Text

Table of Pressurizer Design Data. Related Info Encl
	ML20080T285
Person / Time
Site:	Farley, 05000000
Issue date:	01/25/1984
From:	; ALABAMA POWER CO.
To:	;
Shared Package
ML20079E758	List: ML20080T285; ML20080T296; ML20080T311; ML20080T321; ML20080T345; ML20080T354; ML20080T363;
References
	FOIA-83-789 NUDOCS 8403010129
	Download: ML20080T285 (46)
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FNP TABLE 5.5-10 PRESSURIZER DESIGN DATA Item Value Design pressure, psig 2485 Design temperature, OF 680 Surge line nozzle diameter, in.

14 Heatup rate of pressurizer using heaters only, F/hr 55 3

Interosi volume, ft 1400_r,;;.,

e S

I e

4 PDR FOIA8403010129 840125 MADDEN 83-789 PDR h

/d /4

j;edb DG TABLE 11.2-3 (Sheet 6 of 15)

EQUIPMEhT PRINCIPAL DESIGN PARAMETERS.

Component Value TANKS

1.,Lasct- _ ---'- _i t? = cenip Number 1

Usable.volasma.- sallona -

350~.

Type horizontal Design pressure, psig*

100 o

Design temperature, F 250 Material SS Diaphragm No 2.

Wrste holdup tank Number 1

Usable volume, gallons 10,000 Iype vertical Design pressure, psig atmos.

o

. Design temperature, F 200 Material SS l

Diaphragm No

External design pressure - 60 psig 9

9

+

. <.[I ~, r A1M pyp

-/

TABLE 9.3-5 (Sheet 4 of 8)

PRINCIPAL COMPONENT DATA

SUMMARY

'Tolemusesserek-hm Number i

vow *ft,b

300-,.

Design pressure, psig 75 Design tempera'ture, 'F 250 Material Austenitic stainless steel Boric Acid Tanks Number 2

Capacity 21,000 Design pressure, psig

- Atmospheric 2

hsign temperature, *F 170 Material Austenitic stainless steel tarie Acid Batchina Tank Nunbar 1

Catacity, gal 400 Design pressure, psig Atmospheric De ign temperature, < F 300 Ma terial -

Austenitic stainless steel Recycle Holdup Tank Number 3

Volume, gal 28,000 Design pressure, psig Atmospheric Design temperature, 'F 200 Material Aus tenitic s tainless '

steel Reevele Evaporator Reagent Tank Number i

Volume, gal 5

D: sign prassure, psig 150 D2 sign tempera ture, 'F' 200 Material Austenitic stainless steel e

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$ Pt.fi (5)-

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F No Change Allowed LI-459 97 Pressurizer i

LI-460 vi Level LI-461

'li (Avg. of Readings)

Nk U. h 2

B = 93.66 x AZ = 0 Cal.

.i LI-115 VCT Level d.f I

2 'l I

C - 14.06 x 6% "//.e 6 Cal.

LI-1003 3l 2

3/

Z

__(Waste Panel)

RCDT Level ses

Cal.

IIS-

Gal.

D=

0 Cal.

C. t}

Z to y 2

.LI-470 PRT Level (o s so

Gal.

0 55o

Gal.

E=

d Cal.

dc3 332 Gal.

.3 o 4 T f L Ca1.

RHW/ Total Flov' Gal.

Gal.

Dilution and Blended FIS-168 Batch In.tegrator Gcl.

Gal.

K=

0 Cal. Hakeup o 3102 5' Gal.

o '3 9 o gs Gal.

Boric Acid Cal.

cal _

FIS-Il3 Batch Integrator Cal.

Cal.

C-O Cal.

Boration Only Total Leakage = F + C - B - C

-)

,)3 CPM

From Tank Curve Book A

Identified Leakage = D + E.

O cpg A

UTHER LEAKACE

ttsidentified.

i 5

Leeksge'

= Total Identified Other

.G Source RATE (CPM)

-/; tTG' CPM Wl[T

, T 3 (W Lankage Leakage Leakage l-(Note 1)

/'

l.

f. 2.3 "

o

.s 3 NOTE 13 ' I'dantified Leakage does not include leakage which mt'y be known to (TOTAL)

, k"h 4

exist such as steam generator tube Icakage.

