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

0 Methodology

O Input Data

l:&:lTransmittal to BVRC

l:&:lOriginal RP ERF FILE

0 MGR, Radiation Protection

D Results

D References

D Data Sheets

D Illustrations

D Printouts

D Code Listings

D Supt, Rad Ops l:&:l Author: Rebecca Novak

D Supv, RP Services l:&:l """'R=o=be""'rt~W.-i ..... n""'"te ...... rs......_ ____ _

D Supv, Rad Waste/Effluents D D

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Radiation Protection Section

DISCUSSION

ERS-HHM-87 -014 Page 2 ~ 35 Revision 8

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 ST A TION

Radiation Protection Section

ERS-HHM-87-014 Revision 8

Unit land 2 Technical Specification Requirements (References I, 2}

Page 3 ~ 3S

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

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Radiation Protection Section

.::;3000 mrem/yr to the Skin

ERS-HHM-87-014 Revision 8

Instrument Error Considerations (References 9, 10, 11)

Page 4 1;; 3S

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

Ai= Particulate Activity from the release path (Ci/yr)

x/Q =Dispersion Parameter (sec/m3)

F =Discharge Flowrate (cfrn)

Ei =Monitor Sensitivity (cpm/uCi/cc)

Ki = Total Body Dose Factor (mrern/yr/uCi/m3)

Li ='Skin Dose Factor (mrem/yr/uCi/m3)

Mi = Gamma Air Dose Factor (mrad/yr/uCi/m3)

Vi = Total Body Dose Rate Factor (mrem/yr/uCi/m3)

Bi= Gamma Air Dose Rate Factor (mrad/yr/uCi/m3)

METHODOLOGY

References

[4, 7 & Attachment 4]

[7]

[7]

[7]

[7]

[7]

[7]

[7]

[7]

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 Qt= (x/Q) L KiSi 'or

500 Qt = (x/Q) L ViSi

where:

i i

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 Q,=-~~~"=-~~~~~ or

(x/Q) Li (Li+ 1. lKi)Si ' 3000

Q,=---~~~~~~~~~

(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

Unit I Mirion:

HSP = (CR *0.60)/Eia = 300 mrem/yr

Unit 2: HSP ~ (CR*0.60)/Eia = 300 mrem/yr

HSP = 0.30 *CR= 900 mrem/yr

ASP= (CR*0.30)/Eia = 900 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.

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Radiation Protection Section

REFERENCES

ERS-HHM-87-014 Revision 8

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

Page 7 "'Q 35

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-107 A 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-87-014 to correct the upper display limits.

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Radiation Protection Section

ATTACHMENTS

ERS-HHM-87-014 . Page 8 Pb 35 Revision 8

I. Alarm Setpoint Summary: Contains the Final Process Alarm Setpoins. This ATTACHMENT is comprised of data from A TI ACHMENT 2 and A IT ACHMENT 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 Si Qt (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

RM-1VS·109 Low

Nuclide

Ar-41

2 Kr-83m

3 Kr-85m

4 Kr-85

5 Kr-87

6 Kr-88

7 Kr-89

8 Kr-90

9 Xe-131m

10 Xe-133m

11 Xe-133

12 Xe-135m

13 Xe-135

14 Xe-137

15 Xe-138

Totals

_Ai_· --- Si Ki ~A7i/~S~u-m-.,.Ai~. "'"""---

~ 2.5E+o1

2.2E-02

1.5E-01

6.1Et-01

5.4E-02

2.4E-01

4.7E-04

0.0E+DO

7.4E-01

8.9E-01

8.9Et-01

4.SE-03

7.0E-01

1.0E-03

1.5E-02

= ---raE+02

1.41E-01

1.24E-04

8.44E-04

3.43E-01

3.04E-04

1.35E-03

2.64E-06

O.OOE+OO

4.16E-03

5.01E-03

5.01E-01

2.53E-05

3.94E-03

5.62E-06

8.44E-05

mrem/yr peruCUm3

8.84E+03

7.56E-02

1.17E+03

1.61E+01

5.92E+03

1.47E+04

1.66E+04

1.56E+04

9.15E+01

2.51E+02

2.94E+02

3.12E+03

1.81E+03

1.42E+03

B.83Et-03

Ki Si mremlyr peruCUm3

1.24E+03

9.35E-06

9.87E-01

5.52E+OO

1.BOE+OO

1.9BE+01

4.39E-02

O.OOE+OO

3.81E-01

1.26E+OO

1.47E+02

7.90E-02

7.13E+OO

7.99E-03

7.45E-01

1.43E+03

LI

mrem/yr peruCUm3

2.69E+o3

O.OOE+oO

1.46E+o3

1.34E+o3

9.73E+03

2.37E+03

1.01E+04

7.29E+03

4.76E+o2

9.94E+o2

3.06E+o2

7.11E+02

1.86E+03

1.22E+04

4.13E+03

Ml

mrad/yrper uCUm3

9.30E+03

1.93E+01

1.23E+03

1.72E+01

6.17E+03

1.52E+04

1.73E+04

1.63E+04

1.56E+02

3.27E+02

3.53E+02

3.36E+03

1.92E+03

1.51E+03

9.21E+03

(Li+1.1MQSi mrem/yr peruCi/m3

1.B2E+03

2.63E-03

2.37E+o0

4.66E+02

5.02E+OO

2.58E+01

7.70E-02

O.OOE+DO

2.70E+o0

6.78E+o0

3.48E+02

1.12E-01

1.56Et-01

7.BOE-02

1.20E+oo

2.69E->-03

QI Cl .:Eo.:.i __ _ SiQt (2.12E-3Ql)F ___ _

~ 1.4BE+02

1.31E-01

8.90E-01

3.62E+02

3.20E-01

1.42E+OO

2.79E-03

O.OOE+OO

4.39E+OO

5.28E+o0

5.2BE+02

2.67E-02

4.15E+oo

5.93E-03

B.90E-02

uCVcc

1.0SE-05

9.22E-09

6.29E-OB

2.56E-05

2.26E-OB

1.01E-07

1.97E-10

O.OOE+OO

3.10E-07

3.73E-07

3.73E-05

1.B9E-09

2.93E-07

4.19E-10

6.29E-09

7.45E-05

cps per uCi/cc

1.60E+05

O.OOE+OO

1.14E+05

1.14E+05

1.77E+05

1.05E+05

1.B9E+05

1.B9E+-04

7.22E+-04

1.28E+o5

4.39E+04

3.28E+-04

1.37E+05

1.83E+05

1.43E+-05

Attachment 2 , C... Page \\. C\)3~

CR CiEi

cps

1.6BE+OO

O.OOE+OO

7.17E-03

2.92E+OO

4.01E-03

1.0SE-02

3.72E-05

0.00E+oO

2.24E-02

4.78E-02

1.64E+o0

6.19E-05

4.02E-02

7.67E-05

B.99E-04

6.36E+OO

3.32E..Q4 sec/m3 = x/Q (from ODCM procedure 1/2-0DC-2.02, Section 8.1.1) 30000 elm = Flowrate (from ODCM procedure 1/2-0DC-2.02, Section B.1.1)

Qt (Total Body)= 500/ (x/Q) sum (KiSQ= 1.05E+o3 uCi/sec 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

Process HSP = ((CR) x (30%: Sfte Noble Gas Dose Rate Limft)) I Eia 2.24E-05 uCI I cc= Process ASP

Note: All equations used above are from ODCM procedure 1/2-0DC-2.02, Section B.1.2

Unusual Event = Alert=

1.05E-+03 uCi I sec x 1.05E+03 uCI/ sec x

2 = 2.10E+o3 uCUsec 200 = 2.10E+-05 uCl/sec

632.BB uCi/sec 316.44 uCi/sec

Batch Release ERS-HHM-ll7-014 Revision 8

Unit 1 - Containment Purge VIA Ventilation Vent Pathway Gaseous Effluent Monitor Attachment2

RM-1VS-109 High

2

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7

8

9

10

11

12

13

14

15

Nuclide _A_i ___ Si Ki LI Mi Qi Ci Ei Ai/SumAI Ki Si (ll+1.1Mi)Si Si Qt (2.12E-3 Oi)F

mremJyr mrem/yr mrem/yr mrad/yr per mrem/yr amps per

~ ear uCVm3 eeruCVm3 eeruCVm3 uCVm3 eeruCVm3 uCVsec uCVcc uCVcc

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

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

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

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

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

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

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

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

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

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

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

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

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

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

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

Totals 1.8E+ii2 1.43E+03 2.69E+03 7.45E-05

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}= 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=

Lowest Qt Value = 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•) ff 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

Process HSP = ((CR) x (30%: Site Noble Gas Dose Rate Limit)) I Eia 2.24E-05 uCi I cc= Process ASP

Note: All equations used above are tram ODCM procedure 112-0DC-2.02, Section B.1.2

Unusual Event = Alert=

1.0SE+o3 uCi I sec x 1.05E+o3 uCJ I sec x

2 = 2.1 OE+03 uCVsec 200 = 2.10E+05 uCilsec

Page \'2-o\- 36 CR CiEi

am es 1.57E-15

4.37E-18

1.06E-17

4.SBE-15

2.44E-18

2.32E-17

3.49E-20

0.00E+OO

8.59E-17

8.47E-17

1.82E-14

2.26E-20

5.72E-17

4.90E-20

1.00E-18

2.47E-14

1.05E+o3 uCi/sec 3.36E;-03 uC!/o:ec 1. 05E+o3 uCi/sec

632.88 uCVsec 316.44 uCi/sec

Batch Release

Unit 1 • Containment Purge VIA Rx Containmeni/SLCRS Vent Pathway Gaseous Effluent Monilcr (Victoreen)

