ML16277A115

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ERS-HHM-87-014, Rev. 8, Unit 1 / Unit 2 ODCM Gaseous Effluent Monitor Setpoints.
ML16277A115
Person / Time
Site: Beaver Valley
Issue date: 01/30/2015
From: Novak R
FirstEnergy Nuclear Operating Co
To:
Office of Nuclear Reactor Regulation
References
ERS-HHM-87-014, Rev 8
Download: ML16277A115 (35)
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{{#Wiki_filter:FORM 1/2-ADM-1611.F28, Rev. 2 RTL# A9.621A Beaver Valley Power Station Radiation Protection Technical Position/Evaluation/Calculation Subject No. PAGE 1 OF Unit 1 I Unit 2 ODCM Gaseous Effluent Monitor Setpoints ERS-HHM-87-014 35 Reference HPP EPP T/S CR ECP-10-0150 Category Unit 1 Unit 2 D Technical Position IX I Technical Evaluation D Calculation [8J D Purpose The purpose of this package is to provide Unit 1 and Unit 2 ODCM pre-calculated (default) gaseous effluent monitor alarm setpoints that are traceable to ODCM alarm setpoint methodology. This is applicable for batch and continuous releases of nobles gases in gaseous effluents for the following gaseous effluent monitors. D ORIGINAL ISSUE Ix I REVISION # 8 Revision description: This revision corrects an error in an equation on pg 22, revised equation #7 on page 6 to reflect current calculations for the Mirian monitors at Unit 1, and formatting was revised on pages 2-8 to show all text. All other pages were unaffected. independent review (calculation only) Checklist Attachments O Purpose D Results D Data Sheets 0 Methodology D References D Illustrations O Input Data D Printouts D Code Listings l:&:lTransmittal to BVRC D Supt, Rad Ops l:&:l Author: Rebecca Novak l:&:lOriginal RP ERF FILE D Supv, RP Services l:&:l """'R=o=be""'rt~W.-i..... n""'"te......rs......__ _ _ __ 0 MGR, Radiation Protection D Supv, Rad Waste/Effluents D D

BEAVER VALLEY POWER STATION ERS-HHM-87 -014 Page 2 ~ 35 Radiation Protection Section Revision 8 DISCUSSION All eight gaseous effluent pathways at Unit 1 and Unit 2 are continuously monitored for radioactive materials via the RMS and DRMS. Each of the monitors on these effluent pathways contain at least one channel that is used for monitoring noble gases. The objective of this calculation package is to provide consistent methodology for both units and to provide a bases that is traceable to ODCM setpoint methodology. Revision l: The RSC determined that this revision was not valid. This revision was not issued. Revision 2: This revision converts the alarm setpoints for the Unit 2 WRGM [2HVS-RQ109] from uCi/cc to uCi/sec. Specifically, the alarm setpoints for this gaseous monitor are not set in the "B" Channel (uCi/cc), like the other Unit 2 gaseous effluent monitors. Rather, the alarm setpoints are set in the "E" Channel (uCi/sec). Revision 3: CR00-3928-01: Recalculated alarm setpoints for all gaseous effluent radiation monitors. Specifically, the Lower and Upper Alarm Setpoints were raised, respectively, from 10% and 30% of the ODCM Site Dose Rate Limit to 30% and 60% of the ODCM Site Dose Rate Limit. (Reference 13) Revision 4: CR03-04830-05: Recalculated alann setpoints for [RM-1GW-108B] and [RM-lGW-109 Ch 5] due to' installation of High Capacity Containment Vacuum Pumps for Unit 1 via ECP-02-0079. The new pumps have a maximum capacity of 70 c:fin, where as, previous source-term determinations were based on a pump capacity of 5 cfm. (Reference 14) Revision 5: CR13-04092-13: Corrected the upper range limit value for the SPING radiation monitors listed on, Page 9. Monitor alarm setpoints are unaffected by this change. The alann setpoint percentage of the scale lmit values previously discussed on Page 6 and used in place of calculated off-scale values are removed. The associated alarm setpoint values calculated in Revision 4 remain on-scale and are not changed in this revision. All other pages and other content on Pages 6 and 9 are unaffected. (Reference 15) Revision 6: This revision includes low and high range calculated setpoints for new radiation monitors being installed under ECP-10-0150, Replacement ofBVl Effluent Monitoring System. Radiation monitors being replaced include RM-lVS-109, RM-lVS-110, andRM-IGW-109. The ECP will install vendor-recommended replacement components provided by Mirion Technologies Inc, that will duplicate or exceed the original components functions and operation. High and low monitor efficiencies (reference ERS-SFL-85-031 pg 23) provided by the vendor were used in the calculation. Effected pages include 11, 12, 14, 15, 17, 18, 22, 23, 25, 26, 28, and 29. All other pages are unaffected. Revision 7: This rev~sion incorporates comments from a third party review performed by Rolls Royce. The continuous release activity value, Ai, forXe-13lm via RM-1GW-108B, RM-IGW-109 Low, and RM-lGW-109 High was corrected to be consistent between all three monitors. Also the links in Attachment 1 were corrected to display the correct Final Process Points. Affected pages include 9, 27, 28, 29. All other pages are unaffected. Revision 8: This revision corrected an error in an equation on pg 22. All other pages are unaffected. Original Alarm Setpoint Bases ( The original alarm setpoint calculations for Unit I monitors were implemented in Jan 1984 via Unit 1 Technical Specification Amendment 66 (RETS implementation). The setpoints for Unit 2 monitors were implemented in July 1987 via initial issue of the Unit 2 Technical Specifications. The setpoints are based on the following:

1. The process alarm setpoints were traceable to ODCM procedure Yz-ODC-2.02. The upper alarms are set at 30% of the ODCM site dose rate limit for noble gases, and the lower alarms are set at ~I 0% of the ODCM site dose rate limit for noble gases.

BEAVER VALLEY POWER STATION ERS-HHM-87-014 Page 3 ~ 3S Radiation Protection Section Revision 8 Unit land 2 Technical Specification Requirements (References I, 2} Section 6.8.6.a.1 indicates that the Radioactive Effluent Control Program shall include monitor setpoint determinations that are performed in accordance with the ODCM. BVPS-1 UFSAR Requirements (Reference 3) I. Section 11.3.3.3.2 indicates that a high-high activity alarm on RM-1GW-108B will cause automatic closure of valves downstream of the decay tanks, thus terminating the waste gas flow from the decay tank.

2. Section 11.3.3.3.3 does not contain any requirements for alarm setpoints of RM-lVS-lOlB.
3. Section 11.3.3.3.4 does not contain any requirements for alarm setpoints ofRM-1VS-107B.
4. Section 11.3.3.3.23 does not contain any requirements for alarm setpoints ofRM-lGW-109 Cb 5, RM-IVS-109 Ch 5, and RM-lVS-110 Ch 5.

BVPS-2 UFSAR Requirements (Reference 4)

1. Section 11.5.2.4.1 does not contain any requirements for alarm setpoints of2INS-RQ101B.
2. Section 11.5.2.4.2 does not contain any requirements for alarm setpoints of2HVS-RQ109B.
3. Section 11.5.2.4.4 does not contain any requirements for alann setpoints of2HVL-RQ112B.
4. Section 11.5.2.4.6 indicates that a high alarm on 2RMQ-RQ303B causes flow diversion through filters before being released to the atmosphere.
5. Section 11.5.2.4.7 does not contain any requirements for alarm setpoints of2RMQ-RQ301B.

BVPS-1 USNRC SER Requirements (Reference 5) Although Section 11.6 and 11.7 do not contain any requirements for alarm setpoints of the gaseous channels of any Unit l gaseous effluent monitors, it does indicate that the process monitoring system is adequate for monitoring effluent discharge paths as described in GDC 64. BVPS-2 USNRC SER Requirements (Reference 6) Although Section 11.5 does not contain any requirements for alarm setpoints of the gaseous channels of any Unit 2 gaseous effluent monitors it does indicate that the process monitoring system is adequate for monitoring effluent discharge paths as described in GDC 64. Other Regulatmy Commitments There are no other known regulatory requirements for the alarm setpoints of the gaseous channels of these gaseous effluent monitors. Offsite Dose Calculation Manual (ODC:M) Requirements (References 7, 8) Section 8.1 of ODCM procedure %-ODC-2.02 describes the methodology to be used for alann setpoint determination. All setpoints are based on a fraction of the limits specified in Control 3.11.2.1 of procedure %-ODC-3.03 for re1ease of noble gases from the site. The limits are as follows: S500 mrem/yr to the Total Body

BEAVER VALLEY POWER STATION ERS-HHM-87-014 Page 4 1;; 3S Radiation Protection Section Revision 8 

  .::;3000 mrem/yr to the Skin Instrument Error Considerations (References 9, 10, 11)

The original Unit 1 alarm setpoint calculations did not consider the effect of instrument and process errors on the alarm setpoints. Unit 2 alarm setpoints did assess this effect for most monitors, and the Unit 2 UFSAR does contain a commitment to Regulatory Guide 1.105. The Radiation Safety Committee discussed this issue in meeting BV-RSC-25-87. From these discussions, a position with regard to the applicability ofRG 1.105 to the radiation monitors was developed and documented in ERS-SFL-87-036. From this position, it is inferred that, as a licensing item, RG 1.105 does not apply to the gaseous channels of the gaseous effluent monitors at Unit 1 and Unit 2. The alarm setpoints will be calculated using ODCM procedure \,'2-0DC-2.02 methodology for gaseous monitor setpoints so that the limits will not be exceeded in the Unrestricted Area. INPUT DATA/ASSUMPTIONS References Ai= Particulate Activity from the release path (Ci/yr) [4, 7 & Attachment 4] x/Q =Dispersion Parameter (sec/m3) [7] F =Discharge Flowrate (cfrn) [7] Ei =Monitor Sensitivity (cpm/uCi/cc) [7] Ki = Total Body Dose Factor (mrern/yr/uCi/m3) [7] Li ='Skin Dose Factor (mrem/yr/uCi/m 3) [7] Mi = Gamma Air Dose Factor (mrad/yr/uCi/m3) [7] Vi = Total Body Dose Rate Factor (mrem/yr/uCi/m3) [7] Bi= Gamma Air Dose Rate Factor (mrad/yr/uCi/m3) [7] METHODOLOGY An EXCEL spreadsheet was generated to perform the alarm setpoint calculations (see Attachment 2 for batch release setpoints and see Attachment.3 for continuous release setpoints).

1. Si: Calculated using 1/2-0DC-2.02 equation [(2.1(1)-1] for BV-1, [2.1(2)-1] for BV-2 and [2.1-9] for BV-112:):

Si=~ L:Ai i where: Si= the fraction of total radioactivity Ai= the appropriate individual nuclide source term values from BVPS-2 UFSAR Tables 11.3-1 & 11.3-2, Yz-ODC-2.02 Tables 2.1-la & 2.1-Ib, Yz-ODC-2.02 Section 8.1, and Attachment 4 (Ci/yr)

BEAVER VALLEY POWER STATION ERS-HHM-87-014 Page 5 C[J 3S Radiation Protection Section Revision 8 2 Q,: Calculated for whole body exposure using 1/2-0DC-2.02 equation [(2.1(1 )-2), [2.1(2)-2], and [2.1-JO]: 500 500 Qt= (x/Q) L KiSi 'or Qt =(x/Q) L ViSi i i where: Qi the max acceptable total release rate (uCi/sec) 500 = TS/ODCM Total Body Dose Rate Limit due from Noble Gases (mrem/yr) x/Q = appropriate dispersion parameter from the ODCM procedure Yz-ODC-2.02 (sec/m3) Ki= total whole body dose factors from ODCM procedure Yz-ODC-2.02, Table 2.2-11 (mrem/yr/uCi/m3) Vi= total whole body dose factors from ODCM procedure Yz-ODC-2.02, Table 2.2-12 (mrem/yr/uCi/sec) Si = previously described 3 Q,: Calculated for skin exposure using l/2-0DC-2.02 equation [(2.1(1)-3], [2.1(2)-3), and [2.1-11]: 3000 3000 Q,=-~~~"=-~~~~~ or Q,=---~~~~~~~~~ (x/Q) Li (Li+ 1. lKi)Si ' (x/Q) L [Li(x/Q) + 1.1 Bi] Si i i where: Qi= the max acceptable total release rate (uCi/sec) 3000 = TS/ODCM Skin Dose Rate Limit due from Noble Gases (mremlyr) x/Q = previously described 

                  ,Lj =      skin dose factors from ODCM procedure Yz-ODC-2.02, Table 2.2-11 (mrem/yr/uCi/m3)

Mi= gamma air dose factors from ODCM procedure Yz-ODC-2.02, Table 2.2-11 (mrad/yr/uCi/sec) Bl'= gamma air dose rate factors from ODCM procedure Y..-ODC-2.02, Table 2.2-12 (mrad/yr/uCi/sec) ' Si = previously described 4 Qi: Calculated using 1/2-0DC-2.02 equation [(2.1(1)-4], [2.1(2)-4], and [2.l-12]: Qi=s1:Qt Si = previously described Qt = previously described

BEAVER VALLEY POWER STATION ERS-HH M-87-014 Page 6 ~ ?6 Radiation Protection Section Revision 8 5 Ci: Calculated using l/2-0DC-2.02 equation [(2.1 (1)-5], [2.1(2)-5], and [2.1-13]: Ci 2.12E-3 Qi F where: Ci= max acceptable radioactivity concentration for each radionuclide (uCi/cc) F= the max acceptable effluent flow rate at the point of release for the appropriate pathway (cfm) 2.12E-3 =conversion factor (60 sec/minx 3.53E-5 ft3/cc) 6 The monitor count rate (CR) was calculated using 1/2-0DC-2.02 equation (2.1-6): where: CR= monitor count rate attributed from each radionuclide (ncpm) Ci = previously described Ei = detection efficiency for the appropriate monitor fonn ODCM procedure !6-0DC-2.02, Table 2 .. l-2a and 2. l-2b.

7. The monitor alarm process setpoints were calculated using l/2-0DC-2.02 equation [2.1-7] and [2.1-8] as follows:

Unit I Victoreen: HHSP = 0.60* CR= 300 mrem/yr HSP = 0.30 *CR= 900 mrem/yr Unit I Mirion: HSP = (CR*0.60)/Eia = 300 mrem/yr ASP= (CR*0.30)/Eia = 900 mrem/yr Unit 2: HSP ~ (CR*0.60)/Eia = 300 mrem/yr ASP = (CR*0.30)/Eia = 900 mrem/yr where: the process upper alarms'(HHSP and HSP) and the process lower alarms (HSP and ASP) are the monitor alarm setpoints above background for the process stream (net cpm, net cps, net uCi/s or net uCi/cc) CR = previously described Bia= for Unit 2 monitors and Unit 1 Mirion monitors only; this calculation was calculated per l/2-0DC-2.02 equation [2.1-8] where Eia is calculated as follows: Eia = CR/(~Ci for the respective mix) 0.60 and 0.30 =fractions of total radioactivity concentration that may be released via the monitored pathway to ensure that the TS/ODCM Dose Rate Limits are not exceeded.

8. The monitor process setpoints were then compared to Routine Mean Background and Instrument Display Range. The final monitor process setpoints ensure that no gaseous monitor calculated setpoint is close enough to the Routine Monitor Background that would cause an alarm. This. did not occur for any of these setpoints. Also, when a calculated setpoint was greater than the Instrument Display Range, on-scale values were substituted.

RESULTS See Attachment 1 for a summary of the gaseous monitor alarm setpoints for batch and continuous releases of gaseous effluents at Unit 1 and Unit 2.

BEAVER VALLEY POWER STATION ERS-HHM-87-014 Page 7 "'Q 35 Radiation Protection Section Revision 8 REFERENCES

1. FENOC, Unit 1 Technical Specification 6.8.6a
2. FENOC, Unit 2 Technical Specification 6.8.6a
3. FENOC, Section 5 and Section 11 of Updated Final Safety Analysis Report for Unit l
4. FENOC, Section 11 of Updated Final Safety Analysis Report for Unit 2
5. USNRC, Safety Evaluation Report Related To The Operation Of The Beaver Valley Power Station Unit l, (Through Supplement 3)
6. USNRC, Safety Evaluation Report Related To The Operation Of The Beaver Valley Power Station Unit 2, (Through Supplement 6)
7. FENOC, ODCM procedure l/2-0DC-2.02, Gaseous Effluents
8. FENOC, ODCM procedure l/2-0DC-3.03, Controls for RETS and REMP Programs
9. USNRC, Instrument Setpoints, Regulatory Guide 1.105; 1976
10. DLC, Minutes Of Radiation Safety Committee Meeting 25-87, BV-RSC-25-87; 1987
11. FENOC, Applicability ofRG 1.105 To BVPS Radiation Monitors, ERS-SFL-87-036, Revision O; 1987
12. SWEC, Gaseous Releases from Containment Vacuum Pumps, UR(B)-262, Revision O; 1983
13. CR00-3 928, RM- I VS-107A Recurring High Alarms, CA-0 I; Revise Calculation Packages to re-calculate the alann setpoints for the gaseous effluent pathway radiation monitors. Specifically, the lower and upper alarm setpoints will be raised from 10% and 30% of the ODCM Site Dose Rate Limit (for Noble Gas releases) to 30% and 60% of the ODCM Site Dose rate Limit (for Noble Gas Releases).
14. CR03-04830, Containment Vacuum Pump Replacement Increases ODCM Source-Term, CA-05; Revise Calculation Package ERS-HHM-87-014 to show adjustment of Containment Vacuum Pump Source. Specifically, the Old Source-Term was developed using a flowrate of 5 cfm, where as, a New Source-Term needs developed using a flowrate of 70 cfm.
15. CR13-04092, SPING Radiation Monitors RM-lVS-110 Channel 5 and RM-IGW-109 Channel 7 are unable to display levels at or above the EAL setpoint, CA-13; Update 1-HPP-4.02.010, ERS-MPD-93-007, and ERS-HHM 014 to correct the upper display limits.

BEAVER VALLEY POWER STATION ERS-HHM-87-014 . Page 8 Pb 35 Radiation Protection Section Revision 8 ATTACHMENTS I. Alarm Setpoint Summary: Contains the Final Process Alarm Setpoins. This ATTACHMENT is comprised of data from ATIACHMENT 2 and AITACHMENT 3)

2. Batch Releases: Detennination Of Gaseous Monitor Alarm Setpoints
3. Continuous Releases: De CR00-3928-0ltennination Of Gaseous Monitor Alarm Setpoints
4. Adjustment of Unit 1 Containment Vacuum Pump Source Term

ERS-HHM-87-014 Al.arm Setpoint Summary Revision 6 

 !lrooesG Alarm Sctpoints: For Gaseous Effluent (Noble Gas) Monitors                                                      Attachment 1 page9
                                                                                                                             ~oS Raw       Routine Instrument Display Ran.QeS                                Final Unit l. ' 2                                       Process        Mean >r range (cpm), or (uCilcc)                             Process Continuous Releases                              Setpoin1s Bacl<Qround tr range (cpm), or (uCilcc)                           SetPoin1s RM-1VS-1018                   HHSP (cpm) =     1.80E+03             75                          10            NA: See Raw HHSP RM-1VS-101B                     HSP(cpm) =     9.00E-+02            75                     1E+06              NA; See Raw HSP RM-1VS-109 Low                HSP (uCi/cc) =    5.42E-05              0                         10            NA; See Raw HSP RM-1VS-109 Low                ASP (uCVcc) =     2.71E-05              0                5.01E+05               NA: See Raw ASP RM-1VS-109 High               HSP (uCi/cc) =    5.42E--05             0                        10             NA: See Raw HSP RM-1VS-109 High               ASP(uCi/cc) =     2.71E-05              0                5,01E+05               NA: See Raw ASP RM-1VS-107B                   HHSP(cpm)=       3.87E+03             99                         10             NA; See Raw HHSP RM-1VS-107B                     HSP(cpm)=      1.93E-+03            99                     1E+06              NA; See Raw HSP RM-1VS-110 Low                HSP (uCl/cc) =    9.78E-05              0                        10             NA: See Raw HSP RM-1VS-110 Low                ASP {uCilcc) =    4.89E-06              0                5.01E+05               NA; See Raw ASP RM-1VS-110 High                HSP(uCl/cc) =     9.78E-05             0                         10             NA: See Raw HSP RM-1VS-110 High                ASP(uCi/cc} =     4.B9E-05             0                 5.01E+05               NA: See Raw ASP RM-1GW-10BB                    HHSP{cpm)=      209E-+07            323                          10                          3.60E+06 RM-1GW-10BB                      HSP{cpm)=     1.05E-+07           323                   1.2E+06                            1.20E-+05 RM-1GW-109 Low                HSP CuCi/cc} =    9.59E-01              0                         10             NA: See Raw HHSP RM-1GW-109 Low                 ASP(uCi/cc) =    4.BOE-01              0                  5.0E+05               NA: See Raw HHSP RM-1GW-109 High               HSP (uCi/cc) =    9.59E-01              0                         10             NA; See Raw HHSP RM-1GW-109 High               ASP (uCi/cc) =    4.BOE-01              0                  5.0E+OS               NA; See Raw HHSP 2HVS-RQ101B                   HSP (uCi/cc) =    1.81E-04     1.92E-06                           10   3.65E-07  NA; See Raw HSP 2HVS-RQ101 B                  ASP (uCi/cc) =    9.04E-05     1.92E-06                      1E+07     3.65E-01  NA; See Raw ASP 2HVS-RQ109B                  HSP (uCi/sec) =   1.77E+03             NA                         NA          NA       NA; See Raw HSP 2HVS-RQ109B                  ASP (uCi/sec) =   8.83E+02             NA                         NA          NA       NA: See Raw ASP 2RMQ-RQ301 B                  HSP (uCi/cc} =    1.89E-03     2.20E-06                           10   5.56E-07 NA; See Raw HSP 2RMQ-RQ301 B                  ASP (uCi/cc) =    9.44E-04     2.20E-06                      1E+07     5.56E-01 NA; See Raw ASP 2RMQ-RQ303B                   HSP (uCi/cc) =    1.55E-02     2.BBE-06                           10   2.63E-07 NA: See Raw HSP 2RMQ-RQ303B                   ASP (uCl/cc) =    7.74E-03     2.SBE-06                      1E+07     283E-01  NA: See Raw ASP 2HVL-RQ112B                   HSP (uCi/cc) =    9,63E-04     3.09E-05                          10    5.56E-07 NA: See Raw HSP 2HVL-RQ1128                   ASP (uCilcc) =    4.82E-04     3.09E-05                      1E+07     5.56E-01 NA: see Raw ASP Unit 1 Batch R.elea11e - Contai.nment   ~gei RM-1VS-101B                   HHSP (cpm)=      7.1BE+02             75                         10             NA: See Raw HHSP RM-1VS*101B                     HSP(cpm)=      3.59E+02             75                     1E+OB              NA; See Raw HSP RM-1VS-109 Low                 HSP CuCi/cc) =    4.47E-05             0                         10             NA; See Raw HSP RM-1VS-109 Low                 ASP (uCi/cc) =    2.24E-05             0                 5.01E+05               NA; See Raw ASP RM*WS-109 High                HSP [uCi/cc) =    4.47E-05             0                         10             NA; See Raw HSP RM-1VS-109 Hi11h               ASP CuCi/cc) =   2.24E-05              0                 5.01E+05               NA; See Raw ASP RM-1VS-107B                    HHSP (cpm)=     7,63E+03             99                          10             NA; See Raw HHSP RM-1VS-107B                      HSP(cpm)=     3.81E+03             00                     1E+06               NA; See Raw HSP RM-1VS-110 Low                   HSP(cpm}=      1.93E-04              0                         10             NA; See Raw HSP RM-1VS-110 Low                   ASP (cpm}=     9.64E-05              0                 5.01E+05               NA; See Raw ASP RM-1VS-110 High                  HSP (cpm)=     1.93E-04              0                         10             NA; See Raw HSP RM-1VS-110 High                  ASP (cpm)=     9.64E-06              0                 5.01E+05               NA; See Raw ASP Unit 1 ' 2 Ba toh Releas* - De:oay Tan.le Discharges RM-1GW-10BB                    HHSP {cpm)=     2.36E+05            323                          10             NA; See Raw HHSP RM-1GW-108B                      HSP (cpm)=    1.1BE+05            323                     1E+06               NA; See Raw HSP RM-1GW-109 Low                   HSP (cpm)=     1.97E-01              0                         10             NA; See Raw HSP RM*1GW*109 Low                   ASP (cpm)=     9.87E-02              0                 5.01E+05               NA; See Raw ASP RM-1GW-109 High                 HSP (cpm)=      1.97E-01              0                         10             NA; See Raw HSP RM-1GW-109 High                 ASP (cpm)=      9.87E-02              0                 5.01E+OS               NA; See Raw ASP Unit 2 Batch Release - Containment Purge 2HVS-RQ101B                   HSP CuCi/cc) =    4.43E-05     1.92E-06                          10    3.85E-07  NA; See Raw HSP 2HVS-RQ101B                   ASP (uCi/cc) =    222E-05      1.92E-06                      1E+07     3.85E-01  NA; See Raw ASP 2HVS-RQ109B                  HSP CuCl/sec) =   6.76E+02             NA                         NA          NA       NA; See Raw HSP 2HVS-RQ1098                  ASP (uCilsec) =   3.38E+02             NA                         NA          NA       NA: See Raw ASP

