ML20203K823
| ML20203K823 | |
| Person / Time | |
|---|---|
| Site: | Vogtle  |
| Issue date: | 05/13/1985 |
| From: | Gethen J, Holmes K GEORGIA POWER CO. |
| To: | |
| Shared Package | |
| ML20203K798 | List: |
| References | |
| RO-LP-202, NUDOCS 8608210360 | |
| Download: ML20203K823 (20) | |
Text
r e Geolgia l'owel (,t .3 i
rowea ornemien rec:.7.went VOGTLE ELECTRIC GENE
, (. F IpMTT].
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TRAINING LESS0i y g g REACTOR C0% ANT SYSTEM 3/4.4 - R0-LP-202 TITLE: DUMBER: ,
.SIMRATOR ,,,,-,,* .- ..'
PROGRAM: REVISION: -
AUTHOR: JIM GETHEN 3/11/85
, g DATE:
APPROVED: jgj DAIE: g/j3/{
REFERENCES:
TECHNICAL SPECIFICATIONS SECTION 3/4.4 REACTOR COOLANT SYSTEM INSTRUCTOR GUIDELINES:
, ONE HOUR LECTURE WHITE BOARD WITH MARKERS
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8608210360 860814 w i PDR ADOCK 05000424 l V PDR 2
R0-LP-202
- I. PURPOSE STATEM55T:
TO TEACH THE STUDENT THE APPLICABILITY ANL ACTIONS OF LIMITING CONDITION FOR OPERATION SECTION 3/4.4 REACTOR C00IJ.NT SYSTEM.
II. LIST OF OBJECTIVES:
- 1. The student will be able to determine if in violation of an LCO if given a list of equipment and a given applicability condition.
- 2. The student will be able to give the required action statement from memory if the time limit for action is one hour cr less.
- 3. The student will be able to look up the required action if given the applicable LCO if action required in more than one hour.
- 4. The student will be able to explain the bases for each of the LCO's.
l l
l 3 I l
- a n. s f- 19 70 4. o0
^
111. LESSON OUTLINE: NOTES t o -Tt- ?1to b .- oo - e o s o.nc s v.r
' <> o r ' ' ' ' ' ' (**"' C' ' ' o < ~ > o a A. 7 c ~ <s.L too t s o,-
ro a s t. Offc'**^ ; V4 WV'I
( y, ,, ,. ,, y p., ,,
.e s't
- 0 t f / n 'o 2 I a) 11ppe ,e a,s f ,
~-
.> stei. u e ,es. ea<eem s eer. .,- z .> o . . o r, r?i:.<s '
s i r. 3 ycaat,to V** f*L o s 2 ssa.< ac o' of'!s- - "". .
b) A t s.- M*e e t. c oo ua,,,- i , ,, , e -- ca cc ,,, oa ~r~ . r. .p y a,1 rec roove -c. 1 I
c.) m,1 <eu r.. ..a 4 c~c u re,,.a c., ee <. o . n ., o . . r. , ,.-
ir . - - r-,, o c 3 ( <d i r 5:n +rf ) io. r .. . s 6 aov ' .
2 sose. s
- a. Plant designed for all loops in operation
- 1) Maintain DNBR above 1.3 during:
a) Normal operations b) All anticipated transients 3- la or Sse~o ay -
T/s 3/,, 4 . e , L,,
e') A#v c an . C . -s
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Hav Foo o gge , g _ y ,j ,,
l b) te tem r t't.) w o pe. soaps w., s,.u , , . , , , , o c , , , ,,. ,
l I?c P c/veics( ncao.oro.
I i c) A , ,, ou Ft r,.p .s .a co T. . .
'd i) w . m 'ess+M4a gen ,,.,,.r r netsr cr es't r '. f ""
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'LI ad a T 5s i RC Looc ,4 o p t e 4,,, a f, . , p ,,, , / , ,,, m f.
