ML21125A334
Text
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.1-3 Revision 21 PALISADES SCRAM CURVE
+,J *->
+,J u
0 Q) a:::
E 0
~
u
(/)
1:::>
Q)
N 0
E
~
0 z 1.0
.75
.5
.25
.o
.0
.5 1.0 1.5 2.0 2.5 Time (seconds)
Note: Time measured from the point at which the control rod drive clutch receives the signal to release the control rods.
3.0
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.2.1-1 Revision 21 CONTROL ROD WITHDRAWAL INCIDENT HZP REACTIVITY INSERTION CURVE B
al 1-1 aj
,-4
,-4 0
.6 0 -
l7l Q) -
+) -> -
.4
+)
0 aj Q) 0::
.2
.0 10.0
~.o
~.o
~.o 50.0 60.0 Time (seconds)
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.2.1-2 Revision 21 CONTROL ROD WITHDRAWAL INCIDENT HZP REACTIVITY FEEDBACKS 17.1 M
CIS
.-I
.-I 0
0 17.1 Q)
..-4
+>
..-4 >
,"4
+>
0 CIS Q)
~
.1 _,......__,.......,.--,-.....,...-,-"'T"""-,--"T"'"",--,--,,.......,__,.--,----.--,-....,..-""T"""-r-"T""""-r--,--,,--,--,.--,---,--,
-.0
-.1
-.2 a----c Dk-Doppler o-----o Dk-Moderator
-.s....__.__.__.,___.___.___._..................__....._..__..._..__........ __.___._............................._..__..._........... __.,__.___.___.___,
.0 10.0 20.0 SO.O 40.0 60.0 60.0 Time (seconds)
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.2.1-3 Revision 21 CONTROL ROD WITHDRAWAL INCIDENT HZP TOTAL REACTIVITY rn
.75 "4
11 as
..-4
..-4 0
Q -
.15
.0 10.0 20.0 30.0
~.o 50.0 60.0 Time (seconds)
Total Reactivity
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.2.1-4 Revision 21 CONTROL ROD WITHDRAWAL INCIDENT HZP POWER AND HEAT FLUX 80.0 10--0 Neutron Power I
o--------0 Pm,,,- ""°' e..t nm:
80.0
~ -
"4 G) 40.0
~
0
~
't1 G)
N -
20.0 II 8 "4
0 z
.0
-20.0._._........._....1....11..,,,1_,.i....i....i....i,--'-._._..............1....11..,,,1_,.i....i....i....i,--'-._._..__._....1....11..,,,1_,.i....i....i....i,--'-._._""-'-'
JJ 10.lJ 20.0 30.0 40.0 50.0 80.lJ 70.lJ 80.0 Time (seconds)
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.2.1-5 Revision 21 CONTROL ROD WITHDRAWAL INCIDENT HZP SYSTEM PRESSURE 2150.0 IS -~ m
~ -
I) 2100.0 s.. ::, m m
I) s..
'1.
2050.0 30.0 40.0 50.0 80.0 70.0 80.0 Time (seconds)
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.2.1-6 Revision 21 CONTROL ROD WITHDRAWAL INCIDENT HZP INLET ENTHALPY
-8 540.0
.c
.-4 '
- l
+J e 537.5
~
.-4
< a:
6.0 t.O 2.0 0
5 10 IS JD 2S Tit£, SEC
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.2.2-4 Revision 21 PRESSURIZER PRESSURE FOR UNCONTROLLED BANK WITHDRAWAL AT FULL POWER 2600 2GJ cc....
(/)
Q..
2200 w
a:::
=>
(/)
(/)
w a:::
Q..
2000 1800 1600._.__.__........_...__.__.__._............ __ _._...._...... _.__.__._.............. _....__.,__.__.__,__,......,.........__.__,__.__.__.__.......
0 5
10 15 20 30 35 Tit£, SEC
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.2.2-5 Revision 21 PRESSURIZER LIQUID LEVEL FOR UNCONTROLLED BANK WITHDRAWAL AT FULL POWER 14 13
..J W
12 w
..J 11 10 9.__ ____
0 5
10 15 20 30 Tit£, SEC
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.2.2-6 Revision 21 PCS MASS FLOW RATE FOR UNCONTROLLED BANK WITHDRAWAL AT FULL POWER 0
X 50.0 r--------,r--.--.......,..._....,. ___.......... --,..------,---..----
45.0 -
(.)
u (I')
10.0
- z:
~
~
u t-a:
a::
35.0
~
..J (I')
(I')
a:
JO.O *
- c 25.0
- 20.0.._ _ _.__.....,__,..__._..__.__.,__
0 5
10 15 20 25 30 15 TU£, SEC
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.2.2-7 Revision 21 PCS TEMPERATURES FOR UNCONTROLLED BANK WITHDRAWAL AT FULL POWER
(,.J 650,.....,......__,._--r ________....., __
_,,. ______.,....,....., ___ --r ___.,.._ ____,......, ___
625
- * * * * * * * *.. * *
- PCS AVERAGE:
---COLO LEG
---HOT LEG
CORE INLET
~ 575 ****************...................................................................................
a: I 500.__...._. ____________....._._......,_......_ ______....._. _
0 s
10 1s ao 25 30 lS TU£, SEC
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.2.2-8 Revision 21 SECONDARY PRESSURE FOR UNCONTROLLED BANK WITHDRAWAL AT FULL POWER cc -
U')
a....
w a=:
~
U')
~
a..
..,.............. -----r----------....-..---,......,1"""'""---........ -,---...-----~-..-.-""""T........ _____ --r--,
um 900 IOQ STEAtl SEtERATOR *1 STEftH GENERATOR *2 600 '--....., __
IS 30 30 3S 0
s 10 Tit£, SEC
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.2.2-9 Revision 21 S/G LIQUID LEVEL FOR UNCONTROLLED BANK WITHDRAWAL AT FULL POWER o.o ~----,.--,---.--.--..,.....~...--........---r--,.--.---.--r-..,........-...-~,--,---.---.--.--,-..,.....~"T""""""I
-2.0 w-------.i--------w-------t+-----~----
.O
--- STEAtl GENERATOR
- 1
--- STEAtl GENERATOR *2
-e.o
-10.0.__ ___
Q s
10 IS 30 25 35 Tit£, SEC
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.7.1-1 Revision 21 PRIMARY COOLANT SYSTEM MASS FLOW RATE FOR LOSS OF FORCED FLOW 0....
llC u w en '
J::
m
_J w
a:
a::
- x 0
...J I&..
en en a:
J::
Ji.0 JO.0 26.0 22.0 18.0 L-.....L..__. _
_.___.__L-......L..--1--L-....... _L-......L..--'-_.__....... _.__--L-__. _ _.__........ _£.__.____. ___ _.___.__.___.____.____.
o.o 1.0 a.o 3.0 t.0 5.0 8.0 7.0 TINE, SEC
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.7.1-2 Revision 21 REACTOR POWER LEVEL FOR LOSS OF FORCED FLOW 3500.0
...---.--r--,,r-*?"""-------..--....... --,~-r---.,--r---.---r--.------,.--... p~--,*-----r-~
DIO.O am.o am.o
~
11111.0 IIIIO.O
!ilJO.O 0.0
~-.- _____....., ________ ~_
...... ______________ ----*~
0.0 1.0 a.o 3.o s.o 1.0 1.0 Tit£., SEC
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.7.1-3 Revision 21 CORE AVERAGE HEAT FLUX FOR LOSS OF FORCED FLOW LJ C\\I....
l...
I ex:
~
ID
- I l...
a:
t.J
- c w
(.!)
a:
a::
(.J a:
IH.O 15.6...
13.2...
10.1 --
l.t --
b.O o.o I
I 1.0 J.O t.0 5.0 6.0 7.0 Tlf1t:, SEC
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.7.1-4 Revision 21 PRESSURIZER PRESSURE FOR LOSS OF FORCED FLOW a: -
fl)
CL..
~ ;
ZIIO.O am.a IIOD.O IIOD.O ltlll.O o.o
~----....,-.. r-------........ -----.. *---*-*r---------------~
~--
-~----~--.._....... ___..__~___. ____.L,..~----L-...................... ---1..-----~ ~--
l.D a.a J.D t.O 5.0 1.0 7.0 Tit£., SEC
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.7.1-5 Revision 21 PRIMARY COOLANT SYSTEM TEMPERATURES FOR LOSS OF FORCED FLOW li50.0 I
I I
- PCS AVERA&[
---COLO L£Q m.o..
tt>T L£Q
r.oRE IN..ET
~
IIID.O -
~
~
S7S.O..................................................................................
