ML19318A426: Difference between revisions
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{{#Wiki_filter:. | {{#Wiki_filter:. | ||
'- 1' SRV DISCHARGE INTO SUPPRESSION POOL v - | |||
'- 1' SRV DISCHARGE INTO SUPPRESSION POOL | |||
v - | |||
o HATCH PRESENTATION - FEBRUARY 1978 | o HATCH PRESENTATION - FEBRUARY 1978 | ||
- SIMILAR TO SNPS PRELIMINARY TRANSIENTS PRESENTED IN JANUARY 1976 2 | - SIMILAR TO SNPS PRELIMINARY TRANSIENTS PRESENTED IN JANUARY 1976 2 | ||
- EVALUATED AGAINST 150 F/40 LBM/FT -SEC LIMIT o NRC EXPRESSED SERIOUS ~ RESERVATIONS WRT R/H LIMITS-MAY/ JUNE 1978 | - EVALUATED AGAINST 150 F/40 LBM/FT -SEC LIMIT o NRC EXPRESSED SERIOUS ~ RESERVATIONS WRT R/H LIMITS-MAY/ JUNE 1978 | ||
- STRONGLY SUGGESTED QUENCHERS FOR MK II | - STRONGLY SUGGESTED QUENCHERS FOR MK II o ZIMMER/LA SALLE CLOSURE REPORTS - JULY 1978 | ||
o ZIMMER/LA SALLE CLOSURE REPORTS - JULY 1978 | |||
- INCLUDED TRANSIENTS EVALUATED AGAINST R/H LIMITS o MK II COMMITS TO QUENCHERS - AUGUST / SEPTEMBER 1978 | - INCLUDED TRANSIENTS EVALUATED AGAINST R/H LIMITS o MK II COMMITS TO QUENCHERS - AUGUST / SEPTEMBER 1978 | ||
-l l :FCR | -l l :FCR | ||
.4/3/80. | .4/3/80. | ||
Line 41: | Line 32: | ||
* 7 _ n | * 7 _ n | ||
SRV DISCHARGE INTO SUPPRESSION POOL (CONTINUED) - | SRV DISCHARGE INTO SUPPRESSION POOL (CONTINUED) - | ||
o LP ACCEPTANCE CRITERIA /LER ISSUED SEPTEMBER /0CTOBER 1978 | o LP ACCEPTANCE CRITERIA /LER ISSUED SEPTEMBER /0CTOBER 1978 200 F (LOCAL)-LIMIT ESTABLISHED FOR QUENCHERS INVITED ADDITIONAL DATA TO SUPPORT HIGHER OR NO LIMIT o MK II APPROACH WORK WITH NRC 200 F LIMIT G0AL: TO MEET LIMIT INDEPENDENT OF RVP MASS FLUX VERY LOW FOR T APPROACHING P00L MAXIMUM ADDITIONAL INFORMATION SUPPORTING STABLE CONDENSATION FOR QUENCHER UNDER ALL CONDITIONS | ||
200 F (LOCAL)-LIMIT ESTABLISHED FOR QUENCHERS | |||
INVITED ADDITIONAL DATA TO SUPPORT HIGHER OR NO LIMIT o MK II APPROACH | |||
WORK WITH NRC 200 F LIMIT | |||
G0AL: TO MEET LIMIT INDEPENDENT OF RVP | |||
MASS FLUX VERY LOW FOR T APPROACHING P00L MAXIMUM | |||
ADDITIONAL INFORMATION SUPPORTING STABLE CONDENSATION FOR QUENCHER UNDER ALL CONDITIONS | |||
.FCR 4/3/80 | .FCR 4/3/80 | ||
- - _ - - _ _ . _ f | - - _ - - _ _ . _ f | ||
3, NRC REQUESTED MK IIs EVALUATE THE SUPPRESSION-POOL TEMPERATURES FROM THE FOLLOWING TRANSIENTS A. A STUCK-0 PEN SRV DURING POWER OPERATION ASSUMING REACTOR SCRAM AT 10 MINUTES AFTER THE P0OL TEMPERATURE REACHES 110 F AND.ALL RHR SYSTEMS OPERABLE | |||
3, | |||
NRC REQUESTED MK IIs EVALUATE THE SUPPRESSION-POOL TEMPERATURES FROM THE FOLLOWING TRANSIENTS A. A STUCK-0 PEN SRV DURING POWER OPERATION ASSUMING REACTOR SCRAM AT 10 MINUTES AFTER THE P0OL TEMPERATURE REACHES 110 F AND.ALL RHR SYSTEMS OPERABLE | |||
: B. SAME AS EVENT (A) AB0VE EXCEPT THAT ONLY ONE RHR TRAIN AVAILABLE C. A STUCK-0 PEN SRV DURING HOT STANDBY CONDITIONS, ASSUMING 120 F P0OL TEMPERATURE INITIALLY AND ONLY ONE RHR TRAIN AVAILABLE D. THE AUTOMATIC DEPRESSURIZATION SYSTEM (ADS) ACTIVATED | : B. SAME AS EVENT (A) AB0VE EXCEPT THAT ONLY ONE RHR TRAIN AVAILABLE C. A STUCK-0 PEN SRV DURING HOT STANDBY CONDITIONS, ASSUMING 120 F P0OL TEMPERATURE INITIALLY AND ONLY ONE RHR TRAIN AVAILABLE D. THE AUTOMATIC DEPRESSURIZATION SYSTEM (ADS) ACTIVATED | ||
-FOLLOWING A SMALL LINE BREAK, ASSUMING AN INITIAL P0OL TEMPERATURE OF 120 F AND ONLY ONE RHR TRAIN AVAILABLE E. THE PRIMARY SYSTEM IS ISOLATED AND DEPRESSURIZED AT A RATE OF 100 F/HR. WITH AN INITIAL P0OL TEMPERATURE AT 120 F AND ONLY ONE RHR TRAIN AVAILABLE | -FOLLOWING A SMALL LINE BREAK, ASSUMING AN INITIAL P0OL TEMPERATURE OF 120 F AND ONLY ONE RHR TRAIN AVAILABLE E. THE PRIMARY SYSTEM IS ISOLATED AND DEPRESSURIZED AT A RATE OF 100 F/HR. WITH AN INITIAL P0OL TEMPERATURE AT 120 F AND ONLY ONE RHR TRAIN AVAILABLE FCR'JLK/1433-4/3/80 | ||
FCR'JLK/1433-4/3/80 | |||
EVENTS EVALUATED FOR MK II SUPPRESSION POOL TEMPERATURE ANALYSIS o STUCK-0 PEN RELIEF VALVE (SORV) o WITH ONE RHR TRAIN AVAILABLE o SPURIOUS ISOLATION - LOSS OF MAIN CONDENSER (WITH ALL RHR SYSTEMS AVAILABLE) o ISOLATION SCRAM i | |||
EVENTS EVALUATED FOR MK II SUPPRESSION POOL TEMPERATURE ANALYSIS o STUCK-0 PEN RELIEF VALVE (SORV) o WITH ONE RHR TRAIN AVAILABLE o SPURIOUS ISOLATION - LOSS OF MAIN CONDENSER (WITH ALL RHR SYSTEMS AVAILABLE) | |||