I f-

-dZrsr 31 51 l

W' el'1 21.i' 28 f

m rcy m r l K C 'in. W T M U r".E U 't?[k S h'ds/d dil e b [d kj[g h,I $ h

. _-wwn eww.

e g,i

/ (h FNP-1-57F-9.0

~

@l RCS LEAKACE DATA SHEET Rev. 2 Data Sheet ll [3 INSTRUMEfff INITIAL l

FINAL (HCB)

NAME RI'ADINc READING FINAL - INITIAI.

g :

,e, TIME

/ *73T

/(J I A=

Y L-Minutes TI-453 Pressurizer

.,14 Temperature 6,$D

'F bb

'F No Change Allowed v

.1 PI-455 Pressurizer PI-456 Pressure L M PI-457

_(A_vg._of ReadlBas)

,7 2 A PSIG c7 8 ol[ PSIC No ChanRe Alloved TI-411A RCS Temperature TI '*21A TAVC.

a TI-4 31A (Avg. of Readings)

S~ 7 0

'F S~ 20

'F No Change Allowed v

7 in i LI-459 Pressurizer LI-460 Level y

LI-461 (AvR. of Readings)

Yb N

B = 93.66 x A% = 0 Cal.

L1-115 VCT Level

'YO M

C = 14.06 x A% =gf >(e Cal.

9 JP LI-1003 Jo I

Jl I

g,/

. P; (Waste P.;nel)

RCtYr Level Y"

,g o

Gal.

/p i

Cal.

D = g [ Cal.

76 N'7:st 74 %

I LI-470 PRT Level

Cal.

cal.

E=

()

Cal.

lf 3o6171 Cal.

T ov'77/ Cal.

;a RHW/ Total Flow Cal.

Cal.

!.fd FIS-168 Batch Integrator Dilution and Blended i

Cal.

F=

()

Cal. Makeup

[b' 0 3'7 trG/

Cal.

o39(Z/

Cal.

Boric Acid

{'

FIS II3 Cal.

Cal.

Batch Integrator Cal.

Cal.

C=

d Cal.

Boration Only Total leakage = F + C - B - C'.

7-A

~ g4, / </

, 9 4/

CPH

From Tank Curve Book j

6e

1dentified Leakage = D + E =

j I

A

/3 CPM

~

=

1hidentified be UTHER LEAFACE I 1..

Leakage

= Total Identified Other Source RATE (CFM)

1 a

Leakage Leakage

, If CPM 6)// T o

l Leakage

=

W l3

.'/

(Note 1) 6

?2 h)$[

O e

ECTE 1: Identified Leakage does not include leakage which may be known to (TOTAL)

O exist such as steam generator tube leakage.

unn son blT 15?i 9

9

a. x 3

a (r -e.

j

.]'

8; :

I M.:LhLbbbhki NA dsdb$::Sh :_mtbY E

$ yst ifj k

t

,, ;< d E*'

g j l) I g

FNF-1-STF-9.

l Data Sheet

.7 RCS LEAKAGE DATA SHEET Rev. 2

,e

w,.l{ cacttCa.tbz u t;i knist. h t a 4.k &..,.3,g a ofj.r.*

p,u..

..,,.g.

m;

. upl,[- q 33.

-.+.

-c,.,

p. y 9- -

o.

. q

.,,,.x g i.

u

.O.. u...u a.rJu.GdZ.s f!k.

s r

~

n.:..,

i PNP-1-STP-9.0 2

/ [ h /

^.

~

Data Sheet RCS LEAKAGE DATA SHEET Rev. 2 INSTRUMENT INITIAL FINAL (HCB)

NAME READINf:

REgINC FIN _AL - INITIAL TIME

[735

/eT30 A= bO Hinutes Pressurizer TI-453 MO

'F b

'F No Change Allowed Temperature PI-455 Pressurizer PI-456 Pressure PI-457 (Avy,. of Readines)

(12 PSIG

,/)) \\ PSIC No Channe Allowed e

TI-411A RCS Temperature TI-421A TAVG.

TI-431A (Avg. of Readings)

/

'F IW

'F No Change Allowed L1-459 Pressurizer LI-460 Level LI-461 (Avg. of Readings)

II Y7 B = 93.66 x A% =

O Cal.

