ML20085B087
| ML20085B087 | |
| Person / Time | |
|---|---|
| Site: | Crane |
| Issue date: | 06/17/1982 |
| From: | BABCOCK & WILCOX CO. |
| To: | |
| References | |
| TASK-*, TASK-GB GPU-0555, GPU-555, NUDOCS 8307070498 | |
| Download: ML20085B087 (21) | |
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ET*:'A T1
? ?
Q
'There are three ' basic classe L
aus111sry feed.ater.
s of break response for musil b
. s
, ~:o Thesepres reaks withouc a g.,
a II. These breaks capable of relie i
. h,/
seL:.:!.
-, ;.lj o
v 3reaks/tha. t relieve decay hng all decay heat via the break
.,. y*..
~..w ead with both the EFI injection a=d
~ _ ;...:.c, w*.
~ 5ber bre,ak',.. G,
^
q.
.. G
.,o.
via 3.
Breaks *which do not accesaci
-.f3.f
- ca12, syst7rerepressurization.
actuate the EFI and result in
.*; u
.r
~.3
..,j The systeur pressure graasient jf
-Q, For Class 1, it is s for these breaks are depicted i seen that the Ec n Figure 3.
throughout the transient system pressure dircreases rather
? o.
and LPI injection vill probablyFor the, larger btraks in this y
smoothly Dj
=
a class. CFT actu.stfou occur.
only. CTr actuation will occur For the smaller breaks of thi y
for the short term stabilisati Auxiliary feedvatar " injection i s class on of these breaks.
~
s not necessary,.
For Class 2 breaks. the RC pr
~
j signal'(s2 to 3 mia).
essure will rapidly reach the EST With the EPIs e2
.n.
be established coincident with a slow systen depressurizatian s-ill AS trip lq
~.]I tion la expected.
the decrease in care decay h Auxiliary feedvster is not No CFT actua-eat.
stabilization of these breaks necessary for the short term Antonatic ESTAS actuation vill
- ^
SC secondary side' inventory i not oscur for Class 3 breaks.
,q, as the break is not capable ofs boiled off, system repressuriza i Cace the t on will occur 7
Systes repressucitation to thremoving all the decay hea the core.
4 generated in
\\
velves will occur for smaller b e FORT or the pressurizer safety
,a reaks la this class.
case, repressurication to the PDFV a1 d e the ":cro" break
~ :'
will occur in the first F,'trhf O f.; L*,...~. ' 7: ' s "9*,.
tes a,.Operat,g,r
.,s
' ~ ~ ~ ~ ~ '
^ 7 ;.-
. n.. '.7.. =,..
-.c
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't
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- ~ ~ ~ '
- ~
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(
~ t:':::.
_:i
. }.
5 J
t g
act. ion is j,
required within the first 20 a
C...
~ i.3,,..
- t.
out the transient.
For the 177-TA lowered lminutes either era;;e through-manual actuation est1h31ahment of auxilithe auxiliary fe
. J*
of The c.an ba
. a.1 v
/ -}y.-
to the ESTAS actuaticary feedvater vill rapidler syste M
RCS es..
secondary side SG pressa pressure, and sys y depressurize the J>
either the
~
l gd;
,s.
ssure vill stabill:e at
.r..h the la'ak rate.
ure or at a pressure where th
'r s
- "j For the Davis-Resse pla e EFI equals.
.s ?
accessery at some time gr nts (raired loop design) e y
~ 3 f."'
the itcreased ir. venteater than 20 caaures (p operator action is 4,.
..-N$.'
actor w e l.
ory in the loops that is robably I.0 ninutes) due to e
However, due to the lov available to drain into th i-operator rg,s,t, establish auxiliary feedwater inshutoff head e re-4.'
Pressuriter level respon
'".I,
ystem, the similar to that depicted f se for the first two clasorder to depres m
.;-jf CS.
.\\
or Case 1 and 2 of breaks will be ses section.
For the Class 3 breaks breaks discussed in the
,,, j.
Sa T!gure 4.
4 break and is shownThe minimum refill time f, pressu previous J
ill be as shown or the pressurizer is that f on Tigure 4
.y, pressurizer, the sacrease, possibly to full presssystem p or the " sero" nventory from the
- j.,
n auxiliary feedwater has b urizer levs*.cause th n'
atore o
Or :e the opetator actic result la een taken, the
' T eutaufge from the pre'ssuri systen depressurization will o to re s,
of pressurizer level.