o ISOLATION SCRAM i | |||
o WITH ONE-RHR TRAIN AVAILABLE o STUCK-0 PEN RELIEF VALVE AT ISOLATION | o WITH ONE-RHR TRAIN AVAILABLE o STUCK-0 PEN RELIEF VALVE AT ISOLATION | ||
.(WITH ALL RHR SYSTEMS AVAILABLE) | .(WITH ALL RHR SYSTEMS AVAILABLE) o -SMALL BREAK o WITH ONE RHR' TRAIN AVAILABLE o WITH SHUTDOWN COOLING UNAVAILABLE (WITH ALL RHR SYSTEMS AVAILABLE FOR P0OL C00l.ING) | ||
o -SMALL BREAK | |||
o WITH ONE RHR' TRAIN AVAILABLE o WITH SHUTDOWN COOLING UNAVAILABLE (WITH ALL RHR SYSTEMS AVAILABLE FOR P0OL C00l.ING) | |||
FCR: JLKri434 4/4/80 | FCR: JLKri434 4/4/80 | ||
_. 2 ._ | _. 2 ._ | ||
_._.:__m_..___..____..__._______.._.__ | _._.:__m_..___..____..__._______.._.__ | ||
==SUMMARY== | ==SUMMARY== | ||
Line 108: | Line 55: | ||
4.& -- ,,,, . -. ,e 1+ . ..,,..---..--r .--~,+i.,-.c. e e .. - | 4.& -- ,,,, . -. ,e 1+ . ..,,..---..--r .--~,+i.,-.c. e e .. - | ||
^- | ^- | ||
,; | ,; | ||
ZIMMER PLANT UNIQUE SUPPRESS 10ii POOL TEMPERATURE ASSESSMENT , | ZIMMER PLANT UNIQUE SUPPRESS 10ii POOL TEMPERATURE ASSESSMENT , | ||
10NCLUSIONS BASED ON THE PRELIMINARY EVALUATIONS PERFORMED | 10NCLUSIONS BASED ON THE PRELIMINARY EVALUATIONS PERFORMED | ||
-ON ZIMMERi ZIMMER MEETS THE NRC SUPPRESSION POOL TEMPERATURE LIMITS FOR THE B0UNDING EVENTS EVALUATED, | -ON ZIMMERi ZIMMER MEETS THE NRC SUPPRESSION POOL TEMPERATURE LIMITS FOR THE B0UNDING EVENTS EVALUATED, FCR:atx/1436 4/3/80 | ||
FCR:atx/1436 4/3/80 | |||
; | ; | ||
GENERALIZED ASSUMPTIONS USED FOR P0OL TEMPERATURE ASSESSMENT o ' MAXIMUM SERVICE WATER TEMPERATURE o- INITIAL SUPPRESSION P0OL TEMPERATURE AT MAXIMUM | GENERALIZED ASSUMPTIONS USED FOR P0OL TEMPERATURE ASSESSMENT o ' MAXIMUM SERVICE WATER TEMPERATURE o- INITIAL SUPPRESSION P0OL TEMPERATURE AT MAXIMUM | ||
- NORMAL' TECHNICAL SPECIFICATION LIMIT o DECAY HEAT PER ANS-5 o FULLY CRUDDED RHR HEAT EXCHANGERS o HOT FEEDWATER DUMPED INTO THE SYSTEM TO MAINTAIN LEVEL (FEEDWATER TERMINATED WHEN FURTHER ADDITION WILL RESULT IN REDUCTION OF P0OL TEMPERATURE) o 122.5% ASME RATED FLOW RATE FOR SRV o MINIMUM POOL TECHNICAL SPECIFICATION LEVEL | - NORMAL' TECHNICAL SPECIFICATION LIMIT o DECAY HEAT PER ANS-5 o FULLY CRUDDED RHR HEAT EXCHANGERS o HOT FEEDWATER DUMPED INTO THE SYSTEM TO MAINTAIN LEVEL (FEEDWATER TERMINATED WHEN FURTHER ADDITION WILL RESULT IN REDUCTION OF P0OL TEMPERATURE) o 122.5% ASME RATED FLOW RATE FOR SRV o MINIMUM POOL TECHNICAL SPECIFICATION LEVEL | ||
'o SHUTDOWN COOLING NOT UTILIZED FOR CASES WHERE TWO RHR AVAILABILITY' ASSUMED | 'o SHUTDOWN COOLING NOT UTILIZED FOR CASES WHERE TWO RHR AVAILABILITY' ASSUMED I | ||
FCR: JLK/1437 4/3/80 | |||
:+<- | :+<- | ||
-MASS ENERGY INPUT ASSUMPTIONS . | -MASS ENERGY INPUT ASSUMPTIONS . | ||
-SORV AT~ FULL POWER, WITH ONE RHR TRAIN AVATLABLE o | -SORV AT~ FULL POWER, WITH ONE RHR TRAIN AVATLABLE o | ||
MANUAL SCRAM AT-TP00L = 110 F | MANUAL SCRAM AT-TP00L = 110 F | ||
-o GRADUAL CLOSURE 0F THE TURBINE CONTROL-VALVES WITH DECREASING REACTOR PRESSURE o- ONE RHR IN POOL COOLING TEN MINUTES AFTER HIGH | |||
-o GRADUAL CLOSURE 0F THE TURBINE CONTROL-VALVES | |||
WITH DECREASING REACTOR PRESSURE | |||
o- ONE RHR IN POOL COOLING TEN MINUTES AFTER HIGH | |||
-TEMPERATURE ALARM L | -TEMPERATURE ALARM L | ||
.o MAIN CONDENSER REESTABLISHED THROUGH BYPASS SYSTEM TWENTY MINUTES AFTER SCRAM AND-MAINTAINED UNTIL REACTOR VESSEL PERMISSIVE FOR RHR SHUTDOWN COOLING i | .o MAIN CONDENSER REESTABLISHED THROUGH BYPASS SYSTEM TWENTY MINUTES AFTER SCRAM AND-MAINTAINED UNTIL REACTOR VESSEL PERMISSIVE FOR RHR SHUTDOWN COOLING i | ||
Line 157: | Line 79: | ||
; | ; | ||
FOR RHR TRANSFER FROM POOL COOLING TO SHUTDOWN COOLING, l | FOR RHR TRANSFER FROM POOL COOLING TO SHUTDOWN COOLING, l | ||
FCR 4/4/80 | FCR 4/4/80 | ||
1, MK II MASS ENERGY ASSUMPTIONS SORV AT FULL POWER - SPURIOUS ISOLATION 0-MANUAL SCRAM AT TP00L = 110 F o ISOLATION AT SCRAM WITH 3,5 SECOND MAIN ISOLATION VALVE CLOSURE o .TWO RHRs IN POOL COOLING TEN MINUTES AFTER HIGH POOL TEMPERATURE ALARM o MANUAL DEPRESSURIZATION (IF REQUIRED) INITIATED AT TP00L = 120 F | |||
1, | .o -RHR SHUTDOWN COOLING NOT USED FOR POOL TEMPERATURE ASSESSMENT 4 | ||
FCR- ; | |||
