CPSES-200402431, License Amendment Request 04-011, Revision to Technical Specification (TS 3.3.3) Post Accident Monitoring Instrumentation and 3.6.8 Hydrogen Recombiners

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License Amendment Request 04-011, Revision to Technical Specification (TS 3.3.3) Post Accident Monitoring Instrumentation and 3.6.8 Hydrogen Recombiners
ML043070519
Person / Time
Site: Comanche Peak  Luminant icon.png
Issue date: 10/28/2004
From: Madden F
TXU Power
To:
Document Control Desk, Office of Nuclear Reactor Regulation
References
00236, CPSES-200402431, LAR 04-011, TXX-04167
Download: ML043070519 (111)


Text

A TXU 4"'

Power TXU Power Comanche Peak Steam Electric Station P.O. Box 1002 (EO1)

Glen Rose, TX 76043 Tel: 254 897 5209 Fax: 254 897 6652 mike.blevinsetxu.com Mike Blevins Senior Vice President &

Chief Nuclear Officer Ref: 1 OCFR5O.90 CPSES-200402431 Log # TXX-04167 File # 00236 October 28, 2004 U. S. Nuclear Regulatory Commission Attn: Document Control Desk Washington, DC 20555

SUBJECT:

COMANCHE PEAK STEAM ELECTRIC STATION (CPSES)

DOCKET NOS. 50-445 AND 50-446 LICENSE AMENDMENT REQUEST (LAR)04-011 REVISION TO TECHNICAL SPECIFICATION (TS 3.3.3) POST ACCIDENT MONITORING (PAM) INSTRUMENTATION AND 3.6.8 HYDROGEN RECOMBINERS Gentlemen:

Pursuant to 1 OCFR50.90, TXU Generation Company LP (TXU Power) hereby requests an amendment to the CPSES Unit I Operating License (NPF-87) and CPSES Unit 2 Operating License (NPF-89) by incorporating the attached change into the CPSES Unit 1 and 2 Technical Specifications. This change request applies to both units The proposed change will delete Technical Specification (TS) 3.6.8, "Hydrogen Recombiners," and references to the hydrogen monitors in TS 3.3.3, "Post Accident Monitoring (PAM) Instrumentation." The proposed TS changes support implementation of the revisions to 10 CFR 50.44, "Standards for Combustible Gas Control System in Light-Water-Cooled Power Reactors," that became effective on October 16, 2003. (The deletion of the requirements for the hydrogen recombiner and references to hydrogen monitors resulted in numbering and formatting changes to other TS, which were otherwise unaffected by this proposed amendment.)

A member of the STARS (Strategic Teaming and Resource Sharing) Alliance A,

2)\\

Callaway

  • Comanche Peak
  • Diablo Canyon
  • Palo Verde
  • Wolf Creek

TXX-04167 Page 2 of 3 provides a detailed description of the proposed changes, a safety analysis of the proposed changes, TXU Generation Company LP's determination that the proposed changes do not involve a significant hazard consideration, a regulatory analysis of the proposed changes and an environmental evaluation. Attachment 2 provides the affected Technical Specification pages marked-up to reflect the proposed changes. Attachment 3 provides proposed changes to the Technical Specification Bases for information only. These changes will be processed per CPSES site procedures. Attachment 4 provides retyped Technical Specification pages that incorporate the requested changes. Attachment 5 provides retyped Technical Specification Bases pages that incorporate the proposed changes. Attachment 6 provides preliminary marked-up pages of the Final Safety Analysis Report (for information only) to reflect the proposed changes to the FSAR.

TXU Generation Company LP requests approval of the proposed License Amendment by November 1, 2005, to be implemented within 120 days of the issuance of the license amendment. The approval date was administratively selected to allow for NRC review but the plant does not require this amendment to allow continued safe full power operations.

In accordance with IOCFR50.91(b), TXU Generation Company LP is providing the State of Texas with a copy of this proposed amendment.

This communication contains the following new commitment which will be completed as noted:

Commitment Number Commitment 27324 TXU Power has verified that a hydrogen monitoring system capable of diagnosing beyond design-basis accidents is installed at CPSES and is making a regulatory commitment to maintain that capability. The hydrogen monitors will be retained in the CPSES Final Safety Analysis Report (FSAR). This regulatory commitment will be implemented within 120 days of issuance of the license amendment.

TXX-04167 Page 3 of 3 Should you have any questions, please contact Mr. J. D. Seawright at (254) 897-0140.

I state under penalty of perjury that the foregoing is true and correct.

Executed on October 28, 2004.

Sincerely, TXU Generation Company LP By:

TXU Generation Management Company LLC, Its General Partner Mike Blevins By: ITL L

tr:7, Fred W. Madden Director, Regulatory Affairs jds Attachments 1.

2.

3.

4.

5.

6.

Description and Assessment Markup of Technical Specifications pages Markup of Technical Specifications Bases pages (for information)

Retyped Technical Specification Pages Retyped Technical Specification Bases Pages (for information)

Proposed FSAR changes (for information) c -

B. S. Mallett, Region IV W. D. Johnson, Region IV M. C. Thadani, NRR Resident Inspectors, CPSES Ms. Alice Rogers Bureau of Radiation Control Texas Department of Public Health 1100 West 49th Street Austin, Texas 78756-3189

ATTACHMENT 1 to TXX-04167 DESCRIPTION AND ASSESSMENT to TXX-04167 Page 1 of 4 LICENSEE'S EVALUATION

1.

DESCRIPTION

2.

PROPOSED CHANGE

3.

BACKGROUND

4.

TECHNICAL ANALYSIS

5.

REGULATORY SAFETY ANALYSIS 5.1.

No Significant Hazards Consideration 5.2 Applicable Regulatory Requirements/criteria

6.

ENVIRONMENTAL CONSIDERATION

7.

PRECEDENT

8.

REFERENCES to TXX-04167 Page 2 of 4

1.0 DESCRIPTION

By this letter, TXU Generation Company LP requests an amendment to the CPSES Unit 1 Operating License (NPF-87) and CPSES Unit 2 Operating License (NPF-89) by incorporating the attached change into the CPSES Unit 1 and 2 Technical Specifications. Proposed change LAR 04-011 deletes Technical Specification (TS) 3.6.8, "Hydrogen Recombiners," and references to the hydrogen monitors in TS 3.3.3, "Post Accident Monitoring (PAM) Instrumentation." The proposed TS changes support implementation of the revisions to 10 CFR 50.44, "Standards for Combustible Gas Control System in Light-Water-Cooled Power Reactors," that became effective on October 16, 2003. (The deletion of the requirements for the hydrogen recombiner and references to hydrogen monitors resulted in numbering and formatting changes to other TS, which were otherwise unaffected by this proposed amendment.)

The changes are consistent with Revision 1 of NRC-approved Industry/Technical Specification Task Force (TSTF) Standard Technical Specification Change Traveler, TSTF-447, "Elimination of Hydrogen Recombiners and Change to Hydrogen and Oxygen Monitors." The availability of this TS improvement was announced in the Federal Register on September 25, 2003 as part of the Consolidated Line Item Improvement Process (CLIIP).

The initial preliminary proposed FSAR changes are also included for information only (See ). These changes reflect that Regulatory Guide 1.7 no longer applies to CPSES, that the hydrogen recombiners no longer have a design function, and that calculations of hydrogen post-LOCA are no longer required. The changes also reflect the reduced requirements for the hydrogen monitors.

2.0 PROPOSED CHANGE

Consistent with the NRC-approved Revision 1 of TSTF-447, the proposed TS changes include:

TS 3.3.3, Condition C Note: Reference to Hydrogen Monitors Deleted TS 3.3.3, Condition D Inoperable Hydrogen Monitors Deleted SR 3.3.3.2 Sensor Module Calibration for Hydrogen Monitors Deleted Table 3.3.3-1 Item 11, Hydrogen Monitors Deleted TS 3.6.8 Hydrogen Recombiners Deleted (Other TS changes included in this application are limited to renumbering and formatting changes that resulted directly from the deletion of the above requirements related to hydrogen recombiners and hydrogen monitors.)

to TXX-04167 Page 3 of 4 As described in NRC-approved Revision 1 of TSTF-447, the changes to TS requirements (and associated renumbering of other TSs) result in changes to various TS Bases sections. Proposed changes to the TS Bases are provided for information only in Attachment 4. The TS Bases changes will be submitted with a future update in accordance with TS 5.5.14, "Technical Specifications Bases Control Program."

3.0 BACKGROUND

The background for this application is adequately addressed by the NRC Notice of Availability published on September 25, 2003 (68 FR 55416), TSTF-447, Revision 1, the documentation associated with the 10 CFR 50.44 rulemaking, and other related documents.

4.0 TECHNICAL ANALYSIS

TXU Power has reviewed the safety evaluation (SE) published on September 25,2003 (68 FR 55416), as part of the CLIIP Notice of Availability. This verification included a review of the NRC staffs SE, as well as the information provided to support TSTF-447, Revision 1. TXU Power has concluded that the justifications presented in the TSTF proposal and the SE prepared by the NRC staff are applicable to Comanche Peak Steam Electric Station (CPSES), Units 1 and 2, and justify this amendment for the incorporation of the changes to the CPSES TS.

4.1 Verification and Commitments As discussed in the model SE published in the Federal Register on September 25, 2003 (68 FR 55416), for this TS improvement, TXU Power is making the following verifications and regulatory commitments:

1. TXU Power has verified that a hydrogen monitoring system capable of diagnosing beyond design-basis accidents is installed at CPSES and is making a regulatory commitment to maintain that capability. The hydrogen monitors will be retained in the CPSES Final Safety Analysis Report (FSAR). This regulatory commitment will be implemented within 120 days of issuance of the license amendment.
2.

CPSES does not have an inerted containment.

5.0 REGULATORY SAFETY ANALYSIS 5.1 No Significant Hazards Consideration TXU Power has reviewed the proposed no significant hazards consideration determination published on September 25,2003 (68 FR 55416), as part of the CLIIP. TXU Power has concluded that the proposed determination presented in the notice is applicable to CPSES

Attachment I to TXX-04167 Page 4 of 4 Units I and 2 and the determination is hereby incorporated by reference to satisfy the requirement of 10 CFR 50.91(a).

5.2 Applicable Regulatory Requirements/Criteria The applicable regulatory requirements and guidance associated with this application are adequately addressed by the NRC Notice of Availability published on September 25, 2003 (68 FR 55416), TSTF-447, Revision 1, the documentation associated with the 10 CFR 50.44 rulemaking, and other related documents.

6.0 ENVIRONMENTAL CONSIDERATION

TXU Power has reviewed the environmental evaluation included in the model SE published on September 25, 2003 (68 FR 55416), as part of the CLIIP. TXU Power has concluded that the staff's finding's presented in that evaluation are applicable to CPSES and the evaluation is hereby incorporated by reference for this application.

7.0.

PRECEDENT This application is being made in accordance with the CLIIP. TXU Power is not proposing variations or deviations from the TS changes described in TSTF447, Revision 1, or the NRC staff's model SE published on September 25, 2003 (68 FR 55416).

8.0 REFERENCES

Federal Register Notice: Notice of Availability of Model Application Concerning Technical Specification Improvement to Eliminate Hydrogen Recombiner Requirement and Relax the Hydrogen and Oxygen Monitor Requirements for Light Water Reactors Using Consolidated Line Item Improvement Process, published September 25, 2003 (68 FR 55416).

ATTACHMENT 2 to TXX-04167 PROPOSED TECHNICAL SPECIFICATION CHANGES (MARK-UP)

Pages ii 3.3-36 3.3-37 3.3-38 3.3-39 3.6-22 3.6-23

TABLE OF CONTENTS (continued) 3.4 REACTOR COOLANT SYSTEM (RCS)...............................................

3.4-1 3.4.1 RCS Pressure, Temperature, and Flow Departure from Nucleate Boiling (DNB) Limits...............................................

3.4-1 3.4.2 RCS Minimum Temperature for Criticality...............................................

3.4-4 3.4.3 RCS Pressure and Temperature (PIT) Limits............................................... 3.4-5 3.4.4 RCS Loops - MODES 1 and 2...............................................

3.4-7 3.4.5 RCS Loops - MODE 3...............................................

3.4-8 3.4.6 RCS Loops - MODE 4...............................................

3.4-11 3.4.7 RCS Loops - MODE 5, Loops Filled...............................................

3.4-14 3.4.8 RCS Loops - MODE 5, Loops Not Filled...............................................

3.4-17 3.4.9 Pressurizer...............................................

3.4-19 3.4.10 Pressurizer Safety Valves...............................................

3.4-21 3.4.11 Pressurizer Power Operated Relief Valves (PORVs)..................................... 3.4-23 3.4.12 Low Temperature Overpressure Protection (LTOP) System.......................... 3.4-27 3.4.13 RCS Operational LEAKAGE...............................................

3.4-33 3.4.14 RCS Pressure Isolation Valve (PIV) Leakage............................................... 3.4-35 3.4.15 RCS Leakage Detection Instrumentation...............................................

3.4-40 3.4.16 RCS Specific Activity...............................................

3.4-44 3.5 EMERGENCY CORE COOLING SYSTEMS (ECCS)............................................ 3.5-1 3.5.1 Accumulators...............................................

3.5-1 3.5.2 ECCS - Operating...............................................

3.5-4 3.5.3 ECCS - Shutdown...............................................

3.5-8 3.5.4 Refueling Water Storage Tank (RWST)...............................................

3.5-10 3.5.5 Seal Injection Flow...............................................

3.5-12 3.6 CONTAINMENT SYSTEMS...............................................

3.6-1 3.6.1 Containment...............................................

3.6-1 3.6.2 Containment Air Locks...............................................

3.6-2 3.6.3 Containment Isolation Valves...............................................

3.6-7 3.6.4 Containment Pressure...............................................

3.6-16 3.6.5 Containment Air Temperature...............................................

3.6-17 3.6.6 Containment Spray System...............................................

3.6-18 3.6.7 Spray Additive System...............................................

3.6-20 3.6.8 Hydrogon Rocombinore...............................................

3.6 22 (continued)

COMANCHE PEAK - UNITS 1 AND 2 ii Amendment No. 44

PAM Instrumentation 3.3.3 ACTIONS (continued)

CONDITION REQUIRED ACTION COMPLETION TIME C.

NOTE C.1 Restore one channel to 7 days Not applicable to hydrogon OPERABLE status.

monitor channels.

One or more Functions with two required channels inoperable.

OR One required Thot channel and one required Core Exit Temperature channel inoperable.

OR One required TCOld channel and one required Steam Line Pressure channel for the associated loop inoperable.

D.

T-wo hydrogen monitor D.1 Restore one hydrogen 2 hours2.314815e-5 days <br />5.555556e-4 hours <br />3.306878e-6 weeks <br />7.61e-7 months <br /> chaRnRls inoperable.

monitor channel to OPERABLE status.

ED. Required Action and ED.1 Enter the Condition Immediately associated Completion referenced in Time of Condition C eo-Table 3.3.3-1 for the not met.

channel.

(continued)

COMANCHE PEAK - UNITS 1 AND 2 3.3-36 Amendment No. 464

PAM Instrumentation 3.3.3 ACTIONS (continued)

CONDITION REQUIRED ACTION COMPLETION TIME FE. As required by Required FE.1 Be in MODE 3.

6 hours6.944444e-5 days <br />0.00167 hours <br />9.920635e-6 weeks <br />2.283e-6 months <br /> Action ED.1 and referenced in AND Table 3.3.3-1.

FE.2 Be in MODE 4.

12 hours1.388889e-4 days <br />0.00333 hours <br />1.984127e-5 weeks <br />4.566e-6 months <br /> GF. As required by Required GF.1 Initiate action in Immediately Action ED.1 and accordance with referenced in Specification 5.6.8.

Table 3.3.3-1.

SURVEILLANCE REQUIREMENTS


NOTE----------------------------------------------------------------

SR 3.3.3.1 and SR 3.3.3.3 apply to each PAM instrumentation Function in Table 3.3.3-1.

SURVEILLANCE FREQUENCY SR 3.3.3.1 Perform CHANNEL CHECK for each required 31 days instrumentation channel that is normally energized.

SR 3.3.3.2 Deleted


NOTE Applicable to hydrogen monitor channels only.

Q2 days Perform a sensor module calibration.

SR 3.3.3.3 Perform CHANNEL CALIBRATION.

18 months COMANCHE PEAK - UNITS 1 AND 2 3.3-37 Amendment No. 64

PAM Instrumentation 3.3.3 Table 3.3.3-1 (page 1 of 2)

Post Accident Monitoring Instrumentation FUNCTION

1. Refueling Water Storage Tank Level
2.

Subcooling Monitors

3.

Reactor Coolant System (RCS) Hot Leg Temperature (Wide Range) (Tw)

4.

RCS Cold Leg Temperature (Wide Range)

(Tcdd)

5. RCS Pressure (Wide Range)
6. Reactor Vessel Water Level
7. Containment Sump Water Level (Wide Range)
8. Containment Pressure (Intermediate Range)
9. Steam Une Pressure
10. Containment Area Radiation (High Range)
11. Hydrogon MneitorDeleted
12. PressurizerWaterLevel
13. Steam Generator Water Level (Narrow Range)
14. Condensate Storage Tank Level REQUIRED CHANNELS 2

2 1 per loop 1 per loop 2

2(a) 2 2

2 per steam line 2

2(b) 2 2 per steam generator 2

CONDITION REFERENCED FROM REQUIRED ACTION D&.I FE FE FE FE FE GF FE FE GF F

FE FE FE (continued)

(a) A channel is eight sensors In a probe. A channel Is OPERABLE If four or more sensors, one or more in the upper section and three or more In the lower section, are OPERABLE.

(b) A channel consistr of two onomrs ner train. A channol is considorod OPERABLE if one Aron or In OPEPRABLE. Deleted COMANCHE PEAK - UNITS 1 AND 2 3.3-38 Amendment No. 64

PAM Instrumentation 3.3.3 Table 3.3.3-1 (page 2 of 2)

Post Accident Monitoring Instrumentation 15.

16.

17.

18.

19.

FUNCTION Core Exit Temperature - Quadrant 1 Core Exit Temperature - Quadrant 2 Core Exit Temperature - Quadrant 3 Core Exit Temperature - Quadrant 4 Auxiliary Feedwater Flow

a.

AFW Flow OR

b.

AFW Flow and Steam Generator Water Level (Wide Range)

REQUIRED CHANNELS 2(c) 2(c) 2(c) 2(c) 2 per steam generator 1 each per steam generator CONDITION REFERENCED FROM REQUIRED ACTION D&1 FE FE FE FE FE FE (c) A channel consists of two core exit thermocouples (CETs).

COMANCHE PEAK - UNITS 1 AND 2 3.3-39 Amendment No. r64

Hyd~e~eR ReGembinw&

U R^r 3.6 CONTAINMENT SYSTEMS 3.6.8 Hydrogen Rccombincrs a '% %

^

t^ n T. A A.

.I

..._..L

_A

.I__I Lf

_1_

-1 I-, I 1-L':.J v.b.v I WO nyaUrogn roFEiddfiUnHrE bsnad UD Il-I-tI.

ADDI Ir'A RllITV-

^R~nf'NM 1

-^. f3

.. I I.

AGT4QNS GONDITION REQUIRED ACTION COMPLETION TIME A. Ono hydrogon roombino A.1 RoStoro hydrogon 30 days 4^r~phl^

t^FeGembinRe t9 OPERABLE statu6.

B. Two hydrogon rocombinors B.1-Vorify by administmtivo 1 hour1.157407e-5 days <br />2.777778e-4 hours <br />1.653439e-6 weeks <br />3.805e-7 months <br /> iRperabe moanS that the hydrogen control function iS AN Dn Once per 12 hours1.388889e-4 days <br />0.00333 hours <br />1.984127e-5 weeks <br />4.566e-6 months <br /> theFeafteo AND

_.2 Rto one hyde R

7 days reGOmbiRne to OPERABLE 6tatus.

(3ontiNued)

COACEPEAK U

-NITS 1 AND 2 3.2 S2 A mnndmnet Ncl. 109 1109

HydFrgon RocombinorF 2.6.8 ACTIONS (continued)

CONDITION REQUIRED ACTION COMPLETION TIME C. RoquFrod Action and C.1 Be in MODE 3.

aSociatod Complption Time nret met SURVEILLANCE REQUIREMENTS SURVEILLANCE FRSQUENCY SP 3.6.8.1 Perform a system functional test for each hydrogon 48 months reGmbinor.

SR 3.6.8.2 Visual!lex n each hydFrogon ecomFbinr encRoSUre9 1 8 months and verify thee ie. noRe evidence f nrml conditions.

SR 3.6.8.3 Perform a resistance to ground test for each heator phase.

COMANCHE PE-AK U NITS; 1,AND 2 3.6232 Amendment No. 10-9

ATTACHMENT 3 to TXX-04167 PROPOSED TECHNICAL SPECIFICATION BASES CHANGES (MARK-UP)

(For Information Only)

Pages B 3.3-124 B 3.3-131 B 3.3-138 B 3.3-139 B 3.3-141 B 3.6-52 B 3.6-53 B 3.6-54 B 3.6-55 B 3.6-56 B 3.6-57 B 3.6-58

PAM Instrumentation B 3.3.3 BASES (continued)

BACKGROUND Determine whether other systems important to safety are (continued) performing their intended functions; Provide information to the operators that will enable them to determine the likelihood of a gross breach of the barriers to radioactivity release; and Provide information regarding the potential release of radioactive materials to allow for early indication of the need to initiate action necessary to protect the public, and to estimate the magnitude of any impending threat.

These variables are identified by the unit specific Regulatory Guide 1.97 analyses (Ref. 1). These analyses identify the unit specific Type A and non-Type A Category 1 variables and provide justification for deviating from the NRC proposed list of Category 1 variables.

The selected non-Type A Category 1 variables are Reactor Vessel Water Level, and Containment Area Radiation (High Range), aRd HydrogeR Monitors. These selected variables are considered essential to the operator for LOCA management. Non-Type A Category 1 variables that are not included are Neutron Flux, Containment Pressure (Wide Range),

Steam Generator Water Level (Wide Range), and Containment Isolation Valve Status. Although they are important variables, effectiveness of the operator response to a DBA would not be reduced because other variables provide sufficient in formation for operator response. Neutron Flux is not required since reactor coolant temperatures provide sufficient confirmation of subcriticality. Containment Pressure (WR) is not required since the Containment Pressure intermediate range exceeds the containment design pressure and would provide sufficient confirmation of peak containment pressure. Steam Generator Water Level (WR) is not required since the Steam Generator water level narrow range would provide sufficient confirmation of level. The Wide range level is included as an alternative to auxiliary feedwater flow. Containment Isolation Valve Status is not a CPSES Category 1 variable.

The specific instrument Functions listed in Table 3.3.3-1 are discussed in the LCO section.

(continued)

COMANCHE PEAK - UNITS 1 AND 2 B 3.3-1 24 Amendment Pie. 64 Revision

PAM Instrumentation B 3.3.3 BASES (continued)

LCO (continued)

9.

