Text

New York State Pre-Filed Revised Evidentiary Hearing Exhibit NYSR00141, IP2 FSAR Update Table 14.3-3
	ML12228A650
Person / Time
Site:	Indian Point
Issue date:	08/15/2012
From:	; - No Known Affiliation
To:	; Atomic Safety and Licensing Board Panel
	SECY RAS
References
	RAS 23294, 50-247-LR, 50-286-LR, ASLBP 07-858-03-LR-BD01
	Download: ML12228A650 (188)
	v • d • e

NYSR0014I Corrected: August 15, 2012 NYS000298 Revised: December 22, 2011 IP2 FSAR UPDATE Parameter Initial Transient Range I Uncertainty 1.0 Plant Physical Description

a. Dimensions Nominal $~r#pl~@

b. Flow resistance Nominal $~mPl~g;

c. Pressurizer location Opposite broken loop Bounded

d. Hot assembly location Under limiting location Bounded Bounded

e. Hot assembly type M?XA?l.lp~#~g~q,4IR©gTM claO

arid* N6ri4f'BA Bounded(1j

f. SG tube plugging level High (10%)

2.0 Plant Initial Operating Conditions 2.1 Reactor Power

a. Core average linear heat rate (Af'l..PX) Nominal - Based on 100%

of uprated power (3216 MWt)

b. HptRpg Peak Linear heat rate (PLHR) Derived from desired Tech Spec (TS) nl"rJiff:'S#2.QaN:J m~@Wn *

ij~~~lq?9 * *E8 * #.;2.Q c.~otrodaverage linear heat rate Derived from TS F"H = 1.7 (HRFI..t.JX) d:Hotassembly average heat rate HRFLUXl1.04 (HAPWOX)

$§MPI~g)

e. Hot assembly peak heat rate (BAeHR) PLHR/1.04

$",r1"lpl~@

f. Axial power distribution (PI1l9t,pMiP) Pigl.lt~

1.W$f4q sM.lhd~dm

g. Low power region relative power o.~

(PLOW)

$",r1"lPI~@

4100 MWDlMtO

i. Prior operating history Equilibrium decay heat sM.lhdM:l

j. Moderator Temperature Coefficient Tech Spec Maximum (0)

(MTC)

k. HFP boron Generic Chapter 14, Page 150 of 218 Revision 20, 2006 OAG10000215_1505

IP2 FSAR UPDATE Parameter Initial Transient Range / Uncertainty 2.2Fluid Conditions

a. Tav9

b. Pressurizer pressure NQmib?I* (m2$Q,Q * *~i?) $~mpl~B?

c. Loop flow $O;ZOOQpm S(mM~qW

d. TUH o

e. Pressurizer level o

$~MPI~g)

f. Accumulator temperature NqlJ'lih~I * (1.Q$.~t)

$",@?I$@

g. Accumulator pressure NpMiri~I * (:)$:),~

p§i~)

h. Accumulatorlic@(j volume Nqmiri~1 (795 ft3) $~mpl~B?

$~mpW(~)

i. Accumulator line resistance Nominal Bounded

j. Accumulator boron 3.0 Accident Boundary Conditions

a. Break location Cold leg Bounded

b. Break type Guillotine (pg$¢'W) $~Mpl~g)

c. Break size Nominal (cold leg area) $~MPlM;;

d. Offsite power Available (R¢,$pWMp§ SQt.lhq~qm r4Dhih9j Bounded

e. Safety injection flow Minimum (T;:jpl$14-@S$Sl

$",@?I$@

f. Safety injection temperature Nominal (%~MF)

Bounded

g. Safety injection delay Max delay ($~.Q~$M Bounded

h. Containment pressure Bounded

i. Single failure Bounded

j. Control rod drop time No control rods Chapter 14, Page 151 of 218 Revision 20, 2006 OAG10000215_1506

IP2 FSAR UPDATE Parameter I nitial Transient Range / Uncertainty 4.0 Model Parameters

a. Critical Flow Nominal (Q8:::@.0) §§ImPl~~n

b. Resistance uncertainties in broken Nominal (as coded) §§lmpl~e~

loop

c. Initial stored energy/fuel rod Nominal (as coded) behavior

d. Core heat transfer Nominal (as coded)

e. Delivery and bypassing of ECC Nominal (as coded) Conservative

f. Steam binding/entrainment Nominal (as coded) Conservative

g. Noncondensable Nominal (as coded) Conservative gases/accumulator nitrogen

h. Condensation Nominal (as coded)

Notes:

1.

Chapter 14, Page 152 of 218 Revision 20, 2006 OAG10000215_1507

IP2 FSAR UPDATE TABLE 14.3-4 t..Imifirigl...argeSrealdROTaridoxidatiOriResl.IltsforlridHal"lRoil"lfIJl"lif2 Parameter Result

<13%

Chapter 14, Page 153 of 218 Revision 20, 2006 OAG10000215_1508

IP2 FSAR UPDATE Parameter Operating Range 1.0 Plant Physical Description a) Dimensions No grid deformation duri b) Flow resistance N/A c) Pressurizer location N/A d) Hot assembly location e) Hot assembly type 15 X 15 f) SG tube plugging level 2.0 Plant Initial Operating Conditions 2.1 Reactor Power a) Core average linear heat rate Core power ~ 102% of 3216 MWt b) Peak linear heat rate FQ ~2.5

~PLOW~0.8 h) Hot assembly burnup ~ 75,000 MWD/MTU, lead rod i) Prior operating history All normal operating histories j) MTC ~ 0 at hot full power (HFP) k) HFP boron Chapter 14, Page 154 of 218 Revision 20, 2006 OAG10000215_1509

IP2 FSAR UPDATE Parameter Operating Range 2.2 Fluid Conditions a) T avg b) Pressurizer pressure c) Loop flow d) TUH e) Pressurizer level Normal level, automatic control f) Accumulator temperature g) Accumulator pressure h) Accumulator liquid volume 723 fe :'S: Vacc:'S: 875-fe i) Accumulator fUD Current line configuration j) Minimum ECC boron ~ 2000 ppm 3.0 Accident Boundary Conditions a) Break location N/A b) Break type N/A c) Break size N/A d) Offsite power e) Safety injection flow f) Safety injection temperature g) Safety injection delay h) Containment pressure i) Single failure j) Control rod drop time NOTE:

Chapter 14, Page 155 of 218 Revision 20, 2006 OAG10000215_1510

IP2 FSAR UPDATE Chapter 14, Page 156 of 218 Revision 20, 2006 OAG10000215_1511

IP2 FSAR UPDATE TABLE 14.3-6 Broken Loop Accumulator and Safety Injection Spill to Containment During Blowdown DELETED TABLES 14.3-7 through 14.3-10 DELETED TABLE 14.3-11 Initial Parameters For Small Break LOCA Analysis Licensed Core Power (MWt) (includes 2% calorimetric 3281 uncertainty)

Total Peaking Factor, Fq 2.5 Axial Offset, % 13 Hot Channel Enthalpy Rise Factor, Fb.H 1.70 Maximum Assembly Average Power, PHA 1.51 Fuel Assembly Array 15 x 15 upgraded with IFMs Nominal Accumulator Water Volume, fe 795 Accumulator Tank Volume, fe 1100 Minimum Accumulator Gas Pressure, psia 613 Loop Flow (gpm) 80700 Vessel Inlet Temperature, of 537.451 Vessel Outlet Temperature, of 606.549 RCS Pressure with Uncertainty, psia 2310 Steam Pressure, psia 735.645 Steam Generator Tube Plugging, % 10 Maximum Refueling Water Storage Tank 110 Temperature, of Maximum Condensate Storage Tank Temperature, of 120 Non-I FBA Fuel Backfill Pressure, psig 275 Reactor Trip Setpoint, psia 1860 Safety Injection Signal Setpoint, psia 1715 Safety Injection Delay Time, sec. 25 Signal Processing Delay and Rod Drop Time, sec. 4.7 (2.0 + 2.7)

Feedwater Trip Processing Delay Time, sec. 2 Time for Main Feedwater Flow Coastdown, sec. 8 Auxiliary Feedwater Flow - gpm (1) 380 Auxiliary Feedwater Pump Start Delay Time, sec. 60 Maximum Loop Specific Purge Volume, fe 268.8 NOTE:

(1) The flow from one motor-driven Auxiliary Feedwater Pump is modeled.

Chapter 14, Page 157 of 218 Revision 20, 2006 OAG10000215_1512

IP2 FSAR UPDATE TABLE 14.3-12 Small- Break LOCA Time Sequence of Events EVENT Break Size 2.0 Inch 3.0 Inch 4.0 Inch I I Break Initiation, sec. 0.0 0.0 0.0 Reactor Trip Signal, sec. 43.3 18.2 10.4 Safety Injection Signal, sec. 61.0 26.4 14.9 Top of Core Uncovered, sec. 1711 629 692 Accumulator Injection Begins, sec. NA 1689 850 Peak Clad Temperature Occurs, sec. 1967 1308 955 Top of Core Recovered, sec. 3854 1924 1170 TABLE 14.3-13 Small Break LOCA Analysis Results RESULT Break Size 2.0 Inch 3.0 Inch 4.0 Inch I I Peak Clad Temperature, of 938 1028 878 Peak Clad Temperature Location, ft. 10.75 11.00 11.00 Local Zr/H 2 0 Reaction (max), % <17 <17 <17 Local Zr/H 2 0 Reaction Location, ft. 11.25 11.00 11.25 Total Zr/H 2 0 Reaction, % <1.0 <1.0 <1.0 Hot Rod Burst Time, seconds NA NA NA Hot Rod Burst Location, ft. NA NA NA Chapter 14, Page 158 of 218 Revision 20, 2006 OAG10000215_1513

IP2 FSAR UPDATE TABLE 14.3-14 Internals Deflections Under Abnormal Operation Allowable No Loss-of-Limit1 Function Limit1 (inches) (inches)

Upper barrel, expansion/compression (to Inward - 4.1 8.2 ensure sufficient inlet flow area/and to prevent the barrel from touching any guide tube to avoid disturbing the rod Outward - 1.0 1.0 cluster control guide structure)

Upper package, axial deflection (to 0.100 0.150 maintain the control rod guide structure geometry)2,3 Rod cluster control guide tube, deflection 1.0 1.60/1.75 as a beam (to be consistent with conditions under which ability to trip has been testedh Fuel assembly thimbles, cross-section 0.036 0.072 distortion (to avoid interference between the control rods and the guidesh Notes:

1. The deflection limit values given above correspond to stress levels for the internals structure well below the limiting criteria given by the collapse curves in WCAP-5890 (Reference 30).

Consequently, for the internals the geometric limitations established to ensure safe shutdown capability are more restrictive than those given by the failure stress criteria.

2. See Reference 26.

3. See Reference 27.

Chapter 14, Page 159 of 218 Revision 20, 2006 OAG10000215_1514

IP2 FSAR UPDATE TABLE 14.3-15 SYSTEM PARAMETERS FOR 3216 MWt Parameters RCS Pressure (psia) (with 60 psi uncertainty) 2310 Core Thermal Power (MWt) (without uncertainties) 3216 Reactor Coolant System Total Flowrate (Ibm/sec) 34,250 Vessel Outlet Temperature (OF) (with uncertainty) 613.3 Core Inlet Temperature (OF) (with uncertainty) 545.7 Vessel Average Temperature (OF) 579.5 Initial Steam Generator Steam Pressure (psia) 788 Steam Generator Tube Plugging (%) o Initial Steam Generator Secondary Side Mass (Ibm) 104,300.1 Assumed Maximum Containment Backpressure (psia) 61.7 Accumulator Water Volume (fe) per accumulator (including line volume) 770 N2 Cover Gas Pressure (psia) 700 Temperature (OF) 130 Safety Injection Delay, total (sec) (from beginning of event) 49.1 (Minimum ECCS case) 45 (Maximum ECCS case)

Chapter 14, Page 160 of 218 Revision 20, 2006 OAG10000215_1515

IP2 FSAR UPDATE TABLE 14.3-16 (Sheet 1 of 4)

DOUBLE-ENDED PUMP SUCTION GUILLOTINE MIN SI BLOWDOWN MASS AND ENERGY RELEASES FOR 3216 Mwt TIME BREAK PATH NO.1* BREAK PATH NO.2**

FLOW ENERGY FLOW ENERGY SECONDS LBM/SEC THOUSANDS LBM/SEC THOUSANDS BTU/SEC BTU/SEC .00000 .0 .0 .0 .0

.00102 84849.3 45618.7 38460.5 20632.5

.00204 40171.1 21550.8 39870.6 21387.9

.00312 40159.2 21545.3 39615.5 21250.0

.101 39922.0 21501.5 19727.2 10572.6

.201 40974.9 22258.1 22318.8 11974.5

.302 44538.4 24465.2 23349.8 12534.5

.402 44682.9 24869.9 23496.8 12619.0

.502 43717.2 24675.3 23121.9 12423.6

.601 44127.3 25230.0 22645.7 12173.7

.701 43629.7 25226.5 22265.5 11975.3

.801 42265.6 24676.5 22065.9 11873.3

.902 40921.3 24115.0 21964.7 11823.2 1.00 39778.0 23661.6 21916.4 11800.6 1.10 38622.2 23215.4 21868.9 11777.7 1.20 37319.2 22690.8 21834.5 11761.1 1.30 35944.7 22103.1 21808.2 11748.2 1.40 34695.2 21548.2 21802.4 11746.0 1.50 33741.2 21128.7 21829.4 11761.1 1.60 32976.7 20806.2 21824.2 11758.5 1.70 32268.2 20512.2 21705.1 11693.9 1.80 31535.6 20200.6 21555.6 11612.9 1.90 30716.4 19828.7 21402.4 11530.0 2.00 29976.9 19501.2 21256.3 11451.0 2.10 29196.0 19140.5 21112.8 11373.8 2.20 28344.1 18723.1 20957.2 11290.1 2.30 27335.3 18191.3 20784.2 11197.1 2.40 26135.3 17523.8 20600.6 11098.5 2.50 24599.3 16613.7 20405.2 10993.7 2.60 22535.4 15316.1 20199.6 10883.6 2.70 21036.9 14396.0 19989.1 10771.0 2.80 20639.2 14205.3 19798.0 10668.9 2.90 19987.2 13800.9 19602.5 10564.7 3.00 19522.8 13516.0 19407.4 10460.8 3.10 19376.6 13446.0 19204.5 10352.8 3.20 19201.3 13342.5 18988.4 10237.7 3.30 18810.9 13089.4 18759.2 10115.5 3.40 18480.2 12877.9 18531.2 9994.0 3.50 18122.3 12639.8 18312.4 9877.7 3.60 17692.9 12347.4 18094.2 9761.8 3.70 17211.2 12017.4 17873.1 9644.3 3.80 16724.6 11684.5 17658.8 9530.6 3.90 16264.9 11369.3 17458.8 9424.7 Chapter 14, Page 161 of 218 Revision 20, 2006 OAG10000215_1516

IP2 FSAR UPDATE TABLE 14.3-16 (Sheet 2 of 4)

DOUBLE-ENDED PUMP SUCTION GUILLOTINE MIN SI BLOWDOWN MASS AND ENERGY RELEASES FOR 3216 Mwt TIME BREAK PATH NO.1* BREAK PATH NO.2**

FLOW ENERGY FLOW ENERGY SECONDS LBM/SEC THOUSANDS LBM/SEC THOUSANDS BTU/SEC BTU/SEC 4.00 15820.9 11062.9 17267.5 9323.6 4.20 14978.6 10480.2 16898.7 9128.8 4.40 14290.6 10002.9 16558.4 8949.6 4.60 13707.5 9594.2 16243.5 8784.0 4.80 13236.1 9259.0 15953.9 8632.0 5.00 12820.2 8956.5 15678.5 8487.5 5.20 12481.3 8705.1 15423.5 8353.9 5.40 12234.8 8509.6 15184.4 8228.7 5.60 12013.2 8329.5 14948.5 8105.1 5.80 11845.2 8184.2 14736.2 7994.2 6.00 11685.0 8040.9 14523.9 7883.0 6.20 11581.6 7932.9 14331.5 7782.7 6.40 11553.1 7869.2 14292.3 7767.5 6.60 12293.5 8327.7 14710.1 8000.1 6.80 11952.9 8084.8 14733.3 8016.3 7.00 10706.7 7749.8 14578.9 7935.9 7.20 9189.8 7146.8 14522.0 7909.0 7.40 8892.9 6975.6 14368.8 7828.6 7.60 8891.4 6931.8 14262.7 7774.8 7.75 8873.2 6896.3 14156.0 7719.6 7.80 8859.4 6880.4 14108.8 7694.8 8.00 8797.6 6810.4 13887.9 7577.7 8.20 8769.7 6749.4 13661.1 7457.0 8.40 8796.7 6713.6 13513.7 7379.2 8.60 8840.2 6682.9 13477.8 7360.1 8.80 8856.5 6634.0 13353.8 7289.4 9.00 8859.7 6593.2 13187.4 7194.4 9.20 8823.9 6536.6 13058.2 7120.2 9.40 8768.8 6472.5 12930.8 7047.5 9.60 8705.1 6398.9 12780.7 6962.8 9.80 8632.0 6315.4 12629.7 6878.0 10.0 8548.7 6227.9 12492.6 6801.4 10.2 8442.2 6132.4 12355.1 6724.5 10.401 8328.6 6042.5 12216.2 6646.9 10.402 8328.1 6042.1 12215.6 6646.6 10.403 8327.4 6041.6 12214.9 6646.2 10.6 8200.0 5951.8 12080.4 6571.1 10.8 8065.0 5865.6 11944.4 6495.3 11.0 7923.0 5780.9 11806.4 6418.6 11.2 7779.9 5700.5 11668.3 6342.2 11.4 7631.7 5620.8 11530.0 6265.9 11.6 7480.7 5541.8 11389.2 6188.4 11.8 7327.0 5463.6 11250.5 6112.2 Chapter 14, Page 162 of 218 Revision 20, 2006 OAG10000215_1517

IP2 FSAR UPDATE TABLE 14.3-16 (Sheet 3 of 4)

DOUBLE-ENDED PUMP SUCTION GUILLOTINE MIN SI BLOWDOWN MASS AND ENERGY RELEASES FOR 3216 Mwt TIME BREAK PATH NO.1* BREAK PATH NO.2**

FLOW ENERGY FLOW ENERGY SECONDS LBM/SEC THOUSANDS LBM/SEC THOUSANDS BTU/SEC BTU/SEC 12.0 7176.5 5390.8 11111.5 6036.0 12.2 7026.3 5316.4 10968.4 5957.5 12.4 6883.8 5243.8 10826.9 5880.1 12.6 6747.1 5172.2 10685.1 5802.7 12.8 6615.8 5101.2 10544.3 5726.0 13.0 6488.9 5030.5 10403.6 5649.5 13.2 6366.6 4960.4 10263.5 5573.5 13.4 6249.0 4891.3 10125.0 5498.4 13.6 6135.2 4822.6 9987.3 5423.8 13.8 6026.2 4755.4 9853.5 5351.4 14.0 5919.5 4688.6 9716.7 5277.2 14.2 5816.8 4623.7 9595.4 5206.8 14.4 5713.0 4557.7 9502.1 5137.0 14.6 5602.6 4486.4 9411.0 5054.8 14.8 5476.2 4402.2 9352.2 4978.2 15.0 5328.9 4296.1 9293.2 4893.3 15.2 5176.5 4174.4 9247.0 4809.1 15.4 5038.0 4049.0 9247.1 4747.4 15.6 4932.8 3939.5 9212.9 4671.6 15.8 4851.8 3846.7 9144.7 4586.4 16.0 4778.1 3768.8 9017.4 4479.5 16.2 4704.7 3700.7 8935.1 4400.9 16.4 4630.2 3639.4 8875.9 4338.7 16.6 4554.4 3583.5 8757.9 4251.9 16.8 4479.1 3533.9 8641.2 4168.4 17.0 4403.7 3489.6 8576.6 4112.2 17.2 4326.9 3449.9 8497.4 4051.1 17.4 4248.8 3415.1 8359.4 3964.2 17.6 4169.2 3386.2 8225.0 3880.8 17.8 4088.8 3361.4 8059.9 3783.8 18.0 4003.3 3338.9 8074.0 3771.4 18.2 3911.2 3320.1 7968.5 3702.9 18.4 3816.0 3306.6 7735.9 3574.5 18.6 3711.0 3295.4 7557.1 3468.0 18.8 3599.3 3288.9 7489.2 3409.1 19.0 3476.9 3281.6 7426.3 3351.2 19.2 3339.5 3274.3 7291.6 3261.6 19.4 3112.8 3201.9 7025.2 3115.2 19.6 2872.0 3112.9 6504.2 2859.2 19.8 2656.5 3017.4 5888.0 2563.0 20.0 2468.0 2906.1 5468.7 2349.1 20.2 2308.0 2789.5 5535.0 2328.4 Chapter 14, Page 163 of 218 Revision 20, 2006 OAG10000215_1518

IP2 FSAR UPDATE TABLE 14.3-16 (Sheet 4 of 4)

DOUBLE-ENDED PUMP SUCTION GUILLOTINE MIN SI BLOWDOWN MASS AND ENERGY RELEASES FOR 3216 Mwt TIME BREAK PATH NO.1* BREAK PATH NO.2**

FLOW ENERGY FLOW ENERGY SECONDS LBM/SEC THOUSANDS LBM/SEC THOUSANDS BTU/SEC BTU/SEC 20.4 2123.5 2598.3 6023.0 2465.5 20.6 1956.7 2408.2 6647.5 2649.6 20.8 1812.0 2238.1 6252.1 2446.3 21.0 1685.8 2087.7 5729.5 2214.5 21.2 1569.8 1948.2 5441.1 2075.4 21.4 1456.6 1811.1 5220.4 1957.8 21.6 1354.4 1686.8 5013.5 1843.9 21.8 1255.2 1565.8 4785.1 1723.3 22.0 1167.3 1458.1 4545.6 1601.6 22.2 1080.0 1351.1 4308.3 1484.2 22.4 1007.1 1261.7 4080.5 1374.5 22.6 925.4 1160.7 3859.9 1271.9 22.8 867.4 1089.4 3646.6 1176.7 23.0 825.3 1037.2 3444.0 1089.3 23.2 789.4 992.7 3240.0 1005.3 23.4 746.7 939.5 3027.4 922.4 23.6 698.4 879.3 2818.3 844.1 23.8 652.2 821.7 2632.9 775.9 24.0 605.7 763.5 2411.8 700.2 24.2 558.3 704.1 2167.0 620.5 24.4 510.1 643.7 1892.7 535.3 24.6 461.8 583.1 1579.6 442.0 24.8 413.7 522.6 1221.0 338.7 25.0 364.5 460.6 822.5 226.8 25.2 313.9 396.9 427.8 117.6 25.4 261.3 330.6 101.7 28.0 25.6 207.1 262.2 .0 .0 25.8 156.1 197.8 .0 .0 26.0 102.9 130.6 .0 .0 26.2 40.0 50.9 .0 .0 26.4 .0 .0 .0 .0 Notes:

mass and energy exiting the SG side of the break

- mass and energy exiting the pump side of the break Chapter 14, Page 164 of 218 Revision 20, 2006 OAG10000215_1519