LI-115 VCT Level

, ~2 R Jg C = 14.06 x 6% = 0 Cal.

L1-1003 d(p v2(p 2

(Waste Panel)

RCDT Level

Cal.

Cal.

D=

0 Cal.

7/

LI-470 PRT Level

Cal.

Abal.

E=

C2 Cal.

y / /(f 5 3 Cal.

3/ 7M > Cal 7 RHW/ Total Flow Cal.

Cal.

Dilution and Blended FIS-168 Batch Integrator Cal.

Cal.

F=

O Cal.

Makeup

%).1 L, (p Gal.

y o ) pt, Cal.

Boric Acid Cal.

CL TIS-Il3 Batch Integrator Cal.

Cal.

C=

D Cal.

Boration Only O

CPM

From Tank Curve Book Total Leakage = F + C - B - C O

_ 0 A

gy

Identified leakage = D + E =

0 O

CPH

=

A

- 0 UI'IIER LEAKACE 6>

Unidentifled S urce RATE (CPH)

Leakage

- Tots.1 Identified Other O

CPM Leakage - Lenkage Leakage

=

(Note 1)

NOTE 1 Identified I.eakage does not include leakage which say be known to (TOTAL) exist such as steam generator tube ! rSnge.

l A

O f'h

EG i'i'l ;ZXC.EiICE3E["'C5Gi#10%3EGI}S:P_"dfi",LT5EO75%'ECGA. ELE 51IdiiMfg.f n

TXP-1-STP-9.0 Q t' Data Shaet lil Tb d

RCS LEAKAt,E DATA SHEET Rev. 2 r;

a fi INSTRUMEtir INITIAL TINAL y

M (j'CR)

N.A. tE Rggq READJNC FI':AL - IgrJJAL i

i TIME 7yC

~' V E A.

HJnulea d

Pressurizer l

Tenpe ra t ure 6 ': f.'

'F

'F No Chanr.c Allowed TI-453 PI-455 Pressurizer

[;j PI-456 Pressure P' 'g 2 '> ' ' '

PSIC No Channe A11ouco PSIC

[j PI-457 JA_vg. of Readinen) y

_ TI-4llA RCS Temperatute p

I14421A TAVG.

cy., t, t, y C, TI-43tA (Avg. of Readings)

,F

,F No Change Allowed

,5 ki L 1 -4 5')

Pressurizer Y

y4 d'$

L1-460 Level

,L1-461 (Avg. of Readings)

B = 93.66 x A% = C' Cal.

a C = 14.06 x A% = O Cal.

h Y7

% j

\\1 1.1-115 VCT Level l

26

. L L1-1003 (Waste Pancl)

RCDT Level

Gal.

Gal.

D=

Gal.

72 5

~. ' ' '

f,i LI-470 PRT Level

Cal.

Gal.

E=

Cal.

1., << w v cat.

. i, -

Cal.j i

Rl!W/ Total Flow Cal.

G.J. '

t.'

Dilution and Blended

(

FIS-168 Batch Integrator

(;a l.

Cal.

F=

Cal. Makeup (orx n i.

Gal.

O ' ' *, -ll.

t;n t.

Boric Acid Cal.

Cal.

{J y

FIS-Il3 Batch Integrator Cct.

Cal.

C=

Cal.

Boration Only

Trom Tank Curve Book

(.

CPff Total Leakage = F + G - B - C A

t' CPM UTIIER LEAKAGE

1 dent l'f ied Leakage = D + E.

A

th ident i f Led S urce RATE (CPtt)

Leakage

= Total Identified Other L.

CPff rrr -

i.-

Leakage Leakage

=

Leakage (Note 1)

(TOTAL)

NOTE 1: Identified Leakage does not include leakage which may be known to exist such as steam generator tube leakage.

4

itam: WsacRad$1dib5a3I.fM..g$}$d5bNhbsgJAihAy&k hh2 3 f

. 4,

,.,m,_g

,. s.

