _____ _____________________________________________________________________________________________________________________________________________________________________ WAX - 2-1 o -- Boo 2o_____________________________ 1 ___ \.o -- .... -- ----------------------------------------------------------------------------------------------------------------------------------------------- 1 OF Al^-TRUCTibAJ ...................................................................................... ... . ...................................................... ................................... ................................................................................................................................................. 4-cxiAT iorO Fc\j- Z i rO volL" ______ Fci;- ll\J MiA.-|7 N^r^s - r 1 1) ^ 1?6GU ~A To To f? F. kATFs__ 3D6L - /i ^ /-/ , O-Z To 7 ------------------------------------------------------------------------------------------------------------------------------------------------------------------------ i.o & m P-ftN V. Qg-Cowpariy fiPPHoveo ^raufli. -?.__ Fflcrofty rer 1----------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------- ---------------------------------------------------------------------------------------------------------------------------------------------------- Po >WT To 0V / <S r/W ri t irt`- -rrr SHEET t 1 < H 'll- 7/11/80 1 R&frAB.OOOl 1 F-270-9A Pago 14 CONOCO ENGINEERING CENTER PONCA CITY, OKLAHOMA SPECIFICATION SHEET GAUGE GLASSES & COCKS PI ANT Ok.Lfi MomA C it/ A.F.E. NO________________ _____ DATE W.O.NO MADE BY til.TiJ INO. NO. APP'D BY t/J&ir REQ. NO B. M. NO- Metier C^ior* P. O. NO. 1 GAUGE GLASSES 2 SUPPLY GAUGES & COCKS ^ GAUGES ONLY 3 4 5 6 7 a "~9 TYPE NO NIPPLES REQUIRED (TRANSPARENT CONNECTIONS 11/2" TOP & BOTTOM X WELDING PAD MATERIAL STEEL MINIMUM PIATING |TUBULAR ) 3/4** ^ SIDE OTHER OTHER PSIG REFLEX ^ ii BACK F U)' ' 11 .........................................................-- ---------- - -- ------------ - ------------------ - 1-------------*-*-*-- ------------- ^ -------------------- * - -- -------------p* "i 2 13 14 15 16 17 18 19 ACCESSORIES ILLUMINATORS: 31 GAUGE COCKS 32 SUPPLY COCKS ONLY 33 TYPE OFFSET 34 CONNECTIONS-NPT ANGLE 35 VESSEL GAUGE 36 MALE 37 1/2" FEMALE 1/2" 38 3/4" 39 OTHEH 3/4" 40" S*H 41 42 MAT'L MINIMUM RATING BODY PSIG <P 43 CONSTRUCTION: PLAIN 44 CLOSING 45 HANDWHEEL 46 VESSEL CONN. PLAIN UNION 4 SPHERICAL UNION 48 49 GAUGE CONN. PLAIN UNION GAUGES FEMALE 1/2" 3/4" 1 ] | j J j TRIM j F QUICK CLOSING LEVEL HANDLE SOLID SHANK OTHER | PLAIN 20 21 22 23 ' 24 1 25 MICA SHIELOS: HEATING-COOLING CHAMBERS internal NON FROSTING TYPE: CALIBRATED SCALE SUPPORT PLATES: [external 50 SPHERICAL UNION OTHER 51 52 BONNET SCREWED | UNION |BOLTED 53 SCREW 1 INSIDE ] OUTSIDE 54 RENEWABLE SEAT YES NO 55 BALL CHECKS YES NO ! 26 GUARD RODS: 56 PACKING MFR STD OTHER ! 27 28 29 30 ' 61 62 63 64 65 OTHER ------------ 1 TAG NO. REV. QUAN. 1 .......- - -- - 57 58 MFR MODEL NO. 59 60 NO. OF SECT. 3 VISIBLE LENGTH 38 Ya * - ------- -- -- Q_ CPLGS MFR. MOD. NO. --- --- PRESS 3cn -- -------- OPER. TEMP. SERVICE N) F- ACCES* SORIES ------------------1 NOTES -- ----- r 66 67 ! 68 69 1 70 * 71 72 73 ' 74 75 76 77 78 1 79 80 NOTES -4 4 6 --S 7/1.1/80 INSTRUMENT SOCIETY OF AMERICA SHEET REV 023 Page PLANT CONOCO V ENGINEERING CENTER PONCA CITY, OKLAHOMA SPECIFICATION SHEET LIQUID LEVEL INSTRUMENTS PROJECT ;KAaLtie A.F.E. NO_____________________ DATE fl-lW. O. NO MADE BYjMiiL. INQ, NO. APP'D BY REO. NO B.M.NO CWrflL P.0. NO. L ri 2 3 4 5 6 '7 [81 TAG NO. SERVICk E INSTRUMENT, TYPE LOCATION ELEMENT, TYPE LOCATION RANGE. INCHES LX -/ N fz-l , Lerveu d> C AT oft. Hottieci 0) d/p C&BL <JLl 0 F-l 7 LftW - 1 Nf-( MlSH _______ LAL.-2-________7T LS -H _w MF-I Lou~> Uov> LtuEL^wiTcrtM Urvctl L^xjCL f\uAAfY\ EottRD CO CpifPlCiTfiMC^ PAo Loul LGjeL ALfHe<V\| (L) CO CftPfle.rrftfcicg* Peoife 1 ............ ... ... IftWctJAruurrtL f^LortT NF-I O) _ . ______F-I __ J /UF-2- ________L)'_____________________ L________ Clh _ 9 INTERFACE LlQ/\)f\P Mi <5 a 5 //ims Cl J<sY 10 UPPER DENSITY, LB./CU. FT. &.x _; 11 LOWER DENSITY, LB./CU. FT. .. ... __________________ 12 TEMPERATURE F 1*70________ _ 13 PRESSURE PSIG O - Jl^Q 14 VALVE TYPE .. ._. 1 - S'S' S"6. 0 A in Rie'njr 3^ O O c 15 16 17 18 19 1 20 21 LOCATION MATERIAL BODY SIZE | PORT SIZE PLUG FORM &P | MIN. 1 NOR. | MAX. CALC. Cv { VALVE Cv __________ i......... .... .............. ............. 1 . ...____________1 _ 1, ________________ 1 1__________ __________I I _ _________ 1 _________ _______________ 1________________ , 1 1 _i . 