RM·1VS-107B

Nuclide Af Si Ki LI

Ai/Sum Al Ki Si

mrem/yr mrem/yr mremlyr per per per

Cl/yr uCi/m3 uCl/rn3 UCi/m3

1'Ar-41 2.5E+01 1.41E--01 8.84E+03 1.24E+03 2.69E+03

2 Kr.a3m 2.2E-02 1.24E--04 7.56E.{)2 9.35E--06 0.00E+OO

3 Kr-85m 1.SE-01 8.44E.{)4 1.17E+03 9.87E--01 1.46E+03

4 Kr-85 6.1E+01 3.43E--01 1.61E+01 5.52E+OO 1.34E+03

5 Kr-87 5.4E·02 3.04E-04 5.92E+03 1.80E+OO 9.73E+03

6 Kr-88 2.4E-01 1.35E-03 1.47E+04 1.98E+01 2.37E+03

7 Kr-89 4.7E-04 2.64E-06 1.66E+04 4.39E-02 1.01E+04

8 Kr-90 O.OE+OO O.OOE+OO 1.56E+04 O.OOE+OO 7.29E+03

9 Xe-131m 7.4E-01 4.18E-03 9.15E+01 3.81E-01 4.76E+02

10 Xe·133m B.9E-01 5.01E-03 2.51E+02 1.26E+OO 9.94E+02

11 Xe-133 8.9E+01 5.01E-01 2.94E+02 1.47E+02 3.06E+02

12 Xe-135m 4.SE-03 2.53E-05 3.12E+o3 7.90E-02 7.11E+02

13 xe-135 7.0E-01 3.94E-03 1.81E+03 7.13E+OO 1.86E+03

14 Xe-137 · 1.0E-03 5.62E-06 1.42E+03 7.99E-03 1.22E+04

15 Xe-138 1.SE-02 B.44E-05 B.83E+03 7.45E-01 4.13E+03

Totals = 1.8E+02 1.43E+03

3.0BE-04 sec/m3 = X/Q (From ODCM procedure 1/2-0DC·2.02, Section 8.1.1) 7500 elm= Flowrate (From ODCM procedure 1'2-0DC-2.02. Section 8.1.1)

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

Mi

mrad/yr per

uCi/m3

9.30E+03

1.93E+01

1.23E+03

1.72E+01

6.17E+03

1.52E+04

1.73E+04

1.63E+04

1.56E+02

3.27E+02

3.53E+02

3.36E+03

1.92E+03

1.51E+03

9.21E+03

Qi Ci

(Li+1.1Ml}SI SI Qt (2.12E..J Qi)/F

mremlyr per

UCl/m3 uCUsec UC I/cc

1.82E+03 1.60E+02 4.52E-05

2.63E--03 1.41E-01 3.9BE-08

2.37E+OO 9.59E-01 2.71E-07

4.66E+02 3.90E+02 1.10E-04

5.02E+OO 3.45E.{)1 9.76E-08

2.58E+01 1.53E+OO 4.34E-07

7.70E-02 3.01E-03 8.49E·10

O.OOE+OO O.OOE+OO O.OOE+OO

2.70E+OO 4.73E+OO 1.34E-06

6.7BE+OO 5.69E+OO '1 1.61E-06

3.4BE+02 5.69E+02 1.61 E.{)4

1.12E.{)1 2.BBE-02 B.13E-09

1.56E+01 4.4BE+OO 1.27E-06

7.BOE--02 6.39E--03 1.81E-09

1.20E+OO 9.59E-02 2.71E-08

2.69E+03 3.21E·04

Qt(Total Body)= 500/(x/Q) sum(KiSQ = Ql(Skin) = 3000/(x/Q) sum(U+1.1Ml)SI =

Lowest Qt Value -

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 = HSP =(CR x 0.3) wtlere; 0.3 = 30% Of the Site Noble Gas Dose Rate Limit=

7.63E+03 cpm = Process HHSP 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 Trip

-HHSP= -HSP=

7.63E+03 /(1 +.35+.10)= 3.81E+03 /(1 + .35+ .10)=

5.26E+03 cpm 2.63E+03 cpm

ER5-HHM-8HJ14

El

cpm per

uCUcc

7.19E+07

O.OOE+OO

5.16E+07

5.04E+07

9.60E+07

5.16E+07

9.59E+07

9.87E+07

2.94E+07

4.17E+07

2.2BE+07

1.51E+07

6.42E+07

1.05E+08

7.35E+07

Revision 8 Attachment2

page ~\~4J~S

CR

CiEi

cprn

3.25E+03

O.OOE+OO

1.401:-t-01

5.56E+03

9.37E+OO

2.24E+01

8.15E-02

O.OOE+OO

3.93E+01

6.71E+01

3.67E+03

1.23E-01

8.12E+01

1.90E-01

1.99E+OO

1.27E+04

1.14E+03 uCVsec 3.62E+03 uCi/sec 1.14E+03 uCi/sec

Batch Release ERS-ttHM-87-014

Revision 8

Unit 1 - Containment Purge VIA Rx Containment I SLCRS Vent Pathway Gaseous Effluent Monitor Attachment 2

Page IL.\: cQ :£:i RM-1VS-110 Low

2

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12

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14

15

Nuclide _A_i ___ SI Ki LI Mi QI Ci El CR

NI Sum Ai Ki Si (Li+1.1 MllSI Si Qt (2.12E-3 Qi)F CIEi

mremlyr mremtyr mrem/yr mrad/yrper mremlyr cps per

~ eeruCVm3 ear uCVm3 eeruCVm3 uCVm3 eeruCVm3 ~ uCVcc uCVcc £l!S

Ar-41 2.5Et01 1.41E-01 8.B4Et03 1.24E-t03 2.69E+03 9.30E-t03 1.82E-t03 1.60E+o2 4.52E-05 1.60E+05 7.23E+OO

t<r-83m 2.2E-02 1.24E-04 7.56E-02 9.35E-Q6 O.OOE+OO 1.93E.,01 2.63E-03 1.41E-01 3.98E-OS O.OOE+oo O.OOE+OO

Kr·85m 1.SE-01 B.44E-04 1.17E+03 9.87E-01 1.46E+03 1.23E.,03 2.37E+OO 9.59E-01 2.71E-07 1.14E1"05 3.09E-02

Kr-85 6.1E+o1 3.43E-01 1.61E+01 5.52E.,OO 1.34E+03 1.72E+01 4.66E+02 3.9DE+o2 1.10E-o4 1.14Et05 1.26ET01

Kr-87 5.4E-Q2 3.04E-Q4 5.92E+03 1.80E+OO 9.73E+o3 6.17E.,03 5.02E+OO 3.45E-01 9.76E-08 1.77Et05 1.73E-02

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 1.05E+05 4.55E-02

Kr-89 4.7E-04 2.64E-Q6 1.66E+04 4.39E-02 1.01E+04 1.73E.,04 7.70E-02 3.01E-03 8.49E-10 1.89E+o5 1.61E-Q4

Kr-90 O.OE+OO 0.00E+oo 1.56E+o4 0.00E.,00 7.29E+o3 1.63E.,04 O.OOE+oo O.OOE.,00 O.OOE+OO 1.89E+04 O.OOE+OO

Xe-131m 7.4E-01 4.16E-03 9.15E+01 3.81E-01 4.76E+02 1.56E+02 2.70E+OO 4.73E+OO 1.34E-06 7.22E+04 9.66E-02

Xe-133111 8.9E-01 5.01E-03 2.51E+02 1.26E+oo 9.94E+02 3.27E+o2 6.78E+OO 5.69E+OO 1.61E-06 1.28E+o5 2.06E-01

Xe-133 8.9E+o1 5.01E-01 2.94E+02 1.47E+o2 3.06E+02 3.53E+o2 3.4BE+02 5.69E+02 1.61E-04 4.39E+04 7.06E+OO

Xe-135m 4.SE-03 2.53E-05 3.12E+03 7.90E-02 7.11E+02 3.36E+o3 1.12E-01 2.SBE-02 8.13E-09 3.28E+04 2.67E-04

Xe-135 7.0E-01 3.94E-03 1.81E+03 7.13E+o0 1.86E+03 1.92E+03 1.56E+01 4.4BE+OO 1.27E-06 1.37E+05 1.73E-01

Xe-137 1.0E-03 5.62E-06 1.42E-t03 7.99E-03 1.22E+04 1.51E-t03 7.SOE-02 6.39E-03 1.B1E-09 1.83E+05 3.31E-04

Xe-138 1.SE-02 B.44E-05 8.83E+03 7.45E-01 4.13E+03 9.21E+03 1.20E-t00 9.59E-02 2.71E-08 1.43Et05 3.88E-03

Totals 1TE+02 1.43E+03 2.69E+D3 3.21E-04 2.74E+01

3.08E-Q4 secJm3 = xlQ (from ODCM procedure 112-0DC-2.02, Section B.1.1) 7500 elm = Flowrate (from ODCM procedure 1/2-0DC-2.02, Section 8.1.1)

Qt (Total Body)= 500/ (xlQ) sum (KiSi)= 1.14E+o3 uCVsec 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) fl Efficiencies found in Mirian MCNP Analysis for NGM204 Monitor, pg 16

CR= Sum(CiEi) = 2.74E+D1 Eia = (CR) I (Sum Ci) = 8.54E+04

Conversation Factor= 1 I Ela = 1.17E-05 Conversation Factor = 1 I Ela = 4.33E+05

DV = CR I Ela = 3.21 E-04 Process HHSP =((CR) x (60%: Site Noble Gas Dose Raia Limit)) I Eia 1.93E-04

Process HSP = ((CR) x (30%: Site Noble Gas Dose Rate Limit)) I Ela 9.64E-05

cps cps I uCi/ cc uCi/cc/cps Bq/m3/cps uCilcc uCI I cc = Process HSP uCI I cc = Process ASP

Note: All equations used above are from ODCM procedure 112-0DC-2.02, Section 8.1.2

Unusual Evant= Alert=

1.14E+03 uCi I sec x 1.14E+03 uCI/ sec

2 = 2.28E+03 uCVsec 200 = 2.28E+05 uCVsec

662.19 uCVsec 341.10 uCVsac

Balch Release ERS-HHM-87..014

Revision 8

Unit 1 - Containment Purge VIA Rx Containment I SLCRS Vent Pathway Gaseous Effluent Monitor Attachmant2

t&S RM-1VS-110 High

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Nuclide _Al ___ Si Ki Li Mi Qi Ci El

