ML17328A554

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Proposed Tech Specs Changing 3/4.7.1.5.b, Steam Generator Stop Valves & Table 3.3-5 5.h,6.h & 7.c, Steam Line Isolation Response Times, Required for Accident Analyses
ML17328A554
Person / Time
Site: Cook American Electric Power icon.png
Issue date: 01/31/1990
From:
INDIANA MICHIGAN POWER CO. (FORMERLY INDIANA & MICHIG
To:
Shared Package
ML17328A555 List:
References
AEP:NRC:1120, NUDOCS 9002070468
Download: ML17328A554 (93)


Text

ATTACHMENT 2 TO AEP:NRC:1120 PROPOSED REVISED TECHNICAL SPECIFICATION PACES 9002070468 900131 Pea saacK osooosr5 P

TABLE 3.3-5 Cont:inued ENGINEERED SAFETY FEATURES RESPONSE TIMES INXTIATING SXGNAL AND FUNCTION

RESPONSE

TIME IN SECONDS 3.

Pressurizer Pressure-Low a.

b.

C.

d.

e.f.

g ~

Safety Injection (ECCS)

Reactor Trip (from SI)

Feedwat:er Isolat:ion Cont:ainment: Isolation-Phase "A"

Containment:

Purge and Exhaust Xsolation Auxiliary Feedwater Pumps Essential Service Water System

< 27.0 /13.0¹

< 3.0

< 8.0

< 18.0¹ Not: Applicable Not Applicable

< 48.0 /13.0¹ 4.

Differential Pressure Between Steam Lines-Hi h a.

b.

co d.

e.f.

g ~

Safety Injection (ECCS)

Reactor Trip (from SX)

Feedwater Isolation Containment Isolation-Phase "A"

Containment:

Purge and Exhaust Isolation Auxiliary Feedwater Pumps Essential Service Water System

< 13.0¹/23.0¹¹

< 3.0

< 8.0

< 18.0¹/28.0¹¹ Not Applicable Not Applicable

< 13.0¹/48.0¹¹ 5.

Steam Flow in Two Steam Lines - Hi h Coincident with T

--Low-Low a.

b.

c ~

d, e.f.

g h.

Safety Injection (ECCS)

Reactor Trip (from SI)

Feedwater Isolation Containment Isolation-Phase "A"

Containment:

Purge and Exhaust Isolation Auxiliary Feedwater Pumps Essential Service Water System St:earn Line Isolation

< 15,0¹/25.0¹¹

< 5.0

< 10.0

< 20.0¹/30,0¹¹ Not Applicable Not Applicable

< 15.0¹/50.0¹¹

< 13.0 COOK NUCLEAR PLANT - UNIT 1 3/4 3-28 AMENDMENT NO.

TABLE 3.3-5 Continued ENGINEERED SAFETY FEATURES RESPONSE TIMES INITIATINGSIGNAL AND FUNCTION

RESPONSE

TIME IN SECONDS 6.

Steam Flow in Two Steam Lines-Hi h Coincident With Steam Line Pressure-Low a.

b.

c ~

d.

e.f.

g ~

h.

Safety,Infection (ECCS)

Reactor Trip (from SI)

Feedwater Isolation Containment Isolation-Phase "A"

Containment Purge and Exhaust Isolation Auxiliary Feedwater Pumps Essential Service Water System Steam Line Isolation

< 13.0¹/23.0¹¹

< 3.0

< 8.0

< 18.0¹/28.0¹¹ Not Applicable Not Applicable

< 14.0¹/48.0¹¹

< 11.0 7.

Containment Pressure--Hi h-Hi h a.

b.

c ~

d.

Containment Spray Containment Isolation-Phase "B"

Steam Line Isolation Containment Air Recirculation Fan

< 45.0 Not Applicable

< 10.0

< 660.0 8.

Steam Generator Water Level--Hi h-Hi h a.

Turbine Trip b.

Feedwater Isolation

< 2.5

< 11.0 9.

Steam Generator

'Water -Level--Low-Low a.

Motor Driven Auxiliary Feedwater Pumps b.

Turbine Driven Auxiliary Feedwater Pumps

< 60.0

< 60.0 10.

4160 volt Emer enc Bus Loss of Volta e a.

Motor'riven Auxiliary Feedwater Pumps 11.

Loss of Main Feedwater Pum s

a.

Motor Driven Auxiliary Feedwater Pumps

12. Reactor Coolant Pum Bus Undervolta e

< 60.0

< 60.0 a.

Turbine Driven Auxiliary Feedwater Pumps

< 60.0 COOK NUCLEAR PLANT - UNIT 1 3/4 3-29 AMENDMENT NO.

I

PLANT SYSTEMS

'STEAM GENERATOR STOP VALVES LIMITING CONDITION FOR OPERATION 3.7.1.5 Each steam generator stop valve shall be OPERABLE.

APPLICABILITY: MODES 1, 2 and 3.

ACTION:

MODE 1 - With one steam generator stop valve inoperable but open, POWER OPERATION may continue provided the inoperable valve is restored to OPERABLE status within 4 hours4.62963e-5 days <br />0.00111 hours <br />6.613757e-6 weeks <br />1.522e-6 months <br />; otherwise, reduce power to less than or equal to 5 percent of RATED THERMAL POWER within the next 2 hours2.314815e-5 days <br />5.555556e-4 hours <br />3.306878e-6 weeks <br />7.61e-7 months <br />.

MODES 2 - With one steam generator stop valve inoperable, subsequent and 3

operation in MODES 2 or 3 may proceed provided:

a.

The stop valve is maintained closed.

b. 'he provisions of Specification 3.0.4 are not applicable.

Otherwise, be in HOT SHUTDOWN within the next 12 hours1.388889e-4 days <br />0.00333 hours <br />1.984127e-5 weeks <br />4.566e-6 months <br />.

SURVEILLANCE RE UIREMENTS 4.7.1.5.1 Each steam generator stop valve that is open shall be demonstrated OPERABLE by:

a.

Part-stroke exercising the valve at least once per 92 days, and b.

Verifying full closure within 8 seconds on any closure actuation 0

signal while in HOT STANDBY with T greater than or equal to 541 F during each reactor shutdown except that verification of full closure within 8 seconds need not be determined more often than once per "92 days.

4.7.1,5.2 The provisions of Specification 4.0,4 are not applicable for entry into MODE 3.

4.7.1.5.3 The provisions of Specification 4.0.4 are not applicable for entry into MODE 2 when performing PHYSICS TESTS at the beginning of a cycle provided the steam generator stop valves are maintained closed.

COOK NUCLEAR PLANT - UNIT 1 3/4 7-10 AMENDMENT NO.

I

ATTACHMENT 3 TO AEP:NRC:1120 ANALYSIS OP MAIN STEAM LINE BREAK INSIDE CONTAINMENT (WCAP-11902 SUPPLEMENT 1)

l

iiESTINGHOUSc, CLASS iii MCAP-11902 Supplement 1

RERATED POMER ANO REVISEO TEMPERATURE ANO PRESSURE OPERATION FOR

, DONALD C.

COOK NUCLEAR PLANT UNITS 1 5 2 LICENSING REPORT September 1989 NEST INGHOUSE ELECTRIC CORPORATION Energy Systems Business Unit P.O.

BOX 355 Pittsburgh, Pennsylvania 15230 9144e:1d/092189

TABLE S-2.1-1 COOK NUCLEAR PLANT UNITS 1

ANO 2 OESIGN POWER CAPABILITY PARAMETERS FOR RERATING PROGRAM Parameter NSSS Power, MWt Core Power, MWt RCS Flow,(gpm/loop)"

Minimum Heasured Flow, (total gpm)*"

RCS Temperatures,

'F Core Outlet Vessel Outlet Core Average Vessel Average Vessel/Core Inlet Steam Generator Outlet Zero Load RCS Pressure, psia Steam Pressure,6psia Steam flow, (10 lb/hr.tot.)

feedwater Temperature,

'F 5

SG Tube Plugging (Unit 1, Original)

Case 1

3250 3250 88,500 366,400

'602.0 599.3 570.5 567,8 536.3 536.3 547.0 2250 758 14.12 434.8 (Unit 2, Current)

Case 2

3423 3411 364,960 575.5 574.1

'547.0 2250 794;4 14.6 423.4 1PA avg./

15A peak Flow Oefinitions:

t

  • RCS Flow (Thermal Oesign Flow) - The conservatively low flow used for thermal/hydraulic design.

The design parameters listed above are based on this flow.

  • "Minimum Measured Flow - The flow specified in the Tech.

Specs.

which must be confirmed or exceeded by the'flow measurements obtained during plant startup and is the flow used in reactor core ONB analyses for plants applying the Improved Thermal Oesi.gn Procedure.

~flow values supplied in FSAR6for Unit 2 are 141.3 x 10 lb/hr for vessel 6

coolant flow, and 134.9 x 10 lb/hr for active core flow.

Note:

Oashes in Case 2 indicate information which was not contained in the

FSAR, and is therefore information which is unavailable to Westinghouse.