1 , 1...... j 1 22 AIR TO OPEN OR CLOSE i 23 24 25 26 27 MAXIMUM SHUTOFF &P FLUID TEMPERATURE F PRESSURE PSIG API IM.W.I JC w/poc Si uftRV i no _______________ VCN\/P0C Slu.I?LY \^0 'LOO Ocivi /pvc 5LuftRy | iQpL_______________________ | 28 SP. OR. AT STD, COND. 29 SP. GR. AT P. ft T. 30 WEIGHT % VAPOR IN-OUT 31 VISCOSITY AT P. & T. 32 RATE, NORMAL 334 H- + RATE: MAX. I MIN. 35 NOTES: | _____________ _I___ _____________ _____________ Zil_______________ ________________1___________________ ------------- ,--------------- ----------- J All ^iC-.nmL TO f?<pr=iR.O FcecrrP-orJ Ic. 2.) d P Cecc t o PAD ywOUfjrr^> f*TTwDtfO DlAPMf^Gm TyPS ,, tfpL.fWCg' se-fiLZP p/ftPrtRPG m to er /Nsrritt^O oiJ pftuvn- (5 TO 0 ilih I.. /iLflpivi "1 <5 S`cj(- PO va-H FJ L.6-I 2*/ IMOlf'S FRom TaP pf= pfcum Cvf'L C)-flP.*Y* T# o LilvA^ri Ltruec i mucHCS Fftcuvi OF PRu rs 5.) 15-W I L H / IIM > L^Ufi. SwiTC.I-1 fUUS / lUj iiFCT/OAj W p I Nte clock ui iri-l cu- WHt'H Ii- yjl-i i S ti B low BS-1^ j Ol>-W SI-IchxLD CLOS&. 6) LT-tj SfIoulO ff T/e'D 74 v/6C pAcKup Pow*K SUPPLY 7 ^ "TIlE: LOt_4j Lf UtTL. SvajiTcH 15 FoTTOirvi <5F WF'i- J + *+-'- ' j...............\* SHEET 7/11/80, rev VAB.CKjOl100024 PLANT CONOCO KVC. ENGINEERING CENTER PONCA CITY, OKLAHOMA SPECIFICATION SHEET PRESSURE GAUGES PROJECTfk roft. Page a \ r NO OAT F.___ faztt. CIV O NO MADE BY APP'O BYJJxicl INQ. NO. REQ. NO B M. NO P.O NO. Q*ta i iUT - ffowtowrO OiLmm nr I3 14 NO. PG--l PG " L ISERVICE N-/ ^u,criovj MG-2. DiSc-HARSe Pftess 1 RANGE. PSIG O- 2.00 O -- 2.00 |5 P6'3 ... . pco -i Outlet 6 P-V. . PCv-t Ptf^ss. 7 o- 4 oo O -- 3000 8 P6 - <& ..... CRFKLG = Uift !.' dr HOg'lJ. PPC'SS* 9 %...-1. ^fiOTOA. P^fY(9 10 (v- 3_____ . JNA-l ScAL virile*'. SuePLy - 11 P6 -V Nft i Sc'FW- WAini Rerun sJ .". 12--i .JP.6-.IC? l'1 A ^ J?rrftL icA 5 ypp* y J3 fG _H_____ i- ttL ViOATCK-.. fcBFTPtflU 14 O Joo _o- 3.^*2 O - i/OO 0- H 00 O- 0 0 - </*o 15 16 1 17 1 18 1| 2109 1 PRESS. PSIG 1 TEMP.. F 1 !AO 1O0 ... 14 3 / S'? VS-9 ipiOtf _.. 7^ 2 2-0 <0 70 Liiv) JHV)-12_ Ljms .x n - iz- "300 AJ , 2....0 0 M Mcaft. Pa-6 2.0 0 2Zo V <t ** 1 70 So uleAft CU^ 1 vhu -- 1 L vWC mu - 1 G, 2 2.0 2?o r STTT' n - 1 -1 L iNG wn " 1 7 SV`> L\(0C uiu 12 I 21 I 22 I 23 L 24 j 25 1 26 11 2278 1 29 I1' 30 1 31 1 --32"i 1 33 ~r~____________________________________________________ .. _. _ 1 34 I 35 I 36 11 3378 I 39 1 m 4-0- -- 11 4412 1 43 44 1 51 54 55 56 QUOTATION WILL NOT BE CONSIDERED IF SUPPLIER DOES NOT COMPLETE RIGHT HAND COLUMN. SHEET -" :f Ii" il v r iq, ft- iFf :i4 t|i 4 Aft- 7/11/80 REV VAB.0001100025 conoeo PLANT^)|i^^ C iTy P\JC Continental Oil Company Engineering Center Ponca City, Oklahoma Pressure Instruments PROJECT R& ^Top, j?c:t ig Page 17 SPECIFICATION SHEET PROJECT NO. __________ A.F.E. N DATE J> 1 'S INQ. NO. MADE BY REQ. NO APP'D. BY P.O. NO. " DLOvmPv*-^ On.* v* 1 TAG NO SERVICE INSTRUMENT. TYPE LOCATION RANGE. PSIG ELEMENT TYPE LOCATION MATERIAL TEMPERATURE F 11 PRESSURE PSIG VALVE TYPE A F-l PdSSSaRg PR^SS Jr)Dic.ftTC>.r4 BQ 3oo PAL - PA-L-6 HP*'2--i>H.GSSUjfL6 IUkka fJA-t S&fiL. Wflrrgg- &&TUitv Alar no B0aao r n 3e?Q ( 2-) RittPftMffgL.1..ilk .22* $ ?,.r I ns: 1H uj i j&di $ E.-A Li N WU-" 1^ PSI<^ \AI MPi-Z- V7 PP^SS . TU itlU tug-f S fluftg i *if~P 14 LOCATION MATERIAL BODY SIZE PLUG FORM PORT SIZE A P MIN NOR, MAX CALC Cv VALVE Cv AIR TO OPEN OR CLOSE MAX SHUTOFF AR FLUID 125 |26 27 28 | 29 | 30 31 32 TEMPERATURE *F mftx PRESSURE PSIG "API (M W.) SP. GR. AT STO. COND. SP. GR. AT P.&T. WEIGHT % VAPOR IN-OUT VISCOSITY AT P.ST. RATE. NORMAL RATE | MAX. | MIN, NOTES UCrn \) ft p a & HA 22^ O J r.'ou-M'o^s ^rJO ALAgws ftRt to ^ r iwtotHef ?) ^T'PoitOT TO I Gr flfjp f\$lTa*rflBt-: WpiTg fe t c> O gfiCKU? UJfrT e R too Sys+eryi. SHEET 7/11/80 REV 0001100026 .'P fii 1- ''p 'if I1" M- t J I- IH R * , fc. -.! IP* - ^ Page 18 CONOC o ENGINEERING CENTER PONCA CITY. OKLAHOMA SPECIFICATION SHEET A F NO .......... _ DATE .. MADE BV JtftZTtL W O NO i^-O NO h 4 .. ^ SELF-CONTAINED PRESSURE REGULATORS APP'D BY _i_' .. KIO NO B M NO ___________*' o no PROJECT^fldnH rw if A.) T * O W rU IAPV\ ITEM NO Poi - Service PA-/ o)........................................................ Manufacturer f~t 0 h!C fi _____ ___ Model No. \30{-G- Line Size, Inches; i.............._................................... Stream and Valve |\) IT &(- f\j Cx" A S Temperature, F; no Inlet Pressure, psig, Naum Max X3-QO (D&Lui&aeo p e: s su ng) | Outlet Pressure, ps ig/Horm-Max | Specific Gravity T- and P 0*9*7 O - 3o o -- 5c>o | Viscosity at T and P, cp t 0*0 {2 \ Molecular Weight 2-<? | Rate, SCFH, Norm l*V' | Body Size, Inches Orifice Size, Inches V Notes: ftl/rlflgETAJ (jyj-ir.l&gg (\ Pir^-5rft r .T ^ r I fcr \1 hvyi.ez Kfc 6 u L/3 T ^ Wirt* BMQ. SHEET 7/11/80 OF ____Ft VAB.0001100027 ii i *if!" <ft:: h: * | |- ; f. r-n -jp - |f-- PLANT ENGINEERING CENTER rONCA CITY, OKLAHOMA P SPECIFICATION SHEET RELIEF VALVES ClTV P'dc, PROJ ECT I'nRP A I1 I NO DATE___ W O NO* MADE BY__ 1NQ. NO APP*D nv ( / REQ. NO a. M. NO_______ P. O NO g s=- Com-rAt rUtt?gJT - - urt* P5>\M FS') -?a#>StI''3 ITEM NO. ft TAG Pso-*/ P50- RELIEVES EQUIPMENT NO MANUFACTURER MODEL NO 5 rOumW SERVICE CONDITIONS r\) f-/ mpr 30 rl Si MFH ^0^ S 1 Cc>*> 1 <0-30 -Z Tc. l2 lftX5 tL_________________________________________________________ LitJg- 3-up-2. FLU IO STATE REQUIRED CAPACITY MOL WT SP. OR VISCOSITY MCM /QUofe) y/PVcQ \icirv Li O /. O 1 1 COMPRESSIBILITY FACTOR OSSIGN PRESS. OF EQUIPMENT PRESS (^>f&>PERATINQ RELIEVING TEMP 0 FLOWING RELIEVING BACK PRESSURE PS /& DIFFERENTIAL SET PRESSURE } 40 2^ S'" l *4o zrsr n<2. 360 *2.too 9>oo /OO / OO ACCUMULATION % BLOW DOWN to ( V) BASIS OP SELECTION CODE REQUIREMENT -- EXPOSED AREA FIRE INSULATION THICKNESS OTHER BASIS DESIGN DETAILS DESIGN TYPE SEAT TYPE T&tr fiC-Tt O PiSCL u-rO Avjjfty 0ALA|QCeP PiS Oo*)vj CeVT T rt-g (Ztf\ft L. AtJSiovJ co*I'IJtiopAl SONNET < OPEN OR CLOSED > INLET SIZE. RATING. rACINO OUTLET SIZE. RATING. FACING CALCULATED AREA ORIFICE LETTER ACTUAL AREA MATKRIALS BODY I BONNET SEAT A DISK OUIOE ft RING SPRING BELLOWS ACCESSORIES cs 7 ?oo*flF .JOLLSjSSJLE. 1 3^ (pmO CS S_5 cs ss Cl OZ joa* #50 F, -CP cs CS I 1*^0 %i l.ffl fa 8 g vM t: ol i" PumUfe- Scet^p .1(0 c s 1 <<: r9 cs LIFTING LEVER (PLAIN OR PACK EDI GAG CODE STAMP CAP (SCREWED OR BOLTED I OTHER SCfU&^lU gP scft&ujeo j-CAli uU CQ NOTES )> 3-> JWtM SO 5ot it)*, 6 i IO > U .||- MANUFACTURER SHALL VERIFY SELECTION OF ORIFICE SIZE AND MATERIALS. ?)?><>/) r.\ n tf /i ' VALVES SHALL MEET DIMENSION REQUIREMENTS OF API RP-02- tl 'S C>fif 0 ' O'fi er * Kt (./: I~ VALVKS SHALL MEET TEST REQUIREMENTS OF API RP-827. ^ KCcavJ (Rfc P rOft S-)nfW gui.u-r-ui* SUPPLIER TO COMPLETE FORM BY FURNISHING ,, _ INFORMATION FOR BLANK SPACES fiACk PlteSSUfte <Jp | SHEET OP. REV MR Btoco^o I? IM6- HPTo B< LJQuiD 100028 I____ 0 l -L plant >K(-Au<3vma ENGINEERING CENTER PONCA CITY, OKLAHOMA * SPECIFICATION SHEET RELIEF VALVES c try__pyjL PROJECT A F E NO DATE__ MADE BV APP'D BY B M NO . rna IA W O NO INQ. NO* REO NO P O NO i tOMzitr -6W Page 20 1 2 3 4 S 6 7 a 0 1o 11 12 [ 13 14 10 1 16 I 17 1 10 16 ITEM NO * TAG RELIEVES EQUIPMENT NO. manufacturerLPlfiggiS.. Cl)l MODEL NO. Ps ^ - 7 M r-2. 26> DO :z Z- SERVICE CONDITIONS FLUID STATE REOUlRED CAPACITY MOL WT. 1 SP. GR. VISCOSITY COMPRESSIBILITY FACTOR fT DESIGN PRESS. OF EQUIPMENT P5 PRESS Psi<^OPERATING RELIEVING TEMP <?p FLOWING RELIEVING BACK PRESSURE DIFFERENTIAL SET PRESSURE ACCUMULATION % BLOW DOWN % A rUS . t-f au 10 MS _ 11$ l 0.9/ _ ...........-................. . oAn . >400 ^00 l^oo 1o O LfOC> O BASIS OP SELECTION CODE REQUIREMENT 1 22 [ I 23 1 24 nruT*****6* AREAFT-3INSULATION THICKNESS OTHER BASIS (7-2. . 1 25 1 20 DESIGN DETAILS DESIGN TYPE SEAT TYPE 57 fttJPh RD 1 27 BONNET (OPEN OR CLOSED) 1 23 I 23 L 30 I 3i INLET SIZE. RATING. FACING OUTLET SIZE. RATING. FACING CALCULATED AREA | f0 ^ ORIFICE LETTER | ACTUAL AREA MATERIALS BODY I BONNET SKAT A DISK OUIDE a KINO 1" -3^Q*F a" f&o* mO^ b D 1 oJ!& C5 C S SPRING BELLOWS TJ- NGST'g ACCKSSORIKB LIFTING LEVER (PLAIN OR PACKED)! 38 GAG CODE STAMP CAP < SCREWED OR BOLTED) OTHER NOTES |.) OH. Cowif>Wf APftfoJti D MANUFACTURER 6HALL VERIFY SELECTION OF ORIFICE SIZE AND MATERIALS VALVES SHALL MEET DIMENSION REQUIREMENTS OF API RP*62. VALVES SHALL MEET TEST REQUIREMENTS OF API RP- 827. SUPPLIER TO COMPLETE FORM BY FURNISHING INFORMATION FOR BLANK SPACES Riv. iaa ....................1 ..........................1 . 1 / 7/11/80 SHEET. OF. REV VAB.0001100029 - *r-r - f\ if |` ' ` > ii'C'ii-.-p ii . r-,,, i h h rr-'-ifit1 .*i" RUPTURE DISC SPECIFICATIONS REACTOR RELIEF CONTAINMENT--BLOWDOWN DRUM OKLAHOMA CITY PVC PLANT Item No. Location Line Size, In Rupture Disc Size, In Manufacturer Type Set Conditions Pressure, psig Temperature, F Operating Conditions Pressure, psig Temperature, F Disc Material Flange Material Inlet Outlet Flange Rating ED-1(2) NF-1 8 8 BS&B S-90(3)(4) RD-2 thru RD-4(2)(1) NF-1 8 8 BS&B S-90(3)(4) RD-7(2) NF-2 .1 1 BS&B S-90(3)(4) 215 225 400 178 182 725 FV-140 60-225 Nickel FV-140 60-225 Nickel 300 70 Nickel SS SS 300-Lb RF SS SS 300-Lb RF SS SS 300-Lb RF (1) One required for 18,000-gallon drum. Three required for 30,000-gallon drum. (2) Rupture disc to be furnished with 2 1/2*pressure gauge. Gauge is to include stainless steel excess flow check valve. The pressure gauge is to have a second needle that stays at the maximum pressure seen. (3) Reverse buckling. (4) To be equipped with BS&B type SRB-7RS safety head assemblies. MJH-lkm 7/11/80 VAB.0001100030 II P!1 14-' t f........................