Ai /Sum Ai Ki Si (Li+1.1Mi)Si SiQt (2. 12E-3 Ql)F

mrem/yr mrem/yr mrem/yr mradlyr per mrem/yr amps per

.E!!E_ eeruCUm3 ~ruCUm3 earuCVm3 uCVm3 eeruCVm3 ~ uCUcc uCVcc

Ar-41 2.5E+01 1.41E-01 B.84E+03 1.24E+o3 2.69E+03 9.30E+o3 1.82E+o3 1.60E+o2 4.52E..05 1.50E-10

Kr-83m 2.2E-02 1.24E-04 7.56E..02 9.35E-06 O.OOE+OO 1.93E+01 2.63E..03 1.41E-01 3.98E..08 4.74E-10

Kr-85m 1.SE..01 8.44E-04 1.17E+03 9.87E..01 1.46E+o3 1.23E+o3 2.37E+OO 9.59E-01 2.71E-07 1.69E-10

Kr-85 6.1E+01 3.43E-01 1.61E+01 5.52E+OO 1.34E+03 1.72E+o1 4.66E+02 3.90E+o2 1.10E-04 1.79E-10

Kr-87 5.4E-02 3.04E-04 5.92E+o3 1.BOE+OO 9.73E+03 6.17E+o3 5.02E+DO 3.45E-01 9.76E..Q8 1.0BE-10

Kr-88 2.4E-01 1.35E-03 1.47E+04 1.98E+D1 2.37E+03 1.52E+04 2.5BE+01 1.53E+oo 4.34E-07 2.31E-10

Kr-89 4.7E-04 2.64E-06 1.66E+04 4.39E-02 1.01E+04 1.73E+D4 7.70E-02 3.D1E-03 8.49E-10 1.77E-10

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 2.37E-11

Xa-131m 7.4E-01 4.16E-03 9.15E+01 3.81E..01 4.76E+D2 1.56E+02 2.70E+OO 4.73E+DO 1.34E-06 2.77E-10

Xa-133m B.9E..01 5.01E-03 2.51E+o2 1.26E+OO 9.94E+02 3.27E+D2 6.78E+OO 5,69E+o0 1.61E-06 2.27E-10

Xe-133 8.9E+01 5.01E-01 2.94E+02 1.47E+02 3.06E+02 3.53E+02 3.48E+02 5.69E+D2 1.61E-04 4.69E-10

Xa-135m 4.5E-03 2.53E-05 3.12E+o3 7.90E-02 7.11E+02 3.36E-+-03 1.12E-01 2.88E-02 8.13E-09 1.20E-11

Xa-135 7.0E..01 3.94E-03 1.81E+o3 7.13E+OO 1.86E+03 1.92E-+-03 1.56E+01 4.4BE+OO 1.27E-06 1.95E-10

Xa-137 1.0E-03 5.62E-06 1.42E+o3 7.99E-03 1.22E+04 1.51E+-03 7.BOE-02 6.39E-03 1.81E-09 1.17E-10

Xe-138 1.SE-02 8.44E-05 8.83E+03 7.45E-01 4.13E+03 9.21E+03 1.20E+OO 9.59E-02 2.71E-08 1.69E-10

Totals 1.6E+li2 1.43E+03 2.69E+D3 3.21E-04

3.0BE-04 sec/m3 = x/Q (from ODCM procedure 1/2-0DC-2.02. Section 8.1.1) Qt (T D1al Body) = 500 I (x/Q) sum (KISI)=

7500 cfm = Flowrate (from ODCM procedure 112-0DC-2.02, Section 8.1.1) Ql (Skin)= 3000 I (x/Q) sum (Li+1.1Mi)Si= Lowest Qt Value =

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

Process HSP =((CR) x (30%: Site Noble Gas Dose Rate Limit)) I Eia 9.64E-05 uCi I cc= Process ASP

Nola : All equations used above are from ODCM procadure 1/2-0DC-2.02, Section B.1.2

Unusual Event = Alert=

1. 14E+03 uCI/ sec 1.14E+03 uCi I sec x

2 = 2.28E+03 uCi/sac 200 = 2.28E+05 uCi/sac

Page~ \I'S

CR CiEi

am!:!s

6.7BE-15

1.BBE-17

4.58E-17

1.97E-14

1.05E-17

1.00E-16

1.SOE-19

O.OOE+oo

3.70E-16

3.65E-16

7.87E-14

9.76E-20

2.47E-16

2.11E-19

4.SBE-18

1.0GE-13

1.14E+03 uCVsec 3.62E+03 uCVsec 1.14E+03 uCVsec

682.19 uCVsac 341.10 uCi/sec

Batch Release

Unit 112 - Decay Tank Discharge VIA Process Vent Pathway Gaseous Effluent Monitor (Victoreen)

RM-1GW-10BB

Nuclide Ai SI VI LI Bl

Al/Sum Ai VISi (Li(X/Q)+1.1Bi)SI

mremlyr mrem/yr mremtyr per per per

Cl/yr uCl/sec uCl/sec uCilm3

1 Ar-41 O.DE+OO O.OOE+OO 2.BBE-03 O.OOE+OO 2.69E+03

2 Kr-B3m O.OE+OO O.OOE+OO 4.58E-D8 0.00E+OD O.OOE+OO

3Kr~m 7.3E-02 2.87E-04 4.70E-04 1.35E-D7 1.46E+03

4 Kr-BS 2.3E+02 9.04E-01 5.54E-ll6 5.01E-06 1.34E+03

5 Kr-87 D.OE+OO O.OOE+DO 1.45E-03 0.0DE+OO 9.73E+03

6 Kr-88 0.0E+OO O.OOE+DO 4.09E-03 0.0DE+OO 2.37E+03

7 Kr-89 O.OE+OO O.OOE+OO 1.25E-03 O.OOE+OO 1.01E+04

8 Kr-90 O.OE+OO O.OOE+OO O.OOE+OO O,OOE+OO 7.29E+03

9 Xe-131m 1.3E+OD 5.11E-03 1.67E-04 8.53E-07 4.76E+02

10 Xa-133m 0.0E+OO D.OOE+OO 1.32E-04 O.ODE+OO 9.94E+02

11 Xe-133 2.3E+01 9.04E-02 1.54E-04 1.39E-05 3.06E+02

12 Xe-135m O.OE+OO 0.00E+OO 6.21E-04 O.ODE+OO 7.11E+02

13 Xe-135 O.OE+OO O.OOE+OO 6.96E-04 0.0DE+OO 1.86E+03

14 Xe-137 0.0E+OO O.OOE+OO 9.66E-05 0.DOE+OD 1.22E+D4

15 Xe-138 O.OE+OO O.OOE+OO 2.22E--03 O.OOE-tOO 4.13E+03

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) 1450 ctm = Flowrate (From ODCM procadure 1/2-0DC-2.02, Section 6.1.3)

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

mradlyr per

uCVsec

4.02E-D3

3.96E-05

7.06E-04

B.40E-06

2.19E-03

6.16E-03

1.BSE-03

O.OOE+OD

3.09E-04

2.61E-04

2.76E-D4

9.SOE-04

1.0SE-03

1.46E-04

3.34E-03

Qi Cl

SI Qt (2.12E-3 Ql)Jf

mrem/yr per

uCi/sec uCi/sec uCi/cc

D.DOE+OO O.OOE+OO o.OOE+OO

O.OOE+OO O.ODE+OO O.OOE+OO

4.71E-06 6.46E+01 9.44E-05

1.30E-02 2.04E+05 2.98E-01

O.OOE+OO O.OOE+OO O.OOE+OD

0.00E+OD O.OOE+OO O.OOE+OO

O.OOE+OO O.OOE+OO O.OOE+OO

O.OOE+OO O.OOE+OO 0.00E+OO

2.78E-05 1.15E+03 1.68E-03

O.ODE+OO O.OOE+OO O.OOE+OO

3.23E-04 2.04E+04 2.98E-02

O.OOE+OO D.OOE+OO O.ODE+OO

O.OOE+OO 0.0DE+OD D.ODE+OD

D.OOE+OO 0.0DE+OO O.ODE+OD

O.OOE+OO O.OOE+OO 0.00E+OO

1.33E-02 3.29E-01

Qt(Total Body) = 500/sum(VISi) = Ql(Skln) = 3000/sum(Li(X/Q)'+1.1Bi)SI =

Lowest Qt Value

Ei: From ODCM procedure 1/2-0DC-2.02, Attachment 8, Table 2.1-2• CR= Sum(CIEI) = 3.93E+05 cpm = CR

2.36E+05 cpm = Process HHSP 1.18E+05 cpm= Process HSP

HHSP =(CR x 0.6) 'Mlere;'0.6 = 60% of lhe Site Noble Gas Dose Rate Limit= HSP = (CR x 0.3) Wiere; 0.3 = 30% of the Site Noble Gas Dose Rate Umlt =

NOTE: All equations used above are from ODCM procedure 112-0DC-2.02, Secijon 8.1.3

Trip Trip

-HHSP= -HSP=

2.36E+05 1(1 + ,35+ .10) = 1.18E+05 I (1 + .35 + .10) =

1.63E+05 cpm 6.13E+04 cpm

ERS-HHM-87-014

El

cpm per

uCVcc

6.59E+D7

D.OOE+OO

9.00E+07

3.56E+05

6.78E+07

1.05E+OB

1.2BE+08

1.23E+08

2.07E+06

1.16E+07

9.24E+06

6.58E+07

1.03E+OB

2.91E+07

1.06E+08

Revision B Attachment2 S page fj 11..o ctJ 3

CR

Ci El

cpm

O.OOE+OO

O.OOE+OO

6.60E+03

1.06E+D5

O.OOE+DO

O.OOE+DO

O.OOE+OO

O.OOE+OO

3.48E+D3

O.OOE+OO

2.75E-tD5

0.00E+OO

O.ODE+OD

O.ODE+OO

O.OOE+OO

3.93E+05

2.51E•07 uCVsec 2.25E+05 uCVsec 2.25E+05 uCVsec

Batch Release ERS-HHM-87--014 Revision 8

Unit 1 - Decay Tank Discharge VIA Process Vent Pathway Gaseous Effluent Monitor Attachment 2 f 6,S Page P'.J l 1- O

RM-1GW-109 Low

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Nuclide Al Si VI Li Bl Qi Cl Ei Ai/SumAI Vi Si {Li(x/Q)+1.1 Bl)SI SI Qt (2.12E-3 Ql)/F