9144 e:1d/092189 S-2.1-5

TABLE S-2.1-1 (Cont'd)

COOK NUCLEAR PLANT UNITS 1 ANO 2 DESIGN POWER CAPABILITY PARAMETERS FOR RERATING PROGRAM Parameter (Revised)

(Revised)

(Revised)

(Revised)

Case 3

Case 4

Case 5

Case 6

NSSS

Power, MWt Core Power, MWt RCS Flow, (gpm/loop)"

Minimum Measured

Flow, (total gpm)"*

3262

. 3250 88,500 366,400 3425 3413 88,500 366,400 3425 3413 88,500 366,400 3425 3413 88,500 366,400 RCS Temperatures,

'F Core Outlet Vessel Outlet Core Average Vessel Average Vessel/Core Inlet Steam Generator Outlet Zero Load RCS Pressure, psia Steam Pressure,6psia Steam Flow, (10 lb/hr.tot.)

Feedwater Temperature,

'F 610.1 607.5 579.2 576.3 545.2 545.0 547.0 583. 6 580.7 549.7'47.0 513.3

. 513.1 547.0 614. 0 611.2 581.8 578.7 546.2 546.0 547.0 2250 2250 2250 or of or 2100 2100 2100 807 603 820 14.20 14.98 15.07 434.8 442.0 442.0 613.9 611.2 581.8 578.7 546.2 546,0 547.0 2250 or 2100 806 15,06 442.0

%%d SG Tube Plugging (avef age) 15 10 10 15 Flow Definitions:

  • RCS Flow (Thermal Design Flow) - The conservatively low flow us'ed for thermal/hydraulic design.

The design parameters listed above are based on this flow.

""Minimum Measured Flow - The flow specified in the Tech.

Specs.

which must be confirmed or exceeded by the flow measurements obtained during plant startup and is the flow used in reactor core DNB analyses for plants applying the Improved Thermal Design Procedure.

91440:1d/091889 S-2.1-6

TABLE S-2.1-1 (Cont'd)

COOK NUCLEAR PLANT UNITS 1 AND 2 DESIGN POWER CAPABILITY PARAMETERS FOR RERATING PROGRAM Parameter (Revised)

(Revised)

(Revised)

(Revised)

Case 7

Case 8

Case 9

Case 10

Power, MWt Core Power, MWt RCS Flow, (gpm/loop)"

Minimum Heasured

Flow, (total gpm)"*

3600 3588 88,500 366,400 3600 3588 88,500 366,400 3600 3588 88,500 366,400 3600 3588 88,500 366,400 RCS Temperatures,

'F Core Outlet Vessel Outlet Core Average Vessel Average Vessel/Core Inlet Steam Generator Outlet Zero Load a

RCS Pressure, psia Steam Pressure,6psia Steam Flow, (10 lb/hr.tot.)

Feedwater Temperature,

'F 585.4 582.3 549.9 547.0 511.7 511.4 547.0 618. 0 585. 4 615.2 582.3 584.6 549.9 581.3 547.0 547,3 511.7 547.1 511.4 547.0 547.0 618.1 615.2 584.7 581.3 547.4 547.2 547.0 2250 2250 2250 2250 or or or ol 2100 2100 2100 2100 587 820 576 806 15.90 16.00 15.89 15.99 449.0 449.0 449.0 449.0 5

SG Tube Plugging (average) 10 10 15 15 Flow Definitions:

~

"RCS Flow (Thermal Design Flow) - The conservatively low flow used for thermal/hydraulic design.

The design parameters listed above are based on this flow.

~Minimum Heasured Flow - The flow specified in the Tech.

Specs.

which must be

. confirmed or exceeded by the flow measurements obtained during plant startup and is the flow used in reactor core DNB analyses for plants applying the Improved Thermal Design Procedure.

9144e:1d/091889 S-2.1-7

S-3.3 NON-LOCA SAFETY EVALUATION S-3.3.1 Introduction This section evaluates the effects of the Cook Nuclear Plant Rerating Program on the non-LOCA'transients:

The non-LOCA safety evaluation provided within is applicable only for Unit 1, with the exception of the steamline break mass/energy releases (inside and outside containment).

The effort performed is to support Unit 1 operation with an uprated core power of 3413 MNt in the range of reactor vessel average temperatures between 547'F and 578.7'F at primary pressure values of 2100 psia or 2250 psia.

Table S"2. 1-1 (Cases 4

and 5) presents the range of conditions possible for the rerating of'nit 1.

The steamline break mass/energy release analyses are performed to support the potential future Unit 1 rerating as well as to bound a potential rerating of Unit 2.

Table S-2.1-1 (Cases 7 and 8) presents the range of conditions possible for the future rerating of Unit 2.

In addition, the evaluation

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perfbrmed is to support a maximum average steam generator tube plugging level of 104, with a peak steam generator tube plugging level of 15%.

The following non-LOCA safety evaluation also supports the change and/or relaxation of certain plant parameters to provide Unit 1 with increased operating margin and flexibility.

Included in the non-LOCA safety evaluation are:

Increased Most Negative Moderator Temperature Coefficient (MTC)

(Tech Spec 3.1.1.4b)

Degraded ECCS Charging Pump Flow (Tech Spec 4.5.2f)

Increased Main Steamline Isolation Valve (MSIV) Closure Time (Tech Spec 4.7.1.5b and Tech Spec Table 3.3-5 items 5h, 6h,

& 7c)

The evaluation conservatively assumes 0 ppm boron concentration in the Boron Injection Tank (BIT).

9144e:1d/091889 S-3,3-1

r The evaluation also supports a change to the steam generator water level program.

The existing level program is a ramp function from 33'A narrow range span (NRS) to 44K NRS from 05 power to 204 power and a constant level at 44%

NRS between 205 power and 100'A power.

The proposed steam generator water level program is a constant level at 44A NRS between 0/

power and lOOA power.

S-3.3.4.1 Steamline Break Mass/Energy Releases This section will discuss -the analyses of.the steamline break event to determine the mass and energy releases inside containment and the superheated mass and energy releases outside containment for the Cook Rerating Program.

The analyses were performed to support the range of conditions possible for the rerating of Unit 1 as well as to position Unit 2 for a potential rerating.

The analyses also consider the relaxation of certain plant parameters (Section S-3.3-1).

91446:1d/091889 S-3.3-6

Steamline Break Mass/Energy Releases Inside Containment The current mass/energy releases for the inside containment analysis is based on work performed for Unit 2, which is applicable for Unit 1.

The calculation of the mass/energy release following a steamline break is described in the Cook Unit 2 FSAR Section 14.1.5.

The steamline break mass/energy releases were recalculated to address the rerating of both Units and the relaxation of the plant parameters described in Section S-3.3. 1.

Steamline ruptures occurring inside a reactor containment structure may result in significant releases of high energy fluid to the containment environment, possibly resulting in high containment temperatures and pressures.

The quantitative nature of the releases following a steamline rupture is dependent upon the many possible configurations of the plant steam system and containment designs as well as the plant operating conditions and the size -of the rupture.

These variations make it difficult to reasonably determine the 4

single "worst case" for both containment pressure and temperature evaluations following a steambreak.

The FSAR'analysis determined that the limiting scenario of the steambreak cases analyied for the containment response evaluation were a break size of 0.942 ft occurring at 305 power for the 2

split rupture scenario and a break size of 4.6 ft occurring at full power 2

for the double-ended rupture scenario.

{The 30'A power split break case was slightly more limiting.)

However, it is difficult to conclude if these

FSAP, cases remain bounding for the range of conditions possible for the reratings of both Units.

Adding to the difficulty in determining the effect of the rerating conditions are the plant parameters changes incorporated into the Cook Rerating Program.

The potential changes of certain plant parameters (i.e, relaxed most negative MTC limit, degraded ECCS performance, increased MSIV closure time, and 0 ppm BIT boron concentration requirement) are penalties in the calculation of mass/energy releases.

'It is not readily apparent as to the total impact of the combination of these changes.

As such, a series of steamline

breaks, consistent with the cases presented in the FSAR, were analyzed to determine the containment response to a variety of postulated pipe breaks encompassing wide variations in plant operation, safety system performance, and break sizes.

9144e:1d/091889 S-3.3-7

'I

The LOfTRAN computer code (Reference

2) was used to calculate the break flows and enthalpies of the release through the steambreak.

Blowdown mass/energy releases determined using LOFTRAN include the effects of core power generation, main and'uxiliary'feedwater additions, engineered safeguards

systems, reactor coolant thick metal heat storage, and reverse steam generator heat transfer.

A bounding analysis was performed to address the range of conditions possible for the potential Unit 1 rerating and the potential Unit 2 rerating.

The assumptions on the initial conditions are taken to maximize the mass and total energy released.

The higher primary temperatures along with the higher uprated power level associated with the Unit 2 rerating parameters are conservative for the mass/energy release calculations.

The upper bound temperature of Table S"2.1-1, Case 8 was used, Since the mass blowdown rate is dependent on steam pressure and the steam pressure is less for the lower bound temperature

case, the steam pressure of the upper bound temperature case is limiting for the range of operating conditions possible for the reratings of Unit 1 and Unit 2.