*w***r*-ji - ft.................................................( i -- ' -fW > ' f _ revYAROOO1100031 F-270-9A 0032 F-270-9A PIPING SCHEDULE REACTOR RELIEF CONTAINMENT--BLOWDOWN DRUM OKLAHOMA CITY PVC PLANT The piping schedule conforms to the CED standard line designation. This system denotes line size, service, line number, insulation requirements. and piping specification as follows: Sample Line Designation 3-SL-350-H-A2-3 Piping Specification Insulation Requirement Line Number Service Nominal Line Size, Inches Sample Piping Specification A2-3 Third Specification of A2 Group Piping Material Nominal Pressure Classification Service Designation Used Designation Service SL XO WH WC HM WP PS WU AB CL Insulation Requirement Low Pressure Steam (51 to 150 psig) Sodium Hydroxide Solution Cooling Water Return Cooling Water Supply Miscellaneous Hydrocarbons Process Water Slurry Utility Water Breathing Air Low Pressure Condensate (Up to 150 psig) H Hot Service S Steam Traced and insulated N No Insulation Required I ^,v s............... .................................r.iz- wnf>.'I-.* , - limiHff rtlr- r1- t k>- | ' 1' r-' f..................ppil*-:. h J Hp. If- . ..,gip 4-bnf. . VAB.0001100033 Piping Schedule Page 2 Service Designation Used (Continued) Nominal Pressure Rating A B M N Piping Material 2 13 16 Service 150-Pound Class 300-Pound Class 125-Pound Class 250-Pound Class Carbon Steel 304 or 304L Stainless Steel 316L Stainless Steel MJH-lkm 7/11/80 VAB.0001100034 * *'-.p 'rr b * _ | t g r* |CvJ 0) \J o _ , v3 ^ S D ?v VJ \il \ c*: v. 01 4J (0 Q Ot fit J ril O 0> -*J r-i C O <0 u Page 26 7/11/80 i : i -i:- 1 ! ' 1' Ti:f -p ' I1' * 1 i-a J ill 3 l. -h :* -i --I.- -* t .0001100035 WORK LIST REACTOR RELIEF CONTAINMENT--BLOWDOWN DRUM OKLAHOMA CITY PVC PLANT 1. Install new blowdown drum NF-1 and associated piping and instrumenta tion, as indicated on the P&I diagram, south of D-306. The existing road may need to be rerouted. 2. Tie in new line HM-1 to the existing recovery header near D-306. Install new CV-1 on the existing header. 3. Install new CV-6 and CV-7 on discharge of G-301/G-302 charge water pumps downstream of reactor rinse line tie-in. 4. Tie in new line HM-4 to the existing hot water charge line at D-306. 5. Tie in new line PS-6 to the existing slurry dump header between D-306 and the dump Sweco. 6. Tie in new line HM-11 to the existing EPA system outside V-20 building. 7. Tie in new line WP-5 to the existing two-inch line to the water strippers F-210/F-211 outside the V-20 building. 8. Tie in new line HM-3 to the existing one-inch line from the AMS holding tank, F-387, to the D-306 emergency AMS pot. 9. Tie in new line WU-12 to existing HPSW line at D-306. 10. Tie in new lines WU-15 and WU-17 to the existing 3/4-inch agitator seal water return line at D-306. 11. Tie in new lines WU-14 and WU-16 to the existing 1 1/2-inch agitator seal water supply line at D-306. MJHilkm 7/11/80 - - -S'- : ^rfi .. y "i^- = 'll W Pl< j-- '*! r *. . * i 1 .. .|- .r VAB.0001100036 ft tl .j . cr n- = . i-J *S*it T)001100037 1. ^Capital Budgets h 1981 VAB.0001100038 conoco Interoffice Communication From Date Subject J. R. Pavao - Room 193^ " Houston C. L. Miller April 7, 1981 1981 CAPITAL BUDGET ITEMS A We do not plan to AFE item A-ll, Water Preheater in the New Module ($19,000). With the installation of the V-ll Centrate Heat Recovery Project, AFE 9551, this item is no longer required. We do not plan to AFE item A-*3, Rigid Pelletized Production - Line V. Emphasis is being placed on developing a bottle compound instead of rigid pellets. Unless there are objections from the Business Area this project will not be AFE'd in 1981. Item A-2A, Replacement Gearbox for Farrel Mixer ($75,000) was approved in 1980; therefore, the project will not be AFE'd in 1981. A major portion of item A-12, Compliance with EPA VCM Standard, was approved in 1980. Thus $962,000 of this item will not be requested in 1981. C. L. Miller CRM, SJV VAB.0001100039 Interoffice Communication To R. E. Lehmkuh1 From R. A. Frohre i ch Date August 8, 1980 Subject 1981 CAPITAL BUDGET Attached is the second issue of the 1981 Capital Budget for the Aberdeen PVC Plant. This issue incorporates the comments from the review of the first issue. The budget contains 25 projects with a construction capital requirement of $7,133,000 and a transportation capital requirement of $691,000. These projects have a combined DCF rate of