Document 2q27dDDm08Dp5Dg4RpJyDa50L

FILE --r- - . - 7-/J- (r7 no- 7T- 04- - Z plant OYSTER manufacturer DUTY/UNIT CR.E\ PLAf/r 51*7-Kloo?- P.O. NO. BTU/HR [NO. UNIT5 Q&E |sHELLS/UN)T ftfjL. JOB NO. 8300 Z charge no. TEMA SIZE/TYPE 1 to hori x- (fT^ Ith Ezp. Join. U-Tub' K.ttl. Coil Hoi ipln Box Floating HA-Pull Thn*-Clomp Rlng-Paek.d Th.rmo.yphen ^intubT^ Othors Additionol Pmc. Deto on Sheet No. Inl.t - SHELL SIDE - Owll.t Ini.* - TUBE SIDE - OuH.I Flui d Torol Flow 1b/ht End^-h NOKt - Cok/A ,_____ __________________CjruJ_______________ 3/. '7nr> 2.-74, IQO___________________ Li quid lb/hr O 24,300 Donsi ty Ib/cu ft 1L .3 Vi scesity CS-CP 0.1*5 Co Specific Heot Thermal Condueti vi fy Vopor Btu/lb. F n ,31 Bfu/he-sq ft*F/ft rt.D7$ -- b/hr 3t. 70D 3400 ... g Dow-2063 g Uol tfl Vi scosity Specifi e Heat Oonslty Ib/cu ft CS-CP Btu/lb- F '0,241*_____ _ 0,147 n.mb o.nt.4 n>.30 . 0,34 S TU4 b /bn Thermal Conductivity L otent Hoof Bhi/hiwsq ft-F/ft Btu/lb o.Q! ... 0,012. 1AH____ ______140_________ Non* Condensables Velocity Mox./Min. Norm. (Max. Operating Temp. OporoHnff Praia, (Inlet) i b/hr ft/ sec F psjg psl --? 1,1________________________________ /S' B,i / $5 1 220 104 ! 2 XO \ IQO mo 1/2 n %,7__________ Allow. .*?, /) c.ic. 3,3 Allow 30 Calc. /M,4" Film Cooff. BTU/Hr. Sq. Ft. c?/ 23 Feulrno Resistance. 24 Over-oil Coefficient- Uo 25 In.lull.d A,.o/Unit hr-q ft- F/Btw: n\ oo I____________ 67OOO 5 3u/hr-sq ft. F; Cleon *7fo Service LMTD (Corrected) /3& O q It (Out.ido) Inclodi ig^xcludina. J Areo in tube sheets 1 ^25 SHELL SIDE TUBE SIDE Shell D (Approximate) D Dotion Temoeroture Design Pressure psig SQ 300 No. Tubes (Approximate) J) ^Yf? ^ /A\ ) Tube OD f |In. Tube Cage l/p .BWG Hydro fttotfc Test piig 1on Tube Length Corrosion Allow./Lining in. '/ X* Tube pitch fA)n O k____is___ Number of Pdftftos Ohi b^ F6UP. F______________________ 32 Insulation noli e. KlO L.K5. sTba-m/o?Mak./Typ. Fintub.* WfiiVePlh/e. 33 Cross Boifl as: Type CJT* t L- Segment Cu*Ser p,Z % No. Fins per tube; 1 ^ par In. / {34 .t No. 21 Fin Height In. F|n Thfdt. fn. f35 Provide in. Horizontal Cut on Bottom for Condensate Droln Vessel Supports oddlesjL Lugs Other; Long Baffles: Type # Nurs ber Weir Height n.; Shell After Weir in. Impingement Baffle Ye^No^ j Con den sore Lift Yes 1TEMA Clast CL. I, ethol Yes-fNo^ (Code JZtRemovable Bundle Yes Cathodic Protection Yes <No/ ^C$ME3 Notional Board Other: | Stamp (y*4 No 39 Spot Radiograph: Shell Shell Cover Chonnol Stress Reli eve: Shall Sh.ll Cov.f Channel 40 Weight Comploto Empty/Full of Water / |lb Weight Bwntfle Only ib V41 Sandblast: [paint; ^ ) *7 ^^(Mointain f'Shafl IDv Tube Count R- %Installed Area* 42 SHELL SIDE TUBE SIDE Tub.. C. ST(_, Chan, Nox. Necks C. . 5sTL.i 43 Servi ce Mb Slz. Rfg Foes Typ. Hk Si xe Rtg Face Typ. Stot Tuba Sheet <Z7 - VTl-- Chon. Noz. Fiona*. FI . STL., 44 Inlet c \x 1*71? RF 45 OuH^(v n % 1=1,0 RF 45 Drain F ? \=>n _fiJL 47 Vent A 6' t$0 fF b" 150 FP FIfg. Tube Sheet Channel Flanges Cross Bof./Tube Sup. ^ , ^JLi FItg. Head Lona Boffles Impinge. Baffle FI to. Hd. Fiona# Clamp Ring 0* STL. t 48 OulldfLJI fr 4 nr pr 49 50 P6 H l 5c? JEg 51 T(a/ j 4- i rp Rf^ W.lr/Lift Boit./stuj. A- 13 *3- 0.1 Tl e Rods & Spacers C. ^>TL . Nu>. Shall C. <,TL , Vessel Supports Shell Cover GA5KET5 & PACKING 52 53 S*. Nozzl. SIcotch on Shoot No. 2: Channel C. * STL i Shall Cover Ch. Cover/Bonnet ShJI-Chon. Sid. 54 Shelf Side: 55 Tub* Side;: Porollef Bonks of P oral!{ Bonk * of Shell s in Seri et Shall ft in Seri Shall Noz. N.ck. Ci STL. , Chonnol ^"JkA-toO; Shell Nos. Flanges C*_ . X^e Chain.1 Cov.r >4, XKA. -- L. D 1 Shell Flanges C~. . S I Li Flfg. HA SPEC BY ML_5> CHECKED: ^ 4X THE DOW CHEMICAL COMPANY P.V. NO. EQUIP. NO. E-Z APP*D: T-Z OW Co^DEkJSEk Z'^Al- 17-83002 DATE: 4-2%-^T R-EVISION DATE 7T--*ahVCNOOn TO COMPLETE 17150 3.5B6t t --------GIVEN PURCHASER RivTT applicable information NOT HA \1 J*7Jt6ir^- ^*X/.t-5(/.v77 c **S'"HEET \i lOF o^ ' ' HEAT EXCHANGER SPECIFICATIONS ST0415758 ST0415759 FILE _p _____ J-OH-Z plant OYSTtg. CRFtr\C PtArtT- : manufacturer B/M NO. P.0. NO. JOB NO. CHARGE NO. noz DUTY/UNI T 5?2.QOn BTU/HR NO. UNITS OtJE. [sHELLS/UNIT QtJ t jTEMA SIZE/TYPE Harli. ^rQ Slop.d to ho pi x. Floating Hd.*PuH Thru-Clomp Ring-Packed ^Thermotyptan^} U-Tube Fi ifube Kettle Other Coll Hoi rpin Box Additional Proc, Oato on Sheet No. Fluid Inl.t - SHELL 51DE - Oultot S+ieo_v\_______ Inl.t . TUBE SIDE - Ourt.t __________ EQC^+-.RCi_____________ Total Flaw Li quid Density Vi scosi ty Specific Heet Thermol Conductivity Vopor Mol Wt Density b/br b/hr b/cu ft CS-CP Bfu/lb-' F Htu/he-sq ffcF/ft b 'h r b/cu ft fzin /? 570 ________11__________ 0.30 0.355 a- * S Tilb 1 S7hn 3952 9 7.90. Vi scosi ty CS-CP $pci fie Heat Btu/lb.0 F Thermal Conductivity L ofent Heat NorwCandensobl es Btu/hr-sq ft- F/ft Btu/lb b/hr 92. 5 M.W. . >3s M.W. = -CU Velocity Mox./Min. f*/s*c 1 Norm. IMox. Operating Temp. F 75 U?/ 215 1 lit 20*; \22t 2*S \22t Operating Press. (Inlet) Pressure Drop psig psi ___________________an____________________ Allow. Col c. Allow & 9 Cole. - Film Coeff. Fouling Resistance, BTU/Hr. Sq. Ft. >r- sq ft- F/Btu; /j2 on 235 .00 >3S Over-all Coefficient- "U'o Installed Area/Un* Jtu/hr-sq ft. F; Clean J2&3 Service / xq ft (Outside) Including^xcludingj^ LMTD (Corrected) Areo in tuba sheets 16 rtf SHELL SIDE TUBE SIDE Shell |D (Approximote) /) in. Deiian Temperature Design Pressure F psig 2aO fan 300 20 No. Tubes (Appioximote) *2** Tube OD / In. | Tube Gage /P BWG Hydro static Test Corrosion Allow./Lining psig .. in. 9a </jl" HO /?" Tube Length Tub* Pitch f 0 0 y ! 7/ ft In. Number of Posses '/ 1 Join* /2 + F Insulation Cross Bodies; Type Number Class &i Class 6 ; Segment Cut ; Spocing Approx. Equal - See She et No. Moke/Type Fintubes % No. Fins per tubs; Fin Height In. | Fin Thi dc. per In. :n. Provide in. >fe<i lonfal Cut on Bottom for Condensate Droin Long Baffles: 1 ype / ,^ Number Vessel Supports Saddles '/LugsjOther; Weir Height in.; Shell After Weir in. Impin9rent Balfl<rVi>'3 / Cond.n.or. Li It (VJ). No Removable Bundle Yes Cathodic Protection Yes -fTlcO TEMA Class ol I Cod* Notionel Board Other I Stamp No Spot Radiograph: Shall_____ Shell Cover Charmol (Stress Relieve; Shell Shall Covor Che Floating Hood Weight Complete Empty/ Fall of Water lb Weight BunfleQnly lb I M A TE R IA L SPECIFICATIONS NOZZLES PER SHELL 42 SHELL SIDE TUBE SIDE Tub.. 10-30 Ck-Aa Chon. No*. Necks CL *\T~L. 43 Service Mb Size Rtg Fee# Typ* Mb S* z# Rtg Fee* Typ. Sfat Tube Sheet , ^7"i_ Chan. Nox. Fiona** /" . <77. A44 Inlet .ZiL 2L RF J2_ 15a. gf Fltg. Tub* Sheet Channel Flonges C- . 45 Outl et $ ML /50 ELL L In \l5o ML Cmss Baf./Tube Sup. , 5/7. Fltg. Head 44 Drai n Long Beffl es Flta. Hd. Fiona. 47 Vent Imping*. Baffle C. , 7""lL * Damp Ring 48 W#ir/Li ft . 5 Tl-- Bolts/Studs A~t9*A 7 49 Tie Rod* & Spacers C. ^TL. Nut. A -/9V-P-A/ 50 Sh.H C.S Tl. Vessel Supports . ^T*- 51 Shell Caver GASKETS & PACKING 52 53 See Nozzle Sketch on Sheet No. 54 . Shell Side: Parallel Banks of Shells In Series Channel Ch, Cover/Bonnet Sh.lt Not. N.cb. C.STL Shell Cover ShelLChan. Sid* Channel fa --LSD CONF 55 Tube Side;: Poroll*! Bonks of Shells In Series Shell Nox. Flanges C- , Chonnel Cover 54 Stocked: Wld. High Shell Flanges T L. Fltg. Hd. SPEC. BY Ml 5 THE DOW CHEMICAL COMPANY CHECKED: APP'O: ' T-3 RE.Bou_.tRL DATE: VENDOR TO COMPLETE ALL APPLICAS _ INFORMATION NOT GIVEN BY PURCHASE!*______________________ 17 130 3-et EQUIP. NO. I-- no!c A/- 7-83QOZ HEAT EXCHANGER SPECIFICATIONS ST0415760 plant oyjr^s? C:*r PZ/*uT MANUFACTURER B/M NO. P.0. NO. 9 FILE - / NO. _C JOB NO. 83002. CHARGE NO. 1 L&\s-i<l sid -e^/ c\ h T& Y c< w/ to lTa\M STOU15761 WpTc" 10 " ^I i 45 48 49 SO 51 52 S3 55 SPEC BY MLS L CHECKED; tCT APP'D: /JL,. /~j THE DOW CHEMICAL COMPANY \2-e.&o,Ui2 DATE, ^-12- (el REVISION DATE | 3? | jv! / 7 VENDOR TO COMPLETE ALL APPLICABLE INFORMATION NOT CIVCN BY PURCHASER 28430 3-08 |B| C 2 tioT' EOUIP.' g-- ^ Ah 7 -8300Z SPECIFICATIONS ST0415761 plant P)MSTE Cuft K PLP.M' MANUFACTurer B/M NO. S/ 7- f P.O. NO. FILE ND. T-0 JOB NO. 550c: CHARGE NO. UJ 1 a. Vert. Sloped to hori z, 2 >t- Floating Hd.-Pull Thru-Clomp Ring-Packed ^FTS^ith Exp. Joint Thermosyphon U-Tubo Fintube Kettle Other Coil Holrpin Box 3 Additional Proe. Oeto on Sheet No. 4 Flui d s Totol Flow 6 Liquid 7 Density a Vi scosity 9 t-- 10 2 3 Speclfi c Heat Thermol Conductivity 11 UJ Vapor Ib/hr lb/hr th/cu ft CS-CP Btu/lb-F Btu/h*sq ft- F/ft lb/hr Inl.t - SHELL SIDE - Outlet STEAM isn isn 1 <217 Inlot . TUBE SIDE - Outlet C-Moriu a/Ed UvdroCAfKat. Z/S. 7 24 2 10. 724' Z/ff. 7ZVST.5 . 534- .055______ 12 O 13 u_ Mol Wt Vi seosity Density lb/cu ft CS-CP u UJ Spec!fi c Heot Btu/lb. F ST04I5762 15 2 Thermal Conductivity Btu/hn-sq ft-F/ft 16 5 Latant Heot 17 Norv Condon sobles Velocity Mox./Min. Norm. |Mox. Operating Temp. Operating Press. (Inlet) Btu/lb .lb/hr ft/ PC M.W. = 2S0\ 2Zi SO 12?t 20 1I4 M.W. ZO zqtL. Prti Drop Film Cosff. 23 Fowling Resistonce, Ovr-o|| Coefficient- Up p>i BTU/Hr, Sq. Ft. hr-sq ft- F/Btu: A) lav Cal c. Alia Calc. i4oa Wo ~To-W\ billing i?gnri'iooce. -- o.oo 14- Bfu/hr-sq ft. F; Cleon f Servt'c , 90.0 LMTD (Corrected) 91 F 26 Oesian Temperature Design Pressure F psig SHELL SIDE 3QO YoO TUBE SIDE r\.36Q 4- HO Shell ID (Approximate) (3 In. No. Tubes (Approximate) 2.7L l<Ar// Tuba OD $/4- in. ( Tube Gage *\*2~ Hydrostatic Test psig 90 -- 1Z0 Tube Length 1 2d ft Corrosion Ailow./Limng iru Zllo '/l(p Tub. Pitch rZSDO / " In. 1 Number of Passes Insulation OKI S' Cs U E Joint Ef F __________n________ _________ jSi__________ Make/Type Fintubes Q A/4E ------ 33 Cross Boffles:Type ^ g la. ^ ` Segment Cut 34 Numbe Spacing Approx. Equal Sea Sheer No. 35 Provide i/a in. Hotizontol Caron Bortom lor Condensate Droin Long Baffles: Type ; Numbor N*. Fin* p.r tub.; Fin Height in. I Fin Thf dt. V.**el Support* {Soddl'es^ Lug* Oth.r; W.ir Height in.; Sh.ll Aft.r W.ir In.-. \3 Impingement Bofflo^r^N Cond.nsole Lift Y* Removable Bundle Y. 4No^I Cathodic Prot.cHon Y*i -(NoJ TEMACIo*. Q. Il.iFoI Yc*-{No^ [Cod. pCSMgJ_______ Notionol Board Oth art | Stomp Qy . Q- Nq~ 39 Spot Radiograph; Sh.ll Sh.il Covr Cbann.l 40 Weight Complot. Empty/Full of Water |str.* R.li Shall Sf--II Covor Chonn.l lb | Wolght Bun Jo Only Floating Hoad lb 41 42 SHELL SIDE TUBE SIDE 43 Service Mk Si 1* Rtg Face typ; Mk Si** Rtg Face Typo 44 Inlet c 4' iso P 7 Aj 4" jLSq _EL A/fte t 45 Outi et D zm \5(i 46 Droi n 47 Vent r 4' 15a _Ei_ it r /5 0 a: Alt//' CT /" !5o /./ 48 PGi E LcdO `rl? H T`49 Outlet" ISO. P-F- w/c'. 50 51 Tuba* 70-30 CjUL-bJl Stot Tube Sheet C. ^ / L. Chan. No*. Necks C STiChan. No*. Fiona.* C. . STl_ Fltg. Tube Sheet Cn>** Baf./Tubo Sup. Channel Flanges STL. Fltg. Head <77 Lona Baffles Impinge. Baffle Fite. Hd. Fiona# . S T'T-- Qomp Ring Woir/Lift C. ^TL. Tie Reds & Spocers Bolt*/Stud* A -17T-- 7 Nut. A-l94-2.fr Sh.ll c. STL- V.II.I Support. 577, CASKETS & PACKING 52 Channel C. L. Sliell Cover ^ 53 See Nozzle Sketch on Sheet No. Ch. Cover/Bonnet ST'C Shell-Chon. Side^l -___ - ^ 54 Shell Side: Parallel Banks of Shells In Series Sh.ll No*. N.clc* ^. <;TL ChonnM J'/Yi-fcO or r<jual 55 Tub. Sid.;: Poroll.l Bonlt of Sh.ll* in Soria* Shell No*. Flonges , Channel Cover m-- *9 55 Stocked: Wld. High Shell Flonges Fltg. Hi SPEC. BY CHECKED: fk.iX~ APP-D: /J.L, 6. T-20 Thepcrr REBOILER EQUIP. `40. -20 A^B no!c AI - 32- 93ooz DATE; 4,2%-k7 REVISION DATE A-2J& UT7 eh: vendor to complete all applicable information not given BY PuRCHAtee 17150 3-56 Y RAT' lu J V i HEAT WA+P* EXCHANGER SHEET | of2. SPECIFICATIONS fax' ST0415762 $T041,5^63 ST0415763 STOU15764 PLAN ~OVSiTER <LRtl <''~PL*/vT^t B/M NO. S,Ct - C MANUFACTURER P.O. NO. DUTY/UNIT 3^5 MM BTU/HR |nO. UNITS quc ISHELLS/UNIT Okie FILE NO. JOB NO. CHARGE NO. 0^4 - 2 TYPE 1 fleri Vert. Sloped to horlx. f^TSpwith E*p, Joint U-Tube Kettle Coil Hairpin Box 2 Floating Hd.