f ~iddixon/cbe_433_pid.pdf · p-1741 h-1741 115'00 170 •• yes es , 4, '2 44 5 85 40 -...

3
1 1<8-230230 ~ @rC;V @ ~~0 1 FROM VENTURI SCRUBBER TRAIN 1 I Alt-2J02JO ~ @][ 0 f ~ @rC;V FROl,fvENTURI SCRUBBER TRAIN 2 I AB-2J0230 ~ ~][0 fROW WASTE HEAT BOILER TRAIN 1 I 1<8-230230 ~~~ "AO ••- WAstE HEAT eOILER TRAIN 2 I 1.8-230230 e-+ "9fE 2 F " ,'3 0 .. :' 22 ~ OXfOATIOH e-1 10"~RB~'ll'E" FROW OEIONIZER NOTE 1 l '. " ~ 0- ,e EFFLUENT TO Ncepw SEW ACE F"CIL.ITY ~. Hi~:~~~~1R~ €3 1ST WASTE ,NEUTRALIZER 0p@ ~ 1ST HOLD TANK" PUW' 2NO WASTE ~NEUTR"IZ" kv f&€ ~ 2ND pHC NEUTRALIZER HOLD TANK s: 2ND HOLD T~NK PU';;P r- ~ CAUSTIC -TRUCK -J c. -- - -- ',-: ~i e®~ I CAUSTIC: I TANK I I 1---- d=':J lEGEND: ~ o .- STRE"''' NO. 0 - TEMPER •••TURE, T 'It 0 - PRESSURE, PSIG .''1>. ar - FLOW, CPW ~ -- 14 14 HOTES: 1. BASIS IS 320 1.8/W'N. OF 10- WOISTURE F'EED PER WODULE TO CALCIHERS. 2. FLOWS TO 8£ R(STRlenD TO LIMIT EXTRANEOUS 11,0 rRO" 1313 -'3'3 [NTERING PROCESS. ,. " 3. WA)(IWUW COO TO aE 30 Ppw. 7 7 17. ". COMPONENTS'IMOLECULARI ST"'HO-~415_..l4-lS-'lIl 424 WEIGHT . 05 1 "'I CAUSTIC SUBMERGED PUMP 549-I 549-31 701 I 702 I 1704 I 1706 10 10 20 7 7 ,. 10~ 10S 210 8" '3' 12&& 7 7 ,. ''11:.'' 0, §. HaD{v) CoSO.• CoSo.-2H,:O W,O WolOHlt N9S,? WgIHSO,)% lroIgSa,. S10% 32.0 LaS.lHR j, 709 710 711 712 713 714 715 O. 2.0 20 20 20 1. 1. " 1. 106 ". 210 . 21 <1 1254 12U 1264 lJt2 ,. ,. " " 12. "2 7 2~ 2. 177 38,816 usa 2.' 3S,279 27 39,310 3S,071 17 <1 " 32$0 •• r.o, ••• 13,000 3'40 40,171 36 40,'07 -40,701·· 1 70 "1 20.120 .$/0. 10.1'2 0.1/0.2 80.192 .O/I~ - - - - - - - No,SO, ~ 111.0 LaS.lHR L:BS/HR NOiSO .• 138.1 LBS.ltiR 172..1 LBS/HR 40.3 LOS/HR I '" ~O(L) 18.0 L8S/HR ~OO 500" 2200 17,823 17,823 35,$48 3200 I I 1$0 I I 1$0 H SO.HOO-' S8.1 LIS/HR " 3 3 " NoOH(100_' • 0.0 LBS/HR " " TOTAL - LaS.lHR ~OO ~OO 2222 18,$81 18,581 37.178 3222T T lsoT T 1S0 ILIQ FLOW,AVC/wAX - GPW 0.8.110 0.8.110 ".5/S0 5.6.14 5.6.14 70.180 7.110 .25.110 .25.110 :VU' 'LOW.AVG,;"'WA.)(. SCFW 4.152 4.152 - - - - - - OCSSOLWO souos.ftH - PPW - ",'I:'!:•• -" .. ~ •• ,'l""....J ---:lW'·;:,ag_1 - 1susI'<J«D_1IH - PPW i ..,~~ '''M~ '''. - - - LlO. SP CRAVITY - Cr/L 0.96 0.96 1.02 1.02 1.02 1.02 1.01T T 1.0 pH - - 7.~ 7.' 1 To 131 p..o T_1.$O T_ 2.SI I I 2.$ t1 To 131 13 To al 13 To a: $8.3 LIS/HR IrlV~144,OOO\'44.ooOf~·rl~'K4.0001 V;t.,.,. I _ I _ I 70~,'U. 1 r- I 7C1"" •. I 70" .• 1.03 1 1.3 To 121 I. 1.3 1 1.03 1 1.3 1 1.03 1 1.03 14 14 To 51 I. Ie To 114 To .• 182$ I 2331 I 4 140,7051-40,705 - , - io.ovo.1eO.l.2Ieo/92 - 14",000 - - - - 1.03 - e6;"1 400/~2/7OC ~' 3 13',074131,07. 104.4 LBS/HR Figure 2.6 Typical process flow sheet. (Adapted with permission of United Engineers & Construc- tors Inc., Philadelphia.) 186.3 LBS/HR 120.4 LBS/HR LBS/HR I \ SO.1 126.t LBS/HR 142.1 LaS.ltiR ~:=-~.~ MECHANICAL PROCESS FLOW SHEET MgO REGENERATION PLANT WASTE TREATMENT ALLIEO-CHE-"'ICAL CORP. CLAYWONT, OEL. ~IU:CTIIIIII:IO. ~~ ••••.......... ~~ AB-230231 I~v 1