IP2 FSAR UPDATE TABLE 14.3-16a (Sheets 1, 2, 3, & 4 of 4)

DELETED TABLE 14.3-16b (Sheets 1, 2, 3, 4 & 5 of 5)

DELETED TABLE 14.3-16c (Sheets 1 & 2 of 2)

DELETED TABLE 14.3-16d DELETED TABLE 14.3-16e DELETED TABLE 14.3-16f (Sheets 1 & 2 of 2)

DELETED TABLE 14.3-169 DELETED TABLE 14.3-16h DELETED TABLE 14.3-16i DELETED Chapter 14, Page 165 of 218 Revision 20, 2006 OAG10000215_1520

IP2 FSAR UPDATE TABLE 14.3-17 (Sheet 1 of 5)

DOUBLE-ENDED PUMP SUCTION GUILLOTINE MIN SI REFLOOD MASS AND ENERGY RELEASES FOR 3216 MWt TIME BREAK PATH NO.1* BREAK PATH NO.2**

FLOW ENERGY FLOW ENERGY SECONDS LBM/SEC THOUSAND LBM/SEC THOUSAND SBTU/SEC S BTU/SEC 26.4 .0 .0 .0 .0 26.9 .0 .0 .0 .0 27.1 .0 .0 .0 .0 27.2 .0 .0 .0 .0 27.3 .0 .0 .0 .0 27.4 .0 .0 .0 .0 27.4 .0 .0 .0 .0 27.5 31.9 37.5 .0 .0 27.6 13.9 16.4 .0 .0 27.7 12.9 15.2 .0 .0 27.8 18.5 21.8 .0 .0 27.9 23.4 27.6 .0 .0 28.0 29.8 35.1 .0 .0 28.1 35.0 41.2 .0 .0 28.2 39.7 46.7 .0 .0 28.3 44.2 52.1 .0 .0 28.4 47.1 55.5 .0 .0 28.5 51.2 60.3 .0 .0 28.7 54.5 64.2 .0 .0 28.8 58.2 68.6 .0 .0 28.84 60.4 71.1 .0 .0 28.9 61.2 72.1 .0 .0 29.0 64.6 76.1 .0 .0 29.1 67.4 79.4 .0 .0 29.2 70.6 83.1 .0 .0 29.3 73.2 86.2 .0 .0 29.4 75.6 89.1 .0 .0 30.4 97.2 114.5 .0 .0 31.4 115.0 135.6 .0 .0 32.4 130.5 153.9 .0 .0 33.4 144.3 170.2 .0 .0 33.7 148.5 175.2 .0 .0 34.4 279.2 329.8 2803.8 441.0 35.5 382.8 453.1 4084.0 671.4 36.5 380.7 450.7 4057.5 673.4 37.5 374.3 443.1 3986.8 665.2 38.5 367.8 435.4 3914.7 656.5 Chapter 14, Page 166 of 218 Revision 20, 2006 OAG10000215_1521

IP2 FSAR UPDATE TABLE 14.3-17 (Sheet 2 of 5)

DOUBLE-ENDED PUMP SUCTION GUILLOTINE MIN SI REFLOOD MASS AND ENERGY RELEASES FOR 3216 MWt TIME BREAK PATH NO.1* BREAK PATH NO.2**

FLOW ENERGY FLOW ENERGY SECONDS LBM/SEC THOUSAND LBM/SEC THOUSAND SBTU/SEC S BTU/SEC 38.7 366.6 433.8 3900.4 654.8 39.5 361.5 427.8 3843.7 647.9 40.5 355.4 420.5 3774.2 639.4 41.5 349.5 413.5 3706.6 631.0 42.5 343.8 406.7 3640.9 622.9 43.5 338.3 400.2 3577.1 614.9 44.5 333.0 393.9 3515.2 607.2 44.7 332.0 392.6 3503.0 605.7 45.5 327.9 387.8 3455.1 599.8 46.5 412.6 487.9 233.8 276.9 47.5 566.9 673.5 318.8 379.0 48.5 551.8 655.3 310.6 369.1 49.5 470.2 557.7 326.3 288.5 50.3 446.6 529.3 314.3 272.8 50.5 444.3 526.6 313.1 271.3 51.5 434.2 514.5 307.9 264.6 52.5 424.5 502.9 302.9 258.3 53.5 415.1 491.7 298.1 252.1 54.5 405.9 480.7 293.3 246.1 55.5 397.0 470.1 288.7 240.3 56.5 388.2 459.7 284.2 234.6 56.6 387.4 458.6 283.8 234.0 57.5 379.7 449.5 279.8 229.0 58.5 371.4 439.5 275.6 223.6 59.5 363.2 429.8 271.4 218.4 60.5 355.2 420.3 267.3 213.2 61.5 347.4 411.0 263.3 208.2 62.5 339.8 401.9 259.4 203.3 63.5 332.3 393.0 255.5 198.5 64.5 324.9 384.3 251.8 193.8 65.5 317.8 375.7 248.2 189.2 66.5 310.8 367.4 244.6 184.8 67.5 303.9 359.3 241.1 180.4 68.5 297.2 351.3 237.7 176.2 69.5 290.7 343.5 234.4 172.0 70.5 284.3 336.0 231.1 168.0 71.5 278.1 328.6 228.0 164.1 72.4 272.6 322.1 225.2 160.7 Chapter 14, Page 167 of 218 Revision 20, 2006 OAG10000215_1522

IP2 FSAR UPDATE TABLE 14.3-17 (Sheet 3 of 5)

DOUBLE-ENDED PUMP SUCTION GUILLOTINE MIN SI REFLOOD MASS AND ENERGY RELEASES FOR 3216 MWt TIME BREAK PATH NO.1* BREAK PATH NO.2**

FLOW ENERGY FLOW ENERGY SECONDS LBM/SEC THOUSAND LBM/SEC THOUSAND SBTU/SEC S BTU/SEC 72.5 272.0 321.4 224.9 160.3 73.5 266.1 314.3 221.9 156.6 74.5 260.3 307.5 219.0 153.0 75.5 254.7 300.9 216.2 149.5 76.5 249.3 294.4 213.5 146.2 77.5 244.0 288.2 210.8 142.9 78.5 238.9 282.0 208.2 139.7 79.5 233.9 276.1 205.7 136.6 80.5 229.0 270.3 203.3 133.6 81.5 224.2 264.7 200.9 130.7 82.5 219.6 259.2 198.6 127.9 83.5 215.1 253.9 196.4 125.2 84.5 210.8 248.8 194.3 122.5 85.5 206.6 243.8 192.2 120.0 86.5 202.5 239.0 190.2 117.5 87.5 198.6 234.3 188.2 115.1 89.5 191.0 225.4 184.5 110.6 91.5 184.0 217.0 181.0 106.4 93.5 177.4 209.3 177.8 102.4 94.6 174.0 205.2 176.2 100.4 95.5 171.3 202.0 174.9 98.8 97.5 165.6 195.3 172.1 95.5 99.5 160.3 189.1 169.6 92.4 101.5 155.5 183.3 167.2 89.5 103.5 151.0 178.0 165.1 86.9 105.5 146.8 173.1 163.1 84.5 107.5 143.0 168.6 161.3 82.3 109.5 139.5 164.5 159.7 80.3 111.5 136.4 160.8 158.2 78.5 113.5 133.5 157.4 156.8 76.9 115.5 130.8 154.3 155.6 75.4 117.5 128.5 151.4 154.5 74.0 119.5 126.3 148.9 153.5 72.8 121.5 124.4 146.6 152.6 71.7 123.5 122.6 144.6 151.8 70.8 125.0 121.5 143.2 151.2 70.1 125.5 121.1 142.8 151.1 69.9 127.5 119.7 141.1 150.4 69.1 Chapter 14, Page 168 of 218 Revision 20, 2006 OAG10000215_1523

IP2 FSAR UPDATE TABLE 14.3-17 (Sheet 4 of 5)

DOUBLE-ENDED PUMP SUCTION GUILLOTINE MIN SI REFLOOD MASS AND ENERGY RELEASES FOR 3216 MWt TIME BREAK PATH NO.1* BREAK PATH NO.2**

FLOW ENERGY FLOW ENERGY SECONDS LBM/SEC THOUSAND LBM/SEC THOUSAND SBTU/SEC S BTU/SEC 129.5 118.5 139.7 149.8 68.4 131.5 117.4 138.4 149.3 67.8 133.5 116.4 137.2 148.9 67.3 135.5 115.6 136.3 148.5 66.8 137.5 114.9 135.4 148.2 66.4 139.5 114.2 134.6 147.9 66.0 141.5 113.7 134.0 147.6 65.7 143.5 113.2 133.4 147.4 65.4 145.5 112.8 133.0 147.2 65.2 147.5 112.5 132.6 147.0 65.0 149.5 112.3 132.4 146.9 64.9 151.5 112.1 132.2 146.8 64.8 153.5 112.0 132.0 146.8 64.7 155.5 111.9 131.9 146.7 64.6 157.5 111.8 131.8 146.7 64.6 159.5 111.8 131.8 146.6 64.5 161.1 111.8 131.7 146.6 64.5 161.5 111.8 131.8 146.6 64.5 163.5 111.8 131.8 146.6 64.5 165.5 111.8 131.8 146.6 64.5 167.5 111.9 131.9 146.7 64.6 169.5 112.0 132.0 146.7 64.6 171.5 112.1 132.2 146.7 64.6 173.5 112.2 132.3 146.8 64.7 175.5 112.4 132.5 146.8 64.8 177.5 112.5 132.6 146.9 64.8 179.5 112.7 132.8 146.9 64.9 181.5 112.9 133.0 147.0 65.0 183.5 113.0 133.3 147.1 65.1 185.5 113.2 133.5 147.1 65.1 187.5 113.4 133.7 147.2 65.2 189.5 113.6 133.9 147.3 65.3 191.5 113.8 134.2 147.4 65.4 193.5 114.0 134.4 147.4 65.5 195.5 114.3 134.7 147.5 65.6 197.5 114.5 134.9 147.6 65.7 199.5 114.7 135.2 147.7 65.8 201.5 114.9 135.4 147.8 65.9 Chapter 14, Page 169 of 218 Revision 20, 2006 OAG10000215_1524

IP2 FSAR UPDATE TABLE 14.3-17 (Sheet 5 of 5)

DOUBLE-ENDED PUMP SUCTION GUILLOTINE MIN SI REFLOOD MASS AND ENERGY RELEASES FOR 3216 MWt TIME BREAK PATH NO.1* BREAK PATH NO.2**

FLOW ENERGY FLOW SECONDS LBM/SEC THOUSAND SECONDS LBM/SEC SBTU/SEC 203.5 115.1 135.7 147.9 66.0 205.5 115.3 135.9 147.9 66.1 207.5 115.5 136.1 148.0 66.2 209.5 115.7 136.4 148.1 66.3 211.5 115.9 136.6 148.2 66.4 213.5 116.1 136.9 148.3 66.5 215.5 116.3 137.1 148.4 66.6 217.5 116.5 137.4 148.4 66.7 219.5 116.8 137.6 148.5 66.8 221.5 117.0 137.9 148.6 66.9 223.5 117.2 138.1 148.7 67.0 225.5 117.4 138.4 148.8 67.1 227.5 117.6 138.7 148.9 67.2 229.5 117.9 138.9 149.0 67.4 231.5 118.1 139.2 149.1 67.5 233.5 118.3 139.5 149.1 67.6 235.5 118.5 139.7 149.2 67.7 237.5 118.8 140.0 149.3 67.8 239.5 119.0 140.3 149.4 67.9 239.7 119.0 140.3 149.4 67.9 Notes:

mass and energy exiting the SG side of the break

- mass and energy exiting the pump side of the break Chapter 14, Page 170 of 218 Revision 20, 2006 OAG10000215_1525

IP2 FSAR UPDATE TABLE 14.3-18 DOUBLE-ENDED PUMP SUCTION GUILLOTINE MIN SI POST-REFLOOD MASS AND ENERGY RELEASES FOR 3216 MWt TIME BREAK PATH NO.1* BREAK PATH NO.2**

FLOW ENERGY FLOW ENERGY SECONDS LBM/SEC THOUSANDS LBM/SEC THOUSAN BTU/SEC OS BTU/SEC 239.8 218.7 272.7 208.8 137.2 244.8 218.2 272.0 208.5 136.8 249.8 217.7 271.4 208.2 136.4 254.8 217.1 270.7 207.9 136.0 259.8 216.5 269.9 207.5 135.6 264.8 216.6 270.0 207.2 135.2 269.8 215.9 269.2 206.9 134.8 274.8 215.2 268.3 206.5 134.4 279.8 215.2 268.3 206.2 134.0 284.8 214.4 267.3 205.9 133.6 289.8 214.3 267.1 205.5 133.2 294.8 213.4 266.1 205.2 132.9 299.8 213.2 265.8 204.9 132.5 304.8 212.9 265.4 204.5 132.1 309.8 211.9 264.2 204.2 131.7 314.8 211.5 263.7 203.8 131.3 319.8 211.0 263.1 203.5 130.9 324.8 210.5 262.4 203.2 130.4 329.8 210.5 262.4 202.8 130.0 334.8 209.8 261.5 202.5 129.6 339.8 209.6 261.3 202.1 129.2 344.8 208.7 260.2 201.8 128.8 349.8 208.3 259.7 201.4 128.4 354.8 207.8 259.1 201.1 128.0 359.8 207.2 258.3 200.7 127.6 364.8 207.0 258.0 200.4 127.2 369.8 206.6 257.6 200.0 126.8 374.8 206.0 256.9 199.7 126.3 379.8 205.3 255.9 199.3 125.9 384.8 204.8 255.3 199.0 125.5 389.8 204.6 255.0 198.6 125.1 394.8 204.0 254.3 198.3 124.7 399.8 203.5 253.8 197.9 124.2 404.8 202.8 252.8 197.5 123.8 409.8 202.4 252.4 197.2 123.4 414.8 202.3 252.2 196.8 123.0 419.8 201.6 251.4 196.5 122.6 424.8 201.1 250.7 196.1 122.2 429.8 205.4 256.1 199.9 126.6 Chapter 14, Page 171 of 218 Revision 20, 2006 OAG10000215_1526

IP2 FSAR UPDATE TABLE 14.3-18 (Cont.)

DOUBLE-ENDED PUMP SUCTION GUILLOTINE MIN SI POST-REFLOOD MASS AND ENERGY RELEASES FOR 3216 MWt TIME BREAK PATH NO.1* BREAK PATH NO.2**

FLOW ENERGY FLOW SECONDS LBM/SEC THOUSANDS SECONDS LBM/SEC BTU/SEC 434.8 205.1 255.7 199.5 126.1 439.8 204.6 255.1 199.1 125.7 444.8 204.0 254.3 198.8 125.3 449.8 203.4 253.6 198.4 124.8 454.8 85.7 106.9 310.3 154.0 627.6 85.7 106.9 310.3 154.0 627.7 87.5 108.4 308.4 147.8 629.8 87.5 108.3 308.5 147.6 1262.4 87.5 108.3 308.5 147.6 1262.5 74.8 86.1 321.1 31.0 1500.5 71.4 82.2 324.5 31.6 1500.6 71.4 82.2 167.3 63.8 2334.0 64.4 74.1 174.3 65.0 2334.1 64.4 74.1 174.3 65.0 3600.0 57.2 65.8 181.5 66.3 3600.1 54.3 62.5 184.3 48.7 10000.0 39.5 45.5 199.2 52.6 23400.0 31.9 36.7 206.8 54.6 23400.1 31.9 36.7 73.3 19.4 100000.0 21.1 24.3 84.1 22.2 1000000.0 9.1 10.4 96.1 25.4 10000000.0 2.8 3.3 102.4 27.0

mass and energy exiting the SG side of the break

- mass and energy exiting the pump side of the break Chapter 14, Page 172 of 218 Revision 20, 2006 OAG10000215_1527

IP2 FSAR UPDATE TABLE 14.3-19 DOUBLE-ENDED PUMP SUCTION GUILLOTINE MIN SI MASS BALANCE FOR 3216 MWt Mass Balance

.00 26.40 26.4+8 239.71 627.68 1262.40 3600.00 Time (Seconds)

Mass (Thousand Ibm) 714.25 714.25 714.25 714.25 714.25 714.25 714.25 Initial In RCS and ACC

.00 .00 .00 74.24 227.83 479.16 1074.54 Added Pumped Mass Injection

.00 .00 .00 74.24 227.83 479.16 1074.54 Total Added 714.25 714.25 714.25 788.50 942.08 1193.41 1788.79

- - TOTAL AVAI LABLE ***

524.25 58.26 84.53 144.26 144.26 144.26 144.26 Distributio Reactor n Coolant 190.00 126.74 100.47 .00 .00 .00 .00 Accumulator 714.25 185.00 185.00 144.26 144.26 144.26 144.26 Total Contents

.00 529.24 529.24 644.22 801.15 1052.40 1647.79 Effluent Break Flow

.00 .00 .00 .00 .00 .00 .00 ECCS Spill

.00 529.24 529.24 644.22 801.15 1052.40 1647.79 Total Effluent 714.25 714.24 714.24 788.48 945.41 1196.65 1792.04

- - TOTAL ACCOUNTABLE Chapter 14, Page 173 of 218 Revision 20, 2006 OAG10000215_1528

IP2 FSAR UPDATE TABLE 14.3-20 DOUBLE-ENDED PUMP SUCTION BREAK GUILLOTINE MIN SI ENERGY BALANCE FOR 3216 MWt Energy Balance

.00 26.40 26.4+8 239.71 627.68 1262.40 3600.00 Time (Seconds)

Energy (Million Btu) 781.41 781.41 781.41 781.41 781.41 781.41 781.41 Initial Energy In RCS, ACC, Steam Gen

.00 .00 .00 5.79 17.78 37.38 177.08 Added Pumped Energy Injection

.00 7.52 7.52 30.60 63.24 107.96 235.94 Decay Heat

.00 8.54 8.54 8.54 8.54 8.54 8.54 Heat From Secondary

.00 16.07 16.07 44.94 89.56 153.89 421.56 Total Added 781.41 797.48 797.48 826.35 870.98 935.30

- - TOTAL AVAI LABLE ***

305.58 13.36 15.98 38.17 38.17 38.17 38.17 Distribution Reactor Coolant 18.95 12.64 10.02 .00 .00 .00 .00 Accumulator 27.00 13.89 13.89 3.95 3.78 3.55 2.71 Core Stored 166.68 158.73 158.73 131.10 92.65 69.95 53.20 Primary Metal 40.99 41.26 41.26 38.20 29.44 20.05 15.21 Secondary Metal 222.23 237.68 237.68 217.15 162.06 107.20 80.60 Steam Generator 781.41 477.56 477.56 428.56 326.09 238.91 189.88 Total Contents

.00 319.44 319.44 389.59 537.57 680.69 998.74 Effluent Break Flow

.00 .00 .00 .00 .00 .00 .00 ECCS Spill

.00 319.44 319.44 389.59 537.57 680.69 998.74 Total Effluent 781.41 797.01 797.01 818.15 863.66 919.61 1188.62

- - TOTAL ACCOUNTABLE Chapter 14, Page 174 of 218 Revision 20, 2006 OAG10000215_1529

IP2 FSAR UPDATE TABLE 14.3-21 DOUBLE-ENDED PUMP SUCTION GUILLOTINE MIN SI PRINCIPLE PARAMETERS DURING REFLOOD FOR 3216 MWt Time Flooding Carry- Core Downcomer Flow Injection over Height Height Fraction Temp Rate Total Accum Spill Enthalpy Fraction Secon (OF) (in/sec) (-----) (Feet) (Feet) (-----) (Pounds Mass Per Second) Btu/Lbm ds 26.4 190.0 .000 .000 .00 .00 .250 .0 .0 .0 .00 27.1 188.6 20.878 .000 .50 1.17 .000 6713.2 6713.2 .0 99.50 27.4 187.2 24.643 .000 1.09 1.23 .000 6647.4 6647.4 .0 99.50 27.8 186.9 2.520 .126 1.34 2.09 .225 6528.7 6528.7 .0 99.50 28.1 187.0 2.568 .184 1.39 2.78 .288 6457.6 6457.6 .0 99.50 28.8 187.3 2.426 .300 1.50 4.37 .322 6325.9 6325.9 .0 99.50 29.4 187.5 2.365 .373 1.58 5.66 .333 6214.4 6214.4 .0 99.50 33.7 189.4 2.656 .616 2.00 14.86 .353 5534.7 5534.7 .0 99.50 35.5 190.2 4.041 .665 2.18 16.12 .552 4887.5 4887.5 .0 99.50 37.5 191.2 3.817 .693 2.39 16.12 .548 4666.9 4666.9 .0 99.50 38.7 191.8 3.708 .703 2.51 16.12 .545 4554.1 4554.1 .0 99.50 44.7 195.4 3.354 .726 3.00 16.12 .529 4072.9 4072.9 .0 99.50 45.5 195.9 3.319 .727 3.06 16.12 .527 4017.0 4017.0 .0 99.50 46.5 196.5 3.905 .732 3.14 16.05 .638 .0 .0 .0 .00 47.5 197.3 4.688 .732 3.24 15.59 .640 .0 .0 .0 .00 50.3 199.4 3.866 .735 3.51 14.51 .608 358.5 .0 .0 78.02 56.6 204.5 3.371 .738 4.00 13.08 .603 367.3 .0 .0 78.02 64.5 211.7 2.865 .737 4.54 11.70 .596 375.5 .0 .0 78.02 72.4 219.2 2.447 .735 5.00 10.70 .587 381.4 .0 .0 78.02 83.5 229.1 1.994 .731 5.54 9.81 .571 386.6 .0 .0 78.02 94.6 236.8 1.674 .727 6.00 9.37 .554 389.8 .0 .0 78.02 o 109.5 244.9 1.407 .723 6.52 9.23 .532 392.0 .0 .0 78.02 G) 125.0 251.7 1.265 .721 7.00 9.42 .516 393.0 .0 .0 78.02 o

o o

o N

Chapter 14, Page 175 of 218 1(J1 Revision 20, 2006 (J1 0) o

IP2 FSAR UPDATE TABLE 14.3-21 (Cont.)