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

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

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

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

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

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

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

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

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

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

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

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

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

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

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

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 ----Totals 2.5E+02 1.99E-05 1.33E-02 3.29E-01

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) = 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 =

Lowest Qt Value = 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 Eia = (CR) I (Sum Cl) = 1.07E+05

ConverseUon Factor= 1 / Eia = 9.31 E-06 Conversation Factor c 11 Ela = 3.44E+05

DV = CR I Ela = 3.29E-01 Process HHSP = ((CR) x (60%: Site Noble Gas Dose Rate Limit)) I Eia 1.97E-01

Process HSP = ((CR) x (30%: Site Noble Gas Dose Rale Limit)) I Ela 9.87E-02

cps cps luCi I cc uCI I CC/ cps Bq /rn3 /cps uCl/cc uCI I cc = Process HSP uCI I cc = Process ASP

Note : All equations used above are from ODCM procedure 1/2-0DC-2.02, Section 8.1.2

CR CIEi

cps

O.OOE+OO

0.00E+OO

1.08E+01

3.39E+04

O.OOE+OO

O.OOE+OO

0.00E+OO

O.OOE+OO

1.21E+02

0.00E+OO

1.31E+03

O.OOE+OO

O.OOE+OO

O.OOE+OO

O.OOE+OO

3.54E+04

2.51E+07 uCl/sec 2.25E+05 uCi/sec 2.25E+05 uCl/sec

135048.79 uCi/sec 67524.39 uCllsec

Batch Release ERS-HHM-87-014

Unit 1 - Decay Tank DIScharga VIA Process Vent Pathway Gaseous Effluent Monitor

RM-1GW-109 High

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~ _A_I ___ SI Vi _LI ___ Bl Qi Ci El Al I Sum Ai ----~ (Ll(x/Q)+1.1 Bi)Si Si Qt (2.12E.J 01)/F

~ mrad/yr mrem/yr mrem/yr per mrem/yr per per amp per

.9!l!._ ~ruCVm3 ~ peruCl/m3 uCVmJ ~ ~ ~ .!!9!!£_ 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

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

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

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

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

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

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

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

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

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

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

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

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

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

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

~ = 2.5E+02 ----~ ~ 3.29E-01

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) = 1450 cfm = Flowrate (from ODCM procedure 1/2-0DC-2.02, SecUon 8.1.3) Qt(Skln)= 3000/sum(Ll(x/Q) + 1.1BQSi =

Lowest Qt Value = 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 Ela= (CR) I (Sum Ci) = 2.08E-10

Conversauon Factor= 11 Ela = 4.82E+09 Conversation Factor= 1 /Ela = 1.7BE+20

DV = CR I Ela = 3.29E-01 Process HHSP =((CR) X (60%: Sile Noble Gas Dose Rate Umlt)) I Ela 1.97E-01

Process HSP = ((CR) x (30%: Site Noble Gas Dose Rate Umlt)) I Ela 9.B7E-02

amps amp/uCl/cc uCl/cc/ amp Bq/m3/amp uCi/cc uCI I cc= Process HSP uCi I cc= Process ASP

Note: All equations used above are from ODCM procedure 1/2-0DC-2.02, Section B.1.2

Revision 8 Attachment 2

l'b~~6 Page~

CR CIEi

ame:s 0.00E+OO

O.OOE+OO

1.SOE-14

5.33E-11

O.OOE+OO

0.00E+OO

0.00E+OO

O.OOE+OO

4.66E-13

O.OOE+OO

1.46E-11

0.00E+OO

O.OOE+OO

0.00E+OO

0.00E+OO

6.83E-11

2.51 E+07 uCi/sec 2.25E+05 uCVsec 2.25E+05 uCVsec

135048.79 UCl/sac 67524.39 uCJ/sec

Batch Release

Unit 2 - Conlainment Purge VIA SLCRS Unfiltered Pathway Gaseous Effluent Monitor

2HVS-RQ1018

Nuclide Al SI Kl Li Ml Qi Cl

AUSumAI KiSI (Ll+1.1Ml)SI Si Qt (2.12E-3 Ql)/F

mremlyr mram/yr mrem/yr mrad/yr mrem/yr per per per per per

CliYr uCl/m3 UCi/m3 uCi/m3 uClhn3 uCl/m3 uCJ/sec uCi/cc - -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

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

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

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

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

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

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

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

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

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

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

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

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

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

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

Totals = 1.7E+02 1.44E+03 2.72E+03 7.39E-05

3.32E-04 sac/m3= x/Q (From ODCM procedure 112-0DC-2.02, Seclion B.1.2) 30000 cfm = Flowrate (From ODCM procedure 112-0DC-2.02, Section B.1.2)

Q1[rotal Body)= 500/(x/Q) sum(KiSI) = Qt(Skln) = 3000/(x/Q) sum(Ll+1.1 Mi)SI =

Lowest 01 Value 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) = Eia = (CR) I (Sum Cl) =

Converalon Faclor = 1 I Eia = DV=CR/Ela=

Process HSP = ((CR) x (60%: Site Noble Gas Dose Rate Limit)) I Ela= Process ASP =((CR) x (30%: Site Noble Gas Dose Rate Umll)) I Ela=

2.02E+03 cpm 2.74E+07 cpm/UCi/cc 3.65E-OB uCi/oclcpm 7.39E-05 UCl/cc 4.43E-05 UCl/cc = Process HSP 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 Trip

-HSP= -ASP=

4.43E-05 /(1 + .35+ .10) = 2.22E-05 /(1 + ,35+ .10) =

3.06E-05 uCi/cc 1.53E-05 uCVcc

ERS-HHM-87-014

Ei

cpm per

uCVcc

3.79E+07

O.OOE+OO

3.20E+07

3.60E+07

3.73E+07

3.05E+07

3.72E+07

3.86E+07

2.44E+07

2.86E+07

1.80E+07

7.22E+06

3.86E+07

3.7BE+07

3.52E+07

Revision B Attachment 2

page ,q '{) ~S

CR

Ci El

cpm

4,08E+02

O,OOE+OO

1.93E-01

9.44E+02

8.50E-05

5.38E·02

O.OOE+DO

O.DOE+DO

7.56E+OO

9.35E+DO

6.50E+02

O.OOE+DO

3.98E+DO

O.OOE+OO

O.OOE+OO

2.02E+03

1.0SE.,.03 uCi/sec 3.32E+03 uCVeec 1.05E+03 uCVsec

Batch Release

Unit 2 - Containment Purge VIA SLCRS Fntered Pathway Gaseous Effluent Monttor

2HVS-RQ1098

Nuctida /'J SI Kl Li Mi Qi Cl

AVSumAi Ki Si (Li+1.1Ml)SI SI Qt (2.12E-3 Ql)/F

mrem/yr mrem/yr mrem/yr mrad/yr mremlyr per per par par per

Cl/yr uCi/m3 UCl/m3 uCi/m3 uCi/m3 uCl/m3 uCi/sec ucvcc

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

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

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

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

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

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

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 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

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

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

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

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

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

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

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

Totals= 1.7E+02 1.44E+03 2.72E+03 3.18E-04

3.0BE-04 serJm3 = x/Q (From ODCM procedure 112-0DC-2.02, Section 8.1.2) 7500 cfm = Flowrate (From ODCM procedure 1/2-0DC-2.02, Section 8.1.2)

Qt(Total Body)= 500/(xlQ) sum(KiSi) = Qt(Skin) = 3000/(x/Q} sum(Ll+1.1Ml}SI =

Lowest Qt Value 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) = Ela= (CR} I (Sum Ci)=

Conversion Factor= 1 I Ela= DY= CR/Eia=

Process HSP =((CR) x (60%: Site Noble Gas Dose Rate Limit))/ Ela= Process ASP= ((CR) x (30%: Site Noble Gas Dose Raio Limit)) I Eia =

1.64E+04 cpm 5.15E+07 cpm/UCi/cc 1.94E--08 UCl/cc/cpm 3.18E-04 UCt/cc 1.91 E-04 UCt/cc = Process HSP 9.55E--05 UC!lcc = Process ASP

NOTE: All equations used above are from ODCM procedure 112-0DC-2.02, Section B.1.2

Tr1p Trip

-HSP= -ASP=

1.91E-04 /(1 + .35 + .10) = 9.SSE-05 I (1 + .35 + .10) =

1.32E-04 uCl/cc =Trip HSP = 6.59E-05 uCi/cc = Trip ASP =

ERS-HHM-87-014

El

cpm per

uCVcc

7.90E+07

O.OOE+OO

5.83E+07

7.19E+07

8.85E+D7

6.80E+D7

8.73E+07

8.BOE+07

4.61E+04

6.06E+04

2.94E+07

1.55E+04

7.48E+07

9.07E+07

7.74E+07

Revision B Anachment 2 f5'

page p~ 2o 'b 3.