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Page 1: F ~iddixon/CBE_433_PID.pdf · p-1741 h-1741 115'00 170 •• yes es , 4, '2 44 5 85 40 - - w a st etre m nt, h no 2 414- 1 4t2- 12 -wl • 170 so yes yes 434 3 70 p-1742 wu< ns 170

1 1<8-230230~ @rC;V @ ~~0

1FROM VENTURISCRUBBERTRAIN 1

I Alt-2J02JO~ @][ 0 f

~ @rC;VFROl,fvENTURISCRUBBERTRAIN 2

I AB-2J0230

~ ~][0fROW WASTEHEAT BOILERTRAIN 1

I 1<8-230230

~~~"AO ••- WAstEHEAT eOILERTRAIN 2

I 1.8-230230 e-+"9fE 2

F" ,'3 0 .. :'22 ~

OXfOATIOHe-1 10"~RB~'ll'E"

FROW OEIONIZER

NOTE 1

l'."

~

0-,e EFFLUENT

TO NcepwSEW ACE F"CIL.ITY

~.

Hi~:~~~~1R~

€3

1STWASTE

,NEUTRALIZER

0p@~

1ST HOLD TANK" PUW'

2NOWASTE

~NEUTR"IZ"

kv f&€

~

2NDpHC NEUTRALIZER

HOLD TANK

s:2ND HOLD T~NK PU';;P

r-

~

CAUSTIC-TRUCK

-Jc.-- --- ',-:~i e®~

ICAUSTIC: I• TANK I I1---- d=':J

lEGEND: ~o .-STRE"''' NO.

0 - TEMPER •••TURE, T

'It

0 - PRESSURE, PSIG

.''1>.

ar - FLOW, CPW

~--

14 14 HOTES:

1. BASIS IS 320 1.8/W'N. OF 10-WOISTURE F'EED PER WODULE TO

• • CALCIHERS.

2. FLOWS TO 8£ R(STRlenD TOLIMIT EXTRANEOUS 11,0 rRO"

1313 -'3'3 [NTERING PROCESS.,. " 3. WA)(IWUW COO TO aE 30 Ppw.7 7

17. ".

COMPONENTS'IMOLECULARI ST"'HO-~415_..l4-lS-'lIl424WEIGHT . 051 "'I

CAUSTICSUBMERGED

PUMP

549-I 549-31 701 I 702 I 1704 I 1706

10 10 207 7 ,.

10~ 10S 2108" '3' 12&&7 7 ,.

''11:.''

0,§.

HaD{v)

CoSO.•CoSo.-2H,:O

W,OWolOHlt

N9S,?WgIHSO,)%

lroIgSa,.

S10%

32.0 LaS.lHR

j,

709 710 711 712 713 714 715O.

2.0 20 20 20

1. 1."

1.

106 ". •210 . 21 <1

1254 12U 1264 lJt2,. ,." "12. "2 7

2~ 2. 177

38,816 usa 2.' 3S,279 27 39,310 3S,071

17 <1

" 32$0 •• •r.o, ••• 13,000 3'40 40,171 36 40,'07 -40,701··

170"120.120 .$/0. 10.1'2 0.1/0.2 80.192 .O/I~- - - - - - -

No,SO,

~111.0

LaS.lHR

L:BS/HR

NOiSO .•

138.1 LBS.ltiR172..1 LBS/HR40.3 LOS/HR I '"

~O(L) 18.0 L8S/HR ~OO 500" 2200 17,823 17,823 35,$48 3200 I I 1$0 I I 1$0H SO.HOO-' S8.1 LIS/HR " 3 3 • "NoOH(100_' • 0.0 LBS/HR " "TOTAL - LaS.lHR ~OO ~OO 2222 18,$81 18,581 37.178 3222T T lsoT T 1S0