MK II MASS ENERGY ASSUMPTIONS SORV AT FULL POWER - SPURIOUS ISOLATION 0-MANUAL SCRAM AT TP00L = 110 F o ISOLATION AT SCRAM WITH 3,5 SECOND MAIN ISOLATION VALVE CLOSURE o .TWO RHRs IN POOL COOLING TEN MINUTES AFTER HIGH POOL TEMPERATURE ALARM o MANUAL DEPRESSURIZATION (IF REQUIRED) INITIATED AT TP00L = 120 F | |||
.o -RHR SHUTDOWN COOLING NOT USED FOR POOL TEMPERATURE ASSESSMENT | |||
4/3/80 | 4/3/80 | ||
; | ; | ||
~ | ~ | ||
~ | ~ | ||
Line 185: | Line 92: | ||
o ISOLATION. SCRAM AT T = 0 WITH 3.5-SECOND MAIN ISOLATION VALVE CLOSURE | o ISOLATION. SCRAM AT T = 0 WITH 3.5-SECOND MAIN ISOLATION VALVE CLOSURE | ||
; | ; | ||
o ONE RHR IN P0OL COOLING TEN MINUTES AFTER.THE' EVENT o WHEN TP00L = 120 F, BEGIN MANUAL DEPRESSURIZATION | o ONE RHR IN P0OL COOLING TEN MINUTES AFTER.THE' EVENT o WHEN TP00L = 120 F, BEGIN MANUAL DEPRESSURIZATION o RHR OUT OF P0OL COOLING WHEN PRESSURE PERMISSIVE FOR | ||
o RHR OUT OF P0OL COOLING WHEN PRESSURE PERMISSIVE FOR | |||
. 'RHR SHUTDOWN COOLING IS REACHED. SIXTEEN-MINUTE DELAY'FOR-RHR TRANSFER FROM P0OL COOLING TO SHUTDOWN COOLING. | . 'RHR SHUTDOWN COOLING IS REACHED. SIXTEEN-MINUTE DELAY'FOR-RHR TRANSFER FROM P0OL COOLING TO SHUTDOWN COOLING. | ||
; | ; | ||
1 l | |||
l | |||
- FCR: JLK/1440-l : 4/3/80-l i | |||
1 | |||
- FCR: JLK/1440-l : 4/3/80- | |||
l i | |||
G (w | G (w | ||
* WS---''.8'-h +A- mm aP h.id ewm | * WS---''.8'-h +A- mm aP h.id ewm | ||
* We,.=.w M 459e uwgrea t W @ WO 4W -^ -9cI4W9 W,Aem er ww - * -e. _-, -W, pgg,g,p g .g gp e ,,+ | * We,.=.w M 459e uwgrea t W @ WO 4W -^ -9cI4W9 W,Aem er ww - * -e. _-, -W, pgg,g,p g .g gp e ,,+ | ||
MASS ENERGY ASSUMPTIONS ISOLATION SCRAM WITH S0RV o . ISOLATION SCRAM AT T'= 0 WITH 3.5-SECOND MAIN ISOLATION VALVE CLOSURE o' SORY AT T = 0 | |||
. o 'TWO RHRs IN P0OL COOLING AT TEN MINUTES AFTER THE EVENT o -WHEN-TP00L = 120 F, BEGIN MANUAL DEPRESSURIZATION o RHR SHUTDOWN-COOLING NOT USED FOR P0OL TEMPERATURE | |||
MASS ENERGY ASSUMPTIONS ISOLATION SCRAM WITH S0RV o . ISOLATION SCRAM AT T'= 0 WITH 3.5-SECOND MAIN ISOLATION | |||
VALVE CLOSURE o' SORY AT T = 0 | |||
. o 'TWO RHRs IN P0OL COOLING AT TEN MINUTES AFTER THE EVENT o -WHEN-TP00L = 120 F, BEGIN MANUAL DEPRESSURIZATION | |||
o RHR SHUTDOWN-COOLING NOT USED FOR P0OL TEMPERATURE | |||
. ASSESSMENT FCR: JLK/1441L 4/3/80- - | . ASSESSMENT FCR: JLK/1441L 4/3/80- - | ||
- . . . . .. _ .. . . . . - . - = . | - . . . . .. _ .. . . . . - . - = . | ||
g:;:. ; | g:;:. ; | ||
.7 | .7 MASS ENERGYJASSUMPTIONS SMALL BREAK'WITH ONE RHR. TRAIN AVAILABLE | ||
MASS ENERGYJASSUMPTIONS SMALL BREAK'WITH ONE RHR. TRAIN AVAILABLE | |||
- 01 SCRAM AT T = 0 ON HIGH DRYWELL PRESSURE o ISOLATION AT T =-0 WITH 3.5-SECOND MAIN ISOLATION VALVE CLOSURE | - 01 SCRAM AT T = 0 ON HIGH DRYWELL PRESSURE o ISOLATION AT T =-0 WITH 3.5-SECOND MAIN ISOLATION VALVE CLOSURE | ||
- o- ONE RHR IN POOL COOLING TEN MINUTES AFTER HIGH P0OL TEMPERATURE ALARM o WHEN TP00L.= 120 F, BEGIN' MANUAL DEPRESSURIZATION o' RHR OUT 0F-P00L C00 LING'WHEN PRESSURE PERMISSIVE FOR. | - o- ONE RHR IN POOL COOLING TEN MINUTES AFTER HIGH P0OL TEMPERATURE ALARM o WHEN TP00L.= 120 F, BEGIN' MANUAL DEPRESSURIZATION o' RHR OUT 0F-P00L C00 LING'WHEN PRESSURE PERMISSIVE FOR. | ||
RHR. SHUTDOWN COOLING IS REACHED. SIXTEEN-MINUTE DELAY FOR RHR TRANSFER FROM POOL COOLING TO SPJTDOWN COOLING. | RHR. SHUTDOWN COOLING IS REACHED. SIXTEEN-MINUTE DELAY FOR RHR TRANSFER FROM POOL COOLING TO SPJTDOWN COOLING. | ||
FCR:atx/1442-4/3/80- | FCR:atx/1442-4/3/80- | ||
*7 @ - | *7 @ - | ||
Vs-i-n+'=g i, gv- g .a_wW .eg,4-p s , E4h g Wi 9p,g -w uv.wy.w p ,_- p.,9_,reym-,g,4,p ,,g , ,_,., , _i ,p , .e pp g g. %_,, | Vs-i-n+'=g i, gv- g .a_wW .eg,4-p s , E4h g Wi 9p,g -w uv.wy.w p ,_- p.,9_,reym-,g,4,p ,,g , ,_,., , _i ,p , .e pp g g. %_,, | ||
MASS ENERGY ASSUMPTIONS SMALL BREAK WITH SHUTDOWN COOLING UNAVAILABLE cr SCRAM AT T = 0 ON HIGH DRYWELL PRESSURE - | |||
MASS ENERGY ASSUMPTIONS SMALL BREAK WITH SHUTDOWN COOLING UNAVAILABLE | |||
cr SCRAM AT T = 0 ON HIGH DRYWELL PRESSURE - | |||
o ISOLATION AT T = 0 WITH 3.5 MAIN ISOLATION VALVE CLOSURE o .TWO RHRs IN P0OL COOLING TEN MINUTES AFTER HIGH P0OL TEMPERATURE ALARM | o ISOLATION AT T = 0 WITH 3.5 MAIN ISOLATION VALVE CLOSURE o .TWO RHRs IN P0OL COOLING TEN MINUTES AFTER HIGH P0OL TEMPERATURE ALARM | ||