SID.I r.. *---------..i..az.:.:..:.:.:=-=.:=-=..:-=.:.:.;-:.:-:.:-:.:-:..:-~-.:.-:.:--:.:-:.:-:.:-:.:-:.:-.:.-:.---..,~=----.-.="'-..::--::--=:
535.0 500.0 ________ _. *.__.._ _ ___, ____...,. _____ ---L.....*......... _.__.__.....__,___,,.._...__...._
o.o 1.0 a.o 1.0 t.o s.o 1.0 1.o Tit£. S£C
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.7.2-1 Revision 21 PRIMARY COOLANT SYSTEM MASS FLOW RATE FOR REACTOR COOLANT PUMP ROTOR SEIZURE
-I u
u Tit£, 9EC
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.7.2-2 Revision 21 REACTOR POWER LEVEL FOR REACTOR COOLANT PUMP ROTOR SEIZURE 31500.0 ----*---~-------.---..--*---------*------,-------------
DJO.O Jlilll.O aaoa.a 1sao.a IDDD.O SDO.O 0.0,.__..._ __________________.._ _ _._,.__L,~.-------....... --a.--.---__._..L....-------
0.0 1.0 2.0 3.o t.a s.a 1.0 1.0 Tit£, SEC
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.7.2-3 Revision 21 CORE AVERAGE HEAT FLUX FOR REACTOR COOLANT PUMP ROTOR SEIZURE N
18.0 lo..
I
~
CD..
lt.O
...J lo..
a:
~
lJ 12.0 C,
a:
a:::
lJ a:
10.0 8.0,._......____.,_..___.____.._.............. __._.............. __._.L.......... __._...__.___._...__---1......_~---'-.L..._...__._~
o.o 1.0 2.0 1.0 t.O s.o 6.0 7.0 Tit£. SEC
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.7.2-4 Revision 21 PRESSURIZER PRESSURE FOR REACTOR COOLANT PUMP ROTOR SEIZURE l'R£5Sllt£, PSJA i
I I -
I i
I 0
0 0
0 0
~
I
\\ \\
i
~r
\\
-I
' l
\\
t:r 1
tf
\\
i l ti t I
'f c~
l t
t i
t 1
I Cr r
1 r
1 1
0
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.7.2-5 Revision 21 PRIMARY COOLANT SYSTEM TEMPERATURES FOR REACTOR COOLANT PUMP ROTOR SEIZURE I
850.0 -----..----.------..--,-...-.-.---.-T""",--....--.--.-..--...... --,,--.,,-.,....-,---,,--.,,-.,.....-,---,~
125.0
- **********
- PCS AVERAQE
---CW) LE8 M
tllT l.E8
CORE ltl.£1' 575.0 ********** ****************************************.***
550.o r
---=--=--.::..;--=-=-:.:-:.:.-.:.:--:.:-:.:-~-.:.:--:.:-::-:.:.-.::--:.:-:.:-~-=--::-:.:-:.:-.::--::-:.:-:.:-=--:.:-::-:.:-:.:--:.::-:..:-.:.-_--
m.o..
500.0 L............... _..........L_........... __._.1....*-----................1.*_....__._............... _...... _.__,___..___,,_....__.___................... _.._...
o.o a.o a.o 3.o t.a s.o 1.0 1.0 TU£, SEC
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.10-1 Revision 25 POWER COMPARISONS - EXCESS LOAD 0
5 10 15 20 25 30 Time (s) 90 100 110 120 130 Power (% RTP)
Actual Reactor Power Decalibrated NI Power Decalibrated Thermal Power VHPT setpoint
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.10-2 Revision 25 PCS COOLANT TEMPERATURE - EXCESS LOAD 0
5 10 15 20 25 30 Time (s) 520 530 540 550 560 570 580 590 600 610 620 Temperature (
oF)
Thot Tcold
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.10-3 Revision 25 PRESSURIZER PRESSURE - EXCESS LOAD 0
5 10 15 20 25 30 Time (s) 1800 1900 2000 2100 2200 Pressure (psia)
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.10-4 Revision 25 PRESSURIZER COLLAPSED LIQUID LEVEL - EXCESS LOAD 0
5 10 15 20 25 30 Time (s) 20 30 40 50 60 70 Level (% Span)
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.10-5 Revision 25 COMPONENTS OF REACTIVITY - EXCESS LOAD 0
5 10 15 20 25 30 Time (s) 0.5 0.4 0.3 0.2 0.1 0.0 0.1 0.2 0.3 0.4 0.5 Reactivity ($)
Total Doppler Moderator Scram L _____________ _
1
\\
\\
___________________________ \\-
\\
\\
/
\\
\\
\\
I I
I I
I I
I I
FSAR CHAPTER 14-SAFETY ANALYSIS PARTIAL OPERATING FLOOR PLAN EL 649'-0" Portions of this page have been redacted per 10 CFR 2.390(d)(l).
FIGURE 14.11-1 Revision 23
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.12-1 Revision 23 REACTOR POWER LEVEL FOR LOSS OF EXTERNAL LOAD EVENT
-~
0 a..
. JoQ.o.o 2500.0 2000.0 1500.0 1000.0
- 500.0.
. 0
.0 2.5 12.5 17.5 20.0
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.12-2 Revision 23 PRIMARY PRESSURES FOR LOSS OF EXTERNAL LOAD EVENT 2500.0 2600.0 0
. iii
- a.
Q) 2400.0
-~
VI e 0..
2200.0 2000.0
.0 2.5 5.0 o--.:--a Pressurizer o---o Reactor Vessel 7.5 10.0 12,5 15.. 0 17.5
, Time (sec) 20.0
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.12-3 Revision 23 PRESSURIZER LIQUID VOLUME FOR LOSS OF EXTERNAL LOAD EVENT 10~0.0 1040:0 102'.0.0 1000.0 960.0 1:~Uf
- ~a.~
Tim**** J*ec.),,.*
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.12-4 Revision 23 PRIMARY COOLANT SYSTEM TEMPERATURES FOR LOSS OF EXTERNAL LOAD EVENT (I.)
I...
0
~
a..
E (I.)
I-540,0 520.0
,0 2.5 5.0 0.0*
12.5.
5 1 '
.)
7.. Time (sec 15.0 17.5
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.12-5 Revision 23 SECONDARY PRESSURES FOR LOSS OF EXTERNAL LOAD EVENT 0
. iii 0..
Q) 3
(/)
(/)
Q)...
a..
1000.0 900.0 800.0
. 700.0 600.0
.o 2.5 C Steam G.enerat9r 1 0
Steam Gen.erator 2 5.0 7;5 15.0 17.5 20;0
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.13-1 Revision 33 Reactor Power, LNFF Analysis with Off-Site Power Available and Steam Dump System Disabled 1(10 llO 110
-40 *..... -............ -.............
20 *.*... -.............,.............
O 0L====1j00Jt:=====2000:i::;;;;;;:;;;;;;;;;;;;;;:;;;;;;;:;;3:IC+/-O===;;;,..;;;;;;;;;.!f.lJ0+/-;;;;;;;;;;;;;;;;;;;;...,-5000.t;;;;;;;;;;;;;;;;;,,.;;;;;;;;;600J;t;;;;;;;;,,,,;;;;;;;;;;,,-J
]OOII Time tseci,
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.13-2 Revision 33 Primary Coolant System Loop Temperatures, LNFF Analysis with Off-Site Power Available and Steam Dump System Disabled
... """"'... '-.'\\-..~1,o... ~,,. '\\,i"I 1000
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.13-3 Revision 33 Primary Coolant System Loop Flow, LNFF Analysis with Off-Site Power Available and Steam Dump System Disabled 3
- O i:i:
- a.
0 j (j
er:
7WQ *..... *..... ** ***
al!OQ
<l5l.lQ
,ooo.................,.....
OH **OM0,00 t,.,....,,,,,o,.., ** **-*+* 0 00000 0 0 000,00 ******H!***" 00 00000 00 ou,oo o,oo~oo,.,.,,,,..,.,..,,,., -
- i*** 0 0 O**"*******"******
~**.. **
- 1** ***** ******* ******
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.13-4 Revision 33 Pressurizer Pressure, LNFF Analysis with Off-Site Power Available and Steam Dump System Disabled
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.13-5 Revision 33 Pressurizer Spray Flow, LNFF Analysis with Off-Site Power Available and Steam Dump System Disabled
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.13-6 Revision 33 Pressurizer SRV Flow, LNFF Analysis with Off-Site Power Available and Steam Dump System Disabled 15 -----..... -....---..... -...---..... -...---..... ------...---..... -...---
,o...... -...............,..................................................,.....................,.....
~...... -............. '.... -.....
