ML023040302
| ML023040302 | |
| Person / Time | |
|---|---|
| Site: | Kewaunee |
| Issue date: | 10/21/2002 |
| From: | Coutu T Nuclear Management Co |
| To: | Document Control Desk, Office of Nuclear Reactor Regulation |
| References | |
| NRC-02-096 | |
| Download: ML023040302 (63) | |
Text
Kewaunee Nuclear Power Plant Point Beach Nuclear Plant N490 Highway 42 6610 Nuclear Road Kewaunee, Wl 54216-9511 Two Rivers, Wl 54241 NMC 920 388 2560 920 755 2321 Committed to Nuclear Excellence Kewaunee I Point Beach Nuclear Operated by Nuclear Management Company, LLC NRC-02-096 October 21, 2002 10 CFR 50.67 U.S. Nuclear Regulatory Commission Attention: Document Control Desk Washington, D.C. 20555 Ladies/Gentlemen:
Docket 50-305 Operating License DPR-43 Kewaunee Nuclear Power Plant Kewaunee Nuclear Power Plant Alternate Source Term Report - Revision 2
References:
- 1)
Letter from Mark E. Warner (NMC) to Document Control Deck (NRC),
"Revision to the Design Basis Radiological Analysis Accident Source Term,"
dated March 19, 2002.
- 2)
Letter from John G. Lamb (NRC) to Mark E. Warner (NMC), "Kewaunee Nuclear Power Plant - Request for Additional Information Related to Proposed Revision to the Kewaunee Nuclear Power Plant Design-Basis Radiological Analysis Accident Source Term (TAC NO. MB4596), dated July 3, 2002.
- 3)
Letter from Thomas Coutu (NMC) to Document Control Desk (NRC), dated September 13, 2002, "Response to Request for Additional Information Related to Proposed Revision to the Kewaunee Nuclear Power Plant Design Basis Radiological Analysis Accident Source Term."
In accordance with 10 CFR 50.67 the Nuclear Management Company (NMC) is submitting Revision 2 to the engineering report for the radiological consequences of accidents using alternative source term methodology (Regulatory Guide 1.183) for the Kewaunee Nuclear Power Plant. In reference 1, NMC submitted the original version of this report for approval. On further review of this report, several changes were identified (see items 1-5 on page 2). Before submitting revision I of the report to the NRC a correction to the reactor coolant gross specific activity limit was discovered (item 6 on page 2). Immediately revision 2 was issued correcting the reactor coolant gross specific activity limit and is hereby submitted.
Docket 50-305 NRC-02-096 October 21, 2002 Page 2 The attached report (attachment 3) is Revision 2 of the engineering report for the radiological consequences of accidents using alternative source term methodology (Regulatory Guide 1.183) for the Kewaunee Nuclear Power Plant. The changes from the original version to Revision 2 are:
- 1. The report provided in reference 1 erroneously lists the spray fall height as 65 feet (on Pages 10 and 44). The correct spray fall height is 150 feet. This spray fall height of 150 feet was used to calculate the spray removal coefficients used in the LOCA dose analysis.
Investigation of this error concluded that the value of 65 feet was the fall height modeled for the LOCA dose analysis of another plant. The report of that plant was used as a template when Westinghouse initially drafted the Kewaunee report.
- 2. A typographical error in the description of the assumed airborne fraction for ECCS leakage to the auxiliary building ECCS in Section 2.2.4 of the report was corrected (page 11). The original engineering report listed this assumed airborne fraction as 10%. This value was in error. The correct assumed airborne fraction is 1% and the calculations for this report used the airborne fraction of 1%.
- 3. In the LOCA and rod ejection analyses, the TITAN5 model used for the releases from the shield building was not modified in the noble gas runs to prevent the filters from reducing the activity released to the atmosphere. The two calculation notes have been revised to correct this error. This results in an increase in the calculated doses for these two events.
Investigation of this error concluded that the TITAN5 User Manual incorrectly states that the filters are ignored for noble gas cases (pages 12 and 21). Below are the changes in dose.
Dose Change in rem TEDE Site Boundary Low Population Zone Control Room Original Revised Original Revised Original Revised LOCA 0.7 1.31 0.15 0.24 4.30 4.95 Rod Ejection 0.50 0.52 No Change No Change
- 4. In response to an RAI received from the NRC on Revision 0 of the report (reference 2, question 13) the LOCA dose results have been expanded to specify the contributions from the three release paths (page 12).
- 5. Editorial corrections (pages 11, added "the", and 45, capitalized Generator).
- 6. The identification of the technical specification value for the reactor coolant gross specific activity limit as 100/E-bar [tCi/gm was corrected. The correct value is 91/E-bar jtCi/gm (pages 14 and 25).
Additionally, during a conference call between the NRC staff, NMC staff, and Westinghouse staff, to discuss these report changes, a question arose concerning Kewaunee Updated Safety Analysis Report (USAR) Section 11.1.3, "Gaseous Waste." In this section, it states that release specifications for the gas decay tanks are contained in the Kewaunee Off-Site Dose Calculation Manual (ODCM).
Docket 50-305 NRC-02-096 October 21, 2002 Page 3 The KNPP ODCM contains release specification concerning the gas decay tanks but not for accident conditions. This specification is provided to ensure that the dose, at any time, at and beyond the site boundary from gaseous effluents will be within the annual dose limits of 10 CFR 20 to unrestricted areas. Therefore, these limits are concerned with normal plant operation and its gaseous effluents not for accident conditions. to this letter contains additional information for NMC response (reference 3) to the NRC questions 5, 11, 12, and 13. Attachment 2 contains Kewaunee Nuclear Power Plant's Final Safety Analysis Report (FSAR) page 14.3-68, dated June 16, 1972. Attachment 3 contains the Engineering Report for the Radiological Consequences of Accidents Using Alternative Source Term Methodology (Regulatory Guide 1.183) for the Kewaunee Nuclear Power Plant - Revision 2.
This submittal contains no proprietary information and makes no new commitments. If there are any further questions or comments contact Jerry Riste at (920) 388-8424 I declare under penalty that the foregoing is true and correct.
Executed on October 21, 2002.
Thomas Coutu Site Vice President GOR Attach.
cc -
US NRC, Region mH US NRC Senior Resident Inspector Electric Division, PSCW
ATTACHMENT 1 Letter from Thomas Coutu (NMC)
To Document Control Desk (NRC)
Dated October 21, 2002 Re: NMC Response to Request for Additional Information (Questions 5, 11, 12, and 13 of Reference Letter 2)
Docket 30-305 NRC-02-096 October 21, 2002, Page 1 NRC Ouestion #5 Table 12 of Attachment 2 lists containment vessel volume as 1.32E6 ft3. State the sprayed and unsprayed volumes of the containment vessel.
NMC Response The containment vessel volume is stated as the net volume (i.e., total volume less structures and components). Therefore, the containment vessel volume of 1.32E6 ft3 is the sprayed containment volume. This is consistent with the licensing basis value used to determine Containment Spray capability in previous submittals to the NRC (reference Updated Control Room Habitability Evaluation Report dated February 1989)(1).
The NRC has previously accepted this Updated Control Room Habitability Evaluation Report (UCRHER). NRC acceptance is documented in the NRC Safety Evaluation (SE) associated with TS amendment 88(2). TS amendment 88 revised action statements concerning containment cooling, shield building ventilation, auxiliary building ventilation, and control room post-accident recirculation system specifications. The basis for the acceptance of TS amendment 88 was the NRC staff's review of the February 1989, Kewaunee Control Room Habitability Evaluation Report. In the SE for TS amendment 88, the NRC staff describes the two different cases that were run to obtain acceptable control room dose results. The UCRHER describes these two cases on page 21 of the report. The results of the analysis listed on page 2 of the SE are the same as the results listed on page 22 of the UCRHER. Table 4 of the UCRHER lists the control room dose analysis parameters. As listed in Table 4, the volume used in the analysis for the containment was the containment free volume of 1.32E+6 ft3.
Also, the spray evaluation parameters that were used to develop the containment spray removal rates for the February 1989 UCRHER are documented in Table 2 of a Fluor Engineering calculation entitled "Control Room Immersion and Inhalation Doses", dated 1-12-89. This calculation supported the 1989 UCRHER. As shown in Table 2 of the Fluor Engineering calculation the containment volume used to determine the spray removal rates is 1.32E6 ft3. This same containm'ent sprayed volume is used in the alternate source term methodology. Therefore, the containment sprayed volume in the current licensing basis analysis for control room habitability is 1.32E6 ft3.
(1) Letter from C.R. Steinhardt (WPSC) to Document Control Deck (NRC), "Submittal of Kewaunee's Control Room Habitability Evaluation Report to Address NRC Concerns Over Control Room Ventilation, dated February 28, 1989 (2) Letter from Michael J. Davis (NRC) to Ken H. Evers (WPSC), Amendment No. 88 to Facility Operating License No.
DPR-43 (TAC No. 76824), dated October 16, 1990
Docket 30-305 NRC-02-096 October 21, 2002, Page 2 NRC Question #11 In Section 2.2.4 of Attachment 2, you also assumed that the iodine partition factor is reduced to 1 percent once the auxiliary building sump water temperature is below 212 F. Provide the technical bases to justify the lower iodine partition factor assumed.
NMC Response This 1% iodine partitioning factor is taken from the original Final Safety Analysis Report (FSAR) and is considered licensing basis. KNPP's USAR Section 6.2.5, "Effects of Leakage From Residual Heat Removal System," identifies the iodine partitioning factors used in the analysis. This section states:
... Various estimates of the fraction of iodine that may be expected to escape from the liquid are approximately 1 OE-4; however, it is conservatively assumed that 1% of the iodine is released (3).
The referenced Kewaunee USAR section 6.2.5 (page 6.2-32) indicates its revision is USAR Rev. 17, dated June 1, 2002. Although this information was not originally in USAR section 6.2.5, it is not a change to KNPP's licensing basis. This information was originally contained in FSAR section 14.3.7, page 14.3-68, which was approved by the Atomic Energy Commission (AEC). In 1999, the USAR was changed and the information was relocated from section 14.3.7 to section 6.2.5, page 6.2
- 32. This change was transmitted to the NRC on December 1, 2000 as USAR revision 16. contains a copy of KNPP's original FSAR, page 14.3-68. As this information was part of our original license, it is still a part of our current licensing basis.
NRC Question #12 In Section 2.2.4 of Attachment 2, you also assumed that half of the iodine activity that becomes airborne from two leak sources in the auxiliary building is removed by plateout on surfaces. Justify your assumption.
NMC Response KNPP's USAR Section 6.2.5, Effects of Leakage From Residual Heat Removal System, identifies that the iodine released from spilled coolant would largely be plated out with approximately 50%
within structures before release through the ventilation system. The area of the release is the same and therefore the plate out assumption was carried forward.
() KNPP USAR, Rev. 17, page 6.2-32
Docket 30-305 NRC-02-096 October 21, 2002, Page 3 The referenced Kewaunee FSAR section 6.2.5 (page 6.2-32) indicates USAR Rev. 17 dated June 1, 2002. This information was originally contained in FSAR section 14.3.7, page 14.3-68, which was approved by the Atomic Energy Commission (AEC). In 1999, the information was relocated from section 14.3.7 to section 6.2.5, page 6.2-32. Attachment 2 contains a copy of FSAR section 14.3.7, page 14.3-68. As this information was part of our original license, it is a part of our current licensing basis.
NRC Question #13 Table 1 of Attachment 2 shows the radiological consequences of the postulated design-basis accidents. List dose contributions from each fission product release pathway (containment leak, ECCS leak, and RWST back-leakage release) to the LOCA doses (EAB, LPZ and control room).
NMC Response Response to this question is included in Revision 2 to the engineering report for the radiological consequences of accidents using alternative source term methodology (Regulatory Guide 1.183) for the Kewaunee Nuclear Power Plant (see attachment 3). A table that lists the dose contributions from each fission product release pathway (containment leak, ECCS leak, and RWST back-leakage release) to the LOCA doses (EAB, LPZ and control room) is located on page 12 of the report.