For the zer, probably resulting l
.. s system repressurization f ll smaller breaks aa couplete loss of class 3 which results l I
o level vill increase and th actuation of the MPI syste owing the 3
a a.
t en stabilize.
Without auxiliary' feed m, pressurizar.
will saturate early in the uster, both the jgt leg sa turated.
transient and, for the Cl and e,oJ]d, leg ' temp remain g*s For the Class 3 breaks ass 1 and 2 breaks, will
.Q
?y,-
, once auxiliary feedwa.
. - l.
, -S g
ter'is estah.ished k
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.* e cold 1** Ce:peratures will rapid 1 d
kg, C W erature correspondinZ to the SG seco sid there thr'oughout the re:mainder of the tracs'
- eng, g,g y
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. r=ia saturated throughout the event.
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, c 4
The system pressure transient for a small break in the pressurizer will 1
behave in a simil.ar manner to that previously discussed.
The initial depres-aurization, however. vill be more rapid due to staan relief out the break.
The pressurizer level response' for these accidents vill initially behave like a very sr.all break without auxiliary feedwater.
As shown on rigure 5, an s
u initial rise in pressurizer level vill occur doe to the pressure reduction in the pressuriser and the subsequent insurge into the pressurizer from the RCS.
~
Once the reactor trips, systes contraction results in a decreasing level in
~
I the pressurizer.
Tlashing vill ultimately occur in the hot leg piping causing
- d i !
a an insurge into the pressuri:ce a:.d vill rapidly fill the pressuri:er.
For
?
the remainder of the transient, the pressurizer vill re= sin solid". Towards
"'j the later stages of the transient, the pressuri:er vill be filled by a two-j phase cinture.
Ecwver, the indicated level vill show that the pressurizer 1
is only partially full '
4 J
d
~,
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~
w..
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m
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no.
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tur
.r...
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,.-.-..,.....-.a..
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-r-
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_1
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.= m
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- s. i s s
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PREssug ozFr? LEVEL Vr TME
{
c
.~
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- r 7
. et FoR
au u
PREstuRiaCK
~
- z. u u
u.
e s.
n.
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25 e.
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=
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.- ~......
I ' '
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s.
.i r'
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.t,..
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4 1
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=a w..
pm.,
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..-~- -
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_- s We 1
Babcock & Wilcox C *? *.
~
~,.
- C<
Curve 3 cf Tigure 1 abovs the pressure transient for a break which is d
c too small in conhination with the operating IIPI to depressurize the KCS m
The d
steam Cenerators are being relied upon to remove a p.ortion of core decay heat
' -W If the reactor coolant pumps are not operating, and the pressure has stabilized
. Y
~~-
wear the secondary side pressure. EC; pressure may eventually begin falli
~ -
-- ~~
- * * - ~ " *
~.-
ng again as the decay heat level decreases.
i
..N If the Itc pumps are ore--P' L ?ressure may, or ::ay not decrease, it could eventually increase to some the EP1 refill and repressurize the RCS.
stable level as
. *b
~
The assur.ption for this case is that seccedary cooling is caintained. Curv,e 3 of Figure 2 shows pressuri:er behavior.
Curve 6 of Tigure 2 shows refilling by the KPI.
The hot leg te=pera-J ture quickly falls to the saturated te=sersture of the pri=ary s.
secondary side and controls ystes pressure at saturation.
The cold leg te=perature re= sins s1fghtly 1
subcooled.
If the E?T refill _and renressurf te the RCS. the hot legs can - _
l'
~
.}
more beco=e subcooled.
ence
{
N The operator needs esly to verify ESTAS actions and, if f
EC pumps have not. failed, leave one rur. sing iasch loop.
- t e.
1
{
,e-S l
r..}~.
- 'l i
e d
f S
e W
f l4
.]
g
)
t g
l r
b.
- +
=
.*[
I e, ----
. =.. _
.L
.g j
g W
f._
..n.
s i
,...-*.,o
_ e
~
I k
f=
~
f
,.. ~ '
s 7,,. 9.
y
.p
.w.-
49.
'W--bW a-
,-w---
m r~
e -"***Y. 0 2
.* '.}r'.-
~~
~E s
H
,.y.
z_3 s
~
...N Babcock & Wdcox
,.a g
.f
~
}.yg i
'.' ~.:3
'*"-~""*
s
(
j l
.a
- = i Curve 4 of Figure 1 show
. 5'> f.>.0 _.s, n
/L.