Main Steam Line Pressure (Steam Generator Pressure)

Main Steam Line Pressure (Steam Generator Pressure) is a Type A Category 1 variable for event diagnosis, natural circulation, and RCP trip criteria. It is also a Type B Category 1 variable for monitoring heat sink status tree. It is a variable for determining if a secondary pipe rupture has occurred. This indication is provided to aid the operator in the identification of the faulted steam generator and to verify natural circulation.

10.

Containment Area Radiation (Hiah Ranae)

Containment Area Radiation Level (High Range) is a Type E Category 1 variable used to determine if an adverse containment environment exists due to a high containment radiation level.

Containment Area Radiation is provided to monitor for the potential of significant radiation releases and to provide release assessment for use by operators in determining the need to invoke site emergency plans.

11.

NV-IFUpgO.'P.URRE:FoSelee~ie Hydrogne Monitoer-e ro Typoe 1 Catoor; 1 Yasiablos for hydrogon rocombinor oporatin. It is also a TPeo G Catog; 1 Yariablo fo detectiOn of potential broah Of Gcntainmont boendaSy. Hydo9gen onitors aro aprovided to detect high hydrgern conRontration conditionR that reprosont a potential for cOntainment broach from a hydrogeon oxploieR.

This Yariable is also important in Vorifying the adeauacy of mitigating actions.

12.

Pressurizer Water Level Pressurizer Water Level is Type A Category 1 variable for Si termination/reinitiation. It is also Type B Category 1 for monitoring RCS inventory status tree. Pressurizer Level is used to determine (continued)

COMANCHE PEAK - UNITS 1 AND 2 B 3.3-131

.Arnnndmwit bin 64 Re - -

vision

PAM Instrumentation B 3.3.3 BASES (continued)

ACTIONS C.1 (continued)

Continuous operation with two required channels inoperable in a Function is not acceptable because the alternate indications may not fully meet all performance qualification requirements applied to the PAM instrumentation. Therefore, requiring restoration of one inoperable channel of the Function limits the risk that the PAM Function will be in a degraded condition should an accident occur. Condition C is modified by a Note that eXGludec hydrogen monitoFr channele.

P4 Condition D applie6 whonetwo hydrogen monitor channels are inoporablo.

Required Action D.1 requires rFetoring one hydrogen monitor channol to OPERABLE statur vithin 72 hour8.333333e-4 days <br />0.02 hours <br />1.190476e-4 weeks <br />2.7396e-5 months <br />.

The 72 hour8.333333e-4 days <br />0.02 hours <br />1.190476e-4 weeks <br />2.7396e-5 months <br /> Complotion Time is reasonable based on the backup capability of the contingency sampling plan to monitor the hydrogon concentration for evaluation of core damage or other coro damago aecssesmnt capabilities available (e.g. core exit thormocouple6, containment radiation monitore) and to proFide information for operator decisions. Also, it is unlikely that a LOCA (which would cause co r

damage) would occur during this time.

26 ED.1 Condition ED applies when the Required Action and associated Completion Time of Condition C oF D-ae is not met. Required Action 9D.1 requires entering the appropriate Condition referenced in Table 3.3.3-1 for the channel immediately. The applicable Condition referenced in the Table is Function dependent. Each time an inoperable channel has not met any Required Action of Condition C e-Q, and the associated Completion Time has expired, Condition ED is entered for that channel and provides for transfer to the appropriate subsequent Condition.

(continued)

COMANCHE PEAK - UNITS 1 AND 2 B 3.3-1 38 Revision 26

PAM Instrumentation B 3.3.3 BASES (continued)

ACTIONS PE.1 and FE.2 (continued)

If the Required Action and associated Completion Time of Conditions C er-D ae is not met and Table 3.3.3-1 directs entry into Condition FE, the unit must be brought to a MODE where the requirements of this LCO do not apply. To achieve this status, the unit must be brought to at least MODE 3 within 6 hours6.944444e-5 days <br />0.00167 hours <br />9.920635e-6 weeks <br />2.283e-6 months <br /> and MODE 4 within 12 hours1.388889e-4 days <br />0.00333 hours <br />1.984127e-5 weeks <br />4.566e-6 months <br />.

The allowed Completion Times are reasonable, based on operating experience, to reach the required unit conditions from full power conditions in an orderly manner and without challenging unit systems.

GF.1 Alternate means of monitoring Reactor Vessel Water Level and Containment Area Radiation have been developed. These alternate means may be temporarily used if the normal PAM channel cannot be restored to OPERABLE status within the allotted time. If these alternate means are used, the Required Action is not to shut down the unit but rather to follow the directions of Specification 5.6.8, in the Administrative Controls section of the TS. The report provided to the NRC should discuss the alternate means used, describe the degree to which the alternate means are equivalent to the installed PAM channels, justify the areas in which they are not equivalent, and provide a schedule for restoring the normal PAM channels.

SURVEILLANCE A Note has been added to the SR Table to clarify that REQUIREMENTS SR 3.3.3.1 and SR 3.3.3.3 apply to each PAM instrumentation Function in Table 3.3.3-1. SR 3.3.3.2 applieo only to the hydrogen Mcntnu6d (continued)

COMANCHE PEAK - UNITS 1 AND 2 B 3.3-1 39 Amendment No. 64 Revision

PAM Instrumentation B 3.3.3 BASES (continued)

SURVEILLANCE SR 3.3.3.2 Deleted REQUIREMENTS (continued)

For the hydgen monitors, a senorr module calibmrtioR is perfotrmed overy 92 days. Tho calibration seoqueRn user, sample gas in acrGGdaneo Yith the manufacturer' recommendatiens and eorifies that the current calibration constants are contained in the iropro orr database. This SR is modified by a Neto indicating that this SR is nly applicable to tho hyrgon monritors. The Frequency is based on manufacturers recommendationes.

SR 3.3.3.3 A CHANNEL CALIBRATION is performed every 18 months, or approximately at every refueling. CHANNEL CALIBRATION is a complete check of the instrument loop, including the sensor. The test verifies that the channel responds to measured parameter with the necessary range and accuracy. The calibration method for neutron detectors is specified in the Bases of LCO 3.3.1, Reactor Trip System (RTS) Instrumentation." Whenever an RTD is replaced in Function 3 or 4, the next required CHANNEL CALIBRATION of the 19 RTDs is accomplished by an inplace cross calibration that compares other sensing elements with the recently installed element. Whenever a core exit thermocouple replaced in Functions 15 thru 18, the next required CHANNEL CALIBRATION of the core exit thermocouples is 9

accomplished by an in-place cross calibration that compares the other sensing elements with the recently installed sensing element.

The Frequency is based on operating experience and consistency with the typical industry refueling cycle. Containment Radiation Level (High Range) CHANNEL CALIBRATION may consist of an electronic calibration of the channel, not including the detector, for range decades above 1 OR/hr and a one point calibration check of the detector below 1 OR/hr with an installed or portable gamma source.

(continued)

COMANCHE PEAK - UNITS 1 AND 2 B 3.3-141 Revision,-

HydFegen -GeGembieF&

B 3.6 CONTAINMENT SYSTEMS 1B 3.6.8 HydFOgen ReOcombinors BACKGROUND The function of the hydrogen rocombiners is to oliminate the potontial breach of containmont duo to a hydrogen oxygen roaction.

Per 10 CFR 60.14, "Standards for Combustiblo Gas Control Systoms in Light Water Coolod RoactorvF (Rof. 1), and GDC 1t, GContainmont Atmosphoro Cleanup (Ref. 2), hydrogon rocombinors are required to reduce the hydFG*eron coRert{ation in the ontainRmnt follow*nga loss of coolant accident (LOCA). Tho recombinors accomplivh thi_

by roFemFbining hydrgeR and oxygen to form wate or.h var remains in containmont, thus oliminating any discharge to tho enVironment. The hydrogen rocombinors are menaually initiatedi soG flammable limits would not bo roachod until 6everal days aftor a Design Bjasis Accident (DBA.

Two, 1 00% Gapaci' indopenondet hydrogeln rormbinor systems ar provided. Each consistS of controls, lecatod in accGesible aroas outside con~taiRnment (Rof. 6), a poWer supply and a recombioRef.

Recombination is accomplished by hoating a hydrogen air mixture above 11 I90F. The rmsulting watFor vaporand discharge gases are cooled prior to discharge from the recombiner. A single recombinor is capable of nain;taiRRnn the hydrogen conr ntrRatioR in onRtaiRmenR below the 1.0 volume percent (vo) flammability limit. TP.o recombinors are provided to meet the requirement for redundancy ard indepe nn.

E-ch recmhbinor is poWered from a separate Engineered Safety Featuroe bus, and is provided with a separate powerFpainl and control panel.

I leiril vv.ttrrvrv GGIVIANGHS RE-AK UNITS 4 AND -

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H4ydrogen ReGcombinors B 3.6.8 BASES (continuod)

APPDDICABLEC The hyderogon roemhbinere provide for tho capabilit' Of controlling the SAFEY bulk hydrogon concentration in containmont to less than the lower ANALIYSES fla mmale cenconratioR of 4.0 W folloying a DBA. This control would provent a containment wido hydrogon burn, thus ensuring the pressure and temnporatur assumod i;n the aralyeo aro not exceodod. Tho limiting DB3A Felative to hydrogon genreation is a LOCA.

Hydrogen may accumulate in containment following a LOCA as a Fesult of:

a.

A metal 6team reaction between the zirconium fuel rod cladding and the reactor coola-nt;

b.

RadiGo4ic decomposGition Of Water iFn the Reactor Coolant SyStem (RCS) and the containment sump;

c.

Hydrogen in the RCS at the time of the LOCA (i.e., hydrogen dissolved in the reactor coolant and hydrogen ga, in the pressurizer vapor space); or

d.

Corrosion of metals exposed to containment Spray and Emergency Core Cooling System 6outiORs.

To evaluate the potential for hydFrogen acumulation in containment following a LOCA, the hydrogen generation as a function of time following the initiation of the accident is calrulated. Conserwative asumnptions recommended by Reference 3 are used to maximize the amount of hydGroen caIculated.

Based On the conserwative assumptions used to calculate the hydrenR concentration versus time after a LOCA, the hydrogen conc;e-ntration in the primary containment would reach 3.6 v/o about 3 days after the LOCA and 1.0 n ' about 3 days later if no rFecmbinrer Was functi;n;ng (Ref. 5).

Initiating the hydrogen rocembinoRe when the primary containmont hydrogeRn concen;traton reaches 3.6 v'o YAill maintain the hydrogern concentration in the primary containment below flammability limits.

(continued)

COMANCHE PEAK UNITS 1 AND 2-B 3.6 63 Amendment No. 61

Hy-dF9neRReGembiners B-3.6.8 APPLIGABIES The hydrogen roFmGbiners a-r designed 6uch that, vith the SAFETY consorvativoly calculated hydrogen gonoration rates discussod above, a ANALYSES

'^

Onbi~eF iS Gapable Of ijmitiRg the peak hy gR GGnoentoati (continued) in containment to loss than 1.0 v/o (Ref. 1). Tho Hydrogon Purgo System

s similarly designed ruch that one Of tMG edunrdant tranrs is an adoquato backup to the redundant hydrogen recombiners.

The hydrogen recombinores satisfy Criterion 3 of 1 OCFR60.36(c)(2)(ii).

LCO Tweo hydrogen recombinerS must be OPERABLE. This ensures operation of at least one hydrogen roombiinor in the event of a Worst Gaso sr ein atiefai!Ue-.

Operation with at least one hydrogen rocombinor ensures that the post ILOCA hydrogeRn concentration can be prseVented from exNeedin; the flammability-limit.

AD IGABILII In Mnd" 1 and

'W hdFroren rFecmbinereF6 are ire to oRntl the hydrogen concentration within containment bolow its flammabilit' limit of 1.0 We folloAing a LOCA, assuming a worst case single failur-.

In MODE 3 and 4, both the hydrogen production rate and the total hydrogen produced after a LOCA would be less than that calculated for the DnRA IOCA. Also, because of the limited time in there MODES, the probability of an accident requiring the hydrogen rocombiners is loGW.

Therefore, the hydrogen reoGmbinors are not required in MODE 3 or 4.

In MODES 6 and 6, the probability and conSequences of a LOCA are low, due to the pressure and temperature limitations in these MODES.

Therefore, hydrogen recombiners are not required in those MODES.

(continued)

COMANCHE PEAK UNITS 1 AND 2 B 3.6 61 Amendment No. 61

Hydrogen Recombinor^S B 3.6.8 BASES (continued)

ACTIONS With ono containment hydrogon rocombinre inop!rable,tho innop o rcmhbinr must be roStr4ed to OPERABLE ^tatur within 30 dayr. In this condition, the remaining OPERABLE hydrogon recO.mbiner is adequato to poor fRthe hydrogen conrol functon.-

Howevor, tho ovarall reliability i6 reducod because a single failure in tho OPERABLE roc^mhbinr could resUlt in roedueod hydFrogn cntrol capability. Tho 30 day Completion Time is based on tho availability of the other hydsrgen recombiner, tho small pbabili' of a LOCA ourri (that would generate an amount of hydrogen that exceeds tho flaFmmability limit), and the amount of time available aft.r a IOCA (should onGe occur for operator action to provent hydrogen accumulation from exceeding the liammabilit4 !i~mt 34 (cntinued)

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Hydrogen Rocombinorv B3 3.6.8 ACTIONS 8.1 and 8.2

-(GORtifiued)

With two hydrogon rocombiners inoperablo, tho ability to porform tho hydFrogon controlI functi-on via altornato capabilities must bo vYreified b adminiStrativo moans within 1 hour1.157407e-5 days <br />2.777778e-4 hours <br />1.653439e-6 weeks <br />3.805e-7 months <br />. The alternate hydrogen control capabilities aro providod by the containmnnt HydrogoR Purge System.

Tho 1 hour1.157407e-5 days <br />2.777778e-4 hours <br />1.653439e-6 weeks <br />3.805e-7 months <br /> Complotion Time allows a roasonablo poriod of timo to vorify that a lossr of hydrogon control functin doos not exist. In addition, tho altornato hydrogeAn control systom capability must bo vorifiod once por l hnurrs threaeForto ensre ;tS contiRued aailabil;ty. Both the initial vorification and all subsequent verifications may bo porformed as an ad9ninintotiye~ Ghe~lk by nexamnin~ 19-r 9F etheF intfrrnation to denteFRine tho availability of tho altomato hydrogon control systom. It doos not moan to porform tho SurFeillanres Rneedd to demonstr-ate OPERABIl IT of the alternate hydrogen control system. If the ability to perform the hydrogen control function is maintained, continued operation is permitted with two hydrogen recombinors inoperable for up to 7 days. Seven days is a reasonable time to allow tvw hydrogen recomnbiners to be inoperable because the hydrogen control function is maintained and because of the low probability of the occurrence of a LOCA that would generate hydrogen in the amounts capable of exceeding the flammability limit.

C.1 If the inoperable hydrogen recombiner(s) cannot be restored to OPERABLE status within the required Completion Time, the plant must be brought to a MODE in which the LCO does not apply. To achieve this status, the plant mrust be brought to at least MODE 3 Within 6 hours6.944444e-5 days <br />0.00167 hours <br />9.920635e-6 weeks <br />2.283e-6 months <br />. The Completion Time of 6 hours6.944444e-5 days <br />0.00167 hours <br />9.920635e-6 weeks <br />2.283e-6 months <br /> is reasonable, based on operating exriFene, to reach MODE 3 frm full poWer conditions iRn an orderly manner and without challenging plant systems.

(continued)

A COMAPIGHE PEAK UNITS 1 AND 2 13 M rb~

H-eYI6lon i1

Hydogeon ReoambinorS B 3.6.8 BASES (continued)

SURVEILLANCE SR 3.6.8.1 Performance of a systom functional tost for each hydrogon rocombiner ensuros tho recombiners aro operational and can attain and sustain the temperature necessary for hydrogen rocembination. In particulr, this SR verifios that tho minimum heator sheath tomporaturo increaces to 2 700°F in e D0 minutes. Aftor reaching 700°F, the power is incroased to maximusm pwoSr for approximately 2 minutes and power iS verified to be Operating experience has shown that these components usually pass the Surveillance when performed at the 18 month requency. Therefore, the FRequeRcy WaE concludod to be accoptablo !from a roliability Gtandpeint.

SR. 3.6.8.2 This SR eInsures there are no physical problems that ceuld affect recombiner operation. Since the recombinerS are mechanically passive, they are Rnt subject to mechanical failure. The only credible failure nvolves lOss EOf power, blockage of the internal flow, missile impact, etc.

A visual inspection is Sufficiont to deteFrmine abnormal conditions that could cause such faIlures (i.e., loose wigng or srtreur-al eonnec;tiRs, deposits of foreign materials, etc.). The 18 month Frequency for this SR was developed considering the incidence of hydrogen recombiners failing the SR in the past is low.

SRE 3.6.8.3 This SR., which is performed following the functional test of SR 3.6.8.1, require performrance9 of a rFesitance to grund test for each heater phase to ensure that there are no detectable grounds in any heater phase. This is accomplished by verifying that the resistance to ground for any heater phase is 2 10,000 ohms.

The 18 month FrequeAncy for this Surveillance was developed considering tho incidence of hydrogen recombiners failing the SR in the past is low.

(continued)

COMANNCHE PEAK UNITS 1 AND 2 B 3.6 57 Rvision 31

Hydrogen Recombinore 13 Q._

BASES (continued)

REFERENCES

1.

10 CFR 60.11.

2.

10 CER 60, Appendix A, GDC 11.

3.

Regulatory Guide 1.7, Revision 2.

1.

FSAR Section 6.2.5.

5.

FSAR Section 6.2.6A

6.

FSAR, Section !I.B.2

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ATTACHMENT 4 to TXX-04167 RETYPED TECHNICAL SPECIFICATION PAGES Pages ii 3.3-36 3.3-37 3.3-38 3.3-39

TABLE OF CONTENTS (continued) 3.4 REACTOR COOLANT SYSTEM (RCS)...............................................

3.4-1 3.4.1 RCS Pressure, Temperature, and Flow Departure from Nucleate Boiling (DNB) Limits...............................................

3.4-1 3.4.2 RCS Minimum Temperature for Criticality...............................................

3.4-4 3.4.3 RCS Pressure and Temperature (PIT) Limits............................................... 3.4-5 3.4.4 RCS Loops - MODES 1 and 2...............................................

3.4-7 3.4.5 RCS Loops - MODE 3...............................................

3.4-8 3.4.6 RCS Loops - MODE 4...............................................

3.4-11 3.4.7 RCS Loops - MODE 5, Loops Filled...............................................

3.4-14 3.4.8 RCS Loops - MODE 5, Loops Not Filled...............................................

3.4-17 3.4.9 Pressurizer...............................................

3.4-19 3.4.10 Pressurizer Safety Valves...............................................

3.4-21 3.4.11 Pressurizer Power Operated Relief Valves (PORVs)..................................... 3.4-23 3.4.12 Low Temperature Overpressure Protection (LTOP) System.......................... 3.4-27 3.4.13 RCS Operational LEAKAGE...............................................

3.4-33 3.4.14 RCS Pressure Isolation Valve (PIV) Leakage............................................... 3.4-35 3.4.15 RCS Leakage Detection Instrumentation...............................................

3.4-40 3.4.16 RCS Specific Activity...............................................

3.4-44 3.5 EMERGENCY CORE COOLING SYSTEMS (ECCS)............................................ 3.5-1 3.5.1 Accumulators...............................................

3.5-1 3.5.2 ECCS - Operating...............................................

3.5-4 3.5.3 ECCS - Shutdown...............................................

3.5-8 3.5.4 Refueling Water Storage Tank (RWST)...............................................

3.5-10 3.5.5 Seal Injection Flow...............................................

3.5-12 3.6 CONTAINMENT SYSTEMS...............................................

3.6-1 3.6.1 Containment...............................................

3.6-1 3.6.2 Containment Air Locks...............................................

3.6-2 3.6.3 Containment Isolation Valves...............................................

3.6-7 3.6.4 Containment Pressure...............................................

3.6-16 3.6.5 Containment Air Temperature...............................................

3.6-17 3.6.6 Containment Spray System...............................................

3.6-18 3.6.7 Spray Additive System...............................................

3.6-20 (continued)

COMANCHE PEAK - UNITS 1 AND 2 ii Amendment No. 94

PAM Instrumentation 3.3.3 ACTIONS (continued)

CONDITION REQUIRED ACTION COMPLETION TIME C.

One or more C.1 Restore one channel to 7 days Functions with two OPERABLE status.

required channels inoperable.

OR One required Tht channel and one required Core Exit Temperature channel inoperable.

OR One required TCod channel and one required Steam Line Pressure channel for the associated loop inoperable.

D.

Required Action and D.1 Enter the Condition Immediately associated Completion referenced in Time of Condition C not Table 3.3.3-1 for the met.

channel.

(continued)

COMANCHE PEAK - UNITS 1 AND 2 3.3-36 Amendment No. 6;4

PAM Instrumentation 3.3.3 ACTIONS (continued)

CONDITION REQUIRED ACTION COMPLETION TIME E.

As required by Required E.1 Be in MODE 3.

6 hours6.944444e-5 days <br />0.00167 hours <br />9.920635e-6 weeks <br />2.283e-6 months <br /> Action D.1 and referenced in Table 3.3.3-1.

AND E.2 Be in MODE 4.

12 hours1.388889e-4 days <br />0.00333 hours <br />1.984127e-5 weeks <br />4.566e-6 months <br /> F. As required by Required F.1 Initiate action in Immediately Action D.1 and referenced accordance with in Table 3.3.3-1.

Specification 5.6.8.

SURVEILLANCE REQUIREMENTS NOTE---------------------------------------------------------------

SR 3.3.3.1 and SR 3.3.3.3 apply to each PAM instrumentation Function in Table 3.3.3-1.

SURVEILLANCE FREQUENCY SR 3.3.3.1 Perform CHANNEL CHECK for each required 31 days instrumentation channel that is normally energized.

SR 3.3.3.2 Deleted SR 3.3.3.3 Perform CHANNEL CALIBRATION.

18 months i

I COMANCHE PEAK - UNITS 1 AND 2 3.3-37 Amendment No. 6;4

PAM Instrumentation 3.3.3 Table 3.3.3-1 (page 1 of 2)

Post Accident Monitoring Instrumentation FUNCTION

1. Refueling Water Storage Tank Level
2. Subcooling Monitors
3.

Reactor Coolant System (RCS) Hot Leg Temperature (Wide Range) (Tho)

4.

RCS Cold Leg Temperature (Wide Range)

(Tcdd)

5. RCS Pressure (Wide Range)
6. Reactor Vessel Water Level
7. Containment Sump Water Level (Wide Range)
8. Containment Pressure (Intermediate Range)
9. Steam Line Pressure
10. Containment Area Radiation (High Range)
11. Deleted
12. Pressurizer Water Level
13. Steam Generator Water Level (Narrow Range)
14. Condensate Storage Tank Level REQUIRED CHANNELS 2

2 1 per loop 1 per loop 2

2(a) 2 2

2 per steam line 2

2 2 per steam generator 2

CONDITION REFERENCED FROM REQUIRED ACTION D.1 E

E E

E E

F E

E E

F E

E E

(continued)

(a) A channel Is eight sensors in a probe. A channel is OPERABLE if four or more sensors, one or more in the upper section and three or more In the lower section, are OPERABLE.