. It I
- . 11 11 1'
11 I
. 11 II II
- 11 I
+**..... IJ....... 1 I
I*
- I
~
I I
. I I
.... ~ ** I **
I 1
I I
I I
I
... l.. 1.*,;... J... ;...
- ......... *..)**......... "..*.... * *. ****I.. *............... *.......
I l
I
.... J ;... *****........
I * '. '
- 1.
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.13-7 Revision 33 Pressurizer Level, LNFF Analysis with Off-Site Power Available and Steam Dump System Disabled o~----,----
-~-
dO.............
30................,.. :*****"******
~--*......... *-*.
............ ~
.. """" --~---.... *-*"-**!*.................
~:
- ~
- 1 "\\
.. -~*..
...... -:-***.............. -~*..
....... ~--*................
- o ~
;ioo1000----.:.-~~~Ll 2000 ffil!O Tim _ (seel ro:x, dro:J 100!)
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.13-8 Revision 33 SG Auxiliary Feedwater Flow, LNFF Analysis with Off-Site Power Available and Steam Dump System Disabled 35----------------.-------------.--------.
~,u*
~. *****. ***** ******* j..... ********
- ;.....** ******* ****..*.. (.*.*....*.*...*. *!*....... -***.... :.. ******* ******** ******i** ******** *****.
e J:I ::.
,.. -..... ******* *i****.......... * ***,... T* ****.......,.......... j,.
- ** '"'" ***** *o~u,"' * *****
- _,.,, ** ****** ******" '"' '"'"" j.. ******** ****** -*****
--****'............. ~............. -***....:... ******* ******',,..., :.. ********..,.,..........
O*~---"':':':-..--""':':':':"""'--...""""':":':':"---""":':'=""""'--"""'=c='=""-......,-":':':':.......,..--~.
0 1000 2000
~
&!'.Ill dOO'.l 7000 Time (sect
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.13-9 Revision 33 SG Dome Pressure, LNFF Analysis with Off-Site Power Available and Steam Dump System Disabled 1000
'i I
! I
- a. I i~~......................... ~............................ ~....................................................................................... ~.......................................................... ~
I 5llXl
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.13-10 Revision 33 SG Liquid Mass Inventory, LNFF Analysis with Off-Site Power Available and Steam Dump System Disabled i
,o:iooo Ill I ti el;1IXKI
'5 !l
.J.. s i *
(S E
J -
"'"u~,..,.u~
10CO
- ml ml Tim* (sac)
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.13-11 Revision 33 Reactor Power, LNFF Analysis with Off-Site Power Available and Steam Dump System Available 51D 1cm DX) mi 3IXll Time,*)
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.13-12 Revision 33 Primary Coolant System Loop Temperatures, LNFF Analysis with Off-Site Power Available and Steam Dump System Available i
j l
' ' ' l
' ' 1 :
j l
IF<<.,,~,,..,..,..,,~,...;,,..,.,~.,,,.._,.,..,u,.,.,.,~,~*"""'"'"""w,,u,~*~..,, "' '"'""
i i
~
1oo:I 1500 2B 2D DD T1111(11eJ i
I n,,..,.,..,...,.,.,.,:.,,.,,.F,..,.,.,.,,,.,~.,..,;:,,,.._,_,n,w,.,.,...,,.,,.,
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.13-13 Revision 33 Primary Coolant System Loop Flow, LNFF Analysis with Off-Site Power Available and Steam Dump System Available 1~~
...............,.*.................,................. +
.............. +............... +,............. -,+...............,.*.................,................. +
.. ***.......... ~
J II.
-tlOO i
o---------------------------
0
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.13-14 Revision 33 Pressurizer Pressure, LNFF Analysis with Off-Site Power Available and Steam Dump System Available i i 2100 1-*****,**......... '1'.................... t...................,i.................... r...........,....... l..........,...........,.................. '1'...,................ 1.................... 1....................
.. i
.. :m:J~.,.............. ~..........,...........,.................,,..............,...... k.................. b.......,......,... ~.................. ~
- ,.................................... ~..............,... ~
- a.
J i 1000...,.....,.............,.....................,...................,,....................,.............,....... ?.........,.......... ~....................,....,................,..................... ~.................. ~
i
!llO 4Clll
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.13-15 Revision 33 Pressurizer Spray Flow, LNFF Analysis with Off-Site Power Available and Steam Dump System Available I~
.a -
i~~................ ~******.. *****......,
................... 1.................... r................... ~.................. 1.................. ~................... 1................... 1.................. ~
,~~
................. -............................................................. ~..................,................... ~.................. -....................................... ~.................. ~
11 ro j 1~~................ ~............................................................ ~.................. ~................... ~.................. ~...................,....................................... ~
... i 11~ ---------------------
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.13-16 Revision 33 Pressurizer SRV Flow, LNFF Analysis with Off-Site Power Available and Steam Dump System Available
,;ti) 1[);170011Wcb1Dli 07:32;22 lfflLT 1100 2'0J
'1111 Tlme(HC)
-eFi\\1-16 "tiA\\l--1N
- <:i RV-104*I
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.13-17 Revision 33 Pressurizer Level, LNFF Analysis with Off-Site Power Available and Steam Dump System Available
~
'i:
U) 60 *..................................
................ *-:.... '............ *t****.............. -~'..... '........................... '.. -~-'................ -~-*............ '... -~****.............. **j***............ '... -~*.................
UI 40 -........ * *+****.......... :............. **+*****..........
C.
I I
I I
. V\\ :..
JQ.... *************j................
500 1000 15~0 2000 2500 3000 Time (sec) 4000 00 0000
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.13-18 Revision 33 SG Auxiliary Feedwater Flow, LNFF Analysis with Off-Site Power Available and Steam Dump System Available 30 *******--*..... * **i*** *** * ** * *** *** --* *r**--........ -- *-- -
~ * ** * ** * ******... *..
- ***** *** *.. *.. * --*r*...... *** ** --*.. * *r*******-* --... * --* *1* ** * ***.......... * --i --* * ***... --* --* --r * --*********--...
- I~
I I
I I
I I
I I
I
~
11'1 25 I
I I
I I
I
........ y,,,, **, **.**.***.**, ***.**.**..**.**.**.,,..............................................................,................... y,,,..* *.* * *.**.**.
I I
I I
I I
I E
,,Q -
I I
I I
I I
I I
I I
I I
I 1
I I
I
- ,**************-**-**.******************..-*******************1*******-************,-**-**********-*************************.,*********-**********1*******************.,..--.......*.......
I I
I I
I I
I I
I I
I I
- ** * ***************** * ******** * ******u*u*****u*- ******* * ****** ** * **
- ********** ***u******* *** **
I I
I I
I I
- *** *****"' ********* * ******* ******.. ** ***********-******************* ********.. **********'-*****H**** *** *** ** ***** **************..!********* * ** * ** ***** *******n**********-***--* * ***** *** ***
I I
I I
I I
5 *** ** ** *******1 ***************H**: **.. *.. **********:******************
- .. **********:**h>******** ** **!*******************:*******************
1 1
I l
I 1
I I
I I
I I
I I
011-'.....................................................,...................................,.....................................,.......................................................
0 500 1000 2000 2500 3000 4000 4500 5000 Time (seo)
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.13-19 Revision 33 SG Dome Pressure, LNFF Analysis with Off-Site Power Available and Steam Dump System Available 1000 -------------------------------
900 * ------~~::..:::.:;:a:**.. ** * * * * * * * * * * *.. * *.. * * *.. *.. * * * * * * *.. * *
- u Ill dJ...
~
000.................., ******************: ******************~*.................................. *~**
~
- a.
700................................
.............................. 1......................................
000.......... ****1"*******************... *******"'***** 1..................
** ************1,************* *****h*-****************-' ******** ********
fi(]Q........................................................................................................................................................................................................... ~
0 500 1000 2000 2500 3000 4000 0000 Time (sec)
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.13-20 Revision 33 SG Liquid Mass Inventory, LNFF Analysis with Off-Site Power Available and Steam Dump System Available E
.0 -
1500JO _________________________..__..,.,"'!',..__
125000
~
~
I
- * ** * ** * ** * ** * ****.i ***, ** ' ** ' * * *** *** ** ~....................... ' ** ' ** ' ****** *** * * *
- ** * * ' * *********** * "'*......,........... ~.......................................
1 I
I I
I I
t I
I I
I I
I I
I t
I I
I I
I I
I I
I I
I I
I I
I I
I I
ill 1000JO I
I I
I I
I I
1/1 m 2
]
- I D'
- J 75000
.................. J.................... :................... :,..,................................. :................... t**................. :...................................... :,..................
