ML18040A350

Forwards Response to NRC 980601 RAI Re GL 96-06 W/Regard to Water Hammer & two-phase Flow Assessments Associated w/post- Accident Operation of Drywell Air Coolers

ML18040A350
Person / Time
Site:	Nine Mile Point
Issue date:	08/28/1998
From:	Conway J NIAGARA MOHAWK POWER CORP.
To:	NRC OFFICE OF INFORMATION RESOURCES MANAGEMENT (IRM)
References
GL-96-06, GL-96-6, NMP1L-1353, TAC-M96836, TAC-M96837, NUDOCS 9809090009
Download: ML18040A350 (30)

Text

CATEGORY 1 REGULA'I Y INFORMATION DXSTRIBUTIO YSTEM (RIDS)

ACCESSION NBR:9809090009 DOC.DATE: 98/08/28 FACIL:50-220 Nine Mile Point Nuclear Station, 50-410 Nine Mile Point Nuclear Station, AUTH.NAME AUTHOR AFFILIATION CONWAY,J. T.

'iagara Mohawk Power Corp.

RECIP.NAME RECIPIENT AFFILIATION Records Management Branch

-NOTARIZED: NO Unit 1, Niagara Powe Unit 2, Niagara Moha (Document Control Desk)

DOCKET 05000220 05000410 NOTES:

It

'I RECIPIENT

• ID CODE/NAME PD1-1 PD RECIPIENT ID CODE/NAME NRR/WETZEL,B.

HOOD COPIES LTTR ENCL 1

1 COPIES LTTR ENCL 1::

1

SUBJECT:

Forwards response to NRC 980601 RAI re GL 96-06 w/regard to C

water hammer 6 two-phase flow assessments associated w/post-accident operation of drywell air coolers.

A DISTRIBUTION CODE: A072D COPIES RECEIVED:LTR ENCL SIZE:

T TITLE: GL 96-06, "Assurance of Equip Oprblty 8 Contain.Integ.

during Design E

6 INTERNAL:

NRR/DSSA/SCSB EXTERNAL:INOAC 1

1 1

1 1

1 NRR/DE/EMEB NRR/DSSA/SPLB 1

1 1

1 NRC PDR 1

1 NOTE TO ALL "RIDS" RECIPiENTS:

PLEASE HELP US TO REDUCE WASTE. TO HAVE YOUR NAME OR ORGANIZATION REMOVED FROM DISTRIBUTION LISTS OR REDUCE THE NUMBER OF COPIES RECEIVED BY YOU OR YOUR ORGANIZATION, CONTACT THE DOCUMENT CONTROL DESK (DCD)

ON EXTENSION 415-2083 TOTAL NUMBER OF COPIES REQUIRED:

LTTR 9

ENCL 9

~+*

4

,C

.Niagara Mohawk John T. Conway Vice President Nucfear Generation Office: (3t5) 349<2t3 Fax:

(3t5) 349-2605 August 28, 1998 NHP1L 1353 U. S. Nuclear Regulatory Commission Attn: Document Control Desk Washington, DC 20555 RE:

Nine MilePoint Unit 1 Docket No. 50-220 Nine MilePoint Unit 2 Docket No. 50-410

Subject:

Request forAdditional Information Regarding Generic Letter 96-06 Dated June I, 1998 Concerning Nine MilePoint Units I and 2 (TAC Nos. M96836

&M96837)

Gentlemen:

On February 7, 1997, Niagara Mohawk Power Corporation (NMPC) submitted to the NRC its response to Generic Letter 96-06 for Nine MilePoint Units 1 and 2 (NMP1 and NMP2). On December 16, 1997, NMPC revised the commitments made in that earlier response.

On June 1, 1998, the NRC forwarded a Request for Additional Information (RAI) to NMPC concerning NMPC's February 7, 1997, submittal.

The attachments to this letter provide the requested information with regard to water hammer and two-phase flow assessments associated with post-accident operation of drywell air coolers for NMP1 (Attachment 1) and NMP2 (Attachment 2).

