ML19206A327
| ML19206A327 | |
| Person / Time | |
|---|---|
| Site: | Crane  |
| Issue date: | 05/31/1976 |
| From: | Metropolitan Edison Co |
| To: | |
| References | |
| NUDOCS 7904190319 | |
| Download: ML19206A327 (85) | |
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EVALUATION OF TE THREE MILE ISLAND NUCLEAR STATION UNIT 2 to demonstrate conformance to the DESIGN OBJECTIVES OF 10 CFR 50 APPENDIX I METRCPOLITAN EDISCN COPJANY Prepared by Nuclear Safety Associates Bethesda, Maryland 20016 May, 19 %
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Three Mile Island Unit #2 May, 1976
1.0 INTRODUCTION
On April 30, 1975 the Nuclear Regulatory Cc=missian issued its Final Opinion in the matter of the Rule Making Hearings (RM-50-2) on " numerical Guides for Design Objectives and limiting Conditions for Operation to meet the Criterion 'As Low As Practicable' for Radioactive material in Light '4ater-Cooled Nuclear Power Reactor Effluents." This opinion provides in part that:
"The Applicant shall provide reasonable assu.ance that the following design objectives will be met.
11 A.
"The calculated annual total quantity of all radioactive material above background to be released from each light-water-cooled nuclear power reactor to unrestricted areas will not result in an estimated annual dose or dose commitment from liquid effluents for any individual in an unrestricted area from all pathways of exposure in excess of 3 millirems to the total body or 10 millirems to any organ.
B.1.
"The calculated annual total quantity of all radioactive material above background to be released from each light-water-cooled nuclear power reactor to the atmosphere will not result in an esti=ated anrual air dose from gaseous effluents at any location near ground level which could be occupied by individuals in unrestricted areas in excess of 10 millirads for gamma radiation or 20 millirads for beta radiation.
2.
"Notwithstanding the guidance of paragraph B.l.
(a) The Cemmission may specify, as guidance on design objectives, a lower quantity of radioactive material above background to be released to the atmosphere if it appears that the use of the design objectives in paragraph B.1 is likely to result IHere and elsewhere in the Appendix background means radioactive materials in the environment and in the effluents from light-water-cooled power reactors not generated in, or attributable to, the reactors of which specific account is required in determining design objectives.
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TMI-2 May, 1976 page two in an esti=ated annual external dose from gaseous effluents to any individual in an unrestricted area in exces s of 5 millirems to the total body; and (b) " Design cbjectives based upon a higher quantity of radioactive material above backgr und to be released to the atmosphere than the quantity specified in paragraph 3.1 will be deemed to meet the requirements for keeping levels of radioactive material in gaseous effluents as low as practicable if the applicant provides reasonaole assurance that the proposed higher quantity will not result in an estimated annual external dose from gaseous effluents to any individual in unrestricted areas in excess of 5 millirems to the total body or 15 millirems to the skin.
C.
"The calculated annual total quantity of all radioactive iodine and radioactive material in pcrticulate form above background to be released frem each light-water-cooled nuclear power reactor in effluents to the atmosphere will not result in an estimated annual dose or dose commitment from such radioactive iodine and radioactive material in particulate form for any individual in an unrestricted area from all pathways of exposure in excess of 15 millirems to any organ.
D.
"In addition to the provisions of paragraphs A, B, and C above, the applicant shall include in the radwaste system all items of reasonably demonstrated technology that, when added to the system sequentially and in crder of diminishing cost-benefit return, can for a favorable cost-benefit ratio effect reductions in dose to the population rea-sonably expected to be within 50 miles of the reactor. As an interin measure and until establishment and adoption of better values (or other appropriate criteria), the values $1000 per total hady man-rem and $1000 per man-thyroid-rem (or such lesser values ar, may be dem-onstrated to be suitable in a particular case) shall ce used in this cost-benefit analysis."
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,a TMI-2 May, 1976 page three Sections 2.0 and 3.0 are provided to show whether TMI-2 does indeed meet the requirements of Paragraphs II A, B,
and C of Appendix 1 as well as those of Paragraph II D, that is, to show that there are no augments (of reasonably demonstrated technology) which can be added to the system an! result in a favorable cost-benefit ratio.
In carrying out the calculations described herein use has been made, to the greatest extent possible, of the Regulatory Guides which the liRC Staff has issued to provide guidance in the implementation of Appendix 1.
Except where specifically r. ted the equations, methods, and suggested parameters of these guides have been used throughout.
Specifically the Regulatory Guides which were used in the development of these sections are:
1.109 Calculation of Annual Average Doses to Man from Routine Releases of Reactor Effluents for the Purpose of Imple=enting Appendix 1 Issue Date: March, 1976 1.3B Calculation of Releases of Radioactive Materials in Liquid and Gaseous Effluents from PWR Issue Date: Reissued as Reg Guide 1.112 in April, 1976 1.110 Cost-Benefit Analysis for Radwaste Systems for Light-Water-Cooled Nuclear Power Reactors Issue Date: March, 1976 1.111 Methods of Estimating Atmospheric Transport and Dispersion of Gaseous Effluents in Routine Releases from Light Water Reactors Issue Date: March, 1976
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TMI-2 May, 1976 page four 2.0 LIQUID RADWASTE SYSTEMS 2.1 Introduction The requirements of Appendix I to 10 CFR Part 50 were outlined in Section 1.0; likewise Regulatory Guides which were used to make the necessary calculations were described. This section demonstrates com-pliance with appropriate requirements of 10 CFR50 Appendix I for liquid systems.
2.2 Description of Base Case Equipment The waste systems to be used at IMI-2 have been described in some detail in Chapter 11 of the Safety Analysis Report and in Section 3.5 of the Final Environmental Statement.
For an orderly presentation of this discussion, however, a brief and simplified description of the base case iaste treatment systems proposed for handling the liquid wastes frem IHI-2 is included herein.
Liquid wastes from any FWR come frcm a variety of sources which have a considerable disparity in chemical and radio-chemice.1 composition and concentration. Normally these wastes are collected and treated sepa-rately. The liquid wastes from TMI-2 fall into the following 3 categories:
- 1) Shim Bleed
- 2) Dirty Waste
- 3) Turbine Building Drains The systems proposed for TMI-2 are shown in a very simplified schematic way in Figure 2-1.
A brief discussion of each of the three categories follows:
The Shim Bleed System is that set up to control the concentration of boric acid in the primary coolant.
In a sense it is not a waste system at all but rather an integral part of the control system for the reactor.
However, a portion of the product needs to be discarded to centrol the concentration of tritium in the primary system; thus the system contributes L'
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TMI-2 page five May, 1976 to the discharge of radioactivity in liquids and needs to be considered as a waste system.
(Note that Equipment Drain Wastes from the primary system are processed with the Shim Bleed.)
The Shim 31.eed (L Equipment Drain) Was te 5ystem f o r T'41-2 consists of a flash tank, holdup tanks, pre-concentrator ion exchange, evaporator, and condensate ion exchange (for the removal of boric acid).
A single waste system, called herein Dirty Waste, processes all the wastes from TMI-1 other than the shim bleed. This same system also processes the wastes frem TMI-2.
It consists of tankage, a mixed bed ion exchanger, an evaporator and two condensate polishers.
Most PWR have steam generator blowdcwn as a potential liquid radwaste stream.
Since TMI-2 uses a once-through steam generator, there is no blowdown.
Turbine Building drains usually contain only very low levels of radioactivity even if there is scme steam generator tube leakage.
It is not generally the practice to provide any treatment for this stream and TMI-2 is no exception. Allowance has been made for the contri-bution of this stream to total liquid discharges, hcwever.
TMI-2 has no on-site laundry so detergent wastes are not considered.
2.3 Description of Alternativo Systems Considered In order to carry out the sequential cost-benef f' analysis required by paragraph II D of Appendix 1, it is necessar) to consider additions (or subtractions) to the Base Case systems. The liquid treat-ment altarnates which were considered in this study are listed in Table 2-1.
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TMI-2 May, 1976 page six 2.4 Source Ter=s The liquid emission source terms for the Base Case and for all of the alternatives considered were calculated using the PWR-CALI code and the parameters outlined in Reg Guide 1.112.
The detailed inputs for each of these cases and the resulting source term outputs are described in this section.
2.4.1 Basic inputs to GALE Code There are certain fundamental input terms which describe the subject reactor, which are com=on to all cases, and which are specific to the particular reactor. These coccan input terms for TMI 2 are given in Table 2-2.
2.4.2 Base Case Input Terms and Resulting Releases The input terms required to describe the Base Case liquid radwaste treatments (outlined in paragraph 2.2) are shown in Table 2-3.
The resulting liquid releases by isotope for the Base Case are shown in Table 2-4 2.4.3 Inputs of Alternative Cases and Resulting iteases Similarly the input ter=s required to describe each alternate case are shown in Table 2-5.
For the alternates the resulting source terms represent the differences between the Base Case release and the release of the alternate. Thus in the case of an additional augment, the difference will be positive, representing a reduction in release.
In the case of the elimination of an aug=ent, the difference will be negative, representing an increase in release. These differences for the alternate cases described in Table 2-1 are shown in Table 2-6.
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page seven 2.4.4 Inputs 1,r Cost-Beneficial Case The indicateu cost-beneficial equipment is shewn in Paragraph 2.9.2.
Since the cost-ber eficial case involves the removal of equipment pieces which were included in thi tase case, it is necessary to rra the individual doses for the cost-beneficial case to determine whether or not the cost-beneficial case is ab'_e to meet the requirements of Paragraph II A of Appendix 1.
The cost-beneficial case is shawn on Figure 2.2.
The GALE inputs for this cost-beneficial case are shown in Table 2-7 and the resulting liquid releases are shown in Table 2-8.
2.4.3 Compliance Case As indicated in paragraph 2.9.3 the case which is used to establish compliance which Appendix I is neither the Base Case nor the Cost-Beneficial Case but a case intermediate between the two.
This Compliance Case is shnwn schematically on Figure 2-3.
The GALE inputs are shown in Table 2-9 and the resulting liquid releases in Table 2-10.
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page eight 2.5 Environ = ental Inputs In order to convert the releases described in Section 2.0 into either individual or population doses it is necessary to develop a considerable amount of information which desribes the pathways at and near the site by which radioactivity released in liquid effluents might make its way back to individuals.
In this section there are described the parameters which were used in making dose calculations to individuals and to populations. Extensive use has been made of the parameters outlined in Reg Guide 1.109, but these have been supple-mented, particularly in the case of population doses, with site specific information.
In the calculation of population doses considerable reliance has been placed on the selection of clearly conservative assumptions.
2.5.1 Characteristics of Maximum Individual In the calculation of doses to individuals maximumly exposed to the liquid discharges from TMI-2 the usage factors given in Table A-2 of Reg Guide 1.109 have been assumed.
2.5.2 Mixing Ratios For,all calculations the mixing ratios (inverse of the dilution faction) have been conservatively estimated. A mixing ratic of 0.2 was used, per Table A-1 of RG 1.;;>, :or calculation of individual doses from fish, shoreline, twic=ing and boating. For the potable water pathway it was assumed that the first place potentially contaminated water could be taken by a resident would be just below the dam immediately below the plant site. Dilution with 25* of the average river flow (8a00 cfs) was assumed at this point which leads to a mixing ration of 0.004 For all population doses complete mixing with tne average river flow of 34,000 cfs was assumed for a mixing ratio of 0.001.
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TMI-2 May, 1976 page nine 2.5.3 Water Use While there are some other domestic water users of the river downstream from IMI-2, by far the largest source of population dose from potable water comes via the withdrawal of river water to supply the City of Baltimore. Saltimore is censiderably more than 50 miles from IMI-2, but the water intake point is 49 miles downstream. There-fore this pathway was included in these calculations. A total 1980 population of 5 million persons was assumed to consume Susquehanna River water.
No removal of radioactivity by the water treatment process was assumed.
2.5.4 Recreation Because suitable statistics are unavailable, populations of 10,000 persons were assumed for purposes of evaluating doses from each of the swimming, boating, and shoreline recreation pathways. This is considered a conservative estimate of the relatively low-level recrea-tional usage for the stretch of the Susquehanna River between the station and the Chesapeake Bay.
2.5.5 Aquatic Foods There are no shellfish in the Susquehanna River that are consumed.
However, approximately 69,500 lbs (31,600 kg) of fish are taken from the ri/tr below the TMI-2 site on an annual basis.
2.5.6 Other Pathways No other pathways which would be likely to produce 1C% of the dose calculated by those pathways described above were identified for the liquid discharges for TMI-2.
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TMI-2' May, 1976 page ten 2.6 Individual Doses Individual doses for the various Base Cases described in Section 2.4 are discussed in this Section.
2.6.1 With Base Case The liquid releases described in Paragraph 2.4.2 were combined with the para =eters outlined in Paragraph 2.5.1 and the individual doses were calculated using the =ethods outlined in RG 1.109.
The results of those calculations are summarized in Table 2-11.
It can be seen that the Base Case liquid -e' aases meet all of the requirements of Paragraph II A of Appendix I.
2.6.2 With Cost-Beneficial Case The ligeid releases described in Paragraph 2.L.4 were treated in a similar manner and the results are su=marized in Table 2-12.
It can be seen that the doses from this case do not meet the requirements of Paragraph II A of Appendix I.
2.6.3 With Compliance Case In a like =anner the liquid releases described in Paragraph 2.4.5 were calculated and the results are su==arized in Table 2-13.
It can be seen that doses from the Compliance Case do meet all the requirements of Paragraph II A of Appendix I-5,? ' E 3
TMI-2 May, 1976 page eleven 2.7 Population Doses Five liquid pathways have been evaluated in determining population doses from liquid discharges. They are:
a) potable water; b) consumption of fresh water fish;
'c ) exposure from shoreline residues; d) swimming; e) boating.
The first of these is dependent on the population using the water. The second is dependent on the fish catch outlined in Paragraph 2.5.5.
The last three are dependent on recreational pressure as outlined in Paragraph 2.5.4 Population doses have been evaluated for the Base Case cescribed in Section 2.7.2 and the change in population dose for each of the alternatives described in Section 2.7.3 have also been calculated.
2.7.1 Base Case The population doses resulting from the liquid releases from the Base Case described in Section 2.2 and Paragraph 2.4.2 are shown in Table 2-14 for 1980 populaticas.
It is clear from the small totals shown in that table that the Base Case treatments have undcubtedly already gone beyond the point of cost-effectiveness.
T'4.s point will be examined in more detail in Section 2.9.
2.7.2 Change in Population Doses for Alternates Considered Although there ap7 ears to be an almost a orieri case that the liquid augments already included in TMI-2 have gone beyond the point of cost effectiveness, to prove the point conclusively and to respond fully to the requirements of Paragraph 11 D of Appendix 1 requires that a series of augments (or subments) be hypothetically applied to the Base Case and a cost-benefi*. analysis be performed on these changes. To this end the alternates described in Section 2.3 were developed, the changes in the liquid releases were determined (see Paragraph 2.4.3) and the changes in population dose resulting therefrom were calculated. The results of these calculations are shown in Table 2-15.
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dip TMI-2' May, 1976 page twelve 2.8 Cost Changes Associated with Alternates 2.8.1 Methodology For each of the alternate cases listed in Table 2-1 estimates have been made of the capital and operating cases associated with the described change.
The. capital costs have been annualized and added to the annual operat.ing costs to arrive at a total annual cost.
For addi-tional augments, the resulting costs are additional costs to be co= pared to the savings in environmental cost which result frco population dose reductions. For the instances in which an equipment sequence is removed (either actually or hypothecically), the resulting costs are cost savings to be cocpared to increases in environmental cost which result frem environmental dose increases.