ATTACHMENT 3 Letter from Thomas Coutu (NMC)
To Document Control Desk (NRC)
Dated October 21, 2002 Westinghouse Engineering Report for the Radiological Consequences of Accidents Using Alternative Source Term Methodology (Regulatory Guide 1.183) for the Kewaunee Nuclear Power Plant
Westinghouse Proprietary Class 3 Engineering Report for the Radiological Consequences of Accidents Using Alternative Source Term Methodology (Regulatory Guide 1.183) for the Kewaunee Nuclear Power Plant Revision 2 September 24, 2002 Prepared by:
- f.
aný U. Bachrach Containment and Radiological Analysis Reviewed by:
-,-f -e
/Containment and Radiological Analysis
-Westinghouse Proprietary Class 3 Table of Contents 1.0 Radiological Consequences Utilizing Alternative Source Terms..............................
2 2.0 Large Break Loss of Coolant Accident Radiological Analysis................................. 7 3.0 Steam Generator Tube Rupture Radiological Analysis............................................
13 4.0 Locked Rotor Radiological Analysis...............................................................
16 5.0 Rod Ejection Radiological Analysis...................................
18 6.0 Fuel Handling Accident Radiological Analysis............................................................
22 7.0 Steam Line Break Radiological Analysis.................................................................
25 8.0 Gas Decay Tank Rupture and Volume Control Tank Rupture Radiological Analyses..... 28 9.0 Conclusions...........................................................................................................
30 10.0 References.................
31 Table 1: Committed Effective Dose Equivalent Dose Conversion Factors.......................... 32 Table 2: Average Gamma Disintegration Energies and Noble Gas Dose Conversion Factors..... 33 Table 3: Offsite Breathing Rates and Atmospheric Dispersion Factors................................
34 Table 4: Control Room Parameters.........................................................................................
35 Table 5: Core Total Fission Product Activities.....................................................................
36 Table 6: RCS Coolant Concentrations....................................................................... 37 Table 7: Nuclide Decay Constants....................................................................... 38 Table 8: Iodine Chemical Species...................................................................... 39 Table 9: Fission Product Release Timing................................................................
40 Table 10: Core Fission Product Release Fractions.................................................... 41 Table 11: RG 1.183 Nuclide Groups.................................................................. 42 Table 12: Assumptions Used for Large Break LOCA Dose Analysis......................................
43 Table 13: Bounding Steam Generator Tube Rupture Thermal Hydraulic Results.................. 45 Table 14: Assumptions Used for Steam Generator Tube Rupture Dose Analysis................. 46 Table 15: Assumptions Used for Locked Rotor Dose Analysis........................................ 47 Table 16: Assumptions Used for Rod Ejection Dose Analysis................................ 48 Table 17: Assumptions Used for Fuel Handling Accident Dose Analysis.......................... 51 Table 18: Assumptions Used for Steam Line Break Dose Analysis.................................. 52 Table 19: Assumptions Used for GDT and VCT Rupture Dose Analyses...............................
53 Page 1154
Westinghouse Propnetary Class 3 1.0 Radiological Consequences Utilizing Alternative Source Terms 1.1 Introduction The Kewaunee Nuclear Power Plant (KNPP) licensing basis for the radiological consequences analyses for Chapter 14 of the UFSAR is currently based on methodologies and assumptions that are derived from TID-14844 (Reference 1) and other early guidance.
Regulatory Guide (RG) 1.183 (Reference 2) provides guidance on application of alternative source terms (AST) in revising the accident source terms used in design basis radiological consequences analyses, as allowed by 10CFR50.67 (Reference 3). This includes modeling consistent with NUREG-1465, "Accident Source Terms for Light Water Nuclear Power Plants" (Reference 4). The alternative source term methodology as established in RG 1.183 (based on NUREG-1465) is being used to calculate the offsite and control room radiological consequences for the KNPP to support the control room habitability program. The following UFSAR chapter 14 radiological consequences analyses are analyzed: LBLOCA, Steam Generator Tube Rupture (SGTR), Locked Rotor, Rod Ejection, Fuel Handling Accident (FHA), Main Steamline Break (MSLB),
Gas Decay Tank (GDT) Rupture, and Volume Control Tank (VCT) Rupture. Each accident and the specific input assumptions are described in detail in subsequent sections in this report.
1.2 Common Analysis Inputs and Assumptions The assumptions and inputs described in this section are common to analyses discussed in this report. The accident specific inputs and assumptions are discussed in Sections 2 through 8.
The total effective dose equivalent (TEDE) doses are determined at the site boundary (SB) for the limiting two hour interval, at the low population zone (LPZ) and to control room personnel (CR) for the duration of the event. The dose conversion factors (DCFs) used in determining the committed effective dose equivalent (CEDE) or inhalation dose are from Reference 5. The TEDE dose is equivalent to the CEDE dose plus the acute dose for the duration of exposure to the cloud. The CEDE dose DCFs are given in Table 1.
The y-body (acute) doses are based on the average disintegration energies from Reference 6 for the iodine isotopes and from Reference 7 for the remainder of the nuclides (except the noble gases). The dose conversion factors for the noble gases are taken from ICRP Publication 30 (Reference 8). The average disintegration energies and dose conversion factors for the y-body doses are listed in Table 2.
The offsite breathing rates and the offsite atmospheric dispersion factors used in the offsite radiological calculations are provided in Table 3.
Parameters modeled in the control room personnel dose calculations are provided in Table 4. These parameters include the normal operation flowrates, the emergency operation flowrates, control room volume, filter efficiencies and control room operator Page 2/54
Westinghouse Proprietary Class 3 breathing rates. In the analyses presented in this report, the control room is modeled as a discrete volume. The atmospheric dispersion factors calculated for release of activity from the release point to the control room intake are used to determine the activity available at the intake. The inflow (filtered and unfiltered) to the control room and the control room recirculation flow are used to calculate the activity introduced to the control room and cleanup of activity from that flow.
The core fission product activity is provided in Table 5 for all nuclides. The Technical Specification nominal reactor coolant activity based on 1% fuel defects for noble gases and other nuclides and 1.0 ptCi/gm Dose Equivalent 1-131 for iodine nuclides is provided in Table 6. The core and coolant activities in Tables 5 and 6 are based on a core power of 1650 MWt increased to 1683 to cover 2% uncertainty. These activities are conservatively increased by an additional 10% prior to input into the analyses presented in this report to allow this analysis to cover future uprating of the plant. Decay constants for each nuclide are provided in Table 7.
1.3 Dose Calculation Models 1.3.1 Offsite Dose Calculation Models Offsite inhalation doses (CEDE) are calculated using the following equation.
DCEDE X
C (:
(IAR)J (BR)j (X /Q)J where:
DCEDE
= CEDE dose via inhalation (rem).
- DCF,
= CEDE dose conversion factor via inhalation for isotope i (rem/Ci) (Table 1)
(IAR),J = integrated activity of isotope i released during the time interval j (Ci)
(BR)j
= breathing rate during time interval j (m3/sec) (Table 3)
(IQ)j
-= atmospheric dispersion factor during time interval j (sec/m 3) (Table 3)
Page 3/54
Westinghouse Proprietary Class 3 Offsite gamma doses from noble gases are calculated using the following equation:
where:
Dy
= gamma dose via cloud submersion (rem)
- DCF,
= gamma dose conversion factor via external exposure for isotope i (rem'm 3/Ci'sec) (Table 2)
(IAR)ýj = integrated activity of isotope i released during the time interval j (Ci)
(X/Q)j = atmospheric dispersion factor during time interval j (sec/m 3) (Table 3)
Offsite gamma doses from other isotopes are calculated using the following equation:
where:
Dy
= gamma dose via cloud submersion (rem)
- 1Fy,
-= gamma disintegration energy for isotope i (mev/dis) (Table 2)
(IAR),j = integrated activity of isotope i released during the time interval j (Ci)
(X/Q)j = atmospheric dispersion factor during time interval j (sec/m3) (Table 3) 1.3.2 Control Room Dose Calculation Models CEDE doses (due to inhalation) and gamma doses (due to external exposure) are calculated for 30 days in the control room.
The control room is modeled as a discrete volume. The atmospheric dispersion factors calculated for the transfer of activity to the control room intake are used to determine the activity available at the control room intake. The inflow (filtered and unfiltered) to the control room and filtered recirculation flow are used to calculate the concentration of activity in the control room.
Control room parameters used in the analyses are presented in Table 4.
Page 4/54
Westinghouse Proprietary Class 3 Control room inhalation doses are calculated using the following equation:
DCEDE =" 1:[DCF(XIConcJ * (BR)1JI where:
DCEDE = CEDE dose via inhalation (rem)
- DCF,
= CEDE dose conversion factor via inhalation for isotope i (renr/Ci) (Table 4)
Conc
-= integrated concentration in the control room of isotope i, during time interval j, calculated dependent upon inleakage, filtered inflow, filtered recirculation total outflow and CR volume (Ci-sec/m3)
(BR)j
= breathing rate during time interval j (m3/sec) (Table 4)
Control room external exposure doses due to noble gas activity in the control room volume are calculated using the following equation:
D, 1--)*
DCF{ YConcuJ where:
Dy
= gamma dose via cloud submersion (rem)
GF
= geometry factor, calculated based on Reference 11, using the equation:
GF = 1173, where V is the control room volume in ft3 vO338
- DCF,
= gamma dose conversion factor via external exposure for isotope i (remrm3/Ci'sec) (Table 2)
Conc11 = integrated concentration in the control room of isotope i, during time interval j, calculated dependent upon inleakage, filtered inflow, total outflow and CR volume (Ci-sec/m3)
Page 5154
Westinghouse Proprietary Class 3 Control room external exposure doses due to activity in the control room volume, other than noble gas activity, are calculated using the following equation:
Dr =0.25(A1)*jXri{IConc1 1J where:
Dy
= gamma dose via cloud submersion (rem)
GF
= geometry factor, calculated based on Reference 11, using the equation:
1173 GF = 1173",where V is the control room volume in ft3 IEy1
= gamma disintegration energy for isotope i (mev/dis) (Table 2)
Conc,, = integrated concentration in the control room of isotope i, during time interval j, calculated dependent upon inleakage, filtered inflow, filtered recirculation total outflow and CR volume (Ci-sec/m3)
Page 6/54
Westinghouse Proprietary Class 3 2.0 Large Break Loss of Coolant Accident Radiological Analysis An abrupt failure of the main reactor coolant pipe is assumed to occur and it is assumed that the emergency core cooling features fail to prevent the core from experiencing significant degradation (i.e., melting). This sequence cannot occur unless there are multiple failures, and thus goes beyond the typical design basis accident that considers a single active failure. Activity from the core is released to the containment and from there released to the environment by means of containment leakage and leakage from the emergency core cooling system.
2.1 Comparison of RG 1.183 Source Term Methodology to TID-14844 The reanalysis of the LBLOCA offsite and control room doses for KNPP uses the following RG 1.183 source term characteristics in place of those identified in TID-14844 and Regulatory Guide 1.4 (Reference 12):
Iodine chemical species Fission product release timing Fission product release phases through early in-vessel Fission product release fractions Fission product groups A comparison of RG 1.183 to TID-14844 is provided in Tables 8 through 11.
2.2 Input Parameters and Assumptions The input parameters and assumptions are listed in Table 12. Activity from the reactor coolant system and melted fuel is released into the containment. The analysis considers the release of activity from the containment via containment leakage. In addition, once recirculation of the emergency core cooling system (ECCS) is established, activity in the sump solution may be released to the environment by means of leakage from ECCS equipment outside containment in the Auxiliary Building. The total offsite and control room doses are the sum of the doses resulting from each of the postulated release paths.
The following sections address topics of significant interest.
2.2.1 Source Term The use of RG 1.183 source term modeling results in several major departures from the assumptions used in the existing LOCA dose analysis as reported in the UFSAR.