Balch Release ERS-HHM-87-014 Revision 8 Unit 1 - Containment Purge VIA Vw1Ulation Vent Pathway Gaseous Effluent Monitor (Vlctoroon) Attachment 2 ~ RM-1VS-101 B page LO C{) Nuclide Ai SI Ki Li Ml QI Cl El CR Ai/Sum Al KiSI (U+1.1Ml)SI SiQt (2.12E-3 Qi)JF CIEi mremtyr mrem/yr mrem/yr mrad/yr mremtyr cpm per per per per per per Ci/yr uCi/m3 uCl/m3 uCi/m3 UCVm3 uCVm3 uCilsec uCl/CC uCi/cc cpm 1 Ar-41 2.5E+01 1.41E-01 8.84E+03 1.24E+03 2.89E+03 9.30E+03 1.82E+03 1.4BE+02 1.0SE-05 7.17E+07 7.51E+02 2 Kr-83m 2.2E-02 1.24E-04 7.56E-02 9.35E-06 O.OOE+OO 1.93E+01 2.63E-03 1.31E-01 9.22E-09 O.OOE+OO O.OOE+OO 3 Kr-85m 1.5E-01 B.44E-04 1.17E+03 9.B7E-01 1.46E+03 1.23E+03 2.37E+OO B.90E-01 6.29E-08 9.80E+07 6.1BE+OO 4 Kr-85 B.1E+01 3.43E-01 1.B1E+01 5.52E+OO 1.34E+03 1.72E+01 4.66E+02 3.62E+02 2.56E-05 3.88E+05 9.92E+OO 5 Kr-87 5.4E-02 3.04E-04 5.92E+03 1.BOE+OO 9.73E+03 6.17E+03 5.02E+OO 3.20E-01 2.26E-08 7.38E+07 1.67E+OO 6 Kr-88 2.4E-01 1.35E-03 1.47E+04 1.98E+01 2.37E+03 1.52E+04 2.5BE+01 1.42E+OO 1.01E-07 1.14E+08 1.15E+01 7 Kr-89 4.7E-04 2.64E-06 1.66E+04 4.39E-02 1.01E+04 1.73E+04 7.70E-02 2.79E-03 1.97E-10 1.39E+08 2.74E-02 8 Kr-90 0.0E+OO 0.00E+OO 1.58E+04 O.OOE+OO 7.29E+03 1.63E+04 O.OOE+OO O.OOE+OO O.OOE+oo 1.34E+08 O.OOE+OO 9 Xe-131m 7.4E.{)1 4.16E-03 9.15E+01 3.B1E-01 4.76E+02 1.56E+02 2.70E+OO 4.39E+OO 3.10E-07 2.25E+OO 6.98E-01 10 Xe-133m 8.9E-01 5.01E-03 2.51E+02 1.2BE+OO 9.94E+02 3.27E+02 6.7BE+OO 5.28E+OO 3.73E-07 1.26E+D7 4.7DE+OO 11 Xe-133 8.9E+D1 5.01E-01 2.94E+02 1.47E+02 3.06E+02 3.63E+D2 3.48E+02 5.28E+D2 3.73E.05 1.01E+07 3.77E+02 12 xe-135m 4.5E.{)3 2.53E-05 3.12E+03 7.9DE-02 7.11E+02 3.36E+03 1.12E.01 2.67E-02 1.89E-09 7.15E+07 1.35E-01 13 Xe-135 7.0E-01 3.94E-03 1.81E+03 7.13E+OO 1.B6E+03 1.92E+03 1.56E+01 4.15E+OO 2.93E-07 1.12E+08 3.29E+01 14 Xe-137 1.0E-03 5.62E-06 1.42E+03 7.99E-03 1.22E+04 1.51E+03 7.BOE-02 5.93E-03 4.19E-10 3.16E+07 1.32E-02 15 Xe-138 1.SE-02 B.44E-05 8.83E+03 7.45E-01 4.13E+03 9.21E+03 1.20E+OO 8.00E-02 6.29E-09 1.15E+OB 7.23E-01 Totals = 1.BE+D2 1.43E+03 2.69E+03 7.45E-05 1.20E+03 3.32E-04 seclm3 = x/Q (From ODCM procedure 1f.2-0DC-2.02, Section 8.1.1) Qt(Total Body)= 500/(x/Q) sum(KISI) = 1.05E+D3 uCi/sec 30000 elm= Flowrate.(From ODCM procedure 1/2-0DC-2.02, Seclion 6.1.1) Qt(Skln) = 30001(x/Q) sum(U+ 1.1 Ml)SI = 3.36E+03 uCi/sec Lowest Qt Value 1.05E+03 uCVsec Ai: From ODCM procedure 1/2-0DC-2.02, Attachment A, Table 2.1-1a Kl.LI & Ml: From ODCM procedure 112-0DC-2.02, Attachment G, Table 2.2-11 El: FromODCM procedure 1/2-0DC-2.02, AttachmentB, Table 2.1-2a CR = Sum{CIEI) = 1.20E+03 cpm = CR HHSP =(CR x 0.6) V\11ere; 0.6 = 60% of the Site Noble Gas Dose Rate Limit= 7.18E+D2 cpm =Process HHSP HSP = (CR x 0.3) 'M1era; 0.3 = 30% of the Sita Noble Gas Dose Rate Limit= 3.59E+D2 cpm = Process HSP NOTE: All equations used above ere from ODCM procedure 1/2-0DC-2.02, Section 8.1.1 Trip -HHSP= 7.18E+02 I (1 + .35 + .10) = 4.95E+02 cpm Trip -* HSP= 3.59E+02 1(1 + .35 + .10)= 2.48E+02 cpm

Batch Release ERS-HHM-87-014 Revision 8 Unit 1 - Containment Purge VIA Ventilation Vent Pathway Gaseous Effluent Monitor Attachment 2 , C... Page \\. C\)3~ RM-1VS*109 Low Nuclide _Ai_*- - - Si Ki LI Ml QI Cl .:Eo.:.i_ __ CR 

                                    ~A7i/~S~u-m-.,.Ai~. "'"""---        Ki Si                                    (Li+1.1MQSi SiQt            (2.12E-3Ql)F _ _ __             CiEi mrem/yr        mremlyr      mrem/yr      mrad/yrper     mrem/yr                                      cps per
                     ~                                   peruCUm3       peruCUm3     peruCUm3     uCUm3          peruCi/m3 ~                 uCVcc            uCi/cc        cps Ar-41               2.5E+o1        1.41E-01           8.84E+03       1.24E+03     2.69E+o3     9.30E+03        1.B2E+03     1.4BE+02       1.0SE-05          1.60E+05     1.6BE+OO 2     Kr-83m              2.2E-02       1.24E-04            7.56E-02       9.35E-06    O.OOE+oO     1.93E+01        2.63E-03      1.31E-01      9.22E-09          O.OOE+OO     O.OOE+OO 3     Kr-85m              1.5E-01       8.44E-04           1.17E+03        9.87E-01    1.46E+o3     1.23E+03       2.37E+o0       8.90E-01      6.29E-OB          1.14E+05     7.17E-03 4     Kr-85              6.1Et-01       3.43E-01           1.61E+01       5.52E+OO     1.34E+o3     1.72E+01       4.66E+02      3.62E+02       2.56E-05          1.14E+05    2.92E+OO 5    Kr-87               5.4E-02        3.04E-04           5.92E+03      1.BOE+OO      9.73E+03     6.17E+03       5.02E+OO       3.20E-01      2.26E-OB         1.77E+05      4.01E-03 6    Kr-88               2.4E-01        1.35E-03           1.47E+04      1.9BE+01      2.37E+03     1.52E+04       2.58E+01      1.42E+OO       1.01E-07         1.05E+05       1.0SE-02 7    Kr-89               4.7E-04        2.64E-06           1.66E+04        4.39E-02    1.01E+04     1.73E+04        7.70E-02      2.79E-03      1.97E-10          1.B9E+05     3.72E-05 8    Kr-90              0.0E+DO        O.OOE+OO            1.56E+04      O.OOE+OO      7.29E+03     1.63E+04       O.OOE+DO      O.OOE+OO     O.OOE+OO           1.B9E+-04    0.00E+oO 9    Xe-131m             7.4E-01        4.16E-03           9.15E+01        3.81E-01    4.76E+o2    1.56E+02        2.70E+o0      4.39E+OO       3.10E-07         7.22E+-04     2.24E-02 10    Xe-133m             8.9E-01        5.01E-03           2.51E+02      1.26E+OO      9.94E+o2    3.27E+02        6.78E+o0      5.28E+o0       3.73E-07         1.28E+o5      4.78E-02 11    Xe-133             8.9Et-01        5.01E-01           2.94E+02      1.47E+02      3.06E+o2    3.53E+02        3.48E+02      5.2BE+02       3.73E-05        4.39E+04      1.64E+o0 12    Xe-135m             4.SE-03        2.53E-05           3.12E+03       7.90E-02     7.11E+02    3.36E+03         1.12E-01      2.67E-02      1.B9E-09         3.28E+-04     6.19E-05 13    Xe-135              7.0E-01        3.94E-03          1.81E+03       7.13E+OO      1.86E+03    1.92E+03        1.56Et-01     4.15E+oo      2.93E-07          1.37E+05      4.02E-02 14    Xe-137              1.0E-03        5.62E-06          1.42E+03        7.99E-03     1.22E+04    1.51E+03         7.BOE-02     5.93E-03      4.19E-10         1.83E+05       7.67E-05 15    Xe-138              1.5E-02        8.44E-05          B.83Et-03       7.45E-01    4.13E+03     9.21E+03        1.20E+oo      B.90E-02      6.29E-09         1.43E+-05      B.99E-04 Totals        =---raE+02                                            1.43E+03                                  2.69E->-03                  7.45E-05                       6.36E+OO 3.32E..Q4     sec/m3       = x/Q (from ODCM procedure 1/2-0DC-2.02, Section 8.1.1)                                       Qt (Total Body)= 500/ (x/Q) sum (KiSQ=        1.05E+o3 uCi/sec 30000     elm          = Flowrate (from ODCM procedure 1/2-0DC-2.02, Section B.1.1)                                 Qt (Skin)= 3000 I (x/Q) sum (Ll+1.1Mi)Si=      3.36Et-03 uCl/sec Lowest Qt Value=       1.05Et-03 uCi/sec Ai: From ODCM procedure 1/2-0DC-2.02, Attachement A, Table 2.1-1a)

Ki, Li, & Mi: From ODCM procedure 112-0DC-2.02, Attachment G, Table 2.2-11) Ei: From ODCM procedure 1/2-0DC-2.02, Attachment B, Table 2.1-2a)- Efficiencies found In Minon MCNP Analysis for NGM204 Monitor, pg 16 CR= Sum(CiEi) = 6.36Et-00 cps Eia = (CR) I (Sum Ci) = 8.54E+04 cps I uCi I cc ConversationFactor=1 /Eia = 1.17E-05 uCi/cc/cps Conversation Factor= 1 I Eia = 4.33E->-05 Bq I m3 /cps DV =CR I Eia = 7.45E-05 uCi I cc Process HHSP =((CR) x (60%: Site Noble Gas Dose Rate Limft)) I Eia 4.47E-05 uCi I cc= Process HSP 632.BB uCi/sec Process HSP = ((CR) x (30%: Sfte Noble Gas Dose Rate Limft)) I Eia 2.24E-05 uCI I cc= Process ASP 316.44 uCi/sec Note: All equations used above are from ODCM procedure 1/2-0DC-2.02, Section B.1.2 Unusual Event = 1.05E-+03 uCi I sec x 2 = 2.10E+o3 uCUsec Alert= 1.05E+03 uCI/ sec x 200 = 2.10E+-05 uCl/sec

Batch Release ERS-HHM-ll7-014 Revision 8 Unit 1 - Containment Purge VIA Ventilation Vent Pathway Gaseous Effluent Monitor Attachment2 Page RM-1VS-109 High \'2-o\- 36 Nuclide _A_i___ Si Ki LI Mi Qi Ci Ei CR Ai/SumAI Ki Si (ll+1.1Mi)Si Si Qt (2.12E-3 Oi)F CiEi mremJyr mrem/yr mrem/yr mrad/yr per mrem/yr amps per 

                     ~                            ear uCVm3      eeruCVm3     eeruCVm3      uCVm3         eeruCVm3        uCVsec       uCVcc          uCVcc           am   es Ar-41             2.5E+01        1.41 E-01    8.84E+03       1.24E+03      2.69E+03     9.30E+03        1.82E+03     1.4BE+02       1.05E-05        1.SOE-10        1.57E-15 2     Kr-a:lm           2.2E-02        1.24E-04      7.56E-02       9.35E-06     O.OOE+OO     1.93E+01        2.63E-03      1.31E-01      9.22E-09        4.74E-10       4.37E-18 3     Kr-85m             1.SE-01       8.44E-04     1.17E+o3        9.87E-01     1.46E+o3     1.23E+03       2.37E+DO       8.90E-01      6.29E-08        1.69E-10       1.06E-17 4     Kr-85             6.1E+01        3.43E-01      1.61E+01      5.52E+OO      1.34E+-03    1.72E+o1        4.66E+D2     3.62E+02       2.56E-05        1.79E-10       4.SBE-15 5    Kr-87              5.4E-02        3.04E-04     5.92E+03       1.BOE+OO     9.73E+o3      6.17E+03       5.02E+OO       3.20E-01      2.26E-06        1.0BE-10       2.44E-18 6    Kr-88              2.4E-01        1.35E-03     1.47E+04       1.98E+o1     2,37E+o3      1.52E+o4       2.58E+01      1.42E.. oo     1.01E-07        2.31E-10       2.32E-17 7    Kr-89              4.7E-04        2.64E-06     1.66E+04        4.39E-02    1.01E+D4     1.73E+04         7.70E-02     2.79E-03       1.97E-10        1.77E-10       3.49E-20 8    Kr-90              O.OE+OO      0.00E+oO       1.56E+04      O.OOE+oo      7.29E+03     1.63E+o4        0.00E+OO     O.OOE+OO       O.OOE+OO         2.37E-11      0.00E+OO 9    Xa-131m            7.4E-01        4.16E-03     9.15E+01        3.81E-01    4.76E+02     1.56E+o2        2.70E+OO     4.39E+OO        3.10E-07        2.77E-10       8.59E-17 10    Xe-133m            8.9E-Ot        5.01E-03     2.51E+D2      1.26E+OO      9.94E+02     3.27E+o2        6.78E+OO     5.28E+OO       3.73E-07         2.27E-10       8.47E-17 11    Xe-133            8.9E+o1         5.01E-01     2.94E+D2      1.47E+02      3.06E+o2     3.53E+02        3.48E+o2     5.28E+o2       3.73E-05         4.89E-10       1.82E-14 12    Xa-135m            4.5E-03        2.53E-05    3.12E+03        7.90E-02     7.11E+o2     3.36E+03         1.12E-01     2.67E-02       1.89E-09        1.20E-11       2.26E-20 13    Xa-135             7.0E-01        3.94E-03     1.81E+03      7.13E+OO      1.BSE+-03    1.92E+o3        1.56E+01     4.15E+OO       2.93E-07         1.95E-10       5.72E-17 14    Xe-137             1.0E-03        5.62E-06     1.42E+03       7.99E-03     1.22E+o4     1.51E+o3         7.BOE-02     5.93E-03      4.19E-10         1.17E-10       4.90E-20 15    Xe-138             1.SE-02        B.44E-05    8.83E+03        7.45E-01    4.13E+o3      9.21E+-03       1.20E+OO      B.SOE-02      6.29E-09         1.69E-10       1.00E-18 Totals         1.8E+ii2                                      1.43E+03                                   2.69E+03                    7.45E-05                        2.47E-14 3.32E-04     sec/m3      = x/Q (from ODCM procedure 1/2-0DC-2.02, Section 8.1.1)                                  Qt (Total Body)= 500 I (x/Q) sum (KiSI}=      1.05E+o3 uCi/sec 30000     cfm         = Fiowraie (irom ODCiVi procedura 1/2-0DC-2.02, Section 8.1.1)                          Qt (Skin)= 3000 I (x/Q) si.m (l.1+1.1 Ml)Si=   3.36E;-03 uC!/o:ec Lowest Qt Value =      1. 05E+o3 uCi/sec Al: From ODCM procedure 1/2-DDC-2.02, AttachementA, Table2.1-1a)

Ki, Li, & Ml: From ODCM procedure 112-0DC-2.02, Attachment G, Table 2.2-11) Ei: From ODCM procedure t/2-0DC-2.02, Attachment B, Table 2.1-2*) f f Efficiencies found in Mirian MCNP Analysis for NGM204 Monttor, pg 16 CR= Sum(CiEi) = 2.47E-14 amps Eia= (CR)/(SumCi) = 3.31E-10 amps/uCl/cc Conversation Factor ~ 1 I Eia = 3.02E+09 uCi I cc I amps Conversation Factor= 1 / Eia = 1.12E+20 Sq I m3 /amps DV =CR I Eia = 7.45E-05 uCI I cc Process HHSP = ((CR) x (60%: Stte Noble Gas Dose Raia LlmH)) I Eia 4.47E-05 uCi I cc= Process HSP 632.88 uCVsec Process HSP = ((CR) x (30%: Site Noble Gas Dose Rate Limit)) I Eia 2.24E-05 uCi I cc= Process ASP 316.44 uCi/sec Note: All equations used above are tram ODCM procedure 112-0DC-2.02, Section B.1.2 Unusual Event = 1.0SE+o3 uCi I sec x 2 = 2.1 OE+03 uCVsec Alert= 1.05E+o3 uCJ I sec x 200 = 2.10E+05 uCilsec

