ML20059E019

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Rev 0 to CAP-0002, Odcm
ML20059E019
Person / Time
Site: Rancho Seco
Issue date: 08/03/1990
From:
SACRAMENTO MUNICIPAL UTILITY DISTRICT
To:
Shared Package
ML20059E008 List:
References
CAP-0002, CAP-2, NUDOCS 9009100005
Download: ML20059E019 (48)
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Text

{{#Wiki_filter:. I V MANUAL: CHEMISTRY ADMINISTRATIVE PROCE08)RES MANUAL NUMBER: CAP-0002 REVISION: 0 I TITLEr OFFSITE DOSE CALCULATION MANUAL PAGE 1 OF 48-LEAD DEPARTMENT: EgFFCTgVEDATE 0 g CHEMISIRY / / ' ' ' ~ s s. s. s o. s 9. 7. n.w '. W g Al A - - i J. ' i i./,,j4,.n 7 (NSRC) (MA G (PRC) REVISION

SUMMARY

for Revision Sumary, see Attachment 1 of 50.59 Review. 3 .I I I y e I _ _.. _.. _ _ _ _ _...... _. _ _.L.* ?. TION ONLY AND i T H I S F R G C E f' '.: R E.. ! 't' ' ', " '. .e m d ... ;.r, 0 ?. ? N. )' ' S H ALL N OT U f. '. i t._ a.--wun . e- - -~ :2. wn. m.nseamame man __._. _ a 4 I. I. HP5032C D-5007C I gG910000590093o R ADOCK 05000312 'Ij R PDC

&R, 'I MANUAL:- CHEMISTRY ADMINISTRATIVE PROCEDURES MANUAL NUMBER: CAP-0002= i REVISION: 0 ,I . TITLE: OFFSITE DOSE CALCULATION MANUAL PAGE 2 0F 48 TABLE OF CONTENTS EAGE SECTION f 4 1.0 PURPOSE 4 c 2.0 SCOPE 4-

3.0 REFERENCES

/ COMMITMENT DOCUMENTS 6

4.0 DEFINITIONS '9 I 5.0 RESPONSIBILITIES 9 -l 6.0 PROCEDURE l 9 6.1-General Considerations 12 6.2 Liquid Monitor Setpoints 6.3' Maximum Permissible Concentrations in Liquid Effluents. 13 15 6.4 Liquid Dose Calculations 1 E 16 l 16.5' Liquid Dose Projections l; 18 6.6 Gaseous Monitor Setpoints 21-t 6.7 Maximum Permissible Concentrations in Gaseous Effluents 22 6.8 Gaseous. Dose Rate Calculations l 24 6.9 Gamma and, Beta Air Dose Calculations-25 6.10 Gaseous organ Dose Calculations l 27 6.11 Gaseous Dose Projecttons 28 l 6.12 Fuel Cycle Dose 28 6.13 EPA Reporting Requirements (CCTS T890828001) 28 7.0 RECORDS i 1 h I 5:

B' I CHEMISTRY A. INISTRATIVE PRC2DURES MANUAL NUMBER:. CAP-0002 MANUAL: -REVISION: 0 PAGE 3 0F 48 8 _ITLE:- 0FFSITE DOSE CALCULATION MANUAL T TABLE OF CONTENTS (Continued) EAGE SECTION I 8.0 ATTACHMENTS 29 1 Liquid Effluent Flow Diagram 30-i 2 Gaseous Effluent Flow Diagram 31 3 Dose Factor Parameters 34 Atmospheric Dispersion and Deposition Parameters 4 35-5 Exclusion Area Boundary 36 6 Site-Boundary for Liquid Effluents = 37 Site Boundary for Gaseous and Liquid Effluents 7 l 38 8 Historical Liquid Source Terms 39 9 Liquid Monitor Detector Efficiencies ~ 40 L10 Organ Dose Factors for liquid Effluents 41 11 Historical Gaseous Source Terms I Gaseous Monitor Detector Efficiencies 42-12 43 Dose Factor for Noble Gases an.d Daughters 13 44 14_ Organ Dose Factors for Gaseous Effluents I 4 i5 8

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i y t EMUAL: CHEMISTRY ADMINISTRATIVE PROCEDURES MANUAL.- NUMBER: CAP-0002 REVISION: -0 'I PAGE 4 0F 48 TITLE:~ OFFSITE DOSE CALCULATION MANUAL 1.0 PURPOSE ,E The Offsite Dose Calcuittion Manual (00CM) contains the methodology' and parameters used in the calculation of offsite doses due'to radioactive gaseous and liquid effluents. Also, the 00CM contains the methodology for determining effluent monitoring instrumentation alarm / trip setpoints. Methods are described for assessing compliance with Rancho Seco Technical Specifications as-they apply to 10 CFR F Part 20.106, 10 CFR Part 50 Appendix I, and 40 CFR 190.10a for liquid- ~ I and gaseous effluents. c 2,0 SCOPE l This procedure functions as a manual that provides the basis-for l development of detailed implementing procedures that address dose' tE s5 calculations for liquid / gaseous releases and monitor setpoints.

3.0 REFERENCES

/CIBWITNENT DOC 1mENTS 3.1 Commitment' Documents i

Code of Federal Regulations, Title 10, Chapter 1 -Parts 20, -3.1.1-50.36a'and Part 50 Appendix I i 3 '.1. 2 Rancho Seco Technical Specifications 3.1.3 CCTS T890828001, EPA 40 CFR Parts 332, 355 Reporting lf Requirements 40.CFR 190, Environmenta-1 Radiation Protection Standards for E 3.1.4 Nuclear Power Plant Operations 5 3.2 Reference Documents USNRC Re'gulatory Guide 1.109,'Rev. 1,-Calculation of Annual' 3.2.1. Doses to Man from Routine Releases of-Reactor-Effluents for the Purpose of Evaluating Compliance with 10 CFR Part 50, FI Appendix I, October 1977-T 3.2.2 H.C. Burke, et.al.,' Preparation of Radiological Effluent 3 Technical Specifications'for Nuclear Power. Plants, NUREG-0133, 4

W USNRC:NRR, October 1978 ORNL, User's Manual for LADTAP II, NUREG/CR-1276, May 1980 3.2.3 I

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. - ~ I E MANUAL: CHENISTRY ADMINISTRATIVE PROCEDURES MANUAL NUM8tR: CAP-0002 REVISION: 0-I 0FFSITE DOSE CALCULATION MANUAL PAGE 5 0F 48 TITLE: sE 3.2.4 D.L._ Strange, et.al., LADTAP-II, Technical Reference anc, User Guide, NUREG/CR-4013, Pacific Northwest Laboratory, Apr11.1986 W. 3.2.5 Eckerman, K.F., et.al., User's Guide to GASPAR Code, o I NUREG-0597. USNRC:NRR, bme 1980, in RSIC CCC-463-- USNRC Regulatory Guide 1.111, Mithods for Estimating-3.2.6 Atmospheric Transport and Disptrston of Gaseous Effluentsiin Routine Releases from Light-Mater-Cooled Reactors 3 3.2.7 USNRC Regulatory Guide 1.21, Measuring, Evaluating, and Reporting Radioactivity.in Solid Hastes and Releases of-og Radioactive Materials in Liquid and Gaseous Effluents from I l' Light-Water-Cooled Nuclear Power Plants L, 3.2.8 USNRC Regulatory Guide 4.1, Programs for Monitoring-- l Radioactivity in the Environs of Nuclear Power Plants-l i 3.2.9 REIMS Software Life Cycle Documents (Software Requirement Specification, Design Document, Acceptance Test Plan)- 3.2.10 USNRC & Pacific Northwest Laboratory, TDMC Computer Code / Data Collections, X0000Z-82, Radiological Assessment Code: System Meteorological Evaluation of: Routine Effluent Releases at Nuclear Power Stations 3.2.11 1989 Rancho Seco Land Use Census 3.2.12 RSNGS USAR Chapters 11.1-11.5 e 3.2.13 RSNGS P&ID Drawing M-563, M-551, M-552, M-503 3.2.14 Pacific Northwest Laboratory, X0000Q: Computer Program for the Meteorological Evaluation of Routine Effluent Releases at Nuclear Power Stations ' 2.15 Congel, F.J., Methods for Demonstrating LWR Compliance with the EPA Uranium Fuel Cycle Standard (40 CFR Part 190), g' NUREG-0543, USNRC:NRR, February 1980 .gf x I: j I I

m MANUAL: CHEMISTRY ADMINISTRATIVE PROCEDURES MANUAL NUMBER:.. CAP-0002-REVISION: O s I TITLE: 0FFSITE DOSE CALCULATION MANUAL PAGE 6 00 48-4.0 DEFINITIONS I 4.l Member of the Public 4 A Member of the Public shall be any real individual who by virtue I of their occupational status have no formal association with the plant, that can receive a radiation dose in the general -3 environment. This category shall include nonemployees of the licensee who are permitted to use portions of the site for. g' recreational,' occupational, or other purposes not associated with.. plant functions. This category shall DQ1 include nonemployees such as vending machine servicemen or postmen who, as part of their I formal job function, occasionally enter an area that is controlled by the licensee for purposes of protection of individuals from L l-exposure to radiation and radioactive materials. 4.2 Batch Release _A Llauid Batch Release is the discharge of liquid radioactive-4 wastes of discrete volume. Batch releases are normally from one of. the retention basins to the Waste Water discharge canal (Environmental Release Point). A-Gaseous Batch Release is the discharge of gaseous radioactive. wastes of discrete volume. Batch releases for the gaseous pathway

I include initial Reactor Building purges and Waste Gas Decay Tank i

j releases. An initial RB purge includes all the radioactive gas released from j the first opening of the containment =until the R8 atmosphere concentration of activity reaches a new equilibrium (normally 7 -1 ![ volume changes) due-to leakage of Reactor Coolant during cold W-shutdown. Further release from this pathway is called a continuing Reactor Building purge and considered a continuous release. l 4.3 Continuous Release A continuous radioactive gaseous release is the discharge of gaseous wastes of.a nondiscrete volume from a system that may have an input flow during the release. These include the Auxiliary Building Stack (ABS), Auxiliary Building Grade Level Vent (ABGLV), and continuing Reactor Building purges (see Definition 4.2'above). Continuous radioactive 11guld releases are not planned to be made from Rancho Seco Nuclear Generating Station (RSNGS). l-1

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L MANUAL: CHEMISTRY ADMINISTRATIVE Pe0CEDURES MANUAL. NUMBER: CAP-0002 REVISION: 0 PAGE 7 0F 48' TITLE: OFFSITE DOSE CALCULATION MANUAL l f2 4.4 Default Radionuclide Mix g A historical mixture of radionuclides that may be used to determine monitor setpoints. 4.5 Dilution Flow The volume or volume rate of fluid (11guld or gas) which,s added to a radiological release stream for the purpose of decreasingLthe instantaneous concentration of the stream. 4.6 Maximum-Exoosed (Hvoothetical) Individual g The Maximum Exoosed Individual is characterized as " maximum" wit regard to food consumption, occupancy, and other usage or exposure (I -pathway parameters in the vicinity of Rancho Seco that'would. L represent an individual with habits greater than usually expected-l for the average of the population in general. E Maximum dose factor parameters will be determined using site ( specific data from tho' Land Use Census. If information needed to: determine a parameter is not available, RG 1.109 parameters will:be- ] I' used. :All dose factor parameters used are listed in Attachment 3; I 4.7' RSNGS Rancho Seco Nuclear Generating Station. 4.8 Unrestricted Area Any area at or beyond.the site boundary to which access is not controlled by the' licensee for purposes of protection of I,- individuals from exposure to radiation and radioactive materials, .j ~ and any area within the site boundary used for3 residential quarters-or industrial, commercial, institutional and recreational ) facilities. For environmental protection / effluent control purposes, the Rancho Seco Unrestricted Area is the area outside the, -Site Boundary as shown in Attachment ~7. j 4.9 Exclusion Area Any area within a 640 meter radius from the center of the Reactor - ) I This boundary (Attachment 5) is used for determining-Building. Gaseous Dose Rate compliance per Technical Specification 3.18.1. I I I ......L. -.

