RS-15-301, Phase 1 (Updated) and Phase 2 Overall Integrated Plan in Response to June 6, 2013 Commission Order Modifying Licenses with Regard to Reliable Hardened Containment Vents Capable of Operation Under Severe Accident Conditions..

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Phase 1 (Updated) and Phase 2 Overall Integrated Plan in Response to June 6, 2013 Commission Order Modifying Licenses with Regard to Reliable Hardened Containment Vents Capable of Operation Under Severe Accident Conditions..
ML15364A014
Person / Time
Site: Limerick  Constellation icon.png
Issue date: 12/15/2015
From: Jim Barstow
Exelon Generation Co
To:
Document Control Desk, Office of Nuclear Reactor Regulation
References
EA-13-109, RS-15-301, TAC MF4418, TAC MF4419
Download: ML15364A014 (65)


Text

  • ExeL~on Generation Order No. EA-1 3-1 09 RS-1 5-30 1 December 15, 2015 U.S. Nuclear Regulatory Commission.

ATTN: Document Control Desk Washington, DC 20555-0001 Limerick Generating Station, Units 1 and 2 Renewed Facility Operating License Nos. NPF-39 and NPF-85 NRC Docket Nos. 50-352 and 50-353

Subject:

Phase 1 (Updated) and Phase 2 Overall Integrated Plan in Response to June 6, 2013 Commission Order Modifying Licenses with Regard to Reliable Hardened Containment Vents Capable of Operation Under Severe Accident Conditions (order Number EA-13-109)

Ref erences:

1. NRC Order Number EA-13-109, "Issuance of Order to Modify Licenses with Regard to Reliable Hardened Containment Vents Capable of Operation Under Severe Accident Conditions," dated June 6, 2013
2. NRC Interim Staff Guidance JLD-ISG-2015-01, "Compliance with Phase 2 Order EA-1 3-109, Order Modifying Licenses with Regard to Reliable Hardened Containment Vents Capable of Operation under Severe Accident Conditions", Revision 0, dated April 2015
3. NEI 13-02, "Industry' Guidance for Compliance With Order EA-13-1 09, BWR Mark I & II Reliable Hardened Containment Vents Capable of Operation Under Severe Accident Conditions", Revision 1, dated April 2015
4. Exelon Generation Company, LLC's Answer to June 6, 2013, Commission Order Modifying Licenses with Regard to Reliable Hardened Containment Vents Capable of Operation Under Severe Accident Conditions (Order Number EA-1 3-1 09), dated June 26, 2013
5. Exelon Generation Company, LLC Phase 1 Overall Integrated Plan in Response to June 6, 2013 Commission Order Modifying Licenses with Regard to Reliable Hardened Containment Vents Capable of Operation Under Severe Accident Conditions (Order Number EA-13-109), dated June 30, 2014 (RS-14-060)
6. Exelon Generation Company, LLC First Six-Month Status Report Phase 1 Overall Integrated Plan in Response to June 6, 2013 Commission Order Modifying Licenses with Regard to Reliable Hardened Containment Vents Capable of Operation Under Severe Accident Conditions (Order Number EA-13-i109), dated December 17, 2014 (RS-14-304)
7. Exelon Generation Company, LLC Second Six-Month Status Report Phase 1 Overall Integrated Plan in Response to June 6, 2013 Commission Order Modifying Licenses with Regard to Reliable Hardened Containment Vents Capable of Operation Under Severe Accident Conditions (Order Number EA-13-109), dated June 30, 2015 (RS-15-150)

U.S. Nuclear Regulatory Commission Integrated Plan Report to EA-13-109 December 15, 2015 Page 2

8. NRC letter to Exelon Generation Company, LLC, Limerick Generating Station, Units 1
  • and 2 - Interim Staff Evaluation Relating to Overall Integrated Plan in Response to Phase 1 of Order EA-13-109 (Severe Accident Capable Hardened Vents) (TAC Nos. MF4418 and MF441 9), dated April 1, 2015 On June 6, 2013, the Nuclear Regulatory Commission ("NRC" or "Commission") issued an order (Reference 1) to Exelon Generation Company, LLC (EGC). Reference 1 was immediately effective and directs EGC to require their BWRs with Mark I and Mark II containments to take certain actions to ensure that these facilities have a hardened containment vent system (HCVS) to remove decay heat from the containment, and maintain control of containment pressure within acceptable limits following events that result in loss of active containment heat removal capability while maintaining the Capability to operate under severe accident (SA) conditions resulting from an Extended Loss of AC Power (ELAP). Specific requirements are outlined in Attachment 2 of Reference 1.

Reference 1 requires submission of an Overall Integrated Plan (OIP) by June 30, 2014 for Phase 1 of the Order, and an OIP by December 31, 2015 for Phase 2 of the Order. The interim staff guidance (Reference 2) provides direction regarding the content of the OIP for Phase 1 and Phase 2. Reference 2 endorses industry guidance document NEI 13-02, Revision 1 (Reference 3) with clarifications and exceptions identified in Reference 2. Reference 4 provided the EGC initial response regarding reliable hardened containment vents capable of operation under severe accident conditions. Reference 5 provided the Limerick Generating Station, Units 1 and 2, Phase 10OIP. References 6 and 7 provided the first and second six-month status reports pursuant to Section IV, Condition 0.3 of Reference 1 for Limerick Generating Station.

The purpose of this letter is to provide both the third six-month update for Phase 1 of the Order pursuant to Section IV, Condition 0.3, of Reference 1, and the OIP for Phase 2 of the Order pursuant to Section IV, Condition D.2 of Reference 1, for Limerick Generating Station, Units 1 and 2. The third six-month update for Phase 1 of the Order is incorporated into the HCVS Phase 1 and Phase 2 overall integrated plan document which provides a complete updated Phase I OIP, a list of the Phase 10OIP open items, and addresses the NRC Interim Staff Evaluation open items for Phase 1 contained in Reference 8. Future six-month status reports will provide the updates for both Phase 1 and Phase 20OIP implementation in a single status report.

Reference 3, Section 7.0 contains the specific reporting requirements for the Phase 1 and Phase 20OIP. The information in the Enclosure provides the Limerick Generating Station, Units 1 and 2 HCVS Phase 1 and Phase 20OIP pursuant to Reference 2. The enclosed Phase 1 and Phase 20OIP is based on conceptual design information. Final design details and associated procedure guidance, as well as any revisions to the information contained in the Enclosure, will be provided in the six-month Phase 1 and Phase 20OIP updates required by Section IV, Condition D.3, of Reference 1.

This letter contains no new regulatory commitments. If you have any questions regarding this report, please contact David P.' Helker at 610-765-5525.

U.S. Nuclear Regulatory Commission Integrated Plan Report to EA-13-109 December 15, 2015 Page 3 I declare under penalty of perjury that the foregoing is true and correct. Executed on the 1 5 th day of December 2015.

Respectfully submitted, James Barstow Director - Licensing & Regulatory Affairs Exelon Generation Company, LLC

Enclosure:

Limerick Generating Station, Units 1 and 2, Overall Integrated Plan for Phase 1 and Phase 2 Requirements for Reliable Hardened Containment Vent System (HCVS) Capable of Operation Under Severe Accident Conditions cc: Director, Office of Nuclear Reactor Regulation NRC Regional Administrator - Region I NRC Senior Resident Inspector - Limerick Generating Station NRC Project Manager, NRR - Limerick Generating Station Mr. Charles H. Norton, NRR/JLD/PPSD/JOMB, NRC Mr. John D. Hughey, NRR/JLD/JOMB, NRC Director, Bureau of Radiation Protection - Pennsylvania Department of Environmental Resources R. R. Janati, Chief, Division of Nuclear Safety, Pennsylvania Department of Environmental Protection, Bureau of Radiation Protection

Enclosure 1 Limerick Generating Station, Units 1 and 2 Overall Integrated Plan for Phase 1 and Phase 2 Requirements for Reliable Hardened Containment Vent System (HCVS) Capable of Operation Under Severe Accident Conditions (61 pages)

Limerick Generating Station Units 1 and 2 Overall Integrated Plan for Reliable Hardened Vents Table of Contents:

Introduction Part 1: General Integrated Plan Elements and Assumptions Part 2: Boundary Conditions for Wet Well Vent Part 3: Boundary Conditions for EA-13-109, Option B.2 Part 3.1 Boundary Conditions for SAWA Part 3.1A Boundary Conditions for SAWA/SAWM Part 3.1B Boundary Conditions for SAWAISADV Part 4: Programmatic Controls, Training, Drills and Maintenance Part 5: Implementation Schedule Milestones : HCVS/SAWA Portable Equipment A: Sequence of Events Timeline - HCVS .1.A: Sequence of Events Timeline - SAWA / SAWM .1.B: Sequence of Events Timeline - SADV .1.C: SAWA I SAWM Plant-Specific Datum .1.D: SAWM SAMG Approved Language : Conceptual Sketches : Failure Evaluation Table : References : Changes/Updates to this Overall Integrated Implementation Plan : List of Overall Inte2rated Plan Oven Items Page 1 of 61

Limerick Generating Station Units 1 and 2 Overall Integrated Plan for Reliable Hardened Vents Introduction In 1989, the NRC issued Generic Letter 89-16, "Installation of a Hardened Wetwell Vent," (Reference 2) to all licensees of Boiling Water Reactors (BWRs) with Mark I containments to encourage licensees to voluntarily install a hardened wetwell vent. In response, licensees installed a hardened vent pipe from the suppression pool to some point outside the secondary containment envelope (usually outside the reactor building). Some licensees also installed a hardened vent branch line from the drywell.

On March 19, 2013, the Nuclear Regulatory Commission (NRC) Commissioners directed the staff per Staff Requirements Memorandum (SRM) for SECY-12-0157 (Reference 26) to require licensees with Mark I and Mark II containments to "upgrade or replace the reliable hardened vents required by Order EA-12-050 with a containment venting system designed and installed to remain functional during severe accident conditions." In response, the NRC issued Order EA-13-109, Issuance of Order to Modify Licenses with Regard to Reliable Hardened Containment Vents Capable of Operation Under Severe Accidents, June 6, 2013 (Reference 4). The Order (EA-13-109) requires that licensees of BWR facilities with Mark I and Mark II containment designs ensure that these facilities have a reliable hardened vent to remove decay heat from the containment, and maintain control of containment pressure within acceptable limits following events that result in the loss of active containment heat removal capability while maintaining the capability to operate under severe accident (SA) conditions resulting from an Extended Loss of AC Power (ELAP).

The Order requirements are applied in a phased approach where:

o"Phase 1 involves upgrading the venting capabilities from the containment wetwell to provide reliable, severe accident capable hardened vents to assist in preventing core damage and, if necessary, to provide venting capability during severe accident conditions." (Completed "no later than startup from the second refueling outage that begins after June 30, 2014, or June 30, 2018, whichever comes first.")

  • "Phase 2 involves providing additional protections for severe accident conditions through installation of a reliable, severe accident capable drywell vent system or the development of a reliable containment venting strategy that makes it unlikely that a licensee would need to vent from the containment drywell during severe accident conditions." (Completed "no later than startup from the first refueling outage that begins after June 30, 2017, or June 30, 2019, whichever comes first.")

The NRC provided an acceptable approach for complying with Order EA-13-109 through Interim Staff Guidance (JLD-ISG-2013-02) issued in November 2013 (Reference 6) and JLD-ISG-2015-01 issued April 2015 (Reference 31). The ISGs endorse the compliance approach presented in NEI 13-02 Revisions 0 and 1, Compliance with Order EA-13-109, Severe Accident Reliable Hardened Containment Vents (Reference 9), with clarifications. Except in those cases in which a licensee proposes an acceptable alternative method for complying with Order EA-13-109, the NRC staff will use the methods described in these ISGs to evaluate licensee compliance as presented in submittals required in Order EA-13-109.

The Order also requires submittal of an overall integrated plan which will provide a description of how the requirements of the Order will be achieved. This document provides the Overall Integrated Plan (OWP) for complying with Order EA-13-109 using the methods described in NEI 13-02 and endorsed by NRC JLD-ISG-2013-Q2 and JLD-ISG-2015-0l. Six month progress reports will be provided consistent with the requirements of Order EA- 13-109.

Page 2 of 61

Limerick Generating Station Units 1 and 2 Overall Integrated Plan for Reliable Hardened Vents The submittals required are:

  • OIP for Phase 1 of EA-13-109 was required to be submitted by Licensees to the NRC by June 30, 2014. The NRC requires periodic (6 month) updates for the Hardened Containment Vent System (HCVS) actions being taken. The first update for Phase 1 was due December 2014, with the second due June 2015.
  • OIP for Phase 2 of EA-13-109 is required to be submitted by Licensees to the NRC by December 31, 2015. It is expected that the December 2015 six month update for Phase 1 will be combined with the Phase 20ITP submittal by means of a combined Phase 1 and 20GIP.
  • Thereafter, the 6 month updates will be for both the Phase 1 and Phase 2 actions until complete, consistent with the requirements of Order EA-13-109.

Not___e: Per the Generic OIP, at the Licensee's option, the December 2015 six month update for Phase 1 may be independent of the Phase 20ITP submittal, but will require separate six month updates for Phases 1 and 2 until each phase is in compliance. Exelon has not selected this option.

The Limerick venting actions for the EA-13-109, Phase 1 severe accident capable venting scenario can be summarized by the following:

  • The HCVS will be initiated via manual action from either the Main Control Room (MCR) or from a Remote Operating Station (ROS) at the appropriate time based on procedural guidance in response to plant conditions from observed or derived symptoms. The ROS capabilities are limited to the Order EA-13-109 Requirement 1.2.5. Specifically, in case the HCVS flow path valves or the Argon purge flow cannot be opened from the MCR, the ROS provides a back-up means of opening the valve(s) that does not require electrical power or control circuitry.
  • The vent will utilize Containment Parameters of Pressure and Suppression Pool Level from the MCR instrumentation to monitor effectiveness of the venting actions.
  • The vent operation will be monitored by HCVS valve position, temperature and effluent radiation levels.
  • The HCVS motive force will be monitored and have the capacity to operate for 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> with installed equipment. Replenishment of the motive force will be by use of portable equipment prior to the installed motive force being exhausted.
  • Venting actions will be capable of being maintained for a sustained period of up to 7 days.

The Phase 2 actions can be summarized as follows:

  • Utilization of Severe Accident Water Management (SAWM) to control injection and Suppression Pool level to ensure the HCVS (Phase 1) Severe Accident Wetwell Vent (SAWV) will remain functional for the removal of decay heat from containment.
  • Ensure that the decay heat can be removed from the containment for seven (7) days using the HCVS or describe the altemnate method(s) to remove decay heat from the containment from the Page 3 of 61

Limerick Generating Station Units 1 and 2 Overall Integrated Plan for Reliable Hardened Vents time the HCVS is no longer functional until alternate means of decay heat removal are established that make it unlikely the drywell vent will be required for DW pressure control.

