st. lucie unit 1 - drawing 8770-c-057, 'heat balance 2690

877~W57 SH 15

(%)

ZLDZ

I5)

j

211 ' P

1110-7

I10ISTURE

SEPARATOR

934283 '1195 ' H

CDClUl

OCu

REHEATER «I 8101180 ~ Q

198 ' P498 9 F1268 ' H

ZU tt)

Z0

C3 Q)

CC

0)

(9Z

116857404)885 ' P1195 2 H0.25%

STERN GEN

2692.2,'IHTI

1

I1

II1

I1

1

II

I1

1

III1

I1

II1

1

III1

1

II1

1

1

IIIIIII1

I1

cl.I

cd

O)

1

II

II1

II

I

ccr

cn Qcd

lU I

o I

1

1

1

1

I

I

I

lzlzZZ CEIOO I

ClZ 'OO IO

110

I

I

1

430 ~ SF409 ~ 2H

RUX STER)1

25000 LB/HR

10722333. Q851.7 P1195 2 H

0 ~ 40%

8507. 0

312 ~ 0

1110 6 H

cu

EC

J=-g I

CS z cull

~cn

I

1

I

I

FW-HTR ¹5

5.5 FTD

SG-F P ~

I

l

I

FW-HTR ¹4

~ 5.5 FTD

365 ' P

436-0 F

IG ~ 9 DE CD

)7)3437 D 11719437 D

1

II

1

1581602 0391 ~ 4 F365 ~ 8 H

206-7 P

384 ~ 6 F

11 ~ 0 F81 ~ 1 H

1

I1

I

<35392064)384 6 F358 ' H

HIGH PRESSURE TURBINE

EXTRRCTIONS AND LEAKS ARE SYHHETRICAL

311 'F281 'H

Z

OtcnlCD)cnC3

,Iml

2I

InlCl

I

I

I

1

1

I1

III1

IIII

1

1

II

1

I

I

1

I

I

II

I

DRRIN

278 'F247-SH

',3539206c7310.5 F280 ~ 5 H

I

COOLER

320 DC

Zl1

'I

InlI

I

Ol1

ICCTC

cnlI

I

II

II1

I

I1

1

II

I

II1

1

1

I

I1

I

I

STEANSEAL

I

REGULRTOR1

8101)BG ~ Q194.7 P

THO SCHEt(RTIC DOUBLE FLOW L.P.TURBINFS

EXTRACTIGNS RND LERKS RRE SYtlt1ETRICAL

BDHL PRESSURE 194.7

J

gcncn ~

I

I

cd

ccc

I

«2I

J .

I

I

I

I

CX

I

cd3

1

L

I

5' P

283 ~ 8 F

224 .2F192.5H

20 ~ 59

229.5

180.0F148 ~ OH

8 ~ 71 P

186-8 F

10 ~ 4 0-CD

I1

1

1

467229. Q

234 ~ 6 F203 ~ 0 H

10 ' D-C.

I1

I1

4 843832 '190.7 F158 ' H

11 ' DENCE

I1

II

1444426 Q116 ~ 6 F84 ' H

1

i

I

j I

I 1

f' I

II

I

II

IO]Z4. Ojzlu

~~(cncn Q.CDCn CDj!DO

jFWHTR «3 I FWHTR ¹2

]FW HTR ¹I

I 5.3 FTO '.3 FTD 6.7 FTO

6S61193- 0

1195.2 H

51813. 012214 H49923 '1030.6 H

Ocn

4616. 0

1177 ' H

GENERATOR OUTPUT

903247. KH

)1L« 3045 'HGL= 10666 4(H

RT 60.PSIG H2

CONDENSERBP ELEP CEP

IN HOT H H

2 '0 967-5 982-3

180231.0104.3 F

723 H

I UHPCOND

SJRE

1104-7 H172 ~ 7F1

I1

GSC

1105.3 H1 73.3 FIII1

J19)(E=VP

WJBitL AUX COND ~

II

II1

1

I1

1

I

1

1I

II II

I I

II

II

1

I

1

I

II

1

II

III

I1

III

I1

1

1

I1

I

I

DDgSc¹t

STIFICS J~D

NS 3."I)6* ** STATE OF

CQRCD

rrrl(D 6'"G

(C

0)

Z(9Z

PERFDRNRNCE

GROSS GENERRTIONKH ~

903247.

TURBIN« HEAT-RRTEBTU/KH-HR

10168-4

LEGEND

Q—FLOH~BS/HRF----TEt1PERRTURE- F

P ——PRESSURE-LBS/SOD IN ABS.H——ENTHALPY OF STEAI1-BTU/LBFTD —TERtlINAL DIFFERENCE (F)ELEP-EXPRNSION LINE END POINTUEEP-USED ENERGY END POINTD.C.-DRAIN COOLER APPROACH (F)S.CC-SUBCOOLING (F)

STEAN

HATER

EXTRRCTION STERN

THO PHASE FLOH

HAIN PATH

SHEET NO

I(I.

IAI6.l7.

IB.

(9.

20.2L

THROTTLE FLOWLBS/HR

10722336'0722333

'0722331

'0722328

'0722326

'G722323.

10722321'D722319~

THROTTLE PRESSUREPS IR

852

852

852

852

852

BS2

852

852

BACK PRESSUREIN'G RBS

2-002-202 ~ 40

2 ~ 60

2 ~ 80

3 ~ 00

3 20

3.40

CYCLE LOSSESLBS/HR

18697'8697

'8697

~

18697 ~

18697'8697

'8697

'8697

'LDHDOHN

LBS/HR

ISGDO.

15000.15000.15000

'5000

'5000

'5000

~

15GDO ~

DATE

DRAWlNG ORIGINALLYAPPROVED

AS BCS-12~1.303 SH 2 OF 3

REVISION BY CH ~

THIS DOCUMENT IS THE PROPERTY OF EBASCO SERY1CESINCORPORATED. ITS USE 13 EXPRESSLY RESTRICTED SY THETERMS OF THE CONTRACT. DATED AS OF AUGUST 1D, 10«SBETWEEN EBASCO SERYlCES INCORPORATED AND FLORIDAPOWER 2 LIGHT COMPANY.

FLORIDA POWER 6 LIGHT COt1PRNYST.LUCIE PLANT

1976 — 890.000 KH INSTALLATION UNIT NO.)HEAT BALANCE

2690 MWT VARIABLEBACK PRESSURE2ZO INCHES HG ABSOLUTE

EBRSCD SERVICES INCDRPDRRTED NEW YORK

DATE 9- 8-8gSCRLE-NONE

DIV.DR ~

Rt PROVED

RPPROVEO

8770-C-057SH 15.

1

r/Par krr CZ.C

N.&D,. FM~