return of 17.8%. The eleven revenue generating projects have a capital requirement of $3,^9,000 with a DCF rate of return of 36.7%. Two major compound projects are included. One provides for the moderniza tion of Line I. The other provides the capabilities to produce rigid compound pellets on Line V. These projects will supply the added volume of flexible compounds and rigid compounds to meet the projected sales requirements. Cost saving projects include a system to upgrade sifter overflow, conver sion of the automatic bagging and palletizing system t' resin use, a vacuum clean-up system for the dryer building, a slurry delumper, and a direct steam heated charge water preheater for the new reactor module. Major projects in the safety category include replacement of the agitators in two of the old module reactors and new initiator charge pots for the reactors. The final phase of the ongoing plan to upgrade the firewater protection system is included. Modernization projects will provide needed railroad tr?:kage for VCM storage inside the plant and also a storage track paralleling the lead into the plant. Projects to provide the capability to produce 10-8 plasticizer and a project to upgrade the reactor recovery systems are also included. I MMtilrii.it'itji. <hht 'i. J.K t VAB.0001100041 R. E. Lehmkuhl August 8, 1980 1981 Capital Budget Page 2 A project in the pollution abatement category will reduce the probability oUlf pe.xxpDeerrieienncciinnga VvCuMn relief valve discharges. This project should complete the major expenditures which have been required to meet the EPA VCM standard, barring a change in the regulation. Also, a project to upgrade.the plant waste water treating facilities to meet the tougher discharge limits is 1 nr 1 1 iHp.H . The plastics long range plan includes a new 25 MM pound per year compound line for start-up in 1984. The capital requirement.for the new lme .s estimated to be $5,000,000 and the project will be included in the 1982 budget. The plan also calls for a 20 MM pound per year resin debottle necking project in the 1982 budget. The capital requirement of this proiect is estimated to be $4,000,000. EPA is currently developing effluent guidelines for control of priority (toxic) pollutants for the chemical industry. The effect on plastics manufacturers is unknown at this time, but will likely require going one step beyond the current treatment. The Clean Water Act requires these improvements be operational by the end of 19^. Although specula tive at this time, a $2,000,000 project to meet the new requirements will likely be required in the 1983 budget. /tCl$. fyyrAAjtuJ^ R. A. Frohreich Attachments DISTRIBUTION: R. W. Gerwig/G. Husen - Stamford J. D. Burns - Houston W. C. Kolar - Houston R. E. Lehmkuhl - Houston P. E. Markey - Houston J. McCleskey/J. R. Friday - Houston J. J. Hall - Houston B. D. Ratliff - Houston D. E. Michels - Houston H. R. Flammer - Houston E. L. Kieschnick - Houston C. L. Sanderson - Houston J. Friend - Oklahoma City CLM, CRM, JRM, AHS, RDJ, TBD, SJV, VEM, JAD, RAD(2) ABERDEEN DISTRIBUTION: VAB.0001100042 CONOCO CHEMICALS 1981 CAPITAL BUDGET ABERDEEN PVC PLANT ($000) Plant Expansion and Modernization _____________CAP ITAL___________________ CONSTRUCT I ON TRANSPORTAT I ON A-l A-2 A-3 A-4 A-5 A-6 Compound Line I Modernization Recovery System Revisions Rigid Pelletized Compound Production-Line V 10-8 Plasticizer Production New Railroad Storage Track New VCM Rail spur Subtotal 1,800 385 236 210 35O 183 "3,166 Cost Savings 292 61 338 59T A-7 A-8 A-9 A-10 A-1.1 Sifter Overflow Reclaim System Automatic Resin Bagging Vacuum Clean-Up System for DryerBuildings Slurry Delumper Water Preheater in New Module (Energy) Subtotal 226 101 77 35 19 Tihr Pollution Abatement A-12 A-13 A-l4 A-15 Compliance With EPA VCM Standard (Air) Waste Water Treatment Revision (Water) Plasticizer Spill Containment (Water) Groundwater Monitoring (Solid) Subtotal 1,^54 560 50 30 2 094 8/8/80 VAB.0001100043 CONOCO CHEMICALS 1981 CAPITAL BUDGET ABERDEEN PVC PLANT ($000) Safety and Health A-16 A-17 A-18 A-19 A-20 A-21 Reactor Agitator Replacement Vinyl Initiator Charge Pots Fire Protection Improvements - Phase IV Safety Equipment and Projects Normal Kill Solution Addition System Plasticizer Initiator Handling System Subtotal Mi seel 1aneous A-22 A-23 A-2^ A-25 Miscellaneous Projects Under $10,000 Capability to Receive Oklahoma City Pond Resin Replacement Gearbox for Farrel Mixer Laboratory Equipment Subtotal CAPITAL CONSTRUCTION TRANSPORTATION 310 165 160 106 76 38 S55 3A0 105 73 k2 5&0 GRAND TOTAL 7,133 691 8/8/80 VAB.0001100044 Aberdeen PVC Plant