The functions which actuate safety injection and steamline isolation during a

steamline rupture event are commonly referred to as the Steamline Break Protection System.

A plant's steamline break protection system design can have a large effect on steamline break results.

The steamline break protection system designs for Unit 1 and Unit 2 are different.

Unit 1's design is referred to as an "OLD" steamline break protection system design.

Unit 2's design is referred to as a

"HYBRID" steamline break protection system design.

The two systems have the following characteristics:

9144e:1d/091889 S-3.3-8

Unit 1 - "OLD" Steamline Break Protection Safety Injection Signals 1.

High-high steam flow coincident with low steamline pressure

{two out of four lines) 2.

High-high steam flow coincident with low-low Tavg (two out of four lines) 3.

Two out of three differential pressure signals between a steam line and the remaining steam lines 4.

Two out of three low pressurizer pressure signals 5.

Two out of thre'e hi containment pressure signals Steamline Isolation Signals 1.

High-high steam flow coincident with low steamline pressure

{two out of four lines) 2.

High-high steam flow coincident with low-low Tavg (two out of four lines) 3.

Two out of four hi-hi containment pressure signals Unit 2 - "HYBRID" Steamline Break Protection Safety Injection Signals 1.

Low steamline pressure (two out of,four lines) 2.

Two out of three differential pressure signals between a steam line and the remaining steam lines 9144':1d/091889 S-3.3"9

I 3.

Two out of three low pressurizer pressure signals 4.

Two out of three hi containment pressure signals Steamline Isolation Signals 1.

Low steamline pressure (two out of four lines) 2.

High-high steam flow coincident with low-low Tavg (two out of four lines) 3.

Two out of four hi-hi containment pressure signals The only differences between the Unit 1 and Unit 2 designs is the actuations from a high-high steam flow and low-low Tavg signal and the logic associated with the low steamline pressure signal required to actuate safety injection and steamline isolation.

For Unit 1, a high-high steam flow coincident with low-low Tavg signal actuates both safety injection and steamline isolation.

For Unit 2, a high-high steam flow coincident with low-low Tavg signal actuates only steamline isolation.

However, the difference is not significant for the calculation of the mass/energy releases since the analysis does not take credit for any fSF actuations on a high-high steam flow coincident with low-low Tavg signal.

Unit 1's design requires a coincidence between the low steamline pressure and high-high steam flow for protection actuation.

Unit 2's design only requires the low steamline pressure signal for protection actuation; no coincidence with steam flow is required.

The coincidence logic required for safety injection initiation and steamline isolation on high-high steam flow and low steam pressure for Unit 1 is more limiting for the calculation of mass/energy releases inside containment than Unit 2 s design.

Actuation of safety injection and steamline isolation will limit the mass/energy released to the containment.

Delaying the safeguards initiation will result in a conservative calculation of the mass/energy 9144e: id/091889 S-3.3-10

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releases for the containment pressure and temperature evaluation.

The coincidence requirement for high-high steam flow with low steam pressure of the Unit 1 design increases the likelihood that safeguards initiation might be delayed compared to Unit 2's design where only a low steam pressure signal is required.

In the case where the coincidence logic prohibits safety injection and steamline isolation on high-high steam flow with low steam pressure, one of the other signals must be received before the safeguards are initiated.

As

such, the Unit 1 steamline break protection system design was assumed in this bounding analysis for the calculation of the mass/energy releases inside containment.

Assumptions A series of steamline breaks were analyzed to determine the most severe break condition for the containment temperature and pressure response.

The following assumptions were used in the analysis:

a.

Oouble-ended pipe breaks were assumed to occur at the nozzle of one steam'enerator and also downstream of the flow restrictor.

Split ruptures were assumed to occur at the nozzle of one steam generator.

b.

The blowdown is assumed to be dry saturated steam.

c.

As discussed

above, the Unit 1 steamline break protection system design is assumed.

However, credit was not taken for safeguards actuation on high steam line differential pressure or high-high steam flow coincident with low-low Tavg.

d.

Steamline isolation is assumed complete 11 seconds after the setpoint is reached for either high-high steam flow coincident with low steam

, pressure or hi-hi containment pressure.

The isolation time allows 8 seconds for valve closure plus 3 seconds. for electronic delays and signal processing.

The total delay time for steamline isolation of 11 seconds is assumed to support the relaxation of the main steam isolation valve (MSIV) closure time, 9144e:1d/092189 S-3.3-11

4-ll lq

e.

4.6 ft and 1.4 ft double-ended pipe breaks were evaluated at

102, 70, 30, and zero percent power levels.

f.

Split, pipe ruptures were evaluated at 0.86 ft,

102'A power; 2

0.908 ft, 7(5 power; 0.942 ft, 30/ power; and 0.4 ft, hot 2

2 2

shutdown.

These split break sizes for each power level were modeled because they reflect the largest breaks for which ESF actuations (i.e., steamline isolation, feedwater isolation, and safety injection) must be generated by high containment pressure trips.

The high-high steam

'flow coincident with low steam pressure is not reached for these break sizes or smaller break sizes.

(Reference 5) g.

Failure of a main steam isolation valve, failure of a feedwater isolation valve or main feed pump trip, and failure of auxiliary feedwater runout control were considered.

Two cases for each break

- size and power level scenario were evaluated with one case modeling the HSIV failure and the other case modeling the AFM runout control failure.

Each case assumed conservative main feedwater addition to bound the feedwater isolation valve or main feed pump trip fai lure.

h.

The auxiliary feedwater system is manually re-aligned by the operator after 10 minutes.

A shutdown margin of 1.3/ hk/k is assumed.

This assumption includes added conservatism with respect to the Unit 1 end-of-life shutdown margin requirement of 1.6% 4k/k at no load, equi librium xenon conditions, and the most reactive RCCA stuck in its fully withdrawn position.

The Unit 1 end-of-life'hutdown margin requirement was used as the basis for this assumption since it is more limiting than the existing Unit 2 shutdown margin requirement.

j.

A moderator density coefficient of 0.54 hk/gm/cc is assumed to support the relaxation of the most negative moderator temperature coefficient limit.

9144e:1d/091889 S-3.3-12

k.

Minimum capability for injection of boric acid (2400 ppm) solution corresponding to the most restrictive single failure in the safety injection system.

The Emergency Core Cooling System (ECCS) consists of the following systems:

1) the passive accumulators,
2) the low head safety injection (residual heat removal)
system,
3) the high head (intermediate head)- safety-injection
system, and 4) the charging safety injection system.

Only the charging safety injection system and the passive accumulators are modeled for the steam line break accident analysis.

The modeling of the safety injection system in LOFTRAN is described in Reference 2.

Figure 3.3-52 of WCAP-11902 presents the safety injection flow rates as a function of RCS pressure assumed in the

analysis, The flow corresponds to that delivered by one charging pump delivering its full flow to the cold legs.

The safety injection flows assumed in this analysis take into account the degradation of the ECCS charging pump performance.

No credit has been taken for any borated water that might exists in the injection lines, which must be swept from the lines downstream of the boron injection tank isolation valves prior to the delivery of boric acid to the reactor coolant loops.

For this analysis, a boron concentration of 0 ppm for the boron injection tank is assumed.

After the generation of the safety injection signal (appropriate delays for'nstrumentation, logic, and signal transport included),

the appropriate valves begin to operate and the safety injection charging pump starts.

ln 27 seconds, the valves are assumed to be in their final position (VCT charging pump suction valve has closed following opening of RHST charging pump suction valve) and the pump is assumed to be at full speed and to draw suction from the RHST.

The volume containing the low concentration borated water is swept into the core before the 2400 ppm borated water reaches the core.

This delay, described above, is inherently included in the modeling.

For the at-power cases, reactor trip is available by safety injection

signal, overpower protection signal (high neutron flux reactor trip or OPhT reactor trip), and low pressurizer pressure reactor trip signal.

9144e:1d/091889 S-3.3-13

m.

For reactor coolant pump (RCP) operation, offsite power is assumed available.

Continued operation of the reactor coolant pumps maximizes the energy transferred from the reactor coolant system to the steam generators.

n.

No steam generator tube plugging 'is assumed to maximize the heat transfer characteristics.

Single Failure Effects a.

Failure of a main steam isolation valve (HSIV) increases the volume of steam piping which is not isolated from the break.

When all valves

operate, the piping volume capable of blowing down is located between the steam generator and the first isolation valve.

If this valve fails, the volume between the break and the isolation valves in the other steamlines, including safety and relief valve headers and other connecting lines, will feed the break.

For the cases which modeled a

failure of a HSIV, the steamline volumes associated with Unit 2 were assumed since the volume available for blowdown for this scenario is greater than Unit 1.

for the cases which did not model a failure of a HSIV, the steamline volumes associated with Unit 1 were assumed since the volume available for blowdown for this scenario is greater than Unit 2.

b.

failure of a diesel generator would result in the loss of one containment safeguards train resulting in minimum heat removal capability.

c.

Failure of a feedwater isolation valve would result in additional inventory in the feedwater line which would not be isolated from the steam generator.

The mass in this volume can flash into steam and exit through the break.