CR

CiEi

cpm

3.66E+03

O.OOE+OO

1.51E+OO

8.13E+03

8.70E-04

5.17E-01

O.OOE+OO

O.OOE+OO

6.16E-02

8.54E-02

4.58E+03

O.OOE+OO

3.33E+01

O.OOE+OO

O.OOE+OO

1.64E+04

1.13E+03 uCVsec 3.58E+03 uCilsec 1.13E+03 uCVsec

6. 76E+02 uCVaec 3.36E+02 uCVsec

4.86E+02 uCl/sec 2.33E+02 uCl/sec

Continuous Release

Unil 1 - Ventilation Vent Palhway Gaseous Effluent Monitor (Vlc1oreen)

RM-1VS-1018

Nudide Al SI Kl Li

Ai/Sum Ai KISI

mrem/yr mrem/yr mrem/yr per per per

Ci/yr uCl/m3 uCVm3 uCi/m3

1 Ar-41 O.OE+OO O.OOE+OO 8.84E+03 O.OOE+OO 2.69E+03

2 Kr-63m 4.2E-01 7.SOE--03 7.SSE-02 5.B7E--04 O.OOE+OO

3 Kr-65m 1.9E+OO 3.57E-02 1.17E+03 4.18E+01 1.46E+03

4 Kr-85 2.5E+OO 4.70E-02 1.61E+01 7.57E-01 1.34E+03

5 Kr-87 1.3E+OO 2.44E-02 5.B2E+03 1.45E+02 9.73E+D3

6 Kr-88 3.8E+OO 7.14E-02 1.47E+04 1.05E+03 2.37E+03

7 Kr-89 1.2E-01 2.26E-o3 1.66E+04 3.75E+01 1.01E+04

8 Kr-90 O.OE+OO o.OOE+OO 1.56E+04 O.OOE+OO 7.29E+03

9 Xe-131m 1.3E-01 2.44E-03 9.15E+01 2.24E-01 4.76E+02

10 Xe-133m B.9E-01 1.67E-02 2.51E+02 4.20E+OO 9.94E+02

11 Xe-133 3.8E+01 6.77E-01 2.94E+02 1.99E+02 3.06E+02

12 Xe-135m 3.2E-01 6.02E-03 3.12E+03 1.88E+01 7.11E+02

13 Xe-135 4.5E+OO B.46E-02 1.81E+03 1.53E+02 1.86E+03

14 Xe-137 2.1E-01 3.95E-03 1.42E+03 5.61E+OO 1.22E+D4

15 Xe-138 1.1E+OO 2.07E-02 8.83E+03 1.83E+02 4.13E+03

Totals = 5.3E+01 1.84E+03

1.03E-04 sec/m3 = x/Q (From ODCM procedure 1'2-0DC-2.02, Section B.1.1) 62000 cfm = Flowrate (From ODCM procedure 1'2-0DC-2.02, Section 8.1.1)

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

HHSP = (CR x o.8) 'Mlere; 0.6 = 60% of the Site Noble Gas Dose Rate Limit= HSP =(CR x 0.3) Wtere; 0.3 = 30% of the Site Noble Gas Dose Raia Limit=

Mi

mradlyr per

uCi/m3

9.30E+03

1.93E+01

1.23E+03

1.72E+01

6.17E+03

1.52E+04

1.73E+04

1.63E+04

1.56E+02

3.27E+02

3.53E+02

3.36E+03

1.92E•03

1.51E+03

9.21E•03

QI Cl

(Li+1.1Mi)Si Si Qt (2.12E-3 Ql)/F

mrem/)lr per

uCUm3 uCVsec uCi/cc

0.00E+OO O.OOE+OO O.OOE+OO

1.68E-01 2.09E+01 7.13E-07

1.00E+02 9.43E+01 3.23E-06

6.39E+01 1.24E+02 4.24E-06

4.04E+02. 6.45E+01 2.21E-06

1.36E+03 1.89E+02 6.45E-06

6.57E+01 5.96E+OO 2.04E-07

O.OOE+OO O.OOE+OO O.OOE+OO

1.5BE+OO 6.45E+OO 2.21E-07

2.27E+01 4.42E+D1 1.51E-06

4.70E+02 1.79E+03 6.11E-05

2.65E+01 1.59E+01 5.43E-07

3.36E+02 2.23E+02 7.64E-06

5.47E+01 1.D4E+01 3.56E-07

2.95E+02 5.46E+01 1.87E-06

3.20E+03 9.03E-05

Ql(Total Body)= 500/(xlQ) sum(KISI) = Ql(Skln) = 3000/(xlQ) sum(Li+1.1 Mi)Si =

Lowest Qt Value

CR= sum(CIEl) = 3.00E+03 cpm =CR 1.80E+03 cpm =Process HHSP 9.00E+02 cpm = Process HSP

NOTE: All equations used above are from ODCM procedure 112-0DC-2.02, Section B.1.1

Trip Trip

-HHSP= -HSP=

1.80E+03 /(1 + .35+ .10)= 9.00E+02 I (1 + .35 + .10) =

1.24E+03 cpm 6.21E+02 cpm

ERS-HHM-87-014

Ei

cpm per

uCi/cc

7.17E+07

O.OOE+OO

9.80E+07

3.88E+05

7.38E+07

1.14E+OB

1.39E+08

1.34E+08

2.25E+06

1.28E+07

1.01E+07

7.15E+07

1.12E+OB

3.16E+07

1.15E+08

Revisicn8 Attachment~

page ;;).\

CR

CiEI

cpm

O.OOE+OO

o.ooe+oo

3.16E+02

1.85E+OO

1.63E+02

7.35E+02

2.83E+01

O.OOE+OO

4.97E-01

1.90E+01

6.17E+02

3.88E+01

8.56E+02

1.13E+01

2.15E+02

3.00E+03

2.64E+03 uCl/sec 9.09E+03 UCl/sec 2.64E+03 UCiloec

Continuous Release ERS-HH~?-014

Unit 1 - Ventilation Vent Pathway Gaseous Effluent Monitor

RM-1VS-109 low

2

3

4

5

6

7

B

9

10

11

12

13

14

15

~ N Si Kl Li Mi Qi Ci Ei Ai/Sum Ai KiSi lli+1.1Mi)Si SiQt (2.12E-3 Qi)F

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

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

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

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

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

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

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

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

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

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

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

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

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

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

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

Tui8is-- 5.3E+o1 1.64E+o3 3.20E+03 9.03E-05

1.03E-04 secJm3 • )(}Q (from ODCM procedure 112-0DC-2.02, Section 8.1.1) QI (Total Body)= 500 I ("1Q) sum (KiSi)= 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=

Lowest Qt Value = 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) = Ela = (CR) I (Sum Ci) =

Conversation Factor• 1 /Ela = Conversation Factor = 1 /Ela =

DV=CR/Eia = Process HHSP =((CR) x (60%: Site Noble Gas Dose Rate Limil)) I Eia

Process HSP = ((CR) x (30%: Sile Noble Gas Dose Rate Limit)) I Eia

6.25E+OO 6.92E+04 1.45E--05 5.35E+05 9.03E--05 5.42E-05 2.71E-05

cps cps/uCi/cc uCi I eel cps Bq I m3 /cps uCilcc · uCi I cc = Process HS P uCi I cc= Process ASP

Note : All equations used above are from ODCM procedure 1/2-0DC-2.02, Section 8.1.2

Unusual Event= Alen=

2.64E+03 uCi I sec 2.64E+o3 uCi I sec

2 = 5.28E+03 uCVsec 200 = 5.2SE+o5 uCVsec

Revision B Attachment 3 o-\ Page ;;):;} 35 CR CiEi

~· O.OOE+OO

0.00E+OO

3.68E-01

4.B4E-01

3.91E-01

6.77E-01

3.85E-02

O.OOE+OO

1.59E-02

1.93E-01

2.6BE+oo

1.7BE-02

1.DSE+oo

6.52E-02

2.67E-01

6.25E+OO

2.64E+03 uCUsec 9.09E+o3 uCVsec

2640.52199 uCVsec

1584.3132 uCVsec 792.156598 uCVsec

Continuous Release ERS-HHM-87--014 Revisions

Unit 1 - Ventilation Vent Pathway Gaseous Effluent Monitor Attachment 3 !!J5 Page :;:i~'b

RM-1VS-109 High

1

2

3

4

5

6

7

8

9

10

11

12

13

14

15

~ _Ai_. __ Si Ki Li Mi Qi Ci Ei Ai/Sum Ai KiSI (Li+1.1 MilSi SiQt (2.12E-3 Qi)F

mrem/yr mremlyr mrem/yr mrad/yr per mrem/yr amps per

~ eeruCVm3 2eruCVm3 eeruCUm3 uCUm3 ~ruCi/m3 uCVsec uCUcc uCUcc

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

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

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

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

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

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

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

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

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

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

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

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

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

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

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

~ = 53E+01 1.84E+03 3.20E+03 9.03E--05

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)= 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=

Lowest Qt Value = 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

amps amps I uCi I cc uCi/ cc I amps Bq/m3 /amps uCi/cc

CR= Sum(CIEI) = Eia = (CR) I (Sum Ci) =

Conversation Fader = 1 I Ela = Conversation Factor= 1 I Ela =

DV=CR/Eia = Process HHSP = ((CR) x (60%: Sita Noble Gas Dose Rate Limit)) I Eia

Process HSP =((CR) x (30%: Site Noble Gas Dose Rate Limit)) I Eia

3.55E-14 3.94E-10

2.54E+09 ·9.40E+19 9.03E--05 5.42E--05 2.71E--05

uCI I cc= Process HSP uCi I cc = Process ASP

Neta: All equations used above are from ODCM procedure 112-0DC-2.02, Section 8.1.2

Unusual Event = Alert=

2.64E+D3 uCi I sec 2.64E+03 uCI I sec x

2 = 5.28E+o3 uCUsec 200 = 5.28E+o5 uCUsec

)

CR CiEI

am es

O.OOE+-00

3,38E-16

5.45E-16

7.60E-16

2.38E-16

1.49E-15

3.61E-17

O.OOE+-00

6.11E-17

3.43E-16

2.99E-14

6.52E-18

1.49E-15

4.17E-17

3.16E-16

3.55E-14

2.64E+03 uCUsec 9.09E+03 uCUsec 2.64E+03 ucusec

1584.31 uc~sec 792.16 uCUsec

ConUnuous Release

Unit 1 • Rx Con!alnment/SLCRS Vent Pathway Gaseous Effluent Monitor (Victoreen)