: o. WHEN TP00L = 120 F, BEGIN MANUAL DEPRESSURIZATION c- RHR SHUTDOWN COOLING NOT USED FOR P0OL TEMPERATURE I ASSESSMENT: | |||
: o. WHEN TP00L = 120 F, BEGIN MANUAL DEPRESSURIZATION | |||
c- RHR SHUTDOWN COOLING NOT USED FOR P0OL TEMPERATURE I ASSESSMENT: | |||
1 l | 1 l | ||
l | l | ||
'FCRiJLK/1443 4/3/80 | 'FCRiJLK/1443 4/3/80 | ||
=r,.-ims __ .4A: 4 e m | =r,.-ims __ .4A: 4 e m | ||
Line 262: | Line 127: | ||
A, | A, | ||
.;.>.?' ' ''-;lL + ~ | .;.>.?' ' ''-;lL + ~ | ||
+ | + | ||
.--y :- elm:.1 | .--y :- elm:.1 | ||
'+ = | '+ = | ||
y .4..' * [ 93... t | y .4..' * [ 93... t p,.-: L_gn% | ||
l L, c- , | |||
p,.-: L_gn% | |||
l L, | |||
c- , | |||
._; ; , , | ._; ; , , | ||
k..) < , .v_- | k..) < , .v_- | ||
, ., 4 t- <- , * | , ., 4 t- <- , * | ||
; [.- e | ; [.- e | ||
* s ';-L'1 ~ | |||
s ';-L'1 ~ | |||
, r ev,y L | , r ev,y L | ||
? | ? | ||
* T_ | * T_ | ||
: b. N - | : b. N - | ||
c c. , 1 . . | c c. , 1 . . | ||
$ n m 4 | $ n m 4 | ||
.~j v | |||
J i | |||
.~j | |||
i | |||
-* I' | -* I' | ||
'A' | 'A' | ||
Line 316: | Line 151: | ||
OF AVAILABLE TEST RESULTS- | OF AVAILABLE TEST RESULTS- | ||
_ . ON'P RFORMANCE OF QUENCHERS AT HIGH SUPPRESSION POOL TEMPERATURES ,.=. | _ . ON'P RFORMANCE OF QUENCHERS AT HIGH SUPPRESSION POOL TEMPERATURES ,.=. | ||
h T | |||
h | |||
T | |||
? $ f | ? $ f | ||
? | ? | ||
"t y | "t y i t | ||
i t | |||
- + | - + | ||
c l | c l | ||
., 'I | ., 'I | ||
Line 337: | Line 162: | ||
(_ | (_ | ||
4 | 4 | ||
.m' . | .m' . | ||
- 7 | - 7 | ||
. l u | |||
. l | |||
u | |||
^ ~ | ^ ~ | ||
O- - - - ;, Q- __ | O- - - - ;, Q- __ | ||
< - i :., ,1 - l | < - i :., ,1 - l | ||
,' \}i_ , * ,I ' ; | ,' \}i_ , * ,I ' ; | ||
p ,*- _, ,- . - - ' ' | p ,*- _, ,- . - - ' ' | ||
~ | ~ | ||
,M'*. | ,M'*. | ||
y 3 S- = | y 3 S- = | ||
.._e. %' s | .._e. %' s | ||
.< .] | .< .] | ||
, d .5 _ . < , - , . | , d .5 _ . < , - , . | ||
1 | 1 | ||
, t , sb s | , t , sb s | ||
.' + +< t t' . 'l | .' + +< t t' . 'l | ||
"'t?- | "'t?- | ||
.c- + < .e c > s.<;; _ u;_ i - - | .c- + < .e c > s.<;; _ u;_ i - - | ||
_9 | _9 | ||
~ ~ '' | ~ ~ '' | ||
: e. ;. , | : e. ;. , | ||
, , . l' | , , . l' 4-CONTENTS | ||
4-CONTENTS | |||
' .1. - Title' 2.. Objective: | ' .1. - Title' 2.. Objective: | ||
/3. -Main Questions | /3. -Main Questions | ||
Line 402: | Line 192: | ||
* 7. - LResults from Tests of Various Hole Patterns | * 7. - LResults from Tests of Various Hole Patterns | ||
*8. -Temperature Dependence of Pressure Loading for Five Versions of Perforated Pipe Segments up to 100*C | *8. -Temperature Dependence of Pressure Loading for Five Versions of Perforated Pipe Segments up to 100*C | ||
~ .*9. Important Results from Small-Scale Tests | ~ .*9. Important Results from Small-Scale Tests | ||
*10. . Test: Stand forLPerforated Pipe Experiments | *10. . Test: Stand forLPerforated Pipe Experiments | ||
Line 411: | Line 200: | ||
*14.: SSES T-Quencher | *14.: SSES T-Quencher | ||
*15;. ' Observed Condensation Phases. | *15;. ' Observed Condensation Phases. | ||
: 16. Schematic of Condensation Tank in SRI Tests | : 16. Schematic of Condensation Tank in SRI Tests | ||
*17. . Effect .of Mass Flux'on Steam Jet - | *17. . Effect .of Mass Flux'on Steam Jet - | ||
Line 417: | Line 205: | ||
*19. .Results from SRI Tests | *19. .Results from SRI Tests | ||
~20.- | ~20.- | ||
! Pool Temperature Limit | ! Pool Temperature Limit | ||
. 1 | . 1 | ||
~ | ~ | ||
. ..L . | . ..L . | ||
7 | 7 | ||
*21. Va'riation of the Maximum Pressure Fluctuation Amplitudes | *21. Va'riation of the Maximum Pressure Fluctuation Amplitudes | ||
~with Pressure Ratio Across the Nozzle in SRI ~ Tests | ~with Pressure Ratio Across the Nozzle in SRI ~ Tests | ||
*22. Variations of the Maximum Pressure Fluctuation Amplitudes with Pressure Ratio Across the T-Quencher Holes | *22. Variations of the Maximum Pressure Fluctuation Amplitudes with Pressure Ratio Across the T-Quencher Holes | ||
*23. Comparison of' Test Results Obtained by SRI and KWU 24.~ Bubble Drift | *23. Comparison of' Test Results Obtained by SRI and KWU 24.~ Bubble Drift | ||
: 25. 'Subcooling | : 25. 'Subcooling | ||
: 26. . Bubble Rise Path | : 26. . Bubble Rise Path | ||
