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=Text= | =Text= | ||
{{#Wiki_filter:}} | {{#Wiki_filter:EMERGENCY CORE COOLING SYSTEMS SURVEILLANCE RE UIREMENTS Continued | ||
: 2. At least once per 18 months. | |||
Boron Injection Safety Injection Throttle Valves Throttle Val ves Valve Number Valve Number | |||
: l. 2-SI-141 Ll 1. 2-SI-121 N | |||
: 2. 2-SI-141 L2 2. 2-SI-121 'S | |||
: 3. 2-SI-141 L3 | |||
: 4. 2-SI-141 L4 | |||
: h. By performing a flow balance test during shutdown following completion of modifications to the ECCS subsystem that alter the subsystem flow characteristics and verifying the following flow rates: | |||
Boron Injection System Safety Injection System Sin le Pu Sin le Pumo"" | |||
Loop 1 Boron Injection Loop 1 and 4 Cold Leg Flow 117.5 gpm . Flow > 300 @pm Loop 2 Boron Injection Loop 2 and 3 Cold Leg Flow 117.5 gpm Flow > 300 gpm Loop 3 Boron Injection **Combined Loop 1,2,3 and 4 Cold Flow 117.5 gpm Leg Flow (single pump) <640 gpm. | |||
Total SIS (single pump) flow, Loop 4 Boron Injection including miniflow, shall not Flow 117.5 gpm exceed 700 gpm. | |||
"The flow rate in each Boron Injection (BI) line should be adjusted to provide 117.5 gpm (nominal) flow into each loop. Under these conditions there is zero mini-flow and 80 gpm simulated RCP seal injection line flow. The actual flow in each BI line may deviate from the nominal so long as the difference between the highest and lowest flow is 10 gpm or less and the total flow to the four branch lines does not exceed 470 gpm. Minimum flow (total flow) required is 345.8 gpm to the three most conservative (lowest&low) branch lines. | |||
84032002i4 8403l5 PDR ADOCK 05000316 P PDR | |||
: 0. C. COOK - UNIT 2 3/4 5-6 Amendment No. | |||
SPECIAL TEST EXCEPTION POSITION XNDXCATOR CHANNELS SKJTDONN LIMITING CONDITION FOR OPERATION 3.10.5 The limitations of Specification 3.1.3.3 may be suspended duzing the performance of individual full length (shutdown and control) rod drop time measuzements provided; | |||
: a. Only one shutdown or control bank is withdrawn from the fully inserted position at a time, and | |||
: b. The group demand position indicator is OPERABLE during the withdrawal of the rods. | |||
APPLICABILITY: MODES 3, 4 and 5 during performance of rod drop tlme measurements. | |||
ACTION | |||
>lith the group demand position indicator inoperable, or more than one bank of rods withdrawn, immediately open the reactor trip breakers. | |||
SURVEILLANCE REQUIREMENTS 4.10.5 Each of the above required group demand position indicator(s) shall be detexmined to be OPERABLE by movement of the associated shutdown or control rods at least 8 steps in any one direction within 24 hours prior to the start of the rod, drop time measurements. | |||
D. C. COOK - UNIT 2 3/4 10-5 | |||
Mr. Harold R. Dent AEP: NRC:~ 0860A | |||
~ | |||
ATTACHMENT 4 TO AEP:NRC:0860A WESTINGHOUSE | |||
==SUMMARY== | |||
OF THE SAFETY EVALUATION FOR INCREASED SZ PUMP MINIFLOW | |||
LOCA EVALUATION FOR D. C. COOK UNIT 2 WITH REDUCED HIGH HEAD SAFFTY INJECTION This evaluation assesses the impact of reduced high head safety injection on ECCS performance in response to a LOCA for the 0. C Cook Unit 2 plant. W Safeguards Systems performed an independent calcula-tion evaluating the impact to high head safety injection {HHSI) of incmasing HHSI pump miniflow from 30 gpm to 60 gpm. The calculation assumed a 60 gpm miniflow and that each pair of cold legs receives greater than 300 gpm during flow balance testing. The ECCS flowrates were then calculated using the vendor performance curve degraded by 5% of design head. The total delivered safety injection flowrates to the RCS for both 30 gpm and 60 gpm are shown in Table I. The reduction of t'otal 'afety injection is 5X in the range of 1200-600 psia important for'- this'valuation. | |||