Overall Economic Bases 1981 CAPITAL BUDGET 1. Rated Production Capacity as of January 1, 1981 MM Lbs./Yr. Res in Compound Dry Blend Plasticizer 335 65 70 25 2. Gross margins for the various products (selling price less variable costs not including utilities) as supplied by the Business Area are as foilows: Year 1981 1982 1983 198i 1985 1986 1987 1988 1989 1990 1991 3 Utility Costs Resin 6.7 7-4 8.1 8.9 9.9 10.9 11.9 13.1 14.3 15.6 17.1 Gross Margin Rigid Compound Pellets C/Lb. 1 1.0 11.6 12.1 12 7 13.4 14.0 14.7 15.5 16.2 17.1 18.8 10-8 Plasticizer 4.2 4.4 4.6 4.4 4.0 4.1 4.3 4.5 4.7 4.9 5.1 Yea r 1981 1982 1983 1984 1985 1986 1987 1988 1989 1990 1991 Mi tin 8/8/80 Electricity C / KWH 3.74 4.12 4.53 4.98 5.48 6.03 6.63 7.30 8.03 8.83 9.72 id* y 4 Natural Gas $/MCF 3.15 3.47 3.74 4.03 5.41 5.84 6.83 7.37^ 7-96 8.40 ,i 9.07 ^ <7.17 1f u0 .1 t> 0KJ Steam $/M# 4.32 4.76 5.13 5-53 7.42 8.01 9.36 10.10 10.91 11.52 12.43 1 VAB.0001100045 ll Overall Economic Bases Page 2 3. Cont. a. Electrical costs are based on the present price of 3.12C/KWH with a 20% increase October 1, 1980, and a 10% per year increase there after per the Aberdeen Light and Water Department. b. Natural gas costs are based on the present price of $2.51/MCF. Escalation estimate is per W. H. Higgins of the Gas Activities Department of North American Production Division. The estimated costs includes an allowance of 5% of the natural gas cost to cover the expected surcharge based on No. 6 high sulfur fuel oil. c. Steam costs are based on the natural gas estimate. 4. Railcar Revenues Service Resin $/Year/Car 10-a PIasticizer Compound Year 1981 1982 1983 1984 1985 1986 1987 1988 1939 1990 1991 2200 21+00 2600 2900 3200 3500 3900 1*300 1*800 5300 5800 1*200 4600 5100 5600 6200 6800 7600 8400 9200 10200 11300 2800 3100 3400 3700 4100 4500 5000 5500 6000 6600 7300 Railcar requirements, revenues and escalation as provided by Chemical Supply and Transportation are based on the following 1980 experience. Load Size Turnaround, Days Miles Per Revenue Trip Loaded Mi Res i n 10-8 Plasticizer Compound 170,000 Lb. 20,000 gal . 170,000 Lb. 46 46 26 1030 1407 846 0.23 0.31 0.23 1, i I j i fl lj. 8/8/80 11 n . ;i-1 . ;j !l j . ] 'l .1 1 VAB.0001100046 Overall Economic Bases Page 3 5. Utility Requirements are as follows: m Rigid io-8 Res i n Pel lets PIasticizer Compound d Electricity, KWH/Lb. Natural Gas, CF/Lb. Steam, Lb./Lb. Product 0.123 0.75 0.66 0.217 - - 0.032 0.028 1.12 0.223 0.28 .6 Budget preparation per D. Michels IOC dated June 5, 1980. i t i i i i i i i i i i 8/8/80 |M 4M|I . .11111, | VAB.0001100047 I,.'. ?1lrPk<*r|L 'ihUrr" 'L mu* CO o -H oO oo ~n OO om zn o cn oc *n cr 73 0 CD r-r 0> lll l l tIl1l l l i l ION>N>IO|oro--* -- -- ONVH vn x~ vj ro -- o^O oo^i \-nvjj ro TJ T o V--* CD O r-tUN c o c CD CD 3 c vn CD 1IIt111IIII II1 Lfl o (/> oc "n or c* 77 O CD O C --- IIII II - - -\D OONI 3 ON -- o III vo ro -- vn i i i vn i i i i io "O 70 o CD* Oo rt m m > CD < (D 3 C CD v i io ON V*J ON ON -- VO -- -- --* vn x------- vj O X* VJ 'O O (JN CJN VJ ON Vn OO Vn fO VJ Vn o CO On On O Ul O o X- VH O ooooooooooo ro VD VJ VD -- vn -- VD O O VD vn -- IO IO IO VJ VJ O ro --* vj oo vn -- on o on vn o oooooooooo VI VJ cjn -- k> ro cr\ oo ro fo vn vd vj vj x- vo ro o --* vj oo on vj VD VJ \_n vo vn -- -- *-0 ro ON vn vj -- vj vn x- x- vn vo ro vn vj VD O on vn -- --vn VD vn vn ro o n vo rovjvnvo 1- o>oo ON ro ro oo on o \jJ 'JVN N> W ui O'- -- w o - ro -- ro on x-vo vi * oo ON o vo on vn vn x- vn vo ro coo U) ro vj ON on vj vn x- on ro VD IO -- ON vj vn x- on oo c on vj vj vn x- io vd o on vn vd vn vn [ro > co VD m oo 7? <n C3 mo fr- ON ro --* Nj -L/> vn CTN ro on -- VD ON VJ --J VJ -- vn oo iw g .hI1. o -- VJ vn - u w --4---------- vn oo vn * VD x- ctn ro .pt* VJ *--J "'J vn Vn VD Q tfIr r vo VD VJ vj ^ x- x- ?o vn VJ oo ro '-J ON OO '-J o oo VD VJ X- VJ c~> i -n "0 oo fc j i; h ON vn VD --' VO vn vn ON VJ ro -- VJ -- O OO - o i. i- vn --* ro io vd -- io k> o -- vo vn vo ON vd vn oo ro vn ro VJ "O vn vn ro i i' r vn ro -- ocoroo--'X-vovncorovoovn VJ o vj VJ vo -- "J ^1 o ON o I iI >vn vj vn ro J __. ON -- VD N4 On ro O '-*J O VJ OOO -- -- OOVJ--'VJ ON on ON VJ VJ --p VD o VD ---* OO vo VD ON oo VJ ON --J vn --- oo |vn 7> *-J X- O XPN? vo -- w --r xui u n -- '-o ro o "' TM"* ON VJ o oo fo vn VJ oo o ovoooro-* -- oovo--*vo ro vo --wnv) X" vn vo o --ro vn VJ -- ---1 ON "-j ON VJ VJ --- --* o VD ---* *sj oo VD -O VD VJ "'"J o o On OO VD -- o ON^J oo o O' ro oo Ion Vo -- ro vo ro --- ro vn vn io vn -- O' VO ON vo CO oo on -N vo on x- oo VD VD --. --< ro oo oo o vn VJ ro --- ON vn ON VJ VJ ro vo o VJ vn VD X- oo oo OO "O o ON ON VD O oo ON VJ o o CO vj io N> VJ ro -- IO vo ro ON O NJ OO VD -- o oo -- -- ON O' vn W ONSJ OO - oo ro o w . vn vn ON VJ --r --* -F" ON oo o x- o VJ ro ON vn vo o o CD O on ro vj vn ro vj -- oo to -- [oo __ VO IO ON VJ IO ---* ON O' vn ro vo -- ro ro x- Vj VD --J ro I i CO io ro on to ro vn vo o io vo on io vj o ro o o vn vo oo oo vn x- |VD I I O' co co VD vn o on vo o ro --- cjn oo o oo-^j * o -- vn ro on vn ro ro ON CO - * vo -- NN O --' X~ VJ VJ O OOOVJ VJ ro VD vn ro -- oo On VD vn on vo vn vd ro VJ -J ro --* o vn -- Jr* --* ro vn -- vn VD ^i x- x- ro -- o VJ VD on vn oo -o vn x- x- ON vo oo ^1 'O ^4 O ___ oo VAB.0001100048 r 1 3 7 ^ .0 1 6 7 0 .3 1628.3 1566.1 1^ 76 1. 