ML19221A927
| ML19221A927 | |
| Person / Time | |
|---|---|
| Issue date: | 03/31/1976 |
| From: | NRC OFFICE OF STANDARDS DEVELOPMENT |
| To: | |
| References | |
| REGGD-01.110, REGGD-1.110, NUDOCS 7907100403 | |
| Download: ML19221A927 (89) | |
Text
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'U.S. NUCLEAR Rr"3ULATORY COMMISSION March 1976 REGU LATORY GU i OE OFFICE OF STANDARDS DEVELOPMENT e
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REGULATORY GUIDE 1e110 g
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i COST-BENEFIT ANALYSIS FOR RADWASTE SYST9tiFOR
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h5 USNRC REGULATORY GUIDES Comments show'd be seas to the secretary of she Commes. on u s socies,
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TAB!F OF CONTENTS Pale A.
INTRODUCTION.
1.110-5 B.
DISCUSSION.
1.110-5 C.
REGULATORY POSITION.
1.110-6 D.
IMPL EMENTATION.
1.110-6 APPENDIX A, PROCEDURES FOR PERFORMING COST-BENEFIT ANALYSES.
1.110-7 APPENDIX B, BASES FOR PARAMETERS USED IN PERFORMING COST-BENEFIT ANALYSES.
1.110-17 LIST OF APPENDIX B COST ESTIMATE SHEETS.
1.110-19 REFERENCES TO APPENDIX B.
1.110-85 APPENDIX C DATA NEEDED FOR RADWASTE TREATMENT SYSTEM COST-BENEFIT ANALYSIS FOR LIGHT-WATER-COOLED NUCLEAR REACTORS.
1.110-86 SAMPJ ESTI" ATE SHEETS.
1.110-88
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s 1.110-3
LIST OF TABLES Table Paje A-1 Direct Co*ts - Gaseous Radwaste Augnents.
1.110-8 A-2 Annual Operating Costs - Gaseous Radwaste Augments; Liquid Radwaste Augments.
1.110-10 A-3 Annual Maintenance Costs - Gasecus Radwaste Augments; Liquid Radwaste Augments.
1.110-12 A-4 Labor Cost Correction Factors.
1.110-13 A-5 Indirect Cost Factors.
1.110-14 A-6 Capital Recovery Factors.
1.110-15 B-1 Indirect Costs.
1.110-18 LIST OF FIGURES Figure Fage A-1 Electric Power Supply Areas in the United States.
1.110-16 h
1.110-4
A.
INTRODUCTION Section II.D of Appendix I, " Numerical Guides for Design Objectives and Limiting Conditions for Operation to Meet the Criterion 'As Low As is Reasonably Achievable' for Radicactive Material in Light-Water-Cooled Nuclear Power Reactor Effluents,' to 10 CFR Part 50, Licensing of Produc-tion and Utilization Facilities," requires that liquid and gaseous raddaste systems for light-water-cooled nuclear puwer reactors include all items of reasonably demonstrated technology that, when added to the system sequentially and in order of diminishing Cost-benefit return, can, for a favorable cost-benefit ratio, effect reductions in dose to the population reasonably expected to be within 50 railes of the reactcr. Values of $1000 per man-rem and 51000 per ra ~ thyroid-rem are given as interim criteria pending the development and establishrent of better criteria.
Compliance with Section 11.0 of Appendix I tc 10 CFR Part 50 (wtich specifically addresses doses to the population) and Sections !!.A II.B. and II.C (which address doses to nearby individuals) is required to meet the criterion, "as low as is reasonably achievable.'
To implement the requirements of Apoendix I, the MC staff has developed a series of ouides providing rxthods acceptable to the staff for the calculation of effluent releases, dispersicn of effluents in the atmosphere and dif ferent water bodies, associated radiation doses to man, and Cost-benefit aspects of treating radmastes. This regulatory guide describes a rethod for perforring a cost-benefit analysis for liquid aad gaseous radwaste system comperents.
The procedures anet mdels rmvided in tnis guide will be subject to continuing review by the staf f with the aim of providing greater flexibility to the applicant in reeting the require-ments of Appcndix I.
As a result of such reviews, it is expected that dlternative acceptable cethods for calculation will be made available to applicants and that calculaticral procedures found to be unnecessary will be eliminated.
B.
DISCUSSION Each applicant for a permit to construct or a license to cperate a lignt-water-cooled nuclear power reactor and each licensee with a license to operate a light-water-cooled nuclear power reactor is required to provide reasonable assurance that the design cLactives for as icw as is reasonably achievable effluent releases are satisfied by the liquid 3rd casecus radwaste system designs. It is the objective of this guide to provide an acceptable mechod of performing cost-benefit analysis, in conformance with Section II.D of Appendix I, to demonstrate that the plant design includes all items of reasonably de onstrated technology for reducing the cumula-tive population dose due to releases of radioactive materials from the reactor to levels as ice as reasonably achievable. As an interim reasure the Commission chose values of $1000 per man-rem and $1000 per man-thyroid-rem (or lesser values if demonstrated to be suitable for a particu-lar site) to be used to implement the cost-benefit aralysis.
Eecause the Commission has not outlined any procedures for including the effects of inflation in the analysis, the NRC staff's analysis is based on 19 % dollars; i.e., neither the costs nor the interim criteria are escalated for the predicted ef.. cs of inflaticn. Since the worth of a man-rem or man-thyroid-rem to the public is subject to the same fluctuations in value as the cost of equipment to reduce radioactive emissions, the MC staff believes this approach to be reasonable.
The NRC staff has outlined a method for perforcing the r? quired cost-benefit analysis and has provided cost parameters for estimating the costs for the various radwaste treatment equip-ment iters in u'.e, or proposed for use, at light-water-cooled nuclear power reactors. The rethodology and cost parameters are presented in Appendix A to this guide. The costs presented consider the direct equipment cost and the costs of building space, supportive services, cai.te-nance, interest, and operating as well as other Costs generally considered in an3lyziro Capital and operating costs in power plant estimating. The bases for the costs calculated by tre ',RC staff are given in Appendix B.
126 266 1-110-5
C.
REGULATCdY P05t!'ON 1.
In accordance with Section II.D. Appendix I to 10 CFR Part 50, each applicsnt for a pemit to construct a light-water-cooled nuclear power reactor should demonstrate by means of a cost-benefit analysis that further reductions to the cumulative dose to the population within a 50-mile radius of the reactor site cannot be effected at an annual cost of $1000 per men-rem or
$1000 per man-thyroid-rem (or such lesser costs as demonstrated to be suitable for a particular Ca50).
2.
The cost-benefit analysis should consider the reduction in releases of radioactive material from all effluent pathways. Liquid and gaseous radwaste system augments considered in the analysis should be selected in order of diminishing cost-benefit returns.
3.
All costs shculd be given in terms of 1975 dollars (as is the $1000 per man-rem cost with which they are compared). Allowances for inflation after 1975 should not be factored into the cost estinates.
4.
The method of calculation described in Appendix A and the parameters presented in Appendix 3 of this guide are acceptable to the NPC staff for performing the cost-benefit analysis.
5.
in support of the cost-benefit analysis, the applicant should provide a complete evaluation including methodology used, components considered, and all ass eptions and parameters used.
Infomation to be submitted by the applicant is described in Appendix C to this guide. Use of parfmeter5, assumptions, and models different from those given in Appendices A and B to this guide may result in differences between the evaluations by applicants and those by the NRC staf f.