Sincerely, xc:

980909000'9 980828 PDR ADOCK 05000220 P

PDR JTC/KLL/sc Attachments b

John T. Conwa e President Nuclear i r b

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Mr. H. J. Miller, NRC Regional Administrator Mr. S. S. Bajwa, Acting Director, Project Directorate I-l, NRR Mr. B. S. Norris, Senior Resident Inspector Mr. D. S. Hood, Senior Project Manager, NRR Records Management Nine Mile Point Nuclear Station, P.O. Box 63, Lycoming, New York 13093 www.nimo.corn

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NMP1 RESPONSE TO GL 96-06 RAI e uet 0

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Discuss specific system parameter requirements to be maintained to assure that water hammer willnot occur in the MCLCSystem (MCLCmakeup tank level requirements, temperature requirements, etc), and state the minimum margin to boiling that willexistfor the worst-case scenario, including consideration ofmeasurement and analytical uncertainties.

Describe and justIfy reliance on any non-safety related instrumentation and controlsfor assuring that water hammer willnot occur and explain whyitwould not be appropriate to establish Technical Specification requirements formaintaining these parameters.

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n The two key parameters for assuring that no water hammer occurs in Reactor Building Closed Loop Cooling (RBCLC) piping are (1) static head due to RBCLC fluid and (2) post-accident drywell temperature.

The static head is provided by a 2,000 gallon capacity makeup tank located in the Turbine Building at floor elevation 351'-0". Makeup to the tank is provided automatically from the Condensate Transfer System through a level control valve. The tank is also provided with a level indication and high/low level alarms in the Control Room. The normal tank level is maintained by the level control valve between 4 feet and 8 feet from the bottom ofthe tank. The tank low level alarm set point is 3 feet above the bottom ofthe tank. The level at which the saturation temperature ofRBCLC fluid at the highest point in the drywell would equal the conservatively assumed peak accident drywell temperature of281 degrees F is approximately 5 feet below the low level alarm set point. Peak drywell temperature based on a reconstituted analysis is about 270 degrees F. The water level in the makeup lines, at which a saturation temperature of270 degrees F willbe reached at the highest location ofRBCLC piping inside the drywell, is about 24 feet below the low level alarm set point. Due to the fact that a large margin exists, tank level measurement uncertainty was not explicitlyconsidered in determining the adequacy ofstatic head.

Drywelltemperature measurement or analytical uncertainty is not a factor in preventing water hammer because a conservatively high drywell peak temperature was assumed for the calculation ofsaturation pressure.

The actual analyzed temperature based on the reconstituted analysis is about 270 degrees F. The drywell temperature is at maximum only for a short duration and is below 250 degrees F within the first 100 seconds ofthe accident, and therefore, the bulk temperature ofthe RBCLC fluid inside the drywell is expected to be significantly less than the conservatively assumed peak drywell temperature.

Based on these facts, margin to boiling for RBCLC piping inside the drywell under post Loss ofCoolant Accident (LOCA) conditions, although not explicitly calculated, is considered to be substantial.

The tank level control and alarm instrumentation are non-safety related.

The tank level control valve fails open on loss ofair or power. Makeup to the Closed Loop Cooling (CLC) tank is provided by the Condensate Transfer pumps which are powered by power boards 161B and

171B. These power boards are supported by the diesel generators.

The Condensate Transfer pumps are automatically supplied power &om the diesel generators in less than 1 minute after a Loss ofOffsite Power (LOOP). Therefore, it is highly unlikely that the makeup to the RBCLC system willbe lost concurrent with the first few minutes ofinitiation ofa Design Basis Accident (DBA)LOCAevent when maximum post LOCAdrywell temperature is reached.

In the unlikely event that makeup is lost, disruption ofmakeup to the CLC tank for a few minutes after LOOP or loss ofmakeup to the CLC tank due to any other reason willnot immediately render the RBCLC system inoperable due to the lowRBCLC system makeup requirement.

Tank inventory ensures that sufBcient time is available to restore makeup to the CLC tank by operator actions based on the low tank level alarm response procedure.