i MANUAL: CHEMISTRY ADM?NISTRATIVE PROCEDURES MANUAL-NUMBER: CAP-0002 1 REVISION:- 0 I ' TITLE: OFFSITE DOSE CALCULATION MANUAL PAGE a OF 4R l' 4.10 Nuttance Pathways I (1) Secondary system gaseous pathways.where the calculated dose totals contribute less than 5% of the annual limits and do not. need to be tracked for dose' calculational purposes unless I secondary activity reaches.a predetermined Action Level.. i L (2) Sources of trace levels of radioactivity in liquid effluents where the calculated dose totals contribute less than 1% of the annual limits and do not need to be tracked for dose-Trace levels'arei efined to be less i d calculational purposes. I than IE-8 pCi/mi for the nuclides typically released from RSNGS. Examples include the oily water separator, plant l, 1 effluent inlet, and store drains. 4.11 Unnlanned Release The unexpected release.of radioactive materials to unrestrict'ed h I areas in gaseous and liquid effluent. All unplanned releases shall. be discussed in the Semiannual Radiological Effluent Release Report. to the NRC. 4.12 Miscellaneous Release Release pathways which are considered-planned but are not defined l lI explicitly with-monitoring requirements in Technical l Specifications. These pathways contribute a relatively small percentage (<5%) to the annual dose limits but shall be tracked for. effluent activity accounting and dose calculation-purposes. [ . Miscellaneous releases shall not be' reported in the SAER as abnormal or unplanned rvleases. Examples include the IOSF and the Respirator Cleaning Facility. ? '4.13 Safety Factor (SF) A number greater than unity used in calculations to introduce greater conservatism (larger margin of safety) to offset various-uncertainties in instrumentation and methods. Safety fac' tors are set by Chemistry Supervision based on either analysis or . professional judgement. Unless otherwise specified, the default value is two (2). 4.14 Llauld Effluent Radwaste Treatment System The Liould Effluent Radwaste Treatment System refers to the iI-slutceable domineralizer skid (see Drawing M-563 Sheet 3) designed and installed to reduce the quantity of radioactive materials in I l 11guld effluents. LI

m7 ) 1 4 MANUAL: CHEMISTRt ADMINISTRATIVE PROCEDURES MANUAL NUMBER: CAP-0002 REVISION: 0 I PAGE-9 0F 48 TITLE: OFFSITE DOSE CALCULATION MANUAL-4.15 Gaseous Radwaste Treatment Systems (GRTS). 'I The term Gaseous Radwaste Treatment Systems refers to.the Waste Gas j 1 System and the Ventilation Exhaust Treatment System. I 1 j 5.0 RESPONSIBILITIES It is the responsibility of the Chemistry Manager for the following: I 5.1 (1) 00CM Revision ud Reporting the Revisions in the SRERR (Semiannual Ldioactive Effluent Release Report) (2) SRERR Preparation and Submittal (3) REIMS Database j (4) Meteorological Database ,l LADTAP, GASPAR & X0QOOQ Computer Program Verifications and 'W (5) Changes The PRC and MSRC are re'sponsible for reviewing and approving all 5.2 changes to ther00CM per Technical Specifications. J E[. 6.0 PROCEDURE 6.1 General considerations 6,1,1 Liauid Effluert Pathways provides a simplified diagram of the radioactive 11guld effluent produced by'RSNGS. The liquid effluent discharge of RSNGS forms the-headwaters of Clay Creek. Dilution of the 11guld eff)uent occurs offsite at:the-confluence of Clay and Hadselville Creeks, and of Hadselville-i and Laguna Creeks, and at the confluence of Laguna Creek and I the Cosunnes River. Radioactive 11guld releases from secondary plant systems are normally directed through the'A or B RHUTs to ensure 'I compliance with 10 CFR 50 Appendix I prior to their discharge to the retention basins (North or South). Prior to discharge the from the retention basins to the plant effluent (offsite), !I1 discharge rate from the retention basins and the amount of dilution from Folsom South Canal are controlled to ensure compilance with the concentration requirements in 10 CFR 20.

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l MANUAL: CHEMISTRY ADMINISTRATIVE PROCEDURES MANUAL: NUMBER:

CAP-0002 REVISION:

0 TITLE: OFFSITE DOSE CALCULATION MANUAL' PAGE 10 0F 48 I 6.1.2 Gateous Effluent-Pathw1Lys ^ Airborne radioactive material in the various rooms and systems at RSNGS is routed and discharged in airborne effluent as-illustrated schematically in Attachment 2..The figure shows I the functional arrangements of these-Streams, treatment and controls, radioactivity mohitoring points, and effluent release points. Before the gas in the reactor building _(initial purge)'or in a waste gas decay tank is released, noble gas concentrations-are determined and prerelease dose and dose rate calculations are I done in accordance with~the methodology of Steps 6.8 and 6.9. These measured concentrations are used to establish maximum effluent discharge rates and monitor setpoints. Other potential release pathways than those specified in have been identified. These release pathways are-classified as NUISANCE pathways and include the following: (1) Auxiliary Boiler Vents / Reliefs (2) ' Miscellaneous Secondary System Steam Discharges- ~I. (3) Tank Atmospheric Vents (4) Condenser Hogging Air Ejectors (S) Routine Secondary Plant Steam Leakage (6) Auxiliary Feedwater Pump Turbine Exhaust (7) Service Air /Hitrogen Supply Steam Past experience-has shown that the above release pathways do I not contribute to the dose totals because of the small: quantities released and the low concentration of radioactive 3 1 materials. Therefore, Action levels may be established for the secondary system concentrations of radioactive material to' g, trigger when the above routine gaseous effluent releases shall be evaluated for offsite dose impact. The Action Levels shall be based on levels that could contribute more than 5% to the most restrictive yearly dose limit. -Action Levels shall be maintained through RSNGS procedures. Unplanned releases shall be evaluated on a case by case basis. The Respirator Cleaning Trailer and Interim Onsite Storage Facility (IOS) are miscellaneous releases. I I I

I i I MANUAL:. CHEMISTRY ADMINISTRATIVE PROCEDURES MANUAL NUMBER: CAP-0002: REVISION: 0 I PAGE 12 OF is TITLE! OFFSITE DOSE CALCULATION MANUAL 6.2 'Liouid Monitor Setnoints I The High alarm setpoint for the Retention Basin Effluent Discharge-i Monitor (R15017A) is set to ensure the limits of Specification 3.17.1'are not exceeded. When'the high: alarm level 1s reached, the-I release of the basin 1s-terminated automatically. o A SAFETY FACTOR is included in the setpoint calculations to I incorporate a margin of conservatism. When a batch release is not occurring or the calculated setpo' int is so low that it will cause spurious alarms, the-monitor setpoint I i should be set as close to background without causing spurious alarms or as determined by Chemistry Supervision. I The conversion factor and setpoint calculations should be performed' l based on the same radionuclide mix. 6.2.1 Conversion Factort for R15017A Provided here is the methodology to determine the conversion j factor of counts per minute'to microcuries per cubic I centimeter for the Retention Basin Radiation Monitor 1 (R15017A). The'converste factor is based on the monitor's efficiency for each nuclide and the abundance of the nuclide. I The mix of isotopes used may be based on the historical mix provided in Attachment 8, current six in the batch release, or i as determined by Chemistry Supervision. The mix fraction I shall be based on gamma emitting isotopes cnly. The following equation shall be used to determine the conversion factor'for R15017A: CF = [ Ij(f ) (Eg)]-1 t Where: CF - pC1/cc per cpm Fraction of nuclide i to total activity of historical-ft- ? mix (Attachment 8) or batch mix Efficiency for nuclide 1 (cpm /pC1/cc) Attachment 9 Et= I g

I MANUAL: CHEMISTRY ADMINISTRATIVE PROCEDURES MANUAL NUMBER:- CAP-0002-REV1510N: 0.. TITLE! 0FFSITE DOSE CAlcuLAT!QN MAlalAL PAfd 13 0F 48 6.2.2 Hlah Alars tetnoint for R15017A (uct/al) HIGH Al.ARN + C I C, (pC1/ml) bkg = SF

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Where: The summation of all amma-omitting nuclide ICi concentrations (pci/m ). I I i The summation of the ratios of all nuclide = concentrations to their MPC values. The most MPCt limiting MPC values should be selected (soluble I or insoluble) for water in unrestricted areas. A SAFETY _ FACTOR which may be applied:to SF = I incorporate a margin of conservatism (SF 1 1). (Default = 2) The background reading of the monitor Cbkg I (pC1/ml). 6.3 Maximum Permissible Concentrations in Lieutd Effluents w The Maximum Permissible Concentration Fraction is calculated to determine compliance with.10 CFR 20 requirements and Technical Specification 3.17.1. Radioactive 11guld effluent discharges I normally originate in_the RHUTs and discharged into a retention basin. Samples are collected and analyzed from each Retention Basin prior to discharge to ensure that compliance wlth Technical I. Specification 3.17.1 can be achieved. In addition; calculations to. determine the. minimum dilution water flow rate and maximum retention basin discharge flow rate to ensure-compliance are provided in this section. Any combination of: minimum dilution flow rate and maximum-discharge' flow rate which satisfy the Technical Specification is acceptable. I g I ~ =^ --..---m-__s..m..:.__m

E MANUAL.: CHEMISTRY ADMINISTRATIVE PROCEDURES MANUAL. NUMBER: CAP-0002- ' REVISION: 0 J PAC.E 14 0F 48- ~ l TITLE!- 0FF11TE DOSE CALCULATION MANUAL Mart== Permissible concentration Fraction (MPCF) -6.3.1-I I Compliance with Technical Specification 3.17.1 is anticipated when the MPCF is less than or equal to 1.0. The MPCF is-calculated as follows: ~ ~ ~ F C r MFCF. I i I MPC Fe+F g r ~ ~ ~ ~ l Nhere: The calculated fraction of Maximum Permissible. MPCF Concentration in the radioactive 11guld effluent discharged into the unrestricted area. The total concentration of radionocitde-1.In the I Ct batch, prior to dilution, of liquid effluent in F pC1/ml. - The MPC of radionucitde i from Appendix 8, Table-II, MPC g-Column 2 of 10 CFR 20 in pct /al. The most-limiting MPC value should be selected (soluble or' l ' ~ E insoluble). Otscharge flow rate; the flow rate of the-r l Fr radioactive 11guld batch release from the retention basin to the Maste Mater Discharge Canal-(Plant Effluent) :in gpm. .The total available dilution water (Plant Effluent) Fc flow rate at the time of discharge of the radioactive liquid effluent in gps. I 4 The minimum dilution water (Plant Effluent) flow rate 6.3.2 (Femin) is calculated'as follows: i , C, ,j Femin - F SF I r g

MPC, Where:

A fixed effluent di: charge flow (gpm) (as required Fr by specific release restrictions). J A factor which may be applied to' incorporate a SF ( margin of conservatism (SF 1 1). I

-j ] MANUAL: CHEMISTRY ADMINISTRATIVE-PROCEDURES MANUAL NUMBER: CAP-0002 -REVISION: 'O. PAGE 15 0F 4R L TITLE! pfff1TE DOSE cat _culATION MANUAL ,I E I 1 SF I (C /MPC ) must be >. 1.

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4 6.3.3 The me.timum effluent discharge flow rate (Frmax) is' j 3 calculated as follows: g a i r I F .. I SF I, rmax C 3 q 3

MPC,

,3 Where: 3 A fixed dilution water flow rate'(gpm) (as required Fc = I by specific. release restrictions). E SF I (C /MPC ) must be >=,1. c I i I 1._......._..._.............................._................._..._.. 1 D 6.4 Linuld Dose Calculations q This section provides the methodology to demonstrate compliance-with Technical Specification 3.17.2. I Site specific organ dose factors for liquid effluents have been -determined for the MAXIMUM EXPOSED INDIVIDUAL-and are listed.in Dosefactors(Ajan)werederivedusingequations 0. l.109, Rev. I and LADTAP. -The dose .I: factor parameters used are listed in Attachment 3. As previously and methods in Regulatory Guide stated, site specific parameters should be used based on the Land Use Census in lieu of the values provided in RG 1.109 whenever l possible. The exposure pathways included in the A13ao are those identified I by the I.and Use Census. The pathways cohsidered for inclusion are: (1) fresh water fish (2) fresh water invertebrate (3) river shoreline deposits 1 I A -- m w%u-

.I I l NUMBER: CAP-0002 MANUAL: CHEMISTRY ADMINISTRATIVE PROCEDURES MANL,%L ' REVISION: 0 l PAGE 16 0F 48 TITLE: OFFSITE DOSE CALCULATION MANUAL l milk from_ cows that eat fresh or stored forage irrigated with. u' g (4) -Clay Creek water meat from cows that eat fresh or stored forage.frrigated with gg (5) Clay Creek water (6) vegetation 4 3 6.4.1 Liouid Effluent Dose Eauntion

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I In <0 t 1 D"O = F Mhere: p Annual calcult.ted dose.(50 year dese commitment)-to. Daj the organ (or total body) j of a maximally exposed. = E' individual of age group a (aree/yr), 1 L 5-Activity of isotope 1 released during the year. g .Qt- = (C)lyr). p3 =Ai Site specific dose factor for an organ (or total' j A jap = l body) j for a person of age group a via pathway 3 p due to isotope 1 (mrem-ft /C1-sec). L Annualaveragedischargevolumetricflowrgte 1 l F = (effluent water plus dilution water) in ft /sec. [ Because the dose rate varies linearly with activity release rate' the dose for a shorter period of time (arem) may.be m ' (' calculated by substituting the activity released (Cl) during- ) that period for Qt in the.above squation.