Because of this, these parameters and assumptions should L,e clearly described and substantiated by the applicant.
D.
IMPLEMENfATION The purpose of this section is to provide infomation t; license applicants and licensees regarding the NRC staff's plan for using this regulatory guide.
Except in those cases in which the applicant proposes an acceptable alternative method for complying with specified portions of the Comission's regulations, the method described herein will be used in the evaluation o.f construction pemit applications docketed after June 4,1976 unless this guide is revised as a result of suggestions from the public or additional staff review.
If an applicant wishes to use this regulatory guide in developing submittals for applications docketed on or befcre June 4,1976. the pertinent portions of the application will be evaluated on the basis of this guida.
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1.110-6
APPENDIX A PROCEDURES FOR PERFORMING COST-BENEFIT ANALYSES Inis appendix contains guidance for performing cost-benefit analyses on individual system augments, as well as the parameters needed for estimating costs. The bases for the rarancters and worksheets appropriate for use with the following cost-benefit procedure are giv en in Appendix B.
1.
The cumulative population man-rem exposure and man-thyroid-rem exposure should be determined for each effluent re'e:se source, e.g., liquid radwaste releases, ventilation releases, etc.
2.
Potential reductions to the cun.dlative population exposure should be determined based on the addition of items of reasonably demonstrated technology which have the potential to reduce releases of radioactive materials.
3.
Acceptable methods for performing some of the calculations need for items 1 and 2 above are contained in Regulatory Guides 1.109, " Calculation of Annual Doses to Man from Routine Releases of Reacter Effluents for the Purpose of Evaluating Compliance with 10 CFR Part 50, Appendix I,'
and 1.111 "Mothodt for F%timating Acmospheric Transport and Dispersion for Gaseous Effluents in
'outine Peleases from light-Water-Cooled Peactors," and in two regulatory guides now in prepara-tien on the subjects of (1) calculation of releases of radioactive materials in liquid and gas-eous ef fluents from light-water-cooled reactors and (2) nethods for estimating aquatic dispersion of liquid ef fluents from routine reactor releases for the purpose of implementing Appendix I.
4.
The totc! annual cost of each augment considered in item 2 above should be determined as follows:
a.
The Total Direct Co3L (IDII' (1) Obtain the direct cost of equipcent and raterials from Table A-1.
(2) Multiply the direct labor cost obtained from Table A-1 by the 6pprnpriate labor cost correction factor from Yable A-4 to obtain the corrected labor cost fur the geographical
=
4 area frsm figure A-1, in which the plant is to be built.
(3) Add the costs obtained from steps 'l) and (2) to obtain the Total Direct Cost.
b.
Obtain one appropriate Indirect Cost Factor (!CF) from Table A-5.
Determine Total Capital Cost (TCC) by using the equm' ion:
c.
Obtain the appropriate Capital Recovery Factor (CRF) from lable A-6.
Petermine the Annual Fixed Cost (AFC) by using the equation:
e.
AFC = TCC x CRF f.
ObtJin the Annual (perating Cost (AOC) and the Arnual Naintenance Cost ( AMC) from Tables A-2 and f-3.
Multi-unit sites using shared radwas'.e systems should multiply the AOC by the number of reactcrs sharing the augment.
=
g.
Determine the Total Annual Cost (TAC) by using the equation:
TAC = AFC + AOC + fMC 5.
Dete.mine the " benefit" of each augment by multiplying the dose reduction calculated in item 2 above by $1000 per man-rem and/or $1000 per man-thyroid-rem, as appropriate.
6.
The system should be augmented with any items for which the TAC from item 4.g above is G
less than the value calculated in item 5, in the order of diminishing costebenefit.
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(l) 1.110-7
TABLE A-1 DIRECT COSTS - GASEOUS RADWASTE AUGMENTS Direct Costs (1975 $1000)
Equipnen t/Ma teri al Labor Total BWR Offgas Recoribiner 553 255 808 3-ton Charcoal Adsorber 53 14 67 Desiccant Dryer 218 176 394 Charcoal Vault Refrigeration 116 38 154 Main Condenser Vacuum Pump Charcoal /HEPA Filtration System 40 8
48 Clean Steam to Turbine Glands 81 215 296 Clean Steam to Steam Valves, 24" and Larger 137 110 247 Clcan Stua tu steam valves. 2 ' '"
an1 Lcas Tia,~. 2, 183 55 238 15,000-cfm HEPA Filtration System 52(49) 16(14) 68(63) 1,000-cfm Charc.al/HEPA Filtration System 28 10 38 15.0C0-cfm Charcoal /HEPA Filtration System 97(93) 31(26) 128(119) 30,000-cfm Charcoal /HEPA Filtration System 157(152) 51(41) 208(193)
Turbine Bldg. Chilled Water HVAC System 614 374 988 3
600-ft Gas Decay Tank 33 24 57 PWR Hydrogen Recombiner 419 147 W
PhR Air Ejector Charcoal /HEPA Filtration Unit 14 10 24 Steam Generator Flash Tank Vent to Hain Condenser 19 14 33
- In cases where the equipment may be located either in the auxiliary building or the turbine building and corinon usage does not indicate a definite preference of one location or the other, cost for both locations are listed with the turbine building location cost in parenthesis.
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TABLE A-1 (Continued)
DIRECT COSTS - LIQUID RADWASTE AUGMENTS Direct Costs (1975 $1000)
Equipment / Material Labor Total 15-gpm Evaporator 386 201 587 30-gpm Evaporator 540 223 763 50-gpm Evaporator 655 231 833 Evaporator Distillate Demineralizer 36 24 60 50-gpm Demineralizer 83 29 50 100-gpm Demineralizer 64 31 95 200-gpm Demineralizer 94 35 129 400-gpm Demineralizer 102 44 146 100-gpn Precoat Filter 1re 56 164 400-gpm Precoat Filter 02 112 314 20-gpm Cartridge Filter 13 11 24 2-gpm Reverse Osmosis 100 33 138 10,000-gal Tank 55 43 98 126 270 1.110-9
TABLE A-2 ANNUAL OPERATING COSTS - GASEOUS RADWASTE AUGMENTS
_otal Operatinq Cost (1975 $1000/yr)
T 3
BWR Offgas Recombiner neg 3-ton Charcoal Adsorber 3
Desiccant Dryer 4
Charcoal Vault Refrigeration Main Condenser Vacuum Pump Charcoal /HEPA 0.4 Filtration System 24 Clean Steam to Tuibine Glands 3
Clean Steam to Steam Valves, 24" and Larger Clean Steam to Steam Valves, 2-1/2" and 3
Less Than 24" 6
15,000-cfm HEPA Filtra:4cn System 2
1,000-cfm Charcoal /HEPA Filtiction System 7
15,000-cfm Charcoal /HEPA Filtration System 9
30,000-cfm Charcoal /HEPA Filtration Sys,em 49 Turbine Bldg. Chilled Water HVAC System 3
6f 0-f t Gas Decay Tank neg 4
PWR Air Ejector Charcoal /HEPA Filtration Unit l
Steam Generator Flash Tank Vent to Main Condenser ANNUAL OPERATING COSTS - LIQUID RADWASTE AUGMENTS 50 Evaporation - PWR Dirty Waste 169 Evaporation - BWR Dirty Waste 114 Evaporation - co~*;a ute Polisher Chemical Waste 20 Evaporation - Detergent Waste 5
Demineralization - E,vaporator Distillate 15 Demineralization - BWR 2nd Waste Demineralizer in Series Operating costs are given for a single reactor. Operating costs for augments in shared i
radwaste systeras should be multiplied by the number of reactors serviced by the augment.
