ML20249B175

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Rev 0 to Calculation IP-M-0435, EOP-6,Potential for Water Hammer
ML20249B175
Person / Time
Site: Clinton Constellation icon.png
Issue date: 01/23/1997
From:
ILLINOIS POWER CO.
To:
Shared Package
ML20249B170 List:
References
IP-M-0435, IP-M-0435-R00, IP-M-435, IP-M-435-R, NUDOCS 9806220136
Download: ML20249B175 (250)


Text

Attachment 3 to U-603026 I'

CALCULATION COVER SHEET SHEETIOF 14 DEIrr/DIV CALCULATION NO.

' TITLE / DESCRIPTION:

NSED/M IP-M-0435 EOP-6. POTENTIAL FOR WATER HAMMER QUALITY SYSTEM CODE TOPIC BLDG /ELEV/ AREA RELATED (or NA)

(or NA)

(Q or N)

O VP M91

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Hydrauli :ofpipelines, J, Paul Tullis, C1989, John [Wiley & Sons.;

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' ASME B & PV C, ode Sec. tion III,.1977)o

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ij w INPUTS ASSUMPTIONS 1)

Per EOP 6 interlocks for VP and WO may be defeated if Drywell temperatures go above i

135 F. This requires operator actions. As such, it is inconceivable that this would occur at the precise point of the LOCA. This analysis will look at a water hanuner as a stand alone event.

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1, Ba, sed on the discu, ssio. n above, water hammer is not a concern relative to containment.11 4,

t.

~7 containme'nt isolation' valves (CIVs),!small diameter piping in the Drywell and multipl8Ei ~ <(b

' Integrity for the;WO tysthmiue'ttthelongdissace between Drywell and the '.pf 1 branches.;VPlon the other hand has a cooler (IVP02SC) that is fed by an eight inch line i

close to the inboard containment isolation valve. This location will be analyzed as the :

worst case. '

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CALCULATION DEPil0nftSECTl0N CALCL'LATION NO.

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Supply side of IVP02SC: Under the scenario ofinterest high temperature in the Drywell.

4

. could result in the formation of vapor (i.e. steam) at high points near coolers (Refd l8)g g,

Thir could only occur if the system were depressurized: Since VP and WO a~re close'd '

I

' be developed since there's nowhere for the expanding v

' loo'p systeins inside containmcht (Ref.1,2,7,' & 8) a significant polume%i%;ifiyduld

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4

valve IVP024B is set'at 140 psid, which gives it a saturation temperature s6id330 F, ' i i

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j Ref.19). Not withstanding the above, the configurations such that Af4ipdiWould be '

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- present in the header supply and return headers as shown beloW (from Ref;14d). L,(

2

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^ ' I (The vapor collapse :.nd impact would occur, on the supply side, in the.4" supply headers :

JF.i

since as water comes in the 8" header it starts to fill the 4" lines, which already liave somed W7~

' water level (they're lower), hence the vapor bubble collapse will occur at the water

[W j intdce in the 4" lines.kince the vapor is readily colla;kible it offers nearly no resistance. a.f f Ml, iUritil all the vapor is collaRnb significant impact occurs. It's logical based on'they#

4J3"

'd pipe c. configurations that any major impact of concern to piping integrity would,thYoccur :

. at the end of the line near node 235. Since smaller impacts would occur in the smaller j

di unet;er lines and, the resulting pressure surge would split at branches, the resulting

, pressure surge on the supply side of the heat exchanger would not be ofconcern (see.

discussion in 3). ' On the return side of the heat exchangers the collapse and impact would l

~

occur somewhere in the 8" pipe. Only the return side will be looked at in detail.

5)

Return sid'e of 1VP025C: The worst case pipe routing i e associated with subsystems.

' IVP03 and IVP04 (Ref.14c and 14d). This analysis will look at these two subsystems as they are similar to the other retums but worst case (Reference also other analyticals in 14.). Piping in these subsystems are shown on P&ID, Ref. 2.

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,s

. IP-M-0435 0

,A N'M,,, j o IE i.

%.;. J.p

6)f lFrom thel figure shown on RLs 14a'and 14c it is apparent that the paths through~thef

'c'g

N N 8%upply leader and the various 4" line are different lengths so that an advancing water;@ O

~

'gM,g, eaches le m the return he~de~r:first,.?T

- tka MM front r.w n~the 8" return header at.different times. ;The brarich flow'with the shortesA A

%3s-F wk4

.Wwq ilis~tance to travel would co. llapse th~e vap~or S,u 44 a

n

- ~

. ~.