However, volumetric flow rates should not-bs. averaged over a period

,.I less than a calendar quarter. More conservative. flow rates d are acceptable, 6.5 auld Dose Proiections Thirty-one (31) day dose projections are calculated to show compliance with Technical Specification 3.17.4. The 31-day dose cm j' projections do not need to be performed when the LIQUID EFFLUENT RADHASTE. TREATMENT SYSTEM (LERTS) is operable. The LERTS is i considered operable by meeting Technical Specifications 3.17.1 and- - i 3.17.2. I n

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l, l ' MANUAL:. CHEMISTRY. ADMINISTRATIVE PROCEDURES MANUAL NUMBER: CAP-0002' l REVISION: 0 I OFFSITE 001E CALCULATION MANUAL-PAGE 17 0F 4R TITLE: If the 31-day dose projection exceeds the limits of Technical' E Specification-3.17.4, then either of the following actions should ,;E be taken untti projections fall within-limits: j-(1) Require the use of LERTS for every RHUT release when activity. can be reduced, n (2). Reduce blowdown from systems known to be.signit'icantly - I contaminated. The following equations shall be used: 31-Day Projection: (D r / t r) f Dp31 31 Y Y Quarterly Projection: J DpQtr 91.3 (DQtr / tQtr) 5 ~ Yearly Projection: ,g ll-' OpYr - 365.25 (D r / t r) Y Y L Where: Dp31 day Projected oose. Dyr - Cumulative. annual dose to date. .t r - Number of days into.the year. Y L pQtr - Quarterly dose projection. D D

  • Cumulative quarterly dose to date.

l: _ Qtr - Number of days into the quarter. tQtr Annual dose projection, f DpYr I I I .Y-. ,-..,-,-e-,--, ,m-

1 .I .\\ !m 1 j MANUAL: CHEMISTRY ADMINISTRATIvi PROCEDURES MANUAL NUMBER: CAP-0002 REVISION:' 0 I PAGE la OF 48 _ITLE: OFFEITE DOSE CALCULATION MANUAL T L 6.6 caseaun Monitor setnoints !I Technical Specification 3.16 states that the gaseous effluent. t monitors shall have t5eir alarm / trip setpoints set to ensure the limits of Technical Specification 3.18.la are not exceeded. Data .I from the sector where the most conservative atmospheric dispersion (maximum X/Q) factor at the Exclusion Area' Boundary occurs is used. This value is obtained from Attachment 4. Compliance with" a +3 the dose rate limits for noble gases in Specification 3.18.la is "g demonstrated by setting each gaseous effluent monitor ~ alarm / trip setpoint so that an alarm / trip will occur at or before the dose rate limit is reached. A SAFETY FACTOR is included in the setpoint calculations to incorporate a matgin of conservatism. Maximum design ficw rates for each release point will be used to-1 I, calculate setpoint1. ConversionFactorsforR15044.R15045.andR15546A-l f 6.6.1 [ Provided here is the methodology to' determine the; conversion f factor of counts per minute to Building Stack Monitor (R15045), Reactor Building Stack Monitor AR15044), and-the i. l Auxiliary Building Grade Level. Vent Monitor (R15546A). The !3 conversion factor is based on the monitor's efficiency of-i g detection for.each nuclide and the mix of the nuclide. The mix of isotopes used may be-based on the. historical mix q (;m provided in Attachment 11, the current mix.in the baten.or l ig continuous release, or as. determined by Chemistry I The mix used for setpoint calculations and L Supervision. conversion factor calculations should be the.same.. The following equation shall be used to determine the L. conversion factor for R15044, R15045 and R15546A: CF = [ I (f ) (E)d g g p Mhere: CF. - pC)/cc per epm-ag fg fraction of nuclide ' to total activity

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Detector sensitivity to nuclide 1, in cpm per Et J5; pC1/ct, Attachment 12. i f e

\\ 1 MANUAL: -CHEMISTRY ADMINISTRATIVE PROCEDURES MANUAL NUMBER: CAP-0002 l ~ kEVISION: ~0-K TITLE: ' 0FFSITE DOSE CALCULATION MAKlAL PAGE 19 0F 48 i 6.6.2 Gaseous effluent release points and maximum design flow rates iI;- used atLRSNGS are as follows: Reactor Building Stack 74,000.CFM-Auxiliary Building Stack 47,740 CFM [ Auxiliary Building Grade Level Vent 21,450 CFM Interim Onsite Storage Building Ventilation

  • 8,050 CFM Respirator Cleaning Facility
  • 1,300 CFM.
)

[ !E The Interim Onsite Storage Building (IOS) and Respirator. Cleaning Facility are not Technical Specification release pathways and are not subject to continuous discharges of nW l = radioactivity. Because of the infrequency of a radioactive Lg. release, asses. ment will be done on each release according to-t '3 administrative procedures.

6. 6. 3'-

Determination of Pirtition factor (P l y Technical Specification 3.18.1 applies to the entire site.-.not Consequently, the total release just one vent or monitor. i3 rate must be partitioned among the'three major vents (A85,: c5 ABGLV, RBS). For routine operations, the partition factor may ~ be calculated by assuming.that_the effluent concentration is LB the same for all pathways'and using a ratio of flow rates. Lg The total volume flow rate for'all threek vents is 143,190 CFM. Therefore: I 0.52. 74.000 CFM Prbs = 141,190 CFM ' 0.33 47.740 CFM Pabs = = 143,190 CFM 0.15 1 21.450 CFM Pabgiv. = 143,190 CFM, +! Chemistry Supervisio_n may elect to use a different set of. i partition factors based on plant conditions. However,-the sum of all the partition factors for the site must be less.than'or-I equal to unity (1). a I I I

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... =. -. _ 1 I+ q j I MANUAL:: CHEMISTRY. ADMINISTRATIVE PROCEDURES MANUAL NUMBER:: CAP-0002-REVISION: 0 -- PAGE 20 0F 48 TITLE: OFFSITE DOSE CALCULATION MANUAL-Channel 4 Noble Gas ~Se$ point for R15044, R15045, and R15546A j 6.6.4-in pC1/sec l' SM

  • P
  • I, C1

- + Skgd y N

  • -K

) ) Ig ' SF * (X/Q)

  • Ig (Cg g

3 Mhew Monitor setpoint for ver-v (i.e., RSS ABS; or-My

ABGLV) in pC1/sec.

Technical Specification limit for total body dose i 500.- rate in eres/yr.. Partition factor, dimensionless, which distributes ( Py the total site release rate among.the three vents, L I Concentration of isotope i in gaseous-effluent in: C~ t The mix of isotopes used may be based _on .i pC1/cc. L' the vent specific historical mix providedLin 1 3 1 or based on the current six in the j

g batch or continuous release.

l5 .i Safety Factor, dimensionless,_(SF 1 1). (Default 2) SF = X/Q = Most conservative atmospheric dispersion factor for-i a ground' level release to a sectgr beyond the Exclusion Area Boundary in sec/mJ. -Elther an-

l annual averige or multiple-year average'is 1

!se e acceptable. Factor converting ground-level concentration of-Kt noble ggs isotope i to total body; dose t (aree-m3/pC1-yr), i Skgd - Monitor background reading in pC1/sec. i I c.

i l

g MANUAL
CPEMISTRY ADMINISTRATIVE PROCEDURES MANUAL NUMBER:-

CAP-0002-REVISION: 0 _ TITLE: OFFSITE DOSE CALCULATION W EAL PAGE 21 0F 48 6.6.5' -Channel 1-Noble Gas Setpoint for R15044, R15045, and_R15546A l in pCl/cc ,E MC H"Y + Skgd = y p5 472 F y L-Where: Monitor setpoint for vent v based on concentration MCy-in pC1/cc. L Monitor setpoint for vent v based'en release rate in ~MR = y pC1/sec excluding the background term.

That_15, My - Bkgd.

Maximum design volumetric flow rate in'CFM as Fy indicated =in 6.6.2. 28317 ml/ft3

  • 1 min /60 sec 472 Skgd -

Monitor background reading in pC1/cc. E1IE I i Channei 1 does not cause any automatic terminations or audible alarms. i'

1...........................................................L 6.7 Maxi== Permittible Concentrations (MPCs) in Gateout Effluents In order to demonstrate compi1ance with 10 CFR 20.106 whtch requires that the total MPC fract!,a not exceed 1 when averaged o'!er an entire year, the calculation is' included in the Semi-Annual Effluent Report.

In addition, a four hour reporting requirement exists when the total MPC fraction exceeds two when. averaged over one hour per 10 CFR 50.72. The fc11owing provides guidance on how i-to perform this calculation. e O

l I H MANUAL;. CHEMISTRY ADMINISTRATIVE PROCEDURES MANUAL . WMBER: CAP-0002. REVISION: 0 I -PAGE 22 OF 48~ TITLE-OFFSITE DOSE CALCULATION MANUAL ? Maximum Permissible Concentration Fraction (MPCf) EquationL 4 I (C,

  • F
  • 4.72E-4)
  • X/Q
  • TR I

MPC 7 MPC g Where: The concentration of nuclide 1 in pC1/cc. Ci 3 The flow. ate of the effluent release point in ft / min. F = The maximum noble gas X/Q at the exclusion area boundary X/Q in sec/m3 1 The most restrictive MPC for nuclide i from MPCt 10 CFR 20.106, Appendix B, Table II, column 1 (pC1/cc). p If the time of release is less than one-hour, then'this TR value is the duration of the transient in minutes divided oy sixty. Otherwise the Time Ratio (TR) is one, j Dimensionless. 4.72E-4 The conversion factor in min *m3/sec*ft, ,i 3 7 y, 4 6.8 Dose Rate Calculations Compliance with the dose rate limits for noble gases 11n-Specification 3.18.la is demonstrated by setting each gaseous I-effluent monitor alarm setpoint so that an alarm will occur at or before either dose rate limit Specification 3'.18.la is reached.= In.- j ~ addition, Specification 3.18.lb provides a-maximum limit on organ dose rate equivalent beyond the Exclusion Area Boundary fros' todine-131, lodine-133, tritium, and for all radioactive materials in particulate form with half-lives greater than eight:(8) days. Compliance is determined by calculating the organ 1 dose rate for the I. MAXIMUM EXPOSED INDIVIDUAL for-the inhalation pathway only. The dose rate due to noble gas is evaluated as follows: Total Body: )

I-btb"(X/0)I (O
  • K}

v1 i v . g -.i.

I 1 i ) MANUAL: CHEMISTRY ADNINISTRATIVE PROCEDURES MANUAL NLMBER: CAP-0002 i REVISION: 0 l t ,I PAGE 21 0F 48 TITLE! 0FF11TE DOSE CALCULATION NANUAL Skin: b,. (X/Q) I Q g (Lg + 1.1 M ) f g y 'E Where: b The total body dose rate from noble gates (aremlyr). tb bs The skin dose rate from noble gases (aren/yr). X/Q.. The most conservative atmospheric disperston factor for a ground level release to a.settor at or beyond the Exclusion Area loundary-(set /m3). Elther an. annual average. multi-year average, or concurrent I meteorology is acceptable. Normally taken from ' Attachment 4. The rolesse rate of noble gas radionuclide 1 from Qvt effluent vent v during the time of the release (pCl/sec). I A factor converting time integrated, ground-level Kg concentration of noble gas radionuclide i to total body dote from its gamma radiation l I (mrom-m3/pC1-yr). See Attachment 13. A factor converting gamma radiation from noble gas Lt I radionucilde t to skin dose (arem-m3/pC1-yr). See Attachment 13. A factor converting gamma radiation from noble gas I Mt radionuclide i to air dose (mrad-m3/pCl-yr), i See Attachment 13, A factor converting air dose from gamma radiation to 1.1 skin dose equivalent (mres/arad). The organ dose rate resulting from Inhalation is calculated with the equation: Organ: g a3. (x= 3 po, Ra3,> w v I: .I ~

j MANUAL: CNEMISTRY ADW1.MISTRATIVE PROCEDURES MANUAL NUMBER: CAP.0002 REVISION: 0 I PAGE 24 0F at TITLEt OFFSITE DOSE CALCULATION MANLlAL l Mhere: boj. The dose commitment rate to organ j of a a person in age group A (ares /yr). The factor to convert air concentration of j Raji. radionuclide i to organ 3 dose coamitment rate of a person in aoe group a exposed by l 'a inhalation Garem-m3/p61-yr). See g 4. 1 Oy t. - The release rate of radionuclide 1 (not including Noble Gas nuclides), via effluent vent v during the time of the release (pC1/sec). Exposure to dose rate factors, Raji, for inhalation are derived by using equation 13 in RG 1.10g, Rev.1. Tables (-5 E-7 E-8, } I E-9, and E-10 are assumed to represent the Maximum Exposed Indiv, dual in the equation to derive Raji-6.9 Air Deze calculations Technical Specification 4.22.2 requires cumulative' dose to air from i radioactive effluent noble gases to be determined in order to I assess compliance with Specification 3.18.2. The air dose is. a evaluated in the sector of the maximum exposure at or beyond the Site Boundary for Gaseous Effluent. I Air dv a from noble gas gamma radiation is calculated cumulatively 9 wtth the equation: i I 9 3.17 x 10-8 7gyjn) y gn ) 0 V n Air dose from noble gas beta radiation is calculated. cumulatively l with the equation: b - 3.17 x 10-8 I(X/0)II(Qvni g

  • N)

O v In Where: The noble gas gamma dose to air (mrad). 0 9 The noble gas beta dose to air (mrad). Db l I I .,m +... -, .~-.e-.- ,b-., -,w, -r.