Instead of assuming instantaneous melting of the core and release of activity to the containment, the release of activity from the core occurs over a 1.8 hour9.259259e-5 days <br />0.00222 hours <br />1.322751e-5 weeks <br />3.044e-6 months <br /> interval.
Instead of considering only the release of iodines and noble gases, a wide spectrum of nuclides is taken into consideration. Table 11 lists the nuclides being considered for the LOCA with core melt (eight groups of nuclides). Tables 9 and 10 provide a comparison between the fission product release fractions and the timing/duration of releases to the containment as assumed in TID-14844 and in RG 1.183.
Page 7/54
Westinghouse Proprietary Class 3 0
Instead of the iodine being primarily in the elemental form, the iodine is mainly in the form of cesium iodide which exists as particulate and the fraction that is in the organic form is much smaller. The iodine characterization from RG 1.183 is compared in Table 8 with that from Regulatory Guide 1.4.
The other groups of nuclides (other than the iodines and the noble gases) all occur as particulates only.
For the containment leakage analysis, all activity released from the fuel is assumed to be in the containment atmosphere until removed by sprays, sedimentation, radioactive decay or leakage from the containment. For the ECCS leakage analysis, all iodine activity released from the fuel is assumed to be in the sump solution until removed by radioactive decay or leakage from the ECCS.
2.2.2 Containment Modeling The Containment System of the Kewaunee plant consists of three buildings: the Reactor Containment Vessel, the Shield Building and the Auxiliary Building. The containment and shield buildings are modeled as discrete volumes, which consider hold-up, removal and decay. Since no hold-up is modeled for the auxiliary building, a separate volume representing the auxiliary building is not included in the model.
The containment is assumed to leak at the design leak rate of 0.5% per day for the first 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> of the accident and then to leak at half that rate (0.25% per day) for the remainder of the 30 day period following the accident considered in the analysis.
During the first 10 minutes of the accident, it is assumed that 90 percent of the activity leaking from the containment is discharged directly to the environment and 10 percent enters the Auxiliary Building where it is released through filters. After 10 minutes, only 1.0 percent of the activity leaking from the containment is assumed to go directly to the environment, 10 percent continues to go to the Auxiliary Building, and 89 percent is assumed to pass into the Shield Building. The air discharged from the Shield Building is filtered to remove iodine. Additionally, once the Shield Building is brought to sub atmospheric pressure at 30 minutes into the event, the iodine is subject to removal by recirculation through filters. A shield building participation fraction of 0.5 is assumed.
2.2.3 Removal of Activity from the Containment Atmosphere The removal of elemental iodine from the containment atmosphere is accomplished only by containment sprays and radioactive decay. The removal of particulates from the containment atmosphere is accomplished by containment sprays, sedimentation and radioactive decay. The noble gases and the organic iodine are subject to removal only by radioactive decay.
One train of the containment spray system is assumed to operate following the LOCA.
Injection spray is credited with no startup delay. Earlier spray actuation is conservative since it results in earlier spray termination. There is no benefit from the earlier actuation since there is little activity in the containment at the time the sprays start. When the Page 8/54
Westinghouse Proprietary Class 3 RWST drains to a predetermined setpoint level, the operators switch to recirculation of sump liquid to provide a source for the sprays. Switchover to recirculation spray is not credited in the analysis and all spray is assumed to be terminated when the RWST drains down. The analysis conservatively assumed that the sprays are terminated 0.91 hours0.00105 days <br />0.0253 hours <br />1.50463e-4 weeks <br />3.46255e-5 months <br /> from the start of the event.
2.2.3.1 Containment Spray Removal of Elemental Iodine The current Standard Review Plan (Reference 9) identifies a methodology for the determination of spray removal of elemental iodine independent of the use of spray additive. The removal rate constant is determined by:
X, = 6KgTF / VD Where: Kg = Gas phase mass transfer coefficient, ft/min T = Time of fall of the spray drops, min F
= Volume flow rate of sprays, ft3/hr V = Containment sprayed volume, ft3 D = Mass-mean diameter of the spray drops, ft Parameters for KNPP are listed below:
Kg = 9.84 ft/min T = 13 sec F
= 1300 gpm V = 1.32 x 106 ft3 D = 0.124 cm These parameters and the appropriate conversion factors were used to calculate the elemental spray removal coefficients. The upper limit of 20 hri1 specified for this model is applied in the analysis in place of the calculated value of> 24 hr"1.
Removal of elemental iodine from the containment atmosphere is assumed to be terminated when the airborne inventory drops to 0.5 percent of the total elemental iodine released to the containment (this is a DF of 200). With the RG 1.183 source term methodology this is interpreted as being 0.5 percent of the total inventory of elemental iodine that is released to the containment atmosphere over the duration of gap and in vessel release phases. In the analysis, this does not occur before spray termination at 0.91 hours0.00105 days <br />0.0253 hours <br />1.50463e-4 weeks <br />3.46255e-5 months <br />.
2.2.3.2 Containment Spray Removal of Particulates Particulate spray removal is determined using the model described in Reference 9. The first order spray removal rate constant for particulates may be written as follows:
X = 3hFE / 2Vd Where: h
= Drop Fall Height F
= Spray Flow Rate V = Volume Sprayed Page 9/54
Westinghouse Proprietary Class 3 E
= Single Drop Collection Efficiency d
= Drop Diameter Parameters for KNPP are listed below:
H
= 150 ft F
= 1300 gpm V = 1.32x10 6 ft3 The E/d term depends upon the particle size distribution and spray drop size. From Reference 10 it is conservative to use 10 m"1 for E/d until the point is reached when the inventory in the atmosphere is reduced to 2% of its original (DF of 50). With the RG 1.183 source term methodology this is interpreted as being 2% of the total inventory particulate iodine that is released to the containment atmosphere over the duration of gap and in-vessel release phases.
These parameters and the appropriate conversion factors were used to calculate the particulate spray removal coefficients. A conservative value of 5.0 hr"' was used in the analysis. The airborne inventory does not drop to 2 percent of the total particulate iodine released to the containment (this is a DF of 50) before spray termination at 0.91 hours0.00105 days <br />0.0253 hours <br />1.50463e-4 weeks <br />3.46255e-5 months <br />.
2.2.3.3 Sedimentation Removal of Particulates During spray operation, no credit is taken for sedimentation removal of particulates, although it would take place. It is assumed that containment spray operation is terminated at 0.91 hours0.00105 days <br />0.0253 hours <br />1.50463e-4 weeks <br />3.46255e-5 months <br />. Recirculation sprays are not credited. Credit is taken for sedimentation removal of particulates after spray termination.
Based on the Containment Systems Experiments (CSE) which examined the air cleanup experienced through natural transport processes, it was found that a large fraction of the aerosols were deposited on the floor rather than on the walls indicating that sedimentation was the dominant removal process for the test (Reference 10). The CSE tests determined that there was a significant sedimentation removal rate even with a relatively low aerosol concentration. From Reference 10, even at an air concentration of 10 gIg/m 3, the sedimentation removal coefficient was above 0.3 h"1. With 2.0 percent of particulates remaining airborne at the end of credited spray removal, there would be more than 10,000 gig/m 3 and an even higher sedimentation rate would be expected.
(This conservatively assumes that the DF of 50 is reached, which is not the case as noted above.) For the analysis the sedimentation removal coefficient is conservatively assumed to be only 0.1 h-1. This value for sedimentation removal of particulates has been accepted by the NRC for Indian Point Unit 2 and Shearon Harris in their Safety Evaluation Reports for the application of the alternate source term methodology. It is also conservatively assumed that sedimentation removal does not continue beyond a DF of 1000.
2.2.4 ECCS Leakage When ECCS recirculation is established following the LOCA, leakage is assumed to occur from ECCS equipment outside containment. There are two pathways considered for the ECCS recirculation leakage. One is the leakage directly into the Auxiliary Page 10/54
Westinghouse Proprietary Class 3 Building and the other is back-leakage into the refueling water storage tank (RWST).
Although recirculation is not initiated until the RWST has drained to the pre-determined setpoint level (at about 0.91 hours0.00105 days <br />0.0253 hours <br />1.50463e-4 weeks <br />3.46255e-5 months <br />) the analysis conservatively considers leakage from the start of the event.
The leakage to the auxiliary building is 6 gallon/hr. In the licensing basis analysis of record 1% of the iodine contained in the leak flow becomes airborne. For this new analysis the airborne fraction is conservatively increased to 10% when the sump temperature is above 212*F. Once the sump solution temperature drops below 2120F, the airborne fraction is reduced to the analysis of record value of 1%. The reduction in airborne fraction is conservatively delayed until 1.5 hours5.787037e-5 days <br />0.00139 hours <br />8.267196e-6 weeks <br />1.9025e-6 months <br /> from the start of the event.
RHR back-leakage to the RWST is assumed at a rate of 3 gpm for the first 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> and 1.5 gpm for the remainder of the event. It is assumed that 1% of the iodine contained in the leak flow becomes airborne. The 1% value is applied even when the sump is above 212'F since any incoming water would be cooled by the water remaining in the RWST.
The RWST vents to the auxiliary building.
It is assumed that half the iodine activity that becomes airborne in the auxiliary building from the two leak sources is removed by plateout on surfaces. Releases from the auxiliary building are subject to filtration by the auxiliary building special ventilation system.
For the analysis, all iodine activity is assumed in elemental form. In the RG 1.183 source term methodology, the iodine is mainly in the form of particulate cesium iodide which would not become airborne. However, to bound a condition where the recirculation liquid was in a low pH environment and changed form, all of the leakage is assumed to be elemental.
2.2.5 Control Room Isolation In the event of a Large Break LOCA, the low pressurizer pressure SI setpoint will be reached shortly after event initiation. The SI signal causes the control room HVAC to switch from the normal operation mode to the accident mode of operation. It is conservatively assumed that the control room HVAC does not fully enter the accident mode of operation until 2 minutes after event initiation.
2.3 Acceptance Criteria The offsite dose limit for a LOCA is 25 rem TEDE per RG 1.183. This is the guideline value of 10CFR50.67. The limit for the control room dose is 5.0 rem TEDE per 10CFR50.67.
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Westinghouse Proprietary Class 3 2.4 Results and Conclusions The calculated doses due to the three release paths considered for the large-break LOCA are:
SB Dose LPZ Dose CR Dose (rem TEDE)
Containment Leakage 1.26E+O 2.21E-1 4.35E+O ECCS Leakage 1.44E-3 1.16E-3 2.79E-2 RWST Back-Leakage 4.33E-2 1.23E-2 5.66E-1 Total 1.305E+0 2.345E-1 4.944E+O The total large break LOCA doses are rounded up:
Site Boundary Low Population Zone Control Room 1.31 rem TEDE 0.24 rem TEDE 4.95 rem TEDE The acceptance criteria are met.
The Site Boundary dose reported is for the worst two hour period, determined to be from 1.8 hours9.259259e-5 days <br />0.00222 hours <br />1.322751e-5 weeks <br />3.044e-6 months <br /> to 3.8 hours9.259259e-5 days <br />0.00222 hours <br />1.322751e-5 weeks <br />3.044e-6 months <br />.
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Westinghouse Proprietary Class 3 3.0 Steam Generator Tube Rupture Radiological Analysis The steam generator tube rupture (SGTR) event is separated into two analyses, a thermal and hydraulic analysis and a radiological consequences analysis. The thermal hydraulic analysis is not impacted by the alternative source term methodology, so the results from the licensing basis analysis, summarized below, are used as input to the dose analysis.
3.1 Steam Generator Tube Rupture Thermal and Hydraulic Analysis Results The major hazard associated with an SGTR event is the radiological consequences resulting from the transfer of radioactive reactor coolant to the secondary side of the ruptured steam generator (SG) and subsequent release of radioactivity to the atmosphere.
The primary thermal-hydraulic parameters which affect the calculation of offsite doses for an SGTR include the amount of reactor coolant transferred to the secondary side of the ruptured steam generator, the amount of primary to secondary break flow that flashes to steam and the amount of steam released from the ruptured steam generator to the atmosphere.