Batch Release ER5-HHM-8HJ14 Revision 8 Unit 1

  • Containment Purge VIA Rx Containmeni/SLCRS Vent Pathway Gaseous Effluent Monilcr (Victoreen) Attachment2 RM*1VS-107B page ~\~4J~S Nuclide Af Si Ki LI Mi Qi Ci El CR Ai/Sum Al Ki Si (Li+1.1Ml}SI SI Qt (2.12E..J Qi)/F CiEi mrem/yr mrem/yr mremlyr mrad/yr mremlyr cpm per per per per per per Cl/yr uCi/m3 uCl/rn3 UCi/m3 uCi/m3 UCl/m3 uCUsec UCI/cc uCUcc cprn 1'Ar-41 2.5E+01 1.41E--01 8.84E+03 1.24E+03 2.69E+03 9.30E+03 1.82E+03 1.60E+02 4.52E-05 7.19E+07 3.25E+03 2 Kr.a3m 2.2E-02 1.24E--04 7.56E.{)2 9.35E--06 0.00E+OO 1.93E+01 2.63E--03 1.41E-01 3.9BE-08 O.OOE+OO O.OOE+OO 3 Kr-85m 1.SE-01 8.44E.{)4 1.17E+03 9.87E--01 1.46E+03 1.23E+03 2.37E+OO 9.59E-01 2.71E-07 5.16E+07 1.401:-t-01 4 Kr-85 6.1E+01 3.43E--01 1.61E+01 5.52E+OO 1.34E+03 1.72E+01 4.66E+02 3.90E+02 1.10E-04 5.04E+07 5.56E+03 5 Kr-87 5.4E*02 3.04E-04 5.92E+03 1.80E+OO 9.73E+03 6.17E+03 5.02E+OO 3.45E.{)1 9.76E-08 9.60E+07 9.37E+OO 6 Kr-88 2.4E-01 1.35E-03 1.47E+04 1.98E+01 2.37E+03 1.52E+04 2.58E+01 1.53E+OO 4.34E-07 5.16E+07 2.24E+01 7 Kr-89 4.7E-04 2.64E-06 1.66E+04 4.39E-02 1.01E+04 1.73E+04 7.70E-02 3.01E-03 8.49E*10 9.59E+07 8.15E-02 8 Kr-90 O.OE+OO O.OOE+OO 1.56E+04 O.OOE+OO 7.29E+03 1.63E+04 O.OOE+OO O.OOE+OO O.OOE+OO 9.87E+07 O.OOE+OO 9 Xe-131m 7.4E-01 4.18E-03 9.15E+01 3.81E-01 4.76E+02 1.56E+02 2.70E+OO 4.73E+OO 1.34E-06 2.94E+07 3.93E+01 10 Xe*133m B.9E-01 5.01E-03 2.51E+02 1.26E+OO 9.94E+02 3.27E+02 6.7BE+OO 5.69E+OO '1 1.61E-06 4.17E+07 6.71E+01 11 Xe-133 8.9E+01 5.01E-01 2.94E+02 1.47E+02 3.06E+02 3.53E+02 3.4BE+02 5.69E+02 1.61 E.{)4 2.2BE+07 3.67E+03 12 Xe-135m 4.SE-03 2.53E-05 3.12E+o3 7.90E-02 7.11E+02 3.36E+03 1.12E.{)1 2.BBE-02 B.13E-09 1.51E+07 1.23E-01 13 xe-135 7.0E-01 3.94E-03 1.81E+03 7.13E+OO 1.86E+03 1.92E+03 1.56E+01 4.4BE+OO 1.27E-06 6.42E+07 8.12E+01 14 Xe-137
  • 1.0E-03 5.62E-06 1.42E+03 7.99E-03 1.22E+04 1.51E+03 7.BOE--02 6.39E--03 1.81E-09 1.05E+08 1.90E-01 15 Xe-138 1.SE-02 B.44E-05 B.83E+03 7.45E-01 4.13E+03 9.21E+03 1.20E+OO 9.59E-02 2.71E-08 7.35E+07 1.99E+OO Totals = 1.8E+02 1.43E+03 2.69E+03 3.21E*04 1.27E+04 3.0BE-04 sec/m3 = X/Q (From ODCM procedure 1/2-0DC*2.02, Section 8.1.1) Qt(Total Body)= 500/(x/Q) sum(KiSQ = 1.14E+03 uCVsec 7500 elm= Flowrate (From ODCM procedure 1'2-0DC-2.02. Section 8.1.1) Ql(Skin) = 3000/(x/Q) sum(U+1.1Ml)SI = 3.62E+03 uCi/sec Lowest Qt Value - 1.14E+03 uCi/sec Ai: From ODCM procedure 1/2-0DC-2.02, Attachment A, Table 2.1-1 a Kl,LI & Ml: From ODCM prowdure 1'2-0DC-2.02, Attachment G, Table 2.2-11 Ei: From ODCM procedure 1/2-0DC-2.02, Attachment B, Table 2.1 *2a CR= sum(CiEi) = 1.27E+04 cpm =CR HHSP =(CR x 0.6) W'lere; 0.6 = 60% of the Site Noble Gas Dose Rate Umlt = 7.63E+03 cpm = Process HHSP HSP =(CR x 0.3) wtlere; 0.3 = 30% Of the Site Noble Gas Dose Rate Limit= 3.81E+03 cpm =Process HSP NOTE: All equations used above are from ODCM procedure 1/2-0DC*2.02, Section 8.1.1 Trip -HHSP= 7.63E+03 /(1 +.35+.10)= 5.26E+03 cpm Trip -HSP= 3.81E+03 /(1 + .35+ .10)= 2.63E+03 cpm

ERS-ttHM-87-014 Batch Release Revision 8 Attachment 2 Unit 1 - Containment Purge VIA Rx Containment I SLCRS Vent Pathway Gaseous Effluent Monitor Page IL.\: cQ :£:i RM-1VS-110 Low _A_i_ _ _ LI Mi QI Ci El CR Nuclide SI Ki CIEi NI Sum Ai Ki Si (Li+1.1 MllSI Si Qt (2.12E-3 Qi)F mremlyr mremtyr mrem/yr mrad/yrper mremlyr cps per eeruCVm3 ear uCVm3 eeruCVm3 uCVm3 eeruCVm3 ~ uCVcc uCVcc £l!S 

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2.69E+03 9.30E-t03 1.82E-t03 1.60E+o2 4.52E-05 1.60E+05 7.23E+OO Ar-41 2.5Et01 1.41E-01 8.B4Et03 1.24E-t03 O.OOE+OO 1.93E.,01 2.63E-03 1.41E-01 3.98E-OS O.OOE+oo O.OOE+OO 2 t<r-83m 2.2E-02 1.24E-04 7.56E-02 9.35E-Q6 1.46E+03 1.23E.,03 2.37E+OO 9.59E-01 2.71E-07 1.14E1"05 3.09E-02 3 Kr*85m 1.SE-01 B.44E-04 1.17E+03 9.87E-01 1.34E+03 1.72E+01 4.66E+02 3.9DE+o2 1.10E-o4 1.14Et05 1.26ET01 4 Kr-85 6.1E+o1 3.43E-01 1.61E+01 5.52E.,OO 9.73E+o3 6.17E.,03 5.02E+OO 3.45E-01 9.76E-08 1.77Et05 1.73E-02 5 Kr-87 5.4E-Q2 3.04E-Q4 5.92E+03 1.80E+OO 1.98E+01 2.37E+03 1.52E.,04 2.58E+01 1.53E+OO 4.34E-07 1.05E+05 4.55E-02 6 Kr-88 2.4E-01 1.35E-03 1.47E+04 1.01E+04 1.73E.,04 7.70E-02 3.01E-03 8.49E-10 1.89E+o5 1.61E-Q4 7 Kr-89 4.7E-04 2.64E-Q6 1.66E+04 4.39E-02 7.29E+o3 1.63E.,04 O.OOE+oo O.OOE.,00 O.OOE+OO 1.89E+04 O.OOE+OO 8 Kr-90 O.OE+OO 0.00E+oo 1.56E+o4 0.00E.,00 4.76E+02 1.56E+02 2.70E+OO 4.73E+OO 1.34E-06 7.22E+04 9.66E-02 9 Xe-131m 7.4E-01 4.16E-03 9.15E+01 3.81E-01 9.94E+02 3.27E+o2 6.78E+OO 5.69E+OO 1.61E-06 1.28E+o5 2.06E-01 10 Xe-133111 8.9E-01 5.01E-03 2.51E+02 1.26E+oo 1.47E+o2 3.06E+02 3.53E+o2 3.4BE+02 5.69E+02 1.61E-04 4.39E+04 7.06E+OO 11 Xe-133 8.9E+o1 5.01E-01 2.94E+02 7.90E-02 7.11E+02 3.36E+o3 1.12E-01 2.SBE-02 8.13E-09 3.28E+04 2.67E-04 12 Xe-135m 4.SE-03 2.53E-05 3.12E+03 1.86E+03 1.92E+03 1.56E+01 4.4BE+OO 1.27E-06 1.37E+05 1.73E-01 13 Xe-135 7.0E-01 3.94E-03 1.81E+03 7.13E+o0 1.22E+04 1.51E-t03 7.SOE-02 6.39E-03 1.B1E-09 1.83E+05 3.31E-04 14 Xe-137 1.0E-03 5.62E-06 1.42E-t03 7.99E-03 4.13E+03 9.21E+03 1.20E-t00 9.59E-02 2.71E-08 1.43Et05 3.88E-03 15 Xe-138 1.SE-02 B.44E-05 8.83E+03 7.45E-01 2.69E+D3 3.21E-04 2.74E+01 Totals 1TE+02 1.43E+03 3.08E-Q4 secJm3 = xlQ (from ODCM procedure 112-0DC-2.02, Section B.1.1) Qt (Total Body)= 500/ (xlQ) sum (KiSi)= 1.14E+o3 uCVsec 7500 elm = Flowrate (from ODCM procedure 1/2-0DC-2.02, Section 8.1.1) Qt (Skin)= 3000/ (x/Q) sum (Li+1.1Mi)Si= 3.62E+03 uCVsec Lowest QI Value= 1.14E+03 uCVsac Ai: From ODCM procedure 112-0DC-2.02, Attachement A, Tabla 2.1-1 a) Ki, Li, & Mt From ODCM procedure 112-0DC-2.02, Attachment G, Table 2.2-11) El: From ODCM procedure 1/2-0DC-2.02, Attachment B, Table 2.1-2a) f l Efficiencies found in Mirian MCNP Analysis for NGM204 Monitor, pg 16 CR= Sum(CiEi) = 2.74E+D1 cps Eia = (CR) I (Sum Ci) = 8.54E+04 cps I uCi/ cc Conversation Factor= 1 I Ela = 1.17E-05 uCi/cc/cps Conversation Factor = 1 I Ela = 4.33E+05 Bq/m3/cps DV = CR I Ela = 3.21 E-04 uCilcc Process HHSP =((CR) x (60%: Site Noble Gas Dose Raia Limit)) I Eia 1.93E-04 uCI I cc = Process HSP 662.19 uCVsec Process HSP = ((CR) x (30%: Site Noble Gas Dose Rate Limit)) I Ela 9.64E-05 uCI I cc = Process ASP 341.10 uCVsac Note: All equations used above are from ODCM procedure 112-0DC-2.02, Section 8.1.2 Unusual Evant= 1.14E+03 uCi I sec x 2 = 2.28E+03 uCVsec Alert= 1.14E+03 uCI/ sec 200 = 2.28E+05 uCVsec

ERS-HHM-87..014 Balch Release Revision 8 Attachmant2 Unit 1 - Containment Purge VIA Rx Containment I SLCRS Vent Pathway Gaseous Effluent Monitor Page~ \I'S t&S RM-1VS-110 High _Al_ _ _ Li Mi Qi Ci El CR Nuclide Si Ki (Li+1.1Mi)Si SiQt (2. 12E-3 Ql)F CiEi Ai /Sum Ai KiSi mrem/yr mrem/yr mrem/yr mradlyr per mrem/yr amps per earuCVm3 uCVm3 eeruCVm3 ~ uCUcc uCVcc am!:!s 

                    .E!!E_                       eeruCUm3       ~ruCUm3 2.69E+03     9.30E+o3        1.82E+o3 1.60E+o2           4.52E..05       1.50E-10     6.7BE-15 1    Ar-41             2.5E+01        1.41E-01      B.84E+03      1.24E+o3 1.93E+01         2.63E..03    1.41E-01       3.98E..08      4.74E-10     1.BBE-17 i    Kr-83m            2.2E-02        1.24E-04      7.56E..02      9.35E-06      O.OOE+OO 4.58E-17 9.87E..01     1.46E+o3     1.23E+o3        2.37E+OO     9.59E-01       2.71E-07        1.69E-10 3    Kr-85m             1.SE..01      8.44E-04      1.17E+03 1.72E+o1        4.66E+02     3.90E+o2        1.10E-04       1.79E-10     1.97E-14 4    Kr-85             6.1E+01        3.43E-01      1.61E+01      5.52E+OO       1.34E+03 9.73E+03     6.17E+o3        5.02E+DO     3.45E-01        9.76E..Q8      1.0BE-10     1.05E-17 5    Kr-87             5.4E-02        3.04E-04      5.92E+o3      1.BOE+OO 2.37E+03     1.52E+04        2.5BE+01     1.53E+oo        4.34E-07       2.31E-10     1.00E-16 6    Kr-88             2.4E-01        1.35E-03      1.47E+04      1.98E+D1 1.73E+D4         7.70E-02     3.D1E-03       8.49E-10       1.77E-10     1.SOE-19 7    Kr-89              4.7E-04       2.64E-06      1.66E+04       4.39E-02      1.01E+04 7.29E+03     1.63E+04        O.OOE+OO     O.OOE+OO       O.OOE+OO        2.37E-11     O.OOE+oo 8    Kr-90             O.OE+OO        O.OOE+OO      1.56E+04      O.OOE+oO 4.76E+D2     1.56E+02        2.70E+OO     4.73E+DO        1.34E-06       2.77E-10      3.70E-16 9    Xa-131m            7.4E-01       4.16E-03      9.15E+01       3.81E..01 3.27E+D2        6.78E+OO     5,69E+o0        1.61E-06       2.27E-10      3.65E-16 10    Xa-133m            B.9E..01       5.01E-03     2.51E+o2       1.26E+OO      9.94E+02 3.53E+02        3.48E+02     5.69E+D2        1.61E-04       4.69E-10      7.87E-14 11    Xe-133            8.9E+01         5.01E-01     2.94E+02       1.47E+02      3.06E+02 7.11E+02     3.36E-+-03       1.12E-01    2.88E-02        8.13E-09       1.20E-11      9.76E-20 12    Xa-135m            4.5E-03       2.53E-05      3.12E+o3       7.90E-02 1.86E+03     1.92E-+-03      1.56E+01     4.4BE+OO        1.27E-06       1.95E-10     2.47E-16 13    Xa-135             7.0E..01       3.94E-03     1.81E+o3      7.13E+OO 1.22E+04     1.51E+-03        7.BOE-02    6.39E-03        1.81E-09       1.17E-10     2.11E-19 14    Xa-137             1.0E-03        5.62E-06     1.42E+o3       7.99E-03 4.13E+03     9.21E+03        1.20E+OO      9.59E-02       2.71E-08       1.69E-10      4.SBE-18 15    Xe-138             1.SE-02        8.44E-05     8.83E+03       7.45E-01 2.69E+D3                     3.21E-04                     1.0GE-13 Totals         1.6E+li2                                       1.43E+03 Qt (TD1al Body) = 500 I (x/Q) sum (KISI)=   1.14E+03 uCVsec 3.0BE-04     sec/m3      = x/Q (from ODCM procedure 1/2-0DC-2.02. Section 8.1.1)

Ql (Skin)= 3000 I (x/Q) sum (Li+1.1Mi)Si= 3.62E+03 uCVsec 7500 cfm = Flowrate (from ODCM procedure 112-0DC-2.02, Section 8.1.1) Lowest Qt Value = 1.14E+03 uCVsec Ai: From ODCM procedure 1/2-DDC-2.02, AttachementA, Table 2.1-1a) Ki, Li, & Mi: From ODCM procadure 1/2-0DC-2.02, Attachment G, Table 2.2-11) Ei: From ODCM procedure 112-0DC-2.02, Attachment B, Table 2.1-2a) ~Efficiencies found in Mirian MCNP Analysis for NGM204 Monitor, p916 CR= Sum(CiEI) = 1.06E-13 amps Eia= (CR)/(SumCi) = 3.31E-10 amps/uCi/cc Conversation Factor = 1 / Eia = 3.02E+09 uCi I cc I amps Conversation Factor = 1 I Eia = 1.12E+2D Bq I m3 I amps DV =CR I Eia = 3.21E-04 uCI/ cc Process HHSP =((CR) x (60%: Sita Noble Gas Dose Rate Limit)) I Ela 1.93E--04 uCi I cc= Process HSP 682.19 uCVsac Process HSP =((CR) x (30%: Site Noble Gas Dose Rate Limit)) I Eia 9.64E-05 uCi I cc= Process ASP 341.10 uCi/sec Nola : All equations used above are from ODCM procadure 1/2-0DC-2.02, Section B.1.2 Unusual Event = 1. 14E+03 uCI/ sec 2 = 2.28E+03 uCi/sac Alert= 1.14E+03 uCi I sec x 200 = 2.28E+05 uCi/sac

ERS-HHM-87-014 Batch Release Revision B Attachment2 S Unit 112 - Decay Tank Discharge VIA Process Vent Pathway Gaseous Effluent Monitor (Victoreen) page fj 11..o ctJ3 RM-1GW-10BB LI Bl Qi Cl El CR Nuclide Ai SI VI (Li(X/Q)+1.1Bi)SI SI Qt (2.12E-3 Ql)Jf Ci El Al/Sum Ai VISi mrem/yr mremtyr mradlyr mrem/yr cpm mremlyr per per per per per per uCilm3 uCVsec uCi/sec uCi/sec uCi/cc uCVcc cpm Cl/yr uCl/sec uCl/sec 4.02E-D3 D.DOE+OO O.OOE+OO o.OOE+OO 6.59E+D7 O.OOE+OO 1 Ar-41 O.DE+OO O.OOE+OO 2.BBE-03 O.OOE+OO 2.69E+03 3.96E-05 O.OOE+OO O.ODE+OO O.OOE+OO D.OOE+OO O.OOE+OO 2 Kr-B3m O.OE+OO O.OOE+OO 4.58E-D8 0.00E+OD O.OOE+OO 7.06E-04 4.71E-06 6.46E+01 9.44E-05 9.00E+07 6.60E+03 3Kr~m 7.3E-02 2.87E-04 4.70E-04 1.35E-D7 1.46E+03 B.40E-06 1.30E-02 2.04E+05 2.98E-01 3.56E+05 1.06E+D5 4 Kr-BS 2.3E+02 9.04E-01 5.54E-ll6 5.01E-06 1.34E+03 9.73E+03 2.19E-03 O.OOE+OO O.OOE+OO O.OOE+OD 6.78E+07 O.OOE+DO 5 Kr-87 D.OE+OO O.OOE+DO 1.45E-03 0.0DE+OO 6.16E-03 0.00E+OD O.OOE+OO O.OOE+OO 1.05E+OB O.OOE+DO 6 Kr-88 0.0E+OO O.OOE+DO 4.09E-03 0.0DE+OO 2.37E+03 1.BSE-03 O.OOE+OO O.OOE+OO O.OOE+OO 1.2BE+08 O.OOE+OO 7 Kr-89 O.OE+OO O.OOE+OO 1.25E-03 O.OOE+OO 1.01E+04 O.OOE+OD O.OOE+OO O.OOE+OO 0.00E+OO 1.23E+08 O.OOE+OO 8 Kr-90 O.OE+OO O.OOE+OO O.OOE+OO O,OOE+OO 7.29E+03 3.09E-04 2.78E-05 1.15E+03 1.68E-03 2.07E+06 3.48E+D3 9 Xe-131m 1.3E+OD 5.11E-03 1.67E-04 8.53E-07 4.76E+02 2.61E-04 O.ODE+OO O.OOE+OO O.OOE+OO 1.16E+07 O.OOE+OO 10 Xa-133m 0.0E+OO D.OOE+OO 1.32E-04 O.ODE+OO 9.94E+02 2.76E-D4 3.23E-04 2.04E+04 2.98E-02 9.24E+06 2.75E-tD5 11 Xe-133 2.3E+01 9.04E-02 1.54E-04 1.39E-05 3.06E+02 9.SOE-04 O.OOE+OO D.OOE+OO O.ODE+OO 6.58E+07 0.00E+OO 12 Xe-135m O.OE+OO 0.00E+OO 6.21E-04 O.ODE+OO 7.11E+02 1.86E+03 1.0SE-03 O.OOE+OO 0.0DE+OD D.ODE+OD 1.03E+OB O.ODE+OD 13 Xe-135 O.OE+OO O.OOE+OO 6.96E-04 0.0DE+OO 1.22E+D4 1.46E-04 D.OOE+OO 0.0DE+OO O.ODE+OD 2.91E+07 O.ODE+OO 14 Xe-137 0.0E+OO O.OOE+OO 9.66E-05 0.DOE+OD 4.13E+03 3.34E-03 O.OOE+OO O.OOE+OO 0.00E+OO 1.06E+08 O.OOE+OO 15 Xe-138 O.OE+OO O.OOE+OO 2.22E--03 O.OOE-tOO 1.33E-02 3.29E-01 3.93E+05 Totals = 2.5E+02 1.99E-05 1.07E-05 sec/rn3 = x/Q (From ODCM procedure 1/2-0DC-2.02, Section 8.1.3) = Qt(Total Body) 500/sum(VISi) = 2.51E*07 uCVsec 2.25E+05 uCVsec 1450 ctm = Flowrate (From ODCM procadure 1/2-0DC-2.02, Section 6.1.3) Ql(Skln) = 3000/sum(Li(X/Q)'+1.1Bi)SI = Lowest Qt Value 2.25E+05 uCVsec Ai: From ODCM procedure 1/2-0DC-2.02, Attachment A, Table 2.1-1a VI & Bi: From ODCM procedure 1/2-0DC-2.02, Attachment G, Table2.2-12 (3) Li: From ODCM procedure 1/2-0DC-2.02, Attachment G, Table 2.2-11 Ei: From ODCM procedure 1/2-0DC-2.02, Attachment 8, Table 2.1-2* CR= Sum(CIEI) = 3.93E+05 cpm = CR HHSP =(CR x 0.6) 'Mlere;'0.6 = 60% of lhe Site Noble Gas Dose Rate Limit= 2.36E+05 cpm = Process HHSP HSP = (CR x 0.3) Wiere; 0.3 = 30% of the Site Noble Gas Dose Rate Umlt = 1.18E+05 cpm= Process HSP NOTE: All equations used above are from ODCM procedure 112-0DC-2.02, Secijon 8.1.3 Trip -HHSP= 2.36E+05 1(1 + ,35+ .10) = 1.63E+05 cpm Trip -HSP= 1.18E+05 I (1 + .35 + .10) = 6.13E+04 cpm