The RBCLC system is not a NMP1 Technical Specification required system. None ofthe RBCLC System parameters have any Technical Specification limits and, since there is a substantial margin against boiling in RBCLC piping inside the drywell which could lead to water hammer, it is not considered necessary to establish Technical Specification limits forRBCLC system static head.

e ce.

o I o mation Question 2 is directed to Nine MilePoint Unit 2 (NMP2), and is not applicable to NMPI.

e uest ratio Implementing measures to assure that water hammer willnot occur, such as maintaining system static pressure orprohibitingpost-accident operation ofthe affected system, is an acceptable approach for addressing the water hammer concern.

However, allscenarios should be considered to assure that the vulnerability to water hammer has been eliminated.

Confirm that allscenarios have been considered, including those where the affected containment penetrati ons are not isolated (ifthis is a possibility), such that the measures that have been established are adequate toprevent the occurrence ofwater hammer during (andfollowing) allpostulated accident scenarios.

The NMP1 design does not include automatic isolation ofthe RBCLC from the diywell coolers on receipt ofa containment isolation signal. A single check valve is provided on the RBCLC supply to the drywell coolers and a motor-operated valve (MOV)is the isolation valve on the return line. As discussed in our 120-day response to Generic Letter (GL)96-06 dated February 7, 1997, the RBCLC containment isolation MOVs are normally open, and no procedure steps require their closure. Per the Response to NRC Question 1 above, prevention ofwater hammer in the drywell cooler piping is based on static pressure ofthe RBCLC fluid, not system isolation.

Rupture ofRBCLC piping, or another passive failure with the potential to result in rapid loss of RBCLC inventory, is not postulated concurrent with a DBAat NMP1. Therefore, consistent with the NMP1 Licensing Basis, no such scenario is considered with respect to GL 96-06 issues.

uest or n ati For those scenarios where the potentialfor two-phase flowhas not been eliminated, explain to what extent twophase flowconditions willexistfollowingaccident conditions and provide the followinginformation:

a.

Identify any computer codes that were used in the two-phase flo>v analyses and describe the methods used to bench mark the codes for the speci/Pc loading conditions involved (see Standard Review Plan Section 3.9.1).

Describe andjustify all assumptions and input parameters (including those used in any computer codes), and explain why the values selected give conservative results.

Also, providej ustij7cation for omitting any effects that may be relevant to the analysis (e.g.,

fluidstructure interaction, flowinduced vibration, erosion).

C.

Provide a detailed description ofthe "worst case" scenario for two-phase flow, taking into consideration the complete range ofevent possibilities, system conftgurations, parameters (e.g., temperatures, pressures, flow rates, load combinations), and component failures. Additional examples include:

the consequences ofsteam formation, transport, and accumulation; cavitation, resonance, and fatigue sects; and

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erosion considerations Licensees mayflnd MJREG!CR-6031, "Cavitation Guide for Control Valves, " helpful in addressing some aspects ofthe two-phase flowanalyses.

(Note: itis importantfor licensees to realize that in addition to heat transfer considerations, two-phase flowalso involves structural and system integrity concerns that should be addressed).

d.

Determine the uncertainty in the two-phase flowanalyses, explain how the uncertainty was determined, and how it was accounted forin the analyses to assure conservative results.

e.

Conftrm that the two-phase flowloading conditions do not exceed any design specifications or recommended service conditions for the piping system and components, including those stated by equipment vendors.

Confir that the system willcontinue to perform its design-basis functions as assumed in the safety analysis reportfor the facility, and that the containment isolation valves willremain operable.

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¹4 Because two-phase flowwith the potential for water hammer in the RBCLC drywell cooler piping is precluded, this question is N/Awith respect to NMP1.

Confirm that the water hammer and hvo-phase flowanalyses included a complete failure modes and effects analysis (IMEA)forall components (including electrical and pneumatic failures) that could impact performance ofthe Cooling Water System.

Also, confirm that the I'ME4is documented and available for review, or explain why a complete andfullydocumented SMEA was notperformed.

Because two-phase flowwith the potential for water hammer in the RBCLC drywell cooler piping is precluded, this question is N/Awith respect to NMP1.

e nest orln or iati Explain andj ustify where engineeringjudgment was usedin lieu ofcalculations in the analysis ofthe RBCLC System.

