Regulatory Guide 1.110

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Cost-Benefit Analysis for Radwaste Systems for Light-Water-Cooled Nuclear Power Reactors
ML003740332
Person / Time
Issue date: 03/31/1976
From:
Office of Nuclear Regulatory Research
To:
References
RG-1.110
Download: ML003740332 (87)
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U.S. NUCLEAR REGULATORY

COMMISSION

REGULATORY

GUIDE OFFICE OF STANDARDS

DEVELOPMENT

REGULATORY

GUIDE 1.110 COST-BENEFIT

ANALYSIS FOR RADWASTE S LIGHT-WATER-COOLED

NUCLEAR PDWE& CRS'March 1976 4 USNRC REGULATORY

GUIDES Commen.l shoutd be Sent to Rhe Secretary of the Comm,ssion U S Nuclea, %equietoy Guido* ate issued to describe and meeks ovelablto ,he pubic Rogulstory Comminssion Washington.

0 C 2065. Attention Docketing end methods acceptable go the NRC staff of4 impementing specific pairt of the S Commission'&

fegulatione.

to definetel technique mused by the state in evild The guides are issued in the following ten broad divisions at"ig *pecific problems or postulated accidents.

0r to provide guidance to eppli cents Regulatory Gudes am not substitutes for regulamons.

end compliance I Power Reactors 5 Products with thenm ile rot reCed Methods end soutione diflerent fron those get out i I Research end Test Reactors 7 Tronsponstion Ihe guidell we be acceptable It they provide a bahis for lthe findings requrlit to 3 Fueuls and Materiels Facilities a Occupolionat

4palt h the mesnee of -permst of Scenes by the Commitssion

4 Environmental and Siting 2 Antitrust Review Commentd Isid uggestiOi$e

  1. 0F imPtoSetfitC

it #hbae gtaldel We entcouraged S Materialt end Plant Protection

10 General ot anll. end guidss Wil be Revised. a. a41pp1rop1riete.

to accommodate corn asmon ed ho wtc intormatiotn or e*perieot Ifowoer comments on Copies of published guides may be obtained by wistten .squett indicating Cth Ofu guide. A received within Oboins two month$ chatret. issuance.

will be divisions desired to the U S Nuclear Regulators Commission Wshtington

0 C ticfady orssIul Mt evaluating the teed = of an srly viision 20566. Attention Director.

Office of Standerde Development TABLE OF CONTENTS Page

A. INTRODUCTION

.......................................................................

1.110-5

B. DISCUSSION

R

.......................................................................

1.110-5 C. REGULATORY

POSITION .........................................................

1.110-6 D. IMPLE14ENTATION

................................

..................................

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 SAMPLE ESTIMATE SHEETS ................................................................

1.110-88 1.110-3 LIST OF TABLES Table Page A-1 Direct Costs -Gaseous Radwaste Augments ................................

1.110-8 A-2 Annual Operating Costs -Gaseous Radwaste Augments;

Liquid Radwaste Augments .....................................................

1.110-10 A-3 Annual Maintenance Costs -Gaseous 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 Page A-1 Electric Power Supply Areas in the United States ........................

1.110-16 1.110-4

A. INTRODUCTION

Section I1.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 Radioactive 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 radwaste systems for light water-cooled nuclear power 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 miles of the reactor. Values of $1000 per man-rem and $1000 per man-thyroid-rem are given as interim criteria pending the development and establishment of better criteria.

Compliance with Section II.D of Appendix I to 10 CFR Part 50 (which specifically addresses doses to the population)

and Sections IL.A, 11.8, 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 Appendix I, the NRC staff has developed a series of guides providing methods acceptable to the staff for the calculation of effluent releases, dispersion of effluents in the atmosphere and different water. bodies, associated radiation doses to man, and cost-benefit aspects of treating radwastes.

This regulatory guide describes a method for performing a cost-benefit analysis for liquid and gaseous radwaste system components.

The procedures and models provided in this guide will be subject to continuing review by the staff with the aim of providing greater flexibility to the applicant in meeting the require ments of Appendix I. As a result of such reviews, it is expected that alternative acceptable methods for calculation will be made available to applicants and that calculational procedures found to be unnecessary will be eliminated.

B. DISCUSSION

Each applicant for a permit to construct or a license to operate a light-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 objectives for as low as is reasonably achievable effluent releases are satisfied by the liquid and gaseous radwaste system designs. It is the objective of this guide to provide an acceptable method 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 demonstrated technology for reducing the cumula tive population dose due to releases of radioactive materials from the reactor to levels as low as reasonably achievable.

As an interim measure the Conmnission 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 analysis.

Because the Commission has not outlined any procedures for including the effects of inflation in the analysis, the NRC staff's analysis is based on 1975 dollars; i.e., neither the costs nor the interim criteria are escalated for the predicted effects of inflation.

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 NRC staff believes this approach to be reasonable.

The NRC staff has outlined a method for performing the required cost-benefit analysis and has provided cost parameters for estimating the costs for the various radwaste treatment equip ment items in use, or proposed for use, at light-water-cooled nuclear power reactors.

The methodology 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, mainte nance, interest, and operating as well as other costs generally considered in analyzing capital and operating costs in power plant estimating.