Based on a primary and secondary side mass and energy balance, the break flow and atmospheric steam releases from the ruptured and intact steam generators were calculated for 30 minutes. After 30 minutes, it was assumed that steam is released only from the intact steam generator in order to dissipate the core decay heat and to subsequently cool the plant down to the RHR system operating conditions. For KNPP, it was assumed that plant cooldown to RHR operating conditions can be accomplished within 8 hours9.259259e-5 days <br />0.00222 hours <br />1.322751e-5 weeks <br />3.044e-6 months <br /> after initiation of the SGTR event and that steam release is terminated at this time. A primary and secondary side mass and energy balance was used to calculate the steam release from the intact steam generator from 0 to 2 hours2.314815e-5 days <br />5.555556e-4 hours <br />3.306878e-6 weeks <br />7.61e-7 months <br /> and from 2 to 8 hours9.259259e-5 days <br />0.00222 hours <br />1.322751e-5 weeks <br />3.044e-6 months <br />.
The limiting tube rupture break flow, break flow flashing fraction and ruptured steam generator atmospheric steam releases from 0 to 30 minutes are provided in Table 13 along with the long term intact steam generator steam releases for use in radiological consequences analysis. The values in Table 13 include an approximate 10% increase in mass flow rates for use in the conservative radiological analysis. Increasing the mass transfer data before performing the radiological consequences analysis allows future plant changes that result in small increases in the mass transfer rates to be evaluated without requiring the radiological analysis to be redone.
3.2 Steam Generator Tube Rupture Radiological Analysis For the SGTR, the complete severance of a single steam generator tube is assumed to occur. Due to the pressure differential between the primary and secondary systems, radioactive reactor coolant is discharged from the primary into the secondary system.
A portion of this radioactivity is released to the outside atmosphere through the main condenser, the atmospheric dump valves, or the safety valves (MSSVs). In addition, iodine activity is contained in the secondary coolant prior to the accident and some of this activity is released to the atmosphere as a result of steaming from the SGs following the accident.
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Westinghouse Proprietary Class 3 3.2.1 Input Parameters and Assumptions A summary of input parameters and assumptions is provided in Table 14.
The analysis of the SGTR radiological consequences uses the analytical methods and assumptions outlined in RG 1.183. For the pre-accident iodine spike case it is assumed that a reactor transient has occurred prior to the SGTR and has raised the RCS iodine concentration to the Technical Specification limit for a transient of 60 ptCi/gm of dose equivalent (DE) 1-131. For the accident-initiated iodine spike case, the reactor trip associated with the SGTR creates an iodine spike in the RCS which increases the iodine release rate from the fuel to the RCS to a value 335 times greater than the release rate corresponding to a maximum equilibrium RCS concentration of 1.0 jtCi/gm of DE 1-13 1.
For this analysis, the spike factor was conservatively increased from 335 to 500. The duration of the accident-initiated iodine spike is limited by the amount of activity available in the fuel-clad gap. Based on having 10 percent of the iodine in the fuel-clad gap, the gap inventory would be depleted within 4.0 hours0 days <br />0 hours <br />0 weeks <br />0 months <br /> and the spike is terminated at that time.
The noble gas activity concentration in the RCS at the time the accident occurs is based on a one percent fuel defect level. This is approximately equal to the Technical Specification value of 91/E bar.tCi/gm for gross radioactivity. The iodine activity concentration of the secondary coolant at the time the SGTR occurs is assumed to be equivalent to the Technical Specification limit of 0.1 JiCi/gm of DE 1-13 1.
The amount of primary to secondary SG tube leakage in the intact SG is assumed to be 500 gpd. This bounds the Technical Specification limit of 150 gpd.
An iodine partition factor in the SGs of 0.01 (curies iodine/gm steam) / (curies iodine/gm water) is used. Prior to reactor trip and concurrent loss of offsite power an iodine removal factor of 0.01 is taken for steam released to the condenser.
All noble gas activity carried over to the secondary side through SG tube leakage is assumed to be immediately released to the outside atmosphere.
Break flow flashing fractions and steam release rates from the intact and ruptured steam generator were calculated. The amount of break flow that flashes to steam is conservatively calculated assuming that all break flow is from the hot leg side of the break and that the primary temperatures remain constant.
At 8 hours9.259259e-5 days <br />0.00222 hours <br />1.322751e-5 weeks <br />3.044e-6 months <br /> after the accident, the RHR System is assumed to be placed into service for heat removal and there is no further steam release to the atmosphere from the secondary system.
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Westinghouse Proprietary Class 3 3.2.2 Control Room Isolation The low pressurizer pressure SI setpoint will be reached at -2.9 minutes from event initiation. The SI signal causes the control room HVAC to switch from the normal operation mode to the accident mode of operation. It is conservatively assumed that the control room HVAC does not fully enter the accident mode of operation until 5 minutes after event initiation.
3.3 Acceptance Criteria The offsite dose limit for a SGTR with a pre-accident iodine spike is 25 rem TEDE per RG 1.183. This is the guideline value of 10CFR50.67. For a SGTR with an accident initiated iodine spike, the offsite dose limit is 2.5 rem TEDE per RG 1.183. This is 10%
of the guideline value of 10CFR50.67. The limit for the control room dose is 5.0 rem TEDE per 10CFR50.67.
3.4 Results and Conclusions The SGTR accident doses are listed below.
For the pre-accident iodine spike:
Site Boundary 1.3 rem TEDE Low Population Zone 0.3 rem TEDE Control Room 3.0 rem TEDE For the accident-initiated iodine spike:
Site Boundary 0.8 rem TEDE Low Population Zone 0.2 rem TEDE Control Room 1.0 rem TEDE The acceptance criteria are met.
The Site Boundary doses reported are for the worst two hour period, determined to be from 0.0 to 2.0 hours0 days <br />0 hours <br />0 weeks <br />0 months <br />.
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Westinghouse Proprietary Class 3 4.0 Locked Rotor Radiological Analysis An instantaneous seizure of a reactor coolant pump rotor is assumed to occur which rapidly reduces flow through the affected reactor coolant loop. Fuel clad damage may be predicted to occur as a result of this accident. Due to the pressure differential between the primary and secondary systems and assumed steam generator tube leakage, fission products are discharged from the primary into the secondary system. A portion of this radioactivity is released to the outside atmosphere through either the atmospheric relief valves or safety valves. In addition, iodine activity is contained in the secondary coolant before the accident and some of this activity is released to atmosphere as a result of steaming from the steam generators following the accident.
4.1 Input Parameters and Assumptions A summary of input parameters and assumptions is provided in Table 15.
The analysis of the locked rotor radiological consequences uses the analytical methods and assumptions outlined in RG 1.183.
It is conservatively assumed that 100% of the fuel rods in the core suffer damage as a result of the locked rotor sufficient that all of their gap activity is released to the reactor coolant system. Eight percent of the total core activity of iodine, five percent of the total core activity for noble gases and 12 percent of the total core activity for alkali metals are assumed to be in the fuel-cladding gap and are released into the primary coolant.
It is assumed that a reactor transient has occurred prior to the locked rotor and has raised the RCS iodine concentration to the Technical Specification limit for a transient of 60 gCi/gm of dose equivalent (DE) 1-131. The noble gas and alkali metal activity concentration in the RCS at the time the accident occurs is based on a one percent fuel defect level. The iodine activity concentration of the secondary coolant at the time the locked rotor occurs is assumed to be equivalent to the Technical Specification limit of 0.1 gCi/gm of DE 1-131. The alkali metal activity concentration of the secondary coolant at the time the locked rotor occurs is assumed to be 10% of the primary side concentration.
The amount of primary to secondary SG tube leakage is assumed to be 500 gpd. This bounds the Technical Specification limit of 150 gpd/SG.
An iodine partition factor in the SGs of 0.01 (curies iodine/gm steam) / (curies iodine/gm water) is used. This partition factor is applied to alkali metals. Prior to reactor trip and concurrent loss of offsite power an iodine removal factor of 0.01 could be taken for steam released to the condenser, but this is conservatively ignored.
All noble gas activity carried over to the secondary side through SG tube leakage is assumed to be immediately released to the outside atmosphere.
For KNPP it was assumed that plant cooldown to RHR operating conditions can be accomplished within 8 hours9.259259e-5 days <br />0.00222 hours <br />1.322751e-5 weeks <br />3.044e-6 months <br /> after initiation of the locked rotor event. At 8 hours9.259259e-5 days <br />0.00222 hours <br />1.322751e-5 weeks <br />3.044e-6 months <br /> after the accident, the RHR System is assumed to be placed into service for heat removal and Page 16/54
Westinghouse Proprietary Class 3 there is no further steam release to the atmosphere from the secondary system.
A primary and secondary side mass and energy balance was used to calculate the steam released from the steam generators from 0 to 2 hours2.314815e-5 days <br />5.555556e-4 hours <br />3.306878e-6 weeks <br />7.61e-7 months <br /> and from 2 to 8 hours9.259259e-5 days <br />0.00222 hours <br />1.322751e-5 weeks <br />3.044e-6 months <br />. The calculated values were increased by 10% for input to the radiological analysis.
Increasing the mass transfer data before performing the radiological consequences analysis allows future plant changes that result in small increases in the mass transfer rates to be evaluated without requiring the radiological analysis to be redone.
4.1.1 Control Room Isolation It is assumed that the control room HVAC system begins in normal operation mode. The activity level in the air supply duct causes a high radiation signal almost immediately. It is conservatively assumed that the control room HVAC does not fully enter the accident mode of operation until 1 minute after event initiation.
4.2 Acceptance Criteria The offsite dose limit for a locked rotor is 2.5 rem TEDE per RG 1.183. This is 10% of the guideline value of 10CFR50.67. The limit for the control room dose is 5.0 rem TEDE per 10CFR50.67.
4.3 Results and Conclusions The locked rotor doses are:
Site Boundary 1.7 rem TEDE Low Population Zone 0.3 rem TEDE Control Room 4.3 rem TEDE The acceptance criteria are met.
The Site Boundary doses reported are for the worst two hour period, determined to be from 6.0 to 8.0 hours0 days <br />0 hours <br />0 weeks <br />0 months <br />.
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.4" Westinghouse Proprietary Class 3 5.0 Rod Ejection Radiological Analysis It is assumed that a mechanical failure of a control rod mechanism pressure housing has occurred, resulting in the ejection of a rod cluster control assembly and drive shaft. As a result of the accident, some fuel clad damage and a small amount of fuel melt are assumed to occur. Due to the pressure differential between the primary and secondary systems, radioactive reactor coolant is discharged from the primary into the secondary system. A portion of this radioactivity is released to the outside atmosphere through either the main condenser or the atmospheric relief valves for the main steam safety valves. Iodine and alkali metals group activity is contained in the secondary coolant prior to the accident, and some of this activity is released to the atmosphere as a result of steaming the steam generators following the accident. Finally, radioactive reactor coolant is discharged to the containment via the spill from the opening in the reactor vessel head. A portion of this radioactivity is released through containment leakage to the environment.
5.1 Input Parameters and Assumptions Separate calculations are performed to calculate the dose resulting from the release of activity to containment and subsequent leakage to the environment and the dose resulting from the leakage of activity to the secondary system and subsequent release to the environment. The total offsite and control room doses are the sum of the doses resulting from each of the postulated release paths and nuclides considered. A summary of input parameters and assumptions is provided in Table 16.
5.1.1 Source Term Less than 15% of the fuel rods in the core undergo DNB as a result of the rod ejection accident. In determining the offsite doses following rod ejection accident, it is conservatively assumed that 15% of the fuel rods in the core suffer sufficient damage that all of their gap activity is released. Ten percent of the total core activity of iodine and noble gases and 12 percent of the total core activity for alkali metals are assumed to be in the fuel-cladding gap. In the calculation of activity releases from the failed/melted fuel the maximum radial peaking factor of 1.7 was applied.