(b) Deleted I

COMANCHE PEAK - UNITS 1 AND 2 3.3-38 Amendment No. 64

PAM Instrumentation 3.3.3 Table 3.3.3-1 (page 2 of 2)

Post Accident Monitoring Instrumentation CONDITION REFERENCED FROM 15.

16.

17.

18.

19.

FUNCTION Core Exit Temperature - Quadrant 1 Core Exit Temperature - Quadrant 2 Core Exit Temperature - Quadrant 3 Core Exit Temperature - Quadrant 4 Auxiliary Feedwater Flow

a.

AFW Flow OR

b.

AFW Flow and Steam Generator Water Level (Wide Range)

REQUIRED CHANNELS 2(c) 2(c) 2(c) 2(c) 2 per steam generator 1 each per steam generator CONDITION REFERENCED FROM REQUIRED ACTION D.1 E

E E

E E

E (c) A channel consists of two core exit thermocouples (CETs).

COMANCHE PEAK - UNITS 1 AND 2 3.3-39 Amendment No. 64

ATTACHMENT 5 to TXX-04167 RETYPED TECHNICAL SPECIFICATION BASES PAGES (For Information Only)

Pages B 3.3-124 B 3.3-131 B 3.3-138 B 3.3-139 B 3.3-141

PAM Instrumentation B 3.3.3 BASES (continued)

BACKGROUND Determine whether other systems important to safety are (continued) performing their intended functions; Provide information to the operators that will enable them to determine the likelihood of a gross breach of the barriers to radioactivity release; and Provide information regarding the potential release of radioactive materials to allow for early indication of the need to initiate action necessary to protect the public, and to estimate the magnitude of any impending threat.

These variables are identified by the unit specific Regulatory Guide 1.97 analyses (Ref. 1). These analyses identify the unit specific Type A and non-Type A Category 1 variables and provide justification for deviating from the NRC proposed list of Category 1 variables.

The selected non-Type A Category 1 variables are Reactor Vessel Water Level, and Containment Area Radiation (High Range) Monitors. These selected variables are considered essential to the operator for LOCA management. Non-Type A Category 1 variables that are not included are Neutron Flux, Containment Pressure (Wide Range), Steam Generator Water Level (Wide Range), and Containment Isolation Valve Status.

Although they are important variables, effectiveness of the operator response to a DBA would not be reduced because other variables provide sufficient in formation for operator response. Neutron Flux is not required since reactor coolant temperatures provide sufficient confirmation of subcriticality. Containment Pressure (WR) is not required since the Containment Pressure intermediate range exceeds the containment design pressure and would provide sufficient confirmation of peak containment pressure. Steam Generator Water Level (WR) is not required since the Steam Generator water level narrow range would provide sufficient confirmation of level. The Wide range level is included as an alternative to auxiliary feedwater flow. Containment Isolation Valve Status is not a CPSES Category 1 variable.

The specific instrument Functions listed in Table 3.3.3-1 are discussed in the LCO section.

(continued)

COMANCHE PEAK - UNITS 1 AND 2 B 3.3-124 Revision

PAM Instrumentation B 3.3.3 BASES (continued)

LCO

9.

Main Steam Line Pressure (Steam Generator Pressure)

(continued)

Main Steam Line Pressure (Steam Generator Pressure) is a Type A Category 1 variable for event diagnosis, natural circulation, and RCP trip criteria. It is also a Type B Category 1 variable for monitoring heat sink status tree. It is a variable for determining if a secondary pipe rupture has occurred. This indication is provided to aid the operator in the identification of the faulted steam generator and to verify natural circulation.

10.

Containment Area Radiation (Hiah Range)

Containment Area Radiation Level (High Range) is a Type E Category 1 variable used to determine if an adverse containment environment exists due to a high containment radiation level.

Containment Area Radiation is provided to monitor for the potential of significant radiation releases and to provide release assessment for use by operators in determining the need to invoke site emergency plans.

11.

Deleted

12.

Pressurizer Water Level Pressurizer Water Level is Type A Category 1 variable for SI termination/reinitiation. It is also Type B Category 1 for monitoring RCS inventory status tree. Pressurizer Level is used to determine (continued)

COMANCHE PEAK - UNITS 1 AND 2 B 3.3-1 31 Revision

PAM Instrumentation B 3.3.3 BASES (continued)

ACTIONS C.1 (continued)

Continuous operation with two required channels inoperable in a Function is not acceptable because the alternate indications may not fully meet all performance qualification requirements applied to the PAM instrumentation. Therefore, requiring restoration of one inoperable channel of the Function limits the risk that the PAM Function will be in a degraded condition should an accident occur.

D.1 Condition D applies when the Required Action and associated Completion Time of Condition C is not met. Required Action D.1 requires entering the appropriate Condition referenced in Table 3.3.3-1 for the channel immediately. The applicable Condition referenced in the Table is Function dependent. Each time an inoperable channel has not met any Required Action of Condition C, and the associated Completion Time has expired, Condition D is entered for that channel and provides for transfer to the appropriate subsequent Condition.

(continued)

COMANCHE PEAK - UNITS 1 AND 2 B 3.3-1 38 Revision

PAM Instrumentation B 3.3.3 BASES (continued)

ACTIONS E.1 and E.2 (continued)

If the Required Action and associated Completion Time of Condition C is not met and Table 3.3.3-1 directs entry into Condition E, the unit must be brought to a MODE where the requirements of this LCO do not apply. To achieve this status, the unit must be brought to at least MODE 3 within 6 hours6.944444e-5 days <br />0.00167 hours <br />9.920635e-6 weeks <br />2.283e-6 months <br /> and MODE 4 within 12 hours1.388889e-4 days <br />0.00333 hours <br />1.984127e-5 weeks <br />4.566e-6 months <br />.

The allowed Completion Times are reasonable, based on operating experience, to reach the required unit conditions from full power conditions in an orderly manner and without challenging unit systems.

F.1 Alternate means of monitoring Reactor Vessel Water Level and Containment Area Radiation have been developed. These alternate means may be temporarily used if the normal PAM channel cannot be restored to OPERABLE status within the allotted time. If these alternate means are used, the Required Action is not to shut down the unit but rather to follow the directions of Specification 5.6.8, in the Administrative Controls section of the TS. The report provided to the NRC should discuss the alternate means used, describe the degree to which the alternate means are equivalent to the installed PAM channels, justify the areas in which they are not equivalent, and provide a schedule for restoring the normal PAM channels.

SURVEILLANCE A Note has been added to the SR Table to clarify that REQUIREMENTS SR 3.3.3.1 and SR 3.3.3.3 apply to each PAM instrumentation Function in Table 3.3.3-1.

(continued)

COMANCHE PEAK - UNITS 1 AND 2 B 3.3-139 Revision

PAM Instrumentation B 3.3.3 BASES (continued)

SURVEILLANCE SR 3.3.3.2 REQUIREMENTS (continued)

Deleted SR 3.3.3.3 A CHANNEL CALIBRATION is performed every 18 months, or approximately at every refueling. CHANNEL CALIBRATION is a complete check of the instrument loop, including the sensor. The test verifies that the channel responds to measured parameter with the necessary range and accuracy. The calibration method for neutron detectors is specified in the Bases of LCO 3.3.1, 'Reactor Trip System (RTS) Instrumentation.

Whenever an RTD is replaced in Function 3 or 4, the next required CHANNEL CALIBRATION of the RTDs is accomplished by an inplace cross calibration that compares other sensing elements with the recently 19 installed element. Whenever a core exit thermocouple replaced in Functions 15 thru 18, the next required CHANNEL CALIBRATION of the core exit thermocouples is accomplished by an in-place cross calibration that compares the other sensing elements with the recently installed 9

sensing element. The Frequency is based on operating experience and consistency with the typical industry refueling cycle. Containment Radiation Level (High Range) CHANNEL CALIBRATION may consist of an electronic calibration of the channel, not including the detector, for range decades above 1bR/hr and a one point calibration check of the detector below 1 OR/hr with an installed or portable gamma source.

(continued)

COMANCHE PEAK - UNITS 1 AND 2 B 3.3-141 Revision

ATTACHMENT 6 to TXX-04167 PROPOSED FINAL SAFETY ANALYSIS REPORT CHANGES (For Information Only) to TXX-04167 Page I of 69 CPSES/FSAR 1.2.2.3.4 Containment Isolation System In the event of postulated accidents, the Containment Isolation System is designed to minimize the leakage of radioactive materials through fluid lines penetrating Containment.

This design objective is achieved by the use of double isolation barriers. The use of double isolation barriers ensures that no single failure of any active or passive component renders the Containment Isolation System partially or wholly inoperable. The isolation valves are checked regularly during normal unit operation and are designed to assume a fail-safe position.

The Containment Isolation System ensures that the offsite radiological consequences of a main steam line rupture or LOCA are within the guidelines of 10 CFR Part 100.

1.2.2.3.5 Combustible Gas Control Systems Two systems are provided to control the concentration of combustible gases in the Containment: the Hydrogen Recombiner System and the Hydrogen Purge System.

See Section 6.2.5 fiordetails. Thcl~dr^^^n-Rceombincr System eonsists oftwo redundant electrie hydrogen

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from the eontainfmeft atmosphere and to limit its eoncentration tc the leNels speeified in NRC-Regulatory Guide 1.7. The eleetrie hydrogen rcoenbiners rocivo air contaiing hlydrogen and induce a reaetion betwcen the hydrogen and theo eXgen present in air. The eontrols for the reeombincrs arc loeated eutside the -ontainmot in an area aeeessible after-a LOCA.

Wel ing as a supplefnentary-systefl for the hydro-egn r-eembiers-s, the Iydr-oegn Purgoe Systim is designed to provide an independent moans ofeentrelling the hydrrogen ecncentratlin in the Containment after a LOCA, in aeeerdanee With NRC R:gulatofr Guidc 1.7. This system purges tho eontainment atmospher-e through filtcrs which reduco radioa.tivc -rleases.

The Hydrgnt RTombiner_ SystA is desig nAd to withstand all loads assAeiatAd with nefal eperatiens and aeeident conditiens, including the SSE and the pr-essur a-ndi eoineidnt tempe-aTuora e f aLOC A. Pfrotetion nfromissil sis alse preided.

The hydrogen purgc system, rejuifeme s a nen safety system, is designed to meet seismie eategefry 1.2.2.3.6 Emergency Core Cooling System The ECCS, with active and passive subsystems, is designed to perform the following functions:

1.2-8 Amendment 97 February 1, 2001 to TXX-04167 Page 2 of 69 CPSES/FSAR Discussion Refer to Appendix IA(B).

Regulatory Guide 1.5 Assumptions Used for Evaluating Potential Radiological Consequences of a Steam Line Break Accident for Boiling Water Reactors Discussion This regulatory guide is not applicable to the CPSES.

Regulatory Guide 1.6 Independence Between Redundant Standby (Onsite) Power Sources and Between Their Distribution Systems Discussion Refer to Appendix IA(B).

Regulatory Guide 1.7 Control of Combustible Gas Concentrations in Containment Following a Loss of Coolant Accident A

Based on a revision to I OCFR50.44, Regulatory Guide 1.7 no longer applies to CPSES. See Section 6.2.5 for a description of Discussion combustable gas control.

CPSES utilizes the assumpticns of Revisicn 1 (976) of this guide in calculating the hydrogen contribution from the various nucilear steam supply system and other potential seurces as discussed in Scetion 6.2.5A.

Also refer to Appendix IA(B).

Regulatory Guide 1.8 Personnel Selection and Training Discussion Refer to Appendix I A(B).

Regulatory Guide 1.9 Selection of Diesel Generator Set Capacity for Standby Power Supplies Discussion Refer to Appendix I A(B).

IA(N)-3 Amendment 97 February 1, 2001 to TXX-04167 Page 3 of 69 CPSES/FSAR Regulatory Guide 1.4 Assumptions Used for Evaluating the Potential Radiological Consequences of a Loss of Coolant Accident for Pressurized Water Reactors.

Discussion The analysis of the radiological consequences of the loss-of-coolant accident presented in Section 15.6.5 complies with the requirements of Revision 2 (6/74) of this regulatory guide except that only gamma radiation contribution is taken into account in the determination of whole body exposures.

Regulatory Guide 1.5 Assumptions Used for Evaluating Potential Radiological Consequences of a Steam Line Break Accident for Boiling Water Reactors.

Discussion This regulatory guide is not applicable to the CPSES which has pressurized water reactor steam supply systems.

Regulatory Guide 1.6 Independence Between Redundant Standby (Onsite) Power Sources and Between Their Distribution Systems Discussion The CPSES design complies with the requirements of Safety Guide 6 (3/10/71). For details see Section 8.3.

Regulatory Guide 1.7 Control of Combustible Gas Concentrations in Containment Following a Loss of Coolant Accident Based on a revision to I OCFR50.44, Regulatory Guide 1.7 no longer applies to CPSES. See Section 6.2.5 for a description of Discussion combustable gas control.

The CPSES design of the hydregen r-eeembiner-s and Hlydr-egen Purge Systeff mooet the.4-)

h rourmnv tJgt o.ft Aio 2 (1 '-~ of~rArA, this wroltoArA n.id aAA s discussod in Sotio 6.2J r-equifemcens of Re,,,siein 2 (11,/78) ofthi3 r-egtlatet-y guide as discussed in Seetiin 6.2.5 with the following exeeptions andjustifications.

Part Ccc The QPSvES desig~n akecs c.;ccption to this r-egulatery position by, de elasiflviwg portions3 ef thc Hydrogen Purgc System (HPS) which contain filtcrs to seismic eategore II. This moAeans that the filter unit is net reAuirAd to bo funetional aftor a seismii eont but it mrlus remain in plaer. This is eensistInt with the aAcident se*naries pestulatrd at CPSES. A LOCA is nrt pesuated to c ur o cidon all with a sAismic eAn ft.

1A(B)-2 Amendment 97 February 1, 2001 to TXX-04167 Page 4 of 69 CPSESJFSAR Also refer to Appendi; l A(N) for further discussion.

Regulatorv Guide 1.8 Personnel Selection and Training Discussion Minimum qualifications of unit staffs, with the exception of licensed Senior Reactor Operators and Reactor Operators, will be in accordance with Regulatory Guide 1.8, Revision 2. Minimum qualifications for licensed Senior Reactor Operators and Reactor Operators will be in accordance with Regulatory Guide 1.8, Revision 3.

The training requirements of Regulatory Guide 1.8, Revision 2 have been superseded by the provisions of IOCFR parts 50 and 55.

Regulatory Guide 1.9 Selection of diesel Generator Set Capacity for Standby Power Supplies Discussion The CPSES Diesel generator sets comply with the requirements of Safety Guide 9 (3/10/71) with the following comment:

The voltage may dip below 75 percent of nominal voltage when the diesel generator breaker closes and energizes the two 2000/2666 kVA, 6.9 kV/480 V unit substation transformers supplied from each diesel generator. The dip is due to transformer magnetizing inrush current which exists for two to three cycles. The diesel generator sets are designed to recover to 80 percent of nominal voltage within 10 cycles for this transient. The effect on the first load groups (see Tables 8.3-1 and 8.3-2) therefore would be a maximum possible delay in motor starting of 12-13 cycles after closure of the diesel generator circuit breaker. However, the objective of the first load group and subsequent load groups is not affected. For details see Section 8.3.

Regulatory Guide 1.10 Mechanical (Cadweld) Splices in Reinforcing Bars of Category I Concrete Structures Discussion Testing and sampling of Mechanical (Cadweld) Splices in Reinforcing Bars of the CPSES Concrete Containment Structure complies with the requirements of Revision 1 (1/2/73) of this regulatory guide. For other seismic Category I concrete structures, the testing and sampling of Mechanical (Cadweld) splices complies with the requirements of this guide except that the location of all splices are not recorded and shown in as-built drawings.

Also refer to Section 3.8.

IA(B)-3 Amendment 99 to TXX-04167 Included for Page 5 of 69 CPSES/FSAR Infornation only ruptures in the primary coolant loop piping, as discussed in Section 3.6B.2.5. 1.

Implementation of this technology eliminates the need for primary coolant loop piping whip restraints and jet impingement barriers. Containment design, emergency core cooling and environmental qualification requirements are not influenced by this modification.

The system is protected from overpressure by means of pressure-relieving devices as required by applicable codes.

In conclusion, the RCS boundary has provisions for inspection, testing, and surveillance of critical areas to assess the structural and leaktight integrity (Scction 5.2). For the reactor vessel, a material surveillance program conforming to applicable codes is provided (Section 5.3).

3.1.2.6 Criterion 15 - Reactor Coolant System Design "The reactor coolant system and associated auxiliary, control, and protection systems shall be designed with sufficient margin to assure that the design conditions of the reactor coolant pressure boundary are not exceeded during'any condition-of normal operation, including anticipated operational occurrences [1]."

Discussion The design pressure and temperature for each component in the RCS and associated auxiliary, control, and protection systems are selected to be above the maximum coolant pressure and temperature under all normal and anticipated transient load conditions.

In addition, RCPB components achieve a large margin of safety by the use of proven American Society of Mechanical Engineers (ASME) materials and design codes, use of proven fabrication techniques, nondestructive shop testing, and of integrated hydrostatic testing of assembled components.

Chapter 5 discusses the RCS design.

3.1.2.7 Criterion 16 - Containment Design "Reactor containment and associated systems shall be provided to establish an essentially leak-tight barrier against the uncontrolled release of radioactivity to the envirohment and to assure that the containment design conditions important to safety are not exceeded for as long as postulated accident conditions require [1]."

Discussion A steel-lined, reinforced concrete containment structure encloses the entire RCS and is designed to withstand the pressures and temperatures resulting from a spectrum of postulated LOCAs and secondary system breaks.

3.1-8 Amendment 97 February 1, 2001 to TXX-04167 Page 6 of 69 CPSES/FSAR The Emergency Core Cooling System cools the reactor core and limits the release of radioactive materials to the environment.

Next, to ensure its integrity, the Containment Spray System and hydrogen removal system iere incorporated in the containment design.

RS 4 3 The Containment Spray System is designed to function after a LOCA to reduce the pressure inside the containment to near atmospheric pressure and to remove fission product activity from the containment atmosphere.

Thce hydfegen rcemeval system eonsists efhydfegen r-eeembiner-s designed to prcvcnft hydroegrn gas from r-eahing a eembustiblo concentfatien in the Gentaifmnet Building as specified in NRG Regflate' Guide 1.7, Centrel ef Combustible Gas Cnctentr-ations in the Containment Following a Loss of Coolant Accident.

Meorcovcr, the Hlydr-gen Purge System aets as a backup system for the hydrogen removal system. This system ean be used to periodically purge fractions of the Containmcnt Building atmosphere to the enviromeent tc reduee th eeoneentration of hydrogen gas to within the limits specified in NRC Regulateory Guidc 1.7.

To sum up, the Containment structure and ESF systems are designed to safely sustain internal and external environmental conditions that may reasonably be expected to occur during the life of the plant, including both short-and long-term effects following a LOCA (See Sections 6.2, 6.5, 15.6, and 3.8.1).

3.1.2.8 Criterion 17 - Electric Power Systems "An onsite electric power system and an offsite electric power system shall be provided to permit functioning of structures, systems, and components important to safety. The safety function for each system (assuming the other system is not functioning) shall be to provide sufficient capacity and capability to assure that (1) specified acceptable fuel design limits and design conditions of the reactor coolant pressure boundary are not exceeded as a result of anticipated operational occurrences, and (2) the core is cooled and containment integrity and other vital functions are maintained in the event of postulated accidents.

"The onsite electric power sources, including the batteries, and the onsite electrical distribution system, shall have sufficient independence, redundancy, and testability to perform their safety functions, assuming a single failure.

"Electric power from the transmission network to the onsite electric distribution system shall be supplied by two physically independent circuits (not necessarily on separate rights of way) designed and located so as to minimize to the extent practical the likelihood of their simultaneous failure under operating and postulated accident and environmental conditions. A switchyard common to both circuits is acceptable. Each of these circuits shall be designed to be available in sufficient time following a loss of all onsite alternating current power supplies and the other offsite electrical power circuit, to 3.1-9 Amendment 97 February 1, 2001 to TXX-04167 Page 7 of 69 CPSES/FSAR isolation valve before the spray nozzles. The delivery capability of the spray nozzles is tested periodically by blowing low pressure air through the nozzles and verifying the flow. The Containment Spray Systems are tested for operational sequence as close to the design as practical (see Section 6.2.2).

3.1.4.12 Criterion 41 - Containment Atmosphere Cleanup "Systems to control fission products, hydrogen, oxygen, and other substances which may be released into the reactor containment shall be provided as necessary to reduce, consistent with the functioning of other associated systems, the concentration and quantity of fission products released to the environment following postulated accidents, and to control the concentration of hydrogen or oxygen and other substances in the containment atmosphere following postulated accidents to assure that containment integrity is maintained.

"Each system shall have suitable redundancy in components and features, and suitable interconnections, leak detection, isolation, and containment capabilities to assure that for onsite electrical power system operation (assuming offsite power is not available) and for offsite electric power system operation (assuming onsite power is not available) its safety function can be accomplished, assuming a single failure [1]."

Discussion The Containment Spray System includes a chemical additive subsystem using a basic sodium hydroxide solution to enhance post-accident fission product removal efficiency as described in Section 6.5.2. The unit is equipped with two independent spray systems supplied from separate buses, as described in Chapter 8, and either system alone can provide the iodine removal capacity for which credit is taken as described in Section 15.6.

Post-accident combustible gas control is ensured by hydrogen recombiners located inside the Containment Building, and by a Hydrogen Purge System. Hydrcgen r-eombinres inzlude reduindancy ef v'ital eempencnts se that a single failure does not pre;'cnt timely operation or cause failure of the system. These plant systems are described in Sections 6.5.3 and 65 3.1.4.13 Criterion 42 - Inspection of Containment Atmosphere Cleanup Systems "The containment atmosphere cleanup systems shall be designed to permit appropriate periodic inspection of important components, such as filter frames, ducts, and piping to assure the integrity and capability of the systems [1]."

Discussion The containment atmosphere cleanup systems are designed and located so that they can be inspected periodically, as detailed in Scetions 6.2.5 and 6.5.

Ho n 3.1-25 Amendment 97 February 1, 2001 to TXX-04167 Page 8 of 69 CPSES/FSAR 3.1.4.14 Criterion 43 - Testing of Containment Atmosphere Cleanup Systems "The containment atmosphere cleanup systems shall be designed to permit appropriate periodic pressure and functional testing to assure (1) the structural and leaktight integrity of its components, (2) the operability and performance of the active components of the systems such as fans, filters, dampers, pumps, and valves and (3) the operability of the systems as a whole and, under conditions as close to design as practical, the performance of the full operational sequence that brings the systems into operation, including operation of applicable portions of the protection system, the transfer between normal and emergency power sources, and the operation of associated systems [1]."