  • The SAWA and SAWM actions will be manually activated and controlled from areas that are accessible during severe accident conditions.
  • Parameters measured should be Drywell pressure, Suppression Pool level, SAWA flowrate and the HCVS parameters listed above.

Note: Although EA-13-109 Phase 2 allows selecting SAWA and a Severe Accident Capable Drywell Vent (SADV) strategy, Exelon has selected SAWA and SAWM.

Page 4 of 61

Limerick Generating Station Units 1 and 2 Overall Integrated Plan for Reliable Hardened Vents Part 1: General Integrated Plan Elements and Assumptions Extent to which the guidance, JLD-ISG-2013-02 , JLD-ISG-2015-01, and NEI 13-02 (Revision 1), are being followed. Identify any deviations.

Include a description of any alternatives to the guidance. A technicaljustification and basisfor the alternative needs to be provided. This will likely require a pre-meeting with the NRC to review the alternative.

Ref: JLD-ISG-2013-02, JLD-ISG-2015-01 Compliance will be attained for Limerick with no known deviations to the guidelines in JLD-JSG-2013-02 and NEI 13-02 for each phase as follows:

  • The (HCVS) will be comprised of installed and portable equipment and operating guidance.
  • SAWV - Permanently installed vent from the Suppression Pool to the top of the Reactor Building.
  • SAWA - A combination of permanently installed and portable equipment to provide a means to add water to the RPV following a severe accident and monitor system and plant conditions.
  • Severe Accident Water Management (SAWM) strategies and guidance for controlling the water addition to the RPV for the sustained operating period. (reference attachment 2.1 .D)
  • Unit 2 Phase 1 (wetwell): by the startup from the second refueling outage that begins after June 30, 2014, or June 30, 2018, whichever comes first. Currently scheduled for 2Q20 17.
  • Unit 1 Phase 1 (wetwell): by the startup from the second refueling outage that begins after June 30, 2014, or June 30, 2018, whichever comes first. Currently scheduled for 2Q2018.
  • Unit 1 Phase 2: (alternate strategy): by the startup from the first refueling outage that begins after June 30, 2017, or June 30, 2019, whichever comes first. Currently scheduled for 2Q20 18.
  • Unit 2 Phase 2 (alternate strategy): by the startup from the first refueling outage that begins after June 30, 2017, or June 30, 2019, whichever comes first. Currently scheduled for 2Q20 19.

If deviations are identified at a later date, then the deviations will be communicated in a future 6-month update following identification.

State Applicable Extreme External Hazard from NET 12-06, Section 4.0-9.0 List resultant determinationof screened in hazardsfrom the EA-12-049 Compliance.

Ref: NEI 13-02 Section 5.2.3 and D.1.2 The following extreme external hazards screen in for Limerick:

  • Seismic, external flooding (Storage and Transportation of Equipment during a Local Intense Precipitation),

Severe Storms with High Winds, Tornados, Snow, Ice, Extreme Cold and High Temperature.

The following extreme external hazards screen out for Limerick:

  • Sustained External Flooding Key Site assumptions to implement NET 13-02 strategies.

Provide key assumptions associatedwith implementation of HCVS Phase 1 Strategies.

Page 5 of 61

Limerick Generating Station Units 1 and 2 Overall Integrated Plan for Reliable Hardened Vents Part 1: General Integrated Plan Elements and Assumptions Ref: NEI 13-02, Revision 1, Section 2 NET 12-0)6 Revision 0 Mark 11II Generic HCVS Related Assumptions:

Applicable EA-12-049 (Reference 3) assumptions:

049-1. Assumed initial plant conditions are as identified in NEI 12-06, Section 3.2.1.2, items 1 and 2 (Reference 8).

049-2. Assumed initial conditions are as identified in NEI 12-06, Section 3.2.1.3, items 1, 2, 4, 5, 6 and 8 (Reference 8).

049-3. Assumed reactor transient boundary conditions are as identified in NHI 12-06, Section 3.2.1.4, items 1, 2, 3 and 4 (Reference 8).

049-4. No additional events or failures are assumed to occur immediately prior to or' during the event, including security events, except for the failure of Reactor Core Isolation Cooling (RCIC) or High Pressure Coolant Injection (HPCI) (Reference NEI 12-06, Section 3.2.1.3, item 9 (Reference 8)).

049-5. At time=0 the event is initiated and all rods insert and no other event beyond a common site ELAP is

  • occurring at any or all of the units.

049-6. At time=l hour (time sensitive at a time greater than 1 hour1.157407e-5 days <br />2.777778e-4 hours <br />1.653439e-6 weeks <br />3.805e-7 months <br />) an ELAP is declared and actions begin as defined in EA-12-049 compliance.

049-7. DC power and distribution can be credited for the duration determined per the EA-12-049 (FLEX) methodology for battery usage, (greater than approximately 6 hours6.944444e-5 days <br />0.00167 hours <br />9.920635e-6 weeks <br />2.283e-6 months <br /> with a calculation limiting value of approximately 7 hrs.) (NEI 12-06, Section 3.2.1.3 item 8 (Reference 8)).

049-8. Deployment resources are assumed to begin arriving at hour 6 and fully staffed by 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br />.

049-9. All activities associated with EA-12-049 (FLEX) that are not specific to implementation of the HCVS, including such items as debris removal, communication, notifications, Spent Fuel Pool (SFP) level and makeup, security response, opening doors for cooling, and initiating conditions for the events, can be credited as previously evaluated for FLEX. (Refer to assumption 109-02 below for clarity on SAWA)

(Reference 34).

Applicable EA- 13-109 (Reference 4) generic assumptions:

109-1. Site response activities associated with EA-13-109 actions are considered to have no access limitations associated with radiological conditions while RPV level is above 2/3 core height (core damage is not expected). This is further addressed in HCVS-FAQ-12 (Reference 35).

109-2. Portable equipment can supplement the installed equipment after 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> provided the portable equipment credited meets the criteria applicable to the HCVS. An example is use of portable air supply equipment that is credited to recharge air lines for HCVS components after 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br />. The portable air supply used must be demonstrated to meet the "SA Capable" criteria that are defined in NEI 13-02 Section 4.2.4.2 and Appendix D Section D. 1.3 (Reference 9). This assumption does not apply to Phase 2 SAWAISAWM because SAWA equipment needs to be connected and placed in service within 8 hours9.259259e-5 days <br />0.00222 hours <br />1.322751e-5 weeks <br />3.044e-6 months <br /> from the time of the loss of RPV injection (Reference 35).

109-3. SFP Level is maintained with either on-site or o'ff-site resources such that the SFP does not contribute to the analyzed source term (Reference 18).

Page 6 of 61

Limerick Generating Station Units 1 and 2 Overall Integrated Plan for Reliable Hardened Vents Part 1: General Integrated Plan Elements and Assumptions 109-4. Existing containment components design and testing values are governed by existing plant containment

, criteria (e.g., Appendix J) and are not subject to the testing criteria from NEI 13-02 (Reference 16 and NEI 13-02, Section 6.2.2 (Reference 9)).

109-5. Classical design basis evaluations and assumptions are not required when assessing the operation of the HCVS. The reason that this is not required is that the order postulates an unsuccessful mitigation of an event such that an ELAP progresses to a severe accident with ex-vessel core debris that classical design basis evaluations are intended to prevent (Reference NEI 13-02, Section 2.3.1 (Reference 9)).

109-6. HCVS manual actions require minimal operator steps and can be performed in the postulated thermal radiological environment at the location of the step(s) (e.g., load stripping, control switch manipulation, valving-in gas bottles) are acceptable to obtain HCVS venting dedicated functionality (Reference 12). This assumption does not apply to Phase 2 SAWA/SAWM because SAWA equipment needs to be connected and placed in service within 8 hours9.259259e-5 days <br />0.00222 hours <br />1.322751e-5 weeks <br />3.044e-6 months <br /> from the time of the loss of RPV injection and will require more than minimal operator action.

109-7. HCVS dedicated equipment is defined as vent process elements that are required for the HCVS to function in an ELAP event that progresses to core melt ex-vessel (Reference 13 and 21). This assumption does not apply to Phase 2 SAWA/SAWM because SAWA equipment is not dedicated to HCVS but shared to support FLEX functions. This is further addressed in HCVS-FAQ-1 1 (Reference 34).

109-8. Use of MAAP Version 4 or higher provides adequate assurance of the plant conditions (e.g., RPV water level, temperatures, etc.) assumed for Order EA-13-109 Beyond Design Basis External Event (BDBEE) and SA HCVS operation (Reference FLEX MAAP Endorsement ML13190A201 (Reference 29)). Additional analysis using RELAP5/MOD 3,' GOTHIC, and MICROSHIELD, etc., are acceptable methods for evaluating environmental conditions in other portions of the plant, provided that the specific version utilized is documented in the analysis. MAAP Version 5 was used to develop EPRI Technical Report 3002003301 (Reference 39) to support drywell temperature response to SAWA under severe accident conditions.

109-9. NRC Published Accident evaluations (e.g. NUREG-1935, SECY-12-0157, NUREG 1465) as related to Order EA-13-109 conditions are acceptable as references (Reference NEI 13-02, Section 8 (Reference 9)).

109-10. Permanent modifications installed or planned per EA-12-049 are assumed implemented and may be credited for use in Order EA-13-109 response.

109-11. This Overall Integrated Plan is based on Emergency Operating Procedure (EOP) changes consistent with Emergency Procedures Guidelines/Severe Accident Guidelines (EPG/SAGs) Revision 3 as incorporated per the site's EOP/Severe Accident Procedure (SAP) procedure change process. This assumption does not apply to Phase 2 SAWM because SAWM is not part of revision 3 (Refer to Attachment 2.1 .D for SAWM Severe Accident Management Guidelines (SAMG) changes approved by the Boiling Water Reactor Owners Group (BWROG) Emergency Procedures Committee).

109-12. Under the postulated scenarios of Order EA-13-109, the Main Control Room is adequately protected from excessive radiatio~n dose as per General Design Criterion (GDC) 19 in 10CFR50 Appendix A and no further evaluation of its use as the preferred HCVS control location is required provided that the HCVS routing is a sufficient distance away from the MCR or is shielded to minimize impact to the MCR dose. In addition, adequate protective clothing and respiratory protection are available if required to address contamination issues (Reference 12 and 20).

109-13. The suppression pool/wetwell of a BWR Mark I1II containment is considered to be bounded by assuming a Page 7 of 61

Limerick Generating Station Units 1 and 2 Overall Integrated Plan for Reliable Hardened Vents Part 1: General Integrated Plan Elements and Assumptions saturated environment for the duration of the event response because of the water/steam interactions.

109-14. RPV depressurization is directed by the EPGs in all cases prior to entry into the SAGs (Reference NEI 13-02 Rev 1, Section 1.1.3 (Reference 9)).

109-15. The Severe Accident impacts are assumed on one unit only due to the site compliance with NRC Order EA-12-049. However, each BWR Mark I and II under the assumptions of NRC Order EA-13-109 (Reference

4) ensures the capability to' protect containment exists for each unit (Reference 12). This is further addressed in HCVS-FAQ-10 (Reference 33).

Plant Specific HCVS Related Assumptions/Characteristics:

Limerick-i EA-12-049 (Reference 3) FLEX actions to restore power are sufficient to ensure continuous operation of non-dedicated containment instrumentation.

Limerick -2 Modifications that allow a FLEX generator to recharge the HCVS battery are assumed to have been installed such that a FLEX generator can be credited for HCVS operation beyond the initial 24-hour sustained operational period.

Limerick -3 The rupture disk will be manually breached from the MCR if required for anticipatory venting during an ELAP.

Limerick -4 The plant layout of buildings and structures are depicted in Sketch 3B. Note the Main Control Room is located in the Control Structure and has substantial structural walls and features independent of the Reactor Building. The HCVS vent routing is through the Reactor Building to the railroad bay hoistway.

This vent is routed vertically in the hoistway and through the South Stack to above the Reactor Building Roof.

Limerick -5 The HCVS external piping is all above 30-feet from ground level, consists solely of large bore (14-inches nominal diameter) piping and its piping supports, and has less than 300 square feet of cross section. The HCVS external piping meets the reasonable protection requirements of HCVS-WP-04 (Reference 32).

Page 8 of 61

Limerick Generating Station Units 1 and 2 Overall Integrated Plan for Reliable Hardened Vents Part 2: Boundary Conditions for Wetwell Vent Provide a sequence of events and identify any time or environmental constraint required for success including the basis for the constraint.

HCVS Actions that have a time constraint to be successfud should be identified with a technical basis and a justification provided that the time can reasonably be met (for example, action to open vent valves).

HCVS Actions that have an environmental constraint (e.g. actions in areas of High Thermal stress or High Dose areas) should be evaluatedper guidance.

Describe in detail in this section the technical basisfor the constraints identified on the sequence of events timeline attachment.

See attachedsequence of events time line (Attachment 2A).

Ref: EA-13-109 Section 1.1.1, 1.1.2, 1.1.3 / NEI 13-02 Section 4.2.5, 4.2.6. 6.1.1 Exelon plans to install a wetwell (WW) flow path in each unit at Limerick that has two dedicated primary containment isolation valves and a downstream rupture disc that is routed separate from the other unit. The discharge from each unit is routed separately through a pipe that discharges above the Reactor Building's roof.

Each unit will have dedicated motive gas bottles for HCVS valves, Argon Purge system, and DC power for HCVS components that are not shared with any other system or function. The HCVS does not rely on FLEX.

The existing containment instrumentation (pressure and WW level) are not considered HCVS components, and power for containment instrumentation is through the FLEX Diesel Generator (DG) provided through the actions for EA-12-049 (Reference 3). Also, the FLEX DG will be credited for recharging the HCVS battery after the initial 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> after the event.

The operation of the HCVS will be designed to minimize the reliance on operator actions in response to hazards listed in Part 1. Initial operator actions will be completed by trained plant personnel and will include the capability for remote-manual initiation from the HCVS control station. A list of the remote manual actions performed by plant personnel to open the HCVS vent path can be found in the following table (Table 2-1). A HCVS ELAP Failure Evaluation table, which shows alternate actions that can be performed, is included in Attachment 4.

Page 9 of 61

Limerick Generating Station Units 1 and 2 Overall Integrated Plan for Reliable Hardened Vents Part 2: Boundary Conditions for Wetwell Vent Table 2-1 HCVS Remote Manual Actions Primary Action Primary Location I Notes Component

1. Energize the HCVS MCR *This action is not required for operation at power supply to the the ROS.

HCVS components

2. Enable the motive air ROS Alternate control via manual valves at the for the HCVS valves ROS.

and enable the Argon purge system

3. Isolate leak-off *ROS Required ste~pto prevent venting into the.

connection upstream of SReactor Build inc throucqh the small leak-off the rupture disc path.