D c air t"/ $ i togro :>et. F i t'. *g
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- vSf C ) ca. s se C.J6 f C *** 67t our se .a r .a R o er o ) (n e r. s s pr <rv e u t'*'
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lli. LESSON OUTLINE: NOTES 4 Bas 6s 3.) In mode 3, single loop provides sufficient heat removal capability for decay heat
- 1) Single failure criteria require two'be operable b) Point out footnotes to 3.4.1.2, 3 and 4 o .,
ou, ,'a u so, c . h ue
- 1) No dilution of RCS
- 2) Core exit temp is 10*F below saturation
- b. RCP not started below 350'F unless
- 1) S/G temperature less than 50*F above BCS
- 5. olor . 5 90, 0 0 6-, A r/s 3/9 i, ,,3 al a r. (e-se 2 tooe 5 / ym,,;3 pen ., . ., e c , , . .rr , e o a t, cooe s w.a u s ic.wo y,, wo ac e, l') P 4 ft. 11L ** **3 -
l e moscate sa m o t. 4 l
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- 4 6 ' C vg4r 1 / too s
( C) *gr ssst , w ,2 S i. o, c if f t1 J P ro e
l l e ra . rS o rC t e* 8 d cM , g e.3 3 3 s(rf ro # U 78 d i nv c. . A rc s g La o t P OPT'AfuE 3 ' **v s AshV if (ECM a,J. A .
h h 4 'l 9 OO %$ d S o!*>LAn o A s s s rc,so 20ao 2 j f) '. h po s.o o t* ) was e .*
g . g ,*.,,.te n o-J R (99tT o d em g
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- W+0 e d 99 . 99$ U W ea , ,g
so- e. f- 3170 9 -oo 111.
LESSON OUTLINE:
NOTES G*Shs a) In mode 4 and mode 5 with loops filled 1)
One removal RCP or RHR train sufficient for heat
- 2) Single failure requires two
'l . lo' 6 Svart.aan tones I's t ur,C ,g5 g,, , ,, , ,
a) I P H R. TPh.J Otsps & E es a ~ . .a e ,a,,, hos p,s o c.4 t. a s
) o ruu It n.t. rossa
- nse...aeer sg
- 2) 'L s/g s qu e, fr< I t,a . s y *), u.es t pa.,a c s cueg i
i b) Aec u. c 44t et i -* - = o t. 5 umer r. . e,3 i
i c) it a. c s c n .a a preno aco v . ..e r # n. .n oesraate o .-
ornan r r/g e- < , r i. rescu pes ,e.t r r> ~> e *.c o, n e oest ... e ., .
d) wim av nAt m~ .' s om..o a , .s .,e nao oevnr>ws' so2 VOLys d e s N. 4 4 * *) '
'7 C<3 J c 7 e 'a *I 77 L- I)' # '* II E '#'# U'
to a r' tr a , r a -h '
- 8. GAS 61
') sAmG A3 (, a.
)
0* (a s.b .$ avs ve vin) - L o o f.s M0f I' IU '$e a) 7. R u L TOsvl3 it CG u CQ O ' " '' ' ' ' ' ' ' '#' '#*
,J d f'f# #'" 0 d b) 'O o sta n is S ,ssA-J 2 ot -J.l e W s ** $ Of f 9& 88 6 1
- 4 CC' ^ 4 ft tj vc s w.e.c o +'s a see r n s o e-
~) ett0 0 of. fr m.'s D e .t is .) (c;ecerat:.0s~O.J /2(edtvr 0 ~3S
. .. . .-..a .. . .. . -- - - - ^ ' - " - -
-- =-- - --a - 6
a0. A t* - 39 tos- oo LESSON OUTLINE:
111.
NOTES
!& EM:s In mode 5 with loops not filled
- 1) RHR train sufficient for heat removal
- 2) Single failure and unavailability of S/G's require two 4
I I I .) No rG '
M Requirement for operation of RCP cr RHR pump
- 1) Provide adequate flow to ensure:
a) Mixing b) Prevent stratification c) Produce gradual reactivity changes during dilution
~
- 2) React,1vi,ty change rate during dilution stays, capability of operator recognition and control i
Restriction on starting RCP less than 350*F
- 1) Prevent pressure transients caused by:
a) Energy additions from secondary
f, 000$e bAfCTy 0LYl$
t.) seco d -
r/s V4 . 4 s ' I eW* C "'* " ' '
l D e e., e e w e , ,, as v u. ee 0'
34tf fing t l '),
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7 Lo tr-S<to8-oo ll1. LESSON . OUTLINE: .