Discussion The containment atmosphere cleanup system can be tested as follows:

X.

The operation of the spray pumps can be tested by recirculation through a test line to the Refueling Water Storage Tank (RWST). The system valves can be operated through their full travel, and the system can be checked for leaktightness during testing. See Section 6.5 for details. Power transfer is described in Chapter 8.

X Thc hydrogen recombincrs can be tested during refueling operations or approximate annual inten.'als and the Hydrogen Purge System can be tested periodically to demonstrate its ability to function. Sec Scetioen 6.2.5 for detail-.

3.1.4.15 Criterion 44 - Cooling Water "A system to transfer heat from structures, systems, and components important to safety to an ultimate heat sink shall be provided. The system safety function shall be to transfer the combined heat load of these structures, systems, and components under normal operating and accident conditions.

"Suitable redundancy in components and features, and suitable interconnections, leak detection, and isolation capabilities shall be provided to assure that for onsite electrical power system operation (assuming offsite power is not available) and for offsite electrical power system operation (assuming onsite power is not available) the system safety function can be accomplished, assuming a single failure [1]."

Discussion The cooling water system for safety-related functions consists of the Station Service Water System (SSWS) and the Component Cooling Water System (CCWS).

The SSWS removes heat from the component cooling heat exchangers.

The CCWS is a closed system. It is designed to remove residual heat from the RCS, cool the letdown flow to the CVCS, cool safety-feature heat loads, and dissipate rejected heat from various plant components. The ultimate heat sink used to dissipate rejected heat 3.1-26 Amendment 97 February 1, 2001 to TXX-04167 Page 9 of 69 CPSES/FSAR I.

In valve arrangements 18, 19, 20, and 21 of Figure 6.2.4-1, the butterfly valves inside the Containment are tested towards the center of the Containment.

Butterfly valve disc leakage is the same in either direction due to the symmetrical design of the valve.

2.

In valve arrangement 22 of Figure 6.2.4-1, the diaphragm valve inside Containment will be tested toward the center of the Containment. Diaphragm valve leakage is the same in either direction due to the symmetrical design of the valve.

3.

In valve arrangements 41 and 42 of Figure 6.2.4-1, the ball valves on the inboard side of the personnel and emergency airlocks are tested toward the center of the Containment. Ball valve leakage is the same in either direction due to the symmetrical design of the valve.

4.

In valve arrangement 45, the manual spring closed valves are tested as part of the barrel test and the two valves on the containment side are tested in the direction away from the reactor due to the valves being unsymmetrical. Under DBA conditions, all of these manual spring closed valves are oriented in the direction which results in increasing seating force (i.e. DBA pressure loads the discharge side). Therefore, leak testing as part of the barrel test is conservative.

Containment isolation valve leakage rates are evaluated by methods discussed in Section 6.2.6.3.

Environmental qualification tests performed on the Containment Isolation System components are discussed in Section 3.11.

6.2.5 COMBUSTIBLE GAS CONTROL IN CONTAINMENT Following a DBA, hydrogen gas may be generated inside the Containment by reactions such as zirconium metal with water, corrosion of materials of construction, exposure of the organic cable materials to radiation and radiolysis of aqueous solution in the core and sump. In addition a small amount of methane is generated by the irradiation of the cables as discussed, in Section 6.1 B.2. The following section is presented to describe the design of the Combustible Gas Control System. To censurc that the hydrogen cnecetration is maintained at a safc level, a redundant Hydregen Rccmbincr system is provided in necrdanec with NRC Regulate-Guides 1.7 [5], 1.22 [6], 1.26 [7] and 1.29 [5], Gcenral Design Criteria 1, 42, and 13, [1] [2] [3], and Braneh Teehnieal PesiticnJ 6 -2 [ 11] an' 6.2.5.1 Design Bases 6.2.5.1.1 Generation, Accumulation, and Mixing of Combustible Gases I.

A combustible mixture can be formed when hydrogen gas concentration in the Containment atmosphere is greater than four volume percent (v/o). Fellewig

(

6.2-58 Amendment 97 February 1, 2001 to TXX-04167 Page 10 of 69 CPSES/FSAR LOCA, hydfrgen gas is generated and builds up inside the Containrnent as described in Appendix 6.2.5A.

2.

A volume of hydrogen is generated by radiolysis in the core and the sump and is released in the compartment where the LOCA occurred and in the Containment sump where the coolant is collected.

All subcompartments are provided with vents at the top and drains at the bottom.

The vents provide for the release, caused by buoyancy, of any hydrogen generated within or beneath the subcompartment. The drains prevent the accumulation of water within a subcompartment, thus preventing substantial generation of hydrogen by radiolysis within that subcompartment.

Arrangement of the subcompartments with bottom and top openings creates a stack effect. In addition to the driving forces generated by diffusion rate, the natural ventilation going through the subcompartments provides mixing and avoids hydrogen stratification. Therefore, the flow caused by the stack effect yields a hydrogen concentration within a subcompartment that does not substantially differ from the bulk Containment conditions.

3.

Although operation of the containment spray effectively prevents hydrogen stratification, neither the containment spray nor the recirculation fans are required to ensure adequate mixing. Use of containment spray during post LOCA conditions would enhance natural circulation by causing a temperature gradient in addition to the driving force of falling drops.

6.2.5.1.2 Electric Hydrogen Recombiners escriptions The following design base-; pply to the electric hydrogen recombiners:

1.

The r-ecbinzers are designed to sustain all normal loads as well as accident loads nelwaAdiont sas+A gshtt-A1-e~a.'El Ae and p-esta~efpftur-etr-ansieftts1 a

bs C

The recombiners are not required to mitigate design basis accidents.

2.

The recombiners are designed for a lifetime of 40 years, consistent with that of the plant.

3.

All materials used in the recombiners are selected to be compatible with the environmental conditions inside the Containment Building during normal operation and during accident conditions.

4.

The recombiners are located so that there is adequate area around the units for maintenance.

5.

The recombiners are protected from damage by missiles or jet impingement from broken pipes.

6.2-59 Amendment 97 February 1, 2001 to TXX-04167 Page 11 of 69 CPSES/FSAR

6.

The recombiners are either located away from high velocity air streams such as could emanate from fan cooler exhaust ports or protected from direct impingement of such high velocity air streams by suitable barriers.

7.

Preeess capaeity is sueh that the Containment hydregen eeneentratien does not4 exeeecd 4 vle' based en the release model indicated in Regulatei-y Guide 12.:

Twc'A Pc1nin IPP$ric h-dr-AOPn r-ccAmhincrs; Ar-Prfreyided to meet the sinaiel 8.

faiture er-itericn I

9.

Inspection and testing of the electric hydrogen recombincrs arc made periodically.

For further details, see Tcehnical Speeifications.

10.

Each Containment Building is provided with separate and independent permanently installed hydrogen recombiners.

11.

The hydrogen recombiners are located in the Containment Building, which is inaccessible to plant personnel during an accident. Therefore, personnel protection from radiation in the vicinity of the operating units is not necessary.

12.

The recombiners are mounted on a substantial foundation with no normal, ambient vibration.

6.2.5.1.3 Hydrogen Purge System

.]design descriptions The following apply to the Hydrogen Purge System:

The Hydrogen Purge System functions as a supplementary system for the electric hydrogen recombiners. This system is designed to operate completely independent of the electric hydrogen recombiners and provides controlled purging of the containment atmosphere to aid in cleanup in accordance with NRc Regulater; Guidc 1.7, and GDC 60.

As required by GDC 41, when the system operates, it is capable of maintaining the hydrogen concentration in the Containment below the lower flammability limit following an accident.

fi The manually actuated Hydrogen Purge System has a process capacity of 70 Msvhkh is sufficicent to ensure-that Containmcent hydrogen eonecentration %will not 4c.d1

./e based on the NRC model as indicated in NRC Regulatore Guide 1.7. For hydrogen

£cncrnticn refer to eelcction 6.2.5.3.1 IF The system is required to be capable of operating with a Containment pressure range of 0 to 5.8 psig and temperature range of 50 to 160'F. '

Protection is provided to preclude damage by missiles. All materials are selected to be compatible with accident and normal operating environments.

6.2-60 Amendment 97 February 1, 2001 to TXX-04167 Page 12 of 69 CPSES/FSAR 6.2.5.1.4 Containment Hydrogen Monitoring System The Containment Hydrogen Monitoring System monitors the hydrogen partial pressure in several well-ventilated areas of the Containment Building in order to obtain typical values for hydrogen gas concentration.

The plant has two hydrogen monitoring systems. Each monitoring system consists of four (4) sensor modules and one (1) microprocessor analyzer. Of the four (4) sensor modules in each system, two (2) are located in each Containment. The microprocessor analyzer is thus shared by Units I and 2. The system can be operational within)0_

I-\\

minutes after an accident and is designed for continuous duty during normal plant I operation. The hydrogen gas analyzers alarm at 3 v/o (wet) hydrogen.

The sensor modules and microprocessors are qualified to function under Seismic Category I requirements and post accident conditions as described in CPSES FSAR Appendix 3A, Table 5-1.

6.2.5.2

System Design

The primary means of reducing hydrogen concentration in the Containment following a LOCA are by the use of the electric hydrogen recombiners. As a supplementary system to the Hydrogen Recombiner System, a Hydrogen Purge System is available for use to aid in cleanup by providing controlled purging of the Containment atmosphere. A Containment Hydrogen Monitoring System is provided to sample the Containment atmosphere in various locations to determine the hydrogen concentration.

6.2.5.2.1 Electric Hydrogen Recombiners The applicable codes, standards, and Regulatory Guides used in the design of the eleetrio /

hydregen rcembinr-s ace listed in Table 6.2.5 1. Redundant recombiners as shown on (

Figure 6.2.5-1 are located inside the Containment Building. The recombiner units are located in the Containment in such a way that they process a flow of Containment air containing hydrogen at a concentration which is generally typical of the average concentration throughout the Containment.

Tz mzceet the r-equireents fcr redtindany and independence, twc eletr-ie hydsregz reeembiners are previded for eaeh Gontainment Building_ Each recombiner is provided with a separate power panel and control panel, and is powered from a separate safeguards bus. There is no interdependency between this system and the other engineered safety features systems.

Containment atmosphere is circulated through the recombiner by natural circulation where hydrogen is removed by heating to a temperature sufficient to cause recombination with the Containment oxygen.

The recombiner consists of a thermally-insulated, vertical metal duct with electric resistance metal-sheathed heaters provided to heat a continuous flow of Containment air 6.2-61 Amendment 97 February 1, 2001 to TXX-04167 Page 13 of 69 CPSES/FSAR (containing hydrogen) to a temperature which is sufficient to cause a reaction between hydrogen and oxygen. The recombiner is provided with an outer enclosure to keep out Containment spray water. The recombiner consists of an inlet preheater section, a heater-recombination section, and a discharge mixing chamber that lowers the exit temperature of the air.

The unit is manufactured of corrosion-resistant, high-temperature material except for the base which is carbon steel. The electric hydrogen recombiner uses commercial-type electric resistance heaters sheathed with Incoloy-800, which is an excellent corrosion-resistant material for this service. These recombiner heaters operate at significantly lower power densities than in commercial practice.

Air is drawn into the recombiner by natural convection and passes first through the preheater section. This section consists of a shroud placed around the central heater section to take advantage of heat conduction through the walls to preheat the incoming air. This process accomplishes the dual function of reducing heat losses from the recombiner and of preheating the air.

The warmed air passes through an orifice plate and then enters the electric heater section where it is heated to approximately 1150 to 1400'F, thus causing recombination to occur.

Tests have verified that the recombination is not a catalytic surface effect associated with the heaters but occurs as a result of the increased temperature of the process gases. Since the phenomenon is not a catalytic effect, saturation of the unit by fission products does not occur. The heater section consists of five assemblies of electric heaters stacked vertically with each assembly containing individual heating elements. Table 6.2.5-2 gives the recombiner design parameters.

Operation of the recombiner is done manually from a control panel located in an accessible area outside the Containment.

The recombiner, power supply panel, and control panel are shown schematically on Figure 6.2.5-2. The power panel for the recombiner contains an isolation transformer plus an SCR controller to regulate power into the recombiner. This equipment is not exposed to the post-LOCA environment. To control the recombination process, the correct power input to bring the recombiner above the threshold temperature for recombination is set on the controller, and monitored by the watt meter. The correct power required for recombination depends upon Containment atmosphere conditions and is determined when recombiner operation is required. For equipment tests and periodic checkouts, a thermocouple readout instrument is also provided in the control panel for monitoring temperatures in the recombiner.

Rzcrefeen

[12] provides the design, and cenvirenmental and seismie qualification cfthe Wsctinghouse electric hydrfgen rceembiner, and a description of the testing of a full scale protetypc eleetric hydrogen r-cembine. Aceeptance for the proto type and production models dsczribed in Rfcrzenez [12] is doeumented in Recerenees [i5] and 6.2-62 Amendment 97 February 1, 2001 I) to TXX-04167 Page 14 of 69 CPSES/FSAR 6.2.5.2.2 Hydrogen Purge System The Hydrogen Purge System shown in Section 9.4 on Figure 9.4-6 is common to both units and is designed to be completely independent of the Hydrogen Recombiner System.

it is net eensider-ed credible that ant aeeident eould happen that weuld recnder beth thc hrfn btn R

h em to uSarc nystemand is not uAse duriAn n e PTAform al (

simnulaneeusly inoeperable. it is alse net eensidered eredible that a LOCA eould ineapaeiate Unit 1 and Unit 2 simnutaneeusly. ThArefer-e, nE saft pr-ebAems related te sharing between the two uniits are anticiplated. This system is not used during normal operation but is capable of operating intermittently or continuously after an accident. The Hydrogen Purge system consists of two 700 cfm blowers for supply, inlet and outlet ductwork, and piping, isolation valves, a flow control valve, two atmospheric cleanup systems and two exhaust fans. The blowers are capable of transporting 700 cfm of the fresh, filtered air to the Containment. Air is drawn from either Containment as required, passed through a filterplenum (particulate, iodine adsorbers, HEPA filters) and discharged through the plant discharge duct. A demister and heater are used to maintain the humidity entering the filters below 70 percent. Two trains are provided (one train is required to operate), each capable of controlling the design airflow of 700 cfm when the containment is less than 5.8 psig.

The Hydrogen Purge System is manually operated and is isolated from the Containment by normally closed valves. Mixing of the Containment atmosphere is by natural convection.

Any radioactivity discharged is measured by the plant vent stack monitoring system.

The expected efficiencies of the filters are in accordance with NRC Regulatory Guide 1.140.

6.2.5.2.3 Containment Hydrogen Monitoring System The hydrogen concentration in each Containment is monitored by four (4) sensors located on four (4) different elevations of the containment. Two (2) sensors from each Containment are coupled to one of the two hydrogen analyzer microprocessors located in the control room. Each microprocessor is supplied from a safety-related uninterrupted power supply train. Thus, two independent analysis trains, each monitoring two points inside each Containment, are provided for measurement.

The analyzers continuously monitor the hydrogen content of the Containment atmosphere during normal plant operation and will be operational within 30 minutes following a LOCA. This monitoring system does not rely on the hydrogen recombiner installation or operation.

The analyzer system meets with the following requirements:

Sensitivity 0.1 percent hydrogen by volume 6.2-63 Amendment 97 February 1, 2001 to TXX-04167 Page 15 of 69 CPSES/FSAR Accuracy

+/-2.0 percent of full scale Range 0-10 percent hydrogen by volume Calibration Fully automatic sequencing for feeding known gaseous mixtures to the sensor modules and adjustment The sensor modules are of the in-Containment measurement type using an electrochemical sensor for specific measurement of hydrogen partial pressure.

Each sensor module consists of the following major components mounted on an integral rack: hydrogen sensor, calibration mechanism, calibration gas bottles, solenoid valves (calibration gas isolation), RTD temperature transducer and an electronics interface terminal box. One absolute pressure transducer is provided with each pair of sensor modules. This transducer is mounted on one of the sensor modules.

The analyzer microprocessor modules accept, process and condition the sensor output signal. The microprocessor has a digital display for the following:

Hydrogen volume percent (wet)

Hydrogen volume percent (dry)

Hydrogen partial pressure Temperature Pressure The control room operators are able to select any display for instantaneous readout. The microprocessors also have two buffered 0- 10 volt dc output signals for remote analog display of hydrogen volume percent (wet) on the Main Control Board.

The alarms from the microprocessor modules are from solid state relays and indicate the following conditions: high hydrogen concentration, power failure and system error.

The Containment Hydrogen Monitoring System is designated as IEEE Class IE and qualified per requirements of IEEE 323-1974.

Based on the revision to 10CFR50.44 6.2.5.3 Design Evaluation effective October 16, 2003, the calculation of hydrogen generation following LOCA 6.2.5.3.1 Hydrogen Generation is no longer needed.

Canlculatins of h'ydrogen generatien fellew ing a LOCA shews that although the hydrogen /

production rate defeases with time fellc ing an accident, the hydregen accumulation 7 can cxceed the loewcr flammability level of 4 Nolumc perccnt. Therefcrc, control mcaturc arc iniplecented to prevent hydrogen accumulation to this lce-cl.

6.2-64 Amendment 97 February 1, 2001 to TXX-04167 Page 16 of 69 CPSES/FSAR Thc potential sourcs of hydrogen, method of analysis, and typieaI assumpt dcscribed in Appcndix: 6.2.5A.

Thc following sourec

. rsw used as input parametcrs for thc hydrogen aeeu eaeulations:

~Fnelaie"i 4-~ ZireeftiufiiWeight Weight _f Azrtnium ladding: 46,500 Corfosion Rates As a Function of Timc f

For aluminum: hydrogen gencrated as a rcsult of aluminum corrosion b spray is based onl corrosion data obtained cxper-imentally by ORN (Rcfcrcnec 3, Section 6.2.5A). Thc long tcrm fate assumed for thcsc calculations is 200 mils per ear. The short tcrm corrosion ratc is detcrmined from thc post LOCA temperatdrc transient gien in Table 6.2.5A ] and a curvc of corrosion ratc v crsus temperaturc given in Appendix 6.2.1A rnfigUrO 6.2.cA 1.

b For zinc (paint: hydrogen gencrated by corrosion of paint containing zinc is conscreatiNcly based on thc corrosion of galvanizcd matcrial e-For zinc (galh'anizcd): The curvc of corrosion rate vcrsus temperature for zinc was deried cxperimcnetally by Wcstinghousc (Rcfcrcecc 9, Scetion Toe account for. any uneec~aint)' in the two zinc (paint and galvanized) corrosion rates, a9, oentingeney w-s includcd in thc analysis.

Surfacc Arca and Weight For aluminum, zinc and zinc paint sec Appendix 6.2.5A, Tablc 6.2.5A 3.

Hydrogen in thc Primaf' Coolant at Stait of an Accident Thc total hydrogen within thc primary system boundary, 1701 sef, is the sum of thc hydrogen dissolved in thc primary coolant watcr and that which is in thc prcssurizcr gas spacc. This valuc is based on thc 50 emr P) if eeelant.i in Seetion r

.s Assumptions for thc pressunzer v'apor spacc hydrogcn arc prcsenteJ 624CA4t 6.2.5.3.2 Hydrogen Mixing As described in Subsection 6.2.5.1. 1, all subcompartments are provided with vents to aid in hydrogen mixing and to avoid high concentration pockets of hydrogen. These vents 6.2-65 Amendment 97 February 1, 2001 to TXX-04167 Page 17 of 69 CPSES/FSAR 6.2.5.3.3 Electric Hydrogen Recombiners Diagrams othe hydregen prdodtion rate fcllcwing the LOCA (r-efer to Figure 6.2.SA 5 in Appendi., 6.2.5A) show that altheugh hydroggen produetien fate deer-easez with time aFler the less ef eoolant aeeident, tetal hydroegen aeumulation can exeeed the lowe flammfability limnifef4 N v/o and pesitivle measures are neeeszaf' te limit hydrogeni aeeumuitlation to acceptabicle ksels. The eicetr-ie hydregen r-eeembiner-provNide the means to preNvent uinsafe leveic ef hydregen eoncentr-atien freom being reached in the Contfainmenlt following a LOCA.

For-the pufpese of sheowing that the electr-ic hydrogen receombinler is capable of mfaintaining the safe hydroegen eeneentratiens, an antalysis was per-fen~ed uising the NRC RegulatofryGuide 1.7 model. The rcesutt for-the Containmcnt veltume is show.n on Fgr 6.2.5A 9. The NRC Recgulatefy Guide 1.7 model is based uponasuin.

fission preduet activity release speifd in Reference [1 3] and the,values for pestaccident hydrogen generatien specified in this guide. Refer-to AppendiL 6.2.5A fer-furdhe ififieffiaieil.

Each electric recombiner is capable of continually processing a minimum of 100 scfm of Containment atmosphere. The hydrogen contained in the processed atmosphere is converted to steam which then exits to the Containment atmosphere, thus reducing the overall Containment hydrogen concentration. Te hydromgn eeneentr-aten in the Containment calculated for the previously described models is based on a reeombiie that the mapirp om hydroigen ncentrgatin will be muh less than the loweri flammabilitc lim~it of I vWo if the Feeembiner is started ene day fellowing the accident. Ther-efere, one of these unit mcets the design criterion efmaintaining a safe hydrogen concentration with contsiderable margin, and the second unit provides a redundant system of equal capability ont a redundant power-supply.

The peak hydrogen concentration occurs whcn the afmount ofhydrogen being generated is equal to the amuint of hydrogen being r-eprocessed. The production rFate ofhydroge decreases with increasing tm followngr the accident. Once thiS Peak has been reached, the eectic r

eombiner esses hydrogea at a faster rate than it is being produced. This results in an overall reduction ef the hydrogen coneontration inside the Centainmospent and pronvides a onteinually increingmrg between the Containment hydroegen coneentration and the lower flammability limit of 4 v/i.

The unit is designed to sustain all nomal leads as well as accident loads suchs loads and iemperaturge and pressure transients from a LOCA.

FTcr futher infoenneain on hydrogen productien and amoultofation, see Appendixi 6.2.5A.

6.2-69 Amendment 97 February 1, 2001 to TXX-04167 Page 18 of 69 CPSES/FSAR 6.2.5.3.4 Hydrogen Purge System The Hydrogen Purge System operates completely independent of the electric hydrogen l

recombiner i C Le f maintain igx a safe hydrAAAn concAn o

ml I v/c) in /

the Contain ns~l The system is capable of continually or intermittently processing a minimum of 700 cfm.

If a supply blower or exhaust fan fails, redundant fans will be able to supply or exhaust air by changing the valve and damper arrangement. Air supply and exhaust lines are arranged so as not to be rendered inoperative by accumulation of water in the line from Containment spray, condensation, or flooding.

All equipment is leaktight, and the filter housings are designed to facilitate replacement without undue exposure of personnel to radioactive sources.

The Hydrogen Purge exhaust air filtration units meet the requirements of NRC Regulatory Guide 1.140 as discussed in Appcndix IA(B).

The supply and exhaust lines are routed through different Containment penetrations.