In either case the test is whether or not the quotient of annual cost in dollars an.tual change in dose in man-rem is greater than $ 1000.
To the greatest extent possible the cost estimates used herein are based on Regulatory Gaide 1.110.
Only where necessary (and where indicated) have other sources of cost data and other methods of cost estimating been used.
2.8.2 Cost of Alternates The resulting c9st increases (or savings) for the alternate cases listed!in Table 2-1 are shown in Table 2-16.
A detailed backup for these values is given.in Appendix A.
This appendix also includes the backup for gaseous alternates (see paragraph 3.8.2).
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May, 1976 page thirteen 2.9 Costr3enefit Ratios By combining the costs associated with the various alternates considered (given in Section 2.8) with the changes in population doses (given in Section 2.7) one obtains the cost per man-rem change in dose for each.
2.9.1 Alternate Cases The cest-benefit ratios for the alternate cases listed la Table 2-1 are shcun in Table 2-17.
It can be seen that indeed so=e of the equipment pieces which have been included in the design are not cost-beneficial.
2.9.2 Indicated Cost-Beneficial Configuration Based solely on the criterion of costebenefit the liquid radwaste systems for IMI-2 should have those icJ'cated in Table 2 18.
This cost beneficial system is shown schematically on Figure 2-2.
Cost-beneficiality is a necessary condition for selection of radwaste equipment, but lack of same is not a sufficient condition for the removal of equipment.
Ita must also be shown that, were the non-bene-ficial equipment removed, the resulting individual doses would still meet the requirements of Paragraph II A of Appendix 1.
To make this determination a new set of CALI inputs and resulting liquid releases were prepared (See Paragraph 2.4.4).
2.9.3 Complience Case Even though some of the Base Case radwaste equipment depicted on Figure 2-1 is not cost-beneficial, some of it is required to meet the design objectives of Paragraph II A of.sppendix A.
The equipment shown on Figure 2-3 was assumed to be operative for compliance with Appendix 1.
All of this equipment is alr:ady installed. A final set of GALE inputs and the resulting liquid re! eases for this config-uration are discussed in Paragraph 2.4.5.
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TMI-2 May, 1976 page fourteen 2.10 Appendix I Compliance For the Compliance Case equipienti discussed in sections 2.4.5 and 2.9.3 and Figure 2-3 it has been shown herein that:
- 1) the individual dose require =ents of Paragraph II A of Appendix 1 are met;
- 2) there ate no additional augments of reasonably demonstrated technology which could be added to the rystem: to provide additional population dose rede,er. tons ac costs less than
$ 1,000 / man-rem.
Therefore, the design of the liquid radwaste syr. tea at TIrar Mile Island Unit #2 meets the As Low As Reasonably Achiev/ ate laLanA) requirements of Appendix 1 to 10 CFR Part 50.
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2 TMI-2 May, 1976 page fifteen 3.0 GASECUS RADWASTE SYSTD1S 3.0 Introduction The requirements of Appendix I to 10 CFR Part 50 were outlined in Sectioni.0; likewise the Regulatory Guides which were used to make the necessary calculat ons were *escribed.
This sectian demonstrates compliance with appropriate requirements of 10 CFR 50 Appendix I for gas systems.
3.2 Description of Base Case Equipment The waste systems to be used at TMI-2 have been described in scoe detail in the Safety Analysis Report and in the final Environmental Statement.
For an orderly presentation of this discussion, however, a brief and simplified description of the base case waste treatment systems proposed for handling the gaseous wastes from TMI-2 is included herein.
TMI-2, in company with an Pressurized Water Reactor, can be expected to have small but discernible losses of gaseous wastes from the following sources:
- 1) Primary Gas System
- 2) Secondary Air Ejector Off-gas
- 3) Containment Purging
- 4) Ventilation of the Auxiliary Building
- 5) Ventilation of the Turbine Building The sy stems proposed for TMI-2 are shown in a very simplified sche =atic way in Figure 3-1.
A brief discussion of the five categories solicws.
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TM'-2 Hd7' 1976 page sixteen The primary coolant in a PWR, if the core centains any signi-ficant fraction of failed fuel, will contain some radicactive fission products some of which are gases. At one ar more points in the system some of thesc gaseous fission products rre drawn off and sent to the Pri=ary Gas System This system in TMI-2 consists of a surge tank, compressor, and two toldup tanks. The gases are ermpressed and stored in the holdup tanks fcr about 60 days prior to discharge. The purpose of the holdup is to allow time for the shorter half-lived components of the waste gas to decay prior to discard. This significantly reduces the dose impact of the discharge.
In PWR the pri=ary coolant is used in a steam generator to transfer heat to a secondary water circuit in which staam is produced for use in the turbine-generator to produce electricity. So long as there are no leaks in the tubes in the steam generator, there will be no radio-activity associated with the secondary system even if there is radioactivity in the pri=sry system. Thus the loss of radioactivity from the secondary system of a PWR is a "second-order" probability, that is, there mus. be simultaneously present significant failed fuel and significant steam generator tube leakage to produce any significant loss of radioactivity from the secondary system. However, the off-gas frem this system is filtered through charcoal prior to discard.
In most PWR the bicwdown taken from the steam generator to maintain proper water chemistry in the system is discharged into a blow-down tank where it is cooled by allowing a good portion of the licuid to flash (boil). The off-gas from this tank has been shewn to be a possibly 4
e TM1-2 May, 1976 page seventeen significant source of radioactivity, particularly iodine. At TM1-2, however, a once-through steam generator is employed.
This type has no bicwdown so this potential source of emission is eliminated.
PWR are pro ~ided with containment buildings and EMI-2 is no exception. There is a great deal of equip =ent inside the contain=ent and it contains the primary coolant at elevated temperature and pressure.
It is si=oly impossible to maintain all of this equipment in a ecmpletely leak-free condition; therefore it is to be expected that sene of the primary conlant will escape into containment, and that some of the escaped material will becoce and remain airborne. When it is necessary to enter containment foe ;ny length of time, it is generally desirable t' purge the containment atmosphere in order to reduce the radioactivity in the air which will be breathed by the personnel entering.
When this is done the remaining air-bacne activity in the containment atmosphere will be released to the environment. The purge is filtered through high efficiency filters (HEPA) and charcoal on discharge.
The Auxiliary Building of a FWR houses a good deal of ancillary equipment used for the control of radioactivity of the system and for =any other sub-systems needed for the operation of the reactor. Many of these can be expected to leak small quantities of radioactive liquids into the building and some of these will become air-borne.
Thus there is the possi-bility that some radioactivity will escape with the ventilation air from this building. At TMI-2 the Auxiliary Building ventilation air is filtered through HEPA and charcoal filters prior to discharge.
Similarly there is a possibility, albeit less than in the case of the Auxiliary Building, that there can be radioactive material in the air in the Turbine Building. At TMI-2 no treatment is provided for the Turbine Bldg ventilation.
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9 TMI-2 May, 1976 page eighteen 3.3 Description f Alternative Systems considered In order to carry out the sequential cost-benefit analysis required by paragraph II D of Appendix I, it is necessary to consider additions (or subtractions) to the Lase Case systems. The gaseous treatment alternates which were considered in this study are listed in Table 3-1.
3.4 Source Terms The gaseous emission source terms for the Base Case and for all of the alternatives considered were calculated using the FWR-GALZ code and the parameters outlined in Reg Guide 1.112.
The detailed inputs for each of these cases and the resulting source terms outputs are described in this section.
3.4.1 Basic Inputs to GALE Code There are certain fundamental input ter=s which describe the subject reactor and which are common to all cases and which are specific to the particular reactor. These common input terms for TMI-2 were given in Table 2-2 for liquid releases and are also used for gaseous releases.
3.4.2 Base Case Input Terms and Resulting Releases The input terms required to describe the Base Case gaseous radwaste treatmants (outlined in paragraph 3.2) are shown in Table 3-2.
The resulting gaseous releases by isotope for the Base Case are shown in Table 3-3.
Note that there are two gaseous release points and that it is necessary to specify the release terms for each.
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TMI-2 May, 19'6 page nineteen 3.4.3 Inputs of Alternative Cases and Resulting Releases Similarly the input terms required to describe each alternate case are shown in Table 3-4 For the alternates the resulting source terms represent the differences between the base Case release and the release of the alternate. Thus in the case of additional augments, the difference will be positive, representing a reduction in release.
In the case of the elimination of an augment, the difference will be negative, representing an incrcase in release. Thece differences for the alternate cases described in Table 3-1 are shown in Table 3-5.
3.4.4 Inputs for Cost-Beneficial Base The indicated cost-beneficial equipmene for the various waste systems in shown in Paragraph 3.9.2.
Since the cost-beneficial case would involve the recoval of some equipment pieces which were included in the base case, it is necessary to run the individual doses for the cost-beneficial base case to determine whether or not the cost-beneficial case is able to meet the requirements of Paragraphe II B & C of Appendix I.
The cost-beneficial case is shown on Figure 3-2.
The GALE inputs for this cost-beneficial case are shown in Table 3-6 and the resulting gaseouse releases are shown in Table 3-7.
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TMI-2 May, 1976 page twent';
3.5 Environmental Inputs In order to conver the releases described in Section 3.4 into either individual or population doses it is necessary to develop a considerable amount of information which describes the pathways at and near the site by which radioactivity released in gaseous effluents might make its way back to individuals.
In this section there are cescribed the parameters which were used in making dose calculations to individuals and to populations.
Extensive use has been made of the parameters outlined in Reg Guide 1.109, but these have been supplemented, particularly in the case of population doses, with site specific information.
In the calculation of population doses considerable reliance has been pieced on the selection of clearly conservative assumptions.
3.5.1 Characteristics of Maximum Individual In the calculation of doses to individuals maxi =umly exposed to the gaseous discharges from TMI-2, tha usage factors given in Table A-2 of Reg Guide 1.109 have been assumed. Doses to individuals have been calculated at three points:
a) At nearest Residence located 600 meters west frem the site, b) Ar rMarest real goat located 1610 meters north frem the site.
c) At nearest real ccw located 1610 meters east frem the site.
3.5.2 Atmospheric Dispersion One of the most important factors governing potential doses to individuals and to populations from the release of gaseous radionuclides from nuclear reactors is,the atmospheric dispersion available at the site.
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TMI-2 May, 1976 page twenty-one The meterology of the site has been studied in detail as discussed in the Environmental Report. These meteorological data have been evaluated using the techniques outlined in Regulatory Guide 1.111.
The resulting values of discersion (X/Q in sec/n ),
depleted dispersion (X/Q' in sec/m ),
and speciiic deposition (d in 1/m ) are shown in Table 3-8 for releases f' a the plant vent and in Table 3-9 for releases from the turbine building.
It is necessary to treat these two release sources separately since the former is a partially elevated release whereas the latter is essentially 2 ground release. The meteorological parameters are presented separately for the grazing season since it was assumed in all calculations that grazing ani=als were on pasture only six months of the year.
3.5.3 Pcpulation Data Current and future population data have been discussed previously in the Environmental Report. The population data used in these calculations are shown in Table 3-10 for the years 1980 and 2010.
The data are given by sector and distance.
In making the population doses discussed herein the following distribution was assumed:
Adult 667.
Teen 147 Children 207.
3.5.4 Agricultural Products The region within f0 miles of the station is a highly productive egricultural area.
Altinough prodJ tion density (on a total land area basis) is fairly uniform throughout the region, inspection of county production statistics suggests that the ENE, E, ESE, and SE sectors have somewhat higher produ: tion densities than other sectors for most products. Ccunty 6
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G TMI-2 May, 1976 page twenty-two agricultural product data were classified and total 50-mile radius regional yields for each classification were obtained. Vegetables and fruits were classified as follows:
a)
Leafy Grown in open, exterior surface eaten s
b) Exposed Grown in open, exterior surface not eaten c) Root Grewn under surf ace or under shelter (mushroor.m)
The production data are summarized in Table 3-11.
Values of the dispersion par 1 meter for most c: ops were obtained by integratir.g weighted dispersion parameter values dor each of 10 seg=ents in each of 16 sectors in the 50-mile radius region. Each sector segment dispersion parameter value was weighted by the fraction of the regional area (50-mile radius) within the sector segment of interest and by a production density f actor (taken as 2 for all segments in the ENE, E, ESE, and SE sectors and 0.67 for all other segments).
Values of the integrated area-weighted and production density-weighted dispersion para =eter values are also given in Table 3-11.
The dispersion parameter values for mushrooms were derived in a diff arent =taner because =ushroom production is concentrated in the ENE, E, and EEE sectors at distances of 30-50 miles from the plant. The growth medium for there mushroom farms was assumed to be obtained from the center of Lancaster County, approximately 25 miles ESE.
> Note that the population dose calculations have been based on crops, no; on population.
In essentially every instance the crop yield is sufficient to feed many more pecple than actually live in the 50-mile area. Technically in making the cost-benefit analysis pursuant to Paragraph II D of Appendix I, it is necessary only to consider the dose to actual inhabitants of the 50-mile area. The Applicant believes, however, that the project should account for the entire populatien dose produced within the fifty miles, whether or not the food consumption takes place within that area. Therefore the population doses frem the food paths are considerably overstated, at least in a technical Appendix I sense.
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IM1-2 May, 1976 page twenty-three 3.5.5 other Pathways No other pathways which might increese the calculated population doses by a much as 107. were found.
3.6 Individual Doses Individual doses for the various Base Cases described in Section 3.4 are discussed in this Section.
3.6.1 With Base Case The gaseous releases described in Paragraph 3.4.2 were combined with the parameters outlined in Paragraph 3.5.1 and the individual doses were calculated using the methods of Reg Guide 1.109.
The results of those calculations are su=marized in Table 3-12.
It can ba seen that the Base Case gaseous releases meet all of the requirements of Faragrapns II B & C of Appendix 1.
It is this Base Case which is used to establish compliance with Paragraphs 11 B & C of Appendix 1.
3.6.2 With Cost-Beneficial Case The gasecus releases described in Paragraph 3.4.4 were treated in a similar manner and the results are summarized in Table 3-13.
It can be seen that the Cost-Beneficial Case gaseous releases do not meet all of the requirements of Paragraphs 3 & C of Appendix I although only the infant thyroid dose via goats milk is significar tly is excess of the Appendix 1 values (about 30 mres).
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9 TMI-2 May, 1976 page twen ty-f our 3.7 Population Doses Three cajor food pathways:
a) fruits & vegetables b) milk c) meat and three population-orientated pathways:
a) ncble gas i=mension b) ground plane deposition c) inhalation have been evaluated in determining population doses from gaseous discharges.
The first three depend on the crep production described in Paragraph 3.5.4: the last three en the populations described in Paragraph 3.5.3.
Population doses have been calculated for the Base i:ase described in Section 3.2 and the changes in population dose for each of the alternatives described in Section 3.3 have also been calculated.
3.7.1 Base Case The population doses resulting from the gaseous releases from The Base Case described in Section 3.2 and Paragraph 3.4.2 are shown in Table 3-14 It is clear from the s=all total shown in that table that the Base Case treatments may have already gone beycnd the point of cost-effectiveness. This point will be examined in = ore detail in section 3.9.
3.7.2 Change in Population Doses for Alternates Considered To determine that IMI-2 has achieved the requirements of Paragraphs II D of Appendix I requires that a series of augments (or subments) be hypothetically applied to the Base Case and a cost-benefit analysis be performed on these changes. To this end the alternates described in Section 3.3 were developed, the changes in the gaseous releases were determined (See Paragraph 3.4.3), and the changes in populatian dose resulting therefron were calculated. The results of these calculations are shewn in Table 3-15.
