NL-04-121, Reply to Request for Additional Information Regarding Indian Point 2 Stretch Power Uprate

From kanterella
(Redirected from NL-04-121)
Jump to navigation Jump to search

Reply to Request for Additional Information Regarding Indian Point 2 Stretch Power Uprate
ML042720432
Person / Time
Site: Indian Point Entergy icon.png
Issue date: 09/24/2004
From: Dacimo F
Entergy Nuclear Northeast
To:
Document Control Desk, Office of Nuclear Reactor Regulation
References
NL-04-121, TAC MC1865
Download: ML042720432 (15)


Text

I'En tergy Entergy Nuclear Northeast Indian Point Energy Center 450 Broadway, GSB PO. Box 249 Buchanan, NY 10511-0249 Tel 914 734 6700 Fred Dacimo Site Vice President Administration September 24, 2004 Re:

Indian Point Unit No. 2 Docket No. 50-247 NL-04-121 U.S. Nuclear Regulatory Commission ATTN: Document Control Desk Washington, DC 20555-0001

SUBJECT:

Reply to Request for Additional Information Regarding Indian Point 2 Stretch Power Uprate (TAC MC1865)

Reference:

1. Entergy letter to NRC (NL-04-005); "Proposed Changes to Technical Specifications: Stretch Power Uprate Increase of Licensed Thermal Power (3.26%)", dated January 29, 2004.

Dear Sir:

This letter provides additional information, requested by the NRC during recent telephone conference calls, regarding the license amendment request submitted by Entergy Nuclear Operations, Inc (Entergy), in Reference 1. The requested information, provided in Attachment 1 does not alter the conclusions of the no significant hazards evaluation that supports this license amendment request.

There are no new commitments identified in this submittal. If you have any questions or require additional information, please contact Mr. Kevin Kingsley at 914-734-6695.

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

Executed on September..

, 2004.

'Fred R. Dacimo Site Vice President Indian Point Energy Center cc: next page A,DOI

NL-04-121 Docket 50-247 Page 2 of 2 Mr. Patrick D. Milano, Senior Project Manager Project Directorate I, Division of Reactor Projects I/Il U.S. Nuclear Regulatory Commission Mail Stop 0 8 C2 Washington, DC 20555 Mr. Samuel J. Collins Regional Administrator Region I U.S. Nuclear Regulatory Commission 475 Allendale Road King of Prussia, PA 19406 Resident Inspector's Office Indian Point Unit 2 U.S. Nuclear Regulatory Commission P.O. Box 59 Buchanan, NY 10511 Mr. Peter R. Smith President, NYSERDA 17 Columbia Circle Albany, NY 12203 Mr. Paul Eddy New York State Dept. of Public Service 3 Empire State Plaza Albany, NY 12223

ATTACHMENT 1 TO NL-04-121 REPLY TO NRC REQUEST FOR ADDITIONAL INFORMATION REGARDING PROPOSED LICENSE AMENDMENT REQUEST FOR INDIAN POINT 2 STRETCH POWER UPRATE ENTERGY NUCLEAR OPERATIONS, INC.

INDIAN POINT NUCLEAR GENERATING UNIT NO. 2 DOCKET NO. 50-247

NL-04-121 Page 1 of 12 Additional information requested by NRC staff via telephone conference calls in August and September, 2004.

NRC Item 1:

Recognizing the small decrease in the Tcold lower design value corresponding to a lower bound full-power programmed T8,g of 5490F for some components could be significant for fatigue evaluation, verify that the current design basis calculations have sufficient margin for all RCS components (RV, RVls, piping/supports, pressurizer, RCPs, and SGs).

Entercv Response:

The only evaluations for which lower bound Tcold is limiting and for which a value of 515.50F was used are the RCPs and the pressurizer spray nozzle. Engineering judgment indicates that sufficient margin is available to accommodate a 1.50F change. Nevertheless, as indicated in Note 7 for Table 2.1-2 (of WCAP 16157 submitted by NL-04-005), actual operation of Indian Point 2 (IP2) is limited to a minimum Tcold of 5250F to support the vessel integrity calculations discussed in subsection 5.1.2 of the WCAP. Based on this limit, evaluations of NSSS components for a Tcld of 514'F or a T.,d of 515.50F bound the actual operation of IP2 at the SPU power level. Structural evaluations of individual NSSS components are documented in Chapter 5 of the WCAP and show that stress and fatigue limits are met for the SPU evaluation conditions.