I g

p_ f.,,] n i

rwr-1-sTr-,

v Data Sheet PCS LEAKAGE DATA SNEET Rev. 2

5!*~'T.TT INITIAL FINAL MM

_g RQDf P-R @ lMC FIN _AL - INITIAL N

T I.*Z IM' lIff A=

Minytss i

II-'I3 W

'F (S 0 e

7 e t e r

no Change Alio,,a F1-43 5 Fressuriser

' F1-4St Pressure 13gC-g33 I

I'l-43 7 (Ayg ugf_ltedickel PSIC PSTC No Chanste Allowed i II-allA ACS tearper.sture T I-t.fl a TAVC. ~

4d T 578.'I i

n -;~1A (Arit. of Readings)

'T

'F No Change Allowed i L; -ss Pressurizer h9y yry LI-48 0 Level l

t LI-M I (Avg. of Readings)

B = 93.66 x 6% = 0 Cal.

4 N

L!-115 VCT Level

~39 C = 14.06 x ^% - O Cal-LI-iCO3 L I-Z S I' (k*arte Pa el)

RCDT Level

Cal.

Gal.

D=

0 Cal.

73 73 LI-a!O PRT LcSel

Gal.

Gal.

E=

()

Cal.

q

~

bisc/ILC.nl.'

3/96ft Cat.

R.'N/ Total Flow r,a l.

Gal.

Dilution and Blended l

FIS-lE9 Batch Integrator Gal.

Gal.

F=

M Cal. Makeup

.j OVOLO U Ga1*

CV0h$$ Gal 1

Boric Acid Cal.

Cal.

t FIS-113 Batch Integrator Cal.

Cal.

C=

d Cal. Boration Only Total teakage = F + G - B - C O

CPM

From Tank Curve Book A

Identified Leakage = D + 6,,

O CPM I

A UTHER LEAKACE

Lhidentified Leakage

= Total Identified Other S urce RATE (CPM) j h

CPM

,,g-es

-st 6

f Leakage - Leakage Leakage so-

I (Note 1) 6 7-3 gg-a s_. S4 O

j

+

I, NOTE 1: Identified Imakage does not include leakage which may be known to (TOTAL) j exist such as steam generator tube leakage.

I

-I

FMP-1-STP-9.0

( y.,;(g)

Data Sheet PCS LEAKK.E DATA SHEET P.cv. 2 D !371 53 INITIAL TINAL l

I"E.II

. _ _ _ _ _ _ _ U.

g gc RQDI.C TIN _AL - Ifi1JJAL 1

j Titat S 000 J /OO A = 40 xinutes I

rressuriser l TI-4}3 Tenerature

[p50

'T 4 s'D

'F No Change Allowed P'-L))

Fressuriner

?I-;}6 Fressure

? f -F (6yjta[_gt e_d_inen)

,J aidlI~

PSIC

,J.Lil I~ PSIC No Change Allowrd j 11-ilia RCS Terrpersture T* *21A TAVG.

TI-ailA (Avg. of Readings)

$70

'F SJC

'F No Change Allowed L1 -= y1 Pressurizer LI-560 level L1-;61 (Avg. of Readings)

M[o 1/6 B = 93.66 x A% = ()

Cal.

C = 14.06 x A% = /fo4 Cal.

2

.n LI-115 VCT Level 33 Me I

3/Ie 1

L1-1003

cal.

Gal.

D= g Cal.

(Waete Panel)

RCUT Level 7g I

7v LI '.70 PRT Level

Gal.

Gal.

E=

O Gal.

3/'/207 Gal.

3/9ao7 Gal.

l RMW/ Total Flow Cal.

Gal.

Dilution sol Blended I

TIS-168 Batch integrator Gal.

Gal.

F=

O Cal, tLikeur

_ofo 7 fD Ga l.,,

i; ic 7 f7)

Gal.

Boric Acid Cal G11.

i u_,,_

Cal.

C=

O Cal. Ecration Only F15-133 Batch Integrator

From Tank Curve Book

+

,23 CPM Total Leakage = F + C - B - C j

A O

CPM UrilER LEAKAGE

Identified Leakage = D + E =

=

A

Lhidentified Source RATE (CPM)

Leakage

- Total Identified Other

.23 GPM Leakage

=

Leakage I

Leakage (Note 1) l 4

(TOTAL)

O "UIE 1: Identified Leakage does not include leakage which may be known to exist such as steam generator tube leakage.