The bases for the costs calculated by the NRC staff are given in Appendix B.1-110-5 C. REGULATORY

POSITION 1. In accordance with Section II.D, Appendix I to 10 CFR Part 50, each applicant for a permit 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 man-rem or $1000 per man-thyroid-rem (or such lesser costs as demonstrated to be suitable for a particular case). 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 should 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 estimates.

4. The method of calculation described in Appendix A and the parameters presented in Appendix B of this guide are acceptable to the NRC 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 assumptions and parameters used. Information to be submitted by the applicant Is described in Appendix C to this guide. Use of parameters, 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 staff. Because of this, these parameters and assumptions should be clearly described and substantiated by the applicant.

0. IMPLEMENTATION

The purpose of this section is to provide information to 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 Commission's regulations, the method described herein will be used in the evaluation of construction permit 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 before June 4, 1976, the pertinent portions of the application will be evaluated on the basis of this guide.1.110-6 APPENDIX A PROCEDURES

FOR PERFORMING

COST-BENEFIT

ANALYSES This 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 parameters and worksheets appropriate for use with the following cost-benefit procedure are given in Appendix B. 1. The cumulative population man-rem exposure and man-thyroid-rem exposure should be determined for each effluent release source, e.g., liquid radwaste releases, ventilation releases, etc. 2. Potential reductions to the cumulative 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 Reactor Effluents for the Purpose of Evaluating Compliance with 10 CFR Part 50, Appendix I," and 1.111, "Methods for Estimating Atmospheric Transport and Dispersion for Gaseous Effluents in Routine Releases from Light-Water-Cooled Reactors," and in two regulatory guides now in prepara tion on the subjects of (1) calculation of releases of radioactive materials In liquid and gas eous effluents from light-water-cooled reactors and (2) methods for estimating aquatic dispersion of liquid effluents from routine reactor releases for the purpose of implementing Appendix I. 4. The total annual cost of each augment considered in item 2 above should be determined as follows: a. The Total Direct Cost (TOC): (1) Obtain the direct cost of equipment and materials from Table A-1. (2) Multiply the direct labor cost obtained from Table A-1 by the appropriate labor cost correction factor from Table A-4 to obtain the corrected labor cost for the geographtcal area from Figure A-l, in which the plant is to be built. (3) Add the costs obtained from steps (1) and (2) to obtain the Total Direct Cost. b. Obtain-the appropriate Indirect Cost Factor (ICF) from Table A-S. c. Determine Total Capital Cost (TCC) by using the equation:

TCC -TDC x ICF d. Obtain the appropriate Capital Recovery Factor (CRF) from Table A-6. e. Determine the Annual Fixed Cost (AFC) by using the equation:

AFC = TCC x CRF f. Obtain the Annual Operating Cost (AOC) and the Annual Maintenance Cost (AMC) from Tables A-2 and A-3. Multi-unit sites using shared radwaste systems should multiply the AOC by the number of reactors sharing the augment.

g. Determine the Total Annual Cost (TAC) by using the equation:

TAC

  • AFC + AOC + AMC 5. Determine 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 less than the value calculated in item 5, in the order of diminishing cost-benefit.

1.110-7 TABLE A-1 DIRECT COSTS -GASEOUS RADWASTE AUGMENTS Direct- Costs (1975 $1000) Equipment/Material Labor Total BWR Offgas Recombiner

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 Clean Steam to Steam Valves, 2-1/2" and Less Than-24" 183 55 238 15,000-cfm HEPA Filtration System 52(49)* 16(14)* 68(63)* 1,000-cfm Charcoal/HEPA

Filtration System 28 10 38 15,000-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 614 374 988 600-ft 3 Gas Decay Tank 33 24 57 PWR Hydrogen Recombiner

419 147 566 PWR Air Ejector Charcoal/HEPA

Filtration Unit 14 10 24 Steam Generator Flash Tank Vent to Main Condenser

19 14 33 In cases where the equipment may be located either in the auxiliary building or the turbine building and common 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.

1.110-8 TABLE A-1 (Continued)

DIRECT COSTS -LIQUID RADWASTE AUGMENTS Direct Costs 15-gpm Evaporator

30-gpm Evaporator

50-gpm Evaporator Evaporator Distillate Demineralizer

50-gpm Demineralizer

100-gpm Demineralizer

200-gpm Deminieralizer

400-gpm Demineralizer

100-gpm Precoat Filter 400-gpw Precoat Filter 20-gpm Cartridge Filter 2-gpm Reverse Osmosis 10,000-gal Tank Equipment/Material

386 540 655 36 43 64 94 102 108 202 13 100 55 1.110-9 Labor 201 223 233 24 29 31 35 44 56 112 11 38 43 (1975 $1000) Total 587 763 888 60 50 95 129 146 164 314 24 138 98 TABLE A-2 T ANNUAL OPERATING

COSTS -GASEOUS RADWASTE AUGMENTS BWR Offgas Recoatbiner

3-ton Charcoal Adsorber Desiccant Dryer Charcoal Vault Refrigeration Main Condenser Vacuum Pump Charcoal/HEPA

Filtration System Clean Steam to Turbine Glands Clean Steam to Steam Valves, 24" and Larger Clean Steam to Steam Valves, 2-1/2" and Less Than 24" 15,000-cfm HEPA Filtration System 1,000-cfm Charcoal/HEPA