o ,j i i E MANUAL: CHEMISTRY ADNINISTRATIVE PROCEDURES MANUAL NUMBER: CAP-0002 l REVISION: 0 i TITLE: OFFSITE DOSE CALCULATION MANLIAL PAGE 25 0F 48 X/Q = The atmospheric dispersion factor for noble gas effluer,c from a ground-level release to a sector l beyoN the Site Soundary for Gaseous Effluents I (ser,/m3). Either an annual average, multi-year l avrrage, or concurrent meteorology is acceptable, j s /, f actor convertina " aund-level concentration to l Mt gamma radiation frix., nooie gas radionuclide i to lI air dose (mrad-m3lpC1-yr). I A factor converting ground-level concentrattor, to Ng beta radiation f(on noble gas radionuclide i to i air dose (mrad-n' /pCi-yr). l3 Ovni. The quantity of each noble gas radionuclide t in batch n released via effluent stream v (pC1). 3 3.17 x 10-8 1 yr/.3.156 x 107 sec 6 pC1/pC1 times the values in RG l Factors Mg and Ng are 10 1.109, Rev. 1, Table B-1, columns 4 and 2. respectively. The computer codes GASPAR and REIMS may be used to perform these ,E calculations. j L Ornan Dona Calculations for Gateous Effluents l 6.10 Technical Specification 4.22.3 requires the radiation dose or dose l commitment to the Maximum Exposed (Hypothetical) Individual l accumulated from exposure to tritium, iodine-131, iodine-133, a.id radioactive materials in particulate form having half-lives greater than 8.0 days, that originate in effluent air, be determined at least every month. The radiation dose or dose commitment accumulated during a calendar quarter and a year may not exceed values stated in Technical Specification 3.18.3. A person may be exposed to effluent radioactive material of this i type in air by inhalation or indirectly via environmental pathways that involve deposition onto ve etation and the ground. The exposure pathways evaluated wil include the following: P Exnosure Pathway 1 Air--inhalation ,3 2 Deposition onto ground--trradiation i3 3 Deposition onto vegetation--ingested 4 Deposition onto forage--cow--milk--ingestion .g 5 Deposition onto forage--meat animal--meat--ingestion ig 6 Deposition onto forage--goat--milk--ingestion I

._ ~- ~.- - -- ) I f NUMBER: CAP-0002 CHEMISTRY ADN DISTRATIVE PROCEDURES MANUAL REVISION: 0 i MANUAL: PAGE 26 0F 48 TITLE: OFFSITE Dott CALCULATION MANUAL The equation used to calculate the dose comm1teent to the Maximum lEl Exposed (Hypothetical) Individual from radionucildes other than tritium 15: I vi ajip.1h f2 'E

  • N "OiD f

aj "

  1. 0'p.) f f9 D

p p = 1, i.e., air-inhalation, in the.first term, and p = l I 2, 3, 4, 5, and 6 in the second term of the equation Where: i excludes H-3 The dose commitment to organ j of a person in age i Daj group a (ares). The quantity of tritium, radiotodines, or radionucIldes Qvt days in air discharged via effluent st' greate In particulate form having half-lives ream v (pC1). l The atmospheric dispersion factor for a ground-level or t X/Q butiding wake discharge. Either an annual average, yI multi-year averagg, or concurrent meteorology is acceptable (sec/m3). Relative deposition factor. i.e., Factor converting a D/Q ground-level or building wake discharge in air to a real deposition on land (m-2). Either an annual average, multi-year average, or concurrent meteorology is acceptable. The locations used for calculations E should be from the most recent land use census data. 5 A factor converting time integrated concentration of Rajlp radionucilde 1 in air or deposited on vegetation and/or ground to radiation dose commitment to organ who 1s exposed via pathway p. " " '" '" " "'

  • l3 3

'"c'"d'"' * **' 6 dy- l5 has untts of When p.1, representing alt-inhalation, RailpWhen p.2,3,4,5 or IE mree-m3/pC1-yr. equation above, representing pathways involving deposition, Rajlp ,5-has units of mrem-m2-sec/yr-pC1. When the r.dtonuclide is H;3, i lg Rajlp has units of mrem-mJ/pCl-yr. l3 o l

~ i I MANUAL: CHEMISTRY ADMINISTRATIVE PROCEDURES MANUAL NUMBER: cap.0002 REVISION: 0 TITLE! 0FFSITE DOSE CALCULATION MANLIAL PAGE 27 0F at Trlttum is assum d not to deposit onto vegetation or the ground, i Hence, the concentration in vegetation is assumed to be related to ,I the local atmospheric concentration as described in RG 1.109, Rev. 1. Appendix C. The dose commitment to the Maximum Exposed (Hypothetical) Individual from tritium in gaseous effluent is I calculated with the equation: l r D,) 3.17x10-8 7yfq 7gg{.pajip}i.H-3 p y Where: I i p - 1, 3, 4, 5, and 6 1 includes H-3 only i X/Q The atmospheric dispersion factor for a ground-level or building wake discharge. Either an annual average, multi-year averag, or concurrent meteorology.is a:ceptable (sec/m ). l 3.17x10-8 years /sec I Other terms as defined above. Dose factors R for RSNGS are dertw.i using the equations and methodsinRGh<89,Rev.1.AppendixC. Values of parameters in RG 1.109, Rev. 1. Table E-5 are assumed to represent the Maximum Exposed (Hypothetical) Individual unless Land Use Census data ( justify a different value. Any different values from default values will be justified and added as a table to the 00CM. Values of other parameters recommended in RG 1.109, Rev. 1, including those recommended in the absence of site-specific data, are used in .I the equations to derive the dose factors. (GASPAR or REIMS may be used to perform the calculations.) 6.11 Cat Done Proinctions Thirty-one (31) Day Dose projections are calculated to show lE compliance with Technical Specification 3.18.4 Thirty-one (31) l;5 day dose projections do not need to be performed when GASEOUS EFFLUENT RADHASTE TREATHENT SYSTEMS are being fully utilized. l3 These systems are considered operable by meeting Technical ,3 Specifications 3.18.1, 3.18.2 and 3.18.3. The dose projection equations are the same as used for liculd per Steo 6.5. I I

I. MANUAL:- CHEMISTRY ADMINISTRATIVE PROCEDURES MANUAL NUMBER: CAP-0002 REv!$ ION: 0 I TITLE: 0FFSITE DOSE CALCULATION MANUAL PAGE 28 OF 48 -{ 6.12 Fuel Cvele Dose If a calculated dose exceeds twice the limit of Specification 3.17.2.4, 3.17.2.b. 3.18.2.a. 3.18.2.b, 3.18.3 or a level in I Specification Table 3.22-2 is exceeded, an assessment of compilance with Specification 3.25 must be made. Liquid dose calculations shall be made using the general methodology of Step 6.4. Gas dose s calculations shall be made using the general methodology of Steps i !g 6.9 and 6.10. These methodologies are to be used as a guide and n 5 strict adherence is not required because the Fuel Cycle Dose l' l Calculation is done to determine the actual dose received, not a hrPothca' **"'ava- 'h'r" **r**eters such as dilution Lal5 beyond the site boundary and residential shielding may be factored i into the calculation. The total body and organ doses shall be the result of summing the individual ccatributtons from 11guld, gas, and direct radiation sources for ths affected Member of the Pubite. Irradiation, i.e., exposure to an external source of radiation, directly from the RSNGS normally will be evaluated with the aid of environmental dosimetry such as thermoluminescent dosimetry (TLD) I or portable ton chamber (PIC) measurements. 6.13 EPA Renortina Reautrements (CCTS T890828001) If a calculated dose exceeds the limit of Specification 3.17.1, 3.17.2.a. 3.17.2.b. 3.18.1, 3.18.2.a 3.18.2.b. 3.18.3, an assessment of compliance with 40.CFR Parts 302 and 355, Reporte)1e I Quantity Adjustment - Radionuclides, must be made, i This involves determining the maximum quantity of radionuclides released in a 24 hour period and comparing the quantitles to the values listed in 40 CFR 302 Appendix B. The " sum of the ratios" method shall be used to determine compliance. If the " sum of the. lE. ratios" is greater than one, the National Response Center shall be 3 notified. Since Rancho Seco's systems and procedures are set up to normally operate within the above limits, this condttion is not expected to occur, therefore, specific implementation procedures to determine compliance are not required, 1 7.0 RECORDS The following individual / packaged documents and related correspondence completed as a result of the performance or implementation of this procedure are records. They shall be 'I transmitted to Records Management in accordance with RSAP-0601, Nuclear Records Management. None 't .-- ~

E ) MANUAL: CHEMISTRY ADMINISTRATIVE PROCEDURES MANUAL NUMBER: CAP-0002 REVISION: 0 i I TITLEt OFFSITE DOSE CALCULATION MANUAL PAGE 29 0F 4R t LIQUID EFFlutWT FLOW DIAGRAM l l LIQUID EFFLUENT FLOW DI AGRAM I g.m=...,.

    • M w *. r"u."oe"n**en'Ifw"e t

o wosusen.aven g

s. EM* mt e, _ _

= l t'E 4'" A'

e., y : % g..
l'

~"' L. t.?".th.,,,. = t

u a.u

s' ;",2*.5" < =>

  • l'awa ="

~ .mo .a

c...
  • '."."./ *."."

I A,= ANN

  • #8U VALVE SAkkERY f

. svues.Rta) 4 l5 s ecowoo.Y DelLER Auluu 7 I w . wuce u i asGEN ,g 3,n... e com wrens n i U p i q y M c muut l j l A RMut l l 0 mwuT l I g ..E.,. pays. [ l 'gtT s c o o"a.- WIWNO 'l; E5 -+- M = a ,mo, ( soutw CANAL ) I ~ g p p p F*! W4SC Rtit,42068 gyg = PLANT EMUENT ^ I TO CLAY CRCEM f +Yr Ve, \\; e -s>( E =Y M ) t I e . TuRelNE OCCW STORM DRMNS CAN BC DIRECTED TO THE w OILY WATER SEPARATOR (NORWAL) OR THE POUSMCR DCWIN SUWP w

I Page 1 of I

M-W mW W meeeee eee t E' = m c Q9733 m P GASEOUS EFFLUENT FLOW PATH o n. A.,.. .e, -A. --lGt AND SF AL E wS4 A4 fS T l ggggg g ggg, m m j gygg O 5 o Ati f4L f e AttW. 09t DC F WH AlfST Pt ENtted - "" IS i (EtstMS) IlIlil Il 11 ggg R15006 - 6f, p h 3 M st1 SOOT

  • e CoasPACTOct ROOed t

R= til DC Alf M 94LDC eOECON ARE A R/' p w M 2 STACM STACK e PASS SAasPLE SMs0 e CHEtdICAL STORAGE BAtCONY F d e ass 5C WASTE Tasem ROOne $.e I (Ei56.Q e VALW cat tEMY m p Ng $FP 9 TOG R e A* HPer POOas M e L 4 l yn { eEAST/vuEST OH PUesP MOOnes Q [ y t e.ECAv HE AT Suese WMTS eO c Cor== 2~5 E g"*,' "y a e n.oro,. Poe.P,,00m. S .) n e er. ,P oOn. = g C ~ g e SPE*ef RE5sse TAMM #00as g p p (Eisco S fty Q e SEAL nETunN COOLEn mOOnes g g c q ( e 9A CONC MOOas y ,N CTuf stOc HOT LAB gg%] l e es. EVAPostATOft ROOne i m 4/5 t g E J e EAST /tuE3T ON Ctm ROOnes y j ~ g e EON EMCHAseGE ROOne p g e WASTE GAS COnsp mOOne y c" e useOEnc8touseo TAMM5 g ( tNtE T AIR Q@'*" <sd e. esc.AsTE s, PE. <- .AP3 y e ac =AsTt cAs sm*,tn (eAC) cas sunct cAs twCAv _ Q t m 7ANM T AteK WNT k CopeOEteSEtt HO,O,GeeG MC DRAIN TANM WNT e M 9, A. E., ECTO, ,,C.AsTE,LAso T - e e, p< uAME-oe TAMM vt N Ts e My, i 0 ANAtvZER RETURNS e seeTE94Ene 0805sTE sTO.D.Astt-1 2 =A P CtE Ae.I,..t A TON =s, = C 2.. - l ace moc s.u. 0- mea w.T o M SOS WNT { gng ygues l-CHARCOAL (POTFMTIAL gaf LEASE EVAPOftATOst >og P A THWAV) pp e a ~ I r r <a .,n.. ...n. ,m.. n a

I I MANUAL: CHEMISTRY ADMINISTRATIVE PROCEDURES MANUAL, NUMBER: CAP-0002 REVISION: 0 a I l PAGE 31 0F 48 TITLE: OFFSITE DOSE CALCULATION MANUAL DOSE FACTOR PARAMETERS i CONSUMPTION AND USAGE PARAMETERS AG[ 1.109 DEFAULT RigGS PATNWAY Adult 520 kg/yr 520 Irrigated Stored Vegetables Teen 630 kg/yr '630 I Child 520 kg/yr 520 Infant 0 kglyr 0 Adult 64 kglyr 64 Irrigated Fresh Vegetables 4 Teen 42 kglyr 42 Chlid 26 kglyr 26 I Infant 0 kg/yr 0 Adult 310 kg/yr 310 Irrigated Milk Teen 400 kglyr 400 Chtid 330 kg/yr 330 Infant 330 kglyr 330 Adult 110 kg/yr 110 Irrigated Meat & Poultry Teen 65 kg/yr 65 Child 41 kg/yr 41 I Infant 0 kglyr 0 Adult 21 kg/yr 21 fish Teen 16 kg/yr 16 I Child 6.9 kg/yr 6.9 i Infant 0 kg/yr 0 j Adult 5.0 kg/yr 6.9 i Other Seafood Invertebrate Teen 3.8 kg/yr 5.2 (Crayfish) Child 1 7 kg/yr 2.2 Infant 0 kg/yr 0 Adult None 0 Algat Teen None O I Child None 0 Intant None 0 I Hater usage (Drinking Water) Adult 730 1/yr 0 Teen 510 1/yr 0 i Child 510 1/yr 0 Infant 330 1/yr 0 I I i Page 1 of 3