.S b. d. I2[.C[JE.E 7 C E'MEfTr M ygggymy;4m gg.e,jsgg.magg,y.g.

da m~

'=

'

I * 'U l

h l

l 0

)

IN.;

1(CS LEAKAGE DATA Sl!EET 3

I ;ITIAL FINAL I

I::" rin : r.Nr F I' 1..

- u-.M...i.3.'

t

(-

x:E trADU;c RP.W NC T l 'ir.

/9t 5 7005 A,

/c (>

.j g.y g,yy r..

Pressurizer

[SD

[5'O

'F No Chinge Allowed

~

l T N.D Te rcratu;c

- ' ~* i Pressurizer l

i P re s s u r<-

.-M

(.te;. of Rnading) _

7.) S D PSIG

.7230 PSIG No Chang tA11mim!

I.!

'-i I,.

iWS I en;? erat ure l

..' t h TAVG.

l I

.- 1 (Avn. c' m ndings) 1 S'/O

'F

.( )O

'T

o Chan;e Allote<H 1%__-

! Fressurtner

)

j '.... - -

l.

' t Leve:

9' /

g7

% ! P, ' '? 3. (4 x

^.7. " Q Ga ?..

J (Avn. of R21dinns)

' I '. I I

GM.

7. !Ce l. 0 5 x 5 = g l-._..3---..--}-....'.==-.......

,3 gg

.! - l ' -

VCT Leeci

-l

// f3 l

Db

?

J4 l

D Ga'-

i

' - L - fy i

'. t*3

! FCDrIrtel

G il. !

I

(

..N.

.)

5

/ g,.

l I PRT Lev.!

j

G.I

~7b

' 1

]E* d Gal.

g t'

"G;' t.

I 1.. ; _. ? 6..

-I

-~~

L_.

...i.I Dilutic ard E: ended l R:r4/Tntal 710.:

I cit.

(:n d r -

ral.

'.n ce;-

-n...,

O r ' '- - ! <. -'

3tch Ir.t6. ater y.-

l.]& is ti (s'.'

J t( vid] G:* n.-.

l I

i Enric Acid f171 DI.

G.i l.

Gal.

G=

()

Gal.

Boration Only l

"I9 113 Eatch Inter.rator

Tren Tank Curve Book l

1

()

cp :

i

. 11 Loakar,<:

0+G-B-C A

i

' I N -". i t' t ed ir ak.t w = D

E,

/h

_c n-OTilER LEAKAGE a

n',n ic!c -* I f i. d Source RATE (CP")

L.,'.. p e

- Tetal Identified Other

,)

GP?!

Icakage - Lealc age I.caka r.c

=

(Note 1)

~

(TOTAL)

?:0TE 1: Ide nt tf ied Lenkage does not include leakage which may be known to exist such as steam generator tube Icakac.c.

l

.)

1

)

I

(:)

I3P-1-S TP ').'

/

Data Sheet RCS LEAKAGE' DATA SilECT Rev. 2 i!:5Tri ?!.7:i INITIAL FTNAL

(:;CE) i-~-~~"'~

NA?.tE STAD.,#?.L RU' DIM _ _ _ _.

T17tE 888

/N j

._u-_-__

~

'N

)

A.-

71t nut e:

l

!! i.51

/M 5 0 SO

'r No Chance Allcwed T pc.tu PI-C i Prcssurizer P l I ~ f' Pressure M,e230 PSIG No Change Allowed P'-2.7

(.lvg._ o f Rea_d Lng,5) 8.> O PSIC I as !.ilA HCS Temperature 7'-221A TAVG.

T I '. ' ; \\

(Ava. of Readings)

') [O

'T D-

'F No Chant..' Allowed I

l L;-M9 Pressurizer I LI-MO Level l LI-M1 (Avg. of Read!'ngs)

B = 9 3.66 :s t,7. a h Cal.

LI-!15 VCT Level

/-

k Z

C - I f. 06 x.R =/h [. cal.

~'

1.1-1003 M

Z 7/

h Cal.

(*.'ac t e Panel)

RCDT Level

/C 7

' Ga l.

/ O,7

Gal.

D=

70 7

'/0 l

I.I f.70 PRT Level

-' e t' r>

+ cal.

7 O <- c7 ocaI.

cal.

g l

~33 77[7:1.~e i.

3f@ [7 ' t:.e l.

~

l RI:U/Tetal Flow cat.

v l.