ILIQ FLOW,AVC/wAX - GPW 0.8.110 0.8.110 ".5/S0 5.6.14 5.6.14 70.180 7.110 .25.110 .25.110:VU' 'LOW.AVG,;"'WA.)(. SCFW 4.152 4.152 - - - - - -OCSSOLWO souos.ftH - PPW - ",'I:'!:•• -" .. ~ •• ,'l""....J ---:lW'·;:,ag_1 -

1susI'<J«D_1IH - PPW i ..,~~ '''M~ '''. - - -LlO. SP CRAVITY - Cr/L 0.96 0.96 1.02 1.02 1.02 1.02 1.01T T 1.0

pH - - 7.~ 7.' 1 To 131 p..o T_1.$O T_ 2.SI I I 2.$ t1 To 131 13 To al 13 To a:

$8.3 LIS/HR

IrlV~144,OOO\'44.ooOf~·rl~'K4.0001V;t.,.,. I _ I _ I 70~,'U. 1 r- I 7C1"" •. I 70" .•

1.03 1 1.3

To 121 I.

1.3 1 1.03 1 1.3 1 1.03 1 1.03

14 14 To 51 I. Ie To 114 To .•

182$ I 2331 I 4 140,7051-40,705

- , - io.ovo.1eO.l.2Ieo/92

- 14",000

- - -- 1.03- e6;"1

400/~2/7OC

~'

3 13',074131,07.

104.4 LBS/HR

Figure 2.6 Typical process flow sheet. (Adapted with permission of United Engineers &Construc-tors Inc., Philadelphia.)

186.3 LBS/HR

120.4 LBS/HRLBS/HR I \SO.1

126.t LBS/HR142.1 LaS.ltiR

~:=-~.~MECHANICAL

PROCESS FLOW SHEETMgO REGENERATION PLANT

WASTE TREATMENTALLIEO-CHE-"'ICAL CORP. CLAYWONT, OEL.

~IU:CTIIIIII:IO.

~~ ••••..........~~ AB-230231 I~v 1

Page 2: F ~iddixon/CBE_433_PID.pdf · p-1741 h-1741 115'00 170 •• yes es , 4, '2 44 5 85 40 - - w a st etre m nt, h no 2 414- 1 4t2- 12 -wl • 170 so yes yes 434 3 70 p-1742 wu< ns 170

I~fti8li SliP fW'U~3"-44'3-WLN-$O"'(ETA:n . .. - .-. 3"-44S0-RWR-12 I

48-230243- 1"-4J40-CA-l.AIEHIIi 3"-444J-WlN~12([T.U 70"

"'8-230243 48 J -4449-RWS-'2 A8.-2 0 47

,"-44SJ-RWR-12I N~T.n

LA ~ r (E~."CI: J,jIN OIST

,"-4U6-CA-,U,IUA:I) -', J"-44S2-RWR-,2(EUtl) :. TO H-1741

L~-U::-,=H-='=7=4',-,&"'i r ~lf. ---@~ NOTE .•, ----L,,":"-~::;'::::':"~~~-~;-- ~'~12£T.

,"-44·'B-WLN-70fET \

\\

~~~Y7~~~c'TO NCCPW

e SEWAGE IN:'

~~3 &~~~~~H ~ ~8-L'I ~ ~

1 1/2"-.440a-OR-'4AT T z-r I- "• ,"-H14-WI.N-70IET,dJ

NOTES: 3"-4410-WlN-70IET.I)~ J.1. ~ ~~~~A'~3lY~~1P1NC 3"-U1Z-Wl.N-70IET4c1) : f2. SEf Owe NO AB-2J02+8 FOR SEM. : I ~

WATER ~ATIOH 1Hl . -LN: IU&RS.