*Pull Thru-CI amp Ring-Poelced Thermosyphon ^Fintubo^ Other: 3 Additional Proc. Dato on Sheet No. A Fluid s Total Flow 6 Liquid 7 Density 8 Viscosity 9K Specific Heat 10 Z 3 Thermal Conductivity 11 ID Vopor 12 O 13 u. o 14 IU Mol Wt = 9g.c17 Viscosity Specific Heat Density 2 CB Ib/hr Ib/hr Ib/cu ft Qt-CP Btu/lb- F Btu/he*q ft*F/ft Ib/hr Ib/cu It CS-CP 0lu/M*d F Ini St . SHELL SIDE - Outl.t lnl.t . TUBE SIDE - Outl.t CZHLOf? ItJATCD M YOROCAF^OU 2,o. o4e -- Jo.oi9 -- -7<r.S O- 55 -- 0.3 -- ..LQJ83L3 . O.DT4 2?t- ^ 0-03 So, 00*1 7 - 0.2. - C-OOl I J 6Tomeft\>JA-r- R. 108, 3oo. 1 >+0.000 (,2.'3 o. e l. O. 3G.3 - ) M-O, ooo <2, 2.0 O. G 1.0 O. 3<L5 1 r* -- --- 15 z Thermal Conductivity Btu/hr-*q ft-F/ft O-OOSJ -- -- -- ID 16 * v 17 is! 18 19 20 21 22 23 24 25 Latent Heat IE o L. Norv-Condensoblss 0 Ui Velocity Mo*./Min. CL Norm. | Max. Operating Temp. Operating Prats* (inlet) Film Coeff. Foulrna Rasi ttance, Ov.r-oll Co.Wici.nl- "U',,' In.lull.d Ara/Uni t | ? db 6> . Btu/lb Ib/hr *. 1 <h(4,. 2 <5. M.w, = 2.<=i. -- M.W. = --1 \3 ft/see F tte ^ P. * l1 "F >31- 1 ~____ 10 4-. 1 -- 41/ as. I - MO- 1 -- 2 RO. Pi mi 1-l.y A-S._________ _____________C.O. I^SIG.______________ Allow. 0.5 Caic. o. 5 Allow ao . Cole. /I? BTU/Hr. Sq. Ft. 720- 1IOO . hr-sq ft-F/Bh>: 0.001 Btu/hr. sq ft. 0 F; Clean \ Q3 S.rvic. ~J Lf.. C, CD. OOO 5 LMTD (Corr.ct.dl 17.0 F ** f* (Outside) 1 IlM.^-cUrding^ Ar.o in tub. sheets 26 27 28 L 29 u 30 i' 31 a \n 32 33 a. 0 34 35 U1 37 <M 38 39 40 SHELL SIDE TUBE SIDE Oesian Temeerofure F zss. 2.SS. Design Prassur# Hydmstotie Test p*ig 9fJro3l*S--F--G--u---M---s-c-- 80 PSIS ' p*ig zS (20. Corrosion Allow.yihiniwg In. </<' '/its." Ui 1 n __ Mon__________ NowC Cross Bailies: Type VeeTWLAL C.UJT ; Segment Cu( y 2. Tube OD in. | Tube Cage Tuba Length 12. Tube Pitch /7Q0O A J.lnt R%F Hake/Type Fintubee T'YPC No. Fine -- per tube/ >9. BWC ft -LonUTiN per In. N umb. e Provide f*' Spacing eApp &qm*l - See Sheaf No. in. Horizontal Cut on Bottom for Condensate Drain i Fin Height Q. Qg In, | Fin Thick.0,021 ^Mseffupport i "wrar> lu ; Other; Long Baffles: Type lmping.rn.nl Bolfl. TEMA Cl a.. "C" I L eth ol Spot Rodipproph: Sh.1l Number ; Condense!. Lift Y-Nb|r Yti.rfiD |CaJ. (ikSME^ Weir Height in.; Shell After Weir able Bundle Yes-ffjcjT Cothodic Protection Y.s/hh!^ Notionol Bocrd ~ Ot4 | Stomp"" ^fes^No Sh.ll Covor ^-Chonn.1 Istro.s R.liov.: S1i.ll Shall Covor Cho FlooWng H.od Wai ght Comp I at. Etnpfy/Full ol Wot.f lb WdgHl BonJ. Only lb 41 42 43 44 Li a: 45 <t 45 a 47 Id L 49 U 50 'J 51 a 52 V. S3 54 Servi ce Inlet Outlst Drai n Vent TWLCT SHELL SIDE Mb ' * I Rtg Face Typs Mk A : 8" ISott R.F F 0 .6- (S^<* R-F- E O 2" ISO# 13 F 8" R.F. TUBE SIDE Si ze Rtg Foce 4'' ISO* F-F 4` iSOdd F-f Tyoe p.fi. H r ISO* RF 5.. Nazzlo Skmtch on 5b.of No. Shell Si d: Poral 1.1 Bonltz of Tub. Sid.;: Poroll.l Boot's of Shall s In S.ri. Sh.llz in S.H.a Tubs. Caerom Steel Stot Tube Sheet .S Ch on. No z. N eck a ^ ^ . Chi. No*. Fiona#* S' . ^ . Fltg. Tube Sheet -- Cieit Baf./Tube Sup. ^. Lona Baffle* Impinge. Boffla Chonnal Flongaa Fltg. HmJ FI to. HdL Fiona# Clamp Ring ^. ,5 ' /" . S W.lr/LI ft ---- Ti. Rods & Spoe.rs C. S ShH (2a g RtPM StCC u Shell Cover Bolts/Stud* ft-HfVw Nuts *1 Vessel Supports CASKETS A PACKING Channel <D* rt SoU 5-rerc. Ch. Cover/Bonnet CT ^ ' Shall Nox. Neck Shefl No z. Flanges ^ ^ . Shall Cevsr ShW|-Chan. 5ida Channel JM t,0 Channel Cover OT EU4 ) * Stocked: SPEC. BY -7-l4--^C CWB.OY.D CHECKED: APP'D: y/zi/u7 Wid. High Sh.ll Flong.s C-. *3 THE DOW CHEMICAL COMPANY Firs. Hd. P. V. NO. EQUIP. NO. ET-21 2.0 OVEftHCAC> COFJCSCWSCP, A/-31SPEC NO -83032 DATE: T g.| REVISIO N DATE S.-J^L3_ VENDOR TO COMPLETE ALL APPLICABLE INFORMATION NOT GIVEN BY PURCHASER ^ I 71 90 3-ee V I XA'J Y I 5-z^-^L sheet is?rr HEAT 2l:-fa2 EXCHANGER I OF 3 SPECIFICATIONS --t - ST0415764 LO U) l-" LO O >- in r* O 2 > 0* b*i Uf I < cm u 0 ST0415765 ST0415766 99/.SI101S plant oY'r> TER r.RECk MANUF AC : Ut\ L r. "5Stic. {.'SOa S SZRTT-S'iovLs Ss.tS8~ Psao'*/=>/-/) A/r A`O.1 :b 'm no. <-.*>_ fr'loO'i-- |p.O. NO. file , NO. J - ^4- - Z JOB NO. e>30 0'2. CHARGE NO. ^ DUTY/UNIT \&>gr> COO BTU/HR NO. UNI TS Osl = |sHELL5/UN|T c^SJC. TEMA SIZE/TYP c FJeetrwg Mi Pud ThrwGIomp Ping P orknd The eypMm Additional Proc. Dota on Shoot No. Flu! d Inlot . SHELL SIDE - Outlet Ini et TUBE SIDE Outlet ^i-Qg.UrTt> STMAlJg' \> I-- m _o* o >-- CO Totol Flow Li quid Density Vi scosity Spoci He Hoot 10 Thermo! Conducfivfty 11 12 Mol Wt Density Vi scosit Ib/hr Ib/hr Ib/cu ft p*CP Btu/lb- F Btu/h^sq ft- F/ft I b/hr lb/eu ft 1-4- S4 14-SI 2>A hi <s> sJ o. & e&ot. .14SL A. cp&?'Z._ <1 S <=>= -V- 11 74-?- gpo 7?.2- aa2 /.GO _S/_ !, <o "7<2 W O' Aj E .<=>>.StPS <?-^ Me MB Spoci fi c Hoot Btu/lb-F Thermo! Conductivity Bhi/hr-sq ft- F/ft LOtoot Hoot NorvCondensobl e* Velocity Mom./Min. Norm. |Mom. Operating Temp. Bfu/lb Ib/hr ft/s /sr<F= MO ME M-*. Moslg 4-c. 1 *30 1 4-C | c^>6_ n: I/4.S Mo W. Oporotino Press. (Inlet) Pressure Drop Allow. /2<a Cdc. M I L. Allow \ , Q_____Col Co Q* Film Coo If. BTU/Hr. Sq. Ft. rz<& X *V X-* < I- V- <^ NI^X- t N *N> 7^ 1 s> O 'lb r^'< ti J N> I r~ 54 55 Foulrnq Resistance,. hr-sq ft- F/Bhi: Over-oil Coefficient- Up Btu/hr-iq h. F; Clean 73.^ Servj ce LMTD (Corrected) ^ ^ aF Intruded Areo/Unit <^4 *q ft (Oulsido) M SHELL SIDE TUBE SIDE precluding. Area in tube sheets Shell ID f Approximatel /"Z /In. Desion Temoerofure Design P re*sure F psig /&> 3.*>o 'Bc=> No. Tubes (Approximate) Tube OD 3/d_ In. | Tube Gage BWG Hydro statie Test Corrosion Allow./Lining Number of Posses insul-atton Cro ss Boffl e: Type fjgg psig S.V corse. bvcods TubeLenoth in. /,<& Tube Pi tch (*S^Q O / Joint Jp o - i-- /*--Z- A ^ 5i-t40 - J frNTuwwT jv-z/3 Make/Type Fintubes S~UPPOgT S3TMent Co* No# Fins per tube; per In. Numbe Spacing Approx. Equal - See Sheet Noo Fin Height 1 ` ~~in. Fin Thi dr. Provide in. Horizontal Cut on Bottom for Can demote Drain Vessel Support Lugs Other; Long Bailies: Type Impingement Boffl o TEMA Clot. G I Lethal Condeennsote Lift -[No 1 ICoJo S Number L_No fi Rer IaSmEI Weir Height in.; Shell Alter Weir able Bundle $7771 mm j Cathodic Protection ****** "IN' H.iinnl niltwil Oltiow I Stomp Spot Rediogroph: Shell Weight CompI ete Empry/Futl pi c^^ff4fchannol-_ 72^ Stress Relieve; 1225-. Shall SMI Cover Chonnol lb | W.ight Bund. Only 44 lb ^insiotiea Attmi ^ wq SHELL SIDE tube side Service Mk jSi^e Rtg Face Typo Mk su. Rtg Face Typo Tubes -A* 1 7^ -- ^ 1 "T* Slot Tube Sheet C, 5 Chon. No^ Necks ' 'C/S*M Chon. Noi. Flanges ..54 J Ini et Outl et a S Droi n C yotvtl.A, L *t t> 2* *y>0 RF H 2" 3oo X.F # V 3 oo R.F Lv/f/ .2" /Sf> RF z" ISO RF H Cross Bof./Tube Sup. C\ Lona Boffles Kl rt kLF. Impinge. BofRe oMfi" Channel Ranges - Fltg. Hoad ------ F|t(t Hi Fiona# " Clamp Ring ^ +l Lk b <? +' 3a? RF SPitJE F Z3.VO p.x. H, PSV J 3oc KF KF sp/ee K Soo R.P See Nozzle Sketch on Sheet No. x- e4 "2 Shell Side: Parallel Banks of Shell i In Series Woir/LIh MoNE Tio Rod. & Spoe.r. ,,c,s\ : 5hell Cover 1* Channel Ch. Cover/Bonnet , Cj 5^1 Shell Noi. Necks (Z k $ "f) Bolts/Studs Nut. A * 1^4 -Z.H T- Vessel Supports C* S*t" ) CASKETS & PACKING Shell Cover Shell-Chon. Side phannel TubeSide:- Porollel Bonks of Shells fn Series Shell No*. Flanges , S^| Channel Cover T Stack ed: Wide High Shell Flonges , S 1 Fltg. Hi L SPEC BY CHECKED: APP'D: 7'' <2^* THE DOW CHEMICAL COMPANY VcVOOtE om<0*S >SO FJi fVA/ Pump LiO'jiO Chi LL-E12. SPECAl-50-0^2' NO. D^E: .V ... Yrevisiondate rn B r' 1 -5-26-fa/ VgCivMeOnORbvToPUCROCMHPALSEETRE ALL. APPLICABLE INFORMATION NOT 1 F. 57 HEAT EXCHANGER i^ SHEET 1 OF SPECIFICATIONS ST0415767 __ c, S SZ&K - J OOL0/7"L_- S6li8-&3oc3Ssz&rt - 8:o2~ SS2?>\- ?3DC,'~ L.K p/.Af/t//a! 3/m no. id r\ kii~v J- o4- 2 JOB HO. 8 300'S. SPEC. BY VOblTZElS THE DOW CHEMICAL COMPANY CHECKED: APP'D: */- Pump SeaL" Liquid (Twill ER. I EQUIP. MO. B-25 SNOP!ECc.A1-50-S3o^2 DATE: //*/ . , REVISIO N DATE A ft& * *> _VgEivNeDnORbtTOpuCrOcMhPaLsEeTrE ALL APPLICABLE INFORMATION NOT B ^It ^7^7 HEAT EXCHANGER sheet ^r\ ^of_ w3. SPECIFICATIONS ST0415768 plant OYsfre.e MANUFACTURER CBEEb PLAiorN3,T b/m no.S-ZK-fr-ioO-i ^ P.O. NO. FILE HD. J-0-4-2- JOB NO. eisooa~ CHARGE NO. S T 0 415769 13 14 15 16 17 (4)^uAl\y < d 18 IV Scd 'S'O p\pe.u,'dV- 20 21 Lie-IA Cauf>s . op-w 22 w 4-o \je,ss>e4 23 24 25 26 27 28 29 30 31 32 35 36 37 42 43 ^W^s> Ae pr^ec4- -CroA ^^be.\ \ViS\claVvcso ly hi" 4-0 \"% 46 47 48 49 50 Al'&">/?? IVJV %r;7 & /ffff/l OiYS r- 3 9 - <?loo z. /a\ SPEC ST THE DOW CHEMICAL COMPANY CHECKED: APP*D: /J, d? E-Zl ^rost PLUGn date=5-.|^.U7 PIT REVISION DATE S- fS-^7 B VENOOM TO COMPLETE ALL APPLICABLE IN FORMATION NOT GIVEN By PURCHASER DeTAiL C *Tj -*> SHEET ^ OF ^ EQUIP.' ~S E-a SPEC. Al- so-03^4 NO. Mb AT EXCHANGER SPECIFICATIONS ST0415769 plant QjST--_ manufacturer sT0UI 5710 s5Zo[3-8yOO? S&o/i'83oQZr v;e&kf .plAkJt B/M NO. 1 0-- P.O. NO. FILE NO. J-oy- z JOB NO. ggOQ2_ CHARGE NO. g 3007. 1 Ui (fori Vert. Sloped 0 t hori x. 2 >*--- Floating Hd.-Pull Thro-Clomp Ring-Packed ^FTS^kith Exp. Joint Thermosyphon IJ-Tube Fintube Kettle Other Coil Hairpin Box 3 Additional Proc, Doto on Sheet No. 4 Ftui d Inl.t - SHELL SIDE - Outlet Process Pious Inl.t . TUBE SIDE - OutWt MtXET> ^ CL'S s Total Flow 6 Liquid 7 Don lily 1 S/hr It/hr Ib/cu ft sZ 4oo /JO 700 Yn b^O 52.0 B Vi.co.lty CS<CP) OZG>h> PERFORMANCE O F ONE UNIT 9 Specific Heat 10 Thermal Conductivity n Vapor 12 Mol Wt (foeniity} Btu/1^F Btu/hesq ft-F/ft Ib/hr fTb/eu ft,) 52YO0 0.93 szyoo // 0,Boo 0.93 __ 0-3.21____ 0(n / Lgt/ ft?___ 0.98 13 Vi xco.ity u Specific Heat 15 Thermal Conductivity CSJ.P) Btu/lb-0 F Btu/hr-sq ft- F/ft o. on O.Z97 O .Or7^ O.o 19 0-/9 9 0.00*1 .O! 781 . OOP ! .0/2*1 .109 .Oo f ) 16 Latent Heat 17 Non-Condensebl et Bty/lb Ib/hr M.w. = Jr 3 M.W. = ie Velocity Max./Min. 19 Norm. |Mox. 0pmratin^ Temp. ft/sec F '38 1-______ 82.Y | 90 S'fc.S- 1 IZO 87L.SA >ZO 2D Operating Press. (Inlet) p*ig 96 /o& 21 Pressure Drop 22 Film Coaff. p* BTU/Hr. Sq. Ft. Allow. ,2^ Calc. /fCi Y6. / Allow Cole. /oz 23 Foulrna Resistance. hr-sq ft-F/Btu; 34 Ovot-all Coefficient- "U'o 8 tu/h r- sq ft. F; Cleon 3/, ~l S.fyie. 29.7 LMTD (Corrected) 25 Inxtulled Areo'Unil ?rt // */0 xq ft (Out.id.) Includin-fe^*., Af.o in tub. .haat. SHELL SIDE TUBE SIDE Shell I D (Appro ximate) 32* In. 27 Desian Temperature 2R Desi gn Pressure F - &0/2.S0 psip ?otO ->C/?lso 2-t O No. Tubes (Approximate) TubeOD / In. | Tube Gage / ^ BWG 29 Hydro stati c Test X Corrosion AIIow./Lamb? psip I'/Z- X MflWF Ntz _ Tube Length in. '/s /* Tube Pi tch fA^O O ft l In. 31 Number of Posses 32 Insulotien 33 Cross Baffles; Type K\~LOt* TAi* t/ X uoue ; Segment Cut 5C.O' Joint R. f f~ Moke/Type Fintube* * ^ No. Fins -1 per tube; -- per in. ER SHELL 35 P ro vd in. Horixontol Cut on Bottom for Condensate Drain Long Baffles: Typo 7 Numb* /Supports (soddU^ L ugs Other; Wei r Hei gKt Shell After We Impingement Baffle Y g(N^ j Condensple Lift YeT-(fi)| Remo*oble Bundle Yes Cathodic Protection Y*s 38 39 A-- TEMA Class ZH L ethol es -(Ho) Code fASMjp Notional Boord Other; Spot Radiograph;^ Shell Shell Cover^ Chonnel __ |stree's Relieves 5heIIShell Cover ______ |5tqmp Chonnel (VeT)^o Flooring Heod Wei ght Complete Empty/Full of Water frfitfi Sandblast: Vt 5 1 Paint: 5 7~ 'ttyO / J$6(*0 f/3$0Q lb 1**1 ghl Bundle Only (Hn.tollod Ar.tti lb %- & A. SHELL SIDE TUBE SIDE Servi ee Mlt Si >e Rtp Foee Typ. Mk Si i. Rtg Face Typ |nl et A y&* P? (0 D rftn )SO PF 6) c 'OutlH P St*! Droi n Z.'n- zocr Y V.nt 1- iYiVi f JE_ 2l\r\ jsa Hl iQP* PF \f .(3- 7,io 4SL II ~FT\ft :N<? 51^ Of Tl OK t --F svy ?e.Tj 1 See Noixle Sketch on Sheet No. /O gf BT COt>E .. .nzr~ NOZl HP/T/i&L/PQ Tub../}- St4-T %TCStot Tub. Sh..t ST88X- Fltg. Tube Sheet Cross Baf./Tube Sup. 3*TET- Chon. Nol Necks ^ TTZltl Chon. Nex. Flanoes S'TWL* Channel Flanges ^TZZfL. F| tg. Head Long Baffles Impinge. Baffle W.ir/Li ft Ti. Rod. & Spoe.r. _5"TFKL- Sh.ll A-'Z-OZ-S 5hefl Cover FI to. Hd. Flanoe Clomp Ring Bolts/Studs ^ L* *7-- Nut. Si-/*/#- ' ^ Vessel Supports 3 GASKETS & PACKING Chonnel Tt L- Ch. Cover/Bonnet SFCl* Shell Nos. Necks S^LLL* Shell Cover Shell-Chon. Side Channel Shall Not Flong.. Channel Cover Fltg. Hd. SPEC. BY LT THE DOW CHEMICAL COMPANY P.V. NO. EQUIP. NO. CHECKED: /' ' f APP '*-}( z/i / T' ZZO Covoe/oseg DATE: 7~l hGl REVISION DATE > u v/ TT^TT VENDOR TO COMPLETE ALL APPLICABLE INFORMATION NOT |ci ven by purchases 17130 3 *6 t crc //><* -d 7/ u-f* /'Juki SPEC NO. A\- IZX>- S5002- r tet/T-7-F7 HEAT 7 EXCHANGER OF 5 SPECIFICATIONS T ST0415770 S T O U ^ " 11I ST0415771 ST04 I 5772 r^PLANT OYSTf/Z *. Pi AMT MO. / ANUFACTURER SszQ -&Z0O7- B/M NO. f20- 3002 P.O. NO. FILE NO. J-G4-? JOB NO. JS3QOZ CHARGE NO. 3002. 