1.110-10 126 2 1
/
TABLEA-2(Continued)
ANNUAL OPERATING COSTS - LIQUID RADWASTE AUGMENTS Total Operating Cost (1975 $1000/yr)
Deminera112ation - PWR Clean Waste 5
Demineralization - BWR Dirty Waste 88 Demineralization - PWR Dirty Waste 18 Demineralization - PWR Turbine Bldg. Drains 95 Demineralization - PWR Steam Generator Blowdown 25 Precoat Filter - BWR Dirty Waste 53 Cartridge Filter 7
Reverse Osmosis - Detergent Waste 7
10,000-gal Tank 1
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i TABLE A-3 ANNUAL MAINTENANCE COSTS - GASEOUS RACWASTE AUGMENTS l.
p Total Maintenance Cost (1975 $1000/yr)
BWR Offgas Recombiner 20 3-ton Charcoal Adsorber neg 1
Desiccant Dryer 6
Charcoal Vault Refrigeration 3
Main Condenser Vacuum Pump Charcoal /HEPA Filtration System 1
Clean Steam to Turbine Glands 4
$(
Clean Steam to 5 team Valves, 24" and Larger 4
Clean Steam to Steam Valves, 2-1/2" and
- ~
Less Than 24" 12 15,000-cfm HEPA Filtration System 2
1,000-cfm Charccal/HEPA Filtration System 0.6 15,000-cfm Charcoal /HEPA Filtration System 9
30,000-cfm Charcoal /HEPA Filtration System 18 Turbine Bldg. Chilled Water HVAC System 20 600-ft Gas Decay Tank neg PWR Hydrogrn Recombiner 10 PWR Air Ejector Charcnal/HEPA Filtration Unit 2
Steam Generator Flash Tank Vent to Main Condenser 1
ANNUAL MAINTENANCE COSTS - LIQUID RADWASTE AUGMENTS 15-gpm Evapnrator 30 4
30-gpm Evaporator 30 50-gpm Evaporated 30 Evaporator Distillate Demineralizer 2
50-gpm Demineralizer 5
100-gpn Demineralizer 5
200-gpm Demineralizer 5
100-gpm Precoat Filter 10 400-gpm Precoat Filter 10 20-gpm Cartridge Filter 1
7-om Reverse Osmosis 9
10,000-gal Tant 1.110-12
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TABLE A-4 LABOR COST CORRECTION FACTORS FPC Gaographic Labor Lost Correction Renon factor I
1.6 1.5 Ill 1.0 IV 1.4 V
1.'
VI 1.2 VII 1.3 VIII 1.2
.. ee Appendix B. " Labor t Correction factors. "
S See figure A-1.
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fS TABLE A-5 INDIRECT COST FACTORS Type _ Radwaste System fadirect Cost Factor 1.
Single unit site, unitized radwaste system 1.75 2.
Multi-unit site, shared radwaste
- ystem 1.75 3.
Multi-unit site, unitized radwaste system
- 1. 75 + [n-1)l. 5 n
where n is the number of unitized radwaste systems at the site F
Each reactor has a separate, nonshared radwaste system.
O 1.110-14 126 2/5
TABLE A-6 CAPITAL RECOVERY FACTORS Cost of Money Capital Recovery 11 per year,1) rac tor 5
0.0651 6
0.0726 7
0.0806 8
0.0fE8 9
0.0973 10 0.1061 11 0.1150 12 0.1241 13 0.1334 14 0.1428 15 0.1523 Based on a service life of 30 years and the following equation:
- II CRF =
(1 + i)30 j O
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e APPfNDIX B BASES FOR PARAMETERS USED IN PERf0FMING COST-BENEFIT AHLYSIS This appendix contains detailed cost estimate sheets showing the methods and ptrameters used to obtain all costs associated with augments considered for the liquid and gaseaus radwaste systems. The cost estimate sheets are grouped by radwaste system types. The first sheet in each case is an equignent cost worksheet for determining direct equipnent costs. The second sheet is an operating cost worksheet. All costs are stated in terms of 1975 dollars. No attempt has been trade to project the ef fect of inflation. Variations of labor costs and productivity with site locations ar,e considered.* All costs are based on the assumption that the reactor is in the design stage and that augmentation of a radwaste system will not involve backfitting of an existing plant. Backfitting costs should be determined on a case-by-case basis.
1.
Capital Costs Capital costs are reported of grouping items by system and by plant location, which gen-erally follow the NRC (AEC) accounting system given in NUS-S31 (Ref. 1).
The direct costs considered to be applicable to radwaste systems are structures, electrical services, equipment, and instrumentatioP and controls. Spare parts and a contingency alloaance** are included in the direct costs. Total capital costs are of ained by multiplying direct costs by an indirect cost fa c tor.
2.
Direct Cost Direct costs for each augment include equipment, site labor, and site materials. Principal equirnent designs and hardware costr. were obtained from utility companies, architect-engineers, and vendors. Costs for building space, electrical services, piping, and instrumentation were e
estimated considering equipment functior. and arrangements.
Costs for electric services, piping, and instrumentation and controls were determined usin; b
Judgment to estimate equipment layout, points of intncface, and services required. The costs for equipnent and building space are consistent with MC staff recorrendations for radwaste sys-tem quality assurance, materials, and seismic design. Space requirements were determined based on manufacturcr's data or data from existing or proposed layout drawings.
3.
Labor Cost Correction Factors Labor cust adjustnent factors were developed for each of the eight FPC electric power supply a.eas showr. in Figure A-1 of Appendia A by calculating the average labor cost for selected cities (Ref. 2) in each area and adjusting this cost for estimated variations in labor productivity dae only to differences in labor practices in the reqions considered. Manpower costs were calcu-lated by multiplying the estimated labor requirements in nar.-hours by the composite wage rate (Ref. 3).
The calculated labor cost correction factors are tabulated in Table A-4 of Apendix A.
4 Indirect Cost Factor Indirect costs as a percentage of direct costs are calculated in Table B-1.
.g_
= _ _ _
location ef fects of the eight FPC foner Supply areas are estimated and snown in Table A-4 of Appendix A.
se Contingency onsite labor and process equipment and naterial are all based on 10:
8 126 278 1.110-17 I
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TAP 1E B-1 fhDIRfCT COSTS ist Unit.
Subsequent Percentage of Units, Percertage Direct Cost of Direct Cost Construction facilities, e<pipment, and services 10 5
Engineering and construction management services 20 10 Other owner's costs 10 5
e Interest during construction 35 35 Total 75 55
' Based on a 101/yr interest rate and a 4-year construction time for radwaste systems only.
Interest during constnaction is estimated to be 25% of direct costs plus other indirect costs. This is equivalent to 35% of the direct costs.
The indirect escalators (factors) were estimated from preliminary architect / engineering data to be used to update the ORML conce?t and ORCOST computer codes.
5.