17-8% 00 -a- on ur -- CM OO Pit 4 hi rsi rM i i oo -3- on i i 1 --- fM CM an o .-- un o cn o on ltv*-- o*-- on on co on un vO on cn oounvor^cMO--* ch on cn -- rvcncvtO'-iAN on un vO ,-- cm <-- oo - \D N CM - oo rs rovo rs cno 4**tft*4** o fM-a- un --- r^cntrv -- on on un cn -- cm*-- cr> n .^r #-- -- on vo vO *-- cm on fsl m |S CM la o on on cn co vOCO-T vO CO vD tm on on -- o on on vO im M3 -- CM co un an * M3 un ** CM CM m CM 1 1 i CM CM 1 O 1 I 1 l CO CM CM un vo o m3 cn on vo oo cm cmcm *" cm -- fM co un cm on oo o m co im .---- cm cm --- o on im -- o cm --1 un on -- o -- cm un on o on Aw. on on oo o on <-- on o on CM CM vO 3- CM on on CM CM 0000 uncM on on on m n --- im vo im on .-- i-- CM O -* o m3 im CM *-- vO N OvD CM CM on o CM vO * CM P un im CM im on oo CD an im 00 on UJ vo 00 on Ui C3 < co o a, un 1 CJ oc O cn a, o o </> < UJ <_> to oc 00 UJ cn CQ co on on CO CO < cn o CM 03 an co o o -- ooonr^ooon -- on (M o on 00 rM ---- o o CM on -- M3 CM on IM OO on M3 an un --- CM cm on o im co -- on oo 00 vO un un 00 on o o ^ r- r- ---- On I'm cn on md on on .-- on vo on un O CM un o on on cn --- ^9 vO un 1-- <-- vOnO cm vo on 00 un on CM CO o -- on o 00 -- on *-- on uj co on im --- .-- 4-- CM un on im vo cm 00 o -- cn un an un <-- im an on un c\i co un on IM -- --00 on uj -- on on vo un IM ,-- CM un un on 00 rv o n m \D an o un un un -r on_a- cm im _a- I'm vd -- ur rM un cm on *-- on vo on M3 --- -- CM on un an cn un o 00 rM. cn cm on co oncM un -3- -3" on.-- u3 -T -- on cm o co un ur un on on m3 CM -- CM o un on an o rM O CM oo .-- oo un o un .--t on co oo M3 o CO O on M3 un on un on vO on o CM on CM -4* .-- 1-- on cm un un un an on uj --- im cm -- CM CM on .-- vo on cm on CM on 1-- cm on on .-- un n (OvD o rv s moo oj n --- an cm fM CM unuruJOoeMO -- o on o <-- o un CM vO o .-- O CM on co m3 on-3- un >-- an-r- cm an o oonoooonooo un o on an cm m3 co un on co cm cm 00 im an KO rM on 00 --- o on m3 cm -- -- an cm --- o CM un -- J JM on un im^t on -- o cn IM O IM CM ' m3 -a- *-- -- M3 o ur on cm un on cm on >-- o on on 00 00 co co 00 on o on un m3 co un cm o un vo --- cm --- vO on co on un on -3- im CM CM CM on on un -4" o OO an on oo an oo on oo o on oo M3 on 4-- Pon 00 ooounounoovD o un co on o un m3 unco on cm un on -- o un fM rM un vo on -- un cm rM CO im --- on cm -- un \Ti 0 D C O > QJ oo,-r-o-mo^voooomvD CM If) 00 on co o 00 an-a-voonano un o rM d) on rM .-- \0 cm un cm n m^^r o m fM on -- cm un -- on-- c CM (U OC 4-> 3 o u _c co 4-J <D * >- 1_ tCi <Z +-J ~o U c CJ o * TM"n o fo u o Cl. cm on 11 cu o vO r-- D 1 1+-- t l 4CUD <U 3 t/1 o c- CM on un 7 8 an o CM on -2" un --- u un vO ii 1 i i l t i C1M CM1 C1M CM i CM t CM i m M a < < < < 4OU a: <D < < < < < < < < < < < < < < 4o-J _Q LU o JO D CO O o a. u CO ( 3 6 9 5 .3 ) ( 2608 1) IA A 7 .5 1 6 2 2 .1. TOTAL DCF RETURN VAB.0001100049 r-n-fi- ipq-HP'||J|I ip-1- n oo o V) Qj CP CI >o in X? x o CP ~o CP o> -- G> Qj in rf ?c o in O 3 -- CP -- 3 c rt CP 3 3 CT o lO > rt "1 *** X? in O' o 3 CP rr l/> Qj rt o O o "O rt Q> ~o -- --' --* zr CP 3*--* CP 3 qj XJ (p 3 CP "O 3 CP -- 3 3 -- CP 3 3 Qj 3 rt to rr in io Cn O < 3 in in OP n > in O CP QJ 3 CO -- rt < c a> O3 cr QJ o IQ rr rt 3 in O m CP XP rt o 3 Qj O TO CP --3 in O 3 in 3 in O - * CP --t N CP X T fij o 31 o O Ql rr 3n CO XI --* -- cCr O c --* 3 XI rr o 3 rt CL 3 o j-+ CP < Q> 31 in CP 3 3 31 CP CP O 3 in 3 rt QJ O in 2 Cl "U no XI QJ X) o O CP m --- QJ CO O 3 CL 3 -- "O cn o> 3 QJ X O XI C D" c rt 3 O cCP -+i O XD rt rt Qj -- CP O3 o< n Qj 3 CL in 4 c? in rr co ~g~ rt 3 c QJ rt p- CP __ o 33 CP n o m 3 (P fij IT 3 3 X 3 QJ 33 OJ in CP X) O r-r 3 Ql QJ CP CL rt tO -- 3 cr O -- inCP CP O CP SO CO o Qj 3 cl ___ SO ooo Cl qj o rr > rt in --. CP -- * o in > 3 "1 3 ^ Q> ^ in 3 l/> CD in o --> CL CP -- QJ CD in rr (P in < uo rr CP 3 rr in -- rt IQ 33 CP QJ Qj Cl 3 CP CP 3 X3 CP X> in CP t O CL CP Qj o 3 -- CP CL Qj 7T CP * CL CP Cr t-t CP o CP CO 3 v< 3 CD in --* -I "O rt O rr N o in 3 rr 3 