I MANUAL: CHEMISTRY ADMINISTRATIVE PROCEDURES MANUAL NUM8ER: CAP-0002 i REVISION: 0 I PAGE 32 0F 48 TITLE: OFFSITE DOSE CALCULATION MANUAL DOSE FACTOR PARAMETERS (Continued) j I i CONSUMPTION AND USAGE PARAMETERS (Continued) I Afag 1.109 DEFAULT. RiNfa5 l PATHWAY Adult 12 hr/yr 200 Shorvitne Recreation Teen 67 hr/yr 100 I Child 14 hr/yr 14 Infant 0 hr/yr 0 I Adult None 100 Swlming Teen None 100 Child None 14 I Infant None O Adult None 0 E Boating Teen None 0 g Child None 0 I Infant None 0 Adult 8000 m3 8000 i Inhalation Teen 8000 m3 8000 l Chlid 3700 m3 3700 Infant 1400 m3 1400 L IRRIGATION RATES AND FRACTION OF IRRIGATION 1.109 DEFAULT RSHGS I 263 11/m2 mo 263 l / Irrigation Rate Time field has been irrigated prior 15 years 15 I to crop of interest None None Fraction of year fleid is irrigated 'I None 0 Fraction of animal water intake not obtained from the irrigation system (Irrigated Heat) None 1 Fraction of animal water intake not obtained from the irrigation system (Irrigated Milk) I Page 2 of 3

I I MANUAL: CHEMISTRY ADMINISTRATIVE PROCEDURES MANUAL NUMBER: CAP-0002 REVISION: 0 I-TITLE: OFFSITE DOSE CALCULATION MANLIAL PAGE 33 0F 48 DOSE FACTOR PARAMETERS (Continued) I TRANSIT. TRANSFER and HOLDUP TIMES 1.109 DEFAULT 83NGS I ~ Irrigated Stored Vegetables Holdup Time 1440 hrs 1440 Irrigated Fresh Vegetables Holdup Time 24 hrs 24 Irrigated Milk Holdup Time 48 hrs 48 Irrigated Meat Holdup Time 480 hrs 480 Transit Time from time of sample to None 72 brs I time of release TransitTimetodrinkingdater None 0' mm=5 1.109 DEFAULT RSRGS All pathways None 1 (None) Shore-width factor 0.2 0.2 MISCELLANECUS I 1.109 DEFAULT RSRGS Fraction of Leafy Vegetables grown 1.0 1.0 in garden of interest Fraction of produce ingested grown .76 .76 in garden of interest Crop Growing Time for Leafy 60 days 30 Vegetables ingested by men Crop Growing Time for Pasture Grass 30 days 30 l Crop Yield for Leafy Vegetables 2.0 kg/m2 2,0 ingested by man Crop Yield for Pasture Grass 0.7 kg/m2 2.0 I Page 3 of 3

I i l MANUAL: CNEMISTRY ADMINISTRATIVE PROCEDURES MANUAL NUM8ER: CAP-0002 REVISION: 0 PAGE 34 OF 48 l . TITLE-OFFSITE DOSE CALCULATION MANUAL ATMOSPHERIC DISPERSION AND DEPOSITION PARAMETERS I GASEOUS EFFLUENT PATHMAYS 1989 CONTROLLING LOCATIONS" j I 0/0*) = PATHMAY DIRECTION DISTANCE X/Q*. (m-2 (m/sec') Inhalation ENE 1128 M 7.2E-06 4.1E-08 Ground CNE 1128 M Vegetation ENE 1128 M 7.2E-06 4.1E-08 Cow Milk ENE 1128 M 7.2E-06 4.1E-08 I Meat Animal S 195 M 1.2E-04 Meet Animal SSE 198 M 3.4E-07 Exclusion Area NM 640 M 2.2E-05 Site Boundary NNM 670 M 2.1E-05

I GASE0sS EFFLUENT PATHMAYS FOR THE IOS 1989 CONTROLLING LOCATIONS" i

J I D/0*) PATHMAY DIRECTION DISTANCE X/Q*2 (m-2 (m/sec ) Inhalation ENE 1402 M 4.5E-06 l 2.5E-08 Ground ENE 1402 M Vegetation ENE 1402 M 4.5E-06 2.5E-08 Cow Milk-ENE 1402 M 4.5E-06 2.5E-08 Heat Animal MNM 80 M 8.2E-04 1.3E-06 I Exclusion Area NH 272 M ,9.6E-05 Site Boundary NNM 488 M 3.5E-05 Based on msteorological data from January 1977 to December 1987. Based on '989 Land Use Census. 4 1 I Page 1 of 1 ~

. ( 1 ' i4ANUAL: CHEMISTRY ADMINISTRATIVE PROCEDURES MANUAL NUMBER: CAP.0002 REVISION: 0- ,I PAGE 35 0F 48 TITLE: OFFSITE DOSE CALCULATION MANLIAL 4 EXCLUSION AREA BOUNDARY i E E j l f / e. j / \\ \\

f-

~ 3 m.. _ ^~h.. i 1 E 3 t== - u - E L '"'~ ()suus ~ ~ ~, 1. I I L: i LI lI Page 1 of 1 9 - we -, ~ ,.,,,-_...m.

1 i I MANUAL: CHEMISTRY ADMINISTRATIVE PROCEDURES MANUAL NUMBER: CAP.0002 I REVISION: 0 i f I PACE M OF 43 TITLE-0FFSITE DOSE CALCULATION MANUAL i SITE BOUNDARY FOR LIQUID EFFLUENTS I For Compliance Nith 10 CFR 20 l .e I 1 e m A L t / W " )* l Y <. / A an r t \\ ' g &. k* E :: " <""" EEE' ~ lB g --.,=-s.. .3 3. = =- - c wr = ,3 e.. f %.. - L YL %~ T f \\ 'y% t L i y.h',Q,IWL 7 -l /.*... *.*..*... . f,J,s 7l l Q '~, - / I h, p '- 3 C : -Q l w. / +-- s._ e ~ .c c -...V I i i L l l i Page 1 of I l~

I MANUAL: CHEMISTRY ADMINISTRATIVE PROCEDURES MANUAL NUM8ER: CAP-0002 REVISION: 0 I PAGE 37 0F 48 TITLE-0FFSITE DOSE CALCULATION MANUAL SITE BOUNDARY FOR CASEQUS AND LIQUID EFFLUENTS for Compliance With 10 CFR 50 1 i I ll l e I ) / ~ 1 ,+ \\g 3 /anx, 6.

g i

} lE ). 1 ag ,,4,,,,,,,,,,,,,,,,,,,,__,,f,v_ ~ J -l r,;g,;. W p/ 4,r[f f' ~ %' m t l. du \\'5 Nh ::m / 1 1 's- , e, - 7ri=- / s- ..... N ( = 4-..... - -... m d I 0;{ %(~f I \\ u. - g,.. g r...-- .* b,' 1 E ) E Athchment 7 Page 1 of I

I NUMBER: CAP-0002 MANUAL: CHEMISTRY ADMINISTRATIVE PROCEDURES MANUAL REVISION: 0 !lW PAGE 3R OF 48 TITLEt OFFSITE DOSE CALCULATION MANUAL HISTORICAL LIQUID SOURCE TERMS'- ( Gamma Emitters All Nuclides I 'I Relative Relative l fraction fraction Nuclear C' (pC1/ml) ,1 / CO-60 3.34E-09 14.02 0.1402 .33 0.0033 .CS-134 2.09E-09 8.77 0.0877 .21 0.002) CS-137 1.84E-08 77.21 0.7721 1.82 0.0182 l I ] H-3 9.88E-07 0 0 97.64 0.9764 l TOTAL 1.01E-06 100.00 1.0 100.00 1.0

  • Based on Retention Basin Effluent History of Rancho Seco (July 1 -

t December 1, 1989) l

3 i

I J l I I lI I Page 1 of 1

r-l } MANUAL: CHEMISTRY ADMINISTRATIVE PROCEDURES MANUAL NUMBER: CAP-0002 i I REVISION: 0 TITLE

  • OFFSITE DOSE CALCULATION MANUAL PAGE 39 0F 48 f

LIQUID MONITOR DETECTOR EFFICIENCIES guip17A & R15017B* a (Detector Model RD-53) I Nuclide Efficiency ena/uC1/cc MO-99 3.47E+07 I-131 1.90E+08 I I-132 4.17E+08 I I-133 1.53E+08 + I-135 1.74E+08 CS-134 3.25E+08 1 CS-136 4.70E+08 l 'sg CS-137 1.28E+00 CR-51 1.85E+07 l r MN-54 1.30E+08 i I FE-55 7.60E+03 FE-59 1.26E+08 CO-58 1.85E+08 I CO-60 2.40E+08 3 ZN-65 6.49E+07 i SB-124 2.66E+08 BA-140 8.98E+07 I LA-140 2.69E+08 CE-141 7.68E+07 CE-144 1.80E+07 L ) rr. Ca cuiation z-Row-IO261 L.E ! E 1 I Lg 'l-I Page 1 of 1 4 --..n~ ... ~.

J +~- _ \\ MANUAL: CHEMISTRY ADMINISTRATIVE PROCEDURES MANUAL NUMBER: CAP.0002 ~ (L REV1SICm: 0 PAGE 41 0F 4R TITLE: OFFSITE DOSE CALCULATION MANUAL ORGAN DOSE FACTORS FOR LIQUID EFFLUENTS (continued) Oos acwa vastai atti - teen Unite tre area /hr per UC1/01 N u.c. l.i d.e...b.ene.......L..iv e.r......T.h.e.d.y.....T.hyt.e.ld.....E14.nt.y... .....L.ung.*......G..i t.r.e.c.t... I 0.000t+00 1 310t+01 1 310t+01 1.370t+01 1 3708+01 1 370t+01 1.3108*01 S.640t+09 1.130t+0S 1 130t+bl 1.130t+0S 1.130t+0S 1.130t+0S 1.130B+99 M*3 6.360t+01 6.360t*01 6 340t+0 L 6. 3600+01 6.360d+03 6.3608+01 6.3 c.34 NA*34 1.030t+r0 1.030t+00 4.100t+00 9.310$+00 3.1008+00 1.0008+01 1.040s+03 4.440t+0? P*33 I 4.300t*03 3.340t+0S 4.490t+04 4.4000+03 9.6900+04 4.300$+03 6.6300+0S Chall 3.4300 06 0.0000+00 3.4300*04 0.000t+00 1.3400 03 MNel4 MN*l6 0.000t+00 1 9308 049.690t+03 3.360t+03 7.3908 04 1.3901404 4.160[+0) 4.1900+03 1.llot+04 3.610t*04 1.400t+04 1.0008+03 1.000h+03 1.160s+04 0.9300+04 Fr*ll 1.370t+04 1.300t+03 1.000t+0 3 3.330t+03 1.380t+93 1 360'l+03 1 3008+03 1.3308+046.36 frall 1 M*lt C0 60 6.360t+03 1.1000+04 1 690t+04 1.llet+04 0.0008+00 0.0008+00 0.000B+00 9.060g+03 N!*63 4.900t*06 3.100B+04 4.??0 *08 0.0008+00 0.0008+00 0.0000+00 9.6700 03 0.960t*03 9.3808*01 4.000[s*01 0.9908 03 3 31:4+00 8.5908 03 4.930p01 0.1908*04 1.0908*04 N1*65 1.960t+04 3.630t+09 1.330t+0S 3.3900+03 1.600 +0S 3 390 493 1.1100+0S CV*64 0.000t*00 0.000t*00 0.J000+00 0.000$+00 0.000 +00 0.000 +00 0 000$+00 SN 65 0.000t+00 0.000t+00 4.9308*06 0.000t+00 0.000 +00 0 000 +00 0.000B+00 i SN*69 0.000t*00 0.000t+00 0.000t+00 0.0008+00 0.0008+00 0.0008600 0.0008+00 SR*03 0.000t+00 0.000t+00 0.000$+00 0.000$+00 0 000$+00 0.0008*00 0.0000+00 39 84 4.100t+00 1.400$*06 6.940B+04 4.100g+00 4.1008+00 4.100$+00 3.0100+44 99 0% 0.000t*00 0.000$+00 0.000$+00 0.000s+00 0.0000+00 0.0008+0 platl 9t*t6 I 3.930t+09 S.640t*03 4.300$+03 S.640P=03 9.640 +03 S.640 *03 3.400 +4403 6.160 +03 3 99 99 SR*09 1.400t+04 6.1608*03 1.*40t+04 4.1608 03 6.16 01 1 1600-01 3. 6409+01 89 90 $.130t+00 1.1408=01 3.3908 01 1.1008 01 1 10 6.960t-03 0.0008+00 3.3708-04 0.000t+00 0.000 +00 0.000B+00 1.4308 01 Shell 3.350t+00 4.8708 03 1.6708 01 6.0708 03 6.010$*03 4.010 +03 3.710$+04 Statt 0.000t+00 0.000t+00 0.000t+00 0.000t+00 0.0008+00 0.000 +00 0.0009+00 V=to i 3.460t+03 3.1608 01 6.910E+00 3.7808 01 3.7908*01 3.100 +01 1.3100+0S YellM 1.640t*06 4.300$*06 4 990t*06 4.300t*06 4.2003-06 4.300B+06 3.3608 01 V 91 3.130t*03 1.610t*03 1 990B+03 1.8700-03 1.9108 03. 510$*03 1.1000+03 Y 93 1.190t+03 9.670t+01 9.3400+01 0.630t+C1 1. 030B+03 8.6308401 3.430S+04 Yet)