Operation And Maintenance Costs Annual expenses for_cperation and maintenance (03M) of the radwaste treatment systems were estimated for baseload power plants operating at 801 capacity factor. k npower and supply costs were estimated by considering equipment functions in each case. Expenses for gases, steam, resins, at.x111a y power, and other supplies and services were assessed individually. m intenance costs wre evaluated accoMing to the type of service for which the equiprent could be used.
Operating costs include estimate ( manpower costs, costs of utilities and oplies, and effects on supporting plant systems interfaciag with the augmented radwaste systa ~ '.g., effect of an evaporator augment on the solid waste system). Also included are costs of sandling wastes such as spent resins, demineralizer regeneraas, evaporator bottoms, and filter media, as well as offsite handling, transMrtation, and burial costs.
6.
Capital Recovery Factor The capital recovery factor is a levelized annual charge which takes into account the cost of borrowed money and the depreciation of assets. It is calculated from the expression:
1(1 + 1)"
(1 + 1)'-1 k re i = cost of borrowed money expressed as a decimal n = plant operating Ilfetime (yr)
In calculating the values used in Table A-5 of Appendix A, a plant operating Ilfetin* of 30 years was used.
The capital recuvery factor multiplied by the total capital cost will give the annual dollar charges for capital and capital-related expenses.
1.110-18 26 279
LIST OF APPENDIX B COST ESTIMATE SHEETS Page Ntsnber BWR Offgas Recombiner.
1.110-20 3-ton Charcos1 Adsorber.
1.110-22 Desiccant Dryer..
1.110-24 Charcoal Vaalt Ref rigeration.
1.110-26 Charcoal /HEPA Filtration System - Condenser Vacuum Pump.
1.110-28 Clean Steam to Turtine Glands....
1.110-30 Clean Steam to Steam Yalves 24" and Larger...
1.110-32 Clean Steam to Steam Valves 2-1/2" and Less Than 24"..
1.110-34
- 5.000-cfm HEPA Filtration System.
1.110-36 1000-cfm Charcoal /HEPA Filtrati M System.
1.110-39 15.000-cfm Charcoal /HEPA Filtration System............
1.110-41 30.000-cfm Charcoal /HEPA Filtration System.......
1.110-44 Turtine Building Chilled Water HVAC System...
1.110-47 600-ft Ga s Decay Tank......
1.110-49 PWR Hydrogen Recombiner.........
1.110-51 PWR Air Ejector Charcoal /HEPA Filtration Unit.
1.110-53 Steam Generator Flash Tank Vent to Main Condenser..
1.110-55 Eva pora tors..........
1.110-57 Evaporator Distillate Deatneralizer.
1.110-64 Deminerali'ers..
1.110-66 Cartridge Filter....
1.110-76 Precoat Filters.
1.110-78 Reverse 0imosis...........
1.110-81 10.000-gal Tank........
1.110-83
}9b
[. h-cv 1.110-19
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS Description of Augment BWRbffgasRecombiner(Sheet 1)
DIRECT COST.(1975 $1000)
BASIS FOR ITEM LABOR EQU_IPMENT/ MATERIALS TOTAL COST ESTIMATE l.
PROCrSS EQUIPMENT 90 260 350 single unit, catalytic type w/ heater and condenser, w/o instrumentation and controls, stainless steel, ASME VIII 3
2.
BUILDING ASSIGNMENT 100 50 150 30' x 40' x 25' @ $5/ft (turbine building shielded area)
=
3.
ASSOCIATED PIP!NFi SYSTEMS 18 12 30 augment piping connections only 4.
INSTRUMENTATION AND CONTROLS 24 96 120 allowance 5.
ELECTRICAL SERVICE neg 4kw heaters on vessels neglected 6.
SPARE PARTS 85 85 75K for catalyst + 2% E/M in items 1 & 4 above SUBTOTAL 232 503 735 7.
CONTINGENCY 23 50 73 10%
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TOTAL DIRECT COSTS 255 553 808 N
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ANNUAL 0?ERATING AND MA!NTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS Description of Augrent BWR Offgas Recombiner (Sheet 2)
COST (1975 $1000)
ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE f
1.
OPERATING LABOR. SUPFRVISION, 3.3 15 min / shift AND OVERHEAD 2.
MAINTENANCE MATERIAL AND 20.0 routine conditioning of catalyst and LABOR equipment upkeep; ST, of E/M including I&C 3.
CONSUMASLES. CHEMICALS. AND in item 2 y
SUPPLIES 2
4 UTILITIES AN} SERVICES Waste Disposal Water Steam neg intemittent; 4kw heater load is negligible Electricity Building Services Other 5.
TOTAL 0 AND M ANNUAL COST 23.3 GS N
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TOTAL DIRECT COST ESTIMATE SHE Q OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER COOLED NUCLEAR REAITORS Description of Augment 3-ton Charcoal Adsorber (Sheet 1)
DIC P COST (1975 $10ro)
BASIS FOR ITEM LABOR EQUIPMENT /Me.TERIALS TOTAL COST ESTIMATE 3
1.
PROCES$ EQUIPMENT 5
44.0 49.0 carbon steel 350 psig, 200 ft volume (augment to existing train of beds) 2.
BUILDING ASSIGNMENT 8
4.5 12.5 10' x 10' x 25' @ $5/ft3 (turbine building shielded area)
[
3.
ASSOCIAiED PIPING SYSTEMS in item 1 E.
U 4.
INSTRUMENTATION AND CONTROLS neg 5.
ELECTRICAL SERVICE neg 6
SPARE PARTS none existing SUBTOTAL 13 48.5 61.5 7.
CONTINGENCY l
5.0 6.0 10%
8.
TOTAL DIRECT COST $
14 53.5 67.5 N
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ANNUAL OPERAi!NG AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEN FOR LIGHT-WATER-COOLED NUC'. EAR REACTORS Description of Augment Charcoal Vault Refrigeration (Sheet 2)
COST (1975$1000)
ITEM LABOR OTHER TOTAL BAS!$ FOR COST ESTIMATE 1.
OPERATING LABOR SUPERVISION, 3.3 15 min / shift AND OVERHEAD 2.
MAINTENANCE MATERIAL AND LABOR 3.7 5% of equipment P
3.
CONSUMABLES, CHEMICALS, AND in it 2
O SUPPLIES
~
4.
UTILITIES AND SERVICES Waste Disposal Water Steam 0.5 electricity and cooling water Electricity Building Ser<.es Other 5.
TOTAL 0 AND M ANNUAL COST 7.5 CN N
CD GO
. \\.. '. ;e e...'
[l,,'...;,,.....,:..
_,j
.:3 -
. ",.h~..L'
.' 4,f* c TOTAL DIRECT COST ESTIMATE SHEET OF RACWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTCRS Description of Augment Char; cal /H'PA Filtration System - Condenser Vacuum Pumo (Sheet 1)
DIDECT COST (1975 $1000)
BASIS FOR ITEM LABC EQUIPMENT / MATERIALS TOTAL COST ESTIMATE l.
PROCESS EQUIPMENT 2
32.5 34.5 2000 CFM prefilter/4" charcoal bed /HEPA @ $15/cfm, 10 kw heater @ $250/kw 2.
BUILDING ASSIGNMENT 3.1 1.5 4.6 Turbine buildi,ig 8' x 16' x 12'
@ $3/ft3 (nonshielded area) 3.
ASSOCIATED PIPING SYSTEMS 1.3 0.7 2.0 allowance El 4
INSTRUMENTATION AND CONTROLS in item 1 5.