For consistency with the FSAR steamline break mass/energy release analysis, all cases conservatively assumed failure of the feedwater isolation valve, which resulted in the additional inventory available for release through the steambreak and in higher than normal main feedwater flows.

9144e:1d/091889 S-3.3-14

'C

'ailure of the auxiliary feedwater runout control equipment would result in higher auxiliary feedwater flows entering the ste'am generator prior to re-alignment of the AFM system.

For cases where the runout control operates

properly, a bounding constant AFH flow of 670 gpm to the faulted steam generator was assumed.

This value was increased to 1325 gpm to simulate a'failure of the runout control.

Results The steamline break mass/energy releases inside containment were calculated to account for the range of conditions possible for the potential reratings of Unit 1 and Unit 2 and for the relaxation of certain plant parameters.

One set of mass/energy releases were calculated to bound the reratings for both Units incorporating the limiting steamline break protection design of Unit 1.

The analysis assumptions support relaxation of the most negative moderator temperature coefficient limit, degradation of the charging pump performance of e

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he Elhergency Core Cooling System, extension of the main steam isolation valve closure time, and relaxation of the minimum BIT boron concentration requirement.

Section S-3.4.2.1 presents the containment integrity evaluation for a main steamline break using the mass/energy releases calculated here.

As discussed in Section S-3.4.2.1, the limiting scenarios of the steambreak cases analyzed for the containment response evaluation were a break size of 4.6 ft occurring at 102'A power with a main steamline isolation fai lure for the double-ended rupture scenario and a break size of Oe86 ft occurring at 102/

power with an auxiliary feedwater runout protection failure for the split rupture scenario.

Table S-3.3-4 presents the mass/energy releases for these limiting steambreak cases of the containment response evaluation.

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l S-3.

3.6 REFERENCES

1.

Augustine,

0. B., and Cecchett,
0. L., "Reduced Temperature and Pressure Operation for Donald C.

Cook Nuclear Plant Unit 1 Licensing Report,"

MCAP-11902, October 1988.

2.

Burnett, T, M.. T., et al.,

"LOFTRAN Code Description," MCAP-7907-A, April 1, 1984.

3.

4, 5.

6.

Butler, J. C.,

and Love, 0.

S, "Steamline Break Mass/Energy Releases for Equipment Qualification Outside Containment,"

MCAP-10961, Rev.

1 (proprietary) and MCAP-11184 (nonproprietary),

October, 1985.

Hollingsworth, S. 0.,

and Mood, 0. C.,

"Reactor Core Response To Excessive Secondary Steam Releases,"

MCAP-9227, January 1978.

Land, R. E.,

"Mass and Energy Releases Following a Steam Line Rupture;"

MCAP-8860, September 1976.

"American Electric Power Service Corporation Donald C.

Cook Nuclear Plant Unit 1:

Safety Evaluation for Including Uncertainty Due to Operator Readability of Pressurizer Pressure Instrumentation,"

AEP"89-216, Letter from J.

C, Hoebel (M) to R. B, Bennett (AEPSC),

September 1989.

9144e:1d/091889 S-3.3-26

TABLE S-3.3-4

.STEAMLINE BREAK MASS/ENERGY RELEASES INSIOE CONTAINMENT 102'A POMER OER (4.6 FT')

BREAK FAILURE - MSIV TIME

~SEC 0.00 0.20 3.60 6.60 12.80 13.00 13.20 13.40 13.60 14.00 14.40 14.80 15.00 15.20 15.60 15.80 16.00 16.60 17.20 17.60 17.80 18.40 18.60 18.80 19.20 23.80 28.80 30.40, 36.. 40 39.20 50.70 57.20 106.20 109.20 111.20 118.20 125.20 136.20 602.70 MASS

~LBM/SEC 0.00 10430.00 6552.00 5612.00 4978.00 4913.00 4847.00 4781.00 4716.00 4587.00 4458.00 4332.00 4269.00 4206.00 4083.00 4022.00 3961.00 3782.00 3606.00 3492.00 3435.00 3268.00 3213.00 3158.00 3050.00 1876.00 1623.00 1575.00 1461.00 1431.00 1369.00 1356.00 1331.00 1331.00 1184.00 308,70 188.10 98.97 93.24 ENERGY BTU x 10'/SEC 0.0 1.250 7.883

6. 748 5.974 5.895 5.816 5.737 5.660 5.504 5,350

'5.198 5.123 5.047 4.899 4.826

4. 753 4.538 4.328 4.190 4.122 3.921 3.856 3.790 3.660 2.251 1.421 1.883 1.746 1.708 1.634 1.618 1.588 1.587 1.409 0.358 0.217 0.114 0.107 9144e:1d/092189 S"3.3-31

TABLE S-3.3-'4 (Cont'd)

STEAMLINE BREAK MASS/ENERGY RELEASES INSIOE CONTAINMENT 102'A POWER SPLIT (0.86 FT')

BREAK FAILURE - AUXILIARY FEEDWATER RUNOUT PROTECTION I

~'\\

TIME

~SEC 0.00 0.20 1.60 2.00 2.40 2.80 4.20 4.40 8.60 9.40 12.00 12.60 15.80

'8.00 21.40 22.60 23.60 23.80 25.00 32.00 32.20 33.80 42.00 42.60 43.20 43.80 44.40 55.20 67.20 80.20 82.20 96.20 98.70 118.20 124.20 282.70 285.20 290.20 292.70 297.70 302.70 320.20 MASS

~LBM/SEC 0.00 1394.00 1366.00 1358.00 1350.00 1342.00 1316.00 1312.00 1550.00 1575.00 1632.00 1638.00 1635.00 1618.00 1458.00 1400,00 1357.00 1349.00 1302.00 1103.00 1098.00 1064.00 928.70 920.80 913.10 905.70 898.40 799.10 732.60 691.30 686.60 662.50 659.50 645.70

- 643.60 633.20 633.10 615.00 579.70 556.60 490.40 304.70 ENERGY BTU x 10'/SEC 0.0000 1.6690 1.6370 1.6270 1.6170 1.6080 1.5770 1.5730 1.8540 1.8840 1.9500 1.9570 1.9530 1.9340 1.7460 1.6790 1.6280 1.6180 1.5630 1.3260

~

1.3210 1.2810 1.1180 1.1090 1.1000 1.0910 1.0820 0.9625 0.8823 0.8325 0.8269 0.7977 0.7941 0.7775 0.7749 0.7623

, 0.7622 0.7402 0.6977 0.6695 0.5896 0.3643 9144e:1d/092189 S-3.3-32

TABLE S-3.3-4 (Cont'd)

STEAMLINE BREAK MASS/ENERGY RELEASES INSIDE CONTAINMENT 102'/

POWER SPLIT (0.86 FT

)

BREAK FAILURE - AUXILIARYFEEOMATER RUNOUT PROTECTION TIME

~SEC 330.20 340.20 352.70 525.20 535.20 600.20 605.20 MASS

~LBM/SEC 238.70 206.50 190.20 181.90 182.00 182.10 190.70 ENERGY BTU x 10'/SEC 0.2845 0.2456 0.2259 0.2160 0.2160 0.2162 0.2258 9144e:id/092189 S"3.3-33

S-3.4.2. 1 Main Steamline Break (MSLB) Containment Integrity Introduction and Background An evaluation was performed to determine the impact of reduced temperature and pressure operation on the Donald C.

Cook Nuclear Plant Unit 1 Long-Term Main Steamline Break Containment Integrity analysis.

This evaluation is documented 9144e:1d/091889 S-3.4-1

i in Section 3.4.2 of MCAP-11902, "REDUCED TEMPERATURE AND PRESSURE OPERATION FOR DONALD C.

COOK NUCLEAR PLANT UNIT 1 LICENSING REPORT,"

and it was concluded that reduced temperature and pressure operation did not have an adverse impact on the analysis results and conclusions.

This Section documents the analysis performed for both Donald C.

Cook Nuclear Plant Units 1 5 2 to determine 'the-impact of the rerated conditions described in Section S-2.1 on Containment Integrity following a Hain Steamline Break.

A series of main steamline split and double-ended breaks were analyzed as a

part of the original licensing basis for Donald C.

Cook Nuclear Plant Unit 2

'o determine the most severe break condition for containment temperature and pressure response for this design basis event.

The analysis and evaluation are discussed in Reference 1.

These results documented in the FSAR show that the most limiting double-ended break was the 4.6 square foot break, occurring at 102% power with main steam isolation valve failure.

The most limiting split break was the 0.942 square foot break, occurring at 30'A power with the failure of auxiliary feedwater runout protection.

The calculated peak temperatures for these cases were 319.1'F and 328.1'F respectively.

Additional generic sensitivities discussed in Reference 2, illustrate that other smaller breaks were not limiting.

Purpose The purpose of the analysis documented in the following paragraphs's to demonstrate that the peak containment temperature resulting from a design basis main steamline break will not exceed the equipment qualification temperature criterion for Donald C.

Cook Nuclear Plants Units 1 and 2, at the rerated conditions.

The containment pressure response generated for the LOCA Containment Integrity analysis for the double-ended pump suction RCS break case (Reference

3) bounds the Hain Steamline Break containment pressure
response, and therefore is not a concern here.