4..... the Rupture MCR.......Required...............o....a........ic.....pat......ry.....venting 4:..........................................Breach RRe u n andrsevereen[ig-nd e er ....

Disc by opening the accident conditions.

Argon Purge .Line for the specified amount of time

5. Open Wetwell PCIVs Key locked hand switches This action is not required for operation at in the MCR panel the ROS.

6.Aingenerator to RSPrior.to depletion of the HCVS battery HCVS battery charger supply, actions will be required to recharge the battery.

7. Replace pressurized ROS Prior to depletion of the pressurized gas gas source for HCVS sources, actions will be required to connect operation back-up sources at a time greater than 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br />. Replacement of pneumatic bottles and/or compressor.

8..Replenish Argon ROS Prio rto depletion of the pressurized gas bottles sources, actions will be required to connect back-up sources at a time greater than 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br />.

ISE Open Item 1 A, Sequence of Events Timeline, was developed to identify required operator response times and potential environmental constraints. This timeline is based upon the following three sequences:

.1. Sequence 1 is based upon the action response times developed for FLEX when utilizing anticipatory venting in a BDBEE without core damage.

2. Sequence 2 is based on SECY-12-0 157 (Reference 26) long-term station blackout (LTSBO) (or ELAP) with a failure of RCIC after a blackout starts where failure occurs because of subjectively assuming Page 10 of 61

Limerick Generating Station Units 1 and 2 Overall Integrated Plan for Reliable Hardened Vents Part 2: Boundary Conditions for Wetwell Vent over injection.

3. Sequence 3 is based on NUREG-1935 (Reference 37) (SOARCA) results for a prolonged SBO (or FLAP) with loss of RCIC without blackout start.

The following is a discussion of time constraints identified in Attachment 2A for the 3 timeline sequences identified above:

  • The use of HCVS will be governed by site procedures to maintain containment parameters below design limits and within the limits that allow continued use of RCIC. The reliable operation of HCVS will be ensured by designing to the seismic requirements identified in NEI 13-02 (Reference 9), will be powered by DC power from a dedicated power source, and HCVS valves are supplied with motive force from motive gas bottles. HCVS controls and instrumentation will be DC powered. Valves will be operable from the HCVS control panel in the MCR, or at the ROS. DC power and motive gas will be available for 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> from permanently installed sources. Containment pressure and WW indication will be initially powered from existing safety related batteries and maintained by FLEX generators. Thus initiation of the HCVS from the MCR or the Remote Operating Station is acceptable because the actions can be performed any time after declaration of an FLAP until the venting is needed for the BDBEE venting.

This action can also be performed for SA HCVS operation which occurs at a time further removed from an ELAP declaration as shown in Attachment 2.

  • Within 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br />, the permanently installed motive gas bottles at the ROS will be replaced, as required, to maintain sustained operation at the ROS. This can be performed at any time prior to 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> to ensure adequate capacity is maintained; therefore, this time constraint is not limiting.
  • Within 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br />, the permanently installed Argon bottles at the ROS will be replaced, as required, to maintain sustained operation. Argon purging is required only if the FLAP progresses to severe accident conditions.
  • Within 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br />, a DC power source will be installed or aligned through breaker alignment and connected to recharge the dedicated HCVS power supply to maintain sustained operation.
  • The FLEX strategies have been designed to ensure that all critical DC power supplies will be maintained during a FLEX event by ensuring the FLEX diesel generators are deployed and operating prior to complete discharge of the DC batteries which will ensure the availability of containment pressure and WW level indication.

Discussion of radiological, temperature, other environmental constraints identified in Attachment 2A

  • Actions to initiate HCVS operation are taken from the MCR or from the ROS in each unit's Diesel Generator Building corridor. Both locations have significant shielding and/or physical separation from radiological sources. Non-radiological habitability for the MCR is being addressed as part of the Limerick FLEX response. The ROS location in the Diesel Building corridor has no heat sources and will have open doors to provide ventilation.

ISE Open Item 3 Page 11 of 61

Limerick Generating Station Units 1 and 2 Overall Integrated Plan for Reliable Hardened Vents Part 2: Boundary Conditions for Wetwell Vent Provide Details on the Vent characteristics.

Vent Size and Basis (EA-13-109 Section 1.2.1/INEJ 13-02 Section 4.1.1)

What is the plants licensed power? Discuss any plansfor possible increases in licensed power (e.g. MUR, EPU). What is the nominal diameter of the vent pipe in inches? Is the basis determined by venting at containment design pressure, PCPL, or some other criteria (e.g. anticipatory venting)?

Vent Capacity (EA-13-109 Section 1.2.1/INEI 13-02 Section 4.1.1)

Indicate any exceptions to the 1 % decay heat removal criteria, including reasonsfor the exception. Provide the heat capacity of the suppressionpool in terms of time versus pressurizationcapacity, assuming suppression pool is the injection source.

Vent Path and Discharge (EA-13-109 Section 1.1.4. 1.2.2 /NEI 13-02 Section 4.1.3. 4.1.5 and Appendix FIG)t Provide a description of Vent path, release path, and impact of vent path on other vent element items.

Power and Pneumatic Supply Sources (EA 1 09 Section 1.2.5 & 1.2.6 /NEI 13-02 Section 4.2.3. 2.5, 4.2.2.

4.2.6. .6.1)

Provide a discussion of electricalpower requirements, including a description of dedicated 24 hour2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> power supply from permanently installed sources. Include a similar discussion as above for the valve motive force requirements. Indicate the area in the plantfrom where the installed/dedicatedpower and pneumatic supply sources are coming.

Indicate the areas where portable equipment will be staged after the 24 hour2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> period, the dose fields in the area, and any shielding that would be necessary in that area.

Location of Control Panels (EA-13-109 Section 1.1.1. 1.1.2. 1.1.3, 1.1.4. 1.2.4. 1.2.5/NEI 13-02 Section 4.1.3. 4.2.2. 4.2.3. 4.2.5. 4.2.6, 6.1.1. and Appendix FIG)

Indicate the location of the panels, and the dose fields in the 'areaduring severe accidents and any shielding that would be required in the area. This can be a qualitative assessment based on criteria in NEI 13-02.

Hydrogen (EA 1 09 Section 1.2.10. &1.2.11. and 1.2.12/INEI 13-02 Section 2.3,2.4. 4.1.1. 4.1.6, 4.1.7. 5.1,

& Appendix H)

State which approach or combination of approachesthe plant will take to addr~ess the control offlammable gases, clearly demarcating the segments of vent system to which an approachapplies.

Unintended Cross Flow of Vented Fluids (EA-13-109 Section 1.2.3, 1.2.12 / NE1 13-02 Section 4.1.2. 4.1.4, 4.1.6 and Appendix H)

Provide a description to eliminate/minimize unintended crossflow of vented fluids with emphasis on interfacing ventilation systems (e.g. SGTS). What design features are being included to limit leakage through interfacing valves or Appendix J type testingfeatures?

Prevention of InadvertentActuation (EA-13-109 Section 1.2.7/NEI 13-02 Section 4.2.1)

The HCVS shall include means to prevent inadvertent actuation.

Component Qualifications (EA-13-109 Section 2.1 /NEI 13-02 Section 5.1)

State qualification criteria based on use of a combination of safety related and autgmented quality dependent on Page 12 of 61

Limerick Generating Station Units 1 and 2 Overall Integrated Plan for Reliable Hardened Vents Part 2: Boundary Conditions for Wetwell Vent the location,finction and interconnectedsystem requirements.

Monitoring~of HCVS (Order Elements 1.1.4, 1.2.8, 1.2.9/NEI 13-02 4.1.3. 4.2.2, 4.2.4. and Appendix FIG)

Provide a description of instruments used to monitor HCVS operationand effluent. Powerfor an instrument will require the intrinsically safe equipment installed as part of the power sourcing.

Component reliableand ruggi~ed performance (EA-13-109 Section 2.2 I NEI113-02 Section 5.2. 5.3)

HCVS components including instrumentationshould be designed, as a minimum, to meet the seismic design requirements of the plant.

Components including instrumentation that are not required to be seismically designed by the design basis of the plant should be designedfor reliable and rugged performance that is capable of ensuring HCVS functionalityfollowing a seismic event. (Reference JLD-ISG-2012-01 and JLD-ISG-2012-O3for seismic details.)

The components including instrumentation external to a seismic category 1 (or equivalent building or enclosure should be designed to meet the external hazards that screen in for the plant as defined in guidance NEI 12-06 as endorsed by JLD-ISG-12-O1 for Order EA-12-049.

Use of instruments and supporting components with known operatingprinciples that are supplied by manufacturers with commercial quality assuranceprograms, such as 1S09001. The procurementspecifications shall include the seismic requirements and/or instrument design requirements, and specify the needfor commercial design standards and testing under seismic loadings consistent with design basis values at the instrument locations.

Demonstration of the seismic reliability of the instrumentation through methods that predict performance by analysis, qualificationtesting under simulated seismic conditions, a combination of testing and analysis, or the use of experience data. Guidance for these is based on sections 7, 8, 9, and 10 of IEEE Standard 344-2004, "IEEE Recommended Practicefor Seismic Qualificationof Class JE Equipmentfor Nuclear Power Generating Stations," or a substantially similar industrialstandardcould be used.

Demonstration that the instrumentation is substantially similar in design to instrumentation that has been previously tested to seismic loading levels in accordance with the plant design basis at the location where the instrument is to be installed (g-levels and frequency ranges). Such testing and analysis should be similar to that performed for the plant licensing basis.

Vent Size and Basis The HCVS wetwell path is designed for venting steam/energy at a nominal capacity of 1%of 4000 MWt at a drywell pressure of 55 psig accounting for downcomer submergence and assuming nominal suppression pool water level. The thermal power assumes a power uprate of approximately 13.8% above the currently licensed thermal power of 3515 MWt. Although a power uprate is not planned for Limerick at this time, the HCVS wetwell path will be designed for the higher MWt thermal power for any potential future uprates. The size of the wetwell portion of the HCVS will provide adequate capacity to meet or exceed Order EA-13-109 criteria.

Vent Capacity The 1% value at Limerick assumes that the suppression pool pressure suppression capacity is sufficient to absorb the decay heat generated during the first 3 hours3.472222e-5 days <br />8.333333e-4 hours <br />4.960317e-6 weeks <br />1.1415e-6 months <br />. The vent would then be able to prevent containment Page 13 of 6l

Limerick Generating Station Units 1 and 2 Overall Integrated Plan for Reliable Hardened Vents Part 2: Boundary Conditions for Wetwell Vent pressure from increasing above the containment design pressure. As part of the detailed design, the duration of suppression pooi decay heat absorption capability will be confirmed.

1SE Open Item 4 Vent Path and Discharge The WW line will have two dedicated primary containment isolation valves located outboard of the primary containment and a downstream rupture disc. The WW vent line is routed horizontally through the Reactor Building and up through the Railroad Bay, then penetrates the Reactor Building wall into the South Stack. The WW line then is routed vertically on the outside of the Reactor Building wall through the South Stack to a point above the top of the Reactor Building. There are no interconnected systems and there is no sharing of any flow path between the two units.

The HCVS discharge path will be routed to a point above any adjacent structure. The cooling towers at Limerick have a higher elevation but are not adjacent to the Reactor Building. This discharge point is just above that unit's Reactor Building and will follow the guidance of FAQ-HCVS-04 (Reference 15) such that the release point will vent away from emergency ventilation system intake and exhaust openings, main control room location, location of HCVS portable equipment, access routes required following an ELAP and BDBEE, and emergency response facilities to the extent reasonably possible; however, these must be considered in conjunction with other design criteria (e.g., flow capacity) and pipe routing limitations, to the degree practical.

The current design for the external piping meets the reasonable tornado missile protection criteria of HCVS-WP-04 (Reference 38). The external piping consists solely of large bore piping and its supports, is above 30 feet from ground level, and has less than 300 square feet of cross section.

Phase I Open Item 7 Power and Pneumatic Supply Sources All electrical power required for operation of HCVS components will be from a dedicated HCVS DC battery source with permanently installed capacity for the first 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> and design provisions for recharging to maintain sustained operation.

Motive gas supply to the HCVS valves is provided by a dedicated bank of gas bottles with permanently installed capacity for the first 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> and design provisions for replacing motive gas supply to maintain sustained operation. The initial stored motive gas will be designed for a minimum of 8 vent cycles for the HCVS valves for the first 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br />. The 8 vent cycles is defined as initially opening all valves in the WW flow path, and then closing and reopening one of the valves in the flow path 7 times.

The HCVS flow path valves are air-operated valves (AOV) with air-to-open and spring-to-close. Opening the valves from the HCVS control panel located in the MCR requires energizing a DC powered solenoid operated valve (SOV) and providing motive gas.

An assessment of temperature and radiological conditions will be performed to ensure that operating personnel can safely access and operate controls at the Remote Operating Station based on time constraints listed in .

1SE Open Item 3 Page 14 of 61

Limerick Generating Station Units 1 and 2 Overall Integrated Plan for Reliable Hardened Vents Part 2: Boundary Conditions for Wetwell Vent All permanently installed HCVS equipment, including any connections required to supplement the HCVS operation during an ELAP (i.e., DC power and motive force pressurized gas) will be located in areas reasonably protected from defined hazards listed in Part 1 of this report.

All valves required to open the flow path will be designed for remote manual operation following an ELAP, such that the primary means of valve manipulation does not rely on use of a handwheel, reach-rod or similar means that requires close proximity to the valve (Reference 14). The preferred method is opening from the MCR through the control switch that energizes the AOVs SOV. The back-up method is from the ROS by repositioning valves on the pneumatic air line: this allows opening and closing of a valve from the ROS without reliance on any electrical power or control circuit. Accessibility to the ROS will be verified during the detailed design phase.

Any supplemental connections will be pre-engineered to minimize man-power resources and address environmental concerns. Required portable equipment will be reasonably protected from screened in hazards listed in Part 1 of this OTP.

Access to the locations described above will not require temporary ladders or scaffolding.

Location of Control Panels The HCVS design allows initiating and then operating and monitoring the HCVS from the Main Control Room (MCR) and in addition, opening valve(s) from the ROS in case of a DC circuit failure. The tentative location for the ROS is in the Emergency Diesel Generator Corridor. The MCR location is protected from adverse natural phenomena and is the normal control point for Plant Emergency Response actions. The ROS will be evaluated to ensure acceptable temperature and dose consequences.