.1. F\»lT TO PRO'1U CRAB SAloA.£ a«:E t IPER Yt£[K F'CJl pH '" ceo; .f£SU.:fS TOBE ,!'£COROED -. REPORTED EVERYTlREIoO<T!<i

4. PI....AHTTO REt.:X:R) l'EloftRATlJ£ CNXPER VIm AIIJ REP'CRT EVERY l}ft[IoO<T!<i

S. PI..N{T TO FlECOfIO FLOW TOTAlS DALYS. VAlVE TO BE PARTIAL.!.Y ClOSED

ok T "GeED TO I.•••••T NORMAl.. FI..OW

J"-4.06-0V-'4A ICRADE

• J"-44I~T-&:~:-N-70\. / J"-.~~lT~rN-70

1W!Ell! ~~ ":;pm @ 2,., !fl1!8mefHQ! P INt< O_DON ,wAl! ",OWER QX!P{WffiWER Em ,.,l\IJ&(RA! qfR rrdiiWW-fiiw120 GP", 75' TOH,lOHP: 315 S.S. .'-6" 0lA X V-O" ss tnoo CAl);FRP 600 Aa\I,. 1!1PSG 0JTl.[T, <4CtP; CAST RON .' DlA X 38' SS, FRP Sl£U.: J" OIA, & UNITS, J1. S5 120 G:Pt.4..,no' TCH, 5-P.,l1l5 SS L~;;:;~=::::i==~~;;;iii~~~

l(Ucll /). IPPI ~ a:-us lNSTAU...ED SPAI£J 3' DtA X 25' HlCHlPPf}ASTlCPAQ(HG (E1'.n .H-n41 h..

Lll _ Lll 'i' _. EFn ~Ql ER .Lll2ND NEllI H~K AGIHTOR &. Lll Hf~UHP 40 FT 1;3t6 SS PLATES

TURBINE, JHP; ..31& 55 s« X 10'1. X .6'0: COHCR(TE ""~JO

4'W X 4'" ~BRICK ltl£D

2Np WAJt.f=NHfiSt.l rlfB3" OIA, 5 UNITS, Jl& 5.5.

IET.U

REVI 'M. ISlZE1~r""'" T rc 1F~T~1~THSU. TTRACl'lGT REWARJ<S nREV 'M. SIZE ~ ""'" IO WI: TW PG~S HSU. TRA~ _S REV 'M. S!ZE ~.~~

IO F~ TW ~ t<SU. TRACHC _S

.420-A Ir 1J 8 1741 SP-I74, 200 '5 YES PIoRTIM. 440- , 70 H12-~ 5 170 •• YES PARTIAL

4 "''''':rc=~T-=,':tTMMT-~ " .,.

440KA , , •• 4J3.-C~3"-C~ , 4-'0'!+ 404- YES 4- YES 4- -11-, '-'NUl , 70 5101-1741 5 170 40 YES YES3'~ :8!.:g:._-" LM: UU-WUI" ~ .,., 3 443- 3 .OA 433- 5M-1701 115 170 ss YES YES 2 .,.", ~~~~~"!fi.fM .uo ~ ""

3 50A li.CX-1715 V-1 US '00 170 AIM ..•... t_.OA P-1751 WLA '55 AM" .5 YES YES ' ""'" .1Il1l.A~MVIIIOII ... .,.

4401S-oy 3 '4A V-1715 CRADE - 170 ATM - - 4428-cA , 14A 340-CA 340-CA , '00 40 YES YES 1/2 .OA 5M-1551 '0 A'MB +0 - - i ~", IIMv'OfIeotft'_'_ ~ .,.4407-£V 3 ,.. V-171S AT" - 170 AIM - - ~tt --- -~-44Oe~ 1 V-1715 4406-0Y - 170 AIM - - ill 3 12 H-1751 '00 '40 4' YES YES

~.LC.KUQC ,.....,~2 ·3 '2 11m .5 40 PARTIAL PARTIAL

nAft.Go onAWAI'll •. au.,

4"'- 3 70 V-171S P-1715 no 170 HYO YES YES ....,. 4 .OA SP-1741 MX-1741 •• 170 HYO pp - 3 '2 H-1751 """" tOO 11. 30 PARTIAl. PARTIAL MECHANICAL44~wt.J.( 3 70 419- P-171& no '70 HYO YES YES •..•"'" 4 .OA IolX-1741 5104-1741 •• 170 HYO pp - 3 12 4-4 100 es 40 YES YES PPtlG /I< INSTRUMENT A TOO DIAGRAMl412- 3 70 P-171.5 YX-1741 170 .0 YES YES 2-""" 1/2 70 SM-1741 10 170 40 - - t 02 3 12 • 100 ne 30 YES YES MgO REGENERA nON PLANT