DOUBLE-ENDED PUMP SUCTION GUILLOTINE MIN SI PRINCIPLE PARAMETERS DURING REFLOOD FOR 3216 MWt Time Flooding Carry- Core Downcomer Flow Injection Temp Rate over Height Height Fraction Total Accum Spill Enthalpy Fraction Secon (OF) (in/sec) (-----) (Feet) (Feet) (-----) (Pounds Mass Per Second) Btu/Lbm ds 143.5 258.3 1.196 .724 7.52 9.83 .508 393.4 .0 .0 78.02 161.1 263.8 1.177 .728 8.00 10.30 .506 393.5 .0 .0 78.02 173.5 267.2 1.174 .732 8.33 10.64 .507 393.4 .0 .0 78.02 181.5 269.2 1.175 .734 8.54 10.86 .508 393.4 .0 .0 78.02 199.5 273.4 1.179 .740 9.00 11.35 .510 393.3 .0 .0 78.02 219.5 277.5 1.183 .747 9.50 11.89 .513 393.3 .0 .0 78.02 239.7 281.2 1.188 .755 10.00 12.42 .515 393.2 .0 .0 78.02 o

G) o o

o o

N Chapter 14, Page 176 of 218 1(J1 Revision 20, 2006 (J1 0)

IP2 FSAR UPDATE TABLE 14.3-22 (Sheet 1 of 5)

DOUBLE-ENDED PUMP SUCTION GUILLOTINE MAXIMUM ECCS FLOWS BLOWDOWN MASS AND ENERGY RELEASES FOR 3216 Mwt TIME BREAK PATH NO.1* BREAK PATH NO.2**

FLOW ENERGY FLOW ENERGY SECONDS LBM/SEC THOUSANDS LBM/SEC THOUSANDS BTU/SEC BTU/SEC .00000 .0 .0 .0 .0

.00102 84849.3 45618.7 38460.5 20632.5

.00204 40171.1 21550.8 39870.6 21387.9

.00312 40159.2 21545.3 39615.5 21250.0

.101 39922.8 21502.1 19730.1 10574.2

.201 40979.6 22261.5 22314.8 11972.4

.301 44573.7 24485.7 23347.7 12533.3

.401 44733.5 24903.4 23497.2 12619.1

.502 43754.1 24707.6 23117.1 12420.9

.602 44173.0 25273.0 22640.6 12170.9

.701 43682.7 25278.5 22266.0 11975.5

.802 42297.2 24725.0 22065.4 11873.0

.901 40947.3 24164.9 21967.8 11824.8 1.00 39767.1 23698.6 21919.4 11802.2 1.10 38584.1 23240.8 21873.8 11780.4 1.20 37249.5 22702.1 21840.4 11764.4 1.30 35816.5 22086.0 21815.1 11752.1 1.40 34574.8 21534.6 21810.6 11750.5 1.50 33613.4 21111.2 21839.1 11766.5 1.60 32853.5 20790.6 21835.5 11764.7 1.70 32154.3 20501.2 21717.1 11700.6 1.80 31432.8 20195.4 21569.0 11620.3 1.90 30640.2 19839.4 21417.8 11538.5 2.00 29904.6 19514.1 21273.0 11460.3 2.10 29142.5 19163.4 21131.5 11384.2 2.20 28311.2 18759.2 20976.6 11300.9 2.30 27339.3 18251.3 20805.2 11208.8 2.40 26109.9 17561.4 20624.4 11111.9 2.50 24628.0 16684.9 20436.4 11011.2 2.60 22707.6 15483.7 20235.9 10904.1 2.70 21119.5 14495.7 20024.8 10791.3 2.80 20677.2 14277.7 19830.0 10687.6 2.90 20092.1 13921.6 19641.2 10587.2 3.00 19618.0 13629.3 19452.2 10486.9 3.10 19439.5 13538.0 19253.4 10381.6 Chapter 14, Page 177 of 218 Revision 20, 2006 OAG10000215_1532

IP2 FSAR UPDATE TABLE 14.3-22 (Sheet 2 of 5)

DOUBLE-ENDED PUMP SUCTION GUILLOTINE MAXIMUM ECCS FLOWS BLOWDOWN MASS AND ENERGY RELEASES FOR 3216 Mwt TIME BREAK PATH NO.1* BREAK PATH NO.2**

FLOW ENERGY FLOW SECONDS LBM/SEC THOUSANDS SECONDS LBM/SEC BTU/SEC 3.20 19277.2 13446.3 19038.5 10267.5 3.30 18887.7 13195.0 18811.0 10146.7 3.40 18582.5 13000.8 18590.3 10029.7 3.50 18234.9 12768.3 18376.3 9916.6 3.60 17794.6 12467.4 18158.9 9801.7 3.70 17321.2 12144.4 17944.9 9688.6 3.80 16848.6 11822.4 17737.4 9579.2 3.90 16396.6 11512.6 17538.0 9474.3 4.00 15955.2 11206.7 17348.5 9374.9 4.20 15135.8 10639.0 16986.7 9185.4 4.40 14450.3 10162.8 16655.3 9012.6 4.60 13877.1 9759.9 16344.2 8850.7 4.80 13404.7 9422.8 16060.8 8703.8 5.00 13011.8 9135.4 15789.2 8563.0 5.20 12732.5 8922.1 15540.3 8434.4 5.40 12478.1 8723.0 15299.7 8310.1 5.60 12276.0 8558.7 15078.5 8196.2 5.80 12100.2 8407.6 14860.7 8083.8 6.00 11970.8 8286.4 14662.3 7982.1 6.20 11897.3 8198.2 14466.7 7881.5 6.40 11941.5 8184.6 14308.5 7801.8 6.60 12573.4 8577.2 14836.8 8099.2 6.80 12267.5 8335.5 14923.1 8152.2 7.00 11115.9 8022.4 14778.1 8077.9 7.20 9516.4 7395.4 14698.4 8039.6 7.40 9167.6 7210.5 14540.2 7957.4 7.60 9127.7 7152.4 14376.2 7872.8 7.80 9064.7 7090.9 14232.0 7799.4 8.00 8976.5 7009.1 13995.3 7674.5 8.20 8938.7 6944.0 13762.8 7551.6 8.40 8944.4 6890.1 13558.1 7442.5 8.60 8964.5 6847.8 13401.7 7357.6 8.80 8988.7 6815.2 13346.4 7326.0 9.00 8943.5 6738.5 13265.6 7276.9 Chapter 14, Page 178 of 218 Revision 20, 2006 OAG10000215_1533

IP2 FSAR UPDATE TABLE 14.3-22 (Sheet 3 of 5)

DOUBLE-ENDED PUMP SUCTION GUILLOTINE MAXIMUM ECCS FLOWS BLOWDOWN MASS AND ENERGY RELEASES FOR 3216 Mwt TIME BREAK PATH NO.1* BREAK PATH NO.2**

FLOW ENERGY FLOW SECONDS LBM/SEC THOUSANDS SECONDS LBM/SEC BTU/SEC 9.20 8873.3 6665.8 13116.3 7188.5 9.40 8771.5 6589.3 12977.4 7107.1 9.60 8643.0 6499.3 12853.6 7035.2 9.80 8522.7 6406.2 12713.2 6954.8 10.0 8413.6 6305.9 12565.4 6870.7 10.2 8325.3 6213.6 12425.6 6791.3 10.4 8236.9 6121.7 12287.2 6712.8 10.6 8147.1 6034.8 12149.6 6634.7 10.8 8049.5 5950.5 12013.2 6557.5 11.0 7943.5 5868.5 11876.1 6480.1 11.2 7827.4 5787.9 11739.4 6403.4 11.4 7703.1 5708.8 11602.8 6327.0 11.6 7571.4 5630.8 11466.2 6251.0 11.8 7432.6 5552.9 11327.9 6174.2 12.0 7287.4 5475.4 11190.3 6098.1 12.2 7143.9 5404.4 11053.9 6022.8 12.4 6998.6 5332.3 10913.4 5945.4 12.6 6857.7 5261.2 10773.8 5868.7 12.8 6722.4 5191.7 10634.2 5792.3 13.0 6590.5 5122.9 10494.3 5715.9 13.2 6461.5 5054.6 10355.0 5640.1 13.4 6336.3 4987.1 10215.8 5564.4 13.6 6213.6 4920.1 10076.1 5488.5 13.8 6095.2 4854.0 9939.9 5414.5 14.0 5981.4 4789.2 9804.5 5341.0 14.2 5870.0 4725.2 9667.8 5266.6 14.4 5762.4 4663.0 9548.5 5195.8 14.6 5651.0 4597.9 9450.6 5121.3 14.8 5528.1 4523.8 9346.8 5029.6 15.0 5387.0 4432.0 9292.2 4951.8 15.2 5233.8 4321.4 9221.7 4856.4 15.4 5084.6 4200.2 9195.7 4779.9 15.6 4953.8 4082.5 9185.0 4710.7 15.8 4851.5 3981.3 9150.7 4634.3 16.0 4763.9 3896.2 9065.1 4540.5 Chapter 14, Page 179 of 218 Revision 20, 2006 OAG10000215_1534

IP2 FSAR UPDATE TABLE 14.3-22 (Sheet 4 of 5)

DOUBLE-ENDED PUMP SUCTION GUILLOTINE MAXIMUM ECCS FLOWS BLOWDOWN MASS AND ENERGY RELEASES FOR 3216 Mwt TIME BREAK PATH NO.1* BREAK PATH NO.2**

FLOW ENERGY FLOW SECONDS LBM/SEC THOUSANDS SECONDS LBM/SEC BTU/SEC 16.2 4679.7 3824.4 8924.7 4427.4 16.4 4594.8 3761.2 8849.9 4352.3 16.6 4509.0 3704.4 8774.1 4281.8 16.8 4423.0 3654.2 8624.3 4179.2 17.0 4338.2 3611.9 8508.6 4095.2 17.2 4249.9 3574.2 8449.4 4040.2 17.4 4161.1 3542.1 8334.7 3961.4 17.6 4070.4 3517.3 8134.0 3843.5 17.8 3977.6 3498.7 7692.7 3611.5 18.0 3879.6 3483.8 7925.8 3695.0 18.2 3766.4 3467.4 8408.4 3898.6 18.4 3647.5 3459.9 7772.1 3588.3 18.6 3523.9 3459.4 6787.4 3115.0 18.8 3316.3 3392.0 6792.5 3085.4 19.0 3075.5 3296.5 6861.7 3076.2 19.2 2851.5 3194.6 6591.0 2917.6 19.4 2653.8 3085.2 6186.4 2705.8 19.6 2481.6 2968.9 5760.6 2488.9 19.8 2319.3 2822.8 5425.6 2309.7 20.0 2157.3 2647.7 5521.7 2301.1 20.2 1997.9 2463.6 5978.1 2425.4 20.4 1849.6 2288.4 6479.4 2560.5 20.6 1720.9 2134.5 6024.8 2338.2 20.8 1601.7 1991.3 5615.7 2151.8 21.0 1491.6 1857.6 5333.2 2015.1 21.2 1391.2 1735.8 5105.3 1895.5 21.4 1296.0 1619.3 4883.9 1777.2 21.6 1207.7 1511.3 4646.3 1654.6 21.8 1116.9 1399.1 4398.9 1531.3 22.0 1047.8 1314.8 4158.4 1414.7 22.2 968.7 1216.9 3926.8 1305.8 22.4 922.7 1160.5 3713.1 1207.8 22.6 883.2 1111.8 3507.5 1116.8 22.8 840.3 1058.5 3309.9 1032.7 23.0 800.0 1008.2 3105.1 950.2 Chapter 14, Page 180 of 218 Revision 20, 2006 OAG10000215_1535

IP2 FSAR UPDATE TABLE 14.3-22 (Sheet 5 of 5)

DOUBLE-ENDED PUMP SUCTION GUILLOTINE MAXIMUM ECCS FLOWS BLOWDOWN MASS AND ENERGY RELEASES FOR 3216 Mwt TIME BREAK PATH NO.1* BREAK PATH NO.2**

FLOW ENERGY FLOW SECONDS LBM/SEC THOUSANDS SECONDS LBM/SEC BTU/SEC 23.2 755.0 952.2 2893.1 869.5 23.4 706.2 891.1 2726.2 805.7 23.6 656.7 829.2 2523.1 734.2 23.8 606.2 765.9 2294.3 658.1 24.0 555.7 702.5 2035.7 576.5 24.2 504.9 638.5 1740.4 487.3 24.4 454.2 574.8 1396.2 387.3 24.6 403.2 510.5 1003.6 276.4 24.8 350.6 444.2 589.7 161.7 25.0 296.1 375.3 226.7 62.1 25.2 239.7 303.9 .0 .0 25.4 183.3 232.7 .0 .0 25.6 130.6 165.9 .0 .0 25.8 75.7 96.4 .0 .0 26.0 .0 .0 .0 .0

mass and energy exiting the SG side of the break

- mass and energy exiting the pump side of the break Chapter 14, Page 181 of 218 Revision 20, 2006 OAG10000215_1536

IP2 FSAR UPOATE TABLE 14.3-23

[ O* * *E*

L* *

E*

T*

E*

O* * *]

.::::/.:::::. : : : . ::::\.H.::?.::::.:

TABLE 14.3-24

[0 atJam ao]

TABLE 14.3-25

[0 atJam §R]

TABLE ..........................

14.3-26

[0 atJam ao]

Chapter 14, Page 182 of 218 Revision 20, 2006 OAG10000215_1537

IP2 FSAR UPDATE TABLE 14.3-27 (Sheet 1 of 2)

DOUBLE-ENDED PUMP SUCTION GUILLOTINE MAXSI PRINCIPLE PARAMETERS DURING REFLOOD FOR 3216 MWt Time Flooding Carryover Core Downcomer Flow Total Injection Spill Enthalpy Seconds Fraction Height Height Frac Accum Btu/Ibm (ft) (tt)

Temp Rate (Pounds Mass per Second) of in/sec 26.0 189.3 .000 .000 .00 .00 .250 .0 .0 .0 .00 26.7 187.9 20.997 .000 .50 1.18 .000 6759.0 6759.0 .0 99.50 27.0 186.5 24.771 .000 1.10 1.24 .000 6692.1 6692.1 .0 99.50 27.4 186.3 2.530 .127 1.34 2.12 .228 6571.3 6571.3 .0 99.50 27.7 186.4 2.571 .171 1.38 2.64 .279 6514.3 6514.3 .0 99.50 28.4 186.6 2.434 .294 1.50 4.35 .321 6369.9 6369.9 .0 99.50 29.1 186.9 2.368 .379 1.59 5.82 .333 6242.7 6242.7 .0 99.50 33.3 188.8 2.663 .616 2.00 14.96 .353 5562.9 5562.9 .0 99.50 35.2 189.6 4.048 .667 2.19 16.12 .553 4902.2 4902.2 .0 99.50 37.2 190.6 3.818 .694 2.40 16.12 .549 4684.2 4684.2 .0 99.50 38.3 191.2 3.718 .703 2.50 16.12 .546 4579.7 4579.7 .0 99.50 44.3 194.8 3.360 .726 3.00 16.12 .530 4093.2 4093.2 .0 99.50 45.2 195.4 3.530 .727 3.08 16.12 .553 4511.9 3864.4 .0 96.42 46.2 196.1 2.828 .729 3.15 16.12 .410 1858.2 1183.4 .0 91.70 47.2 196.8 3.885 .733 3.23 16.00 .581 629.7 .0 .0 78.02 50.4 199.3 3.715 .737 3.50 15.54 .579 635.3 .0 .0 78.02 56.9 205.1 3.407 .741 4.00 14.78 .573 647.7 .0 .0 78.02 64.2 212.5 3.145 .743 4.52 14.17 .566 658.0 .0 .0 78.02 71.7 220.5 2.923 .745 5.00 13.75 .560 666.2 .0 .0 78.02 80.2 229.4 2.716 .747 5.51 13.47 .552 674.5 .0 .0 78.02 0 II 89.1 237.4 2.544 .749 6.00 13.38 .544 682.4 .0 .0 78.02 G) 0 0

0 0

N (J1 Chapter 14, Page 183 of 218 I Revision 20, 2006 (J1 0)

CD

IP2 FSAR UPDATE TABLE 14.3-27 (Sheet 2 of 2)

DOUBLE-ENDED PUMP SUCTION GUILLOTINE MAXSI PRINCIPLE PARAMETERS DURING REFLOOD FOR 3216 MWt Time Flooding Carryover Core Downcomer Flow Total Injection Spill Enthalpy Seconds Fraction Height Height Frac Accum Btu/Ibm (ft) (tt)

Temp Rate (Pounds Mass per Second) of in/sec 99.2 245.0 2.401 .751 6.52 13.46 .537 688.5 .0 .0 78.02 109.1 251.4 2.305 .754 7.00 13.67 .531 692.3 .0 .0 78.02 121.2 258.0 2.230 .757 7.56 14.04 .527 695.0 .0 .0 78.02 131.2 262.8 2.194 .761 8.00 14.41 .525 696.1 .0 .0 78.02 143.2 267.8 2.170 .765 8.52 14.90 .524 696.7 .0 .0 78.02 147.2 269.3 2.165 .767 8.69 15.06 .524 696.7 .0 .0 78.02 154.7 272.0 2.179 .770 9.00 15.37 .528 695.5 .0 .0 78.02 165.2 275.4 2.200 .773 9.44 15.70 .536 693.0 .0 .0 78.02 167.2 276.0 2.200 .774 9.52 15.74 .538 692.6 .0 .0 78.02 178.9 279.3 2.168 .778 10.00 15.95 .544 692.1 .0 .0 78.02 o

G) o o

o o

N Chapter 14, Page 184 of 218 1U'l Revision 20, 2006 U'l 0)

CD

IP2 FSAR UPDATE TABLE 14.3-28 (Sheet 1 of 5)

DOUBLE-ENDED HOT LEG GUILLOTINE BLOWDOWN MASS AND ENERGY RELEASES FOR 3216 Mwt TIME BREAK PA THNO.1* BREAK PATH NO.2**

FLOW ENERGY FLOW ENERGY SECONDS LBM/SEC THOUSAN LBM/SE THOUSANDS DS BTU/SEC BTU/SEC .00000 .0 .0 .0 .0

.00107 45431.7 28592.9 45428.6 28589.4

.00213 44959.4 28295.7 44682.5 28114.2

.102 45793.5 29109.1 25686.4 16129.1

.201 33239.6 21496.0 22659.2 14136.4

.301 32619.6 21083.9 20264.4 12470.7

.401 31885.0 20590.9 19026.0 11515.6

.502 31493.9 20329.6 18206.6 10840.9

.601 31480.4 20318.8 17625.0 10345.0

.701 31467.6 20326.8 17235.4 9988.6

.801 31177.0 20177.2 16891.0 9682.4

.902 30811.3 19992.6 16655.5 9455.9 1.00 30442.3 19816.4 16457.2 9266.0 1.10 30178.5 19718.7 16334.0 9128.3 1.20 29985.2 19679.7 16264.2 9030.1 1.30 29765.5 19624.5 16277.2 8984.8 1.40 29462.3 19513.9 16329.9 8966.8 1.50 29085.4 19347.4 16416.8 8972.9 1.60 28711.1 19176.2 16524.2 8994.9 1.70 28394.9 19041.5 16647.5 9030.0 1.80 28092.0 18914.9 16773.3 9071.1 1.90 27710.5 18731.3 16894.8 9114.1 2.00 27250.2 18485.7 17006.0 9155.3 2.10 26796.9 18239.2 17106.1 9193.9 2.20 26405.9 18037.0 17195.7 9229.7 2.30 26026.9 17844.1 17274.6 9262.1 2.40 25597.1 17606.7 17340.4 9289.5 2.50 25129.9 17331.2 17393.6 9311.9 2.60 24686.1 17068.7 17437.0 9330.3 2.70 24290.3 16839.1 17470.2 9344.3 2.80 23893.3 16603.8 17493.4 9353.7 2.90 23492.6 16354.8 17505.6 9358.0 3.00 23104.3 16107.1 17508.7 9357.8 3.10 22737.0 15867.2 17504.4 9354.2 3.20 22389.3 15634.4 17493.1 9347.1 3.30 22077.7 15422.8 17476.1 9337.2 3.40 21783.4 15217.4 17454.0 9324.9 3.50 21490.5 15003.4 17426.7 9310.0 3.60 21223.8 14801.9 17394.4 9292.6 3.70 20991.8 14622.4 17358.7 9273.7 Chapter 14, Page 185 of 218 Revision 20, 2006 OAG10000215_1540

IP2 FSAR UPDATE TABLE 14.3-28 (Sheet 2 of 5)