o-- X" CP Ql -* 3 rr -+l (P 3 cn w3 IQ -< -- CP o 3 in CP O r-r 7C t o (p "l 33 CP o 3 < IQ Ql CP (P 3 ii ii II rt iii iii ro i i --. Sn SI hJ 1sn NS N> o sn o sn oooo VjJ -- I N> ro ro o SO sn to o sn o os sn o UJ oo o o ro Os| i so ro O ro i sn sn o xr ro o o o crs so so o so so sn o O os 0C5 Cl iQ CO CP rr SO oo 5 XJ >r- m X m~v -co- zz. CD o O O t-- m on ci m > CD so m TO o m ci m> SL <33 O OP cr> m OO "O 31 os to --1 so 1 sn sn o o o O oooo --t--i ro ro oo -- o o ro -- -- o ii sn o o o o o oo ro so as ro ro ro i sn sn o o o ooooo SO i ro -- i as o o o oo --> i -- i oo oo 11 SO SO oo 1 -- sn sn i ro ro oo ro ro so i ro o t j o sn sn o t i i ro x- i i so SD son scoo ZP K X /O ro c rp so 0J 3 Q- fp in CP in to os sn oo OS cn o sn o sn ooooo O oo oo oof ro o os sn O o sn VJ"l Os SO "-o sn sn o so crs M sj 4^ CP* SO O O CO o o o SO Qs Orr Co ro I J ro i 'O ro t i i i so I I I SO t 1 SO CO ro VAB.0001100050 m u im: .ih1- -js ^,pP: Mr'1 --ni^i-'.ir ihi- 1 -< J H' l-HItlfT 1 If'l liihltl -- . TI'H' -c - -nr k- <NI OoOa CM vO o m j- O CA OO -- vO vO CM CA CM CA oo CT\ M3 O LO CL < CJ 0O OA o tan> in 3 L_ 4-> 4 <D 4-4 "O U_ c co oA o3 CL o' X UJ CO Csl oo cr\ --o o<Xo> TC3"' OA IS 1 Il o o <-- -- 1 .-- I i-- oo o O OA O o OA CM 1 OA oo o o M3 M3 CM 1 CA O oOO O M3 LA CM 1 rA l11 OO CO CM --* 1l\ CM OA A CA m 1l CM LA H. LA o c- lo OA M3 LA * O OA A oo O oo o oo CM -- rA o r-- PA .1 1 11 111 1 0{/3I d) CO m OJ O oc o 03 o_ i CL 1 40-J) 3 0op-- </> J cn M Q- C oo -- (/i 4~J c 4-> tz V cn 4--> c E oO (U E o E oj E ) <>D Oi_ o ou oJ 1L, CL E ooCj CL --E L. 4o~# l-- u * 03 "dO) _c D c Z) L_ in -- *o c CO <0 0 <0o 1CO OA C *o 4o- ) c --o c JZ 4- 4-1 O -BM 4-J o 4-J *-- -- 03 cu 4--1 cn dj < -M c-- 03 4-1 - U- o 03 c<cu L). --* Ll X -- !__ LO o_ 4- tn 3 o o 4-J .--> d) m 13 c *--03 c CJ E (U 4C-OJ 4o--> O uA o >oc OC <CJ <^-- o l-- i 40--)* <L> o 0cu l_ CL 4-- ) </> 21 8/8/80 4 VAB.0001100051 1981 CAPITAL BUDGET ABERDEEN PVC PLANT CAPITAL EXPENDITURE SCHEDULE C$000) "tJ ln 31 :o -- O CJ -*-* CD Cj 3 rt if) CD o *< n r*t Cj rt ----- rr --1 'C ~0 O o3 o-- 7< m N -- _Q rt c 05 o ---- 3 --> LG ft M ft rt rt -- CO r*t QJ => O r3t OZJ O -1 rt O rt c 3 rt o CCJ nt O fl> 3 n -a rt rt O 3 l 3 3 T3 rt a>"I O LQ -- rc > a. -o "i <CD rt cl O 3 3J rnt CL, rt3 -- rt O 3 rt 3 rt ft) --* n rt V> I] -- O rt rt 3 3 rt * to tn tn < 3F "< tn rt rt rr rt rt 3 3 0) rt rt -- Q. IX rt rt rt 3* !3> tI rt I-- Ui Jrui fo O^ O 3) 3 o rt c rt 3 rr Cl ft n rt N rt rt rt rt "1 CO O er 3 cj *0 rt 3r----t rt rt> 33 O rt rt to :x "o -i rt " rt 3 -- rt --* -- rr m rt 3 33 Oort > 30 3 -- 3 rt C3D r--3rtt <3rt3 o to 3Hl/> rt o CL 3 rt 3 i i i i rtot CN) < to c to LQ --* rt rrtt C3 Oc ort 3 '<3 3c r3t 33 rt 3 00-- rt 3" rQt 0) -- o -- n> C 3 C3j prot < 3irt rt "O I V> - rt rt cr -- o 3 3 -O 3 Z to CD -< Qj VI to rt n rt tO rt --rt rt 33 to i* -h OCL O to *< in rt rt rt < 3 rt 3 rt to to t/> >i >1 on tn >J t>ol 2rol> >--I * m X zrtz Z <<3r 3 33 rt rt 13C3 Zr2tZ Z C3J0ft -- 3orCtL crto o LrOt rt r3--tH 7oT ---* O O1Oi 30ft L-G CL 33 rrrttt 3r----t3* 3O--Nrt * rrtt rNt CL -313 roGcnt_ OO oc33O o3 CL 333 o 3n>0 O<rot *trc<n/t> rt 3 3r<t0 v> ro3t OO ~o3Cc3oL f-- 3 rt 3a=. --rti --3* QrNJtft o3 XrQ33tJ o3 o3 CL o3Crtl: 3 rrM-tt> o3 031 3 rt to CO o rt oo c CL to rt tJ -O --O' C--Ts C--Tn' L--O> Cl rt rt O Vi o \J3 vj vi rt tn --' [O -- W Nl o M to tn --* on -- to ho ro to oo OOtn --' LO oo o O O rt VI o CO c --* CL VO LG CO rt -- rt IIIII II 1I II >11111 tO oo >11111 lilt II II II I I I I I I I I t I I I to I I J --' o o w I to -- o III CD -- ro i oo oo o o CD m /O x ro w rt rt [ fI ton ton cvrn* i ro to i --' tn tn tn ooo --I i --i oo tn tn o t3o rt tn j-- tn tn on tn to I -- tn tn tn to o o o -- to I i ro i oo tn tn O Orr rt -- I to M VI rt -- oo rt rt o o tn on tn O O Jr- to ro tn o vi sj - rt i ro ro -- co --' to co o O On tn o tOoO ro VAB.0001100052 OJ CO cn o LT\ un LTV 1 cn I*"* 1 m3 o o on ir\ o o no cn la r^. CM 00 CO U1 <uL> <yc 0 co 0a x CO cn CM o oo o Lf\ on CM m OJ cn tn cn o cn LTV *. CSl o oo o un 11 CM vO cn LT\ tf <C uj (-> LU DC oo LU CTV CO < Oo z </> X LU < CL < CJ III CO -- CJ co an --cn tc3oo o m cn cm cn o cn m -- j M a] | cn ~o D CO .-- LJ nj ccon v0i DC Oo o 4-J L_ 0 X o o 2T *--" </> 0 E0 L. 0 L. 0 r~ U a m 0 c i TM Lu ; i .oX l V) 4-J 0 LO_ o> 0 *^ X ---, 0 0 o L u _Q 0 l_ a. cn 0 0 <n o C3 Z3 oW 0 >s. C a +J 0 0E *-- 0 ,--. * -- u 4-J 0 cn 4c-J *0 0 DO E CL p~ oO 3 cn cr LJ >- 0 Lw OO 4-J 4-J 0 JQ 0 JO 0 O 0 r-- LO LO lo i/> CL CL _o o cnro 0 0 T < .> --1 GJ C CM cn Lf\ 03 CM CM CM CM 11 0-- < < < o </> 1 < LO LU cn ZJ H- -- O 21 LU CL X LU U < O 1-- 4 * VAB.0001100053 Lr I VAR0D011Q0Q54