.a

'. at 1 w w mM

.c M.~

J &a' n c. y p@w 6Ww %y.flo.p~s

~E=-

v-X to co n

1

~

5.5 fthec veloday in the pipe under a full flow condition.?It.is W T W#

w e

' "4@

yd 4 app d_be.i_mu* h_ lo. w_er th,in_t_his ~dup ib ksdon'di,sc,usson above.W _! $j W

J pggj. th_e vil'_esty._w_sd_,5 ft/see wilbe,used in this a, rin E..

Nyg 4,W_ lowWiocityf5]

c.

3,a Moccur[sh destion~ of he' system fo r. -w

-i : y$

~.4..,w-. n 4 my a -. - u _ w,. y..

., r %o. p, a %.q g.

t,

c,

, 4 o

-e s

qm 4

y

.,qv j

8

' 1%, m.[7)hFoEco Rb mu'st d@ocud% thisto h' p~ pen the containmentisolation valv Q'

~YY a

7 ^1the pressure puls'e'would travel through the gate valves L

e o

j g

s N,

tv ; l pip *mg'systembaly using simple Waas e

?

a e

y Q ~ y tf e~q by %,f;pTr y n wu o av n)+O..j A. l.evelD all.owable,Wf 36000, psi. (2,.7-.1

,. f ; y *.s w L 8

-n -,, ov. r

_ g 7F

%g

{L
1. '

Q Hfollowpg6quation:

L'-

p< v Ze p~@tym:p~a~w awtge.

a qlm?y v;;:g y'q.:a{jf (

r a y:g mr

,m

- +

Qxp

.jg{

v ~. p s y; f

cl+4 PDog M,,7 -

v @n nmps w.c M 4t- -

Zuae o A 44+%

aWW O & ;.$ M + 9,b [N N P N JM V;.

u.

.a a

.'Y!

h ;w*

y m$'.h h.4 I,v" V

N mbws;% w mg.w>e

.. cf r s,

r,

.q

+

,, M

,@Me~L.ote tint A shape factor of 1.7 fian Marks l pg. 5-21 could be ap+ li to the allowable.

N 1, 1 ; W.

n.

%ypq above sii w w de.fo.- -.

fth....,-.. OK..- -.ded we. don,t m

nce plastic nnation o e pipmgis provi

~

7.

/g sU Y d Will n$t td ussd is the analysis, which is conservative. J 9n%+ i X

' eq %;l{!

m L }ma gi in 2

%y&3 %

xC V r

wik

.I9)Qw%; wpm.}pmw"s on;c.,,.ThNiiajl siss.nvy: areas clos m

m y.

-mnw y g n u

a ys y up illfoeti 9

fg

'L

',' w[ &v3[wL, 4:g n

+-

~gv

-m v

.n

.s s

e

' '@v.

w

%p;N sthe area ofmterest.gYt i

1p, 4.c c.

e

.Q:n[

Lv n,~f Mj&&W9f, s al*inment walls are very strong. [Thhy will not be' rigo

}

,:& "10)$y A m sa w

~~

a Anchors atDrywelland conta

,..;_.ilooked at here'. They are u ge to not e t e weak link. The configuration is such thath i

jdd b h

'J.

11i l

?.'

! pip lc ' stress.w. ~ill be li:niting. -

u

,y a

.~.y e.

I 6

4 1

. N1117 990)

l i

NF 161-3 (1/90J CALCULADON DEPTfDIVCECTION CALCULATION NO.

REVISION VOLUME SHEET,.

IP-M-0435 0

8-g.

ANALYSJfi The configuration of thepiping in question inside Drywellis shown below.),

v

[ _;p,y a

.y.t

j.

^

~

+

s

!pT dp

,,' g j j

';W. :ri g

... a, g,.

  • u

=, -

n

[..g

/{. ].

[

d

-Qj?

6 i,,. W ):'

n "gg;gy 8

Vk..w.$'Y

.. s

..i-

?.,*.. -

. GQ( o ltypt,,'

/

.,u n

t:No a T* 8' (7) k L t 11E*

1.7M" 8 ! ! ! -l 4.024' '

.(

. ;q a 99f 4VP03DB40h 6

s El. 770.00' g

. EL 7 rOR CONT.SEE 0

/

t

/

71 -

p 9

1VPO4 SHT.4 N:k,

[

(MsM f

0.74 5'~

, )f f

~

. 4.76 5'-

.o :

lV

'LTS(

Y MO.583'- W:,..

r 7'

.e.6%'d 43G.>a 1.rwm

~ hlVPQ3002IV' t'k

.. ( ;

1

/f

+o t

u,,

.=

p '.. h ~, e f

'*tt q

g

.v 'f;l' ' '

r,

&'[t t

~

QvPtBBAk) y

.,f'%,

J s

/

~;i ^

s '.

N n y $, h E

e (4VP03DO 8 Y( Y 34.,723*.