Lar e Break LOCA Im act HHSI pump flow provides an insignificant proportion of the total 6I flow during a large break accident where RCS pressure rapidly drops to near atmospheric. Accumulator and low head safety injection (RHR) flow are important for this postulated accident. For this reason, small changes in HHSI pump flow have a negligible effect on the large LOCA calculated peak clad temperature. | |||
Small Break LOCA Im act The effect of HHSI 'reduction on small break LOCA is determined. via an analysis with the approved W small break LOCA evaluation model nerformed on the 0. C. Cook Unit 1 plant, which was analyzed at 3411 MWt core power. | |||
The calculated PCT increase derived from this LOCA analysis is 86.1'F, calculated on the worst break size. The inclusion of this PCT increase effect to the base PCT of 1668'F (worst break size) for 0. C. Cook Unit 2 yields a value well below the 10CFR50.46 limit of 2200'F and is less limiting than the current worst large break PCT. | |||
The sensit'ivi ty of PCT due to small HHSI flow reductions developed with D. C. Cook Unit is applicable and bounding for 0. C. Cook Unit 2 1 | |||
for the following reasons: | |||
: 1. The two plants'ydraulic characteristics are nearly identical. The only significant difference is Unit 1 has 15x15 fuel and Unit 2 has 17x17 fuel. Hut more importantly the difference in fuel assembly f1ow areas between the two designs is less tha'n 0.3%. | |||
: 2. The effect of reduced HHSI on the transient is hydrau- | |||
. lic. Reduction in SI diminishes the effects of bofloff replenishing fn the core. Thus, small reduction in downcomer level and core mixture height will result. | |||
This effect is well behaved and observed through . | |||
small LOCA analyses performed for numerous plants studying Sl effects. | |||
: 3. The effect of a reduction in core mixture height in-creases the length of core uncovered and thus the enthalpy rise of the steam. The steam enthalpy at the uncovered elevations determines clad temperature since the transient is quasi-steady state during the clad heatup period. | |||
: 4. The small LOCA analysis for Unit 1 was performed at 3411 MMt, similar to the Cook Unit 2 power. There-fore, the additional enthalpy rise will be calculated correctly. | |||
: 5. The heat linear generation rate For Unit 1 is greater than Unit 2 due to fewer fuel rods. Therefore, the effect on PCT of reduced HHSI will be maximized. | |||
: 6. Other conservatisms in the analysis exist. For example, the small LOCA analysis for Unit 2 assumed an Fg of 2.32 while the plant is limited in operation to 2.04 by large break considerations. | |||
This evaluation has assessed the impact of reduced HHSI on the performance of the ECCS at the D. C. Cook Unit 2 plant. The reduced HHSI has a maximum impact of 86.1'F on peak clad temperature for a small LOCA. The inclusion of this PCT increase to the base small LOCA PCT of 1668'F for D. C. Cook Unit 2 yields a value well below the 10CFR50.46 limit of 2200'F and is less limiting than the current worst large break PCT. | |||
Comparison of Total Safety Injection Flow Delivered to the RCS (Includes Charging, HHSI and LHSI Where Applicable) | |||
RCS Pressure 30 60 SIa ow (1b/s) Minx ow 1b/s) | |||
: 14. 7 510.7 509. 3 114.7 213.2 210.8 140.7 105.0 103.3 214.7 103.0 100.,5 414. 7 p | |||
~ | |||
93.5 91.1 614.7 84.3 81.4 814.7 73+6 70.6 1014.7 61.9 59.0 1214.7 48.2 45.4 1314.7 39. 5 36. 6 | |||
APPENDIX OF ADDITIONAL RESULTS FROM THE | |||
: 0. C. COOK UNIT 1 REDUCED (60 GPM MINIFLOW) | |||
HHS I EYALUATION | |||
