ML20024C606
| ML20024C606 | |
| Person / Time | |
|---|---|
| Site: | Crane |
| Issue date: | 09/04/1979 |
| From: | Cullin J, Nirodh Shah BABCOCK & WILCOX CO. |
| To: | Morgan C BABCOCK & WILCOX CO. |
| References | |
| TASK-07, TASK-7, TASK-GB GPU-2215, NUDOCS 8307120867 | |
| Download: ML20024C606 (4) | |
Text
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l THE BABCOCK & WILCOX COMPANY hhh N
NUbii i. POWER GENERATION GROUP To l
C. D. Morgan. Manager. Tec M eni Staff
.cc:
C. E. Parks g
B. M. Duan-I From J
J. J. Cud.lin/3. B. Shah, LOCA Methods, Technical Staff gg g, File No.
Cust.
or Ref.
Date Sud. ANAT.YSIS CODE REOUIRD!ENTS A':D VERITICATION PROJECT:
9/4/19 I
ACTION ITIM 5 t
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A review of four frominent features of the B&W small break evaluation andel
-4=.s has been complaced as specified in Action Item 5 of the Analysis Code Eequire-Ig ~ {
QI~s.y.
- l' I '.'. ' ' w~4 3 ~;
menta and Verific.ation. Project.. This review was aimed at the following af ain=a*=
k
~
M$. ?c' [N._ "'$._ _.,. of CIAFT2 isimulatiods o.Y sma~11$reak trinsients:,,. (1) 'the d i
o a
._- m.
. - - -... ~..
" in vertically-stacked control vol.
-. y>'T '-,
43;-
. nique esplayed t.o prevent phase "p=~--W 9
tt.3 F_
--~..
.. ~.. ~. -....,:..
~
unes', (2) the use of.'a multipliar in conjunction with' the Unaon bubble rise w
- 1. m.
-:- w
..;- r - :r.,.; r+:=:m-..
, v.....
'r
'd; ^ * ' " M8-modal to account for void distributions in large, verticany-orienced control -
c
~
0;.. '
volumes, (3) sinalation of *stema generarv heat transfer particularly that
.{.
, ' attributable to -,~4hy feedwater, an: (4) pressurizar modeling within the 9.
.i s~r a..
present capabilities of CIAFT2.. It was.riginally presumed that the investiga-h D
tion would establish the sensitiivity of tise small break evaluation model to
~~
t
.ceen.~.. -
P c-1.:-E -
these selected features. Early"on, however, it became obvious that the analysis'.. *
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~
results are strongly case-dependent." and that the emphasis should be shifted
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- 1. Dual riow Path Modeline..m small b.reak evaluation.model uti
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i
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... 3.'i.MJ..
nodes to anow for. counter enrrene flow and"also to reduce steam:" pancaking". ' _ ' '
t t.
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between verticany stackad nodes during phase separation In this model; a vertical flow path is divided into two equal area patihk staggered by about I
..T ;.
one foot and assigned opposite directions 'at the node interfa,ce. The pre-I i
.)
sent study ' indicates that the dual fluw path concept as.used adequately de.
3 However, a staggered length scribes the mixtura height in the top node.
i of about 0.5 feet was found to provide'optinun results in the test casa used
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- 3 9/4T/9
..r, Fici 2 C. D. NORCAN in this review.
l 2.
Bubble Risa velocity Multiolier
~
n a Wilson bubble rise velocity nodal is used to calculata phase separation
[.
rates in the reactor core and RCS piping. A factor of 2,38 is applied in L
the cora voluna to account for the effects of the nonuniform void fraction
. distribution largely attributable to tha. axial variation in cora power.
This approach is well-documented in ECCS Analysis --t~f ation films and is In other ves-supported by'%th 70AH2 analyses and level swell test data.
~
sal control.volunas a,'maltipliar of 2.0,is used, again to account for non-
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unifona void, distribut!sa,, p&-ily becauss of stana production af flashing..,..
.c r.
- 5. W*_~."_'a.e._ in conjunction
- with. pr.im.ary metal ham't '.,In.this case, however, the suitipli...
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er has besa established also using FOAM 2 analyses whereis additional heat p.
.w
.1
.'c;99ft...
. ~.:..
sources were introduced. to approv4==e= the fh-W Trocesa. This procedura e
- l
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'..=;;..%,....
T.h. i?h~,..***".=. (.aa equivalence between heat addition at" constant pressura,.and sa t.,g',',.,'
-2
. :...,...... m.
<.w. "
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..aexpansion.:: ::n.e gr'D. :...-,. e present stu.dy concentrated upon con irm p
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li e
O.s"t*.dW.2.. s more defensible.. analysis, that the,v,a.lu.e used for the. bub.ble r.ise mu t -
_mu
- a..
y
. **** $ ~
~
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'. -i l,.:
i M U.-.M%N+':L. yliar is r==adia for its. intended application. -This objective ses met y..
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via GAFT2 de. pressurization casas in which the mixtura level behavior of a--
y r-e smvan
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2-
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single voinae.w. as compared to that of multinode model of equal' total volume.
.:4..
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?.4'Mc !
- Wilson bubbla rise amitipliers,of 2.2'and 1.6 applied to-the single voluna F.
vera found to "brachat" the' level behavior of the multinode modal in which
.~
v a.m.ana a..
smitipliara of 1.3 were used in each control volume.. nis indicatas that..