Line 442: | Line 220: | ||
: 28. . Condensation Rate | : 28. . Condensation Rate | ||
. 29. Conclusions 1 | . 29. Conclusions 1 | ||
-* proprietaty information l | -* proprietaty information l | ||
l l | l l | ||
l | l | ||
, \ | , \ | ||
OBJECTIVE Assess performance of PP&L T-quencher when saturation temperatures are approached in the suppression pool | OBJECTIVE Assess performance of PP&L T-quencher when saturation temperatures are approached in the suppression pool | ||
ga-esww.suw ymy ,~ ~v i | ga-esww.suw ymy ,~ ~v i | ||
f:'. | f:'. | ||
[ I | [ I s | ||
-l a | |||
s | i d | ||
-l | i s | ||
s | |||
?- | ?- | ||
? | ? | ||
Line 479: | Line 242: | ||
i I | i I | ||
3: - | 3: - | ||
1 1 | 1 1 | ||
i i | i i | ||
1 | 1 | ||
: t. _ _ | : t. _ _ | ||
t APPROACH I | |||
t | |||
e Review available results on quencher performance at high pool temperatures e Analyze the results collectively in relation to performance | e Review available results on quencher performance at high pool temperatures e Analyze the results collectively in relation to performance | ||
.. T-quenchers near pool saturation conditions | .. T-quenchers near pool saturation conditions t | ||
3 | |||
."4, 4 | ."4, 4 | ||
_ _ ,,, , , . . - ,---.e t,-- | _ _ ,,, , , . . - ,---.e t,-- | ||
CHRONOLOGICAL LIST OF REPORTS REVIEWED Number Date Source Report Number 1 May 1973 KWU (Germany) KWU E3-2593 2 May 1973 KWU (Germany) KWU E3-2594 3 July 1973 KWU (Germany) KWU E3/E2-2703 4 December 1974 Brunsbuttal Power Plant KWU R113-3267 (Germany) 5 June 1975 General Electric GER SR-19 6 October 1975 General Electric NEDE-21078 7 August 1977 Brunsbuttel Power Plant KWU R521/40/77 (Germany) ATW 5 1 g,Lu E l 8 October 1978 General Electric MS984999t> g o o g 9 December 1978 KWU (Germany) R 14/100/78 55E5 10 February 1979 KWU (Germany) R 54/1/79 [ DAE 11 July 1979 SRI International PYC 5881 | CHRONOLOGICAL LIST OF REPORTS REVIEWED Number Date Source Report Number 1 May 1973 KWU (Germany) KWU E3-2593 2 May 1973 KWU (Germany) KWU E3-2594 3 July 1973 KWU (Germany) KWU E3/E2-2703 4 December 1974 Brunsbuttal Power Plant KWU R113-3267 (Germany) 5 June 1975 General Electric GER SR-19 6 October 1975 General Electric NEDE-21078 7 August 1977 Brunsbuttel Power Plant KWU R521/40/77 (Germany) ATW 5 1 g,Lu E l 8 October 1978 General Electric MS984999t> g o o g 9 December 1978 KWU (Germany) R 14/100/78 55E5 10 February 1979 KWU (Germany) R 54/1/79 [ DAE 11 July 1979 SRI International PYC 5881 | ||
131PORTANT RESULTS FRO.\1 S3f ALL-SCALE TESTS e Coalescence of bubbles sliould be avoided e Adequate circulation of subcooled water is necessary | 131PORTANT RESULTS FRO.\1 S3f ALL-SCALE TESTS e Coalescence of bubbles sliould be avoided e Adequate circulation of subcooled water is necessary | ||
s SCHEMATIC OF CONDENSATION TANK IN SRI TESTS n | |||
SCHEMATIC OF CONDENSATION TANK IN SRI TESTS n | |||
V Water Tank 36-1/4., (at uniform temperature Viewing and pressure) | V Water Tank 36-1/4., (at uniform temperature Viewing and pressure) | ||
Port | Port 1 cm Diameter | ||
1 cm Diameter | |||
" Hole (s) | " Hole (s) | ||
We Steam Inlet i | We Steam Inlet i | ||
POOL TEMPERATURE LIMIT is there a limiting pool temperature above which pressure loads would exceed the values measured during the T-quencher verification tests? | POOL TEMPERATURE LIMIT is there a limiting pool temperature above which pressure loads would exceed the values measured during the T-quencher verification tests? | ||
4 | 4 | ||
BUBBLE DRIFT e is it possible that pool rotation causes large bubbles formed at high pool temperatures to drift into a highly subcooled region and generate excessive pressures as a result of rapid condensation? | BUBBLE DRIFT e is it possible that pool rotation causes large bubbles formed at high pool temperatures to drift into a highly subcooled region and generate excessive pressures as a result of rapid condensation? | ||
l 1 | l 1 | ||
~ - | ~ - | ||
j , . | j , . | ||
SUBCOOLING e Condensation rate strongly depends on the subcooling (subcooling = saturation temperature - local temperature) e An approximately linear increase of saturation temperature is expected with depth 100 C | SUBCOOLING e Condensation rate strongly depends on the subcooling (subcooling = saturation temperature - local temperature) e An approximately linear increase of saturation temperature is expected with depth 100 C | ||