A small fraction of the fuel in the failed fuel rods is assumed to melt as a result of the rod ejection accident. It is assumed that 0.375% of the core melts. This is based on the assumption that 50% of the rods in DNB undergo centerline melting, with the melting limited to the inner 10% and occurring over 50% of the axial length of the affected rods.
For both the containment leakage release path and the primary to secondary leakage release path all noble gas and alkali metal activity released from the failed fuel (both gap activity and activity from melted fuel) is available for release.
For the containment leakage release path all of the iodine released from the gap of failed fuel and 25 percent of the activity released from melted fuel is available for release from containment.
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Westinghouse Proprietary Cliss 3 For the primary to secondary leakage release path all of the iodine released from the gap of failed fuel and 50 percent of the activity released from melted fuel is available for release from the reactor coolant system.
It is assumed that a reactor transient has occurred prior to the rod ejection rotor and has raised the RCS iodine concentration to the Technical Specification limit for a transient of 60 ItCi/gm of dose equivalent (DE) 1-131. The noble gas and alkali metal activity concentration in the RCS at the time the accident occurs is based on a one percent fuel defect level. The iodine activity concentration of the secondary coolant at the time the rod ejection occurs is assumed to be equivalent to the Technical Specification limit of 0.1 pCi/gm of DE 1-131. The alkali metal activity concentration of the secondary coolant at the time the rod ejection occurs is assumed to be 10% of the primary side concentration.
Iodine in containment is assumed to be 4.85% elemental, 0.15% organic and 95%
particulate.
Iodine released from the secondary system is assumed to be 97% elemental and 3%
organic.
5.1.2 Containment Release Pathway The Containment System of the Kewaunee plant consists of three buildings: the Reactor Containment Vessel, the Shield Building and the Auxiliary Building. The containment and shield buildings are modeled as discrete volumes, which consider hold-up, removal and decay. Since no removal or hold-up is modeled for the auxiliary building, a separate volume representing the auxiliary building is not included in the model.
The containment is assumed to leak at the design leak rate of 0.5% per day for the first 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> of the accident and then to leak at half that rate (0.25% per day) for the remainder of the 30 day period following the accident considered in the analysis.
During the first 10 minutes of the accident, it is assumed that 90 percent of the activity leaking from the containment is discharged directly to the environment and 10 percent enters the Auxiliary Building where it is released through filters. After 10 minutes, only 1.0 percent of the activity leaking from the containment is assumed to go directly to the environment, 10 percent continues to go to the Auxiliary Building, and 89 percent is assumed to pass into the Shield Building. The air discharged from the Shield Building is filtered to remove iodine. Additionally, once the Shield Building is brought to sub atmospheric pressure at 30 minutes into the event, the iodine is subject to removal by recirculation through filters. A shield building participation fraction of 0.5 is assumed.
For the containment leakage pathway, no credit is taken for sedimentation or plateout onto containment surfaces or for containment spray operation which would remove airborne particulates and elemental iodine.
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Westinghouse Proprietary Class 3 5.1.3 Primary to Secondary Leakage Release Pathway When determining doses due to the primary to secondary steam generator tube leakage, all the iodine, alkali metals group and noble gas activity (from prior to the accident and resulting from the accident) is assumed to be in the primary coolant (and not in the containment). The primary to secondary tube leakage and steaming from the steam generators continues until the reactor coolant system pressure drops below the secondary pressure. A bounding time of 30 minutes was selected for this analysis, although analyses of the small break LOCA pressure transient have shown that this would occur well before that time. A rod ejection pressure transient is similar to that of a small break LOCA.
The amount of primary to secondary SG tube leakage is assumed to be 500 gpd. This bounds the Technical Specification limit for of 150 gpd/SG. Although the primary to secondary pressure differential drops throughout the event, the constant flow rate is maintained.
An iodine partition factor in the SGs of 0.01 (curies iodine/gm steam) / (curies iodine/gm water) is used. This partition factor is applied to alkali metals. Prior to reactor trip and concurrent loss of offsite power an iodine removal factor of 0.01 could be taken for steam released to the condenser, but this is conservatively ignored.
All noble gas activity carried over to the secondary side through SG tube leakage is assumed to be immediately released to the outside atmosphere.
5.1.4 Control Room Isolation In the small break LOCA analysis, the low pressurizer pressure SI setpoint will be reached within 40 seconds from event initiation. The SI signal causes the control room HVAC to switch from the normal operation mode to the accident mode of operation. It is conservatively assumed that the control room HVAC does not fully enter the accident mode of operation until 2 minutes after event initiation.
5.2 Acceptance Criteria The offsite dose limit for a rod ejection is 6.3 rem TEDE per RG 1.183. This is -25% of the guideline value of 10CFR50.67. The limit for the control room dose is 5.0 rem TEDE per 10CFR50.67.
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I Westinghouse Proprietary Class 3 5.3 Results and Conclusions The rod ejection doses are:
Site Boundary 0.52 rem TEDE Low Population Zone 0.11 rem TEDE Control Room 1.90 rem TEDE The acceptance criteria are met.
The Site Boundary doses reported are for the worst two hour period, determined to be from 0.0 to 2.0 hours0 days <br />0 hours <br />0 weeks <br />0 months <br />.
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Westinghouse Proprietary Class 3 6.0 Fuel Handling Accident Radiological Analysis A fuel assembly is assumed to be dropped and damaged during refueling. Analysis of the accident is performed with assumptions selected so that the results are bounding for the accident occurring either inside containment or in the auxiliary building. Activity released from the damaged assembly is released to the outside atmosphere through either the containment purge system or the fuel pool ventilation system.
6.1 Input Parameters and Assumptions The major assumptions and parameters used in the analysis are itemized in Table 17. All activity released from the fuel pool is assumed to be released to the atmosphere in two hours, using an exponential release model with higher releases in the initial periods since this is conservative for the control room doses. No credit is taken for the spent fuel pool ventilation system operation in the Auxiliary Building. No credit is taken for isolation of containment for the FHA in containment. Since the assumptions and parameters for a FHA inside containment are identical to those for a FHA in the Auxiliary Building, the radiological consequences are the same regardless of the location of the accident.
6.1.1 Source Term The calculation of the radiological consequences following a fuel handling accident (FHA) uses gap fractions of 8% for 1-131, 10% for Kr-85, and 5% for all other nuclides.
As in the existing licensing basis, it is assumed that all of the fuel rods in the equivalent of one fuel assembly are damaged to the extent that all their gap activity is released. The assembly inventory is based on the assumption that the subject fuel assembly has been operated at 1.7 times the core average power.
The decay time used in the analysis is 100 hours0.00116 days <br />0.0278 hours <br />1.653439e-4 weeks <br />3.805e-5 months <br />. Thus, the analysis supports the Technical Specifications limit of 100 hours0.00116 days <br />0.0278 hours <br />1.653439e-4 weeks <br />3.805e-5 months <br /> decay time prior to fuel movement.
6.1.2 Fission Product Form Iodine species in the pool is 99.85% elemental and 0.15% organic. This is based on the split leaving the fuel of 95% cesium iodide (CsI), 4.85% elemental iodine and 0.15%
organic iodine. It assumed that all CsI is dissociated in the water and re-evolves as elemental. This is assumed to occur instantaneously. Thus, 99.85% of the iodine released is elemental.
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, Westinghouse Proprietary Class 3 6.1.3 Pool Scrubbing Removal of Activity Per the technical specifications, it is assumed that there is a minimum of 23 feet of water above the fuel. With this water depth, the overall pool decontamination factor (DF) for iodine is 200. The DF for organic iodine and noble gases is 1.0. [The elemental iodine scrubbing factor is conservatively set to provide the overall effective DF of 200 specified in RG 1.183. By back calculating, it is approximately 286. This is well below the value of 500 indicated in the RG and conservatively accounts for increased rod internal pressures above 1200 psig.]
The cesium released from the damaged fuel rods is assumed to remain in a nonvolatile form and would not be released from the pool.
The split between elemental and organic iodine leaving the pool has no impact on the analysis since the control room filter efficiencies are the same, and no other filtration is credited.
6.1.4 Isolation and Filtration of Release Paths No credit is taken for removal of iodine by filters nor is credit taken for isolation of release paths.
Although the containment purge will be automatically isolated on a purge line high radiation alarm, isolation is not modeled in the analysis. The activity released from the damaged assembly is assumed to be released to the outside atmosphere over a 2 hour2.314815e-5 days <br />5.555556e-4 hours <br />3.306878e-6 weeks <br />7.61e-7 months <br /> period. Since no filters or containment isolation is modeled, this analysis supports refueling operation with the equipment hatch or personnel air lock remaining open.
6.1.5 Control Room Isolation It is assumed that the control room HVAC system begins in normal operation mode. The activity level in the air supply duct causes a high radiation signal almost immediately. It is conservatively assumed that the control room HVAC does not fully enter the accident mode of operation until 1 minute after event initiation.
6.2 Acceptance Criteria The offsite dose limit for a fuel handling accident is 6.3 rem TEDE per RG 1.183. This is -25% of the guideline value of IOCFR50.67. The limit for the control room dose is 5.0 rem TEDE per 10CFR50.67.
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Westinghouse Propnetary Class 3 6.3 Results and Conclusions The fuel handling accident doses are:
Site Boundary 0.6 rem TEDE Low Population Zone 0.11 rem TEDE Control Room 1.0 rem TEDE The acceptance criteria are met.
The Site Boundary doses reported are for the worst two hour period, determined to be from 0.0 to 2.0 hours0 days <br />0 hours <br />0 weeks <br />0 months <br />.
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jr ji Westinghouse Proprietary Class 3 7.0 Steam Line Break Radiological Analysis The complete severance of a main steam line outside containment is assumed to occur.
The affected SG will rapidly depressurize and release radioiodines initially contained in the secondary coolant and primary coolant activity, transferred via SG tube leaks, directly to the outside atmosphere. A portion of the iodine activity initially contained in the intact SG and noble gas activity due to tube leakage is released to atmosphere through either the atmospheric dump valves (ADV) or the safety valves (MSSVs). The steam line break outside containment will bound any break inside containment since the outside break provides a means for direct release into the environment. This section describes the assumptions and analyses performed to determine the amount of radioactivity released and the offsite and control room doses resulting from this release.
7.1 Input Parameters and Assumptions The analysis of the steam line break (SLB) radiological consequences uses the analytical methods and assumptions outlined in the RG 1.183. A summary of input parameters and assumptions is provided in Table 18.
For the pre-accident iodine spike case it is assumed that a reactor transient has occurred prior to the SLB and has raised the RCS iodine concentration to the Technical Specification limit for a transient of 60 gCi/gm of dose equivalent (DE) 1-131. For the accident-initiated iodine spike case, the reactor trip associated with the SLB creates an iodine spike in the RCS which increases the iodine release rate from the fuel to the RCS to a value 500 times greater than the release rate corresponding to a maximum equilibrium RCS concentration of 1.0 gCi/gm of DE 1-131. The duration of the accident initiated iodine spike is limited by the amount of activity available in the fuel-clad gap.
Based on having 10 percent of the iodine in the fuel-clad gap, the gap inventory would be depleted within 4.0 hours0 days <br />0 hours <br />0 weeks <br />0 months <br /> and the spike is terminated at that time.
The noble gas activity concentration in the RCS at the time the accident occurs is based on a one percent fuel defect level. This is approximately equal to the Technical Specification value of 91/E bar giCi/grn for gross radioactivity. The iodine activity concentration of the secondary coolant at the time the SLB occurs is assumed to be equivalent to the Technical Specification limit of 0.1 tCi/gm of DE 1-131.
The amount of primary to secondary SG tube leakage is assumed to be 500 gpd. This bounds the Technical Specification limit for of 150 gpd/SG.
The SG connected to the broken steam line is assumed to boil dry within the initial two minutes following the SLB. The entire liquid inventory of this SG is assumed to be steamed off and all of the iodine initially in this SG is released to the environment. In addition, iodine carried over to the faulted SG by tube leaks is assumed to be released directly to the environment with no credit taken for iodine retention in the SG.