NRC Item 2:

The Entergy response for Piping and Supports Question 1, in letter NL-04-095 dated August 3, 2004, provides a stress summary table for main steam piping. Please provide similar quantitative results for evaluations performed for other balance-of-plant (BOP) piping systems.

Entergy Response:

Stress summary tables are provided below, as requested, for other BOP piping systems.

These four systems reflect the next four SPU-sensitive systems after Main Steam. Pipe stresses were assessed based on pre and post SPU system conditions. The results presented include existing stress levels (i.e., pre-SPU), revised pipe stress levels for post-SPU conditions, allowable stress for the applicable loading condition, and the resulting design margin for each piping analysis that was evaluated to reconcile SPU conditions. The design margin provided is based on the ratio of the calculated post-SPU stress divided by the allowable stress.

NL-04-121 Attachment I Page 2 of 12 Response to Item 2, continued Table 2 Feedwater System Stress Summary Piping Analysis Loading Existing SPU Allowable Design Description Condition Stress (psi)

Stress (psi) Stress (psi)

Margin Feedwater to SG 22 DL + LP 8,614 8,812 15,000 0.59 Feedwaterto SG 22 Thermal 17,456 17,784 22,500 0.79 Feedwater to SG 23 DL + LP 8,507 8,705 15,000 0.58 Feedwater to SG 23 Thermal 4,317 4,441 22,500 0.20 Feedwater to SG 24 DL + LP 8,363 8,561 15,000 0.57 Feedwater to SG 24 Thermal 9,679 10,085 22,500 0.45 Table 3 Extraction Steam System Stress Summary Piping Analysis Loading Existing SPU Allowable Design Description Condition Stress (psi)

Stress (psi) Stress (psi)

Margin Extraction Steam to DL + LP 1,873 1,892 15,000 0.13 Heaters 23AIB/C Extraction Steam to Thermal 4,966 5,054 22,500 0.22 Heaters 23AJB/C Table 4 FW Heater Vents and Drains System Stress Summary Piping Analysis Loading Existing SPU Allowable Design Description Condition Stress (psi) Stress (psi)

Stress (psi)

Margin Heaters 24A/BIC to DL + LP 1,819 1,837 15,000 0.12 Heaters 23A/B/C Heaters 24A/B/C to Thermal 14,262 14,499 22,500 0.64 Heaters 23A/B/C Note: Loading Condition DL + LP corresponds to the combination of stresses due to deadweight + pressure.

NL-04-1 21 Page 3 of 12 NRC Item 3:

Verify that controls are in place to assure that PCT sensitive parameters used in LOCA analyses bound plant-operating conditions.

Enteray Response:

Entergy Nuclear Operations, Inc. and Westinghouse have on-going processes which assure that the ranges and values of LOCA analyses inputs for Peak Cladding Temperature (PCT) sensitive parameters bound the as-operated plant ranges and values for those parameters.

NRC Item 4:

The Entergy response for Steam Generator structural integrity RAI 3 in letter NL-04-073, dated June 16, 2004 applies a quality factor of 0.5 for determining the stress acceptance criteria.

Please explain the use of this factor.

Entergy Response:

The shop weld plug is welded to the tube end using a full penetration weld. This weld geometry is similar to a corner weld configuration as shown in Figure N-462.3 (2) of the 1965 ASME Code, Section 1II, Article 4 (Equivalent to Figure NB-3352.3-1, Type l b of later code years).

The ASME Code of Record for the design of the steam generator is the 1965 ASME Code, through the Summer 1966 Addenda. The ASME Code, Section 1II, Article 4 (Section NB of later codes) does not require or specify a factor to be applied to the stress allowable values to reduce the values due to weld quality. It has been Westinghouse's approach to apply a weld quality factor to this weld of the shop weld plug to a tube. This is a conservative approach since the ASME Code is silent on applying a weld quality factor. The weld was analyzed based on the ASME Code, Section 1I1, Article 4 and all stresses are found acceptable.