Filtration System 15,000-cfm Charcoal/HEPA

Filtration System 30,000-cfm Charcoal/HEPA

Filtration System Turbine Bldg. Chilled Water HVAC System 600-ft 3 Gas Decay Tank PWR Hydrogen Recombiner PWR Air Ejector Charcoal/HEPA

Filtration Unit Steam Generator Flash Tank Vent to Main Condenser Total Operating Cost 3 (1975 $lOOO/yr)neg 3 4 0.4 24 3 3 6 2 7 9 49 neg 4 4 1 ANNUAL OPERATING

COSTS -LIQUID RADWASTE AUGMENTS Evaporation

-PWR Dirty Waste Evaporation

-BWR Dirty Waste Evaporation

-Condensate Polisher Chemical Waste Evaporation

-Detergent Waste Demineralization

-kvaporator Distillate Demineralization

-BWR 2nd Waste Demineralizer in Series 50 169 114 20 5 15 Operating costs are given for a single reactor. Operating costs for augments in shared radwaste systems should be multiplied by the number of reactors serviced by the augment.1.110-10 K B r m m TABLE A-2 (Continued)

ANNUAL OPERATING

COSTS -LIQUID RADWASTE AUGMENTS Total Operating Cost (1975 $1000/yr)5 Demineralization

-PWR Clean Waste Demineralization

-BWR Dirty Waste Demineralization

-PWR Dirty Waste Demineralization

-PWR Turbine Bldg. Drains Desmineralization

-PWR Steam Generator Blowdown Precoat Filter -BWR Dirty Waste Cartridge Filter Reverse Osmosis -Detergent Waste 10,000-gal Tank 88 18 95 25 53 7 7 1 1.110-11 TABLE A-3 ANNUAL MAINTENANCE

COSTS- GASEOUS RADWASTE AUGMENTS Total Maintenance Cost (1975 $1O00/Yr)

BWR Offgas Recombiner

20 3-ton Charcoal Adsorber neg 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 Steam 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 Charcoal/HEPA

Filtration System 0.6 15,O00-cfm Charcoal/HEPA

Filtration System 9 30,000-cfm Charcoal/HEPA

Filtration System 18 Turbine Bldg. Chilled Water HVAC System 20 600-ft 3 Gas Decay Tank neg PWR Hydrogen "Recombiner

10 PWR Air Ejector Charcoal/HEPA

Filtration Unit 2 Steam Generator Flash Tank Vent to Main Condenser

1 ANNUAL MAINTENANCE

COSTS -LIQUID RADWASTE AUGMENTS 15-gpm Evaporator

30 30-gpm Evaporator

30 50-gpm Evaporator

30 Evaporator Distillate Demineralizer

2 50-gpm Demineral izer 5 lO0-gpmi Demineralizer

5 200-gpm Demineral izer S 100-gpm Precoat Filter 10 400-gpm Precoat Filter 10 20-gpm Cartridge Filter 1 2-gpm Reverse Osmosis g 10.000-gal Tank 2 1.110-12 TABLE A-4 LABOR COST CORRECTION

FACTORS Labor Cost Correction Factor 1.6 1.5 1.0 1.4 1.1 1.2 1.3 1.2 See Appendix B, "Labor See Figure A-1.Cost Correction Factors.'1.110-13 FPC Geographic Region I 1II IV V VI VII Vlll TABLE A-5 INDIRECT COST FACTORS Type Radwaste System "1. Single unit site, unitized radwaste system 2. Multi-unit site, shared radwaste system 3. Multi-unit site, unitized radwaste system Indirect Cost Factor 1.75 1.75 1.75 + (n-1)1.5 n where n is the number of unitized radwaste systems at the site Each reactor has a separate, nonshared radwaste system.I..1.110-14 TABLE A-6 CAPITAL RECOVERY FACTORS Cost of Honey (1 per year, i)5 6 7 8 9 10 11 12 13 14 15 Capital Recovery Factor 0.0651 0.0726 0.0806 0.0888 0.0973 0.1061 0.1150 0.1241 0.1334 0.1428 0.1523 service life of 30 years and the follwing equation:

CRF M + 1)3 (I + i)30-1 1.110-15*Based on a LEGEND ¶Im REGIONAL GROUPING OF POWER SUPPLY AREAS FIGURE A-1 ELECTRIC POWER SUPPLY AREAS IN THE UNITED STATES (C C

APPENDIX B BASES FOR PARAMETERS

USED IN PERFORMING

COST-BENEFIT

ANALYSIS This appendix contains detailed cost estimate sheets showing the methods and parameters used to obtain all costs associated with augments considered for the liquid and gaseous radwaste systems. The cost estimate sheets are grouped by radwaste system types. The first sheet in each case is an equipment cost worksheet for determining direct equipment costs. The second sheet is an operating cost worksheet.

All costs are stated in terms of 1975 dollars. No attempt has been made to project the effect of inflation.

Variations of labor costs and productivity with site locaticns are 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 backfltting of an existing plant. Backfltttng costs should be determined on a case-by-case basis. 1. Capital Costs Capital costs are reported by grouping items by system and by plant location, which gen erally follow the NRC (AEC) accounting system given in NUS-531 (Ref. 1). The direct costs considered to be applicable to radwaste systems are structures, electrical services, equipment, and instrumentation and controls.

Spare parts and a contingency allowance**

are included in the direct costs. Total capital costs are obtained by multiplying direct costs by an indirect cost factor. 2. Direct Cost Direct costs for each augment include equipment, site labor, and site materials.