ELECTRICAL SERVICE 1
1.5 2.5 6.
SPARE PARTS 0.5 0.5 SUBTOTAL 7.4 36.7 44.1 7.
CONTINGENCY
.7 3.7 4.4 10%
N 8.
TOTAL DIRECT COSTS 8.1 40.4 48.5 h
CO W
e w
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET CF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTCRS Description of Augment __, Charcoal /HIPA Filtration System - Conden(er Vecuum Pump (5heet 2)
COST (1975 $1000)
ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1.
JPERATING LABOR, SUPERVISION, neg used only during startup and shutdown AND OVERHEAD 2.
MAINTENANCE MATERIAL AND 1.2 4 HEPA filters @ $150 & 2 Charcoal filters LABOR
@ $900, change every 2 years 3.
CONSUMABLES, LHEMICALS, AND in items 2 ana 4
{}
SUPPLIES 4.
UTILITIES AND SERVICES Waste Disposal 0.2
$50/HEPA filter, 5100/ Charcoal filter Water Steam Electricity Building Services Other S.
TOTAL C AF1 M ANNUAL COST 1.4 s
N
~D CD
l-
- .N :..
.I L
.s.
e TOTAL DIRECT COST FSTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS Cescription of Aug-ent Clean Steam to Turbine Glands (Sheet 1)
DIRECT COST (1975 51000)
BASIS FOR ITEM LABOR EQUIPMENT / MAT ERI ALS TOTAL COST ESTIMATE 1.
PROCESS EQUIPMENT 15 150 165 C",000 lb/hr rebo11er 9 $4/lb/hr &
$25K/H.P. turbine glands 3
2.
BUILDING ASSIGNMENT 19 10 29 20' x 30' x 16' 3 $3/ft i
=
3.
ASSOCIATED PIPIN'a SYSTEMS 32 18 50 equiv 1000 ft'@ $50/ft
?
8 4.
INSTRUMENTATION AND CONTROLS 8
12 20 in addition to iten 1 5.
ELECTRICAL SERVICE neg l
6.
SPARE PARTS 5
5 SUBTOTAL 74 195 269 7.
CONTINGENCY 7
20 27 10%
N 8.
TOTAL JIRECT COSTS 81 215 296 CN N
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TOTAL DIRLCT COST EST! MATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS Cescription of Augment 1000-c'n Charcoal /HEPA Filtration System (Sheet 1)
DIRECT COST (1975 $1000)
BASIS FOR ITEM LABOR EQUIPMENT / MATERIALS TOTAL COST ESTIMATE l.
PROCESS EQUIPMENT 2.0 22.0 24.0 prefilter/4" charcoal /HEPA 0 $20/cfm, 5 kw htr @ $400/kw 2.
BUILDING A55IGNMENT 3.8 2.0 5.8 8'x 12' x 12' O $5/ft 3 (nonshielded area) 3.
ASSOCIATED PIPING SYSTEMS 1.3
.7 2.0 o
i i
h4 INSTRUMES{TATION AND CONTROLS i-item 1 5.
ELECTRICAL SERVICE 1.5 1.0 2.5 6.
SPARE PARTS C.5 0.5
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SUBTOTAL 8.6 26.2 34.8 P
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CONTINGENCY 1.0 2.0 3.0 10" 8.
TOTAL DIRECT C1STS 9.6 23.2 37.8 c>
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3 4
5
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U'
u ANNUAL OPERATING AND MAINTENANCE COST ES'IMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LICiHT-WATER-COOLED NUCLEAR REACTORS Description of Auge nt J 5,000-cfm Charcoal /HEPA Filtration System (Sheet 3)
COST (1975 $1000)
ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1.
OPERATING LABOR. SUPERVISION, 3.8 15 min / shift & 40-hr annual test AND DVERHEAD 2.
MAINTENANCE MATERIAL AND 9.0 30 HEPA or prefilters @ $150 er.h & 5 LABOR charcoal filters J $900 each e try 2 yrs 3.
CONSUMABLES, CHEMICALS, AND C
SUPPLIES in items 2 and 4
?
O 4.
UTILITIES AND SERVICES Waste Disposal 1.5
$50/HEPA or prefilter, $100/ charcoal Water Steam
^
Electricity 1.3 8kw additional fin power for filter t,P Building Services
@ 0.018 $/kw-hr L,
Other C
"~ 3.
TOTAL 0 AND M ANNUAL COST 15.6
. ' _ A 5 _. ' $..
... 'k-'..
. '..x,1 :.
C.'
- .. ) ?t '. e 1,,.b. : [
~ '
- I e
'. ~... ' " !." ; R V ^
., L.. '.?"1..
.,q:
- , :l. ;$ -i a...,
..5~.
.._.l' 'i
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^
5,
TOTAL DIRECT COST ESTIMATE SHEFT OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS Description of hugment 30,000-cfm Charcoal /HEPA Filtration System - Auxiliary Building (Sheet 1)
DIRECT COST (1975 $1000)
BASIS FOR ITEM
_ LABOR EQUIPMENT / MATERIALS TOTAL COST EST! MATE 1.
PROCESS EQUIPMENT 15 117.0 132.0 prefilter/4" charcoal /HEPA
@ $4/cfm, 60-kw htr @ $200/kw 3
2.
BUILOING ASSIGNMENT 20 13.6 33.6 28' x 20' x 12' @ $5/ft (nonshielded area) h 3.
ASSOCIATED PIPING SYSTEMS 5
-3.0 8.0 t,a se
?.
4.
INSTRUMENTATION AND CONTROLS in item 1 5.
ELECTRICAL SERVICE 6
4.0 0.C allowance 6.
SPARE PARTS 5.0 5.0 4 elements m -h type SUBTOTAL 46 e42.6
'P8.o 7.
CONTINGEN Y 5
14.0 19.0 10%
8.
TOTAL DIRECT COSTS 51 156.o 207.6 a
m CN Lea L.Tl O
?
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m ANN'JAL OPERATING A.NO MAINTENANCE COST ESTIMATE SHEET OF RA0 WASTE TREATMENT SYSTEM FOR LICHT-WATER-COOLED NUCLEAR REACTORS Description of Augm.at 30,000-cfr Crarcoal/HEPA Filtration System - (Sheet 3)
COST (1975 $1000)
ITEM LAEOR OTHER TOTAL BASIS FOR CCST ESTIWATE i
i 1.
OPERATING LABOR, SUPERVISION.
3.8 15 min / shift + 40 he ancJal test AND OVERHEAD 3
2.
MAINTENANCE MATERIAL AND l
18.0 60 HEPA or prefilte-s 9 $150 each & 30 LASCR charcoal filtera 0 $90C each every 2 yrs
~
3.
CONSUMABLES, CHEMICALS, AND in items 2 c-1 4 StoPL I ES
?
?
i UTILITIES A 4D SERVICES Waste Disp' sal 3.0
$50/HEPA or prefilter, $100/ charcoal filter Water Steam Electricity l
2.6 16kw additional fan HP for filter @
C.018 $/kw '.c Suilding Services l
Other l
S.
T0fAL0ANDMANNOALCOST 27.3 N
Ch us CD
~j O
O
,,n~
~.