Hydrogen As required by EA-13-109, Section 1.2.11, the HCVS design will include an Argon purge system that will be connected just downstream of the second PCJV. It will be designed to prevent hydrogen detonation downstream of the second PCIV. The Argon purge system will have a switch for the control valve in the MCR to allow opening the purge for the designated time, but it will also allow for local operation in the ROS in case of a DC power or control circuit failure. The Argon purge will only be utilized following severe accident conditions when hydrogen is being vented. The installed capacity for the Argon purge system will be sized for 8 purges within the first 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> of the ELAP. The design will allow for Argon bottle replacement for continued operation past 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br />.

The Argon purge system can also be used to breach the rupture disc if anticipatory venting is required before reaching the rupture disc setpoint. The MCR panel will include an indication of Argon pressure to the HCVS path to verify that the Argon purge system flow is occurring.

Unintended Cross Flow of Vented Fluids The HCVS uses dedicated PCIVs for containment isolation. Unit 1 HCVS has a dedicated flow path that has neither any interconnected-systems nor sharing with the opposite unit's HCVS. Unit 2 HCVS shares a primary containment penetration with the Unit 2 Containment Atmospheric Control (CAC) System. However, the Unit 2 HCVS and CAC systems are otherwise independent flow paths including separate PCIVs downstream of the containment penetration.

Page 15 of 61

Limerick Generating Station Units 1 and 2 Overall Integrated Plan for Reliable Hardened Vents Part 2: Boundary Conditions for Wetwell Vent Prevention of Inadvertent Actuation Emergency Procedure Guidelines (EPG) provide guidance that the HCVS is not to be used to defeat containment integrity during any design basis transients and accident. In addition, the HCVS will be designed to provide features to prevent inadvertent actuation due to a design error, or equipment malfunction.

To prevent inadvertent actuation, there are two PCIVs in series and a downstream rupture disc. The PCIV valves are fail-close AOVs. They are air-to-open, spring-to-close AOVs that require energizing a SOV to allow the motive air to open the valve. Each PCIV is controlled by its own key-locked switch. In addition, the DC power to the SOV and the motive air supplied will normally be disabled to prevent inadvertent operation. The rupture disc burst pressure is high enough as to not inadvertently rupture during normal operation but is below the Primary Containment Pressure Limit (PCPL).

Component Qualifications The HCVS components and components that interface with the HCVS are routed in seismically qualified structures.

The PCIVs and rupture disc are safety related as those components are part of the containment pressure boundary. During normal or design basis operations, the closed PCIVs and downstream rupture disc serve as a pressure boundary to prevent release of radioactive material. HCVS components downstream of the rupture disc will not be safety-related, but will be designed to seismic 1 requirements.

The HCVS components (SOVs and instrumentation) except for the radiation monitor will be powered from a normally de-energized, dedicated power supply that will not be safety-related but will be considered Augmented Quality. The configuration of the radiation monitor requires it be powered to maintain calibration and setpoints; therefore, it will not be de-energized. However, if any HCVS electrical or controls component interfaces with Class IE power sources, it will be considered safety-related up to and including appropriate isolation devices such as fuses or breakers, as their failure could adversely impact containment isolation and/or a safety-related power source.

Newly installed piping and valves will be seismically qualified to handle the forces associated with the Safe Shutdown Earthquake. Electrical and controls components will be seismically qualified.

The HCVS instruments, including valve position indication, process instrumentation, radiation monitoring, and support system monitoring, will be qualified by using one or more of the three methods described in the ISG, which includes:

1. Purchase of instruments and supporting components with known operating principles from manufacturers with commercial quality assurance programs (e.g., 1S09001) where the procurement specifications include the applicable seismic requirements, design requirements, and applicable testing.
2. Demonstration of seismic reliability via methods that predict performance described in IEEE 344-2004 (Reference 28).
3. Demonstration that instrumentation is substantially similar to the design of instrumentation previously qualified.

Instrument Qualification Method*

Page 16 of 61

Limerick Generating Station Units 1 and 2 Overall Integrated Plan for Reliable Hardened Vents Part 2: Boundary Conditions for Wetwell Vent HCVS Process Temperature I SO9001 / IEEE 344-2004 / Demonstration HCVS Process Radiation Monitor IS09001 / IEEE 344-2004 ! Demonstration HCVS Valve Position Indication IS09001 I IEEE 344-2004 / Demonstration HCVS Pneumatic Supply Pressure 1SO9001 / IEEE 344-2004 / Demonstration HCVS Electrical Power Supply Availability ISO9001 / IEEE 344-2004 ! Demonstration HCVS Argon System Purge Pressure ISO9001 I IEEE 344-2004 I Demonstration

  • The specific qualification method used for each required HCVS instrument will be reported in future 6-month status reports.

Monitoring of HCVS The Limerick wetwell HCVS will be capable of being remote-manually operated during sustained operations from a control panel located in the main control room (MCR) and will meet the requirements of Order EA 109 element 1.2.4. The MCR is a readily accessible location with no further evaluation required (Generic Assumption 109-12). Additionally, to meet the intent for a secondary control location of section 1.2.5 of Order EA-13-109, a readily accessible ROS will also be incorporated into the HCVS design as described in NEI 13-02 section 4.2.2.1.2.1 (Reference 9). The controls and indications at the ROS location will be accessible and functional under a range of plant conditions, including severe accident conditions with due consideration to source term and dose impact on operator exposure, Extended Loss of AC Power (ELAP), and inadequate containment cooling. An evaluation will be performed to determine accessibility to the location, habitability, staffing sufficiency, and communication capability with Vent-use decision makers.

The wetwell HCVS will include means to monitor the status of the vent system in the MCR and to monitor DC power, Argon pressure, and motive gas pressure at the ROS. The proposed design for the HCVS includes control switches in the MCR with valve position indication. The HCVS controls will meet the environmental and seismic requirements of Order EA- 13-109 for the plant severe accident with an ELAP. The ability to open/close these valves multiple times during the event's first 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> will be provided by dedicated motive air and DC power. Beyond the first 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br />, the ability to maintain these valves open or closed will be maintained by sustaining the motive air and DC power.

The wetwell HCVS will include indications for effluent temperature, valve position, and effluent radiation levels at the MCR.

Other instrumentation that supports HCVS function will be provided in the MCR. This includes existing containment pressure and wetwell level indication. This instrumentation is not required to validate HCVS function and is therefore not powered from the dedicated HCVS batteries. However, these instruments are expected to be available since the FLEX DG supplies the station battery charger for these instruments and will be installed prior to depletion of the station batteries.

Component reliable and rugged performance Unless otherwise required to be safety-related, Augmented Quality requirements will be applied to the components installed in response to this Order.

Non-safety related piping, electrical power supply, valve actuator pneumatic supply, and instrumentation (local and remote) components, will be designed/analyzed to conform to the requirements consistent with the Page 17 of 61

Limerick Generating Station Units 1 and 2 Overall Integrated Plan for Reliable Hardened Vents Part 2: Boundary Conditions for Wetwell Vent applicable design codes (e.g., Non-safety, Seismic Category 1, B3 1.1) for the plant and to ensure functionality following a design basis earthquake.

Additional modifications required to meet Order EA-13-109 will provide reliability at the postulated vent pipe conditions (temperature and radiation levels). The instrumentation/power supplies/cables/connections (components) will be qualified for temperature, pressure, radiation level, and total integrated radiation dose appropriate for that location (e.g., near the effluent vent pipe or at the HCVS ROS location).

Conduit design and/or cable trays will be installed to Seismic Category 1 criteria.

Pipe will exit the Reactor Building greater than 30 feet above grade; therefore, additional missile shielding is not required (refer to Limerick-5 assumption).

If the instruments are purchased as commercial-grade equipment, they will be qualified to operate under severe accident environment as required by NRC Order EA-13-109 and the guidance of NEI 13-02.

For the ITCVS instruments required after a potential seismic event, the following methods will be used to verify that the design and installation is reliable / rugged and thus capable of ensuring HCVS functionality following a seismic event. Applicable instruments are rated by the manufacturer (or otherwise tested) for seismic impact at levels commensurate with those of postulated severe accident event conditions in the area of instrument component use using one or more of the following methods:

  • demonstration of seismic motion will be consistent with that of existing design basis loads at the installed location;
  • substantial history of operational reliability in environments with significant vibration with a design envelope inclusive of the effects of seismic motion imparted to the instruments proposed at the location;
  • adequacy of seismic design and installation is demonstrated based on the guidance in Sections 7, 8, 9, and 10 of IEEE Standard 344-2004, IEEE Recommended Practice for Seismic Qualification of Class lE Equipment for Nuclear Power Generating Stations, (Reference 28) or a substantially similar industrial standard;
  • demonstration that proposed devices are substantially similar in design to models that have been previously tested for seismic effects in excess of the plant design basis at the location where the instrument is to be installed (g-levels and frequency ranges); or
  • seismic qualification using seismic motion consistent with that of existing design basis loading at the installation location.

Page 18 of 61

Limerick Generating Station Units 1 and 2 Overall Integrated Plan for Reliable Hardened Vents Part 2: Boundary Conditions for WW Vent - BDBEE Venting Determine venting capability for BDBEE Venting, such as may be used in an ELAP scenario to mitigate core damage.

Ref: EA-13-109 Section 1.1.4 /NEI 13-02 Section 2.2 First 24 Hour Coping Detail Provide a general description of the venting actionsfor first 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> using installed equipment including station modifications that are proposed.

Ref: EA-13-109 Section 1.2.6 I NEI 13-02 Section 2.5, 4.2.2 The operation of the HCVS will be designed to minimize reliance on operator actions for response to an ELAP and BDBEE hazards identified in Part 1 of this OIP. Immediate operator actions will be completed by qualified plant personnel from either the MCR or the HCVS ROS using remote-manual actions. The operator actions required to open a vent path are as described in Table 2-1.

Remote-manual is defined in this report as a non-automatic power operation of a component and does not require the operator to be at or in close proximity to the component. No other operator actions are required to initiate venting under the guiding procedural protocol.

The HCVS will be designed to allow initiation, control, and monitoring of venting from the MCR. This location minimizes plant operators' exposure to adverse temperature and radiological conditions and is protected from hazards assumed in Part 1 of this report.

Permanently installed electrical power and motive air/gas capability will be available to support operation and monitoring of the HCVS for 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br />.

System control:

i. The PCIVs will be operated in accordance with Emergency Operating Procedures (EOPs)/Standard Operating Procedures (SOPs) to control containment pressure. The HCVS will be designed for at least 8 vent cycles under ELAP conditions over the first 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> following an ELAP. Controlled venting will be permitted in the revised EPGs and associated implementing EOPs.

ii. Inadvertent actuation protection is provided by:

Key locked switches for the dedicated PCIVs located in the Main Control Room and controlled by procedures AND Disabling the HCVS DC power to the SOV and disabling the motive gas bottles for the dedicated PCIV except when required by procedures to initiate containment venting AND Disabling the HCVS purge Argon gas except when required by procedures to initiate containment venting AND A rupture disc downstream of the PCIVs Page 19 of 61

Limerick Generating Station Units 1 and 2 Overall Integrated Plan for Reliable Hardened Vents Part 2: Boundary Conditions for WW Vent - BDBEE Venting Greater Than 24 Hour Coping Detail Provide a general description of the venting actionsfor greater than 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> using portable and installed equipment including station modifications that are proposed.

Ref: EA-13-109 Section 1.2.4 I NEI 13-02 Section 4.2.2 Before the end of the 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> initial phase, available personnel will be able to connect supplemental gas for the motive gas, and purge systems. Purge system is only required if severe accident conditions are reached.

Connections for supplementing electrical power and air/gas required for HCVS will be located in accessible areas with reasonable protection per NEI 12-06 (Reference 8) that minimize personnel exposure to adverse conditions for HCVS initiation and operation. Connections will be pre-engineered quick disconnects to minimize manpower resources.

FLEX is credited solely to sustain power for a BDBEE ELAP to containment instruments used to monitor the containment (e.g,, pressure and wetwell level). The response to NRC EA-12-049 (Reference 3) will demonstrate the capability for FLEX efforts to maintain the power source.

These actions provide long term support for HCVS operation for the period beyond 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> to 7 days (sustained operation time period) because on-site and off-site personnel and resources will have access to the unit(s) to provide needed action and supplies.

Details:

Provide a brief description of Procedures!/ Guidelines:

Confirm that procedure/guidanceexists or will be developed to support implementation.

Primary Containment Control Flowchart will be provided to direct operations in protection and control of containment integrity, including use of the existing Hardened Containment Vent System.

ISE Open Item 13 Identify modifications:

List modifications and describe how they support the HCVS Actions.

EA-12-049 Modifications

  • At this time, no FLEX modifications other than those identified to meet EA-12-049 have been identified that are specific to supporting HCVS.

EA-13-109 Modifications

  • A modification will be required to install the Phase 1 (wetwell) vent path. The vent path is routed horizontally through the Reactor Building, up through the Railroad Bay, then penetrates the Reactor Building wall. The path then is routed vertically on the outside of the Reactor Building wall through the South Stack to a point above the top of the Reactor Building. The path will include a rupture disc to control PCIV leakage during a design basis LOCA. The wetwell vent path will include two PCIVs Page 20 of 61

Limerick Generating Station Units 1 and 2 Overall Integrated Plan for Reliable Hardened Vents Part 2: Boundary Conditions for WW Vent - BDBEE Venting dedicated to this flow path with valve position indication and remote-manual control only. Valve position indication will be provided. There is no sharing of any flow paths with the opposite unit.

  • A modification will be required to install the dedicated batteries needed to supply power to HCVS for the first 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> including capability for recharging from the FLEX-backed diesel generator MCC at or before 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br />. The batteries will be located at the ROS.
  • A modification will be required to install the dedicated motive power (pressurized motive gas) needed to open the HCVS valves for the first 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> including capability for replacing motive gas source after 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br />. The motive gas bottles will be located at the ROS.
  • A modification will be required to install the dedicated Argon purge system needed to prevent hydrogen detonation in the piping with sufficient installed capacity for the first 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> including capability for replacing Argon bottles. The Argon bottles will be located at the ROS. Argon purging is only required following severe accident conditions. It is not required if core damage is prevented. The purge system is used to breach the rupture disc in anticipatory venting and SA.
  • A modification will be required to add (a) HCVS flow path instrumentation consisting of temperature and effluent radiation in the MCR and (b) Motive gas pressure, Argon pressure, and DC battery indication in the MCR and the ROS.

Key Venting Parameters:

List instrumentation creditedfor this venting actions. Clearly indicate which of those already exist in the plant and what others will be newly installed (to comply with the vent order).

Initiation, operation and monitoring of the HCVS venting will rely on the following key parameters and indicators which will be added as part of the HCVS modification.