Principal equipment designs and hardware costs were obtained from utility companies, architect-engineers, and vendors. Costs for building space, electrical services, piping, and instrumentation were estimated considering equipment functions and arrangements.

Costs for electric services, piping, and instrumentation and controls were determined using judgment to estimate equipment layout, points of interface, and services required.

The costs for equipment and building space are consistent with'NRC staff recommendations for radwaste sys tem quality assurance, materials, and seismic design. Space requirements were determined based on manufacturer's data or data from existing or proposed layout drawings.

3. Labor Cost Correction Factors Labor cost adjustment factors were developed for each Of the eight FPC electric power supply areas shown in Figure A-I of Appendix A by calculiting the average labor cost-for selected cities (Ref. 2) in each area and adjusting this cost for estimated variations in labor productivity due only to differences In labor practices in the regions considered.

Manpower costs were calcu lated by multiplying the estimated labor requirements in man-hours by the composite wage rate (Ref. 3). The calculated labor cost correction factors are tabulated in Table A-4 of Appendix A. 4. Indirect Cost Factor Indirect costs asa percentage of direct costs are calculated in Table B-1. Location effects of the eight FPC Power Supply areas are estimated and shown in Table A-4 of Appendix A. Contingency onsite labor and process equipment and material are all based on-l0%.1.110-17 TABLE 8-1 K..INDIRECT COSTS 1st Unit, Subsequent Percentage of Units. Percentage Direct Cost of Direct Cost Construction facilities, equiment, and services 10 5 Engineering and construction managment services 20 10 Other owner s costs 10 S Interest during construction

3S 35 Total 75 SS *Based on a lOs/yr interest rate and a 4-year construction time for radaste systems only. Interest during construction Is estimated to be 25% of direct costs plus other indirect costs. This is equivalent to 351 of the direct costs. The Indirect escalators (factors)

were estimated from preliminary architect/engineering data to be used to update the DOM concept and ORCOST computer codes. S. Operation And Maintenance Costs Annual expenses for operation and maintenance (O&N) of the radwaste treatment systes were estimated for baseload power plants operating at 801 capacity factor. Manpower and supply costs were estimated by considering equipment functions it each case. Expenses for gases, steam, resins, auxiliary por. and other supplies and services were assessed individually.

Maintenance costs were evaluated according to the type of service for which the equipment could be used. Operating costs include estimated manpower costs, costs of utilities and supplies, and effects on supporting plant systems Interfacing with the augmented radmste system (e.g., effect of an evaporator augment on the solid waste syste). Also included are costs of handling wastes such as spent resins, demineralizer regenerants, evaporator bottoms, and filter media, as well as offsite handling, transportation, and burial costs. 6. Capital Recovery Factor The capital recovery factor Is a levelized annual charge which takes into account the cost of borroved money and the depreciation of assets. It Is calculated from the expression:

I(1 #)o (I + ~where i a cost of borrowed money expressed as a decimal P -plant operating lifetime (yr) In calculating the values used in Table A-S of Appendix A. a plant operating lifetime of 30 years was used. The capital recovery factor multiplied by the total capital cost will give the annual dollar charges for capital and capital-related expenses.1.110-18 LIST OF APPENDIX B COST ESTIMATE SHEETS Page Numiber BW Offgas Recmbiner

.............................................................

1.110-20 3-ton Charcoal Adso r ...............................................................

1.110-22 Desiccant Dryer ..............................................................

1.110-24 Charcoal Vault Refrigeration

.........................................................

1.110-26 Charcoal/HEPA

Filtration System -Condenser Vacuun Pump ..............................

1.110-28 Clean Steam to Turbine Glands ........................................................

1.110-30 Clean Steam to Steam Valves 24- and Larger ...........................................

1.110-32 Clean Steam to Steam Valves 2-1/2' and Less Than 24" ................................

1.110-34 1S.000-cftm NEPA Filtration System ....................................................

1.110-36 1000-cfa Charcoal/HEPA

Filtration System .............................................

1.110-39 15.000-cfm Charcoal/HEPA

Filtration System ...........................................

1.110-41 30,000-cfm Charcoal/HEPA

Filtration System ..........................................

1.110-44 Turbine Building Chilled Mater HVAC System ...........................................

1.110-47 600-ft 3 Gas Decay Tank ...............................................................

1.110-49 PIW Hydrogen Recombiner

..............................................................

1.110-S1 PiW Air Ejector Charcoal/HEPA

Filtration Unit ........................................

1.110-53 Stem Generator Flash Tank Vent to rain Condenser

....................................

1.110-55 Evaporators

..........................................................................

1.110-57 Evaporator Distillate Demineralizer

..................................................

1.110-64 Demineralizers

.......................................................................

1.110-66 Cartridge Filter .....................................................................

1.110-76 Precoat Filters ......................................................................

.114 7R Reverse Osmosis .....................................................................

1.110-81 10.000-gal Tank ...........................................................