~
TOTAL DIRECT COST ESTIMATE SHEET CF RA0 WASTE TQEATWENT SYSTE" FCR LISwT-WATER COOLED NUCLEAR REACTr:S Cescription of Augment Turbire Suilding Chilled Water HVAC System (Sheet 1)
DIRECT COST (1975.51000)
BASIS FCR ITEM LABOR EQUIFMENT/"ATERIALS TOTAL.
COST ESTIM TE 1.
PROCESS EQ'JIF"ENT 300 500 800 500-ten capacity, w/o air filters 2.
BUILDING ASSIGN"ENT Ccolers can te installed in 1
existing space saved by I
l deletion of dacting.
3.
ASSOCIATEDPIPINGSYSTEwj in item 1 0
4 INSTRUuENTATION AND CCNTROLS l
in item 1 5.
ELECTRICAL SERVICE 4 -
50 90 6.
SPARE PARTS C
8 1% item 1 s
N SUBTOTAL 340 5...
l l
893 L-J 7.
CCNTINGENCY 34 56 90 10%
CD CO8.
TOTAL DIRECT COSTS 374 614 983
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ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS 3
Description of Augment 600-ft Waste Gas Decay Tank (Sheet 2)
COST (1975 $1000)
! TEM LABOR OTHER TOTAL BASIS FOR COST EST!wATE 1.
OPERATING LABOR, SUPERVISION, I
AND DVERHEAD neg 2.
MAINTENANCE MATERIAL AND LABOR neg 3.
CONSv..,JLES, CHEMICALS, AND C
SUPPLIES neg
?
8 4.
UTILITIES AND SERVICES Waste Disposal Water Steam neg Elect-icity Suilding Services s 1er 5.
TOTAL 0 AND M ANNUAL COST reg CN Gra
-ase-4 O
O O
e py t
C 3
c&
t i!I f
t I
/
yl I 6
T l aV 5
A ai M
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ANNUAL OPtRATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FORJ IGHT-LATER-COOLED NUCLEAR REACTORS Description of AJg ent PWR Hydrogen Reconbiner p heet 2)
COST (1975 $1000)
IfEM L f.B OR OTHER TOTAL BASIS FOR COST ESTIMATE 1.
CPERATING LABOR, SUPERVISION, 3.3 15 min / shift AND OVERHEs0 2.
MAINTENANCE MATERIAL AND 10.0 3% of equipment cost LASOR 3
3.
CONSUMASLES, CHEMICALS, AND 1.0 oxygen 0 $2.5/10 cf &.25 cfm @
SUPPLIES 7000 hrs c$
n 4.
UTILITIES AND SERVICES Waste Disposal Water Steaal neg Electricity Building Services Other l
E.
TOTAL 0 AND M ANNUAL COST 14.3 i
a CN 04 O
O g;
_;9g-;.yaq3 9.g..
- ;.
- .; q
9 TOTAL DIRECT COST EST! MATE SHEET ']F RADWASTE TREATWENT SYSTEM FOR LIGHT-WATER-COCLED NUCLEAR REACTORS Cescription of Augnent PW" Air Ejector Charcoal /HEPA Filt ation Unit (5'ieet 1)
DIRECT COST (1975 51000)
BASIS FOR ITIM LASCR EQUIPMENT / MATERIALS TOTAL COST ESTI%"
1 PROCESS EQUIPMENT 3.0 7.5 10.5 chiller, heater, charcoal HEPA 3
2.
BUILDING ASSIGNMENT 3.0 1.5 4.5 10' x 10' x
'5' 9 $3/ft (unshielded turbim bld))
3.
ASSOCIATED PIPING SYSTEMS 2.0 1.0 3.0 allowance 4.
INSTHUMENTATION AND CCNTEOLS 0.5 1.5 2.0 allc*ance 5.
ELECTRICAL SERVICE 0.5 d.E 1.0 allowance o.
SPARE PARTS 1.0 i.0 N
~
O SI'ST0TAL 9.]
13.0 22.0 7.
CONTINGENC) 1.0 1.0 2.0 10%
- 2 -
L.
TOTAL DIRECT COSTS 10.0 14.0 24.0 i
ANNUAL OPEPATING AND K%INTENANCE COST ESTIMATE SHEE' 0F RADWASTE TREATwENT S QTEM FOR LIGHT-WATER-C00fID N'JClEAR FIACTORS Description of Augment PWR Air Ejector Charcoal /HEPA Filtration Unit (Sheet ?_)._
COST (1975 $1000)
ITEM LABOR OTHER TOTAL BASIS FOR COET EST! MATE 1.
OPERATING LAEOR SUPERVISION.
3.8 15 min / shift + 40 hr annual test AND OVERHEAD 2.
MAINTENANCE MATERIAL AND 2.0 includes replacement filter LABOR 3.
CONSUMABLES, CHEMICALS, AND in item 2 3
SUPPLIES 9
i 4
UTILITIES AND SERVICES l
Waste Disposal
)
neig Water Steam Electricity Building Services Other i
~
S.
TOTAL 0 AND M AN'WAL CCST I
S.8 I
m CN L-4 O
O y.ryg 33
.c
_;.y _,;., m
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEE FOR LIGHT-WATER-COOLED NUCLEAR REACTORS Description of Augment Steam Generator Flash Tank Vent to Main Condenser (Sheet ll DIRECT COST (1975 $1000)
BASIS FOR ITEM LABOR EQUIPMENT / MATERIALS TOTAL COST EST! MATE 1.
PROCESS EQUIPMENT no equipment reeuired 2.
BUILDING ASSIGNMENT neg install in existing scate 3.
ASSOCIATED PIPING SYSTEMS 13 7
20 200 f t of 10-in pipe with 2 valves P
4.
INSTRUMENTATION AfiD CONTROLS 4
6 10 allowance 5.
ELECTRICAL SERVICE neS 6.
SPARE PARTS neg SUBTOTAu 17 13
?O J.
CONTINGENCY 2
1 3
10%
N m"8.
TOTAL DIRECT COSTS 19 14 33 t;4
'.J
--..[ '
' y. 5 ' J' '
[
ANNUAL OPERATE AND MAINTENANCE CCST ESTIKATE SHEET OF RA0 WASTE TREATMENT S(STt'M FOR LICHT-WATER-CODLED NUCLEAR REACTCRS Cescription of Augment Steam f;ererator Flash Tank Ver.t to Main Condenser (Sheet 2)
COST (1975 $1000)
ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1.
OPERATING LABOR, SUPERVISION, I
alle=ance AND OVERHEAD 2.
MAINTENANCE MATERIAL AND 1
2% Total Direct Cost LABOR
[
3.
CONSUMABLE 5, CHEMICALS, AND neg g
SUPPLIES m
4.
UTILITIES AND SERVICES Waste Disposal Water neg Steam Electricity Building Services Other 5.
TOTAL 0 AND M ANNUAL COST 2
Ch LeJ*
O O
O TOTAL DIRECT COST ESTIMATF SHEET CF RA0 WASTE TREATWENT SYSTEM FOR LICHT-WATER-COOLED NUCLEAR REACTORS Description of Augment 15-qpm Evaporator (Sheet 1)
DIRECT COST (1975 51000)
BASIS FOR ITEM LABOR EQUIFMENT/ MATERIALS TO T A'.
COST ESTIMATE 1.
PRGCESS EQUIPMENT 30 225 255 skid mounted, subnerged tube bundle, ASME VIII, Incolay in contact with process fluid 2.