9 JO JJ J2 13 JJ J5 J6 J7 J8 19 20 11 22 23 24 25 26 27 28 29 30 31 32 J3 34 35 36 37 38 39 40 41 _42 43 44 45 46 47 48 49 50 5J 52 53 54 55 /k 56 >PEC. BY /\/J :' 7 ft (d e 4-' J 7d - s THE DOW CHEMICAL COMPANY CHECKED, APP'D: /J4t( "/ultf T-ZZO COfiJDMSE. DATE: ft-l REVISION DATE ABC BVVENDOR TO COMPLETE ALL APPLICABLE INFORMATION NOT GIVEN PURCHASER J 2>^ -- *5 1MEET OF a: EQUIP. NO. -234 1^41-120-33002 SPECIFICATIONS ST0415772 _________ __________^si(-4-HZc;X plant c>YST CY-JYX PLANT .AJ- ' b/mno. SJ. c, -1? S o: manufacturer P.O. NO. DUTY/UNIT ~2 700 Q OO C H<4f> \vort.f fl.p.d Ha--im Hi. mn Tin. a***,, ni.t p.u.d ypTs-w i *_h_ Tk>FIWMll)twi Rnlwbr FILE NO. J-04-2 JOB NO. 5002. CHARGE no. 3 0 0 7- 0 than i $70415773 X Additional Proc. Data on Shoot No. Inl.t . SHELL SIDE OuH.t Inl.t . TUBE SIDE - OuH.t Flui d Steam Totol Flow Liquid Density Vi seoslty Sped fi c Heat 10 Thermal Conductivity Vapor -M*>i We-- Density 13 Vi seosity 14 Speci f*c Heat IS Thermal Conductivity lb/hr lb/hr 1 b/cu ft 0-cp Btu/lb.F Btu/hs-sq ft-aF/ft lb/hr Ib/cu ft *-CP Btu/I b- F Btu/hrwsq ft-F/ft S2 70 -- -- -- -- -- 3270 S3 e> . 1 4- 1 o- *3- 2740 *=>. S37 o.orSi -- -- o- zs -- 0!7 -- / *>*5 0 2 74a 47.Z 04./ 63.2 7 0.34- Zj3 4.24 0.3G> <3 056 47-044 -- /565C -- /. 35 -- O. 3/3 -- 0.24 -- O' GO0& 16 Lotent Heot NorvCondensobl es Btu/lb 1 b/hr -Z<2> -- -- M.W. = -- /CO '-- M.W. = ----- Velocity Mox./Min. 19 Norm. ]mox. Operotino Temp. ft/soc F 25 A.00 I 4/0 4-00 1 4/0 2/70 1 ZAS 344|34&" 20 Operoting Press. (Inlet) Pressure Drop psig psi 2?S Allow. Kill-- Cal e. fs) 11_ /25 Allow /.O Calc. & ' ^ 22 Film Coeff. 23 Fowling Resi Stone#, 24 Over-oil Coefficient- "Uo BTLI/Hr. Sq. Ft. ir-tq ft- F/Btu: 3tu/hrsq ft. F; Cleon / 200 0 .O /^G Service /C8 O. oo 3 LWTD (Corrected) 53 F 25 Inetulled Areo/Unit eo in tube sheets 26 77 Design Temperoture SHELL SIDE F <450 TUBE SIDE 4-00 Shell 1D f Approximate) No. Tubes (Approximate) /3/ in. 2S Design Pressure psig 309 JLSO Tube OD \ in. | Tube Gogs | *2. BWG. 29 Hy dm stoti c Test piig ** * Tube Length 1 ^7 h^ 30 Corrosion Allow./Lining 1 n. 31 Number ol Passes 32 Insulation 33 Cross Baffles; Type "TlJRE. SU /l Co 0 ki e f= ^*9ment Cut /a OKE a <T% Tube Pitch (\ {^^r |l jomtroP-f>ce4Bcr*pL4frrtor6vT- Make/Type Fintubes No. Fins -- per tube; "* In. F" per In. 34 N umber rr-m ; Spocing Approx. Equal - See Sheer No. Fin Height -- in. I Fin Thick. 35 --- Provide -- n. Horizontal Cut on Bottom (or Condensate Orain Vessel Support* ^Lug^f 36 Long Bellies: Type KOM ; Number "" Weir Height in.; Shell Alter Weir 37 Impingement BofflejYej^Hg * Condensate Lift Ffeil- 44% R emo v able Bundle ~-T^n Cathodic Protection 38 TEMA Closi C* I Lethal fNoT j Code rCTjFl Meliunut^ff^rd Other: | Stomp j Ye>[-Mt> 39 Spot Rocfcogroph: j^Shel l^f-^ Shell Cover Channel | Stress Relieve t/' ^helh^^ Sfll Cover ChannelITf FI I H.od 40 41 Sondbl osh fr/oPfe- f676 r/?o> I Point: lb { Weight Bundle Only W*1 woTt T. w Ik In trolled Area* % O ^ SHELL SIDE TUBE SIDE Service Mk Six. Rtg Face Typo MIc Six. Rtg Foce Typo Tubes *70' 50 cl) Ml Chon. Nox. Nock. STL Stot Tube Sheet e STL- Chen. Nos. Flanaee ^ S'TL* |nl et OuHt Droi n Vent TfZ Ju 3oo RF y B "2. Joe RF y s *5^ // 6 4 4, C net e-w/fi A/ 2 RF- X- * RF RF 44 FI tg. Tube Sheet -- Crete Bof./Tube Sop. S TL_ Lena Baffles -- Impinge. Boffle S TL. W#|r/Li ft ______ STL Channel Flanges FI tg. Head Fltn. HdL Fiona* Damp Ring Bollo/Studo^ P, -- -- -T*x"7 ooTU! a: 2 RF * Tie Rode A Spacer* TL Nut. A 1^4-214 - SPARS LEVEL i* 5 M2 SP r P?F it SH .11 Shell Cover T(_ STL Vessel Supports STI__ CASKETS & PACKING TAf> ! D Y-Z feofla NPf, CPL& Channel STL- Shell Cover J M' S.. Npul. Sketch on Shp.t No. 2 X ^ SS a J~S &AJ Ch. Cover/Bonnet TL. Shell-Chan. Sid* \ 54 *-*.- * I CL ________________________ ^ 55 13fZ M A WX ; -//** <yT~CE U SheJJ Nos. Necki - TU Channel Shell Nor. Flong*.. F. STL Channel Cover ^7 9 Shell Flanges 1 ------- n- Fltg. Hi __ SPEC. BY VOMTfc&S's. <&> THE DOW CHEMICAL COMPANY EQUIP. ' E-Z4-2 CHECKED: / ^ / APP'D: Falling Film Exchanger SNOP,ECA\-l25-83ooz DATE: f-Z'CF) *" * tel&g. VENDOR TO COMPLETE ALU APPLICABLE INFORMATION NOT SIVEN BY PURCHASER ^ HEAT c,wm EXCHANGER 1i |*HEET / * OF ^ SPECIFICATIONS ST0415773 ST04I577I* ST0415774 plant oysTee. MANUFACTURER PlAVTVc-\ B/MNO. 5'cL, rf i S fU P.0. NO. FILE NO. J-o4- JOB NO. -& 3 CO CHARGE NO. S'iOO 2. ome OF three vv/eepwoi_ts To F/T \FLAk/6E<, ----------- - * -------- ST0415175 3 " SCHFPVO //" vee NofcAi ALL AROUND-? CO -A / A ^ *\ V ^ A A -T* , .V . . V jf V v- |_A-------------- L--- (seeD^r*'1-* ---------- +H ^)aJ c 32 Removable separato/z --^J L~-- ^)G> <=.LOTS OA/F OF THREE LEES JZEST/A/O ON TU&E SHEET tof hfal> W/TH REMOVABLE UQU)D 0/5 TR/&UTO/R 44 NOTE: M/LL TOE* OF TUBES SO THEY ARE ALL THE SAME HE/dHTABOVE TUBE SHEET BOTTOM OF Slots must Be same ff/sj/t above sheet. Clots MUST BE SHARP, AMD Pi Of BURRS. TOP TU B> E Shi BET 56 C SPEC BY \A>n n?ESS CHECKED: (J, f . APP*D: /Jt& THE DOW CHEMICAL COMPANY Fallisjo Film ExchAt^CEQ. DATE: REVISION DATE A ^rJ-^J- V^^1 B C VCNOOA TO COMPLETE ALU APPLICABLE INFORMATION NOT GIVEN BY PURCHASER jj SHEET __ OF J EQUIP, r'' E-242 m^k\-12^-8300% HEAT EX<fHAMdE SPECIFICATIONS ST0415775 PLANT O Yf TTT/' MANUFacturer JTY/UNIL ST04I5176 ' .____fSL/fi"9>SG(7^Jt.l Eh PLhtJT V0'( |B/MN0- sit-6 i":L P.O. NO. BTU/HR [no. UNITS ~7~ |SHELLS/UNIT MFILE NO. J-0/-2 JOB NO. 007-' CHARGE NO. Sj jQQ'L TEMA SIZE/TYPE</Q-24o//)<J Al . Vrt. Slop.d to horl x, Fleeting Hd.-Pu!l Thru-CJomp Ring-Peeked Thermo syp hon , U-Tub. Fintvbe Kettle Other Coil Hoi rpin Box Addi Hanoi Prpc. Dots on Shoot No. Flu? d Totol Flow !b/hr Ini ot SHELL SIDE - OuHot y~-2. <YJ Gvtayhe.&'J Inlot TUBE SIDE - OuHot L j qui d Ib/hr Density I b/cu ft Viscosity CS-CP Specific Hoot 10 Thermo) Conductivity U Vopor Btu/lb^F Btu/h>*q ftF/ft Ib/hr 12 Mol Wt Density I b/cu ft 13 Vi scosj ty U Spec) fi e Hoot CS-CP Btw/lb- F 15 Thermol Conductivity 16 Latent Heot 17 O NorvCondensobies IB Of Voloc) ty Max./Min, >nn. | Mon, Operating Temp, Operating Press. (Inlet) Pressure Drop Btu/hr-sq ft. F/ft Btu/lb Ib/hr ft/s //JT._ psi Allow. M.W. = Co) c. SSI Allow M.W. = /al Clc- -<? Film Coeff. BTU/Hr. S Ft. oulfno Resrstonee, hr-*q ft- F/Btu: Ovor-oll Coefficient- U'0 Btu/hr-sq ft. F; Cleon Service LMTO (Corroded) j522_ OF Initulied Area/Unit eq ft (Outside) Includino^Excluding^ Aroo in tube sheets SHELL SIDE TUBE SIDE Shall ID (Approximate) </n In. Desion Temoeroture Design Pressure Hydfostetic Test F psig pig 7.50 zztr 33 B 25'<D //dopn No. Tubes (Approximate] Tube OD / Tube Length ,, 78R In. | Tube Goge / BWG fi Corrosion Allow./Lining in. Tube Pitch (W)f~] O jyy_________ in. Number of Posses 5PUTFLOW 4 Joint A>*F 32 Insulation ___ A/ca.C-______ //one. Moko/Typo Fintubes 33 Cross Baffles? Type j QuIl' ' ^p9ment ^-ut ' No. Fins per tube* 34 Number ; Spocing Appro k. Eqmri - S~ee Sheet No. ^ 2* Fin Height .In... .j,F...i..n....T...b...i.ds7" P rovide in. Horizontal Cut on Bottom for Condensate Drain Vessel Supports ^oddTeD^Luos Other: per in. Long Baffles: Typo ; Number Weir Height in.; Shell After Weir 37 Impingement BoffleCy_e^No~ Condensate Lift Yes ble~Bandie Yes -(nq)| Cothodic Protection Yes TEMA Close Q, ILethol Yes /fj5 I Code National Board Spot Radiograph: Shell 0Shell Coy#x^---Cfi I*fiaL____JStress_Rclijpye; Shell Other ~~~ I Stomp Sfwlt Cover______Chonnel ^Y esy No Floating Hood TVsight Complete Empty/Full of Wate /&ex: 3_o, zos/!te<z,7?/4-/,i?<? lb | Wolgh, Bvndl. Only lb Son dbl ost: *~1 PalwF. 7)7-2.4^ 7~j>/^~^VkR,ln SHELL SIDE TUBE SIDE Service Mb SI i. Rtg Face Typ. Mk 5f ze Rtg Face Typ. c 1444 Ini et RF A R/Q fsa f x- fa in. RF45 Outl et fQ (Fo ZF x; Ft 120 F ,RF45 Drain z. tsn RF47 Vent t lf)Q * 648 TW 7. (So RF if Pi49 H 1 (SD fir LWfJ Tub.. Stat Tube Sheet Of A/t ^TY. Fltg. Tube Sheet Cross Baf,/Tube SupC/^TT'l- Leno Baffles Impinge. Baffle 0^7V. Weir/Li ft Tie Rods & SpoeersfV ^ T"/ Sh.il Shell Caver C'STL 52 CKonn.!_____________ Cl ST/. 53 S. Neil Sh.teb on Shot Ne. Z. O tZ, Ch. Cover/Bonnet TV CTL 54 Sb.ll Sid.: P oral l.l Bank, ol Sh.||. In Seri.. Sh.ll Noi. N.ck. C`C7V Tub# Si do:' Porollel Bonk of Shells in Series Shell Noz. Flonge*C^>~"/ . Stocked; amtSPEC. BY Wide Hi gh THE DOW CHEMICAL COMPANY Chan. No s. N.cb. C`S t L Chan. Noz. F(onaes/>PS"TLChannel Flonoes C ^7". Fltg. Head Flta. Hd. Flonoe Oamp Ring B.it./stud%/)-T'?A - R7 No,. /9-jQ</-2.h ^ Vessel Supports GASKETS & PACKING Shell Cover ShJI-Cbon. Sid. Chonnel JAV Uf) ] Chonnel Cover 9FI, . HA p CHECKED: APP'D: /y 9/j/^ CA//s//SR DATE: ^ ^ REVISION DATE \psd?A VENDOR TO COMPLETE ALL APPLICABLE INFORRMmaATtIiOONn NncOT GIVEN BY PURCHASER 171 50 3.0 6 . \cn/"*c7, B \k/ic,./nL / OF y /_________ ^ !>-/Z7-8300% HEAT EXCHANGER SPECIFICATIONS ST0415776 ST0.4 I 5777 ST0415777 ST04 I 5718 _____________________________________ ____________ c?tzor, Iplamt QiSTRCRbn PjIaUT~ /)j , ) I B/M~lNO. MANUFACTURER P.O. NO. t duty/unit 2,7,/7/0<0.0 00 btu/hr NO. UNITS / l-SHELLS/UNIT / FILE . NO- J ' V-i; JOB NO. CHARGE NO. &3ooZ, T EM A SI Z E/TY P EV? - / 92//*^ 9 j. tHori r"^ Vert, Sloped to horix. ^Floating HdJPull Thru^C-lomp Rng)Paehed Additional Proc. Date on Sheet No. Flui d FTSwith Exp. Joint U-Tub. K.nU Thermo syphon FI ntub* Other: Inlet SHELL SIDE - OuH.t Coil Hairpin Bee Inlet TUBE SIDE . Outl.f Total Flow Ib/hr Liqvl d lb/hr Density Vi seosl ty Sped He Heot Thormol Conductivity 1 b/cu ft CS-CP Btu/lb. F Btu/hesg ft-F/ft Vopor lb/hr Mol Wt Density Ib/cu ft Vi scosi *y Speci fi c Heot Thermol Conduct! vi ty CS-CP Btu/I b- F Btu/hr-sq ft- F/ft _________________cn L atent Heot Norw Condensables Velocity Mox./Min. Norm. |Moh. Operating Temp. Operoting Prett. (Inlet) Pressure Drop Fjfm Coeff. Btu/| b lb/hr ft/ sec F psig p si BTU/Hr. Sq. Ft. )St 1 Allow. M.W. = jsT] /J Cole. ,3H2 _____________ . 2 56,1 2t<e 1 - : Allow Cole. 7. P,*4 j Fowling Rfi stance, Over-oli Coefficient- Ub hn*sq ft- F/Btu: Btu/hr-sq fl,F; Cleon Service Zf LMTD (Co rrectod) IndolUd Areo/Untt Design Temporoture Design Pressure Hydiostatic Test Corrosion Allow./Lining Number of Passes F psig psig in. SHELL SIDE 2X0 22i" T TUBE SIDE 300 7.>p * 4? y/h 2, - Shell 10 f Approximate) No. Tubes (Approximate) 831 Tube OD f/ in. Tube Gage Tube Length Tub. Pitch /Ji/ Joint Insulation C~ P %33 Cross Baffles: Type ~7"Vj/ Segment Cut Moke/Type Flntvbes ^ % No. Fins per tube; Number ; Spocing Approx. Equal - See Sheet No. Fin Height |n. | Fin Thidt. Provide in. Horizontal Cut on Bottom for Condensate Droin Vessel Suoports (badges)- Lugs Other; In. BWG ft In. per in. In. Long Boffl.i: Typ. SPLIT FLOlO/________ >N umber /_______________W__e_i_r_H__e_ig__h_t_______________S__h_e_l_l__A__ft_e__r_Weir Impingement B offl e Y os^lp) j Con<jen"iote Lift Yei Removable Bundle CYej)- No j Cothodlc Protection Yes In. TEMA CClolasessCj )1 L eeththol olYeYess--ff'fNioo)/ ||CCooddee (@ASlsMMEEy^________Naotionaol Board ^ OOther ther:||SSttoommp Radiograph: .Shell Shell Cover Channel ^Stre s Relieve:Shell ^ Shell Caver ____ Channol_jifc f(YYees*>NNoo Floating Hood*fr >Wergihtt Complete EEmmpptyty//FFoull oef Water ~ 4/f,t 700 / &4, Z&&0 lb) Weight Bundle Only ^Z^37j 7b Sen dbl ost: | Point; 3 5* P ^Maintain Shdl ID Tube Count ""^netaHej^Xr^ *- o SHELL SIDE TUBE SIDE Tube* nQ-30 cu Ml Chon. Nox. Necks C.% 43 Service Mk SI i. Rtg Face Typ. Mk Si xe Rtg Face Typ. Stot Tube Sheet Q. .^77 Chon. Noll f'ZLZ^T Inlet /? 2/> IS0 cJL| 12. 30d REa t Fjtg, Tube Sheet C. &T- Chonn.l Flonq.K c, ^ T*/ Outl at P 2iy /so RF t JL tz GO'./?? f- Croit Bof./Tube Sup, Q , &f~. Fit,. H..4 C. S7~L Droin R z. ISO KF r Long Bo m.. C. STL PI**. Hd. Fiona. r..T77. Vent psv F \k ?>0Q rsp- t (=f z /so r<p f 30 51 Impinge. Baffle Weir/Lift Tie Rod* & SpocersC, ^ TVn Shell Shell Cover \ZL_ STE g.mp Blna r. C,TL. Bolt/5tud Nut R-m^ZJL V.ot.l Support. C.f^TZ. GASKET5 & PACKING CSTL52 Che Sholl Cov.r v l/V) Ch. Cover/Bonnet C.