I I
I I
I I
I I
I I
I I
I I
I I
I I
I I
I I
I I
I I
500JO **** ',************: ******************i*--****************r****************** *******************r*******************r*******************1*-**-****-**-**--**- ******************t ***.. *-***--***-**
25000
- ~
~
~
,;r'-
-,, + -+ T -*- -:~!-
-+-
- ~
i
~
- ~~
I I
I I
I I
I I
I I
I I
0..............................................................................................,........................................................................................
0 500 1000 15~0 2000 2500 3000 4000 4500 0000 Time 1sec)
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.13-21 Revision 33 Reactor Power, LNFF Analysis without Off-Site Power Available and Steam Dump Systems Disabled
.. I 0
- 0.
1 20------------------------------
100 ********************************! *******************************1 ********************************+********************************+*********************************l********************************
80........................................ '...................... 1... '........................,.. -~---**.................,..... '....t........ '...............,... ****-~--.............. '..............
60............................ ***1****************.. **** ***** ****).............................. ;............................... -:-............................. I**...........................
40 ********************************;********************************************************************:********************************7*********************************,...............................
I I
I I
I I
w **************************.... i............................... +
.............................. ;............................... I................................ ;...............................
D L:::::;:::::::=;;;;;;;;;;;~~-+/-~~~~~~~~~~~~d 0
2000 4000 6000 Time (sec) 10000 12000
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.13-22 Revision 33 Primary Coolant System Loop Temperatures, LNFF Analysis without Off-Site Power Available and Steam Dump Systems Disabled Q,i I.
- J I I.
590-------------------------------
-t Vessel ouuet
- Average
- Vessel lrilt 570........................... 1*****************.. ***.. *******i***********.. ******** ***********}****.....................,..,..,-:-,..............................
i GI 550 CL E
~
1/J (J
a::
530.............................. I******************.... ****.... l******.. *****.................... :****.. *****.. *................. -f*****............................ !................................
510-------...----------------------------..... ---...----------'
0 2000 4000 6000 Tlme(sec) scoo 10000 12000
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.13-23 Revision 33 Primary Coolant System Loop Flow, LNFF Analysis without Off-Site Power Available and Steam Dump Systems Disabled i E
.Q -
9000 -""""'!!!!!!!!!!!!!!!!!!!!!f!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!""""'="'!!!!!!!!""""'"""""!!!!!!!!!!!!!!!!!!!""""'""""'!!!!!!!!!!!!!!!!!!!!f!!!!!!!!""""'!!!!!!!!!!!!!!!!!!!!!f!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!""""'="'!!!!!!!!""""'"""""-
7&10 6000 L oop 1 A
- I Loop 1B
- L oop2A L oop2B I
1 I
I I
- * ************* * *** **u * ** ** * ** * ***** **********u*** * * ** ** *** *****.. ******* * * ** *** u * ** ** * ** * ********** ***** * * *** * ** ** * ************** * *** * * * * ** ** ** * * ***** ********** *** ** ** ** ** *** *** ** * * * ***** * ******** *
- I I
I I
I I
I I
I I
. ************************.. **1**************.. *****************,.,..,......., ********.........,,........................,..,....,........, ***********************,**.. **************************
~ 4SJO I
- ............................ 1.. ***********.................... l................................. :................................ :............................... f**.............................
Q. 8
..I 1/J u "
3000 1:00 *.............................
..... *******j'******--*--...........
...................... f...... "...................... t*******......................
D -
........... --...... iiiiiiiili-=--i.-......... -
..... -iiiiiiiiil-=-iiiiiiiiili-0 2000 4000 6000 Time (s-ec) 8000 10000 12000
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.13-24 Revision 33 Pressurizer Pressure, LNFF Analysis without Off-Site Power Available and Steam Dump Systems Disabled d)
N
- I 1/) !
- 0.
mo 2:00 1000
........ t***...........
.............. -~*.....
-*-***r*
- r****
- l*******
........ t***..
.. ---~*-*****"**
......... 1 ***
*- T
- t********
....... ~-******..
............ ~--*
.................... i****
............... ).*********************************r.***-**-****
- i****
I 2000
- f******
4000
-* ~-.......
6000 Time (sec) 8000 10000
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.13-25 Revision 33 Pressurizer Level, LNFF Analysis without Off-Site Power Available and Steam Dump Systems Disabled
'I-.....
a,
~
.J I.
a, Ill
'i: :,
Ill a,
a;.
Q.
70 1""""'!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!"""""""""'!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!"""""""""'!!!!!!!!!!!!!!!!!!!!!!!!!!!!~
~
60 1 ********************************1"***************.. ***************;***********
- ~ *********************** ***** ****
~ **----*",
I"-
50
- ~*********************************"i ********************************~-********************************~*******************************.. r********************************
40 30................................ :.................................,................................ i******.. *****....................,................................. ;................................
20........... ________________.....,......, ___....., _______....., _____....,......, _____....., __________.....__.
0 6000 Time (sec) aooo 10000 121)00
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.13-26 Revision 33 SG Auxiliary Feedwater Flow, LNFF Analysis without Off-Site Power Available and Steam Dump Systems Disabled ss-------------------------------
30........................................................... ~................................ ~............................................................
- ** ** *** ********************** *******,********************* ************f'********************************
- ** ***********************r** ** ***************************
~ 20............................................................ ;................................ [....................................... ***********************i**.*.........................
- u.
lo, I I 15 I
I 1
t
........................ ***......................,........,...,..,..........................,..,..,.............................................................. -~...........,..,...........
LI.
>i (U
- * *** ***** ** * **u ************* ** * **** *** ****** ************ **** ***** *************** *-* ** *** * ***** ****u*** ********************* *** **** ****** ***** ** ** *
- I o
I 5................................................. **********~*********************.. *********~**********........... **********-;-***........................... ;..............................
D liiiliii=..... -=-...... -...... _...__. ____... ------...-...... -=----=---...... -=-...... =---=--=-.i-=_.
0 2000 4000 6000 Time (sec) 8000 10000 1l'OOO
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.13-27 Revision 33 SG Dome Pressure, LNFF Analysis without Off-Site Power Available and Steam Dump Systems Disabled 1100 -------------------------------
000.... *.. *...................... * *~ *...... *.. *...... *............. *.,...... *.. *............. *...... * ***~* *.................... *.. *.. * *: *............. * *..... *.. *........ ; *................ *.. *.. *... *....
000................................. :................................................................... :*****.. **....................... 7................................................................
700 ********************************j*********************************, ********************************~******************************:*********************************i********************************
ooo --------....... ------------------------------....... ----------------
0 2000 QOOO Time (sec) 8000 10000 12(100
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.13-28 Revision 33 SG Liquid Mass Inventory, LNFF Analysis without Off-Site Power Available and Steam Dump Systems Disabled
.e ro Q;I C:
Q;I
(!)
~ j f/J 1400.'lO """"'""""'""""!!!!!!!!"""""=-!!!!!!!!""""'""""'!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!J!!!!!!!!!!!""""'""""!!!!!!!!""""'=-!!!!!!!!!!!!!!!!=!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!I 1200'.lO * ******************** ********
I I
I I
............................................................. ******************-r**-***.........................,.. -*************-*************
I I
I I
100CCO I
I I
I I
I I
I
- ********************........ 1******************* *************.. ************"* ******************r******* ** *******.. ******.. *****r****** ** *********************** r ** -
- ******************** '"'"'"' ******************** *************-,* ************* ******************,.********** *******.. ************-****** ** *********************--t** -
- u******************
I I
I I
I 60CIJO * ************ ****** ******** !******************* *************+ ************* ******** *********f******* ** *********************+****** ** *********************+* - **************************
400,jQ
- *************.,* **********.. * ******************.-******* ** *******.. ******n****~****** ** ***.. ******************t'".. ********************--****
I I
I I
..*...._____.T"""'i-:- -~*1---~
"-'ltM!!....._...=i+~~~
O -=...... -iiiiiiiiiii--iiiiiiiiii.-liiiiiiiiiiiiiil---..-............ --..... ---..... --...... =----iiiiiiiiiii-iiiiiiiiiiiiiiiOiii-0 woo 4000 6000 Time (sec) 8000 10000 12000
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.14-1 Revision 24 Break Flow Rates During LHR-Limiting Transient 0
50 100 150 200 250 300 350 Time (sec) 0 1000 2000 3000 4000 5000 6000 Break Flow Rate (lbm/sec)
From Unaffected SG From Affected SG I
I I
I I
I
\\
l I
I I
I I
I I
---0
1'::,
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.14-2 Revision 24 Steam Generator Pressures During LHR-Limiting Transient 0
50 100 150 200 250 300 350 Time (sec) 0 100 200 300 400 500 600 700 800 900 1000 1100 Steam Generator Pressure (psia)
--0
t::,.