Dilut ion an.! ?.!. r d. d FIS-168 h Cal.

?!nkrup

~

Batch I,ntegrator Cat.

Gal.

F=

(t/ T(3/

Cat.

((/ rc 3 / Cal.

g Boric Acid Cal.

Cal.

TIS-111 Batch Inter.rator C.31.

Gal.

G=

Cal.

Borntinn Only Tet.*1 Leakage = r + G - B - C

/ y, oh

, 2.3 /

crit

Tren Tnnk Cur.r Le 4 A

1dentifled Leakage = D + E hO CP?!

A OTHER LEAK.\\CE

rn iderit i fied Source L< ak.i; e-

- Total Identified Other g

RATE QP2

,D T CPM a

Leakage Leakage LeakaRe

=

(Note 1) f

0 E 1: I:!catified Leakage does not include leakage which ni?y be known to (TOTAL) 1 f

exist such as steam generator tube leakage, m

. =

J m.a u.n a w atuu m m2r w A M h iJ. m ;w up e rg 2S.E I22 E si211T2 G o _.

x rur-i-stF-,.o Ji -/4-go Data Sweet 3'j

RCS LEAKACE DATA SHEET Rev. 2 I

}

INITIAL FINAL INSTF1 W.WT amm rinAL - INitrat.,_

j NAnt my ripc_____

_(Mts)

/ 75/'

I 3 3 st A-(, o us,,,

Tine

.i 16 0'

Fressuriner b 9

'F 9 to

'F No Change Allcwed T I-453 Tewperature F1-455 Pressurizer FI-456 Fressure h30

>23o No Omnqc__ Allowe I l

1 PSIC PSIC F1-457 (Avst. of.Readi===)

j T1-41IA RCS Tr + reture TAVC.

p7

'F hD

'F No Change Allowed l

TI-421A (Avg. of Readings)

TI-431A L1-459 Freasurizer j

ll{

X X

5 = 93.66 m AX = Q Cal.

L1-460 Level l

L1-461 (Avg. of Readings) 3 Z

1 C = 14.06 n I

-7 0% Cal.

VCT Level

, LI-115 2 (,. f 1

I

o LI-1003

'7 5~

Col.

rp p. / *t;al.

D "'2 S' Cal.

j (Wante Fanel)

RCtfr level 7 'f 1

1'l 1

Cal.

C E E=

V Cal.

LI-470 PRT Level

~"~

' ~ ~ ~

Eh9 OL cal.

r q y i e 5, Cat.

Dilwtlen med Blended Cal.

Cal.

RPN/ Total Flow Cat.

Cal.

F=

0 Cal, mne.,

Batch Integrator FIS-168 canot1 Cal.

o15853 Cal.

cat-cal.

Boric Acid Cal.

C=

0 Cal. Soration Only Cat.

FIS-Il3 Batch Integrator arece Tank C=r,ve M Total Isakage - F + C - B - C O n 0 7. * **

/. / / ~7 nFM

=

~~

A g p a,.,r

, p a{

cry II s

Identified Isakage = D + K.

g t

A g, 0 y}

D.'SI E dO.

th ident i f le d

~'

Inakage

= Total Identifted Othe r

@f f ?

CFM Leakage

=

14akage tankage (Note 1) 4. l l ~) -k O *f )

]

(11FTAL) include leakage which way be known to I

I NUTE 3: Identified laakage does not d

exist such me steam generator tube leakage.

t

=

~"

t e

.=

g e

4 g?

}

L I

zi

=

8 1

l g !

uj i "I

i' i

>. ~

I

}

i

'E O-w:

l H

3 E

5e j

i ki l i

I I

c -

Mi sl a,l C H g

e

.5 E

+

q}

i.

aj

- 6 c9 g,i 7

- i !.

-i f

u

-i s

z; b'

m$t.$

N i.

ua i

c

~#

W a

..,UN

~I a.

E, i

i

= ti

.l

{

oci C

e o

,$,1 5 *:

'F s

(,,

e s

i i

~'

r

!c:,

I h h ";' E?

3;;

ci s]

H 3

<e e J.

,q.

.9 t: ;

j c:

J zl E O(

~j

~ tl j

.i

~

l.:;

Ei xl i

O 2

~'

q 5.f 5 !, i,,

,)

1 b,:.