Each fan is connected to an emergency standby diesel generator bus. (Section 8.3)

The Containment isolation valves, the piping inside the Containment, and the piping between the isolation valves are ANS Safety Class 2. The exhaust equipment beyond the outboard Containment isolation valves is non-nuclear safety, seismic category II.

6.2.5.3.5 Containment Hydrogen Monitoring System The Containment Hydrogen Monitoring System is capable of determining the hydrogen concentration at four elevations in the Containment. Four sensor modules and two microprocessors analyzers are provided to ensure that sufficient redundancy is available.

Deleted 6.2.5.4 Tests and Inspections Tcst programc for preoperational testing and periodic test arc implemented. The insecyice i-pcetiefn as paf eo fs1A Aillanen testA is eenducted prAiedieally througheut the lifredf the Fthat the eleetrmi hydregen rceembiners are r-eady tx per-fcrmn their safeta.

4-Flctrie Hlydrogen Rccombincrs The clectrie hydrogen recombincrs have undergone extensivc testing in the W'estinghousc develepment program. Thcec tcsts encompassed the initial analf ieal studies, laboratory proof of principal tests, and full sealc prototype testing. The full seale prettoyp tests included the effeets ef:

6.2-70 Amendment 97 February 1, 2001 to TXX-04167 Page 19 of 69 OT arj'ing hydrogen eE b.+

1 Alkaline spray atmo:

e:

d-Convwction currnets e-.

Seismie aeefivty CPSES/FSAR ineenir-afteo

pihefe A detailed diseussion f fthse !zsts is giwn in Refercnee [12].

I Prsteper-atinnal tests and inspecticns are per-forfmed in aeeer-danee with Tccehnical the rvembinFr to per-fefc its lnetien. Testing is per-fevd to veify eperation of thc control system and to vcrify functional performanec of thc heaters to tho required temporaturA leA.

Hydrogen Pur-ge Systcm Ceompefnent qualifleatiefn tests demonistrete the ehareetefistieg of m~aterials ineeo-orated into eefmpenentis (e.g., effeieiney efecharc---l filt-O.

Component aceeptance tests demcnstratc thc capabilitV ofthc components incorporated. Fans arc tested by thc manufacturcrs to detceminc that theu eharactcristio curees arc within design limits.

A pest ifmtalat cos t : petfeAe tA demrnsta ^ter eenrianee.with design requirements. DuAnA this test, fans arc t+stin gA in aeor-danie with the standards of the AirWMoing and Conditiening Associatien (AMCA), and filters are tested in Aecrdane with NRC Regulat, Guide 1. 1 4 0 (See Appordii lA_ )). All duetvork'pipiag ofthe *lydregAn PurgA Air cleanup systATm. are quantitatikcly lcak tested from thc outboard containmcnt isolation valvcs.

After-installation the Hydroegen Purge Systcm cant be tested. The system is nrA rally idle. Periedie tests arc perfomicd on majo _Ampenrnts to dAAmoAnstrat*-

their-ability to futnction.

Containmcent Hlydrogen Monitoring System Thc Containment Hydrogenf Monitoeinfg System is calibrated when installcd and periodically r-calibrated in acoerdance with manufaeturcr's instruetions.

The sAnsers will be automatically r-ealibr-ated using known calibration gases containing two (2) and six (6) p-crent hydrogen in high pufity nitrogeni. The calibration cyee wvill be autematically initiated at reular inten.als by the mAAAA A

orA systecml, althouigh manual inirAtiatn is also possiblc.

6.2-71 Amendment 97 February 1, 2001 to TXX-04167 Page 20 of 69 CPSES/FSAR The Centainment H45egen Monitoring System will be field tested in aneerdanee wif Regulaterxy G uid.l "PIeperatina and Iitia 8tasdkFst f~ranS4 Water Cooled Powerr Reactor-s."

6.2.5.5 Instrumentation Requirements The electric hydrogen recombiners do not require any instrumentation inside the Containment for proper operation after a LOCA. The recombiners are started manually after a LOCA. The hydrogen monitoring system is used in determining Containment hydrogen concentration that indicate when the recombiners or the hydrogen purge system should be actuated. This measurement can be taken from any of four sensor locations within the Containment. Control measures can be initiated when the hydrogen concentration reaches 3 v/o (wet). A 3 v/o (wet) hydrogen concentration initiates an alarm in the Control Room thereby alerting the operator. Instrumentation is provided to both monitor the hydrogen concentration in the Containment and to monitor the Hydrogen Purge System operation. Two hydrogen indicators are provided, one mounted on the Main Control Board and the second one on the microprocessor analyzer.

The hydrogen purge supply blowers and exhaust fans are manually started from the Control Room. A humidity control heater located in the filter is interlocked with the fan to come on when the fan is started and to shut off when the fan is stopped. A thermistor is provided on the discharge side of the iodine adsorber to provide a high temperature signal to the Fire Protection Systems panel. Differential pressure switches and/or indicating switches are provided to monitor the differential pressure across the fans and exhaust filtration units. A low alarm is annunciated from the fan switch and a high alarm from the filter bank.

6.2.5.6 Materials The materials of construction for the electric hydrogen recombiners are selected for their compatibility with the post-LOCA environment.

The major structural components are manufactured from 300-Series stainless steel.

Incoloy-800 is used for the heater sheaths and Inconel-600 for other parts such as the heat duct, which operates at high temperature.

There are no radiolytic or pyrolytic decomposition products from these materials.

Materials of construction for Containment Hydrogen Purge System components are listed in Table 6.2.5-6.

REFERENCES

1.

10 CFR Part 50, Appendix A, General Design Criterion 41, Containment Atmosphere Cleanup.

2.

10 CFR Part 50, Appendix A, General Design Criterion 42, Inspection of Containment Atmosphere Cleanup Systems.

6.2-72 Amendment 97 February 1, 2001 to TXX-04167 Page 21 of 69 CPSES/FSAR

3.

10 CFR Part 50, Appendix A, General Design Criterion 43, Testing of Containment Atmosphere Cleanup Systems.

4.

Deleted.

5.

NRC Regulatory Guide 1.7, Revision 2, Control of Combustible Gas Concentrations in Containment Following a Loss-of-Coolant Accident, November 1978, U.S. Nuclear Regulatory Commission.

6.

NRC Regulatory Guide 1.22, Periodic Testing of Protection System Actuation Functions, February 1972, U.S. Nuclear Regulatory Commission.

7.

NRC Regulatory Guide 1.26, Quality Group Classifications and Standards for Water-, Steam-, and Radioactive-Waste-Containing Components of Nuclear Power Plants, Rev. 3, February 1976, U.S. Nuclear Regulatory Commission.

8.

NRC Regulatory Guide 1.29, Seismic Design Classification, Rev. 2, February 1976, U.S. Nuclear Regulatory Commission.

9.

ANSI N 18.2, Nuclear Safety Criteria for the Design of Stationary Pressurized Water Reactor Plants, 1973.

10.

Branch Technical Position APCSB 9-2, Residual Decay Energy for Light Water Reactors for Long-Term Cooling.

11.

Branch Technical Position CSB 6-2, Control of Combustible Gas Concentrations In Containment Following a Loss of Coolant Accident, Nov. 24, 1975.

12.

J. F. Wilson, Electric Hydrogen Recombiner for PWR Containments, WCAP-7709 (Proprietary) and WCAP-7820, Supplements 1, 2, 3, 4 and 5 (Nonproprietary).

13.

TID-14844, Calculation of Distance Factors for Power and Test Reactor Sites, March 23, 1962.

14.

ANSI NI01.1, Efficiency Testing of Air-Cleaning Systems Containing Devices for Removal of Particles, 1972.

15.

Letter from D. B. Vassallo (NRC) to C. Eicheldinger (Westinghouse) dated May 1, 1975.

16.

Letter from J. Stolz (NRC) to T. M. Anderson (Westinghouse) dated June 22, 1978.

This 6.2.5A HYDROGEN PRODUCTION AND ACCUMULATION section has been Hydregen neumulatief in the,ent.inment atmazpher-e fellew.'ifg the design bazi-.

deleted.

eeeident ean be the rscult efpr-eduefeo frem sNveral stfscur

. The c e!

psntircee ef 6.2-73 Amendment 97 February 1, 2001 to TXX-04167 Page 22 of 69 CPSES/FSAR hydrogen are hydroeggn dissolved in thc rcaetor eoolant, thc zirconium water reaetion, corrosion of -onsiruetion matcrials, and radiolytic deeomposition of thc emergeney eorc eooling, anid sump solutiens-.

6.2A. 1 Methed ef Analysis Thc quantity of zirconium whieh reaets with the eore ooling solution depends on the performance ofethe Emcrgeney Cere Coeling Systcm (ECGS).

The critcria for aluation ofthe EGGS requires that thce iraley water reaction be limited to nc more than 1 percent by weight of the total quantit'eofzireonium in the eorc.

ECCS calculations have shown thc zirealoy water-rcaetien to be satisfactory. Regulatory Guidc 1.7 -9 specifies that the amount efhydrogen assumcd to bc gencrated by thc ircaley water-raction should inelude a margint of at least a factor of fiw eyer-ho4 alculatd amountii.

Thus the calciated zircaly water-rveactien is eensevatively assumed ie be -. O-peFeent Thc usc of aluminum inside the Containment is limited, and is not used in saf"ty related eomponents which are in eontaet with the reeireulating eore eooling fluid. Aluminum is mueh more rcaotiv'c with the Containment spray alkalinc boratc solution than other-plant materials sueh as gakvanized stecl, eopper-and eopper nickel alloys.

it should be nioted that the irconium Eter rcatiefn, and alum-inum and zinc eeffsien with Conitaintment spr-ay arc-cemicfial reactionisanid lthusessentially ifndependentof thoe radiation field inside the Containmeet following a lOss of coolant aeeident. Radiolytie deCOmpositiOn of watfC is depcendent en the radiation field intensity. The radiation field inside the Containoent is ealeulated for-the maximum eredible aeeident in whieh the fission produet aetivities giwen in TID-4

[44 ae-used The hydrogen generation ealeulation [10] was perfonmcd using the NRRC model diseussed 1

A

.! - 1s stA7 I 7D1n

_Ir A

!C P.

A-I- -

I-A.-r s APA

_n ft t rcerttwtut), Nctittte -1.I-.  Mitt

,1-..1-.:

-3 t.-

t-UlfUIUIIV5-, unu lec u--ulepllve s

r wX

-1 lio lellewtno E1iseassien eutlin 4-:

Zirconium watcr reaetio SpCulllC patuntetcrs, useae ttt tite fn-tatroef getnetuten.

.is ofRegulatory Guide 1.7 arc summaized in Table Is thc assumptions used in thc ealculations.

Lotion is described by the hamicel ^quation:

O 2-1 v22.

eat 1 due to this reaefien will be eempleted during the first4 eeoolant accident. Thc analysis assumes a 5.0 perecntt Inc zireonium watcr rca Zr- - 211,0

) Zr-Thc hydrogen gencratior day following the loss ol 6.2-74 Amendment 97 February 1, 2001 to TXX-04167 Page 23 of 69 I

I I

I I I

- I I

zirconlum Watcr roaculon. i lle nyaerogen gencratei is assumea to BC releasCa immediately to the Containment atmospherc.

Hy drogen from the Rcaeetor Coolant System The quantity cfhydregen contained in the Reaeter Coolant Systenm during. Stead state epefatin is 1701 SC-F. This inAludos hydrogen ftrni p Arie ga space. The prossunizr gas space hydrogen is based on:

e-

-Ar-eaetsr coolant hvdrcopen eatneentr-a!

__3 n.

ieft ef§

......g (,S:FP) efeeelaw.

--w __

 I I

I I

._rZ Nlormal prfssurizer ncatcrs Fumerd on au percent e1 the time an bea iput go s

thc bilin 44v444rf MinKmum b5ass spray rY:t 1.0 GPM.

d-eallefthe d-NeIal liquid lAvel in the prc1ssuriz'r- (6-0%)

e; Pfessurizefr relief ;,alses being elesed.

The raeetor-oolant ehefmistry speeifeiatiens speeif a-maximum coolant hydrogcn ncneetrationof 50 cm3,1/2g (STP) of coolant. The hydrogon from thc rcactor eeelant systefm is aNvailabl o ocs te the Contaifineoti immediately, follon Corrosion of Plant laterials Oxidation of metals in aqueous solution rcsulis in the generation ef hydrogen gas as onc of thc corrosion products. Extensivc corosion testing has bccn conduod to detcmine tho bchavior of thc arious m

-tals usod in thc Containmcet in the cmergfncy corc cooling solution at dcsign basis accident conditions. Metals tested include Zircaloy, Inconcl, aluminum alloys, cuproniciekl alloys, carbon steel, gaIvanizcdfcarbon steel, and eepper.

Tests conduetcd at Oak Ridge Natienal Laboraories~

(O

,L)r_,3d hac alse

.. rifid the cobnpatibility o fthe ANar-iIus rateials (exiusivo o _alumninumi) with alkaline boratc solution. As applied to the quantitatisc definition of hydrogcn production ratcs, thc rcsults of thc corrosion tests havc shown that only aluminum a_

_in win __nco

_t a rai m

__A A+A_+t.

siguian A Ao_lA_+I.

t b o Ac nron anae Ate *will eeffeae at a fate tnat wi ll signifteantly aac to the hyd argen accumulation in thc Containmcent atmosphere.

Thc corrosion of aluminum may be dsceribed by the overall rcaction:

2Al I-3II,0 Al, 0, -! I.

6.2 75 6Fe$ A icnd, -ac t 49 to TXX-04167 Page 24 of 69 GPSESh1FSAR Therefore, three mobls of hydregen arce p I

_.b

.1

._ F.

Ioedued fr evey twe mdcc ot

. VV;SS I

v.

rJ.

s.

I

.~^W -

.. uminumn th.t is Axiuzea1. k'ppeoximatie 5u standara euaic feet ef yar-egcn for cach peund of aluminum coroded.

Thc corrosion of zine may bc described by thc ovcrall reaction:

ZN 421L20 iZN(OllIX4-Ther-efrc onc molc of hydrogen is produced for cach mlc of zine oxidizcd. This eorrcsponds to 5.5 SC-F IYdrogen proeduced for eaeh pound efkineeeorroded.

The time tefflperaturce cyele (Table 6.2.5A 1) eensiderced in the ealculatien ef aluminuim and zinc eorrosion is based en a eenseryative step wise crsctto of the pestuilated post aceident Gentainmcent transient. The corresin faisatte varieus steps wefe determined fromi the alumfinumn [S] and zine E9] eerrosion rate dTsigni eunAes shewa in Agres 6.2.5A I and 6.2.5A 2. Alumi AorAosion data points inelude the effects of temperature, alley, and spr-ay solution eonditionis.

Based on these corrosion rates and the maximnum allewable aluiminumn and zinc inventeor; given in Table 6.2.5A 3, the eeontdibutieft of alumninum anid z-inc eofrosion to hydrogen aecumfulatien in the Contaifinmnt followinig the design basis aeeident has been calAulatAd.

Fer-eefise~ative estimAAtin, no ercdit was taken for preteetive shielding A t

  • cs A insgulation or-enelesures feomn the spray, and eeomplcei and continuou immorsion was assifumed. Also, no dit was taCt a

fb forprotcctis finish coatings and all zinc prosint inothc thc coatfeeitngs o aumcd allynailabl for sutionc.

Calculationis based on Regulateory Guide 1.7 are per-feomd by allowinig an inercased aluminum orrosion rate during thc efinal step owfthc post acidzn o

oentainmcnt tcmTbporaturc transient (Table 6.2crA i) fonfaspunding to 200 mils n I(

mg!J n2ir). The alumin c

ion rcs earlier-in the aceidcnt seguence arc thc higher rates deterined frfom Pigur 6.2.9A 1.

Radiolysis u

f C 0nr and Sump Watce Watein rtadil iM c isa mlx assumd inv iing r

cactions of nefus Calcnuldiatis. Hwccr-, th e all r-adie1)iie pfrcss may be deseinbd by the Feaeeieft:

1

~

Hh2 +/-; 142 (2 Ofintcrcest here is theo uaiotiatic dufinitihn ofth fiales and extent offadioelti hydogcna pro-dutionief following the design basis accridtnt.

Ain cxcnsivc preogra has been eondueted by Wcstinghouse to invcstigate the radiolysi i

d isacompesitioen ofth re covoling soltion fclleto ing the desig basis aecidenat. in theo eur-c fthis invcstigation, it beacmec apparcnt that two scparat 6.2 -76 Amecdndmnt 97 Febfuay 4T MG1 to TXX-04 167 Page 25 of 69 radielytie nAvironments exist in the Aontainment at design basis aeeidnt eonditions. Ln one case, r-adislysis ef the ce eooling,-, selutioin curJs as a rcesut4 efthe deaye nre of

_.fissien pr-duts in the fue.

Ln *the ther as, th day I

dissel'.d fissien proeduets, whieh have escaped from the

,-.e, results in the r-adielysis cfthe sup souIon. The results ef these investigations are diseussed iRefer-eiee4+3, 6.2.5A.3 Core Solution Radielysis I,

As the emer-geney eoer ceing solution flows through the core, it is subjected to gamma radiation by decay of fission products in thc fucl. This encrgy deposition rcsults in solution radiolysis and thc production of molecular hydrogen and oxygen. Thc initial production ratc of thee species will depend on thc ratc of cner' absorption and the specific radiolytic yiclds.

The energy absorption rate in solution.an be assessed from knewledge ofthe fission products contained in the core, and a detaiAed analysis oftho dissipatio:n of the d^^^

encre' between eore materials and the solution. The results of W'estinghouse studies show essentiall" all of the beta cncrgy will bc absorbed within the fuel and cladding and that this represents approximately 50 perccnt of thc total betagamma deeay cncr-'. This study shows further that of the gamma cencrgy, a makimum of 7.1 pereent will be absorbed by the solution in eore.

Thus, an cevrall absorption faetor of 3.7 percent of the total eorc deeay eferg' (O y) is used to eompute solution radiation dose rates and the

__,A, r-I_

tic integrated AA se. I able 62.5A S presents tlce tetal Eeeay eneef' tv I yj of a reacto core, which considers full power operation with an extended fuci cycle prior to the accident. For-the maximum credible aeeident ease, the eentained decay energy in the eerce aeeounts for the assumed TID 14144 release of 50 pereent halogens and 1 percent other fission produets. :Pie noble gases are assumed by the TID 111 model to escape to the Containment vapor space where little or no water radiolysis -would result from decay of thesc nelides, The r-adiolysis yield ef hydrogen in solutien has been studied extensively by Alesting~heuse and ORNL.

The r-esults of static capsule tests conducted by Westinghouise indicatc that hydrogen yields much lAwer-than the maimum of 0.11 molecules per 100 ev would be the case incore. With little gas spaee to which the hy drog-en fomced in solution can eseape, the rapid back reactions of moleoular radiolytie products in solution to reformn water is sufficient to result in ver' low net hydrogen y iclds.

However, it is recognized that there are diffcerences between the static capsule tests and the dfnamic condition in core, where the core cooling fluid is continuously flowing.

Such flow is reasoned to disturb the steady state eonditions whieh are obserned in static capsule tests, and while the eceuetfefiof eback r-eactions would still be significant, the everall net ield of hydrogen would be soamcwhat higher in the flowingtA systemA.

The study of radiolysis in dynamie systemfis was initiated by Westinghouse, which fonied the basis fr-e-xperimental werk perfoed a--t OL.

Beth studies elearrly illustfate the Amiendment tA97 Fcbruar) 1, ?001 to TXX-04167 Page 26 of 69 reduced yiclds in hydfogen from eore radiolysis, i.c., reduced from thc maximum yicld of 0.11 moileulcs per 100 cv. These results haxe been Inh A

The caleulations ofhydfogen yield from tcre readilysis are bAiouded by the very

.. nserativw value ef0.11 moeccules per-100 ev. That this.val-u io

. ati.. and c

a raximum fr-this trTe ofaqueeus selutinf. and ganifia r-adiation is eefiicd by miany published wors. Thc Westinghouse results frv m the damic studies show 0.11 to be a iaxnimfu* at vcrP' high solution l

ow rates through the gamma r-adiationt field. The Y-efeFefteed ORNP wcrE cise conifirms this value as a maximum at high flow rates. A-.

0Al4enl4 presents a Nvery eempr-ehcnsivc rci w

eof wor pcrifomed te eenfimni the primary hydrogen cied tro be a maimum of 0.11 0.15 meleulcls perr 100 ANA.-

Calculations based en Relater-y Guide 1.7 assume a hydregen yield valuc of 0.5 moeules per-1 00 Nc, 10 perent ofthe gamnmna energy produced from fission prnducts in the fuel reds is absorbed by thc solution in thc region of thc corc,-e and thc noblc gases eseape to thc Centaimfcnt vapOr spaeC.

6.2.5A.4 Sumnp Solution Radiolysis Another potential scurcc of hydrogen assumed for the post aeeident period ariscs from watcr contained in thc rcactor Contaimfcet sump being-subjccted to radiolyic deccmposition by fission preducts. In this consideration, an assessncnt must bc madc as to thc deca) cnefegy deposited in thc solution and thc radiol)4ic hydrogen yicld, much in thc samc mae cr as givcn abevc for corc radiolysis.

The efnig d:pesited in solution is _omputed using the folowing basis:

4-For thc maxiimum crcdiblc accident, a TID 11 4411 relcase mte4nis i

ssd where 50 pereent of the ttal eefe halogens and I perccnt ofall othef fission proeducts, exeluding neble gases, arc released from the eere to the sumnp solution.

The quantity-of fission product rclceasc is based on rcactor operation for an cxenfded fuci cycc prior to the aceident.

3 Thc total dceay cecr'g-from the rclcased fission products, both bete and gamma, is assumcd to bc fully abserbed in the solution.

Within the asscssmcent ofcnergy relcase by fission prduects in water, account is madc of thc deca) of-thc fission products. To anic at thc timc integrated cecrgy rclcasc, the cecrg relcasc rates wcec integrated oecr timc. Thc oewrall contributions from fission p-oducts at varius times afoer a =OCA arc shown in Table 6.2.5.46.

The yield of hydrJgen from sump solution r-adilysis is most nearly repfescnted by the static capsule tests perfomed by Wlestinghouse and O~RN with the alkali sodium.

boratc solution. Thc diffcrceces between thcse tests and thc actuai conditions for the sump solution, howcvcr, arc impoetant and render-the capsule tests consenQativC in theii predictions of radiolytie hydrogen yiclds.

6.28 Amcnetdfnet -97 Febfidaiey -r2O04 to TXX-04167 Page 27 of 69 I

In this assessment, the sump solution will have considerable depth, Which inhibits the ready diffusion of hydrogen from solution, as compared to the case with shallow depth capsule tests. This retention of hydrogen in solution will have a significant effeet in reducing the hydrogen y iclds to thc Containment atmosphere. The build up of hydrogen eeneentrationt in solutioin will enhance the baek rveation te fonnmationi efwater and lewer:

the net hydrAgen yield, in the same iater as a reduetion in gas tc liquid elumne r-atie will reduie the yield. This is illustrated by the date presented in Figure 6.2.5k 3 ft capsule tests with various gas to liquid v

  • lumfie r-atios. The data shew a signifieant r-eduetion in the apparent r-net hydregen yield fomn the published primary maimum yield of 0.11 molecules per 100 e,. Even at the v1er y highest ratios, Where capsule solution depths are v ery low, the yield is less than 0.30, with the highest scatter data point nt 0 3^ IllOlCUlCp ncr-Ion c Calculations based on Regnlatory Guide 1.7 do net take credit fcr a reduced hydrogen yield in the ease f

esup rfadiolysis and a hydr-gen yield value of0.5 molecules per 10i0 eN has been used.