^3T~d. Shell.Chart. Si de 4 B Y ccbi ___________ _________ Shell Noi, Nocks Q., STL Chonnet 5S 5 (/2 MS.V. Am/ -.yVgWdMs or Shell Nox. Flongee^ Channel Cover Fltg. Hd. SPEC.0Y C-rtOL CHECKED: Vtf` / j.- # ^h/tn THE DOW CHEMICAL COMPANY / o T-25D //set /Fez over/ A"e*p/l# P.V. NO. EC_IP. NO. `2<r/ SPEC. NO, fZB-83002. DATE: REVISION DATE VENDOR TO COMPLETE ALL APPLICABLE INFORMATION NOT GIVEN BV purchaser B %S*?'fjt ^ C HEAT EXCHANGER SHEET . / OF ~~ SPECIFICATIONS ST0415778 /JC rt ST0415779 PLANT OYSTER CRkFKj MANUFACTURER o.ono ST04I5780 -85CQ2-_ PlAAJT to.IB.MNO. ~J2 !P.O. NO. BTU/HR |nO. UNITS / |SHELLS/UNIT / FILE NO. )-64'-Z' job no. #3002. CHARGE NO. 8 3 00*2- TEMA SIZE/TYPt 0 to horii. Floating Hd.-Pull Thru-Qomp Ring-Pocked ^Th- tttio.yp hon 1 U-Tube Flntub* K tile OtK.r. Coll Holrpln Bom Additional Proc. Dota on Sheet No. Flui d Inl.l . SHELL SIDE - OuH.t Inl.* - TUBE SIOE Ourt.t _____-T-7S-Q erms______ Totol Flow Liquid lb/hr Ib/hr ?. a. Density lb/cu ft Viscosity CS-CP Specific Heat 10 Thermal Conductivity 1) Vapor 12 Mol Wt Density Bu/lb. F Btu/hwsq ft-F/ft 1 b/hr Ib/cu ft _- . _ 13 Vi scosr ty 14 Speci fi c Hoot CS-CP e*u/lb- F 15 Thermol Conductivity Btu/hr-sq ft-F/ft 16 L atent Heat Btu/lb 17 NorwCondensobl es 1 b/hr M.W. = M.W. = IS Velocity Mo*./Min. Norm. |Mok. Operating Temp. Operating Press. (Inlet) ft/ sec F psig pt 2<C !____ Allow. 2S~D 1 Cal c. ________ ~7s7\ __________ /fz:______________ Allow Cole. . C, F ilm Coeff. BTU/Hr. Sq. Fr. 23 Fouling Resistance, 24 Over-oil Coefficient- Uo 25 fn.tull.d Ar.o/Um* 26 hr-sq ft* F/Btu; 8tu/hrsq fl. F; Clean Service /?/ LMTD (Corrected) ___ yy____ 2j 7 lO .q H (Out.id.) Includinq4&*qludinfl) Am in tub. SHELL 510E TUBE SIDE Sh.ll ID f Appipalmat.l ~W- P..ian T.iwp.fatuf Design Prssswrs Hydrostatic Test Corrosion AHow./Limng .SQQ M:Piff P 9 -J&L. No. Tubes {Approximate) Tub* 00 / In. | Tub. Gog. /Z, Tub* Longth Tub* Pieh^S)0 Q 7ZL BWC' nb*r of Pon*t 32 insulation & JL 33 Cro ss Baffles: Typ* pht Support Only Segment Cut 34 Number ; Spacing Approx., Ee'qqiual * See Sheet No. Joint TZ.. Moke/Typ* Flntvbes No. Fins per tube; Fin Height In. Fin Thidt. p*r in. 35 P ro vi de in. Horizontal Cut on Bottom for Condensate Drain Vessel Supports Saddles ^Lupl^Qther; 36 Long Boffles; Type' _________ j Number____________________ __W__e_i_r _H__e_ig_ ht in,; Shell After We 37 Impingement B*ffl*(Y cs)No ; Condensate Li ft No | Removable Bundle Tes -^31 Cathodic Protection Yes T- E--M -*A- - C---la--s. s. f. .| Lve|t1hr Wa|l IY.eJs---n(Nfuo!) ,||Cod-e u{^ASu ME^, N. ational B^oard O- ther- ____ ____aI S,tom__p___________ __________ Spot Radiograph: Shell Shell Cover Ch.nn.1 jjj IStre RH.y 5b.ll Otv.f Oiaml Flootlnp H.ad Waigbt Cpiwpl*^"Lmply/Fun~pl ZA 70>^/3t.SA//S/,tZ.4o lb | Weight Bundle Only ib Sondblo.f: ) Pointier7-2V7-5P\f*ain'***' Shell ID_______ Tube Count tailed AreoS. ' 42 SHELL SIDE TUBE SIDE 43 Service Mk Site Rtg Face Typ. Mk Si i. Rtg Foce Typ. mTub.. -70-^.Q CJA Ml Chen. Nos. Necks ?! Stat Tub. Sh.x C- AT*l Chan. N. FlanoatT StZT 44 45 Inlet Ovtltt r. f) 10 4- fSQ /?(> RF RF X* >f X*jl 1C Zo ISC s 2A- 4531? KF ft- < KX XK* Fltg. Tube Sheet Cross Bof./Tub* Sup. Chonpel Flonges Fltg. Heed 46 Droi n 47 Vent 2. JQ_ ^. Long Boffles Impinge, Baffle C. &"TL- Fltg, HdL Flonoe Clomp Ring 48 Welr/Llh C- STL Bolte/Studs^^/j^?--&7 Tie Rods & Spocers Shell C.STL Veesel Supports 377, Shell Cover GASKETS & PACKING See Noiil* Sketch on Sheet No. ,.f Channel C.STL Ch, Cover/Bonnet C, STL. Shell Noi. Necks C* GTL Shell Cover Shell-Chan. Side Channel &<0i~ AWP-.A/ev> d--CU> Shell Nos. Flongw k>Tl. Channel Cover Fltg. Hi SPEC. BY QfflL 2S>> THE DOW CHEMICAL COMPANY CHECKED: //; ^//r.. APP'D:^ 7l/& l DATE: / -ZSC REVISIO N DATE A ^wJaV `r-zi-i,: B VENOOR TO COMPLETE ALL APPLICABLE INFORMATION NOT given by purchaser m^"-,**,-&^77, C II.^ _ - * IlSHEET .| of EQUIP. NO. -ZS~Z ~EI'/?/- af -83002. HEAT EXCHANGER SPECIFICATIONS ST0415780 A S T O li 1 5 7 8 /' ST0415781 Iplant OYSTBR CREZK. IMANUF ACTURER duty/unit S&OOOQ S T 0 415782 h Lh! flJQ'l NO. -7~^7 c/- X3Q.O ~z P.O. NO. BTU/HR NO. UNITS |shELLS/UNIT Obj. FILE NO. J - SD4.-2 JOB NO. CHARGE NO *002, 8300 Z___._______________ tema size/type/2 IZO -SSAKJ Additionol Pfqc. Doto on Sheet No. Flui d Inlot SHELL SIDE Out! of Ini of TUBESIDE - Outlet l*/A ~7~g/g Toto) Flow Ib/hr 3C>so /~7 SOO Lt qut d Den si ty Vi scoi ty Ib/hr Ib/cu ft flgCP 3 C>s <=> O. 2.4- nsoo JeLJS- 52 IISOQ. . Q. lo Sped fic Hoot 10 Thormal Conductivity Btu/lb- F Btu/hr* *q (t- F/ft ^ .37S /.O Vapor Ib/hr -3 Densi ty I b/ cu ft 13 Vi scosity -CP 14 Sped fi c Hoot Btu/lb-F <9` 2.4 z> 0O*fP> 15 Thonnol Conductivity Btu/hr-sq ft. F/ft 16 L otont Hoot 17 Norw Con don sabl e* 18 Velocity Max./Min. 19 Norm. |mok. Operating Temp. Btu/lb Ib/Kr ft/see AvV' & /z 32 f 6>Q M.W. = . ^ / Ipj 3Z I JSILL. M.W. = A 42. A/Z /aol/frol q7 l/3o Op.roring Pr.it. (Inlvt) 21 Pr..ur Drop 22 F ilm Coo If. 23 Feulino Rosi stance, BTU/Hr. Sq.Fi. hr-sq ft- F/8fu; Allow /c> <75 AjC4X Cole. A//i- Allo to Cole. /* 3> 3oq 5/7. o. oo> 24 Over-all Coefficient- "U*o Btu/hr-sq ft. F; Cleon i O S.rvieo LMTD (Corrected) So 25 nilulled Areo/Uni ft 2 (S TR.ai<i Ht TlJR ) -qH(0 utiid.) I d--y- Excluding, Ar.o in tub. h..1l 26 27 Design Temperature 2B Design Pressure SHELL SIDE F Af/A/US /O psig tsc> TUBE SIDE 250 Shell ID (Approximate) No. Tubas (Approximate) /4? / /^$ 22 U Tybe OD / In. | Tube Gage /7 In. BWG 29 Hydrostatic Test Corrosion Allow./Lining Number of Passes psiQ in. 1 /\Co V\ Ca Tube Length Tube Pitch joint jzouue'D. AAA X f t FLAiZS^D... I"'^ 32 Insulation C. 1--^ KJ <3 33 Cross Baffles: TyP*TCJBE SUPPORT" Segment Cut % Nu. TtllS pee tube; ^ef ini 34 Fin UWpht In. | Pm Tht iii. in. 35 Vessel Supports Saddles - Legs Other. 36 Weir Height in.; Shell After Weir in. 37 Imping.m.nt Bolfl. X-o\No | | Cond.nsot. Lilt W f Tl~ | Removable Bandl c fY^VW 1 Ccthodic Prol.ction-V | No V TEM A Cl Q> I I L etK ol W.I ^innoT_I| 1|Cod j ASMEJ wAvhuhlplUiiIwIUil,;uBuiwrorud mPil'ignti.h |------- r- Spot Rodiogrophi^t^Shell Shell Cftyor^___Channel^ _ |Stress Relieve: Shall .-ShellXover .__Chonnel ujjrf --^ Flooring Hood rr Sandblosf: |paint* iMoinroin Sitel 1 fO Tebe Ceunt Installed Areo+- ^ %* ^ 91 no zzles per shell M A TE R IA L SPECIFICATIONS 42 SHELL SIDE TUBE SIDE Tub.. A-214-c. STL 43 Servi ce Mk Si i. Rtg Face Typ. Mli Si I. Rtg Foee Typ. Stot Tub. Shoot C, STL A_44 Ini et 2- ISP f?F < 2. lS"o J?F F5W6I Fltg. Tube Sheet -- Iso45 Outl et ? 3 [SO RF rswfJ w 7. RF FSWH Cn* Bof./Tube Sup. c STL 46 Drei n C 2. iso _SE_ EItii Long Baffles 47 Vent -- Impinge. Baffle ~~ 48 tet/F.L D 4- l3o KwN 49 PRESS g 1 >50 RF FSwti 50 Temp F j! 1 So h- FSwtI 5) psv Jk_ JS JESjbuJ 52 5PARt L. z. JSV AT ZT^.-J i 53 See No*ile Sketch on Sheet No. Woir/Li ft - Tlo Rod. & Spac.r. L. Sh.ll 5hell Cover d=-STl_ Chonnel 5TL Ch. Cover/Bonnet $tu 54 1 f MAK/55 Mr & '/I. f (UP . M&v 4-Ceu> ; Sh.ll No. N.clt* 0 >T1_ Shell Nor- Flange* C. STL 56 - Shell Flanges ^ STL SPEC. BY VOMT^E^ THE DOW CHEMICAL COMPANY CHECKED: /P APP'D: /7/<P Vapo2.i3.er Fou S\ctu\C\ Spheres Chan. Not. Necks STL Chan. Not. Flanoes ^iTU" Chann.l Flong.t STt-- Fltg. Mood -- FI to. Hd. Fionas Cl amp Ring -- ~~ Boit./Stud.A W3 B."7 Nut. A \44. 2. H Vessel Supports C CASKETS & PACKING Sh.ll Covtr JM <Z>0 Shell-Chan. Side Chonnel Chann.l Cover Fltg. Hd. EQUIO. MO. l-2GG> 'Al-I34--50O2_ DATE: 7- '"A"? * V 1 REVISION DATE A / / //-/- 7 VENOOR TO COMPLETE ALL APPLICABLE INFORMATION NOT C1VEN 0Y PUHCMASER B ... 1|C "' SHEET J _ OF " HEAT EXCHANGER ST0415782 ST0415783 REVlStD $T04I5784 1. DESCRIPTION AND SCOPE 1.1 ONE EXCHANGER IN ACCORDANCE WITH OWNER'S DRAWINGS B5-901-4380. 85-901A-4380, B5-901B-4380 AND THIS SPECIFICATION. 1.1.1 TAG ITEM -302. 1.2 VENDOR IS TO REVIEW OWNER'S EXCHANGER ARRANGEMENT, PREPARE DETAILED DESIGN CALCULATIONS AND DETAILED SHOP FABRICATION DRAWINGS. FABRICATE. ASSEMBLE. TEST AND DELIVER ALL EQUIPMENT AND ACCESSORIES TO MAKE A COMPLETE JOB AS SHOWN ON OWNER'S DRAWING AND THIS SPECIFICATION. 1.3 WEIGHTS SHOWN ON OWNER'S DRAWING ARE APPROXIMATE WEIGHTS. VENDOR SHALL CALCULATE WEIGHTS BASED ON ACTUAL MATERIAL AND FABRICATED THICKNESSES. l.A USE OF A-- 515 MATERIAL IS PROHIBITED. 2. OESIGN 2.1 OESIGN. FABRICATION, MATERIAL. TESTING AND INSPECTION SHALL BE IN ACCORDANCE WITH THE LATEST EDITION OF THE ASME CODE SECTION VIII. DIVISION I. THE REQUIREMENTS OF TUBULAR EXCHANGER MANUFACTURERS ASSOCIATION (TEMA), AND THIS SPECIFICATION. THE GENERAL CONDITIONS FOR DESIGN SHALL BE AS SHOWN ON THE OWNER'S DRAWING. THE OWNER'S DRAWING IS NOT INTENDED TO COVER COMPLETE DETAILS. BUT INSTEAD IS TO PROVIDE A GUIDE FOR VENDOR'S SHOP DRAWINGS. 2.2 THE VENDOR SHALL NOT DEVIATE FROM THE DESIGN CONDITIONS OF DETAILS AS SHOWN ON OWNER'S DRAWINGS WITHOUT PRIOR WRITTEN APPROVAL. 2.3 DESIGN PRESSURE SFECIFIED ON OWNER'S DRAWING IS THE MINIMUM WORKING PRESSURE ACCEPTABLE. EXCHANGER SHALL BE STAMPED WITH THE DESIGN PRESSURE AS THE MAXIMUM ALLOWABLE WORKING PRESSURE. 2.4 THICKNESS OF SHELL. HEADS AND OTHER PRESSURE PARTS. WHERE SPECIFIED ON OWNER'S DRAWINGS, ARE MINIMUM ACCEPTABLE THICKNESSES WITH ONLY MILL UNDER GAUGE TOLERANCE PERMITTED AT ANY POINT. 3. VEND CR DRAWINGS 3.1 THE FOLLOWING INFORMATION SHALL BE CLEARLY SHOWN ON THE VENDOR'S SHOP DRAWINGS. 3.1.1 EXCHANGER OESIGN CRITERIA 3.1.2 MATERIALS USEC IN CONSTRUCTION SHALL aE SHOWN BY A STM OR ASME DESIGNATION. ALM 12-31-76 MONEL AND C.3. EXCHANGER 4380 S90Cy^-DEC305 1 OF 7 ST0415784 '-S'TOU 15185 3.1.3 nozzle designation shall be the same as USED ON OWNER'S DRAWINGS. 3.1.A HEADS SHALL BE IDENTIFIED BY MINIMUM THICKNESS. 3.1.5 OWNER'S PURCHASE ORDER NUMBER. ITEM NUMBER. AND DRAWING NUMBER SHALL BE SHOWN IN OR ADJACENT TO THE TITLE BLOCK. 3.1.6 HYDFGTEST PRESSURE THAT IS TO BE APPLIED TO THE EXCHANGER. 3.1.7 NAME PLATE LOCATION IN BOTH PLAN AND ELEVATION OR END AND SIDE ELEVATIONS. 3.1.3 ACTUAL WEIGHTS FOR EACH EXCHANGER BASED ON ACTUAL FABRICATED THICKNESSES USED. 3.2 VENDOR'S DRAWINGS AND CALCULATIONS SHALL BE CHECKED PRIOR TO SUBMISSION TO OWNER. 3.2.1UNCHECKED DRAWINGS AND/OR CALCULATIONS WILL BE CAUSE FOR REJECTION. A. NAMEFLATE A. 1 VENDOR SHALL FURNISH AND AFFIX TO A BRACKET ON THE OUTSIDE OF The EXCHANGER A STAINLESS STEEL OR MONEL NAMEPLATE IN ACCORDANCE WITH DOW ENGINEERING SPECIFICATION 92-651. 5. FABRICATION 5.1 PLATE LAYOUT SHALL 8E SO ARRANGED THAT OPENINGS. BRACKETS other attachments will NOT BE WELDED TO OR ON A Plate JOINT. WHERE EXCEPTIONS ARE APPROVED IN WRITING BY OWNER, PLATE JOINT AREAS AFFECTED SHALL BE X-RAYED PRIOR TO INSTALLATION OF ATTACHMENTS. OR 5.2 WELDERS QUALIFIED UNDER THE ASME CODE SECTION IX, WELDING QUALIFICATIONS, SHALL EE USED. 5.3 WELDING DETAILS AND PROCEDURES SHALL BE OPTIONAL WITH THE VENDOR WITHIN CODE LIMITATIONS. 5.4 ALL LONGITUDINAL AND CIRCUMFERENTIAL SEAMS SHALL BE DOUBLE-WELDED BUTT JOINTS. SINGLE-WELDED BUTT JOINTS WITH BACKING STRIP WILL BE PERMITTED ONLY WHERE DOUBLE-WELOED BUTT JOINTS CANNOT BE MADE. 5.5 ALL WELDS SHALL HAVE COMPLETE PENETRATION AND FUSION. DEVIATIONS WILL BE ALLOWED ONLY WHEN AUTHORIZED IN WRITING BY OWNER'S REPRESENTATIVE. THIS HAS NO RELATION TO ANY NOTED JOINT EFFICIENCY. ALM 12-31-76 MONEL AND C.S. EXCHANGER 4380 S 90 P4~DE C 3 0 5 2 OF 7 ST0415785 9-9LS \ ALM 5.6 ANY WELDED ATTACHMENT ON THE INSIDE OR OUTSIDE OF EXCHANGER SHALL BE SEAL WELOED ON ALL JOINTS WITH A wELO HAVING A THROAT DIMENSION OF 1/8 INCH MINIMUM. SEAL WELDS SHALL BE ADDED BETWEEN SKIP WELDS. 5.6.1 SEAL-WELDED PADS SHALL BE PROVIDED WITH AT LEAST ONE PIPE-TAPPED VENT HOLE. AND SHALL HAVE SCREWED PLUGS OF SIMILAR MATERIAL. 5.6.2 VENT HOLES IN PADS SHALL BE DRILLED AND TAPPED BEFORE WELDING PADS TO EXCHANGERS. 5.7 ALL CLIPS. BRACKETS. ETC.. THAT ARE WELDED TO THE EXCHANGER SHALL BE THE SAME QUALITY OF MATERIAL AS THE PART OF THE EXCHANGER TO WHICH THEY ARE ATTACHED. 5.8 FLANGED NOZZLES AND MANHOLES THROUGH 24 INCH SIZE SHALL BE IN ACCORDANCE WITH ANSI STANDARD 016.5. 5.9 NOZZLES AND FLANGED JOINTS SHALL BE FABRICATED WITH FLANGES HAVING A MACHINED FACE SUITABLE FOR TYPE OF GASKET USED. 5.10 REINFORCING PADS AND ROLLED-PLATE NOZZLE NECKS SHALL BE THE SAME GRADE OF MATERIAL AS THE PRESSURE PART TO WHICH THEY ARE ATTACHED. 