This analysis assumes reduced safety injection flow, due to degradation of ECCS performance, closure of the RHR crosstie valves and the current containment heat sink information.

91440:1 1/091889 S-3.4-2

Analytical Assumptions The analysis performed for the Rerating Program is consistent with the Reference 1 analysis except for assumptions directly related to the rerating parameters.

The analytical effort provides bounding system calculations for both Units 1

& 2 at the rerated"plant conditions. described in Section S-2.1.

A spectrum of split breaks is analyzed at 0.86 ft,

102'A power; 0.908 ft,

2 2

70%%u power; 0.942 ft, 304 power and 0.4 ft, hot shutdown.

Double-ended 2

2 breaks of 1.4 ft and 4.6 ft are analyzed at power levels of 102%%u, 70%%u, 2

2 30%%u and zero power 1 eve ls.

The break sizes analyzed in the present analysis are based on the current FSAR analysis.

As in the FSAR analysis, loss of one containment safeguards train was also assumed for all the cases in addition to the single failure assumed in the mass and energy release calculations.

4 The following cases were analyzed for containment response:

A.

S lit break cases 1) 0.86 ft, 102%%u power, 2

2) 0.86 ft, 102% power, 2

3) 0.908 ft, 7% power, 2

4) 0.908 ft, 7(C power, 2

5) 0.942 ft, 30% power, 6) 0.942 ft, 3% power, 2

7) 0.40 ft, hot shutdown, 2

8) 0.40 ft, hot shutdown, 2

MSIV failure AFRP failure MSIV failure AFRP failure MSIV failure AFRP failure MSIV failure AFRP failure Note:

MSIV - Main Steam Isolation Valve AFRP " Auxiliary Feedwater Runout Protection 9144e:1d/091889 S-3.4-3

8.

Double-ended ru ture cases~

1) 4.6 ft, 2) 4.6 ft, 3) 4.6 ft, 4) 4.6 ft, 5) 46 ft, 6) 4.6 ft, 7) 1.4 ft, 8) 1.4 ft,

9) 1.4'ft,
10) 1.4 ft,
11) 1.4 ft, 1025 power, 102K power, 70li power, 70'A power, 30K power, hot shutdown, 1025 power, 102A power, 70'A power, 30'A power, hot shutdown, MSIV failure AFRP failure HSIV failure AFRP failure MSIV failure MSIV failure MSIV failure AFRP failure MSIV failure HSIV failure MSIV failure Note:

~The limiting 4.6 ft double-ended failure cases (1024 and 70'A power), with HSIV failure were analyzed with AFRP failure and found to be less limiting than the corpesponding MSIV failure cases.

Therefore only the most limiting 1.4 ft (102% power) was analyzed with AFRP failure.

The mass and energy releases to the containment as a result of the postulated accident are calculated using the LOFTRAN computer code (Reference 4).

The mass and energy releases are calculated using two different failures for.each case

namely,
1) failure of the auxiliary feedwater runout protection and
2) failure of the main steam isolation valve.

As in Reference',

no credit is taken for entrainment.

Section S-3.3.4.1 presents additional details regarding the calculation of the inside containment steamline break mass and energy releases.

The LOTIC-III computer code (Reference

5) is used to calculate the consequence of these releases, in particular the peak containment temperature.

The main steam line break containment integrity calculations are performed with an additional failure of one of the containment safeguards

trains, which results in minimum spray flow (this includes a 1% degradation in the spray pump flow).

where applicable, input data consistent with that of the LOCA containment integrity analysis (Reference

3) is used.

9144e:1d/091889 S-3.4"4

The total initial ice mass assumed is 2.11 x 10 lbs.

'The initial conditions in the containment are a temperature of 120 F in the lower and dead ended compartments, a temperature of 27'F in the ice condenser, and a temperature of 57'F in the upper compartment.

All volumes are at a

pressure of 0.8 psig and a relative humidity of 15K.

The refueling water storage tank (RNST) temperature is assumed to be 100'F.

spray pump flow of 1900 gpm to the upper compartment and 900 gpm to the lower compartment is assumed, at a temperature of 100'F.

The spray flow is initiated 45.0 seconds after the containment reaches the hi-hi pressure signal of 3.5 psig.

This setpoint includes instrument uncertainties.

Results The results of the analysis show that the maximum calculated containment temperature is 324.9'F for the 4.6 ft double ended rupture at 1025 of the full power.

The mass and energy calculations for this case are based on the main steam isolation valve failure.

The maximum containment temperature calculated for the limiting small split break (0.86 ft at 102% of full power ) is 324.4'F.

The auxiliary feedwater runout protection failure is a'ssumed for this case.

Table S-3.4-1 and Figures S-3.4"1 through S-3.4-4 show the results for the two limiting cases.

Comparison of these results to the current FSAR results with r'espect to the peak containment temperature indicates that the FSAR result was more limiting.

This is due to the lower mass and energy releases inside containment, calculated for the present analysis.

The peak temperature shown in the FSAR for the limiting split break case (0.86 ft at 1025 of full

~

~

~

power, with auxiliary feedwater runout protection failure) is higher than the l

9144e:1d/091889 S-3.4-5

~rq

resent case.

However, the FSAR results for the limiting double-ended rupture case (4.6 ft at 102K power, with main steam isolation valve failure) is lower than the present double-ended results.

A detailed study of the results shows that even though the mass and energy releases within containment are lower in both the present

cases, the double-ended break results in a higher temperature due to reduced flows from the lower compartment into the ice-condenser.

The peak occurs very early in the transient (within the first ten seconds).

At this early time the only heat removal systems that exist are the containment wall heat sinks and the heat flow between the compartments.

In the present

case, heat removal by the walls is better (due to more detailed modeling of the walls), but the heat flow from the lower compartment into the ice-condenser is lower (due to the lower initial temperature assumed in the ice-condenser and the upper compartment, which affects the driving force through the ice-condenser).

Conclusions The main steamline break containment integrity analysis has been performed consistent with the current licensing basis analysis and Donald C.

Cook Nuclear Plant Units 1

8 2 rerating program, considering the present plant operating conditions.

The results of this analysis are bounded by the curren't FSAR results.

This analysis therefore demonstrates that the containment heat removal systems function to rapidly reduce the containment pressure and temperature in the event of a main steamline break accident.

S-3.4.3 References 1.

Mestinghouse letter 8 NS-TN-1946, 9/20/78,

" American 'Electric Power, Projects Donald C, Cook Unit 2 (Docket 50-316)

Response

to Question 022.9".

2.

Mestinghouse letter PAEP-80-525, 3/10/80, "Response to NRC Question 022. 17 - AHP's steamline break analysis".

3.

MCAP-11908," Containment Integrity Analysis for Donald C.

Cook Nuclear Plant Units 1 and 2", July 1988.

4.

MCAP-7907-P-A (Proprietary),

"LOFTRAN Code Description", April 1984.

5.

MCAP-8354-P-A (Proprietary),

Supplement 2,

"Long Term Ice Condenser Containment Code - LOTIC"3 Code", february 1979.

9144e:1d/091889 S-3.4-7

TABLE S-3.4-1 MAIN STEAMLINE BREAKS Type of Break Oouble-Ended Rupture Spl it

,Break Break Size (FT ')

2 4.6 0.86 Type of Failure MSIV AFRP max ('

Time of Tmax (sec)

(psig)

Time of Pmax (sec) 324.9 6.39 8.62 14,01 324.4 50.72 7.24 50.72 Note:

MSIV - Main Steam Isolation Valve AFRP - Auxiliary Feedwater Runout Protection 9144e:1d/092189 S-3.4-8

neer Coeper tment 240.

5 200 0 180.

160.

140.

120.

Upper Coe(portment 100.

50.

100.

150.

200, 250.

500.

550.

400.

450.

500.

550.

600 T1NE (SEC)

CONPARTMEHT TEMPERATVRE Figure S-3,4 4.6 ft Double-Ended

Rupture, 102'A Power, HSIV Failure 2

S-3.4-9

I 9.0 g~ Cceper~t COSpOC t%0flt a.o 7.5 7.0 CL W

CC Vl CC 6.5 Ch ao 5.5 5.0 4.5 4.0 3.5 O.

50.

100.

150.

200.

250.

300.

350.

400.

450.

500-T1lIE (SEC)

COMPARTMENT PRES~RE Figure S-3.4 4.6 ft Double-Ended

Rupture, 102Ã Power, MSIV Failure 9144e:1d/061669 S"3.4"10

500.

250.

LU 200.

175.

150.

125.

100.

e Upper Coapartaent 50.

0.

100.

500.

600.

700 ~

TINE (SEC)

CONPNTNEMT TENPERATURE

'I Figure S-3.4 0.86 ft Split Break, 102'A Power, AFRP Failure 9144e:1d/081689 S-3.4"11

gppqr compartment 7.

~1~r C~rtmnt 6.

le gg 5.

cn

~A LaJ CC O

3.

2.

0.

100.

200.

300.

400.

500.

700.