IKey Parameter IComponent Identifier IIndication Location 1 HCVS Effluent temperature TBD MCR HCVS Effluent radiation TBD MCR HCVS valve position indication TBD MCR HCVS DC Power Voltage/Conditions TBD ROS HCVS Gas Supply Pressure TBD ROS HCVS Purge System Pressure TBD MCR/ROS Initiation, operation, and monitoring of the HCVS will rely on several existing MCR key parameters and indicators which are qualified or evaluated to Regulatory Guide 1.97 per the existing plant design (Reference NEI 13-02 Section 4.2.2.1.9 (Reference 9)) except for drywell pressure indication. Drywell pressure indication will be reviewed for environmental qualifications to ensure this instrument can survive for 7 days.

Key Parameter Component Identifier Indication Locati~on Drywell pressure PI 042-1 (2)70-1 MCR Wetwell level LI-052-1l(2)40A MCR Phase I Open Item 8 Notes: None Page 21 of 61

Limerick Generating Station Units 1 and 2 Overall Integrated Plan for Reliable Hardened Vents Part 2: Boundary Conditions for WW Vent - Support Equipment Functions Determine venting capability support functions needed Ref: EA-13-109 Section 1.2.8, 1.2.9 /NEI 13-02 Section 2.5, 4.2.4, 6.1.2 BDBEE Venting Provide a general description of the BDBEE Venting actions supportfunctions. Identify methods and strategy(ies) utilized to achieve venting results.

Ref: EA-13-109 Section 1.2.9 I NEI 13-02 Section 2.5, 4.2.2, 4.2.4, 6.1.2 All containment venting functions will be performed from the MCR or ROS.

Venting to prevent containment over pressurization will be maintained by permanently installed equipment. The HCVS dedicated DC power source, Argon purge gas, and dedicated motive gas force is adequate for the first 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br />, but it can be replenished to support sustained operation.

Existing safety related station batteries will provide sufficient electrical power for MCR containment instrumentation. Before station batteries are depleted, portable FLEX diesel generators, as detailed in the response to Order EA-12-049 (Reference 3), will be credited to charge the station batteries and maintain DC bus voltage after battery depletion.

Severe Accident Venting Provide a general description of the Severe Accident Venting actions supportfunctions. Identify methods and strategy(ies) utilized to achieve venting results.

Ref: EA-13-109 Section 1.2.8, 1.2.9 / NEI 13-02 Section 2.5, 4.2.2, 4.2.4, 6.1.2 The same support functions that are used in the BDBEE scenario would be used for severe accident venting. The ROS (the location of the HCVS DC power source, Argon purge, and motive gas force) and the FLEX DG location will be evaluated to confirm accessibility under severe accident conditions.

Details:

Provide a brief description of Procedures I Guidelines:

Confirm that procedure/guidanceexists or will be developed to support implementation.

The operation of the HCVS will be governed the same for SA conditions as for BDBEE conditions. Existing guidance in the SAMG directs the plant staff to consider changes in radiological conditions in a severe accident.

Identify modifications.-

List modifications and describe how they support the HCVS Actions.

The same as for BDBEE Venting Part 2.

Key Support Equipment Parameters:

List instrumentation creditedfor the support equipment utilized in the venting operation. Clearly indicate which of those already exist in the plant and what others will be newly installed (to comply with the vent order).

Page 22 of 61

Limerick Generating Station Units 1 and 2 Overall Tntegrated Plan for Reliable Hardened Vents Part 2: Boundary Conditions for WW Vent - Support Equipment Functions The same as for BDBEE Venting Part 2.

Notes: None Page 23 of 61

Limerick Generating Station Units 1 and 2

.Overall Integrated Plan for Reliable Hardened Vents Part 2: Boundary Conditions for WW Vent - Venting Portable Equipment Deployment Provide a general descriptionof the venting actions using portable equipment including modifications that are proposed to maintain and/or support safety functions.

Ref: EA-13-109 Section 3.1 I NEI 13-02 Section 6.1.2, D.1.3.1 Deployment pathways developed for compliance with Order EA-12-049 are acceptable without further evaluation needed except in areas around the Reactor Building or in the vicinity of the HCVS piping.

Before the end of the initial 24 hour2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> period, replenishment of the HCVS dedicated DC power, Argon purge gas, and motive gas will occur at the ROS. The selection of the ROS location will take into account the SA temperature and radiation condition to ensure access to the ROS is maintained. The design will allow replenishment with minimal actions.

Details:

Provide a brief description of Procedures / Guidelines:

Confirm that procedure/guidanceexists or will be developed to support implementation.

Operation of the portable equipment is the same as for compliance with Order EA-12-049; thus, they are acceptable without further evaluation with the exception that severe accident radiological conditions will be considered.

Strategy Modifications Protection of connections Per compliance with Order EA- N/A Per compliance with Order EA-12-049 12-049 (FLEX) (FLEX)

Notes: None Page 24 of 61

Limerick Generating Station Units 1 and 2 Overall Integrated Plan for Reliable Hardened Vents Part 3: Boundary Conditions for EA-13-109, Option 2 General Licensees that use Option B.] of EA-13-109 (SA Capable DW Vent without SA WA) must develop their own QIP.

This template does not provide guidancefor that option.

Licensees using Option B.2 of EA 1 09 (SA WA and SA WM or 545°F SADW Vent (SADV) with SA WA) may use this templatefor their QIP submittal. Both SA WM and SADV require the use of SA WA and may not be done independently. The HCVS actions under Part2 apply to all of the following:

This Partis divided into the following sections:

3.1: Severe Accident Water Addition (SA WA )

3.1.A: Severe Accident Water Management (SA WM) 3.1.B: Severe Accident DW Vent (545 deg F)

Provide a sequence of events and identify any time constraint required for success including the basis for the time constraint.

SA WA and SA WM or SAD VActions supporting SA conditions that have a time constraintto be successful should be identified with a technical basis and ajustificationprovided that the time can reasonably be met (for example, a wallcthrough of deployment). Actions already identified under the HCVS part of this template need not be repeated here.

The time to establish the water addition capability into the RPV or DW should be less than 8 hour9.259259e-5 days <br />0.00222 hours <br />1.322751e-5 weeks <br />3.044e-6 months <br />sfrom the onset of the loss of all injection sources.

  • Electricalgenerators satisfying the requirements of EA-12-049 may be creditedfor powering components and instrumentationneeded to establish aflow path.
  • Time Sensitive Actions (TSAs)for the purpose of SAWA are those actions needed to transport, connect and start portable equipment needed to provide SA WA flow or provide power to SA WA components in the flow path between the connection point and the RPV or drywell. Actions needed to establish power to SA WA instrumentationshould also be included as TSAs.

Ref: NEI 13-02 Section 6.1.1.7.4.1, 1.1.4, 1.1.5 The operation of the HCVS using SAWA and SAWM will be designed to minimize the reliance on operator actions in response to hazards listed in Part 1. Initial operator actions will be completed by plant personnel and will include the capability for remote-manual initiation from the MCR using control switches. In addition, HCVS valve operation, as required by EA-13-109 Requirement 1.2.5, may occur at the ROS.

Timelines (see attachments 2.1 .A for SAWA/SAWM) were developed to identify required operator response times and actions. The timelines are an expansion of Attachment 2A and begin either as core damage occurs (SAWA) or after initial SAWA injection is established and as flowrate is adjusted for option B.2 (SAWM). The timelines do not assume the core is ex-vessel and the actions taken are appropriate for both in-vessel and ex-vessel core damage conditions.

Page 25 of 61

Limerick Generating Station Units 1 and 2 Overall Integrated Plan for Reliable Hardened Vents Part 3: Boundary Conditions for EA-13-109, Option 2 Part 3.1: Boundary Conditions for SAWA Table 3.1 - SAWA Manual Actions Primary Action Primary Locationl Component Notes

1. Establish HCVS capability in U MCR or ROS U Applicable to SAWAISAWM accordance with Part 2 of this strategy.

OIP

2. Connect FLEX pump discharge U Outside of the Reactor Building U No hose connections are to injection piping U Flow path is thru RHRSW required within the Reactor piping to RHR. (Same as FLEX) Building.
3. Connect FLEX pump to water U In Owner Controlled Area U The location of this source, as source (OCA) near the spray pond well as the location of the connect suction hose to diesel FLEX pump, is not challenged driven pump, and connect pump by severe accident radiological discharge to hose. (Same conditions. From this location, Location as FLEX) the flow is to the Reactor Building (action #2, above).
4. Power HCVS components with U At ground level (El. 217'-0") U Electrical connections made in EA-12-049 (FLEX) generator inside the Diesel Buildings the Diesel Building.
5. Inject to RPV using FLEX pump U At MCR U MOVs will be powered from (SAWA) U Requires energizing and opening FLEX generator.

Ultimate Cooling System motor U Initial SAWA flow rate is 500 operated valves (MOVs) to open gpm.

flow path from RHRSW to RHR

  • Requires opening and then adjusting flow through RHR/LPCI MOV
6. Monitor SAWA indications U OCA near spray pond (Pump
  • Pump flow.

Flow) U MOV position indication.

  • MCR (Level and Pressure)
7. Use SAWM to maintain U MCR and OCA near spray pond U Monitor DW pressure and availability of the WW vent (Part Suppression Pool level.

3.1 .A) U Control FLEX Pump flow rate.

Discussion of timeline SAWA identified items HCVS operations are discussed under Phase I of EA- 13-109 (Part 2 of this 0IP).

U 7 Hours - Establish electrical power and other EA-t2-049 actions needed to support the strategies for EA 109, Phase 1 and Phase 2. Action being taken within the reactor building under EA-12-049 conditions after RPV level lowers to 2/3 core height must be evaluated for radiological conditions assuming permanent Page 26 of 61

Limerick Generating Station Units 1 and 2 Overall Integrated Plan for Reliable Hardened Vents Part 3: Boundary Conditions for EA-13-109, Option 2 containment shielding remains intact. (HCVS-FAQ- 12) All other actions required are assumed to be in-line with the FLEX timeline submitted in accordance with the EA-12-049 requirements.

U Less than 8 Hours - Initiate SAWA flow to the RPV. Having the HCVS in service will assist in minimizing the peak DW pressure during the initial cooling conditions provided by SAWA.

Determine operatingrequirementsfor SA WA, such as may be used in an ELAP Scenario to mitigate core damage.

Ref: EA-13-109 Attachment 2, Section B.2.2, B.2.3 / NEI 13-02 Section 1.1.6, 1.1.4.4 It is anticipated that SAWA will be used in Severe Accident Events based on presumed failure of injection systems or presumed failure of injection systems in a timely manner. This does not preclude the use of the SAWA system to supplement or replace the EA- 12-049 injection systems if desired. SAWA will consist of both portable and installed equipment.

The motive force equipment needed to support the SAWA strategy shall be available prior to T=8 hours from the loss of injection (assumed at T=0).

The SAWA flow path (same as FLEX Flow path) includes methods to minimize exposure of personnel to radioactive liquids / gases and potentially flammable conditions by inclusion of backflow prevention. RHR LPCI injection mode has an installed ECCS check valve, qualified for accident scenarios, to prevent reverse flow from the RPV.

Table 3.2 - SAWA Manual Actions Timeline Time Action Notes T<I hour U No Action. U No evaluation required for actions inside Reactor Building.

T=l-7 hours* U Connect FLEX hose inside of the OCA near spray U Evaluate core gap and early in pond (Step 2 of Table 3.1I). vessel release impact to reactor

  • Connect FLEX pump to water supply at OCA near building access for SAWA spray pond (Step 3 of Table 3.1). actions. It is assumed that
  • Establish electrical power to HCVS and FLEX using reactor building access is EA-12-049 generator (Step 4 of Table 3.1). limited due to the source term
  • Establish flow of 500 gpm to the RPV using FLEX at this time unless otherwise systems flow paths. (StepS5 of Table 3.1I). noted. (Refer to HCVS-FAQ-12 for actions in T=1-7 hour timeframe.

T<8-12 hours U Monitor and Maintain SAWA flow at 500 GPM or U SAWA flow must commence less, depending on level and pressure in reactor vessel at T=8 hours but should be Step 6 of Table 3.1). done as soon as motive force is

___________ _________________________________________ available.

Page 27 of 61

Limerick Generating Station Units 1 and 2 Overall Integrated Plan for Reliable Hardened Vents Part 3: Boundary Conditions for EA-13-109, Option 2 T<12 hours U Proceed to SAWM actions per Part 3.1.A (Step 7 of U SAWA flow may be reduced Table 3.1). to 100 GPM four hours following SAWA initiation.

  • The assumed times of T=I hour to T=8 hours to establish the bounds of applicability of radiological evaluations have been reduced to T= 1 hour1.157407e-5 days <br />2.777778e-4 hours <br />1.653439e-6 weeks <br />3.805e-7 months <br /> to T=7 hours in order to provide sufficient margin to inform operator action feasibility evaluations and will be further informed by emergency response dose assessment activities during an actual event. This accounts for the one hour gap between 7 and 8 hours9.259259e-5 days <br />0.00222 hours <br />1.322751e-5 weeks <br />3.044e-6 months <br /> in this time line.

Provide a general description of the SA WA actionsfor greater than 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> using portable and installed equipment including station modifications that are proposed.

Ref: EA-13-109 Attachment 2, Section B.2.2, B.2.3/ NEI 13-02 Section 4.2.2.4.1.3.1, 1. 1.4, SAWA Operation is the same for the full period of sustained operation. If SAWMV is employed, flow rates will be directed to preserve the availability of the HCVS wetwell vent (see 3.1.A).

Details of Design Characteristics/Performance Specifications SAWA shall be capable of providing an RPV injection rate of 500 gpm within 8 hours9.259259e-5 days <br />0.00222 hours <br />1.322751e-5 weeks <br />3.044e-6 months <br /> of a loss of all RPV injection following an ELAP/Severe Accident. SA WA shall meet the design characteristicsof the HCVS with the exception of the dedicated 24 hour2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> power source. Hydrogen mitigation is provided by backflow preventionfor SA WA.

Ref: EA-13-109 Attachment 2, Section B.2.1, B1.2.2, B.2.3/ NET 13-02 Section 1.1.4 Equipment Locations/Controls/Instrumentation Limerick has not performed a site specific evaluation to justify the use of a lower site unique initial SAWA flow rate. Consequently, Limerick will assume an initial flow rate of 500 GPM. This is based on the industry generic value of 500 gpm per NEI 13-02 (Reference 9). This initial flow rate will be established within 8 hours9.259259e-5 days <br />0.00222 hours <br />1.322751e-5 weeks <br />3.044e-6 months <br /> of the loss of all RPV injection following an ELAP/Severe Accident and will be maintained for four hours before reduction to the Wetwell vent preservation flow rate of 100 gpm.

The locations of the SAWA equipment and controls, as well as ingress and egress paths will be evaluated for the expected severe accident conditions (temperature, humidity, radiation) for the Sustained Operating period.