DOUBLE-ENDED HOT LEG GUILLOTINE BLOWDOWN MASS AND ENERGY RELEASES FOR 3216 Mwt TIME BREAK PA THNO.1* BREAK PATH NO.2**

FLOW ENERGY FLOW SECONDS LBM/SEC THOUSAN SECONDS LBM/SEC DS BTU/SEC 3.80 20770.1 14444.9 17319.3 9253.0 3.90 20560.5 14270.0 17275.4 9230.1 4.00 20383.2 14116.6 17227.8 9205.6 4.20 20059.6 13822.3 17120.7 9150.8 4.40 19813.2 13575.6 16995.4 9087.4 4.60 19604.3 13349.2 16852.0 9015.4 4.80 19455.3 13162.8 16689.9 8934.5 5.00 19357.0 13009.0 16509.6 8845.2 5.20 19365.9 12932.0 16313.3 8748.6 5.40 19406.3 12882.9 16099.0 8643.5 5.60 19468.9 12860.5 15867.0 8530.1 5.80 19556.2 12870.9 15615.7 8407.4 6.00 19707.4 12910.1 15356.3 8281.5 6.20 11028.8 8300.7 15067.3 8140.3 6.40 14455.2 10617.0 14672.0 7941.4 6.60 14508.9 10566.7 14237.6 7722.0 6.80 14629.0 10544.4 13845.1 7525.9 7.00 14807.5 10579.1 13465.1 7335.8 7.20 14990.4 10601.2 13051.2 7125.5 7.40 15147.5 10624.3 12651.4 6922.1 7.60 15324.6 10652.1 12283.8 6735.6 7.80 15406.3 10588.1 11920.3 6549.8 8.00 15644.1 10638.4 11545.0 6356.1 8.20 15556.0 10536.5 11181.0 6167.9 8.40 15808.7 10588.4 10841.7 5992.4 8.60 16038.3 10635.9 10516.7 5824.0 8.80 16243.1 10677.0 10199.7 5659.1 9.00 16434.6 10716.8 9899.8 5502.5 9.20 16619.4 10756.8 9613.9 5352.9 9.40 16808.2 10802.1 9342.8 5210.8 9.60 17018.1 10862.2 9081.5 5073.5 9.80 17302.6 10968.3 8833.8 4943.2 10.0 17347.4 10951.5 8587.4 4813.4 10.2 17122.8 10772.8 8345.5 4686.2 10.4 15365.1 9795.4 8104.7 4559.7 10.602 14402.9 9265.0 7870.3 4437.2 10.604 14399.0 9262.5 7866.6 4435.2 10.607 14396.3 9260.9 7864.2 4433.9 10.609 14394.2 9259.5 7862.2 4432.9 Chapter 14, Page 186 of 218 Revision 20, 2006 OAG10000215_1541

IP2 FSAR UPDATE TABLE 14.3-28 (Sheet 3 of 5)

DOUBLE-ENDED HOT LEG GUILLOTINE BLOWDOWN MASS AND ENERGY RELEASES FOR 3216 Mwt TIME BREAK PA THNO.1* BREAK PATH NO.2**

FLOW ENERGY FLOW SECONDS LBM/SEC THOUSAN SECONDS LBM/SEC DS BTU/SEC 10.8 14314.8 9194.1 7642.1 4318.4 11.0 14303.2 9168.8 7427.1 4207.3 11.2 14286.7 9144.1 7231.0 4106.7 11.4 14268.5 9117.2 7039.7 4008.3 11.6 14235.3 9078.9 6850.8 3911.2 11.8 14133.9 9001.0 6665.1 3816.0 12.0 13860.2 8831.1 6483.7 3723.3 12.2 13361.0 8543.6 6304.3 3632.2 12.4 12862.1 8261.1 6126.6 3542.6 12.6 12547.5 8079.7 5955.6 3457.0 12.8 12329.5 7951.6 5788.3 3373.8 13.0 12138.1 7840.4 5628.4 3294.8 13.2 11932.6 7723.9 5474.2 3219.1 13.4 11697.7 7593.9 5327.5 3147.3 13.6 11418.6 7442.6 5182.9 3076.7 13.8 11117.0 7281.9 5044.5 3009.5 14.0 10808.3 7119.7 4908.8 2944.0 14.2 10513.3 6967.5 4777.7 2881.1 14.4 10232.1 6825.1 4650.0 2820.0 14.6 9944.6 6681.6 4522.3 2759.0 14.8 9642.7 6534.6 4391.9 2696.5 15.0 9312.3 6377.9 4248.5 2627.8 15.2 8962.9 6217.0 4092.0 2554.0 15.4 8607.5 6059.7 3918.8 2473.7 15.6 8230.6 5898.9 3734.6 2389.4 15.8 7823.9 5728.2 3547.8 2303.4 16.0 7408.1 5558.9 3361.8 2216.0 16.2 7003.5 5399.7 3189.1 2131.5 16.4 6605.4 5247.9 3034.3 2052.1 16.6 6205.0 5096.2 2898.8 1978.6 16.8 5809.6 4945.4 2784.2 1913.1 17.0 5418.6 4794.4 2687.3 1855.1 17.2 5037.9 4645.9 2604.3 1803.6 17.4 4654.9 4468.2 2532.0 1757.9 17.6 4317.7 4214.3 2465.5 1715.5 17.8 4092.9 4020.9 2404.2 1676.5 18.0 3912.3 3859.9 2346.2 1640.3 18.2 3471.5 3595.3 2289.7 1606.7 18.4 3010.9 3305.0 2234.0 1575.2 Chapter 14, Page 187 of 218 Revision 20, 2006 OAG10000215_1542

IP2 FSAR UPDATE TABLE 14.3-28 (Sheet 4 of 5)

DOUBLE-ENDED HOT LEG GUILLOTINE BLOWDOWN MASS AND ENERGY RELEASES FOR 3216 Mwt TIME BREAK PA THNO.1* BREAK PATH NO.2**

FLOW ENERGY FLOW SECONDS LBM/SEC THOUSAN SECONDS LBM/SEC DS BTU/SEC 18.6 2713.6 3107.4 2178.1 1544.9 18.8 2476.1 2875.7 2123.0 1515.5 19.0 2277.1 2699.9 2073.9 1487.3 19.2 2102.0 2522.1 2025.1 1455.8 19.4 1987.8 2406.6 1972.2 1422.9 19.6 1858.1 2262.5 1904.6 1390.6 19.8 1732.1 2117.2 1821.2 1366.2 20.0 1620.5 1990.4 1718.2 1345.1 20.2 1508.6 1860.9 1595.9 1316.2 20.4 1405.8 1743.3 1474.1 1276.4 20.6 1309.4 1633.1 1369.7 1240.5 20.8 1222.1 1531.5 1267.3 1214.7 21.0 1146.3 1445.3 1143.8 1196.4 21.2 1074.3 1361.7 1014.4 1163.9 21.4 1011.3 1284.7 856.4 1034.6 21.6 959.8 1221.2 744.5 912.0 21.8 916.3 1166.8 642.3 790.3 22.0 877.2 1117.9 575.6 710.2 22.2 825.8 1053.1 520.8 643.3 22.4 774.8 989.3 442.9 548.5 22.6 726.6 929.0 403.6 500.8 22.8 654.6 838.1 374.4 464.9 23.0 611.8 785.3 360.8 448.2 23.2 580.1 746.3 343.4 427.4 23.4 545.2 702.3 325.1 404.9 23.6 504.4 650.4 317.1 395.2 23.8 509.9 654.9 295.6 368.6 24.0 522.0 673.2 269.9 337.2 24.2 514.7 663.5 275.4 344.2 24.4 509.9 657.6 278.5 348.3 24.6 504.6 650.7 274.1 342.8 24.8 493.8 636.8 256.7 321.2 25.0 484.3 624.5 254.1 318.3 25.2 474.5 611.6 241.9 303.2 25.4 470.6 606.4 238.5 299.0 25.6 462.9 596.3 227.1 285.0 25.8 450.9 580.8 189.6 238.2 26.0 423.4 545.3 167.1 210.4 Chapter 14, Page 188 of 218 Revision 20, 2006 OAG10000215_1543

IP2 FSAR UPDATE TABLE 14.3-28 (Sheet 5 of 5)

DOUBLE-ENDED HOT LEG GUILLOTINE BLOWDOWN MASS AND ENERGY RELEASES FOR 3216 Mwt TIME BREAK PA THNO.1* BREAK PATH NO.2**

FLOW ENERGY FLOW SECONDS LBM/SEC THOUSAN SECONDS LBM/SEC DS BTU/SEC 26.2 388.3 500.6 178.8 225.3 26.4 381.0 487.6 153.7 193.7 26.6 407.2 521.4 136.6 172.6 26.8 395.8 499.9 156.5 197.7 27.0 430.6 530.6 174.5 220.1 27.2 408.0 513.6 186.8 235.5 27.4 450.7 557.4 175.5 221.5 27.6 432.8 543.9 200.1 252.3 27.8 436.3 542.5 181.9 229.3 28.0 513.0 630.5 183.0 230.9 28.2 537.6 661.0 216.2 272.5 28.4 552.1 677.6 224.9 283.2 28.6 492.9 615.3 203.0 256.0 28.8 316.7 407.5 201.8 254.4 29.0 89.2 116.7 60.2 76.2 29.2 .0 .0 .0 .0 D

mass and energy exiting from the reactor vessel side of the break

- mass and energy exiting from the SG side of the break Chapter 14, Page 189 of 218 Revision 20, 2006 OAG10000215_1544

IP2 FSAR UPDATE TABLE 14.3-29 DOUBLE-ENDED HOT LEG GUILLOTINE MASS BALANCE FOR 3216 MWt Time (Seconds) .00 29.20 29.20+8 Mass (Thousand Ibm)

Initial In RCS and ACC 731.97 731.97 731.97 Added Mass Pumped Injection .00 .00 .00 Total Added .00 .00 .00 TOTAL AVAILABLE 731.97 731.97 731.97 Distribution Reactor Coolant 524.25 96.33 123.07 Accumulator 207.72 129.91 103.17 Total Contents 731.97 226.24 226.24 Effluent Break Flow .00 505.71 505.71 ECCS Spill .00 .00 .00 Total Effluent .00 505.71 505.71 TOTAL ACCOUNTABLE 731.97 731.95 731.95 Chapter 14, Page 190 of 218 Revision 20, 2006 OAG10000215_1545

IP2 FSAR UPDATE TABLE 14.3-30 DOUBLE-ENDED HOT LEG GUILLOTINE ENERGY BALANCE FOR 3216 MWt Time (Seconds) .00 29.20 29.20+8 Energy (Million Btu)

Initial Energy In RCS, ACC, Steam Gen 784.57 784.57 784.57 Added Energy Pumped Injection .00 .00 .00 Decay Heat .00 8.37 8.37 Heat From Secondary .00 -.23 -.23 Total Added .00 8.14 8.14 TOTAL AVAILABLE 784.57 792.72 792.72 Distribution Reactor Coolant 305.58 22.91 25.57 Accumulator 20.67 12.93 10.27 Core Stored 27.00 10.30 10.30 Primary Metal 166.68 155.81 155.81 Secondary Metal 40.99 40.76 40.76 Steam Generator 223.66 222.24 222.24 Total Contents 784.57 464.94 464.94 Effluent Break Flow .00 327.28 327.28 ECCS Spill .00 .00 .00 Total Effluent .00 327.28 327.28 TOTAL ACCOUNTABLE 784.57 792.23 792.23 Chapter 14, Page 191 of 218 Revision 20, 2006 OAG10000215_1546

IP2 FSAR UPDATE TABLE 14.3-31 DOUBLE-ENDED PUMP SUCTION GUILLOTINE MIN SI SEQUENCE OF EVENTS FOR 3216 MWt Time (sec) Event Description 0.0 Break occurs, reactor trip and LOOP power are assumed 0.604 Reactor trip on pressurizer low pressure of 1860 psia 1.75 Containment HI-1 pressure setpoint reached 4.1 Low pressurizer pressure SI setpoint @ 1695 psia reached (SI begins coincident with low pressurizer pressure SI setpoint) 7.75 Main Feedwater Flow Control Valve closed 11.43 Containment HI-3 pressure setpoint reached 13.9 Broken-loop accumulator begins injecting water 14.2 Intact-loop accumulator begins injecting water 26.40 End-of-blowdown phase 45.806 Broken-loop accumulator water injection ends 46.256 Intact-loop accumulator water injection ends 49.1 SI begins 61.75 Reactor containment air recirculation fan coolers actuate 71.48 Containment spray pump(s) (RWST) start 239.706 End-of-reflood for MIN SI Case 1264.1 Peak pressure and temperature occur 1500.46 RHR/HHSI alignment for recirculation 2354 Containment spray is terminated due to RWST LO-LO signal 23400 Hot leg recirculation 1.0x107 Transient modeling terminated Chapter 14, Page 192 of 218 Revision 20, 2006 OAG10000215_1547

IP2 FSAR UPDATE TABLE 14.3-32 DOUBLE-ENDED PUMP GUILLOTINE MAX SI SEQUENCE OF EVENTS FOR 3216 MWt Time (sec) Event Description 0.0 Break Occurs, and Loss of Offsite Power are assumed 1.75 Containment HI-1 Pressure Setpoint Reached 4.1 Low Pressurizer Pressure SI Setpoint - 1695 psia reached in blowdown 11.32 Containment HI-3 Pressure Setpoint Reached 14.0 Broken Loop Accumulator Begins Injecting Water 14.3 Intact Loop Accumulator Begins Injecting Water 26.0 End of Blowdown Phase 45.0 Safety Injection Begins 45.6 Broken Loop Accumulator Water Injection Ends 46.15 Intact Loop Accumulator Water Injection Ends 61.75 Reactor Containment Air Recirculation Fan Coolers Actuate 71.32 Containment Spray Pump(s) (RWST) start 178.9 End of Reflood Phase 319.0 Peak Pressure and Temperature Occur 1085. Cold Leg Recirculation Begins 1536. Containment Spray is terminated due to RWST LO-LO Signal 23400. Hot Leg Recirculation Begins 1.0E+07 Transient Modeling Terminated Chapter 14, Page 193 of 218 Revision 20, 2006 OAG10000215_1548

IP2 FSAR UPDATE TABLE 14.3-33 DOUBLE-ENDED HOT LEG GUILLOTINE SEQUENCE OF EVENTS FOR 3216 MWt Time (sec) Event Description 0.0 Break Occurs, and Loss of Offsite Power are assumed 1.86 Containment HI-1 Pressure Setpoint Reached 3.8 Low Pressurizer Pressure SI Setpoint - 1695 psia reached in blowdown 9.87 Containment HI-3 Pressure Setpoint Reached 14.0 Broken Loop Accumulator Begins Injecting Water 14.2 Intact Loop Accumulator Begins Injecting Water 23.5 Peak Pressure and Temperature Occur 29.2 End of Blowdown Phase and Transient Modeling Terminated TABLE 14.3-34 CONTAINMENT PEAK PRESSURE AND TEMPERATURE FOR 3216 MWt Peak Press. Peak Steam Pressure Steam (psig) Temp. (psig) Temperature Case (OF) @ 24 hours2.777778e-4 days 0.00667 hours 3.968254e-5 weeks 9.132e-6 months (OF)

@ 24 hours2.777778e-4 days 0.00667 hours 3.968254e-5 weeks 9.132e-6 months Double-Ended 45.71 @ 266.81 @ 17.05 @ 204.97@

Pump Suction 1264.1 sec 1264.1 sec 24 hrs 24 hrs Min SI Double-Ended 39.67@ 257.596 @ 21.38 @ 216.192@

Pump Suction 319 sec 319 sec 24 hrs 24 hrs MaxSI Double-Ended 40.62 @ 259.98@ NA NA Hot Leg 23.50 sec 23.49 sec Chapter 14, Page 194 of 218 Revision 20, 2006 OAG10000215_1549

IP2 FSAR UPDATE TABLE 14.3-35 CONTAINMENT HEAT SINKS NO. MATERIAL HEAT TRANSFER AREA THICKNESS (FT2) IN

1. Carbon Steel 41530 0.375 Concrete 54.0

2. Carbon Steel 26012 0.5 Concrete 42.0

3. Concrete 13636 12.0

4. Concrete 55454 12.0

5. Stainless Steel 9091 0.375 Concrete 12.0

6. Carbon Steel 62538 0.5

7. Carbon Steel 74276 0.375

8. Carbon Steel 25407 0.25

9. Carbon Steel 63454 0.1875

10. Carbon Steel 2727 0.125

11. Carbon Steel 20000 0.138

12. Carbon Steel 9090 0.0625

13. Stainless Steel 714 0.019 PVC Insulation 1.25 Carbon Steel 0.75 Concrete 54.0 Chapter 14, Page 195 of 218 Revision 20, 2006 OAG10000215_1550

IP2 FSAR UPDATE TABLE 14.3-35 (CONT.)

CONTAINMENT HEAT SINKS NO. MATERIAL HEAT TRANSFER AREA THICKNESS (FT2) IN

14. Stainless Steel 6226 0.019 PVC Insulation 1.25 Carbon Steel 0.5 Concrete 54.0

15. Stainless Steel 3469 0.025 Foam Insulation 1.5 Carbon Steel 0.5 Concrete 54.0

16. Stainless Steel 3965 0.025 Foam Insulation 1.5 Carbon Steel 0.375 Concrete 54.0 Note:

1. All carbon steel exterior surfaces are modeled with 0.00033-ft layer of paint on top of a 0.000258-ft layer of carbozinc primer.

2. Approximately 25-fF of the PVC insulation was replaced with fiberglass. As described in Section 14.3.5.1.1, modeling the PVC insulation, instead of the fiberglass insulation was determined to be conservative and bounding.

3. Approximately 7100-fF of the liner top coat material (Phenoline 305) was replaced with Carboline 890. As described in Section 14.3.5.1.1, modeling the Phenoline 305 top coat material, instead of the Carboline 890 top coat material was determined to be conservative and boundin 4.

Chapter 14, Page 196 of 218 Revision 20, 2006 OAG10000215_1551

IP2 FSAR UPDATE TABLE 14.3-36 THERMOPHYSICAL PROPERTIES OF CONTAINMENT HEAT SINKS Material Thermal Conductivity Volumetric Heat (Btu/hr-ft - OF) Capacity

{Btu/fe - OF}

Paint layer 1, Phenoline 0.08 28.8 Paint layer 2, Carbozinc 0.9 28.8 Carbon Steel 26.0 56.35 Stainless Steel 8.6 56.35 Concrete 0.8 28.8 PVC Insulation 0.0208 1.20 Foam Insulation 0.0417 1.53 Chapter 14, Page 197 of 218 Revision 20, 2006 OAG10000215_1552

IP2 FSAR UPDATE TABLE 14.3-37 LOCA CONTAINMENT RESPONSE ANALYSIS PARAMETERS Service water temperature (OF) 95 RWST water temperature (OF) 110 Initial containment temperature (OF) 130 Initial containment pressure (psia) 16.7 Initial relative humidity (%) 20 Net free volume (fe) 2.61x 106 Reactor Containment Air Recirculation Fan Coolers Total 5 Analysis maximum 4 Analysis minimum 3 Containment Hi-1 setpoint (psig) 10.0 Delay time (sec)

With Offsite Power NA Without Offsite Power 60.0 Containment Spray Pumps Total 2 Analysis maximum 1 Analysis minimum 1 Flowrate (gpm)

Injection phase (per pump)- see Table 14.3-40 2180 Recirculation phase (total) o Containment Hi-3 setpoint (psig) 30.

Delay time (sec)

With Offsite Power (delay after High High setpoint) NA Without Offsite Power (total time from t=O) 60.0 ECCS Recirculation Switch over, sec Minimum Safeguards 1500.

Maximum Safeguards 1085.

Containment Spray Termination on LO-LO RWST Level, (sec)

Minimum Safeguards 2345.

Maximum Safeguards 1536.

Chapter 14, Page 198 of 218 Revision 20, 2006 OAG10000215_1553

IP2 FSAR UPDATE TABLE 14.3-37 (CONT.)

LOCA CONTAINMENT RESPONSE ANALYSIS PARAMETERS Emergency Core Cooling System (ECCS) Flows (GPM)

Minimum ECCS Injection alignment 2871.2 Recirculation alignment 1864.0 Maximum ECCS Injection alignment 5394.5 Recirculation alignment 6320.5 Residual Heat Removal System RHR Heat Exchangers Modeled in analysis

1 Recirculation switchover time, sec Minimum Safeguard 1500.

1085.

Maximum Safeguard UA , 106

BTU/hr-OF 0.767 Flows - Tube Side and Shell Side - gpm Minimum Safeguard 4936.

Maximum Safeguard 9871.

Component Cooling Water Heat Exchangers Modeled in analysis 2 6

UA , 10

BTU/hr-OF 2.40 Flows - Shell Side and Tube Side - gpm Shellside

4936.

Tubeside *

(service water) 5000.