5.11 ALL NOZZLES ANO MANHOLES SHALL BE FLUSH WITH INSIDE OF EXCHANGER. EXCEPT AS SHOWN. 5.12 VENOOR SHALL FURNISH 80LTING AND GASKETS FOR ALL COVERED OPENINGS. 5.13 THE INSIDE EDGE OF NOZZLES SHALL BE ROUNDED TO A MINIMUM OF 1/8 INCH RADIUS. 5.14 FLANGE BOLT HOLES SHALL STRADDLE MAJOR CENTERLINES OF EXCHANGER. 5.14.1 MAJOR CENTERLINES FOR EXCHANGER ARE DEFINED AS FOLLOWS. 5.14.1.1 FOR VERTICAL EXCHANGER THE MAJOR CENTERLINE FOR TOP ANO BOTTOM HE AOS WILL BE THE NORTH-SOUTH CENTERLINE. THE MAJOR CENTERLINE OF THE SHELL WILL BE THE AXIAL CENTERLINE OF THE SHELL CYLINDER. 5.15 BOLT HOLES IN STRUCTURAL MEMBERS SHALL BE DRILLED OR PUNCHED, burning of holes will not 3E permitted. 5.16 VENDOR SHALL LUBRICATE ALL EXTERNAL BOLTING WITH A METALLIC BASE WATERPROOF LUBRICANT TO PREVENT GALLING IN USE AND AQUEOUS CORROSION DURING TESTING, SHIPPING AND STORAGE. LUBRICANT SHALL c MONEL ANO C.S. EXCHANGER 43B0 S90Q4--DEC30 5 12-31-76 3 OF 7 K ST0415786 BE APPLIED TO THE FULL LENGTH CF THE THREAD. c 5.17 EXCHANGER SHALL EE FABRICATED WITHIN THE TOLERANCES SHOWN ON DOW ENGINEERING SPECjFICAT I ON DETAIL E92-601 . 5.18 VENDOR SHALL FURNISH A SPARE SET OF ALL GASKETS REQUIRED. 6. TESTING 6.1 THE VENDOR SHALL WAKE TUBE JOINT SHEAR LOAD TEST IN ACCORDANCE WITH APPENDIX A OF ASME CODE SECTIJN VIII. DIVISION l. 6.2 THE UNIT SHALL 9E SUBJECTED TO A HELIUM TEST AS DESCRIBED IN THE FOLLOWING PARAGRAPHS. PRIOR TO HYDROSTATIC TESTING. STM I 57*7 6.3 THE TEST SHALL BE PERFORMED IN AN AREA FREE OF DRAFTS. WIND, RAIN. AND VAPORS SUCH AS WELDING, CLEANING AND PAINTING. REV. C 6.3.1 AT OWNER'S OPTION HELIUM TEST SHALL 8E PERFORMED IN THE PRESENCE OF OWNER'S INSPECTOR. 6.4 ALL OPENINGS AND VEnT VALVES SHALL BE CLOSED AND THE VESSEL TESTED WITH AIR TO ASSURE A CLCSED SYSTEM. 6.5 FOLLOWING AIR TEST, PRESSURIZE THE VESSEL TO 25 PSIG WITH A DRY, NON-COMBUSTIBLE GAS MIXTURE CONTAINING IX {MINIMUM), BY VOLUME. OF HELIUM, ALLOW TO SOAK FOR FOUR (41 HOURS. MINIMUM. AND^ TEST ALL JOINTS WITH AN ACCEPTABLE LEAK DETECTING INSTRUMENT. THE DRY PRESSURIZING GA 5 IS TO BE INTRODUCED .TO THE VESSEL AFTEP THE REQUIPED HELIUM HAS BEEN INTRODUCED INTO THE VESSEL. THIS MAY BE DONE BY ONE OF THE FOLLOWING METHODS.' REV. 6.5.1 PRESSURE THE VESSEL WITH HELIUM SUFFICIENT TO INCREASE THE STATIC ABSOLUTE FRESSURE INSIDE BY 7.G INCHES OF WATER COLUMN MEASURED WITH SUITABLE GAGES OR U-TUBE MANOMETER. REV. 6.5.2 INTRODUCE A WEIGHTED AMOUNT OF HELIUM TO THE VESSEL TO BE TESTED. CALCULATED AS FOLLOWS: HELIUM (OUNCES) = (2.37)(VOLUME TO BE TESTED. CU. FT.) / (TEST TEMPERATURE. DEGREES RANKINE); ASSUMING TEST PRESSURE. TOTAL. IS 39.7 PSIA. REV. REV. 6.6 DELETED 6.7 DELETED 6.8 LEAK TESTS SHALL EE PERFORMED AS FOLLOWS: 6.8.1 VESSEL SEAMS. WELDED JOINTS AND ATTACHMENT WELDS (<- L ALM 6.8.1.1 MOVE DETECTOR PROBE OVER WELDED SEAM AT A TRAVEL SPEED DF 1/2 INCH PER SECOND WHILE KEEPING THE PROBE APPROXIMATELY 1/16 INCH AWAY FROM THE SURFACE TO PREVENT _ MCNEL AND C.S. EXCHANGER 4 380 S90CJ^-OEC305 12-31-76 T 4 OF 7 c ST0415787 ALM CONTAMINATION 6.8.2 TU8E TO TUBESHEET WELDS. 6.8.2.1 MOVE DETECTOR PROBE OVER WELDED SEAM AT A TRAVEL SPEED OF 1/2 INCH PER SECOND WHILE KEEPING THE PROBE APPROXIMATELY 1/16 INCH AWAY FROM THE SURFACE TO PREVENT CONTAMINATION. 6.8.3 THE INSIDES OF TUBES 6.8.3.1 HOLO LEAK DETECTOR PROBE INSIDE EACH TUBE END FOR TWO SECONDS. 6.9 SHOULD ANY LEAK LARGER THAN .00001 STANDARD CUBIC CENTIMETERS PER SECOND ARE DETECTED. THE EXCHANGER SHALL BE DEPRESSURED BY VENTING THROUGH A HOSED CONNECTION TO AN AREA AWAY FROM THE TEST AREA. ALL LEAKS SHALL BE REPAIRED AND THE EXCHANGER RETESTED FOLLOWING THE TEST PROCEDURES OUTLINED IN THE PRECEEOING PARAGRAPHS. 6.10 AFTER COMPLETION OF A SATISFACTORY HELIUM TEST. THE VESSEL IS TO BE PURGED OF HELIUM WITH AIR TO OUTSIDE ATMOSPHERE. f "cri j co vo 0 6.11 EXCHANGER SHALL BE HYDROSTATICALLY TESTED IN ACCORDANCE WITH PARAGRAPH UG-99 OF THE ASME CODE (SECTION VIII. DIVISION I I BY THE VENDOR. 6.12 HYDROSTATIC TEST SHALL CONSIST OF F.ILLING THE EXCHANGER WITH WATER AND APPLYING TEST PRESSURE SPECIFIED ON DRAWING FOR PERIOD CF AT LEAST A (FOUR) HOURS AND VISUALLY INSPECTING FOR LEAKS. A 6.12.1 THE WELDS OF EACH NOZZLE PAD OR ANY OTHER SEAL--WELDED PAO OR DOUBLE PLATE SHALL BE TESTED WITH AIR AND SOAP SOLUTION BEFORE HYDROSTATICALLY TESTING EXCHANGER. TEST PRESSURE USED ON PADS SHALL BE A MINIMUM OF 10 PSI WITH A MAXIMUM OF 15 PSI. 6.12.2 THE SHELL SIDE AND THE TUBE SIDE ARE TO BE TESTED SEPARATELY IN SUCH A MANNER THAT LEAKS AT THE TUBE JOINTS CAN BE DETECTED FROM AT LEAST ONE SIDE. WHEN CONSTRUCTION PERMITS AND THE TUBE SIDE DESIGN PRESSURE IS THE HIGHER PRESSURE. THE TUBE BUNDLE SHALL BE TESTED OUTSIDE OF THc SHELL. WELOED JOINTS ARE TO BE SUFFICIENTLY CLEANED PRIOR TO TESTING THE EXCHANGER TO PERMIT PROPER INSPECTION DURING THE TEST. 6.13 TEST GASKETS SHALL BE USED ONLY ON EXCHANGER OPENINGS. SERVICE GASKETS FURNISHED 3Y THE MANUFACTURER SHAlL BE USED FCR TEST ON BODY FLANGES. MANHOLES, ETC., AND THESE JOINTS SHALL NOT BE BROKEN AFTER TEST IS COMPLETE. 6.14 ANY OEFECTS FOUNC SHALL BE SATISFACTORILY REPAIRED. AFTER c MONEL AND C.S. EXCHANGER 4380 S 90 04*DE C 3 0 5 12-31-76 T 5 OF 7 ST0415788 W K 'S l+ iO is c c REPAIRS APE MADE The EXCHANGER and parts shall be completely RETESTED. i 7. INSPECTION 7.1 SUPPLEMENTAL To THE INSPECTION BY THE VENDOR. A REPRESENTATIVE OF THE OWNER WILL INSPECT THE EXCHANGER AND WITNESS TEST, HAVING AT ALL TIMES THE SAME PREROGATIVES GIVEN INSPECTOR UNDER THE ASME CODE, INCLUDING THAT OF REJECTION. AN 7.2 INSPECTION AND APPROVAL BY THE OWNER'S REPRESENTATIVE SHALL NOT RELIEVE THE VENDOR FROM COMPLIANCE WITH THESE SPECIFICATIONS. 7.3 THE VENDOR SHALL MAINTAIN PERMANENT RECORDS OF WELDER QUALIFICATIONS AND ALL PERTINENT DATA PERTAINING TO EACH EXCHANGER. 7.4 PRIOR TO OWNERS FINAL INSPECTION OF EACH UNIT. THE VENDOR SHALL HAVE PREPARED IN FINISHED FORM AND NOTARIZED 3 SETS OF RECCRDS. EXCEPT FINAL TEST DATA. INCLUDING THE FOLLOWING: 7.4.1 FORM U-l MANUFACTURERS* OATA REPORT FOR PRESSURE VESSELS 7.4.2 MATERIAL MILL TEST REPORTS 7.4.3 NAMEPLATE RUB ElN G 7.4.4 AWS CLASSIFICATION AND MANUFACTURER OF ELECTRODE OR FILLER METAL 7.4.5 TEST CHARTS 7.5 THESE FORMS SHALL BE SUBMITTED TO THE OWNER'S REPRESENTATIVE AT THE TIME OF FINAL TEST SO THAT HE MAY CERTIFY CORRECTNESS BY AFFIXING HIS SIGNATURE TO EACH FORM. 7.6 THESE FORMS, TOGETHER WITH FINAL TEST DATA, SHALL BE ASSEMBLED INTO 3 COMPLETE SETS FOR EACH ITEM. EACH SET ShALL BE IN 600KLET FORM, NO LARGER THAN 9-1/2 INCHES BY 12 INCHES. WITH EACH AND EVERY SHEET BEARING THE OWNER'S ORDER NUMBER AND EXCHANGER SERIAL NUMBER. IN NO CASE SHALL A RECORD BOOK PERTAIN TO MORE THAN ONE EXCHANGER NUMBER. 7.7 THE OWNER'S REPRESENTATIVE WILL AT THE TIME OF WITNESSING THE FINAL TESTS AND CERTIFYING CORRECTNESS OF FORMS, COLLECT THE APPROPRIATE NUMBER OF BOOKLET FORMS FOR EACH ITEM TESTED. 8. CLEANING AND COATING 8.1 the inside and OUTSIDE of THE EXCHANGER INCLUDING BRACKETS. AND ALL CAPBON STEEL ATTACHMENTS WELDED TO THE EXCHANGER SHALL BE CLEANED OF WELD SPLATTER. WELD SLAG, FLUX DEPOSITS, BURRS ANO ALM 12-31-76 MONEL AND C.S. EXCHANGER T 4380 S9C0A-DEC3O5 6. OF 7 ST0415789 STO4 15790 SPLINTERS, loose mill scale, and all other foreign matter. 0.2 all EXTERIOR carbon steel surfaces including brackets ALL CARBON STEEL ATTACHMENTS WELDED TO THE EXCHANGER SHALL SANDBLASTED AND COATED IN ACCORDANCE WITH DOW ENGINEERING SPECIFICATION E57--2A7. and BE 0.3 ZINC THEY MONEL SURFACES SHALL Be PROTECTED FROM COATINGS CONTAINING OR LEAD PIGMENTS. IN CASE SUCH COATINGS DO CONTACT MQNEL SHALL BE PROMPTLY AND COMPLETELY REMOVED. 0.A SANDBLASTING AND COATING SHALL NOT BE DONE UNTIL FINAL INSPECTION AND TESTING ARE COMPLETED. 9. PREPARATION FOR SHIPMENT 9.1 ALL FLANGE FACES, NOZZLES. LUGS, SUPPORTS, ETC., SHALL BE PROTECTED FROM DAMAGE DURING SHIPMENT. ALL PARTS SHALL BE SHIPPED AT THE SAME TIME. 9.1.1 FLANGED OPENINGS COVER USING SOFT GASKET PROOF CLOSURE. SHALL BE COVERED WITH LIGHT STEEL PLATE AND AOEQUATE BOLTING TO INSURE WEATHER 9.2 THE EXCHANGER SHALL BE CLEANED OF ALL FOREIGN OBJECTS INCLUDING HYDROSTATIC TEST WATER BEFORE SHIPMENT. 9.3 THE EXCHANGER SHALL BE IDENTIFIED BY PAINTING THE PURCHASE ORDER NUMBER AND THE ITEM NUMBER ON 2 OPPOSITE SIDES IN CLEARLY VISIBLE POSITIONS AND IN LETTERS AT LEAST 3 INCHES HIGH. IDENTIFICATION NUMBERS TO BE ONLY ON THE CARBON STEEL PORTION OF THE EXCHANGER. 9.4 IF SPECIAL HANDLING IN THE MOVING OF AN EXCHANGER IS REQUIRED. LIFT POINTS AND/OR ANY SPECIAL INSTRUCTIONS DEEMED NECESSARY SHALL BE CLEARLY MARKED ON THE EXCHANGER WITH PAINT LETTERS AT LEAST 3 INCHES HIGH. IN ALM 12-31-76 MONEL AND C.S. EXCHANGER T 4380 C S900>K>EC305 7 OF 7 ST0415790 plant CrS'^ MANUFACTURER FIELD ERECTED .............................................- C#R PlAMTVoJ El' M NO. t- P.O. NO. -|pnT\ NO. UNITS TWOO I & re @ 0 . JL tile 1^ _ 4 N- J - Od - 0 JOB NO. 300 2-- charge no. &3U0 2- |TOTAL VOLUME J 2 O O <D 5 T G 4 5 1 9 1I 4 T )"0 UOZ.ES DRILLED /-V 7 ABOUT //"square pitcm TO W/rRJN 6" OR -- Vassal. kVALL. USE MO SCREWED OETAIL MOtlLS C 27 Operating Pressure 2B Operating Temperature 29 Liquid Sped ft c Gravity Cofllenti L.tfial 31 Design Prtuuft P`Q <\e> Z8o ' . O'*. Ihlo I \so 32 Design Temperature sao 0<Ol)PL.I M<5S For Further Details, See Sheet No. Type Support*: SADDLE Insulotion: Fireproo hng; Sondbl o*ft MftSTI C- S7--2.I3 ygs I Point: f57- ZZH SP Manhole:________ _______________ ___________________________________ Platform Clip*: ^GSiLaddf Clips: U |lnul.~~Rings: ^ Q*~ 33 Max. All. Pf. (Nev&Cold) pig 34 Limi led By 35 Hydrostatic Test IV57 zX l-'A A vTp LZez:Shell Head* Corr. Allow, in. Wt. Empty Servi ce Mode 1b Wt. Full of Water No. Si xe Rating Foce lb. Typ Shell Heads Joint EfC % IMlet A 'i 12 5oo *P Cod: k S. Nl ~ Stomp Reqfd |Ye { VAR. OUT B \ 14 ISO RF Rodioarceh: doDfc. Stress Relieve; 0^0^ Shell Heads Lining Thi diness Mat'l Can in. Mot*l-Minmum Quality____ cAR&oh1 SYseC LIS. OUT DRAIN C 2 12 150 RF 0 * 2 e ISO RF LEVEL COUT. E 2 2 ISO RF leve l ALfty F 2 150 P H(AtJHOL-E '"``t * | ISO COND. IWL. H l ft 1 50 RF PREZS. n. j ) r 1 SO RF PRESS. R. K 1 2. 150 RF i 0 f ___ A a! Q 6 Motile Neck Flange CouolinQ M.H. Cover Se -J T. P- S-V. L 1 6 ISO Rf Spake * L 1 Q IrsILFT *'*N n | i & 2 ISO )5o RF RF P il Supports Befts/Studs Nuts _L i -.2 riAl^3-S>7 ,\ 4 Q R S Goskets T No 2 tl e to be Blind.A PR OJECT IWTo spec, by voM Teess. IKED: i l.f-P fyiUi -<SE> THE DOW CHEMICAL COMPANY FUKMACE OUENltTlA DRUM- EQUIP. D-2.1C D-ZZ.O SPEE.Cc.-A\-!05-83OOZ NO DATE: 1- {i ~ b"7 REVISION DATE A VEN^OS To COMPLETE ALL *pPl |give n ft p.iaCHASi;`' NFOflMATlOSI MOT B c |smce:t / ^4- HORIZONTAL VESSEL SPECIFICATIONS ST0415791 PLANT OYSTEg CR E=rL pLAfjT Ah -1 B/M N0 MANUFACTURER P.O. NO. FIELD ERECTED YES NO. UNITS 1 Operating Pressure psig |OZ 2 Operating Temperature F 6Z 3 Liquid Sped f c Grovl ty 4 Contents Lethal O. 74-s, *ax [Nql 5 Oesjgn Pressure psig 6 Design Temperature 7 Mas All. Prass. (New&Cold) psig /5TO /S-O 8 Limited By , 9 Hydrostatic Test psig Viz. K fAAWp (bRcl 10 Shall Heods Corr. Allow. in. \ /{=; u Shall Heods Joint Eff. % 12 Coda: A ^ NT Stomp (V **"l No 13 Radiograph: 14 Type Supports: LUGS 15 Insulotion: roorJgi 16 Fireproofing: M OM C 17 Sondblost: I potntt 57-247 SP 18 MonKoU jtegyy _____________ ______ _____________ r4o I ^4 ~$CL19 Platform Clips: L odder" Clips: O jlnsul. Rings' 20 Pie* Supports: NjO 21 wind 22 Nokh. Wt. Empty Seismic: Wt Full KloNJf 23 I tom Thickness Mat'l Class Mot*l - Minimum Quality 24 Sholl 25 Hoods <= =. Tl. <=- STL 26 Lining 27 28 VANES i^t tONJ E L 29 No rile Nock l_ 30 Flo IflOS 31 Coupling Do MOT USE TW. -S--TL- 32 M.H. Cov>f 33 Supports 34 Bolts/Studs 35 Nuts 36 Gaskets 37 O S T c_ A I T3 BJ7 A \cT-a ~Z~ m wj r>4 cL-<o> Service l si LET Mark OUTLET HIGH LEVfL. Al C LIQUID OUT No. Si la Rating 14 I >o Face 15Q JEJL 150 -SF. ISO RF Typ>i -fif-Sx A HamUOlE f1 ja i s~o RF THU noe J- 04.-2 JOB NO. 83op; CHARGE NO. g300 2- TOTAL VOLUME GAL r ----- !-----1 ~"1 1: --1 1 i 1 *1 1 1 ""1 V2''_ i i k-- b~ in /* ' Ji CK VO ) V> - c> C.1 --J O ro Nettle to be Plugged or Blinded. CHECKED: t'f -f p App, tfte'ehki T- 22O For Further Details, See Sheet No. EQUIP. NO. D-222 5EPAATO/e . SPEC. NO. A)-l 0&-85OOL DATE: 7-M-67 REVISION DATE . 