FORCgT.SEE PLAN B SHI2 e

4 Reference 14? Plan A l

Ntt1 4 W)

r

]

. o..

NF.1613 0190) -

CALCULATION DEPrfJNI5ECTION CALCULATION NO.

REVISION VOLUME SHEET.

\\

~

. IP-M-0435 0

9 2

\\

a

.r.

1

  • mar e

. e m m m a;ca y 4

s c,m..., +

+

ss.aswr.

.we go

,.3

._ewsmo g,.n

, y,:

%n U

s a

(
x

.o w.c w :S sL.

1,. _. o s

2 s.

m..

7 g.y y?dge 4

< p Mj. 3l _f ;,,.gn _.

i __."u$

i w

.4 e.

m 3,e

.,v n @ sy w u.
:,4 x

.s.,

x,. g;+ -.

a m_. p; w,.i u.a o

w

e o

,#.m,

gp..

y, T

,,.s i. e O.

~

~ ?v. ;

q

,g' p

g g

"; q q c

h.2 Mbda=Md y

^

i m.

~

d,[w-.e; M M

.L e

~=

, posAm a AE.8, 99,

WPoem W

, ~.

_p.

1 7.-

.sccinon 'e-2'

~b.,'.

m f

Reference 14c.

.y.

.,L"

.e

.c ; -

u

, +;;

e... :.

p z a-3

.]

iThe inipact would be~ expected to occur'near node 85. Coriservativel[u, sing 5.5 ft/se

,a j'i(assumption [6)andu, sing AP7. 29 AV(Input,2)'

. c $C g

c c, y.a.am',:

.y

~,

y%m m

n:

. w :...

"L_APM.29..t.5,57160 psi,

s w..

e.

m, p q.y qQ -.., Q >p j,,, sb,ov,t is;ap. jparent that as the press,ure wave travels upstream 1

the sectioriview

, y )'3:

4 ?.

1 s, x Based on,7 ei jx;4

' it'would be dissipited by the many branches..The header piping between node 85 and 230

,is well restrained by four 4" pipes connected to equipment anchors. The wave impam at -

d" vd.

",f.i,.t n.od..e 85;80 a.n.d,60 wo. uld. be.c,on. sequent.ly card.ed by the subject h.eade.r whic.h is w

'.%s.M~/.

?

w

. c 00 1 L

  • i restrained.?Hence the. worst case scenario wasjudged to be an impact at node 45 resulting -

7

.... ;,.ifoEe perpendicular to the pipe as follows below.-

.o 1 q

.3 y

u +

, [ !. Using pressure ilmes fl6w area of 8" pipe (50 sq. in Ref.19) the force at no e.d 45 would m.

be F=='160

  • 50== 8000 lb. NOTE that pressure times area is conservative since it.

assumes a full... flect.. ion.

re Conservatively, model the pipe as a cantilever Ognoring supports) as follows:

4 p

L 4 8000 lb. at node 45 4

N111-7 (9!90)

  • sa

=

NF 161-3 (1f/J)

CALCULATION DEPTOVCECTK)N CALCULATION NO.

REVISION VOLUME SHEET,

~

IP-M-0435 0

>10 From the figures above L can be calculated as follows:

1 A

s.

..a

~

,.c-g y

's_

[,x.

_q w.., r M w.e yi c.

.se f f r, " 4 *.

f'

~,

.g 4y;v

.k ; y, g,: [ r,," ~

f,

s

., A e 2.146 + 1,761 +.9 +.472 + A29 +.603 +.1A9,2 + 4.021.+ 7.863 - 14.723(& 7 4,4

' 4. 4. :.

s y

.f

, 1 e

a;

.a. -. <;.

.. - =.4.974' r ~

B=

1.752 + 1'.436 = 3.188' S.

~

r: 3

.,?

s

..m,

.Le.;[(4.974)2,[3,3gg)2j% =.5.91'

..5,.....

and

. M = 8000

  • 5.91= 47300 fL. Ib..

p

. It should be noted tidt the peak pressure at the highest stress point (node 7, Pg. 8) due to '

this sce.,nario would be red,uced due to branches, etc. as follows:

\\ c.

~ DLie to tlic largerires in the 10".' pipe' '

3 y

.:.{,, ;r y; J r ' 't W,;.

.c r

b 2; s

, P o'= 160 *

'-JD.10d.

I

> a i

! r7,98132-

,4.

.a.

y m ;.

r.. = 160

  • s

-; j.

~'

(10.02s c.,'.T 4

,c;.

.+3..

4

,. n,

,x.

gw g,

2p

m.c.101 psid 1-t e

8.

4 e

4 N1111(J/90)

S l T, ' g,4r'- -

4 o

?