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The RBCLC System at NMP1 has two piping sections which penetrate the drywell as is discussed in the response to Issue 1A and 1B in the February 7, 1997, GL 96-06 response.

The RBCLC piping section which supplies the drywell coolers enters through penetration X-12B and exits through penetration X-13B. The RBCLC piping section which supplies the recirculation pump coolers enters through penetration X-157 and exits through penetration X-156. Both piping sections are considered safety related pressure boundaries since these piping sections are not isolated from the safety related loads under LOCAconditions. NMPC's GL 96-06 response addressed the potential for two-phase flowin both sections ofRBCLC piping.

The determination that no boiling would occur in RBCLC piping supplying water to the diywell coolers which could potentially lead to water hammer is based on straightforward comparison of piping elevations to determine the required static head required to maintain the saturation temperature above that ofthe peak drywell temperature due to a DBALOCA. This determination was based on analysis ofexisting configuration ofRBCLC piping and not on engineering judgment.

The evaluation ofthe potential for two-phase conditions in the RBCLC piping which supply cooling to the recirculation pump seals was considered as part ofthe two-phase flow evaluation.

The Station Blackout (SBO) Qualification testing ofthe NMP1 recirculation pump seals

determined that natural circulation and boiling heat transfer in the recirculation pump coolers provides significant cooling to the seals under loss ofRBCLC pump cooling to the seals.

The SBO testing ofthe seals was performed using a fullscale pump seal cooler mockup and the simulation ofthe RBCLC piping and RBCLC system head.

These SBO tests demonstrated that the boiling in the pump coolers remains localized and that adequate natural circulation flow develops to prevent any vapor void formation. Engineering judgment was applied to confirm that these tests were applicable to the LOCAconditions in two respects:

1) Natural circulation will develop in the RBCLC piping, and 2) The potential for localized two-phase conditions in the pump coolers did not lead to the potential for hydrodynamic loads. NMPC discussed the RBCLC recirculation seal cooler piping and the potential for two-phase conditions in the piping post-LOCAfor completeness because ofthe NMP1 specific RBCLC piping system interrelationship.

Provide a simplifieddiagram ofthe affected Cooling 8'ater Systems showing major components, active components, relative elevations, lengths ofpiping runs, and the location ofany orifices andflowrestri ctions.

The attached sketch provides all the requested information except lengths ofpiping runs.

Complexity ofRBCLC piping inside the drywell does not allow inclusion ofpiping lengths in the simplified sketch. Piping isometrics can be provided ifmore detail than shown on the simplified sketch is desired.

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o Mtio Describe in detail any modifications that have been made (orwillbe made) to system design or operating requirements to resolve the water hammer and two-phase flowissues.

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'Since there is no potential for water hammer in the drywell coolers or in the RBCLC piping supplying cooling water to the drywell coolers due to two-phase flow, and since the heat removal function ofthe RBCLC System is not credited for post LOCAdecay heat removal, no modifications were required for resolution ofwater hammer and two-phase concerns.

Furthermore, RBCLC return piping from the drywell, beyond the drywell penetrations, was also reviewed for two-phase flow concerns.

An engineering assessment has been performed which demonstrates that the process fluid temperature willremain below the saturation temperature in the piping outside the drywell, therefore, no modifications were required for the RBCLC piping outside the drywell.

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NVIP2 RESPONSE TO GL 96-06 RAI Question I is directed to Nine Mile Point Unit 1 (NMPl), and is not applicable to NMP2.

For the small break scenario, describe the minimum time required for operators to initiate RBCLCflowin order to prevent steam formation, and explain how this action willbe assured.

Although the EOPs have been revised to eliminate the potential for water hammer following a large break loss ofcoolant accident, explain how water hammer willbe avoided after drywell temperature drops below 250 degrees F (steam pockets that have been formed are not expected to dissipate very readily).

This question consists of two parts: (a) what is the minimum response time for small breaks; (b) how is water hamme'r precluded ifdrywell temperature exceeds 250 degrees F, then goes back below 250 degrees F'l ao As stated in our February 7, 1997 response, the heat removal capability of the drywell coolers is not required nor credited in any post-accident mitigation scenario.