TINE (SEC)

CONPARTMEHT PRESSURE Figure S-3.4 0.86 ft Split Break, 102% Power, AFRP Failure 9144e:1d/081689 S-3.4-12

ATTACHMENT 6 TO AEP'NRC'1071E FIGURE 3.3-52 AND JUSTIFICATION FOR PRESSURIZER LEVEL FROM WCAP 11902

WESTINGHOUSE CLASS III WCAP-11902 REDUCED TEMPERATURE AND PRESSURE OPERATION FOR DONALD C.

COOK NUCLEAR PLANT UNIT 1 LICENSING REPORT D. L. Cecchett D. B. Augustine October 1988 WESTINGHOUSE ELECTRIC CORPORATION Energy Systems Business Unit P.O.

Box 355 Pittsburgh, Pennsylvania 15230 7980e:1d/100588

~l

5N F)gure 3.3-52 Safety Lngection Flow Supplied by One Charg)ng Pump

ATTACHMENT 4 TO AEP:NRC:1120 ANALYSIS OF STEAM LINE BREAK CORE RESPONSE

S-3.3.4.13 Rupture of a Steam Pipe The rupture of a. steam pipe event was analyzed in Section 3.3.4.13 of HCAP-11902 to support the reduced temperature and pressure operation as well as to bound the range of conditions possible for the rerating of Unit 1.

Table S-3.3-3 presents the initial conditions assumed in the HCAP-11902 analysis.

The relaxation of the Technical Specification most negative moderator temperature coefficient refers to the core HTC limit in the unrodded configuration.

This MTC limit relaxati'on is incorporated into the steamline 9144a:1d/091889 S-3.3-22

break core response analysis.

The HCAP-11902 analysis assumed a negative moderator coefficient corresponding to the end-of-life rodded core with the most reactive RCCA in the fully withdrawn position.

The reactivity feedback assumption is adjusted to conservatively predict the return to power transient.

Verification is performed to show that the reactivity feedback employed in the analysis is conservative.

The analysis conservatively assumed the minimum capability for injection of boric acid solution corresponding to the most limiting single failure in the Emergency Core Cooling System (ECCS).

The analysis assumed that the safety injection flow was provided by one charging pump.

The analysis assumed degraded performance of the charging pump.

Figure 3,3-52 of WCAP-11902 presents the safety injection flow rates as a function of RCS pressure, which takes into account the degraded performance of this ECCS (charging pump) system.

The analysis also conservatively assumed a boron concentration of

~

~

~

0 ppm for the boron injection. tank (BIT).

As such, the analysis supports degradation of the charging pump performance and positions Unit 1 for relaxation of the minimum BIT boron concentration requirement.

The steamline break core response analysis assumed steamline,isolation to occur wjthin 11 seconds from receipt of the signal generated by high steam

, flow coincident with low steam pres'sure.

The 11 second delay is assumed to account for signal processing and electronic delay plus the closure time of the main steamline isolation valves (NSIV).

The analysis models only the total delay from the time the setpoint is reached until the time the MSIV is fully closed.

Although the HCAP-11902 analysis specified that a HSIV,closure time of 7 seconds was assumed, margin is available in the total delay time assumed to support an 8 second MSIV closure time.

The 8 second HSIV closure time represents an increase of 3 seconds from the existing Technical Specification limit (5 seconds).

As such, the HCAP-11902 steamline break core response analysis supports a relaxation'f the MSIV closure time requirement.

The HCAP-11902 steamline break core response analysis is performed at Hot Zero

~

~

~

~

~

~

~

~

~

~

~

Power, with a corresponding initial steam generator level at 33/ NRS.

Increasing the initial level to 44/

NRS insignificantly impacts the results of 4

9144 e:1d/091889 S-3.3-23

tr

the analysis.

Increasing the water level will not have an unacceptable effect on the minimum ONBR for the double-ended rupture (4.6 ft, 1.4 ft )

steamline break core response analysis.

This evaluation is based on sensitivity studies presented in HCAP-9227, "Reactor Core Response to Excessive Secondary Steam Releases" (Reference 4).

Although this report was not used in support of the HCAP"1'1902 analysis, the'conclusions presented are generic in nature and as such can be applied to Cook Unit 1.

Thus, the safety analysis and conclusions presented in Section 3.3.4.13 remain applicable for the parameters of the Unit 1 rerating.

ATTACHMENT 1 TO AEP'NRC'1107 REASONS AND 10 CFR 50.92 ANALYSES FOR CHANGES TO THE DONALD C.

COOK NUCLEAR PLANT UNITS 1 AND 2 TECHNICAL SPECIFICATIONS

L'

Attachment 1 to AEP:NRC:1107 Page 1

Introduction Many of the T/Ss applicable during Mode 6 refueling are vague and subject to interpretation.

Consequently, on the advice of our former Project Manager, and in an attempt to avoid any future confusion over the intent of the T/Ss, we are requesting the T/S changes presented in this submittal to clarify any ambiguities that may exist.

These changes may be categorized into four types:

Clarification of Mode 6

Clarification of Applicability of T/Ss Clarification of the Intent of T/Ss Changes to Reflect Industry Norms Clarification of Mode 6 - T S 1.4 T/S 1.4 defines operational mode as follows, "An OPERATIONAL MODE shall correspond to any one inclusive combination of core reactivity condition, power level and average reactor coolant temperature specified in Table 1,1."

In Table 1.1, Mode 6 refueling has a

footnote stating, "Reactor vessel head unbolted or removed and fuel in the vessel."

As such, when no fuel is in the vessel the plant is not in Mode 6, or any other mode.

Hence, conditions such as movement of irradiated fuel with no fuel assemblies in the reactor vessel are categorized as "other conditions specified for each specification,"

as discussed in T/S 3/4.0.1 and T/S 3/4.0.4.

The fact that both the statements, "At all times" and "All Modes" can be found in the applicability statements of the Cook Nuclear Plant's T/Ss supports this position.

Clearly there must be times when the units are not in a mode to necessitate the use of the phrase "At all times."

Consequently, to clarify the definition of operational mode we are proposing to modify T/S 1.4 as follows, "An OPERATIONAL MODE shall correspond to any one inclusive combination of core reactivity condition, power level and average reactor coolant temperature specified in Table 1.1 with fuel in the reactor vessel."

The phrase "with fuel in the reactor vessel" was taken from the most recent version of MERITS, and was verbally agreed to by the NRC in T/S improvement meetings.

Clarification of A licabilit of T Ss As a result of the proposed clarification of the definition of Mode 6 and change to the definition of operational

mode, we are proposing to add statements to the applicability section of numerous T/Ss that state conditions when the T/Ss are applicable, but the unit is not in a mode.

t V

'II II ff

Attachment 1 to AEP:NRC:1107 Page 2

T S 3.1.1.3 Bases 3 4.1.1.3 T/S 3,1.1.3 states the LCO for boron dilution.

Currently this LCO is only applicable when the units are in a mode.

We are proposing to add the following condition under APPLICABILITY, "During movement of irradiated fuel assemblies within containment."

When no fuel is in the reactor vessel, reactivity changes in the Reactor Coolant System are not a concern.

However, to ensure that the Reactor Coolant System is capable of responding to reactivity changes that may occur if/when irradiated fuel is inserted into the core as a result of an unanticipated event during fuel handling, this condition is being added.

The following statement is being added to Bases 3/4.1.1.3 for clarification, "When no fuel is in the reactor vessel, reactivity changes in the Reactor Coolant System are not a concern.

However, prior to any irradiated fuel being moved into containment the minimum flow rate shall be established."

We are also making a correction to the Unit 2 Bases of this

section, In AEP:NRC:0916W we requested that the minimum required Reactor Coolant System flow rate for dilution and Mode 6 operation be decreased from 3000 GPM to 2000 GPM.

This T/S change was issued on February 9,

1989.

While the change in flow.rate was made in both Unit 1 and Unit 2 T/Ss 3/4.1.1.3 and 3/4.9.8.1, and the Unit 1 Bases, it was inadvertently not made in the Unit 2 Bases.

Consequently, we would like to correct the 3000 GPM stated in Bases 3/4.1.1.3 to 2000 GPM.

I T Ss 3.1.2.1, 3.1.2.3 3.1.2.5 3.1

~ 2.7 Bases 3 4.1.2 The T/Ss in 3/4.1.2 address the Boration Systems.

Currently, T/Ss 3,1,2.1, 3.1.2.3, 3 '.2.5 and 3.2 '.7 are applicable during Modes 5 and 6.

We are proposing to add the following condition to the applicability of each, of these T/Ss, "During movement of fuel assemblies within containment."

As explained for the proposed change to T/S 3.1.1.3, this condition is being added to ensure that the Reactor Coolant System is capable of responding to reactivity changes that may result from an unanticipated fuel handling event requiring insertion of fuel into the vessel.

However, when no fuel is in the reactor vessel, reactivity changes in the Reactor Coolant System are not a concern.

4'h 4

C'>

Attachment 1 to AEP;NRC:1107 Page 3

The following statements are being added to Bases 3/4.1.2 for clarification:

"Negative reactivity control in the Reactor'oolant System is not a concern when no fuel is in the reactor vessel.

However, prior to any irradiated fuel being moved into containment the minimum flow paths shall be operable."