BUILDING ASSIGNMENT 68 3'
102 evap & services 25' x 30' x 20' 3
3
@ $6/ft plus 2,000 ft increase in solid waste storage area 3.
ASSOCIATED PIPING SYSTEMS 35 30 65 inludes ervice piping
?
4.
INSTRUMENTATION AND CONTROLS 10 10 20 allowance 5.
ELECTRICAL SERVICE 40 25 65 allowance 6.
SPARE PARTS 27 27 2% of item 1 plus tube bundle SUBTOML183351534 N
7.
CONTINGENCY 18 35 53 10 by
-* 8.
TOTAL DIRECT COSTS 201 386 587 03 t
TOTAL DIRECT COST ESTIMATE SHEET OF RnDWASTE TREATMENT SYSTEM FOR LICHT-WATER-COOLED NUCLEAR REACTORS Description of Augment 30-qpm Evaporator (Sheet 2)
DIRECT COST (1975 $1000)
BASIS FCR ITEM LABUR EQUIPMENT / MATERIALS TOTAL COST ESTIUTE 1.
PROCESS EQUIPMENT 30 350 380 ASME VIII skid mounted, submerged, tube bundle, Incolay in contact with process fluid evap + senices - 25' x 40' x 20' 2.
BUILDING ASSIGNMcNT 88 44 132 3
3 9 56/ft plus 2.000 ft increase in solid waste storage area 3.
ASSOCIATrD PIPING SYSTEMS 35 35 70 includes service piping
?
4.
INSTRUMENTATION AND CONTROLS 10 10 20 allowance 5.
ELE'TRICAL SERVICE 40 25 65 allowanr.c 6.
SPARE PARTS 27 27 2% or item 1 plus tube bundle SUBTOTA'.
203 491 694 7.
CONTINGENCY 20 49 6) 10%
8.
TOTAL DIRECT COSTS 223 540 763 CN DJ O
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ANNUAL OPEPATING AND MAINTENANCE COST ESTIMATE SHEET OF RA? WASTE TREATWENT SYSTEM FOR LIGHT-WATER-COOLED v CLEAR REACTORS s
Description or Augment Evaporator - BWR Dirty Waste - Floor Cra;rs (Sheet 4)
COST (1975 51000)
ITEM LABOR OTHER TOTAL BASIS FOR COST ESTI" ATE 6
l.
OPERATING LABOR, SUPERVISION, 12 2.6 x 10 g y; 1000 hrs /yr labor AND CVERHEAD T
2.
MAINTEMNCE MATERIAL AND 30 7-1/2t of equipment cost LABOR I
reg concentrate solidification chemicals
[
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'ONSUMABLF S, CHEMICALS, AND f
in item 4 PPLIES
?
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L.
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UTILITIES AND SERVICES l
CD:1 feed to concentrate ratio 9 20/ft Waste Disposal 70 oisposal cost Water 27 1000 gpm @ 1500 hrs @ 30?/1000 gal Steam 60 1500 brs stea.1 3 20,000 lb'hr 3 $2/1000 lbs Electricity Building Services Othe r
.a l
199 S.
TOTAL 0 AND M ANNUAL COST i
C3 CA N
O 9
9 ANYJAL CFERATING AND MAINTEN%CE CCST ESTI* ATE SHEET CF RA0 WASTE TREAT _wEM SYSTES FOR LIGHT-WATER-CCOLED NUCLEAR REACTORS Descriptien of Augment Evaporator PWR Dirty Waste (Sheet 51 CCST (1975 11000)
ITEM LABOR OTHER TOTAL BASIS FCR COST ESTIwATE i
i 1.
CP[ RATING LABOR, SUPERVISION, I
l AND OVERHEAD j
j 6.n E00,C00 g;y; 500 hrs /yr lator l=
i i
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MAINTENANCE MA'ERIAL AND l
LABOR 30.0 7-1/2* of egai; rent cost
[
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4.
UTILITIES AND SERVICES 3
a}g:1feedtoconcentrateratio3$20/ft Waste Disposal 27 0 scosal cost Water 5.0 1000 gpm 3 277 hrs 9 300/1C00 gal Steam 12.0 277 Frs steam 9 20,000 lbs/Pr ? $2/1000 lbs Electricity Building Services l
Other i
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5.
TOTAL 0 AND b' ANNUAL COST S0.0 i
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ANNUAL 0?ERATING AND KAINTENANCE COST ESTIMATE SWEET OF RA7 WASTE TREATMENT SYSTEM FCR LIGHT-WATER-CCOLED NUCLEAR REACTORS Description of Augment Evaporator - Cetercent Waste (Sheet 7)
COST (1975 $1000)
ITEM LABOR OTWER TOTAL BASIS FOR COST ESTIMATE 1.
OPERATING LABOR. SUPERVISION, AND OVERHEAD 6.0 160,000 gpy; 500 hrs /yr 2.
MAINTENANCE MA,6 RIAL AND LABOR 30.0 7-1/2% of equipment cost 3.
CONSUMABLES, CHEMICALS, AND i:
SUPPLIES concentrate solidification chemicals in item 4
?m t,
UTILITIES AND SERVICES 3
Waste Disposal 8.6 50:1 feed to concentrate ratio 3 $20/ft disposal cost Water 1.6 1000 gpn 3 90 hrs 3 30t/1000 gal Steam 3.6 90 hrs steam 9 20,000 lb/hr 3 $2/1000 lbs Electricity Building Services Other rd c;ps 5.
TOTAL 0 AND M ANNUAL COST 49,8 Gra N
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ANNUAL OPERATING AND MAINTENANCE COST ESTI6/_TE. < 'ET CF PA WASTE TREAT *ENT SYSTEM FOR LIGHT-WATER-COOLED NUCtEAR REACTORS Description of Augnent Evaporator Distillate Demineralizer (Sheet 2)
COST (1975 51000)
ITEM LABOR OTHER TOTAL BASIS FCR COST ESTIMATE 1.
OPERATING LABOR. SUPERVISION, 1.8 1500 hrs operatien @ 10% attendance AND OVERHEAD 2.
MAIN ENANCE MATERIAL AND LAP.]R 2.0 allowance
~
3.
C0f:SUMABLES, CHEMICALS, AND 3
jj SUPPLIES 2.3 1 change per yr 0 $75/fL g
4.
UTILITIES AND SERVICES 3
3 Waste Disposai 0.6 30 ft a $20/ft disposal cost Water Steam Electricity Building Services Other t.
TOTAL 0 AND M ANNUAL COST 67 l
= ~ -
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DIRECT COST (1975 $1000)
BASIS FOR IT;M LABOR EQUIPufNT/WATERIALS 7TAL COST EST!w. ATE 3
1 PROCESS EQUIPMENT 5
35.0 40.0 50 ft. 55. ASME VI!!. 150 psi.
nonregenerative, with resin 3
2.
BUILDING ASSIGNMENT 9
4.8 13.8 12' x 12' x 16' 9 $6/ft (shielded area) 3.
ASSOCIATED PIPING SYSTEMS 13 10.0 20.0 2-1/2" pipina O
P 4.
INST >:cMENTATION AND CONTROLS 4
6.0 10.0 5.
ELECTRICAL SERVICE neg 6.
SPARE PARTS 2.0 2.0 miscellaneous supplies SUBTOTAL 28 1
57.8 85.6 7.