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TMI-2 May, 1976 page twenty-five 3.8 Cost Chang;s Associated with Alternates 3.8.1 Metho dolo gy For each of the alternate case; listed in Table 3-1 estimates have been made of the capital and operating costs assccisted with the described change. The capital costs have been annualized and added to the annual operating costs to arrive at a total annual cost.
For additional augaints the resulting costs are additional costs to be compared to the savings in environmental cost which result from population dose reductions.
For the instances in which an equipment sequence is removed (either actually or hypothetically), the resulting costs are cost savings to be compared to increases in environmental cost which result from environ = ental dose increases.
In either case the test is whether or not the quotient of annual cost in dollars annual change in dose in man-rem is greater than $1000.
To the greatest extent possible the cost estimates used herein art based on Regulatory Guide 1.110.
Only where necessary (and where indicated) have other sources of cost data and other methods of cost estimating been ased.
3.8.2 Cost of Alternates The resulting cost increases (or savings) for the alternate cases listed in Table 3-1 are shcwn in Table 3-16.
A detailed backup for these values is given in Appendix A.
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A TMI-2 May, 1976 page twenty-six 3.9 Cost Benefit Ratios By combining the costs associated with the various alternatea considered (given in Section 3.8) with the changes in population doses (given in Section 3.7) one obtains the cost per man-rem change in dose for each.
3.9.1 Alternate Cases The cost-benefit ratios for the alternate cases listed in Table 3-1 are shcwn in Tabic 3-17.
The values given are based on the 1980 population values.
It can be seen that there is one additional augment which appears justified by cost-benefit when calculated in accordance with RG 1.110.
Ecwever, when the backfitting costs are evaluated it may not be.
At present it is under consideration.
It should be noted that this source is only significant when there is significant tube leakage--which is not presently the case.
On the other hand there are a numb er of equipment pieces which have been included in the design which are not cost-beneficial.
3.9.2 Indicated Cost-Beneficial Configuration Based solely on the criterion of cost-benefit the gaseous radwaste systems for TMI-2 sF auld have been those indicated in Table 3-18.
This cost beneficial system is shown schematically on Figure 3-2.
Cost-beneficiality is a necessary condition for selection cf radwaste equipment, but lack of same is not c sufficient condition for the removal of equipment.
It =ust also be shown that, were the non-beneficial equipment removed, the resulting individual doses would still meet the requirements cf Paragraphs II 3 & C of Appendix 1.
To make this determination a new set of GALE inputs and resulting liquid releases were prepared (See Paragraph 3.4.4).
Even though it would be possible to eliminate the charcoal and EEPA on the Gas Decay Tanks, this is a trivial change (less than 2 man-rem g
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TMI-2 May, 1976 page twenty-seven and there is no iodine in this release anyway), the charcoal which serves the Auxiliary Building and air ejector, while not cost-beneficial, is required to mee; individual dose objectives. The same is true of the charcoal on the high volume purge. Therefore, for TMI-2, the base case is selected for demonstration of compliance with 10 CFR 50, Appendix 1.
3.10 Appendix I Compliance For the Base Case equipment, discussed in sections 3.2 and 3.9 and shown schematically on Figure 3-1 it h.s been shewn herein that:
1) the individual dose require =ents of Paragraphs II B & C are met; 2) there are no additional augments of reasonably demonstrated technology which could be added to the systems to provide additional population dose reductions at costs less than
$ 1,000 / man-rem.
Therefore the design of the gaseous radwaste system at Three Mile Island Unit-2 meets the As Low As Reasonably Achievable ( ALARA) requirements of Appendix I to 10 CFR Part 50.
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TMI-2 May, 1976 Table 2-1 Licuid Treatment Al ternates Run Designation
'Jaste System Description of Alternate Affected H-1 Dirty Remove demineralizer H-?
Dirty Remove condensate polisher H-3 Dirty Remove evaporator only H4 Dirty Remove both ion exchangers H-3 Dirty Discard without treatment I-1 Regeneration Solutiori Remove demineralizer I-2 Regeneration Solutions Remove condensate polisher I-3 Regeneration Solutions Remove both demineralizers I-4 Regeneration solutions Discard without treatment Corresponds to identifyinc, number on all GALE code inputs a
and outputs as well as on LIP inputs and outputs.
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TMI-2 May, 1976 Table 2-2 GAG Incut Terms Common to All Cases Card No.
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UN MIU I" 1
33-60 Reactor Name UNIT 2 2
73-80 2772 Maximum Thermal Power mut 3
73-80 717.4 liass Pri=ary Coolant 103 lb 4
73-80 45 Purification Letdown Flow gpm 5
73-80 0
Cation Demin Flow gpm 6
73-80 2
No. of Steam Generators 7
73-80 5.6 Total Steam Flow 106 lo/hr 8
73-80 1.425 liass Steam each Generator 103 lb 9
73-80 26.6 Mass Liquid each Generator 103 lb 10 73-80 2000 Total Mass Secondarv 103 lb 11 37-44 Blank Blowdown Rate ib/hr 80 Blank Blowdown Treatment Blowdown not recycled to Secondary 12 73-80 28 Cond. Demin Regen Time days No Cond. I'emin 13 73-80 0.74 Fraction Cond to Demin 14 73-80 15 Annual Ave Dilution Flow 103 gpm 8
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TMI-2 May, 1976 Table 2-3 page 1 of 2 GALE Incut Terms for Base Case-Licuids, Card Spaces Encry Ite2 Units
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As 17-33 Shim Bleed Waste Stream 42-49
- 2. E+03 Volume gal / day 57-61 Blank Fraction Pricary Cool-ant Activity 16 21-23 1E+04 1 DF 34-41 2E+04 Cs, Rb DF 47-54 lE+05 Other DF 17 28-33 51 Collection Ti=e days 48-53 3.7 Process Ti=e days 72-77 1.0 Fractior. Discarded 18 17-33 Equip Drain Waste Waste Streas 42-49 200 Volume gal / day 57-61 1
Fraction Pri=ary Coolant Activity 19 21-28 LE+04 I DF 34-41 2E+04 Cs, Rb DF 47-54 lE+05 Other DF 20 28-33 31 Collection Time days 48-53 3.7 Process Time days 72-77 1.0 Fraction Discardcd 21 17-33 Clean Waste Waste Streas 42-49 0
Volu=e gal / day 57-61 1
Fraction Primary Coolant Activity 22 21-28 1
1 DF 34-41 1
Cs, Rb DF 47-54 1
Other DF 23 28-33 1
Collection Ti=e days 48-53 1
Process Ti=e days 72-77 1
Fraction Discarded
TMI'- 2 May, 1976 Table 2-3 (cont) page
,c.,
CALE Incut Terms for Base Case--Licuids Card Spaces Entry Itaa Units
,3 24 17-33 Dirty Waste Waate Streaa 42-49 1800 Volume gal /d2y 57-61 0.075 Fraction Pr. Coolant Activity 25 21-28 1E+06 I DF 34-41 2E+05 Cs, Rb DF 47-54 1E+07 Other DF 26 28-33 8.9 Collection Ti=e days 48-53 0.9 Process Ti=e days 72-77 1
Fraction Discarded 27 73-20 Blank Fraction Slowdown Proc.
28 21-28 L
I DF 34-41 1
Cs, Rb DF 47-54 1
Other DF 29 28-33 0
Collectica Ti=e days 48-53 0
Process Ti=e days 72-77 0
Fraction Discarded
" C "d 30 73-80 5000 Cond. Regen Waste Vot gal / day demin 31 21-28 1E+06 I DF 34-41 2E+05 Cs, Rb DF 47-54 1E+07 Other DF 32 28-33 0
Collection Time days 48-53 0
Erocess Ti=e days 72-77 0
Fr. ction Discarded 45 73-00 0
Detergent Vaste Treatment 53^.759
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05/31/76 TaaLE 2-4 LICUIO RELE ASES 9aSE CASE (CUCIES/ yea:)
ISOTOPE RELEASE H----3 5.F0E+C2 CR--51 1 705-04 MN--54 4.10E-05 FE--55 1 809-04 FE--59 9.90E-05 C0--58 1.70E-03 CO--60 2.10E-04 9P--83 3.10E-05 R9--96 3.209-05 SR--89 3.90E-05 SR--91 1.80E-05 Y--91w 1.20E-05 MO--99 4 90E-02 TC-99" 3.005-02 TE127" 2.40E-05 TE-127 3.30E-05 TE129M 1.30E-04 TE-129 8.60E-05 TE131M 5.002-C5 TE-132 1.30E-03 I--130 6.90E-0E I--131 3.40E-02 I--1?2 1.70E-03 I--133 1.60E-02 I--134 1.40E-05 I--135 4.20E-03 CS-134 1 90E-02 CS-136 3.80E-03 CS-137 1.405-02 BA137M 1.30E-02 9a-140 1.70E-09 LA-140 1 20E-05 NP-239 7 10E-05 OTHECS 6.20E-05
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2 TMI-2 May, 1976 Table 2-5 GALE Inout Terms for Licuid Alternates Run Ca rd Chances Recuired De s 12na tion Purpose Carc No.
Lines Entry Dirty Waste H-1 Remove first demineralizer 25 21-28 1E+04 34-41 1E+05 47-54 1"605 H-2 Remove condensa e demineralizer 25 21-28 1E+05 34 41 2E+04 47-54 1E+06 H-3 Remove evaporator 25 21-28 1E+03 34-41 2E+01 47-54 1E+03 H-4 Remove both demineralizers 25 21-28 1E+03 34 41 1E+04 47-54 1E+04 H-5 Discard w/o treatment 25 21-28 1
34 41 1
47-54 1
Receneration Waste 1-1 Remove demineraliser 31 21-28 1E+04 34 41 1E+05 47-54 1E+05 1-2 Remove condensate polisher 31 21-23 1E+05 34 41 2E+04 47-54 1E+06 I-3 Remove both demineralizers 31 21-28 1E+03 34 41 1E+04 47-54 1E+04 I-4 Discard w/o treatment 31 21-28 1
34-41 1
47-54 1
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I I'2 09/31/76 Ta9LE 2-6 PAGE 1 UF 4 OECUCTICNS IN LIOUID PELEASES COCM ALTE3NaTE TRESTMcNTS (CURIES / yea 9)
IS070:E CASE H-1 CASE u-2 CASE H-3 CASE s-4 CASE--
CR--51
-4.07E-06
-3.70E-07
-4 11E-04
-4.11E-05
-4.115-Ci MN--54
-7.61E-07
-6 92E-08
-7.69E-05
-7.69E-06
-7.ECE-02 FE--59
-3 97E-06
-3.61E-07
-4.01E-04 4.01E-C5
-4.315-01 F:--59
-2 27c-06
- -2 065-07
-2 2cE-04
-2.29E-C5
-2.295-01 C0--58
-3 75E-05
-3.41E-06
-3 795-03
-3.77E-C4
-3.79E*0:
CO--60
-4.475-06
-4.52E-07
-5 0 E-04
-5.02E-05
-9.022-01 93--33
-2.01E-09
-2.03E-03
-2.C25-0; o9--36
-9.69E-Ga
-7.975-07
-8 85E-04
-1.69E-06
-1.775-02 So--39
-9 04E-07
-7.31E-06
-8.12E-05
-3.11E-06
,.12E-02 SR--c0 0.
3.
O.
C.
-2 915-0?
S?--91
-1 395-03
-1.26E-09 3 79E-06
-1.40E-07
-1.4CE-13 Y---c0 0.
O.
O.
3.
-1.622-03 Y--31M
-3 94E-09
-S.13E-10 2 44E-06 2.+4E-06
-9.C3E-04 Y---91 0.
O.
-1 70E-05 0.
-1.57E-02 Y---93 0.
G.
O.
O.
-S.47'-05 Z2--95 0.
O.
-1.54E-05 3.
-1.41E-02 NA-95M 0.
O.
O.
O.
-1 625-04 NO--95 0.
O.
-1 36E-05 3.
-1.266-O' MO--99
-5.775-05
-5.25E-05
-5.33E-03
-5.325-04
-5.83E+C0 TC-99M
-5.4SE-05
-4 99E-06
-5.54E-03
-5.53E-04
-5.54E+00 RU-103 3.
O.
-1 11E-05 0.
-1.025-0' CU-106 0.
O.
O.
O.
-2.4tE-03 44103M 0.
O.
. 10E-05 0.
-1.02E-02 RH-106 0.
O.
O.
G.
-0.49E-03 TE125M 0.
O.
D.
O.
-6. 7 8 E -2 7 TE127M
-6.70E-07
-6.09E-03
-6.775-05
-6.76E-06
-6. 7 7E-0?
TE-127
-6.7oE-07
-6.17E-06
-6.86E-05
-6.35E-06
-6. 3 6 E-; 2 TE129M
-3.0BE-06
-?.BOE-07
-3.11E-04
-3.11c-05
-3.11E-01 75-129
-1 97E-06
-1.79E-07
-1.99E-04
-1 99E-05
-1.99E-;1 TE131M
-5.77E-07
-5 25E-08
-5.83E-05
-5.82E-06
-5.93E-02 TE-ill 0.
D.
-1 25E-05 0.
-1.06E-02 TE-132
-2 17E-05
-1 975-06
-2 19E-03
-2 19E-04
-2 19E+00 I--130
-8.40E-07
-7.63E-09
-3.47E-06
-3.'72-06
-3.485-03 I--131
-4 05E-03
-3.68E-04
-4.09E-02
-4 09E-02
-4.09E+01 I--132
-2.2SE-05
-2.06E-06
-2 26E-03
-2.29E-04
-2.26c+0]
I--137
-4.655-04
-4.23E-05
-4.70E-03
-4.70E-03
-4.70E+00 I--134
-1.375-13
-1 24E-14 2 97E-06 2 97E-06 2.07E-06
!--135
-1.33E-05
-1 21E-06
-1 34E-04
-1.34E-04
-1. 3 4 E - 01 CS-174
-3.30E-05
-2 97E-04
-3 3CE-01
-6.275-04
-6.60E+CJ CS-136
-1 23E-05
-1.10E-04
-1.22E-01
-2.33E-04
-2 45E+0]
CASE
- -1 REMOVE CATION JIMINERALIZER F;CM OIRTY WASTE SYSTEM CAS: H-2 REMOVE CONCENSATE DEMIN?,aLI?ER ROM 0IRTY WASTE SYSTE" CASE H-3 REMOV~ EVaPORaT03 F30" OIRTY WASTE SYSTEM Cas:
H-4 RE"0VE 30TH OEMINEoaLIZEoS F=CM JIRiv was E SYSTE" CASE H-5 JISCa30 OI?TY WASTE WITHOUT T;ESTMENT N 3 T E -- N E G A T IV E VALUES :E3RES:NT' INCREASE 0 SELEAS?S urq
.9C.'d
TNI-'
05/31/76 TABLE 2-6 PAGE 2 0F 4 DEOUCTIONS IN LIQUID RELE ASES FDCM ALTERNATE T7ESTMENTS (CUGIES/Y E AG )
! S O T 'J o E CASE H-1 CASE H-?
CASE H-3 CASC H-4 CAEE N-5 CS-137
-2 39E-05
-2 15E-04
-2.39E-01
-4 54E-04
-4.78E+:1 Sa137M
-2 23E-09
-2 02E-04
-2.24E-01
-4 25E-04
-4.47E600 9a-140
-3.98 E-0 7
-3.62E-08
-4 02E-05
-4.02E-C6
-4.025-02 La-t40
-4.01E-07
-3.65E-06
-4.05E-05
-4.05E-06
-4 05E-02 CE-141 0.