D. C. COOK 1 REDUCED HHSI SENSITIVITY SHALL BREAK TIME SEQUENCE OF EVENTS (SEC) | |||
TIME EVENT 4 IlICII START 0.0 REACTOR TRIP SIGNAL 17.5 TOP OF CORE UNCOVERY 413.0 ACCUMULATOR INJECTION BEGINS 800.0 PEAK CLAD TEMPERATURE OCCURS 823.3 TOP OF CORE COVERED 1310 | |||
D. C. COOK UNIT 1 ~ ~ | |||
REDUCED HHSI SENSITIVITY St1ALL BREAK RESULTS RESULTS 4 INCH PEAK CLAD TEMPERATURE (oF) 1716 PEAK CLAD TEMPERATURE LOCATION (FT) 11.75 LOCAL Zr/H20 REACTION, HAXIHUM (X) 0.93 LOCAL Zr/H20 LOCATION (FT) 11.75 TOTAL Zr/H20 REACTION (X) 0.3 HOT ROD BURST TINE (SEC) | |||
HOT ROD BURST LOCATION (FT) | |||
CALCULATION NSSS Power MWt 102K of 3411 peak Linear Power kw/ft 102K of 15.50 Hot Rod Power Distribution ( | |||
Accumulator Hater Volume, cu. ft. 950 Fuel region + cycle analyzed Cycl e Region 8 'kl FUEL UNIT 1 | |||
*SAME COOK UNIT 1 CYCLE 8 RELOAD SHALL BK ANALYSIS | |||
R$ 00.0 0 C COOK UNlf l AEP SH BK 4 ls SK RCOUCE Sl SE~S 3all RCS PRCSSURE OPSIA tS00.0 Vl | |||
; O. | |||
F000.0 | |||
. ih | |||
~~ ~ | |||
VI l500.0 l000.0 | |||
: y. ~ | |||
500.00 | |||
~ .0 4 | |||
TIHE (SEC) | |||
T Fig. 1 RCS PRESSURE - 4IH DIA. CL BK | |||
II.OOO COOK Ullll I AEP SH SK C | |||
IH SK AfDUCf SI Sf NS 3i I I Af HE ICHOR lAi I2.S00 I0.000 | |||
,L l> | |||
l~ | |||
'I 7 5000 R.SOOO 1~ | |||
r} | |||
ll | |||
~ .0 Ck yl | |||
:r 8. 8 Ch CI Jl 8 | |||
TIHE lSECI Fig. 2 . CORE flIXTURE HEIGHT - 4IN DIA CL BK gl | |||
5000.0 D C COOK UNlf l AfP SH BK lN SK RCOUCC Sl SCNS 3ill CLAD AVC.ffHP Nof ROD BURST 12.00 foal l PEAK ll.lS fBel | |||
;w 2500.0 h~ | |||
.'w 2000.0 Ch 4. | |||
g lSoo.o l000.0 soo.oo 0.0 8 Ch C | |||
tlHE lSCCl If thh Fig. 3 HOT SPOT CLAD TEt1PERATURF - 4IN OK | |||
4$ 0.00 0 C COOK .:)IF l AEP SH QK I IN QK.k(tjUCE Sl SENS 311 l | |||
$ 00.00 SIEAH Flou <LBISEC | |||
~8 | |||
~ | |||
%0.00 5 | |||
o IOO.OO X | |||
0.0 | |||
-l00.00 | |||
-200.00 | |||
-)OO.OO | |||
-N0.00 8 | |||
lIHE DECI Fig. 4 CORE STElN FLO'l RATE 4IN BK | |||
0 C ~ | |||
,r}} |
Latest revision as of 00:59, 4 February 2020
ML17326B106 | |
Person / Time | |
---|---|
Site: | Cook |
Issue date: | 03/15/1984 |
From: | INDIANA MICHIGAN POWER CO. (FORMERLY INDIANA & MICHIG |
To: | |
Shared Package | |
ML17326B107 | List: |
References | |
NUDOCS 8403200214 | |
Download: ML17326B106 (17) | |
Text
EMERGENCY CORE COOLING SYSTEMS SURVEILLANCE RE UIREMENTS Continued
- 2. At least once per 18 months.
Boron Injection Safety Injection Throttle Valves Throttle Val ves Valve Number Valve Number
- l. 2-SI-141 Ll 1. 2-SI-121 N
- 2. 2-SI-141 L2 2. 2-SI-121 'S
- 3. 2-SI-141 L3
- 4. 2-SI-141 L4
- h. By performing a flow balance test during shutdown following completion of modifications to the ECCS subsystem that alter the subsystem flow characteristics and verifying the following flow rates:
Boron Injection System Safety Injection System Sin le Pu Sin le Pumo""
Loop 1 Boron Injection Loop 1 and 4 Cold Leg Flow 117.5 gpm . Flow > 300 @pm Loop 2 Boron Injection Loop 2 and 3 Cold Leg Flow 117.5 gpm Flow > 300 gpm Loop 3 Boron Injection **Combined Loop 1,2,3 and 4 Cold Flow 117.5 gpm Leg Flow (single pump) <640 gpm.
Total SIS (single pump) flow, Loop 4 Boron Injection including miniflow, shall not Flow 117.5 gpm exceed 700 gpm.
"The flow rate in each Boron Injection (BI) line should be adjusted to provide 117.5 gpm (nominal) flow into each loop. Under these conditions there is zero mini-flow and 80 gpm simulated RCP seal injection line flow. The actual flow in each BI line may deviate from the nominal so long as the difference between the highest and lowest flow is 10 gpm or less and the total flow to the four branch lines does not exceed 470 gpm. Minimum flow (total flow) required is 345.8 gpm to the three most conservative (lowest&low) branch lines.