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Westinghouse Proprietary Class 3 An iodine partition factor in the intact SG of 0.01 (curies iodine/gm steam) / (curies iodine/gm water) is used. Prior to reactor trip and concurrent loss of offsite power an iodine removal factor of 0.01 could be taken for steam released to the condenser, but this is conservatively ignored.
All noble gas activity carried over to the secondary side through SG tube leakage is assumed to be immediately released to the outside atmosphere.
Eight hours after the accident, the RHR System is assumed to be placed into service for heat removal. After eight hours there are no further steam releases to the atmosphere from the intact steam generator. The calculated intact steam generator steam release values were increased by 10% for input to the radiological analysis. Increasing the mass transfer data before performing the radiological consequences analysis allows future plant changes that result in small increases in the mass transfer rates to be evaluated without requiring the radiological analysis to be redone.
Within 72 hours8.333333e-4 days <br />0.02 hours <br />1.190476e-4 weeks <br />2.7396e-5 months <br /> after the accident, the reactor coolant system has been cooled to below 212'F, and there are no further steam releases to atmosphere from the faulted steam generator.
7.1.1 Control Room Isolation In the event of a SLB, the steamline pressure SI setpoint will be reached shortly after event initiation. The SI signal causes the control room HVAC to switch from the normal operation mode to the accident mode of operation. It is conservatively assumed that the control room HVAC does not fully enter the accident mode of operation until 5 minutes after event initiation.
7.2 Acceptance Criteria The offsite dose limit for a SLB with a pre-accident iodine spike is 25 rem TEDE per RG 1.183. This is the guideline value of 10CFR50.67. For a SLB with an accident initiated iodine spike, the offsite dose limit is 2.5 rem TEDE per RG 1.183. This is 10%
of the guideline value of 10CFR50.67. The limit for the control room dose is 5.0 rem TEDE per 10CFR50.67.
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Westinghouse Proprietary Class 3 7.3 Results and Conclusions The SLB accident doses are listed below.
For the pre-accident iodine spike:
Site Boundary 0.05 rem TEDE Low Population Zone 0.02 rem TEDE Control Room 0.7 rem TEDE For the accident-initiated iodine spike:
Site Boundary 0.2 rem TEDE Low Population Zone 0.05 rem TEDE Control Room 2.3 rem TEDE The acceptance criteria are met.
The Site Boundary doses reported are for the worst two hour period, determined to be from 0.0 to 2.0 hours0 days <br />0 hours <br />0 weeks <br />0 months <br /> for the pre-accident iodine spike and from 4.0 to 6.0 hours0 days <br />0 hours <br />0 weeks <br />0 months <br /> for the accident initiated iodine spike.
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Westinghouse Proprietary Class 3 8.0 Gas Decay Tank Rupture and Volume Control Tank Rupture Radiological Analyses For the gas decay tank rupture, a failure is assumed that results in the release of the contents of one gas decay tank. For the volume control tank rupture, a failure is assumed that results in the release of the contents of the tank plus the noble gases and a fraction of the iodines from the letdown flow until the letdown path is isolated.
8.1 Input Parameters and Assumptions The major assumptions and parameters used to determine the doses due to the gas decay tank failure and the volume control tank failure are given in Table 19.
The control room HVAC is modeled as being initially in the normal operating mode.
Actuation of the accident mode of operation would be initiated by high radiation detected in the air supply duct. The HVAC would be in the accident mode within 30 seconds of accident initiation.
8.1.1 Gas Decay Tank Rupture The inventory of gases in the tank are based on operation of the plant with 1.0 percent fuel defects and with no purge of activity from the volume control tank to the gas decay tank during the cycle. This is followed by shutdown of the plant and degassing of the primary coolant to the tank. A failure in the gaseous waste processing system is assumed to result in release of the tank inventory with a release duration of five minutes.
8.1.2 Volume Control Tank Rupture The inventory of gases in the tank is based on continuous operation with 1.0 percent fuel defects and without any purge of the gas space. The inventory of iodine in the tank is based on operation of the plant with 1.0 percent fuel defects and with 90 percent of the iodine removed by the letdown demineralizer.
As a result of the accident, all of the noble gas in the tank and 1.0 percent of the iodine in the tank liquid is assumed to be released to the atmosphere over a period of 5 minutes.
After event initiation, letdown flow to the volume control tank continues at the maximum flow rate of 88 gpm (maximum letdown flow plus 10-percent uncertainty) for 5 minutes when the letdown line is assumed to be isolated. The primary coolant noble gas activities used in the volume control tank rupture dose calculations are based on operation with 1.0 percent fuel defects. The primary coolant iodine activity is conservatively assumed to be at the pre-existing iodine spike level of 60 gCi/gram dose equivalent 1-131, which is reduced by 90 percent by the letdown demineralizer. All of the noble gas and 1.0 percent of the iodine in the letdown flow are assumed to be released to the environment.
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Westinghouse Proprietary Class 3 1 +
8.1.3 Control Room Isolation It is assumed that the control room HVAC system begins in normal operation mode. The activity level in the air supply duct causes a high radiation signal almost immediately, for both postulated tank ruptures. It is conservatively assumed that the control room HVAC does not fully enter the accident mode of operation until 30 seconds after event initiation.
8.2 Acceptance Criteria The offsite dose limits for a gas decay tank rupture or a volume control tank rupture are assumed to be the same as those for the fuel handling accident. That is 6.3 rem TEDE per RG 1.183. This is -25% of the guideline value of 10CFR50.67. The limit for the control room dose is 5.0 rem TEDE per 10CFR50.67.
8.3 Results and Conclusions The gas decay tank rupture doses are:
Site Boundary 0.1 rem TEDE Low Population Zone 0.02 rem TEDE Control Room 0.1 rem TEDE The acceptance criteria are met.
The volume control tank rupture doses are:
Site Boundary 0.1 rem TEDE Low Population Zone 0.01 rem TEDE Control Room 0.05 rem TEDE The acceptance criteria are met.
The Site Boundary doses reported are for the worst two hour period, determined to be from 0.0 to 2.0 hours0 days <br />0 hours <br />0 weeks <br />0 months <br />.
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Westinghouse Proprietary Class 3 9.0 Conclusions NUREG-1465 defines an alternate source term model for use in evaluating the radiological consequences of a postulated large break Loss-of-Coolant Accident with core melt. This alternative source term model also forms the basis for determining the radiological consequences for other design basis accidents as provided in Regulatory Guide 1.183.
Implementation of this alternative source term methodology on the Kewaunee Nuclear Power Plant's design basis accidents has been made to support potential changes in the plant design and operation. Analyses of the radiological consequences of the large break LOCA, steam generator tube rupture, locked rotor, rod ejection, fuel handling accident, steamline break, and gas decay tank and volume control tank ruptures have been made using the Regulatory Guide 1.183 methodology. The analyses used assumptions consistent with proposed changes in plant design and operation and the calculated doses do not exceed the defined acceptance criteria.
This report supports the following changes to Kewaunee Nuclear Power Plant's design and operation:
"* Movement of fuel in the containment with the equipment hatch and/or personnel air lock open.
"* Removal of the requirement for recirculation sprays in containment following a large break LOCA, for radiological concerns.
Relaxation of the time requirements for establishing recirculation in the shield building following a large break LOCA or rod ejection accident.
"* Relaxation of the Technical Specification limits for primary coolant iodine activity.
"* Removal of limitation on calculated rods-in-DNB for a locked rotor.
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Westinghouse Proprietary Class 3 10.0 References
- 1. TID-14844, "Calculation of Distance Factors for Power and Test Reactor Sites," U.S. AEC, Division of Licensing and Regulation, J. J. DiNunno, et. al, March 23, 1962.
- 2. Regulatory Guide 1.183, "Alternative Radiological Source Terms for Evaluating Design Basis Accidents at Nuclear Power Reactors", July 2000.
- 3. NRC Final Ruleo1OCFR50.67, issued in Federal Register, Vol. 64, No. 246, pages 71990 72002, 12/23/99.
- 4. U.S. Nuclear Regulatory Commission NUREG-1465, "Accident Source Terms for Light Water Nuclear Power Plants," February 1995.
- 5. EPA Federal Guidance Report No. 11, "Limiting Values of Radionuclide Intake and Air Concentration and Dose Conversion Factors for Inhalation, Submersion, and Ingestion,"
EPA-520/1-88-0202, September 1988.
- 6. SAE-CRA-98-104, "Revision 1 to the TITAN5 User's Guide," 4/9/98.
- 7. International Commission on Radiological Protection, "Radionuclide Transformations, Energy and Intensity of Emissions," ICRP Publication 38, 1983.
- 8. International Commission on Radiological Protection, "Limits for Intakes of Radionuclides by Workers," ICRP Publication 30, 1979.
- 9. NUREG-0800, Standard Review Plan 6.5.2, "Containment Spray as a Fission Product Cleanup System," Revision 2, December 1988.
- 10. Industry Degraded Core Rulemaking (IDCOR) Program Technical Report 11.3, "Fission Product Transport in Degraded Core Accidents," Atomic Industrial Forum, December 1983
- 11. Murphy, K. G., Campe, K. M., "Nuclear Power Plant Control Room Ventilation System Design for Meeting General Criterion 19," Proceedings of the Thirteenth AEC Air Cleaning Conference held August 1974, published March 1975.
- 12. Regulatory Guide 1.4, "Assumptions Used For Evaluating the Potential Radiological Consequences of a Loss of Coolant Accident," (Rev. 2, June 1974).
Page 31/54
Westinghouse Proprietary Class 3 Table 1: Committed Effective Dose Equivalent Dose Conversion Factors Isotope DCF (rem/curie)
Isotope DCF (rem/curie) 1-131 3.29E4 Cs-134 4.62E4 1-132 3.81E2 Cs-136 7.33E3 1-133 5.85E3 Cs-137 3.19E4 1-134 1.31E2 Rb-86 6.63E3 1-135 1.23E3 Ru-103 8.95E3 Kr-85m N/A Ru-105 4.55E2 Kr-85 N/A Ru-106 4.77E5 Kr-87 N/A Rh-105 9.56E2 Kr-88 N/A Mo-99 3.96E3 Xe-131m N/A Tc-99m 3.3EI Xe-133m N/A Xe-133 N/A Y-90 8.44E3 Xe-135m N/A Y-91 4.89E4 Xe-135 N/A Y-92 7.80E2 Xe-138 N/A Y-93 2.15E3 Nb-95 5.81E3 Te-127 3.18E2 Zr-95 2.37E4 Te-127m 2.15E4 Zr-97 4.33E3 Te-129m 2.39E4 La-140 4.85E3 Te-129 9.OE1 La-141 5.81E2 Te-131m 6.4E3 La-142 2.53E2 Te-132 9.44E3 Nd-147 6.85E3 Sb-127 6.04E3 Pr-143 1.09E4 Sb-129 6.44E2 Am-241 4.44E8 Cm-242 1.73E7 Ce-141 8.96E3 Cm-244 2.48E8 Ce-143 3.39E3 Ce-144 3.74E5 Sr-89 4.14E4 Pu-238 3.92E8 Sr-90 1.3E6 Pu-239 4.3E8 Sr-91 1.66E3 Pu-240 4.3E8 Sr-92 8.1E2 Pu-241 8.26E6 Ba-139 1.7E2 Np-239 2.5 1E3 Ba-140 3.74E3 Page 32/54
Westinghouse Proprietary Class 3 Table 2: Average Gamma Disintegration Energies and Noble Gas Dose Conversion Factors Energy (mev/dis)
Isotope Energy (mev/dis) 0.38 2.2 0.6 2.6 1.4 4.86E-3 0.0112 0.0375 0.0591 1.42 0.233 0.688 1.44 0.076 0.282 0.021 1.81E-3 8.08E-4 1.73E-3 2.54E-6 0.172 1.55 2.16 0.564 0.0945 DCF (rem m3 /Ci. sec'
0.0307 0.000484 0.146 0.37 0.00152 1-131 1-132 1-133 1-134 1-135 Xe-133m Xe-133 Xe-135m Xe-135 Xe-138 0.468 0.775 0.0 0.078 0.15 0.126 1.7E-6 3.61E-3 0.251 0.0889 0.766 0.739 0.179 2.31 0.0427 2.68 0.14 8.9E-9 0.0324 1.83E-3 1.7E-3 8.45E-5 0.0 0.693 1.34 0.043 0.182 Ru-103 Ru-105 Ru-106 Rh-105 Mo-99 Tc-99m Y-90 Y-91 Y-92 Y-93 Nb-95 Zr-95 Zr-97 La-140 La-141 La-142 Nd-147 Pr-143 Am-241 Cm-242 Cm-244 Sr-89 Sr-90 Sr-91 Sr-92 Ba-139 Ba-140 Isotope 0.00553 0.00624 0.0775 0.0482 0.198 Page 33/54 Isotope DCF (rem. m3 /Ci - sec)
Te-127 Te-127m Te-129m Te-129 Te-131m Te-132 Sb-127 Sb-129 Ce-141 Ce-143 Ce-144 Pu-238 Pu-239 Pu-240 Pu-241 Np-239 Cs-134 Cs-136 Cs-137 Rb-86 Isotope Kr-85m Kr-85 Kr-87 Kr-88 Xe-131m Isotone DCF (rem-m3 /Ci - sec)
Westinghouse Proprietary Class 3 Table 3: Offsite Breathing Rates and Atmospheric Dispersion Factors Offsite Breathing Rates (m3/sec) 0 - 8 hours9.259259e-5 days <br />0.00222 hours <br />1.322751e-5 weeks <br />3.044e-6 months <br /> 3.47E-4 8 - 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> 1.75E-4
>24 hours 2.32E-4 Offsite Atmospheric Dispersion Factors (sec/m 3)
Site Boundary*
2.232E-4 Low Population Zone 0 - 2 hours2.314815e-5 days <br />5.555556e-4 hours <br />3.306878e-6 weeks <br />7.61e-7 months <br /> 3.977E-5 2 - 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> 4.100E-6 1 - 2 days 2.427E-6
> 2 days 4.473E-7 This site boundary atmospheric dispersion factor is conservatively applied during all time intervals in the determination of the limiting two hour period.