O.
-1 67E-05 3.
-1.E5E-0?
CE-143 0.
O.
O.
O.
-1.09E-03 CE-144 0.
O.
-9 06E-06 0.
-8 18E-03 PR-143 0.
O.
-1.06E-05 0.
-9 96E-23 PC-144 C.
O.
-9.06E-06 0.
- 8 1 a :- 0 2 No-239
-6.78E-07
-6.17E-Od
-6.89E-05
-6 34E-06
-6 85E-02 TOTAL
-4 84E-03 1.26E-03
-9.94E-01
-4 96E-C?
-8.64E+01 CASE H-1 REMOVE CATION DIMINERALIZER cROM OIRTY WASTE SYSTEM CASE H-2 REMOVE CONDENSATE DEMINERALIZER FROM JIRTY WASTE SYSTEM CASE H-3 DEMOVE EVAPORATOR FROM OIRTY WASTE SYSTEM CASE H-4 REMOVE 30TH OEMINERALIZERS FRCM OIRTY WASTE SYSTEM CASE H-5 JISCARD DIRTY WASTE WITHOUT TREATMENT NOTE -- NEo A TIV E V ALUES D EPRE S ENT INCREASE 0 CELEASES A
e de.. -. i.. 3
T M I - F' 05/31/76 TAELE 2-6 PAGE 3 0F 4 3CJUCTICNS IN LICUIO RELEASES FRCM ALTERNATE T3EaTMENTS (CURIES / YEAR)
ISOTOPC C A SE I-1 CASE I-2 CASE I-3 CASE I-L CR--Si
-2 3 3E-0 7
-2 12E-08
-2 35E-06
-2 35E-02 MN--54
-3 33E-08
-3.03E-09
-3.91E-07
-8.92E-0?
22--55
-3.66E-07
-3.335-08
-3.70E-06
-?.70E-02 FE--59
-1 61E-07
-1.47E-08
-1.63E-06
-1.63E-32 CO--5S
-2 95E-06
-2.63E-07
-2 96E-05
-2.98E-01 CO--60
-4 17E-07
-3.79E-Da
-4.215-06
-4.21E-02 93--83 0.
O.
3.
6.61E-06 C9--36
-3.9 3 E-09
-3.59E-03
-7.575-03
-7.975-04 SR--89
-6.76E-08
-6.15E-00
-6.825-07
-6 33E-03 54--90 0.
O.
G.
-2.35E-04 SS--91 0.
S.
-3.62E-16 3.795-C6 Y---90 0.
G.
O.
-2.36E-04 Y--91M
-5.5]E-17
-5 00E-15
-5.55E-16 2 445-06 Y---91 0.
O.
G.
-1.11E-03 Y---93 0.
O.
O.
O.
ZR--95 0.
O.
O.
-1.005-03 NS-95M 0.
O.
O.
-2.235-05 N '3 -- 9 5 0.
O.
O.
-1.03E-03 M0--99
-2. 0 2 E- 0 6
-1.84E-07
-2 04E-05
-2 04E-01 TC-99M
-1 93E-06
-1.76E-07
-1 95E-05
-1.95E-01 PU-103 0.
O.
O.
-6.20E-04 RU-106 0.
O.
O.
-2.25E-04 P4103*
0.
O.
O.
-6.21E-04 RM-106 0.
C.
O.
-2.25E-04 TE125M 0.
G.
O.
-3.53E-04 TE127M
-4 00E-08
-3.64E-Oo
-4.0 4E-0 7
-4.04E-03 TE-127
-3.95E-08
-3.59E-09
-3.99E-07
-3.99E-03 TE129M
-2.01E-07
-1.83E-Oe
-2.03E-06
-2. 0 3E-0 2 TE-129
-1.29E-07
-1.17E-08
-1.3 0 E- 0 6
-1.30E-02 TE131M
-4.93E-11
-4.535-12
-5 03E-13
-5 03E-06 TE-131 0.
O.
O.
O.
TE-132
-8.41E-08
-7.64E-09
-8.4aE-07
-8 49E-03 I--130
-1.55E-13
-1 41E-14
-1.57E-12
-1 57E-Go I--131
-9.13E-05
-3 34E-06
-9.26E-04
-9 27E-31 I--132
-8.81E-03
-3.01E-09
-3.89E-07
-a.75E-03 I--133
-1.14E-08
-1.04E-09
-1 15E-07
-1 15E-04 I--134 0.
O.
O.
2 97E-Oc I--135 0.
O.
-9.53E-16
-9 53E-13 CS-134
-2.71E-06
-2.43E-05
-5.14E-05
-5.41E-01 CS-136
-3 93E-07
-3 575-06
-7.55E-06
-7.95E-02 C'SE I-1 REMOVE FIRST OEMINERALIZEo FROM REGENERANT WASTE SYSTE" Ca!E I-2 REMOVE CONDENSATE DEMINERALIZEP FCOM 35 GENE; ANT WASTE SYST:"
CASE I-3 PEMOVE 90TH OEMINERALIZECS FROM OEGENEcaNT WASTE'SYSTE" Cae: I-4 O IS C A 3.0 REGENERANT WASTE WITHOUT TREATMENT NOTE -- NEGATIVE VALUES REoRESEN7 INCREASEO
- 3. E L E A S E S I
Yt.] syc /t r.
..s. 1
74[-2 O c / 31/ 7; 3
TAELE 2-6 CAGE Ce 4
RFOUCTICMS IN LIQUID RELEASES FPCM ALTERNATE T:E TMENTS (CURIES / YEAR)
!SOTOPE C, Si I-1 CASE I-2 CASE I-3 CASE I-4 C3-137
-2 07E-06
-1 86E-05
-3.93E-05
-4 14E-01 EA137"
-1 94E-06
-1.75E-05
-3.69E-05
-3 385-01 EA-14]
-1.36E-08
-1.23E-09
-1 3 7E- 0 7
-1.37E-0' LA-140
-1 56E-08
-1.4?E-09
-1.59E-07
-1.5eE-03 CE-141 0.
G.
3.
-9.50E-04 CE-143 0.
O.
O.
C.
CE-144 3.
D.
3.
-3.895-04 PR-143 0.
3.
O.
-3.24E-04 00-144 0.
3.
O.
-d.99E-04 No-239
-1.575-09
-1 43E-10
-1.59E-03
-1.59E-0L TOTAL
~1.03E-04
-7.31E-05
-1.155-03
-3.25E+0J CASE I-1 GEMOVE FIRST DEMINERALIZER FRCM RE GE N ERA NT WASTE SYSTE" CASE I-2 SE10VE CONDENSATE DEMINERALIZER CROM REGENERANT WASTE SYSTEM CASF I-3 REMOVE 80TH OEMINERALIZERS FROM REGENERANT WASTE CYSTEM CASE I-4 CISCaiO REGENERANT WASTE WITHOUT TREATMENT NOTE -- NEG ATIV E V ALUES REPRESENT INCREASE 0 PELEASES r,-
o c.c-... )
L r.
TMI-2 May, 1976 Table 2-7 pa e 1 of 2 CALE Inout Terms for Cost-Beneficial Base Case--Liquids rd
",o.
Spaces Entry Item Units Ccement o
15 17-33 Snia Bleed Waste Stream 42-49 2.'E+03 Vo lume gal / cay 57-61 Blank Fraction Primary Cool-Cale by Ccde ant Activity 16 21-28 1E+C4 1 DF 34-41 2E+04 Cs, Rb DF 47-54 1E+05 Other DF 17 28-33 51 Collection Time days 48-53 3.7 Process Ti=e days 72-77 1.0 Fraction Discarded 18 17-33 Equip Drain Waste Waste Streas Processed with 42-49 200 Volu=e gal / day SHIM BLIED 57-61 1
Fraction Pri=ary Coolant Activity 19 21-28 lE+04 1 DF 34-41 2E+04 Cs, Rb DF 47-54 1E+05 Other DF 20 28-33 51 Collection Time days 48-53 3.7 Process Ilse days 72-77 1.0 Fraction Discarded 21 17-33 Clean Waste Waste Stream 42-49 0
Volume gal / day 57-61 1
Fraction Primary Coolant Activity 22 21-28 1
1 DF 34 41 1
Cs, Rb DF 47-54 1
Other DF 23 28-33 1
Collection Time days 48-53 1
Process Time days
~
72-77 1
Fractior. Discarded r
a, p g, 7 LJ r.
...O
~
t d
TMI-2 M3Y. 1976 Table 2-7 (cont) page 2 of 2 GALE Inout Terms for Cost-Beneficial Base Case--Licuids Spaces Entry Item Units Cc=ments ao.
24 17-33 Dirty Waste Waste Stream 42 49 1800 Volume gal / day 57-61 0.075 Fraction Fr. Coolant Activity 25 21-28 CDe03 I DF 34-41 1E+01 Cs, R'a DF 47-5 4 1E+03 Other DF 26 28-33 --
8.9 Collection Ti=e days 48-53 09 Process Time days 72-77 il Fraction Discarded 27 73-80 Blank Fraction Blowdown Proc.
28 21-28 1
1 DF 34-41 1
Cs, Rb DF 47-54 i
Other DF 29 28-33 0
Collection Time days 48-53 0
Frocess Time days 72-77 1
Fraction Discarded 30 73-80 5000 Cond. Regen Waste Vol gal / day 31 21-28 1
1 DF 34-41 1
Cs, Rb DF 47-54 1
Other DF 32 28-33 0
Collection Time days 48-53 0
Process Time days 72-77 0
Fraction Discarded 45 73-80 0
Detergent Waste Treatment r_c ?g r* $
L;t.
..a-
I"!-2 05/31/76 Ta9LE 2-S LI1UID RELEASES -- COST-9ENECICIAL CASC (CURIES / YEAR)
ISCTCPE RELEASE ISOTOPE PELEASE H----3 5.50E+02 TE-127 4.20E-03 CR--51 2.50E-02 TE129u 2.10E-02 MN--54 9 30E-03 TE-129 1 406-02 FE--55 3.90E-02 TF131M 7.50E-05 FE--59 1 70E-07 E-131 1.40E-05 CO--58 3.10E-P1 TE-132 1 10E-02 CO--60
- .40E-J2 I--130 2.40E-05 RS--36 1.70E 03 I--131 1.00E+00 SP--89 7. 2 0 F. - 0 3 I--132 1 20E-02 SR--90 2.50E-04 I--133 3 40E-03 Y---90 2. 5 r. E - 0 4 I--135 1 10E-03 Y---91 1.2JE-03 CS-134 9.10E-01 ZR--95 1.10E-03 CS-136 2.10E-01 NP-95M 2.30E-05 CS-137 6.30E-01 N9--95 1.10E-03 E A13 7M 6.40E-C1 MO--99 2.30E-01 9a-140 1.50E-03 TC-99M 2.10E-01 LA-140 1.70E-03 S, U - 10 3 6.50E-04 CE-141 9.00E-04 RU-106 2.40E-04 CE-144 9.30E-04 Ru1O3M 6.50E-04 OR-143 3.50E-04 CH-106 2.40E-04 PR-144 9.30E-04 TE125M 3.70E-04 NP-239 2.50E-04 TE127M 4.30E-03 CTWERS 2 20E-05 O
, ~)
p r.
.w
T::1-2 May, 1976 Table 2-9 page,
o,m GALE Incut Terms for Como11ance Case-Licuids Card Spaces Entry Item Units
.,o.
s.
15 17-33
. Shim Bleed Waste Stream 42-4}J 2.4E+03 Vo lume gal / day 57-61 Blank Fraction Primary Cool-ant' Activity 16 21-23 lE+04 I DF 34-41 2E+04 Cs, Rb DF 47-54 lE+05 Other DF
~
17 28-33 51 Collection Ti=e days 48-53 3.7 Process Ti=e-days 72-77' l.0 Fraction Discarded l
18 17-33 Equip Drain Waste Waste Strean 42-49 200 Volume gal / day 57-61 1
Fraction Pricary Coolant Activity 19 21-28 lE*04 I DF 34 2E+04 Cs, Rb DF l
l 47-54 IE+05 other DF 20 23-33 51 Collection Time days 48 3.7 Precess Time days 72-77 1.0 Fraction Discarded 21 17-33 Clean Waste Uaste Streas 42 49 O
Volume gal / day 57-61 1
Fraction Primary i
Coolant Activity l
22 21-28 l 1
1 DF 34-41 1
Cs, Rb DF 47-54 1
Other 22 23 28-33 1
Collection Time days 48-53 1
Process Time days 72-77 1
Fraction Discarded
(( " ^ "
TMI-2 May, 1975 Table 2-9 (cont)
P3 5"' 2 I2 CALE Inout Terms for Co:aplianca Case-Linu' !s Ca~d Spaces Entry item Units 3do.
24 17-33 Dirty Vaste Waste Straa 2 42-49 1300 Volume gal /d2-j i
57--61 0.075 Fraction Pr. Coolant 1.ctivity 25 21-28' 1E+06 I DF 34-41 2E+05 Cs, Rb DF 47-54 1E+07 Other DF i
26 28-33' 8.9 Collection Time days 48-53 0.9 Process Time days I
72-77 1
Fraction Discarded l
l, 27 73-80 Blank Fraction Blowdown Proc.
23 21-28 1
1 DF l
34-41 1
Cs, Rb DF 47-54 1
Other DF 29 28-33 0
Collection Ti=e days 48-53 0
Process Time days 72-77 0
Fraction Discarded C 'd 30 73-80 5000 Cond. Regen Waste Vol gal / day ~ "demin 31 21-28 lE+C6 1 DF 34 41 2E+05 Cs, Rb DF 47-54 LE+07 other DF 0
Collection Time days 32 28-33 l
48-53 0
Process Time days 72-77 0
Fraction Diccarded 45' 73-80 0
Detargent liaste Treatment
)
u~
LJ
?
a TMI-?
04/31/7A Ta9LE 2-10 LIOUID RELEASES -- COMPLIANCE C;SE (CUPIES/YEAD) g ISOTCAE RELEASE H----3 5.50E+C2 CR--51 2.105-04 MN--54 4.605-05 FE--55 2.20E-04 FE--59 1 205-04 C0--58 2 005-03 CC--60 2.60E-C4 9R--93 1.30E-05 R9--66 2.20E-C5 SR--89 4.50E-05 SR--91 1.60E-05 M0--99 2 90E-02 TC-99M 1 60E-02 TE127M 3.20E-05 TE-127 4.00E-05 TE129M 1.60E-04 T6-129 1.00E-04 TE131M 4.?05-05 TE-132 1 30E-03 I--130 6.10E-05 I--131 1.30E-01 I--132 1.60E-03 I--133 2.10E-02 I--135 2.70E-03 CS-134 1.30E-02 CS-136 2.70E-03 CS-137 9.30E-03 9A137M 6.70E-03 BA-140 2.00E-05 LA-140 1.80E-05 NP-239 5 80E-05 OTHERS 3.60E-05
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w TMI-2 May, 1976 Table 2-14 Base Case Pooulation Doses from Licuid Effluents Pooulation Doses ( lo 90 " at'lation)
Pathway Thyroid Total Body Tctal MIR/ year man-rem /yr
. san-rem /> ear Potable Water 8.94E 00 47E 00
'. 34E+01 Fresh Water Fish 5.88E-04
.69E-03 7.2f'-03
?.ive Shoreline 3.39E-05 3.39E-05 6.78m->5 Swimming 8.31E-07 8.3tE-07 1.66E-06 Boating 4.14E-07 4.14E-07 8.28E-07 Total 8.94E 00 4.48E
'1 1.34E+01 R353E1E 5/15/76 16.14.16
' *-.. L.)
v"e, g
=
W T*I-7 05/31/76 TAELE 2-15 PAGE 2 Cr a c:JUCTIONS IN 000UL ATION DOSES RESULTING Fo.09 LIQUIO ALTEDNATES 7
CASF H-3 REMOVE EVAPORATOR FRCW OIoTY WASTE SYSTEw caTHWAY THYoCIO TOTAL en0Y TCTat MAN-REM /YR MAN-REM /Y{
MAN-REM /Vi oCTaoLE WATER
-5.32E+00
-3.11E+00
-8.33E+C:
FDESw WATER FISH
-6 22E-04
-1.16E-01
-1.16E-C1 CIVER SHCRELINE OEPOSITS
-5.73E-04
-5.73E-04
-1.15E-C3 SWIMiING
-6.57E-06
-8.57E-06
-1.715-05 9CATING
-4 29E-06
-4.295-06
-8.57E-C6 TCTaL
-5.32E+CC
-3 13E+0]
-8 45E+0" CASE H-4 CEMOVE 90TH OEMINERALIZERS ROM OIRTY WASTE SYSTEM PATHWAY THYROIO TOTAL 300Y TOTAL MAN-REM /Y^
MA N-RE M/Y R MAN-REM /TR PCTA9LE WATEP
~5.31E+0C
-1 63E-0?