1 /VAX' \f-n->7 VENDOR to COMPLETE all APPLICiE .E INFORMATION NOT 2GlVLN H V PuLCmASE^ SSSO 3-fcfc o 4;T /V<T y-/-&7 C f! j SM E E T Of VERTICAL DRUM SPECIFICATIONS ST0415792 1 f plant OYSTER. c^/ReElcL Pl/iAir/jbV B/M NO. manufacturer P.0. NO. N0.e J-C4-2 JOB NO. &30C5Z. CHARGE NO. PEERLESS |vTFc5 co. Dallas TEXAS BULLFTikJ Ho tol TYPE " /AS Fi<$ OZ. I=C>U V- PEooess ^moitionJS ; .lly T= &z.sDF "P * \c>~z. PS I6 10 YAPOT FLOW = IOSOOO CS./W/2-- n LIAS U I D Plow - ^ <2x00 LB./WR. 12 13 vapor t>eosnv - lo>s ft 14 LIQUID TENSITY = c- L^/^LJ F" 15 MOL WT = 14 17 COMPRESS/liiLiTY' 16 YAPo/z load at /4.7PSJA 19 Ft * 1.02 20 ~ Aocoo 21 P^W= I-S2. 22 23 S.IEE Reo2 U M2EMEMT = (&<-0 ^\.OZ)6 .sz) 67^') -- id Z O 24 25 S. DO NOT USE "HiBEADED Co UPuikJCS - 4. max pr,lssuE DfZoP allowable -= 6" s. L\^V4T LOElOiMT IKJTeT2n1AI-*S M<oNeL. Be MADE $1041519-3 43 45 44 47 48 49 50 51 52 53 55 SPEC. BY VOW TRE? <5>> THE DOW CHEMICAL COMPANY CHECKED: ^ V p T-220 SEPARATOR APP'D: DATE: f-J-L"? REVISION DATE A y,,v-2--e/-rJ7-6,-A7TJLs VENDOR TO COMPLETE ALL APPLICABLE INFORMATION NOT 5IVEN BY PURCHASER B C JSHEET ^ OF EOUIP- * D-ZZ NPo!eA 1-/0(5-83002 V612TiO\L"Df2uM SPECIFICATIONS ST0415793 Fn'oL.E J-&4-? PLANT MANUFACTURER <TEEF1^ PLAA-^T AJo J B/MNO. 5-//G-jQ32QZL- P.O. NO. JOB NO. 85002- CHARGE NO. flgoQX, Operofing Pressure Operating Temperature Liquid Specific Gravity Contents Lethol ptia 1 O F 32 .)&(*>-4-e \ .bbl(s>\00o va- ird I TOTAL VOLUME ^ . K C; ft. QQg) VESSEL SKETCH SEE: slQTES SHEET z Design Temperature ________ss____________ F -4-F r<D 50"F Mo*. All. Press.(New&Gbld) psig Limited By Hydrostati c Test psig f'/z. X MAlA^/NiC) Shall Hoods Corr, Allow. in. '/l c2> Shall H.ads Join) Eff. Cod.: ASME V III 7. Stamp |Yss +4w Rodtogroph; Stress Relieve: GAVJ. `STAIRWAY e "PI-ATTCOE.M ('TOP) Typ. Support!: MOTE 2 g -4. SHCE 2- <In.utorion: 11 0<?og>L.. Wall with perlits Fireproofing: c-otJCegTE OKI l&SS^ALBI Sondblost; ^*7 -- Monho to COp<ni:S7-2^7 white: Plotfemi ClIpcVFS |Loddr CHp:\frs |lnul. Rinat: Yl pip. Support*: VPS WnJ.L,J... (t5MPH, eAfq- _ Seismic: IsiQ hj /: Wt. Empty lb W Full I fon Thickness Mot'l Closs Mof'l - Minimum Quolity Shell A - >)> - 70 1K (p\ J S' i Hoods in* Lining GAL CO -H O poo S.L& wall Coi4STRUCT toH Nozzl eNe&s FlanflM -J.l. Coupling M.H. Cover Supports Bolts/Studs Nuts Gasket* Sorvlce Mark Nb. LIQ. IN OUT A v/EUT B Manway *C Safety Valve D 1 1 ) 1 LEVEL E3 Thermowell F MANWAY -*G SHfLL PuttfE H 1 A- l?3 -B7 A - I-34--2K J M-GO SI x. Rating Face Typ. to ISo 4- RE fT 20 4- 3 O 2 L____ z __Q____ 20 r? 5 DiMEMSiOkIS KEFER TO BOTTOM TAM6ENT ^I-D.)oF SPHElZG ' ID LEVEL REFER J LEVL ALARM K l2 22 jtt SPARE SPARH Man wav' XL >t M N ^Kl) 0 2 2 2. > 2 12 ' 4.f i -!^OTe 04 R Naxxl. *> b. Plu9B.d or Blind.d spec b rVonTeersc OUTER! 5VAELL. QKIOV For Further Dotolls, See Sheet No THE DOW CHEMICAL COMPANY EQUIP. NO- v-z&o,/$z - //VCHECKED; APP'O: DATE: J/l/j7 Product "Storage Spu^ees \J- 2C*0, V- 2<2>l 5V- 2<^2 REVISION DATE A B c EC-Al- i45-S300Z_ VERTICAL VESSEL VCN30 to COMPLETE all APPLICABLE information not GIVEN BY PURCHASER 25640 3-06 IsHEET ) Of SPECIFICATIONS ST0415794 ST0M\57$5 ?E J-04-2 PLANT cdYSTER lTREEL PLAJUT AJi>. / B/MNO. ^110-^300^ JOB NO. SSOOZ. c MANUFACTURER thebe UkTTt^ P.0. NO. CHARGE NO. 6 3 OO Z. --V 0 ALEV^LAI) &^> ^Kl L<^WER, VAEMlSPAEee 2) A.E Ik/ FO(?C ED CCMCRETf SONOTUSE T 012 4" ALVA M-l'EED STtEU fill-ed anp <^ased 'Witm <r<p^<rf2eTe" 3) VENDOR. To OUOTE AUTERMATE ^(NCLE WALL 5P4J&13E 4.) MAIN SUPPORTS U WDER _|USULATIONl To rSE A-SI<S-?o IF^EOUieeD TSY STRESS -TEMPfRATUCE <TAL<1 U LATlOlfe 5; IQ <0 N4Z2LES MARK M AEE SPARE ALTE R. NATES. FOJE NOEELL MARK. E AND SHOULD E> <3N APPROX 1 MATE. LY SAME ME2.1D1AN DRY IUERT <TAS PAD To BE USED B-ETWt&U IMMER OUTEE SPHETELE. SEAL OUTER SPHERE, PA RTJC U L A R LY arou wo sjo^elEs with Flexible metal expansion .BELLOWS TO MINIMIZE LOSS OF FUK6E <SF\S. &) NOZELLS To BE ORIENTED SO THAT INSTRUMENTS CAN E>E SERVicep FROM <SR.OL)n1D, LADDER, OR. PLAT FORH. Thermo wEu_s (nobles MkJ F) To be distributed AT $E.ATTST SPACING. PRACTICAL. X NOZZLES B,C,D,H U To BE IN UPPER. PLATFORM4u- 5Hex.L oPeuru^S To HAV? SCfcEEM LVcX. To pReVc'MT LsS- Or PeR.t_iTC / M 5Ju AT10 N . lD.) T>eSl G.N TO SUPPORT PULL OP WATER. v\.) \Mo2ZLes "P"A^.e porl filling AnTD dum?iu$ "PSRliTE 3?kCe ^ctuut^o CfcteuL.s. Locate: /yt v^tct4 low 'Fo.vJT^ CD S?KBRC A-S DSAB.LY AS ?OSS IMS' 11J SPEC BY V^nTRELS THE DOW CHEMICAL COMPANY CHECKED: APP-0: J /f ^ SProduct torage Spheres V- ZG>o, V* Z> f S~ \Z-ZZ DATE: jj4^7 "R EVISIO N DATE A ^ VENOOK TO COMPLETE ALL APPLICABLE INFOAMATlON NOT CIVEN or PURCHASER B C ^ F-9 ~ ^ -r> |>MEET 1/260, SPEC NO. Al- I46 S30OZ. MESSEL SPECIFICATIONS ST0415795 -* 'T*ns 1 .*=.- '/ - C' ISSuSO c- -i ' '6 ir T S-~< f- J * / FILE NO. j - O 4- - /C- PLANT C YZ 7V>- manufacturer CA'f//C Plaut -&\ b/m no. 5 soi'pynn-^. P.O. NO. JOB NO. dSOOZ CHARGE NO. TYPE FIELD ERECTED YES (NO) |NO. UNITS Op. Prill. Dpt. Prass. } psig Op. Tamp 5 Q ptig Dpi. Tamp. 270 Liquid Sp. Gr. 1,3 0 SOO F Cat. tan ts Lathol TOWER^ SKETCH "w Mom. Allow. Prats. (Naw & Cald)pIg; Limited By Hydro. Tast 7-5 p si q | Code: A 5 l^~F Stomp (jfay) No JLC Corr, Allow, in.: Shalt OtfTflflf Haods kt**6U'htJe, Rodtogroph 8V COOS Joint Efficiancy_____ %: Shall bY CODE ; Haad* BY Strait, Ral. 8Y Coq In ul atian: fsj g_______ |$alf Supporting ffas) No Sondbl ost: Fl rap roofing: See Note?) (S 4^^ Point: 57'247-SP Manhol a;_____ Hingad______Qovi tad______ Qthar , /9Z?LJT~7D Platform Clips: Lodder Clips: "00-H JJt ------------- ^ # 30 /. q SI Pi pa Supports; yes In sul. Ring *; H Wind Lood; 115 M PH WIMQS Sal tml < Shipping Wt, lb Wt. Full 14 Tray No. D< e Sp od n g Typ. Matarioi Tray Jnttaliarlon lb 15 Thr JJ 14-4 IS v>. 16 lZlhatJR. 144 ' X4" \h I ri" Ramovobla ic. lYatl No Cortri dga (Support Ring3 17 19 TKru ZO 1++1 18' 14 kc Mo ijc 1 TrqyMonwoy No 1141IS 20 Thru 2 | 111 h W(L IAolk* I Monwoy Si xm >TD. In. 19 sm TVttxie 1+4" 111 V&We rAoioel Watr Sat. (Abova Floor) In. CqM4dLc.^- ~Devce: VfllVg.SL. Adjustobia to 21 (Ad|. Slott Saolad at All S*tHga) 22 Pocking; / "0-t T / " ^ / /5 . rx .. 70. /5 .8 r r <f0 . \4 p* \ 2H(,` , \ N% ik 9 1 24 *21 1 tam Sh^LTep Thi cknass Mat*l Class Matari al -(Minimum Quail tv) i ru MONEL 0 0. ;c % Mope 1 C lad C. STL (T) * 26 Intarmad In. 27 Bottom 2B Haods-Tap 29 */ Intarmad in. In. HP KIEL Qk. XOA Mrrrl Clod C.STL in. if) Xo Bottom 31 h< Cona Sadi on 32 U Lining in. MotJFL in. in. e. jc'/r FA o... \ C lad C. STL & 33 u mi 34 UJ Hozzla Hacks 35 v> FIbiom 36 < Couolino QC 37 UJ M.H. Cov.r t- X < Skirt in. kfilSZL.sHof/L ALL 5 /HoveL (S) 'Monel C STL. FL 65. WITH MokJEL FACP V/r.'Y-'N.) Monel C.STl. pace 39 Bolts/Studs A - 753 - 6 7 40 Nut* 6 - i9*i - u H 41 Not Goskatt GAtiLocK 9co or equal 42 Troy Gozkatz GAffL OOAT 9cC or &(jAL 43 Sand ca Mk No. Six. Rtg Faca Typ. Sarvica Mk No. Six. Rtg Foea Typ. 44 XyUt i A / 2* l?p^ ftF Ity'M Cpn-+ N / 7" iso' JLE_ 45 Raflu x B /- i5cm r46 UJ OH Vapor r /-,> 4? ClAssMi 47 z> Q Bnii, Out D 7Z &* \l5o RF 48 UJ E / 4n /5o* L aval Cait p / ?" Sompla* 0 2" 6.3 T~<rt R 4 5 e" AE. XE_ RF H_ 49 U SO UJ Oral n tf H-" /So G/ ffo' RF kig1 AIpu , T (?civc/e U 2" i 4* r/e-A/f -6_j 051 Menholss *H / Zo" iso* IfF Misc. tv 3 4" Ml. 52 MprtVmlai i M' ISO* RF *w / V RF -2L 53 TS. W.ll. K 1 X' j !5or RF iw <x / J1 54 Pr. Goga* L / 1" , ISO" RF Tamp Coni Y / L RF S5 j, i.i ty M i Z~ | ISo' 1_ Dip CT 1 1 z / 2' Ifo" _Lf_ SPEC. BY J.L.T <0> THE DOW CHEMICAL COMPANY CHECKED: /f-f~ APP`D: /l//?/.. REACTOR DATE: T-/3-'(f6 REVISION DATE St mLT +- P ^___S-1-(p7 I V' 1 i 1/ '5-z<z-fS7 c TtyW a-/-7-7 Pivcn urchaserVENDOR to complete all APPLICABLE information not by _ "__ fy- --'-- 1 1 ... /sheet OF pj ;S / 'J .# !. 3 ,x \ \ . \ ST0415796 CT r-- LO -3- O -- CO - 0 30300 0-00 THE DOW CHEMICAL COMPANY TOWER DATA SHEET SPEC. BY .1 i .77 DATE *7*--3. 2-U approvalTM5 plant oyster creek pr/wr#f SERVICE MANUFACTURER TYPE FIELD ERECTED YES Troy No, (Bottom Troy=No*l) Total Troys in Section Tower Inside Diometer Troy Spocing, inches Number of Liquid Posses Mox.AP, per troy^total, mm Hg Minimum Areo/Downcomer, sq ft NO. UNITS * zz zz 14-4- " IS" O r*1 ITEM MO, SPEC _^ \ *"> /V z- Z36QZ. FILE NO. J-oi-ZL [DATE lo/l7//,. O A/5 * l Yc 2 1 Z? 144" \8" ON JOB NO. gjQQJ? CHARGE NO. b/mno. .0. NO. >_____ " Vapor to Tray(s), Ib/hr T emperoture,*F Pres sure, mm Hg*psio Density, lb/cu ft Design Range, % o 2,32.0 221 2.9-1 O. -.9,H 50% -- toc-A Sc 2. 5s c J.7 7 29. 7 0.597 rc/- - / CO 7. Liquid from Tray(s), Ib/hr Temperature, *F Viscosity, cp Surface Tension, dynet/cm Density, lb/cu ft r- Foaming Tendency Solids Design Range, % 2?3,ooo 2 2 1= C 5vIS. 7Y 7c. cr AfC /v 50% -- 17.*5% 28 3. O o o 22 7 9 o. =v /S.7 7o. o o MCAJB SDVt - ISO'/* c / " J, o Od <3 $H3 1.9 if a> ruO* 1I<o1-1 L ` Tower Diometer Req'd at 100% Design Tray Spacing Req'd at 100% Design, Inchas Downcomer Area Req'd at 100% Design, sq ft Actual Downcomer Ar#o>Stde , sq ft Center , sq ft Doweomer WidtlwSide, Inches Center ,inches Weir LengthSide , inches Center,inches Weir Height, inches Downcomer Clearance, Inches Volw Unl,BubbU Capi/Troy Sise/Type Parlor at ions/Troy Diameter, Inches Pitch, inches HoleSlot Area, sq ft Active Area, sq ft Max* Vapor ot 100% Liquid Rate, Ib/hr Min* Vapor at 100% Liquid Rate, Ib/hr /Tore: r)?/? Y : pacing. Rrr \uKf TRAYi ft f n Ann tpa yS zn 2! -fc ^ts._____24 w. !->rn\f tAc*. rTrcLujO-f-Y <.ll Af/i /9 Aaj D D / /nr r/n r-2. / < <&- 71' flwn Entrainment at 100% Design, Ib/hr > TotolAP per Troy, mm Hg 7i> fJoz.-2.lc, fit) AaJD (~rj lo C*J SAMr nRiiArrATiof J. IT) Design Tray* -hr M0.XIM Uia Ca.pa.tiHy by pro Dor 4-lo uiwc^, Cm A cCoujiJf.ftVji.P-r 0-r<Lo_ %{ pgr CPU b OV -C lon^ 4- 3 r _ t>r CZ+Jc pi, T |oqA___ -Cor ___ h >Q-A ,-s. t'Ki. os fnvc area v ioa-A is e^ujqJ 4-r CO Min C LAOD tcJCb 3/1?" (fj piuaeb A/ozuss uy-r k/ x.% r)'T***us /??mrunhi/~ "Tt'nj ZO* A7R> w / o /f', . %x (3'l5-V --O Nc,xz)e A/trcJe-. r A/=rr ZestA^ . W G . S. LL V W.Jr.f CfS) 57-214 f-iqstic ouTsi/p-^^rr. f'r?, V rC22lf 3 "insid' <hsH- Mo J r If s a-r A.tAAl.fV-R. 2 /Vj .fro/ Pgr rn hJn>. .Y.-j'.i c:/..rr S 77 + , h- /ctotca rs- 1 "LC r foe: i__ occv~ 7?oai 4-. P i hr. Alio m '7-L. cr.-/r `r/a.t_ wa j__ f A- l. l M....'Ki: *m*rlV Tr rra~ i. 7/>. . . ^ .U.-...... ' 60 ~ e c4 la o - c - _ jCC K* Z/t~f7C/? ? f- l>" ~ * /y. * oy/vjV /<S 3c ' Tf-a^ 2? Vendor to Complete All Dofo Not Specified by Dow 7~H / j / r/r// r / c c. - r Ipage 3 OF 7 7~ els'Jr jO yv cS " ~ . 4 ST0415797 6T0l\\Slt^A,, iV/-PLANT (OYSTEg, C5.E5K. ~PUMJT AJj1|b/mnQ- S'*//--'% % Q Q MANUFACTURER 1 P.0. NO. FILE NO. J-04--Z- JOB NO. g^OQZ, CHARGE NO. g > O O 2_, 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 4B 49 50 51. 52 53 54 55. S'.rti-- -ji 56 SPEC BY -J A'W CHECKED: /j / f kPP'o-./<fl i/t jL-> |\1ozzle: Elevations THE DOW CHEMICAL COMPANY LHAN -U(J \OWCkc. DATE: 7- | | -C7 REVISION DATE A VENOOR TO COMPLETE ALL APPLICABLE INFORMATION NOT GIVEN BY PlIRCHAien B C | A __ /\ f SMEET ft- OF . EQUIP. NO. T-ZZO SPEC NO. Ams^-SSodz. SPECIFICATIONS ST0415797A PLANT '-.'.5 1 manufacturer TYPE Fno.E %. f- LAUT" f. . B/M NO. >/// _ %300-`- JOB NO. P.0. NO. CHARGE NO. NO. UNITS OM* S ;ICO'c. &^,ao~2- SPEC BY JAW CHECKED; /J APP-D^S. THE DOW CHEMICAL COMPANY WCl CoLun^ DATE: 7_n_^7 REVISION DATE GIVEN BY PURCHASER 14630 3-66 Bc r- AlSPEC. NO, - I4l-8?ooz TOWER SPECIFICATIONS ST0415798 plant j'rcneK. CeeEn R_Au;T JJv-t B/M NO. *5V/ -%30 O a-" MANUFACTURER P.0. NO. no.E 4 - 0<L - 2. JOB NO. 7_ CHARGE NO. 03OOX vv r< tS c & ~r Jr weep/-kPL.G. 'ScAlPakI "Detail . W r& 4-40JL& X 0 */ __\__>_ l. - JL. BELL- K\oo-rHi OR 30 C.OME 1 WLer c yy r Ii u i , / , Appear. SPEC BV gAw THE DOW CHEMICAL COMPANY CHECKED: APP'Dty^^j' ; /,, 7 {~1Cl lolumm DATE: 7-||~i.7 REVISION DATE A VENDOR TO COMPLETE ALL APPLICABLE INFORMATION NOT GIVEN BV PURCHASER B c SHEET uL F~f EOUIP- NQ. T-Z2Q no!c A I - |4I-83ooz TOWEE. SPECIFICATIONS ST0415799 * plant Qysvefc. C.ig.c.^.> manufacturer ti- gX.OOA PLANT Mo-l |b/mno.^/- noo, P.O. NO. NO. JOB NO. CHARGE NO. M c-- S 3002. 