Equipment will be evaluated to remain operational throughout the Sustained Operating period. Personnel exposure and temperature / humidity conditions for operation of SAWA equipment will not exceed the limits for Emergency Response Organization (ERO) dose and plant safety guidelines for temperature and humidity.

The flow path will be from the FLEX pump suction at the Spray Pond through the FLEX pump hoses to the RHRSW piping in the Spray Pond Pump House. Once in the RHRSW system, underground piping is used to deliver water to the RHR system in the Reactor Building. This flow path requires opening two RHRSW to RHR MOVs and then opening and throttling (if required) through a RHR/LPCI MOV. These valves will be energized from the FLEX diesel generator to allow remote-manual opening. The flow control method will be accomplished at the FLEX Pump by adjusting the pump throttle or using a bypass valve when the flow requirement is below the pump capability.

DW pressure and Suppression Pool level will be monitored and flow rate will be controlled by adjusting the FLEX pump speed and/or by throttling the RHR/LPCI MOV. Communication will be established between the MCR and the SAWA flow control location (at Spray Pond).

Page 28 of 61

Limerick Generating Station Units 1 and 2 Overall Integrated Plan for Reliable Hardened Vents Part 3: Boundary Conditions for EA-13-109, Option 2 The FLEX pump suction source is a significant distance from the discharge of the HCVS pipe with substantial structural shielding between the HCVS pipe and thepump deployment location. Pump refueling will also be accomplished from a dedicated diesel fuel tank located in the FLEX Pump storage building as described in the EA-12-049 compliance documents.

Evaluations of actions outside the Reactor Building for projected SA conditions (radiation / temperature) will have to be completed to ensure support activities will not exceed the ERO-allowable dose for equipment operation or site safety standards (Reference 22). Evaluation of actions inside the Reactor Building for projected SA conditions (radiation/temperature) will be performed to determine that personnel can complete the initial and support activities without exceeding the ERO-allowable dose for equipment operation or site safety standards (reference HCVS-FAQ-12).

Electrical equipment and instrumentation will be powered from the power sources noted in the table below with portable generators to maintain battery capacities during the Sustained Operating period. The indications include

(*are minimum required instruments):

Parameter Instrument Location Power Source I Notes DW Pressure* P1-042-1(2)70-1 MCR Division 1 battery via EA- 12-049 generator and battery charger Suppression Pool Level* LI-052-1(2)40A MCR RG 1.97 qualified Division 1 battery via EA- 12-049 generator and battery charger SAWA Flow* (FLEX TBD FLEX Pump Self-powered from Pump Flow indicator) diesel pump internal

___________________ ________________ battery Equipment Protection Portable equipment used for SAWA implementation will meet the protection requirements for storage in accordance with the criteria in NEI 12-06 Revision 0.

Ref: EA-13-109 Attachment 2, Section B.2.2, B.2.3 / NET 13-02 Section 5.1.1, 5.4.6, 1.1.6 Provide a brief description of Procedures / Guidelines:

Confirm that procedure/guidanceexists or will be developed to support implementation.

Ref: EA-13-109 Attachment 2, Section A.3.1, B.2.3 I NEI 13-02 Section 1.3, 6.1.2

1. Connect FLEX pump discharge to RHRSW piping in spray pond pump house.
2. Power SAWAIHCVS components with EA-12-049 (FLEX) generator.
3. Verify other RHR modes are isolated using Control Room switches.
4. Open MOVs to lineup injection to RPV using FLEX (SAWA) pump.

Page 29 of 61

Limerick Generating Station Units 1 and 2 Overall Integrated Plan for Reliable Hardened Vents Part 3: Boundary Conditions for EA-13-109, Option 2

5. Start FLEX pump to establish SAWA flow.
6. Adjust SAWA flow using SAWA flow indication to establish and maintain 500 gpm.

Identify modifications."

List modifications and describe how they support the SA WA Actions.

Ref: EA-13-109 Attachment 2, Section B.2.2, I NET 13-02 Section 4.2.4.4, 7.2.1.8, Appendix I The list of modifications, below, is limited to those required to upgrade EA-12-049 equipment to meet EA-13-109 Phase 2 requirements.

Electrical Modifications:

  • None Mechanical Modifications:
  • Min flow return from FLEX pump to spray pond to protect pump during low flow conditions Instrument Modifications:
  • Flow meter on FLEX pump Component Qualifications:

State the qualification usedfor equipment supportingSA WA.

Ref: EA-13-109 Attachment 2, Section B.2.2, B.2.3 / NEI 13-02 Section 1.1.6 Permanently installed plant equipment shall meet the same qualifications* as described in Part 2 of this OIP.

Temporary/Portable equipment shall be qualified and stored to the same requirements as FLEX equipment as specified in NEI 12-06 Rev 0. SAWA components are not required to meet NET 13-02, Table 2-1 design conditions.

Notes:

None Part 3.1 .A: Boundary Conditions for SAWAISAWM SA WM Actions supporting SA conditions that have a time constraintto be successful should be identified with a technical basis and a justificationprovided that the time can reasonably be met (for example, a walkthrough of deployment). Actions already identified under the HCVS part of this template need not be repeated here.

There are three time periodsfor the maintaining SA WM actions such that the WWV vent remains available to remove decay heatfrom the containment:

  • SAWM can be maintainedfor >7 days without the need for a drywell vent to maintainpressuredbelow PCPL or containment design pressure, whichever is lower.

o Under this approach, no detail concerningplant modifications or procedures is necessary with Page 30 of 61

Limerick Generating Station Units 1 and 2 Overall Integrated Plan for Reliable Hardened Vents Part 3: Boundary Conditions for EA-13-109, Option 2 respect to how alternate containment heat removal will be provided.

  • SAWM can be maintainedfor at least 72 hours8.333333e-4 days <br />0.02 hours <br />1.190476e-4 weeks <br />2.7396e-5 months <br />, but less than 7 days before DWpressure reaches PCPL or design pressure, whichever is lower.

o Under this approach, afunctional description is requiredof how alternate containment heat removal might be established before DW pressure reaches PCPL or design pressure whichever is lower. Under this approach, physical plant modifications and detailedprocedures are not necessary, but written descriptionsof possible approachesfor achieving alternate containment heat removal and pressure control will be provided.

  • SAWM can be maintainedfor <72 hours SAWM strategy can be implemented but for less than 72 hours8.333333e-4 days <br />0.02 hours <br />1.190476e-4 weeks <br />2.7396e-5 months <br /> before DW pressure reaches PCPL or design pressure whichever is lower.

o Under this approach, a functional description is required of how alternate containment heat removal might be established before DW pressure reaches PCPL or design pressure whichever is lower. Under this approach,physical plant modifications and detailedprocedures are required to be implemented to insure achieving alternate containment heat removal and pressure control will be providedfor the sustained operatingperiod.

Ref: NET 13-02 Appendix C.7 SAWM can be maintained for >7 days without the need for a drywell vent to maintain pressure below PCPL.

Basis for SAWM time frame i,  :**  :::  : :  :  ::*:i!i*

SAWM can be maintained >7 days:

Limerick has not performed a site specific evaluation to justify the use of a lower site unique initial SAWA flow rate. Consequently, Limerick will assume an initial flow rate of 500 GPM.

This initial flow rate will be established within 8 hours9.259259e-5 days <br />0.00222 hours <br />1.322751e-5 weeks <br />3.044e-6 months <br /> of the loss of all RPV injection following an ELAP/Severe Accident and will be maintained for four hours before reduction to the WW vent preservation flow rate of 100 gpm.

Instrumentation relied upon for SAWM operations is Drywell Pressure and Suppression Pool level and SAWA flow. Except for SAWA flow, SAWM instruments are initially powered by station batteries and then by the FLEX (EA-12-049) generator which is placed in-service prior to core breach. The FLEX Generator will provide power throughout the Sustained Operation period (7 days). DW Temperature monitoring is not a requirement for compliance with Phase 2 of Order EA-13-109, but some knowledge of temperature characteristics provides information for the Operations Staff to evaluate plant conditions under a severe accident and provide confirmation to adjust SAWA flow rates (C.7.1.4.2, C.8.3.1).

Suppression Pool level indication is maintained throughout the Sustained Operation period, so the HCVS remains in-service. The current Limerick Suppression Pool level indication spans above the HCVS wetwell penetration. No additional suppression pool level indication is required. The time to reach the level at which the WW vent must be secured is >7 days using SAWM flowrates (C.6.3, C.7.1.4.3).

Procedures will be developed that control the Suppression Pool level, while ensuring the DW pressure indicates the core is being cooled, whether in-vessel or ex-vessel. Procedures will dictate conditions during which SAWM flowrate should be adjusted (up or down) using suppression pool level and DW pressure as controlling parameters to remove the decay heat from the containment (this is similar to the guidance currently provided in the BWROG SAMGs) (C.7.l.4.3). .l.A shows the timeline of events for SAWA / SAWM (C.7.1.4.4).

Page 31 of 6l

Limerick Generating Station Units 1 and 2 Overall Integrated Plan for Reliable Hardened Vents Part 3: Boundary Conditions for EA-13-109, Option 2 Table 3.1)B,-SAWM ManUal Actions i,:  :: *! i Primary Action Primary Location!/Component Notes

1. Lower SAWA injection rate to OCA near spray pond pump house
  • Control to maintain control Suppression Pool Level or MCR containment and WW and decay heat removal parameters to ensure WW vent remains functional.
  • 100 gpm minimum capability is maintained for greater than 7 days.
2. Control SAWM flowrate for OCA near spray pond pump house
  • SAWM flowrate will be containment control/decay heat and MCR monitored using the following removal instruments:

- SAWA Flow

- Suppression Pool Level

- Drywell Pressure

3. Establish alternate decay heat Various locations SAWM strategy can preserve the removal WW vent path for >7 days.
4. Secure SAWA / SAWM MCR When alternate decay heat removal is established.

SAWM Time Sensitive Actions* :i(  : i:* ii Time Sensitive SAWM Actions:

12 Hours - Initiate actions to maintain the WW vent capability by lowering injection rate, while maintaining the cooling of the core debris (SAWM). Monitor SAWM critical parameters while ensuring the WW vent remains available.

SAWM Severe Accident Operation Determine operating requirementsfor SA WM, such as may be used in an ELAP scenario to mitigate core damage.

Ref: EA-13-109 Attachment 2, Section B.2.2, B.2.3 / NET 13-02 Appendix C It is anticipated that SAWM will only be used in Severe Accident Events based on presumed failure of plant injection systems per direction by the plant SAMGs. Refer to Attachment 2.1 .D for SAWM SAMG language additions.

~First 24 Hour Coping Detail Provide a general description of the SA WM actionsfor first 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> using installed equipment including station modifications that are proposed.

Given the initialconditionsfor EA- 13-1 09:

Page 32 of 61

Limerick Generating Station Units 1 and 2 Overall Integrated Plan for Reliable Hardened Vents Part 3: Boundary Conditions for EA-13-109, Option 2

  • Failure of all injection systems, including steam-powered injection systems Ref: EA-13-109 Section 1.2.6, Attachment 2, Section B.2.2, B.2.3 / NEI 13-02 2.5, 4.2.2, Appendix C, Section C.7 SAWA will be established as described above. SAWMV will use the installed instrumentation to monitor and adjust the flow from SAWA to control the pump discharge to deliver flowrates applicable to the SAWM strategy.

Once the SAWA initial flow rate has been established for 4 hours4.62963e-5 days <br />0.00111 hours <br />6.613757e-6 weeks <br />1.522e-6 months <br />, the flow will be reduced while monitoring DW pressure and Suppression Pool level. SAWM flowrate can be lowered to maintain containment parameters and preserve the WW vent path. SAWIV will be capable of injection for the period of Sustained Operation.

i:/ **i:=  : i *:

  • Greater Than 24 HoUr Coping Detail  :*'

Provide a general description of the SA WM actionsfor greater than 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> using portable and installed equipment including station modifications that areproposed.

Ref: EA-13-109 Section 1.2.4, 1.2.8, Attachment 2, Section B.2.2, B.2.3 / NET 13-02 Section 4.2.2, Appendix C, Section C.7 SAWM can be maintained >7 days:

The SAWM flow strategy will be the same as the first 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> until alternate reliable containment heat removal and pressure control is reestablished. SAWM flow strategy uses the SAWA flow path. No additional modifications are being made for SAWM.

Details of Design Characteristics/Performance Specifications Ref: EA-13-109 Attachment 2, Section B.2.2, B.2.3 / NET 13-02 Section Appendix C SAWM shall be capable of monitoring the containment parameters (DW pressure and Suppression Pool Level) to provide guidance on when injection rates shall be reduced, until alternate containment decay heat/pressure control is established. SAWA will be capable of injection for the period of Sustained Operation.

Equipment Locations/Controls/Instrumentation Describe locationfor SA WM monitoring and control.

Ref: EA-13-109 Attachment 2, Section B.2.2, B.2.3 ! NEI 13-02 Appendix C, Section C.8, Appendix I The SAWM control location is the same as the SAWA control location. OCA Spray pond pump house indication of SAWM flow rate is provided at FLEX Pump by flow instrument designed to operate under the expected environmental conditions.

Injection flowrate is controlled by throttling FLEX pump flow or throttling a RHR/LPCI MOV.

Suppression Pool level and DW pressure are read in the control room using indicators powered by the FLEX DG installed under EA-12-049. These indications are used to control SAWM flowrate to the RPV.

Key Parameters:

Page 33 of 61

Limerick Generating Station Units 1 and 2 Overall Integrated Plan for Reliable Hardened Vents Part 3: Boundary Conditions for EA-13-109, Option 2 List instrumentationcreditedfor the SA WM Actions.

Parameters used for SAWM are:

  • Drywell Pressure
  • Suppression Pool Level
  • SAWM Flowrate The Suppression Pool level instrument is qualified to RG 1.97 and is the same as listed in Part 2 of this OIP.

Drywell pressure indication is not qualified to RG 1.97. The SAWM flow instrumentation will be qualified for the expected environmental conditions expected when needed.

Notes:

None Page 34 of 61

Limerick Generating Station Units 1 and 2 Overall Integrated Plan for Reliable Hardened Vents Part 3: Boundary Conditions for EA-13-109, Option 2 Part 3.1 .B: Boundary Conditions for SAWA/SADV AplIblt ofW/einCnieain Page 35 of 61

Limerick Generating Station Units 1 and 2 Overall Integrated Plan for Reliable Hardened Vents Part 4: Programmatic Controls, Training., Drills and Maintenance Identify how the programmatic controls will be met.

Provide a description of the programmatic controls equipment protection, storage and deployment and equipment quality addressing the impact of temperature and environment.