NOTES
- 6) p('p tanesst6 14 os taci t 4 AM [
l C) uE o'ru sue tooE Soe r r *
- r r es o's o a, e
- f*
') 00* Y ' 'f "T**' 1. C 3 st , ty 3 ._. (, p$ a t) EdSU* E fil6 t $ut'E ,1 c u , r o:'
c a p,, f, , , ;., yu ss us,4 ? , s ,r e aor.
d) Bases I) Oue J s t o L. as e ,. na s, ,-e e4 Sjo a) o, et. c.c. a or ra e s c-$ 3 J A Cof' r
-e. e.,. es "L) T2 +4. 4 o c.ry. an e. , / s yo o pc'9
-?.) Orts +v u a. - 7/3 3/y . 4. 2. 7 D) kJ P t A. Ce o s .S a r r, .y vanatt Jelon e s. Rr O t'W e C e t' '" 5 'I Le 5 ( vsre'4 2 de 24 Sf gg,j z. / 7
- 6) mse a n c .- toats * , 2. , ^~'-
- 3 C.) wiru o, e La o t. C are v' y
- J o !w*^ its C *C;'*tC J ^ ' a t-
- oven,ee e4 s s e .~vre s e c.
- ) wr eraae ey ,8 (, uo s e. r g, f.ee r f,* st u o .J -a sd (G o t e , u t *> w o u te.1 d) 6A5e5 O Prevent pressurizing RCS above safety limit a) Each safety relieves 420,000 lbs/hr J -) Combined capacity of all valves sufficient -
d) Maximum surge rate from loss of all load J,)jr7 No trip i.. ) b) No steam dump 3, c) No PORV's -
~ - - - - =
- L e - L P. 3 4 tob- 00 Ill. LESSON OUTLINE: NOTES c.. Pacs w o u r i
- l. ' p(,t44,cn ty o 73, Bj y . </ 3
- 8) P e rt. - , , , , .r t. o r e *
- e t C ~
- m'
,) v o c .m r 6 ( c.,,,.t. ) te.e. rc< a . s,u- $ ,,s. va. I tua e 4 0 * * - C.
,, ,, , 9,7, a) t c ..a s'4 ,,. ,,,.,s c ,, , ., . . . . . . 4 <--o,,.
f ec *s o e.s .
- 6) Heecoc<c a -- eav e s t , z. , a - . 1 c.) Ac.rto-> S h t*
- m o .* ' p Pr ot.,
I gr ea ? ei-
.n se
- r*> t g o tro n s' r e* A f t !!
'a g , e, , e s r .> o r* s * * < , ! .r..... .s . ., ;'t. xa v se e o,s n) H.r a m.sc ary .> d e s.s .o.1 s
- 6) a.r sw rvo.,s , ,4 rn .... .. , 6 vo o,e :
i j2.) wen. Pa st_ ornse w, s s ,o.e...ner r*, e , -a "*r svervo 87 w, w n r c ',c o p e. , e., , r n , , ' "0 0.r t a ., o . a . r-s~,..,, . . , r . .a a . . ,, ...n 9
- d. Bases .
/ Maximum level J,y/ That is stays with FSAR analysis bE Steam bubble formed and not solid l 2)/. Heaters Eng[ Establish and control natural circulation A
B. Po tu t a. octun o Fe u er va a s (toe vi )
~
- s. ps..cf va. as - Ts V4 4.y i
O) M '- h0&$$ MQ $b $f 0 C . a v fe) EtCrW Vt\t sp t ( o f*Te rs Gt f h) M G O l.$ f , '2, , A~ Ds3 )
=
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~
ll1. LESSON OUTLINE: -
NOTES
- c. . ) e,.. a l
n) w a sy 404 oronf f0*JE J' ' ***f' f *" ' ' ' 6 ' f tS* * '
,,,,r-3 r.d a r ,e ,< 4 4 ( , rt(t ro.t r er u,> t ** s a.*t..-s sau4 SA a ., ,,aa r r o.s. .*
f* * # et dre /"v t
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5to uc va'*dt) ' '
- tsu.. tE ge ,a .s cr e . .a * * *
- d co c ' ' '
Ar e c.a ts- s o or- Jrnaa N ." r'es s- h oko et s s.u . a4 e s uerceaa waru." fo * * *
- J % (s riaur,(
$ t o n. us es Po n%s 's , ~ o r e.u n e .c t o .** n> . .*tsu.;'t s! o v-C v e.c s s . s t,, .5 (n - c ee .c ,4 c,.E 7' t v e .r a re:ree r '8"'d '""
O t. CLOSC e. u O f *4 rsu t,, FO#fc (*** ' S W " O# N ' " ' '< ' /d ' '# f g3 *Ji3 ,
- 0 A 0 W 'l O PQ s ele. ( d[U n.* f % C> t* r* e de f P *t
' *~ 900 r- 81r**JD g, ,.8 /g
- 4 9 eb < f A 29 o .2 t< or ,s.o.r , v o ,, ,, . .s .