9. 410t*01 9. 3 7 0t *01 9. 37 08*01 9. 3 608 *01 9. 3 40t* 01 9. 3 608*01 3.4 3 00+03 3R*tt 4.130t+03 3.0308+03 1.790t+03 4.460t+01 3.tl0t+03 4.460$+01 1.0300+06 Sp*tt I

6.360t*01 4.330B+03 e.300t+01 6. 3608-01 9.8100+03 4.360[*01 7 ND*tt Mo*tt 0.000t+00 0.000t+00 0.0000+00 0.0008+00 0.000B+00 9.0008+00 0.000t*00 4 6408-04 TCellM l.060t+03 3.910t+01 3.710t+03 3.9108+01 1.900t+03 3.510t*01 4.6100+041 70 101 RU+103 S.000t=04 1.010t*04 4.9308-04 RU 106 1 990E+04 1.400B+03 3.140t+03 1.400B+03 3.060t*04 1.400t*03 1.8108+0S 90 105 I AG*11cM 1.870t+03 1.830$+03 1.930t*03 1.0008+03 3.930E+03 1.060t+03 3.1700+06 f.4308+03 3.7900+03 S.7508+0J 4.910t*01 4.0108 01 6.010$+04 Trat3?M l.930t+04 3 100t+04 7.000t+03 1.410t+04 3.400t+0$ 3 930t=03 1.4000+0S Tt=13SM 2.060t+04 S.040B+01 6.9308 01 3.330t*01 1.4108 01 4.5100*01 3.440t+00 1.S708 043.5008+04 3.340t+0 TE=131 1.330t+04 7t*13tM 1.750t+04 3.000t+04 0.000t+00 0.000$+00 0.000t+00 0.000B+00 0.000B+00 0.000t+00 0.000$+00 Tt*131M 1.190t+0J S.610$+03 4.740t+03 8.9000+03 S.060R+03 S.300t+00 4.510g+04 TE*139 0.004t+0C 0.000t+00 0.000t+00 0.000R+00 0.000t+00 0.000t+00 0.000s+00 6.5008603 4.170t+03 3.930t+03 4.400t+03 4.000t+04 3 0708400 1 330t+05 TE*131 3.000l+00 9.4908+00 4.360t+00 7.0608+03 1.410B+01 0.0008*01 7.4500+00 TE 133 9.130s+03 1.360t+03 7.330R+03 3.9308+0S 3.330t+03 1 000t+01 3.110t+03 1*130 1*131 1.4608-04 3.010B*04 1.3700*04 1.3908 03 4.0108-04 0.000t+00 1.6608 04 3.3 70t+01 3.110t+01 1.330t+01 S.1300+03 6.64 0t+01 1 060t+00 3.0000+01 !=133 0.00nF+00 0.000B+09 0.000t+00 0.0008+00 0.000E+00 0.0008+00 0.000t+00 1*133 S.2003 01 I*134 1.050t*01 4.160t=01 1.??0t*01 3.0608+01 1.S30t*01 4.490t*04 S.0408+0S 1 100t+04 S.4000+0S 3.030$+03 3 7700+0$ 1.490t+0S 1.670B+04 1*139 Cl*134 1.300t+0S t.630t+04 1.150t+01 6 960t*04 1.110t+04 1.0408+04 3.310t+04 6.990E+0S 9.300t+0$ 3.340t+09 3.030t+03 3 1008605 1.360t+0S 1.630B+04 CS*136 CS*131 0.000t+00 0.000t+00 0.000t+00 0.0008+00 0 000t+00 0.000t+00 0.0000+00 C8=135 0.000t+00 0.000t+00 0 000t+00 0 0008+00 0.000B+00 0.000t+00 3 940t*06 DA*139 9.340t+03 1 640t+01 3.510t+03 9.010t+00 1.310t+01 1.430t+01 0.330t+03 0.000t+00 0.000B+00 0.000t+00 0.000t+00 0.000B+00 0.000t+00 0.000t+00 EA*140 0.000t+00 0.000t+00 0.000t+00 0.000t+00 0.000E+00 0.000t+00 0.000E+00 OA*141 SA*143 3 300t+00 3 000t+00 1.910B+00 1.860t+00 1.090t+00 1.tlet+00 1.310t+04 0 000t+00 0.000t+00 0.000t+00 0.000t+00 0.000t+00 0.000t+00 3.360t=0S LA*140 LA-143 1 690t+01 1.300t+01 6.0008+00 9.190t+00 9.640t+00 9.150t+00 3.390t+04 CE*141 1.190t*00 1.460E+03 1.410t+00 1.990t+00 1.660E*00 1.590t+00 4.410t+03 1.300E+03 S.100t+03 8.470t+01 3.130t+01 3.130t+03 3.130t+01 3.970t*0% CE*143 7.900E+00 3.100t+00 3.970t*01 0.000t+00 1.el0E+00 0.000t+00 3 630t+04 Ct*144 PR*143 0.000t+00 0.000t+00 0.000t+00 0.000t+00 0.000t*00 0.000t+00 0.000t+00 PR-144 7.730E*00 8.170t+00 3.830t+00 3.4?CE*00 9.830t+00 3.470t+00 3.060t+04 ND*141 3.170t+ 01 1.790t +01 7.110B+00 1. 360$+00 1.3 60t+00 1. 3 60t+ 00 4. 510t+ 03 Walt? 1.500t+00 1.340t+00 1.3900+00 1.3408+00 1.390t+00 1.340t*00 3.410t*03 NP-339 0 l Page 2 of 4 l

lll I NUMBER: CAP-0002 CHEMISTRY ADMINISTRATIVE PROCEDURES MAWAL MAWAL: REVISICM: 0 I OFF111E DOSE cat ellLATION MANLIAL PAGE 42 OF 48 TITLE

  • ORCAN DDSE FACTORS FOR LIdulD EFFLUENTS (continued)

~ I 0005 PACNR TA01At A(Al

  • Calid Units are eres/hr per uct/m1 j

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P*33 3.5408 01 3 540t*01 7.9900+00 4.930'l+00 1.430$+00 0.090 +00 4.000$+03 CRell S.000t*01 3.9300+0S 4.7408* 04 S.0008601 1.100$+04 S.000 +01 2 130 pet i RN*64 0.0008+00 3.510B+04 S.6000*09 0.0000+00 3.040$*04 0.000 +00 3.440s*03 MW=to 1 0309 04 1.190 +03 3.390h+03 Ftell 3.400t+04 1.370t+04 3.940$+03 1.0300*441.400$+01 1.400$+01 1 040 +04 3.7301 1+ 04 ) 3.990B+04 1.?t0t+04 I 3 310t+04 Frelt f* 0 3 1.790B+01 1.300t+03 3.000B+03 1.790$+01 1.1998+01 1.790 +01 1.300 0.090t+03 7.910S+03 3.0400+04 0.090ll+03 0.090g+03 0.090 +03 3.700i l+44 t c0*Se C0 60 p!*s) 3 030t+06 S.4008*04 3.400t+04 0.000 t+00 0.000s+00 0.000 +00 3.690' l+ 0 3 r N1 66 1.5308 03 1.430B+44 0.390B*06 0.000 l+00 0.000g+00 0.000 +00 1.790 l*03 CU 44 1 3005 03 1.370t+00 7.700$*01 1.300 l*03 3.000s+00 1.300 *03 S.09011+01 1N*66 9.S30t+64 3.940B+0S 1.900t+0S 3.310 l+01 1.6000+0S 3. 310 +01 4.460$+04 I l+00 0.000S+00 0.000 +00 0.000s+00 0.000t+00 0.0000+00 0.0008+00 0.900 3Ne49 0.000t+00 0.0000+00 9.900B+0S 0.000'l+00 0.000$+00 0.000 +00 0.0008+00 SR*03 0.000t+00 0.0098+00 0.000$+00 0.000g++00 0.000$+00 0.000 +00 0.0000+00 0A.04 0.00Ct+00 0.000B+00 0.000B+00 0.000p 00 0.000s+00 0.000 +00 0.000$+00 i i SR*05 S.7408 01 1.610B+0S 9.000B+04 S.7408 01 S.140$*01 S.740 *01 1.0308+04 R$*06 0.000t+00 0.000B+00 0.000B+00 0.000$+00 0.0000+00 0.000 +00 0.000$+00 RO*00 0.000t+00 0.000B+00 0.000B+00 0.000$+00 0.000N+00 0.000 +00 0.0008+00 l R9*09 l Shatt 6.400t+0S 7.900B 03 1.090$+04 7.9003 03 1.900 1 03 7.900 +03 3.910S+04 i Sp=90 1.470B+0? 8.6308 04 3.9308+04 0.630B*04 0.630 l*04 0.430 +04 3.970$+0S i 1*03 1.680 +03 3.300 +01 SR*91 1.0408+01 1.4308 03 4.000l>01 1.4301,*03 1.430 l 89 93 1.0308-03 0.0000+00 4.090ll*04 0,000l l+00 0.000 i+00 0.000 +00 1.930 +01 l 1*90 4.300B+00 9.680t*03 1.340!l*01 9.630 W93 9.630 +0S 9.630 *03 1.330 +04 I 0.000t+00 0.000$+00 0.000.l+00 0.000l+00 0.0001 t+00 0. 000 +00 0.000S+00 Yet1M 4.490t+03 S.390t*03 1.310$+01 S.3900 08 S.390 Met S.390 *03 S.900S+04 Y 91 3.3103 09 0.0000+00 1.330$*04 0.0000+00 0.0008+00 0.000 +00 4.900$*01 Y*93 1.0908*03 3.3000 03 3.430B+03 3.300$*03 3.3008*03 3.300 +03 1.3408+03 [ r*93 0.330B+01 3.770R+01 3.600B+01 1.3108+01 3.4903+01 1.310 +01 1.430$+04 i 1R 96 5 1.400t*01 1.3308 01 1.3308*01 1.3108 01 1.3308-01 1.310 *01 1.9008+03 1 Ret? S.300t+03 3.060B+03 1.4908+03 6.390 +00 1.940 +03 4.390 +00 3.700g+0S N0*95 8.900t*03 7.010$+03 1 130t*03 0.900 +03 1.500 +03 0.900 +03 S.000s+03 Mo*99 4.3408-04 1.500t*04 1 1008 03 9.770 +0S 9.690 03 4.330 +04 3.7608 01 1 TC 99M 0.000t+00 0.0009+00 0.000E+00 0.000R+00 0.0000+00 0.000 +00 0.0003+00 TC*101 1.030t+03 4.930B+00 3.9608+03 4.930$+00 3.970B+01 4.930 +00 3.430B+04 I ~; RU+103 1.3108 03 3.9308 08 4.900B+04 3.830g*06 1.130B*03 3 830 +0S 3.3908 01 RU+105 RU+106 3.100f+04 3.070$+01 3 900$+03 3.070s+01 4.390B+04 3.070 +01 4.940$+0S A0 110M 1.790B+03 1.340B+03 1 040t+03 1.400B+00 3.330t+03 1 400 +03 1.330t+0S TE 13SM 3.040B+04 0.380B+03 4.0408+03 0.540B+03 6.7308 03 6.730 +03 3.9400+04 1.100B+04 3.330B+04 3.450t+09 4.100 *03 7.9308+04 TE*137M 9.300B+04 3.9008+04 0.9408-01 3.410B+01 1 9308 01 4.1908 01 3.940t+00 3.300 +0S 3.4 908+01. I TE 137 3.310t+0S 1 000 +00 1.3 30B+0S Tt*139M 1.090t+0S 3.0808+04 1 7008+04 3.930t+04 0.000B+00 0.000B+00 0.000E+00 0.000t+00 0.000t+00 0.000 +00 1.1408 06 T!*139 TE=131N 1 4008+03 S.1308+03 S.4608+03 1.0S0S+03 4.960t+03 7.300 -01 2.000B+04 0.000B+00 0.000B+00 0.000t+00 0.000B+00 0.0005+00 0.000 +00 0.000B+00 i Tt*131 0.180B+03 3.010S+03 4.360S+03 S.3608+03 3.390t+04 4 300 +01 3.630B+04 75-133 6.3600+00 1.370B+01 6.630t+00 1.3903+03 1 9008+01 1.130 -01 6.0305+00 !*130 3.0408+03 3.070B+03 1.1008+03 6.040$+09 3.400t+03 1 910 +00 1.060$+03 r 1+131 3.600$*04 4.700g*04 3 300$*04 3.3308*03 1.3308 04 0.000 +00 S.4309 04 1*133 9.960B+01 1.490 +01 3.3308+01 y 4.690$+01 S.740s+01 3.100B+01 1 0000+04 1 133 0.000B+00 0.000B+00 0.00034 00 0.0000+00 0.000t+00 0.000 +00 0.0008+00 !*134 3.7908 01 4.0303 01 3.3308 01 6.0405+01 1.0$0r+00 6.340.*09 S.3003 01 1=135 7.610t+0S 1.380S+06 3.640t+0S 3.0900+03 3.070t+0S 1.390 +0S 7.030t+03 CS*134 4.140t+04 1.140t+0S 7.3708+04 1 090S+01 6.060B+04 9.090 +03 4.010S+03 CS*134 1.130B+06 1.070B+04 1.990t+0S 4.390B+03 3.500t+0S 1.360 +0S 7.180t+03 ,9 C6*137 0.000t+00 0.000t+00 0.000t+00 0.000$+00 0.000t+00 0.000 +00 0.0008+00 CS*130 0.000t+00 0.0008+00 0.0008+00 0.000B+00 0.000t+00 0.000 +00 3.8108 08 y SA*139 0.640t+03 8.960B+00 6.0$0t+03 1.300B+00 3.050E+00 S.090 +00 4.300$+03 SA-140 0.000t+00 0.000t+00 0.000t+00 0.000$+00 0.000t+00 0.000 +00 0.000t+00 0A=141 0.000E+00 0.000t+00 0.000t+00 0.000B+00 0.000t+00 0.000 +00 0.000t+00 SA+143 0.300t*01 4.9908 01 3.3708*01 3.6908-01 3.590E*01 3.990 *01 S.560t+03 LA*140 0.000t+00 0.000t+00 0.000t+00 0.0008+00 0.000t+00 0.000 +00 1.990E-04 LA=14 3 3.040t+0! 1.090t+01 3.1008+00 7.3108-01 S.030E+00 7.31C +01 1.330t+04 CE*141 4.0$0t*01 1.43 0t+03 3.440t*01 3 330Ba01 3.030t*01 2.330 -01 3.000t+03 I CE*143 3.390t+03 7.510B+02 1.300t+03 3.970B+00 4.170t+03 3.970 +00 1.950t+0S CE*144 1 110t+01 3.330t+00 S.510t*01 0.000B+00 1.000t*00 0.000 400 1.200E+04 PR=143 0 000t+00 0.000t+00 0.000t+00 0 000B+00 0.000B+00 0.000 +00 0.000t+00 PR=144 7.300t+00 6.040t+00 7.000t*01 3.47 08*01 3.4 708+00 3. 4 7 0 +01 9.030t+0 3 ND=147 3.650t+01 1.500t+01 1.170t+00 1 1708-01 1.7708 01 1.770 +0! 2.190E*03 M*197 4.000$=01 3.0308 01 1.9908*01 1.0008*01 3.330t*01 1 000 +01 1.130t+03 I-NPa339 Attach 8ent 10 Page 3 of 4 Ill