Batch Release ERS-HHM-87--014 Revision 8 Unit 1 - Decay Tank Discharge VIA Process Vent Pathway Gaseous Effluent Monitor Attachment 2 Page P'.J l1- O f 6,S RM-1GW-109 Low Nuclide Al Si VI Li Bl Qi Cl Ei CR Ai/SumAI Vi Si {Li(x/Q)+1.1 Bl)SI SI Qt (2.12E-3 Ql)/F CIEi mrern/yr mrad/yr mremlyr mrern/yr per mrern/yr per per cps per Cl!:ir eeruCilm3 uCl/m3 eeruCi/m3 ~ ~ uCi/sec uCi/cc uCi/cc cps Ar-41 O.OE+OO O.OOE+OO 2.BSE-03 O.OOE+OO 2.69E.,03 4.02E-03 O.OOE+oo 0.00E+OO O.OOE+OO 1.60E+05 O.OOE+OO 2 Kr-83m O.OE+OO O.OOE+OO 4.58E-08 O.OOE+OO 0.00E+OO 3.96E-05 O.OOE+OO O.OOE+OO O.OOE+OO O.OOE+OO 0.00E+OO 3 Kr-85m 7.3E-02 2.B7E-04 4.70E-04 1.35E-07 1.46E.,03 7.0SE--04 4.71E-06 6.46E+01 9.44E--05 1.14E+05 1.08E+01 4 Kr-85 2.3E+02 9.04E-01 5.54E-06 5.01E-06 1.34E+03 8.40E-06 1.30E-02 2.04E+05 2.98E-01 1.14E+05 3.39E+04 5 Kr-87 O.OE+OO O.OOE+OO 1.45E-03 O.OOE+OO 9.73E+03 2.19E-03 O.OOE+OO O.OOE+OO O.OOE+OO 1.77E+05 O.OOE+OO 6 Kr-88 O.OE+OO O.OOE+OO 4.09E-03 O.OOE+OO 2.37E+03 8.16E-03 O.OOE+OO O.OOE+OO O.OOE+OO 1.0SE+OS O.OOE+OO 7 Kr-89 O.OE+OO 0.00E+OO 1.25E-03 O.OOE+OO 1.01E+04 1.BBE-03 0.00E+OO O.OOE+OO O.OOE+OO 1.B9E+05 0.00E+OO 8 Kr-90 O.OE+OO O.OOE+OO O.OOE+OO O.OOE+OO 7.29E+03 0.00E+OO O.OOE+OO O.OOE+OO O.OOE+OO 1.89E+04 O.OOE+OO 9 Xe-131m 1.3E+OO 5.11E-03 1.67E-04 8.53E-07 4.76E+02 3.09E-04 2.78E-05 1.15E+03 1.BBE-03 7.22E+04 1.21E+02 10 Xe-133m O.OE+OO O.OOE+OO 1.32E-04 O.OOE+OO 9.94E+02 2.61E-04 O.OOE+OO O.OOE+OO O.OOE+oo 1.28E+05 0.00E+OO 11 Xe-133 2.3E+01 9.04E-02 1.54E*04 1.39E-05 3.06E+02 2.76E-04 3.23E-04 2.04E->04 2.9BE--02 4.39E+04 1.31E+03 12 Xe-135m O.OE+OO O.OOE+OD 6.21E-04 O.OOE+OO 7.11E+02 9.SOE-04 0.00E+OO O.OOE+OO O.OOE+OO 3,28E+04 O.OOE+OO 13 Xe-135 O.OE+OO O.OOE+oo 6.96E-04 O.OOE+OO 1.86E+03 1.0SE-03 O.OOE+OO O.OOE+OO O.OOE+OO 1.37E+05 O.OOE+OO 14 Xe-137 O.OE+OO O.OOE+OO 9.66E--05 O.OOE+OO 1.22E+04 1.46E-04 O.OOE+OO O.OOE+OO O.OOE+OO 1.83E+05 O.OOE+OO 15 Xe-138 O.OE+OO O.OOE+OO 2.22E-03 O.OOE+OO 4.13E+03 3.34E-03 O.OOE+oo O.OOE+OO O.OOE+OO 1.43E+05 O.OOE+OO Totals 2.5E+02 1.99E-05 1.33E-02 

                                                                                                                     ----             3.29E-01                   3.54E+04 1.07E-05    sec/m3      = x/Q (from ODCM procedure 1/2-0DC-2.02, Section 8.1.3)                                      Qt (Total Body)= 500 I sum(ViSi) = 2.51E+07 uCl/sec 1450    cfm         = Flowrate (from ODCM procedure 1/2-0DC-2.02, Section B.1.3)                          Qt (Skin)= 3000 I sum(Li(x/Q) + 1.1Bl)SI = 2.25E+05 uCi/sec Lowest Qt Value = 2.25E+05 uCl/sec Al: From ODCM procedure 1/2-0DC-2.02, Attachement A, Table 2.1-1a)

Vi & Bi: From ODCM procedure 1/2-0DC-2.02, Attachment G, Table 2.2-12) Li: From ODCM procedure 1/2-0DC-2.02, Allachment G, Table 2.2-11) Ei: From ODCM procedure 1/2-0DC-2.02, Attachment B, Tabla 2.1-2a)-Efficiencies found in Minon MCNP Analysis for NGM204 Monitor, pg 16 CR= Sum(CIEi) = 3.54E+04 cps Eia = (CR) I (Sum Cl) = 1.07E+05 cps luCi I cc ConverseUon Factor= 1 / Eia = 9.31 E-06 uCI I CC/ cps Conversation Factor c 11 Ela = 3.44E+05 Bq /rn3 /cps DV = CR I Ela = 3.29E-01 uCl/cc Process HHSP = ((CR) x (60%: Site Noble Gas Dose Rate Limit)) I Eia 1.97E-01 uCI I cc = Process HSP 135048.79 uCi/sec Process HSP = ((CR) x (30%: Site Noble Gas Dose Rale Limit)) I Ela 9.87E-02 uCI I cc = Process ASP 67524.39 uCllsec Note : All equations used above are from ODCM procedure 1/2-0DC-2.02, Section 8.1.2

Batch Release ERS-HHM-87-014 Revision 8 Unit 1 - Decay Tank DIScharga VIA Process Vent Pathway Gaseous Effluent Monitor Attachment 2 RM-1GW-109 High Page~ l'b~~6 _A_I_ _ _ _LI_ _ _ 

     ~                           SI            Vi                                      Bl                           Qi             Ci            El           CR Al I Sum Ai
                                              ---- ~        ~                          mrad/yr (Ll(x/Q)+1.1 Bi)Si mrem/yr Si Qt          (2.12E.J 01)/F             CIEi mrem/yr       per         mrem/yr       per            per                                        amp per
                  .9!l!._                      ~ruCVm3      ~            peruCl/m3     uCVmJ         ~ ~ ~ .!!9!!£_ ame:s 1   Ar-41           0.0E+OO      O.OOE+OO        2.68E-03    O.OOE+OO     2.69E+03      4.02E-03      O.OOE+OO      O.OOE+OO       O.OOE+OO      1.50E-10       0.00E+OO 2   Kr-B3m          0.0E+OO      0.00E+OO       4.5'1E-08    0.00E+OO     O.OOE+OO     3.96E-05       0.00E+OO      0.00E+OO       0.00E+OO      4.74E-10       O.OOE+OO 3   Kr~m             7.3E-02     2.87E-04       4.70E-04      1.35E-07    1.46E+03      7.00E-04       4.71E-06     6.46E+01        9.44E-05     1.69E-10        1.SOE-14 4   Kr-85           2.3E+02      9.04E-01       5.54E-06     5.01E-06     1.34E+03     8.40E-06        1.30E-02     2.04E+05        2.98E-01     1.79E-10        5.33E-11 5   Kr-87           0.0E+OO      O.OOE+OO       1.45E-03     O.OOE+OO     9,73E+03     2.19E-03       O.OOE+OO      O.OOE+OO       0.00E+OO      1.0BE-10       O.OOE+OO 6   Kr-88           0.0E+OO      O.OOE+OO       4.09E-03     0.00E+OO     2.37E+03     6.16E-03       O.OOE+OO      O.OOE+OO       0.00E+OO      2.31E-10       0.00E+OO 7   Kr-89           0.0E+OO      O.OOE+OO       125E-03     0.00E+OO      1.01E+04     1.88E-03       O.OOE+OO      O.OOEtOO       O.OOE+OO      1.77E-10      0.00E+OO 8   Kr-90           0.0E+OO      O.OOE+OO      O.OOE+OO     0.00E+OO      7.29E+03     O.OOE+OO       O.OOE+OO      O.OOE+OO       O.OOE+OO      2.37E-11      O.OOE+OO 9   Xe-131m        1.3E+OO       5.11E-03      1.67E-04      B.53E-07     4.76E+02     3.09E-04        2.7BE-05     1.15E+03        1.6BE-03     2.77E-10       4.66E-13 10    Xe-133m        O.OE+OO      O.OOE+OO       1.32E-04     0.00E+OO      9.94E+02     2.61E-04       O.OOE+OO     O.OOE+OO        O.OOE,.00     2.27E-10      O.OOE+OO 11    Xe-133         2.3E+01       9.04E-02      1.54E-04      1.39E-05     3.06E+02     2.76E-04       3.23E-04     2.04E+04         2.9BE-02     4.89E-10       1.46E-11 12   Xe-135m         O.OE+OO      O.OOE+OO       6.21E-04     0.00E+OO     7.11E+02      9.50E-04       O.OOE+OO     O.OOE+OO        0.00E+OO      1.20E-11      0.00E+OO 13   Xe-135          0.0E+OO      O.OOE+OO       6.98E-04     0.00E+OO     1.B6E+03      1.0SE-03       O.OOE+OO     O.OOE+OO        0.00E+OO      1.95E-10      O.OOE+OO 14   Xe-137          0.0E+OO      O.OOE+OO       9.66E-05     0.00E+OO     1.22E+04      1.46E-04       O.OOE+OO     O.OOE+OO        0.00E+OO      1.17E-10      0.00E+OO 15   Xe-138          0.0E+OO      O.OOE+OO       2.22E-03     0,00E+OO     4.13E+03      3.34E-03      O.OOE+OO      O.OOE+OO        O.OOE+OO      1.69E-10      0.00E+OO
    ~=              2.5E+02                  ----          ~                                         ~                              3.29E-01                     6.83E-11 1.07E-05    seclm3      = x/Q (ficm ODCM procedure 1/2-0DC-2.02, Section B.1.3)                                    Qt (Total Body) = 500 I sum(ViSi) =    2.51 E+07 uCi/sec 1450   cfm         = Flowrate (from ODCM procedure 1/2-0DC-2.02, SecUon 8.1.3)                         Qt(Skln)= 3000/sum(Ll(x/Q) + 1.1BQSi =        2.25E+05 uCVsec Lowest Qt Value =    2.25E+05 uCVsec Ai: From ODCM procedure 1/2-0DC-2.02, Attachament A, Table 2.1-1 a)

Vi & Bi: From ODCM procedure 1/2-0DC-2.02, Attachment G, Tabla 2.2-12) Li: From ODCM procedure 1/2-0DC-2.02, AttachmentG, Table 2.2:11) Ei: From ODCM procedure 1/2-0DC-2.02, Attachment B, Table 2.1 *2a) .. Efficiencies found In Minon MCNP Analysis for NGM204 Monitor, pg 16 CR= Sum(CiEI) = 6.83E-11 amps Ela= (CR) I (Sum Ci) = 2.08E-10 amp/uCl/cc Conversauon Factor= 11 Ela = 4.82E+09 uCl/cc/ amp Conversation Factor= 1 /Ela = 1.7BE+20 Bq/m3/amp DV = CR I Ela = 3.29E-01 uCi/cc Process HHSP =((CR) X (60%: Sile Noble Gas Dose Rate Umlt)) I Ela 1.97E-01 uCI I cc= Process HSP 135048.79 UCl/sac Process HSP = ((CR) x (30%: Site Noble Gas Dose Rate Umlt)) I Ela 9.B7E-02 uCi I cc= Process ASP 67524.39 uCJ/sec Note: All equations used above are from ODCM procedure 1/2-0DC-2.02, Section B.1.2

Batch Release ERS-HHM-87-014 Revision B Unit 2 - Conlainment Purge VIA SLCRS Unfiltered Pathway Gaseous Effluent Monitor Attachment 2 2HVS-RQ1018 page ,q '{) ~S Nuclide Al SI Kl Li Ml Qi Cl Ei CR AUSumAI KiSI (Ll+1.1Ml)SI Si Qt (2.12E-3 Ql)/F Ci El mremlyr mram/yr mrem/yr mrad/yr mrem/yr cpm per per per per per per CliYr uCl/m3 UCi/m3 uCi/m3 uClhn3 uCl/m3 uCJ/sec uCi/cc uCVcc cpm - -w*-.-..* 1 Ar-41 2.5E+01 1.46E-01 8.B4E+03 1.29E+03 2.69E+03 9.30E+03 1.88E+03 1.52Et02 1.0SE-05 3.79E+07 4,08E+02 2 Kr-83m 4.0E-05 2.33E-07 7.56E-02 1.76E-OB O.OOE+OO 1.93E+01 4.94E-06 2.43E-04 1.72E-11 O.OOE+OO O,OOE+OO 3 Kr-85m 1.4E-02 8.15E-05 1.17E+03 9.54E-02 1.46E+03 1.23E+03 2.29E-01 8.52E-02 6.02E-09 3.20E+07 1.93E-01 4 Kr-85 6.1E+01 3.55E-01 1.61E+01 5.72E+OO 1.34E+03 1.72E+01 4.83E+02 3.71E+02 2.62E-05 3.60E+07 9.44E+02 5 Kr-87 5.3E-06 3.0SE-08 5.92E+03 1.83E-04 9.73E+03 6.17E+03 5.10E-04 3.23E-05 2.28E-12 3.73E+07 8.50E-05 6 Kr-88 4.1E-03 2.39E-05 1.47E+04 3.51E-01 2.37Et03 1.52E+04 4.56E-01 2.50E-02 1.76E-09 3.05E+07 5.38E*02 7 Kr-89 0.0E+OO O.OOE+DO 1.66E+04 0.DOE+OO 1.01E+04 1.73E+04 O.OOE+OO O.OOE+OO O.OOE~DO 3.72E+07 O.OOE+DO B Kr-90 0.0E+OO O.OOE+DO 1.56E+04 0.00E+OO 7.29E+03 1.63E+04 O.OOE+OO 0.00E+OO O.OOE+DO 3.86E+07 O.DOE+DO 9 Xe-131m 7.2E-01 4.19E-03 9.15E+01 3.B4E-01 4.76E+02 1.56E+02 2.72E+OO 4.3BE+OO 3.10E-07 2.44E+07 7.56E+OO 10 Xe-133m 7.6E-01 4.43E-03 2.51E+02 1.11E+OO 9.94E+02 3.27E+02 5.99E+OO 4.63E+OO 3.27E-07 2.86E+07 9.35E+DO 11 Xe-133 B.4E+01 4.89E-01 2.94E+02 1.44E+02 3.06E+02 3.53E+02 3.4DE+02 5.11E+02 3.61E-05 1.80E+07 6.50E+02 12 Xe-135m O.OE+OO O.OOE+DO 3.12E+03 O.OOE+OO 7.11E+02 3.36E+03 O.OOE+OO O.OOE+OO O.OOE+OO 7.22E+06 O.OOE+DO 13 Xe-135 2.4E-01 1.40E-03 1.B1E+03 2.53E+DO 1.B6E+03 1.92E+03 5.55E+OO 1.46E+OO 1.03E-07 3.86E+07 3.98E+DO 14 Xe-137 O.OE+OO O.OOE+OO 1.42E+03 O.OOE+OO 1.22E+04 1.51E+03 O.OOE+OO O.OOE+OO O.OOE+DO 3.7BE+07 O.OOE+OO 15 Xe-138 O.OE+OO O.OOE+OO 8.83E+03 0.00E+OO 4.13E+03 9.21E+03 O.OOE+OO O.OOE+OO O.OOE+OO 3.52E+07 O.OOE+OO Totals = 1.7E+02 1.44E+03 2.72E+03 7.39E-05 2.02E+03 3.32E-04 sac/m3= x/Q (From ODCM procedure 112-0DC-2.02, Seclion B.1.2) Q1[rotal Body)= 500/(x/Q) sum(KiSI) = 1.0SE.,.03 uCi/sec 30000 cfm = Flowrate (From ODCM procedure 112-0DC-2.02, Section B.1.2) Qt(Skln) = 3000/(x/Q) sum(Ll+1.1 Mi)SI = 3.32E+03 uCVeec Lowest 01 Value 1.05E+03 uCVsec Al: From ODCM procedure 1/2-0DC-2.02, Attachment A, Table 2.1-1b Ki.Li & Mi: From ODCM procedure 1/2-0DC-2.02, Attachment G, Table 2.2-11 El: From ODCM procedure 112-0DC-2.02, Attachment B, Table 2.1*2b CR= Sum(CIEI) = 2.02E+03 cpm Eia = (CR) I (Sum Cl) = 2.74E+07 cpm/UCi/cc Converalon Faclor = 1 I Eia = 3.65E-OB uCi/oclcpm DV=CR/Ela= 7.39E-05 UCl/cc Process HSP = ((CR) x (60%: Site Noble Gas Dose Rate Limit)) I Ela= 4.43E-05 UCl/cc = Process HSP Process ASP =((CR) x (30%: Site Noble Gas Dose Rate Umll)) I Ela= 2.22E-05 UCilcc = Process ASP NOTE: All equations used above are from ODCM procedure 1/2-0DC-2.02, Section 8.1.2 Trip -HSP= 4.43E-05 /(1 + .35+ .10) = 3.06E-05 uCi/cc Trip -ASP= 2.22E-05 /(1 + ,35+ .10) = 1.53E-05 uCVcc

Batch Release ERS-HHM-87-014 Revision B Unit 2 - Containment Purge VIA SLCRS Fntered Pathway Gaseous Effluent Monttor Anachment 2 f5' 2HVS-RQ1098 page p~ 2o 'b 3. Nuctida /'J SI Kl Li Mi Qi Cl El CR AVSumAi Ki Si (Li+1.1Ml)SI SI Qt (2.12E-3 Ql)/F CiEi mrem/yr mrem/yr mrem/yr mrad/yr mremlyr cpm per per par par per per Cl/yr uCi/m3 UCl/m3 uCi/m3 uCi/m3 uCl/m3 uCi/sec ucvcc uCVcc cpm 1 Ar-41 2.SE+01 1.46E-01 8.84E+03 1.29E+03 2.69E+03 9.30E+03 1.B8E+03 1.84E+02 4.64E-05 7.90E+07 3.66E+03 2 Kr-B3m 4.0E-05 2.33E-07 7.56E-02 1.76E-08 0.00E+OO 1.93E+01 4.94E-06 2.62E-04 7.42E-11 O.OOE+OO O.OOE+OO 3 Kr-85m 1.4E-02 B.15E-05 1.17E+03 9.54E-02 1.46E+03 1.23E+03 2.29E-01 9.18E-02 2.60E-08 5.83E+07 1.51E+OO 4 Kr-65 6.1E+01 3.55E-01 1.61E+01 5.72E+OO 1.34E+03 1.72E+01 4.83E+02 4.00E+02 1.13E-04 7.19E+07 8.13E+03 5 Kr-87 5.3E-06 3.09E-08 5.92E+03 1.83E-04 9.73E+03 6.17E+03 5.10E-04 3.48E-05 9.83E-12 8.85E+D7 8.70E-04 6 Kr-88 4.1E-03 2.39E-05 1.47E+04 3.51E-01 2.37E+03 1.52E+04 4.56E-D1 2.69E--02 7.60E-09 6.80E+D7 5.17E-01 7 Kr-89 O.OE+OO 0.00E+OO 1.66E+04 O.OOE+OO 1.01E+04 1.73E+04 O.OOE+OO O.OOE+OO O.OOE+OO 8.73E+07 O.OOE+OO 8 Kr-00 O.OE+OO O.OOE+OO 1.56E+04 0.00E+OO 7.29E+03 1.63E+04 O.OOE-tOO O.OOE+OO O.OOE+OO 8.BOE+07 O.OOE+OO 9 Xe-131m 7.2E-01 4.19E-03 9.15E+01 3.84E-01 4.76E+02 1.56E+02 2.72E+OO 4.72E+OO 1.34E-06 4.61E+04 6.16E-02 10 Xa-133m 7.BE-01 4.43E-03 2.51E+02 1.11E+OO 9.94E+02 3.27E+02 5.99E+OO 4.99E+OO 1.41E-06 6.06E+04 8.54E-02 11 Xe-133 B.4E+01 4.69E-01 2.94E+02 1.44E+02 3.06E+02 3.53E+02 3.40E+02 5.51E+02 1.56E-04 2.94E+07 4.58E+03 12 Xe-135m O.OE+OO 0.00E+OO 3.12E+03 O.OOE+OO 7.11E+02 3.36E+03 O.OOE-tOO 0.00E+OO O.OOE+OO 1.55E+04 O.OOE+OO 13 Xe-135 2.4E-01 1.40E-03 1.81E+03 2.53E+OO 1.86E+03 1.92E+03 5.55E+OO 1.57E+OO 4.45E-07 7.48E+07 3.33E+01 14 Xe-137 O.OE+OO O.OOE+OO 1.42E+03 O.OOE+OO 1.22E+04 1.51E+03 O.DOE+oo O.OOE+OO O.OOE+OO 9.07E+07 O.OOE+OO 15 Xe-138 O.OE+OO O.OOE+OO 8.83E+03 0.00E+OO 4.13E+03 9.21E+03 O.OOE+OO O.OOE+OO O.OOE+OO 7.74E+07 O.OOE+OO Totals= 1.7E+02 1.44E+03 2.72E+03 3.18E-04 1.64E+04 3.0BE-04 serJm3 = x/Q (From ODCM procedure 112-0DC-2.02, Section 8.1.2) Qt(Total Body)= 500/(xlQ) sum(KiSi) = 1.13E+03 uCVsec 7500 cfm = Flowrate (From ODCM procedure 1/2-0DC-2.02, Section 8.1.2) Qt(Skin) = 3000/(x/Q} sum(Ll+1.1Ml}SI = 3.58E+03 uCilsec Lowest Qt Value 1.13E+03 uCVsec Al: From ODCM procedure 1/2-0DC-2.02, Attachment A, Table2.1-1b Kl,LI & Ml: From ODCM procedure 112-0DC-2.02, Attachment G, Table 2.2-11 Ei: From ODCM procedure 112-0DC-2.02, Attachment B, Table 2.1-2b CR= Sum(CiEi) = 1.64E+04 cpm Ela= (CR} I (Sum Ci)= 5.15E+07 cpm/UCi/cc Conversion Factor= 1 I Ela= 1.94E--08 UCl/cc/cpm DY= CR/Eia= 3.18E-04 UCt/cc Process HSP =((CR) x (60%: Site Noble Gas Dose Rate Limit))/ Ela= 1.91 E-04 UCt/cc = Process HSP 6. 76E+02 uCVaec Process ASP= ((CR) x (30%: Site Noble Gas Dose Raio Limit)) I Eia = 9.55E--05 UC!lcc = Process ASP 3.36E+02 uCVsec NOTE: All equations used above are from ODCM procedure 112-0DC-2.02, Section B.1.2 Tr1p -HSP= 1.91E-04 /(1 + .35 + .10) = 1.32E-04 uCl/cc =Trip HSP = 4.86E+02 uCl/sec Trip -ASP= 9.SSE-05 I (1 + .35 + .10) = 6.59E-05 uCi/cc = Trip ASP = 2.33E+02 uCl/sec