6
-A. - J.-. <.
n-It-a:
g u::;;:saryp.t. the bubbla rise amitipliar used in small break analyses-is reasonable..
".. 'p-
:b,.l. should ba noted;e,.....however, that the. effects.of spatial variations in void
.. : +.
s.--
?.
'.J.$
-m.. -
.m.~
-... - e
- ..;;..m g:;.2%
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y f
i ly b a proximated.by %..this technique.. Accurate best estimata.,
i'
- . ;.e..a
. g& g,.,,....,ract on,can on
,..e.presults will'.11kaly requir.e a finer discretization or, at laast,.a m S.l; O
af,.
l:;
..n. m.,
g.2 m;In Z
.. sj
- r ;,.r..,c.~,..1sticated method for phase. separation within large control volumes.
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Steam Cenerator Heat Transfer.-
.The evaluation' model uses, for each steam generator, one control volume to
- a. mme..
represent the secondary sida and two contro1 volumes to represent the pri-
.w.
- c. g. ;
l t25 mary side.~ The top primary node generally comprises the hot leg,after the s.,.
r "U" ' bend, SC inlet plenum *'and half the tube lengths. The steady state heat I
load in each'senarator is* equally distributed betvean the two primary volumes.
~ E.".[-hy.
6 The ov.erall heat transfer conductance is c h ulated based on the M H.t
.w..
Ioad and the initial camperatura difference across the corresponding primary
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and. secondary volunas. The UA value thus calculated is generally kept con- -
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.n stant during the transient if =u14=ry feedvst...e is actuated and naintained.
m P.
Aa --=d anefaa of the Davis Bessa 1 natural circhlation data Ofesor2ndum E.
V. Winks to E. C. Jones, " Description of T.a*urni circulation Test conducted at Davis Besse 1", NSS-14/T3.5, January '15,1979.) fn,14eates that, subsequest.-
to reactor and RCP trip, the bulk of the heat tzar.sfer la the SC occurs with.
in the secondary mixtura height even when the sydiary TV is injected ne. air i
the top of the tube bundia. The conductanes val.ca for the botton noda during
. a low flow b 52 initial flow) drops to about 20: of the 4=4eM value..Ia f
the top half of the tuba hundia, the heat transfer would seem to taka pimem i
only 'in tubes naar tha outar periphery, cone =4afny about 10 to 15% of tha f
.g v. t:
tubes, which are directly impinged span by the ATV' spray. The primary fluid
.a c..
in the r--*=ia-tubes. vill only be cooled below the secondary mixture level.
f, waan ;..
A more accurate. s4=sf ation of this behavior would require that a =ifefehmanal p
- (;y M.
sed.
g
- t..?..
c&.p,.....
SC model k.u... It.is at least clear, from the Davia Besse 1 data, thht g
.~-
- n
- n.: -
. ~. -
- a..
tha ganarator heat deman.d assumed in-small break analyses is optimistia.
,Qh',.~. ; tW,%. O n & W.v.%-'.s -4
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- Q *'*D T
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=4.ce-4.
Pressurizer Modeline in CitAFT2
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In. the ECCS ev=ta=E4a= andel, the pressurizar behavior is typically simm1stad.
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'niing's single equi 11srink con' tal volumi. ~Thus, during a transient..ths. -
II
'.'WM
.staan and' liquid regions remain at equal'tamperaturas' corresponding to satof *
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~ ration stacas at tha, pressurizer pressure. - Obviously,,the effect of this *.
g.I.
-.~.-""..1 WA."_.-.5
- limitationuponresultsis.Watirelycase-dependen't;thedirection,andrata-N
.s
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t
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of surge flow, hen.ce the interattien between' the praissarizar voluna and the..
1.
Q>,
t
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...RCS, vi21 vary acc.ord'ing' to. both breik's' ze and location and tha. timeduring M
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c,.; -~~a In shor
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ther tzansient.. :... t,'the d=Ff e4=ae4== associated with an'..equilibrisma '.
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volume....simula.tio.n~ of pres.s.urizar behav.ior eannot be concise.:ly datatsmined.' *
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For a: s---d a wr
.#C t:ransienti. say an insurgi so' sequent, 'to 53rW, th's shirt"comia'as... f.,.....'
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which are intuitively expected.are borne ou..t'.by a.,nalyses the equilibrium g
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W 17........
- v..
p
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delay or.entiraly =iss ths itp -c of high pressure setpoints and} trips.;'.. '.
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- rr.. cartata.atine, this limit.ation; am be onreona br =.:ing a==1:1=1==e-(
model for tha, pressurizar as.in the DEI simulation performed'by ECCS Analy5iss.
P
.~.
That case study was carried out wing both single equilibrium. volume and mi-f.
F tivolumepressurizermode~is.' Fre'dicted systen pressure and pressurizar level
're :ia.exeillene gree.dne, d.iff' r'ing, as would be.expdet.d',' i 'the'early. ',.
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pressure rise following th'e los's of generato.r heae. demand.
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9/4/79.;
/
- 6. D. HOW",AN Psee 4
,r DCAIID REstTLTS L
Specific casa studias and e='~'* cions performed for Action Itan.3 have been f
assembled in a e=' ~'= tion file retained by Loca Methods.
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