84032002i4 8403l5 PDR ADOCK 05000316 P PDR
- 0. C. COOK - UNIT 2 3/4 5-6 Amendment No.
SPECIAL TEST EXCEPTION POSITION XNDXCATOR CHANNELS SKJTDONN LIMITING CONDITION FOR OPERATION 3.10.5 The limitations of Specification 3.1.3.3 may be suspended duzing the performance of individual full length (shutdown and control) rod drop time measuzements provided;
- a. Only one shutdown or control bank is withdrawn from the fully inserted position at a time, and
- b. The group demand position indicator is OPERABLE during the withdrawal of the rods.
APPLICABILITY: MODES 3, 4 and 5 during performance of rod drop tlme measurements.
ACTION
>lith the group demand position indicator inoperable, or more than one bank of rods withdrawn, immediately open the reactor trip breakers.
SURVEILLANCE REQUIREMENTS 4.10.5 Each of the above required group demand position indicator(s) shall be detexmined to be OPERABLE by movement of the associated shutdown or control rods at least 8 steps in any one direction within 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> prior to the start of the rod, drop time measurements.
D. C. COOK - UNIT 2 3/4 10-5
Mr. Harold R. Dent AEP: NRC:~ 0860A
~
ATTACHMENT 4 TO AEP:NRC:0860A WESTINGHOUSE
SUMMARY
OF THE SAFETY EVALUATION FOR INCREASED SZ PUMP MINIFLOW
LOCA EVALUATION FOR D. C. COOK UNIT 2 WITH REDUCED HIGH HEAD SAFFTY INJECTION This evaluation assesses the impact of reduced high head safety injection on ECCS performance in response to a LOCA for the 0. C Cook Unit 2 plant. W Safeguards Systems performed an independent calcula-tion evaluating the impact to high head safety injection {HHSI) of incmasing HHSI pump miniflow from 30 gpm to 60 gpm. The calculation assumed a 60 gpm miniflow and that each pair of cold legs receives greater than 300 gpm during flow balance testing. The ECCS flowrates were then calculated using the vendor performance curve degraded by 5% of design head. The total delivered safety injection flowrates to the RCS for both 30 gpm and 60 gpm are shown in Table I. The reduction of t'otal 'afety injection is 5X in the range of 1200-600 psia important for'- this'valuation.
Lar e Break LOCA Im act HHSI pump flow provides an insignificant proportion of the total 6I flow during a large break accident where RCS pressure rapidly drops to near atmospheric. Accumulator and low head safety injection (RHR) flow are important for this postulated accident. For this reason, small changes in HHSI pump flow have a negligible effect on the large LOCA calculated peak clad temperature.
Small Break LOCA Im act The effect of HHSI 'reduction on small break LOCA is determined. via an analysis with the approved W small break LOCA evaluation model nerformed on the 0. C. Cook Unit 1 plant, which was analyzed at 3411 MWt core power.
The calculated PCT increase derived from this LOCA analysis is 86.1'F, calculated on the worst break size. The inclusion of this PCT increase effect to the base PCT of 1668'F (worst break size) for 0. C. Cook Unit 2 yields a value well below the 10CFR50.46 limit of 2200'F and is less limiting than the current worst large break PCT.
The sensit'ivi ty of PCT due to small HHSI flow reductions developed with D. C. Cook Unit is applicable and bounding for 0. C. Cook Unit 2 1
for the following reasons:
- 1. The two plants'ydraulic characteristics are nearly identical. The only significant difference is Unit 1 has 15x15 fuel and Unit 2 has 17x17 fuel. Hut more importantly the difference in fuel assembly f1ow areas between the two designs is less tha'n 0.3%.
. lic. Reduction in SI diminishes the effects of bofloff replenishing fn the core. Thus, small reduction in downcomer level and core mixture height will result.
This effect is well behaved and observed through .
small LOCA analyses performed for numerous plants studying Sl effects.
- 3. The effect of a reduction in core mixture height in-creases the length of core uncovered and thus the enthalpy rise of the steam. The steam enthalpy at the uncovered elevations determines clad temperature since the transient is quasi-steady state during the clad heatup period.
- 4. The small LOCA analysis for Unit 1 was performed at 3411 MMt, similar to the Cook Unit 2 power. There-fore, the additional enthalpy rise will be calculated correctly.
- 5. The heat linear generation rate For Unit 1 is greater than Unit 2 due to fewer fuel rods. Therefore, the effect on PCT of reduced HHSI will be maximized.