Continuous Release ERS-HHM-87-014 Revisicn8 Unil 1 - Ventilation Vent Palhway Gaseous Effluent Monitor (Vlc1oreen) Attachment~ page ;;).\ RM-1VS-1018 SI Kl Li Mi QI Cl Ei CR Nudide Al KISI (Li+1.1Mi)Si SiQt (2.12E-3 Ql)/F CiEI Ai/Sum Ai mrem/yr mrem/yr mrem/yr mradlyr mrem/)lr cpm per per per per per per uCl/m3 uCVm3 uCi/m3 uCi/m3 uCUm3 uCVsec uCi/cc uCi/cc cpm Ci/yr 8.84E+03 O.OOE+OO 2.69E+03 9.30E+03 0.00E+OO O.OOE+OO O.OOE+OO 7.17E+07 O.OOE+OO 1 Ar-41 O.OE+OO O.OOE+OO 7.SOE--03 7.SSE-02 5.B7E--04 O.OOE+OO 1.93E+01 1.68E-01 2.09E+01 7.13E-07 O.OOE+OO o.ooe+oo 2 Kr-63m 4.2E-01 3.57E-02 1.17E+03 4.18E+01 1.46E+03 1.23E+03 1.00E+02 9.43E+01 3.23E-06 9.80E+07 3.16E+02 3 Kr-65m 1.9E+OO 4 Kr-85 2.5E+OO 4.70E-02 1.61E+01 7.57E-01 1.34E+03 1.72E+01 6.39E+01 1.24E+02 4.24E-06 3.88E+05 1.85E+OO 5 Kr-87 1.3E+OO 2.44E-02 5.B2E+03 1.45E+02 9.73E+D3 6.17E+03 4.04E+02. 6.45E+01 2.21E-06 7.38E+07 1.63E+02 6 Kr-88 3.8E+OO 7.14E-02 1.47E+04 1.05E+03 2.37E+03 1.52E+04 1.36E+03 1.89E+02 6.45E-06 1.14E+OB 7.35E+02 7 Kr-89 2.26E-o3 1.66E+04 3.75E+01 1.01E+04 1.73E+04 6.57E+01 5.96E+OO 2.04E-07 1.39E+08 2.83E+01 1.2E-01 O.OE+OO o.OOE+OO 1.56E+04 O.OOE+OO 7.29E+03 1.63E+04 O.OOE+OO O.OOE+OO O.OOE+OO 1.34E+08 O.OOE+OO 8 Kr-90 1.3E-01 2.44E-03 9.15E+01 2.24E-01 4.76E+02 1.56E+02 1.5BE+OO 6.45E+OO 2.21E-07 2.25E+06 4.97E-01 9 Xe-131m B.9E-01 1.67E-02 2.51E+02 4.20E+OO 9.94E+02 3.27E+02 2.27E+01 4.42E+D1 1.51E-06 1.28E+07 1.90E+01 10 Xe-133m 3.8E+01 6.77E-01 2.94E+02 1.99E+02 3.06E+02 3.53E+02 4.70E+02 1.79E+03 6.11E-05 1.01E+07 6.17E+02 11 Xe-133 6.02E-03 3.12E+03 1.88E+01 7.11E+02 3.36E+03 2.65E+01 1.59E+01 5.43E-07 7.15E+07 3.88E+01 12 Xe-135m 3.2E-01 B.46E-02 1.81E+03 1.53E+02 1.86E+03 1.92E*03 3.36E+02 2.23E+02 7.64E-06 1.12E+OB 8.56E+02 13 Xe-135 4.5E+OO 3.95E-03 1.42E+03 5.61E+OO 1.22E+D4 1.51E+03 5.47E+01 1.D4E+01 3.56E-07 3.16E+07 1.13E+01 14 Xe-137 2.1E-01 1.1E+OO 2.07E-02 8.83E+03 1.83E+02 4.13E+03 9.21E*03 2.95E+02 5.46E+01 1.87E-06 1.15E+08 2.15E+02 15 Xe-138 5.3E+01 1.84E+03 3.20E+03 9.03E-05 3.00E+03 Totals = 1.03E-04 sec/m3 = x/Q (From ODCM procedure 1'2-0DC-2.02, Section B.1.1) Ql(Total Body)= 500/(xlQ) sum(KISI) = 2.64E+03 uCl/sec 62000 cfm = Flowrate (From ODCM procedure 1'2-0DC-2.02, Section 8.1.1) Ql(Skln) = 3000/(xlQ) sum(Li+1.1 Mi)Si = 9.09E+03 UCl/sec Lowest Qt Value 2.64E+03 UCiloec Al: From ODCM procedure 1f2*0DC-2.D2, Attachment A, Table 2.1-1a Kl,LI & Ml: From ODCM procedure 1'2-0DC-2.02, Attachment G, Table 2.2-11 Ei: From ODCM procedure 1'2-0DC-2.02, Attachment B, Table2.1-2a CR= sum(CIEl) = 3.00E+03 cpm =CR HHSP = (CR x o.8) 'Mlere; 0.6 = 60% of the Site Noble Gas Dose Rate Limit= 1.80E+03 cpm =Process HHSP HSP =(CR x 0.3) Wtere; 0.3 = 30% of the Site Noble Gas Dose Raia Limit= = 9.00E+02 cpm Process HSP NOTE: All equations used above are from ODCM procedure 112-0DC-2.02, Section B.1.1 Trip -HHSP= 1.80E+03 /(1 + .35+ .10)= 1.24E+03 cpm Trip -HSP= 9.00E+02 I (1 + .35 + .10) = 6.21E+02 cpm

Continuous Release ERS-HH~?-014 Revision B Unit 1 - Ventilation Vent Pathway Gaseous Effluent Monitor Attachment 3 o-\ RM-1VS-109 low Page ;;):;} 35 

     ~ N                            Si            Kl                           Li           Mi                           Qi             Ci             Ei             CR Ai/Sum Ai                     KiSi                                     lli+1.1Mi)Si SiQt            (2.12E-3 Qi)F                 CiEi mremlyr        mrem/yr       mrem/yr      mrad/yrper    mrem/yr                                      cps per
                     ~                            eeruCUm3       eeruCUm3      ~ruCVm3      uCVm3          eeruCUm3 uCVsec              ucvcc          uCVcc Ar-41              0.0E+oO       O.OOE+oO      8.84E+o3        0.00E+OO      2.69E+o3    9.30E+o3        O.OOE+OO     0.00E+oo       O.OOE+OO        1.60E+o5
                                                                                                                                                                      ~*O.OOE+OO 2     Kr-<i3m            4.2E-01       7.90E-03      7.56E-02        5.97E-04     0.00E+oo    1.93E+o1         1.68E-01    2.09E+01        7.13E-07      O.OOE+oo         0.00E+OO 3     Kr-llSm           1.9E+OO        3.57E-02     1.17E+o3        4.1BE+Ot      1.46E+o3    1.23E+o3        1.00E+02     9.43E+01        3.23E-06      1.14E+o5         3.68E-01 4     Kr-85            2.5E+OO         4.?0E-02     1.61E+o1        7.57E-01      1.34E+o3    1.72E+01        6.39E+01     1.24E+02        4.24E-06      1.14E+05         4.B4E-01 5     Kr-87             1.3E+oo        2.44E-02     5.92E+o3        1.45E+02      9.73E+03   6.17E+o3         4.04E+02     6.45E+01        2.21E-06      1.77E+-05        3.91E-01 6    Kr-ll6            3.8E+OO         7.14E-02     1.47E+04       1.05E+03      2.37E+03     1.52E+o4        1.36E+03     1.B9E+02        6.45E-06      1.0SE+-05        6.77E-01 7    Kr-89               1.2E-01       2.26E-03     1.66E+04       3.75E+01      1.01E+04     1.73E+04        6.57E+01     5.96E+oo        2.04E-07      1.89E+o5         3.85E-02 B    Kr-90             O.OE+OO        0.00E+-00     1.58E+04       O.OOE+OO      7.29E+o3    1.63E+04         O.OOE+OO     O.OOE+OO       0.00E+OO       1.89E+04        O.OOE+OO 9    Xe-131m             1.3E-01       2.44E-03     9.15E+01        2.24E-01     4.76E+o2    1.56E+02         1.58E+OO     6.45E+o0        2.21E-07      7.22E+04         1.59E-02 10    Xe-133m            8.9E-01        1.67E-02     2.51E+02       4.20E+OO      9.94E+o2    3.27E+o2         2.27E-+01    4.42E+01        1.51E-06      1.2BE+05         1.93E-01 11    Xe-133            3.6E+01         6.77E-01     2.94E+02       1.99E+o2      3.06E+02    3.53E+02         4.70E+02     1.79E+03        6.11E-05      4.39E+04        2.6BE+oo 12    Xe-135m            3.2E-01       6.02E-03      3.12E+03       1.BBE+o1      7.11E+o2    3.36E+03        2.65E+01      1.59E+o1        5.43E-07      3.2BE+04         1.7BE-02 13    Xe-135            4.5E+o0         8.46E-02     1.81E+03       1.53E+02      1.86E+o3    1.92E+03         3.36E+02     2.23E+o2        7.64E-06      1.37E+o5        1.DSE+oo 14    Xe-137             2.1E-01       3.95E-03      1.42E+03       5.61E+OO      1.22E+04    1.51E+03        5.47E+o1      1.04E+01       3.56E-07       1.83E+o5         6.52E-02 15    Xe-138            1.1E+o0        2.07E-02     8.83E+03        1.63E+02      4.13E+03    9.21E+03        2.95E+o2      5.46E+01       1.B7E-06       1.43E+o5         2.67E-01 Tui8is-        -   5.3E+o1                                     1.64E+o3                                  3.20E+03                     9.03E-05                       6.25E+OO 1.03E-04      secJm3      * )(}Q (from ODCM procedure 112-0DC-2.02, Section 8.1.1)                                 QI (Total Body)= 500 I ("1Q) sum (KiSi)=       2.64E+03 uCUsec 62000     elm         = Flowrate (from ODCM procedure 112-0DC-2.02, Secilon 8.1.1)                            Qt (Skin) = 3000 I (ll1Q) sum (Li+1.1 Mi)Si=    9.09E+o3 uCVsec Lowest Qt Value = 2640.52199 uCVsec Al: From ODCM procedure 1/2-0DC-2.02, Attachement A, Table 2.1-1a)

Ki, Li, & Mi: From ODCM procedure 112-0DC-2.02, Attachment G, Table 2.2-11) Ei: From ODCM procedure 1/2-0DC-2.02, Attachment B, Table 2.1-2a) - Efficiencies found in Mirian MCNP Analysis for NGM204 Monitor, pg 16 CR= Sum(CiEi) = 6.25E+OO cps Ela = (CR) I (Sum Ci) = 6.92E+04 cps/uCi/cc Conversation Factor* 1 /Ela = 1.45E--05 uCi I eel cps Conversation Factor = 1 /Ela = 5.35E+05 Bq I m3 /cps DV=CR/Eia = 9.03E--05 uCilcc

  • Process HHSP =((CR) x (60%: Site Noble Gas Dose Rate Limil)) I Eia 5.42E-05 uCi I cc = Process HS P 1584.3132 uCVsec Process HSP = ((CR) x (30%: Sile Noble Gas Dose Rate Limit)) I Eia 2.71E-05 uCi I cc= Process ASP 792.156598 uCVsec Note : All equations used above are from ODCM procedure 1/2-0DC-2.02, Section 8.1.2 Unusual Event= 2.64E+03 uCi I sec 2 = 5.28E+03 uCVsec Alen= 2.64E+o3 uCi I sec 200 = 5.2SE+o5 uCVsec

Continuous Release ERS-HHM-87--014 Revisions Unit 1 - Ventilation Vent Pathway Gaseous Effluent Monitor Attachment 3 Page :;:i~'b 

                                                                                                                                                                                   !!J5 RM-1VS-109 High

_Ai_._ _ Ci Ei CR 

     ~                              Si            Ki                          Li            Mi                          Qi Ai/Sum Ai                   KiSI                                      (Li+1.1 MilSi SiQt          (2.12E-3 Qi)F                CiEI mrem/yr       mremlyr       mrem/yr       mrad/yr per   mrem/yr                                    amps per
                    ~                             eeruCVm3      2eruCVm3      eeruCUm3      uCUm3         ~ruCi/m3      uCVsec        uCUcc          uCUcc         am es 1   Ar-41             0.0E+OO        O.OOE-tOO      8.84E+03     O.OOE+OO       2.69E+D3    9.30E+03       0.00E+OO      O.OOE+DO      0.00E+oo        1.50E-10      O.OOE+-00 2   Kr-83m             4.2E--01       7.90E--03     7.56E-02      5.97E..Q4     O.OOE-tOO    1.93E+01       1.68E-01     2.09E+D1       7.13E--07      4.74E-10      3,38E-16 3   Kr-85m            1.9E-+00        3.57E--02
  • 1.17E+03 4.18E+01 1.46E+03 1.23E+03 1.00E+D2 9.43E+01 3.23E--06 1.69E-10 5.45E-16 4 Kr-85 2.5E+OO 4.70E--02 1.61E+01 7.57E-01 1.34E+D3 1.72E+01 6.39E+D1 1.24E+02 4.24E--06 1.79E-10 7.60E-16 5 Kr-87 1.3E-+OO 2.44E--02 5.92E+03 1.45E+D2 9.73E+03 6.17E+a3 4.04E+D2 6.45E+01 2.21 E--06 1.0BE-10 2.38E-16 6 Kr-86 3.SE+OO 7.14E--02 1.47E+04 1.05E+D3 2.37E+D3 1.52E+04 1.36E+o3 1.89E+D2 6.45E--06 2.31E-10 1.49E-15 7 Kr-89 1.2E--01 2.26E--03 1.66E+04 3.75E+D1 1.01E+D4 1.73E+04 6.57E+D1 5.96E+DO 2.04E--07 1.77E-10 3.61E-17 8 Kr-90 0.0E+OO O.OOE+OO 1.56E+04 0.00E+OO 7.29E+03 1.63E+04 0.00E+OO O.OOE+DO O.OOE+OO 2.37E-11 O.OOE+-00 9 X&-131m 1.3E--01 2.44E--03 9.15E+01 2.24E-01 4.76E+02 1.56E+D2 1.58E+OO 6.45E+OO 2.21E-07 2.77E-10 6.11E-17 10 Xe-133m B.9E--01 1.67E-;02 2.51E+02 4.20E+OO 9.94E+D2 3.27E+02 2.27E+01 4.42E+01 1.51E--06 2.27E-10 3.43E-16 11 Xe-133 3.6E+01 6.77E--01 2.94E+02 1.99E+02 3.06E+02 3.53E+D2 4.70E'tQ2 1.79E+03 6.11E--05 4.89E-10 2.99E-14 12 X<>-135m 3.2E--01 6.02E-03 3.12E+03 1.88E+D1 7.11E+02 3.36E+03 2.65E+01 1.59E+01 5.43E-07 1.20E-11 6.52E-18 13 Xe-135 4.5E+OO B.46E-02 1.81E+03 1.53E+D2 1.86E+03 1.92E+03 3.36E+D2 2.23E'tQ2 7.64E--06 1.95E-10 1.49E-15 14 Xe-137 2.1E--01 3.95E-03 1.42E+03 5.61E+OO 1.22E+04 1.51E+a3 5.47E+01 1.04E+01 3.56E--07 1.17E-10 4.17E-17 15 Xe-138 1.1E+OO 2.07E-02 8.83E+03 1.83E+02 4.13E+03 9.21E+03 2.95E+o2 5.46E+01 1.87E--06 1.69E-10 3.16E-16
    ~ =53E+01                                                     1.84E+03                                  3.20E+03                    9.03E--05                     3.55E-14 1.03E--04    sec/m3       = x/Q (from OOCM procedure 1/2-0DC-2.02, Section 8.1.1)                                 Qt (Total Body) = 500 I (x/Q) sum (KISI)=   2.64E+03 uCUsec 62000     elm          = Flowrate {from ODCM procedure 1/2-0DC-2.02, Section 8.1.1)                           Qt (Skin)= 3000 I (x/Q) sum (Li+1.1 Mi)Si=   9.09E+03 uCUsec Lowest Qt Value =   2.64E+03 ucusec Ai: From ODCM procedure 1/2-0DC-2.02, Attachement A, Table 2.1-la)

Ki, LI, & Ml: From ODCM procedure 112-0DC-2.02, Attachment G, Table 2.2-11) El: From ODCM procedure 1/2-0DC-2.02, Attachment B, Table 2.1-2a) "Efficiencias found in Mirian MCNP Analysis for NGM204.Monitor, pg 16 CR= Sum(CIEI) = 3.55E-14 amps Eia = (CR) I (Sum Ci) = 3.94E-10 amps I uCi I cc Conversation Fader = 1 I Ela = 2.54E+09 uCi/ cc I amps Conversation Factor= 1 I Ela = *9.40E+19 Bq/m3 /amps DV=CR/Eia = 9.03E--05 uCi/cc Process HHSP = ((CR) x (60%: Sita Noble Gas Dose Rate Limit)) I Eia 5.42E--05 uCI I cc= Process HSP 1584.31 uc~sec Process HSP =((CR) x (30%: Site Noble Gas Dose Rate Limit)) I Eia 2.71E--05 uCi I cc = Process ASP 792.16 uCUsec Neta: All equations used above are from ODCM procedure 112-0DC-2.02, Section 8.1.2 Unusual Event = 2.64E+D3 uCi I sec 2= 5.28E+o3 uCUsec Alert= 2.64E+03 uCI I sec x 200 = 5.28E+o5 uCUsec 

                                                                                                                                                       )

ERS-HHM-87--014 ConUnuous Release Revision a Unit 1

  • Rx Con!alnment/SLCRS Vent Pathway Gaseous Effluent Monitor (Victoreen) Attachment 3 {

page <S)L{ 0 .~ RM-1VS-107B Li Ml Qi Ci El CR Nuclide Al Si Kl KISI (LI+ 1.1 Ml)SI SIQt (2.12E-3 Qi)/F Ci El Ai/Sum Ai mrem/yr mrem/yr mremtyr mrad/yr mrem/yr cpm per par per per per per cpm uCiim3 uCi/m3 uCi/m3 UCl/m3 uCUm3 uCl/sec uCUcc uCUcc Cl/yr 2.69E+03 9.30E+03 1.B2E+03 5.33E+02 2.29E-05 7.19E+07 1.65E+03 1 Ar-41 2.5E+01 1.41E-01 8.B4E+03 1.24E+03 O.OOE+OO 1.93E+01 2.63E-03 4.69E-01 2.02E-08 O.OOE+OO O.OOE+OO 2 Kr-B3m 2.2E-02 1.24E-04 7.56E-02 9.35E-06 1.46E+03 1.23E+03 2.37E+OO 3.20E+OO 1.37E-07 5.16E+07 7.09E+OO 3 Kr-85m 1.SE-01 8.44E-04 1.17E+03 9.87E-01 1.34E+03 1.72E+01 4.66E+02 1.30E+03 5.59E-05 5.04E+07 2.82E+03 4 Kr-85 6.1E+01 3.43E-01 1.61E+01 5.52E+OO 5.92E+03 1.BOE+OO 9.73E+03 6.17E+03 5.02E+OO 1.15E+OO 4.95E-08 9.60E+07 4.75E+OO 5 Kr-87 *S.4E-02 3.04E-04 2.37E+03 1.52E+04 2.58E+01 5.12E+OO 2.20E-07 5.16E+07 1.14E+01 6 Kr-86 2.4E-01 1.35E-03 1.47E+04 1.9l!E+01 4.39E--02 1.01E+04 1.73E+04 7.70E-02 1.00E-02 4.31E-10 9.59E+07 4.13E--02 7 Kr-89 4.7E-04 2.64E-06 1.66E+04 1.56E+04 0.00E+OO 7.29E+03 1.63E+04 O.OOE+OO 0.00E+OO O.OOE+OO 9.87E+07 O.OOE+OO 8 Kr-90 0.0E+OO O.OOE+OO 3.81E-01 4.76E+02 1.56E+02 2.70E+OO 1.58E+01 6.78E--07 2.94E+07 1.99E+01 9 Xe-131m 7.4E-01 4.16E-03 9.15E+01 1.26E+OO 9.114E+02 3.27E+02 6.78E+OO 1.90E+01 B.16E--07 4.17E+07 3.40E+01 10 Xe-133m 8.9E-01 5.01E-03 2.51E+02 2.94E+02 1.47E+02 3.06E+02 3.53E+02 3.48E+02 1.90E+03 8.16E-05 2.28E+07 1.86E+03 11 Xe-133 8.9E+01 5.01E-01 3.12E+03 7.00E-02 7.11E+02 3.36E+03 1.12E--01 9.59E-02 4.12E-09 1.51E+07 6.23E--02 12 Xe-135m 4.SE-03 2.53E-05 7.13E+OO 1.B6E+03 1.92E+03 1.56E+01 1.49E+01 6.42E-07 6.42E+07 4.12E+01 13 Xe-135 7.0E-01 3.94E-03 1.81E+03 1.42E+03 7.99E--03 1.22E+04 1.51E+03 7.BOE-02 2.13E-02 9.17E-10 1.05E+06 9.62E-02 14 Xe-137 1.0E-03 5.62E-06 6.63E+03 7.45E-01 4.13E+03 9.21E+03 1.20E+OO 3.20E-01 1.37E-08 7.35E+07 1.01E+OO 15 Xe-138 1.SE-02 B.44E-05 1.43E+03 2.69E+03 1.63E-04 6.44E+03 Totals= 1.8E+02 9.24E-05 sec/m3 = x/Q (From ODCM procedure 1/2-0DC-2.02, Section 8.1.1) Qt(To!al Body) = 500/(x/0) sum(KiSI) = . 3.79E+03 UCl/sac 49300 cfm = Rowrate (From ODCM procedure 1/2-0DC-2.02, Section 8.1.1) Ql(Skin) = 3000/(x/Q) sum(Li+1.1 Mi)Si = 1.21 E+04 UCUsec 3.79E+03 uCl/sec Lowest Oi Value Ai: From ODCM procedure 1/2-0DC-2.02, Attachment A, Table 2.1-1a Ki.Li & Mi: From ODCM procedure 112-0DC-2.02, Attachment G, Table 2.2-11 El: From ODCM procedure 1/2-0DC-2.02, Attachment B, Table 2.1-2a CR= Sum(CiEi) = 6.44E+03 cpm =CR HHSP =(CR x 0.6) IM!ere; 0.6 = 60% of the Sile Noble Gas Dose Raio Limit= 3.87E+03 cpm = Precess HHSP HSP =(CR x 0.3) \Miera; 0.3 = 30% of the Site Noble Gas Dose Rate Limit= 1.93E+03 cpm = Process HSP NOTE: All equations used above are from ODCM procedure 1/2-0DC-2.02, Section 8.1.1 Trip -HHSP= 3.87E+03 I (1 + .35 + .10) = 2.67E+03 cpm Trip -HSP= 1.93E+03 I (1 + .35 + .10) = 1.33E+03 cpm