l11. 1 ll ) MANUAL: CHEMISTRY ADMINISTRATIVE PROCEDURES MANUAL NUMBER: CAP-0002 REVISION: 0 ( 8 PACJ 43 OF 48 j TITLE OFFSITE DOSE CALCOLATION MAHLlAL ) l ORGAN DOSE FACTORS FOR LIC1110 EFFLUENTS (continued) ) D003 FACTot T& Slat &(1)

  • Infant i

Units are area /hr por uci/a1 .........i t teet... I Nu c.l.i d e... to.ne.......L..i ve.r.....Thed y.........T.hy r.o..it.....R..i oney........L.u.ng s I 0.000t+00 1.1408+01 1.140t+01 1.1408+b1 1.140t+01 1 140[+01 1.140 +01 M*3 S.000t+0S 1 3408+0S 1.340t+0S 1 3408+0S 1.340$+0S 1.340s+0S 1.340 +99 C+14 1.760t+03 1.760t+03 1.740t+03 1.7600+03 1.160 +03 1.140 +03 1.100 +03 Nh*24 0.000B+00 0.000 +00 0.000 +00 1.330 +04 9.000t+0S S.390t+04 3.490t+04 I P-33 0.000t+00 0.000t+00 1.030t*01 S.1000-01 1c 130 +01 9.930$*01 3.300 +01 j CR*St 0.000t*00 1 600B+03 3.0308+01 0.000$+00 3 7308+01 0.000 +00 6.100 +01 MN*S4 0.000t*00 1 3308-06 0.0000+00 0.0000+00 1.0908-06 0.999 +00 1.119 +44 RN 56 S.610t+03 3 630t+03 9.690t+01 0.000B+00 0.0000+00 1.??D +03 4 619 +41 rt-SS s 1.040t+03 1 0100+03 1.1408+03 0.0000+00 0.00b t+00 S.3648+03 0.600 +43 Ft*S9 0.000t+00 1.000t+03 3.700t+03 0.0000+00 0.0006'*00 0.000$*00 3.70s +43 I-Co*Se 0.000t+00 3.010t+03 0.990B+03 0.000$*00 0.00f #96 0.000N+00 9.944 +43 co+60 1.?20B+0S 1 040$+04 9.910t*03 0.0000+00 0.De +00 0.000l l+99 S.390 +44 N1 43 1.4708-04 1.640$*09 1.9608-06 0.000 +0E 6.400 +DO 0.999 1+04 1 316 +43 l CU+44 0.000t+00 3.390t+00 1.060B+00 0.000 +00 3.010 +00 0.999 l+00 4.706 +01 N1*65 1.030$+0S 4.110t+04 0.0008+60 9 039 +04 0.000: 1+00 0.740 +44 l 3.030t+04 0.000t+00 0.000t*00 0.0008+00 0.0000+00 0 909 +00 0.000 l+00 0.9D9 +00 l 1N*49 'I 1N*49 0.000t+00 0.000t+00 4.1908 09 0.000B+00 0.009 +00 0.000l+00 0.990 +49 93 03 0.000t*00 0.000$+00 0.0008+00 0.000$+00 0.000$+00 0.0000+00 0.Dee +4e l 00 64 0.000t+00 0.0008*00 0.000t+00 0.000t+00 0.0000+00 0.D998+00 0.000 +94 t 8R.05 0.000t+00 1.1408+0S 9.690t+04 0.000B+00 0.999 +00 0.D00 +00 3.939 +03 90 04 0.000t+00 0.0008+00 0.0000+00 0.0008+00 0.000 +00 0.000 +00 0.000 +00 80 00

0. 000t+00 0. 0000 +00 0. 000t+00 0.000B +00 0.090 +00 0.000 +90 9.000! I+00

'I B0 03 3R*09 5.770t+04 0.000B+00 1 460t+03 0.000t+00 0.000 +00 0.000 +DO 1.100 i+0 3 3.910t+0S 0.000B+00 1.090t+0S 0.0008+00 0.000 +00 0.000 +0C 7.380 i+ 0 3 l 59 90. 4.010t+00 0.000t+00 1.4908-01 0.000$+00 0.000g++00 0.0000+00 4.tte l+00 88*91 1.040t*04 0.0008+00 6.030t*06 0.0000+00 0.000g 00 0.000S+00 1.9001-03 l. 89*93 0.0000+00 0.000B+00 0.000R+00 6.30 M+De 4.5902-03 0.000t+00 1.330t*04 fe90 0.000B+00 0.0008+00 0.000t+00 0.000$+00 0.0000+00 0.000$+00 0.000$+00 T*91M 3.3308-01 0.000B+00 0.0308-03 0.000$*00 0.000$+00 0.0000+00 3.3898+01 yett 0.000t+00 0.0000+00 0.0008+00 0.0000+00 0.000{+00 0.0000+00 3.310 +04 Y.93 3.060t=0p 0.000t+00 0.000t+00 0.0000+00 0.000s+00 0.0000+00 3.439 *e1 Ye93 +00 3.060t*03 1.4908 03 S.300t*03 0.0008+00 0.030$*03 0.000$+00 3.11 1R.99

  • 01 4.310t*06 7.400t*06 3.300t*06 0.0000+00 7.460$*06 0.9000+00 4.18 1R.91

-3.010t+00 1.160B+00 4.700B*01 0.0008+00 0.3108 01 0.0000+00 9.1998+03 N0*99 0.000t+00 1.300$+03 3 600B+03 0.0008+00 3.0000+03 0.000B+00 4.8900+03 N0*99 S.610t=04 1.160B=03 1.490t*03 0.000t+00 1.3508-03 6.000$*04 3.34M *01 TC+99M 0.000B+00 0.0008+00 0.0008+00 0.000R+00 0.0008+00 0.000$+00 0.0000+00 f t i TC+101 4.000t*03 0.000$+00 1.310t*03 0.0000+00 0.S00B*03 0.000t+00 4 9793*01 RU+103 0.000B+00 0.000B+00 0.000t+00 0.0000+00 1.930B*06 0.0000+00 0.380$*09 I RU+105 0.4008 01 0.000t+00 1 0508-01 0.000g+00 9.940t*01 0.000t+00 6.3098+00 RU+106 AG=110M 1.010B+03 1.330t*03 0.140B+03 0 000s+00 1.0908+03 0.000t+00 6.0900+04 ? ft=13SM 0.4005+03 3.030R+03 1.1908+03 3.0600+03 0.000B+00 0.000B+00 4.0400+03 ~ TE=131M 3.6308+03 0.690t+03 3.170t+03 7.9700+03 6.490t+03 0.000B+00 1.000B+03 9.610t*03 3.3808-03 3.0702-03 7.630$*03 3,3a0t*01 0.0000+00 3.0300+00 l TE 131 Tt*139N 3.0S0B+03 1.090t+03 4.700B+03 1.1100+03 7.630t+03 0.000B+00-1.0300+03 0.000t+00 0.000t+00 0.000S+00 0.000B+00 0.000t+00 0.0008+00 0.0008+00 TE-139 tt=131N 3.070t+01 1.160$+01 9.990B+00 3. 3400+01 1.9608+01 0.00084 0V 1.990t+03 0.000t+00 0.000t+00 0,0008+00 0.000B+00 0.000t+00 0.000t+00 0.000B+00 ~ TE 131 1.4108+03 6.900B+01 6.910B+01 1.030B+03 4.360t+03 0.0008+00 3.8008+03 TE=133 0.9308+00 1.9408+01 7.000t+00 3 3008+03 3.1408+01 0.000t*00 4.310B+00 !*130 3.010B+03 3.610B+03 1.9908+03 1.1900+06 4.3 30t+03 0.0000+00 1.390$+03 I 3*131 1.300$*06 3.640B+0S 9.4108*06 1 3408-03 3 990t*09 0.000t+00 3.140$*05 1*133 6.9908+01 1.030B+03 3.900B+01 1.0908+04 1.2008+03 0.000t+00 1.130B+01 1 133 0 000t+00 0.000t+00 0.000B+00 0.000B+00 0.000B+00 0.000t+00 0.0003+00 !=134 4.3308-01 4.4108 01 3.0708-01 7.9400+01 9.3008 01 0.000B+00 3 040S*01 1*138 1.990t+0S 3.090t+00 3.930$*04 0.0008+00 1.430B+04 3.0900+04 1.0400+03 l C0=134 1.060t+04 3.000B+04 1.1608+04 0.0000+00 1.330t+04 3.510B+03 4.610$+03 I CS*134 3.330t+0S 3.710t+0S 1.930t+04 0.000B+00 1.3708+04 3.9400+04 0.4700+03 CS*137 0.000t+00 0.000B+00 0.0008+00 0.0003+00 0.0008+00 0.000B+00 0.000$+00 CS*130 0.000t+00 0 0008+00 0.000$+00 0.0008+00 0.000t+00 0.000B+00 0.0000+00 BA*139 1.300t+03 1.3008+00 6.610$+01 0.000t+00 3.0908 01 1.000t*01 3.190R+03 BA*140 0 000t+00 0.000t+00 0.000t+00 0.0008+00 0.000t+00 0.0000+00 0.0000+00 Baal 41 0.000E+00 0.000t+00 0.000t+00 0.000t+00 0.000t+00 0.000t+00 0.000t+00 SA*143 3.050E*04 1.300t.04 3.090t*0S 0.000B+00 0.000B+00 0.000B+00 1.410t+33 LA*140 0.000t+00 0.000t+00 0.0000+00 0.000B+00 0.000t+00 0.000t+00 0.000t+00 LA*144 2.0702 01 1.360t*01 1.4908 02 0.0008+00 3.090E*03 0.000t+00 6.530t+01 i CE*141 3.300t.03 3.130t+00 3.4208 04 0.0008+00 6.100t=04 0.000t+00 1.3400+01 CE*143 9.030t+00 4 030t+00 S.500t*01 0.000t+00 1.430t+00 0.000t+00 S.6300+03 E-C E *14 4 0 000B+00 1.090t*03 0.000B+00 4.190t+00 1.060E*03 3 9408 03 3.900t=04 FR=143 0.000t+00 0.000t+00 0.000t+00 0.000B+00 0.000t+00 0.000B+00 0.0008+00 PR-144 4.01C E*01 4.940B=03 3.0300 04 0.0000+00 1.9003-03 0.000B+00 3.130B+00 ND*147 5.550t.01 3.060t*01 1.330B+01 0.0000+00 0.000t+00 0.000B+00 3.370B+01 Walt? NP*239 3.5108 04 3.340B-05 1.3708 09 0.0000+00 4.470B-05 0.000B+00 6.4003-01 l5.- Attachnent 10 Page 4 of 4

d' MANUAL: CNEMISTRY ADMINISTRATIVE PROCEDURES MANUAL AP-0002 ~ PAriE 44 0F at TITLE

  • OFFSITE DOSE CALCULATION MANLIAL HISTORICAL GASEQUS SOL)RCE TERMS I-Continuous Mode
  • 8atch Mode" Relative Relative