-5.33E*0C FoESH WATER FIS.-
-6 21E-04
-2.21E-04
-S.43E-C4 oIVED SHCRELINE DEFOSITS
-1.3?E-06
-1.325-06
-2.642-06 SWIMw!NG
-1.88E-07
-1.38E-07
-3.756-07 ocaTING
-9 38E-08
-9 38E-03
-1.88E-07
- CTAL
-5.31E+00
-1.655-02
-5.33E+C:
CASE H-5 OISCARD OIRTY WASTE WITHOUT TREATMENT oaTHWAY THYROID TOTAL E00Y TOTat MAN-REM /YR MAN-REM /Yo man-REM /Yo 00TA8LE WATER
-5.33 E + 0 3
-7 22E+01
-5.40E+03 FDESW WATER FISH
-6.23E-01
-2 32E+00
-2.94E+0:
DIVED SH03ELINE OEPOSITS
-1.30E-02
~1 30E-02
-2 60E-CL SWIMMING
-4.43E-04
-4.43E-04
-9 862-c4 00ATING
-2.22E-OL
-2.225-04
-4.43E-C4 total
-5.33E+03
-7.46E+01
-5.L7E+C3 NEGATIV E V ALUES oEFR ESENT 00S E INCRESSES
'r.
' W F NCTE u-
- t. O R3'?C IA
TMI-2 05/31/7; TAPLE 2-15 PAG:
C: 4 REQUCTIONS IN POPULATION 00SES RESULTING FROM LIQUIC ALTERNATEc C*FE I-i FEMOVE FIDST DEMINERALIZER FROM REGENERANT WASTE SYSTEM PATHWAY THYGOIO TOTAL 200Y TOT *L MAN-REM /YC MAN-REW/YR MAh-RE*/Y; 00TA9LE WATEC
-1.17E-02
-4 355-05
-1.135-C?
CCESw WATER FISH
-1.40E-06
-9 565-07
-2.3 E-06 P I V E C. SH0iELINE OEPOSITS
-6.23E-09
~6.23E-09
-1.25E-C6 SWIMMING
-4.07E-10
-4 07E-13
-8 14E-!3 9CATING
-2.03E-10
-2.03E-10
-4.07E-10 TCTAL
-1.17E-02
-4 94E-05
-1.17E-C2 CA5E I-2 REMOVE CONDENSATE DEMINERALIZER FROM REGENERANT WASTE SYSTEM PATHWAY THYROID TOTAL BODY TCTAL MAN-REM /YR MAN-REM /YR MAN-REM /v4 POTA=LE WATER
-1 07E-03
-2.22E-04
-1 29E-C3 F:ESH WATER FISH
-1.27E-07
-8.55E-06
-8.6BE-0E SIVED SHORELINE DEPOSITS
-4 34E-08
-4.345-03
-a.67E-09 SWIMMING
-5.39E-10
-5.39E-10
-1.03E-09 90ATING
-2.70E-10
-2.70E-10
-5.395-1C TOTAL
-1.07E-03
-2 30 E-0 4
-1.30E-C' CASE I-3 REMOVE 9OTHOEMINERALIkERS FROM REGENERANT WASTE SYST:tt DSTHWAY THYROID TOTAL 9001 TOTAL MAN-REM /YD MA N-0.E M/Y R M A fs - R E M / T ;
POTA:LE WATER
-1.19E-01
-7.36E-04
-1 195-Ci FESu WATER FISW
-1.41E-05
-1 91E-05
-1 22E-GE DIVER SHORELINE OEPOSITS
-1 06E-07
-1.06E-07
-2.11E-C7 SWIMMING
-4.61E-09
-4.61E -9.22E-C7 BCATING
-2.30E-09
-2.30E-03
-4.615-C9 TOTAL
-1. ice-01
-7.25E-04
-1 205-01 t99 +l Or.
r NOTE -- NEGATIVE VALUFS REPRESENT DOSE INC3EiSES R37251A
7"I-?
c5/31/76 TaaLE 2-15 PAGE 4 Ce a RE3UCTIONS I4 30PULATICN 00SES RESULTIS:G FROM LIQUID ALTEPNATE5 CASE I-4 OISCARO REGENERANT WASTE WITHOUT TREATHENT DaTHWAY THYRCIO TOTAL 900y TCTaL MAN-REM /YR MAN-RE"/YR M A N - 3 E " / Y ;.
PCTa3LE WATER
-1.19E+02
-5.24E+00
-1 24E+02
~;ESd WATER FISM
-1.415-02
-1 90E-01
-2.355-C1 DIVE 3 SHCRELINE CEPOSITS
-1.0?E-03
-1 09E-G3
-2.17E-03 SWIM"ING
-1.895-05
-1 39E-05
-3.795-19 9C*TI'4G
-9 47E-06
-9 47E-06
-1 39E-Oc TOTAL
-1.19E+02
-5.43E+00
-1.24E+C2 JOIE -- !EGATIVE VALUES REPRESENT DOSE INCREASES R372Ela
'...7 ( g.
r. <-
c..
e
~
TMI-2 May, 1976 Table 2-16 unual Cost of Licuid Alternates Case Designation Purpose dCost, S/ year
- Dirtv 'daste H-1 Remove demineralizer
( 30,100)
H-2 Remove conder. sate polisher
(
7,800)
H-3 Remove evaporator (110,100)
H-4 Famove both demineralizers
( 37,900)
H-5 Discard without processing (148,000)
Recenerant 'Jastes I-1 Remove demineralizer
( 84,500)
I-2 Remove condensate polisher
( 19,300)
I-3 Remove both demineralizers (103,800)
I-4 Disuard without treatment (364,400)
Note: Values in (
) are cost savings a See Appendix A for details of cost estimating IL r* _q; q v e.
. t. a SSS 5/18/76
Till-2 tiay c, 1976 Table 2-17 Cast-ilenefit Ration f o_r Al t e rna t e Dise s
- 1. i r p a i d s Annual A Doses" AnnualA Costs Cost-Benefit Ratios Case Purpose from Base from Prev Case from 13ase f rom L'rev Case from Base from Prev Case man-rem man-rem
$ / ma n - r cr.i
$/ man-rem Dirty Waste 11 - 2 kemove cond pol 1 sher
-5.09E-02
-7800 1.5E+05 M@
e d
11 - 1 Remove demineralizer
-5.29E-Ol
-4.7HE-01
-30100
-22300 5.7E+04 4.7E+04 Il-4 Remove both lonex
-5. 31E 00
-4. HOE 00
-37900
-7800 7.lE403
- 1. 6 E+ 0 ~'
11 - 3 Remove evaporator
-H.43E 00
-3.lOE 00
-110100
-72200
- 1. 3E+ 04 2.3Ee04 11 - 5 Discard withoat
-5.41E+03
-S.40E+03
-148000
-37900 2.7E+01 7.01 00 t reatmer.t Repen Waste 1-2 Remove cond polisher. -1.30E-03
-19300 1.5E407 I-I Remove demineralizer
-1.lHE-02
-1.05E-02
-84500
-65200 7.2E+06 6.2E+06 1-3 Remove both demin
-1.2dE-01
-1.ONE-01
-103800
-19300 H.7E+05 4.HEt05 1-4 Discard without
-1.24E+02
- .24E+02
-364400
-261000 2.9E+ 0 3 2.lEt03 treatment a From Table 2-15 b From Table 2-16 c Negative valucs are dose increases d Negative values are cost savings O
1 O)*
O GI O
(3)
TMI-2 May, 1976 Table 2-18 Cost-Beneficial Licuid Radwaste Systems Waste Stream Cost-Beneficial Treatment Shi.m Cleed & Equipment Drains Holdup Tanks" lon Exchance*
Evaporator" Condensate Polisher" Dirty Waste Discard after two stages of Ion Exchange Regenerant Waste Discard w/o treatment Turbine 31dg Suaps Discard w/o treatment a This equipment is required for process reasons.
No cost-benefit analyses were done since the equipment cannoc be removed in any event.
ed
[b w
TMI-2 May, 1976 Figure 3-1 G,taecus Was te Schematic--Ba se Ca t 3 from to Plant Primary
]
Vant CAS DECAY System l
[
Surge Tank 2 Holdup Tanks HEPA from to Plant STEAM JET AIR Vent EJECTOR Main Condensor i
L REPA Charcoal to Plant HIGH VCLL'ME Containment Atmosphere j
Vent FURG.
o.
EEPA Charcoal to Plant Aux Side Vent AUXILIARY 3 LOG Ventila1.on VENT *.LAT10:;
EEPA Charcoal to Turbine TURBI.'E BLDG 2 rom.urbine Bldg Vent VE. 1LATION
.u
,,e n t i la t io n
~
M37' 1970 TML-2 Figure 3-2 Gaseous '4aste Schematic-Cost.3eneficial Case to Plant Vent from Primat.
_1 CAS DECAY System Surge Tank 2 Holdup Tanks l
to Plant Vent STEAM JET AIR from Main
- ,aECTOR r
Condensor HEPA Charcoal Containment to Plant Vent HIGH VOLD E Atmosphere pggcz Aux Bldg to Plant Vent Vencilation Al"ULIAAY 3LDO
'E iTILATIC:;
from Turbine to Turbine Vent TURBINE ELDG 31dg Ventila....
f-
'E;cIL,clon m
P4 h14
EF1I-2 May, 1976 2
Table 3-1 Gaseous Treatment A l t e rn a t e s Run Designation" Waste Sys em Description of Alternate Affectec C-1 Gas Decay Add One Decay Tank C-2 Gas Decay Delete HElw C-3 Gas Decay Delete Charc'al D-2 Aux Bldg Ventilatien Remove Charcoal D-3 Aux 31dg Ventilation Remove HEPA & Charcoal E-1 Containment Purge Add Kidney E-3 Containment Purge Remove Cnarcoal from Purge E-4 Containment Purge Remove Charcoal and HEPA from Purge F
Condenser Air Ejec:or Remove Charcoal aCorresponds to identifying number on all GALE code inputs and cutputs.
5 /19 / 76
'a AR t-r, ~ y +,s s) *.i i.11
~
TM.1 - 2 May, 1976 Table 3-2 GALE Inout Terms for Ease Case--Gases
",o.
Spaces Entry Iten Units 33 80 2
Letdown Stripping 34 73-80 0
Holdup Time Xe days 35 73-80 0
Holdup Time Kr days 36 73-80 99 Collectica Time days 37 39-41 yes Wasta Gas Release 33 47-49 yes Aux Bldg Release 56-58 788 Aux Bldg Release 30 73-80 2.0 Containment Volume.
105 cu f t 40 73-30 0
3 Kidnay Throughput 10 cfm 41 47-49 yes Hig's Vol Parge 56-58 yes 78-80 20 42 46-53 0
tow yot Purge efm 63-65 Blank Blank 72-74 43 73 80 0
c, ten-Cen Blowdown Vent 44 73-80 0.1 Condenser Air Ejector re
_ y e ;-
LDi w
.)
5/19/76
'4AR
I"I-2 J6/01/7c TAALE 3-2 GASECUS REL E ASES EASE CASF (CURIES / TEA 7)
RELEASE Fo0M ISOTCDE P L A NT VENT TU90INE OLOG total
- ----3 4.58E+02 9 17E+01 5.50E+02 C --- 14 3.00E+00 3.
8 00E+00 AR--41 2.50E+11 0.
2.50E+01 MN--54 4.45E-04 0.
4.45E-04 rE--59 1.50E-04 3.
1.505-34 CO--58 1.50E-03 0.
1.50E-03 CO--60 6.80E-04 3.
6 80E-'4
<R-83M B.00E+00 0.
8 00E+JO
<D-85M 4 90E+01 3.
4 90E+01 KR--85 2.15E+02 3.
2.15E+02 vo--87 2.40E+01 3.
2.40E+01 vR--S$
9.00E+01 0.
9 00E+01
<R--89 2.00E+00 0.
2.00E+0C SR--89 3.33E-05 0.
3.33E-05 SR--90 6 00E-06 9.
6.00E-06
- E131M 9.80E+0i 0.
9 30E+01 XE133M 1 40E+02 0.
1.40E+02 xE-133 1.37E+04 0.
1.37E+04 YE135M 5.00E+00 J.
5.00E+00 XE-135 1.6SE+02 0.
1 68E+02 XE-137 4.00E+00 0.
4.00E*00
)E-138 1.80E+0i 0.
1 30E+01 I--131 2.88E-02 2.10E-03 3.09E-02 I--133 1.305-02 2 20E-03 1.52E-02 CS-134 4.45E-04 3.
4.45E-04 CS-137 7.55E-04 0.
7.555-04 en _ rp o n
~
dt:
. O. 0
Gli TMI-2 May, 1976 Table 3-4 GALE Input Terms for Gaseous Alternates Run Card Chan2es Recuired Designation Purpose Card No.
Lines Entry C-1 Add one decay tank 34 73-80 90 35 73-80 90 C-2 Delete HEPA Waste Gas release 37 39-41 leave blank C-3 Delete charcoal frora Waste Gas release Not necessary to run.
No iodine release this system.
D-2 Delete charcoal Aux Sidg 38 47-49 leave blank D-3 Delete HZPA & charcoal Aux Bldg 38 47-49 leave blank 56-58 leave blank E-1 Add kidney 40 73-80 20 E-3 Eliminate charcoal High Vol Purge 41 47-49 leave blank E-4 Eliminate HEPA & charcoal High Vol Purge 41 47 49 leave blank 56-58 leave blank F
Eliminate charcoal from Condenser Air Ejector Off Gas 44 73-80 1
l J.
o 7"I-?
06/01,76 TABLE 3-5 PAGE 1 or 2 350UCTICNS IN G ASECUS RELE2 SES DESULTING FGCM ALTERNATE TREATMENTE (C Uf(I'i S / Y E A R )
PLANT VENT ISCTor:
CASE C-1 CASE C-2 CASE 0-2 CASE 0-3 "N--54 D.
-4.45E-03 0.
-1.73E-02 eE--59 C.
-1 49E-03 0.
-5.c46-03 CO--53 0.
-1.48E-02 0.
-5.94E-02 CO--6C 0.
-6 93E-03 0.
-2.67E-G2
<3-839 e.00E+00 3.
O.
3.
<3-SAM 4.7CE+01 0.
O.
G.
KR--55 1 00E+01 0.
G.
O.