Continuous Release ERS-HHM-87--014 Revision 8 Unit 1 - Rx Containment I SLCRS Vent Pathway Gaseous Effluent Monitor Attachment 3 RM-1VS-110 Low Page  :;FJ ~35 Nuclide _A_I_ _ Si Ki Li Mi Qi Ci Ei CR Ail Sum Ai KiSi (Li+1.1Mi!Si SiQt (2.12E-3 Qi)F CiEi mrem/yr mrem/yr mremlyr mradlyr per mrem/yr cps per 

                                                  ~ruCVm3         ~ruCVm3                   uCVm3          ~eruCVm3     uCVsec         uCVcc          ucvcc        cps Ar-41
                     .£!!l'.!:_

2.5E+01 1.41E--01 B.84E+03 1.24E+o3 2er uCVm3 2.69E+o3 9.30E+D3 1.B2E+o3 5.33E+02 2.29E--05 1.60E+05 3.67E+oo 2 Kr-SJm 2.2E--02 1.24E-04 7.56E--02 9.35E--06 0.00E+OO 1.93E+D1 2.63E-03 4.69E-01 2.02E-OB O.OOE+OO o.ooE+oo 3 Kr-B5m 1.5E-01 B.44E-04 1.17E+03 9.87E-01 1.46E+03 1.23E+03 2.37E+oo 3.20E+OO 1.37E-07 1.14E+05 1.57E-02 4 Kr-85 6.1E+01 3.43E-01 1.61E+o1 5.52E+OO 1.34E+03 1.72E+01 4.66E+02 1.3DE+03 5.59E-05 1.14E+OS 6.37E+o0 5 Kr-87 5.4E-02 3.04E-04 5.92E+03 1.BOE+OO 9.73E+03 6.17E+03 5.02E+OO 1.15E+OO 4.95E-OB 1.77E+o5 8.76E-03 6 Kr-88 2.4E-01 1.35E-03 1.47E+04 1.98E+01 2.37E+03 1.52E+o4 2.5BE+01 5.12E+OO 2.20E-07 1.05E+05 2.31E-02 7 Kr-89 4.7E-04 2.64E..Q6 1.66E+04 4.39E-02 1.01E+04 1.73E+o4 7.70E-02 1.00E-02 4.31E-10 1.89E+05 8.14E-05 8 Kr-90 0.0E+OO O.OOE+oo 1.56E+04 0.00E+OO 7.29E+03 1.63E+o4 O.OOE+OO O.OOE+OO O.OOE+oo 1.B9E+04 O.OOE+OO 9 Xe-131m 7.4E--01 4.16E-03 9.15E+01 3.81E--01 4.76E+02 1.56E+02 2.70E+OO 1.5BE+01 6.7BE--07 7.22E+04 4.90E-02 10 Xe-133m 8.9E-01 5.01E-03 2.51E+02 1.26E+OO 9.94E+02 3.27E+02 6.78E+OO 1.9DE+o1 8.16E-07 1.28E+05 1.04E-01 11 Xe-133 B.9E+01 5.01E-01 2.94E+02 1.47E+02 3.06E+02 3.53E+02 3.4BE+02 1.90E+03 B.16E-05 4,39E+04 3.SBE+OO 12 Xe-135m 4.SE--03 2.53E-05 3.12E+o3 7.90E--02 7.11E+02 3.36E+03 1.12E-01 9.59E-02 4.12E-09 3.28E+04 1.35E-04 13 Xe-135 7.0E-01 3.94E-03 1.81E+03 7.13E+OO 1.86E+03 1.92E+03 1.56E+01 1.49E+01 6.42E-07 1.37E+05 B.79E-02 14 Xe-137 1.DE-03 5.62E-06 1.42E+03 7.99E-03 1.22E+04 1.51E+o3 7.SOE-02 2.13E-02 9.17E-10 1.B3E+05 1.68E-04 15 Xe-138 1.5E-02 8.44E-05 8.63E+03 7.45E-01 4.13E+03 9.21E+03 1.20E+OO 3.20E-01 1.37E-08 1.43E+o5 1.97E-03 Totals 1:BE+o2 1.43E+03 2.69E+03 1.63E-04 1.39E+01 9.24E-05 secim3 = x/Q (from ODCM procedure 1/2-0DC-2.02, Section 8.1.1) QI (Total Body)= 500 I (x/Q) sum (KiSi}= 3.79E+03 uCVsec 49300 elm = Flowrate (from ODCM procedure 1/2-0DC-2.02, Section B.1.1) Qt (Skin)= 3000/ (x/Q) sum (Li+1.1Mi)SF 1.21E+04 uCVsec Lowest Qt Value = 3. 79E~03 uCVsec Ai: From ODCM procedure 1/2-0DC-2.02, AttachementA, Table 2.1-1a) Ki, Li, & Mi: From ODCM procedure 1/2-0DC-2.02, Attachment G, Table 2.2-11) . Et From ODCM procedure 1/2-0DC-2.02, Attachment B, Table 2. 1-2a) " Efficiencies found in Mirian MCNP Analysis for NGM204 Monitor, pg 16 CR = Sum(CiEi) = 1.39E+-01 cps Ela = (CR) I (Sum Ci) = 8.54E+04 cps /uCi I cc Conversation Factor= 1 / Eia = 1.17E--05 uci I cc/cps Conversation Factor= 1 I Ela = 4.33E+-05 Bq/ m3/cps DV= CR/Ela = 1.63E-04 uCi/cc Process HHSP =((CR) x (60%: Site Noble Gas Dose Raia Limit)) I Eia 9.78E-05 uCi I cc = Process HSP 2273. 97 uCVsec Process HSP =((CR) x (30%: Site Nobie Gas Dose Rate Limit)) I Eia 4.89E-05 uCI I cc= Process ASP 1136.99 uCVsec Note : All equations used above are from ODCM procedure 112-0DC-2.02, Section 8. 1.2 Unusual Event = 3.79E+03 uCi I sec 2= 7.SBE+-03 uCYsec Alert= 3.79E+03 uCi I sec 200 = 7.58E+05 uCYsec

Continuous Release ERS..HHM-87-014 Revision a Untt 1 - Rx Containment I SLCRS Vent Pathway Gaseous Effluent Monttor Attec/vnent 3 Page ;;,Jl.9 .,-{ 3S RM-1VS-110 High _A_i___ Li Mi QI Cl Ei CR 

    ~                              Si            Ki
    ----                           Ai I Sum Ai mrem/yr KiSI mrem/yr      mrem/yr        mradlyrper (Ll+1.1Ml}Si Si Qt mrem/yr (2.12E~    Qi)F amps per CiEi
                    ~                            peruCUm3       peruCUm3     peruCilm3      uCVm3         peruCVm3 uCVsec               ucvcc           uCVcc         amps Ar-41             2.5E+o1        1.41E-D1     B.84E+o3        1.24E+03     2.69E+D3      9.3DE+03      1.82E+o3       5.33E+o2        2.29E--05       1.SDE-10     3.44E-15 2   Kr-83m            2.2E-02        1.24E-04      7.56E-02        9.35E-06     D.OOE+OD     1.93E+01       2.63E-03       4.69E-01       2.02E-08        4.74E-10     9.56E-1B 3   Kr-e5m             1.5E-01       8.44E-04     1.17E+03        9.B7E-01     1.46E+03      1.23E+03      2.37E+oo       3.20E+OD        1.37E-07        1.69E-10     2.32E-17 4   Kr-85            6.1E+01         3.43E-01     1.61E+o1        5.52E+OD      1.34E+03    1.72E+o1       4.66E+o2       1.30E+03        5.59E--05       1.79E-10     1.0DE-14 5   Kr-87             5.4E-02        3.04E-04     5.92E+o3        1.80E+OD      9.73E+D3    6.17E+03       5.02E+o0       1.15E+OO        4.SSE--08       1.08E-10     5.35E-1B 6    Kr-88             2.4E-01        1.35E-03     1.47E+o4        1.9BE+01     2.37E+o3     1.52E+o4       2.58E+o1       5.12E+OD        2.20E-07        2.31E*10     s.oeE-17 7    Kr-89             4.7E-04        2.64E-06     1.66E+o4        4.39E-02     1.01E+o4     1.73E+o4        7.70E-02       1.00E-02       4.31E-10        1.77E-10     7.62E-20 B    Kr-90            0.DE+oo        o.ooe+oo      1.56E+04       O.OOE+OO      7.29E+03     1.63E+04       0.00E+OO      O.OOE+OO        O.OOEt-00        2.37E-11    0.00E+OO Xe-131m           7.4E-01        4.16E-03     9.15E+o1        3.B1E-01     4.76E+02     1.56E+02       2.70E+QO       1.5BE+01        6.7BE-07        2.77E-10     1.BBE-16 10   Xe-133m            8.9E-01        5.01E-03     2.51E+o2       1.26E+OO      9.94E+o2     3.27E+o2       6.78E+oo      1.90E+01         B.16E-07        2.27E-10     1.85E-16 11   Xe-133            B.9E+o1         5.01E-01     2.94E+02       1.47E+02      3.06E+02     3.53E+o2       3.48E+02      1.90E+03         B.16E--05       4.89E-10     3.99E-14 12   Xe-135m            4.5E-03        2.53E-05    3.12E+03         7.SOE-02    1:11E+02      3.36E+03        1.12E-01      9.59E-02     . 4.12E-09         1.20E-11     4.95E-20 13   Xe-135             7.0E-01        3.94E-03     1.81E+03       7.13E+OO      1.86E+03     1.92E+03       1.56E+01      1.49E+01        6.42E-07         1.95E-10     1.25E-16 14   Xe-137             1.0E-03        5.62E-06    1.42E+03         7.99E-03    1.22E+04      1.51E+03        7.80E-02      2.13E-02       9.17E-10         1.17E-10     1.07E-19 15   Xe-138             1.SE-02        B.44E-05    8.83E+03         7.45E-01    4.13E+03      9.21E+03       1.20E+OO       3.20E-01       1.37E-OB         1.69E-10     2.32E-18 Totals        =1]E+Q2                                         1.43E+D3                                 2.69E+03                       1.63E-04                      5.39E-14 9.24E-05     sec/m3      = xJQ (from OOCM procedure 1/2-0DC-2.02, Section 8.1.1)                                   QI (Total Body) = 500 I (x/Q) sum (KiSi)=    3.79E+03 uCUsec 49300     cfm         = Flowra\e (from OOCM procedure 112-0DC-2.02, SecUon B.1.1)                              Qt (Skin) = 3000 I (x!Q) sum (Li+1.1 Mi)Si=   1.21E+D4 uCVsec Lowest Qt Value=    3. 79E+03 uCUsec Ai: From ODCM procedure 1/2-0DC-2.02, Attachement A, Table 2.1-1a)

Ki, Li, & Mi: From ODCM procedure 1/2-00C-2.02, Attachment G, Table 2.2-11) Ei: From ODCM procedure 112-0DC-2.02, Attachment B, Table 2.1-2a) - Efficiencies found in Mirian MCNP Analysis for NGM204 Monttor, pg 16 CR = Sum(CIEi) = 5.39E-14 amps Eia = (CR) I (Sum C~ = 3.31E-10 amps I uCi I cc Conversation Factor = 1 I Eia = 3.02E+09 uCI I cc I amps Conversation Fac1or = 11 Eia ~ 1.12E+20 Bq/m3/amps DV= CR/Eia = 1.63E-04 uCl/cc Process HHSP = ((CR) x (60%: Sile Nobie Gas Dose Rate Limit)) I Eia 9.78E--05 uCI I cc = Process HSP 2273.97 uCl/sec Process HSP = ((CR) x (30%: Sile Noble Gas Dose Rate Limit)) I Eia 4.B9E-05 uCi I cc = Process ASP 1136.99 uCl/sec Nole : All equations used above are from ODCM procedure 1/2-0DC-2.02, Section 8.1.2 Unusual Even\= 3.79E-t-03 uCi I sec 2= 7.58E+03 uCUsec Alert= 3.79E+03 uCI /sec x 200 = 7.58E+05 uCUsec

Contlnuous Release ERS*HHM-a7-ll14 Revision 8 Unit 112 - Process Vent Pathway Gaseous Effluent Monitor (Vlctoreen) Attactvnent3 page t?j OJ-:\- o.f 3? RM-1GW.108B Nuclide Al SI Vi Li Bi QI Cl Ei CR Ai/Sum Al VlSI (Li(X/Q)+1.1 Bi)Si Si Qt (2.12E-3 Qi)/F CIEi mrem/yr mrem/yr mrem/yr mrad/yr mrem/yr cpm per per per per per per UC I/sec uCl/sec uCi/m3 uCl/seo uCl/sec uCl/sec uCl/cc UCl/cc cpm Cl/yr O.OOE+OO 2.68E-03 O.OOE+OO 2.69E+03 4.02E-03 O.OOE+OO O.OOE+OO O.OOE+OO 6.59E+07 O.OOE+OO 1 Ar-41 O.OE+OO 4.58E-08 2.32E-10 O.OOE+OO 3.96E*05 2.20E-07 5.53E+03 8.0~E-03 O.OOE+OO O.OOE+oo 2 Kr-a3m 5.SE-01 5.06E-03 4.70E-04 1.07E-05 1.46E+03 7.06E-04 9.46E-D5 2.49E+04 3.64E-02 9.00E+07 3.28E+06 3 K'r-asm 2.5E+OO 2.2BE-02 5.54E--06 7.19E-07 1.34E+03 6.40E.Q6 4.03E-04 1.42E-t05 2.07E-01 3.56E+05 7.39E+04 4 Kr-1!5 1.4E+01 1.30E--01 1.53E--02 1.45E-03 2.22E-D5 9.73E+03 2.19E-03 3.81E-04 1.87E+04 2.45E-02 6.78E+07 1.66E+06 5 Kr-1!7 1.7E+OO 4.9E+OO 4.52E-02 4.09E-03 1.85E-04 2.37E+03 6.16E-03 5.54E-04 4.94E+04 7.22E-02 1.05E+OB 7.59E+06 6 Kr-1!8 1.43E-03 1.25E--03 1.79E-06 1.01E+04 1.88E-03 3.63E-05 1.56E+03 2.2BE-03 1.28E+08 2.92E+05 7 Kr-1!9 1.SE-01 8 Kr-90 0.0E+OO O.OOE+OO O.OOE+OO O.OOE+OO 7.29E+03 0.00E+OO O.OOE+OO O.OOE+OO O.OOE+OO 1.23E+08 ~ O.OOE+OO 3.SE-01 3.29E-03 1.67E-04 5.SOE-07 4.7BE+02 3.09E-04 4.74E--06 3.60E+03 5.26E-03 2.07E+06 1.09E+04 9 Xe-131m 1.34E-02 1.32E-04 1.77E-06 9.94E+02 2.BIE-04 3.47E-05 1.47E+04 2.15E-02 1.16E+07 2.49E+05 10 Xe-133m 1.5E+OO 7.5E+01 6.91E-01 1.54E-04 1.06E-04 3.06E+02 2.76E-04 6.9BE-04 7.55E+05 1.10E+OO 9.24E+06 1.02E+07 11 Xe-133 3.71E-03 6.21E-04 2.31E-06 7.11E+02 9.SOE-04 9.98E--06 4.06E+03 5.94E-03 6.58E+07 3.91E+05 12 Xe-135m 4.0E-01 5.9E+OO 5.46E-02 6.96E-04 3,80E-05 1.86E+03 1.0SE-03 2.97E-04 5.97E+04 8.72E-02 1.03E+08 8.98E+06 13 Xe-135 9.66E-05 2.33E-07 1.22E+04 1.46E-04 6.83E-05 2.64E+03 3.65E-03 2.91E+07 1.12E+05 14 Xe-137 2.6E-01 2.41E-03 1.23E-02 2.22E-03 2.72E-05 4.13E+03 3.34E-03 1.62E-04 1.34E+04 1.96E-02 1.06E+OB 2.08E+06 15 Xe-138 1.3E+OO 3.97E-04 2.74E-03 1.80E+OO 3.49E+07 Totals = 1.1E+02 2.31 E-06 seclm3 = )tJQ (From ODCM procedure 1/2-0DC-2.02, Section 8.1.3) Qt(Total Body)= 500/sum(ViSi) = 1.26E+06 uCl/sec 1450 cfm = Flowrate (From ODCM procedure 1/2-0DC-2.02, Secllon 8.1.3) Qt(Skin) = 3000/sum(Li(X/Q)+1.1Bi)Si = 1.09E+06 uCl/sec Lowest Qt Value 1.09E+06 uCi/sec Ai: Derived from ODCM procedure 1/2-0DC-2.02, Attactvnent A, Table 2.1-1 a, as follows: Al= (2 x Main Cond Air Ejector)+ (U2 RBC Vac Pump)+ (14 x Old U1 RBC Vac Pump) Note: The values for the New U1 RBC Vac Pump (ie; 14 xOld U1 RBC VacPump) are documented In Attachment4 Vi & Bt From ODCM procedure 1/2-0DC-2.02, Attachment G, Table 2.2-12 (3) Li: From ODCM procedure 1/2-0DC-2.02, Attachment G, Table 2.2-11 Ei: From ODCM procedure 112-0DC-2.02, Attactvnent B, Table 2.1-2a CR = Sum(CIEI) = 3.49E+07 cpm = CR HHSP = (CR x 0.6) Vlliere; 0.6 = 60% of the Site Noble Gas Dose Rate Limit= 2.09E+07 cpm = Process HHSP HSP =(CR x 0.3) 'Mlere; 0.3 = 30% of the Site Noble Gas Dose Rate Lim~= 1.05E+07 cpm = Process HSP NOTE: All equaUons used above are from ODCM procedura 1/2-0DC*2.02, Section 8.1.3 Trip -HHSP= 2.09E+07 I (1 + .35 + .1 O) = 1.44E+07 cpm Trip -HSP= 1.05E+07 /(1 + .35+ .10) = 7.22E+06 cpm

Continuous Release ERs-HHM-87-014 Revision B Unit 1 - Process Vent Pathway Gaseous Effluent Mon~or Attachment 3 of* Page :;; f) ~ RM-1GW-109 High Nuclide _N_* _ _ Si VI Li Bl Qi Ci Ei CR Ail Sum Ai Vi Si (Li(x/Q)+1.1 Bi) SiQI (2. 12E-3 Ol)IF CiEi mrem/yr mremlyr mram/yr mrad/yrper mrern/yr amps per 