. fraction Nuclide C (pCl/cc) fraction C,(pCl/cc) Kr-85 0 0 0 2.89E-08 .23 0.0023 Kr-85M 6.89E-09 .36 0.0036 0 0 0 Kr-88 1.37E.71 0.0071 0 0 0' '. i Xe-131M 0 0 0 1.04E--07 .81 0.0081 Xe-133 1.77E-06 2.03 0.9203 1.26E-05 98.35 0.9835 Xe-133M 2.47E-08 1.28 0.0128 7.70E-08 .60 0.0060 Xe-135 1.08E-07 5.62 0.0562 1.70E-09 .01 0.000) 1 TOTAL 1.92E-06 100.00 1.0 1.28E-05 100.00 1.0 Based on effluent history of Rancho Seco (January to June 1989 SRERR) This source term is appitcable for ABS and ABGLV. This source term is applicable for RSS (initial and continuing I releases) and WGDT. I I I I 1 Page 1 of 1

NUNSER: CAP-0002 CHEMISTRY ADMINISTRATIVE PROCEDURES MANUAL REVISION: 0 MANUAL: PAGE 45 0F 48 0Frstir oost CAtculATION MANUAL nitt-( GASEQUS MONITOR DETECTOR EFFICIENCIES R15C44.1504E. and R11546A (Detector Model RD-52) ~ ~ l ~ Efttalency

Wucitd, enaluti/cc KR-83M 0.0 gg ggg 7.30E+07 KR-85 7.19E+07 I

KR-87 8.70E+07 KR-88 8.70E+07 KR-89 8.70E+07 KR-90 8.70E+07 XE-131M 0.0 XE-133M 0.0 XE-133 2.94E+07 I XE-135M 0.0 XE-135 7.75E+07 XE-137 8.70E+07 XE-13g 8.70E+07 AR-41 7.80E+07 From Calculation Z-RDM-10261 1 2 Page 1 of I

J CHEMISTRY ADMINISTRATIVE PROCEDURES MANUAL NUMBER: CAP-0002 ~ MANUAL: REVISION: 0 TITLf; 0FFSITE DOSE CALCtlLATION Matt.lAL PAGE 16.0F 48 DOSE FACTORS FOR NOBLE GASES AND DALICHTERS I FAC13R$ FOR tRP0eust 10 A 98ml luttulit CLOWD I OF WOBLE GAM S Dese to People

  • Dese to Air 8 l

Genne teWy Dete h ie Gasme Sete aucties E(1) L(1) mil) W(I) Aa 61 8.k M *03 2.690t+03 9.300E+03 3.200t43 sa 63m 7.560t 02 0.000t+00 1.930841 2.0008 4 2 te.85 1.61M+01 1.360t+03 1.720t41 1.930t+03 an 85m 1.170t+03 1.66bt+03 1.230t+03 1.970843 tt 87 5.92M +03 9.730E+03 6.170t+03 1.030t+M En 88 1.670t+k 2.370t+03 1.520E+06 2.930t+03 te 89 1.660t+M 1.010E+04 1.730E +M 1.060t+06 tt 90 1.560t +M 7.290t+03 1.630t+N 7.4308 4 3 st 131m 9.15M *01 4.760t+02 1.560t*02 1.11M+03 st 133

2. Mot +02 3.060t+02 3.$30t+02 1.050E+03 st.133m 2.51M *02 9.94M+02 3.270t+02 1.480t+03 st.135 1.81M +03 1.060t+03 1.920t*03 2.660t+03 st 135m 3.12M+03 7.11M+02 3.360t*03 7.390t+02 at 137 1.62M+03 1.22M+%

1.510t*03 1.270t+M st.138 4.830t+03 6.13M+03 9.210t+03 4.750t+03 +.. arem/yr per uC1/cu.s

  1. . ared/yr per uCl/cu.m I 3 Page 1 of 1

i NUMBER: CAP 0002 CHEMISTRY ADMINISTRATIVE PROCEDURES MANUAL REVISION: 0 ,3 MANUAL: PACE 47 0F 44 '5 0FF11TE botE CALCULATitW MARIAL TITLE-N AN DOSE FACTott FOR GASEQUE EFFLUENTS i f 0006 FACf 3 TAM E: t(l). Adelt, Ifteletten 1 ) iI t Units ate areW yr Der WCf/eu.e f huctlee gone Liver theWy thyreld tieurr Lee Gitract i 0.000t 40 1. Mot 43 1.260E+03 1.860t+ N3 0.000t+00 3.960t406 6.300t 4 3 0.000t+00 9. M el+03 1.60 CR 51 ) 2.40t* 1.700t+M 3.950843 0.000t+00 0 j L m 56 78 55 0.000E+001.$00E43 2.070t+03 0.000E+00 0.000 ff.59 i Co 58 i l C0 60 3.260t+041.30E*05 4.44084 0.00C440 6.000t+06 8. Mal + I 3.M0t+0S 0.000E*00 8.720t43 0.000E+ f l tu 65 St.t1 L 1.070t+05 3.460t+M 2.330E+06 0.000t+00 $.620I41.770E*0 l St e0 2.520E+M 3.500t*M 2.050t+061.190t47 24 95-iI 1 1 131 i 1 133 3.730t45 8.600E45 7.200E45 0.000t to 2.470846 9.740t+0l 3.910t+M 1.6ect 45 1.100t+05 0.000t+00 4.540t+06 1.200t l C5 136 ? 6.790!+05 6.210E+05 6.200t+0S 0.000t+00 2.230t+05 7.5 CS 136 3.910t+M 4.910E412.570E+03 0.000t+001.670t+01 1.270 Cl 137 1.990t+M 1.350t+06 1.550t+03 0.000t+ l DA 140 CE 161 [ tt.166 DC88 FACf 3 TAME: Atl)

  • Teen, inhetetten.

Units are areW yr por utf/cu.m i l Wuellde tone Liver tho0y thyreld Klewy Lee Gitract l l f f 0.000E+00 1.270843 1.270843 1.2700+03 1.270t +03 1.270 0.000t+00 0.000t+00 1.350842 7.500E+01 3.070t+01 2.100t u3 0.000t40 5.110t+06 8.600E43 0.000t*001.270E+M 1.900E+0 CR 51 3.390E 06 2.390s*06 5.550E43 0.000s+00 0.000E401.240E m 54

  • I 1.$90t+ M 3.700E+06 1.430E+06 0.000t*00 0.044E 40 1.5 it 55 0.000t+00 2.070E+03 2.700E+03 0.000E+00 0.000E 40 1.3 ft 59 0.000t+001.510E+061.900t+M 0.0000+00 0.000t40 8.720t co $4 3.060544 1.360845 6.260E+M 0.000t+00 4.M0E+M 1.260 Co 60 6.3$0t+05 0.000E+00 1.250t+04 0.000E*00 0.000t+00 2.6 Zu 65 1.000t+04 0.000t40 6.600s4 0.000E40 0.000t+001.650E+0 st.09 1.660E+05 4.590E+M 3.150E+04 0.000E+00 4.760E+06 2 j

St 90 "I 3.550t+06 4.910E+06 2.M0E+M 1.660047 4.600t*M 0.000 2R 95 1.2208+06 2.050t+ M 6.230s+03 2.920E+06 3.590t+ M 0.00 l 131 5.030t 45 1.130t+06 5.490t+05 0.000t*00 3.750t+05 1.660 1 133 5.150t+06 1.940t+05 1.370t+05 0.000t+00 1.100E45 1.780t +M 1,090t+M Ct 134 6.710t+05 8.6aot+05 3.110t+05 0.000t40 3.M0t+05 1.210 Cs 136 5.470t+06 6.710t+01 3.520f+03 0.000E+00 2.200t+01 2.03 l CS 137 2.840E+M 1.900t+06 2.170t+03 0.000E40 8.000t+03 6.16 SA 160 6.090E+06 2.020E+06 2.630t*05 0.000t+001.210t+061.360 i Ct 161 i CE 166 l AttSchoent 14 1 P8ge 1 of 2 W

i ~, I s 1 i C i NWMBER: CAP.00 CHEMISTRY ADMINISTRATIVE PROCEDURES MANUAL REVISION: 0 MANUAL.: I OFFRITE DOSE CALCULATION MAIEllAL PAGE 48 0F 47., TITLEt ORGAN 005'E FACTOLI FOR CASEdL11 EFFLUENTS (Continue Dolt FACTOR TABLtt t(l)

  • Chlte, leeletten Unitt are erem/yr per wCt/cu.e e

mucties Some Liver The#y Thyreld *Klewy Lee Gltreet _t 0.00M +00 1.130t +03 1.130t +03 1.130E *03 1.130E +03 1.130E*03 1 I 0.00M40 0.000t+001.560842 8.550t412.630541 1.90E41.000E43 u3 Ct.51 0.000t+00 4.290E+M 9.510843 0.000E+001.000t+M 1.500E+06 2.290t+ l, sm 54 4,740t+M 2.520E+M 7.770843 0.00N*00 0.000E*001.110t+05 2.870E43 I 2.070t+04 3.35M*M 1.670t+M 0.000t+00 0.000t+001.270t4 7.07W+M 7t 55 it 59 0.000t+001.770843 3.160t+03 0.000E+00 0.000E+001.110t46 3.660E4 C0 58 0.000t401.310E+06 2.2700+06 0.0000+00 0.000t+00 7.070E4 9.680E*06 l-Co 60 4.260t+ M 1.130E+05 7.030E+06 0.000E+00 7.140E+M 9.968t*05 1.43 I 6.00M+05 0.0008401.720E*M 0.000E+00 0.00N+00 2.160E461.670E+ 2m 65 1.010t+08 0.000t+00 6.440t+06 0.000E*03 0.000E+001.640E47 3.660 St+89 sa 90 5.9000+C5 4.100t+ M 3.700t*06 0.000E*00 5.900E+06 2.830E*06 6.110 4 4.81M+M 4.810E+M 2.730t+061.630847 7.000E*M 0.000E*00 2. Mat 12 95 I f.131

1. Mot +M 2,030E+ M 7.700t+03 3.050E 4 3.300E*06 0.000E*00 5.640t+03 1 133 6.510t 45 1.010E 4 2.250E+05 0.000E+00 3.31N +05 1.210t+05 3.050 Cl.134 6.510E*M 1.7108451.160E+05 0.000E*00 9.550E+061.650E46 6.ie0E Cs 136 Cs 137 9.07M45 8.250t+051.200t45 0.000E+00 2.820t+M 1.06N+05 3.6

,I 7.400t+M 6.6408414.330E*03 0.000t+00 2.110E+01 1.760t+061.0P0t+ SA 140 3.920t+061.950E+04 2.90W43 0.00N+00 4.55M+03 5. Met +05 5. east e 6.770t+# 2.120t+# 3.620E45 0.000E+001.170E41.800t+07 3.09W+05 Ct 141 Ct 144 Dost FACTOR 16BLt R(1)

  • Inf ant, leetetten LMitt are eres/yr per WCl/cu.m muclide tone that Thedy thyreld tiewy Lung Citract I

0.000t40 6.470E*02 6.670t+02 6.670E42 6.670E42 6.470t+02 6.470842 w3 CR 51 0.000t+00 0.000E+00 8.950t+01 5.760E*01 1.320E+01 1.200E*06 3.570t+02 0.0000+00 2.540E46 4.990t+03 0.000t+00 4.900E+031.000E46 7.060E+03 les 54 7t 55 1.970E+M 1.100E*M 3.330843 0.000840 0.000E40 8.700E+04 1.100t+03 I 78 59 1.360t+06 2.350E+M 9.600E*03 0.000E+00 0.0008401.020E4 2.440t+M Co 58 0.000t+00 1.220t +03 1. 520E 43 0.000t+00 0.000t40 7.770845 1.110t+06 C0 60 0.000t40 8.030t+03 1.100t+M 0.000E+00 0.0WE+00 4.510E4 3.190t+04 2m 65 1.930E*04 6.260E+M 3.110E+M 0.000E+00 3.250E+04 6.470E+05 5.140t+M I 3.9tM*05 0.000E+001.140E+M 0.000E+00 0.000t+00 2.030E4 6.600E*M sa 09 4.090(+07 0.000t+00 2.590t+06 0.000E*00 0.000E+001.120t+071.310E45 se 90 28 95 1.15M+05 2.790E+M 2.030E+06 0.000t+00 3.110t+04 1.750t+06 2.170t+M I l 131 3,800E+M 4.640E+M 1.960t+M 1.600E47 5.100t+M 0.000t+001.060543 1 133 1.320t+04 1.920t+M 5.600E+03 3.560t+06 2.260E+ M 0.000t+00 2.160E+03 CS 134 3.960t+05 7.030t+05 7.450E+M 0.000t+001.900E+05 7.970t+M 1.330E+03 CS 136 4.830t44 1.350E+05 5.290t+M 0,000E+00 5.M0E*06 1.100E+M 1.430t+03 I C5 137 5.490E*05 6.120t+05 4.550t+04 0.000t+001.720t+05 7.130t+04 1.330E+03 8A 140 5.600E+04 5.600t+01 2.900t+03 0.000t40 1.340t+01 1.600t+06 3.M0E*M Ct 141 2.770E+04 1.670t+M 1.990t+03 0.000E+00 5.250t+03 5.170t+M 2.160E+M Ct i&4 3.190t @ 1.2108 4 1.760E 45 0.000E+00 5.340E 45 9.850t+06 1.640t+05 4 Page 2 of 2

g -...--R--_,_-, JANUARY JUNE 1990 I I I I I APPENDIX B REMS 60N TO THE RADIOLOGICAL EtMRONMENTAL MONITORING PROG 8%M RAoioLOOtCAL ENVIRONMENTAL MONITORING PROGRAM MANUAL I 4 -..... _ _ _ -. -}}

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