<R--87 2.40E+01 0.
O.
O.
<R--gg a.30E+01 0.
G.
O.
<R--89 2.00E+00 3.
O.
O.
SR--89 3.
-3.27F-04 0.
-1.29E-03 SR--90 0.
-5.94E-05 0.
-2.33E-04 XE1319 S.4CE+01 3.
O.
O.
XE133M 1 15E+02 0.
O.
O.
XE-137 1 11E+04 0.
O.
O.
XE139" 5.00E+03 0.
O.
O.
XE-135 1 52E+02 0.
D.
O.
XE-137 4.00E+0C 0.
O.
O.
- 1. 8 0 E +01 0.
O.
O.
I--131 0.
O.
-4 86E-02
-4 86E-02 I--133 0.
D.
-5 22E-02
-5.22E-02 CS-134 0.
-4.45E-03 0.
-1.78E-G2 CS-137 0.
-7.42E-03 0.
-2.975-02 TOTAL 1 17E*04
-4 00E-02
-1.01E-01
-2 6]E-01 TUR3INE 9UILDING TOTAL 0.
G.
O.
O.
CASE C-1 ADO ONE GAS DECAY TAN <
CASE C-2 3.EMOVE PE3A CRCM WASTE GAS RELEASE CASE D-2 REMOVE CHAPCOAL F30M AUXILIARY CUILCING CASE 0-3 3.EMOVE HEDA AND CHARCOAL FRCP AUXILIARY SUILDING NOTE NESATI1E VALUES REPRESENT INCREA$EC RELEASES LU '
O N
IM!t?
06/31/76 T ELE 3-5 ca3E ? CF 2 25'UCTIONS IN GaSECUS RELEASES RESULTING FRC" aLTiFNOTE T. EAT-ENTS
( C U o. I E S / Y E A P )
PLANT V9NT ISCTCP~
CASE E-1 CASE :-3 CASE E-4 CASE 7 MN--54 2 185-04 3.
-2 18E-02 0.
FE--59 7.43E-05 0.
-7.42E-C3 0.
CC--94 7.43E-04 0.
-7.43 E-0 2 0.
Co--6:
3.372-04 J.
-3 37E-02 3.
< o. - a 3 M 0.
9.
3.
C.
Ko-559 0;
0.
O.
D.
<o--85 O.
G.
G.
O.
<o--97 C.
O.
D.
3.
<R--Sa 0.
3.
O.
G.
<R--89 0.
3.
O.
O.
So--69 1.68E-05 3.
-1.63E-03 0.
SR--91 2.97E-06 0.
-2 97c-04 0.
XE131M C.
O.
G.
O.
XE137" 0.
O.
C.
O.
XE-133 0.
O.
O.
O.
XE1359 0.
G.
O.
O.
xE-135 0.
G.
O.
O.
XE-137 0.
O.
O.
O.
XE-138 0.
O.
O.
O.
I--131 1.96E-02
-1.80E-01
-1.8 0 E- 01
-3.065-02 I--133 3.30E-03
-3.24E-02
-3 24E-0 2
-3.24E-C2 CS-134 2.18E-04 3.
-2.19E-02 0.
CS-137 3.76E-04 0.
-3.762-02 0.
total 2.49E-02
-2.12E-01
-4 115-Ci
-6.30E-02 TUR3INE QUIL DI N G total 0.
O.
O.
O.
CASE E-1 300 <IONEY CASE E-3 3.EMOVE CHARCOAL FDOM HIGH VOLUME DURGE CASE E-4 CEMCVE HEPA AND CHARCOAL FRCM HIGH VOLUME PUPGE Cas: F RE"CVE CHARC0aL FRG" CCN0ENSE4 AIo EJECTOR OFrGas NOTE -- NEGATIVE VALUES RED 4ES9NT INCR:ASEO REL AS S A
IMI-2 May, 1976 Table 2-6 CALE Inout Terms for Cost-Beneficial Base Case--Gases Car Spaces Entry item Ur. i t s 33 80 2
Letdown Stripping 34 73-80 0
Holdup Time Xe days 35 73-80 0
Holdup Time Kr days 36 73-80 99 Collection Time days 37 39-41 Blank
'4as te Gas Release 33 47-49 Blank Aux Bldg 56-58 Blank 39 73-80 2.0 Containment Vol 10 cu ft 3
40 73-80 0
Containment 10 cu f t 41 47-49 Blank High Vol Purge 56-53 Blank 78-80 20 42 46-53 0
Low Vol Purge cfa 63-65 Blank 72-74 Blank 43 73-80 0
Steam Generator Blowdown Vent 44 73-80 0.1 Condenser Air Ej ector O
f' t} r.',w f..
e
'e
e S
1.tI-2
[9/CI/zs 17G15 E-z 9755093 bd13753$ -- DOSI-ESN3dIDI71 3753
)0nbI3S/A57e(
b575755 ehCW IsolodE d1;NI AENI inhcINB 61CD 10171 m----E t*555+02 c*T23+0T 5*50i+02 J---in E*005+JC C*
5*005+DC 76--9T 2*505+D1 C*
2*505+CT wN--59 t'9SS-02 C*
t'955-C2 35--56 T'505-02 0*
i*505-C2 30--SE I*502-0T O*
T'505-0T 30--50 9*905-02 0*
9'505-02 w b-B I*
9*005+00 O'
E*C05+LC ab-95W 9*603+01 C*
w-603+CT
/b--95 2*T55+02 0*
2'T55 w
)6--92 2*903+0T 0*
2*t03+01
)8--s9 6*003+0T 0*
6*C03+01
>b--06 2'003+00 0*
2*002+00 Sb--96 E*EES-DE 0*
E*EC5-0a 5b--60 9*003-09 C*
9*005-09 x5TETW 6*905+0T 0*
6*E03+CT x3TEEW T*403+02 0*
I'905+02 x5-TEE T*E25+09 0*
T'E25+0$
<5iE5W 5*005+00 O'
5*005+00 x3-IES T'992+02 C*
T*965+02 X3-TEZ t*003+00 O'
- 005+CC x5-TEG T'905+GT C*
T*&05+0T I--TET 2*523-01 2*T03-0E 2*565-DT I--TEE 6*292-02 2'203-OE 6*695-C2 3S-TEM t'955-02 C*
n**SE-02 DS-TEZ 2*553-02 C*
2*555-C2 22. - G o b, o,-
IL /, l')70
'1111 - 2 Q
Table a-8 Atmospheric Dispersion Factors-Vent / Reactor Illdg page 1 of 2 IN Puti TYPF-y/O sfC/ul DISTANCF INETFRS)
OlufCTICN (FCrnN 610
/411 or s611 7p40 IP067 24115 40725 56115 72405 N
1.77f-06 1 13f-05
%.DA 1.63f-07 l.?SF-07 8.00E-0A 2.59F-n8 1.lSE-08 7.49f-09
- 5. 41 f - 0 7 NNr 1.41f-06 P.57f-06 6.A1F-1.i4E-07
?.?3f-07 9.54E-08 2.96f-n8 1 30f-08 8.66f-09 6.llf-09 PT 1.4Pf-06 1.61E-n6 5.44f-07 1.44f-n7 7.31F-07 9.91f-nH 1.07f-08 1.150-03 c.71F-09 6.26f-t9 FNr 1 1/f-06 1 17F-n3 6.7ar-07
/.6?r-n7 P.03r-07 9.0/f-03 2.8tf-n8 1.24E-08 0.05f-n9 5.h4f F 1.96f-06 1.27f-06 4.inr-07 1.1HF-07 P.76F-07 9.61f-08 P.9ef-n8 1.31f-08 8.48f-09 0.12f-09 FSF P.13f-0$
1.67f-no 6.n?r-01 1 Gir-n7
?.0?f-07 H.shf-nH 2.65f-c8 1.16f-08 7.5?f-09 5.4tE-09
<r P..lf-06 1.69f-06 5.sof-07 P.77f-07 1.85r-07 7.90f-0A 2.46f-08 1.0AE-06 7.01f-09 5.04f-09 sSr P.3SF-06 6.89E-n7 4.97r-07 2.61f-07 1.Hlf-07 8.91f-nB 2.79f-nH 1.23f-08 7.99f-09 5.77E-09 S
1.95f-06
- 7. '/ 7 f - n ?
5.P6r-07 2.0Sf-07 1 37f-07 S.Alf-n3 1.a0f-na 7.90f-09 5.12f-09 3.70f-09 SSW 7.%kf-07 4.00f-07 1.unr-n7 1.PHf-07 A.76F-04 4.13f-OR 1.26f-08 S.49f-09 3.52f-09 2.51f-09 EW A.07f-07 4.07f-07 3.'PF-07 P.41F-07 1.36F-07 S.76E-08 1.79F-08 7.HAF-09 5.12f-09 3.70f-09 wSW l.1?"-n6 9.87F-07 S.47r-07 P.76f-07 1 84f-07 7.88f-08
?.46F-na 1.0RF-Ou 7.01f-09 ~~ 5.09f-09 V
- 1. F. ;. - 0 6 8.33f-07 6.04F-07 1.Hlf-07 P.60F-07 1.Ilf-07 3.42f-08 1.50f-08 9.74f-09 7.04f-09_
wNs 1.A0f.06 8.09f-07 6.H0f-07 1.'6f-07 P.4AF-07 1 06f-07 3.31F-n8 1.45E-08 9.43f-09
- 6. 8 t E-O' NW l.68F-n6 1.75E-06 1.6]f-06 1.n4f-06 7.43F-07 1.66f-07 6.54f-08 1.44E-08 9.42E-09 6.87E-09 CNW l.17f-06 9.44E-07 4.14r-07 1.68f-07 1.76r-07 9.94f-08 1.11f 1.38E-08 9.00f-09 c.55E-09 IN RUN TYPE-DEPLETrn x/C SEC/H3 DISTANCE IHETERS!
DiofCTION siCirA 61n 7413 40??
s631
??40 12067 24115 40??s 56315 72405 N
1.66r-06 1.0HE-06 4.74r-07 1.44f-07 1.lAF-07 6.7PE-08 1.88F-n8 7.10E-09 4.01f-09 2.60F-09 NNr 1.*IE-06 1 95f-06
- 4. /.9 F - n 7 2.21E-07 1.41F-07 5.SSE-n8 1.43f-n8 5.29E-09 2.99f-09 1.94E-09 NE 1.15E-Os 1.51F-06 4.aor-07 2.11F-n7 1.49r-n7 5.77f-08 1.49f-08 5.47E-09 3.09f-09 1.99E-09 ruf j Psf-n6 1.13f-06 4.19r-n7 P.16F-07 1.54r-07 5.?SF-nA 1.
if-08 5.n1E-09 2.uSF-09 1.65f-09 E
I.A9f-08 1.21f-06 4.n7f-07 P.?SF-07 1.44r-07 S.59f-Oe 1.44F-nn 5.3?f-09 3.00f-09 1.94E-n9 FSr 1.19f-n6 1.51F-06 4.97f-07 P.opf-07 1 29f-07 4.99E-na 1.?8f-08 4.72f-09 2.66f-09 1.72f-09 s'
P.?SF-06 1.49f-06 3.4af-07 1.nSF-07 1.lAr-07 4.59f-08 1.19f-08 4.40E-09 2.48f-04 1.60E-09 SSr 1.91f-n6 6.54E-07 4.396-07 P.llf-07 1.57F-07 5.14E-na 1.1Sf-na 4.94f.-09 2.b3f-09
- 1. 8 3 f - 0 's S
1.*6E-n6 7.14f-07 4.14f-07 1.16E-n7 A.7SF-nA 3.38E-08 8.6Af-n9 3.21E-09 1.alf-n9 1.17f-09 SSW 7.?lf-07 3.83f-n?
1.70f-07 1.14f-07 7.60r-08 P.4SE-03 6.24F-n9 2.?eE-09 1.27E-09 6.13E-10 SW 7.A7f-07 1.9?f-n7 3.ner-n7 1.?Sf-07 8.64f-08 3.17E-08 H.68f-04 3.20f.09 1.Hlf-09 1.17f-09 wsw
- 1. PSF-06 H.3sf-07 3.97f-u7 1.44f-07 1.18F-07 4.S8f-na 1 19F-n8 4.40t-09 2.49f-09 1.61F-09 w
1.w3f-06 7.96E-07 5.44f-07 P.wif-07 1.66f-07 6.43E-08 1.66f-nh 6.10f-09 3.45E-09 2.23F-09 wow
- 1. 7 0 f -0 6 7.71F-07 5.s6f-n7 2.6PF-07 1.59f-07 6.17f-08 1.60f-08 5.90E-09 3.34f-n9
- 2. lee-09 Nw l.49f-06 1.6AF-06 1.4PF-n6 9.17f-07 6.Svf-07 1.06E-07 6.20f-08 8.82f-09 5.0lf-09 1.27f-09 NNW l.?9E-06 0.0?f-07 4 14f-07 1.60E-07 1 59f-07 5.7bE-n8 1.Slf-n8 5.60E-09 _
3.19E-09 2.00f-09.
IN RUN TYPf-DEPGslTInN D/9 M-2 OlSTANCF INETERS)
DlorCTICH cfCTOR 610 2411 6n97 6631 7240 17067 24115 40??C 56319 72405 to 4.1SE nA 6.s/i-09 1.90r-n9 4.44f-In P. 81 f -10 1.69f-10 5.97r-11
?.09f-11 1.13f-l!
6.91f-12 NDF 4.dHf-04 9.PDF-09
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%.16F-10 1.95f-10
%.46F-ll 1.46f-Il 7.3HF-12 4.53F-12
(/I Nr P.64E-04 2.64F-09 6.Flf-10 3.71F-In 1.4WF-10 1.6af-10 3.H4F-Il 1.P5f-Il 6.36f-1?
3.9Si-l?
C.) E 1.44F-OR 1.78E-n9 8.h9f-10 9.1SF-In 5.66E-10 2.14f-10 4.09f-Il I.60f-Il 8.10f-12 5.03E-12 F5r 4.lSf-08 4.7?f-09 2.10f-09 1.0lf-09 6.llF-10
?.12L-10 S.30F-il I.71f-11 8.71f-12 5.45f-l?
Ir
- 7. ;N F - 0 9 7.53f-09 2.77F-09 1.28f-00 7.71f-In 2.93f-10 6.6SF-Il
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- 9. I t t - 11 2.l?f-Il 6.94E-12 3.$1F-12 2.19f-12 tw
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2.55f-12
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4.WF-09 4.75f-09 1.P9F-n9 9.14f-10 6.80f-10 2.SHf-In 5.6HP-Il 1.NPE-11 9.7st-12 6.0tf-12 wcs 4.a?f-04 4.10f-09 1.4sE-09 4.P9f-In 6.6?f-In 2.5lt-10 5.7?f-ll 1.H7E-Il 9.400-12 5.65f-12 Ns 1.;CF-0A b.tHF-09 2.%7f-09 1.60f-04 1.lPF-09 6.68f-In 1.54F - 10 2.ON -11 1.0 t -l l
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W W
4 7
N N h
4 L=.
k 3
1 7
7 N N 6
4 4
W 3
7 7
7
- U V Z / 6 Z W V g i f D V 29 v'3Z3Z ZUUZZW WVWVVf7 V 3 : 1 ;
ZUUZZ6
% rwVv T
- 't 1l r M
C V.
C V-3 4 s i w w u /
V y 3 3 c N
~k a
Zis uVV VV3 3 Z "6k L Zk LVV VJ 3 JZ
~%k w
m C
C C
"J Q v e y W
~r.%e).