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.14-3 Revision 24 Steam Generator Heat Transfer Rates During LHR-Limiting Transient 0
50 100 150 200 250 300 350 Time (sec) 0 500 1000 1500 2000 2500 Steam Generator Heat Transfer Rate (MW)
'\\
I "'
I I
I I
I
\\
\\
C\\)
I I
\\_
---0
6
\\_
-:--0, -
---0----, -
-e -
-G-- - -e -
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.14-4 Revision 24 Steam Generator Secondary-Side Total Fluid Inventories During LHR-Limiting Transient 0
50 100 150 200 250 300 350 Time (sec) 0 50000 100000 150000 200000 250000 Steam Generator SecondarySide Total Fluid Inventory (lbm)
--B
6
-B----0--B----O--B---0--B---0--&---0--&---0--&
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.14-5 Revision 24 Core Inlet Temperatures During LHR-Limiting Transient 0
50 100 150 200 250 300 350 Time (sec) 250 300 350 400 450 500 550 600 Core Inlet Temperature (
oF)
Unaffected Sector Affected Sector
---0
6
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.14-6 Revision 24 Core Inlet Flow Rates During LHR-Limiting Transient 0
50 100 150 200 250 300 350 Time (sec) 0 5000 10000 15000 20000 Core Inlet Flow Rate (lbm/sec)
Stuck Rod Region Rest of Affected Sector Unaffected Sector
/~~--O--~--&--o--B--~-~--&--o--~--&---0---
/
- --0
A
---0
__ EJ- _ -B __ --- _ --D- _
- B-- - -G -
- -B- - -
El- - ----B - -
-D---- - --D- -
- B-- - -G
~G--B
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.14-7 Revision 24 Pressurizer Pressure During LHR-Limiting Transient 0
50 100 150 200 250 300 350 Time (sec) 600 800 1000 1200 1400 1600 1800 2000 2200 Pressurizer Pressure (psia)
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.14-8 Revision 24 Pressurizer Liquid Level During LHR-Limiting Transient 0
50 100 150 200 250 300 350 Time (sec) 0 10 20 30 40 50 60 70 Pressurizer Liquid Level (% of span)
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.14-9 Revision 24 Total HPSI Flow Rate During LHR-Limiting Transient 0
50 100 150 200 250 300 350 Time (sec) 0 10 20 30 40 50 Total HPSI Flow Rate (lbm/sec)
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.14-10 Revision 24 Reactivity During LHR-Limiting Transient 0
50 100 150 200 250 300 350 Time (sec) 10 5
0 5
10 Reactivity ($)
Moderator Doppler Boron Scram Total
---0
- ---0
A
E>----------E>----------E>----------E>----------E>----------E>----------E>----------l>----------l>----------l>-----------1>-----------!>-----------!>---------- -
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.14-11 Revision 24 Reactor Power During LHR-Limiting Transient 0
50 100 150 200 250 300 350 Time (sec) 0 5
10 15 20 25 30 Reactor Power (% of rated)
Total Stuck Rod Region Rest of Affected Sector Unaffected Sector
0
- ---0
A
---0
- --B - - - - -G -
- -B - -
--G---
o I
p
\\
0- -
---G- -
-B -
0- - -- -
--- \\
'--- El ----
/,,,-
--a__ ----
0
~--
/
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.14-12 Revision 24 Break Flow Rates During DNBR-Limiting Transient 0
100 200 300 400 500 600 700 Time (sec) 0 1000 2000 3000 4000 5000 6000 Break Flow Rate (lbm/sec)
From Unaffected SG From Affected SG
---0
6.
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.14-13 Revision 24 Steam Generator Pressures During DNBR-Limiting Transient 0
100 200 300 400 500 600 700 Time (sec) 0 100 200 300 400 500 600 700 800 900 1000 1100 Steam Generator Pressure (psia)
---0
6
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.14-14 Revision 24 Steam Generator Heat Transfer Rates During DNBR-Limiting Transient 0
100 200 300 400 500 600 700 Time (sec) 0 500 1000 1500 2000 2500 Steam Generator Heat Transfer Rate (MW)
/1 I
I I
\\
\\
\\
---0
A (SJ
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.14-15 Revision 24 Steam Generator Secondary-Side Total Fluid Inventories During DNBR-Limiting Transient 0
100 200 300 400 500 600 700 Time (sec) 0 50000 100000 150000 200000 250000 Steam Generator SecondarySide Total Fluid Inventory (lbm)
--B
f:,
-B---O---B---0---&---0---&---0---&---0---&-~--&-~-
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.14-16 Revision 24 Core Inlet Temperatures During DNBR-Limiting Transient 0
100 200 300 400 500 600 700 Time (sec) 250 300 350 400 450 500 550 600 Core Inlet Temperature (
oF)
Unaffected Sector Affected Sector
---0
6.
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.14-17 Revision 24 Core Inlet Flow Rates During DNBR-Limiting Transient 0
100 200 300 400 500 600 700 Time (sec) 0 5000 10000 15000 20000 Core Inlet Flow Rate (lbm/sec)
Stuck Rod Region Rest of Affected Sector Unaffected Sector I
I I
I I
I I
I I
I I
\\
\\
\\
(S)
\\
- '\\
- ---0
A
---0
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.14-18 Revision 24 Pressurizer Pressure During DNBR-Limiting Transient 0
100 200 300 400 500 600 700 Time (sec) 600 800 1000 1200 1400 1600 1800 2000 2200 Pressurizer Pressure (psia)
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.14-19 Revision 24 Pressurizer Liquid Level During DNBR-Limiting Transient 0
100 200 300 400 500 600 700 Time (sec) 0 10 20 30 40 50 60 70 Pressurizer Liquid Level (% of span)
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.14-20 Revision 24 Total HPSI Flow Rate During DNBR-Limiting Transient 0
100 200 300 400 500 600 700 Time (sec) 0 10 20 30 40 50 Total HPSI Flow Rate (lbm/sec)
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.14-21 Revision 24 Reactivity During DNBR-Limiting Transient 0
100 200 300 400 500 600 700 Time (sec) 10 5
0 5
10 Reactivity ($)
Moderator Doppler Boron Scram Total I
SU I
I I
I
/'---e-_-0--
---0
- ---0
6
&--0--~
0-- - e- - - -
---e
&--0--~-B-
~----------l>---------!>----------l>----------l>----------l>----------~----------1>---------!>----------l>----------I>----------~----------~---------!>--
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.14-22 Revision 24 Reactor Power During DNBR-Limiting Transient 0
100 200 300 400 500 600 700 Time (sec) 0 5
10 15 20 25 30 Reactor Power (% of rated)
Total Stuck Rod Region Rest of Affected Sector Unaffected Sector
0
- ---0
A
---0
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.15-1 Revision 21 SGTR WITH LOAC: CORE POWER vs TIME l 2 0 ------
1 ----.-,-----r----.,.,---.,.i-----,
(00 -
-I 80...
~
i 60 -
I 40.,_
za-I I
I 300 600 900 lZ00 TIME, SECONDS 1500 l800
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.15-2 Revision 21 SGTR WITH LOAC: CORE COOLANT TEMPERATURE vs TIME 660r---"T-"----.-----.----,.----,,-...--
~ 630 w !
~ 600 I
m 570
... i y,..
i 540 i
SLO 48Q.._ __
--1,... ___
..1..-__
......r.. __
300 600 900 l 200 1500 lBOO T{ME. SECONDS
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.15-3 Revision 21 SGTR WITH LOAC: PRIMARY COOLANT SYSTEM PRESSURE vs TIME 2200r---~--~----,-------,-----,----,
3' 2000
"'.. -i 1800
~
"' I 1600
~
1400 l200 l 000.._ __
~
1800 300 600 900 1200 1500 TI NE. SECONDS
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.15-4 Revision 21 SGTR WITH LOAC: STEAM GENERATOR PRESSURE vs TIME llSQr---...--------.------,,--------
10S0 c -
950
... * -i 4'I !
850
! s 750 650 sso.._ __
~30_0 ___
6~0-0--~90-0--~12_0_~-~~~50_0 _ __.1800 Tif'1E SECONDS
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.15-5 Revision 21 SGTR WITH LOAC: TUBE LEAK FLOW RATE vs TIME 60.----,---.-----.-----.----:-----,
so 40
~
i
_, -=
- I 30 3
w !
20 lO I
I I
3GO soo goo l.Zoo*
TIME. SECON05-LSOO i :00
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.15-6 Revision 21 SGTR WITH LOAC: INTEGRATED TUBE LEAK FLOW vs TIME 10000,----r---~~---,----.--~---
60000
~
~ 50000
~
..J w
40000 CQ E-Q
~
30000
~
0
~ 20000 I
I I
10000 I I
I 600
'300.
l ZCO.