- 6. Other conservatisms in the analysis exist. For example, the small LOCA analysis for Unit 2 assumed an Fg of 2.32 while the plant is limited in operation to 2.04 by large break considerations.
This evaluation has assessed the impact of reduced HHSI on the performance of the ECCS at the D. C. Cook Unit 2 plant. The reduced HHSI has a maximum impact of 86.1'F on peak clad temperature for a small LOCA. The inclusion of this PCT increase to the base small LOCA PCT of 1668'F for D. C. Cook Unit 2 yields a value well below the 10CFR50.46 limit of 2200'F and is less limiting than the current worst large break PCT.
Comparison of Total Safety Injection Flow Delivered to the RCS (Includes Charging, HHSI and LHSI Where Applicable)
RCS Pressure 30 60 SIa ow (1b/s) Minx ow 1b/s)
- 14. 7 510.7 509. 3 114.7 213.2 210.8 140.7 105.0 103.3 214.7 103.0 100.,5 414. 7 p
~
93.5 91.1 614.7 84.3 81.4 814.7 73+6 70.6 1014.7 61.9 59.0 1214.7 48.2 45.4 1314.7 39. 5 36. 6
APPENDIX OF ADDITIONAL RESULTS FROM THE
- 0. C. COOK UNIT 1 REDUCED (60 GPM MINIFLOW)
HHS I EYALUATION
D. C. COOK 1 REDUCED HHSI SENSITIVITY SHALL BREAK TIME SEQUENCE OF EVENTS (SEC)
TIME EVENT 4 IlICII START 0.0 REACTOR TRIP SIGNAL 17.5 TOP OF CORE UNCOVERY 413.0 ACCUMULATOR INJECTION BEGINS 800.0 PEAK CLAD TEMPERATURE OCCURS 823.3 TOP OF CORE COVERED 1310
D. C. COOK UNIT 1 ~ ~
REDUCED HHSI SENSITIVITY St1ALL BREAK RESULTS RESULTS 4 INCH PEAK CLAD TEMPERATURE (oF) 1716 PEAK CLAD TEMPERATURE LOCATION (FT) 11.75 LOCAL Zr/H20 REACTION, HAXIHUM (X) 0.93 LOCAL Zr/H20 LOCATION (FT) 11.75 TOTAL Zr/H20 REACTION (X) 0.3 HOT ROD BURST TINE (SEC)
HOT ROD BURST LOCATION (FT)
CALCULATION NSSS Power MWt 102K of 3411 peak Linear Power kw/ft 102K of 15.50 Hot Rod Power Distribution (
Accumulator Hater Volume, cu. ft. 950 Fuel region + cycle analyzed Cycl e Region 8 'kl FUEL UNIT 1
- SAME COOK UNIT 1 CYCLE 8 RELOAD SHALL BK ANALYSIS
R$ 00.0 0 C COOK UNlf l AEP SH BK 4 ls SK RCOUCE Sl SE~S 3all RCS PRCSSURE OPSIA tS00.0 Vl
- O.
F000.0
. ih
~~ ~
VI l500.0 l000.0
- y. ~
500.00
~ .0 4
TIHE (SEC)
T Fig. 1 RCS PRESSURE - 4IH DIA. CL BK
II.OOO COOK Ullll I AEP SH SK C
IH SK AfDUCf SI Sf NS 3i I I Af HE ICHOR lAi I2.S00 I0.000
,L l>
l~
'I 7 5000 R.SOOO 1~
r}
ll
~ .0 Ck yl
- r 8. 8 Ch CI Jl 8
TIHE lSECI Fig. 2 . CORE flIXTURE HEIGHT - 4IN DIA CL BK gl
5000.0 D C COOK UNlf l AfP SH BK lN SK RCOUCC Sl SCNS 3ill CLAD AVC.ffHP Nof ROD BURST 12.00 foal l PEAK ll.lS fBel
- w 2500.0 h~
.'w 2000.0 Ch 4.
g lSoo.o l000.0 soo.oo 0.0 8 Ch C
tlHE lSCCl If thh Fig. 3 HOT SPOT CLAD TEt1PERATURF - 4IN OK
4$ 0.00 0 C COOK .:)IF l AEP SH QK I IN QK.k(tjUCE Sl SENS 311 l
$ 00.00 SIEAH Flou <LBISEC
~8
~
%0.00 5
o IOO.OO X
0.0
-l00.00
-200.00
-)OO.OO
-N0.00 8
lIHE DECI Fig. 4 CORE STElN FLO'l RATE 4IN BK
0 C ~
,r