1.11" 1.110-19 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment ITEM 1. PROCESS EQUIPMENT 2. 3. 4. 5. 6. 7. 8.RUD D r.mh4n.... 11 I___MIXL_

1 IVIML COST ESTIMATE DIRECT COST.(1975

$1000) r1 T DMUT'/MATrD

TAt BASIS FOR 90 260 350 single unit, catalytic type w/heater and condenser, w/o instrumentation and controls, stainless steel, ASME VIII BUILDING ASSIGNMENT

100 50 ISO 30' x 40' x 25' @ $5/ft 3 (turbine building shielded area) ASSOCIATED

PIPING SYSTEMS 18 12 30 augment piping connections only INSTRUM4ENTATION

AND CONTROLS 24 96 120 allowance ELECTRICAL

SERVICE neq 4kw heaters on vessels neglected SPARE PARTS 85 85 75K for catalyst + 2% E/M in items 1 & 4 above SUBTOTAL 232 503 735 CONTINGENCY

23 50 73 10% TOTAL DIRECT COSTS 2S5 553 808 r a O (S...... ..................

w BWR Off %e Darr-M---

Ick- a, I a W i IARND TflYAi K A ANNUAL OPERATING

AND MAINTENANCE

COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR-LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment BWR Offgas Recombiner (Sheet 2) COST (1975 $1000)ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE OPERATING

LABOR, SUPERVISION, 3.3 15 m.n/shift AND OVERHEAD MAINTENANCE

MATERIAL AND. 20.0 routine conditioning of catalyst and LABOR equipment upkeep; 5% of E/M including I&C CONSUMBLES, CHEMICALS, AND -initem 2 SUPPLIES UTILITIES

AND SERVICES Waste Disposal Water Steam neg intemittent;

4kw heater load is negligible Electricity Building Services Other TOTAL 0 AND M ANNUAL COST 23.3 1. 2.C2 ,01 3. 4. 5.I

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment !TFM 1. PROCESS EQUIPENT

2. BUILDING ASSIGNMENT

3. 4. S. 6. 7. 8.3-ton Charcoal Adsorber (Sheet 1)LABOR 5 DIRECT COST (1975 $1000) EOUIPMENTIMATERIALS

TOTAL-------44.0 49.0 BASIS FOR COST ESTIMATF carbon steel, 350 psig, 200 ft 3 volume (augment to existing train of beds)4. 4. 4. 4 8 4.5 12.5 10' x 10' x 25' * $5/ft 3 (turbine building shiel4ed area)ASSOCIATED

PIPING SYSTES -in item I INSTRUKENTATION

AND CONTROLS neg ELECTRICAL

SERVICE neg SPARE PARTS none existing SUBTOTAL 13 48.5 61.5 CONTINGENCY

1 5.0 6.0 10% TOTAL DIRECT COSTS 14 53.5 67.5 r r a S.. .... ....r m K ANNUAL OPERATING

AND MAINTENANCE

COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment 3-ton Charcoal Adsorber (Sheet 2) COST (1975 $1000)I TFM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE OPERATING

LABOR. SUPERVISION.

neg AND OVERHEAD MAINTENANCE

MATERIAL AND allowance of 3% of equipment cost LABOR neg is negligible CONSUMABLES.

CHEMICALS, AND SUPPLIES neg lifetime use of charcoal assumed UTILITIES

AND SERVICES Waste Disposal Water Steam neg Electricity Building Services Other TOTAL 0 AND M ANNUAL COST neg K 1. 2. 3. 4.I..5.

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment Desiccant Drver fSheet !1 I TEN I ARflR DIRECT COST (1975 $1000)IL 1% COTETMT BASIS FOR 1. PROCESS EQUIPMENT 25 75 100 redundant dryer vessels with 1 regeneration skid BUILDING ASSIGNMENT

95 50 145 40' x 36' x 20' @ $5/ft 3 turbine building (shielded area) ASSOCIATED

PIPING SYSTEMS 10 5 15 augment piping connections only INSTRUMENTATION

AND CONTROLS 12 48 60 allowance ELECTRICAL

SERVICE 18 17 35 service for heaters, blowers, pumps, and compressors SPARE PARTS 3 3 SUBTOTAL 160 198 358 CONTINGENCY

16 20 36 10% TOTAL DIRECT COSTS 176 218 394 r 2.8i 3. 4. 5.6. 7. 8.(r Desiccant Drver (Sheet I)

K ANNUAL CPERATING

AND MAINTENANCE

COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment Desiccant Dryer (Sheet 2) COST (1975 $1000)I Ahfl flTIIP TflTAI BASIS FOR COST ESTIMATE ITEM itri,,, ........ .... OPERATING

LABOR, SUPERVISION, 3.3 15 min/shift AND OVERHEAD MAINTENANCE

MATERIAL AND 6.1 5% of equipment including I&C LABOR CONSUMABLES, CHEMICALS, AND neg SUPPLIES UTILITIES

AND SERVICES Waste Disposal neg operating time does not require Water neg significant utilities and services Steam Electricity neg Building Services Other TOTAL 0 AND M ANNUAL COST 9.4 K K 1. 2. 3 4.C U'S.