The automatic isolation of the RBCLC System containment isolation valves prevents boiling during all design basis accidents by maintaining the isolated segment above the saturation pressure.

This is described in detail in the February 7, 1997 response.

The system is susceptible to boiling only after the isolation signal is manually defeated.

As such, post-accident Operator initiation ofRBCLC flow is not required to prevent steam formation in the piping network.

Steam formation and subsequent water hammer are prevented by restricting the operation of the system during conditions that may induce boiling in the piping network.

Initiation of the RBCLC coolers is symptom-based as a function of drywell temperature.

The administrative limitof 250 degrees F ensures the system is not operated during conditions conducive to boiling. Itis not expected nor required that the isolation interlocks be defeated to support operation of the RBCLC coolers for medium to large break scenarios.

The system can be initiated during small break scenarios where the drywell temperature increases at a slower rate.

Again, system availability during this scenario is not required and has not been credited in the plant design.

b. 4 to procedure N2-EOP-6 defines the conditions in which the LOCA 1

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isolation signal may be defeated for the RBCLC drywell cooler containment isolation valves (2CCP*MOV265, 2CCP*MOV273, 2CCP*MOV122, 2CCP*MOV124). This procedure has been revised to preclude reopening of the containment isolation valves if the drywell temperature has exceeded 250 degrees F during the event, until an evaluation of drywell and RBCLC parameters concludes that water hammer willnot occur.

A Implementing measures to assure that water hammer willnot occur, such as maintaining system static pressure orprohibiting post-accident operation ofthe a+ected system, is an acceptable approach for addressing the water hammer concern.

However, all scenarios should be considered to assure that the vulnerability to water hammer has been eliminated.

Confirm that all scenarios have been considered, including those where the a+ected containment penetrations are not isolated (ifthis is a possibility) such that the measures that have been established are adequate to prevent the occurrence ofwater hammer during (and following) all postulated accident scenarios.

Isolation ofRBCLC from the drywell coolers is accomplished by MOVs 2CCP*MOV265 and 2CCP*MOV273 on the drywell cooler supply piping and 2CCP*MOV122 and 2CCP*MOV124 on the return piping.

Containment isolation is single failure proof, and would be achieved in the event of any LOCA/Main Steam Line Break (MSLB) resulting in high drywell pressure or low reactor water level. EOP restrictions on defeating the isolation signal are symptom-based, and are not specific to any scenario.

Scenarios involving breaks with insufficient energy release to generate a LOCA isolation signal would not result in water hammer, as described below in the response to Question 6. The combination of a single failure proof isolation scheme and symptom-based EOP guidance covers any postulated scenarios with respect to preventing water hammer in the RBCLC drywell cooler piping.

For those scenarios where the potentialfor two-phase flowhas not been eliminated, explain to what extent two-phase flowconditions willexistfollowing accident conditions and provide the followinginformation:

a.

Identify any computer codes that were used in the two-phase flowanalyses and describe the methods used to bench mark the codes for the specific loading conditions involved (see Standard Review Plan Section 3.9.1).

b.

Describe andjustify all assumptions and input parameters (including those used in any computer codes), and explain why the values selected give conservative results.

Also, providejustijicationfor omitiing any effects that may be relevant to the analysis (e.g.,

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fluidstructure interaction, flowinduced vibration, erosion).

l Provide a detailed description ofthe "worst case" scenario for two-phase flow, taking into consideration the complete range ofevent possibilities, system configuration, parameters (e.g., temperatures, pressures, flowrates, load combinations), and component failures. Additional examples include:

the consequences ofsteam formation, transport, and accumulation; cavitation, resonance, and fatigue sects; and

~

erosion considerations Licensees mayjind NUREGICR-6031, "Cavitation Guide for Control Valves, " helpful in addressing some aspects ofthe two-phase flowanalyses.

(Note: it is importantfor licensees to realize that in addition to heat transfer considerations, two-phase flowalso involves structural and system integrity concerns that should be addressed).

d.