RM-1VS-107B

Nuclide Al Si Kl Li

Ai/Sum Ai KISI

mrem/yr mrem/yr mremtyr per per par

Cl/yr uCiim3 uCi/m3 uCi/m3

1 Ar-41 2.5E+01 1.41E-01 8.B4E+03 1.24E+03 2.69E+03

2 Kr-B3m 2.2E-02 1.24E-04 7.56E-02 9.35E-06 O.OOE+OO

3 Kr-85m 1.SE-01 8.44E-04 1.17E+03 9.87E-01 1.46E+03

4 Kr-85 6.1E+01 3.43E-01 1.61E+01 5.52E+OO 1.34E+03

5 Kr-87 ·S.4E-02 3.04E-04 5.92E+03 1.BOE+OO 9.73E+03

6 Kr-86 2.4E-01 1.35E-03 1.47E+04 1.9l!E+01 2.37E+03

7 Kr-89 4.7E-04 2.64E-06 1.66E+04 4.39E--02 1.01E+04

8 Kr-90 0.0E+OO O.OOE+OO 1.56E+04 0.00E+OO 7.29E+03

9 Xe-131m 7.4E-01 4.16E-03 9.15E+01 3.81E-01 4.76E+02

10 Xe-133m 8.9E-01 5.01E-03 2.51E+02 1.26E+OO 9.114E+02

11 Xe-133 8.9E+01 5.01E-01 2.94E+02 1.47E+02 3.06E+02

12 Xe-135m 4.SE-03 2.53E-05 3.12E+03 7.00E-02 7.11E+02

13 Xe-135 7.0E-01 3.94E-03 1.81E+03 7.13E+OO 1.B6E+03

14 Xe-137 1.0E-03 5.62E-06 1.42E+03 7.99E--03 1.22E+04

15 Xe-138 1.SE-02 B.44E-05 6.63E+03 7.45E-01 4.13E+03

Totals= 1.8E+02 1.43E+03

9.24E-05 sec/m3 = x/Q (From ODCM procedure 1/2-0DC-2.02, Section 8.1.1) 49300 cfm = Rowrate (From ODCM procedure 1/2-0DC-2.02, Section 8.1.1)

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

HHSP =(CR x 0.6) IM!ere; 0.6 = 60% of the Sile Noble Gas Dose Raio Limit= HSP =(CR x 0.3) \Miera; 0.3 = 30% of the Site Noble Gas Dose Rate Limit=

Ml

mrad/yr per

UCl/m3

9.30E+03

1.93E+01

1.23E+03

1.72E+01

6.17E+03

1.52E+04

1.73E+04

1.63E+04

1.56E+02

3.27E+02

3.53E+02

3.36E+03

1.92E+03

1.51E+03

9.21E+03

Qi Ci

(LI+ 1.1 Ml)SI SIQt (2.12E-3 Qi)/F

mrem/yr per

uCUm3 uCl/sec uCUcc

1.B2E+03 5.33E+02 2.29E-05

2.63E-03 4.69E-01 2.02E-08

2.37E+OO 3.20E+OO 1.37E-07

4.66E+02 1.30E+03 5.59E-05

5.02E+OO 1.15E+OO 4.95E-08

2.58E+01 5.12E+OO 2.20E-07

7.70E-02 1.00E-02 4.31E-10

O.OOE+OO 0.00E+OO O.OOE+OO

2.70E+OO 1.58E+01 6.78E--07

6.78E+OO 1.90E+01 B.16E--07

3.48E+02 1.90E+03 8.16E-05

1.12E--01 9.59E-02 4.12E-09

1.56E+01 1.49E+01 6.42E-07

7.BOE-02 2.13E-02 9.17E-10

1.20E+OO 3.20E-01 1.37E-08

2.69E+03 1.63E-04

Qt(To!al Body) = 500/(x/0) sum(KiSI) = . Ql(Skin) = 3000/(x/Q) sum(Li+1.1 Mi)Si =

Lowest Oi Value

CR= Sum(CiEi) = 6.44E+03 cpm =CR 3.87E+03 cpm = Precess HHSP 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 Trip

-HHSP= -HSP=

3.87E+03 I (1 + .35 + .10) = 1.93E+03 I (1 + .35 + .10) =

2.67E+03 cpm 1.33E+03 cpm

ERS-HHM-87--014

El

cpm per

uCUcc

7.19E+07

O.OOE+OO

5.16E+07

5.04E+07

9.60E+07

5.16E+07

9.59E+07

9.87E+07

2.94E+07

4.17E+07

2.28E+07

1.51E+07

6.42E+07

1.05E+06

7.35E+07

Revision a Attachment 3 {

page <S)L{ 0 . ~

CR

Ci El

cpm

1.65E+03

O.OOE+OO

7.09E+OO

2.82E+03

4.75E+OO

1.14E+01

4.13E--02

O.OOE+OO

1.99E+01

3.40E+01

1.86E+03

6.23E--02

4.12E+01

9.62E-02

1.01E+OO

6.44E+03

3.79E+03 UCl/sac 1.21 E+04 UCUsec 3.79E+03 uCl/sec

Continuous Release ERS-HHM-87--014 Revision 8

Unit 1 - Rx Containment I SLCRS Vent Pathway Gaseous Effluent Monitor Attachment 3

Page :;FJ ~35 RM-1VS-110 Low

2

3

4

5

6

7

8

9

10

11

12

13

14

15

Nuclide _A_I __ Si Ki Li Mi Qi Ci Ei CR Ail Sum Ai Ki Si (Li+1.1Mi!Si SiQt (2.12E-3 Qi)F CiEi

mrem/yr mrem/yr mremlyr mradlyr per mrem/yr cps per

·---- .£!!l'.!:_ ~ruCVm3 ~ruCVm3 2er uCVm3 uCVm3 ~eruCVm3 uCVsec uCVcc ucvcc cps

Ar-41 2.5E+01 1.41E--01 B.84E+03 1.24E+o3 2.69E+o3 9.30E+D3 1.B2E+o3 5.33E+02 2.29E--05 1.60E+05 3.67E+oo

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

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

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

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

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

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

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

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

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

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

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

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

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

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) 49300 elm = Flowrate (from ODCM procedure 1/2-0DC-2.02, Section B.1.1)

QI (Total Body)= 500 I (x/Q) sum (KiSi}= 3.79E+03 uCVsec 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) = Ela = (CR) I (Sum Ci) =

Conversation Factor= 1 / Eia = Conversation Factor= 1 I Ela =

DV= CR/Ela = Process HHSP =((CR) x (60%: Site Noble Gas Dose Raia Limit)) I Eia

Process HSP =((CR) x (30%: Site Nobie Gas Dose Rate Limit)) I Eia

1.39E+-01 8.54E+04 1.17E--05

4.33E+-05 1.63E-04 9.78E-05 4.89E-05

cps cps /uCi I cc uci I cc/cps Bq/ m3/cps uCi/cc uCi I cc = Process HSP uCI I cc= Process ASP

Note : All equations used above are from ODCM procedure 112-0DC-2.02, Section 8. 1 .2

Unusual Event = Alert=

3.79E+03 uCi I sec 3.79E+03 uCi I sec

2 = 7.SBE+-03 uCYsec 200 = 7.58E+05 uCYsec

2273. 97 uCVsec 1136.99 uCVsec

Continuous Release ERS..HHM-87-014 Revision a

Untt 1 - Rx Containment I SLCRS Vent Pathway Gaseous Effluent Monttor Attec/vnent 3 .,-{ 3S

RM-1VS-110 High

2

3

4

5

6

7

B

10

11

12

13

14

15

~ _A_i ___ Si Ki Li Mi QI Cl Ei

---- Ai I Sum Ai KiSI (Ll+1.1Ml}Si Si Qt (2.12E~ Qi)F mrem/yr mrem/yr mrem/yr mradlyrper mrem/yr amps per

~ peruCUm3 ---- peruCUm3 peruCilm3 uCVm3 peruCVm3 uCVsec ucvcc uCVcc

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

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

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

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

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

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

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

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

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

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

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

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

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

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

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

Totals = 1]E+Q2 1.43E+D3 2.69E+03 1.63E-04

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)= 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=

Lowest Qt Value= 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) = Eia = (CR) I (Sum C~ =

Conversation Factor = 1 I Eia = Conversation Fac1or = 11 Eia ~

DV= CR/Eia = Process HHSP = ((CR) x (60%: Sile Nobie Gas Dose Rate Limit)) I Eia

Process HSP = ((CR) x (30%: Sile Noble Gas Dose Rate Limit)) I Eia

5.39E-14 3.31E-10

3.02E+09 1.12E+20 1.63E-04 9.78E--05 4.B9E-05

amps amps I uCi I cc uCI I cc I amps Bq/m3/amps uCl/cc uCI I cc = Process HSP uCi I cc = Process ASP

Nole : All equations used above are from ODCM procedure 1/2-0DC-2.02, Section 8.1.2

Unusual Even\= Alert=

3.79E-t-03 uCi I sec 3.79E+03 uCI /sec x

2 = 7.58E+03 uCUsec 200 = 7.58E+05 uCUsec

Page ;;,Jl.9

CR CiEi

amps

3.44E-15

9.56E-1B

2.32E-17

1.0DE-14

5.35E-1B

s.oeE-17

7.62E-20

0.00E+OO

1.BBE-16

1.85E-16

3.99E-14

4.95E-20

1.25E-16

1.07E-19

2.32E-18

5.39E-14

3.79E+03 uCUsec 1.21E+D4 uCVsec 3. 79E+03 uCUsec

2273.97 uCl/sec 1136.99 uCl/sec

Contlnuous Release

Unit 112 - Process Vent Pathway Gaseous Effluent Monitor (Vlctoreen)

RM-1GW.108B

Nuclide Al SI Vi Li Bi QI Cl

Ai/Sum Al VlSI (Li(X/Q)+1.1 Bi)Si Si Qt (2.12E-3 Qi)/F

mrem/yr mrem/yr mrem/yr per per per

Cl/yr UC I/sec uCl/sec uCi/m3

1 Ar-41 O.OE+OO O.OOE+OO 2.68E-03 O.OOE+OO 2.69E+03

2 Kr-a3m 5.SE-01 5.06E-03 4.58E-08 2.32E-10 O.OOE+OO

3 K'r-asm 2.5E+OO 2.2BE-02 4.70E-04 1.07E-05 1.46E+03

4 Kr-1!5 1.4E+01 1.30E--01 5.54E--06 7.19E-07 1.34E+03

5 Kr-1!7 1.7E+OO 1.53E--02 1.45E-03 2.22E-D5 9.73E+03

6 Kr-1!8 4.9E+OO 4.52E-02 4.09E-03 1.85E-04 2.37E+03

7 Kr-1!9 1.SE-01 1.43E-03 1.25E--03 1.79E-06 1.01E+04

8 Kr-90 0.0E+OO O.OOE+OO O.OOE+OO O.OOE+OO 7.29E+03

9 Xe-131m 3.SE-01 3.29E-03 1.67E-04 5.SOE-07 4.7BE+02

10 Xe-133m 1.5E+OO 1.34E-02 1.32E-04 1.77E-06 9.94E+02

11 Xe-133 7.5E+01 6.91E-01 1.54E-04 1.06E-04 3.06E+02

12 Xe-135m 4.0E-01 3.71E-03 6.21E-04 2.31E-06 7.11E+02

13 Xe-135 5.9E+OO 5.46E-02 6.96E-04 3,80E-05 1.86E+03

14 Xe-137 2.6E-01 2.41E-03 9.66E-05 2.33E-07 1.22E+04

15 Xe-138 1.3E+OO 1.23E-02 2.22E-03 2.72E-05 4.13E+03

Totals = 1.1E+02 3.97E-04

2.31 E-06 seclm3 = )tJQ (From ODCM procedure 1/2-0DC-2.02, Section 8.1.3) 1450 cfm = Flowrate (From ODCM procedure 1/2-0DC-2.02, Secllon 8.1.3)