~ | ~ | ||
1 m l 23 ft ' | |||
1 | |||
m l | |||
23 ft ' | |||
107 C 4 Suppression Pool Saturation Temperature ! | 107 C 4 Suppression Pool Saturation Temperature ! | ||
l i | l i | ||
Line 574: | Line 280: | ||
pool rotation l | pool rotation l | ||
l l | l l | ||
9 . | 9 . | ||
BUBBLE RISE PATH e Maximum pool speed is approximately15 cm/sec e Bubble drift is less than 10 ft (much less than pool perimeter) e Only depthwise temperature variation can influence condensation rate l | BUBBLE RISE PATH e Maximum pool speed is approximately15 cm/sec e Bubble drift is less than 10 ft (much less than pool perimeter) e Only depthwise temperature variation can influence condensation rate l | ||
i 9 _ | i 9 _ | ||
I | I | ||
; | ; | ||
Line 597: | Line 290: | ||
l l | l l | ||
CONDENSATION RATE e Pool is hotter near the bottom around the quenchers e Changes in local temperature and saturation temperature tend to offset each other e Approximately constant condensation rate is expected | CONDENSATION RATE e Pool is hotter near the bottom around the quenchers e Changes in local temperature and saturation temperature tend to offset each other e Approximately constant condensation rate is expected | ||
CONCLUSIONS e Near or at saturation conditions, pressures are smaller than those measured in T-quencher verification tests e Unnecessary to assign a limit for suppression pool temperature on the basis of quencher operation e Violent collapse of large steam bubbles due to drift has no practical significance at SSES l | CONCLUSIONS e Near or at saturation conditions, pressures are smaller than those measured in T-quencher verification tests e Unnecessary to assign a limit for suppression pool temperature on the basis of quencher operation e Violent collapse of large steam bubbles due to drift has no practical significance at SSES l | ||
I l | I l | ||
9 -m}} | 9 -m}} |
Revision as of 06:30, 1 February 2020
ML19318A426 | |
Person / Time | |
---|---|
Site: | Nine Mile Point, Susquehanna, Columbia, Limerick, LaSalle, Zimmer, Shoreham, Bailly File:Long Island Lighting Company icon.png |
Issue date: | 04/10/1980 |
From: | STONE & WEBSTER, INC. |
To: | |
Shared Package | |
ML19318A421 | List: |
References | |
REF-GTECI-A-39, REF-GTECI-CO, TASK-A-39, TASK-OR NUDOCS 8006230007 | |
Download: ML19318A426 (28) | |
Text
.
'- 1' SRV DISCHARGE INTO SUPPRESSION POOL v -
o HATCH PRESENTATION - FEBRUARY 1978
- SIMILAR TO SNPS PRELIMINARY TRANSIENTS PRESENTED IN JANUARY 1976 2
- EVALUATED AGAINST 150 F/40 LBM/FT -SEC LIMIT o NRC EXPRESSED SERIOUS ~ RESERVATIONS WRT R/H LIMITS-MAY/ JUNE 1978
- STRONGLY SUGGESTED QUENCHERS FOR MK II o ZIMMER/LA SALLE CLOSURE REPORTS - JULY 1978
- INCLUDED TRANSIENTS EVALUATED AGAINST R/H LIMITS o MK II COMMITS TO QUENCHERS - AUGUST / SEPTEMBER 1978
-l l :FCR
.4/3/80.
t.
89
- 2 *
- 7 _ n
SRV DISCHARGE INTO SUPPRESSION POOL (CONTINUED) -
o LP ACCEPTANCE CRITERIA /LER ISSUED SEPTEMBER /0CTOBER 1978 200 F (LOCAL)-LIMIT ESTABLISHED FOR QUENCHERS INVITED ADDITIONAL DATA TO SUPPORT HIGHER OR NO LIMIT o MK II APPROACH WORK WITH NRC 200 F LIMIT G0AL: TO MEET LIMIT INDEPENDENT OF RVP MASS FLUX VERY LOW FOR T APPROACHING P00L MAXIMUM ADDITIONAL INFORMATION SUPPORTING STABLE CONDENSATION FOR QUENCHER UNDER ALL CONDITIONS
.FCR 4/3/80
- - _ - - _ _ . _ f
3, NRC REQUESTED MK IIs EVALUATE THE SUPPRESSION-POOL TEMPERATURES FROM THE FOLLOWING TRANSIENTS A. A STUCK-0 PEN SRV DURING POWER OPERATION ASSUMING REACTOR SCRAM AT 10 MINUTES AFTER THE P0OL TEMPERATURE REACHES 110 F AND.ALL RHR SYSTEMS OPERABLE
- B. SAME AS EVENT (A) AB0VE EXCEPT THAT ONLY ONE RHR TRAIN AVAILABLE C. A STUCK-0 PEN SRV DURING HOT STANDBY CONDITIONS, ASSUMING 120 F P0OL TEMPERATURE INITIALLY AND ONLY ONE RHR TRAIN AVAILABLE D. THE AUTOMATIC DEPRESSURIZATION SYSTEM (ADS) ACTIVATED
-FOLLOWING A SMALL LINE BREAK, ASSUMING AN INITIAL P0OL TEMPERATURE OF 120 F AND ONLY ONE RHR TRAIN AVAILABLE E. THE PRIMARY SYSTEM IS ISOLATED AND DEPRESSURIZED AT A RATE OF 100 F/HR. WITH AN INITIAL P0OL TEMPERATURE AT 120 F AND ONLY ONE RHR TRAIN AVAILABLE FCR'JLK/1433-4/3/80