NF 1614 $90) 3f,

CALCut.ATION

' DEPWlVSECDON CALCULADON NO.

REVISOf YOLUME

' $HEET h s q, h 3

W IP-M-0435 0-11 s

-p 4e m,v-se a,.

,a i

ld be reduced as m-

Then due to 4" branches IVP71 AB and IVP03BB th s pressure wou v wu 7W~ f-..

-:.~.

, e' AjQ; :%, if.

M U Ag;~3.{O O Wp,

3 -

s,

.m.

2./.'d.-

b'"

b d l-.~

. s ;.

--p..

4.Q 4L L.M,.M N.- $;h~..

sc Nff

.Y

  • J J

j.p.d r.f J v U k % h"')%f

%Mepnm a w

,A:.N[f. Br. a;& 'h,i= 12.73 sq{., +.4(R'd" /eU9)m-p~

-7a/C M b d

y h

h@T h

" n

@e e awt M Mg C"E A

C rea nc m,

y mr

'2 S

. s

Ares;1,0$a w.chg7,8.9 sq. h..
(Rd.y 9)<;f 7w,r+engpy
4. y~ ~,,

j r

gg,.

a p

Bran J

, %ae y

M, ~,W:pp;

%n $+~

~+, +ggn, i

, n, w, x.

a.

A e s'# '

?

~ ~ -

u~

A,.,'. e

~

' ' E ~ %m(For&@&*hes)w@

r n'+@m

. 4 Jl G

M 4: ?5 D d

W' ! 4 5 6 J r CM A

%p;.

v 4 -

i, w,e I P

    • e

~ 'wt9-

%':Q

. s 4? Ia' Jr m :.6C M-j y &r b' 1 Mt "

. ?". A 2~' ! ' w T

w 91.@mmF

~ v r'7 w 1 8.9 y' mwmm

..,n

,, y

- s ump e,.y@

g. m f

to branc r

a;jgn 101.

NJ WW Par.%

3,7ep. ym 7, W e.e. ",- _M,.~W._r F U.8 ', 4 2 73 y 7

1.

4 4

~,

a 4

5

$3 i, ' : ),.. $ ', '; Vn]a. + - e. -

n

~.

e'

'n.,.n. r

  • 4

.,.ur s

o 6 unu n.

.m

,,L,,; k ]i l'

. -. '&,x.p.~q.

  • e [ j QJm, ^2 N.

n y

e,.

.sn

.92

,3 s"m" s s

.a r

> c a*.

e s

nt p

w w+,e z~p'

9. r 3J. g,.. -..

4 q

m n.-

m_..O l w ';

L wy c.

Ed.

+

dz w s...; u nom input 8,l10" pipe data from Ref' 19 and using a maximum ww.

w+

smg the equation i

4.

MlJ j

r-operating pressure Dom Ref"14c, pg. 5, the above moment' and 151.0 (since we have fat

'o

.f straight p' y + highest stress po'mt)..

. W y4 4 4 m 4;3 m.. t,1 #,'

1.

n:

e.,

=

x-f ' ' vi :.

Mb r*

r

~,~n W,

M t%,

~ %f.

%;,%RW

' ': @,. r 47300*12-M* m.l - T T. f 1

Mty pr(1,35 t75)l0.75 k

L L.>

J M'

+~'"--~r

+

h f 7 N,.i4,3.,6$ k._>.f f

+ i 299-M9 v. gtM M _, p g[., hh.h

._.f. n

Q.

y.

Q U YY. gll..

m.. ~.

o M )+;1, i :

.c..

+ +

~

d

. m l( ' m c54.

%., w;,

3G.,&M l'

3. :

c

~ p' o

.,v. n..

g, y-2... -

m '. 1 ",

~

c

-~

't~

~.+

  1. s pu,p, ':

.5 K....S_li r.. r,..

4 4d '

H o m, #.WR*

- N A;aQ t:6 9 M, b 2.

.m.

3.,. o

.o.

%g{

y

-4 j l, L. j,, #,

w - p" 1.

%g p h'[,I. [ p.

~

,. 6. ',L;.,,,., e

)+.?. ~ '.f,y} O/]a(

y "

,> T ~'

c p3 J4

j

,3 g

t, c +4,

-#,,.~.,

a

'4

~,a

., m,

/m 3 qn.. v a,. 7;

,w w

,.t.

. m m, s

  • n v

This%

c--.~1. + r 4_.ou.rl.ev.,el.D allowable.

s. 3 y

7F fa., :r s-p ;.. a Y.,

JGe P 1~ v..T,,/ *.1,6 %.9

,y- ' 4,

,e. #. N. w.

kyrwell.

,,,. l

,g:

  • a 3, q'), b.,

J

_,., -o.s ip t

> b' E

7 m... _..