CONTINGENCf 3
6.0 9.0 m
8.
TOTAL DIRECT COSTS 31 63.8 94.8 m
N Co
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TOTAL DIRECT COST EST!4 ATE SHEET OF PA0 WASTE TPEATuENT SYSTEM F OR t IGHT 'WAT_E, r00 LED NUCLEAR REACTORS E
Cescription of Augment _ 200-grn Demineralizer (Sheet 3)
DIPECT COST (1975 $1000)
BASIS FOR ITEM LASOR EQUIPMENT / MATERIALS TOTAL COST EST!* ATE 1.
PROCESS EQUIPMENT 5
60.0 65.0 120 ft, f,S, ASME VIII, 150 psi, 3
nenrecenerative, with resin 2.
BUILDING ASSIGNvCNT 11 5.2 16.2 13' x 13' x 16' 0 16/ft 3
(shielded area) 3.
ASSOCIATED PIPING SYSTEMS 12 12.0 24.0 4" piping 5
? 4 INSTRUMENTATION AND CONTROLS 4
6.0 10.0 5.
ELECTRICAL SERVICE ncg 6.
SPARE PARTS 2.0 2.0 miscellaneous supplies SUBTOTAL 32 65.2 117.2 7.
CONTINGENCY 3
9.0 12.0 8.
TOTAL CIRECT COSTS 35 94.2 129.2 D
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1.110-69
-. 9 2 6 v.,- J J'
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ANNUAL CPERATING AND MAINTENANCE CCST ESTIMATE SWEET CF RADWASTE TREATwENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTCRS Cescription of Aug-ent BWR - 2nd Waste De-ineralizer In Series (Skeet 5)
COST (1975 $1000)
ITEM LABOR OTHER TOTAL BASIS FCR COST ESTIMATE 1.
CPERATING LABOR, StiPERVISICN, 3.3 15 min / shift AND OVERHEAD 2.
MAINTENANCE MATERIAL AND LABOR 5.0 allowance 3
[
3.
CONSUMA2LES, CHEMICALS, AND 9.u 1 chance per year 9120 ft 3 $75/ft3 (one g
SUPPLIES vessel cnance per year, regardless of size) b 4.
UTILI'IES AND SERVICES 3
Waste Disposal 2.4 120 ft /yr 3 $20!ft disposal cost Water Steam Electricity Building Services N
Other CN i
L-;
5.
TOTAL 0 AND M ANNUAL COST l
19.7 04 9
9
.; x g= 4 ; s
...g. _;..... ;. -
y _ -
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.. '_ ;.n
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e a
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ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET CF RACWt.STE TREATMENT SYSTEM FOR LIGHT-WATER-CCOLED NUCLEAR REACTCRS Description of Augment Demineralizer - PWR Clean Wastes (Sheet 6)
COST (1975.$1000)
ITEM LABCR OTWER TOT 3L BASIS FCR CCST ESTIMATE 1.
OPERATING LABOR. SUPERVISION.
1.8 1C% cf SRS shim bleed (50,000 gpy),
AND OVERHEAD 30 min / day 2.
MAINTENANCE /ATERIAL AND LABOR 5.0 allowance 3.,
CONSUr 3LES, CHEMICALS, AND
~
SUPPLIES 2.3 30 ft /yr 3 $75/ft 3
3
?5 4.
UT!i! TIES AND SERVICES 3
3 Waste Disposal 0.6 30 ft /yr 3 $20/ft disposal cost Water Steam Electricity Building Services i
I Other t
t 5.
TCTAL 0 A C M AMNUAL COST 9.7 a
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ANNUAL OPERATING AND MAINTENANCE COST ESTIwATE SHEf_T OF ECa'ASTE TREATMENT _
SYSTEM FOR LIGHT-WATER-COOLED NJCLEAR REACTORS neralizer - BWR Dirty Waste (Sheet 7)
Description of Augment tev COST (1975 51C00)
ITEM LABOR OTHER TOTAL AASIS FOR COST EST!v. ATE I
1.
OPERATING Lt30R, SUPERVISION, 6
AND OVERHEA0 6.5 2.6 x 10 gpy, 30 min / shift 2.
MAINTENANCE MATERIAL AND LABOR 5.0 allowance 3.
CONSUMABLCS, CHEMICA S AND 3
3 SUPPLIES 64.5 850 ft resin 9 $75/ft 8
D 4.
UTItITIES AND SERVICES Waste Disposal 17.2 860 ft3 @ $20/ft3 disposal cost Water Steam Electricity Building Services Other-5, TOTAL 0 AND M ANNUAL COST 93.2 I
GS era k)N trl 9
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COST (1975$1000)
ITEM LABOR OTHER TOTAL BASIS FCR COST ESTIMATE 1
OPERATING LABOR. SUPERVISIOM' 6
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ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA*ER-COOLED NUCLEAR REACTORS Description of Augment Demineralizar - PWR Steam Generator Blowdown (Sheet 10)
COST (1975 $1000)
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COST (1975 $1000)
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1.
OPERATIN1 LABOR. SUPERVISION, AND DVERHEAD 1.1 5 min / shift - log level readings 2.
MAINTENANCE MATERIAL AND LABOR 1.6 1/2% of equipment
((
3.
CONSUMABLES, o'HEMICALS, AND neg SUPPLIES 4.
UTILITIES AND SERVICES Was.e Disposal Water Steam neg Electricity Building Services Other S.
TOTAL 0 AND M ANf;UAL COST 2.7 CN
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9 REFERENCES TO APPENDIX B 1.
" Guide for Economic Evaluation of Nuclear Reactor Plant Designs," USAEC Report NUS-531, NUS Corporation, January 1969.
2.
" Wage Rates for Key Construction Trades," Engineering News 'e:Ord, pp. 36-a~7, x
January 2, 1975.
3.
" Projections of Labor Requirements for Electric Power Plants Constructinn, 1974 - 2000,"
USAEC Report WASH-1334, Washington, D.C., August 1974.
s 1.\\'D-85
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f 9
APPENDIX C DATA NEEDED FOR RADWASTE TREATMENT SYSTEM COST-BENEi!T AHALYSIS FOR L 3HT-WATER-COOLED NUCLEAR REACTORS This appendix describes informatioa that should be subnitted in support of radwaste treat-ment system cost-benefit analyses for light-water-cooled nuclear reactors. The info mation should be consistent with the contents of the Safety Analysis Report (SAR) and Environmental Report (ER) for the proposed reactor. Appropriate sections of the SAR and ER containing nare detailed discussions of the required information should be referenced as appropriate. Each response, hcweser, should be indasendent of the ER and SAR. All responses should be on a per reactor basis and should provide the following informa'. ion:
1.
Detailed cost estimate sheets similar to those shown on the following pages listing all parameters (and their bases) used in determining capital, operating, and maintenance costs associated with all augments considered in the cost-benefit analysis. All costs should be stated in terms of 1975 dollars.
2.
The cost of borrowed money used in the cost analysis and the method of arriving at this cost.
If methods and parameters 6 sed in the cost-benefit analysis are different from those aiven 3.
in this guide, describe the methods used in detail and provide bases for all parameters. Includ the following information:
Decontamination factors assigned to each augment and fraction of "on-line" time a.
assumed, i.e., hour'. per year used, b.
Parameters and method used to determine the Indirect Cost Factor and the Capital Recovery Factor.
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