                    ~                           ear uCVm3      ear uCVm3     eeruCVm3      uCVm3           ear uCVm3      uCVsec          uCVcc           uCVcc         ame;s Ar-41            0.0E+OO      O.OOE+DO        2.68E-03      0.00E+OO       2.69E+03      4.02E-03        O.OOE+OO       O.OOE+-00      0.00E+OO         1.SOE-10     0.00E-tOO 2    Kr-83m           5.SE-01       5.06E-03      4.58E-OB       2.32E-10      0.00E->00     3.96E-05        2.20E-07       5.53E+o3        B.09E-03        4.74E-10     3.B3E-12 3    Kr-85m          2.5E->OO       2.2BE-02      4.70E-04       1.07E-05      1.46E+o3      7.06E-04        9.46E-05       2.49E+o4        3.64E-02        1.69E-10     6.16E-12 4   Kr-85            1.4E+01        1.30E-01      5.54E-06       7.19E-07      1.34E+03      B.40E-06        4.03E-04       1.42E+o5        2.07E-01        1.79E-10     3.71E-11 5     Kr-87           1.7E+OO        1.53E-02      1.45E-03       2.22E-05     9.73E+o3       2.19E-03        3.81E-04       1.67E+o4        2.45E-02        1.08E-10     2.64E-12 6    Kr-86            4.9E+OO        4.52E-02      4.09E-03       1.BSE-04     2.37E+o3       6. 16E-03       5.54E-04       4.94E+o4        7.22E-02        2.31E-10     1.67E-11 7    Kr-89             1.SE-01       1.43E-03      1.25E-03       1.79E-06      1.01E+o4      1.88E-03        3.63E-05       1.56E+03        2.2BE-03        1.77E-10     4.04E-13 a    Kr-90            0.0E+OO      O.OOE+oo      O.OOE->00       O.OOE->00     7.29E+o3     O.OOE->00        0.00E+OO        O.OOE+-00      O.OOE+oo         2.37E-11    O.OOE+oo 9    Xe-131m           3.SE-01       3.29E-03      1.67E-04       5.SOE-07     4.76E+02       3.09E-04        4.74E-06       3.60E+03        5.26E-03        2.77E-10     1.46E-12 10    Xe-133m          1.SE+OO        1.34E-02      1.32E-04       1.77E-06     9.94E+o2       2.61E-04        3.47E-05       1.47E+o4        2.15E-02        2.27E-10     4.BBE-12 11    Xe-133           7.5E+01        6.91E-01      1.54E-04       1.0SE-04     3.06E+D2       2.76E-04        6.98E-04       7.55E+05       1.10E+oo         4.B9E-10     5.40E-10 12    Xe-135m           4.0E-01       3.71E-03      6.21E-04       2.31E-06     7.11E+o2       9.SOE-04        9.9BE-06      4.06E+03         5.94E-03        1.20E-11     7.13E-14 13    Xe-135           5.9E+OO        5.46E-02      6.96E-04       3.BOE-05     1.B6E+03       1.05E-03        2.97E-04      5.97E-t-04       B.72E-02        1.95E-10     1.70E-11 14    Xe-137           2.6E-01       2.41E-03      9.66E-05       2.33E-07     1.22E+o4        1.46E-04        6.83E-05      2.64E+03        3.BSE-03         1.17E-10     4.51E-13 15    Xe-138           1.3E+oo        1.23E-02     2.22E-03       2.72E-05      4.13E+o3       3.34E-03        1.62E-04       1.34E+D4       1.96E-02         1.69E-10     3.31E-12 Totais- 1.iE+o2                                              3.97E-04                                     2.74E-03                      1.60E+OO                      6.34E-10 2.31E-06     sec/m3
  • xJQ (from ODCM procedure 1/2-0DC-2.02, Section B.1.3) Qt (Total Body) = 500 I sum(ViSi)* 1.26E+06 uCVsec 1450 elm = Flowrate (from ODCM procedure 1/2-0DC-2.02, Section 8.1.3) QI (Skin) = 3000 I sum(Ll(xlQ) + 1.1 BQSI= 1. 09E+o6 uCVsec Lowest QI Value
  • 1.09E+o6 uCUsec Ai: Derived from ODCM procedure 1/2-0DC-2.02, Allachemen!A, Table 2.1-1 a, as follows PJ = (2 x Main Cond Air Ejector)+ (U2 RBC Vac Pump) -t (14 x Old U1 RBC Vac Pump)

Note: The values for the New U1 RBC Vac Pump (ie: 14 x Old U1 Vac Pump) are documented in Attachemenl 4 Vi & Bi: From ODCM procedure 1/2-0DC-2.02, Attachment G, Table 2.2-12) Li: From ODCM procedure 1/2-0DC-2.02, Attachment G, Table 2.2-11) Ei: From ODCM procedure 1/2-0DC-2.02, Attachment B, Table 2.1-2a) -Efficiencies found in Mirion MCNP Analysis for NGM204 Monitor, pg 16 If Alarm setpolnt are above Instrument display range, use 10% for lower and 30% upper of the display range for the set points CR

  • Sum(CiEi) = 6.34E-10 amps 4.93E-04 cps Eia = (CR) I (Sum Ci)
  • 3.97E-10 amps I uCi I cc 3.0BE-04 cps I uCi I cc Conversation Factor* 1 I Eia
  • 2.52E-t09 uCi I cc I amps 3.24E-t03 Conversation Factor* 1 I Eia
  • 9.33E+19 Bq/m3/amps 1.20E+14 Bq/m3/amps DV= CR/Eia
  • 1.60E-t00 uCi/cc 1.60E->OO uCVcc Process HHSP * ((CR) x (60%: Sile Noble Gas Dose Rate Limft)) I Ela 9.59E-01 uCi I cc
  • Process HSP 4.BOE-01 uCVcc 655975.35 uCUsec Process HSP = ((CR) x (30%: Sile Noble Gas Dose Rate Limit)) I Ela 4.80E-01 uCi I cc
  • Process ASP 1.60E--01 uCUcc 327987.68 uCVsec Note : All equations used above are from ODCM procedure 1/2-0DC-2.02, Section 8.1.2

Continuous Release ERS-HHM-87-014 Revision 8 Unit 1 - Process Vent Pathway Gaseous l;:ffluent Monttor Attectvnent 3 Page ~c.f~ RM-1GW-109 Low Nuclide _A_i_ _ _ Si V1 LI Bi QI Ci El CR Ai/ Sum Ai ViSI (Li(x/0)+1.1 Bi) SiQI {2.12E-3 Qi)/F Ci El mrem/yr mrem/yr mrem/yr mrad/yr per mrem/yr cps per 

                    ~                            eer uCi!m3     2eruCVm3      eeruCi/m3      uCi!m3         eeruCi/m3      uCi/sec         uCi/cc         uCVcc
                                                                                                                                                                         ~*0.00E+OO 1    Ar-41            0.0E+oo       O.OOE+OO       2.68E-03       0.00E+oo     2.69E+o3        4.02E-03      O.OOE+OO        O.OOE+OO       O.OOE+oo       1.60E+o5 2    Kr-83m            5,5E-01       5.06E-03      4.58E-08       2.32E-10     O.OOE+OO        3.96E-05       2.20E-07       5.53E+03        8.09E-03      0.00E+oO        0.00E+OO 3    Kr-85m           2.5E+oo        2.28E-02      4.70E-04       1.07E-05      1.46E+03       7.0SE-04       9.46E-05       2.49E+o4        3.64E-02      1.14E+o5        4.15E+03 4     Kr-85            1.4E+01        1.30E-01      5.54E-06       7.19E-07      1.34E.. 03     8.40E-06       4.03E-04       1.42E+05        2.07E-01      1.14E+05       2.37E+04 5    Kr-87            1.7E+DO        1.53E-02      1.45E-03       2.22E-05     9.73E+03        2.19E-03       3.81E-04       1.67E+04        2.45E-02      1.77E+05       4.33E+03 6     Kr-88            4.9E+OO        4.52E-02      4.09E-03       1.BSE-04     2.37E+03        6.16E-03       5.54E-04       4.94E+04        7.22E-02      1.05E+05       7.59E+o3 7     Kr-89             1.SE-01       1.43E-03      1.25E-03       1.79E-06     1.01E+04        1.BBE-03       3.63E-05       1.56E+03        2.2BE-03      1.89E+05       4.31E+o2 6     Kr-90            0.0E+OO      0,00E+OO       O.OOE+-00      O.OOE+OO      7.29E+03      0.00E+OO        O.OOE+oO        O.OOE+OO       O.OOE+OO       1.89E+04       O.OOE+oo 9    Xe-131m           3.SE-01        3.29E-03      1.67E-04       5.SOE-07     4.76E+02        3.09E-04      4.74E-06        3.60E+03        5.26E-03      7.22E+04       3.60E+02 10    Xe-133m          1.5E+OO         1.34E-02      1.32E-04       1.77E-06     9.94E+02        2.61E-04       3.47E-05       1.47E+04        2.15E-02      1.2BE+05       2.75E+03 11    Xa-133           7.SE+01         6.91E-01      1.54E-04       1.06E-04     3.06E+02        2.76E-D4       6.98E-04       7.SSE+05       1.10E+oo       4.39E+04       4.85E+04 12    Xe-135m           4.0E-01       3.71E-03      6.21E-04        2.31E-06     7.11E+02        9.SOE-04      9.98E-06       4.06E+03         5.94E-03    . 3.28E+04       1.95E+02 13    Xe-135           5.SE+OO         5.46E-02     6.96E-04        3.SOE-05     1.86E+03        1.0SE-03      2.97E-04        5.97E+04        8.72E-02      1.37E+o5       1.19E+04 14    Xe-137            2.SE-01        2.41E-03      9.66E-05       2.33E-07     1.22E+04        1.46E-D4      6.83E-05       2.64E+o3         3.85E-03      1.83E+05       7.05E+02
                                                                                                 ~

15 Xe-138 1.3E+OO 1.23E-02 2.22E-03 2.72E-05 4.13E+03 3.34E-03 1.62E-04 1.34E+04 1.96E-02 1.43E+05 2.80E+03 

    ~              """""1.iE+o2                                    3.97E-04                                   2.74E-03                       1.60E+OO                      1.07E+05 2.31E-06     secJm3      = x!Q (from ODCM procedure 1/2-0DC-2.02, Section 8.1.3)                                            Qt (Total Body)= 500 I sum(ViSi)=       1.26E+06 uCi/sec 1450    cfm         = Flowrale (from ODCM procedure 1/2-0DC-2.02, Section 8. 1.3)                               Qt (Skin) = 3000 I sum(Li(x/Q) + 1.1 Bi)Si=    1.09E+06 uCi/sec Lowest Qt Value=       1. 09E+06 uCVsec Ai: Derived from OOCM procedure 1/2-0DC-2.02, Attachemenl A, Table 2.1-1a, as follows Ai = (2 x Main Cond Air Ejector)+ (U2 RBC Vac Pump)+ (14 x Old U1 RBC Vac Pump)

Note: The values for the New U1 RBC Vac Pump (ie: 14 x Old U1 Vac Pump) are documented In Altachement 4 Vi & Bi: From ODCM procedure 1/2-0DC-2.02, Attachment G, Tabla 2.2-12) LI: From OOCM procedure 1/2-0DC-2.02, Attachment G, Tabla 2.2-11) Ei: From ODCM procedure 112-0DC-2.02, Attachment 8, Table 2.1-2a) "EfliClencies found In Mirian MCNP Analysis for NGM204 Monitor, pg 16 If Alarm setpoint are above instrument display range, use 10% for lower and 30% upper or the display range for the setpolnts CR= Sum(CIEi) = 1.07E+05 cps 4.93E-04 cps Eia = (CR) I (Sum Cl) = 6.72E+D4 cps/uCi/cc 3.0BE-04 cps I uCI I cc Conversation Factor = 1 I Eia = 1.49E-05 uCi/ cc/ cps 3.24E+03 Conversation Factor= 1 I Eia = 5.51E+05 Bq I m3 /cps 1.20E+14 DV=CR/Eia = 1.60E+oo uCi/ cc 1.60E+OO uCVcc Process HHSP =((CR) x (60%: Site Noble Gas Dose Rate Limit)) I Eia 9.59E-01 uCi I cc = Process HSP 4.80E-01 uCVcc 655975.35 uCVsec Process HSP = ((CR) x (30%: Site Noble Gas Dose Reta Limit)) I Ela 4.BOE-01 uCi I cc = Process ASP 1.60E-01 uCi/cc 327987.68 uCi/sec Note : All equations used above are from ODCM procedure 1/2-0DC-2.02, Section B.1.2

Continuous Release ERS*HHM-87.{)14 Revisions Unit 2

  • SLCRS Unfiltered Pathway Gaoeoua Effluent Monitor Attachment3 page30~ "55 2HVS-RQ101B Nuclide Ai SI Kl LI Ml Qi Ci El CR Ai/Sim Al Ki Si {Ll+1.1 Mi)Si Si Qt (2.12E~ Ql)IF CiEI mrem/yr mrem/yr mrem/yr mradlyr mrem/yr epm per per per per per per Ci/yr uCi/m3 uCl/m3 uCi/m3 uCilrn3 uCUm3 uCi/sec uCi/cc UC Vee cpm 1 Ar-41 2.5E+01 1.46E.{)1 B.84E+03 1.29E+03 2.69E+03 9.30E+03 1.88E+Q3 4.90E+02 4.39E.{)5 3.79E+07 1.66E+03 2 Kr-83m 4.0E.{)5 2.33E.{)7 7.56E-02 1.76E-OB 0.00E+OO 1.93E+01 4.94E*06 7.85E.{)4 7.02E*11 0.00E+OO O.OOE+OO 3 Kr-85m 1.4E.{)2 8.15E.{)5 1.17E+03 9.54E-02 1.46E+03 1.23E+03 2.29E-01 2.75E.{)1 2.46E.{)8 3.20E+07 7.BBE.{)1 4 Kr-85 6.1E+01 3.55E.{)1 1.61E+01 5.72E+OO 1.34E+03 1.72E+01 4.83E+02 1.20E+03 1.07E.{)4 3.60E+07 3.85E+03 5 Kr-87 5.3E-06 3.09E.{)8 5.92E+03 1.83E.{)4 9.73E+03 6.17E+03 5.10E.{)4 1.04E-04 9.3DE-12 3.73E+07 3.47E.{)4 6 Kr-88 4.1E.{)3 2.39E.{)5 1.47E+04 3.51E.{)1 2.37E+03 1.52E+04 4.56E.{)1 8.04E.{)2 7.19E.{)9 3.05E+07 2.19E.{)1 7 Kr-89 O.OE+OO O.OOE+OO 1.66E+04 O.OOE+OO 1.01E+04 1.73E+04 O.OOE+OO O.OOE+OO O.OOE+OO 3.72E+07 0.00E+OO e Kr-90 O.OE+OO 0.00E+OO 1.56E+04 O.OOE+OO 7.29E+03 1.63E+04 O.OOE+OO O,OOE+OO O.ODE+OO 3.86E+07 O.OOE+OO 9 Xe-131m 7.2E.{)1 4.19E.{)3 9.15E+01 3.84E.{)1 4.76E+02 1.56E+02 2.72E+OO 1.41E+01 1.26E.{)6 2.44E+07 3.0BE+01 10 Xe-133m 7.SE-01 4.43E.{)3 2.51E+02 1.11E+OO 9.94E+02 3.27E+02 5.99E+OO 1.49E+01 1.33E-06 2.86E+07 3.81E+01 11 Xe-133 8.4E+01 4.89E.{)1 2.94E,.02 1.44E+02 3.06E+02 3.53E+02 3.40E+02 1.65E+03 1.47E.{)4 1.80E+07 2.65E+03 12 Xe-135m O.OE+OO O.OOE+OO 3.12E+03 O.OOE+OO 7.11E+02 3.36E+03 0.00E+OO O.OOE+OO O.OOE+OO 7.22E+06 O.oOE+OO 13 Xe-135 2.4E-01 1.40E-03 1.81E+03 2.53E+OO 1.86E+03 1.92E+03 5.55E+OO 4.71E+OO 4.21E.{)7 3.86E+07 1.63E+01 14 Xe-137 O.OE+OO O.OOE+OO 1.42E+D3 O.OOE+OO 1.22E+04 1.51E+03 O.OOE+OO O.OOE+OO O.OOE+OO 3.78E+07 O.OOE+OO 15 Xe-138 0.0E+OO O.OOE+OO 8.83E+03 O.OOE+OO 4.13E+03 9.21E+03 O.OOE+OO O.OOE+OO O.OOE+OO 3.52E+07 O.OOE+OO Totals= 1.7E+02 1.44E+03 2.72E+03 3.01E-04 8.26E+03 1.03E.{)4 sec/m3 = xJQ (From ODCM procedure 1/2*0DC-2.02, Section 8.1.2) Qt(Total Body)= 500/(x/Q) sum(KiSi) = 3.37E+03 uCVsec 23700 cfm = Flowrate {From ODCM procedure 1/2-0DC-2.02, Section 8.1.2) Qt(Skin) = 3000/(xJQ) si.m(Li+1.1Ml)SI = 1.07E+04 uCusec Lowest Qt Value 3.37E+03 uCVsec Ai: From ODCM procedure 1/2-00C-2.02, Attachment A, Tabla 2.1-1b Kl,LI & Ml: From ODCM procedure 1/2-0DC-2.02, Attachment G, Table 2.2*11 Ei: From ODCM procedure 1/2-0DC-2.02, Attachment B, Table 2.1-2b CR= Sum(CiEi) = 8.26E+03 cpm Eia = {CR) I (Sum Ci) " 2. 74E+07 cpm/uCl/cc Conversion Faclor = 1 /Ela= 3.65E.{)8 uCUcc/cpm DV=CR/Ela= 3.01 E-04 uCVcc Process HSP ={{CR) x (60%: Site Noble Gas Dose Rate Limit)) I Eia = 1.81E.{)4 uCucc= Process HSP Process ASP= ((CR) x (30%: Stte Nobie Gas Dose Rate Limit)) I Ela; 9.04E.{)5 uCUcc = Process ASP NOTE: All equations used above are from ODCM procedura 112-00C-2.02, Seclion 8.1.2 Trip -HSP= 1.B1E.{)4 I (1 + .35 + .10) = 1.25E.{)4 uCVcc Trip -ASP; 9.04E-05 I (1 + .35 + .10) = 6.24E-05 uCVce

Continuous Release ERS-HHM-87-014 Revision 8 Unit 2 - SLCRS Filtered PathWay Gaseous Emuent Monitor Attachment 3 2HVS-RQ109B page 3\ ctJ:55 Nuclide N Si Kl Li Ml QI Ci El CR AilSumAi KISI (Ll+1.1Mi)Si Si Qt (2.12E-3 Qi)/F CIEl mrem/yr mrem/yr mremJyr mrad/yr mrem/yr cpm per per per per per per Ci/yr uCl/m3 uCUm3 uCl/m3 uCVm3 uCi/m3 ucvsec uCi/cc UCUcc cpm 1 Ar-41 O.OE+OO O.OOE*OO 8.84E+03 O.OOE+OO 2.69E+03 9.3qE+03 O.OOE+OO O.OOE+OO O.OOE+OO 7.00E+07 O.OOE+OO 2 Kr-83m 4.2E-01 7.90E-03 7.56E-02 5.97E-04 O.OOE+OO 1.93E+01 1.SBE-01 2.32E+01 8.35E-07 0.00E+OO O.OOE+OO 3 Kr-B5m 1.9E+OO 3.57E-02 1.17E+03 4.18E+01 1.46E+03 1.23E+03 1.00E+02 1.05E+02 3.76E-06 5.63E+07 2.20E+02 4 Kr-85 2.5E+OO 4.70E-02 1.61E+01 7.57E-01 1.34E+03 1.72E+01 6.39E+01 1.38E+02 4.97E-06 7.19E+07 3.57E+02 5 Kr-87 1.3E+OO 2.44E-02 5.92E+03 1.45E+02 9.73E+03 6.17E+03 4.04E+02 7.19E+01 2.56E-06 8.65E+07 2.29E+02 6 Kr-86 3.6E+OO 7.14E-02 1.47E+04 1.05E+03 2.37E+03 1.52E+04 1.36E+03 2.10E+02 7.56E-06 6.BOE+07 5.14E+02 7 Kr-89 1.2E-01 2.26E-03 1.66E+04 3.75E+01 1.01E+04 1.73E+04 6.57E+01 6.64E+OO 2.39E-07 8.73E+07 2.06E+01 8 Kr-90 O.OE+OO O.OOE+OO 1.56E+04 O.OOE+OO 7.29E+03 1.63E+04 O.OOE+OO O.OOE+OO O.OOE+OO 8.BOE+07 O.OOE+OO 9 xe-131m 1.3E-01 2.44E-03 9.15E+01 2.24E-01 4.76E+02 1.56E+02 1.5BE+OO 7.19E+OO 2.56E-07 4.61E+04 1.19E-02 10 Xe-133m 8.9E-01 1.67E-02 2.51E+02 4.20E+OO 9.94E+02 3.27E+02 2.27E+01 4.93E+01 1.77E-06 6.06E+04 1.07E-01 11 Xe-133 3.6E+01 6.77E-01 2.94E+02 1.99E+02 3.06E+02 3.53E+02 4.70E+02 1.99E+03 7.16E-05 2.94E+07 2.10E+03 12 xe-135m 3.2E-01 6.02E-03 3.12E+03 1.88E+01 7.11E+02 3.36E+03 2.65E+01 1.77E+01 6.36E-07 1.55E+04 9.BSE-03 13 Xe-135 4.5E+OO 8.46E-02 1.81E+03 1.53E+02 1.86E+03 1.92E+03 3.36E+02 2.49E+02 8.95E-06 7.48E+07 6.69E+02 14 Xe-137 2.1E-01 3.95E-03 1.42E+03 5.61E+OO 1.22E+04 1.51E+03 5.47E+01 1.16E+01 4.1BE-07 9.07E+07 3.79E+01 15 Xe-138 1.IE+OO 2.07E-02 6.63E+o3 1.63E+02 4.13E+03 9.21E+03 2.95E+02 6.09E+01 2.19E-06 7.74E+07 1.69E+02 Totals = 5.3E+01 1.84E+03 3.20E+03 1.0SE-04 4.32E+03 9.24E-05 sec/m3 = xJQ (From ODCM procedure 1IZ-ODC-2.02, Section 6.1.2) Qt(Totsl Body) = 500/(X/Q) sum(KlSi) = 2.94E+03 uCVsec 59000 elm= Fiowrate (From ODCM procedure 112-0DC-2.02, Section 8.1.2) Qt(Skln) = 3000/(x/Q) sum(Li+1.1 Mi)SI = 1.01E+04 ucvsec Lowest Qt Value 2.94E+03 uCVsec Ai: From ODCM procedure 11Z-ODC-2.02, Attachment A, Table 2.1-1b Kl.LI & Mi: From ODCM procedure 112-0DC-2.02, Attachment G, Table 2.2-11 Ei: From ODCM procedure 112-0DC-2.02, Attachment B, Tabla 2.1-2b CR= Sum(CIEI) = 4.32E+03 cpm Eia =(CR) I (Sum Cl)= 4.09E+07 cpm/uCUcc Conversion Faclor = 1 / Eia = 2.45E-08 uCl/cc/cpm DV=CR/Eia= 1.0SE-04 uCl/cc Process HSP = ((CR) x (60%: Site Noble Gas Dose Rate Limn)) I Eia = 6.35E-05 uCl/cc = Process HSP 1.77E*03 uCUsec Process ASP =((CR) x (30%: Sita Noble Gas Dose Rate Limit)) I Ela= 3.17E-05 uCi/cc= Process ASP 8.83E+02 uCVsec NOTE: All aquaUons used above are frt1m ODCM procedure 11Z-ODC-2.02, Section 8.1.2 Trip -HSP= 6,35E-05 /(1+.35+.10)= 4.38E-05 uCVcc = Trip HSP = 1.22E+03 uCl/sac Trip -ASP= 3.17E-05 /(1 +.35+.10)= 2.19E-05 uCVcc = Trip ASP = 6.09E*02 uCl/sec