6-3002, fsjoTGs ; |.)"PeSI<SM ToojE(<L -TO 5Cl?POie.T PULL- OF WATTS rC_ 2.) LoCA-rei LEl/El- (00 2-7-LETS AMD M\Exe:e_ AfJTs SAUSE MOZZLES ^cT p^OMi teBDlLER. VAPO& I9JLE.T", OPPOSITE BoTTOA DOWM COH o(E.. 9 -5-) P/2-OU (DC AIR- U^AJ-r-S ANT) lDSr-^ZT!OtJ GALWAY IN SkLiET10 1) 12 Ax- MIZZLES "kL" MAX CLOfJXAitO VAPoKL, IuTR/ODOCE" ST04I580G 13 FEED THK-OOOH A 5PAP-6E R_ WITH POLE' -Foo-iT-iKicS "DOW U. _M ~[jO MOT" Pt-tD INTO DOWNCOMEk., 15 16 17 18 5,) Feed Ax "S"will ^uth/u lOoj0 by weight VApot. 19 I OSTAUL fAdl-l IJOZZLE 1-4 ALF WAY bCTWEEN THE FEED 20 21 "Ti^Ax a mtd t"H e teax AiRol/c. Z?<5 Nc - f^e6o /ht& cdmf/z. 22 ^) IwEOlATioM : NpOAM(Si--A$/ T=c>^- E'nJXI'^.G: COUOMH, 23 24 25 7.) h^oviLF tEFtLiy. iMcerr weirR. od xeay S'. Wens. hgisw'- 26 - \Z". Locate i kj tiJe jame Po-stxtOKj ArS "THiB 27 28 let- wei^2. oo the tieay Below- - 29 30 S.) UzxLAXE Al-U THERMOWELLS IN3 VAPOfe STALE. 11 32 <?.') "pi ee PLDOFi X <S POI2. CO lUMN Td IVJEluDE : 33 or) ALBI 8^ o M ekteriok. of stiEr 34 35 b) lA/ATEE. SPAX TO ILJS|-De OF DNHiRT @ o.ZS SP^a/ft'' 36 C) iToLDKU 5?R|UIZLC-D TO AFlE>HT OF 0.1^ 6PM/FT 37 38 \C.) All kamwaxs 'R.e mom A t^lc FRoh abomc amo i^oow 39 ,4 v'er?^1w-cY /U-toner). ^w 40 11.') L/<3uib withdrawal piRoM DOZZLes U TO Be F<om 1 42 Se.AU PANS. Boxro K1 OF KOOZZ-UR: T"D Be TF_1_>S H W IT R 43 -pRA Y AS NEARLY Ae POS5 | BlE . 44 45 46 \2.)"pRjoi/i ^e Alkslc frokJ i^eAaAErs inside- column 4- fx 47 48 Bfilovy bottom xi-i-Ax Fo(R. EEAfpol."o *l)ppor.3 , See 49 50 51 l3.)poutDe 4p,/ujesp iJoue iw Bottok SCAi_ PAaJ AKib Vd." 52 53^ UMDeePLOvV HOLE |fO KCFllK IMLtT WElR, 54 55 15-A)A>-^.m All laa/oujArR l'fr.tiCIAllt- 56 SPEC BY vj Aw 1t CHECKED: jtf.p APP'D:/^ ffj/* 7 THE DOW CHEMICAL COMPANY HCl Col O M K EQUIP- C "N T-* = SPEC A I- I4-I-5300Z. NO. DATE: 7_n_C=>7 REVISION DATE A B C ToWUR. VENDOR TO COMPLETE ALL APPLICABLE INFORMATION NOT GIVEN V PURCHASER 2 5-430 _6ft SHEET 3 F V SPECIFICATIONS ST0415800 y n q l *i PLANT CYSTC'i CeFP.lL. "Pi- A fJT i * MANUFACTURER $S<SlA-B.Y)C<?~ b/mno. 5^4f-%3.cm P.0. NO. _1_ 2 3 l4.) Twv 4 5 6 7 g 9 10 11 12 13 14 15 16 17 ia 19 20 21 22 23 24 25 26 27 28 29 30 31 32 FILE NO. | -, -1 JOB NO. 5^5002 CHARGE NO. C/> --*4 o 37 |S.^ UpPC- Sec-TIOM cf TH-e CO l_U FA M OPe^TES A-T- Lo W - 38 -p<= (2.Arue.e. a^d w/cl T5.ee3oi<e-e speciftL 5reEu. Te M?eftA - 39 40 tor.e 9er>piv_G im O'P'Pee. spctioij * 41 42 43 44 45 46 47 48 49 JO 51 52 _53 54 55 Temp, t- 56 SPEC BY s|kW CHECKED: ^ APP-D.rflt iVj/' 7 THE DOW CHEMICAL COMPANY HCl CoLUfAN EOUIP. NO. T-2SO no!0- a 1-141-8300,7 DATE: 7- J/-=7 REVISION DATE A T-/-6 7 evVENDOR TO COMPLETE ALL APPLICABLE INFORMATION NOT GIVEN PURCHASER 2543O a-96 B C <J_ /* SHEET OF Towe^ SPECIFICATIONS ST0415801 c PLANT OY^TC? manufacturer Cb.CIL TT'AM f A'O-! a/M NO. _// P.0. NO. K*) O^iT . FILE NO. -0- - - JOB NO. ^3002.. CHARGE NO. 3gfit ST04 I 5802 H,) j,FreFABRICATION) OF CduLmrO A,h\b "PR-lCiR. To I^^TA l_bA - TlOfvl OF TRAY^, OOL.O FA M IUTCxMAL ^UUL IS TO B Io <C LCA KiC b OF l^iu, SOA l A/oTi A 'PROTOCTlue COAT1O61 A?^Ll.G0 \NAM0Q l ATLY Vo THE SocH CoAtmJCn (exAMPce ClEiSOftPACSS. iTIZ.1 C->) 5AOUI.D CATBA-B l of e/AS T m O vAl pteoTj AFTeR. E2.gc.ti onj . WiTH WATG e. I VO T->4 (E \S-)Locate, kjesoicee. vAFore. l/met tRay towMeoMefe. from bottom 1^.) "po yiDE. LA"DDe:fc_ to lEuel Me~rE.S-.-b Atot) /U.A2.M5, 2& ) T3o w ^ Co clgar.Amaes vo "fee ty?'^ iM. , I \ M Ax. f-ieiGHT of oveeFL-oW wefe oh Bottom ^gal ?an r 6?,/- t SPEC BY 7 / W V CHECKED! wo-.jtjleT Ej THE DOW CHEMICAL COMPANY MCl Columm EQUIP. ' "\ T"-2 no!c AI-14/-83COZ. DATE: 7-- 1 1 ~ <0*7 REVISION DATE A VENDOR TO COMPLETE ALL APPLICABLE INFORMATION NOT GIVEN BY PURCHASER 2B430 S-e B c SHEET _5" <>F 7 TOWifci SPECIFICATIONS ST0415802 PLANT 6V3TCPMANUFACTURER FIELD ERECTED CSfcC.,'. pLA/JT ' B/M NO. |P.O. NO. NO. UNITS tj r - / - FILE NO. j vJ JOB NO. CHARGE NO. TYPE *' . - - ^ 5 r croz. 3&c> ~z. i Troy No* (Bottom Troy--No* 1) 2 Tofol Troys in Section 3 Tower Inside Diameter 4 Iroy Spacing, inches 5 Number of Liquid Posses 6 Maa.AP, |BK3ZB>^otai^ mm Hg 7 Minimum Area/Downcomer * iq ft a< 9 1< VopordL Trt>y(), |b/hr 10 a T emperoture,*F li z PresH^psia 12 is* 13 ui Density, Ib/cu ft Design Range, % 14 n 15 Ui 16 u Liquid from Tray(s), Ib/hr 17 oc 18 a. Temperoture, #F Viscosity, cp 19 Surfoce Tension, dynes/cm 20 Density, Ib/cu ft 21 Rooming Tendency 22 Solids 23 Oesign Ronge, % 24 z 1 35 17 4-3 '5 A' -4=>" ____ 7L d.'-* Co 15 " 15 " OWE owe ---------------------- -- 5210 NA t-A 4-5 50 4-' --fc" ____________ IS7' Owe difdlo oc 54 it 1.15 -- 2ff &ex> 2B.4eo 29,4e>o .. 44- 2.3 o.es o.fifo o.S4- -50 ff /o To IOC3 cl/o OF 7 14-.ooo 0-65 7C..400 -34- 5(2.6.0 o-ss 0 d0 In 1-2.0,000 44,100 4Z.SOD ZS,Soo I2Z- e- .C 4-4- 23 & -54- o. is o.m 0-47 0-31 0.3 14- 3.2, 57.0 57. & 54.5 IS ^Z.4 ? ------ tdONJfc -- ------- hioUG -- ---S-- -------i-t----------=--70c)l0 T o roc. f. 1 n r>r~ 7 Pi ouj5 ----- - 3 25 26 27 Tower Diameter Req'd at 100% Design 28 Troy Spacing Req*d at 100% Design, inches n Downcomer Area Req*d ot 100% Design, sq ft 30 Actuoi Downcomer Are^Side, sq ft 31 - Center , sq ft 32 Dowcomer WldfhSide, inches 33 Center ,inches 34 Weir LengthSide , inches 35 h- Center, inches 36 Weir Height, inches 37 38 39 Haei UOI Downcomer Clsoronce, Inches Valve Units*Bubble Caps/Troy Sixe/Type 40 K Perforations/Troy 41 42 o3J Diameter, inches Pitch, inches 43 J Hole*5iof Areo, sq ft 44 u Active Area, sq fl 45 Max. Vopor at 100% Liquid Rate, (b/hr 46 Min, Vapor of 100% Liquid Rate, Ib/hr 47 Entrainment ot 100% Oesign, Ib/hr 48 TotalAP per Troy, mm Hg 49 50 51 52 S3 Tj^SiS.M 'VnvJEriP. PO TE. M/V< 1 KUM I'jtlPAC.I T7 A-1------TFigr VAK)t4 "TO________ LIGMJLP___RAT7P5 <S>IVJaJ. 55 56 57 58 59 SPEC BY J AW CHECKED: / < /'' APP-D://^ 4/j 4 7 THE DOW chemical COMPANY 1-1 Cl Colu^ki EQUIP. MO. T -Z5Q .SPEC. NO Al - |dl-85COZ DATE: 7-/ |-6,7 REVISIO N DATE ABC VENDOR TO COMPLETE ALL APPLICABLE INFORMATION NOT GIVEN BV ouncMASEA __ ji IjSMEET C^ TOWER DATA SHEET ST0415803 STOU1580k plant Ovstce. Cec&(. pi-Awr C manufacturer S>5WA-fl-\oo2b/m no. say/- ^JOO 2---P.0. NO. fn'oL.E '/J ~ O 4. - JOB NO. 83002- .-- ^ charge no. 6'bocn-' V a,,* Bi'-e" TfAY SO -1(5 8'-2."Z 78- It' -77-z" iOr.: 7Z'- S ' --3 " --------|(^j) --~3 tCatSIl --1@ .&-***" -t^ay' .ai. --1@ _^al3" -reAT a a-. ; <5i?AOe fsJo-re. 1 ThC5 SiOZ-Z-UE' ELEVATiOtOS A^-^ C.iTi46l 'BDaf.USE CP zS&AUiT'r FEEDS SPEC BY \JAtW sg^F THE DOW CHEMICAL COMPANY CHECKED: ^ f APP*D: fi& 2/lki HC _ (SoluMki DATE: -7-H-47 REVISION DATE A VENDOR TO COMPLETE ALL. APPLICABLE INFORMATION NOT GIVEN BY PURCHASER B C f f^ _ _ "T SHEET OF T-Z: NO? A-1 - |4-I-S5oo2. TO^^~ SPECIFICATIONS ST0415804 o T U4 1 bbUo S5WC-.2? u PLANT JVSTEfl - ^S5-/iA-% ?r:~CTGEEKl PiAAJT /Uo . 1 B/MNO. <4// - y^cL n.-------- manufacturer P.O. NO. FILE no. 1 J _ <04 -- Z. JOB NO. S.Z.C.0 7. charge no. y 30 0 z. TYPE VALVE TR' -f FIELD ERECTED rroj NO. UNITS O Op. Preae. Pat, Press, ISO Op. Temp. pit Dpi. Temp. Mox. Allow. Press. (Naw & Cold) 3<> O Liquid Sp. Gr. J . o4- 4flO Contents Lethal p si g; Limited By JE&1 TOWER SKETCH Hydro. Test CODE p*|g j Code: A6>ME Corr. Allow. In.: Shall ; Beads ______ C%) Stomp _E2_ RodlogropK C ODE Joint Efficiency %i Shell ; Heads Sfraee. Ral, CODE Intulolion Cz\ | Sal f Supporting [Y esf "Hff Sondblosh Y'E Fireproofing; 57*214- OUTSIDE SfelgT Pcdnh57 24-7 SP Monhole; P>otform Clips: Pipe Supports: Vers YES Ladder Clips: Insul. Rings: VfeS dfi4- Wind Lood: 12 5 MPH + NOEWAL Opg^. ~P&E.SS. SKippinn Wt. Troy No. Of a Spoang lb I W(. Full Typo Mot.rial Troy .In*to!lotion lb 1 Thru Z 14 tf-tfebt 2 Thru d 54- ZO 4 Thru /2 54 2.0 / Thru 2? 4-fe JC, Contact D.vi co: Buhhl. C. V q'l v. s^ i VI cmStv- Remevobl e Troy Manway \5!juuppppoo rtT?Vn g [ s Monwoy Site ' Weir Sat. (Above Floor) 2. In. D..crib.: MONEL VA LVf5 ON Ad[ustobIa to ^ TD In. Steel ~T~~2 aV-^ - TRAYS_________ |(Adj. slot, s.oi.d ot aii sth^) gfigfcfceg; i ~7 ~rL'gcr>LJgh4'ZZ MoMfL Y. OaJ MgNeLD&K Demi star: W*NIt Item SKafLTop Thickness Mot'l Cl o in. Motoric! - Minimum Quality C. 5T-, In termed In. Bottom Haods* Top Interned In. 1 -IN Bottom In, Lining In, Hco- Hossle Nodes FI angst Coupling M.H. Coyer Skirt Bolts/Studs See J.I. C^TEEL S^EPTfe) Ixo A-1^,1 c S T<-- Hot u^SE Q-Stl ^-STL A-HT*. ^A Nuts Nos. Goeliats j-M&q oeE^L Troy Gosh at s A-s i^g<.-r<gs Sarvica Mk No, Si1 Rtg Type Service Mk No. Six. Rtfl Foe. Typ Feed Reflux OH Vopor Btms. Out R^ol V<sv ffcfal Llg. 50 Drain W SI Manholes 52 Mandhofei 53 Th. Wells So RE 8 Pl RHi.l .aval Coit /2 Z4 * 0 Semple T51F" -r ifl FEETp FEED l Q ei LEOAlA. T 20 0 jfPCEU. V-- U 0-z- IO iso RF igo RF a yi -FT ISA F ISO gr_ o /5o RF ISO SE. rr *rif 54 Pr. Cages L* iro RF >iL BlinpR-AsIse A-Z'V'-i, 55 Goga Gl. gr^.?-i,S-3.L-l.K-Z.. !<:-! specbr\jo$ THE DOW CHEMICAL COMPANY CHECKED: /' APP-Dy<//^rf/v/fc7 RECYCLE 66LUMU T24^) .___________ J- <N J-`"(o) 'tTT H'O' EQUIP. NO* T-2Ao no!cA1- 143 -s 3002, DATE: 7-||-61 REVISION DATE * ENDOR TO COMPLETE ALL APPLICABLE INFORMATION NOT GIVEN BY PURCHASER 1 4030 3-00 B C 4-4 -Lt TOWER OF SPECIFICATIONS ST0415805 ST04 I 5806,-y CALCULATED RESULTS S5<V;f - PLANT oiSTBK C RE ET^. Pi-AAn A B-'M NO. 5^Z_ 'ci; manufacturer P.O. NO. c FIELD ERECTED YfcS * Troy No. (Bottom Troy=No. 1) TnoI NO. UNITS i Ar 2 Totol Tray* in Section 3 Tower Inside Diometer 4 Troy Spacing, inches ^ 1 P4Z-*4- S'420 5 Number of Liquid Pastes OKE ome & Mos.AP, peeWsa^totol, mm Hg l o *><o 7 Minimum Area/Downcomef , sq ft FILE NO. . J * 0^4- " 2 JOB NO. eroo2 CHARGE NO. /?3QQ Z. TYPE v/a LVE TTZaY c& 7_________ ,2o ONlS -Z.4= A_ Z 04- 2.0 nvJG 2.0 * 8< 9 1- Vapor to Troy()m lb/hr 10 o T mpeeature.'F 11 z Pressure, mm Ht^peee 12 13 iU Density, lb/cu ft Design Range, % 6,00 342 Ce 340 1 <4-0 S' ^OO 34-0 ^7>o l 1-54 OT 7=7 rivN "5 -T a A7o>C3 3,2,62* <>26-2. 1 - 3ft Maxiwon _______ 32^ ^262 1-3.-2. - 14 15 Uwl/nli 16 u Liquid from Troy(s), Ib/hr 17 oc IB L Temperature, *F Viscosity, cp 19 Surfoce Tension, dynes/cm 20 Density, lb/cu ft 21 Fooming Tendency 22 Solids 23 Design Range, % 24 /7<S? *7oS> 3-4-2 Z-41 *3 <2>2.S KIONE --------- Sio *Io T 1 "7 <> 250 ^46? 2*41 *9 to'Z. S' HoNt OC CU'>VJ^ 174 , 065 336 .2S _________ 20 <> 2 .T M o Kie K 1 "> MAXI 14 UF 1 <ST 060 72.7 Zo 63,t NJ OKI Ft -----------------k. . 25 26 27 Tower Diometer Req'd at 100% Design 2B Troy Spacing Req*d at 100% Design, inches 29 Downcomer Areo Req'd ot 100% Design, sq ft 30 Actual Downcomer ArrwSiJr , sq ft 31 Center , sq ft N 32 Dowcomer Width$ide, inches 33 Center ,inches 34 Weir LengthSide, inches 35 Center,inches 36 Weir Height, inches 37 Downcomer Clearance, Inches 38 Valv. Unitl-Bubbl. Copv/Tray 39 Site/Type 40 Perforot ions/T ray 41 Diameter, inches 42 Pitch, inches 43 HoieSlot Areo, sq ft 44 Active Areo, sq ft 45 Max. Vapor ot lOOTi Liquid Rote, Ib/hr 46 Min. Vapor ot 100% Liquid Rote, Ib/hr 47 Entroinment ot 100% Design, Ib/hr 48 TotalAP per Troy, mm Hg 49 50 51 52 53 ehpct deeaTE. Amount c7F AfiOkJ 54 <5F MAT(?f2iA/. jnJ P/5TTOt-*\ ACTION C>F C^LUMLi 55 LO 56 UJ 57 o PettskStm 1=072. F? s7a DP f=t.oejT5 kiAk. A-t- max. Flow 58 lA="Sl& M TD\WF-L FOE. (AdKIMUM r&'?A|TV AT* TUP l/A'Poi? Tn 59 ______ UQUO RATIOS____ osi V/gNj .__________________________________________________ __________________________________________ __ spec by VortfeESS. CHECKED: ? PP app-d^^t -p/74? 3*^ THE DOW CHEMICAL COMPANY T-24Zecycie Column o r-. T-24>- SNOPE!CC.AI-143-85002 DATE: REVISION DATE A d-4 -C, $,,___ VENDOR TO COMPLETE ALL APPLICABLE INFORMATION NOT CIVCN B> l*URCHA5q B C ; |SMEET ^ _ OF TOWER DATA SHEET ST0415806 ST0415807 ______________________________________ -j-- >rc- .----------- PLANT OYSTER manufacturecrd CRS-&K PLAiQT A.<|b/>a no. IdP.On.kNjrO\ . cj//ft - ZZ&ci- FILE NO. J-o4-~Z JOB NO. L3001, CHARGE NO, Q 3 00Z- FIELD ERECTED - NO. UNITS C?KlE type VALV& TT2A''</ 1 Troy No* (Bottom Troy=No.l) 2 Total Tray* in Section 3 Tower Inside Diameter 4 Troy 5pocing, Inches s Number of Liquid Posses 6 Mar.AP, po H>eyitotal, mm Hg 7 Minimum Area/Downcomer , sq ft 12 A SA - Zo <> K-l AG 1<S> A Ae> \<z> oME. AG 22 ___________ <J2.