  • i '

i i; i1

.] }f j

,[.

m.

, h}

., / w.;. 4, p.,_

.. mu.A A,_m p,..p.g.n:6, u n, M],h h"{!

  1. /g gay 5"l l _l

,J hf. ?0 hk

_Xu %rget

.g. h ;

a.

m k

+ hg &g{.m=. n -,i t i4. -

khi h.h,,.{1 g

h5%.

w

.a :%*:: <~ w w 'v% Y. s.cv

+

4v ;.- a i lv ge > -

1 2

mt

.{.

j: g!

(,

h. 4 V.c tSe w

a v s+

<,. -. y Ni

. +w h4 2 3.Q; n b.. - t p

4 i

j,;.=..,yy g!

f yW

.p w, ? f gu;

4. 4.. p

,z;._..q); y Q

u-e.

k.r...y.

s L,

c s.w a, 3 y-M, g ". p a e.

3 gis m

c.e.

1

.,- c n e, sw o

f :. };... 3 a

(s 4

[

y

.,m m,

s 4

n, e'"

c_

t

..u a,+ S svQ Q.'. [ct, wd::~a{. [;. j;

..,e

+

Y t

1

..a,

.., n _

2:

m'.a

  1. a,

tu i i, i.,, -

4

'.-,3,$,..i _.4.. t a.

.t:

,m

, er

- _. c _->.

. s v _.

t

- +

l l

l lu lW ef i u

I I

M111,7 "m"~

e

m NF 161-3 p001 CALCULATK)N DEPTOWSECTION CALCULATION NO.

  • REVISION YOLUME SHEET.

< - 0' 12 %

IP-M.0435 m-v

. The configuration inside containment, outside Drywell is as shown below:

f p-

[

  1. ,y j

~ _, p. $.

i.

.i, r, s '

i u., y..,,

r. 7. r, v..-

, _...y s c.,g,u,

,~

t

' -.m'.'.

1 a.,

+

'j' +

,T'1i O 6, p e y [;

v

, J,k'g*7 [

d

.y'

'g.. j~'

).k 1

.C h *4 4

hTh [t dh 3

y r

& tuypo.o*[ l; ;,. &,./, nfg-MQ4.l;l Ql+3;k.Q 7%$g.~.

' [

'ElvP02 BB 40}--

ij I y

i

+

Q%,

' % Q, <,,

.di..-

. me,

...m y n

,. t,., a

,,a

+a-

'.S (&'. h Q.y.

,h.$..g ' '-QQg, Ikh.

v.. e.

..r

  • ht v

f; Y$

4(

(

') 3 I,

'Ekj)* h

).y y% n;p.:

.'q p

Lsyposa WT, l l,. t,3...

f._

s n x.

  1. .u g s..,

m

- u-

-,3 5

j

' im '

'/'

  • / -iwporooslA]; W j; ~,,,

.h flh '.

~c

+

a

' % k $).3.

.u '

7 g,

mgg W.

r.

. G.4

8

.i.

wt i

i.

(..

W..

y s

a j

e s

sy,

..-c_,,,

1e /

s

~

q.

l'.'

's ',

Y ih t

f s

. m

-su o-sp.

s

- n.sse

~

u, ew

{'

i A

1 " ' -

2

. 9 TO SUI,T -

,l

.oa.

+

3 c'

t

[

.. ft l

- (

(~

' i e

r c

3

.z/

c 1 -'

2 a

e ii

!,y t

e

.('

y 3

j

')

y,j '-' g (.' '=

,~r

. sw.

'q. og,.

.g g,W' t _',, gog

+

t 4

i

(

..,.c

.4',

p I

5

~

(,

4 4,.,.

f,LAtl m,

'l '

<0+ M.e.

Y i A.,,%

k.

(',

.r vj j,

r f;.'^?

l

?~

[ ',.)j w 4 ),.

y$

^"

.x,(

3. ", p c'+k-p y-'

N,

) y

+

;i

  • Q [b, h r e,. :
[5 'l M 7:

s 1.-

j

,s.

t s3

>e

,9 97

."U, 1.. < wu..J-

7

.e.

i, ? 'w. D f yg,,',

Reference 14b, JE F,, {,

w~ v i.'s'u, /a G.;;..

^ I U l!i U. Wi.

< j J.w.-s L.b s.

+N,*2

^

b, e a m%

.,g%g.

-9t 4

6 i-

.y r

3

  • ^3

'd

. + +. -

.;w 4

L-

,F

.'t,' ~ ' *. (;:? y asj/M'

$,)h '. f.

r

,s

  • j' <?.,D; t

't

., q',,$,4,7 37 y, -

'[;E M>i

+

+ 3., s..

5 s

i

,e

,. y *

- (-..