Ai: Derived from ODCM procedure 1/2-0DC-2.02, Attactvnent A, Table 2.1-1 a, as follows:

mrad/yr per

uCl/seo

4.02E-03

3.96E·05

7.06E-04

6.40E.Q6

2.19E-03

6.16E-03

1.88E-03

0.00E+OO

3.09E-04

2.BIE-04

2.76E-04

9.SOE-04

1.0SE-03

1.46E-04

3.34E-03

mrem/yr per

uCl/sec uCl/sec uCl/cc

O.OOE+OO O.OOE+OO O.OOE+OO

2.20E-07 5.53E+03 8.0~E-03

9.46E-D5 2.49E+04 3.64E-02

4.03E-04 1.42E-t05 2.07E-01

3.81E-04 1.87E+04 2.45E-02

5.54E-04 4.94E+04 7.22E-02

3.63E-05 1.56E+03 2.2BE-03

O.OOE+OO O.OOE+OO O.OOE+OO

4.74E--06 3.60E+03 5.26E-03

3.47E-05 1.47E+04 2.15E-02

6.9BE-04 7.55E+05 1.10E+OO

9.98E--06 4.06E+03 5.94E-03

2.97E-04 5.97E+04 8.72E-02

6.83E-05 2.64E+03 3.65E-03

1.62E-04 1.34E+04 1.96E-02

2.74E-03 1.80E+OO

Qt(Total Body)= 500/sum(ViSi) = Qt(Skin) = 3000/sum(Li(X/Q)+1.1Bi)Si =

Lowest Qt Value

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

HHSP = (CR x 0.6) Vlliere; 0.6 = 60% of the Site Noble Gas Dose Rate Limit= HSP =(CR x 0.3) 'Mlere; 0.3 = 30% of the Site Noble Gas Dose Rate Lim~=

CR = Sum(CIEI) = 3.49E+07 cpm = CR 2.09E+07 cpm = Process HHSP 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 Trip

-HHSP= -HSP=

2.09E+07 I (1 + .35 + .1 O) = 1.05E+07 /(1 + .35+ .10) =

1.44E+07 cpm 7 .22E+06 cpm

ERS·HHM-a7-ll14 Revision 8

Attactvnent3

page t?j OJ-:\- o.f 3?

Ei

cpm per

UCl/cc

6.59E+07

O.OOE+OO

9.00E+07

3.56E+05

6.78E+07

1.05E+OB

1.28E+08

1.23E+08 ~

2.07E+06

1.16E+07

9.24E+06

6.58E+07

1.03E+08

2.91E+07

1.06E+OB

CR

CIEi

cpm

O.OOE+OO

O.OOE+oo

3.28E+06

7.39E+04

1.66E+06

7.59E+06

2.92E+05

O.OOE+OO

1.09E+04

2.49E+05

1.02E+07

3.91E+05

8.98E+06

1.12E+05

2.08E+06

3.49E+07

1.26E+06 uCl/sec 1.09E+06 uCl/sec 1.09E+06 uCi/sec

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

CR • Sum(CiEi) = Eia = (CR) I (Sum Ci) •

Conversation Factor• 1 I Eia • Conversation Factor• 1 I Eia •

DV= CR/Eia • Process HHSP • ((CR) x (60%: Sile Noble Gas Dose Rate Limft)) I Ela

Process HSP = ((CR) x (30%: Sile Noble Gas Dose Rate Limit)) I Ela

6.34E-10 3.97E-10 2.52E-t09 9.33E+19 1.60E-t00 9.59E-01 4.80E-01

amps amps I uCi I cc uCi I cc I amps Bq/m3/amps uCi/cc uCi I cc • Process HSP uCi I cc • Process ASP

If Alarm setpolnt are above Instrument display range, use 10% for lower and 30% upper of the display range for the set points

4.93E-04 cps 3.0BE-04 cps I uCi I cc

3.24E-t03 1.20E+14 Bq/m3/amps 1.60E->OO uCVcc 4.BOE-01 uCVcc 655975.35 uCUsec 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 ~· 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 0.00E+OO

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

CR= Sum(CIEi) = Eia = (CR) I (Sum Cl) =

Conversation Factor = 1 I Eia = Conversation Factor= 1 I Eia =

DV=CR/Eia = Process HHSP =((CR) x (60%: Site Noble Gas Dose Rate Limit)) I Eia

Process HSP = ((CR) x (30%: Site Noble Gas Dose Reta Limit)) I Ela

1.07E+05 6.72E+D4 1.49E-05

5.51E+05 1.60E+oo 9.59E-01 4.BOE-01

cps cps/uCi/cc uCi/ cc/ cps Bq I m3 /cps uCi/ cc uCi I cc = Process HSP uCi I cc = Process ASP

If Alarm setpoint are above instrument display range, use 10% for lower and 30% upper or the display range for the setpolnts

4.93E-04 cps 3.0BE-04 cps I uCI I cc

3.24E+03 1.20E+14 1.60E+OO uCVcc 4.80E-01 uCVcc 655975.35 uCVsec 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

Unit 2 • SLCRS Unfiltered Pathway Gaoeoua Effluent Monitor

2HVS-RQ101B

Nuclide Ai SI Kl LI Ml Qi Ci

Ai/Sim Al Ki Si {Ll+1.1 Mi)Si Si Qt (2.12E~ Ql)IF

mrem/yr mrem/yr mrem/yr mradlyr mrem/yr per per per per per

Ci/yr uCi/m3 uCl/m3 uCi/m3 uCilrn3 uCUm3 uCi/sec uCi/cc

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

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

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

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

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

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

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

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

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

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

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

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

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

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

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

Totals= 1.7E+02 1.44E+03 2.72E+03 3.01E-04

1.03E.{)4 sec/m3 = xJQ (From ODCM procedure 1 /2·0DC-2.02, Section 8.1.2) 23700 cfm = Flowrate {From ODCM procedure 1/2-0DC-2.02, Section 8.1.2)

Qt(Total Body)= 500/(x/Q) sum(KiSi) = Qt(Skin) = 3000/(xJQ) si.m(Li+1.1Ml)SI =

Lowest Qt Value 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) = Eia = {CR) I (Sum Ci) "

Conversion Faclor = 1 /Ela= DV=CR/Ela=

Process HSP ={{CR) x (60%: Site Noble Gas Dose Rate Limit)) I Eia = Process ASP= ((CR) x (30%: Stte Nobie Gas Dose Rate Limit)) I Ela;

8.26E+03 cpm 2. 7 4E+07 cpm/uCl/cc 3.65E.{)8 uCUcc/cpm 3.01 E-04 uCVcc 1.81E.{)4 uCucc= Process HSP 9.04E.{)5 uCUcc = Process ASP

NOTE: All equations used above are from ODCM procedura 112-00C-2.02, Seclion 8.1.2

Trip Trip

-HSP= -ASP;

1.B1E.{)4 I (1 + .35 + .10) = 9.04E-05 I (1 + .35 + .10) =

1.25E.{)4 uCVcc 6.24E-05 uCVce

ERS·HHM-87.{)14

El

epm per

UC Vee

3.79E+07

0.00E+OO

3.20E+07

3.60E+07

3.73E+07

3.05E+07

3.72E+07

3.86E+07

2.44E+07

2.86E+07

1.80E+07

7.22E+06

3.86E+07

3.78E+07

3.52E+07

Revisions Attachment3

page30~ "55

CR

CiEI

cpm

1.66E+03

O.OOE+OO

7.BBE.{)1

3.85E+03

3.47E.{)4

2.19E.{)1

0.00E+OO

O.OOE+OO

3.0BE+01

3.81E+01

2.65E+03

O.oOE+OO

1.63E+01

O.OOE+OO

O.OOE+OO

8.26E+03

3.37E+03 uCVsec 1.07E+04 uCusec 3.37E+03 uCVsec

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 1 IZ-ODC-2.02, Section 6.1.2) Qt(T otsl 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

Unit 2 - DecontarrJnatlon Building Vent PathWay Gaseous Effiuenl Monitor

2RMQ-RQ301 B

Nucfide Al SI Kl LI Ml Qi Ct

AVSumAI KISi (U+1.1Ml)SI SiQt (2.12E-3 Qi)/F

mremJyr mrern/yr mrern/yr mredtyr mrem/yr per per per per per

Ci/yr uCUm3 uCUm3 uCi/m3 ucl/m3 uCi/m3 uCUsec uCi/cc

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

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

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,

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

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

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

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

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

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

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

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

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

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

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

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

Totals = 1.0E+UO 2.94E+02 6.94E+02 3.15E-03

9.24E-05 sec/m3 = x/Q (From ODCM procedure 1/2-0DC-2.02, Section 8.1.2) 12400 elm= Aowrale (From ODOM procedure 1/2-0DC-2.02, Sec1ion 8.1.2)

Qt[Total Body)= 500/(x/Q) sum(KiSI) = Qt(Skin)=3000/(x/Q) sum(U+1.1Mi)Si =

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) = Ela= (CR) I (Sum Ci)=

Conversion Factor= 1 I Ela= DV=CR/Eia=

Process HSP = ((CR) x (60%: Site Noble Gas Dose Rate Limit)) I Ela= Process ASP = ((CR) x (30"/o: Site Noble Gas Dose Rate Limit)) I Eia =