I e T L #C C T T D @ @ ^= T D CD
@ @ T & & ? ? C' & ? r% C' 7 Y N N N t% 4% N N N G% t% N t% %. % *%-,
' C'D C O OaCGOOCC CO O O O O O o,3 C C O O O O 3
- = = = = - - = = = = =. = - -
T 4 e f e 8 4 I l B 6 4 8 8 6 4 1
- B 4 4 8 I t I l e I e I I B B t it'*
8 e i I e I t t t t 4 t # B # e
- =
s.;. G d 6 LaJ 6* 6 6 6 LJ i J LJ W 6 LJ L LJ O66666 6 W LJ 6 LJ W LJ 6 6 LaJ W O 6 La 6J.J6 6 tu 6 ;
L 6 4 Q's 4 D t'J <en-M 1 =e 4"% N ? M== 4 1: r* O 4C D Ci @ M '11 D C= MN P%. C a ~
6
-T D t"
D r*
- CG O 4 N J. * ** ** ~,T N4.OON I.I== 4.("e'1 W n N 4 @ @.-.
N ' M. W ? C sJ N J &==
t"'
f r*
7
- % we. r%. A.
. N C C=== M O. M C J
. c r.
N e e e e e o e o e e o e r=
e e o e o e e o e e c
e a e e e
. e e e a
e e
e W
= = * * * - = = = *e ** @ ** r* O r* ** ** - sa* *'*
OO4MMf"MMN==NM f4JJ
@ E J r" d M 4 'C O N N " Ud **
J.
I i
C M
l e
N
'"'e'* T C c~ W ~~ ? : TCC
=
?: ;* 2??
??: ??C ??
"J *% '% ^ ! N = N * ; * : ' ? : '
G GC OCCCCOOCCCOOOO OCC CCCCOOCCCCCCC
== -= - - - - - - = - -==- - - -
,,,e 0
@ t 8 I I l I e t 8 0 0 0 4 9 I I W 9 9 4 5 0 8 I B 5 6 9 I l I I B
@ $ 4 1 1 I 1 8 9 8 9 4 i t M
-6 in.
e 6 6 6 6 6 6 6 w w 6 66.n.
-66w66,6 66666666w
- 6 La-6 66'.6 *' ' 'i I f" ? C t'== P= a 4 Z e ot***-n Q4 @ r P%
R 4 t*' 4 ?== t% =e ?T@ G'
("' N f t% 4 f*'
t=> t%
ACCH k ** C-
? T
~)
=
y I
4 4 P*
t** 44AMPOOOM@ ? ?
P'=
44ON.4}M 4N4M
- ) **"'=**7""
- M N f A 7 CC O O N.
?. '*e' CAOJ O
A e e e e e e. e o e e e o e e e
@ e e e e o e e e o e o e o e
@ e e e o
e e e e e o e e o e
==
u.a
== --e== -e e.
- r=
,e.-e
=
-e O 4 4 @ @ @ 4 @ m N cat 4 4 Pi. r* 4 CD <C f* 4 4 C== 7 a, 9 ? 4 & O %.
M t
e I
I t
i
NN-----
cemeereeTeeemeeem e e e e m & C' & & ? ? e cc m m e C
OOCO CCOOOCBCOOOO OCCOCCCOCOCOCCOC
- - - = - * * * * = = - - - = = - - * = -
- 4 8 5 1 8 i B 1 8 I I I I 4 I 8 f B 6 3 I I e I I i 3 e e a I 3 3 U*
I e I i 5 1 0 9 1 8 I e t I e e r% 6 6 6 L J 6 W 6 6J W 6 w 6 6 LJ 6 LJ N W w W 6 w 6 6 6J 6 W 6 LJ 6 LJ 6" 6 N 6 Lad 6 ' W 6 ' W 6 LJ 6 c 6._
N
- % f - t\\ 4 f* - Q sw J@ &
t"' L f R C t% P= 4 C u.1 O== I ** t"== 4 = 4 t*1 C t%si'C 4 f C t'. L i 4 - 4 f% % w a
@ M. Q. 4 7. O. @, e & O O &
Q O O. =.= O O 4 @ C M 4 M 4. t% (%, N m==
- 4. P* ** @ O C - N. @. I. /.
O F 4. N.
a C 4 t'* 4 t%
at J
l rr 4 e e
e e e e
4 e e e e e e e o e
e.
4 e e e e
. e e e e.
C NNNNNNNN-e-NNnRN 0----@C@444D---.
N--4%-----
N i
O l
8 l
W m
I O
cccce C cec rec e meer*m e m e m e c e r e m e c cc m o m
o-k C C CC CCCC C CC CC C CC CCCCCCC CC CC C C C C C
= = = = = * * * - - - - * - - - - - -
O B B e i I e 8 5 3 5 I e 6 5 I O U*
I e I I a e e f 8 0 t t t e I I T 4 0 I I I I 4 8 8 I I B B 4 5 6 t" 6 6 6 6 6664k666 6666 t* 6 4 6666 61.n 6 6 666666 d** 6 6 6 n a. a. 6 = 6 m 4
.a. 6k u6-U}
- " 4 P* '% N P"* t% - t" O I ? I r% @== N
Z J ti r== C' r"" T, t" @ C & -* W== P=
=== # C 4 I C O 4% 3.
% : "% e'
- 1 Z'
F W e a=
T P'= f% r* 4 0. J. J. r* f6. G.: tt. O.
4 4 C 7 4.r* O t% 4 4. N 4t" N. m P= @
1 M. *C O N== 4. T. T.%.N.~.
4CN4T N. e e e e e e tg e e
. e e e e e e e e N e e e o e e e e e D D'CC f f4 tint %t"44 4*=4 N N t% N t% N t% 4%== *= - N r* t" (C t%
@@4n4D C 4 P N t%
(*' f f *= e#
I i
C l
i l
2 f* r* P* P=
P* N P* P= A T r= P= P= P= P= r=
P= P= t* r* P= T e T e e e T. r* P= tm P=
c C C C C C O O C -= C C o C O c C
CC GC CCCCCCCCCCCO CCCC CCCCCCCCCCCC
- - ~* - - - === - - - - - - - -
'2 P' t t t 0 I I I I f 8 I I 0 t 9 i r* 1 9 I I I I i 0 8 0 t I 3 0 0 s P=
5 9 I 1 1 I t I I I I I 1 6 I a
- C i 6 W 6 6 6 W W ' LJ.a 6 6 6 W l.aJ W 4 6 W knJ 6 W 4 J W 6 i.nd 6 6 kJ W 6: W6 4 La.; 6 W W kJ 6 4 k LnJ 1
- sa. 6 6 L --
l
=
C#*
CV r*s t% 4 & C== -F C 7 N 4 0 4
==
C N M f% O 4 M # & 4 f% E Pa= r*1 @ & r==
t% f% t% ? 4
-d M@ C4NC40$T O=== C T Z. 4 t% (" -T N (""' ?
'.?
E a=
0 C
V.
t% P= 3 C P= C 4 4 r* -= @
e 4..* a o. CC &.
f NOO - G O 4 4G;74f*14 N4%C O L.
Q
- e a e e e e e....
2
==* * * * *
- e * * *
- e e o e
- e 2
- e *
- e * * *
- e e
- e
't W
ea
.=
=-===-Pm
,= m t% t% r* -e uJ
. n.=
ce @ CC 7 4.F aC C - c e t==
t,,,J t% tb==== t% r% t% N== 0 - - N t% P=.--
O P-P-
8 e
w 6
W i
I.
2
.I.
I P= P= r* r* P* rm W P= P= P= f= - P= P= P= 4 P=
P= P= >= Pm P* P= P= P= r= P* P= P* P= P=
4 76 CCCCCCCCCOCCC C *= r-W L
CCCC CCOCCCCCCCCC U
CCCCCCCCCCCCCOCC W
= = - * * - - - = = - = = = - - - - Ce 2
U C 4 1 9 3 5 5 8 9 6 1 0 t 0 9 6 3 V
C 0 t t 8 5 g 8 4 I B B 3 0 3 3 I G
C I I t I I I 1 8 I I l 3 I I l 4 1
2 4 k 6 6. 6 k 6 k L.h W6k66666 2
4k6 L.L'6 6 6 k 6 k h.LJ 6666 2
4 6 6 W 6 6 6Ln'b
'.a. k6 iL 6L '.
O
>4 4
t% C t* / C
("'i E (I" -F N '
4 t% w 4 C 7 4 N iC 4 - P= 7 W I & P 4 as ry 4 t% 4 4 O. en t*> Q - r*
t*. Q f. g"1 s.'
4.= m f 44.t*9 g g g eer* f. x. r* 4 4 4.
. 4 4. om p me c. O. O. g
@ O.
. 4. x. em. r. 7. r* 4. t'D. 4. T. 4. s %4 4 -
M.= 4 # 4%.' C fb - i*
S P=
>=
e.,
rm w
..... w
. w 4 4 4 f*; 4 t*' f* ("' C% - (% f*1 4 4 en 4 e==
t\\ is f% t% t% t% t% t% eeme e.= t% to r" - t%
- =
J 4 f 4 V 4 rm 4 te.'% t% 4 4.
C = 4 t
C C
C m
I i
e t'*
r=
P=
f* r=
- = P. e= r* &
P= r r-r= em 4 r=
r= & e= P. P= f* r= r= P= em r= r* r= & < r=
C C CCC C c,; C C C C c c c.-
CCC C CCCCCCCCCCCO CCCCCC CCCC CCOCCC
--== - - C C C -= - - - C C --
== t t 4 I l t 1 i 4 j g 5 9 I L a
=== t t I I t I i t t I. t t t 8 p
== 1 3 I t I t I i B t 4 l t 1 #
(* 6 W64
- w W LaJ b; 6 6 kJ 4 W 6 L f"* 6J tr 6 W 6 La 6 6
=a.' 6 6 L L '6 W W "W6 6. 6w6W6 66 66Wki
<4 ON T ff' m - f P* 4D mC e 4 f C J O A
'.t' 4 C t% a3 C tV,s's 4
<f4 %4 f - % f *% 4 r* '% O th -
- 7. C. <*. <. C. tt. C'= t% T C 4. c. C. C t' C.
ff C. C. tV. e. C. P. t~. r= 4. <t. 4. t%. e= r-f. C.
v 4. c. 's. e t*. C. ts.
e
.t'.
\\1 4 4. r=
C P~
-CC~
e
. e e.
D 'C 4 f 4 7 4 f t t% m 4 t-r~. N 4 m
t" 4 4 I"" 4 t' I** n t% - N t=1,1 ~t - e 4 2 O T P=
===== 4 4 4 t*
t** *=-
I t%,
e O
I E
W e--
4
C* C C 4 < t* 4,C m 5 P
,C 4,.C 4 0
4 r*= e* r* P= P* t* P* P* P* P* P= r* P=
C4 C
C' O C* C' ?
"l* C' ? O O C ??? e^
l OC CC CCCCC CCCGCCC CCCCCCCCCC CCCCC C N
CCCC CCCCC-C C C C C 2 1
f% 8 9 1 4 I t 1 i I t 8 I 4 1 1 I O
tt e 4 4 a l I t e I a 6 e i I e s O
rN 8 I I a t a e I I e : 1 I t C
t% 4 La L 6 L6L 4 La k a k 6 L tc k
'N t\\ 46L 6664 6 6 6 6 k L 6 La. 6 t\\ w 6
.6 6 W 6 L6 6L% 44 h ts 6
t*
C C aC t% q 4 P= f* a.
t' re y r= ( r44 C c s(
t-
,.L' - 4 7 t% C C c% r". 4.C 4 t%
7 C ;\\ 't J C % CP C - r'= <4'=-='c"C ra W cs ~
- - A. C. *=. C.(f. G.("e t% T.t* t* t'.
P= *=
J., u 4 g.
C 4Qe 1 L
4
,; 4 t% 4 4 t% u, em 44 t= C 4
=
t(
F=
4 1 t'
v e
e e C
= * * * * *
- e *
= a e e
- e e *. *
- e 1
G t% -== - - = O - - @ 4 e tn t%
6
- G
%P=CP=4P=Gc14,C y @ N =
P-t~ c% - = = % % t% % t% C -= - t% % c ~.
C 6
P-
==
e-a l'8 ss; as 1 O
.J C
6 4
C 0,
o, l
6 e444 D D t.C < C.c,C 4 Z <,0 W
4 4 4' Z 4 ~C 4 D e C < < a < < 4' W
C 2 ? ? th C' r T 2 ? 2 3 W ~~ ~ :
as C CC C CCCCC oCC OOCO O
CCOOCOCCOCCOCCOC C
C C C O C C 5.3 C C C C O C C C L l 2 F'
0 1 I t 1 I I 6 1 3 8 4 9 9 1 6 t"! l B I I i 9 3 6 1 I I I B $ I I 4"=
0 4 1 6 1 I t 5 a 1 3 5 t I 6 I i c I
- W 6 6 L. u. W u. W u 6 6 u W u. W W
.I
- W u u. 6 W 6 u. u.1 w u. W u. 6 w 6 3
- u. 6 u. 6. W L 6 6 u.1 u. t : 66.
LaJ 4 4 P'- I 4% 4N( a -= T T o rm N4 W
f - 4 N r"i4
("' (*'
("' NT7 4 T r* fa m
.aJ
-F m 7 ("9 -("' N f% o t.D 4 v'* J % 4 't.
a f% t'== f"i E.==.e
<D. F. 4. tb. & 4, t="
C. C. cc. P=
N -== (*t 7 - 7. <C. C N. 4 % f. 4.,C. C,=
1 N W J. s-=.C. ?. iC. N. - ;e" C f. C. C. C. 4 -
CL 7,
e e.
e e. e o e e e e e e
e aJ D'"
4 4 4 t** 4 f*) t" f"1 4== t% t"4 4 4 P* ic P=
@ t"" t*9 (% 1 N t% N M== se t% f** f**. W @
D.
== 0 C P'= C 7 - - C" t" 4 P= - as - * -
rt V
2 7
D 3
C 2
ct a
'." / *P f t' f t.' W T tl'tP T tt'U'tf D T T T ll' f f f Ll' d' f 'f f f t!' tf f r* r= P=
- k *= tm != t*
T PC % !* Pm WT U
CC CC CC CCCCCC CCCC CCC CCC CCC C CC CCCC CCC C CCCC C C CCCC C "
+
- C 4 4 0 6 t 3 i I g I I g e g g g C 0 1 I f 8 1 9 I I t t i g I g i C e a i I e I e 3 I I I t 8 3 g C
- La. 6 6 r. 6 kJ t.a. 6 Ln.J W u.J tv kJ La 6 6
- uJ LaJ L 6 L i.aJ 6 6 kJ w 6 E ;66J
- L. 6 6 6 b.; W 6u u6*6 i_
W 41
(*
T J" i @ (*i C O 61 r=. N f% 4 4'l i%
4-G 7 r"' C 4 4 a t' P=
f"'
t*' 4 P* e P.
t% t%,1 g w
,,g.
..=.=""."'."'r'=0 m.
4
.% T :" N?c
.. " *. ~. ~ ~ ~
'.e 5==
% s - -
L 0 -
f*
1 *=
t' V r* t' 4 t'
C s' 9m-CI. sf. C. %. C..F. 1. et,. G..
e e o e e e a 4.
. = P... C.
3==
.(
t'
% tr t.