- g y

j 9...*

,'C f

y-l l

,; (. e s

+

i l

t i

'm l

y I

?;n

)

s I

- s 4

1 l

l 1

1 N1117 (HO)

I i

1 i

l

[

7 i s

.o

! 'o

. +

NF 161;3(1/90)

CALOJLATION !,

^ DEPilDMSECTION CALCULATION NO.

REY!$10N YOLUME SHEET ~

.i.

1'~.

" - m

~.-

i IP-M-0435 0-

.131.

&,qg-g, e

A a,

x y

J

....-,,...:: n..s.

c 1

e t

?

e a.

.?

);(

i The afrect of the 75 psid pressure surge 'on the above piping can be assessed using ths 7:2 a ffollowing simple' beam modeltTlie worst case force being at N. ode 20.

~ 3..
@c[:,;

3 m

3 v..,e.. :.m $;?)4 p A'jy,. s,.

m m s. q. %n.g?,(;x,,

xA.

el p.g.y;;'p g' T, &p* 5 p 3,, ;

,. y nep y*

.a; gps.m.k 'o - -. [5,6<;.pmw} i;;+!t. a.g; S, q,a-l.

g

.m t

w

-,d

.eyAyy

+

.p g.

m 44 nr j,

., t

- 'f e

e j;p e.u.

'r c

'V

(?,. psp f.y.-

~.y.

.. a g l.1 M,.D s y n y p q(M6g;\\.

y,

t

.. wj?q1.;m m,

A; ** ; o, 9 ohW, _

r ad-

  1. -
  • y, o..:

e m.;,,, J. ; _

' pfy%g?

w

,$[ L 7yy4

...a m.

p o g.9 s'%

n. wry.:*nf wrme p* *3 3 l.- -+

g

%y; 9/

$Wy

.Q

, &); Wh; bk h $ h ] A h2g'4U15 % iK M h??;. '

A-.y.y :

4&f& f l

&R

& kdL, J GQ 1

y, %w@N.%n.uw!)a pm Wpwyngkw ;ppkg.-w. : 4 u' age 11 as follows!

v

.1 > p+@:.u:s.i ax.4 pn u

y 7:gny j;4b~cinbe%m Ry4 ra

,f 1igt calculated froin~the, figure on p 1 T O Thele:

. ;W.

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NF.1613 (1/90)

CALCULATION DEPTIDIVISECTON CALCULATON NO.

REYislON VOLUME SHEET IP-M-0435 0

14 Calculating i (stress intensification factor) for 10" standard (1.5 dia) elbow using equation from Reference 22 i =.9/(tn R/r )2a 2

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= 26.4 KSI This is well below level D allowables.

CONCLUSION Based on the simplified analysis of worst case piping both inside Drywell and containment, recognizing the robustness of typical piping systems, the conservativeness of this calculation and the relatively low pressures introduced by the transients the effect of the transient is judged to be insufficient to cause a catastrophic failure of containment.

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PRESSURE TIME (SEC.)

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DATE PREPARED CHECKED ENG'R APP'L R EV. DESCRIP1

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260 45 F

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REV.

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c PIPING MATE RIAL MAO R NODE POINTS LINE PIPE DESIGN S' NUMBER CLASS v. FROM TO BLE SPEC. G R. PRESS. PRESS. 5 3.5 i WO55 lA-4 8 IOGCP S410G B 250 205 5s 19 0 IWos50A-4 D 100 Alos B 250 205 l'2 13 IWO559A % 8 loc cP sA-toc, a 250 205 3 19 18 iWos57A /4-B 3 40 146 IWoS5GA /+ D too AibG B E50 2.09 4 19s 250 nuloHts & 9 loo g-los e, zgo 205 495 20.9 i w'oJ & 6 4 9 10 0 A-IW 290 ZoS i i = VAN l R NODE POINTS VAL. STROKING VALJFIT. WT. LBS. OPERATOR wit PRESSURE TIME (SEC.) E TYPE RATING PRELIM. ACTUAL PRELIM. A2 V. FROM TO OPEN CLOSE 26 36 abOOA 15 0 340 50 56 gam VA. ISO 91 Y a k ? 8 itW n 't i 4% aa RELEASE RECORD x< REV. DATE PREPARED CHECKED ENG'R APP'L R EV. DESC@ g 0 01-14 -AG if'a #1h/ ofk2dbitats -

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l l PIPE DATA WALL INSUL. WEIGHTS - LBS/ LINEAL FT. O.D. SCHED. THICK THICK 2.ftN Th L

1. PIPE 1+2+3
4. WATER HYDRO 1+4
3. INSUL.

4500 40 0 267 t.5 10.79 5.51 1.98 18.28 5.51 IG. 80 4500 40 0.237 15 10.7 9 5.51 1.98 40.28 ~~ I. cGO Bo D.154 O.38