Lowest QI Value

5.66E+04 cpm 1.80E+07 cpm/uCUcc 5.SBE-08 uCVcc/cpm 3.1 SE-03 uCUcc 1.89E-03 uCUcc = Process HSP 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 Trip

-HSP= -ASP=

1.89E-03 I (1 + .35 + .10) = 9.44E-04 I (H .35 + .10) =

1.30E-03 uCUcc 6.51E-04 uCUcc

ERS-HHM-87-014

El

cpm per

uCUcc

3.79E+07

0.00E+OO

3.20E+07

3.BOE+07

3.73E+07

3.05E+07

3.72E+07

3.66E+07

2.44E+07

2.86E+07

1.80E+07

7.22E+06

3.86E+07

3.78E1'07

3.52E+07

Revision B Attachment 3 page 3.;l ok

CR

CIEi

cpm

O.OOE+OO

O.OOE+OO

O.OOE+OO

O.OOE+OO

0.00E1'00

0.00E+OO

O.OOE"OO

O.OOE+OO

O.OOE+OO

O.OOE+OO

5.66E+04

O.OOE+OO

0.00E+OO

0.00E+OO

O.COE+OO

·5.66E+04

1.84E+04 uCUsec 4.68E+04 uCVsec 1.84E+04 uCUsac

35

Continuous Release

Unil 2 - Wasle Gas Slorage Vault Vent Pathway Gaseous Effluent Monitor

2RMQ-RQ303B

Nuclide Ai SJ Kl LI Mi QI CJ

Ai/Sum Al KISi (U+1.1Mi)SI Si QI (2.12E-3 OQ/F

mrem/yr mremtyr mremtyr mradlyr mremtyr per per per per per

Ci/yr uCilm3 uCVm3 uCVm3 uCl/m3 uCilm3 uCl/sec uCVoc

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

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

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

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

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

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

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

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

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

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

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

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

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

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

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

Tolals = 2.4E+02 2.60[;+01 1.33E+03 2.58E-02

9.24E--05 sec/m3 = xJQ (From ODCM procedure 112-0DC-2.02, Sectlon B.1.2) 2000 dm = Flowrale (From ODCM procedure 1/2-0DC-2.02, Section B.1.2)

Qt(Total Body)= 500/(xlQ) sum(KISI) = Qt(Skln) = 3000/(x/Q) sum(U+1.1MQSi =

Lowest Qt Value 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) = Ela = (CR) I (Sum Cl) =

Conversion Factor= 1 / Eia = DV=CR/Eie =

Process HSP =((CR) x (60%: Stte Noble Gas Dose Rate LlmH)) I Ela= Process ASP= ((CR) x (30%: Site Noble Gas Dose Rate Llmil)) I Ela=

9. 12E+05 cpm 3.53E+07 cpmluCVoc 2.63E-OB uCVcc/cpm 2.68E--02 uCVcc 1.SSE-02 uCVoc = Process HSP 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 Trip

-HSP= -ASP=

1.55E-02 I (1 + .35 + .10) = 7.74E-03 I (1'+ .35 + .10) =

1.07E-02 uCVoc 5.34E-03 uCVoc

ERS-HHM-87-014

El

cpm per

uCllcc

3.79E+07

O.OOE+OO

3.20E+07

3.BOE+07

3.73E+07

3.05E+07

3.72E+07

3.66E+07

2.44E+07

2.66E+07

1.BOE+07

7.22E+06

3.66E+07

3.78E+07

3.52E+07

Revision 8 Attactvnenl 3

3~0..\-?£ page

CR

CIEi

c:pm

O.OOE+OO

O.OOE+OO

4.15E+01

B.94E+05

o.ooe .. oo

O.OOE+OO

O.OOE+OO

O.OOE+OO

2.19E+03

0.00E+OO

1.59E+04

O.OOE+OO

0.00E+OO

O.OOE+OO

O.OOE+OO

9.12E+05

2.09E+05 uCllsec 2.43E+04 uCllsec 2.43E+04 uCllsec

ERS-HHM-87-014 Continuous Release Revisions

Unit 2 - Condenste Polishing Bulldln~ Vent Pathway Gaseous Effluent Monitor Atta<::hment 3

Ok page:, ll: ~5 2HVL-R0112B

Nuclide Al Si Kl LI Mi Qi Cl Ei CR

Al/Sum Ai KISI (Lf+1.1Ml)SI SIQI (2.12E-3 01)/F Ci El

mrem/yr mremtyr mremtyr mrad/yr mromtyr cpm

per per per per per per

Ci/yr uCl/m3 uCVm3 uCVm3 uCVm3 UCl/m3 uCVsec uCi/cc UC I/cc 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.a3m 0.0E+OO O.OOE+OO 7.56E-02 O.OOE+OO O.OOE+OO 1.93E+01 O.OOE+OO O.OOE+OO O.OOE+OO O.OOE+OO O.OOE+OO

3 Kr-85m 0.0E+OO O.OOE+OO 1.17E+03 O.OOE+OO 1.46E+03 123E+03 D.OOE+OO O.OOE+OO D.OOE+OO 3.20E+07 D.OOE+OO

4 Kr-85 O.OE+OO O.OOE+OO 1.61E+01 O.OOE+OO 1.34E+03 1.72E+01 O.OOE+OO O.OOE+OO O.OOE+OO 3.60E+07 O.OOE+OO

5 Kr-87 0.0E+OO D.OOE+OO 5.92E+03 O.OOE+OO 9.73E+03 6.17E+03 D.OOE+OD O.OOE+OO D.OOE+OO 3.73E+07 0.00E+OO

6 Kr-88 O.DE+OO O.OOE+OO 1.47E+04 O.OOE+OO 2.37E+D3 1.52E+04 O.OOE+OO D.OOE+OO O.OOE+OO 3.05E+07 O.OOE+OO

7 Kr-89 O.OE+OO D.OOE+OO 1.66E+04 O.OOE+OO 1.01E+04 1.73E+04 D.OOE+OO 0.00E+OO O.OOE+OO 3.72E+07 D.OOE+OO

8 Kr-90 0.0E+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 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 O.OOE+OO O.OOE+OO O.OOE+OO 2.44E+07 0.00E+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 O.OOE+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 2.31E+04 1.61E-03 1.80E+07 2.89E+D4

12 Xe-135m O.OE+OO .Q,OOE+OO 3.12E+03 O.OOE+OO 7.11E+02 3.38E+03 O.OOE+OO O.OOE+OO O.OOE+OO 7.22E+06 O.OOE+OO

13 Xe-135 O.OE+OO O.OOE+OO 1.81E+03 O.OOE+OO 1.86E+03 1.92E+03 0.00E+OO D.OOE+OO O.OOE+OO 3.86E+07 O.OOE+OO

14 Xe-137 O.OE+OO O.OOE+OO 1.42E+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

15 Xe-138 0.0E+oo O.OOE+OD 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 = 1.0E+OO 2.94E+02 6.94E+02 1.61E-03 2.89E+04

7.35E-05 sec/m3 = xJQ (From ODCM procedure 1/2-DDC-2.02, Section 6. 1.2) Qt(Total Body)= 500/(xJQ) sum(KiSI) = 2.31 E+04 uCVsec

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 Lowest Qt Value 2.31E+04 uCVsec

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 1 E-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

Adjustment of Unit 1 Containment Vacuum Pump Source Term

Due to Installation of High Capacity Containment Vacuum Pumps during 1 R15 (ECP-02-0079)

Nuclide

1 Ar-41 2 Kr-63m 3 Kr-85m 4 Kr-85 5 Kr-87 6 Kr-88 7 Kr-89 8 Kr-90 9 Xe-131m

10 Xe-133m 11 Xe-133 12 Xe-135m 13 Xe-135 14 Xe-137 15 Xe-138 16 1-131 17 1-132 18 1-133 19 1-134 20 1-135 21 Co-58 22 Co-60 23 Mn-54 24 Fe-59 25 Sr-89 26 Sr-90 27 Cs-134 28 Cs-137 29 C-14

NG Totals= Pl Totals = Slim Totals

Ai Ai

OLD VERSION NEW VERSION

from to

112-0DC2.02 1/2-0DC2.02

Attachment A Attachment A

Table 2.1-1a Table 2.1-1a

and/or and/or

Table 2.2-2a Table 2.2-2a

Revision O Revision 1

(Ci/yr) (Ci/yr)

O.OE+OO O.OE+OO

3.7E-04 S.2E-03

3.9E-03 5,5E-02

7.2E-01 l.OE+Ol

7.8E-04 1. lE-02

5.0E-03 7.0E-02

3.1E-06 4.3E-05

O.OE+OO O.OE+OO

1.3E-02 1. SE-01

2.2E-02 3.lE-01

1.9E+OO 2.7E+Ol

4.4E-05 6.2E-04

1.9E-02 2.7E-Ol

6.3E-06 8.BE-05

1.2E-04 l.7E-03

4.7E-04 6.6E-03

2.5E-06 3.SE-05

8.4E-05 1. 2E-03

4.7E-07 6.6E-06

1.4E-05 2.0E-04

1.GE-05 2.2E-04

7.4E-06 1. OE-04

4.9E-06 6.9E-05

1.6E-06 2.2E-OS

3.7E-07 S,2E-06

6.6E-OB 9.2E-07

4.9E-06 6.9E-OS

8.4E-06 l.2E-04

O.OE+OO O.OE+OO

2.7E+OO 3.8E+01

6.1E-04 8.SE-03

2.7E+OO 3.8E+01

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

INCREASE

from OLD VERSION

to NEW VERSION

(Ci/yr)

0.00E+OO 4.81E-03 5.07E-02 9.36E+OO 1.01E-02 6.50E-02 4.03E-05 O.OOE+OO 1.69E-01 2.86E-01 2.47E+01 5.72E-04 2.47E-01 8.19E-05 1.56E-03 6.11E-03 3.25E-05 1.09E-03 6.11E-06 1.82E-04 2.08E-04 9.62E-05 6.37E-05 2.08E-05 4.81E-06 8.58E-07 6.37E-05 1.09E-04

O.OOE+OO

3.49E+01 7.99E-03 3.49E+01

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

ERS-HHM-87-014 Revision 8

Attachment4

page~ cA35