I

v.,

b ls:

\\

1 m

i

=

7 i

. = -

es s

k I

he w

cj

~,,

V g

P U

8:

-u

l l

W g

I x

i 2,J

-C.

4; ss Er

=!

1 j~li,3.~'3.;3333.:{la; e.;

e 1

(

'l

)

[

,.p My 1

i.-

r 1.. y i,

g

=

~

ET i

v i

I e

)

[

j y

~

a,j h',

Y,,, j '.

c

'!. :,$ N O i

D i

'A i

3 q

\\.

j 3

i

( f.,,;

}

I ADI N.

k

,.,,skg ~

i-s s

v-

<w 2

. m y 5 s o.\\'N 3

s N

.a.'

m-.- 1 c

s

., l,-

p m! ev N.it. Q D'

's i

}

3 s

I

'N i

a

i s

) i ~ f'

,,, 'I

s

~.

l'

- '.

v

[

l I

l ll l

-a 5

>l l

l

hn N,k hkNY y

7

(

$y e$

~--

\\

..\\

.=

n a

a e

e e = u c=

i i

s j hN y-I 9%d

$j.

i s !.

(

{

!',ff 4

i

\\

L

.~

hi Is (t

l N

.b.#N NI E

', Q f:'9 ' %]

~.:o u ',.

i L

~F

't b

'W

[ ;,

.('

\\,],

.v, N'

g h,

'jS I

}

^ '

~

1 e-oz

' y n.

z 7 < U; ~

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01 6S0 l-U73 n:r_i_.nr_9 o e

rat sheet APR 1 t~U RCS LEAKAGE DATA S!!ECT Rev. 2

~

INSTPtfMINT INITIAL FINAL

("9)

J _DYNC RQig

_ _, f[.L,-]?((TJ E',

I NAME TIME O/00 osco

._A -

SP Pffmitys Freasuriser 71-453

.T tm 6m

'F

'T ffo Ch9nre Alleuad

(

F1-455 Freneurizer i

FI-456 rressure 21-457 Syg, of Rejsdinrm) 22ps" FSIC

.3.23r FSIC_

Hn_rpinga A11oved

{

II #+11A RCS Temperature TI-471A TAVC.

I TI-431A (Av6. of Readings) g-(, 9

'F f 6 tf

'r

~ fin ' l " e*a Allo r d

'Ll ~Ie h Pressurizer LI-460 Level LI-461 (Avg. of Readings) yy, 6 -

v 5. t.

I It - 91.66 x A% -

Cnt, i

C - 14.06 x AI - fy cat.

Lt-115 VCT Level gj g2 Jo Z

3/

i LI-1003 98Y D*

3 Cal-l j

(Usete Fanel)

RCDT Level

//o

/[6'

Gal.

// 3 i

J l

7(.

I l

8LT-470 PRT Level 7(.1 ( *Gnl.

f a.sy-

GnI7 E-6 Cal.

~ ~ ~ ~ ~ ~ - ~ '

Asj37f Gal.

p 33M Uni.

Rml/ Total. Flow c.t.

cat.

Dtintion and Iller.te d i F18-16M Batch Integrator cnl.

ca t.,

r-O cal. Ita anp e sp ffc Gnt.

pmsc C it.

Boric Acid Unla.

Cal.

2 Ft't-l l 3 Pstch Integrator Unt.

Cnt.

C-o t' i l.

I' ' "' ' -

/

Y g/Mo ci rt F

Tetat laaki,*,, a FFG-B-C A

2[W C

cy;t

Id-9tified Leeb gt a D+E.

u 3

A l

Ptto mttfled 0

Tot 91 Identified Othar

, ry.

1.,t **. n g,

=

fT Ica'n"*

LeekaRa 1.

e ne (fio t e 1) p.

0 k+$ *

f. $ f

{ *, f*

$1 ! '

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et 4h e

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k d4

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},k a I.1 1...

L,,,- y oI 6SS I G I rwr-1-STr-9.o Lll Data Sheet

!; y RCS LEAKAGE DATA BHEET Rev. 2

@4.

INSTRUMENT INITIAL FINAL FINAL - INITIAL lb yQB)

NAME.