0 "The OPERABILITY of the boron injection system during Mode 6

ensures that this system is available for reactivity control.

When no fuel is in the vessel RCS reactivity is not a concern.

However, prior to any irradiated fuel being moved into containment the requirements of Specifications 3.1.1.3, 3.1.2,1, 3.1.2.3, 3.1.2.5, 3.1.2.7 shall be met."

T S 3 4.3.3.1 Table 3.3-6 Item 2 The following condition is being proposed to be added to the APPLICABILITYof Item 2 in T/S 3/4.3.3.1, Table 3.3-6, "Fuel in Containment'

The primary purpose of the Radiation Monitoring Instrumentation listed as Item 2 of Specification 3.3.3.1 is to detect abnormal levels of radiation in the containment building and to actuate equipment to minimize the release of radioactive material to the outside environment in the event of a fuel handling accident within the containment building.

Even with no fuel in the

vessel, they are needed if fuel is being transported, or is in the containment building for any reason.

While in a condition with no fuel in the containment building, the radiation monitoring instrumentation channels are not necessary.

This, as well as changes to'Action 22 of this table, are elaborated on in Bases 3/4.3.3.1.

The changes to Action 22 are discussed later in this submittal.

Since the page orientation of Table 3.3-6 has been changed all three pages of the table are being submitted.

T S 3.8.1.2 To ensure that the A.C. electrical power sources that may be needed to mitigate the consequences of a fuel handling accident are available, the following statements are being proposed to be added to the APPLICABILITYof T/S 3.8.1.2:

"During movement of irradiated fuel with no fuel assemblies in the reactor vessel.

During loaded crane operation over irradiated fuel assemblies with no fuel assemblies in the reactor vessel."

7 a

~ 4 0

Attachment 1 to AEP:NRC:1107 Page 4

In addition, we are requesting that the ACTION statement be modified to read as follows:

"With less than the above'minimum required A.C. electrical power sources OPERABLE, immediately suspend all operations involving CORE ALTERATIONS, positive reactivity changes,*

movement of irradiated fuel, or crane operation with loads over the fuel storage pool, until the minimum required A.C. electrical power sources are restored to OPERABLE status."

This change to the ACTION statement makes it more restrictive than the current ACTION statement.

The current ACTION statement does not require the suspension of movement of irradiated fuel, or crane operation with loads over the fuel storage pool.

T S 3.8.2.2 To ensure that the A.C. electrical busses that may be needed to mitigate the consequences of a fuel handling accident are available, the following statements are being added to the APPLICABILITYof T/S 3.8,2.2; "During movement of irradiated fuel with no fuel assemblies in the reactor vessel.

During loaded crane operation over irradiated fuel assemblies with no fuel assemblies in the reactor vessel."

The ACTION statement of this specification is also being changed to reflect these statements.

However, this is being addressed later in the submittal since the proposed change goes beyond reflecting the revised APPLICABILITYstatement.

T S 3.8.2.4 As in T/S 3.8.1,2 and T/S 3.8.2,2 the APPLICABILITYstatement is being changed to address movement of irradiated fuel and loaded crane operation as follows:

"During movement of irradiated fuel with no fuel assemblies in the reactor vessel.

During loaded crane operation over irradiated fuel assemblies with no fuel assemblies in the reactor vessel."

Ve are also proposing changes in the ACTION statement to reflect the revised APPLICABILITYstatement.

However, as in T/S 3.8.2.2, since we are proposing other changes as well to this ACTION statement these changes will be addressed later in this submittal,

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Attachment 1 to AEP:NRC:1107 Page 5

T S 3.9.8.1 Bases 3 4.9.8 T/S 3.9.8.1 states that, "At least one residual heat removal loop shall be in operation" and is applicable in Mode 6.

We are proposing to also make it applicable, "During movement of

'irradiated fuel within containment."

The requirement that at least one residual heat removal (RHR) loop be in operation ensures that (1) sufficient cooling capacity is available to remove decay heat and maintain the 0

water in t'e reactor pressure vessel below 140 F as required during Mode 6, and (2) sufficient coolant circulation is maintained through the reactor core to minimize the effect of a boron dilution incident and prevent boron stratification.

Likewise, we are proposing to make T/S 3.9.8.2 also applicable "During movement of irradiated fuel within containment."

T/S 3.9.8.2 currently states that, "Two independent Residual Heat

., Removal (RHR) loops shall be OPERABLE" and is applicable in, "MODE 6 when the water level above the top of-the reactor pressure vessel flange is less than 23 feet."

We present the justification for both proposed changes in Bases 3/4.9.8 as follows:

"When no fuel is in the vessel the residual heat removal system is not needed to remove decay heat.

However, prior to any irradiated fuel being moved into containment the provisions of Specification 3.9.8.1 and 3.9.8.2 shall be met."

Bases 3 4.9.1 We are proposing to add a statement to the Bases to emphasize that T/S 3.9.1 is not applicable when no fuel is in the vessel.

Zt reads as follows:

"When no fuel is in the vessel, maintaining the reactor subcritical and reactivity control in the water volume is not a concern."

Bases 3 4.9.2 When no fuel is in the vessel there is no need for neutron flux monitors.

For clarification and emphasis we are proposing to add the following statement to Bases 3/4.9.2, "When no fuel is in the vessel this is not a concern."

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Attachment 1 to AEP:NRC:1107 Page 6

T/S 3/4.9.9 states:

"The Containment Purge and Exhaust Isolation System shall be OPERABLE.

APPLICABILITY: During core alterations or movement of irradiated fuel within containment."

We are proposing to add to Bases 3/4.9.9, which addresses this T/S, the following statement for clarification and emphasis:

"When no irradiated fuel is in containment, a radiation hazard that potentially could have environmental consequences is impossible'."

Clarification of the Intent of T Ss The changes that are being proposed to these T/Ss are not intended to change the meaning of the existing T/Ss, but to clarify them.

The way these T/Ss are currently worded, they are subject to interpretations that may put an unreasonable burden on the plant without providing any additional safety.

Consequently, we are requesting these changes so that the T/Ss clearly state their intents T

S 3.3.3.1 Table 3.3-6 TABLE NOTATION ACTION 22 We are proposing to add the words, "and Specification 3.9.9 is applicable" to ACTION 22.

Specification 3.9.9 states:

"The Containment Purge and Isolation System shall be OPERABLE.

APPLICABILITY: During core alterations or movement of irradiated fuel within the containment."

The addition of this statement to Action 22 emphasizes that when core alterations or movement of irradiated fuel are not taking place the Containment Purge and Exhaust System is not required.

As previously stated, the primary purpose of the Radiation Monitoring Instrumentation listed as Item 2 is to detect abnormal levels of radiation in the containment building and to automatically isolate the Containment Purge and Exhaust valves.

However, when no fuel is present within the containment building, protection against a fuel handling accident is unnecessary.

Therefore the automatic isolation of the Containment Purge and Exhaust System is not required and the containment RMS Channels listed in Item 2 of Specification 3.3.3 '

are not required to be OPERABLE.

Attachment 1 to AEP:NRC:1107 Page 7

This T/S is further clarified by the addition of the following sentences to Bases 3/4.3.3.1:

"When the Containment Area, Particulate and Noble Gas Radiation Monitoring Instrumentation Channels detect an abnormally high radiation level they initiate containment isolation.

However, when no fuel is in containment it is highly unlikely for a radiation hazard that could potentially have environmental consequences to develop."

T S 3 4.4.7 Table 4.4-3 T/S 3.4.7 states the LCO as:

"The Reactor Coolant System chemistry shall be maintained within the limits specified in Table 3.4-1.

APPLICABILITY: At all times."

The SURVEILLANCE REQUIREMENTS of 4.4.7 state:-

"The Reactor Coolant System chemistry shall be determined to be within the limits by analysis of those parameters at the frequencies specified in Table 4.4-3."

We are proposing to modify TABLE 4.4-3 by making the ~ footnote read as follows:

"~Not required when the Reactor Coolant System is drained to half loop and RHR is removed from service."

The reason we are adding the words, "and RHR is removed from service" to this footnote is that when the Reactor Coolant System is at half loop and there is no forced circulation it is impossible to take a representative coolant sample.

Any sample that would be obtained would be impacted by the effects of settlement and stagnation.

However, we recognize the fact that T/S 3.4.7 requires that the Reactor Coolant System chemistry be maintained at all times.

Consequently, we address this in the paragraph being added to Bases 3/4.4.7.

It states:

"Since corrosion inhibitors are added to the reactor coolant, the threat of corrosion is minimized during this condition.

Since it is impossible to obtain a representative coolant sample when the Reactor Coolant System is drained to half loop and RHR removed from service, sampling is not required under these conditions.

However, prior to fuel being removed from or returned to the reactor vessel the Reactor Coolant chemistry shall be determined to be within the limits by analysis of those parameters specified in Table 3.4-1."

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Attachment 1 to AEP:NRC:1107 Page 8

T S 3.7.2.1 This specification presently reads as follows:

"3.7.2.1 The temperature of both the primary and seconda~

coolants in the steam generators shall be greater than 70 F when the pressure of either coolant in the steam generator is greater than 200 psig.