Ref: EA-13-109 Section 3.1, 3.20 / NEI 13-02 Section 6.1.2, 6.1.3, 6.2 Program Controls:

The HCVS venting actions will include:

  • Site procedures and programs are being developed in accordance with NEI 13-02 to address use and storage of portable equipment relative to the Severe Accident defined in NRC Order EA 109 and the hazards applicable to the site per Part 1 of this OIW.
  • Routes for transporting portable equipment from storage locations to deployment areas will be developed as the response details are identified and finalized. The identified paths and deployment areas will be accessible when the HCVS is required to be functional during Severe Accidents.

Procedures:

Procedures will be established for system operations when normal and backup power is available, and during ELAP conditions.

The HCVS and SAWA procedures will be developed and implemented following plant processes for initiating or revising procedures and contain the following details:

  • appropriate conditions and criteria for use of the HCVS and SAWA
  • when and how to place the HCVS and SAWA in operation
  • location of system components
  • instrumentation available
  • normal and backup power supplies
  • directions for sustained operation (Reference 9), including the storage and location of portable equipment
  • location of the remote control HCVS operating station (panel)
  • training on operating the portable equipment
  • testing of portable equipment Provisions will be established for out-of-service requirements of the HCVS and compensatory measures that comply with the criteria from NEI 13-02 (Reference 9).

The following provisions will be documented in the HCVS Program Document:

The provisions for out-of-service requirements for HCVS/SAWA are applicable in Modes 1, 2 and 3

  • If for up to 90 consecutive days, the primary or alternate means of HCVS/SAWA operation are non-functional, no compensatory actions are necessary.
  • If for up to 30 days, the primary and alternate means of HCVS/SAWA operation are non-functional, no compensatory actions are necessary.
  • If the out of service times exceed 30 or 90 days as described above, the following actions will be Page 36 of 61

Limerick Generating Station Units 1 and 2 Overall Integrated Plan for Reliable Hardened Vents Part 4: Programmatic Controls., Training, Drills and Maintenance performed through the site corrective action program:

  • Determine the cause(s) of the non-functionality,
  • Establish the actions to be taken and the schedule for restoring the system to functional status and to prevent recurrence,
  • Initiate action to implement appropniate compensatory actions, and
  • Restore full HCVS functionality at the earliest opportunity not to exceed one full operating cycle.

Describe training plan List trainingplansfor affected organizationsor describe the plan for trainingdevelopment.

Ref: EA-13-109 Section 3.2 I NEL 13-02 Section 6.1.3 Personnel expected to perform direct execution of the HCVS/SAWA/SAWM actions will receive necessary training in the use of plant procedures for system operations when normal and backup power is available and during ELAP conditions. The training will be refreshed on a periodic basis and as any changes occur to the HCVS/SAWA/SAWM actions, systems or strategies. Training content and frequency will be established using the Systematic Approach to Training (SAT) process.

Identify how the drills and exercise parameters will be met.

Alignment with NEI 13-06 and 14-01 as codified in Near-Term Task Force (NTTF) Recommendation 8 and 9 rulemaking.

The Licensee should demonstrate use in drills, tabletops, or exercises for HCVS operation as follows:

  • Hardened containment vent operation on normal power sources (no ELAP).
  • During FLEX demonstrations (as requiredby EA-12-049): Hardenedcontainment vent operation on backup power andfrom primary or alternate location during conditions of ELA P/loss of UHS with no core damage. System use is for containment heat removal AND containmentpressure control.
  • HCVS operation on backup power andfrom primary or alternate location during conditions of ELA P/loss of UHS with core damage. System use is for containment heat removal AND containmentpressure control with potentialfor combustible gases (Demonstrationmay be in conjunction with SAG change).
  • Operation for sustainedperiod with SA WA and SA WM to provide decay heat removal and containmentpressure control.

Ref: EA-13-109 Section 3.1 I NEI 13-02 Section 6.1.3 Limerick will utilize the guidance provided in NEI 13-06 and 14-01 (References 10 and 11) for guidance related to drills, tabletops, or exercises for HCVS operation. In addition, Limerick will integrate these requirements with compliance to any rulemaking resulting from the NTTF Recommendations 8 and 9.

Describe maintenance plan:

  • Th, nrnaintonnn-op nrnaram n vl, rO tliat ahtl' tlip F4-G1~/,qiA WA/S'A WA/ paatnmant raliahilitv iv haina.

achieved in a manner similar to that requiredfor FLEX equipment. Standardindustry templates (e.g.,

Page 37 of 61

Limerick Generating Station Units 1 and 2 Overall Integrated Plan for Reliable Hardened Vents Part 4: Programmatic Controls, Training, Drills and Maintenance EPRI) and associatedbases may be developed to define specific maintenance and testing.

o Periodic testing andfrequency should be determined based on equipment type and expected use (furtherdetails are provided in Part 6 of this document).

o Testing should be done to verify design requirements and/or basis. The basis should be documented and deviationsfrom vendor recommendations and applicablestandards should be justified.

o Preventive maintenance should be determined based on equipment type and expected use. The basis should be documented and deviationsfrom vendor recommendations and applicable standardsshould be justified.

o Existing work control processes may be used to control maintenance and testing.

  • HCVS/SA WA permanent installed equipment should be maintained in a manner that is consistent with assuring that it performs its finction when required.
  • o HCVS/SAWA permanently installed equipment should be subject to maintenance and testing guidanceprovided to verify properfunction.
  • HCVS/SA WA non-installedequipment should be stored and maintained in a manner that is consistent with assuring that it does not degrade over long periods of storage and that it is accessiblefor periodic maintenance and testing.

Ref: EA-13-109 Section 1.2.13 / NEI 13-02 Section 5.4, 6.2 Limerick will utilize the standard EPRI industry PM process (similar to the Preventive Maintenance Basis Database) for establishing the maintenance calibration and testing actions for HCVS/SAWA/SAWM components. The control program will include maintenance guidance, testing procedures, and frequencies established based on type of equipment and considerations made within the EPRI guidelines.

Limerick will implement the following operation, testing and inspection requirements for the HCVS and SAWA to ensure reliable operation of the system.

Table 4-1: Testing and Inspection Requirements Description Frequency Cycle the HCVS valves. Once per every 1 operating cycle Cycle the HCVS not used to maintain Once per every other3 operating cycle containment integrity during unit operations.

Perform visual inspections and a walk down of Once per every other 3 operating cycle HCVS and installed SAWA components.

Functionally test the HCVS radiation monitors. Once per operating cycle Validate the HCVS control system by Once per every other operating cycle conducting an open/close test of the function from its control location.

After two consecutive successful performances, the test frequency may be reduced to a maximum of once per every other operating cycle.

Page 38 of 61

Limerick Generating Station Units 1 and 2 Overall Integrated Plan for Reliable Hardened Vents Part 4: Programmatic Controls. Training. Drills and Maintenance 2Ntrequired if integrity of check function (open and closed) is demonstrated by other plant testing requirements.

SAtrtwo consecutive successful performances,-the test frequency may be reduced by one operating cycle to, a maximum of once per every fourth operating cycle.

Notes:

Per generic assumption 109-4, existing containment component's design and testing values are governed by existing plant containment criteria (e.g., Appendix J) and are not subject to the testing criteria from NEI 13-02 (Reference HCVS-FAQ-05 , Reference 16 and NEI 13-02, §6.2.2 , Reference 9).

Page 39 of 61

Limerick Generating Station Units 1 and 2 Overall Integrated Plan for Reliable Hardened Vents Part 5: Milestone Schedule Provide a milestone schedule. This schedule should include:

  • Modifications timeline
  • Procedure guidance development complete o HCVS Actions o Maintenance
  • Storage plan (reasonable protection)
  • Staffing analysis completion
  • Long term use equipment acquisition timeline
  • Training completion for the HCYS Actions The dates specifically required by the order are obligated or committed dates. Other dates are planned dates subject to change. Updates will be provided in the periodic (six month) status reports.

Ref: EA-13-109 Section D.1, D.3 / NEI 13-02 Section 7.2.1 The following milestone schedule is provided. The dates are planning dates subject to change as design and implementation details are developed. Any changes to the following target dates will be reflected in the subsequent 6 month status reports.

Phase 1:Mil~estones:* *  ::  :  :?:'  :.  ::

Milestone Target Activity Comments Completion Status

___________________________________________________ Date Hold preliminary/conceptual design meeting July 2014 Complete Submit Overall Integrated Implementation Plan Jun 2014 Complete Submit 6 Month Status Report Dec 2014 Complete Submit 6 Month Status Report Jun 2015 Complete Submit 6 Month Status Report Dec. 2015 Complete Simultaneous with Phase 2 with this OIP submittal U2 Design Engineering Complete November Started Preliminary/Conceptual 2016 design revised Sept. 2015 U2 Maintenance and Operation Procedure Changes February Not Started Developed, Training Complete 2017 U2 Procedure Changes Active, Walk-Through May 2017 Not Started Demonstration/Functional Test U2 Implementation Outage (Completion date) May 2017 Not Started UI Design Engineering Complete March Not Started 2017 U1 Maintenance and Operation Procedure Changes February Not Started Developed, Training Complete 2018 U1 Procedure Changes Active, Walk-Through April 2018 Not Started Page 40 of 61

Limerick Generating Station Units 1 and 2 Overall Integrated Plan for Reliable Hardened Vents Part 5: Milestone Schedule Demonstration/Functional Test U 1 Implementation Outage (Completion date) April 2018 Not Started Submit Completion Report May 2018 Not started

Phase 2 Milestone Schedule: *~ i** **i i *:):: i:  : -',  :,,::*

Phase 2 Milestone Schedule Milestone Target Activity Comments Completion Status Date Submit Overall Integrated Implementation Plan Dec 2015 Complete Simultaneous with with this Phase 1 Updated OIP submittal Hold preliminary/conceptual design meeting June 2015 Complete Submit 6 Month Status Report (Phases 1 and 2) June 2016 Not Started Submit 6 Month Status Report (Phases 1 and 2) Dec 2016 Not Started Submit 6 Month Status Report (Phases 1 and 2) June 2017 Not Started Submit 6 Month Status Report (Phases 1 and 2) Dec 2017 Not Started Submit 6 Month Status Report (Phases 1 and 2) June 2018 Not Started Submit 6 Month Status Report (Phases 1 and 2) Dec 2018 Not Started U1 Design Engineering Complete March 2017 Not Started Simultaneous with Phase 1 Ul Maintenance and Operation Procedure Changes February Not Started Simultaneous with Developed, Training Complete 2018 Phase 1 Ul Procedure Changes Active, Walk-Through April 2018 Not Started Simultaneous with Demonstration/Functional Test Phase 1 Ul Implementation Outage (Completion date) April 2018 Not Started Simultaneous with Phase 1 U2 Design Engineering Complete March 2018 Not Started U2 Maintenance and Operation Procedure Changes February Not Started Developed, Training Complete 2019 U2 Procedure Changes Active, Walk-Through May 2019 Not Started Demonstration/Functional Test U2 Implementation Outage (Completion date) May 2019 Not Started Submit Completion Report June 2019 Not Started Page 41 of 61

Limerick Generating Station Units 1 and 2 Overall Integrated Plan for Reliable Hardened Vents Part 5: Milestone Schedule Notes:

None Page 42 of 61

Limerick Generating Station Units 1 and 2 Overall Integrated Plan for Reliable Hardened Vents Attachment 1: HCYS/SAWA/SADV Portable Equipment BDBEE Severe Performance Maintenance/PM requirements List portable equipment Venting Accident Criteria Venting Motive Gas Cylinders X X TBD Check periodically for pressure, replace or replenish as needed Argon Cylinders NA X TBD Check periodically for pressure, replace or replenish as needed FLEX Diesel Generators X X TBD Per response to EA-12-049 FLEX (SAWA) pump X X 500 GPM Per response to EA-12-049 Phase I Open Item 9 Page 43 of 61

Limerick Generating Station Units 1 and 2 Overall Integrated Plan for Reliable Hardened Vents Attachment 2A: Sequence of Events Timeline - HCVS Begin monitoring HCVS support systems. No replenishment expected to Replenishment of HCVS End of Sustained ELAP RCIC Anticipatory starts venting be required until 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br />. supports systems required. Operation Sequence 1 5 U 5 SFLEX successful T=0s T*0.5m ThXXX Tz l 8 hrs I Ref: Station FLEX OIP~

SAWA Injection begins No Injection Injection Lost Level at TAF Sequence 2

~'RCIC Late Failure Containment Venting Ref: SECY-I12-0157 (based on preventing Tz 23 hrs T 24 hrs T *34 hrs exceeding PCPL)

Stop anticipatory venting Start containment (anticipatory venting not venting (based on represented in SECY- 12-0157) preventing exceeding PCPL) Sequence 3 RCIC Early Failure Ref: SOARCA Tzlhr Tz T~ l 2hrs T 24 hrs 8 hrs T

  • 168 hrs SAWA Legend lnieetinn

...........No core damage; Adequate core cooling maintained Not to Injection lost Scale i Core damage but no venting; containment shine dose in Rx Bldg but not from HCVS pipe i Post-RPV breach Page 44 of 61

Limerick Generating Station Units 1 and 2 Overaill Integrated Plan for Reliable Hardened Vents Attachment 2.1 .A: Sequence of Events Timeline - SAWA / SAWM Sustained Operation period T=168 hours I

SAWA T=168 hours Time Action T=O hours Start of ELAP T=8 hours Initiate SAWA flow at 500 gpm as soon as possible but no later than 8 hours9.259259e-5 days <br />0.00222 hours <br />1.322751e-5 weeks <br />3.044e-6 months <br /> T=12 hours Throttle SAWA flow to 100 gpm 4 hours4.62963e-5 days <br />0.00111 hours <br />6.613757e-6 weeks <br />1.522e-6 months <br /> after initiation of SAWA flow T= 168 hours0.00194 days <br />0.0467 hours <br />2.777778e-4 weeks <br />6.3924e-5 months <br /> End of Sustained Operation Page 45 of 61

Limerick Generating Station Units 1 and 2 Overall Integrated Plan for Reliable Hardened Vents .1 .B: Sequence of Events Timeline - SADV Not applicable to Limerick Page 46 of 61

Limerick Generating Station Units 1 and 2 Overall Integrated Plan for Reliable Hardened Vents .1 .C: SAWA/SAWM Plant-Specific Datum Not To Scale Page 47 of 61

Limerick Generating Station Units 1 and 2 Overall Integrated Plan for Reliable Hardened Vents Attachment 2.1 .D: SAWM SAMG Approved Language The following general cautions, prioritiesand methods will be evaluatedfor plant specific applicability and incorporatedas appropriateinto the plant specific SAMGs using administrativeproceduresfor EPG/SAG change control process and implementation. SAMGs are symptom based guidelines and therefore address a wide variety of possible plant conditions and capabilitieswhile these changes are intended to accommodate those specific conditions assumed in Order EA -109. The changes will be made in a way that maintains'the use of SAMGs in a symptom based mode while at the same time addressing those conditions that may exist under extended loss of AC power (ELAP) conditions with significant core damage including ex-vessel core debris.