Additional heat loads, (BTU/hr) 19.675x106

Minimum safeguard data representing 1 EDG Chapter 14, Page 199 of 218 Revision 20, 2006 OAG10000215_1554

IP2 FSAR UPDATE TABLE 14.3-38 SAFETY INJECTION FLOW MINIMUM SAFEGUARDS Res Pressure Total Flow (psia) (gpm)

INJECTION MODE (Reflood Phase) 14.7 3250.0 34.7 3097.8 54.7 2932.7 61.7 2871.2 74.7 2753.6 94.7 2558.3 114.7 2330.3 214.7. 872.1 INJECTION MODE (Post-Reflood Phase) 61.7 2871.2 COLD LEG RECIRCULATION MODE 61.7 1864.0 HOT LEG RECIRCULATION MODE 61.7 822.0 Chapter 14, Page 200 of 218 Revision 20, 2006 OAG10000215_1555

IP2 FSAR UPDATE TABLE 14.3-39 SAFETY INJECTION FLOW MAXIMUM SAFEGUARDS Res Pressure Total Flow (psia) (gpm)

INJECTION MODE (Reflood Phase) 14.7 6320.50 34.7 5996.18 54.7 5652.86 74.7 5283.84 94.7 4862.22 114.7 4389.80 174.7 1865.02 214.7 1651.00 INJECTION MODE (Post-Reflood Phase) 61.7 5523.7 COLD LEG RECIRCULATION MODE 61.7 6320.5 HOT LEG RECIRCULATION MODE 61.7 6320.5 TABLE 14.3-40 CONTAINMENT SPRAY PERFORMANCE Containment Pressure (psig) with 1 Pump(gpm) 0-47 2180 Containment Pressure (psig) with 2 Pumps(gpm) 0-47 4200 Chapter 14, Page 201 of 218 Revision 20, 2006 OAG10000215_1556

IP2 FSAR UPDATE TABLE 14.3-41 DELETED TABLE 14.3-42 DELETED Chapter 14, Page 202 of 218 Revision 20, 2006 OAG10000215_1557

IP2 FSAR UPDATE TABLE 14.3-43 Core Fission Product Inventory Inventory Inventory Nuclide (Ci) Nuclide (Ci) 1-130 3.S0E+06 Ru-106 4.S9E+07 1-131 9.16E+07 Rh-105 S.S6E+07 1-132 1.33E+OS Mo-99 1.75E+OS 1-133 1.SSE+OS Tc-99M 1.53E+OS 1-134 2.06E+OS 1-135 1.75E+OS Ce-141 1.52E+OS Ce-143 1.42E+OS Kr-S5M 2.43E+07 Ce-144 1.20E+OS Kr-S5 1.10E+06 Pu-23S 4.13E+05 Kr-S7 4.66E+07 Pu-239 3.50E+04 Kr-SS 6.56E+07 Pu-240 5.23E+04 Xe-131M 1.01E+06 Pu-241 1.1SE+07 Xe-133M 5.S7E+06 Np-239 1.SSE+09 Xe-133 1.S0E+OS Xe-135M 3.6SE+07 Y-90 9.11 E+06 Xe-135 4.77E+07 Y-91 1.14E+OS Xe-13S 1.55E+OS Y-92 1.20E+OS Y-93 1.39E+OS Cs-134 2.06E+07 Nb-95 1.56E+OS Cs-136 6.01E+06 Zr-95 1.54E+OS Cs-137 1.19E+07 Zr-97 1.55E+OS Cs-13S 1.71E+OS La-140 1.73E+OS Rb-S6 2.3SE+05 La-141 1.53E+OS La-142 1.4SE+OS Te-127 9.S4E+06 Nd-147 6.11E+07 Te-127M 1.29E+06 Pr-143 1.37E+OS Te-129 2.92E+07 Am-241 1.41 E+04 Te-129M 4.30E+06 Cm-242 3.52E+06 Te-131M 1.33E+07 Cm-244 3.S2E+05 Te-132 1.31E+OS Sb-127 9.95E+06 Sb-129 2.97E+07 Sr-S9 S.S3E+07 Sr-90 S.75E+06 Sr-91 1.11 E+OS Sr-92 1.20E+OS Ba-139 1.67E+OS Ba-140 1.61 E+OS Ru-103 1.40E+OS Ru-105 9.62E+07 Chapter 14, Page 203 of 21S Revision 20, 2006 OAG10000215_155S

IP2 FSAR UPDATE TABLE 14.3-43a Core Fission Product Release Fractions Ga~ Release (1) Early In-Vessel (2)

Noble gases 0.05 0.95 Halogens 0.05 0.35 Alkali Metals 0.05 0.25 Tellurium group 0 0.05 Barium, Strontium 0 0.02 Noble Metals 0 0.0025 (Ruthenium group)

Cerium group 0 0.0005 Lanthanides 0 0.0002 Note:

(1) Release is initiated at 30 seconds and is terminated at 0.5 hours5.787037e-5 days 0.00139 hours 8.267196e-6 weeks 1.9025e-6 months .

(2) Released over a 1.3 hour3.472222e-5 days 8.333333e-4 hours 4.960317e-6 weeks 1.1415e-6 months period starting at the end of the gap release phase.

TABLE 14.3-44

{DELETEDl Chapter 14, Page 204 of 218 Revision 20, 2006 OAG10000215_1559

IP2 FSAR UPDATE TABLE 14.3-45 Data Used in Evaluating Offsite Doses (Isotope Dependent Data)

COMMITTED EFFECTIVE DOSE EQUIVALENT DOSE CONVERSION FACTORS Isotope DCF (rem/curie) Isotope DCF (rem/curie) 1-130 2.64E3 Cs-138 1.01E2 1-131 3.29E4 Cs-134 4.63E4 1-132 3.81 E2 Cs-136 7.33E3 1-133 5.85E3 Cs-137 3.19E4 1-134 1.31 E2 Rb-86 6.62E3 1-135 1.23E3 Ru-103 8.95E3 Kr-85m N/A Ru-105 4.55E2 Kr-85 N/A Ru-106 4.77E5 Kr-87 N/A Rh-105 9.55E2 Kr-88 N/A Mo-99 3.96E3 Xe-131m N/A Tc-99m 3.26E1 Xe-133m N/A Xe-133 N/A Y-90 8.44E3 Xe-135m N/A Y-91 4.89E4 Xe-135 N/A Y-92 7.81E2 Xe-138 N/A Y-93 2.15E3 Nb-95 5.81 E3 Te-127 3.18E2 Zr-95 2.36E4 Te-127m 2.15E4 Zr-97 4.33E3 Te-129m 2.39E4 La-140 4.85E3 Te-129 8.95E1 La-141 5.81 E2 Te-131m 6.4E3 La-142 2.53E2 Te-132 9.44E3 Nd-147 6.85E3 Sb-127 6.03E3 Pr-143 8.10E4 Sb-129 6.44E2 Am-241 4.44E8 Cm-242 1.73E7 Ce-141 8.95E3 Cm-244 2.48E8 Ce-143 3.39E3 Ce-144 3.74E5 Sr-89 4.14E4 Pu-238 3.92E8 Sr-90 1.3E6 Pu-239 4.29E8 Sr-91 1.66E3 Pu-240 4.29E8 Sr-92 8.07E2 Pu-241 8.25E6 Ba-139 1.7E2 Np-239 2.51E3 Ba-140 3.74E3 Chapter 14, Page 205 of 218 Revision 20, 2006 OAG10000215_1560

IP2 FSAR UPDATE TABLE 14.3-45 (Cont.)

Data Used in Evaluating Offsite Doses (Isotope Dependent Data)

EFFECTIVE DOSE EQUIVALENT DOSE CONVERSION FACTORS DCF DCF Nuclide (rem-m 3/Ci-sec) Nuclide (rem-m 3/Ci-sec) 1-130 3.848E-01 Cs-134 2.801 E-01 1-131 6.734E-02 Cs-136 3.922E-01 1-132 4.144E-01 Cs-137(1) 1.066E-01 1-133 1.088E-01 Cs-138 4.477E-01 1-134 4.810E-01 Rb-86 1.780E-02 1-135 2.953E-01 Ru-103 8.325E-02 Kr-85m 2.768E-02 Ru-105 1.410E-01 Kr-85 4.403E-04 Ru-106 O.OOE+OO Kr-87 1.524E-01 Rh-105 1.376E-02 Kr-88 3.774E-01 Mo-99 2.694E-02 Xe-131m 1.439E-03 Tc-99m 2.179E-02 Xe-133m 5.069E-03 Xe-133 5.772E-03 Y-90 7.030E-04 Xe-135m 7.548E-02 Y-91 9.620E-04 Xe-135 4.403E-02 Y-92 4.810E-02 Xe-138 2.135E-01 Y-93 1.776E-02 Nb-95 1.384E-01 Te-127 8.954E-04 Zr-95 1.332E-01 Te-127m 5.439E-04 Zr-97 3.337E-02 Te-129m 5.735E-03 La-140 4.329E-01 Te-129 1.018E-02 La-141 8.843E-03 Te-131m 2.594E-01 La-142 5.328E-01 Te-132 3.811 E-02 Nd-147 2.290E-02 Sb-127 1.232E-01 Pr-143 7.770E-05 Sb-129 2.642E-01 Am-241 3.027E-03 Cm-242 2. 105E-05 Ce-141 1.269E-02 Cm-244 1.817E-05 Ce-143 4.773E-02 Ce-144 3.156E-03 Sr-89 2.860E-04 Pu-238 1.806E-05 Sr-90 2.786E-05 Pu-239 1.569E-05 Sr-91 1.277E-01 Pu-240 1.758E-05 Sr-92 2.512E-01 Pu-241 2.683E-07 Ba-139 8.029E-03 Np-239 2.845E-02 Ba-140 3.175E-02 Note:

1. Decay of Cs-137 does not result in gamma radiation. The EDE DCF listed for Cs-137 is actually the value associated with the decay of the short-lived daughter product Ba-137m.

Chapter 14, Page 206 of 218 Revision 20, 2006 OAG10000215_1561

IP2 FSAR UPDATE TABLE 14.3-46 Input Values for Doses Atmospheric Dilution Time Period x/Q (S20m) x/Q (1100m)

!hrl (sec/m3) (sec/m3) 0-8 7.5 X 10-4 3.5 X 10-4 8-24 1.2x 10-4 24-96 4.2 x 10-5 96-720 9.3 X 10-6 Containment Leakage Time Period (hr) Leak Rate (percent/day) 0-24 0.1 24-720 0.05 Breathing Rate Offsite Time Period (hr) Breathing Rate (m 3/sec) 0-8 3.5 x 10-4 8-24 1.8 X 10-4 24-720 2.3 X 10-4 TABLE 14.3-47 DELETED TABLE 14.3-48 DELETED Chapter 14, Page 207 of 218 Revision 20, 2006 OAG10000215_1562

IP2 FSAR UPDATE TABLE 14.3-49 ASSUMPTIONS USED FOR LARGE LOCA DOSE ANALYSIS Iodine Chemical Species Elemental 4.85%

Methyl 0.15%

Particulate 95%

Iodine Removal in Containment Containment Spray Spray Start Delay 60 sec Injection spray flowrate 2135 gpm Injection spray duration 37.8 min Recirculation spray flowrate 1080 gpm Recirculation spray duration Note 1 Iodine removal coefficient Elemental, As during spray injection 20.0/hr OF < 200 during spray recirculation 5.0/hr OF < 200 Particulate Ap during spray injection 4.4/hr OF ~ 50 during spray recirculation 2.25/hr OF ~ 50 Sedimentation Particulate Removal 0.1/hr OF < 1000 (Note 2)

Fan Cooler Units Containment Filters Start Delay Time 60 sec Number of Units 3 Flow Rate per Unit 64,500 cfm Containment Free Volume Containment Leak Rate 0-24 hr 0.10%/day

> 24 hr 0.05%/day Notes:

1. Total spray duration assumed is 3.4 hours4.62963e-5 days 0.00111 hours 6.613757e-6 weeks 1.522e-6 months following the initiation of the event.

2. Credit for sedimentation removal is limited to the unsprayed portion of the containment until sprays are terminated (at 3.4 hours4.62963e-5 days 0.00111 hours 6.613757e-6 weeks 1.522e-6 months ).

Chapter 14, Page 208 of 218 Revision 20, 2006 OAG10000215_1563

IP2 FSAR UPDATE TABLE 14.3-49a DELETED TABLE 14.3-50 ASSUMPTIONS USED FOR ANALYSIS OF CONTROL ROOM DOSES Volume 102,400-fe Unfiltered Inleakage 700 cfm Filtered Makeup 1800 cfm Filtered Recirculation o cfm Filter Efficiency Elemental 95%

Organic 90%

Particulate 99%

Breathing Rate Atmospheric Dispersion Factors See Table 14.3-51 Occupancy Factors 0-1 day 1.0 1-4 days 0.6 4-30 days 0.4 Chapter 14, Page 209 of 218 Revision 20, 2006 OAG10000215_1564

IP2 FSAR UPDATE TABLE 14.3-51 ATMOSPHERIC DISPERSION FACTORS USED FOR ANALYSIS OF CONTROL ROOM DOSES Atmospheric Dispersion Factors Release Point (sec/m 3 )

Containment Surface Leak (1) 0-2 hr 3.82x 10-4 2-8 hr 2.81 x 10-4 8-24 hr 1.05 X 10-4 24-96 hr 8.31 X 10-5 96-720 hr 7.04 X 10-5 Side of the Auxiliary Boiler Feedwater Building (2) 0-2 hr 1.09 X 10-3 2-8 hr 1.02 X 10-3 8-24 hr 4.99 X 10-4 24-96 hr 3.86 X 10-4 96-720 hr 2.99 X 10-4 Vent Stacks on the Roof of the Auxiliary Boiler Feedwater Building (3) 0-2 hr 9.49 X 10-4 2-8 hr 8.65x 10-4 8-24 hr 4.17 x 10-4 24-96 hr 3.30x 10-4 96-720 hr 2.54 x 10-4 Containment Vent (4) 0-2 hr 6.44 X 10-4 2-8 hr 4.69 X 10-4 8-24 hr 1.72 X 10-4 24-96 hr 1.37 X 10-4 96-720 hr 1.17 X 10-4 Notes:

1. Used for Containment Leakage Releases in Rod Ejection (14.2.6.9), Large Break LOCA (14.3.6.5) and Small Break LOCA (14.3.6.7).

2. Used for Steamline Break (14.2.5.7).

3. Used for Locked Rotor (14.1.6.5.3) and Steam Generator Tube Rupture (14.2.4) and Secondary Side Releases for Rod Ejection (14.2.6.9) and Small Break LOCA (14.3.6.7).

4. Used for Fuel Handling Accident (14.2.1.1) and Large Break LOCA ECCS Recirculation Leakage (14.3.6.6).

Chapter 14, Page 210 of 218 Revision 20, 2006 OAG10000215_1565

IP2 FSAR UPDATE TABLE 14.3-52 CALCULATED CONTROL ROOM DOSES TEDE Event Dose (rem)

Large Break LOCA Containment Leakage 3.5 Direct Dose from Activity in Containment 0.02 ECCS Recirculation Leakage With Boundary Layer Effects 0.14 ECCS Recirculation Leakage Without Boundary Layer Effects 1.36 Total With Boundary Layer Effects 3.68 Total Without Boundary Layer Effects 4.90 Small Break LOCA 3.5 Locked Rotor 0.65 Rod Ejection 1.4 Fuel Handling Accident 3.0 Steamline Break Pre-Existing Iodine Spike 0.18 Accident-Initiated Iodine Spike 0.52 Steam Generator Tube Rupture Pre-Existing Iodine Spike 1.4 Accident-Initiated Iodine Spike 0.48 Volume Control Tank Rupture 0.12 Holdup Tank Rupture 0.06 Gas Decay Tank Rupture 0.05 Chapter 14, Page 211 of 218 Revision 20, 2006 OAG10000215_1566

IP2 FSAR UPDATE 14.3 FIGURES Chapter 14, Page 212 of 218 Revision 20, 2006 OAG10000215_1567

IP2 FSAR UPDATE Chapter 14, Page 213 of 218 Revision 20, 2006 OAG10000215_1568

IP2 FSAR UPDATE Figure 14.3-104a Deleted Figure 14.3-104b Deleted Figure 14.3-104c Deleted Figure 14.3-104d Deleted Figure 14.3-104e Deleted Figure 14.3-104f Deleted Figure 14.3-104g Deleted Figure 14.3-104h Deleted Figure 14.3-104i Deleted Figure 14.3-104j Deleted Figure 14.3-104K Deleted Figure 14.3-105 Double-Ended Pump Suction Break for 3216 MWt Minimum Safeguards Integrated Wall Heat Removal Figure 14.3-106 Double-Ended Pump Suction Break for 3216 MWt Minimum Safeguards Integrated Fan Cooler Heat Removal Figure 14.3-107 Double-Ended Pump Suction Break for 3216 MWt Minimum Safeguards Integrated Spray Heat Removal Figure 14.3-108 Double-Ended Pump Suction Break for 3216 MWt Minimum Safeguards Structural Heat Transfer Coefficient Figure 14.3-109 Double-Ended Pump Suction Break for 3216 MWt Minimum Safeguards Containment Pressure Figure 14.3-110 Double-Ended Pump Suction Break for 3216 MWt Minimum Safeguards Containment Temperature Figure 14.3-111 Double-Ended Pump Suction Break for 3216 MWt Maximum Safeguards Containment Pressure Figure 14.3-112 Double-Ended Pump Suction Break for 3216 MWt Maximum Safeguards Containment Temperature Figure 14.3-113 Double-Ended Hot Leg Break for 3216 MWt Containment Pressure Figure 14.3-114 Double-Ended Hot Leg Break for 3216 MWt Containment Temperature Figure 14.3-115 Fan Cooler Heat Removal as a Function of Containment Temperature 95°F Service Water, 1600 GPM SW Flow Figure 14.3-116 Deleted Figure 14.3-117 Deleted Figure 14.3-118 Deleted Figure 14.3-119 Deleted Figure 14.3-120 Deleted Figure 14.3-121 Deleted Figure 14.3-122 Deleted Figure 14.3-123 Deleted Figure 14.3-124 Deleted Figure 14.3-125 Deleted Figure 14.3-126 Deleted Figure 14.3-127 Deleted FIGURE 14.3-128 Deleted FIGURE 14.3-129 Radiation Levels Surrounding 14-ln. Residual Heat Removal Pipe (FIGURE RETAINED FOR HISTORICAL PURPOSES)

Chapter 14, Page 214 of 218 Revision 20, 2006 OAG10000215_1569

IP2 FSAR UPDATE 14.4 ANTICIPATED TRANSIENTS WITHOUT SCRAM An anticipated transient without scram (ATWS) is an anticipated operational occurrence (such as loss of feedwater, loss of load, or loss of offsite power) that is assumed to be accompanied by a failure of the reactor trip system to shut down the reactor. As presented in Reference 1, the reactor is adequately protected against anticipated plant transients by the reactor protection system in the Westinghouse design, which is both redundant and diverse. As a result, failure to trip was not considered a credible event and the effects of ATWS were not considered part of the design basis for transients analyzed for Westinghouse plants. Nevertheless, in response to an AEC request for further information at the time of Indian Point Unit 2 initial licensing, the hypothetical effects of anticipated transients with no credit taken for reactor trip were provided in Supplement 6 to the original Indian Point Unit 2 FSAR. Those assessments were historical and were superseded by a later series of generic studies on ATWS (References 2 & 3) that showed acceptable consequences would result for Westinghouse designed plants provided that the turbine trips and auxiliary feedwater flow is initiated in a timely manner. The final USNRC ATWS Rule (Reference 4) requires that all US Westinghouse-designed plants install ATWS Mitigation System Actuation Circuitry (AM SAC) to initiate a turbine trip and actuate auxiliary feedwater independent of the reactor trip system. The Indian Point Unit 2 AMSAC is described in Section 7.10.

REFERENCES FOR SECTION 14.4

1. T. W. T. Burnett, et aI., Reactor Protection System Diversity in W PWRs, WCAP-7306, Westinghouse Electric Corporation, April 1969.

2. Burnett, T.W.T, et aI., "Westinghouse Anticipated Transients Without Trip Analysis," WCAP-8330, August 1974.

3. Letter from T.M. Anderson (Westinghouse) to S.H. Hanauer (USNRC), "ATWS Submittal," NS-TMA-2182, December 1979.

4. ATWS Final Rule, Code of Federal Regulations 10 CFR 50.62, "Requirements for Reduction of Risk from Anticipated Transients Without Scram (ATWS) Events for Light-Water-Cooled Nuclear Power Plants.

TABLE 14.4-1 DELETED TABLE 14.4-2 DELETED TABLE 14.4-3 DELETED TABLE 14.4-4 DELETED TABLE 14.4-5 DELETED Chapter 14, Page 215 of 218 Revision 20, 2006 OAG10000215_1570

IP2 FSAR UPDATE TABLE 14.4-6 DELETED TABLE 14.4-7 DELETED TABLE 14.4-8 DELETED Chapter 14, Page 216 of 218 Revision 20, 2006 OAG10000215_1571

IP2 FSAR UPDATE 14.4 FIGURES Figure No. Title Figure 14.4-1 Deleted Figure 14.4-2 Deleted Figure 14.4-3 Deleted Figure 14.4-4 Deleted Figure 14.4-5 Deleted Figure 14.4-6 Deleted Figure 14.4-7 Deleted Figure 14.4-8 Deleted Figure 14.4-9 Deleted Figure 14.4-10 Deleted Figure 14.4-11 Deleted Figure 14.4-12 Deleted Figure 14.4-13 Deleted Figure 14.4-14 Deleted Figure 14.4-15 Deleted Figure 14.4-16 Deleted Figure 14.4-17 Deleted Figure 14.4-18 Deleted Figure 14.4-19 Deleted Figure 14.4-20 Deleted Figure 14.4-21 Deleted Figure 14.4-22 Deleted Figure 14.4-23 Deleted Figure 14.4-24 Deleted Figure 14.4-25 Deleted Figure 14.4-26 Deleted Figure 14.4-27 Deleted Figure 14.4-28 Deleted Figure 14.4-29 Deleted Figure 14.4-30 Deleted Figure 14.4-31 Deleted Figure 14.4-32 Deleted Figure 14.4-33 Deleted Figure 14.4-34 Deleted Figure 14.4-35 Deleted Figure 14.4-36 Deleted Figure 14.4-37 Deleted Chapter 14, Page 217 of 218 Revision 20, 2006 OAG10000215_1572

IP2 FSAR UPDATE APPENDIX 14A DELETED Chapter 14, Page 218 of 218 Revision 20, 2006 OAG10000215_1573

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NUCLEAR POWER AND CORE HEAT FLUX vs TIME UFSAR FIGURE 14.1-5 REV. No. 19 OAGI0000215_1579

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3.5 3

25 2

15 0 2 8 INDIAN POINT UNIT No. 2 UNCONTROLLED RCCA BANK WITHDRAWAL FROM FULL POWER WITH MINIMUM REACTIVITY FEEDBACK (70 pcm/sec WITHDRAWAL RATE).

ICORE WATER AVERAGE TEMPERATURE AND DNBR vs TIME I UFSAR FIGURE 14.1-7 REV. No. 19 II OAGI0000215_1581

1.2 1

\5 c:: .s

.Q U

0

'- 6 w...

0::::

L.i..J 3:: .4 0

Q..

~

L.i..J .2

--l U

z: 0 I) 20 40 60 60 100 120 140 160 TIME (SECONDS) 1.2.,.--------------_---.

T':~

z:

o

\59 i"-

.6 is

r:

5

\

4 0 20 40 60 80 160 120 140 160 INDIAN POINT UNIT No. 2 UNCONTROLLED RCCA BANK WITHDRAWAL FROM FULL POWER WITH MINIMUM REACTIVITY FEEDBACK (1 pcm/sec WITHDRAWAL RATE).

NUCLEAR POWER AND CORE HEAT FLUX vs TIME UFSAR FIGURE 14.1-8 REV. No. 19 OAGI0000215_1582

2~~------------------------------~

2150 +0..l..-J,....;....-,-.,..l.....l......I-o....................,.-'-'--'-;r-'-'-'-r'-"--'-'!":"""--'-'-1'T:\-'-'--'-:1 20 40 60 80 100 120 U

'W 160 TIME (SECONDS) 1600

<l)

< .)

0 1500 w

<.)

ri:

> 1~

0 a:::

w

~ 1300 3::

a:::

w f'J a:::

> 1200

(/)

w a:::

a..