Determine the uncertainty in the two-phase flow analyses, explain how the uncertainty was determined, and how it was accounted forin the analyses to assure conservative results.

e.

Confirm that the two-phase flowloading conditions do not exceed any design spectflcations or recommended service conditions for the piping system and components, including those stated by equipment vendors.

Confir that the system willcontinue to perform its design-basis functions as assumed in the safety analysis reportfor the facility, and that the containment isolation valves willremain operable, As discussed in our February 7, 1997 response and further clarified in the response to Questions 2 and 3 above, two-phase flow and the resulting potential water hammer is precluded from occumng in the RBCLC drywell cooler piping. Therefore, Question 4 is not applicable to NMP2.

Conflrm that the water hammer and two-phase flow analyses included a complete failure modes and sects analysis (FMEA)for all components (including electrical and pneumatic failures) that could impact performance ofthe cooling water system.

Also, confir that the FMEAis documented and available for review, or explain why a complete and fullydocumented FMEA was not performed.

Question 5 is not applicable to NMP2 because two-phase flow with potential for water hammer is precluded.

Explain andjustify where engineering judgement was used in lieu ofcalculations in the analysis ofthe RBCLC system.

The temperature limitestablished to preclude boiling in the RBCLC coolers is based on pressure considerations established in design calculations.

The discussion in the response to Question 2, regarding breaks which do not result in a LOCA isolation signal, is not based on

. any calculations performed specifically to address Generic Letter 96-06 concerns.

The judgment that such breaks would not result in steam formation in the RBCLC piping is based on a qualitative assessment of existing accident response models, considering the temperature and pressure input from design calculations.

One of the diverse means of automatic initiation of the LOCA isolation function is the drywell pressure - high signal, which has a set point limitof (1.68 psig (16.38 psia) and an allowable value of < 1.88 psig (16.58 psia), per Technical Specification Table 3.3.2-2.

During normal plant operation, the drywell pressure must be maintained between 14.2 psia and 15.45 psia, and the maximum allowable drywell average temperature is 150 degrees F (per Technical Specifications 3.6.1.5 and 3.6.1.6, respectively).

With containment integrity intact in accordance with Technical Specification 3.6.1, a significant increase in drywell temperature would have a corresponding increase in drywell pressure, such that a temperature increase on the order of that required to induce boiling in the RBCLC piping (e.g., approximately 100 degrees F), without a high drywell pressure condition, is not credible, As described in NMP2 Updated Safety Analysis Report (USAR) Section 6C, Humphrey Concern 5.8 considered the possibility of high temperatures in the drywell without reaching the drywell pressure - high limit, due to drywell bypass leakage.

In response to this concern, a transient analysis was performed assuming the loss of all drywell coolers.

Based on normal heat loads and normal leakage from the RCS, the analysis concluded that the drywell high pressure signal would be generated in approximately one hour, and the maximum drywell temperature was predicted to be 204'degrees F. This analysis, though not performed specifically to address water hammer concerns, illustrates that the drywell pressure-high signal provides protection against high drywell temperatures in response to transients with relatively low energy release rates.

Provide 'a simplified diagram ofthe a+ected cooling water systems showing major components, active components, relative elevations, lengths ofpiping runs, and the location ofany oriflces and flowrestrictions.

The attached sketch provides all the requested information except lengths ofpiping runs.

Complexity of RBCLC piping inside the drywell does not allow inclusion ofpiping lengths in the simplified sketch.

Piping isometrics can be provided ifmore detail than shown on the simplified sketch is desired.

Describe in detail any modifications that have made (or willbe made) to system design or operating requirements to resolve the water hammer and two phase flowissues.

As described above in the response to Question 2, changes to procedure N2-EOP-6, 4, have been implemented to restrict defeating the LOCA isolation signal for the RBCLC drywell cooler containment isolation valves.

Specifically, a restriction has been added such that the isolation valves willnot be reopened to establish drywell cooling ifthe drywell temperature has exceeded 250'F during the event, unless an evaluation of drywell and RBCLC parameters concludes that water hammer willnot occur. No plant design modifications are required to prevent water hammer from occurring.

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