1500 TtnE, 5EC0"fCS 1900
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.15-7 Revision 21 SGTR WITH LOAC: PRESSURIZER LIQUID VOLUME vs TIME 900.---~---,---------,.---.----
750 600
... t: -
450 I
Cl !
300
--= -I lSO I
t I
300 600
<300 l200 L500 lSOO T[ME. 5ECONOS
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.15-8 Revision 21 SGTR WITH LOAC: AFFECTED STEAM GENERATOR SAFETY VALVE (MSSV)
FLOW RATE vs TIME 360 C.)
~
~
- E 300
~ §
~ 240
~
u, u,
2 180 ix: !
z 120 i:tl 0 i Q
60 nn I
l I I* I I I 300 600 900 l C:00 lS00 l8G0 Tff1E, 5ECOND5
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.15-9 Revision 21 SGTR WITH LOAC: AFFECTED STEAM GENERATOR SAFETY VALVE (MSSV)
INTEGRATED FLOW vs TIME soooo...---~---r------r-----r-------
i.:.
50000
~ -
~
40000 30000 20000 lOOOO I
300 soo goo 1200 LSOO 1800 T(ME, 5Ea:ONOS
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.15-10 Revision 21 SGTR WITH LOAC: STEAM GENERATORS LIQUID MASS vs TIME 360000 300000
-! 240000
... i Q !
l 80000 i
- I !
l20000 60000 300 AFFECTED SO
/
UNAFFECTED SG I 7 I I
600 900 l,00 T f ME, SECONDS l5CO 1800
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.15-11 Revision 21 SGTR WITH LOAC: CORE POWER vs TIME I
- I I
I 120 r----T1----,,---~
1 --,,----,1----,
20 -
I I
I I
I 5000 lOOOO 15000 20000 25000 30000 r I ME, SECONOS
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.15-12 Revision 21 SGTR WITH LOAC: CORE COOLANT TEMPERATURES vs TIME 650r---.---.---,----r---,----,
ssa sao I 0 1M
.. Q 4S0 en I
- ,... 400 a:
~ -
1M CL.
- c "'...
350
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.15-13 Revision 21 SGTR WITH LOAC: PRIMARY COOLANT SYSTEM PRESSURE vs TIME 2500r-----,---,------.-------r----.-----.
2000 C -
¥: -I 1500
! =
VI I 1000 I
~
500 I
I 5000 10000 l 5000 20000 25000 30000 TIME. SECONDS
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.15-14 Revision 21 SGTR WITH LOAC: STEAM GENERATORS PRESSURE vs TIME l40Or---r----ir------r-----.----.---
t200
- lOOO
- s I! -I 800 AFFECTED SO I 600
/
I 400 200
/
UNAFFECTED SG 5000 10000 25000 30000
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.15-15 Revision 21 SGTR WITH LOAC: PRESSURIZER LIQUID VOLUME vs TIME 2000r---~--~----------,-----..---
11500 w
2 3 1000 0 >
Q 5
0
- 3 500 1¥ w
N c2 ell
~
1¥
~
-500---~~-----~~-~~-~~~~~~~
5000 lOOOO 15000 20000 25000 30000 TIME. SECONDS
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.15-16 Revision 21 SGTR WITH LOAC: TUBE LEAK FLOW RATE vs TIME so--------------------
50 20 10 5000 LOOOO LSOOO 20000 25000 30000 T[f'1E. SECONDS
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.15-17 Revision 21 SGTR INTEGRATED LEAK FLOW vs TIME 700 600 500
~*
...1,-..
- u. ID 00
~ '2
"' a
~ !
0.2 300 WI-
~v w i 200 100
- /
0 0
INTEGRATED LEAK FLOW
/ V J
4 8
~/
/
V /
12 16 CThou*&nd*)
TIME, li4ilCOnd&
/
/
V 20
/'
/
28
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.15-18 Revision 21 SGTR ADV FLOW RATE vs TIME ADV FLOW RATE 300 280 260 Affected SIG 240 220 u
200 QI II
~
180
.Q 160 w'
I-140
~
~
120
~
100 BO lntac:t. SIG 60 40 20 0
a 4
8 12 16 20 24 28 (Thousands)
T1Me, s.econds
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.15-19 Revision 21 SGTR INTEGRATED ADV FLOW vs TIME INTEGRATED ADV FLOW 800 700 600 a
500 Intact SIG
'f"I ~-
..I~
400 o*
w:,
I-i It, 300
'z 200 100 A1'1'ected SIG 0
0 12 16 20 24 29 (Tnoueande)
TIME, seconds
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.15-20 Revision 21 SGTR PCS SUBCOOLING vs TIME 100 90 80 70 u..
I 0
60
~
,.3 50
- a 8
40 Cil
- i r./l 30 I
{\\
I
\\ V 20 10 0
0 4
RCS SUBCOOLING 1\\
/
e I
~
I
/~ v
./
V 12 16 (Thousands)
Tl~E. seconds.
I V
20 A
Ji'\\
l.- V V
\\V I
24 28
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.15-21 Revision 21 SGTR HPSI FLOW RATE vs TIME 60 50
\\)
40 QI UI
\\ '
30 w
I-
~
3111 0
..J
- u.
20
.i\\
10 0
a HPSI FLOW RATE
\\
\\
8
\\,
V 12 16 (Thou*anda)
TIME, s.aconds.
n r
\\ I 20 I
I I
I \\
j
\\
I
\\
24 29
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.16-1 Revision 23 CONTROL ROD EJECTION, EOC HZP CASE: CORE POWER 60000 50000
~*
... *~**
.* :30000.*...***
~
- I 0
&120000.*
10000*.
0 ***._........,,.;.i.,...;,;::,i..-.i.__,ii.,..;....ia,.....J..;;._,L..-,J;,i...-L-i.-.1,;,;...,.._-+-,--1...,.._.&-l--......i--
o ',
s 10:
15 20 Tfme(s)
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.16-2 Revision 23 CONTROL ROD EJECTION, EOC HZP CASE: CORE AVERAGE HEAT-FLUX-BASED LHR
- 8.
6.4
-=
~
JI: -
4.8 Ill:
3 Ill Cit e l 3.2 I!
0 u 1.6
.0 0
5 10 Time (s) 0---0 Core Ave. LHR 15 20
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.16-3 Revision 23 CONTROL ROD EJECTION, EOC HZP CASE: TOTAL CORE REACTIVITY
- 2.
0c-_,c Total
- 1.
0 e
f
-1.
0 0
- a::
-2.
-3.
-4.
0 5
10-,
15 20 Time (s)
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.17.1-1 Revision 28 SCATTER PLOT OF OPERATIONAL PARAMETERS 0.0 1.0 2.0 3.0 4.0 5.0 0.0 5000.0 10000.0 15000.0 2565.0 2570.0 2575.0 2580.0 2585.0 12.0 13.0 14.0 15.0 16.0 0.4 0.3 0.2 0.1 0.0 0.1 0.2 0.3 0.4 2000.0 2020.0 2040.0 2060.0 2080.0 2100.0 40.0 50.0 60.0 70.0 536.0 538.0 540.0 542.0 544.0 OneSided Break Area (ft 2/side)
Burn Time (hours)
Core Power (MW)
LHGR (KW/ft)
ASI Pressurizer Pressure (psia)
Pressurizer Liquid Level
(%)
RCS (Tcold)
Temperature
(
oF) 130.0 135.0 140.0 145.0 1000.0 1050.0 1100.0 1150.0 1200.0 210.0 220.0 230.0 240.0 1.60e+06 1.65e+06 1.70e+06 1.75e+06 1.80e+06 80.0 100.0 120.0 140.0 Total Loop Flow (Mlb/hr)
SIT Liquid Volume (ft 3)
SIT Pressure (psia)
Containment Volume (ft 3)
SIT Temperature
(
oF) l -*-~-:-:*----* :*-J l--*--~*... ***H J
l *. -~----~-* j l : : ~ ~---: : : : : j l -~-- ---: -* ~.. -,
l --*- --~--- j l :- :--*----:-**--1 l-*--*- -*:----**-*-J l :. ---* : *~ *- j l :-------*: --,
l : *~---*. -~:-,
r-----.... -~.. *-**J
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.17.1-2 Revision 28 PCT VERSUS PCT TIME SCATTER PLOT FROM TRANSIENT CALCULATIONS PCT vs Time of PCT 1800 1§1
~
1600 l 1400
[2J LL 0 i=' 1200
(.)
D..
~
1000 I
800 Split Break Guillotine Break 600 400 ~~-~-~-~-~-~-~~-~-~
0 100 200 300 400 500 Time of PCT (s)
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.17.1-3 Revision 28 PCT VERSUS BREAK SIZE SCATTER PLOT FROM TRANSIENT CALCULATIONS 1800 1600 1400 LL 0;:- 1200
(.)
a..