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Westinghouse Proprietary Class 3 Table 4: Control Room Parameters Volume (ft3) 127,600 Normal Ventilation Flow Rates (cfm)
Filtered Makeup Flow Rate Filtered Recirculation Flow Rate Unfiltered Makeup Flow Rate Unfiltered Recirculation Flow Rate Emergency Ventilation System Flow Rates (cfm)
Filtered Makeup Air Flow Rate Filtered Recirculation Flow Rate Unfiltered Inleakage Unfiltered Recirculation Flow Rate Filter Efficiencies (%)
Elemental Organic Particulate R-23 Sensitivity (cpm/4iCi/cc for Xe-l 33)
Setpoint for Control room isolation (cpm)
Location of R-23 Delay to Initiate Switchover of HVAC after S-signal Delay to Complete Switchover of HVAC Breathing Rate - Duration of the Event (m3/sec)
Atmospheric Dispersion Factors (sec/m3) 0 - 8 hours9.259259e-5 days <br />0.00222 hours <br />1.322751e-5 weeks <br />3.044e-6 months <br /> 8 - 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> 1 -4 days 4 - 30 days Occupancy Factors*
0 - 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> 1 - 4 days 4 - 30 days 0.0 0.0 2500 (+/-10%)
(Not modeled - no impact on analyses) 0.0 2500 (+/-10%)
200 (Not modeled - no impact on analyses) 90 90 99 2.32E7 1.0E4 R-23 is located at a junction of the intake and the recirculation ducts such that it monitors the mixed air stream.
63 seconds
< 10 seconds 3.47E-4 2.93E-3 1.73E-3 6.74E-4 1.93E-4 1.0 0.6 0.4 These occupancy factors (from Reference 11) have been conservatively incorporated in the atmospheric dispersion factors. This is conservative since it does not allow the benefit of reduced occupancy for activity already present in the control room from earlier periods.
Page 35/54
Westinghouse Proprietary Class 3 Table 5: Core Total Fission Product Activities Based on 102% of 1650 MWt Activitv (Ci) 1-131 1-132 1-133 1-134 1-135 Kr-85m Kr-85 Kr-87 Kr-88 Xe-131m Xe-133m Xe-133 Xe-135m Xe-135 Xe-138 Te-127 Te-127m Te-129m Te-129 Te-131m Te-132 Sb-127 Sb-129 Ce-141 Ce-143 Ce-144 Pu-238 Pu-239 Pu-240 Pu-241 Np-239 Isotope 4.48E7 6.49E7 9.22E7 1.02E8 8.62E7 1.24E7 5.84E5 2.38E7 3.36E7 5.00E5 2.87E6 9.03E7 1.79E7 2.51E7 7.68E7 4.60E6 6.07E5 2.07E6 1.39E7 6.42E6 6.39E7 4.65E6 1.41E7 7.61E7 7.07E7 5.99E7 1.67E5 1.65E4 2.38E4 6.37E6 8.22E8 Activity (Ci)
Cs-134 Cs-136 Cs-137 Rb-86 Ru-103 Ru-105 Ru-106 Rh-105 Mo-99 Tc-99m Y-90 Y-91 Y-92 Y-93 Nb-95 Zr-95 Zr-97 La-140 La-141 La-142 Nd-147 Pr-143 Am-241 Cm-242 Cm-244 Sr-89 Sr-90 Sr-91 Sr-92 Ba-139 Ba-140 Page 36/54 Isotooe 9.54E6 2.49E6 6.26E6 9.66E4 6.73E7 4.48E7 2.36E7 4.19E7 8.26E7 7.23E7 4.86E6 5.82E7 6.08E7 6.98E7 7.77E7 7.72E7 7.63E7 8.34E7 7.56E7 7.33E7 3.03E7 6.89E7 8.03E3 2.20E6 1.58E5 4.54E7 4.68E6 5.63E7 6.05E7 8.29E7 8.00E7 IsotoDe
Westinghouse Proprietary Class 3 Table 6: RCS Coolant Concentrations Based on 1.0 giCi/gm DE 1-131 for Iodines and 1% Fuel Defects for Noble Gases and Alkali Metals Isotope 1-131 1-132 1-133 1-134 1-135 Kr-85m Kr-85 Kr-87 Kr-88 Xe-131m Xe-133m Xe-133 Xe-135m Xe-135 Xe-138 Cs-134 Cs-136 Cs-137 Rb-86 Activity (piCi/gm) 0.782 0.717 1.153 0.161 0.640 1.64 7.51 1.07 3.09 2.52 3.96 215.0 0.469 7.82 0.607 2.26 2.59 1.91 0.0232 Iodine concentrations are converted to dose equivalent (DE) 1-131 using the dose conversion factors in ICRP-30 (Reference 8) for direct thyroid doses.
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Westinghouse Proprietary Class 3 Table 7: Nuclide Decay Constants Decay Constant (hr"i) 1-131 1-132 1-133 1-134 1-135 Isotove 0.00359 0.303 0.0333 0.791 0.105 0.155 7.37E-6 0.547 0.248 0.00241 0.0130 0.00546 2.72 0.0756 2.93 7.41E-2 2.65E-4 8.6E-4 0.598 2.3 1E-2 8.86E-3 7.5E-3 0.16 8.89E-4 0.021 1.02E-4 9.02E-7 3.29E-9 1.21E-8 5.5E-6 0.0123 Decay Constant (hfr1)
Cs-134 Cs-136 Cs-137 Rb-86 Ru-103 Ru-105 Ru-106 Rh-105 Mo-99 Tc-99m Y-90 Y-91 Y-92 Y-93 Nb-95 Zr-95 Zr-97 La-140 La-141 La-142 Nd-147 Pr-143 Am-241 Cm-242 Cm-244 Sr-89 Sr-90 Sr-91 Sr-92 Ba-139 Ba-140 Page 38/54 Thntone 3.84E-5 2.2E-3 2.64E-6 1.55E-3 7.35E-4 0.156 7.84E-5 1.96E-2 1.05E-2 0.115 1.08E-2 4.94E-4 0.196 0.0686 8.22E-4 4.5 1E-4 4.1E-2 1.72E-2 0.176 0.45 2.63E-3 2.13E-3 1.83E-7 1.77E-4 4.37E-6 5.72E-4 2.72E-6 0.073 0.256
, 0.502 2.27E-3 Kr-85m Kr-85 Kr-87 Kr-88 Xe-131m Xe-133m Xe-133 Xe-135m Xe-135 Xe-138 Te-127 Te-127m Te-129m Te-129 Te-131m Te-132 Sb-127 Sb-129 Ce-141 Ce-143 Ce-144 Pu-238 Pu-239 Pu-240 Pu-241 Np-239 Is tp Co stn
- 1) tlr
Westinghouse Proprietary Class 3 Table 8: Iodine Chemical Species Iodine Form RG 1.4 RG 1.183 Elemental 91%
4.85%
Organic 4%
0.15%
Particulate 5%
95%
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Westinghouse Proprietary Class 3 Table 9: Fission Product Release Timing Release Phase Gap Activity Early In-vessel Duration (TID-14844) instantaneous release instantaneous release Duration (RG 1.183)(1) 0.5 hour5.787037e-5 days <br />0.00139 hours <br />8.267196e-6 weeks <br />1.9025e-6 months <br /> 1.3 hour3.472222e-5 days <br />8.333333e-4 hours <br />4.960317e-6 weeks <br />1.1415e-6 months <br />
- 1. Releases are sequential.
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Westinghouse Proprietary Class 3 Table 10: Core Fission Product Release Fractions Noble gases Halogens Alkali Metals Tellurium group Barium, Strontium Noble Metals (Ruthenium group)
Cerium group Lanthanides Gap Release (1)
TID-14844 RG 1.183 n/a(2) 0.05 n/a(2) 0.05 n/a 0.05 n/a 0
n/a n/a n/a n/a 0
0 0
0 Early In-Vessel TID-14844 RG 1.183 1.0 0.95 0.5 (3) 0.35 0.01(4) 0.25 0.01(4) 0.05 0.01(4) 0.02 0.01(4) 0.0025 0.01(4) 0.0005 0.01(4) 0.0002 (1) The TID-14844 methodology does not specifically address the gap release. The RG 1.183 methodology assumes that gap and early in-vessel (core melt) releases are sequential. The TID-14844 source term model assumes the instantaneous release of 50% of core iodine and noble gases, with no distinction made between gap activity release and early in-vessel release. The RG 1.183 source term assumes a release of gap activity (5% of core) followed by 35% in-vessel release for a total release of 40% of core.
(2) Gap fraction is not defined by TID-14844.
(3) Per TID-14844, half of this is assumed to plate out instantaneously.
(4) Referred to in TID-14844 as "other fission products" but not typically included in dose analyses.