Actual Approved Language that will be incorporated into site SAMG Cautions:

  • Addressing the possible plant response associated with adding water to hot core debris and the resulting pressurization of the primary containment by rapid steam generation.
  • Addressing the plant impact that raising suppression pooi water level above the elevation of the suppression chamber' vent opening elevation will flood the suppression chamber vent path.

Priorities:

With significant core damage and RPV breach, SAMGs prioritize the preservation of primary containment integrity while limiting radioactivity releases as

'follows:

  • Water addition is managed to preserve the Mark 11II suppression chamber vent paths, thereby retaining the benefits of suppression pool scrubbing and minimizing the likelihood of radioactivity and hydrogen release into the secondary containment (SAWM).

Methods:

Identify systems and capabilities to add water to the RPV or drywell, with the following generic guidance:

  • Use controlled injection if possible.
  • Inject into the RPV if possible.

Maintain injection from external sources of water as low as possible to preserve suppression chamber vent capability.

Page 48 of 61

Limerick Generating Station Units 1 and 2 Overall Integrated Plan for Reliable Hardened Vents Attachment 3: Conceptual* Sketches (Conceptual sketches, as necessary to indicate equipment which is installed or equipment hookups necessary for the strategies)

Sketch 1A : Electrical Layout of System (preliminary)

  • Instrumentation Process Flow
  • Electrical Connections Sketch 2A and 2B: P&ID Layout of WW Vent, Pathways and Site Layout (preliminary)
  • Piping routing for vent path - WW Vent
  • Demarcate the valves (in the vent piping) between the currently existing and new ones
  • WW Vent Instrumentation Process Flow Diagram
  • Egress and Ingress Pathways to ROS, Battery Transfer Switch, DG Connections and Deployment location
  • Site layout sketch to show location/routing of WW vent piping and associated components. This should include relative locations both horizontally and vertically
  • Sketch 3a and 3h: P&ID Layout of SAWA, Pathways and Site Layout (preliminary)
  • Piping routing for SAWA path
  • SAWA instrumentation process paths.
  • Include a piping and instrumentation diagram of the vent system. Demarcate the valves (in the vent piping) between the currently existing and new ones.
  • Ingress and egress paths to and from control locations and manual action locations.
  • Site layout sketch to show locations of piping and associated components. This should include relative locations both horizontally and vertically.

Page 49 of 61

Limerick Generating Station Units 1 and 2 Overall Integrated Plan for Reliable Hardened Vents Sketch 3A: P&ID Layout of SAWA UNIT 1 I o.,T21 NI Page 53 of 61

Limerick Generating Station Units 1 and 2 Overall Integrated Plan for Reliable Hardened Vents Sketch 3B: Site Layout and FLEX/SAWA Deployment ( SAWA)

Point of i*FLEX use Generator Page 54 of 61

Limerick Generating Station Units 1 and 2 Overall Integrated Plan for-Reliable Hardened Vents Attachment 4: Failure Evaluation Table Table 4A: Wetwell HCVS Failure Evaluation Table Functional Failure Failure Cause Alternate Action Failure with Alternate Mode Action Prevents

__________________________ Containment Venting?

Fail to Vent (Open) Valves fail to open/close due to loss of normal None required - system SOVs utilize No on Demand AC power/DC batteries, dedicated 24-hour power supply Valves fail to open/close due to depletion of Recharge system with provided portable No dedicated power supply. generators Valves fail to open/close due to complete loss Manually operate backup pneumatic No of power supplies, supply/vent lines at ROS Valves fail to open/close due to loss of normal No action needed. Valves are provided with No pneumatic supply. dedicated motive force capable of 24-hour operation Valves fail to open/close due to loss of Replace bottles as needed and/or recharge No alternate pneumatic supply (long term)., with portable air compressors Valve fails to open/close due to SOV failure. Manually operate backup pneumatic No

______________supply/vent lines at ROS Fail to stop venting Not credible as there is not a common mode N/A No (Close) on demand failure that would prevent the closure of at least 1 of the 2 valves needed for venting.

_______________Both valves designed to fail shut.

Spurious Opening Not credible as key-locked switches prevent N/A No mispositioning of the HCVS PCIVs and additionally, DC power for the solenoid valve is normally de-energized.

Spurious Closure Valves fail to remain open due to depletion of Recharge system with provided portable No dedicated power supply. generators Valves fail to remain open due to complete Manually operate backup pneumatic No loss of power supplies, supply/vent lines at ROS Valves fail to remain open due to loss of Replace bottles as needed and/or recharge No alternate pneumatic supply (long term). with portable air compressors Page 55 of 6l

Limerick Generating Station Units 1 and 2 Overall Integrated Plan for Reliable Hardened Vents Attachment 5: References

1. Overall Integrated Plan in Response to March 12, 2012 Commission Order Modifying Licenses with Regard to Requirements for Mitigation Strategies for Beyond-Design Basis External Events (Order Number EA-12-049),

dated February 28, 2013 (ML13060A127)

2. Generic Letter 89-16, Installation of a Hardened Wetwell Vent, dated September 1, 1989
3. Order EA-12-049, Mitigation Strategies for Beyond-Design-Basis External Events, dated March 12, 2012
4. Order EA- 13-109, Severe Accident Reliable Hardened Containment Vents, dated June 6, 2013
5. JLD-ISG-2012-0l, Compliance with Order EA-12-049, Mitigation Strategies for Beyond-Design-Basis External Events, dated August 29, 2012
6. JLD-ISG-2013-02, Compliance with Order EA-13-109, Severe Accident Reliable Hardened Containment Vents, dated November 14, 2013
7. NRC Responses to Public Comments, Japan Lessons-Learned Project Directorate Interim Staff Guidance JLD-IS G-2012-02: Compliance with Order EA-12-050, Order Modifying Licenses with Regard to Reliable Hardened Containment Vents, ADAMS Accession No. ML12229A477, dated August 29, 2012
8. NEI 12-06, Diverse and Flexible Coping Strategies (FLEX) Implementation Guide, Revision 0, dated August 2012
9. NEI 13-02, Industry Guidance for Compliance with Order EA-13--109, Revision 1, Dated April 2015
10. NEI 13-06, Enhancements to Emergency Response Capabilities for Beyond Design Basis Accidents and Events, Revision 0, dated March 2014
11. NEI 14-0 1, Emergency Response Procedures and Guidelines for Extreme Events and Severe Accidents, Revision 0, dated March 2014
12. NEI HCVS-FAQ-01, HCVS Primary Controls and Alternate Controls and Monitoring Locations
13. NEI HCVS-FAQ-02, HCVS Dedicated Equipment
14. NEI HCVS-FAQ-03, HCVS Alternate Control Operating Mechanisms
15. NEI HCVS-FAQ-04, HCVS Release Point
16. NEI HCVS-FAQ-05, HCVS Control and 'Boundary Valves'
17. Not Used
18. NEI HCVS-FAQ-07, Consideration of Release from Spent Fuel Pool Anomalies
19. Not Used
20. NEI HCVS-FAQ-09, Use of Toolbox Actions for Personnel
21. NEI White Paper HCVS-WP-01, HCVS Dedicated Power and Motive Force
22. NEI White Paper HCVS-WP-02, HCVS Cyclic Operations Approach
23. Not Used
24. Not Used
25. Not Used
26. SECY-12-0 157, Consideration of Additional Requirements for Containment Venting Systems for Boiling Water Reactors with Mark I and Mark II Containments, 11/26/12
27. Limerick USAR, Rev. 17, Updated Safety Analysis Report
28. IEEE Standard 344-2004, IEEE Recommended Practice for Seismic Qualification of Class 1E Equipment for Nuclear Power Generating Stations
29. FLEX MAAP Endorsement ML13190A201
30. Not Used
31. JLD-ISG-2015-01, Compliance with Phase 2 of Order EA-13-109, Order Modifying Licenses with Regard to Reliable Hardened Containment Vents Capable of Operation under Severe Accident Conditions, dated April 2015
32. NEI White Paper HCVS-WP-04, Missile Evaluation for HCVS Components 30 Feet Above Grade, Revision 0, dated August 17, 2015
33. NEI HCVS-FAQ-10, Severe Accident Multiple Unit Response
34. NEI HCVS-FAQ- 11, Plant Response During a Severe Accident
35. NEI HCVS-FAQ-12, Radiological Evaluations on Plant Actions Prior to HCVS Initial Use
36. Not Used Page 56 of 6l

Limerick Generating Station Units 1 and 2 Overall Integrated Plan for Reliable Hardened Vents

37. NUREG-1935, State-of-the-Art Reactor Consequence Analyses (SOARCA) Report, Nov 2012
38. NEI White Paper HCVS-WP-04: Missile Evaluation for HCVS Components 30 Feet Above Grade
39. EPRI Technical Report , Technical Basis for Severe Accident Mitigating Strategies: Volume 1, April, 30, 2015, Product'ID 3002003301 Page 57 of 61

Limerick Generating Station Units 1 and 2 Overall Integrated Plan for Reliable Hardened Vents Attachment 6: Changes/Updates to this Overall Integrated Implementation Plan This Overall IntegratedPlan has been updated in format and content to encompass both Phase 1 and Phase 2 of Order EA-13-109. Any significant changes to this plan will be communicated to the NRC staff in the 6 Month Status Reports.

Page 58 of 61

Limerick Generating Station Units 1 and 2 Overall Integrated Plan for Reliable Hardened Vents Attachment 7: List of Overall Integrated Plan Open Items The following tables provide a summary of the open items documented in the Phase]I Overall Integrated Plan or the Interim Staff Evaluation (ISE) and the status of each item.

Open Phase]1 Open Items from QIP Status Item IDetermine how Motive Power and/or HCVS Battery Power will be disabled during normal Deleted. Closed to ISE Open Item number 1.

operation.

2 Confirmn that the Remote OperatingStation (ROS) will be in an accessible areafollowing a Deleted. Closed to ISE Open Item number 3 Severe Accident (SA).

3 Determine wetwell line size to meet 1% venting criteria. Deleted. Closed to 1SE Open Item number 4.

4 Confirm suppression pool heat capacity. Deleted. Closed to ISE Open Item number 4.

5 Determine the approachfor combustible gases. Deleted. Closed to ISE Open Item numbers 9 and 10.

6 Provide proceduresfor HCVS Operation. Deleted. Closed to ISE Open Item number 13.

7 Verify the external piping consists solely of large bore piping and its supports have less than 300 Not Started squarefeet of cross section.

8 Evaluate drywell pressure indicationfor environmental qualifications to ensure this instrument Not Started can survive for 7 days after an event.

9 Determine Performance Criteriafor Motive gas Cylinders, Argon Cylinders, FLEX Diesel Not Started Generator, and FLEX (SA WA) pump pressure at 500 gpm.

I0 Perform radiologicalevaluationfor Phase 1ivent line impact on ERO response actions. Not Started

  • Open Interim Staff Evaluation (ISE) Open Items Status Item 1 Make availablefor NRC staff audit documentation of a method to disable HCVS Started Page 59 of 61

Limerick Generating Station Units 1 and 2 Overall Integrated Plan for Reliable Hardened Vents Open Interim Staff Evaluation (ISE) Open Items Status Item during normal operation to provide assurances against inadvertent operationthat also minimizes actions to enable HCVS operationfollowing an ELAP.

2 Make availablefor NRC staff audit the final sizing evaluationfor HCVS Not Started batteries/batterycharger including incorporationinto FLEX DG loading calculation.

3 Make availablefor NRC staff audit an evaluation of temperatureand radiological Not Started conditions to ensure that operatingpersonnel can safely access and operate controls and support equipment.

4 Make availablefo~r NRC staff audit analyses demonstratingthat HCVS has the Started - The required one percent capacity at capacity to vent the steam/energy equivalent of one percent of licensed/rated thermal the lower of Primary Containment Pressure power (unless a lower value is justified), and that the suppression pool and the HCVS Limit or containment design pressure will be together are able to absorb and reject decay heat, such that following a reactor verified using Reactor Excursion and Leak shutdown from full power containmentpressure is restored and then maintained Analysis Program(RELAP). In addition, below the primary containment design pressure and the primary containment pressure Modular Accident Analysis Program (MAAP) limit, analyses will be credited to verify that venting can be delayed for, at least three hours and that anticipatory venting can be credited to maintain Reactor Core Isolation Cooling (RCIC) functional.

5 Make availablefor NRC staff audit the seismic and tornado missile final design Started. As discussed in the December 2015 criteriafor the HCVS stack. QIP submittal, the Limerick design complies with the reasonable tornado protection criteria of HCVS-WP-04.

6 Make availablefor NRC staff audit the descriptions of local conditions (temperature, Not Started radiationand humidity) anticipatedduring ELAP and severe accidentfor the components (valves, instrumentation,sensors, transmitters, indicators, electronics, control devices, etc.) requiredfor HCVS venting including confirmation that the components are capable of performing theirfunctions during ELAP and severe accident conditions.

7 Make availablefor NRC staff audit documentation of the HCVS nitrogen-pneumatic Not Started system design including sizing and location.

8 Make availablefor NRC staff audit documentation that demonstratesadequate Not Started commnunication between the remote HCVS operation locations and HCVS decision makers during ELAP and severe accident conditions.

9 Provide a description of the final design of the HCVS to address hydrogen detonation Started. As discussed in the December 2015 and deflagration. OIP submittal, the Limerick design will use an

______ _______________________________________________________ Argon purge system to prevent the possibility Page 60 of 61

Limerick Generating Station Units 1 and 2 Overall Integrated Plan for Reliable Hardened Vents Open Interim Staff Evaluation (ISE) Open Items Status Item of hydrogen detonationand deflagration.

10 Provide a description of the strategiesfor hydrogen control that minimizes the Started. As discussed in the December 2015 potentialfor hydrogen gas migration and ingress into the reactor building or other QIP, the Limerick wetwell vent line for each buildings. unit has a dedicated HCVS flowpath from the wetwell penetration to the outside with no interconnected system. The dischargepoint meets the guidance of HCVS-FAQ-04.

11 Make availablefor NRC staff audit documentation of a seismic qualification Not Started evaluation of HCVS components.

12 Make availablefor NRC staff audit descriptions of all instrumentation and controls Not Started (existing and planned) necessary to implement this order including qualification methods.

13 Make availablefor NRC staff audit the proceduresfor HCVS operation. Not Started Open Item Phase 2 Overall IntegratedPlan (OIP) Open Items Status 1 Nonet I t Page 61 of 61