1000 800 600 PCT vs One-sided Break Area
~
I 1111 Cb 8
1:J fa
§ c§J Do w
Split Break Guillotine Break 400 ~~-~-~-~-~-~-~~-~-~
0.0 1.0 2.0 3.0 4.0 5.0 Break Area (ft2/side)
FSAR CHAPTER 14 - SAFETY ANALYSIS TABLE 14.17.1-4 Revision 28 Page 1 of 1
SUMMARY
OF MAJOR PARAMETERS FOR THE LIMITING PCT CASE 6.0 % Gad Rod Core Average Burnup (EFPH) 7,381.22 Core Power (MWt) 2,572.79 Hot Rod LHR, kW/ft 14.60 Total Hot Rod Radial Peak (Fr T) 2.040 Axial Shape Index (ASI) 0.1602 Break Type Guillotine Break Size (ft2/side) 3.339 Offsite Power Availability Not Available Decay Heat Multiplier 1.01073
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.17.1-5 Revision 28 MAXIMUM OXIDATION VERSUS PCT SCATTER PLOT FROM TRANSIENT CALCULATIONS 0.9 0.8 0.7 0.6 C:
Maximum Oxidation vs PCT Split Break Guillotine Break
- 8 0.5 cu
'O
~
0.4 0.3 0.2 0.1
~-
0.0 ::-=--~:-::--=------"--l-!lllllllllll:--~~-=-1=-:-~-:--:1-=-~----:--:=1-=-=-~::1=--=-~~
400 600 800 1000 1200 1400 1600 1800 2000 PCT (°F)
FSAR CHAPTER 14 - SAFETY ANALYSIS TABLE 14.17.1-6 Revision 28 Page 1 of 1 CALCULATED EVENT TIMES FOR THE LIMITING PCT CASE Event Time (sec)
Break Opened 0
PCP Trip 0
SIAS Issued 0.6 Start of Broken Loop SIT Injection 14.9 Start of Intact Loop SIT Injection (loops 1B, 2A and 2B, respectively) 17.1, 17.1 and 17.1 Beginning of Core Recovery (Beginning of Reflood) 27.2 PCT Occurred 27.2 Start of HPSI 40.6 LPSI Available 40.6 Broken Loop LPSI Delivery Began 40.6 Intact Loop LPSI Delivery Began (loops 1B, 2A and 2B, respectively) 40.6, 40.6 and 40.6 Broken Loop HPSI Delivery Began 40.6 Intact Loop HPSI Delivery Began (loops 1B, 2A and 2B, respectively) 40.6, 40.6, 40.6 Broken Loop SIT Emptied 50.7 Intact Loop SIT Emptied (loops 1B, 2A and 2B, respectively) 50.8, 54.6 and 53.1 Transient Calculation Terminated 300
+----- I
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.17.1-7 Revision 28 BREAK FLOW FOR THE LIMITING CASE Break Flow
-- Vessel Side
- - - - Pump Side
--- Total 60 0.....
40
~
E I
g I
Q)
I I
cu 0:::
I
~
I u:::
20 0
-20 ~--~--~--~--~--~--~
0 100 200 300 Time (s)
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.17.1-8 Revision 28 CORE INLET MASS FLUX FOR THE LIMITING CASE Core Inlet Mass Flux
-- Hot Assembly
- - - - Surround Assembly
- - - Average Core Outer Core 500 u,
I NE E
.0 u:::
u, u,
(U 0
-500 ~--~--~--~--~---~-~
0 100 200 300 Time (s)
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.17.1-9 Revision 28 CORE OUTLET MASS FLUX FOR THE LIMITING CASE Core Outlet Mass Flux
-- Hot Assembly
- - - - Surround Assembl)
- - - Average Core Outer Core 500 0
I I : t II 1,l\\\\1,1
"/
Iii I
I I
I
-500 I
I I
I I
-1000 ~--~--~-----~---~--
0 100 200 300 Time (s)
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.17.1-10 Revision 28 VOID FRACTION AT PCS PUMPS FOR THE LIMITING CASE C:
0 u I!!
't:I
~
0.8 0.6 0.4 0.2 Pump Void Fraction Broken Loop 1 Intact Loop 2 Intact Loop 3 Intact Loop 4 0.0 ~--~---~---~---~---~--~
0 100 200 300 Time (s)
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.17.1-11 Revision 28 ECCS FLOW (INCLUDES SIT, HPSI, AND LPSI) FOR THE LIMITING CASE ECCS Flows 3000
-- Loop 1 (broken)
- - - - Loop 2
--- Loop 3
--- Loop4 I
ii,1 I I I
I
\\
\\
l I 2000 ~
\\ \\
\\ \\;,.
\\' '
-.!!?
\\\\
I E
\\'~
.c JJ Q)
,I II cu a:
'I
~
!1 U::
II
'I 11 1000 ~
11
'I
!1 11
,1 11 ii
,1 I\\
'1 I_
lf I\\
0
,_,r-,._ --
~
0 100 200 300 Time (s)
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.17.1-12 Revision 28 UPPER PLENUM PRESSURE FOR THE LIMITING CASE cu "iii E::
~
i a..
2000 ~
1000 0
0 Upper Plenum Pressure 100 200 300 Time (s)
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.17.1-13 Revision 28 COLLAPSED LIQUID LEVEL IN THE DOWNCOMER FOR THE LIMITING CASE g
Q) >
(I)
...J
- 2 C"
- i 20 I
i I 10
- I I i'i Ii
- :
I I I
i
I Downcomer Liquid Level
-- Sector 1 {broken}
Sector 2
- - - - Sector 3
-- - Sector4
-- Average o~~-~--~---~--~---~--~
0 100 200 300 Time (s}
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.17.1-14 Revision 28 COLLAPSED LIQUID LEVEL IN THE LOWER PLENUM FOR THE LIMITING CASE Lower Vessel Liquid Level 8
6 -
~
j Q)
....I 4 r o~--~--~--~--~-~~-~
0 100 200 300 Time (s)
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.17.1-15 Revision 28 COLLAPSED LIQUID LEVEL IN THE CORE FOR THE LIMITING CASE Core Liquid Level
-- Hot Assembly
- - - - Center Core
- - - Average Core Outer Core 10 g
Q) >
(I)
...J
- 2 O"
- i 5
100 200 300 Time (s)
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.17.1-16 Revision 28 CONTAINMENT AND LOOP PRESSURES FOR THE LIMITING CASE Containment and Loop Pressures 100
-- Containment 90
- - - - SG Outlet (primary side)
Upper Plenum Downcomer Inlet 80 70 60 cu "iii
.8,
~
50 U)
U)
~
- a. 40 30 20 10 0 0 100 200 300 Time (s)
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.17.1-17 Revision 28 CORE EFFECTIVE FLOODING RATE DELETED in Revision 28
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.17.1-18 Revision 28 CORE COLLAPSED LIQUID LEVEL DELETED in Revision 28
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.17.1-19 Revision 28 CORE QUENCH LEVEL DELETED in Revision 28
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.17.1-20 Revision 28 PCT-NODE HEAT TRANSFER COEFFICIENT DELETED in Revision 28
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.17.1-21 Revision 28 PEAK CLADDING AND RUPTURE LOCATION CLADDING TEMPERATURE FOR THE LIMITING CASE DELETED in Revision 28
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.17.2-1 Revision 28 Break Mass Flow Rate (Limiting Case)
ID:08968 240ct2007 20:59 0.08 ft2 Break 1000
- 00 pal_M5_0.08ft2_DMX I
.c =
500 0..._.....___.__...._............. ___....._.............. ___.~..,__....... ___._..._....... ___._..._....... ___._...._......____._...._....... __.___.
0 500 1000 1500 2000 2500 Time (sec)
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.17.2-2 Revision 28 Primary and Secondary Pressures (Limiting Case)
ID:06968 240ct2007 20:59:00 pal_M5_0.06fl2_DMX 2400 2200 2000 1800 1600 i 1400
.e,
~ 1200
- I
~ 1000
- a.
800 600 400 200 0 0 500 0.08 ft2 Break 1000
e Pressurizer
- -**** SG-1
---SG-2 1500 Time (sec) 2000 2500
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.17.2-3 Revision 28 Normalized Reactor Power (Limiting Case)
ID:08968 240ct2007 20:59:00 pal_M5_0.08ft2_DMX 0.08 ft2 Break 120 110 100 90 80
§' 70 6 I 60 0..
I!! 50 0
(.)