Page 41/54
Westinghouse Proprietary Class 3 Table 11: RG 1.183 Nuclide Groups Title Noble Gases Halogens Alkali Metals Tellurium Group Barium, Strontium Noble Metals Lanthanides Cerium Group Elements in Group Xe, Kr I, Br Cs, Rb Te, Sb, Se Ba, Sr Ru, Rh, Pd, Mo, Tc, Co La, Zr, Nd, Eu, Nb, Pm, Pr, Sm, Y, Cm, Am Ce, Pu, Np Page 42/54 Group 1
2 3
4 5
6 7
8
Westinghouse Proprietary Class 3 Table 12: Assumptions Used for Large Break LOCA Dose Analysis Source Term Core Activity Activity release fractions and timing Iodine chemical form in containment (%)
Elemental Organic Particulate (cesium iodide)
Iodine chemical form in sump & recirculating liquid (%)
Elemental Organic Particulate (cesium iodide)
See Table 5 See Tables 9 & 10 4.85 0.15 95 97 3
0 Containment 1.32E6 3.74E5 0.5 Not Modeled, No holdup Credited Containment net free volume (ft3)
Shield building volume (fA3)
Shield building participation fraction Auxiliary building volume Containment leak rates (weight %/day) 0 - 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br />
> 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> Containment Leak Path Fractions 0-10 minutes Through Shield Building Through Auxiliary Building SV Direct to Environment 10 minutes - 30 days Through Shield Building Through Auxiliary Building SV Direct to Environment Shield Building Air Flows (cfm) 0-10 minutes Shield Building to Environment Shield Building Recirculation 10 minutes - 30 minutes Shield Building to Environment Shield Building Recirculation
> 30 minutes Shield Building to Environment Shield Building Recirculation 0.5 0.25 0.0 0.1 0.9 0.89 0.10 0.01 Not applicable Not applicable 6000+/-10%
0.0 3100 2300 Page 43/54
Westinghouse Proprietary Class 3 Table 12 Assumptions Used for Large Break LOCA Dose Analysis (continued)
Spray Operation Time to initiate sprays 0.0 seconds Time to terminate injection spray operation 0.91 hours0.00105 days <br />0.0253 hours <br />1.50463e-4 weeks <br />3.46255e-5 months <br /> Time to establish recirculation spray Not credited Spray flow rates (gpm) 1300 Spray fall height (ft) 150 Removal Coefficients (hrf )
Injection spray elemental iodine removal 20.0 Injection spray particulate removal 5.0 Sedimentation particulate removal (after spray termination) 0.1 Credited sump volume (gal) 315000 ECCS leak rate to auxiliary building (gph) 6 Airborne fraction for ECCS leakage to auxiliary building (%)
0- 1.5 hours5.787037e-5 days <br />0.00139 hours <br />8.267196e-6 weeks <br />1.9025e-6 months <br /> 10.0
> 1.5 hours5.787037e-5 days <br />0.00139 hours <br />8.267196e-6 weeks <br />1.9025e-6 months <br /> 1.0 ECCS leak rate to RWST (gpm) 0 - 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> 3.0
> 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> 1.5 Airborne fraction for ECCS leakage to RWST (%)
1.0 ECCS leakage plateout in auxiliary building (%)
50 Shield building and auxiliary building filter efficiencies (%)
Elemental 90 Organic 90 Particulate 99 Time to start crediting emergency control room HVAC (min) 2 Page 44/54
. I
Westinghouse Proprietary Class 3 Table 13: Bounding Steam Generator Tube Rupture Thermal Hydraulic Results For Radiological Consequences Analysis Reactor Trip Time (see) 173.7 Loss of offsite power At reactc Tube rupture break flow (Ibm)
Pre-Trip 16,800 Post-Trip (until 30 minutes) 138,000 Tube rupture break flow flashing fraction (%)
Pre-Trip 19.71 Post-Trip (until 30 minutes) 14.76 Steam Released to Environment Ruptured SG Pre-Trip (Ibm/sec) 991.7 Post-Trip (until 30 minutes) (Ibm) 85,000 Intact SG Pre-Trip (Ibm/see) 991.7 0 - 2 Hour (Ibm) 243,800 2 - 8 Hour (Ibm) 506,600 r trip Page 45/54
Westinghouse Propnetary Class 3 Table 14: Assumptions Used for Steam Generator Tube Rupture Dose Analysis Source Term Coolant Activity Reactor coolant noble gas activity prior to accident (% fuel defect level)
Reactor coolant iodine activity prior to accident (gCi/gm of DE 1-13 1)
Pre-accident iodine spike Accident-initiated iodine spike (QCi/gm of DE 1-131)
Reactor coolant iodine appearance rate increase due to the accident-initiated spike (times equilibrium rate)
Duration of accident-initiated iodine spike (hr)
Release Modeling Intact SG tube leak rate (gpd)
Thermal & hydraulic data SG iodine water/steam partition coefficient Time to start crediting emergency control room HVAC (min)
See Table 6 1.0 60 1.0 500 4.0 500 See Table 13 0.01 5
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Westinghouse Proprietary Class 3 Table 15: Assumptions Used for Locked Rotor Dose Analysis Source Term Core Activity See Table 5 Fraction of fuel rods in core assumed to fail for dose considerations (% of core) 100 Gap Fractions (% of core activity) 1-131 8
Kr-85 10 Other Iodine and Noble Gas nuclides 5
Alkali Metals 12 Iodine chemical form in after release to atmosphere (%)
Elemental 97 Organic 3
Particulate (cesium iodide) 0 Reactor coolant noble gas and alkali metal activity prior to accident (% fuel defect level) 1.0 Reactor coolant iodine activity prior to accident (giCi/gm of DE 1-131) 60 Secondary coolant iodine activity prior to accident (ptCi/gm of DE 1-13 1) 0.1 Secondary coolant alkali metal activity prior to accident (% of primary concentration) 10 Release Modeling SG tube leak rate (gpdISG) 500 Steam release to environment (Ibm) 0 - 2 Hours 213,000 +10%
2 - 8 hours9.259259e-5 days <br />0.00222 hours <br />1.322751e-5 weeks <br />3.044e-6 months <br /> 418,000 +10%
SG iodine and alkali metal water/steam partition coefficient 0.01 Time to start crediting emergency control room HVAC (min) 1 Page 47/54
Westinghouse Proprietary Class 3 Table 16: Assumptions Used for Rod Ejection Dose Analysis Source Term Core Activity See Table 5 Fraction of fuel rods in core that fail (% of core) 15 Gap Fractions (% of core activity)
Iodine 10 Noble Gas 10 Alkali Metals 12 Fraction of fuel melting (% of core) 0.375 Radial peaking factor 1.7 Fraction of activity released from melted fuel (%)
Containment leakage Iodine 25 Noble Gas 100 Alkali Metals 100 Primary to secondary leakage Iodine 50 Noble Gas 100 Alkali Metals 100 Reactor coolant noble gas and alkali metal activity prior to accident (% fuel defect level) 1.0 Reactor coolant iodine activity prior to accident (gtCi/gm of DE 1-13 1) 60 Secondary coolant iodine activity prior to accident (ptCi/gm of DE 1-13 1) 0.1 Secondary coolant alkali metal activity prior to accident (% of primary concentration) 10 Page 48/54
Westinghouse Proprietary Class 3 Table 16 Assumptions Used for Rod Ejection Dose Analysis (continued)
Containment Leakage Release Path Containment net free volume (ft3)
Shield building volume (ft3)
Shield building participation fraction Auxiliary building volume Containment leak rates (weight %/day) 0 - 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br />
> 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> Containment Leak Path Fractions 0-10 minutes Through Shield Building Through Auxiliary Building SV Direct to Environment 10 minutes - 30 days Through Shield Building Through Auxiliary Building SV Direct to Environment Shield Building Air Flows (cfm) 0-10 minutes Shield Building to Environment Shield Building Recirculation 10 minutes - 30 minutes Shield Building to Environment Shield Building Recirculation
> 30 minutes Shield Building to Environment Shield Building Recirculation Iodine chemical form in containment (%)
Elemental Organic Particulate (cesium iodide)
Spray and sedimentation removal in containment Shield building and auxiliary building filter efficiencies (%)
Elemental Organic Particulate 1.32E6 3.74E5 0.5 Not Modeled, No holdup Credited 0.5 0.25 0.0 0.1 0.9 0.89 0.10 0.01 Not applicable Not applicable 6000+/-10%
0.0 3100 2300 4.85 0.15 95 Not Credited 90 90 99 Page 49/54
Westinghouse Proprietary Class 3 Table 16 Assumptions Used for Rod Ejection Dose Analysis (continued)
Primary to secondary Leakage Release Path SG tube leak rate (gpd/SG) 500 Steam release to environment (Ibm/sec) 0 - 200 seconds 800 200 - 1800 seconds 100
> 1800 seconds 0.0 SG iodine and alkali metal water/steam partition coefficient 0.01 Iodine chemical form in after release to atmosphere (%)
Elemental 97 Organic 3
Particulate (cesium iodide) 0 Time to start crediting emergency control room HVAC (min) 2 Page 50154
Westinghouse Proprietary Class 3 Table 17: Assumptions Used for Fuel Handling Accident Dose Analysis Radial peaking factor Fuel damaged (number of assemblies)
Time from shutdown before fuel movement (hr)
Activity in the average fuel assembly after 100 hours0.00116 days <br />0.0278 hours <br />1.653439e-4 weeks <br />3.805e-5 months <br /> shutdown (Ci) 1-131 1-132 1-133 1-134 1-135 Kr-85m Kr-85 Kr-86 Kr-87 Xe-131m Xe-133m Xe-133 Xe-135m Xe-135 Xe-138 Gap Fractions (% of core activity) 1-131 Kr-85 Other Iodine and Noble Gas nuclides Water depth Overall pool iodine scrubbing factor Iodine chemical form in release to atmosphere (%)
Elemental Organic Particulate Filter efficiency Isolation of release Time to releases all activity (hours)
Time to start crediting emergency control room HVAC (min) 1.7 1
100 2.65E5 2.24E5 2.79E4 0.0 1.99E1 1.98E-2 4.83E3 0.0 0.0 3.99E3 9.75E3 5.18E5 3.19 9.80E2 0.0 8
10 5
23 feet 200 70 30 0
No filtration assumed No isolation assumed 2
1 Page 51154
Westinghouse Proprietary Class 3
,,Table 18: Assumptions Used for Steam Line Break Dose Analysis Reactor coolant noble gas activity prior to accident (% fuel defect level) 1.0 Reactor coolant iodine activity prior to accident (tCi/gm of DE 1-131)
Pre-accident iodine spike 60 Accident-initiated iodine spike (pCi/gm of DE -13 1) 1.0 Reactor coolant iodine appearance rate increase due to the accident-initiated spike (times equilibrium rate) 500 Duration of accident-initiated iodine spike (hr) 4.0 SG tube leak rate (gpd/SG) 500 Steam release from faulted SG to environment during first two minutes (lbm) 150,000 Time to release initial mass in faulted SG (min) 2 Steam releases from intact SG (Ibm) 0 -2 hours 220,000 +10%
2 - 8 hours9.259259e-5 days <br />0.00222 hours <br />1.322751e-5 weeks <br />3.044e-6 months <br /> 393,000 +10%
Time to cool RCS below 212'F and stop releases from faulted SG (hr) 72 SG iodine water/steam partition coefficient Faulted SG 1.0 Intact SG 0.01 Time to start crediting emergency control room HVAC (min) 5 Page 52/54
Westinghouse Proprietary Class 3 Table 19: Assumptions Used for GDT and VCT Rupture Dose Analyses Gas Decay Tank Rupture Source Term Gas decay tank inventory (Ci)
Kr-85m 83 Kr-85 2480 Kr-87 15 Kr-88 184 Xe-131m 430 Xe-133m 558 Xe-133 34,300 Xe-135m 26 Xe-135 606 Xe-138 2
Volume Control Tank Rupture Source Term Volume control tank gas inventory (Ci)
Kr-85m 62 Kr-85 637 Kr-87 15 Kr-88 232 Xe-131m 164 Xe-133m 257 Xe-133 14,000 Xe-135m 33 Xe-135 407 Xe-138 2
Volume control tank liquid iodine inventory (Ci) 1-131 0.69 1-132 0.63 1-133 1.02 1-134 0.14 1-135 0.57 Reactor coolant noble gas activity prior to accident (% fuel defect level) 1.0 Reactor coolant iodine activity prior to accident (jtCi/gm of DE 1-13 1) 60 Page 53/54
Westinghouse Proprietary Class 3 Table 19 Assumptions Used for GDT and VCT Rupture Dose Analyses (continued)
Release modeling Time to release all GDT activity (min) 5 Time to release all VCT activity (min) 5 Letdown flowrate to VCT (gpm) 80 +10%
Letdown demineralizer decontamination factor 10 Time to isolate letdown flow (min) 5 Time to start crediting emergency control room HVAC (min) 0.5 Page 54/54