NRC Item 5:

The Licensing Report (WCAP 16157 submitted by NL-04-005) describes the time to boil upon loss of cooling to the spent fuel pool changing from 1.8 hours9.259259e-5 days <br />0.00222 hours <br />1.322751e-5 weeks <br />3.044e-6 months <br /> to 1.67 hours7.75463e-4 days <br />0.0186 hours <br />1.107804e-4 weeks <br />2.54935e-5 months <br />. Discuss this change which the staff considers a change to the licensing basis needing prior NRC approval.

EnterciY ResPonse:

Entergy has reevaluated the time to boil estimate for the IP2 SPU and the existing 1.8 - hour time to boil estimate is maintained.

NL-04-121 Page 4 of 12 NRC Item 6:

Table 5.9-5 of WCAP 16157-P provides information regarding the fracture integrity evaluation for the pressurizer. The table indicates use of a flaw depth less than u% t " for the corner region of the safety and relief nozzles (0.5 inch flaw size used) and for the upper shell (0.15 inch flaw size used). Since these values do not meet the requirements of Appendix G of Section III of the ASME Code please cite the staff safety evaluation that approved the use of flaw sizes less than

/4 t " or provide other explanation regarding use of the specified flaw sizes.

Entergy Response:

In order to quantify the acceptable flaw size for the 1P2 pressurizer upper shell and the safety and relief nozzles, an analysis using the ASME code Section 1II, Appendix G requirements was performed. This analysis was recently revised. The fracture mechanics analysis for the IP2 pressurizer upper shell has been revised to consider an updated technical evaluation of the spray characteristic of the inadvertent spray transient based on tests and analytical solutions that showed the spray droplet envelope remains well removed from the pressurizer wall at pressures above 1030 psia. This fracture mechanics analysis also included modified through-wall stresses for the governing location. Since the section thickness for the upper shell is 4.1875 inches, a 1/4t (1.05 inches) deep defect was conservatively postulated per Paragraph G-2120 of the ASME Code, Appendix G 1998 Edition. The analysis for the safety and relief nozzle was also revised using modified through-wall stresses. A defect of 1 inch was again postulated since the section thickness of the governing location for the pressurizer safety and relief nozzle is less than 4 inches. The results show that the maximum stress intensity factor Kfor the governing transient is less than KIR. Therefore, it is concluded that the Indian Point Unit 2 Pressurizer Upper Shell and Safety & Relief Nozzle are in compliance with the ASME Code, Section 1II, Appendix G 1998 Edition requirements for the SPU conditions. The results are summarized below.

Fracture Integrity Evaluation Summary Indian Point Unit 2 - Pressurizer Upper Shell and Safety & Relief Nozzle Flaw Location Governing Transient Depth KIIKIR (inch)

Upper Shell Loss of Load 1/4t (1.05) 0.73 Safety & Relief Nozzle Loss of Load 1

0.66

NL-04-121 Page 5 of 12 NRC Item 7:

During a CVCS malfunction to induce a boron dilution transient, Entergy chose to use a mixing volume that is equal to the RHR and RCS volumes. This appears to be non-conservative. The staff feels that the transient involves, conservatively, only diluted water from the primary water storage tank is injected into the cold leg through the charging lines at maximum letdown rate.

This flow would then only mix with the volume of water in the cold leg and downcomer and lower plenum provided the RCPs were on. If they are not on, then there is less justification for mixing and it may be a dilute slug entering the core to cause a local power spike. The staff questions why the licensee is assuming RHR and RCS volume as the mixing volumes.

Entergy Response:

The CVCS malfunction event is discussed in WCAP-16157 Licensing Report Section 6.3.5. The question is best addressed by plant mode and the operation of the Reactor Coolant Pumps and the RHR System.

Modes 1, 2, 3: One or more Reactor Coolant Pumps are in service and thus adequate mixing is assured.

Modes 4 and 5: At least one Reactor Coolant Pump is in service on shutdowns until Reactor Coolant System temperature is less than approximately 1700F. The RHR System is placed in service when the Reactor Coolant System temperature is less than approximately 3500F thus assuring adequate mixing. Similarly, during startup, the RHR System is in service and a Reactor Coolant Pump is placed in service while Reactor Coolant System temperature is less than 2000F. In addition, the Westinghouse Interim Operating Procedure was developed specifically for these modes, addressing the potential effects of a "dilution front" and a limited active mixing volume, and has been incorporated in plant procedures. The discussion of the supporting analysis for this event was held with the staff in a September 8, 2004 phone call.