r
- e . e a . . , s .*. G ov,,.e $
t 1
- 0) t 4 0 ?So t 10 8 'l 't o r's < 1 ', o ( , It(tsno.C z,6 gut ops *.stef s's 'l eno us2 $ e a. ite y t smao.r j -o
(.o w o.o I a o
*'~
$ Sul 01410. e.
- e a)
I h 't t>a o. 8 / , (,Hogg(
N *% i
- M.-
I' 0 =* f 7e oo,se yp7y(z ,-e es's osot e or J
/ e s r es r ( co Uac.'
a e
c HoJts et,.
& (Lost a.a Q(ecst. Pou tt. fens, r t e or w. .ha s u t t- o , t,,
poev -
b) c.co sc , m .a av . . t Pe.- ut r,, . . fa,e a <.,se.,o..a o ral cl) Bases f g. PORV's relieve RCS pressure up to 50% load e
decrease p With steam dump L y. Minimizes opening of code safeties 37 Block valve provides positive shutoff QA) Should PORY become inoperable
.py .g d $@ G8I h eM 88 N #4 * * *
, __ g L k hk-,--A y M^ ^ "
l t
e o . e f. p 2 tes0 - 0 0 Ill. LESSON OUTLINE: NOTES f bTt'st *4 !O A
- l. 7. f 3/V- V f a, ra.v m . sa .e -a r o'r'*c'!
b) Net e t.1 ea MoeEt 1,t,I d a Y C-) Ac, r o+3 :. *a r k w o n me, C J/s,ts r'er><A*Ct'? ffh **' f *#"*''
8 4
- c t- n IPs**J,we. T, ,- ,$ge w t Zuo'/.
Q o l'ckh' *'n t 's o e n~*~ . '-es w o n* r*'r sn't e s** " ' ' ' '
.s ,cce,3. s v. - c av,,;.. , ,, . .. e e co-6.. ,r.i ~"'-
Rra o e rtres s = Je sCe s o c ~s t D C,n s. C A **
1'"''''f '""*
di s se.
l .r.) Ensures structural integrity of RCS L X.)
Details inspection rigorous program of inservice
- f. LCAR DC,-re 170d 3 'f $ 7 E ' d E j, g,s ic. ,y( v r. s r ci. )
J y l ' Fs ' F "TI. -
' . M 4 I
- 0) Ec os o nes e M &- 4't$tte TL(Q .p . g(,4 off0AEip e.) (onm.datat
( A
- m oir Jf s ta (Aarrous v.
Me.s ev ed . % J V S T f.m P4e*
- c .e 64,r ) P eo 've ' > < *,,
! 7 *) ON N Jn Nr
>Jo , , a s Jn.g
- c. r e.
a- D I tow
/I r** e n t. %*
- f b , * ' #*
- e .<. toe.,s., J yJ r n , awo j
- 3. ) (irve re, n,t t 'o e.+4,. r- <- 1. 's c < c. r e ete o ' > u .er Co., . A . e- . r., e F' * * * ' ' ' ' e i- 4 m osphe.<c (s en e o.u Me "
- ven r. ~ lyt s s m Pas,.ces .r)!u on# ** ',
as s e n .r , a e, ., , ; s ,,,, .
/. ) gr o,r h b h , %$
$Y 4 h On, Q C) w* o<n 1 n Lt.e4 D C,r b ras) snss aa ca+< e asve, (. - le etqp,gg g ,Ot(em po .) ,s,n s .p te- m,.s e~ e.c pre s,a e or g,a h t ..p 'r r --m.<en en mc A, e ,o eps o g p . ,:,
u ,ie r ,...,,,,
,,a a , ., pe,, c'd* y 7 v M' C '_ .