~ 3 70 P-171S 12- 110 170 SO YES YES 33-WU 3 .•.... P-1741 H-1741 115'00 170 •• YES YES , 4 , '2 44 5 85 40 - - WASTE TREATMENT, SH NO 2414- 1 4t2- 12-WL • 170 SO YES YES 434- 3 70 P-1742 WU< ns 170 •• YES YES 1 4454-R ,

'2 • CRACE- - - - - RELIEF All.lED CHEMICAL CORP. CLAYMONT, DEL.<415- 2 70 412- 412 .0 t 0 80 YES YES 4,...."", 1/2 70 433-....,. 5tr.4-1741 '0 170 40 - - JOHILAO[LPt4JA U[CTlttC CO.4"-WL , 70 4'2J, V-171S 5 170 00 YES YES 3O-WU< 2 70 "'" 33-"", '00 170 ss YES. YES 4 4456-SA , 1J 5302-5A 51.1-1741 ec A"" 90'lS - - AIR LANCE• ,7- 1 7012 41&- GRADE 2 170 ATU - - 4J7-Wl.N 1 '0' 'NUl S).4-1741 '0 170 40 YES PARTIAL -4 H$7-lPS , 52 .~ SM-1741 eo •••• 200 15 YES - STEAM lANCE @1I:ItIbd:I~ •.....-.-••418-W\. 1 70 412- rUNNEL 2 170 AIM YES YES J8-WLN , 70 440-"'" 51.1-17.' s 170 40 IoRTIAL PARTIAL4"'~ 1 ~ 70 rUNNEL SP-1741 2 170 ATM - - ...l e:.Q• AS 230244 J.:~v 4

Figure 3.2 Typical piping and instrumentation drawing. Equipment shown in the foregroundof the cover photograph is depictedin this flow diagram. (Adapted wz'th permission of UnitedEngineers & Constructors Inc., Philadelphia)

Page 3: F ~iddixon/CBE_433_PID.pdf · p-1741 h-1741 115'00 170 •• yes es , 4, '2 44 5 85 40 - - w a st etre m nt, h no 2 414- 1 4t2- 12 -wl • 170 so yes yes 434 3 70 p-1742 wu< ns 170

, _.-r..,~",- """- •...•..,,-•.~ , '__.7

,"-433i-CA-14ACET atO

14

1V2"-4408-DR-14AI.

1"~44'4-WLN-70(ET.1)

~PH

r-pH 1"-4426-CA-14A{ET acu

,".,..4417-WLN-12·12

~70

_I TOi GRADE~loW(5,...I

%-'~I

CD•..••:1•..

NOTES: . ·IJ"-4410-WLN-70(ET.U~,1. SEE DWG NO A8-230232 FOR.PIPING J" -4412 WLN 7dlET ad)

ANO t6lRlAtEHT A liON SYt.I8QL~' • -,' - - •• j • .,-12. :fT&W~l~UOR ~M.

LN: tUotBERS.3. FUHT TOPROva: GRAB SN.A.£ONCE ;

PER 'II£EK' FeR pH ac COO; R;S&J.:!T'S TO '·BEiAECXHlED·. f&"ORl ED EVERYllftE IiDmtS

4. Pl.ANT TO RECORD TfJ,ftRA TUE: ONCEPER WEE< N{) REfIaU EVERYTIft.E, 't.CHTHS ,

5.P\..ANT TO RECORD FLOWTOTALS DALY6. VALVE TO BE PARTIALLY ClOSEDac TAGGED TO LIMIT NORMAL FLOW

. ~H'4"~440;-EV-.14A=:lQ-:- "-441,-WU,.-70lEToItll AIT

3" ' 00-4405-WLA-50AI I CHEMICAL •• ' pH

LPLW p 1ZP :>, IH MX-1715 H~ I r-ADDITION 1'XJ/f/fi\1,'X:J/4'.- ••• --.. (ETatU& S:., ± .& - ~

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