6.2. A..5 Results FiguFe 6.2.5A 5 shows hydrogen production rate as a funtion of time folloeiing a loss of coolant aceident.

Figture 6.2.5A 7 shows quantity of hydrogen accumulated in the Containment as a ftinetien ef time, with noe recembiners operating.

FicI ure 6.2.5A 9 shows enentratien afhvdr-ren as a funtion f ime-for_ the makimum

_ _ 1 I

--- - --- - - ---- ---- - -- --- -- --1 ---- -

- I I

I I

I

. I reoible aeeeident, w thun a I1 00 Lrrd re-eeomcief stanted alter 24 nours elolewinfg a LUO l'.

and with a recombiner started when the hydrogen concentration reaches 3.5 veolume percene As discussed above, these figures w ere developed using as input parameters the sourees o fhydrgen generation that are discussed in Sectionfs 6.2.5 and 6.2.5A.

As shown in Figure 6.2.5A 9, a single h)ydrogen recombiner has the eapaoity to maintain hydrogen concentration well below the lower flammability limit of 4 volumne perceent it put in operation afler 21 hours2.430556e-4 days <br />0.00583 hours <br />3.472222e-5 weeks <br />7.9905e-6 months <br /> following a LOCA or when the coneentration reaches 3.5 velumc pereet 6.2.5A.6 Conclusion A single hydrogen recombiner_, put in _perati*n befreI the bulk Coanainmffient hAydren, conceentration reaches 3.5 role perc-ent, will maintain the bulk hydro-gen concentration welb b*_.w the Amb ustible limit of I volum1le percen t.

I v 6,2 7Y Am1endment 9 Feb~aiy, O04 to TXX-04167 Page 28 of 69 CPSES/FSAR TABLE 6.2.5-1 APPLICABLE CODES, STANDARDS, AND REGULATORY GUIDES USED IN THE DESIGN OF THE ELECTRIC HYDROGEN RECOMBINER

1.

NRC Regulatory Guides 1.7 (March 10, 1971) 1.2S (Safcty Guidc 28, 6/7/72) 1.29 (Rev. 2, 2/76) 1.38 (Rev. 1, 10/76)

2.

10 CFR 50, Appendix A, GDC 2,11, 42,43l

3.

Industry Codes ASME IX (Welding and Brazing Requirements)

National Electric Code National Electric Manufacutring Association National Fire Protection Association

4.

Underwriters Laboratories, Inc.

5.

Institute of Electrical and Electronics Engineers IEEE 308-1971 IEEE 323-1974 JEE 344-1975 Amendment 97 February 1, 2001 to TXX-04167 Page 29 of 69 CPSES/FSAR TABLE 6.2.54 ZINC CORROSION RATE VERSUS TEMPERATURE ITHIS TABLE HAS BEEN DELETED Teniperfapdte LeIT ee

/

eR (Midm 2hf blaenh 4-5 0.002 2oo 0.046 B

y O3 Data points arc given in Appendix D of the indian Point Unit 3 FSAR.