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREAThENT

SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment ITEM Charcoal Vault Refrigeration (Sheet 1)10AM DIRECT COST (1975 $1000)LAORFlIITDUdCNT/UATCDTA1 C YffAS IfC et.V BASIS FOR 1. PROCESS EQUIPMENT

2. BUILDING ASSIGNMENT

3. 4. 5. 6. 7. 8.10 75 85 10-ton capacity, 3 refrigerators with drives, 32°F design I t 4-4 9 3 12 20' x 10' x 201 0 $2/ft 3 turbine building (nonshielded area)ASSOCIATED

PIPING SYSTEMS In item 1 INSTRUMENTATION

AND CONTROLS 4 6 10 allowance ELECTRICAL

SERVICE 12 18 30 allowance SPARE PARTS 3 3 SUBTOTAL 35 105 140 CONTINGENCY

3 11 14 10% TOTAL DIRECT COSTS 38 116 154 0 N 14 Ch (TftTAI

K ANNUAL OPERATING

AND MAINTENANCE

COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COO.EO

NUCLEAR REACTORS Description of Augment Charcoal Vault Refriceration (Sheet 2)'TIn'COST (1975 $1000) rTeR TOTAL FOR COST OPERATING

LABOR, SUPERVISION.

3.3 15 min/shift AND OVERHEAD MAINTENANCE

MATERIAL AND LABOR 3.7 51 of equlpemt CONSUMABLES, CHEMICALS, AND in Item 2 SUPPLIES UTILITIES

AND SERVICES Waste Disposal Water Steam 0.5 electricity and cooling water Electricity Building Services Other TOTAL 0 AND M ANNUAL COST 7.5 K K 1. 2. 3. 4. S.

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment Charcoal/HEPA

Filtration System -Condenser Vacuum Pump (Sheet 1)ITE4 1. PROCESS EQUIPMENT 2. 3. 4. 5. 6. 7. 8.LABOR__ ~ LrILumLAL

IUIAL COST ESTIMATE D IRECT COST (1975 $1000)2 32.5 34.5 2000 CFM preftlter/4" charcoal bed/HEPA @ S15/cfm, 10 kw heater @ $250/kw BUILDING ASSIGNMENT

3.1 1.5 4.6 Turbine building 8' x 16, x 12' @ $3/ft 3 (nonshielded area) ASSOCIATED

PIPING' SYSTEMS 1.3 0,7 2.0 allowance INSTRUMENTATION

AND CONTROLS in item 1 ELECTRICAL

SERVICE 1 1.5 2.5 SPARE PARTS 0.5 0.5 SUBTOTAL 7.4 36.7 44.1 CONTINGENCY

.7 3.7 4.4 10% TOTAL DIRECT COSTS 8.1 40.4 48.5 (Nm wO (i n *BASIS FOR I

K K ANNUAL OPERATING

ANr MAINTENANCE

COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment Charcoal/HEPA

Filtration System -Condenser Vacuum Pump (Sheet 2) COST (1975 $1000) 'ueD TfllhI RAmie FflQ tOI[IT F¢;TTMATF OPERATING

LABOR, SUPERVISION, neg used only during startup and shutdown AND OVERHEAD MAINTENANCE

MATERIAL AND 1.2 4 HEPA filters @ $150 & 2 Charcoal filters LABOR @ $900, change every 2 years CONSUMABLES, CHEMICALS, AND in items 2 and 4 SUPPLIES UTILITIES

AND SERVICES Waste Disposal 0.2 S50/HEPA filter, $100/Charcoal filter Water Steam Electricity Building Services Other 1.4 5. TOTAL 0 AND M ANNUAL COST_______________________

I _________

________ _______________________________

K I.2. 3. 4.'.4 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment STT F M 1. PROCESS EQUIPMENT 2. 3. 4. 5. 6. 7. 8.Clean Steam to Turbine Glands (Sheot 1)I ARAR DIRECT COST (1975 $1000) FOIITDMFNTIMATPRTAI

ITEMP 15 150 TflTAI 165 BASIS FOR VCTttMATO 25,000 lb/hr reboiler I $4/lb/hr I $25K/H.P.

turbine glands BUILDING ASSIGNMENT

19 10 29 20' x 30' x 16' 6 $3/ft 3 ASSOCIATED

PIPING SYSTEMS 32 18 50 equiv 1000 ft 0 $50/ft INSTRUMENTATION

AND CONTROLS 8 12 20 in addition to Item I ELECTRICAL

SERVICE nag SPARE PARTS 5 5 SUBTOTAL 74 195 269 CONTINGENCY

7 20 27 10% TOTAL DIRECT COSTS 81 215 296 r C r K K SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment Clean Steam to Turbine Glands (Sheet 2) COST (1975 $1000)1TR4 LABOR OTHER TOTAL BASIS FOR COST ESTIMATE OPERATING

LABOR, SUPERVISION, 3.3 15 min/shift AND OVERHEAD MAINTENANCE

MATERIAL AND 4.0 40 man-days LABOR CONSUMABLES, CHEMICALS, AND SUPPLIES UTILITIES

AND SERVICES Waste Disposal Water Steam 21.0 10 Btu/kw-hr heat rate increase Electricity Building Services Other TOTAL 0 AND M ANNUAL COST 28.3 ANNUAL OPERATING

AND MAINTENANCE

COST ESTIMATE SHEET OF RADWASTE TREATMENT 9'I. 2. 3. 4. 5.