EVENTS EVALUATED FOR MK II SUPPRESSION POOL TEMPERATURE ANALYSIS o STUCK-0 PEN RELIEF VALVE (SORV) o WITH ONE RHR TRAIN AVAILABLE o SPURIOUS ISOLATION - LOSS OF MAIN CONDENSER (WITH ALL RHR SYSTEMS AVAILABLE) o ISOLATION SCRAM i
o WITH ONE-RHR TRAIN AVAILABLE o STUCK-0 PEN RELIEF VALVE AT ISOLATION
.(WITH ALL RHR SYSTEMS AVAILABLE) o -SMALL BREAK o WITH ONE RHR' TRAIN AVAILABLE o WITH SHUTDOWN COOLING UNAVAILABLE (WITH ALL RHR SYSTEMS AVAILABLE FOR P0OL C00l.ING)
FCR: JLKri434 4/4/80
_. 2 ._
_._.:__m_..___..____..__._______.._.__
SUMMARY
OF ZIMMER RESULTS PRELIMINARY PEAK BULK POOL CASE DESCRIPTION TEMP, F STUCK-0 PEN SRV WITH ONE RHR TRAIN AVAILABLE 179 STUCK-0 PEN SRV, SPURIOUS ISOLATION WITH TWO 179 RHR TRAINS AVAILABLE ISOLATION SCRAM, WITH ONE RHR TRAIN AVAILABLE 181 ,
ISOLATION SCRAM, WITH S0RV 186 SMALL' BREAK, WITH ONE RHR TRAIN AVAILABLE 184 SMALL BREAK, WITH SHUTDOWN COOLING UNAVAILABLE 190 FCR: JLK/1435
.4/4/80 1
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ZIMMER PLANT UNIQUE SUPPRESS 10ii POOL TEMPERATURE ASSESSMENT ,
10NCLUSIONS BASED ON THE PRELIMINARY EVALUATIONS PERFORMED
-ON ZIMMERi ZIMMER MEETS THE NRC SUPPRESSION POOL TEMPERATURE LIMITS FOR THE B0UNDING EVENTS EVALUATED, FCR:atx/1436 4/3/80
GENERALIZED ASSUMPTIONS USED FOR P0OL TEMPERATURE ASSESSMENT o ' MAXIMUM SERVICE WATER TEMPERATURE o- INITIAL SUPPRESSION P0OL TEMPERATURE AT MAXIMUM
- NORMAL' TECHNICAL SPECIFICATION LIMIT o DECAY HEAT PER ANS-5 o FULLY CRUDDED RHR HEAT EXCHANGERS o HOT FEEDWATER DUMPED INTO THE SYSTEM TO MAINTAIN LEVEL (FEEDWATER TERMINATED WHEN FURTHER ADDITION WILL RESULT IN REDUCTION OF P0OL TEMPERATURE) o 122.5% ASME RATED FLOW RATE FOR SRV o MINIMUM POOL TECHNICAL SPECIFICATION LEVEL
'o SHUTDOWN COOLING NOT UTILIZED FOR CASES WHERE TWO RHR AVAILABILITY' ASSUMED I
FCR: JLK/1437 4/3/80
- +<-
-MASS ENERGY INPUT ASSUMPTIONS .
-SORV AT~ FULL POWER, WITH ONE RHR TRAIN AVATLABLE o
MANUAL SCRAM AT-TP00L = 110 F
-o GRADUAL CLOSURE 0F THE TURBINE CONTROL-VALVES WITH DECREASING REACTOR PRESSURE o- ONE RHR IN POOL COOLING TEN MINUTES AFTER HIGH
-TEMPERATURE ALARM L
.o MAIN CONDENSER REESTABLISHED THROUGH BYPASS SYSTEM TWENTY MINUTES AFTER SCRAM AND-MAINTAINED UNTIL REACTOR VESSEL PERMISSIVE FOR RHR SHUTDOWN COOLING i
o RHR OUT OF P0OL COOLING.WHEN PRESSURE PERMISSIVE FOR
~
RHR SHUTDOWN' COOLING IS REACHED, SIXTEEN MINUTES
FOR RHR TRANSFER FROM POOL COOLING TO SHUTDOWN COOLING, l
FCR 4/4/80
1, MK II MASS ENERGY ASSUMPTIONS SORV AT FULL POWER - SPURIOUS ISOLATION 0-MANUAL SCRAM AT TP00L = 110 F o ISOLATION AT SCRAM WITH 3,5 SECOND MAIN ISOLATION VALVE CLOSURE o .TWO RHRs IN POOL COOLING TEN MINUTES AFTER HIGH POOL TEMPERATURE ALARM o MANUAL DEPRESSURIZATION (IF REQUIRED) INITIATED AT TP00L = 120 F
.o -RHR SHUTDOWN COOLING NOT USED FOR POOL TEMPERATURE ASSESSMENT 4
FCR- ;
4/3/80
~
~
MASS ENERGY ASSUMPTIONS ISOLATION SCRAM POSTULATED LOSS OF ONE RHR TRAIN J
o ISOLATION. SCRAM AT T = 0 WITH 3.5-SECOND MAIN ISOLATION VALVE CLOSURE
o ONE RHR IN P0OL COOLING TEN MINUTES AFTER.THE' EVENT o WHEN TP00L = 120 F, BEGIN MANUAL DEPRESSURIZATION o RHR OUT OF P0OL COOLING WHEN PRESSURE PERMISSIVE FOR
. 'RHR SHUTDOWN COOLING IS REACHED. SIXTEEN-MINUTE DELAY'FOR-RHR TRANSFER FROM P0OL COOLING TO SHUTDOWN COOLING.
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- FCR: JLK/1440-l : 4/3/80-l i
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MASS ENERGY ASSUMPTIONS ISOLATION SCRAM WITH S0RV o . ISOLATION SCRAM AT T'= 0 WITH 3.5-SECOND MAIN ISOLATION VALVE CLOSURE o' SORY AT T = 0
. o 'TWO RHRs IN P0OL COOLING AT TEN MINUTES AFTER THE EVENT o -WHEN-TP00L = 120 F, BEGIN MANUAL DEPRESSURIZATION o RHR SHUTDOWN-COOLING NOT USED FOR P0OL TEMPERATURE
. ASSESSMENT FCR: JLK/1441L 4/3/80- -
- . . . . .. _ .. . . . . - . - = .
g:;:. ;
.7 MASS ENERGYJASSUMPTIONS SMALL BREAK'WITH ONE RHR. TRAIN AVAILABLE
- 01 SCRAM AT T = 0 ON HIGH DRYWELL PRESSURE o ISOLATION AT T =-0 WITH 3.5-SECOND MAIN ISOLATION VALVE CLOSURE
- o- ONE RHR IN POOL COOLING TEN MINUTES AFTER HIGH P0OL TEMPERATURE ALARM o WHEN TP00L.= 120 F, BEGIN' MANUAL DEPRESSURIZATION o' RHR OUT 0F-P00L C00 LING'WHEN PRESSURE PERMISSIVE FOR.