40 30 20 10 '--
0 0 500 1000 1500 2000 2500 Time (sec)
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.17.2-4 Revision 28 Total HPSI Mass Flow Rate (Limiting Case)
ID:08968 24Oct2007 20:59:00 pal_M5_0.08ft2_DMX 0.08 ft2 Break 80 u
Q) 60
.!!! E
..0 =
~
0:::
~ 40 Li:
20 0.___._....... _..._....___.__...._...._...... _...._...___.____....._.............. ___._......_....... ___._...__.____._..._....... ___.___,
0 500 1000 1500 2000 2500 Time (sec)
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.17.2-5 Revision 28 Total SIT Mass Flow Rate (Limiting Case)
ID:08968 240ct2007 20:59:00 pal_M5_0.08fl2_DMX 4000 u
~ 3000 E
..c I
0::
~ 2000 u:::
1000 0.08 ft2 Break 0 ~~~-~~~-~~~-~-~~~--~--~-I! __ ~---~-~
0 500 1000 1500 2000 2500 Time (sec)
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.17.2-6 Revision 28 Loop Seal Void Fractions (Limiting Case)
ID:08968 24Oct2007 20:59:00 pal_M5_0.08ft2_DMX 0.08 ft2 Break 1.00
~
~
~
0.90
e Loop 1A
- -****-* Loop 1 B 0.80
---Loop 2A
- -.& Loop 28 (broken) 0.70 c: 0.60 0
~
it 0.50 "C
- o
> 0.40 0.30 0.20 0.10 0.00 0
I ~-
500 1000 1500 Time (sec)
I I I I I I I I I I I~ I 0
I I '" u
- 2000 2500
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.17.2-7 Revision 28 Break Void Fraction (Limiting Case)
ID:08968 240ct2007 20:59:00 pal_M5_0.08fl2_DMX 0.80 0.70 c 0.60 0 u
~
IL 0.50 "O
~ 0.40 0.30 0.20 0.10 0.08 ft2 Break 0.00.___._....._.....,_.__......___.__.__......____.__.___.____.____..___._____.___. _ _.___,._..__.,,___.____. _ _.____.____.___.
0 500 1000 1500 2000 2500 Time (sec)
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.17.2-8 Revision 28 Reactor Vessel and PCS Mass Inventories (Limiting Case)
ID:08968 24Oct2007 20:59:00 pal_M5_0.08ft2_DMX E
g, 0 0 cu
- i!
0.08 ft2 Break 300000.--""T"""r-T"----,-..---.----.----,.--...-----.----.--.--"T""""""T""----r-..--""T"""---.-----,-..---.----,----,.--...-----.----,
250000 200000 150000 100000 50000
ePCS
- -****-*RV i !
I I 0...._.............. _..._.............. _...._.............. _...._..._....... __....._.............. __._....._....... __._....._....... __._..._....... __.__,
0 500 1000 1500 2000 2500 Time (sec)
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.17.2-9 Revision 28 Hot Channel Collapsed Level (Limiting Case)
ID:08968 240ct2007 20:59:00 pal_M5_0.08fl2_DMX 0.08 ft2 Break 12 10 g
j Q) 8
....I "C
- 5 tT
- i "C 6 Q)
II)
Q.
0
(.)
4 2
o~~~-~~~~~~~~-~~~-~~~-~~~-~~~-~~~~
0 500 1000 1500 2000 2500 Time (sec)
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.17.2-10 Revision 28 Fluid and Cladding Temperatures (Limiting Case)
ID:08968 24Oct2007 20:59:00 pal_M5_0.08ft2_DMX 1600 1400 U:::-i 1200
~
- 8.
E 1000
~
800 600 0.08 ft2 Break 400._................ _._................ _.._................ _.._...._....... ___..._................. _._......._........ ___._..._....,____._..._........ __._,
0 500 1000 1500 2000 2500 Time (sec)
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.17.2-11 Revision 28 SG Narrow Range Liquid Levels (Limiting Case)
ID:08968 240ct2007 20:59:00 pal_M5_0.08fl2_DMX
- i
~
1 Q)
....I "Cl
- 5 tT
- i 0.08 ft2 Break 100.----.-----.--.----r-.----r----,--..-"""T""--,--.----,--,----.-----.--.----r----,.----r----,--..-"""T""----.--.---,
80 60 40 20
eSG-1
- -**** SG-2 0.___.____._....___.__.__....,____._..___.____._....___.__.___.____._....___._~.__....,____._..___._____._....____,
0 500 1000 1500 2000 2500 Time (sec)
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.17.2-12 Revision 28 AFW Flow Rates (Limiting Case)
ID:08968 240ct2007 20:59:00 pal_M5_0.08ft2_DMX u
(I)
~
.c i
a:
~
u::
0.08 ft2 Break 50.---r----.--.---r----.-----,.---r----.-----,~-.----.---,--.---.-----.--.---.---,-..-........ _,.-..-........ ---,.--,
40 30 20 10 0
-10
-20
-30
-40
SG-1
- SG-2
-50 ~~~-~~~~~~~~~~~~-~~~-~~~-~~~-~~~~
0 500 1000 1500 2000 2500 Time (sec)
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.17.2-13 Revision 28 Total MSSV Flow (Limiting Case)
ID:08968 240ct2007 20:59:00 pal_M5_0.08fl2_DMX 600 200 0.08 ft2 Break
eSG-1
- SG-2 o... _.___.~......... ----...___._ __...__ __ ___. ___ _.____. ____ ___._..___._ __.___.___.__.........,
0 500 1000 1500 2000 2500 Time (sec)
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.18.1-1 Revision 29 LOCA CONTAINMENT PRESSURE PROFILE 0
10 20 30 40 50 60 1.E-01 1.E+00 1.E+01 1.E+02 1.E+03 1.E+04 1.E+05 1.E+06 1.E+07 Time (sec)
Pressure (psig)
D/G 1-1 Failure D/G 1-2 Failure
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.18.1-2 Revision 29 LOCA CONTAINMENT TEMPERATURE PROFILE 100 120 140 160 180 200 220 240 260 280 300 1.E-01 1.E+00 1.E+01 1.E+02 1.E+03 1.E+04 1.E+05 1.E+06 1.E+07 Temperature (oF)
Time (sec)
D/G 1-1 Failure D/G 1-2 Failure EEQ Profile I
11
--......* ~-
//1/
\\
///
\\ ' *-**---- *-**-*,
/ __,_
V
\\/'
v.
I
\\
- I
/
~
/:__/
\\r
~r- \\
[/
\\ 1\\--,
\\
~,\\'
~ \\
\\ I-**-- * -
'\\ \\'~
'\\
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.18.2-1 Revision 29 MSLB CONTAINMENT RESPONSE MAXIMUM PRESSURE PROFILE PR1 i
i i
i i
i
- -*-*-*-*-*+*- *-**-*-*-*-~,-- - **.. *--~ -- ------*-*-**}----*-*-*-*- *
- -*-*-*-*-.L___________ ~------*-*-*j_-*1* ---*-*-*.l. ___________ _
I I
I I
i i
i i
i i
i i
- -*-*-*-*-*t*- *-** :. *-*-j--*-*-*-*-*-*---;*- *-* *-*-*- **t*-*-*-*-*-*- *
\\
I I
I I
i i
i i
[l_
___________ i_
- _________ L ___________ _j____ __ _ _ _____ i ____________ _
i i
i i
i i
i i
i i
I i
i i
- -*+*- *-**-*-*-*--i-*-*-*-*-*-*---i*-*-*-*-* *-**+*-*-*-*-*-*-
- i i
i i
i i
i i
i
,o mo 18+004!-
1e+005 GOTI-IIC 7.2.a.(Cl\\S.~.Jarrf27/20tD. 1 Ei:31!-:1l!I
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.18.2-2 Revision 31 MSLB CONTAINMENT RESPONSE ENVIRONMENTAL QUALIFICATION PROFILE
~
'?.....
2!
- J -; ;
Cl.
E Cl)
I-300 250 200 100 +---------+--------------------!!--------------- ------<
1.E+OO 1.E 01 EEQLimit
- 5P-7 (0%)
- * * * *
- SIS-6 ( 102/I,}
1.E+03 0% 1-1 EOG Failure 1Mi1:h LOOP
- - - - - *5f'-7 (102%)
1.E+04
- * * * * *0% 1-2 EOG Failure with LOOP SIS*B (0%),
- 1. +{)5
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.22-1 Revision 25 PALISADES CONTAINMENT HYDROGEN ANALYSIS Deleted per FSAR-2479
FSAR CHAPTER 14 - SAFETY ANALYSIS FIGURE 14.22-2 Revision 25 CONTAINMENT TEMPERATURE FOR H2 GENERATION Deleted per FSAR-2479