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment Clean Steam to Steam Valves 2 4" and Larger (Sheet 1)ITEM I AMII DIRECT COST (1975 $1000) n:*.:TDAACLIMATDTai PROCESS EQUIPMENT

100 120 220 22 valves @ $1OK/valve, use existing reboiler BUILDING ASSIGNMENT

neg install in existing space ASSOCIATED

PIPING SYSTEMS -in item 1 INSTRUMENTATION

AND CONTROLS -in Item 1 ELECTRICAL

SERVICE neg SPARE PARTS 5 SUBTOTAL 100 125 225 CONTINGENCY

10 12 22 10% TOTAL DIRECT COSTS 110 137 247 BASIS FOR 0 i%1J I. 2. 3. 4. S. 6. 7. 8.(r TnTAI

-\ANNUAL OPERATING

AND MAINTENANCE

COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM1 FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment Clean Steam to Steam Valves 24" and Larger (Sheet 2) COST (1975 $1000)TT!M LABOR OTHER TOTAL BASIS FOR COST ESTIMATE OPERATING

LABOR, SUPERVISION, 3.3 15 min/shift AND OVERHEAD MAINTENANCE

MATERIAL AND 4.0 40 man-days LABOR CONSUMABLES, CHEMICALS, AND neg SUPPLIES UTILITIES

hND SERVICES Waste Disposal Water Steam neg Electricity Building Services Other TOTAL 0 AND M ANNUAL COST 7.3 K 1. 2. 3. 4.w U,

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment ITEM 1. PROCESS EQUIPMENT 2. 6. 3. 7.e . w .h 4. 5. 6. 7. 8.Clean Steam to Steam Valves 2-1/2N and Less Than 24" (Sheet 1)LAB 0 DIRECT COST (1975 $1000) OR EQUIPMENT/MATERIALS

120 TOTAl_120 BASIS FOR 100 valves 0 $1200 each BUILDING ASSIGNMENT

--neg ASSOCIATED

PIPING SYSTEMS 40 20 60 INSTRUMENTATION

AND CONTROLS 10 20 30 allowance ELECTRICAL

SERVICE -none SPARE PARTS -6 6 SUBTOTAL 50 166 216 CONTINGENCY

5 17 22 10% TOTAL DIRECT COSTS 55 183 238 I (TOTAL COS ESTIMATE

K SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment Clean Steam to Steam Valves 2-1/2" and Less Than 24" (Sheet 2)COST (1975 $1000)ITEM LABOR OTN!R OPERATING

LABOR, SUPERVISION, 3.3 15 min/shift AND OVERHEAD MAINTENANCE

MATERIAL AND 12.0 1% of direct cost of equipment LABOR CONSUMABLES, CHEMICALS, AND -in item 2 SUPPLIES UTILITIES

AND SERVICES Waste Disposal Water Steam neg Electricity Building Services Other TOTAL 0 AND H ANNUAL COST 15.3 A ANNUAL OPERATING

AND MAINTENANCE

COST ESTIMATE SHEET OF RADWASTE TREATMENT K-a a U'1. 2. 3. 4. S.TNTAI

Description of Augment TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS 15,000-cfm HEPA Filtration System -Auxiliary Building (Sheet 1)BASIS FOR rACT rCTTMATr II Anna flTl .r.. --.n .- L , I r. I~p~ ERq~ X rr...L./ n n. v, .., .1. PROCESS EQUIPMENT 40.0 45.0 prefilter/HEPA

@ $3/cfm, use existing fan BUILDING ASSIGNMENT

7 4.5 11.5 16' x 12' x 12' @ $5/ft 3 (nonshielded area) ASSOCIATED

PIPING SYSTEMS 3 2.0 5.0 INSTRUMENTATION

AND CONTROLS in item 1 ELECTRICAL

SERVICE base SPARE PARTS 0.5 0.5 SUBTOTAL 15 47.0 62.0 CONTINGENCY

1 5.0 6.0 10% TOTAL DIRECT COSTS 16 52.0 68.0 ((I ADflD DIRECT COST (1975 $1000) £rI"TDUCMT

MATrTAI C 5 TfllAI ,o L. a'2. 3. 4. 5. 6. 7. 8.(

K FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment 15,000-cfm HEPA Filtration System -Turbine Building (Sheet 2)I AflI DIRECT COST (1975 $1000) lI TDMCWNT IMATrOAIC TflTAL BASIS FOR COST ESTIMATE ITEM !L___ f ______________

PROCESS EQUIPMENT

5 40.0 45.0 skid mounted filter housing w/o fans BUILDING ASSIGNMENT

4.6 2.3 6.9 16' x 12' x 12' @ $3/ft 3 (nonshielded area) ASSOCIATED

PIPING SYSTEMS 3 2.0 5.0 INSTRUMENTATION

AND CONTROLS in item 1 ELECTRICAL

SERVICE base SPARE PARTS 0 0.5 0.5 SUBTOTAL 12.6 44.8 57.4 CONTINGENCY

2 4.0 6.0 10l TOTAL DIRECT COSTS 14.6 48.8 63.4 T TOTAL DIRECT COST ESTIMATE SHEET OF RADWASrE TREATMENT

SYSTEM K-I 1. 2. 3. 4. 5. 6. 7. a.!