.3 & r.o wr p
_ , ,,, ,, , .ma~e********"" ~g ess * ' ' ' ' * " ' ^~"
ay 3 e t
_ _aw a a
r _
,~.i. ,,z.s.c.
ll1. LESSON OUTLINE: . NOTES i
d) 3.,'s cc ny h s., . a . , s. s -..a ne.c<< e c. a. , 4, e . , < . , , , , ,re g p,,,,.,,,,,
co con M r .
. D f f,d o 110_s,fI L L D1 V i ti f*
- l
- 1) 7.' 3 . 3 /4 . 4. 6. Z A Pc5 ( c., ,c ., 4 ( +.,go ro e
- tet t.c. s u n e, r s a t) je, f., , g . , ,, , yo u,,,, 7 o c., ., ,, , .e
- s. ,r e . ..
t s '" * * * " ' *r -
~l \ <'PM usa g e r. os or ca e f a er .t et a r
\) I cafes .,,,q ,2,,, g(e o c m a,-, e,? , , , , . . , , ,
.,,,, a . ,a t er) .wr>
- 1. st eve, "
ss e r o
~/s
<I ) It) s teo s
r e ste . I f.r, t r. s - t # r
\
O . s y- t E. . a sr e fe, .3o . m ,~,
er va . v t. er se 4. <.o,- er S GFM @ e t. c o e crea. r g r enc r sa ,.,;3 f., , ,
,,,_,,, rres for E3 voo rres-a, *p i,.,,, see u a.c 71o r. .<. <n , - ~ .
- *
- w a it. r s. r . . . 3 ,, ,, , . . , ,,,g , , , , , ., , ,g,, , e,,,,,,, ,
B. Assus at .
,} ps. peg, ,,.)
- s se s f e e f ~19 ****n** L'
- ee n s- r
- Pl e - s ** T1
- ce s t e m n e ." ,
,u (, a. u o g s-a fse :, s e n e st ~b **f" " '
g, c,5 . g,, , g , s.,,ecro e.1 e s t '*b '
' I-
- & n o .~r t l
~4 vse ss * \ r. n.cs...e . , , a . , $' ,e ..,r. >
[ L'o~ ;rt / u ototme z so. ....' va- or -, - r as s r.. . - ,.
I k Wy erors e 2 ? Pr
- rg enr 2no, e .o s- .c a' . a st \
\
- c. AFPuratet .- ci oot.s e,2,1 Ma 4.
b' 34 Operational leakage
- 1) Unidentified leakage must be less than 1 gpm
- a. Ensure early detection of additional leakage l
.. . .. . .w e+ es eemd am * .___J - - Larm -
Ag -- - - - _ _ _ = d hiOlp
f
- 0=La' 97FO6*OO
~
ll1. LESSON OUTLINE: .
NOTES
- 2) RCS pressure isolation valves a) Prevents gross valve failure b) Inter system LOCA c) Counts as identified leakage d) Ensures early detection of in-series check valve failure
- 3) 10 gpm identified leakage provides for:
a) Limited leakage from known sources b) Known not to interfere with detection of unidentified leakage
- 4) Total S/G tube leakage of 1 gpm a) Dosage contribution from tube leakage b) Small fraction of 10CFR100 limits c) For SGTR or steam line break
- 5) 500 gpd in any S/G a) Ensures tube integrity for steam line rupture or LOCA
a) Any magnitude is unacceptable b) Indicative of an impending gross failure H, R c. t C u r e. , t ra y
- 1. T. S 3 /q , sf , 7 A. % ., u t:.2 uini.a Li~. I si c.. .y s ** e f. ta n as.e f -
Og ~~
.10 ff.,
S d.