.. e e e sf 44 g t" 4 t* t* t' t=
- er m 4 4 V f 4 t' t*1 t* t*
t' r* t' t\\ e e
*-=-o
- J 4 -----
C 2
>=
e4 2
2 2
N Ca C2 C Lr e
-C
-C
-C
- * =
h ta '
W
't y
't "I
> = >
k W
k k
3 7
3 T
W 6
L W
N r
> =
2UU ei k
'."ta' t/' la: V / V. 'A U" 3
'n :
ZUUZ7k Z k </'6 / V.V ? V. 323 :
- UU
- 6 : W J' 6 *r f V ' f
'M C
- - 6 u
/ i A
- u. P #
eV 3 3 2 2
== LaJ 6 Z2W 6VV V V3
'e ZZ
- i.e ZZw 4 it J V '/ I i.
OV Q#
2 v
==
==
e.=
C C
C r n mn x
Tl!1 - 2 Table 3-9 (contJ luge 2 of 2 flay, 1978 On Mnnual Rf0-Ix-11 JYWS JfT ATuosNEETC D %PFRSIC FA 0 FOR-TMI' VFNi-ASSmFD MOUND
. TYPE-z/0 SFC/H3 DISTANCE (HEffRS)
IN RUN OlaFCTION 72405
<rCTA9 610 2411 cos?
g611 7740
}?O67 24115 40?29 56315
_ 1.04E ~08 t'
4.?)E-09 5.f5f-06
?.??F-06 1.69F-06 1.19F-06 5.71F-07 1.11F-o?
2.20f-08 1 44f-ia NNr 4.46E-09 5.9tE-06 2.6%F-06 1.78F-06 1.?SF-06 6.06E-07 1.40f-0/
?.3%f-08 1 54f-SA 1.12f-04 LE 1.7sr-09 3.74E-06 1.0%F-06 9.49E-07 1.75r-07 1.66E-07 5.11F-08
?.37E-08 1.SSE-o8
..lef-04 FNF 1.60f-05 3.61E-06 1.0Pr-06 5.11f-07 3.65F-07
- 1. 6?t -0 7 5.16f-0A 2.30L-08 1.50F-OH
- 1. G W -0 8 f
4.0AF-05 4 12F-06 1.14F-06 5.46F-07 4.06F-07 1 7HF-07 5.64F-nB
?.50E-08 1.6?f-68 1.llf-Od FSF 1.06E 09 3.95F-06 1.00F-06 5.70f-07 1.89F-07 1.71F-07 5.41F-08 2.40E-08 1.566-J8 1.12f-08 5F 4.l?f-05 4.l?F-06 1.11F-06 5.c0F-07 4.00F-07 1.74F-07 S.4AF-06 2.4?!-00 1.boF-08 1.12t -O d S$F S.57E-05 7.4GF-06 3.16F-06 2.19F-06 1.51E-06 7.?7f-07 1.64f-07 2.71E-08 1.tif-08 1.2tW-08 5
1.89f-05 5.?lf-06
?.49F-06 1.64f-0A 1 0HF-06 5.12E-07 1.16f-07 1.91F-08 1.26f -6 8 9.10F-09 SSw
?.60E-05 3.41F-66 1.6?F-06 9.91F-07 6.91F-07 1.2BF-07 7.40F-08 1.??E-68 7.91r-a9 5.71f-09 SW 7,60f-09 P.63r-06 7.3?F-07 3.a?E-07 7.61f-07 1.15f-07 3.64F-08 1.62E-08 1.05f-J8 7.56E-09 3.34F 17 1.48E-07 4.74f-08 4.96f-09 wSW 1.36F-05 3.35f-06 9.14r-07
- 4. ROE-07 ~
- 4. 3 7F 17 1 92E-07 6.06F-00
' 2.1.E-Od 1.Jdf-08 ~
1.2tf o'
W 4.18F-05 4.43E-06 1.23r-06 6.410-07 2.68E-08 1.74f-id wNJ 4.17f-09 4.35f-06 1.??r-06 6.40f-07 4.39F-07 1.9fa 17 6.28F-08 2.80E-08 1.u]E-08 1.132 tW 4.16E-05 4.16f-06 1.17E-06 6.lAE-07 4.24F-07 1.6vC';7 6.10F-08 2.71E-09 1.7df-06 1.30f.
NNw 4.04f-05 5.3SE-06
?.69F-06 1.61f-06 1 14F-06 5.49.*37
!.?7f-07 2.13E-08 1.39f-08 1.02E-08 i
IN RIN TYPf-DEPLFTFO X/0 SEC/H1 DISTANCF (HETEPSI DIPFCTION (FCTA4 610 2411 40??
E631 7240
!?067 24115 40??5 56316 77405 N
1.66F-05 4.29f-06 1.OPF-06 1.13E-0A 7.%9E-07 1.32E-07 6.36F-08 H.93E-09 5.09f-69 3.11F-G9 NNF 3.96f-05 4.4HF-06 P.0?f-06 1.19E-06 A.0?F-07 3.5?f-07 6.79f-08 9.56F-09 S.4tf-09 1.57F-09 NF 1.?4f-09
?.84F-06 7.40r-0F 3.A6f-07 7.40F-07 9.67E-08
?.5HF-06
.9.64f-09 S.4 e f -0 )
J.5tE-09 FNE,
1.llf-05 2.75F-06 7.20F-07 3.96F-07
?.31F-07 9.40E-08
?.49F-03 9.31E-09 S.30E-69, 3.45E-09 f
1.43F-09 1.13f-06 A.10F-07 3.48F-07
?.60F-47 1.04f-07 2.71F-08 1.0lf-08 5.74f-a9 3.71E-69 ESE 1.43F-05 3.00E-06 7.7%F-07 3.40f-07 2.49F-07 9.93f-08 2.62f-n8 9.74f-09 5.Sif-09 3.56t-09 (E
1.5FE-OS 3.l?E-06 8.01F-07 3.92f-07
?.56F-07 1.01E-07 2.65F-08 9.H3F-09 5.S4f-09 3.57E-09
%5E 4.A?f-05 5.6AE-06
?.EPF-46 1.46E-06 9.80F-07 4.?1F-07 7.96F-08 1.llf-06 6.//f-69 4.06E-09 S
1.16f-05 3.96F-02 1.76r-06 1.01E-06 6.88F-07 2.98F -0 7 5.63F-08 7.ASE-09 4.45f-39
?.89E-09 59W 2.lAF-05
?.59f-06 1.14E-06 6.63F-07 4.41F-07 1.91E-07 3.ShF-0B 4.97f-09 2.hlf-69
- 1. ale-09
%W
?.25F -05 1 99f-06 5.lpr-07
?.%SF-07 1.67F-07 6.6AE-08 1.76F-08 6.5/f-09 3.7?F-09 2.41F-09 VSW
?.41f-05 2.54E-06 6.61F-07 3.26F-07 2.14F-07 8.61E-03 2.29F-08 6.57E-09 4.87f-09 3.ltE-09 W
1.79f-05 3.16E-06 A.7?F-07 4.?8r-07
? 80r-07 1.12f -0 7 2.93F-08 1.09f-08 6.17f-09 3.99E -09 WNW 3.78f-05 3.30F-06 A.63F-07 4.27E-07 7.80E-07 1.13F-07 1.04f-08 1.14E-08 6.47f-09 4.Plf-09
- ??F-07 7 71F-07 1 10E-07 2.95F-08 1.llE-Od u.32E-69 4.122 Nw 1.60E-05 1 16f-06 8.10F-07 Neu 1.44E-05 4.06F-06 1.pir-ne 1.0AE-06 7.??f-07 3.19E-07 6.14f-08 8.64f-09 4.94f-09 3.23f IN RUN TYPE-DEPosl T '.m D/0 H-?
!)l5TANrf (METERS)
OlPFCliCN SFCTAR 616 2413 40??
5611 7740 I?067 24135 40??%.
56115 7240S ta 1 76f-07 1.16E-08 4.44r-09
?.46f-09 i.52F-09 6.?Jf-10 1.0?f-10 1.?4f-ll 6.3tf-12 3.92F-12 tmF 1 11f-07 1.?tF-08 4.67F-09 P.EGE-04 1.59F-09 6.49f-10 1.06f-10 1.10t-il 6.57F-l?
'.Ldf~l?
(f7 NF 1.0%f-07 7.?4F-09 1.64F-09 7.RAF-10 4.59F-10 1.74f-10
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219.
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'I M i - 2 Table 3-11 May, 197h Input Data for Crop-Related Population Doses Vent i Vent 2
~
Patbvay Yield Specific Yield Type of Vegetation X/Q RDEPOS X/Q RDEPOS 2
3
-2 sec/m3 m-2 kg kg/m 3, : !nr m
Cow tillk 1.28E+9 0;179E-7 0.492E-10 0.523E-7 0.933E-10 Beef 1.76E+8 Swine 3.63E+7 Eggs 1.50E&8 Chickens 1.00E+8 Grains 1.50E+9 0.40 exposed Potatoes 1.20E+8 2.6 root Fruit 2.50E+7 1.3 leafy 1.cafy Vegetables 2.20E+8 3.0 leafy 1
J
/
Mushrooms 2.30Et7 root 0.116E-7 0.170E-10 0.231E-7 0.173E-10 Exposed Vegetables 3.70E+7 z.o exposed 0.179E-7 0.492E-10 0.523E-7 0.933E-lC O
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T"I-2 CE/01/7E TABLE 3-14 703ULATION JCSES CROM GASEOUS RELEASES OASE CASE 1990 POPULATICN pat *waY THYCCID TOTAL SC0Y TOTAL MAN-REW/YR M*N-REM /YR
- aN-;E*/YD UC AL E Ga5 I MME ASION (GAMMA) 4.37E+00 4.37E*03 9.73L+J0 G;00NJ 'La43 GECOLTTION 1.10E-01 1.10E-01 2.19E-C1 D.w a t a T I c 7 1.66E+00 1 09E*03 2.74E+:C STQ.E] c-UITS AND siGE TA BL ES 1 02E*01 5 96E+0]
1.61E+01 F;ESH FRUIT 2 aNO 1EG?T
- 3LE S 1.J5E+00 7.34E-01 2.C6 E + 0 C MEAT ( CC N T a 'tINaT E] FCRAGE) 1 15E+00 d.975-01 2.0 5 E + C C
.*Ea7 ( CO N T a.M I N A T E ] C E 5 0) 6 91E-01 8.92E-01 1.73E'CC CCWS MIL < (CONTanI1 F; RAGE) 1.01E+01 1.7*E*CJ 1.19E*C1 CCWS MIL < (CCr.TarIn FiEO)
.72E+00 1.72E+03 3.44E+0C TCTaL 3 15E+01 1 75E+01 4 90E+C1 2010 PCPULATICN PATHWAY THYROID TOTAL aC0Y TOTAL MAN-REM /YR MA N-iE M/ Y R M S N -R E M / Y C NCOLE Gas IM"EPSIJN (GAMMA) 6.49E+00 6.49E+0]
1.3:E+C1 G CUND LLaNE 7EPCSITION 1.660-01 1.66E-01 3.?iE-Ci I ':Ha'. A TI Ld 2 47E+00 1.63E+00 4 10E+00 STC'.~J e*UITS aMO VEGETa3LES 1.02E+0.
5 965+01 1 61 E
- 01 F: ESw F'UITS aNG VEGETABLES 1.35E+00 7.J4E-01 2 36E+00 MEAT (CONTAMINATE] FORAGE) 1 15E+00 8 975-01 2.05 E ' C C MFAT (CONTaMIN ATEQ FEED) 8 91E-01 3.92E-01 1 7eE+r0 CCWS MILK (CCNTAMIN FCRAGE) 1 31E*01 1.76E+00 1 19E+C1 CCWS MIL < (CCNTAMIN FEED) 1.72E+00 1 72E+00 3 44 E + J C TCTal 3.45E+0i 2.02E+01 5.47d+Li R312 ESP R423E79 731?ESr r,, a c q L'
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TM1-2 tia y, 1"76 Table 3-15 PopulationDoseheiluctions f roin Caseous _ A l ternat es Dose Reductions" Population _
Food Case Purptwe Thyroid Total 11ody T! y roid Total llody Total C-l Ashi I gas decar tank 3.61E 00 3.62E 00 0
1.22E-04
'.2lE 00 C-2 Delete llEPA Waste Cas
-6. 2bE '11
-6.31E-01 0
-5.77E-01
-1.t1IE 00 D-2 Reinove Chaccoal Aux illdg
-8.75E-01
-2.69E-03
-2. ole-01
-4.12E-02
-2.*0E*01 D- ~1 Remove llEPA 6 Char aux lilde
-3.31E 00
-2.4HE 00
-2.01E401
-2.35E 00
- 2. ti 3 E+ 0 !
E-1 Add kidney 3.21E-01 3.20E-02 3.13E 00 4.54E-02 ti.SlE 00 E 'l Rennive Charcoal ilV Purge
-2.67E 00
-8.63E-03
-7.44E*01
-1.52E-01
-7.72Etol E-4 Reinove IIEPA & Char ilV Purge
-S.75E 00
-3.12E 00
-7.44E+01
-3.0 3E 00
- ti. 6 :lE + 01 F
R enn n i-Char from Cond Air Ej
-S.49E-01
-1.69E-03
-1.27E+01
-2.59E-02
-1.13E+01
.,: it ave values are dose increases brought about lay the removal of equipment (si R 'i6 'li?O 2 R4H3EPR R4tl6EQD U
5/17/76 5 / l's /76 S/17/70 f
111.49.47 19.V>.Sl 20.11.14 (4
T.3 C
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TM122 May, 1976 Table 3-16 Annual Cost of Gaseous Alternates Case Des.;pation Descriotion 46 Cost, S/ year
- C-l Add one tank 43,700 C-2 Delete EEPA (7,500)b D-2 Remove charcoal (IL4,200)
D-3 Remove EEPA & charcoal (277,400)
E-1 Add kidney 67,300 E-3 Re=ove charcoal from High Vol Purge (61-300)
E-4 Remove EEPA & charcoal frco High Vol Purge (130,500)
F Remove charcoal (14,100)
See Appendix A for details of cost estimating a
b Values in (
) are cost savings
<3
<>,R g e
du
~~s
TM1-2 fla y, 1976 O
Table 3-17 Cost-Ilenef_it Ratlos for Altennate Cases-Gases Annual A Do s e:/*
Annuald Costel)
Cort _llg efit Ratios Case Purpose f roni liase from Prev Case from liase from Prev Case f ro:n base from Prev Case Designation man-rem man-rem
$/ man-rem 0 / nutn - r em Gas Decay C-2 Delete llEPA
-1.81E 00
-7,500'I 6.0E+d3 C-1 Atitt one tank 7.23E 00 43,700 c
4.lE+03 Auxiliary B l alg D-2 Remove citarcoal
-2.10E+01
-144,200 6.9E+03 D-3 Remove llEPA &
.harcoal
-2.03E+01
-7.30E 00
-277,400
-113,200 9.HE*03 1.HEt04 Containment E-1 Ath! kialney H.53E 60 67,300 7.9E+03 E-1 Remove char IIVP
-7.72F+01
-61,300 7.9Et02 E-4 Remove llEPA &
charcoal llVP
-H.6 3E+ 01
-9.10E 00
-130,500
-69,200 1.SE403 7.6E*03 Air Elector F
Remove cliarcoal
-1.33E+01
-14,100
- 1. l E + '13 a From Table 3-15 CG b From Talile 3-16 Q
c Hegative values are dose increases.
,'y Neg *ive values are cost savings.
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a TM1-2 May, 1976 Table 3-18 Indicated Cost-Beneficial Gaseous Radwaste Svstems System Cost-Beneficial Treatment Gas Decay Release from decay tanks without further treatment Auxiliary Bldg Remove HEFA and charcoal Containment Release without treatment Air Ejector Release through charcoal *
- However, this :harconi is the same as that which serves the Auxiliary Bldg.
4
.