1. n470 O.18 8 0.30 I 958 O-l66
l. &&b
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\\ u. u n. v v o \\ I.05 0 60 0 Isq. 0 38 l.470 O. 12 & ~~ C. 4 2 5 40 0.260 I. 9 I&.97 I2.9l

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ipERTQW CABU

m nodhe Cod l

l SPECI AL FITTINGS DATA FLEXIBILITY INFO. k REMARKS VENDOR DRAWING NO. L O.D. THlCK v. 4.500 ANCHOR / DARLING VA. Co, W 842/2128 A I WO 551 A /g-esaa 4.600 CRANE A-4 l397-E lWo550/K-2&sA l 4 i 9 8 0 6 22 013 6 -$~b 1 PIPING ANALYTICAL & PHYSICAL DATA @>(" SARGENT&LUNDY FOR PLANT CHILLED WATER SYSTEM r(sle .uaime as_ ?)J U M PROJECT CLINTON - 1 k SUB SYSTEM NO. REE CLIENT ILLINOIS POWER CO. p-/379 .X. PROJECT NO. 1WO43 - d-4536-52 l l I SHEET 2 OF 8 o_--------_-

l SCHEMATl3 M E NO. MODE DESCRPTiom NORMAL OPER. 1 MAX. OPER. TEMP-AT Go*F. IMD53 s ) XCX 6 g\\ // h 4\\ NN k t i R. MODE NO. 1 EQUl[ NODE TERMINAL MOVEMENTS CALC BY EQUIPMENT TEMP. EQUINENT TIRE M l 9 POINT X AY oZ VDR S&L NUMBER 5 Go*P 0.00 0 0.0000.000 IMD5s P'NM' " i 220 Go*F 0.000 0.0000.000 sreue. Ancnon, 5 i 8 1 w' W o l l l S RELEASE RECORD REV. DATE PREPARED REVIEWED APPROVED PURPOSQ b O 01-Id -BS Jf'a. Unainshun1).M W ). Ne LA YO6 FDnMAG i i 03-i,- as ~ Mau V A. 4 d J-hA "f%'M !5 5 e g 2 ox-go-as v. c.,<. - ~ Msa,{. , "n.mu<..'a m ?,2 ;.;Li g : s o4-a-8r j'. W fz kMA-P.7d. % 4.;& %%:"ss"LCT?e i A

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EF MODES TO BE ANALYZED TOTAL NO. OF MODES REQUIRED I O. MODE DESCRIPTION: ANSTEC APERTURE CARD Also Avaelp e aim Apertwo M 9 8 0 6 22 018 6~ -8A CENT INFORMATION R MODE NO. NODE A LC. 8Y !NDOR DRAWING NO. h REMARKS TEMP' AX AY AZ VDR S&L v PIPING ANALYTICAL & PHYSICAL DATA FILM SARGENT&LUNDY ntnsid Is FOR PLANT CHILLED WATER SYSTEM .. w.c.. c 2 FATf X PROJECT CLINTON - 1 Mcawgpag; g SUB SYSTEM NO.

REV, 2"

ILLINOIS POWER CO. CLIENT m E0 /3 74/. V PROJECT NO. 4536-52 SHEET 3 OF 3

34,8990 2.50 G'_ (' ' , g g,g I c; g x. CONT.SE E 1 WO45 1a o g7 iwoq4ooil4p y, fp, EL.7 7 5.750 j

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mfsic, FOR SYSTEM r$ T Y

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7 f .,_n R NODE POINTS LINE PIPE PIPING MATE RI AL MAX. OP, DESIGN DES' NUMBER CLASS FROM TO BLE SPEC. GR. PRESS. i

PRESS, 5

20F 1 WO 553A 4 D 100 ^$ B 250 20 5 t A-10 205 270 1 WO 554A 4 B 106 CP gA M 200 275 1 WOS61 A % D 100 A, lof, 3r 5r y 'Es t 132' IWo%5 A % 6 10 6 cp SA.los 6 2.90 105 239 237 iWOMf AD IO(p op p y 2.90 209 Bfo $hh I WO K 3 A 6 D 10 o A-DG 290 209 320 350 i Woki C 4 P loo A-log 2Fo 209 blo blG I Wo Mi er 4 D too A. log E> 2 Fo 206 = = VAL *t a R NODE POINTS VAL. STROKING VAL./ FIT. WT. LBS. OPERATOR WT. PRESSURE TIME (SEC.) E TYPE R ATING PRELIM. ACTUAL PRELIM. AC' V. FROM TO OPEN CLOSE 165 175 GAT E VA. 150 91.00 gpSVA. { 205 215 V D40

c N

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PlPE DATA ^ WALL INSUL. WEIGHTS - LBS/ LINEAL FT. o.D. SCHED. P TONL