RHR. SHUTDOWN COOLING IS REACHED. SIXTEEN-MINUTE DELAY FOR RHR TRANSFER FROM POOL COOLING TO SPJTDOWN COOLING.
FCR:atx/1442-4/3/80-
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MASS ENERGY ASSUMPTIONS SMALL BREAK WITH SHUTDOWN COOLING UNAVAILABLE cr SCRAM AT T = 0 ON HIGH DRYWELL PRESSURE -
o ISOLATION AT T = 0 WITH 3.5 MAIN ISOLATION VALVE CLOSURE o .TWO RHRs IN P0OL COOLING TEN MINUTES AFTER HIGH P0OL TEMPERATURE ALARM
- o. WHEN TP00L = 120 F, BEGIN MANUAL DEPRESSURIZATION c- RHR SHUTDOWN COOLING NOT USED FOR P0OL TEMPERATURE I ASSESSMENT:
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_ . ON'P RFORMANCE OF QUENCHERS AT HIGH SUPPRESSION POOL TEMPERATURES ,.=.
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, , . l' 4-CONTENTS
' .1. - Title' 2.. Objective:
/3. -Main Questions
- 4. Approach 5.1 . Chronological- List.of Reports Reviewed
^*6.. Experimental Set-up for Testing Various Hole Patterns-
- 7. - LResults from Tests of Various Hole Patterns
- 8. -Temperature Dependence of Pressure Loading for Five Versions of Perforated Pipe Segments up to 100*C
~ .*9. Important Results from Small-Scale Tests
- 10. . Test: Stand forLPerforated Pipe Experiments
- 11.~ - - Floor- Pressure as a Function of Pool Temperature for
. Perforated Pipe Tests
'*12. ; Distribution. of Temper ature on the Face of Perforated Pipe Segment at Various Times
- 13. Full-Scale Tests at Brunsbuttel
- 14.: SSES T-Quencher
- 15;. ' Observed Condensation Phases.
- 16. Schematic of Condensation Tank in SRI Tests
- 17. . Effect .of Mass Flux'on Steam Jet -
- 18.: - Effect 'of'Subcooling on . Steam Jett
- 19. .Results from SRI Tests
~20.-
! Pool Temperature Limit
. 1
~
. ..L .
7
- 21. Va'riation of the Maximum Pressure Fluctuation Amplitudes
~with Pressure Ratio Across the Nozzle in SRI ~ Tests
- 22. Variations of the Maximum Pressure Fluctuation Amplitudes with Pressure Ratio Across the T-Quencher Holes
- 23. Comparison of' Test Results Obtained by SRI and KWU 24.~ Bubble Drift
- 25. 'Subcooling
- 26. . Bubble Rise Path
. *27. Theoretically predicted Temperature Variation in the Suppression Pool of SSES
- 28. . Condensation Rate
. 29. Conclusions 1
-* proprietaty information l
l l
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OBJECTIVE Assess performance of PP&L T-quencher when saturation temperatures are approached in the suppression pool
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i MAIN QUESTIONS e Pool Temperature Limit
- Effects of Bubble Drift a
3 3
i I
3: -
1 1
i i
1
- t. _ _
t APPROACH I
e Review available results on quencher performance at high pool temperatures e Analyze the results collectively in relation to performance
.. T-quenchers near pool saturation conditions t
3
."4, 4
_ _ ,,, , , . . - ,---.e t,--
CHRONOLOGICAL LIST OF REPORTS REVIEWED Number Date Source Report Number 1 May 1973 KWU (Germany) KWU E3-2593 2 May 1973 KWU (Germany) KWU E3-2594 3 July 1973 KWU (Germany) KWU E3/E2-2703 4 December 1974 Brunsbuttal Power Plant KWU R113-3267 (Germany) 5 June 1975 General Electric GER SR-19 6 October 1975 General Electric NEDE-21078 7 August 1977 Brunsbuttel Power Plant KWU R521/40/77 (Germany) ATW 5 1 g,Lu E l 8 October 1978 General Electric MS984999t> g o o g 9 December 1978 KWU (Germany) R 14/100/78 55E5 10 February 1979 KWU (Germany) R 54/1/79 [ DAE 11 July 1979 SRI International PYC 5881
131PORTANT RESULTS FRO.\1 S3f ALL-SCALE TESTS e Coalescence of bubbles sliould be avoided e Adequate circulation of subcooled water is necessary
s SCHEMATIC OF CONDENSATION TANK IN SRI TESTS n
V Water Tank 36-1/4., (at uniform temperature Viewing and pressure)
Port 1 cm Diameter
" Hole (s)
We Steam Inlet i
POOL TEMPERATURE LIMIT is there a limiting pool temperature above which pressure loads would exceed the values measured during the T-quencher verification tests?
4
BUBBLE DRIFT e is it possible that pool rotation causes large bubbles formed at high pool temperatures to drift into a highly subcooled region and generate excessive pressures as a result of rapid condensation?
l 1
~ -
j , .
SUBCOOLING e Condensation rate strongly depends on the subcooling (subcooling = saturation temperature - local temperature) e An approximately linear increase of saturation temperature is expected with depth 100 C
~
1 m l 23 ft '
107 C 4 Suppression Pool Saturation Temperature !
l i
e Local temperature depends on the extent of bubble drift due to l i
pool rotation l
l l
9 .
BUBBLE RISE PATH e Maximum pool speed is approximately15 cm/sec e Bubble drift is less than 10 ft (much less than pool perimeter) e Only depthwise temperature variation can influence condensation rate l
i 9 _
I
i l
l l
CONDENSATION RATE e Pool is hotter near the bottom around the quenchers e Changes in local temperature and saturation temperature tend to offset each other e Approximately constant condensation rate is expected
CONCLUSIONS e Near or at saturation conditions, pressures are smaller than those measured in T-quencher verification tests e Unnecessary to assign a limit for suppression pool temperature on the basis of quencher operation e Violent collapse of large steam bubbles due to drift has no practical significance at SSES l
I l
9 -m