- O $4 Cl * $ .IT few, f ,.$ (Pse S *T fe*s 4 ,7 (.,,
A *'o r N r. , < se u , , ,, r,,, a 12syp
_ . ... .. .._~.>.a-.. - -
-t_._- - - . .a
r
.,...,.m.,..,
III. LESSON OUTLINE: NOTES
- p. , A 6 4 e ra.f. ,, ,o A t.a. p eo,3 r t I
i
(* . A r 1 s e *J e vsre etG f , L , T, a-w si O' l' f* * , s r. a , ,* u es se ser *eer
, 1, ..g g ss ) , ,; , ,. p ,, , , , , , , , , , ,
f # " I ' f* ' r 8e m ;,- ryg; yp, g p,.,,,,,,g,,,,,, ,m,,, qp 4 , , , : ,-
- 1. s4 I10 g,e g r.u e o.4 e r .$ en.w C 3 e .o 4. 2.n .4 . *
- r '..s
( 080 4 o, c ow a s 9 ( ~ ,. , . . e . .s ( 7* **'ve't h) 'F fenir . ra r.r. A{evt
- wa.e s. r- s r- La'*
, u ., ,- a 6 u.sv.o i +**
.s , ,, , . e, , ,,
. r 4, o :.,,,,e,. u~ fn.e.< oi 1e s**1 1
}, , est pss o rp f d. f em* f f '
ce ,no o F- m., t .55 . L . .- /. . .....r r es a - i 7.y ,,v, 1 p ee. ; .o gugg rs *rrs t H T *- . *
- 14 A de E o't tL Ple ct sja( n Leti .. o a .4 s n e p g 3' F .y , - c . , , ,, F. , . .m . , ,, u IC ,q p ._ . ,. u , s-
- D SMGS s, Minimize corrosion a) Reduce potential for failure or leakage from stress corrosion.
s) Within steady state limits a) Provides adequate corrosion protection
'L% Within transient limits 8l)A) Does not have significant effect on ,
. integrity of RCS.
b)I) Damage time and temperature dependent
... .. . ee. 3 an.de.a em -.. . .. "" - "
.. *"***d O
u.J.3*ros.co III. LESSON OUTLINE: NOTES r ,a . ,. . s :. . . .. , / .. ~-
I, st~ r. a. n ,,s.,., - 9.s y., . . _ s
- 4. 4,.,r-
' ' ' f8 Mc P" 3 r 4 -. b. se e, .. . , ,, # . , t oo ,., e 2-) 4,,
'* 0/E p c. p., 5' * ~ lP * * * 'i s
- 8. nev6.ce - e ,, 5 5
' t ,3 , y
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D. bnsG S f, Ensure resulting two hour doses at site boundary are small fraction of 10CFR100 limits a .t) Following a SGTR b 27 Assumed 1.0 gpm tube leakage 2, Based on typical site locations by NRC 8 J) Conservative for Vogtle 3 Action allowing operation greater than 1.0 uc/ gram a ,,1) Allow for iodine spiking b .2) Occur during changes in thermal power
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. 1 L O - L f- 312O b - OLp lli. LESSON OUTLINE:
. NOTES I
u _
c, J7 Must be limited to less than or equal to 800 hours0.00926 days <br />0.222 hours <br />0.00132 weeks <br />3.044e-4 months <br /> / year
- 1. a) Approx. 10% operating time a h) These activity levels increase site boundary dose by a factor of 20 g, s) For SGTR
- q. 5) Must report at 500 hours0.00579 days <br />0.139 hours <br />8.267196e-4 weeks <br />1.9025e-4 months <br /> i,s) Lets NRC evaluate bef. ore 800 hours0.00926 days <br />0.222 hours <br />0.00132 weeks <br />3.044e-4 months <br /> are reached Reducing to below 500*F H M- Prevents release during SGTR l JH l 4--
l b2) Saturation pressure below ARV setting I
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to . < P . 3910 3 - eu lit. LESSON OUTLINE: NOTES b Ra.ses - ASu._n' Eciler and Prassura Code Section Ill, App. G.
) a. Combinations of temp and pressure to right of curves at) Can interpolate other cooldown rates z@. Assure prevention of non-ductile failure only p s. Shall be calculated periodically ,
a4) Using bases described in bases
'f ),d '. Secondary will not be pressurized above 200 psig ,
a-1) If temperature in S/G below 70*F
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lil. LESSON OUTLINE: NOTES K. s,. -- t. m. . .,
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.. Ill. LESSON OUTLINE: NOTES M .g Summary
- 1. Reactor Coolant Loops and Coolant Circulation
- a. Startup and Power operation
- b. Hot standby
- c. Hot shutdown
- d. Cold shutdown - loops filled
- e. Cold shutdown - loops not filled
- 2. Safety Valves
- s. Shutdown
- b. Operating
- 3. Pressurizer
- 4. Relief Valves
- 6. RCS Leakage
- a. Leakage detection systems
- 7. Chemistry
- 8. Specific Activity
- 9. Pressure / Temperature Limits
- b. Pressuriser c.b Overpressure protection systems (coes)
- 10. Structural Integrity is. R t. s v tm s l
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