1. PIPE 2 fL
3. INSUL.

1+2+3

4. WATE R HYDRO 1+4 D

4.500 40 0.237 1.50 l#.790 F. 51 l.96 l$. f.8 4.500 do o.237 1.50 U u 1.90 1r 5.51 16.30 t.o So 80 0.154 o.38 1.470 0.18 e 0.3o 1998 1.05o 0 50 0.So 0.los 1.GS& l.oso e v o.Se u e 0.30 1 0.I60 4, (as B D 6 Hs 40 0.200 l&D 89.910 12.VIO 2.63 34.II 4.900 Ao 02s7 I.50 lo.790

9. 5I 1.96 lb 26 l

D 4.90o do o.237 I.$o~ Io.7 fo F,71 198 10 20 ANSTt:U APERT UHl : CARD .. -... u n,., ~5eWw ccm b SPECIAL FITTINGS DATA F LEXIBILITY INFO. R VENDOR DRAWING NO. E REMARKS 1 0.D. THICK y. 4.500 CRANE A 413 97 E 1 WO 55 4 4.500 ANCHO R / DAR LI NG VA, CO. W 8 4 2 21.2 8 A 1 W O552 A 9806220136-S o PIPING ANALYTICAL & PHYSICAL DAT/ DN Fu SARGENT&LUNDY ggg. g~ FOR P L A N.T CH ILL E D WATER SYSTEM 'ENf INEERS. AT* X PROJECT C LI N TO N - 1 %mmor. SUB SYSTEM NO. REV. $!1%$ y ILLINOlS POW E R CO., CLIENT 1WO44 '".1383 20 K PROJECT NO. h 4 5 3 6-F2 l l l SHEET 2 OF T

y \\; l SCHEMATIC OFl M M-NORMAL OPER. ,g I' l M A X. O P E R. T E M P. AT 60

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  • EQUIPMENT TITLE VE08 POINT AX AY AZ VDR S&L NUMBER-a 270 60*F O.000 0.000 0.000 k

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.* m, M 940 3 J 95 105 GATS <r D o EJ E 245 255 Gloss ojoo '256 3 { _Q70 280 2 FLG S. 150 20 _860 870 L ir 3I / a l 290 295 FL4 IO 885 695 2 FLG S. 20 .EE \\ 905 9o I:LG. 1: IO 'S w 8 -i' E D M ~7 5k yo $ mccupet7 wr. or oPeMToa m-y4 RELEASE RECORD REV. DATE PREPARED CHECKED ENG'R APP'L REV. DESCRi? g oB O ol-14 -Bs 6&k& mni.-

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PIPE DATA l-WALL INSUL. WElGHTS - LBS/ LINEAL FT. ~ O.D. SCHED* WP. THICK THICK P

2. ftU D
1. PlPE
3. INSUL.

1+2+3

4. WATE R HYDRO 1+4 TO 4.500 40 0.237 f.50 10.7 9 s.510 1."/6 f2 18.26 95'l I(c. 30 l

v o.237 4' y y y ( B.500 0 2fG 7.58o 3.200 !. G6'

11. 4 G v

v 4 4 4 i y y S l.050 80 0.154G 0.38 l.470 O.188 0.30 1.958 G V yG v v v v 33 7 o.840 y 0.14 7 s y 1.09 O.IOf 0.30 1 491 ,m_m,.,, - ~ 9 1.oso so 0.154c o.39 1.47o O. 16 8 0.3o; ! 496 fWf G m I.oso so o.15 % 0.S& I.47o 0.Its'& o.so(

t. ") S 6 V"

Y o.! atoo AwaMs on ] Acenure Card ( ) @ SPECIAL FITTINGS DATA B. FLEXIBILITY INFO. VENDOR DRAWING NO. REMARKS LL O.D. THICK V. 4.s o O ANCHOR / DARLINcv VA.co, u/8422l28 _ 48)1 WO552.B CRANE A 41397E T E IWO555 ANCHOF./PARLING VA.Co W692.lg2A 77IWos74 A 3.s00 4 ~ y f' I WOs75 A C rah 1E T \\ o 4 9 8 0 6 22 013 6 - b\\ PIPING ANALYTICAL & PHYSICAL DATA g p,gg FOR P L ANT CHILLED WATER SYSTEM SARGENT&LUNDY g, y " * *** " ~ SW PROJECT C Li NTO N - 1 ww y TSU7a CLIENT ILLI NOIS POW E R COM PANY SUB SYSTEM NO. REV. 1WO45 a PROJECT NO. ] 4536-92 l l [ SHEET 4 OF 5

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