\\,,,_,_,,,
setor coolant pu=ps have b s the behavior of a sman b.-
- [-
~
een lost and the break is Egg reak in whic
.s.
with the RFI av'a nable to dep
~
~
k~
. Q_
r feedvater is available %ressuriae the primary
.,.sg R in cochination
.; i gen.
. l.o.ss of primary system coolant ev Although auxiliary a.**
terru
-B.
r
%ptionof cirealation I
- essurization around the loop.
entually lesds to in-pr the. primary system.
This la fonowed by a gradual of e
that the primary system Although not likely, it is co l-r_e,
q Ccte ttevalves before the pressurecould repressurize as high as nceivable
~2 i
Figure 4 stabilizes.
e pressurizer safety Coce enough inventory has b This is shown by the dash ps g.
direct steam condensation in th een lost from the prinary syst me in j,,
M,,,,,,
secondary side e region of the stess ge.erato em to allow
. a-coolant.
,. { """.".
the primary system down t the steam condensation forc rs adjacent to the saturation pr, essure es a depressurisation of o the since the cooling capabilities of the secondary side.
decay heat, pressure will n of the secondary side are need d d
sufficient to czeeed boil off iot fan below.tt at on t
.m e
to remove' n ary side, removes decay heat energy from thn the core. andcondensation EFI is stabic condition e systes.
steam generators and it will remain there until thThe reactor ecolant system action.
The pressurf ter level transient i e oper'acer takes further na
'l 2 during the depressurization s chsracterized by curve 3 of Ti 1
s.,
repressurization phase. The dashed 11, and Curve 4 of aigur 1
gure
~*
.-T.
. temporary is forced up to the pressurizer saf taeindicates the level behavio
~
bot le e y valve setpoint.
pressure
~g temperature win rapidly approach saturati During this transient,*
depressurization and it win with the initial system on 4.
m
. remain saturated during the whole t leg tempera.ture viu approach s atur ransient. Cold
-slightly subcooled durins' the re'
.at. ion as. circulation is lost, but may re 4
direct steam condensation devel pressurization phase of the tra 3,
main m
g ee l b..
will cause the cold leg te=peratops in the steam generator
, RC3 depressurization
~~ures to quickly reach saturation.
Colkl eg 7.
t..
y 1
,y-
- ~
~.,.
....m=..
C r
A
\\
Q o "b 7
^
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q p p. 9
>vsu
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. A g-s w-3w-a-
-a--
g-ygy w,-.m9
-yy
.n---.----m,,.g-,g
-.we-r-e re----w=.-F---
e mivmi.---
s'-
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gr--w-w---
.=
s c-u.
4 Babccck i
L Wilcox j.
~
ande_
'S ter:peratures.____________
may once a _. _ _ _ _ _ _ _. _ _ _
cre
-~
at secondary side press subcoef sligh Ly.oece the_ _ _. _.J._. _ _
~~
ure.
primary systes has
' ~-
may cause temporary int Subsequent filling of stabilizec
_7 as the primary side lev lerruption of steam the primary systen b q-ytessurization rises above the condensation in the staa y the KPI
~
e n generator secondary side level capability of decoy heat, the break and If the de-the primary system will the EFI is insuffici
,t coolmat is lost sat to once more offset
~ ' ~ ~
to
.3 this potat the primaallow direct steam repressurize
~
.,d pressore.
ry system will oncecondensation in the until eno u
This
.a decay haat or thecyclic behavior will stopagain depressurize to s
.At su.o.dary side
~
operator takes once the E?I and break c 1
~~
1 Curve 3 of Figure 1 sh some action.
an balance i
BC punps are lost, but which ows the behavior of PCS 1
does pressure to
~
tion.
The high pressure injectnot Icad to interruption of a break in which
~
1 the pressurizer has ion is available a d natual circula emptied.
n cirem14 tion to the The primary system remainexceeds the leak flow
\\
.,W Figure 2 shovs' the pressteam generator removes c subcooled and natural ore 4
s
\\ _--*
system pressure.
suciter, sever ore decay heat.
As Curve 5 of empties and continues to
.i centrol primary 4,
.._q.
,... m ~
3-
.)p. _
-
- _~
t
= = = = = =. = * =. =.
y y
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. = =. ',
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