____________ - 1 __________ __________o> M ________ GO 8< 9 Vapor to Troy(s), Ib/hr 10 O 11 z T emper oture,*F Pressure, mm 12 13 Ui Density, Ib/cu ft Design Range, % M IS t/i Ui 16 o Liquid from Troy(s), Ib/hr 17 ct 18 0- Temperoture, *F Viscosity, cp 19 Surfoce Tension, dynes/cm 20 Density, Ib/cu ft 21 Fooming Tendency 22 Solids 23 Design Ronge, % 24 <J> A9CO Z ZA- 6223 1 . 0<> --4------- SO el a / OF <5-A G\&A |. OG 5=N-ONM -F TO G5-OQ&_______ 117_______ 4.1-2 <=> Ml iss: c3.00 -Z.-ZA- 32. . Z.I __________ A G.G klOMC MO Kit- <-- fxO ala nf - *5 'Z. ooO 2. 1 T 2ft l<2> &S. A NOME NOME t= i ow - m 'Z.'Z&oO 11 "7 \G None mone MAX IMG ---- *- *s 23 26 27 Tower Diameter Req*d ct 100% Design 2B Tray Spocing Req'd at 100% Design, inches 29 Downcomer Area Req'd ot 100% Design, sq ft 30 Actual Downcomer ArecwSide, sq tt 31 Center , sq ft 32 Doweomer WtdtfwSide , inches 33 Center ,inches 34 Weir LengtlwSide , inches CALCULATED RESULTS 35 Center, inches 36 Weir Height, inches 37 Downcomer Clearance, inches 38 Volve Units*Bubble Cops/Troy 39 Siie/Type 40 Perforotions/Troy 41 Diameter, inches 42 Pitch, inches 43 Ho)eSlot Area, sq ft 44 45 Mae* Vapor ot 100% Liquid Rote, Ib/hr 46 Min. Vapor ot 100% Liquid Rote, Ib/hr 47 Entrainment ot 100% Design, Ib/hr 48 TotolAP per Tray, mm Hg 49 50 51 VZ.52 1 __ ______________________ 53 I.iwlex WEIR ON -TRAY44 To e> 12." HIGH. 54 55 to 56 UJ 57 O 58 59 spec BvVonTeess CHECKED: J / APP-D0G ^/4? THE DOW CHEMICAL COMPANY T-2doCRecycle oluviu EQUIP. NO. "G240 SNOP,E!CcA. I-l43-83COZ DATE: T-ll-Cl REVISION DATE A VENDOR TO COMPLETE ACL. APPLICABLE INFORMATION NOT GIVEN v PURCHASED B C { --_ |SHEET OF TOWER DATA SHEET ST0415807 plant oTstse. <^kee k MANUFACTURER i'Ty/it-F.'L'-L dstjiA-frinrL:l_ PLAA/r ^>i b/mno. KA//'^,r.oept-------- P.0. NO. FILE I NO. job no. 300 2. CHARGE NO. 8 3dOL 4 N --v Motes; 0 Locate LEVEL COWTK.OL, LEVEL ?R.eSSU?.E (SAUS E. $ A~P cell tMozzues TeerioiuepL v/vpotr imlet 2) LCRR0510-kJ AlloWAMce Fore, she'll *c HEAD A6ove T1ZAY I <2= To BE. 3/^" g) LOCAtc CCLTEE.Li K->E OF ^EftCULE^- VAPoR. IMLET KiO^Z-LE TAK.ALU5L TO "BOTTOK SEAL. PA-sJ OVEE-FLOW WEiZ. 4-T Low^ RADIUS ELI-- MorLE S T 0 4 15808 x 7O WELD IN 2 ASl^LES IMS IDE. COLUHJ ISR'LOW manhole m-2 foie -scaffold supp^ET' see J.I, 27 P/EoviDE WA TET2. NO^.TELES pOE. F IT2.E 28 29 PROTECTION no so FT ATSsOv'E BASE.7 AUD WATER, 30 im-Sioe: -svnz.r Both at ea te of 0.2s 31 32 cpm pee t=t. 33 <2>) USE MO SCREWED COUPLINGS <=>kJ PROCESS SIDE 34 35 10) tpat specs : 36 TRAY NO. 37 36 Dhoc 1 THRU \<. 17 Thru *22 C- STL tcBWCMlM Monel <2 Bv/tf mim- 39 b. VALUES MOMEL 1C EVV<5 MlW MtfMEL IGBW^ Hid- 40 4 c. MahWAV ^ TRAy "Bolts Mohel M-snEL 42 43 4 e. DO MOT PEED IN bOWMCOMEES, 45 46 f, PPoVlDE 3/g" <p UNDERFLOW WEepAOLES AS REG^D. 47 4B TO PR.A1N COLOMM. 49 50 q. TC2.AT t)EFUECT<o>J At dOpeeAT\Klfl' <C<ONDUT<C?lJS 5 '/0' MAA. 52 53 h mawwaTs: Modulate comsteucticM But not 54 LESS THAN )2.mX\<S". TRAY EMTIRY FR.On4 BtUW li AND A0OVE. Mam WAVS AU&MED V^TlC^LLY. 56 SPEC. BY CHECKED: jf /^ app-d^cT Kty'.^r, SSP> THE DOW CHEMICAL COMPANY T^ecyclt. Colu-mM T-Z4-0 EQUIP. r I Tv?A. f&AM43-8300Z DATE: T-| 1-4,7 REVISION DATE A VENDOR TO COMPLETE ALL APPLICABLE INFORMATION NOT given bv purchaser B C t sheet ^ _ of >*.. T~ovmeL SPECIFICATIONS ST0415808 Ssu/A-Bior^PLANT <T?VS-ruE 02.6Ekl PtA/UT jL'o. 1 B/M NO. /5V/ - g"J-a o L-- MANUFACTURER P.0. NO. FILE NO. \^ -J Oid ~2 JOB NO. Q^OOZ- CHARGE NO. S^OO-^ J_ 2 0 All THEKMOWELL5 LOCAT"E"D |N VAPOE SPACE. 3 4 1^) I5UIUO PLAkJ<SES 5 A-Z, H-l} W-Z, K* Z - 6 (?*2, S-3, L-t 7 /2) 8 9 10 11 12 Smell 5.24-1 (Al-124-gSO QZ) 13 14 15 16 17 18 a / > -SHELL- T-24-O 19 20 T)esi<S'^ plate poe. 5psi LiFFeK.5NriAL pressure 21 Plos 2/p" coisHosion AllowamcE. total. 22 Do LOT PP.^5E(JP-6 TCET SUSIL Ak-Oo gXC.I-1 AnJ 23 24 <Se=~K_ JMeLL CSg~p/Af.fe~reLTf 25 26_ TowEC SHE.LL FAa'P.lC^TOl^ "TO FA6RlCAT(= "TO AKJtJ 27 ikjcluuinc-, come tR-Amsitioh piece , 4S " pq 4-3* (5Veo. 5he^t Al - |Z-4--05oOZ.) . ^uq.i_ of El-24/,* 30 5UPPUED BY 0XCHAM6,E(?. FAB-EICATo^j SFOOLD 31 Be wuicL to T- 24-0 shell. REFoee SHiPhEMr; 32 33 34 14.) Dgsi&k Foondayion FoS. tsuelj_ Full OP lA'Arre'_ 35 36 IS) Dow*J6ower<: CLEARAMCES = _37 , l max. 38 \to) Bottom se^vL- TAm BetAtu 39 -f 40 41 42 43 44 45 46 47 48 49 50 <t op (i6oiue4 wwr _51_ 52 5 6.At- UJC'L. TD -hi pftALX*6L Yb 53 M J55 56 SPEC BYs/c^ \ejESS CHECKED: ,/ APP'O:/^ f/?/^7 <2>* THE DOW CHEMICAL COMPANY T2BCYC.LE Columm V-Z40 | EQUIP. NO. |T-2*4.0 ScAI-l4-3-S300Z DATE: 1- 11-61 REVISIONDATE ABC ByVENDOR TO COMPLETE ALL APPLICABLE INFORMATION NOT OVEN PURCHASER TT sheet 2B430 3-.BA O^_ _ or TOYVf2. SPECIFICATIONS 608S IH I1 ST0415809 2101*12810 5T8Hl5 [plant OYSTER. CREEK MANUFACTURER MASH M-d- FLAM r'No. L ________S__?_ /YA-3iftf/ B/M NO. Q- i P.O. NO. QKJE UN-JIT <ONl I---l" VAFeOE: -30 U5./W2AIE. PLUS 2<5& US/MJ2. J *FILE NO. Z JOB NO. Q 300 2. CHARGE NO. cTOMFLDUtUT S PW'YS terAt. Pe^>'PE'R.TlES 4?P ^MPoUeUT & Mol wt. 1.^7, Cvy -Z^s .1 *<Z P* 4*9.2 ATM Tpmp vapoz peESi latejJt Meat] UQ.viscasrc/ liquid Doj .VAPOR SP. MEAT UO SP. MEAT ~C mmU$ Ais l^aL/MHCll.<:WTlP0lSti 4H/ML. cal/'t Mol CAl/i: <SM Mfil o 23 to 4-0 20 30 \ os. 4.0 161 SO 24/ 3.45 S.Z1 ,-07 /. /A i <p.>4- <O.G>S /. 2 7 /. 25 A 24 /.2Z. /.2/ /e>. o 52. 3 Flash Poikit j r.c. t'S.cr,, O.C. I>.3c:., XPLOS. LIMITS .2-15.1%, opgJ2AT/M^ ^oMorrioius -OoviDlTiOfJ PJZ.E 25U/ZB FLOW IJU1T //-/ {J* a &S- AA / W/e j Kl LT 740 40 7 35 OUT LET <27-S 4^4 /4v4X. FtxUp. ' IS SPEED : 7600 07so) ZRpf. MOT0&: 44o , ~3 r/JASZ, 450 'L', DjPECp SZDiJPC'pjwiTH 6UMd P/OXBAL JJJOUC T/OAJ SPSC . 75 - 703Ce*cys-h /.o s, F, ^EAL LIQUIDS Seals MATFlZf AL$ <9 0 Liquid qomp^ueut j- Temp is.&'c PEE5SUKE 20 pst<? {OZ AS PEOUIPjBD) 6AL UOUID IfCCULATED Coe uED *SEA L FLOsV MlOU T ^ d"PMV- MecHALUOAL.. All ieonJ ^tasf 4crcDME, lioduuiz je^o ROTOfi , CK^LOvJALLOY> STE-EL SHAPj ^T^ei- OE "STAINLESS S'TEEi- 5EALS. DO MOT USE TSfcQM^E TO BE MOUNTED OM BASEPLATE AMD DIRECT COUPLED TC rvfoTORL AT VO (JR. PACTO^V'. ffnuthes , VEMPOP W t u l. ^'pecifY FfcAMe/^E ^ DtEEOrfoQ OF/gc?TATioO SPEC BY VN 72ESS THE DOW CHEMICAL COMPANY EQUIP. NO. c-zo CHECKED, VACUUM PUMP C-20 APP^/4//^ f/^7 P^e T- 20 SPEC NO. A I-J5= 63^2 DATE: REVISION DATE J.U.T Ulfltt- VENDOR TO COMPLETE ELL APPLICABLE INFORMATION NOT ClVCN BY PUWCMAHH 20430 |.tl f VACUUM RjKP SPECIFICATIONS ST0415809A PLANT GV^-rK C^ErK- MANUFACTURER FIELD ERECTED YES PlAMT~ Uft 1" B/M NO. P.O. NO. Ino. units Operating Pressure 2 psig OperoHng Temperoture F *2 Liquid Sped ft c Gravity Contents Lethal Y.. TFTSl Design Pressure psig Design Temperature *F Mas All. Press. (New&Cold) psig / 70 SV co-os- Llml ted By SHELL Hydrostotic Test psig _fiy gogg__________ Shall Shall Heods Corr. Allow. in. Hoods Joint Eff. % 1/lCo '//< Cod.: As NT EE Stamp ^Y. | P .S'- Radiograph: T Stress Relieve; 14 Typ. Support.: L-g<S-S S&Z&-3 gVA Insulation: Fireproofing; Sondbl o.t: __________ MO/vJE X*5 | Pcinh J "* ^ 4* 7" S P Oth.t. goLTEP Plotform Clip.: MOKlE |l odd.r Clip: h)0Nfllnul- R'"8'NPAfE Pipo Support*: Wind Load: Wt, Empty Horn Shell Heads Lining MO Si E Hi PH Sei smi c: NOME lb. Wt Full Thickness Mat'l Cl ass Mot*I Minimum Quality in. ASTM ^r- stl d < in. FILE NO. JOB NO. CHARGE NO. total volume ^ ---Vi ZOA SVL L W7 '<T Neixle Necks, Flanges Coupling ASTM A \ 0Ce> ASTM A-IP.I St i--. M.H. Coyer Supports Bolts/Studs Nuts Gosh els ASTM A --~7 AI?3-67 A l -34 - 2M JM -- C>o 37 Service Mark No. Sf xe Rating Face Typo VAF&g our A / 3 /5tO &F 40 \>APCK /V B / J<o PF V--* -K-41 z_y<? &u-r C / 42 P&AIAJ P* Z__ 2' /&? jEP * -K~ Lf=)/L COMT E 2 /^sro JEF MWHOLE PRESS. G6t PS V LEVL MAEM 'TemP INLET F*| G H J K L l / / / f l AS" /&> ISO it ISO Z /So _2_ f So /SQ XF Rf RF /?F R.P Kf- X% * + It X x-te- M N P 0 R XX \/N0<O/Z <nPTiC)Aj FSSQ&FShn * No 1 xl. to b. Pluqp.d or Bllnd.d. For Further Details, See Sheet No. SPEC. BY L?// TfeSS THE DOW CHEMICAL COMPANY EQUIP D- 2. CHECKED: /tty-' APP-D: ^ SGPAZAT&Z OgUM & C-2.0 NSOP,lECc'. Al- 49-8300Z PATE: fc/(tfvL REVISIONDATE 2 3-/S-6,77 BYVENOOR to COMPLETE ALL APPLICABLE INFORMATION NOT SlVFN PURCHASER V1 i^?-ZfcC-w > i t /iI^etc-t ] | fc. fc. 7 Or f VERTICAL DRUM SPECIFICATIONS ST0415810 plant ^'KSTEfZ CREEK manufacturer "7S K VVDUTV/UNIT ST 04 1 58II* APi. I.: -/ b M no. |P.O. NO. =* TWO (3hJE.Ino. units shells/unit no.e j-o4-;. f 3JOB NO. CC CHARGE NO. fiZ C ~ _ tema size/type r 41 Thru-Omni RllUJiPncfccif FTS i Hh En Th. d syphon 1 H oi rninj^ Additional ProCe Data on Sheet No. Flui d Totol Flow lb/hr Inlet . SHELL SIDE - OuHef WATE-e Inlet - TUBESIDE - Ourtef Liquid Density Viscosity Specific Heat 10 Thermo! Conductivity 11 Vopor 12 Mol Wt Density Ib/hr Ib/cu ft CS-CP Btv/lb- F Btu/he-sq ft- F/ft lb/hr Ib/cu ft / / / / / / / Vi teosi ty CS-CP Sped fic Heot 15 Thermal Conductivity Btu/I b- F Btu/hr-sq ft-F/ft 16 Latent Heat 17 Non-Condensobl es 18 Velocity Moi./Min. 19 Norm. fMa*. Operating Temp. Operating Press. (Inlet) Bfu/lb 1 b/hr ft/sec F psig M.W. = 3>~J 1 JSD S3a 1 -ZfO / / M.W. =\ W 21 Pressure Drop > psi Allow. Col e. AJ4ow Cole, \ 22 Film Co.lf. WATTT/S& IN HTIIfH cl ^" 4o MAX 23 Fouling Resistance, hr-sq ft- F/Btu; 24 Ov.r-all Coefficient- '`U'o Btu/hr-eq ft. F; Cleon 5ervi ce LMTD (Corrected) 25 Inctulled Areo/Uni* ,q ft (Outside) In eluding-Excluding. Area in tube sheets 26 27 Desian Temperature SHELL SIDE F 3^0 TUBE SIDE Shelf ID (Approximate) T^ttksjubes (Approximate) In. jt^000' 28 Tube In. | Tube Gage BWG Hydrostatic Test psig z-rz. s Tube L engfh*Sss^ ft X Corrosion Allow./Lining 31 Number of Posses 32 Insulation 33 in. */i Co Of^tm <5 Tube Pitch [\ rT^S< Joint Molce/Type Fintubes 4"Ss^ No. Fin* /^psr hibt; ''Vvs^ In. per In. FIrs HeighIn. | Fin Thl dt."'s',v^ In. 35 VosseJ^Supports Saddles - Lugs Other; "'NsnSw 36 JftHfTr Height in.; Shell After Weir inT^^s^ 37 TEMA Close | L ethol Yes |Code Removable Bundle^ | ASME) -- HuIUhiuI Ooultf --Qlffr I Stamp Spot Rottogroph; Shot I Shell Cover Channel [stress Relieve; Shell Shall Cover Chonnol Floating Hoad M A T E R IA L SPECIFICATIONS 40 Wei ght CompI efo Empty/Foil of Water 41 Sandblast* | Paint; 42 SHELL SIOE 43 Servi ee Mb Si ee Rtg Fece Type Mk 44 -J Ini et A 2'/? /&> RF FS 45 Ui Outlet 46 kO Drain or 47 UJ Vent a. 48 49 UJ Ni X SI o Pi Vh /?<? PP FS. | Maintain TUBE SIDE Size Rtg Face Type 1 Woight Buncfl e Only Shell ID Tube Count Installed Are at % Tube. COPPEP SHEATM Chan. Nox. Necks -- Stot Tube Sheet C ^ TC Chan. Nox. Flonaes - Fltg. Tube Sheet Channel Flanges Cress Baf,/Tube Sup. Fltg, Head --- *9? ^ Lona Boffles Impinge. Baffle " Flta. Hd. Flanoe Clamp Ring ~ Weir/Lift " Tie Rods & Spacers Shell C STL- Shell Caver ^ ^TL Bolte/Stud. A\4S R~7 Nut* A 4- Z H Vessel Supports C? STU GASKETS & PACKING 52 Chonnel She! 1 Co vor S3 See Noxxle Sketch on Sheet No. Ch. Cover/Bonnet -- Shell-Chan. Side 54 Shell Side: Parallel Bonks of Shell s In Series Shell Nox. Necks ^ S T"L- Chann.l 55 2 Tube Side; Parallel Bonks of Shells In Series Shell Nox. Flongas P1 Channel Cover 56 O Stacked: Wide High Shell Flanges ^3 Fltg. Hd. ,, s' Ispec by V0M 1T2EST THE DOW CHEMICAL COMPANY CHECKED: / / ft ELECTRIC: VVATEK ueate APP'0: EQUIP. NQ. C267A5B ,^1-^2-83002- DATE: REVISION DATE ABC VENDOR TO COMPLETE ALL APPLICABLE INFORMATION NOT Given by purchaser __ sheet or Z heat EXCHANGER SPECIFICATIONS ST0415811 plant CP.OVSTee FFJ4 PLANTAA>./ B/M NO. ( manufacturer P.0. NO. no.e J-04-2 JOB NO. JTiooZ, Q 3CHARGE NO. OC>2^ ^ 1 2 3 4 5 6 7 B 9 10 11 12 13 14 15 16 17 IB 19 20 21 22 23 24 25 26 27 C 28 29 30 _3i _32 33 34 35 36 ELECT*1C WATER AtEATEg TWO UNITS 1!4W FACfl 440 V CO ~ 3 PJ/ASE MAX DE-KIS rTV, 40 VVAT TS/$Q nJ. tTLASS I DIV.2 tfOUPD i TOE THERMOSTAT 4 TERM/HAL COVE/?. SUPPORT LU6S ST0415812 37 38 39 40 41 42 43 44 45 46 5ee EtsWfKi U. nNE'IcjAslD CO. PITTS'&UEdH, PA 47 CAT. (CO PG.3C SEdTioM B. 48 49 CBR.OMALOX ClfZCU LATIOV4 USATEE. TYPE NWH"> 50 51 32 53 54 55 56 SPEC. BY YOhl T&E5S CHECKED: jf ' f app'd= /bf THE DOW CHEMICAL COMPANY ElECTZ\C water 14 eater "QUIP. KJ ^N. E2&7, , ho^AI- \<]2-B30D-i- DATE: r-3-^7 REVI5IO N DATE ABC VENDOR TO COMPLETE ALU APPLICABLE INFORMATION NOT GIVEN SV PURCHASER 2S4SO s-ee /SHEET ^ _ -y OF W EAT t<.CV4/LU<Se-T2 - SPECIFICATIONS ST0415812