Amendment 97 February 1, 2001 to TXX-04167 Page 30 of 69 CPSES/FSAR TABLE 6.2.5-5 FAILURE MODE AND EFFECTS ANALYSIS Component of System 4-~ Eleetir-e Hydregefi Reeetimbinre 2A Containment Spray System Malfunction Fails to start or design fttunetie Comments and Consequences perfo-rmits Two redundant clcetrieal hydrogen L

~~~~~.

1 I........

r-cembtecrs arc prosiAce Operation of ne is required. /

)

Fails to operate and provide mixing of containment atmosphere Two redundant containment spray trains are provided. Operation of one train is adequate for mixing of hydrogen in the post-LOCA containment atmosphere.

Containment Hydrogen Monitoring System Any failure in the system that can prevent post-LOCA monitoring of hydrogen in containment atmosphere Two independent microprocessor analyzers, two sensor modules per analyzer and containment, and two alarm systems ensures that the monitoring system is functional during single failure.

I Amendment 97 February 1, 2001 to TXX-04167 Page 31 of 69 CPSES/FSAR TABLE 62. 5A-1 iTHIS TABLE HAS BEEN DELETED (Sheet lof 3)

GENNY POST L=OCA CONTAINENT TEMPDATU S4te e

Tiffie eftea(see) 4-

.2 4

6

'S 9

4-0 44 42-44 44 4-5 4-6 4;7 4-8 4.9 209 24 24 26 2q 0-4-

2-3 4-6-

140-4-G.-

44-5

100 400 300-6180 900 4 000 55200--

i 800-2000 2400 3000-4290-4000-4400-6000-6400-4-a 4

6 40 44 400 450 640 q-5 900 1200 4-00 34g4 2400 5500 3480 4-200 4000

&4500 6000 6400 000 Timcne Re Begfintiig ef ef Sep 4-see 2-see 4-see 6-see 0 see 15 see

-.5 min 15.078 16.7 min 0 fmin 30 min 3373M 4 0 min 15 mnin 50 min 0- fflif 8Q3.3 mfin 91.7 min 100 mi 1.8 hrs

-1.9 hr-s 2.2 hy-s Tempefature (2F3 478 204 226 240

-48 280 280 275 2;;

274 269 262 264 262-ao5 a260 245 244-450 247 243 240 defiR defiR defffi defe+

defft defek defe" defwt' defa'm de~hu defim defati 407 407 4t 407 4t 407 144 407 u4 407-6 44 40.6 44 407 44 407

.h 4

44

407 4~214

+40 1 _. 1 44-.0 47-274 44-.0 42a-4 44.0 1 _.4 44-.0 defalt 1-165 default 11.65 default.65 I e

~lt default default defaulI d4efaut default4 defeul 44--

L-91 Amendment 97 February 1, 2001 to TXX-04167 Page 32 of 69 CPSES/FSAR TABLE 6.2.5A-I GERNY POST LOCA CONTAINMENT TEMPERA T4ffie Step Ne.

Time Lqternl (zcc 28

-29 30 34 3;

-3; 34 34 36 3;

3;8 39 40 44-42 4;

44 44 46 47 48 49 40 544 4i3

-44 44s 80000 8100-9200-10500 1000 14000 1 3000-3400-364000 42000-48000-49000 20000 22000 24000 27000 30000 35000 36000-38000-40000-4 4000-47000-40000-44000-609000 64000-47000-809000 84000-840 SOO 9200

_0000 44000 42000 43400 4-4000 49000 4-0000 49000 24000 26000 330000 36000 38000 40000 44000 47000 44000 60000 64000 74000 80000 g40oo 94000 Timc Frem Begining of LOCA To End ofStep

_.4 hrs 2.6 hr3s 3.1 hr3 3.3 hrF 3-i 4._ hr-9 4.7 hr-s 5.0 h1r 5.3 hrS 5.6 hr-s 6.1 hfs 6.7 hrs 7.5 hfs 9.3 hrs5 9._ hrs hr-S 1.1 hfs 1_._ hrs 13.1 hfs 13.9 hrsE 15.3 hrq 16.7 hr-9

-l8.l hM

_0 -v hrs9 26.4 hr-9

reFfperatufe (2F) ae 237 a2-2 233 24-0 2_7 224 220 2-7 245 243 20W 24W 23 170 495 419 190 488 4-84 4-83 4890 4,77 4-75 4-7-2 4-70 468

'TURES pH Value default default default defIal default default default default default defaul defaul default defailt default default default defautlt default default default default default defaiult default default default default default default default defailt default defailt default default default default default defaul default default default default default default default default defaul default default default default default default default default default defatilt Amcndment-97 Febsuay-I, 2004 to TXX-04167 Page 33 of 69 CPSES/FSAR TABLE 6.2.5A-1 (81;EET-3)

GEMNY F0ST IOC'A CONTQ-ANENT TEMPRATWRPS Step No.

608 g0 TimeFerm Begining ef LOCA Te End Time hientzral (gee) of 94ep 95000 100000

87. hFS 400000 150000 41.7 hi 450000 20000 2-.5 day n0000-1000000 11.6 das~

prWehIe Temper-atue 165 413 4-60 44;3 Min defatil defati def&~u1 default4 defaul de4ul de~ul Constant alumiumco;oien rate of 200 milsycer is ccnzidered for-temperotures equal te or less than 153 de F.

I Atmcendcet 97 Febr-uary 1 00I to TXX-04167 Page 34 of 69 CPSES/FSAR TABLE 62. SA-2 ITHIS TABLE HAS BEEN DELETED I P.A AMTPRR IUvED TO D=TFRMTNT' VTYflPOC;F GAWFRATION Thermal Pewefc Ratin; Centainmcet Frec Veolumc 2-.9-* 4O6 p cntaimnmnt Temeer-ature at Aeeident 0

Weight Zirconium Cadding 46,500 lb Hydfeggen Generated Zireonium Waier-Reaetien Baned en 5.0 pefeent ;'alu IHydregen in Primary Coolant llydrogen Recombiner Capacity 9470 SGF 100 SC-F-NI HYDROGEN PRODUCTION CALCULATION ASSUMPTIONSc OF REGULATORY GUIDE 1.7 rC)Ou rEor Th'n 1OITTTTON R a niOl '-'9T Seur-ees Pereent ef tetal halegens r-etaifted in the eere Percent of total nobl gases-retained in tfle corc 0

^

ileccent of other lizsion product retained in thc corc 99 Enorfgy Distribution 1Peront efttal deeay efnegy gamma rParpnt ^,ftnts 1

l dp'"n' 'rwv-1pt' I

Amendment 97 February 1, 2001

Attachment Page 35 of I 6 to TXX-04167 CPSESJFSAR 59 TABLE 6.2.5A2 2 (Sheet2)

Energy Absorptionq by Core Coeling Selutien

-Perceent ef, gammfa energy abser-bed by seiution P Pereent f beta efnerr absVrJbed by selution Hydrogen Pfoduction

-Melleeules 11, pr-edueed perIOO cv, efiefgy absorbed by soluitoen SUMP SOLUTION -ADIOLY-9IS Peet of ttal halogens released to sump selution Pereent effnoble gases released to sump solutien Poerent ofeother fission products relcased to sump solution 4-0 0

0 4.

4-00 200 46 Energy Absoption by Sump SolutieA_

-Pefent oftotal energ (beta and gamnma) wvhih is absor-bed by the su-m eseu4i4ef Hydrogen Pfoduction Mloecules of h)ydrogen produced per 100 cv of cnr-gy absorbed by the sump solution Long Ter A.luminum Coefsien Rate N41i~l per year Milligrams per square decimtefr per hour Amendmfnett97 Februaiye, 4004 to TXX-04167 Page 36 of 69 CPSES/FSAR TAF THIS TABL INIVCWTORQ l#LMI Flux Mapping DFive System NUcieaF InStrumeltatien Systemn Rod Position Indicators MisEcelkaneous Valves Control Red Drivo Mcchanism Contingoeny Refucling Machine Micollaneous Mechanical Equip Mizecllanegus Electrical Equip l&C Valvo6 and Accos6Ories Miscollaneour Eloctrical Equipmont (Ref. TNE NU CA 0000 14 RA.)

Misocllaneous Electrical Equipmcnt (R/D fTNE NU CA n000 156 RlI7 Othor (Rcf. TE SE 00 681) 3LE 6.2.5A-3 E HAS BEEN DELETED Mate4ial SOU~re Weigh AFea A4 20i 88 A4 280 06 A4 47-7 03 A4 230 86 A4 403 42 A4 260 86 A4 28 6

A4 Pat6 240 38 A4 PaF is 7-44 A4 PaFts 66 20 PA 0

4 A

4 4

A4 A4 TRie 47so nt~e 400 Qther t-ct. I U ranRsmilal Ftb 1'1 Total-Atuminum MiSecllaneous Mechanical Equip Misocllancous Mcchanical Equip Miscellancous Mcchanical Equip 4-i 4078 6324 HVAC Equipmcnt and Ducts HVAC Equipment aRd DUGt6 Misecllancous Eloctrical Equip Eloctrical Cablo Trayc 18C Valves and McocssOries l&C Valvos and Accsecorios 4&0-VaFes and AGcessories Structural Linor StFuctural Miscoelaneeus Steel zinG Zine XAR6 Paint GeIaR 7f~

Pa~ts Pain Gai4van.

Galvan.

Galvan.

Rawn GaivaR.

Parts Rawn Rawn Gaivan.

Galvan.

Galvan.

5435 08 43 630 43 4426 2300 08 8?9 86 4830 2875 2080 388 67-6 4

42272 497177 26000 2260 80900 4242 414330 66284 23838 4000 550000

struciurai r Miscclancous btCCI Othcr (Ref. TCE SE 00 581)

Other (Rcf. TU Transmittal ltS 4111)

Gentingeney Z4I 3443 Amendment 97 February 1, 2001 to TXX-04167 Page 37 of 69 CPSES/FSAR Timc Aftec DQy 4-0 44 40 6e 40 4-00 TABLE 6.2.5A-5 FISSION PRODUCT DECAY ENERGY PIZ TIIE CORE ITHIS TABLE HAS BEEN DELETED I

Corc Fissien Preduct Encrgy*

rLOC-A Energy Rclcasc Rate itegratedEr Al X&atts94Al't W^att De 4.7 3 6.6 3.07E 4103 2.. 0M 2^.41 1F03 3-.411 2.08P 03 4-.V 1.E0

-5.

-1.67E 103 6.114E 1.51E 103

7.22E

.3E03

&^

6-5E 4.20F 03 992 i.08E l 03 lil l 9.14E- 02 1.2 8.5B402 1.39^E 8A<EA_

+

A

.09E 1.48E___

n ayMstAINr-[

M404

-04 Z-04 E-G4 Z-04 p.-04 EG LE-LEG E44 E--

r iIfstu.rs tu pO r ent ut excre naiogens, other fission products in the corc.

n.nnE ;y denotce n.nn x no nofci geacs ana 99 perfcet oe Amendment 97 February 1, 2001 to TXX-04167 Page 38 of 69 CPSES/FSAR TABLE 6.2.5A-6 FISSION PRODUCT DECAY ENERGY Pi SUMP SOLUTION lTHIS TABLE HAS BEEN DELETED I Sump Fissien Preduet Energy)*

ftecr LOCA Encrgy Release RAte Iegiated E-P.e aws Wa~siAPA Watt Days

-Tinie 4 GP, R PAAAA xb

".7 40 40 2$

60 80 90 400 2.32E I02

7.59E 01

.35EI-01 2.66E4I1 2.26E 01 1.62E0 1 1.35 1 40JO1 9 8iE400

-Q.:79E I 00 8.29E-00 8.3 1 B-00 4.87E'02 9.32E I02

.1 3P 03 1.43-E-103 i.18F E 03 4.70E 03 I.98&I03 2.13E4 03 2.26E'03 2.36F-;-03 2.45E-03 2.54E I 03 2.62E- 03 Cnsiders release of 50 pereent ef eere halegens, ne neble gases and I perent f fether-fissien preduets te the sump selutie.n nsnE!.JJVdentes n.nn

+6 Amendment 97 February 1, 2001 to TXX-04167 forInclu d

or Page 39 of 69 CPSES/FSAR only This definition includes comparator accuracy, channel accuracy, each input, and rack environmental effects. This is the tolerance expressed in process terms (or percent of span) within which the complete channel must perform its intended trip function. This includes all instrument errors but no process effects such as streaming. The term "actuation accuracy" may be used where the word "trip" might cause confusion (for example, when starting pumps and other equipment).

16.

Control Accuracy This definition includes channel accuracy, accuracy of readout devices (isolator and controller), and rack environmental effects. Where an isolator separates control and protection signals, :.he i^c.'a or accuracy is added to the channel accuracy to determine control accuracy, but creditis taken for tuning beyond this point; i.e., the accuracy of these modules (excluding controllers) is included in the original channel accuracy. It is simply defined as the accuracy of the control signal in percent of the span of that signal. This will then include gain changes where the control span is different from the span of the measured variable. Where controllers are involved, the control span is the input span of the controller. No error is included for the time in which the system is in a nonsteady state condition.

7.1.1 IDENTIFICATION OF SAFETY-RELATED SYSTEMS 7.1.1.1 Safety-Related Systems The Nuclear Steam Supply System (NSSS) and the balance of plant (BOP) instrumentation discussed in Chapter 7 that is required to function to achieve the system responses assumed in the safety evaluations, and those needed to shutdown the plant safely are given in this section.

Refer to Figure 7.1-3 for location layout drawings of Class I E instrumentation. These figures pertain to location layout drawing requirements as discussed in Sections 7.2, 7.3 and 7.5.

7.1.1.1.1 Reactor Trip System The Reactor Trip System (RTS) is a functionally defined system described in Scction 7.2.

The RTS responsibility falls primarily under the NSSS supplier, with the exceptions of underfrequency, and undervoltage, and turbine trip signal which are under BOP scope (See Figure 7.2-1). The equipment which provides the trip functions is identified and discussed in Section 7.2. Design bases for the RTS are given in Section 7.1.2.1. Figure 7.1-1 is a block diagram ofthis system.

7.1.1.1.2 Engineered Safety Features Actuation System The Engineered Safety Features Actuation System (ESFAS) is a functionally defined system described in Section 7.3. The equipment which provides the actuation functions 7.1-4 Amendment 97 February 1, 2001 to TXX-04167 Page 40 of 69 CPSES/FSAR is identified and discussed in Section 7.3. Design bases for the ESFAS are given in Section 7.1.2. 1.

The ESF and ESF Support Systems requiring actuation are as follows:

ESF Systems:

1.

Emergency Core Cooling System (Section 6.3)

a.

Safety Injection System

b.

Residual Heat Removal System (partial)

c.

Chemical and Volume Control System (partial)

Designed by NSSS vendor.

2.

Containment Spray System (Section 6.2.2)

a.

Containment Spray Chemical Additive Subsystem (Section 6.5.2)

Designed under the Architect-Engineer's (A-E) specifications.

3.

Containment Isolation System (Section 6.2.4)

Containment isolation valves for the following systems are furnished by the NSSS vendor.

a.

Chemical and Volume Control System.

b.

Residual Heat Removal System.

c.

Safety Injection System.

d.

Waste Processing System.

The remaining Containment isolation valves are built to the specifications of the A-E.

4.

tombutiblc Gas Control System (Section 6.2.5) lDeleted.l ctel~cyercgen Rccombiner-Basically similar to the William B. MeGtuir-e Nueclear Station. Hydrogen reeombiners fumished by the NSSS Nvendor.

5.

Control Room Air Conditioning System (Sections 6.4 and 9.4).

Designed and built to the specifications of the A-E.

7.1-5 Amendment 97 February 1, 2001

CPSESIFSAR 01 TAELE 7.1-2.6 Delete column 7

(Sheet I of 5)

SAFETY RELATED INSTRUMENTATION & CONTROL SYSTEMSICODES, STANDARDS & GUIDES/APPLICA3ILITY MATRIX FOR OTHER INSTRUMENTATION SYSTEMS REQUIRED FOR S (1,7)

SWIrCHOVER PROCESS b EFF INTERLOCKS 4.

I & C POWER RHR ISOLATION REFUELING ACCUMULATOR INJECTION TO RADIATION RCPB LEAK RCS PRESSURE UYOROGFN FIRE SUPPLY",

VALVES INTERLOCKS(8)

MO. VALVES RECIRCULATION MONITORS DETECTION CONTROL Mu04TORu PROTECTIONW' GDCt X

X X

X X

X GDC 2 X

X X

X X

X X

GDC 3 X

X X

X X

X X

GDC 4 X

X X

X X

X X

GDCS X

X X

X X

X X

GDC10 X

GDC12 GDC13 X

X X

X X

X X

GDCIS X

X GDC19 X

X X

X X

X X

GDC20 GDC21 GDC22 GDC 23 GDC 24 X

X X

X X

X GDC25 GDC26 GDC 27 Arnendment 97 February 1,2001

CPSESIFSAR TABLE 7.1-2.6 (Sheet 2)

SAFETY RELATED INSTRUMENTATION & CONTROL SYSTEMSICODES, STANDARDS & GUIOESIAPPLICABILITY MATRIX FOR OTHER INSTRUMENTATION SYSTEMS REOUIRED FOR SAFETY (1.7)

SWITCHOVER PROCESS & EFF I & C POWER RHR ISOLATION REFUELING ACCUMULATOR INJECTION TO RADIATION SUPPLY"'

VALVES INTERLOCKS(8)

MO. VALVES RECIRCULATION MONITORS INTERLOCKS RCPELEAK RCS PRESSURE DETECTION CONTROL 0 >

0 00 HYRGE0 FIRE MOp;TORING PROTECTION" GDC 28 GDC 29 GDC 30 X

X GDC 33 GDC 34 GDC 35 GDC 37 GDC 38 X

X X

GDC 40 GDC 41 GDC 43 X

X X

GDC 44 GDC 46 GDC 50 GDC 54 GDC 55 GDC 56 GDC 57 GDC 63 GDC 64 X

X X

Amendment 97 February 1. 2001

CPSESYFSAR TABLE 7.1-2.6 C

(Sheet 3)

SAFETY RELATED INSTRUMENTATION CONTROL SYSTEMS/CODES. STANDARDS S GUIDESIAPPLICABILITY MATRIX FOR OTHER INSTRUMENTATION SYSTEMS REOUIRED FOR SAFETY (1.7)

CD SWITCHOVER PROCESS & EFF INTERLOCKS I & C POWER RHR ISOLATION REFUELING ACCUMULATOR INJECTION TO RADIATION RCPB LEAK RCS PRESSURE YOROGE-0 FIRE SUPPLY",

VALVES INTERLOCKS(8)

MO. VALVES RECIRCULATION MONITORS DETECTION CONTROL ML4NTORING PROTECTION")

RG 1.6 RG 1.7 X

RG 1.11 RG 1.12"° RG 1.22 X

X RG 1.29 X

X X

X X

X RG 1.30 X

X X

X X

X RG 1.32 RG 1.45 X

X RG 1.47 X

RG 1.53 X

X X

X RG 1.62 RG 1.63"'

RG 1.67 'I RG 1.68 RG 1.70 X

X X

X X

X X

RG 1.73 X

RG 1.75 X

X X

X RG 1.78 Amendnment 97 February 1. 2001

CPSESIFSAR TABLE 7.1-2.6 (Sheet 4)

SAFETY RELATED INSTRUMENTATION & CONTROL SYSTEMSICODES, STANDARDS & GUIDESIAPPLICABILITY MATRIX FOR OTHER INSTRUMENTATION SYSTEMS REWUIRED FOR SAFETY (1,7) 0 >

to

-D.~

08

-_i SWITCHOVER PROCESS & EFF I & C POWER RHR ISOLATION REFUELING ACCUMULATOR INJECTION TO RADIATION SUPPLY" VALVES INTERLOCKS(g)

MO. VALVES RECIRCULATION MONITORS INTERLOCKS RCPB LEAK RCS PRESSURE DETECTION CONTROL

X X

X X

X x

X X

X X

X X

X X

X X

76 IEEE STO 279 IEEE STO 3D8 IEEE STD 317 P1 IEEE STO 323 IEEE STD 336 IEEE STO 338 IEEE STD 344 IEEE STD 379 IEEE STD 384 X

X X

X X

K X

X K

K X

X X

X x

X X

X X

X X

X X

X X

X X

NOTES:

Armendment 97 Febtury 1, 2001

CPSES/FSAR TABLE 7.1-2.6 (SheetS)

SAFETY RELATED INSTRUMENTATION & CONTROL SYSTEMS/CODES. STANDARDS & GUIDESIAPPLICABILITY MATRIX FOR OTHER INSTRUMENTATION SYSTEMS REOUIRED FOR SAFETY (1.7) 0 0 CA>

1.

The scope of applicability Is instrumentation & control.

0

2.

Refer to FSAR Section 3.7.B.4 and Appendix 1A (B).

3.

Refer to FSAR Section 8.3.1.2.1 and Appendsx IA (B).

4.

Refer to FSAR Section 3.9 8.3.3. and Appendix IA (8).

0

5.

Refer to FSAR Section 14.2 and Appendsx IA (B).

6.

Refer to FSAR Section 9.5.1 and Appendix 1A (B).

7.

X Signifies compliance as discussed or qualified in the FSAR Sections referenced in Table 7. 1... Not applicable.

8.

Refer to FSAR Sections 7.6.3 and 9.1.4.

Amendment 97 February 1, 2001 to TXX-04167 Page 46 of 69 CPSES/FSAR

2.

Maximum system pressure = 2750 pounds per square inch absolute (psia).

3.

Fuel rod maximum linear power for determination of protection setpoints = 18.0 kilowatts per foot (kw/ft)

The accident analyses described in Chapter 15 demonstrate that the functional requirements as specified for the RTS are adequate to meet the above considerations, even assuming, for conservatism, adverse combinations of instrument errors. A discussion of the safety limits associated with the reactor core and Reactor Coolant System, plus the limiting safety system setpoints, are presented in the Technical Specifications.

7.2.1.2.5 Abnormal Events The malfunctions, accidents or other unusual events which could physically damage RTS components or could cause environmental changes and the protection criteria followed are:

1.

Earthquakes (see Sections 3.7N and 3.7B).

2.

Fire (see Section 9.5.1).

3 Us~45 n; -

-yd egebuild up inside Ccntainment (see Seeiin 6-

.2).

Deleted.

4.

Missiles (see Section 3.5).

5.

Flood (see Section 3.4).

6.

Wind and tornadoes (see Section 3.3).

7.

Loss of coolant accidents (see Section 6.2)

8.

Steam line breaks (see Section 6.2)

9.

Loss of ventilation (see Section 9.4)

The RTS fulfills the requirements of IEEE Standard 279-1971 to provide automatic protection and to provide initiating signals to mitigate the consequences of faulted conditions.

7.2.1.2.6 Minimum Performance Requirements

1.

RTS response times RTS response time is defined in Section 7.1. The maximum allowable time delays tabulated in Table 7.2-3 represent functional design values as opposed to acceptance criteria for response time testing. The Technical Specification response time requirements ensure that reactor protection system functional 7.2-19 Amendment 98 to TXX-04167 Page 47 of 69 CPSES/FSAR 7.3.1.2.4 Limits, Margins and Levels Prudent operational limits, available margins and setpoints before onset of unsafe conditions requiring protective action are discussed in Chapter 15 and Technical Specifications.

7.3.1.2.5 Abnormal Events The malfunctions, accidents, or other unusual events which could physically damage Protection System components or could cause environmental changes are as follows:

1.

Earthquakes (see Sections 3.7N and 3.7B).

2.

Fire (see Section 9.5.1).

3.,

,en build n

iz atainmnt (see Setion 6.2-).

~Deleted.

4.

Missiles (see Section 3.5).

5.

Flood (see Section 3.4).

6.

Wind and tornadoes (see Section 3.3)

7.

Loss of Coolant Accidents (see Section 6.2)

8.

Steam line breaks (see Section 6.2)

9.

Loss of ventilation (see Section 9.4) 7.3.1.2.6 Minimum Performance Requirements Minimum performance requirements are as follows:

I.

System response times The ESFAS response time is defined as the interval required for the engineered safety features sequence to be initiated subsequent to the point in time that the appropriate variable(s) exceed setpoints. The response time includes sensor/process (analog) and logic (digital) delay plus, the time delay associated with tripping open the reactor trip breakers and control and latching mechanisms, although the engineered safety features actuation signal occurs before or simultaneously with engineered safety features sequence initiation (see Figure 7.2-1, Sheet 8). Therefore, the response times to initiating engineered safety features presented herein are conservative. The values listed herein are maximum allowable times consistent with the safety analyses and are systematically verified during plant preoperational startup tests. These maximum delay times thus include all compensation and therefore require that any such network be aligned and operating during verification.

7.3-41 Amendment 99 to TXX-04167 Page 48 of 69 CPSES/FSAR 7.3.2.2 Compliance With Standards and Design Criteria Discussion of GDC are provided in various sections of Chapter 7 where a particular GDC is applicable. Applicable GDC include Criteria 13, 20, 21, 22, 23, 24, 25, 35, 37, 40, 43, and 46. In naddtet thAe Wesbtinghus supplied hyfeit lsrta

-eeembner reet XD 4

Compliance with certain IEEE Standards is presented in Sections 7.1.2.7, 7.1.2.9, 7.1.2.10, and 7.1.2.11. Compliance with Regulatory Guide 1.22 is discussed in Section 7.1.2.5. The discussion given below shows that the ESFAS complies with IEEE Standard 279-1971, Reference [4]. For the list of references to the discussions of conformance to applicable criteria, see Table 7.1-1.

7.3.2.2.1 Single Failure Criteria The discussion presented in Section 7.2.2;2.3 is applicable to the ESFAS, with the following exception.

In the engineered safety features, a loss of instrument powver will call for actuation of engineered safety features equipment controlled by the specific bistable that lost power (containment spray and RWST Low-Low excepted). The actuated equipment must have power to comply. The power supply for the protection systems is discussed in Section 7.6 and in Chapter 8. For containment spray, the final bistables are energized to trip to avoid spurious actuation. In addition, manual containment spray requires a simultaneous actuation of two manual controls. This is considered acceptable because spray actuation on hi-3 containment pressure signal provides automatic initiation of the system via protection channels meeting the criteria in Reference [3]. Moreover, two sets (two switches per set) of containment spray manual initiation switches are provided to meet the requirements of IEEE Standard 279-1971. Also, it is possible for all engineered safety features equipment (valves, pumps, etc.) to be individually manually actuated from the control board. Hence, a third mode of containment spray initiation is available. The design meets the requirements of Criteria 21 and 23 of the 1971 GDC.

7.3.2.2.2 Equipment Qualification Equipment qualifications are discussed in Sections 3.10(B),3.10(N), 3.11(B) and 3.11(N).

7.3.2.2.3 Channel Independence The discussion presented in Section 7.2.2.2.3 is applicable. The engineered safety features slave relay outputs from the solid state logic protection cabinets are redundant, and the actuations associated with each train are energized up to and including the final actuators by the separate alternating current (AC) power supplies which power the logic trains.

7.3.2.2.4 Control and Protection System Interaction The discussions presented in Section 7.2.2.2.3 are applicable.

7.3-45 Amendment 97 February 1, 2001 to TXX-04167 Page 49 of 69 CPSES/FSAR TABLE 7.5-3 (Sheet 2)

SUMMARY

OF TYPE B VARIABLES Function Monitored Variable Function Type/

Category Variable Heat Sink Containment Integrity RCS Pressure (WR)

Steam Generator Level (NR)

Steam Generator Level (WR)

Auxiliary Feedwater Flow to each S/G Main Steamline Pressure (S/G Pressure)

Containment Pressure (IR)

Containment Water Level Containment Hydrogen Concentration Backup (P)

Key B2 BI Key Key Bi BI Key BI Key BI Key BI Key

-lBackup B3 I

Backup (P) - Preferred backup IR - Intermediate Range Amendment 97 February 1, 2001 to TXX-04167 Page 50 of 69 CPSES/FSAR TABLE 7.5-4

SUMMARY

OF TYPE C VARIABLES Function Monitored Variable Function Type/

Category Variable Fuel Cladding RCS Pressure Boundary Core Exit Temperature Reactor Vessel Water Level (RVLIS)

Accident Sampling Radiation Level in Primary Coolant RCS Pressure (WR)

Containment Pressure (IR)

Containment Water Level Containment Radiation Level (HR)

S/G Blowdown Radiation Level Condenser Off-gas Radiation Key Backup (P)

Backup Backup Key Backup (P)

Backup (P)

Backup (P)

Backup (P)

Backup (P)

Cl C2 C3 C3 Cl C2 C2 C2 C2 C2 Containment Boundary Containment Pressure (WR)

Containment Hydrogen Concentration Plant Vent Effluent radioactivity and flow RCS Pressure (WR)

Containment Isolation Valve Status*

Containment Pressure (IR)

Area Radiation Level Adjacent Containment Key Cl Bcy

& Backup C3l Backup (P)

C2 Backup (P)

Backup (P)

Backup (P)

Backup (P)

C2 C2 C2 C3

  • Excludes local manual, check, relief and safety valves.

IR - Intermediate Range WR - Wide Range HR - High Range Amendment 97 February 1, 2001

CPSESIFSAR TABLE 7.5-7A (Sheet 3)

Instrument Summary Data for Variables in Table 2 of Reg. Guide 1.97, Rev 2 oe

-4 0 '

0 W Variable Type/

Category CPSES IRG 1.97t E3 PRIMARY COOLANT AND SUMP (E3 PRIMARY COOLANT AND SUMP)

Ouantity Tag Ntmb GROSS ACTIViTY GAMMA SPECTRUM BORON CONTENT CHLORIDE CONTENT DISSOLVED HYDROGEN Redundance and Sensor Location (1 I1 Instrument MM2111se 1 0uCi/m/ to 10 CVri ISOTOPIC ANALYSIS 500 TO 6000 ppm 25 ppb TO 5 ppm 0.5 TO 2000 cchtg (STP) 0.1 TO 20 ppm OTO 14 0.1 TO 10%

0.1 TO 30%

ISOTOPIC ANALYSIS OA and Power Qualification t19t ZSuo Location at fisotav CR Disa TSC/EOF Lcalio OR TOTAL GAS DISSOLVED OXYGEN pH HYDROGEN CONTENT OXYGEN CONTENT GAMMA SPECTRUM E3 CONTAINMENT AIR (E3 CONTAINMENT AIR)

CONTAINMENT RAD LEVEL (HR)

B2. C2. Et (El, C3) 2 PER UNIT RE-6290A&B YES FIGURE 7.1-3 l.10RAWr.

EO. SO. DA 1E ERFCS.

RAD MONITOR CONSOLE YES CONDENSER OFF-GAS RADIATION CONTAINMENT HYDROGEN CONCENTRATION CONTAINMENT PRESSURE (WR)

PLANT VENT EFFLUENT RADIOACTIViTY AND FLOW

82. C2 1 PER UNIT (C3)

RE-2959 StiC 4 PER UNIT (C1)

AE-5506A THRU D N/A 10'TO FIGURE 7.1-3 la, uCifcc NONE (NOTE 2)

NON IE ERFCS.

RAD MONITOR CONSOLE YES FIGURE 7.1-3 YES FIGURE 7.1-3 0-10%

0-ISO0 psig EQ. sa. OA ERFCS.

INDICATION (I PER TRAIN)

ERFCS.

INDICATION YES YES YES YES C1.D2 (Cl)

C2. E2 (Cl. E2) 2 PER UNIT PT-938 PT-939 I PER VENT STACK X-RE-5570 Ea. SO. OA NONE (NOTE 3)

N/A 10'- 10' FIGURE 7.1.3 uCilc 0-140.000 dm NON IE ERFCS.

RAD MONITOR CONSOLE AREA RAD.

LEVELS ADJACENT C3 (C2)

II PER UNIT RE-6259 A&B RE-6291 A6B N/A IO'-10, FIGURE 7.1-3 R/hr NONE NON IE ERFCS.

RAD. MONITOR CONSOLE YES S

l Amendm ent 99 Amendment 99

CPSES/FSAR TABLE 7.5-7D (Sheet 7)

Specific Deviations from the Guidance in Reg. Guide 1.97, Rev. 2 on >

ro B+

Tor 0.0 0

0\\

Variable PASS Room Area Radiation Item Range Category R.G. 1.97 Rev. 2 10 R/hr to 104R/hr Category 2 CPSES 10' mR/hr to 104mR/hr Category 3 Table 7.5-7E Reference (Justification)

(1)

(6)

Plant Vent Stack Area Radiation Hot Lab Area Radiation Range Category Range Category 10 1 R/hr to 1 04R/hr Category 2 1 O-IR/hr to 104R/hr Category 2 10-1mR/hr to 104mRRhr Category 3 10'mRlhrto 104mR/hr Category 3 (1)

(6)

(1)

(6)

RHR Pump Room Area Radiation Category Category 2 Category 3 (6)

High Level Radioactive Liquid Tank Level Plant and Environs Radioactivity Instrument Range Instrument Range Top to Bottom Multichannel gamma-ray spectrometer 0-100%

Hot Lab NOSF (1)

(23)

CCW Header Temperature Range 320F-2000F 300F-1500F (2)

Hydrogen Monitors Category Category I Category 3 (24)

Amendment 97 February 1, 2001 to TXX-04167 Page 53 of 69 CPSES/FSAR TABLE 7.5-7E REFERENCE FOR TABLE 7.5-7D (Sheet 4 of 4) display in the control room. Local, such as indication gauge level and pump suction pressure indications are available to resolve ambiguities. Sufficient time is available to resolve ambiguities before the operator must act on CST Water Level Information.

(22)

Containment Pressure Wide Range has qualified redundant channels but additional information is not available to resolve ambiguities over the full range of the instruments. The additional information provided by the Containment Pressure Narrow Range is sufficient.

(23)

CPSES field monitoring teams are dispatched, as needed, to collect samples.

These samples are transported to the Nuclear Operations Support Facility or the plant Hot Lab for analysis. At either location gamma spectroscophy equipment is used to analyze the samples. Instrumentation provided for this capability meets the intent of Regulatory Guide 1.97, Revision 2.

(24)