APPLICABILITY: At all times."

The SURVEILLANCE REQUIREMENTS go on to state:

"The pressure in each side of the steam generator shall be determined to be less than 200 psig at least once per hour when the temperature of 0

ei.ther the primary or secondary coolant is less than 70 F."

When coolant pressure is low (less than 200 psig) it is impossible to get an accurate pressure measurement, although the operators intuitively know and engineering analysis can determine the approximate pressure.

However, accurate measurements can be taken when the pressure is greater than 200 psig.

Based upon this, we are also proposing to change the SURVEILLANCE REQUIREMENTS to read as follows:

"When temperature of either the primary or secondary coolants is less than 70 F, perform one of the following:

0 a.

Verify primary and secondary pressure is less than 200 psig hourly, b.

Verify controls are in place which prevent pressure from exceeding 200 psig on the primary and secondary side once per 12 hours1.388889e-4 days <br />0.00333 hours <br />1.984127e-5 weeks <br />4.566e-6 months <br />.

This proposed change makes the T/S more conservative since we are adding the SURVEILLANCE REQUIREMENT to verify that controls are in place.

In addition, we are writing out the mathematical symbols in this specification (), <<,

).

T S 3 4.9.8.1 We are proposing to add the following statement to ACTION a.:

"Immediately initiate a corrective action to return at least one residual heat'emoval loop to OPERABLE status as soon as possible."

Attachment 1 to AEP:NRC:1107 Page 9

It is intuitively obvious that if at least one residual heat removal loop is not available during the applicable operating conditions (Mode 6 and during movement of irradiated fuel within containment) that immediate corrective action should be taken.

This has been the position of Cook Nuclear Plant and is being added for clarification and emphasis.

Chan es to Reflect Indust Norms The purpose of the following T/S changes are to make Cook Nuclear Plant's T/Ss reflect the NRC's interpretations and the industry's standard T/Ss.

T S 3.1.2.3 Bases 3 4.1.2 and T S 3.4.9.3 Bases 3 4.4.9 We are proposing that T/S 3.1.2.3 ACTION b. be changed from:

"With more than one charging pump OPERABLE or with a safety injection pump(s)

OPERABLE when the temperature of any RCS cold leg is less than or equal to 170 F, unless the reactor vessel 0

head is removed, remove the additional charging pump(s) and the safety injection pump(s) motor circuit breakers from the electrical power circuit within one hour."

to:

"With more than one charging pump OPERABLE or with a safety injection pump(s)

OPERABLE when the temperature of any RCS cold leg is less than or equal to 170 F, unless the reactor vessel 0

head is not secured to the vessel, remove the additional charging pump(s) motor circuit breakers from the electrical power circuit within one hour."

Likewise we are proposing to change the APPLICABILITYof T/S 3 '.9.3 from "When the temperature of one or more of the RCS cold legs is less than or equal to 170 F, except when the reactor vessel head 0

is removed."

to:

"When the temperature of one or more of the RCS cold legs is less than or equal to 170 F, except when the reactor vessel head 0

is not secured to the vessel."

The justification for changing these statements from saying, "the reactor vessel head is removed" to, "the reactor vessel head is not secured to the vessel" is stated in the following paragraph which we propose to add to Bases 3/4.1.2 and Bases 3/4.4.9:

Attachment 1 to AEP:NRC:1107 Page 10 When the vessel head is not secured to the vessel, it is not a pressure barrier.

This includes times when the reactor vessel head without the studs is resting on the reactor vessel flange or when the studs are inserted resting on the "mailboxes."

(The mailboxes" are devices which prevent the studs from engaging the threads in the reactor vessel flange.)

The pressure required to lift the head off the reactor with the studs removed is 14.29 psig.

The pressure required to lift the head off the reactor with the added weight of the studs inserted resting on the mailboxes (approximately 38,000 lbs.) is 16.5 psig.

Both of these pressure values are significantly less than the lift setting specified by the T/S for the PORVs and the RHR safety valve.

As a result, cold ovezpressurization is not a concern if the reactor vessel head, without studs is gust lying on the vessel flange or if the reactor vessel head is lying on the vessel flange with the studs inserted resting on the mailboxes, T/S 3.1.2,3 and 3.4.9.3 are met in either case.

For the intent of meeting Action (b) of T/S 3.1.2.3, having either of the above conditions, i.e., the reactor vessle head with studs removed lying on the vessel flange or the reactor vessel head lying on the vessel flange with the studs inserted resting on the mailboxes, is equivalent to having the reactor vessel head removed.

This T/S clarification as it relates to T/S 3.4.9.3 was discussed with the NRC resident inspector, Mr.'B, Jorgensen..

Mr. Jorgensen was in agreement with our interpretation.

For T/S 3.1.2.3, our interpretation was discussed with Mr. David Passehl NRC resident inspector and he agreed with our interpretation.

T S 3.8.2.2 and T S 3.8.2.4 We are proposing to remove the existing ACTION statement from 3.8.2.2, which reads as follows:

"With less than the above complement of A.C. busses OPERABLE and energized, establish CONTAINMENT INTEGRITY within 8 hours9.259259e-5 days <br />0.00222 hours <br />1.322751e-5 weeks <br />3.044e-6 months <br />."

In its place, we are proposing to use the ACTION statement from the Westinghouse Standard Technical Specifications Revision 5, which reads as follows:

t "With less than the above minimum required A,C. electrical power sources OPERABLE, immediately suspend all operations involving CORE ALTERATIONS, positive reactivity changes, movement of irradiated fuel, or crane operation with loads over the fuel storage pool, and within 8 hours9.259259e-5 days <br />0.00222 hours <br />1.322751e-5 weeks <br />3.044e-6 months <br />, depressurize and vent the

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Attachment 1 to AEP:NRC:1107 Page 11 Reactor Coolant System through a greater than or equal to two square inch vent.

In addition, when in MODE 5 with the reactor coolant loops not filled, or in MODE 6 with the water level less than 23 feet above the reactor vessel flange, immediately initiate corrective action to restore the required sources to OPERABLE status as soon as possible."

Similarly, we are proposing to replace the ACTION of T/S 3.8.2.4, which reads as follows:

"With less than the above complement of D.C. equipment and bus OPERABLE, establish CONTAINMENT INTEGRITY within 8 hours9.259259e-5 days <br />0.00222 hours <br />1.322751e-5 weeks <br />3.044e-6 months <br />."

with:

"With the required battery banks and/or full-capacity charger inoperable, immediately suspend all operations involving CORE ALTERATIONS, positive reactivity changes, movement of irradiated fuel, or crane operation with loads over the fuel storage pool, initiate corrective action to restore the required battery bank and full-capacity charger to OPERABLE status as soon as

possible, and within 8 hours9.259259e-5 days <br />0.00222 hours <br />1.322751e-5 weeks <br />3.044e-6 months <br />, depressurize and vent the Reactor Coolant System through a greater than two square inch vent."

This statement is identical to that in the Westinghouse Standard Technical Specifications Revision 5, except that we added, "or crane operation with loads over the fuel storage pool."

The addition of this statement makes the proposed ACTION more conservative than that in the Standard T/Ss.

It is our position that the proposed ACTION statements enhance plant safety.

The current statements call for CONTAINMENT INTEGRITY, but do not require the activities that could possibly lead to a radiation accident to be halted, or that corrective actions be taken.

Establishing CONTAINMENT INTEGRITY causes major scheduling problems during an outage, and does not provide any significant safety benefit over the proposed ACTION.

Anal sis of Si nificant Hazards Per 10 CFR 50.92, a proposed amendment will not involve significant hazards consideration if the proposed amendment does not:

(1) involve a significant increase in the probability or consequences of a previously evaluated

accident, (2) create the possibility of a new or different kind of accident from any previously evaluated, or (3) involve a significant reduction in a margin of safety.

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Attachment 1 to AEP:NRC:1107 Page 12 Criterion 1 The proposed changes do not increase the probability or consequences of a previously evaluated accident.

Their intent is to provide clarification and remove ambiguities, and reflect NRC and industry interpretations and norms.

They do not affect the accident analysis.

Consequently, we believe that these changes do not increase the probability or consequences of a previously analyzed accident.

Criterion 2 The proposed changes do not create the possibility of a new or different kind of accident from any previously evaluated.

They do not require physical alteration of the plant or changes in parameters governing normal plant operation.

We therefore believe these changes do not create the possibility of a new or different kind of accident from any accident previously analyzed or evaluated.

Criterion 3 The proposed changes are consistent with NRC and industry interpretations and norms.

We therefore believe the proposed changes do not significantly reduce a margin of safety.

Lastly, we note that the Commission has provided guidance concerning the determination of significant hazards by providing certain examples (48 FR 14870) of amendments considered not likely to involve a significant hazards consideration.

The first of these examples refers to changes which are purely administrative.

Since the proposed changes are consistent with NRC and industry interpretations and norms, and are intended to provide clarification, we believe these changes fall,within the scope of this examples

ATTACHMENT 2 TO AEP:NRC:1107 PROPOSED REVISED LICENSE PAGES

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