1100 +--'-----...,.....:.-'-'-.-"---r-"--"-r-"---'--r-'--.........,--.--'-'-l o 20 40 50 80 100 120 140 160 (SECONDS)

INDIAN POINT UNIT No. 2 UNCONTROLLED RCCA BANK WITHDRAWAL FROM FULL POWER WITH MINIMUM REACTIVITY FEEDBACK (1 pcm/sec WITHDRAWAL RATE).

PRESSURIZER PRESSURE AND WATER VOLUME vs TIME UFSAR FIGURE 14.1-9 REV. No. 19 OAGI0000215_1583

__ 5 9 5 , . - - - - - - - - - - - - - - - - - ,

W-I as 2'590 20 40 60 80 100 120 140 160 TIME (SECONDS) 3.5 3

a::::

CD 2.5 I--- I z:

Cl 2

I 1.5 1

0 20 40 60 80 100 120 14Q 160 TIME (SECONDS)

INDIAN POINT UNIT No. 2 UNCONTROLLED RCCA BANK WITHDRAWAL FROM FULL POWER WITH MINIMUM REACTIVITY FEEDBACK (1 pcrn/sec WITHDRAWAL RATE).

CORE WATER AVERAGE TEMPERATURE AND DNBR vs TIME UFSAR FIGURE 14.1-10 REV. No. 19 OAGI0000215_1584

- - Minimum Feedbcck

_ - _ - Maximum Feedback 2.2 -r----------------------,

.I

/

2 - /

I

~ - - -.. -.. I I:~"'HIGH NEUTRON 8§ OTa T TRIP of .... ' ; FLUX TRIP

=

= "

\

I I

E

s 1*8 \ I E \ I

'2 \ \ I

.::E ,

\I 1*6 -

-1 o I 2 10 10 10 10 Reactivity Addition Rate [pcm/second]

INDIAN POINT UNIT No. 2 MINIMUM DNBR VERSUS REACTIVITY INSERTION RATE, ROD WITHDRAWAL FROM 100 PERCENT POWER UFSAR FIGURE 14.1-11 IREV. No. 19 OAGI0000215_1585

- - Mir:M,..H"('; F@edback

- - - - Maximum Feedback 2.4 -r--------------------,

2*3 2.2 OTaTTRIP 2.1 2

j~ ,

I I

t ..

§§ I

=

= ....

.... I I

1*9 .... I 1*8 1.7 HIGH NEUTRON FLUX TRIP 1*6 1*5 1*4 18 16 1(~ J 10 Reactivity Addition Rate [pcm/second]

INDIAN POINT UNIT No. 2 MINIMUM DNBR VERSUS REACTIVITY INSERTION RATE, ROD WITHDRAWAL FROM 60 PERCENT POWER UFSAR FIGURE 14.1-12 REV. No. 19 OAGI0000215_1586

- - Minimum ;:."eedbock

- - - - MOxil"r"um FeedbocK 2.4 , - - - - - - - - - - -_ _ _ _ _ _ _- ,

~

I-2.3 _r-r-

/

r-I-

2*2 j- OT.1TTRIP I-2.1 0::: 2 CD

~

.~ 1.9 c:::

i§ 1.8-1.7 -

HIGH NEUTRON 1.6 - V FLUX TRIP 10-. 18 ld ,6 Reactivity Addition Rate [pcm/second]

INDIAN POINT UNIT No. 2 MINIMUM DNBR VERSUS REACTIVITY INSERTION RATE, ROD WITHDRAWAL FROM 10 PERCENT POWER UFSAR FIGURE 14.1-13 IREV. No. 19 OAGI0000215_1587

1.2.---------------------,

0 ,8 Ir-6

.4

.2 0

0 50 100 150 2)0 1*2....----------------------,

o .8 6

.4 INDIAN POINT UNIT No. 2 DROPPED ROD INCIDENT MANUAL ROO CONTROL NUCLEAR POWER AND CORE HEAT FLUX AT BOL (SMALL NEGATIVE MTC) FOR DROPPED RCCA OF WORTH - 400 PCM UFSAR FIGURE 14.1-14 REV. No. 19 OAGI0000215 1588

520 500+-~~~~~~~~~~~~~~~~~

o 50 100 150 200 Time 620

~

LL 600 580 560 540 520 500 0 50 100 200 INDIAN POINT UNIT No. 2 DROPPED ROD INCIDENT MANUAL ROD CONTROL CORE AVERAGE AND VESSEL INLET TEMPERATURE AT BOL (SMALL NEGATIVE MTC) FOR DROPPED RCCA OF WORTH - 400 PCM UFSAR FIGURE 14.1-15 REV. No. 19 OAGI0000215_1589

2600 - , - - - - - - - - - - - - - - - - - - ,

INDIAN POINT UNIT No. 2 DROPPED ROD INCIDENT MANUAL ROD CONTROL PRESSURIZER PRESSURE AT BOl (SMALL NEGATIVE MTC) FOR DROPPED RCCA OF WORTH - 400 PCM UFSAR FIGURE 14.1-161 REV. No. 19 I

OAGI0000215_1590

1.2...,.------------------,

o

.8 t~/

V-

.6

.2 1.2.....-----------------,

o *8 6

.2 INDIAN POINT UNIT No. 2 DROPPED ROD INCIDENT MANUAL ROD CONTROL NUCLEAR POWER AND CORE HEAT fLUX AT EOl (LARGE NEGATIVE MTC) fOR DROPPED RCCA Of WORTH - 400 PCM UFSAR FIGURE 14. 1-17 REV. No. 19 OAGI0000215 1591

620...,...........------------------,

600 580 560 540 520

,I INDIAN POINT UNIT No. 2 DROPPED ROD INCIDENT MANUAL ROD CONTROL CORE AVERAGE AND VESSEL INLET TEMPERATURE AT EOL (LARGE NEGATIVE MTC) FOR DROPPED RCCA OF WORTH - 400 PCM UFSAR FIGURE 14.1-18 REV. No. 19 OAGI0000215_1592

2600 - , - - - - - - - - - - - - - - - - - - - - - . ,

2400 2200 ~

~

2000 1800 o 50 100 150 200 Time INDIAN POINT UNIT No. 2 DROPPED ROD INCIDENT MANUAL ROD CONTROL PRESSURIZER PRESSURE AT EOL (LARGE NEGATIVE MTC) FOR DROPPED RCCA OF WORTH - 400 PCM I

UFSAR FIGURE 14.1-19 REV. No. 19 OAGI0000215_1593

1.2 1

D:1

~::&

.8 00 Q..z k.

.6

~~

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0 2 4 6 8 10 TIME (SECONDS) 1.2 I

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)(0

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x:g

~

.4

.2 0

0 2 4 6 8 10 TIME (SECONDS)

INDIAN POINT UNIT No. 2 LOSS OF ONE PUMP OUT OF FOUR NUCLEAR POWER AND CORE HEAT FLUX vs TIME UFSAR FIGURE 14.1-20 REV. No. 19 OAGI0000215_1594

3l: 750 9

50' zl>>

-III w ........ 700

~t:

8. . . .

";i 15 I- 650 600 0 2 4 6 8 10 TIME (SECONDS) 1.2 3l:

9

~i

~:2

2:0

.8

>Z

Jr.,.

go .6 Q..Z 02 98 .4

°e

!J-

~

.... .2 0

0 2 4 6 8 10 TIME (SECONDS)

INDIAN POINT UNIT No. 2 LOSS OF ONE PUMP OUT OF FOUR TOTAL CORE FLOW AND FAULTED LOOP FLOW 'IS TIME UFSAR FIGURE 14. 1- 21 REV. No. 19 OAGI0000215_1595

2400 1&1 IX 2300

~

)

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IX 0.......

ffi~

NO.

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1

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Il 2 4 & 8 10 TIldE (SECONDS)

INDIAN POINT UNIT No. 2 FOUR PUMP LOSS OF FLOW -

UNDERVOLTAGE TOTAL CORE FLOW AND RCS LOOP FLOW vs TIME UFSAR FIGURE 14.1-24 REV. No. 19 OAGI0000215_1598

2400

~

2300

)
tl II::
0..--.
f!i~
No..
2200 02"""
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a.. 2100 2000 0 2 4- 6 8 10 TIME (SECONDS) 5 4-i
z: 3 0
2
=-----
1 D 2 4- 6 II 10 TIME (SECONDS)
INDIAN POINT UNIT No. 2 FOUR PUMP LOSS OF FLOW -
UNDERVOLTAGE PRESSURIZER PRESSURE AND DNBR vs TIME UFSAR FIGURE 14.1-25 IREV. No. 19
l.2 1
~
a::; a< .8
~::I!
00 a,. %
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2 4 6 8 10 TIME (SECONDS) l.2 t
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0 2 4 6 8 10 TIME (SECONDS)
INDIAN POINT UNIT No. 2 FOUR PUMP LOSS OF FLOW -
UNDERFREQUENCY NUCLEAR POWER AND HEAT FLUX vs TIME UFSAR FIGURE 14.1-26 REV. No. 19 OAGI0000215_1600
800 700 9r.... 600 5(3' zlI.I 500
-~
It!~ 400 8--
~ 300 e
200 100 0 2 4 8 10 TIME (SECONDS) 1.2 3J:
g.--.
r....~
(,)- .8
~~
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~~
§~ .4
~~
.2 I) 0 2 4 6 8 10 TIME (SECONDS)
INDIAN POINT UNIT No. 2 FOUR PUMP LOSS OF FLOW -
UNOERFREQUENCY TOTAL CORE FLOW AND Res LOOP FLOW vs TIME UFSAR FIGURE 14.1-27 REV. No. 19 OAGI0000215_1601
2~~----------------------------~
2~+-~~4-~~~~~~~~-+~~~
o 2 4 6 8 10 nME (SECONDS) s~----------------------------~
3 2
o 2 6 B 10 nME (SECONDS)
INDIAN POINT UNIT No. 2 FOUR PUMP LOSS OF FLOW -
UNDERFREQUENCY PRESSURIZER PRESSURE AND DNBR vs TIME UFSAR FIGURE 14.1-28 REV. No. 19 OAGI0000215_1602
1.2-.--------------------,
0:1 lll:Z .8
~~
b-
.6
~~
(.)2
Jti .4 zQ!i e
.2 0
0 2 4 6 8 10 TIldE (SECONDS) 2700 2600 2500 0:
!.tJ i7l..... 2400 1/)<
UJ-IXCI) o..,e;. 2300 0:
I/)
(.)
2200 2100 2000 0 2 4 6 B 10 TIldE (SECONDS)
INDIAN POINT UNIT No. 2 LOCKED ROTOR NUCLEAR POWER AND RCS PRESSURE vs TIME I UFSAR FIGURE 14.1-29 REV. No. 19 'I OAGI0000215_1603
800 700
.: 600 9r....
!3-a
%UI
-If) 500 UI' "E:
8--- 400 e~ 300 200 I 100 0 2 4 6 8 10 TIME (SECONDS) 1.5
~~ 1
~~
ti:i
EO
Jr....
~o .5 a,. %
02 90 o~
!:le- o
~
r....
-.5 0 2 4 6 8 10 TIME (SECONDS)
INDIAN POINT UNIT No. 2 LOCKED ROTOR TOTAL CORE FLOW AND FAULTED LOOP FLOW vs TIME UFSAR FIGURE 14.1-30 IREV. No. 19 OAGI0000215 1604
2000 1800 bI Di::
I 1600
~bI D..
I bI......
1-1&.
1400 Di::o bIbi
%0
~'-" 1200
~
0
..J bI 1000
I I.i.
800 600 0 2 .4 6 8 10 TIME (SECONDS)
INDIAN POINT UNIT No. 2 LOCKED ROTOR FUEL CLAD INNER TEMPERATURE vs TIME UFSAR FIGURE 14.1-30A IREV. No. 19 OAGI0000215 1605
---. 1,2.....------------------,
(5 c:
'E o
z:
20 40 60 80 100 TIME (SECONDS) 2500 . . . - - - - - - - - - - - - - - - - - - - ,
~2@ V~I~
S
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2300
~
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0::::
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~
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(/)
~ 2000 I
+~""""'O'-.......-.--'---i....------*--,----* --.,.~*=====;i======,
Q 1900 -"-.
o 20 40 60 80 100 TIME (SECONDS)
INDIAN POINT UNIT No. 2 LOSS OF LOAD WITH PRESSURIZER SPRAY AND PORV, NUCLEAR POWER AND PRESSURIZER PRESSURE vs TIME UFSAR FIGURE 14.1-311 REV. No. 19 OAGI0000215_1606
595..,...--------------------,
20 40 60 80 100 TIME (SECONDS) 1700,--------------------,
<::I
~ 1600 w
~1500
§Z a:::
~1400
~
8S N
1300 a:::
~ {
~1~E I 1100 +r--'---'----,-~-'---,-,
o 2'0 40
~-'---'---.-,
60
-'--'-------,,;---'-------'-.---;1 80 100 TIME (SECONDS)
INDIAN POINT UNIT No. 2 LOSS OF LOAD WITH PRESSURIZER SPRAY AND PORV, AVERAGE COOLANT TEMPERATURE AND PRESSURIZER WATER VOLUME vs TIME UFSAR FIGURE 14.1-32 REV. No. 19 OAGI0000215_1607
3.5 3
1.5 INDIAN POINT UNIT No. 2 LOSS OF LOAD WITH PRESSURIZER SPRAY AND POWER OPERATED RELIEF VALVES DNBR vs TIME I
UFSAR FIGURE 14.1-33 REV. No. 19 OAGI0000215 1608
1.2...-----------------------,
o 20 40 60 80 100 TIME (SECONDS)

Rep Out let Pressure

Pressurizer Pressure 2700 . . . - - - - - - - - - - - - - - - - - - - - - - ,

2600 ,~"
-- I"
.~ 2500 I \
Cl.. I \
=; 2400 0::: I I \
\
~ 2300,' \
~ 2200 ,..' \
t3 2100 " '--.-
0::: - - - __ -_~~-------------
2000 ---- - - - - - - - - - -
INDIAN POINT UNIT No. 2 LOSS OF' LOAD WITHOUT PRESSURIZER SPRAY AND PORV, NUCLEAR POWER AND PRESSURIZER PRESSURE vs TIME UFSAR FIGURE 14. 1 -37 I REV. No. 19 OAGI0000215_1609
~~5~-------------------------------------'
u...
I en
~ 59C 20 40 60 80 100 TIME (SECONDS) 1~~------------------------------------~
-- -U'j
~ 1400 Lt..J
E
3 1300
§Z a:::
Lt..J 1200 I;;:i:
3:
8S I'--J 1100 C2
)
~ 1000 Lt..J a:::
C-9oo+-~~~.-~~-'~~~-.~~~-r~~~~
o 20 40 60 80 100 TIME (SECONDS)
INDIAN POINT UNIT No. 2 LOSS OF LOAD WITHOUT PRESSURIZER SPRAY AND POWER OPERATED REUEF VALVES, AVERAGE COOLANT TEMPERATURE AND PRESSURIZER WATER VOLUME vs TIME UFSAR FIGURE 14.1-38 REV. No. 19 OAGI0000215_1610
1200
.2 en 0...
1100 a

:::
(f)
(f)
~ 1000 0...
a::::
0
~ 900 -
a::::
w
z:
w C) 800
~
L5 f-(f) 700 0 20 40 60 80 100 TIME (SECONDS)
INDIAN POINT UNIT No. 2 LOSS OF LOAD WITHOUT PRESSURIZER SPRAY AND POWER OPERATED RELIEF VALVES, STEAM PRESSURE, vs TIME I
UFSAR FIGURE 14.1-39 REV. No. 19 OAGI0000215_1611
2400 . . , . . . . - - - - - - - - - - - - : - - - - - - - ,
~ 2350 o
05 0...
o 10 10 1 2 10 3
10
10 (seconds) 1800.......------------------,
1D t1: 1700 u
.0 21600 o I 2 3 4 10 iO 10 10 10 INDIAN POINT UNIT No. 2 LOSS OF NORMAL FEEDWATER, OFFSITE POWER AVAILABLE, HIGH Tovg PROGRAM, PRESSURIZER PRESSURE AND PRESSURIZER WATER VOLUME vs TIME UFSAR FIGURE 14.1-43. sht.1 REV. No. 19 OAGI0000215_1612
1.2 - . . . - - - - - - - - - - - - - - - - - - - ,
o 1 2 3 4 10 10 10 10 10 Time (seconds) 1.2...,,------------------,
.6
.4
110 n
i 10 1 2 10 i
10 3
10 INDIAN POINT UNIT No. 2 LOSS OF NORMAL FEEDWATER, OFFSITE POWER AVAILABLE, HIGH Tavg PROGRAM, NUCLEAR POWER AND CORE HEAT FLUX vs TIME UFSAR fiGURE 14.1-43, sht.2 REV. No. 19 OAGI0000215_1613
- - HOT LEG
- - - - CO~O LEG SAT RATION 700 -r-----------------,
660 620 580 N
g- 540
.3 Time (seconds)
- - HO LEG
- - - - CO 0 LEG SA URATION 700...,-------------------,
660 620 580 540 10 I 2 10 l
10
10 (seconds)
INDIAN POINT UNIT No. 2 LOSS OF NORMAL FEEDWATER, OFFSITE POWER AVAILABLE, HIGH Tavg PROGRAM, LOOP 21 AND LOOP 23 TEMPERATURE vs TIME UFSAR FIGURE 14.1-43, sht.3 REV. No. 19 OAGI0000215_1614
1200 . . , . - - - - - - - - - - - - - - - - - - - ,
1100 900 E
0
<I.)
u=;
~
800
('.J 0..
0 0
-' 700 600 0 t Z J 4 10 10 10 10 10 Time (seconds) 1200
'0'1100
.u:;
0..
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CL I
900 E
0 Q.)
u=;
1"0 800 C'J
1 10 G
I 10 I
~" I 2
10 t
J 10 i
4 10 Time INDIAN POINT UNIT No. 2 LOSS OF NORMAL FEEDWATER, OFFSITE POWER AVAILABLE, HIGH Tavg PROGRAM, STEAM GENERATOR 21 AND STEAM GENERATOR 23 PRESSURE vs TIME UFSAR FIGURE 14.1-43, sht.4\ REV. No. 19 OAGI0000215_1615
1.2 0
1
'2:
'0
.8
,6
~
3:
0 c;:
if)
.4 I
U 0:::
-0
-+-'
0 .2 0
0 1 2 3 4 10 10 10 10 10 Time (seconds) 25
.....-.2()
U
(!)
CJ1
.Cl
--1

15

~ 10
'C
l CJ1 CJ1
(!)
a: 5 f- I t
.I
\ 2 3 4 10 10 10 10 (seconds)
INDIAN POINT UNIT No. 2 LOSS OF NORMAL FEEDWATER, OFFSITE POWER AVAILABLE, HIGH Tavg PROGRAM ,TOTAL ReS FLOW AND PRESSURIZER RELIEF vs TIME urSAR FIGURE 14.1-43, sht.5 REV. No. 19 OAGI0000215 1616
1.2 1
i 00 0..%
.8 g~ 0
.6 0
~~....... .4
.2 0
0 50 160 150 200 TIME (SECONDS) 1.2
~
1
.8
2 XO It .... .6
,",,0
~%
rS
~
.4
.2 0
0 50 100 150 2)0 TIME (SECONDS)
INDIAN POINT UNIT No. 2 FEEDWATER SYSTEM MALFUNCTION EXCESSIVE FEEDWATER FLOW - HFP CONDITIONS MANUAL ROD CONTROL NUCLEAR POWER AND CORE HEAT FLUX vs TIME UfSAR fiGURE 14.1-45, sht.11 REV. No. 19 OAGI0000215_1617
2400 2200 f
J
~
0..'-'
l;~ 2000
~.,s.
J 0..
1800 1600 0 50 100 150 200 TIME (SECONDS) 5 4
0::
ill z0 3 2
1 fl 50 100 150 200 TIME (SECONDS)
INDIAN POINT UNIT No. 2 FEEDWATER SYSTEM MALFUNCTION EXCESSIVE FEEDWATER FlOW - HFP CONDITIONS MANUAL ROD CONTROL PRESSURIZER PRESSURE AND DNBR vs TIME UFSAR FIGURE 14.1-45, sht.21 REV. No. 19 OAGI0000215_1618
so 60 ~
'\
71:;:'
Ji!"
~f 40 g-l
..3.......
20 0
0 50 100
~ 150 200 TIME (SECONDS) 580 A
e 570
.i!
e
~
~i Qi' 560 eo Ie.......
e 550 (3
540 0 50 100 150 200 TIME (SECONDS)
INDIAN POINT UNIT No. 2 fEEDWATER SYSTEM MAlfUNCTION EXCESSIVE fEEDWATER flOW - HfP CONDITIONS MANUAL ROD CONTROL lOOP DELTA -T, AND CORE Tavg vs TIME UFSAR FIGURE 14.1-45, sht.31 REV. No. 19 OAGI0000215_1619
2360..,..-----------------j 2.i40
.~ 2320 CL
~
as
.2! 2260 (f)
(f) 2:: 2240 CL 2220 o \ 2 l 10 10 10 10 Time (seconds) 1800 - , - - - - - - - - - - - - - - - - - - - - - ,
~
Q)
~ 1700 u
.0 S 1600 Q.)
E g 1500 INDIAN POINT UNIT No. 2 LOSS OF ALL AC POWER, HIGH Tavg PROGRAM, PRESSURIZER PRESSURE AND PRESSURIZER WATER VOLUME vs TIME UFSAR FIGURE 14.1-50, sht.1 REV. No. 19 OAGI0000215_1620
1.2...,...------------------,
I o
10
! j' 10 i
1
~"iO 2
J 10 4
10 (seconds)
'0 .a 1 2 J 4 10 10 10 10 INDIAN POINT UNIT No. 2 LOSS OF ALL AC POWER, HIGH Tavg PROGRAM, NUCLEAR POWER AND CORE HEAT FLUX vs TIME UFSAR FIGURE 14.1-50, sht.2 REV. No. 19 OAGI0000215_1621
- - HOT LEG
- - - - COLD LEG

< SA lJR A T iON 700~--------------------------------~

w..
~ 660 _____________________________ - --'._,------------ ----,____ -,,-
<l.>
~
620
~
~
580 1 ,
~--------------'
I /'-----------
500 _
o 1()
t! l I j I 1
10
(\1 2
10 Time (seconds) j \ II, J
10 ,"I4 10
- - HOT EG
- - - - COL!) EG