The Hydrogen Monitors are capable of diagnosing beyond design-basis accidents. The Hydrogen Monitors were changed from Category 1 to Category 3 based on the revision to IOCFR50.44 on October 16, 2003.

Amendment 97 February 1, 2001 to TXX-04167 Page 54 of 69 CPSES/FSAR TABLE 8.1-1 (Sheet I of 2)

SAFETY LOADS AND FUNCTION Safety Load Function Power Safety injection pumps Charging pumps Residual heat removal (RHR) pumps Containment spray pumps Service water pumps Component cooling water pumps Auxiliary feedwater pumps Spent-fuel pool cooling and cleanup pumps HydI)egef fecombinef Control Room emergency Provide emergency core cooling Provide emergency core cooling Provide emergency core cooling and reactor heat removal during refueling operations Provide cooling spray in containment following a loss-of-coolant accident (LOCA)

Provide cooling water for Component Cooling Water System (CCWS) heat exchangers, and emergency diesel generators Provide cooling water to safety-related equipment Provide adequate water to steam generators in the event of a unit trip coupled with a loss of offsite power Cool spent fuel pool water AC AC AC AC AC AC AC AC Af AC Rcdue hydr*-g^n eeneentfrntin in Containment following a LOCA Maintain safe environmental conditions for operating personnel air cooling units and limit ambient air temperature in safety-related compartments heating, ventilating, and air conditioning.

Amendment 97 February 1, 2001 to TXX-04167 Page 55 of 69 CPSES/FSAR TABLE 8.1-1 (Sheet 2)

SAFETY LOADS AND FUNCTION Safety Load Function Power Heating, ventilating,and air-conditioning (HVAC) water chiller Centaincnt Hydr-eg.n Pur~ge Systemf Provide cooling fluid for emergency air cooling units AC Gentfel pest eeneefttratiens-.

)GA hydfeefi AG)

Motor-operated valves small motors, fans and heaters, associated with Safety-related equipment Insure coordinated operation of safety-related systems AC Reactor Protection System and Engineered Safety Features (ESF)

Actuation System Provide safe plant shutdown AC and DC Plant instrumentation Instrument buses Provide safe reactor operation Provide power to instrumentation and control equipment AC AC Shutdown control and instrumentation Provide control to shutdown plant from outside of Control Room.

AC and DC Instrument bus inverters Provide power to instrument buses DC Amendment 97 February 1, 2001

CPSESIFSAR TABLE 8.3-11 (Sheet 7)

NON-CLASS lE EQUIPMENT CONNECTED TO SAFETY RELATED POWER CIRCUITS SCRIPTION POWER SOURCE ID NO.

-id OcX 0

0 EQUIPMENT ID NO.

DES XEB2-2/6M/TR MC(

XEB1-1/2MITR MC(

XEB2-1/5MITR MCI XEB3-2/2FITR MCI XEB4-2/2FITR MCI 1 EB3-3/3MITR MCI 1EB3-418JITR MCI 1EB4-3/3MITR MC, CPX-ELTRET-06 XFh CPX-ELTRET-10 XFIN CP1-ELTRET-05 XFIA CP2-ELTRET-05 XFI CPX-ELTRET-05 XFP CP2-ELTRET-06 XFl CP1-ELTRET-06 XF?

CPX-ELTRET-07 XF?

CPX-ELTRET-08 XF?

CPl-MEDGEE-O1H GE CP1-MEDGEE-02H GE CPX-VAFNCB-01 HYI CPX-VAFNCB-02 HY CPX-VAFUPK-19 HP CPX-VAFUPK-20 HP CPX-VAFULV-19 FIF CPX-VAFULV-20 FIF

-HV-5526 HP TBX-GHCPEL-01 TBX-GHCPEL-02

'AND MOTOR SPACE HEATER SUPPLY AND MOTOR SPACE HEATER SUPPLY

' AND MOTOR SPACE HEATER SUPPLY

' AND MOTOR SPACE HEATER SUPPLY C AND MOTOR SPACE HEATER SUPPLY 0C AND MOTOR SPACE HEATER SUPPLY C AND MOTOR SPACE HEATER SUPPLY C AND MOTOR SPACE HEATER SUPPLY AR FOR LTG DIST PNL ECB2 & EAB10 AR FOR LTG DIST PNL EABD4. EAB6 & EAB8 AR FOR LTG DIST PNL ECB5 & ECB3 AR FOR LTG DIST PNL 2ECB3 AR FOR LTG DIST PNL EAB9 & ECB1 AR FOR LTG DIST PNL 2ECB4 AR FOR LTG DIST PNL ECB4 & ECB6 AR FOR LTG DIST PNL EAB1, EAB3. EAB11 & EABD1 AR FOR LTG DIST PNL EAB2, EAB4, EAB12 & EABD2 NERATOR SPACE HEATER NERATOR SPACE HEATER DROGEN PURGE SYSTEM (HPS) EXHAUST FAN 01 DROGEN PURGE SYSTEM (HPS) EXHAUST FAN 02 S FILTRATION UNIT HEATERS 19 S FILTRATION UNIT HEATERS 20 tE PROTECTION PANEL 19 tE PROTECTION PANEL 20 S MOTORIZED VALVE CPX-EPMCEB-02 CPX-EPMCEB-07 CPX-EPMCEB-08 CPX-EPMCEB-03 CPX-EPMCEB-04 CPI-EPMCEB-07 CP1 *EPMCEB-09 CP1-EPMCEB-08 CPX-EPMCEB-02 CPX-EPMCEB-02 CP1-EPMCEB-07 CPX-EPMCEB-07 CPX-EPMCEB-07 CPX-EPMCEB-08 CPX-EPMCEB-08 CPX-EPMCEB-03 CPX-EPMCEB-04 CP1-EPMCEB49 CP1-EPMCEB-10 CPX-EPMCEB-01 CPX-EPMCEB-02 CPX-EPMCEB-01 CPX-EPMCEB-02 CPX-ECDPEC-03 CPX-ECDPEC-04 CPX-EPMCEB-03 6M 2M sM 2F 2F 3M 8J 3M 6C 4BL 5BL 5BR 1BL 2BL 2BR 4BL 6A 2BL 2BL 6J 6J 2BR 2BR 9

9 2C NOTE (1)

(1)

(1)

(1)

(1)

(1)

(1)

(1)

(5),(6)

(5),(6)

(5),(6)

(5).(6)

(5),(6)

(5),(6)

(5),(6)

(5),(6)

(5).(6)

(8)

(8)

(1) 0 (1)

(1)

(1)

(5)

(5)

(SB1 Hydrogen Recombiner Hydrogen recombiner IEB3-2 (11)

IEB4-2 (I1) I Amendment 99

CPSESIFSAR EQUIPMENT ID NO.

X-HV-5579 X-HV-5529 X-HV-5580 TABLE 8.3-11 (Sheet 8)

NON-CLASS 1E EQUIPMENT CONNECTED TO SAFETY RELATED POWER CIRCUITS DESCRIPTION POWER SOURCE ID NO, HPS MOTORIZED VALVE CPX-EPMCEB-03 6F HPS MOTORIZED VALVE CPX-EPMCEB-04 2C HPS MOTORIZED VALVE CPX-EPMCEB-04 6D CD rz o

CD

" 0 ON NOTE (5)

(S) 0 (5)

NOTES:

(1)

In accordance with Regulatory Guide 1.75, January 1975, Position C.1, Automatically Tripped on SIAS (accident signal). Reconnection requires operator action(s) after resetting SIAS.

(2)

Breaker trips on SIAS, requires operator action to reset, and connecting cable is black and routed separately. In addition, these loads are also tripped on LOOP.

(3)

This portion of the non-Class IE MCC is tripped on SIAS or Blackout (Loss of Offsite Power) signal, and cable is in dedicated raceway.

(4)

Same as No. 1, except MCC's are tripped from either Unit 1 or 2 independent power supply, thus MCC's, associated and non-Class 1E loads are Isolated by SIAS signal.

During normal operation MCCs are powered by Unit 2, and Unit 1 power is locked out.

(5)

Non-Class 1 E loads fed from Class 1 E supplies are protected by two separate Class 1 E breakers, or Class 1 E breaker and Class 1 E fuse or two separate Class 1 E fuses connected in series. These breakerstfuses are coordinated with their supply breakers, and breakers will be tested and calibrated periodically to ensure coordination.

(6)

The Class 1 E transformers and lighting distribution panels feed non-Class I E loads.

(7)

Breaker trips on SIAS (accident signal), reconnection requires operator action to reset, and connecting cable Is associated. In addition, this load is also tripped on LOOP.

(8)

Breaker trips on SIAS, requires operator action to reset, and connecting cable is black and routed separately. These loads are also tripped by diesel generator breaker auxiliary contacts when the breaker closes to power the Class 1 E bus. Therefore the loads will not be on the bus during a safety injection or loss of offsite power.

(9)

Equipment listed, is for Unit 1; Unit 2 is similar, except for equipment identification numbers.

(10)cib Transfer switch is isolated from Class I E bus by administratively controlled normally open circuit breakers. There are no automatic connections to the 1 E bus. It is only connected to either bus during modes 5 and 6, and only if the plant experiences a loss of offsite power coincident with failure of the Class 1 E Emergency Diesel Generators

11. Hydrogen Recombiners were originally Engineered Safety Features and fully qualified. However, based on a change to 10 CFR 50.44 They no longer have a Nuclear Safety Function. The power supply to the recombiners is locked out during modes where the bus is required operable by Technical Specifications.

A recombiner may be powered and used in the long term post accident if required.

Amendment 99

CPSES/FSAR TABLE II.B.2-4 (Sheet 3)

VITAL AREA ACCESS 00 00 0~

cNo R.

El 0

0 0

-3 P.

ON UNIT 1 UNIT 2 Operator Dose' Vital Access Area Description of Task' Time After LOCA (hrs)

When Access is Required Operator Dose7 Route No.

Route No.

Operator Dose' (rem) 0.84

10.

Rooms No. 84 and 855 Diesel gen-erator control station

11.

Rooms No. 84 and 855 Diesel gen-erator control station To inspect the fuel oil storage tank level, fill the oil storage tanks when needed To inspect the DG lube oil makeup duplex filter and strainers 1.0 1.0 10 Fig. Il.B.2-36 11 Fig. Il.B.2-36 0.86 0.86 10 Fig. ll.B.2-62 Fig. I.B.2-63 Fig. 11.8.2-64 11 Fig. I.B.2-62 Fig. 11.8.2-63 Fig. Il.B.2-64 12 Fig. Il.B.2-65 0.84

12.

Equipment Yard Diesel generator fuel oil tank filling area

13.

Task deleted To rill main diesel generator oil storage tanks from a delivery tanker truck Three days after LOCA 8 12 Fig. I.B.2-37 2.29 2.29

14.

Rooms No. 82,

95. 96,103.113, 133,134 and 241
15.

Reem-N404 or 82 Mer~anieal--equip meaarhydre-gerefeeeffe ee panels

16.

Room No.79 Safeguards Drain Panel (TAG No.

CPI-E1PRLV-24)

17.

Rooms No.150 and 150A. Mechanical To deenergize lights, in the case of loss of the non ESF ventilation after a LOCA to prevent temperature excursions To tehe n-reem-binetrs an a.

Silpower

&mt4h d tempera tar4seahed-Diagnose passive failures in the ESF Systems.

0.5 24-0 24.0 14 Fig. I.B.2-39 45 Fkg--.8.2 40 16 Fig. 11.8.2-41 0.61 G04 0.11 14 Fig. 11.3.2-68 through Fig. I.B.2-73 0.64 46A Fig. 2 74 46g Fig-4.8.2 7-6 Fkjlg. l3B 7 16 Fig. II.B.2-78 0.07 To manually open control room intake dampers.

Within 48 17 0.36 17 Fig. I.B.242 Fig. Il.B.2-79 0.306 Amendment 97 February 1, 2001

CPSES/FSAR TABLE II.B.2-5 (Sheet 2)

DOSE RATES AND TIME SPENT BETWEEN CONSECUTIVE POINTS OF UNIT I OPERATOR ROUTE'

'-9>

0 x cm CD=

0 0A

\\0

-0 cn A

B C

D E

F G

Operator Task and Route No.

t

7.

Switch over the reactor 13 makeup water pump Route #7

8.

Isolation of NNS portion 13 of the reactor makeup water system Route #8

9.

Maintaining the fuel pool 13 water level Route #9

10.

Inspection of the diesel 13 generator fuel tanks level Route #10

11.

Inspection of the diesel 13 generator lube oil makeup duplex filters and strainers Route #11

12.

Filling the main diesel 54 generator fuel storage tank Route #12

13.

Task deleted

14.

Deenergizing the lights 46 Route #14

15.

Powedlg-I4p-the 43 hydrFgen Reeobnbers Roule-#l16

16.

Safeguards Drain Panel 13 Access Route #16

17.

Manually open Control 30 Room HVAC Intake Damper Route #17

19.

Manually realign valves 12.5 to maintain spent fuel pool cooling

20.

Manually isolate steam 12.5 supply to the AFWPT dr 77 33 dr 34 14 dr 4.1 13 dr I

305 37 dr 4.1 15 dr t

dr 5.0 23 28 77 33 34 14 4.1 13 305 37 4.1 15 5.0 23 28 18 33 18 14 3.3 13 170 37 3.3 15 5.0 23 17 27 33 27 14 3.7 13 253 37 3.7 15 5.0 6

5.0 27 33 27 14 3.7 13 253 37 3.7 15 5.0 6.0 5.0 0.3 60 0.6 90 0.5 30 125 Task 3 hrs 2 125 77 14 4.1 67 3,300 14 4.1 13 305 37 4.1 29 5.0 Task 60 sec.

4-0 33 4-0 44 1.0 33 1.0 11 2_6 43 4-70 3;

2-5 46 6f4 6-1.0 24 108 7

2,000 2.000 Task 3 min.

1.0 3

24.8 20 1.66 10 24.8 15 565 Task 30 min.

77 33 34 14.3 4.1 13.3 305 36.7 4.1 16.7 5

47 5

64.3 24.7 18 33 18 14.3 3.3 13.3 170 36.7 3.3 29.3 5

Amendment 97 February 1, 2001

CPSESIFSAR TABLE 11.0.2-5 (Sheet 4)

DOSE RATES AND TIME SPENT BETWEEN CONSECUTIVE POINTS OF UNIT 1 OPERATOR ROUTE' oe D0\\

OO vo CD 0

I-.

H I

J K

L M

Ooerator Task and Route No.

t dr

12.

Filling the main diesel (contd)

13.

Task deleted

14.

Deenergizing the lights 97 Task 24.7 15 (contd) 90 sec.

4&

Pwedgi pi(Gond 38 620 49

16.

Safeguards Drain Panel Access (contd)

17.

Manually open control room HVAC Intake Damper (contd)

19.

Manually realign valves 39.6 3510 126 to maintain spent fuel Task 10 pool cooling min.

20.

Manually isolate steam 14.7 89.5 12 supply to the AFWPT dr t

dr t

dr dr t

dr 5.0 64 5.0 31 4,400 13 Task 30 6,500 8

4,400 6Q 22 2r4 8

5580 39.6 3510 47 sec.

I go 46 zoo 40 1,600 1 5

31.3 5

23.3 28 42 9.3 250 13 96000 Task 124 sec.

N 0

P Q

R S

T Operator Task and Route No.

1.

Post accident (contd)

2.

Sampling of plant (contd)

3.

Filling the CCW (contd)

4.

Filling the safety (contd)

5.

Safety chilled water (contd)

6.

Adjusting the AFW 8

(contd) dr t

dr t

dr I

dr I

dr dr S

dr 29,000 6

1,240 4

13,300 9

13,000 3

1,900 Task 15 min.

Amendment 97 February 1, 2001

CPSESIFSAR TABLE II.B.2-5 (Sheet 5)

DOSE RATES AND TIME SPENT BETWEEN CONSECUTIVE POINTS OF UNIT 1 OPERATOR ROUTE'

-0 0 -4 0~

N 0

P a

R S

T Orerator Task and Route No.

t

7.

Switch over (contd)

8.

Isolation of NNS (contd)

9.

Maintaining the fuel (contd)

10.

Inspection of diesel 12 (contd)

11.

Inspection of diesel 12 (cont) dr I

dr t

dr I

r I

dr r

dr 38,000 11 6,200 16 Task 5 min.

38,000 11 6,200 16 Task 10 min.

5.0 19 6,200 18 9,800 5.0 19 6,200 18 9,800 16 Task 5 min.

16 Task 10 min.

5.0 5.0

12.

Filling the main diesel (contd)

13.

Task deleted

14.

Deenergizing the lights (contd) 22 Task 30 sec. 350 24.3 686 7.3 400 47 29 40 1.100 15 8,500 10 17,700 12 Task 30 sec.

10.800 27 410 Task 15 sec.

15.

Poweuing-u ontd) 42 29 9

96 60

16.

Safeguards Drain Panel Access (contd)

17.

Manually open Control Room HVAC Intake Damper (contd) 19, Manually realign valves to maintain spent fuel pool cooling

20.

Manually isolate steam supply to the AFWPT 30.3 4.1 27.8 380 25 2.5 13.3 25 77.3 25 Task 32 min.

96.6 398 42 25 Task 28 Task min.

5 min.

Amendment 97 February 1, 2001

CPSES/FSAR TABLE II.B.2-6 (Sheet 2)

DOSE RATES AND TIME SPENT BETWEEN CONSECUTIVE POINTS OF UNIT 2 OPERATOR ROUTE' A

B C

D E

F G

CO o

R0 atj 0

4-J Route Operator Task t

dr t

dr t

dr t

dr t

dr t

dr t

dr

6.

Adjusting the AFW flowrate 12.5 77 33 34 5

5 14.7 5

5 2600 9.3 740 9.3 125

7.

Switchover the reactor makeup water pumps in case of low pressure alarm 12.5 77 33 34 5

5 14.7 5

23.3 28 14 66 30.3 1040

8.

Isolation of NNS portion of 12.5 77 33 34 the reactor makeup water system 5

5 14.7 5

23.3 28 14 5

5 14.7 5

23.3 8

17.

66 30.3 1040

9.

Maintaining the fuel pool water level 12.5 6

33 6

3 17 30.3 195

10.

Inspection of the diesel generator fuel tank level

11.

Inspection of the diesel generator lube oil makeup duplex filters & strainers 12.5 27 33 27 12.5 27 33 27 5

5 14.7 5

64.3 5

5 5

14.7 5

64.3 5

38.3 3600 9.8 280 38.3 3600 9.8 280

12.

Filling the main diesel generator fuel storage tank 97 0.3 60 0.6 90 0.5 37.5 125 Task 3 hrs.2 125

13.

Task Deleted

14.

De-energizing lights 12.5 77 33 34 15A.

Pewering-phe-nhge 42-6 4

reoembng es 15B.

Poweng-Wtho-hydrogen 4246 4

reoemboners 33 4

33 4

14.3 4.1 13.3 305 36.7 4.1 66.6 3300 36.7 4.1 Task 1 min.

44-3 2-.

43-43 367 2 S 33&

440 440 6

246 44-7 6

64-3 6

83 520 49 60 2 Amendment 97 February 1 2001

CPSESIFSAR TABLE II.B.2-6 (Sheet 5)

DOSE RATES AND TIME SPENT BETWEEN CONSECUTIVE POINTS OF UNIT 2 OPERATOR ROUTE' H

I I

&r I

dr I

J dr K

dr I

dr t

M N

-9.>

toc 0

0D O

rN wo 9

-0 Route Operator Task dr dr

14.

De-energizing lights 13.3 305 14.3 4.1 29.3 5

96.6 24.7 14.7 5

Task 1.5 64.3 5

30.7 4400 15A.

Power p-he-hydrogen feeebinefis min.

4 96 44-7 M9 40 460i0 4.2 4000 3 29 40 29 15B.

Powefig-iup.4e4'ydrogen 22 rewWORefs 25,4 8

16.

Safeguards drain panel access 1200 Task 3 min.

17.

Manually open Control Room 12 HVAC intake damper 561 Task 30 min.

561

19.

Manually realign valves to 39.6 3510 21.7 5

maintain spent fuel pool cooling 31.3 5

23.3 28 14 66 30.3 1040 27.8 380

20.

Manually isolate steam supply to the AFWPT 9.3 250 13 97000 Task 124 sec 0

P Q

dr dr R

S T

U dr dr Route Operator Task dr dr dr

1.

Post-accident Sampling IA.

Initial valve lineup 10 21700 20 27000 20 27000 1B.

Sample retrieval IC.

Hot lab preparation Amendment 97 February 1, 2001

CPSESIFSAR TABLE II.B.2-6 (Sheet 7)

DOSE RATES AND TIME SPENT BETWEEN CONSECUTIVE POINTS OF UNIT 2 OPERATOR ROUTE' 0

P I

r I

dr 0

R S

Route Operator Task T

U dr t

dr t

dr e

r3Q

-0>0,

_w io CNy t

dr

+/-r I

12.

Filling the main diesel generator fuel storage tank

13.

Task Deleted

14.

De-energizing lights 12.6 6500 7.7 Task 0.5 min.

4400 22 350 24.3 686 7.5 Task 0.5 min.

1100 14.7 8500 10 17700 1 5A.

Pethogen feeembiews 15B.

Powedn-j.hert gen M

Aesembirs

16.

Safeguards drain panel access

17.

Manually open Control Room HVAC intake damper a

Task

19.

Manually realign valves to 25 maintain spent fuel pool cooling 2.5 13.3 25 Task 32 min 77.3 25 96.6 1150 42 Task Task 28 min 5 min 25 13.3 25 25 2.5

20.

Manually isolate steam supply to the AFWPT V

W x

Route Operator Task dr t

dr t

Y Z

M dr t

dr t

dr I

dr BB t

dr

1.

Post-accident Sampling Amendment 97 February 1. 2001 to TXX-04167 Included for Page 65 of 69 CPSES/FSAR Information only RESPONSE TO NRC ACTION PLAN (4)

Pressurizer heater motive and control power interfaces with the emergency buses shall be accomplished through devices that have been qualified in accordance with safety-grade requirements.

NUREG 0737 CPSES Response Power is supplied to four pressurizer heater groups from offsite power, when available, and from the onsite emergency diesel generators through ESF buses. Redundancy is provided by supplying two groups of pressurizer heaters from each redundant ESF train, Control power for manual on/off control of each of these four heater groups is supplied from the 125 volt DC ESF bus in the same train as the main power supply.

Procedures are established to control Reactor Coolant System pressure and temperature.

Per Westinghouse analysis, pressurizer heaters are not required during natural circulation cooldown to Hot Shutdown or Cold Shutdown.

No loads need to be shed from the emergency power source to provide sufficient capacity for the connection of the pressurizer heaters.

The electrical interface between each of the four pressurizer heater groups and its associated F bus of concern is through a circuit breaker which trips on an "S" signal and is qualified in accordance with safety-grade requirements. The manual controls for these breakers are qualified in accordance with safety-grade requirements.

ll.E.4 CONTAINMENT DESIGN OBJECTIVE:

"Improve the reliability and capability of nuclear power plant containment structures to reduce the radiological consequences and risks to the public from design basis events and degraded-core and core-melt accidents."

NUREG 0660, Pg. ll.E.4-1 II.E.4.1 Dedicated Penetration Action Plan Requirements:

Plants using external recombiners or purge systems for postaccident combustible gas control of the containment atmosphere should provide containment penetration systems for external recombiner or purge systems that are dedicated to that service only, that meet the redundancy and single-failure requirements of General Design Criteria 54 and 56 of Appendix A to 10 CFR 50, and that are sized to satisfy the flow requirements of the recombiner or purge system.

fl.E-17 Amendment 97 February 1, 2001 to TXX-04167 Page 66 of 69 CPSES/FSAR RESPONSE TO NRC ACTION PLAN The procedures for the use of combustible gas control systems following an accident that results in a degraded core and release of radioactivity to the containment must be reviewed and revised, if necessary.

NUREG 0737 See Sections 6.2.4 and 6.2.5 for containment penetration isolation and for CPSES Response combustible gas control.

CPSES hag redundant safcty grade hydrogen recomnbincrs located inside each containment for post accident hyddrgefn control. These rfcembincrs arc controlled from/

outsidc the containmcent.

II.E.4.2 Isolation Dependability Action Plan Requirements:

"Provide containment isolation on diverse signals in conformance with Section 6.2.4 of the Standard Review Plan, review isolation provisions for non-essential systems and revise as necessary, and modify containment isolation designs as necessary to eliminate the potential for inadvertent reopening upon reset of the isolation signal."

NUREG 0578, Pg. 8

"(1)

Containment isolation system designs shall comply with the recommendations of Standard Review Plan Section 6.2.4, (i.e., that there be diversity in the parameters sensed for the initiation of containment isolation).

"(2)

All plant personnel shall give careful consideration to the definition of essential and nonessential systems, identify each system determined to be nonessential, describe the basis for selection of each essential system, modify their containment isolation designs accordingly, and report the results of the reevaluation to the NRC.

"(3)

All nonessential systems shall be automatically isolated by the containment isolation signal.

"(4)

The design of control systems for automatic containment isolation valves shall be such that resetting the isolation signal will not result in the automatic reopening of containment isolation valves. Reopening of containment isolation valves shall require deliberate operator action.

"(5)

The containment setpoint pressure that initiates containment isolation for nonessential penetrations must be reduced to the minimum compatible with normal operating conditions.

"(6)

Containment purge valves that do not satisfy the operability criteria set forth in Branch Technical Position CSB 6-4 or the Staff Interim Position of October 23, 11.E-18 Amendment 97 February 1, 2001 to TXX-04167 Page 67 of 69 CPSES/FSAR RESPONSE TO NRC ACTION PLAN Included for Information only IH.F INSTRUMENTATION AND CONTROLS OBJECTIVE:

"Provide instrumentation to monitor plant variables and systems during and following an accident. Indications of plant variables and status of systems important to safety are required by the plant operator (licensee) during accident situations to (1) provide information needed to permit the operator to take preplanned manual actions to accomplish safe plant shutdown; (2) determine whether the reactor trip, engineered safety features systems, and manually initiated systems are performing their intended functions (i.e., reactivity control, core cooling, maintaining reactor coolant system integrity, and maintaining containment integrity); (3) provide information to the operator that will enable him to determine the potential for a breach of the barriers to radioactivity release (i.e., fuel cladding, reactor coolant pressure boundary, and containment) and if a barrier has been breached; (4) furnish data for deciding on the need to take unplanned action if an automatic or manually initiated safety system is not functioning properly or the plant is not responding properly to the safety systems in operation; (5) allow for early indication of the need to initiate action necessary to protect the public and for an estimate of the magnitude of the impending threat; and (6) improve requirements and guidance for classifying nuclear power plant instrumentation, control, and electrical equipment important to safety."

-NUREG 0660, pg. II.F-I JI.F. I ADDITIONAL ACCIDENT MONITORING INSTRUMENTATION.

Action Plan Requirements:

"Item Il.F. I of NUREG-0660 contains the following subparts:

(1)

Noble gas effluent radiological monitor:

(2)

Provisions for continuous sampling of plant effluents for postaccident releases of radioactive iodines and particulates and onsite laboratory capabilities (this requirement was inadvertently omitted from NUREG-0660; see Attachment 2 that follows, for position);

(3)

Containment high-range radiation monitor; (4)

Containment pressure monitor; (5)

Containment water level monitor; and (6)

Containment hudrogen concentration monitor.

"NUREG-0578 provided the basic requirements associated with items (1) through (3) above. Letters issued to all operating nuclear power plants dated Septemeber 13, 1979 II.F-I Amendment 97 February 1, 2001 to TXX-04167 Page 68 of 69 CPSES/FSAR Included for RESPONSE TO NRC ACTION PLAN Infonnation only and October 30, 1979 provided clarification of staff requirements associated with items (1) through (6) above. Attachments I through 6 present the NRC position on these matters."

-NUREG-0737 CPSES Response The use of the additional accident monitoring instrumentation as listed will be integrated into the operating procedures and training programs prior to fuel load:

(1)

Noble Gas Monitor The CPSES design will include wide range noble gas monitors for the plant vent stack which will detect and measure concentrations of noble gas fission products in plant gaseous effluents during and following an accident.

An adjacent-to-line monitor will be provided for each main steam line to monitor the concentration in steam that may be released to the environment by the safety or relief valves.

For description of these monitors, see Section 1 1.5.

(2)

Iodine/Particulate Sampling The wide range noble gas monitor discussed above provides the capability to sample the plant vent stacks as required.

For description, see Section 11.5.

(3)

Containment High Range Radiation Monitor The redundant Category I monitors will be located in each Containment Building at Elevation 905'-9". Exact location is provided in Figure Il.F-l. To ensure valid data, these monitors will be located at least 90E apart and will not be located adjacent to process piping.

Monitor special calibration and environmental qualification will be performed as specified in Table II.F.1-3 of NUREG-0737.

For further discussion, see Section 12.3.

(4)

Containment Pressure The CPSES design will include redundant wide range pressure indication (0 - 150 psig) on the Main Control Board meeting Regulatory Guide 1.97 Rev. 2 requirements. In addition this parameter will be provided as input to the SPDS high level display.

Il.F-2 Amendment 97 February 1, 2001 to TXX-04167 Page 69 of 69 CPSESJFSAR RESPONSE TO NRC ACTION PLAN The present CPSES design includes four channels of intermediate range pressure indication (-5 to + 60 psig) on the Main Control Board meeting Regulatory Guide 1.97 Rev. 2 requirements. In addition this parameter will be provided as input to the SPDS high level display.

(5)

Containment Water Level CPSES design will include redundant wide range containment level indication (elevation 808' to 817' - 6) on the Main Control Board meeting Regulatory Guide 1.97 Rev. 2 requirements. In addition this parameter will be provided as input to the SPDS high level display. These transmitters measure volume in excess of 600,000 gallons. CPSES design will also include normal sump level indications (0 - 3 feet) on the Main Control Board. The containment wide range level indication covers the entire range of expected water level in the Containment for post accident conditions. Therefore, containment narrow range level indication is not considered as required for accident monitoring.

Based on a revision to IOCFR 50.44, the design basis LOCA hydrogen (6)

Containment Hydrogen release has been eliminated and the requirements for hydrogen monitoring has been changed. See Section 7.5 for current requirements."

The redeinA,;!ll include Il, acneceftratien indicationt (0 10346) en the Main CGntrol fBeard meeting Regulatcry Guidc 1.97 ReNv. 2 requiremcets. In addition this parameter -will be provided as input to the SPDS high leNvl display.

II.F.2 IDENTIFICATION OF AND RECOVERY FROM CONDITIONS LEADING TO INADEQUATE CORE COOLING Action Plan Requirements:

"Licensees shall provide a description of any additional instrumentation or controls (primary or backup) proposed for the plant to supplement existing instrumentation (including primary coolant saturation monitors) in order to provide an unambiguous, easy-to-interpret indication of inadequate core cooling (ICC). A description of the functional design requirements for the system shall also be included. A description of the procedures to be used with the proposed equipment, the analysis used in developing these procedures, and a schedule for installing the equipment shall be provided."

-NUREG-0737 CPSES Response The CPSES design will include redundant instrumentation to monitor the approach to, existence of and recovery from inadequate core cooling. The monitored parameters will be the reactor coolant system (RCS) saturation margin, the collapsed water level above the reactor core and the RCS temperature at the core exit.

An indication of a declining margin to saturation in the RCS will provide the earliest warning that conditions are developing which could lead to ICC. If the event is allowed II.F-3 Amendment 97 February 1, 2001