Continuous Release ERS-HHM-87-014 Revision B Unit 2 - DecontarrJnatlon Building Vent PathWay Gaseous Effiuenl Monitor Attachment 3 2RMQ-RQ301 B page 3.;l ok 35 Nucfide Al SI Kl LI Ml Qi Ct El CR AVSumAI KISi (U+1.1Ml)SI SiQt (2.12E-3 Qi)/F CIEi mremJyr mrern/yr mrern/yr mredtyr mrem/yr cpm per per per per per per Ci/yr uCUm3 uCUm3 uCi/m3 ucl/m3 uCi/m3 uCUsec uCi/cc uCUcc cpm 1 Ar-41 O.OE+OO 0.00E+OO 8.84E+03 O.OOE+OO 2.69E+03 9.30E+03 O.OOE+OO O.OOE+OO O.OOE+OO 3.79E+07 O.OOE+OO 2 Kr-83m 0.0E+OO O.OOE+OO 7.56E-02 O.OOE+OO 0.00E+OO 1.93E+01 O.OOE+OO O.OOE+OO O.OOE+OO 0.00E+OO O.OOE+OO 3 Kr-85m O.OE+OO O.OOE+OO 1.17E+03 O.OOE+OO 1.46E+03 1.23E+03 O.OOE+OO O.OOE+OO 0.00E+OO, 3.20E+07 O.OOE+OO 4 Kr-85 O.OE,.00 O.OOE+OO 1.61E+01 O.OOE+OO 1.34E+03 1.72E+D1 O.OOE+OO O.OOE+OO O.OOE+OO 3.BOE+07 O.OOE+OO 5 Kr-87 O.OE+OO O.OOE+OO 5.92E+03 O.OOE+OO 9.73E+03 6.17E+03 0.00E+OO O.OOE+OO 0.00E+OO 3.73E+07 0.00E1'00 6 Kr-86 O.OE+OO O.OOE+OO 1.47E+04 O.OOE+OO 2.37E+03 1.52E+04 O.OOE+OO O.OOE+OO O.OOE+OO 3.05E+07 0.00E+OO 7 Kr-89 O.OE1-00 O.OOE+OO 1.66E+04 O.OOE.. 00 1.01E+04 1.73E+04 O.OOE+OO 0.00E+OO 0.00E+OO 3.72E+07 O.OOE"OO 8 Kr-90 O.OE+OO O.OOE+OO 1.56E+04 O.OOE+OO 7.29E+03 1.63E+04 O.OOE+OO O.OOE+OO 0.00E+OO 3.66E+07 O.OOE+OO 9 Xe-131m O.OE+OO O.OOE+OO 9.15E+01 O.OOE+OO 4.76E+02 1.56E+02 0.00E+OO O.OOE+OO 0.00E+OO 2.44E+07 O.OOE+OO 10 Xe-133m O.OE+OO O.OOE+OO 2.51E+02 O.OOE+OO 9.94E+02 3.27E+02 O.OOE+OO O.OOE+OO 0.00E+OO 2.86E+07 O.OOE+OO 11 Xe-133 1.0E+OO 1.00E+OO 2.94E+02 2.94E+02 3.06E+02 3.53E+02 6.94E+02 1.84E+04 3.16E-03 1.80E+07 5.66E+04 12 Xe-135m O.OE+OO O.OOE+OO 3.12E+03 0.00E+OO 7.11E+02 3.36E+03 O.OOE+OO 0.00E+OO 0.00E+OO 7.22E+06 O.OOE+OO 13 Xe-135 O.OE+OO O.OOE+OO 1.81E+03 0.00E+OO 1.86E+03 1.92E+03 0.00E+OO O.OOE+OO 0.00E+OO 3.86E+07 0.00E+OO 14 Xe-137 O.OE+OO O.OOE+OO 1.42E+03 O.OOE+OO 1.22E+04 1.51E+03 O.OOE+OO O.OOE+OO 0,00E+OO 3.78E1'07 0.00E+OO 15 Xe-138 O.OE+OO O,OOE+OO 8.83E+03 O.OOE+OO 4.13E+03 9.21E+03 O.OOE+OO O.OOE+OO O.COE+OO 3.52E+07 O.COE+OO Totals = 1.0E+UO 2.94E+02 6.94E+02 3.15E-03 *5.66E+04 9.24E-05 sec/m3 = x/Q (From ODCM procedure 1/2-0DC-2.02, Section 8.1.2) Qt[Total Body)= 500/(x/Q) sum(KiSI) = 1.84E+04 uCUsec 12400 elm= Aowrale (From ODOM procedure 1/2-0DC-2.02, Sec1ion 8.1.2) Qt(Skin)=3000/(x/Q) sum(U+1.1Mi)Si = 4.68E+04 uCVsec Lowest QI Value 1.84E+04 uCUsac Al: Assume 100% Xe-133 (ie; No Source-Term In ODOM procedure,1/2-0DC-2.02, Attachment A, Table 2.1-1b Ki.Li & Mi: From ODCM procedure 1/2-0DC-2.02, Attachment G, Table 2.2*11 Ei: From ODCM procedure 1/2-0DC-2.02, Attachment B, Table 2.1-2b CR = Sum(CiEi) = 5.66E+04 cpm Ela= (CR) I (Sum Ci)= 1.80E+07 cpm/uCUcc Conversion Factor= 1 I Ela= 5.SBE-08 uCVcc/cpm DV=CR/Eia= 3.1 SE-03 uCUcc Process HSP = ((CR) x (60%: Site Noble Gas Dose Rate Limit)) I Ela= 1.89E-03 uCUcc = Process HSP Process ASP = ((CR) x (30"/o: Site Noble Gas Dose Rate Limit)) I Eia = 9.44E-04 uCUcc = Process ASP NOTE: All equations used above are from ODOM procedure 1/2-0DC-2.02, Section 8. 1.2 Trtp -HSP= 1.89E-03 I (1 + .35 + .10) = 1.30E-03 uCUcc Trip -ASP= 9.44E-04 I (H .35 + .10) = 6.51E-04 uCUcc

Continuous Release ERS-HHM-87-014 Revision 8 Unil 2 - Wasle Gas Slorage Vault Vent Pathway Gaseous Effluent Monitor Attactvnenl 3 2RMQ-RQ303B page 3~0..\-?£ Nuclide Ai SJ Kl LI Mi QI CJ El CR Ai/Sum Al KISi (U+1.1Mi)SI Si QI (2.12E-3 OQ/F CIEi mrem/yr mremtyr mremtyr mradlyr mremtyr cpm per per per per per per Ci/yr uCilm3 uCVm3 uCVm3 uCl/m3 uCilm3 uCl/sec uCVoc uCllcc c:pm 1 Ar-41 O.OE+OO O.OOE+OO 8.84E+03 0.00E+OO 2.69E+03 9.30E+03 O.OOE+OO o.ooE+oo O.OOE+OO 3.79E+07 O.OOE+OO 2 Kr-83m O.OE+OO O.OOE+OO 7.56E.()2 O.OOE,.00 O.OOE+OO 1.93E+01 O.OOE+OO O.OOE+OO 0.00E+OO O.OOE+OO O.OOE+OO 3 Kr-85m 1.2E-02 5.02E-05 1.17E+03 5.87E-02 1.46E+03 1.23E+03 1.41E.()1 1.22E+OO 1.30E-06 3.20E+07 4.15E+01 4 Kr-85 2.3E+02 9.62E-01 1.61E+01 1.55E+01 1.34E+03 1.72E+01 1.31E+03 2.34E+04 2.48E-02 3.BOE+07 B.94E+05 5 Kr-87 O.OE+OO O.OOE+OO 5.92E+03 O.OOE+OO 9.73E+03 6.17E+03 O.OOE+OO O.OOE+OO 0.00E+OO 3.73E+07 o.ooe ..oo 6 Kr-88 O.OE+OO O.OOE+OO 1.47E+04 O.OOE+OO 2.37E+03 1.52E+04 0.00E+OO O.OOE+OO O.OOE+OO 3.05E+07 O.OOE+OO 7 Kr-69 0.0E+OO 0.00E+OO 1.66E+04 0.00E+oo 1.01E+04 1.73E+04 O.OOE+OO O.OOE+OO 0.00E+OO 3.72E+07 O.OOE+OO 8 Kr-90 O.OE+OO O.OOE+OO 1.66E+04 O.OOE+OO 7.29E+03 1.63E+04 O.OOE+OO O.OOE+OO O.OOE+OO 3.66E+07 O.OOE+OO 9 Xe-131m B.3E-01 3.47E-03 9.15E+01 3.18E.()1 4.76E+02 1.66E+02 2.25E+OO 8.45E+01 6.00E-05 2.44E+07 2.19E+03 10 Xe-133m O.OE+OO O.OOE+OO 2.51E+02 O.OOE+OO 9.94E+02 3.27E+02 O.OOE+OO O.OOE+OO O.OOE+OO 2.66E+07 0.00E+OO 11 Xe-133 B.2E+OO 3.43E-02 2.94E+02 1.01E+01 3.06E+02 3.53E+02 2.38E+01 B.35E+02 B.85E-04 1.BOE+07 1.59E+04 12 Xe-135m O.OE+OO O.OOE+OO 3.12E+03 0.00E+OO 7.11E+02 3.38E+03 O.OOE+OO O.OOE+OO 0.00E+OO 7.22E+06 O.OOE+OO 13 Xe-135 O.OE,.00 O.OOE+OO 1.81E+03 0.00E+OO 1.86E+03 1.92!=+03 O.OOE+OO 0.00E+OO O.OOE+OO 3.66E+07 0.00E+OO 14 Xe-137 O.OE+OO O.OOE+OO 1.42E+03 0.00E+OO 1.22E+04 1.51E+03 O.OOE+OO O.OOE+OO 0.00E+OO 3.78E+07 O.OOE+OO 15 Xe-136 O.OE+OO O.OOE+OO 8.83E+03 0.00E+OO 4.13E+03 9.21E+03 O.OOE+OO O.OOE+OO 0.00E+OO 3.52E+07 O.OOE+OO Tolals = 2.4E+02 2.60[;+01 1.33E+03 2.58E-02 9.12E+05 

                        =

9.24E--05 sec/m3 xJQ (From ODCM procedure 112-0DC-2.02, Sectlon B.1.2) Qt(Total Body)= 500/(xlQ) sum(KISI) = 2.09E+05 uCllsec 2000 dm = Flowrale (From ODCM procedure 1/2-0DC-2.02, Section B.1.2) Qt(Skln) = 3000/(x/Q) sum(U+1.1MQSi = 2.43E+04 uCllsec Lowest Qt Value 2.43E+04 uCllsec Ai: From ODCM procedure 1/2-0DC-2.02, Attachment A, Table 2.1-1b (le; GWS short term) Kl,U & Mi: From ODCM procedure 112-0DC-2.02, Attacllment G, Table 2.2*11 Ei: From ODCM procedure 112-0DC-2.02, Attacllmenl B, Table 2.1-2b CR= Sum(CIEI) = 9. 12E+05 cpm Ela = (CR) I (Sum Cl) = 3.53E+07 cpmluCVoc Conversion Factor= 1 / Eia = 2.63E-OB uCVcc/cpm DV=CR/Eie = 2.68E--02 uCVcc Process HSP =((CR) x (60%: Stte Noble Gas Dose Rate LlmH)) I Ela= 1.SSE-02 uCVoc = Process HSP Process ASP= ((CR) x (30%: Site Noble Gas Dose Rate Llmil)) I Ela= 7.74E--03 uCi/oc =Process ASP NOTE: All equations used above are from ODCM procedure 1/2-0DC-2.02, Section B.1.2 Trip -HSP= 1.55E-02 I (1 + .35 + .10) = 1.07E-02 uCVoc Trip -ASP= 7.74E-03 I (1'+ .35 + .10) = 5.34E-03 uCVoc

ERS-HHM-87-014 Continuous Release Revisions Atta<::hment 3 Unit 2 - Condenste Polishing Bulldln~ Vent Pathway Gaseous Effluent Monitor page:, ll: Ok ~5 2HVL-R0112B Mi Qi Cl Ei CR Nuclide Al Si Kl LI (Lf+1.1Ml)SI SIQI (2.12E-3 01)/F Ci El Al/Sum Ai KISI mremtyr mrad/yr mromtyr cpm mrem/yr mremtyr per per per per per per cpm uCVm3 uCVm3 UCl/m3 uCVsec uCi/cc UCI/cc Ci/yr uCl/m3 uCVm3 O.OOE+OO O.OOE+OO O.OOE+OO 3.79E+07 O.OOE+OO 1 Ar-41 O.OE+OO 0.00E+OO 8.84E+03 O.OOE+OO 2.69E+03 9.30E+03 1.93E+01 O.OOE+OO O.OOE+OO O.OOE+OO O.OOE+OO O.OOE+OO 2 Kr.a3m 0.0E+OO O.OOE+OO 7.56E-02 O.OOE+OO O.OOE+OO 123E+03 D.OOE+OO O.OOE+OO D.OOE+OO 3.20E+07 D.OOE+OO 3 Kr-85m 0.0E+OO O.OOE+OO 1.17E+03 O.OOE+OO 1.46E+03 O.OOE+OO O.OOE+OO O.OOE+OO 3.60E+07 O.OOE+OO 4 Kr-85 O.OE+OO O.OOE+OO 1.61E+01 O.OOE+OO 1.34E+03 1.72E+01 6.17E+03 D.OOE+OD O.OOE+OO D.OOE+OO 3.73E+07 0.00E+OO 5 Kr-87 0.0E+OO D.OOE+OO 5.92E+03 O.OOE+OO 9.73E+03 1.52E+04 O.OOE+OO D.OOE+OO O.OOE+OO 3.05E+07 O.OOE+OO 6 Kr-88 O.DE+OO O.OOE+OO 1.47E+04 O.OOE+OO 2.37E+D3 1.73E+04 D.OOE+OO 0.00E+OO O.OOE+OO 3.72E+07 D.OOE+OO 7 Kr-89 O.OE+OO D.OOE+OO 1.66E+04 O.OOE+OO 1.01E+04 1.63E+04 O.OOE+OO O.OOE+OO O.OOE+OO 3.66E+07 O.OOE+OO 8 Kr-90 0.0E+OO O.OOE+OO 1.56E+04 O.OOE+OO 7.29E+03 1.56E+02 O.OOE+OO O.OOE+OO O.OOE+OO 2.44E+07 0.00E+OO 9 Xe-131m O.OE+OO O.OOE+OO 9.15E+01 O.OOE+OO 4.76E+02 3.27E+02 O.OOE+OO O.OOE+OO O.OOE+OO 2.86E+07 O.OOE+OO 10 Xe-133m O.OE+OO O.OOE+OO 2.51E+02 O.OOE+OO 9.94E+02 3.06E+02 3.53E+02 6.94E+02 2.31E+04 1.61E-03 1.80E+07 2.89E+D4 11 Xe-133 1.0E+OO 1.00E+OO 2.94E+02 2.94E+02 O.OOE+OO 7.11E+02 3.38E+03 O.OOE+OO O.OOE+OO O.OOE+OO 7.22E+06 O.OOE+OO 12 Xe-135m O.OE+OO .Q,OOE+OO 3.12E+03 1.86E+03 1.92E+03 0.00E+OO D.OOE+OO O.OOE+OO 3.86E+07 O.OOE+OO 13 Xe-135 O.OE+OO O.OOE+OO 1.81E+03 O.OOE+OO 1.22E+04 1.51E+03 0.00E+OO O.OOE+OO 0.00E+OO 3.78E+07 O.OOE+OO 14 Xe-137 O.OE+OO O.OOE+OO 1.42E+03 O.OOE+OO 9.21E+03 O.OOE+OO O.OOE+OO O.OOE+OO 3.52E+07 O.OOE+OO 15 Xe-138 0.0E+oo O.OOE+OD 8.83E+03 O.OOE+OO 4.13E+03 6.94E+02 1.61E-03 2.89E+04 Totals = 1.0E+OO 2.94E+02 Qt(Total Body)= 500/(xJQ) sum(KiSI) = 2.31 E+04 uCVsec 7.35E-05 sec/m3 = xJQ (From ODCM procedure 1/2-DDC-2.02, Section 6. 1.2) 30556 ctm = Flowrate (From ODCM procedure 1/2-0DC-2.02, Section 8. 1.2) = Qt(Skin) 3000/(x/Q) sum(Li+1.1Ml)Si = 5.88E+04 uCVsec 2.31E+04 uCVsec Lowest Qt Value Ai: Assume 100% Xe-133 (le; No Source-Term in ODCM procedure 112-0DC-2.02, Attachment A, Table 2.1-1b Ki,Ll & Mi: From ODCM procedure 1/2-DDC-2.02, Attachment G, Table 2.2-11 Ei: From ODCM procedure 1/2-0DC-2.02. Attachment B, Table 2.1-2b CR = Sum(CiEi) = 2.89E+04 cpm 

                                                                                  =

Ela (CR) I (Sum Ci) = 1.80E*07 cpm/uCl/CC Conversion Factor= 11 Ela = 5.56E-08 uCVcclcpm DV=CR/Eia= 1.B 1E-03 uCVcc Process HSP = ((CR) x (60%: Site Noble Gas Dose Rate Limit)) I Ela= 9.63E-04 uCl/cc = Process HSP Process ASP= ((CR) x (30%: Site Noble Gas Dose Rate Limit)) I Eia = 4.82E-04 uCl/cc = Process ASP NOTE: All equations used above are from ODCM procedure 1/2-0DC-2.02, Section 8.1.2 Trip -HSP= 9.63E-04 1(1 + .35+ .10)= 6.64E-04 uCi/cc Trip -ASP= 4.82E-04 /(1 * .35* .10)= 3.32E-04 uCl/cc

ERS-HHM-87-014 Revision 8 Attachment4 Adjustment of Unit 1 Containment Vacuum Pump Source Term page~ cA35 Due to Installation of High Capacity Containment Vacuum Pumps during 1R15 (ECP-02-0079) Ai Ai Nuclide Ai NEW VERSION INCREASE OLD VERSION from to from 112-0DC2.02 1/2-0DC2.02 OLD VERSION Attachment A Attachment A to Table 2.1-1a Table 2.1-1a NEW VERSION and/or and/or Table 2.2-2a Table 2.2-2a Revision O Revision 1 (Ci/yr) (Ci/yr) (Ci/yr) O.OE+OO O.OE+OO 0.00E+OO 1 Ar-41 3.7E-04 S.2E-03 4.81E-03 2 Kr-63m 3.9E-03 5,5E-02 5.07E-02 3 Kr-85m 7.2E-01 l.OE+Ol 9.36E+OO 4 Kr-85 7.8E-04 1. lE-02 1.01E-02 5 Kr-87 5.0E-03 7.0E-02 6.50E-02 6 Kr-88 3.1E-06 4.3E-05 4.03E-05 7 Kr-89 O.OE+OO O.OE+OO O.OOE+OO 8 Kr-90 1.3E-02 1. SE-01 1.69E-01 9 Xe-131m 2.2E-02 3.lE-01 2.86E-01 10 Xe-133m 1.9E+OO 2.7E+Ol 2.47E+01 11 Xe-133 4.4E-05 6.2E-04 5.72E-04 12 Xe-135m 1.9E-02 2.7E-Ol 2.47E-01 13 Xe-135 6.3E-06 8.BE-05 8.19E-05 14 Xe-137 1.2E-04 l.7E-03 1.56E-03 15 Xe-138 4.7E-04 6.6E-03 6.11E-03 16 1-131 2.5E-06 3.SE-05 3.25E-05 17 1-132 8.4E-05 1. 2E-03 1.09E-03 18 1-133 4.7E-07 6.6E-06 6.11E-06 19 1-134 1.4E-05 2.0E-04 1.82E-04 20 1-135 1.GE-05 2.2E-04 2.08E-04 21 Co-58 7.4E-06 1. OE-04 9.62E-05 22 Co-60 4.9E-06 6.9E-05 6.37E-05 23 Mn-54 1.6E-06 2.2E-OS 2.08E-05 24 Fe-59 3.7E-07 S,2E-06 4.81E-06 25 Sr-89 6.6E-OB 9.2E-07 8.58E-07 26 Sr-90 4.9E-06 6.9E-OS 6.37E-05 27 Cs-134 8.4E-06 l.2E-04 1.09E-04 28 Cs-137 O.OE+OO O.OE+OO O.OOE+OO 29 C-14 2.7E+OO 3.8E+01 3.49E+01 NG Totals= 8.SE-03 7.99E-03 Pl Totals = 6.1E-04 2.7E+OO 3.8E+01 3.49E+01 Slim Totals 5 cfm ;,, Old Containment Vacuum Pllmp Flowrate used by S&W in SWEC Calculation UR(B)-262 70 cfm = New High Capacity Containment Vacuum Pump Flowrate DocLJmented in ECP-02-0079, DIE 32 14 = Factor of flowrate increase from the old pumps to the new pumps Ai (OLD VERSION): from ODCM procedure 1/2-0DC-2.02, Attachment A, Table 2.1-1a, Rev 0 These values were developed by S&W in Table 3 of SWEC Calculation UR(B)-262}}

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