< SATURATION 700~--------------------------------,

r---
w..
~ 660 ___________________________ --'--,,_,- - -,- -----------\_ ..... -
<l.>
~
620 {
580 bl-----~~
-f I \
I
~ it /'------' "--
~
500 10 a
---~--~~,------
10 I
r' 2
10 dme l seconds; i
!'f 1
10
.I4 10 INDIAN POINT UNIT No. 2 LOSS OF ALL AC POWER TO THE STATION AUXILARIES, HIGH Tavg PROGRAM, LOOP 21 AND LOOP 23 TEMPERATURE vs TIME UFSAR FIGURE 14.1-50, sht.31 REV. No. 19 OAGI0000215_1622
1200 I\.
0' noo
'u) 0..
'--/
1000 I
900 E
0 Q)
Vi C'-l 0..
800 0
0
.....J 700 600 0 1 2 ,
10 10 10 10 10 Time (seconds) 1200 I\.
-0 1100
'u) 0-
"---' I
l 1000 en en
~ 900{
U) Q) }
r-0 800 C'-l 0-0 0
.....J 700 I
600 0 '1 2 J
I 4
10 10 10 10 10 lime ,secon T' ( dSJ\
INDIAN POINT UNIT No. 2 LOSS OF ALL AC POWER TO THE STATION AUXILARIES, HIGH Tavg PROGRAM, LOOP 21 AND LOOP 23 STEAM PRESSURE vs TIME UFSAR FIGURE 14.1-50, sht.4 REV. No. 19 OAGI0000215_1623
1*2 1
0 c:: .a
.2 U
0
..... .6 6
3::
0 lJ...
(/)
.4 u
0:::
0
-0 .2 f--
0 0 1 2 3 ~
10 10 10 10 10 Time (seconds) 25~-----------------------------.
jl o~~~(\~.~r~
o 10 I
10 10 2
10 J
10 4
Time (seconds)
INDIAN POINT UNIT No. 2 LOSS OF ALL AC POWER TO THE STATION AUXILARJES, INTERMEDIATE Tavg PROGRAM, TOTAL RCS FLOW AND PRESSURIZER RELIEF RATE vs TIME UFSAR FIGURE 14.1-50, sht.5IREV. No. 19 OAGI0000215_1624
16 15 14 13 12 Vl w 11 0::
> 10
...J
(
"'- 9 8
w Q. 7 l-S Vl 5 I.L.
0 4 ci 3
z:
w 2
> 1 i=
j 0
IE
> 86 87 88 89 90 91 92 93 94 95 96 97 98 99 u
CALENDAR YEAR ANALYSIS FAILURE LINE
ACTUAL DATA SV TYPE 1 FAILURE RATE = 2.47-06/HR SLOPE OF ANALYSIS FAILURE LINE = [(SV TYPE 1 F.R.) * (OPERATING HOURS)] / (CALENDAR YEARS)
= [(2.47E-06/HR) * (2.917E+06 HRS)] / (6.42 CAl. YRS.) = 1.1 FAIl./CAL. YR.
INDIAN POINT UNIT No. 2 UFSAR FIGURE 14.1-62 TRACKING 8-95/96 STOP VALVE (SV) TYPE 1 FAILURES STOP VALVE DISC FAILS MIC. No. 2001M81537 REV. No. 17 A OAGI0000215_1625
5 4 f-3 f-2 f-o1 L====c::::c~====:J 86 87 88 89 I
90 I
91 I
92 I
93 I
94 I
95 I
96 I
97 I
98 I
99 CALENDAR YEAR
- - ANALYSIS FAILURE LINE
ACTUAL DATA SV TYPE 2 FAILURE RATE = 2.05-07/HR SLOPE OF ANALYSIS FAILURE LINE = [(SV TYPE 2 F.R.) * (OPERATING HOURS)] / (CALENDAR YEARS)
= [(2.05E-07/HR) * (2.917E+06 HRS)] / (6.42 CAl. YRS.) = 0.093 FAIL.jCAl. YR.
INDIAN POINT UNIT No. 2 UFSAR FIGURE 14.1-63 TRACKING B-95/96 STOP VALVE (SV) TYPE 2 FAILURES STOP VALVE SPRING FAILS MIC. No. 2001MB1538 IREV. No. 17A OAGI0000215_1626
5 4 _
3 >-
V'!
o1 L=:::r==:L~===:=J. I I I I ! I I I I I 86 87 88 89 90 91 92 93 94 95 96 97 98 99 CALENDAR YEAR ANALYSIS FAILURE LINE
ACTUAL DATA sv TYPE 3 FAILURE RATE = 2.05-07/HR SLOPE OF ANALYSIS FAILURE LINE = [(SV TYPE 3 F.R.) .. (OPERATING HOURS)] / (CALENDAR YEARS)
= [(2.05E-07/HR) .. (2.917[+06 HRS>>) / (6.42 CAL. YRS.) = 0.093 FAIL./CAL. YR.
INDIAN POINT UNIT No. 2 UFSAR FIGURE 14.1-64 TRACKING 8-95/96 STOP VALVE (SV) TYPE 3 FAILURES STOP VALVE STICKS OPEN MIC. No. 2001M81539 IREV. No. 17A OAGI0000215_1627
CALENDAR YEAR ANALYSIS FAILURE LINE
ACTUAL DATA CV TYPE 4 FAILURE RATE = 1.22-06/HR SLOPE OF ANALYSIS FAILURE LINE ::: [(CV TYPE 4 F.R.) .. (OPERATING HOURS)] / (CALENDAR YEARS)
[(1.22E-06/HR) .. (3.925E+06 HRS)) / (6.42 CAL. YRS.) = 0.75 FAIL./CAL. YR.
INDIAN POINT UNIT No. 2 UFSAR FIGURE 14.1-65 TRACKING B-95/96 CONTROL VALVE (CV) TYPE 4 FAILURES CONTROL VALVE SPRING BOLT FAILS MIC. No. 2001MB1540 IREV. No. 17A OAGI0000215_1628
5 4 t-3 _
u oz _
1 t-o I I I I I I I I I I 86 87 88 89 90 91 92 93 94 95 96 97 98 99 CALENDAR YEAR
- - ANALYSIS FAILURE LINE
ACTUAL DATA CV TYPE 5 FAILURE RATE = 1.53-07/HR SLOPE OF ANALYSIS FAILURE LINE = [(CV TYPE 5 t.R.) * (OPERATING HOURS)] I (CALENDAR YEARS)
= [(1.53E-07/HR) * (3.925E+06 HRS)] I (6.42 CAL. YRS.) = 0.094 FAIL./cAl. YR.
INDIAN POINT UNIT No. 2 UFSAR FIGURE 14.1-66 TRACKING 8-95/96 CONTROL VALVE (CV) TYPE 5 FAILURES CONTROL VALVE STICKS OPEN MIC. No. 2001M81541 IREV. No. 17A OAGI0000215_1629
Initial Case
.~~~~ WHEN JUSTIRED USING THE APPROPRIATE Ib==::g~ CURVE, NOMINAL TEST INTERVALS UP TO
.--t.:...-:...:...........,:;""'! 3 MONTHS ARE RECOMMENDED.
Probability of Destructive Overspeed (y.....')
.:IIII-.1IiI1I 1 3 5 TurbJn. Valve Test Interval (months)
Curve #1: SlUVeillaoce of stop valve discs occurs every '8 mo"'hs. Testing of valve freedom of movement oocurs at inteJVals of 1 to 6 months (horizontal axis).
Curve 12: Surveillance of stop valve discs occurs every 24 months. Tt.3ting of valve freedom of movement occurs at intervals of 1 to 6 months (horizontal axis).
Estimated 3.7E-06/r for 3 month test interval for Curve #2 INDIAN POINT UNIT No. 2 UFSAR FIGURE 14.1-67 ANNUAL FREQUENCY OF DESTRUCTIVE OVERSPEED FOR VARIOUS BB-95/96 TURBINE VALVE TEST INTERVAL (1-0N-1 SV-CV TURBINE / 1 OUT OF 4 STEAM PATHS)
MIC. No. 2001 MB1542 REV. No. 17A OAGI0000215_1630
- - Safety Injection Flow
- - - - Breck Flow 1800 1750 1700 1650 1600 1550 1500 1450 I
~
0 I
.~ 1400 I
........-- I e
J 1350 I J
en I gs 1300 I 0... I 1250 I I
I 1200 I
I 1150 I I
1100 I I
I 1050 I I
1000 950 900 0 60 80 100 160 Flow Rate (Ibs/sec)
INDIAN POINT UNIT No. 2 STEAM GENERATOR TUBE RUPTURE, BREAK FLOW AND SAFETY INJECTION FLOW VS.
REACTOR COOLANT SYSTEM PRESSURE UFSAR FIGURE 14.2-0 REV. No. 19 OAGI0000215_1631
fLOW MEASURING NOZZLE I/' CONTAINMENT l I r...FA!IT ACTING STOP VALVE
" I CHECK VALVE STEAM GENERATORS f
/ I
\..../ I r'\
I I
STEAM LINE CROSS CONNECTIONS I
\J I r'"\
I I
I V I
(\
I INDIAN POINT UNIT No. 2 UFSAR FIGURE 14.2-1 STEAM LINE VALVE ARRANGEMENT -
SCHEMATIC MIC. No. 2001MB1570 REV. No. 17A OAGI0000215_1632
.16
.14
.12 0 .1£+00
8£-01
)
ri
.6E-Ol
.4E-Ol
2E-01 I
100 200 300 400 TIME (SECONDS) 400
~
200 0
-200
-400
-600
-800
-1000
-1200
-1400 0 100 200 300 400 TIME (SECONDS)
INDIAN POINT UNIT No. 2 STEAM LINE RUPTURE OFFSITE POWER AVAILABLE, EOL CORE HEAT FLUX AND CORE REACTIVITY vs. TIME UFSAR FIGURE 14.2-2, sht.1 REV. No. 19 OAGI0000215_1633
u 1 d

1 tcc

. 1 toe t 100 200 400 TIME (SECONDS) 2400 0'2200 "en 32000 lLJ

§'§1800 (f) i:J1600 0:::: \
CL 1400 \
\
1200 1000 800 600 0 100 200 300 400 INDIAN POINT UNIT No. 2 STEAM LINE RUPTURE OFFSITE POWER AVAILABLE, EOl, REACTOR COOLANT PRESSURE AND RV INLET TEMPERATURE vs. TIME UFSAR FIGURE 14.2-2, sht.2 REV. No. 19 OAGI0000215_1634
-- Quite

Intact xoo~------------------------------~

-.. 2500 u
Q) rn
'-.. 2000 E
..0 100 200 300 400 TIME (SECONDS)
-- ouited

Intact

~1~~----------------------------~
E g 140000
./
r------------------~----
(j')
~ 120000 5 100000
~
w 80000 z:
w
<.::> 60000 40000
<i! 20000 0
>-- 0
() 100 200 300 400 INDIAN POINT UNIT No. 2 STEAM LINE RUPTURE OFFSITE POWER AVAILABLE, EOL, STEAM FLOW AND STEAM GENERATOR PRESSURE vs. TIME UFSAR FIGURE 14.2-2, sht.3 REV. No. 19 OAGI0000215_1635
~ 120 E
a..
a..
6 100
~
!z I..W 80
z 0
60 C> 40 I..W
~
I..W 0:::
20 0 ,
<..:> 0 0 100 200 300 400 TIME (SECONDS)
INDIAN POINT UNIT No. 2 STEAM LINE RUPTURE OFFSITE POWER AVAILABLE, EOL, CORE BORON CONCENTRATION vs TIME UFSAR FIGURE 14.2-2, sht.41 REV. No. 19 OAGI0000215_1636
~,-------------------------~------~
30
~ 20
s (JJ (JJ
~
Q..
10
~2 -I o I z 3 +
10 10 10 10 10 10 lQ Time (s)
INDIAN POINT UNIT No. 2 CONTAIN~ENT PRESSURE TI~E HISTORY (DOUBLE - ENDED ~AIN STEA~ LINE BREAK
~AIN FCV FAILURE
~AXI~U~ CONTAIN~ENT SAFEGUARDS)
UFSAR FIGURE 14.2-7 I REV. No. 20 OAGI0000215_1637
1.6
~
1.4 1.2 0
c:::
'E 0
z: 1 I-0 c:::
0 e
LL.
.8 l-Q) 3::
0 0..
.6 I-0 Q)
s z:
.4 I-
2 I-0 0 2 4 6 8 10 Time (Seconds)
INDIAN POINT UNIT No. 2 ROD EJECTION ACCIDENT, BOL-HFP, NUCLEAR POWER vs. TIME UFSAR FIGURE 14.2-11 I REV. No. 19 OAGI0000215 1638
6@~----------------------------------.
4000 Fuel Centerline Fuel Average 2@ ~ , ~,
/'/ ------------------- --- ---------------
/ -----~-- Fuel Clad I
I Average
,I 1000 'if
[
~ ~
v (,
I I 4 6 8 10 Time (Seconds)
INDIAN POINT UNIT No. 2 ROD EJECTION ACCIDENT, BOL-HFP, FUEL TEMPERATURES vs. TIME UFSAR FIGURE 14.2-12 REV. No. 19 OAGI0000215_1639
10~----------------------------~1 8 -i-
-:=-
0 c
"E 0
z
'+- 6 -I-0 r
Q.)
3:
0 4 -I-CL-Io-0 I-Q.)
U Z
2-I\
o~-L~~~~~--4,~~===9=-~~~
o 2 J 4 Time (Seconds)
INDIAN POINT UNIT No. 2 ROD EJECTION ACCIDENT, BOL-HZP, NUCLEAR POWER vs. TIME UFSAR FIGURE 14.2-13\ REV. No. 19 OAGI0000215_1640
woo~----------------------------------.
3500 -
3000 L2 I
en (l) 3 2500 -t-
~ ........
I /
/
---2 (l) I I
" ...... Fuel Centerline a.. ................ ,
~
I--
Q3
I 2000 .......................... -
LI... "" Fuel Average Fuel Clad Average 5OOf-' I I o 2 4 6 10 Time (Seconds)
INDIAN POINT UNIT No. 2 ROD EJECTION ACCIDENT, SOL-HZP, FUEL TEMPERATURES vs. TIME UFSAR FIGURE 14.2-141 REV. No. 19 OAGI0000215_1641
40 30-
'0 c
'E 0
z
'+-
0 C
0 u
E: 20-LL-Q.)
==
0 a..
0 Q.)
<.3
s Z
10 -
, ,j 0
0 *2 .4 .6 ,13 ;
Time (Seconds)
INDIAN POINT UNIT No. 2 ROD EJECTION ACCIDENT, EOl-HZP, NUCLEAR POWER vs. TIME UFSAR FIGURE 14.2-15\ REV. No. 19 OAGI0000215_1642
5~~--------------------------------.
4000
/'
/'
/.
~
.... .......... Fuel Centerline
~
... ......... ~ Fuel Average Fuel Clad Average 1~-
INDIAN POINT UNIT No. 2 ROD EJECTION ACCIDENT, EOl-HZP, FUEL TEMPERATURES vs. TIME UFSAR FIGURE 14.2-16 IREV. No. 19 OAGI0000215_1643
2~------------------------------.
1*5 -

E

-0 c::
0
z:
'0 g
U
<::I w...
<l) 0 a....
0
<J.>
U
z:
.5 -
o 2 3 4 Time (Seconds)
INDIAN POINT UNIT No. 2 ROO EJECTION ACCiDENT, EOL-HFP, NUCLEAR POWER vs TIME UFSAR FIGURE 14.2-17 IREV. No. 19 OAGI0000215_1644
&OO~---------------------------------.
5000 t:t' 4000 en
~
V I I
I 1'--- . . . . . ,
I Fuel Centerline I ....
I ..........
, I
, I 2000
~,,#------ ... .... Fuel Average
// -------------------
I -~----- ______ _
I I
---------- Fuel Clad Average 1000 '
JI
, , I o 4 6 8 10 (Seconds)
INDIAN POINT UNIT No. 2 ROD EJECTION ACCIDENT, EOL-HFP, FUEL TEMPERATURES vs TIME UFSAR FIGURE 14.2-18 IREV. No. 19 OAGI0000215_1645
494.1l37- o ChaMOI Selm9
!!!J o Gap 444.400- ~
I5iJ ~~ ~ [iOJ ~ ~P§J SectionS (IUS,,)
4:25.156_ '"'T'"
lX:~oe OHISCIFI\I DC
IX:
--r
_, _I . . . . _ . . . . . . . . . . . _ .... t _ Section 7
'_'~_~"'_'.'_'_'~'.i __ '
r 359.321_ _w . . . . . . . . ' ......... . 182.50")
!!]'iiCl I!tJ ~ ~ i!!. ~[EJ ~~ lID ~~f@
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~~ =: :::
~ =:~"="~"=:::::::~:=:::~:=[F!A:~:=:=:=:=~=:=:=:=:=:=
. ~ :.:~::~.:::'::':::::: ~:~ :~: :.::~: :.::.::: ~.::
J l I. I
_. ffif' ; . -. _. i'itl-. -. _. - ':Ti!f~ @~ . _. ;.' - . -~ - . _. -1~ ** -. !il' -g;!it Section 3
. _. _. _.* , _... o' _. _. _ 'ii--, .. ' _ .Ii!lo. _. _, o. lEt, _.
0
.'0 . . . 0 ** ' _ '* * * (144.00")
~
-: .... ...... . . ........ 7. - ..... . - ................. ~ ...... ! ... ~ ..... -. -. -~ ...... -....... - ......... : . .
I I " I 1711.993_
... " ~ .... - - ' ' ' ' ' ' ' ' ' ; ' ' - ..... - . _ ... , ........ ;- * - ~ .... ~ * - .......... ~ .................. -
167.113-156.433_ ...
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. . . . . . . . . . . . . . . . . . . . . . . . . .1 *
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~
131.077_ * ......... t
.. ' ....... ' ...... ' ~ ............ ~ ..... .,. .~ . . , . . ;" ,. '1" ....... _....:........ - .... -. - . . ...' -.'I . . .
I" 121.531_ *. oj *. ... "'... -_~ '* * .;w - . - w' W ....-."r ....... ...- ......... ,w ...... ""..-- ;- w Section 2
~, (69.542")
e~[IJ I 51.!llIll- _. _. _.m. 0 *** _. c. .... , .. .m, _..... E:l" *.
-~4Z+
~ CD . r.1 Section 1 m
~ 10 :
~p'p" 7A (51.989")
Figure 14.3-1: Indian Point Unit 2 WCOBRAlfRAC Vessel Model Noding Diagram INDIAN POINT UNIT No. 2 INDIAN POINT UNIT 2 WCOBRA/TRAC VESSEL MODEL NODING DIAGRAM UFSAR FIGURE 14.3-1 REV. No. 20 OAGI0000215_1646
Accum. Accun.
II ,
ValYe ValVe (C.l. LBLOCA Location) ___ "..F"", VIIve Figure 14.3..2: Indian Point Unit 2 WCOBRAITRAC Model Loop Layout INDIAN POINT UNIT No. 2 INDIAN POINT UNIT 2 WCOBRA/TRAC VESSEL MODEL LOOP LAYOUT UFSAR FIGURE 14.3-2 REV. No. 20 OAGI0000215_1647