In addition, for modes 4 and 5, at the pressures in the Reactor Coolant System associated with RHR operation (less than 450 psig) letdown flow is limited to 120 gpm. Second, only two charging pumps (90 gpm each) are permitted to be available due to low temperature over pressurization restrictions.

Mode 6: At least one RHR pump (providing a minimum flow rate of 1000 gpm) is in service except during short periods. This flow rate is considered adequate for mixing in the lower plenum. The actual flow from one RHR pump would be much higher than 1000 gpm. While the CVCS Malfunction event has been analyzed in the refueling mode, it is administratively precluded. Prior to entering Mode 6 (Refueling), plant procedures require implementation and documentation that dilution paths are isolated. The Indian Point Unit 2 UFSAR will be revised to reference the plant procedures that preclude conditions that would lead to boron dilution in Mode 6.

Based on the above, Entergy concludes that adequate mixing for the active RCS volumes is available or that administrative controls preclude boron dilution.

The staff also requested additional information on how the calculations were performed. The discussion below provides the information requested:

NL-04-121 Page 6 of 12 The time to reach criticality for the CVCS malfunction event, Modes 1, 2 and 6, is calculated based on the following equation.

Cb(t) = Cbi

  • e A [-(mdil / M)
  • t]

Where:

Cb(t) = boron concentration of the system as a function of time Cbi = initial boron concentration of the system mdil = mass flow rate of diluent M = initial mass of the system t = time In using this equation, it is assumed that the system has a constant mass and that the concentration of the diluent is equal to zero.

NRC Item 8:

Section 5.10.4 of the Stretch Power Uprate Licensing Report (WCAP-16157) provides an estimated increase in PWSCC susceptibility of 31 percent for the reactor pressure vessel head penetrations as a result of the stretch power uprate. An increase of greater than 20 percent is considered by the NRC staff to be significant. Please provide additional information regarding the estimated increase in PWSCC susceptibility and is there a plan for RPV head replacement.

Also, Section 5.10.4 of the Stretch Power Uprate Licensing Report provides an estimated increase in PWSCC susceptibility of 12 percent for the RV hot leg nozzle weld as a result of SPU. How will the 12 percent increase be accommodated in the future?

EntergV Response:

The approach used in Section 5.10.4, was to estimate a relative effect of PWSCC susceptibility by estimating the temperature change in the upper head region based on a conservatively wide range of operating temperatures that correspond to a full-power programmed Tavg range from 549 OF to 572 OF. The resulting temperature increase of 3.88 OF was evaluated using the crack initiation probability methodology described in Reference 2 of Section 5.10.

In practice, Entergy is required to establish RPV head inspection requirements in accordance with NRC Order EA-03-009. The Order provides for a time-at-temperature methodology to determine the effective degradation years (EDY) value that is used to determine the inspection category. Based on the current plant operating history and cycle-specific temperature data, the projected EDY value applicable for the next refueling outage (Fall 2004) is 9.6 years. The current temperature used for this analysis is 590 OF, and the current EDY accumulation rate is less than 0.7 EDY per effective full power year of operation. At the current power level, the transition from the moderate susceptibility category to the high susceptibility category (12 EDY) would occur for the inspection during the Spring 2010 refueling outage.

Using a conservatively high estimate of 4 OF for the effect of SPU on the temperatures in the upper head region, the EDY accumulation rate increases to less than 0.8 EDY per effective full

NL-04-121 Page 7 of 12 power year of operation. Under these conditions, the transition from the moderate susceptibility category to the high susceptibility category could potentially occur one refueling outage earlier (Spring 2008). In that case the applicable inspection requirements would be implemented at that time. However, since the actual planned full-power programmed Tavg for SPU (562 OF) is less than the upTper value evaluated, the effect on the upper head temperature would also be less than the 4 F used in this evaluation. As required by the NRC Order, Entergy will recalculate the EDY value to establish the inspection requirements for each refueling outage using plant data for each operating cycle.

Entergy is assessing options to mitigate the effects of PWSCC on continued plant operation.

One possible option involves a modification that would result in reduction of the upper head temperature. Entergy is also assessing eventual replacement of the reactor vessel head.

A similar assessment of PWSCC susceptibility for the RCS hot leg nozzle welds was performed.