,RMpfNc READING TIME M b'f[f 7 y(

A=

Minutes Pressurizer II TI-453

[a8I'

'F f rr~

'F No Change Allowed

'h Temperatute 2 l[#

N F1-455 Prensurizer FI-456 Pressure e

FI-457 (Avn. of Reaslinea) 2 2 ;s. c PSIC 3 2 K C PSIC No Channe A11n: ecd i'

W 11-411A RCS Temperature 7

ijf h 7I-421A TAVC.

f TI-431A (Avg. of Readings) 87

' I' fM

'F No Change Allowed Q ;

L1-459 Pressurizer y7 LI-460 Level vf rc il

/6

'T F6 B = 93.66 x AI - o Cal.

i.j f LI-461 (Avg. of Readings)

Q ",

LI-115 VCT Level 33 sc c = 14.06 x AZ Kpy.y2 Cal.

f LI-1003

.7 8 T 1

3 V. i i-

/p y

Cal.

fp f-

Cal.

D=

/

Cal.

(Waste Panel)

RCDT Level

'7 7Y 7r LT-470 PRT Letel prfy ;rges

Cal.

yffo

Cal.

E = /A9 Cal.

e

-- s 31/ 978 Ga1.

sit ssi Gal.

RHW/ Total Flow Gal.

Gal.

Dilution and Blonded

-i FIS-16f; 3

Batch Integrator Cal.

Cal.

F=

0 Cal. Makeup D 3367v Cal Ob&ry Cal.

[

Boric Acid Gal.

Gal.

FIS-113 Batch Integrator Cal.

Cal.

C=

n Cal.

Boration only f}

f, g y Cpg

From Tank Curve Book

?

Total tankage = F + C - B - C

'/ S. 4 2.

A T

, b-

=

A

Identified Laskage = D + E.

. / o_l-

/. U CPH

=

UTIIER LEAKACE

.g A

(,0 ethidentified

- *=

Source RATE (CFH)

[

IAnk85e

= Total Identified Other Leakage Leakahe

=.d4 S O CPM

>I Leakage (Note 1)

. {j p

NOTE 1: 16ntified Leakage does not include leakage which may be known to (TOTAL) exist such as steam generator tube leakage.

e a

d%

e

<=

D exe f A Oe v' if c S

,i E ActAre i a s 75 -Dm, fssurS _

i ML DotAr7cas i.

._ : OMe Hcoe l

p'c._ cpspc.s_s g5ccento fcg--fc.5. PRES 5ues_

2-

'.A G?.7 W i/' m m e 1%E ? EVBL 5 U 3:

cimprc:e cAMso cftexce ___-LW;rpzpoo,7,osogrf.u_(rgh:

\\

h crHER n=wm iuc6ieona - oim wrx'v', ox Wis l', vseg i vwse carai re Pze w. rug gc.one7 Axe ie w gars 5

=

\\

S66 f>/o Ght. (%6-EllD Ght. /3Ec.. EAta (LAA,

$@SS [D6/2 (JN [Q L

63

62. f[

76 so 'S/

3

,23,05

,/ fr

[f!

o-V 30 %6 -NY2 74 95

/00 %f 3& __ /

/M / 67

.09 5

?._3l W ^W-.23_. ?$_. 9f_ /S

/f

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37 kl Ek& '7I--.2L @0 90 G

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{$

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-8V 36 7(c 'R5 W $0

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'l'l_. W3

~I4E 63 0 0

81. 57 0

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c c

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'24 26 6

_C_ _O _

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7T 3 S' O 73 73 C

26 26 O

c c

C

{

_ ~l'I.% 44 W

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)(,

C

,25 C

3'k 52

_.... 3 NN.=

C,2 l

Ub 4b C

. _96 76 C

'M ?!i G

Q

</6 G(-.g)?

'p, 4( V4 Mc6 7o 70 C

g.9 p.9 C

23( 0 239 ;

& W. f '35 -7.G 3_:(4..R. c?

7G 96 6 24~

.t/ 7.c4 + 017 9 /M N C

17. 11 C

76 C

C 0.0

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27 27 C'

ggg

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./3 E

f 44' 44

/V E 7:L 71 C

77 2-fr 3 f-2/6 asY

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3 c,M M

.t C -

9

ML20080T285

Text

SUMMARY

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