Intact oop

- - - - Broken oop 120 - . - - - - - - - - - - - - - - - - - - - ,
100 20 o 200 400 600 600 1400 ReS Pressure (psig)
INDIAN POINT UNIT No. 2 HIGH HEAD SAFETY INJECTION FLOW RATE UFSAR FIGURE 14.3-3 REV. No. 19 OAGI0000215_1648
~iI \
II ! ! ,i i
___---'-I._____ ~-.:...I _ _
I' , II l i
I I I _ I ,---I" - ! 1-- --1 4'50 I\ I
i-s-r I I I -~I-t--+1__: _r--1 J \1
!2!U1 \
I I I I : I :
I I I ) t I I r-.l-1 l I 1\ I I I ! I I I~
1 100 !
I\ I I \ I I
I i
I I I I I I I I
I I
J 1
I I \; I ; : : ~ ! ! 1
1 I ! I I I I I I I !
INDIAN POINT UNIT No. 2 UFSAR FIGURE 14.3-3A SAFETY INJECTION FLOW vs Res PRESSURE MIC. No. 2000MC4204 I REV. No. 17 A OAGI0000215_1649
Indian Point Unit 2 Best-Estimate LBLOCA Analysis
- - ROD 1 PEAK CLADDING TEt.APERATURE 2~~------------------------------------~
1500 500 o 100 200 300 400 500 Time After Break (s) 14J115JOtl Figure 14.3-6: Peak Cladding Temperature for Reference Transient INDIAN POINT UNIT No. 2 PEAK CLADDING TEMPERATURE FOR REFERENCE TRANSIENT UFSAR FIGURE 14.3-6 REV. No. 20 OAGI0000215_1650
Indian Point Unit 2 Best-Estimate LBLOCA Analysis VESSEL SIDE BREAK FLOW OOOOO~------------------------------------~
I-50000 -
(,t) 40000 M E
..CI W
~ 30000 ~
==
0 l..J...
en en 0
E 20000 I- \
l-i-
10000 Figure 14.3-7: Vessel Side Break Flow for Referenee Transient INDIAN POINT UNIT No. 2 VESSEL SIDE BREAK FLOW FOR REFERENCE TRANSIENT UFSAR FIGURE 14.3-7 IREV. No. 20 OAGI0000215_1651
Indian Point Unit 2 Best-Estimate LBLOCA Analysis PUMP SIDE BREAK FLOW
~~--------------------------------------~
25000 -
20000 -
en E
~
..:::::;... 15000 -
--(l) a a::::
c
~ 10000 cn (f) a o
7~1 Figure 14.3-8: Loop Side Break Flow for Reference Transient INDIAN POINT UNIT No. 2 LOOP SIDE BREAK FLOW FOR REFERENCE TRANSIENT UFSAR FIGURE 14.3-8 I REV. No. 20 OAGI0000215_1652
Indian Point Unit 2 Best-Estimate LBLOCA Analysis INTACT LOOP PUMP VOID FRACTION
- - - - BROKEN LOOP PUMP VOID FRACTION 1*2.....----------------------,
1-I I
I I
8 I f
I c: I Eu 1 J
~ .6 - I I
'"0 11 g ~
I
~
.4 I I
~I
~
.2 - I I
~I o ~J I I I o 100 150 200 Time After Break (s) 15633541 Figure 14.3-9: Void Fraction at the Intact and Broken Loop Pump Inlet for Reference Transient INDIAN POINT UNIT No. 2 VOID FRACTION AT THE INTACT AND BROKEN LOOP PUMP INLET FOR REFERENCE TRANSIENT UFSAR FIGURE 14.3-9 IREV. No. 20 OAGI0000215_1653
Indian Point Unit 2 Best-Estimate LBLOCA Analysis
- - VAPOR FLOW RATE PER ASSEMBLY IN CORE AVERAGE CH 17 10~----------------------------------------~
s en E
...0
.:::=.-
Q)
-+-'
0 a::: 0 3::
0 c:;:
en en
'='
~
-s o 5 10 15 20 25 30 Time After Break (s) 7438ll30111 Figure 14.3-10: Vapor Flow Rate per Assembly at Mid~core in Core Average Channel 17 During Blowdown for Reference Transient INDIAN POINT UNIT No. 2 VAPOR FLOW RATE PER ASSEMBLY AT MID-CORE AVERAGE CHANNEL 17 DURING BLOWDOWN FOR REFERENCE TRANSIENT UFSAR FIGURE 14.3-10 REV. No. 20 OAGI0000215_1654
Indian Point Unit 2 Best-Estimate LBLOCA Analysis
- - VAPOR FLOW RATE r~ CORE HOT ASSEMBLY CHANNEL 19 1O~---------------------------------------,
5
-5 o 5 10 15 20 25 30 Time After Break (s) 1~1 Figure 14.3-11: Vapor Flow Rate at Mid-core in Core Hot Assembly Cbannel19 During Blowdown for Reference Transient INDIAN POINT UNIT No. 2 VAPOR FLOW RATE PER ASSEMBLY AT MID-CORE AVERAGE CHANNEL 19 DURING BLOWDOWN FOR REFERENCE TRANSIENT UFSAR FIGURE 14.3-11 REV. No. 20 OAGI0000215_1655
Indian Point Unit 2 Best-Estimate LBLOCA Analysis LOWER PLENUM COLLAPSED LIQUID LEVEL 12~--------------------------------------~
I-10 - Ir---------~-- __ ~
-+-' 8-Q.)
Q.)
--l
g
l c:r 6 -
..::J
"'0 CJ.)
en 0..
..2 0
u 4-2-
l-f- \
O+-~~L~'_~I~I_~L.L~I~~I~J-J~~-'~I-~I~-~IJ~I-~J o 100 200 300 400 500 Time After Break (8) 743a$31:>>1 Figure 14.3-12: Collapsed Liquid Level in Lower Plenum for Reference Transient INDIAN POINT UNIT No. 2 COLLAPSED LIQUID LEVEL PLENUM FOR REFERENCE TRANSIENT UFSAR FIGURE 14.3-12 I REV. No. 20 OAGI0000215_1656
Indian Point Unit 2 Best-Estimate LBLOCA Analysis INTACT LOOP 2 ACCUMULATOR MASS fLOW RATE 2000 -r----------------------,
I-1500 -
500~
7~1 Figure 14.3-13: Intact Loop 2 Accumulator Flow for Reference Transient INDIAN POINT UNIT No. 2 INTACT LOOP 2 ACCUMULATOR FLOW FOR REFERENCE TRANSIENT UFSAR FIGURE 14.3-13 I REV. No. 20 OAGI0000215_1657
Indian Point Unit 2 Best-Estimate LBLOCA Analysis INTACT LOOP 2 SI MASS FLOW RATE l00~------------------------------------~
80 -

(/')

E 60 -
~
~
(l) 0 0:::
31:
0 c::::
(/') 40-en 0
E 20 -
O~~~~~+-~~~~~~I~J~J~J~~I~I~~
o 50 100 150 200 Ti me After Break (s) 7~1 Figure 14.3-14: Intact Loop 2 Safety Injection Flow for Reference Transient INDIAN POINT UNIT No. 2 INTACT LOOP 2 SAFETY INJECTION FLOW FOR REFERENCE TRANSIENT UFSAR FIGURE 14.3-141 REV. No. 20 OAGI0000215_1658
Indian Point Unit 2 Best-Estimate LBLOCA Analysis
- - LlaUID LEVEL IN CORE AVERAGE CHANNEL 17 12~------------------------------------~
10 2
8 v
~
""'0
.~ 6
..:J
""'0 III Ul 0...
..2 8 4 2
Time After Break (s) 743aQl11 Figure 14.3-15: Collapsed Liquid Level in Core Average Channel 17 for Reference Transient INDIAN POINT UNIT No. 2 COLLAPSED LIQUID LEVEL IN CORE AVERAGE CHANNEL 17 FOR REFERENCE TRANSIENT UFSAR FIGURE 14.3-15 REV. No. 20 OAGI0000215_1659
Indian Point Unit 2 Best-Estimate LBLOCA Analysis
- - LIQUID LEVEL IN INTACT LOOP 2 DOWNCOMER
~~--------------------------------------,
35 30 10 5
TIme After Break (s) 7~1 Figure 14.3-16: Collapsed Liquid Level in Intact Loop Downcomer for Reference Transient INDIAN POINT UNIT No. 2 COLLAPSED LIQUID LEVEL IN INTACT LOOP DOWNCOMER FOR REFERENCE TRANSIENT UFSAR FIGURE 14.3-16 REV. No. 20 OAGI0000215_1660
Indian Point Unit 2 Best-Estimate LBLOCA Analysis VESSEL LIQUID MASS 250000 . . . . . , . . - - - - - - - - - - - - - - - - - - - - - ,
200000 150000 E
...0
~
en (I) 0
E 100000 ~
50000 1438530111 Figure 14.3*17: Vessel Fluid Mass for Reference Transient INDIAN POINT UNIT No. 2 VESSEL FLUID MASS FOR REFERENCE TRANSIENT UFSAR FIGURE 14.3-17 I REV. No. 20 OAGI0000215_1661
Indian Point Unit 2 Best-Estimate LBLOCA Analysis ROD 1 PEAK CLADDING TEMPERATURE LOCATION 12 r
l-I-
10 t l-I-
a r
........ I-e::
l-0 6-0 CJ.)
I-W l-I-
4 r
l-I-
2-l-
I-I-
I I I I 0
0 50 1()O 150 200 Time After Break (s) 7438li3Otl Figure 14.3-18: Peak Cladding Temperature Elevation for Reference Transient INDIAN POINT UNIT No. 2 PEAK CLADDING TEMPERATURE ELEVATION FOR REFERENCE TRANSIENT UFSAR FIGURE 14.3-18 I REV. No. 20 OAGI0000215_1662
Indian Point Unit 2 Best-Estimate LBLOCA Analysis
-- ROD 1 PEAK CLADDING TEMPERATURE

ROD 2 PEAK CLADDING TEMPERATURE

, ROO 3 PEAK CLADDING TEMPERATURE

ROD 4 PEAK CLADDING TEMPERATURE

--- ROO 5 PEAK CLADDING TEMPERATURE 2000~----------------------------------------~
1500 IJ)
.a....o 1000 IJ) 0..
E
~
500 o 100 200 300 500 Time After Break (s) 7431K1J0111 Figure 14.3-19: Peak Cladding Temperature Comparison for Five Rods for Reference Transient INDIAN POINT UNIT No. 2 PEAK CLADDING TEMPERATURE COMPARISON FOR FIVE RODS FOR REFERENCE TRANSIENT UFSAR FIGURE 14.3-19 REV. No. 20 OAGI0000215_1663
Axial Power Distribution for Initial Transient
- - Hot Rod
- - - - Hot Assembly Rod
---~---. Average Rod 2*5 - . - - - - - - - - - - - - - - - - - - - - - - - - ,
2 ,
\
\
' ..... _---""",. \
\
\
,-' '\.
,-" ................... ...,......... .". ... '; 'II.,
\-
~;tt
, ------..... '\
\
\
, \
\
\
\
I \
I \
I \
I \
I \
,I \
\
.5 I I
,I I
t I
I I
I o 2 468 10 12 Core Elevation (ft)
Figure 14.3-20: Indian Point Unit 2 Axial Power Distribution for Initial and Reference Transient INDIAN POINT UNIT No. 2 INDIAN POINT UNIT 2 AXIAL POWER DISTRIBUTION FOR INITIAL AND REFERENCE TRANSIENT UFSAR FIGURE 14.3-20 REV. No. 20 OAGI0000215_1664
0.50 .....- -.. ,.---~-~- -~- --~ ,.. -. _. -... -,.-.-.--~ ~-~
0.45 0.3.0.40 0.43.0.40 0.40 0.35 I-0 m
13..
0.30 0.25 0.3,0.2.4 0.43.0,24 0.20 0.15 0.25 0.30 0.35 0.40 0.45 0.50 PMIO I
Figure 14.3-21: Indian Point Unit 2 PBOTIPMID Analysis and Operating Limits INDIAN POINT UNIT No. 2 INDIAN POINT UNIT 2 PBOT /PMID ANALYSIS AND OPERATING LIMITS UFSAR FIGURE 14.3-21 I REV. No. 20 OAGI0000215_1665
Indian Point Unit 2
- - coco Calculated Containm~nt Pressure 45~------------------------------------~
40 35 20 15 10+-~~~~~~~~~~~+-~~~+-~~~
o 100 200 300 400 500 Time After Break (s)
,~
Figure 14.3*22: Indian Point Unit 2 Lower Bound COCO Calculated Containment Pressure INDIAN POINT UNIT No. 2 INDIAN POINT UNIT 2 LOWER BOUND COCO CALCULATED CONTAINMENT PRESSURE UFSAR FIGURE 14.3-22 REV. No. 20 OAGI0000215_1666
18~----------------------------~
16 14 12
~ 10 c£ o
Q.l c:::
.:J 8
6 4
o 2 468 12 Elevation (ft)
INDIAN POINT UNIT No. 2 SMALL BREAK LOCA AXIAL POWER SHAPE UFSAR FIGURE 14.3-53 REV. No. 19 OAGI0000215_1667
2500 I
2000 * -
.2 en 0...
(1)1500-
I en en (1) 0...
1000 I-500 0
sOo I
1000 I
1500 Time (5) 2000 2500 I '
3000 INDIAN POINT UNIT No. 2 3.0" SMALL BREAK LOCA RCS PRESSURE UFSAR FIGURE 14.3-54 I REV. No. 19 OAGI0000215_1668
- - - - Top of Core = 22.0795 f 32 30 28 24 22 -----
20 o 500 1000 1500 2000 2500 Time (s)
INDIAN POINT UNIT No. 2 3.0" SMALL BREAK LOCA CORE MIXTURE LEVEL UFSAR FIGURE 14.3-55 REV. No. 19 OAGI0000215_1669
1100 . , - - - - - - - - - - - - - - - - - - - ,
1000 -
900 -
g: 800 -
600-500-INDIAN POINT UNIT No. 2 3.0" SMALL BREAK LOCA HOT ROD CLAD AVERAGE TEMPERATURE UFSAR FIGURE 14.3-56 IREV. No. 19 OAGI0000215_1670
300.,.------------------,
250 200 100 50 INDIAN POINT UNIT No. 2 3.0" SMALL BREAK LOCA CORE OUTLET STEAM FLOW UFSAR FIGURE 14.3-57 REV. No. 19 OAGI0000215_1671
4 10 r r--
W-I N
-+-'
~10 I 3 I
en
J U
< I) 0
<I) 2
~ 10 0
i-0
<I)
r::
l-'
1 10 l-I ' I '
500 1000 1~ 2000 2500 3000 (s)
INDIAN POINT UNIT No. 2 3.0" SMALL BREAK LOCA HEAT TRANSFER COEFFICIENT UFSAR FIGURE 14.3-58 IREV. No. 19 OAGI0000215_1672
750..,...-----------------,
700 650
~
..3 600 2
(l) a.
E (l) f--
550 500 50Q 1000 1500 2000 2500 3000 Time INDIAN POINT UNIT No. 2 3.0" SMALL BREAK LOCA HOT SPOT FLUID TEMPERATURE UFSAR FIGURE 14.3-59 REV. No. 19 OAGI0000215_1673
1800 1600 -
1400 -
1200 -
1000 -
<l>
-+-'
0 0::::
3::
G:
0 800-(J')
rV (J')
0
2' 600 -
r 400 -f-200 -
I : I :
0 0 sOc 1000 1500 2000 2500 3000 INDIAN POINT UNIT No. 2 3.0" SMALL BREAK LOCA BREAK FLOW UFSAR FIGURE 14.3-60 IREV. No. 19 OAGI0000215_1674
-- BrOKe" LOop

In t <l C t Loop 100 80-

/
/
/ '"
I
.....--.- I
(/) I
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.0
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40 ,...,. .. ,.1 0 I
E I
I i
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I 20 r- I I
I I
I
! ' I '
0 500 1000 1500 2000 2500 3000 TIme (s)
INDIAN POINT UNIT No. 2 3.0" SMALL BREAK LOCA SAFETY INJECTION MASS FLOW RATE UFSAR FIGURE 14.3-61 IREV. No. 19 OAGI0000215_1675
2400 2200 ~
2000 1800 0
--e:
"in 0...
1600-
l (I)
(I)
CL e:
1400 -
iI1 t-1200 r-1000 -
t-
) 1 ! , I I , ,
800 Ii 1000 2000 3Obo 4Obo 5000 6000 Time (s)
INDIAN POINT UNIT No. 2 2.0" SMALL BREAK LOCA RCS PRESSURE UFSAR FIGURE 14.3-62 I REV. No. 19 OAGI0000215_1676
op ; ~or 2.0795
~~----------------------------~
35 20 o 1000 2000 5000 6000 INDIAN POINT UNIT No. 2 2.0" SMALL BREAK LOCA CORE MIXTURE LEVEL UFSAR FIGURE 14.3-63 REV. No. 19 OAGI0000215_1677
1000 II 900 "-
800 (J)
l 0
(J) 0..
E<l.)
I- 700 f-600 -f-J I I ' I 500 1(00 2000 3000 4doo sooo 6000 Time INDIAN POINT UNIT No. 2 2.0" SMALL BREAK LOCA HOT ROD CLAD AVERAGE TEMPERATURE UFSAR FIGURE 14.3-64 I REV. No. 19 OAGI0000215_1678
2500 2000 0
0Ci5 1500 a..
Q)
I en en Q) 0..
1000 --
500 l-e-
I'! I ' I i '
V 0 sOO 1000 1500 2000 2500 3000 Time (s)
INDIAN POINT UNIT No. 2 4.0" SMALL BREAK LOCA RCS PRESSURE UFSAR FIGURE 14.3-65 REV. No. 19 OAGI0000215_1679
- - - - T P of Core 22.0795 It
~~------------------------------~
34 32 30 o 500 1000 1500 2000 Time (s)
INDIAN POINT UNIT No. 2 4.0" SMALL BREAK LOCA CORE MIXTURE LEVEL UFSAR FIGURE 14.3-66 REV. No. 19 OAGI0000215_1680
9OO~----------------------------~
I 800-
.--.. 700 -
I.J...
500-INDIAN POINT UNIT No. 2 4.0" SMALL BREAK LOCA HOT ROD CLAD AVERAGE TEMPERATURE UFSAR FIGURE 14.3-67 IREV. No. 19 OAGI0000215_1681
UPPER SUPPORT HOLD DOWN PLATE SPRING DEEP BEAM CORE BARREl.
FLANGE LONG COLUMN GUIDE TUBES SHORT COLUMN TOP CORE PLATE CORE BARREL (TOP)
TOP NOZZLE SPRING* THERMAL SHIELD CORE FUEL ASSEMBLY CORe 8ARREl I BOTTOM)
LOWER PACKAGE BOTTOM CORE PLATE INDIAN POINT UNIT No. 2 UFSAR FIGURE 14.3-101 REACTOR VESSEL INTERNALS MIC. No. 2000MC4300 REV. No. 17 A OAGI0000215 1682
UPPER HEAD
- C.G.
_ INTERNALS SUPPORT LEDGE t---!!II~-"'" K]..._ ..... 19_S_ RPV NOZZLE CE.NTERLINE 25
..... sus ",.
TYPICALLY UNSUPPORTED NOZZLE (4)
TYPICAL SUPPORTED NOZZLE (4)
[K] STIFFNESS MATRIX
-H-ILt-N- LINEAR IMPACT LOWER RADIAL
- SUPPORT INDIAN POINT UNIT No. 2 UFSAR FIGURE 14.3-102 RPV SHELL AND SUPPORT SYSTEM MIC. No. 2000MC4301 REV. No. 17 A OAGI0000215 1683
51 ---. UPPER SUPPORT PLATE FLANGE
- CORE BARREL FLAttGE 2
12
[!}-H-t- ~ ..:.: RPV NOZZLE CENTERLI~E UPPER CORE PlAT£ DENOTU NODBS OR
[J RPV SHBLL SUBMODm.
o DENOTES NODES OR IN'l'ERNALs SUBMODBL CORE C.G.
o
-H-I cl-l+- CONCENTRIC IMPACT
-<<-t LJ-H- LINEAR IMPACT

LOWER CORE PLATE

LOWER RADIAL SUPPORT INDIAN POINT UNIT No. 2 UFSAR FIGURE 14.3-103A REACTOR VESSEL INTERNALS CORE BARREL ASSEMBLY MIC. No. 2001MB1166 IREV. No. 17A OAGI0000215_1684

DENOTES NOD!S ON R'" IHULIUIMOOU DENOTII "ODES ON O CO"E ......n IUIMODEL IUP'PORT COLUMNS AND GUtDE TUIU
_ _ .....IRCO.. I PLATE TC.'UEL L HOZZU
_ _ CO"E C.G.
IOnOM PUEL NOZZLE
_ _ LOWE .. CORE PLATE INDIAN POINT UNIT No. 2 UFSAR FIGURE 14.3-1038 REACTOR INTERNALS AND FUEL MIC. No. 2001M81167 REV. No. 17A OAGI0000215_1685
1 UPP~R .. SUPPORT PLATE GUIDE TUBES 2
SUPPORT COLUMNS 3
~
W
~.
t-I ij5
> FUEL
~
I-+-
J
~
ASSEM3LY 0 II: REGION
~ ~
LOWER CORE PLATE LOWER SUPPORT PLA I.E 4 11 11 INDIAN POINT UNIT No. 2 UFSAR FIGURE 14.3-104 RPV SYSTEM MODEL MIC. No. 2000MC4303 REV. No. 1 7 A OAGI0000215 1686
9 10 ~----------------------------------~
8 10 o
o>
E 6 C1i 10 5
10 3
10 o 1 2 J 4 5 5 7 10 10 10 10 10 10 10 10 Time (S)
INDIAN POINT UNIT No. 2 DOUBLE-ENDED PUMP SUCTION BREAK FOR 3216 MWt MINIMUM SAFEGUARDS INTEGRATED WALL HEAT REMOVAL UFSAR FIGURE 14.3-105 REV. No. 19 OAGI0000215_1687
12 10 ------------------------------------~
- 9 o~ 10 to:
= o E
(!)
(!)
r::
10 6
l=
~ § o
o U 6 c 10 t3:
5
~ 10 e
g'4
~ 10 ~
3 10 "
o 1 2 l 4 5 7 10 10 10 10 10 10 10 Time (S)
INDIAN POINT UNIT No. 2 DOUBLE-ENDED PUMP SUCTION BREAK FOR 3216 MWt MINIMUM SAFEGUARDS INTEGRATED FAN COOLER HEAT REMOVAL UFSAR FIGURE 14.3-1061 REV. No. 19 OAGI0000215_1688
II 10
l co 7
'---'" 10 10 o>
E Q) 6 a::: 10 10 Q)
r:
2CL 10
(/)
-0 Q) 10 <4-5-,10 E Q) c:
3 10 2 ' , !' :1'; !i 10 "i!
4 5 6 0
10 10 1 2 10 10 " 10 10 10 11 Time (S)
INDIAN POINT UNIT No. 2 DOUBLE -ENDED PUMP SUCTION BREAK I FOR 3216 MWt MINIMUM SAFEGUARDS INTEGRATED SPRAY HEAT REMOVAL I "UFSAR FIGURE 14.3-1071 REV. No. 19 I OAGI0000215_1689
~~--------------------------------~
(l) 100 o
u O+-~~~~*~'~'~~~~~~~*~;:l~~.I~*~'~~
o 1 2 3 4 5 6 7 10 10 10 10 10 10 10 10 Time (S)
INDIAN POINT UNIT No. 2 DOUBLE-ENDED PUMP SUCTION BREAK FOR 3216 MWt MINIMUM SAFEGUARDS STRUCTURAL HEAT TRANSFER COEFFICIENT UFSAR FIGURE 14.3-1 08 REV. No. 19 OAGI0000215_1690
~~--------------------------------~
40 10
1;1 , 1'1 I I I I I 1 :! i> I 0 " 1 'J
-2 -1 0 1 2 3 4 5 6 7 10 10 10 10 10 10 10 10 10 10 Time (S)
INDIAN POINT UNIT No. 2 DOUBLE-ENDED PUMP SUCTION BREAK FOR 3216 MWt MINIMUM SAFEGUARDS CONTAINMENT PRESSURE UFSAR FIGURE 14.3-109 REV. No. 19 OAGI0000215_1691
o lei me t tmosp ere emperature

on oinmen Sump Water emperot ra 280...,...------------------------,

260 240
\\
\
I C 220 I
"--' I Q.) I
'- I
J o'-
200 I
I Q.)
a.. I E /
/
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/
/
/
160
/
.- /
140 120 -!-w...i.J..;..W,--..l..~~..l....;.;.""r_,U...i,..'""+.....l.-~T__'_.....l.-""r_.....l.-....w.:,.....l.-....i..W.l."'r___'---...i.4
-2 -1 o 1 2 3 4 5 6 7 10 10 10 10 10 10 10 10 10 10 Time (S)
INDIAN POINT UNIT No. 2 DOUBLE -ENDED PUMP SUCTION BREAK FOR 3216 MWt MINIMUM SAFEGUARDS CONTAINMENT TEMPERATURE UFSAR FIGURE 14.3-11 0 REV. No. 19 OAGI0000215_1692

ML12228A650

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