Although the NRC Order does not establish EDY categories and inspection requirements for these locations, Entergy is required to inspect these areas in accordance with ASME Section Xl and the IP2 Inservice Inspection Program. Also, Entergy is participating in industry programs that monitor operating experience and develop recommendations, including augmented inspections. MRP has recently issued recommendations (MRP 2003-039, dated January 20, 2004) that include visual inspection of the hot leg nozzle welds. During the upcoming refueling (Fall 2004) Entergy will be performing volumetric NDE of these welds as part of the 10-year ISI inspection program. This inspection exceeds the visual inspection recommendations of MRP 2003-039.

Additional Item From Entergy:

Attached is an update for the reply to LOCA Transient Question 4, previously provided in Entergy letter NL-04-100 dated August 12, 2004. This update reflects a correction to results reported for heat transfer in the downcomer region, which has a small effect on Figures 1 through 4, but the conclusion regarding the time to reach stable and sustained quench for LBLOCA is not changed by this correction.

NL-04-121 Page 8 of 12 UPDATED REPLY TO LOCA TRANSIENT QUESTION 4 (Replaces response previously provided in NL-04-100, dated August 12, 2004)

LOCA Transient Question 4:

Provide the LBLOCA analysis results (tables and graphs, as appropriate) to the time that stable and sustained quench is established.

Response

In order to demonstrate stable and sustained quench, the WCOBRAITRAC calculation for the maximum local oxidation analysis was extended. Figure 1 shows the peak cladding temperatures for the five rods modeled in WCOBRA/TRAC. This figure indicates that quench occurs at approximately 275 seconds for the low power rod (rod 5), 400 seconds for the core average rods (rods 3 and 4), and 500 seconds for the hot rod (rod 1) and hot assembly average rod (rod 2). Once quench is predicted to occur, the rod temperatures remain slightly above the fluid saturation temperature for the remainder of the simulation. Figure 2 shows the collapsed liquid level in the four downcomer channels and shows steady behavior, with the level in each quadrant remaining near the bottom of the cold leg. Figure 3 shows the collapsed liquid level in the four core channels and indicates a gradual increase in the core liquid inventory. This is consistent with the expected result based on the removal of the initial core stored energy and the gradual reduction in decay heat. Figure 4 shows the vessel liquid mass and indicates stable and increasing trend beginning at about 700 seconds. This indicates that the increase in inventory due to the pumped safety injection is more than offsetting the loss of inventory through the break. Based on these results, it is concluded that stable and sustained quench has been established for the Indian Point Unit 2 Large Break LOCA analysis.

PCT PCT


PCT PCT PCT 1

0 0 HOT ROD 2

0 0 HA AVERAGE ROD 3

0 0 CORE AVERAGE ROD 4

0 0 CORE AVERAGE ROD 5

0 0 LOW POWER ROD 2500 2000 I A 1500 ci-12 0, 1000 500 0

A" 4A I

IA A

A I_

A Y'

- 1, LJI+/-f 1.~ 'r, L,~

J J+/-

0 200 400 600 600 Time (sec) 1000 1200 1400 1600 Figure 1 - Peak Cladding Temperatures NL-04-121 Attachment I Page 9 of 12

LO-LEVEL LO-LEVEL LO-LEVEL LO-LEVEL 7

0 0 DC 1

8 0

0 DC 2

9 0

0 DC 3

10 0

0 DC 4

40 35 30

_ 25

-J c20

'3 cn CD-10 w

cn 5 0

Time (sec)

Figure 2 - Downcomer Collapsed Liquid Levels NL-04-121 Page 10 of 12

LO-LEVEL LO-LEVEL LQ-LEVEL LO-LEVEL 3

0 0 LP CHANNEL 4

0 0 OH/SC/FM CHANNEL 5

0 0 CT CHANNEL 6

0 0 HA CHANNEL 12 10 CD

-J z

0D CD, 8

6 4

11a I lli I I at I

IL.

2 0

0 200 4100 600 8 0 Time (sec) 1000 1200 1400 1600 Figure 3 - Core Collapsed Liquid Levels NL-04-121 Affachment I Page 11 of 12

VFMASS 200000- T 0

0 0 VESSEL WATER MASS 150000 100000 C,-

-0 5n cn aKX 0

Time (sec)

Figure 4 - Vessel Liquid Mass NL-04-121 Page 12 of 12