ANNUAL OPERATING

AND MAINTENANCE

COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment 15,000-cfm HEPA Filtration ITEM LABOR System (Sheet 3) COST (1975 $1000)OTI4FR TflTAI OPERATING

LABOR, SUPERVISION, 3.8 15 min/shift

+ 40 hr annual test AND OVERHEAD MAINTENANCE

MATERIAL AND 2.2 change every 2 yrs @ $150/filter element LABOR CONSUMABLES, CHEMICALS, AND in items 2 and 4 SUPPLIES UTILITIES

AND SERVICES Waste Disposal 0.8 $50/filter element Water Steam Electricity

1.0 additional fan electrical load Building Services Other TOTAL 0 AND M ANNUAL COST 7.8 (I. 2. 3.I RACTC Frn rncT FCTIMATC 4. 5.I_

K TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment 1000-cfm Charcoal/HEPA

Filtration System (Sheet 1)I TEM LABOR DIRECT COST (1975 $1000) EOUIPMENT/MATERIALS

TOTAL BASIS FOR COST ESTIMATE PROCESS EQUIPMENT

2.0 22.0 24.0 prefllter/4" charcoal/HEPA

@ $20/cfm, 5 kw htr @ $400/kw BUILDING ASSIGNMENT

3.8 2.0 5.8 8' x 12' x 12' @ $5/ft 3 (nonshielded area) ASSOCIATED

PIPING SYSTEMS 1.3 .7 2.0 INSTRUMENTATION

AND CONTROLS in item 1 ELECTRICAL

SERVICE 1.5 1.0 2.5 SPARE PARTS 0.5 0.5 SUBTOTAL 8.6 26.2 34.8 CONTINGENCY

1.0 2.0 3.0 10% TOTAL DIRECT COSTS 9.6 28.2 37.8 K 0 I. 2. 3. 4. 5. 6. 7. 8.

ANNUAL OPERATING

AND MAINTENANCE

COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment 1000-cfm Charcoal/HEPA

Filtration System (Sheet 2) COST (1975 $1000) ITEM LABOR OTHER TOTAL BASIS FOR COST £STII4ATF OPERATING

LABOR, SUPERVISION, 1.9 20 min/day + 40 hr annual test AND OVERHEAD MAINTENANCE

14ATERIAL

AND .6 2 HEPA or prefilters

@ $150 each and 1 charcoal @ $900 each every 2 yrs' CONSUMABLES, CHEMICALS, AND in items 2 and 4 SUPPLIES UTILITIES

AND SERVICES Waste Disposal .1 $50/HEPA or prefilter, $100/charcoal Water filter Steam Electricity neg Building Services Other 5. TOTAL 0 AND M ANNUAL COST 2.6____________________________

____________

I I ( __ (1. 2. -3. 0--

K TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment 15,OOO-cfm Charcoal/HEPA

Filtration System -Auxiliary Building (Sheet 1)TTVM 1. PROCESS EQUIPMENT 2. 3. 4. 5. 6. 7. 8.LABOR 10 DIRECT COST (1975 $1000) EQUIPMENT/MATERIALS

71 TOTAL 81 BASIS FOR COST ESTIMATE prefilter/4" charcoal/HEPA

@ $5/cfm, 30kw htr @ $200/kw BUILDING ASSIGNMENT

12 8 20 16' x 20' x 12' @ $5/ft 3 (nonshielded area) ASSOCIATED

PIPING SYSTEMS 3 2 5 INSTRUMENTATION

AND CONTROLS -In Item 1 ELECTRICAL

SERVICE 3 2 5 allowance SPARE PARTS 5 5 4 elements of each type SUBTOTAL 28 88 116 CONTINGENCY

3 9 12 10% TOTAL DIRECT COSTS 31 97 128 K a COST ESTIMATE ITE LABO.....

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment I TEM 1. PROCESS EQUIPMENT 2. 3. 4. 5. 6. 7. 8.15,000-cfm Charcoal/HEPA

Filtration System -Turbine Building (Sheet 2)I fuND DIRECT COST (1975 $1000) CN "I lDMrLT ATEDIlA1 C ITEM x flMrnR 1.3 UTflYAI I_____ ARAL?~urIIn~LJIUL

UIt.IW BASIS FOR 10.0 71.0 81.0 prefilter/4*

charcoal/HEPA

@ $5/cfm, 30 kw htr @ $200/kw BUILDING ASSIGNMENT

7.7 3.8 11.5 16' x 20' x 121 @ $3/ft 3 (nonshielded area) ASSOCIATED

PIPING SYSTEMS 3.0 2.0 5.0 INSTRUMENTATION

AND CONTROLS in item 1 ELECTRICAL

SERVICE 3.0 2.0 5.0 allowance SPARE PARTS 5.0 5.0 4 elements each type SUBTOTAL 23.7 83.8 107.5 CONTINGENCY

2.0 9.0 11.0 10% TOTAL DIRECT COSTS 25.7 92.8 118.5 r (0 .rg (

ANNUAL OPERATING

AND MAINTENANCE

COST ESTIMATE SHEET OF RADWASTE TREAThENT SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment 15,O00-cfm Charcoal/HEPA

Filtration System (Sheet 3)COST (1975 $1000)ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE OPERATING

LABOR. SUPERVISION, 3.8 15 min/shift

& 40-hr annual test AND OVERHEAD MAINTENANCE

MATERIAL AND 9.0 30 HEPA or prefilters

@ $150 each & 15 LABOR charcoal filters @ $900 each every 2 yrs CONSUMABLES, CHEMICALS, AND in Items 2 and 4 SUPPLIES UTILITIES

AND SERVICES Waste Disposal 1.5 $S50/HEPA

or prefilter, $100/charcoal Water Steam Electricity

1.3 8kw additional fan power for filter aP Building Services 0.018.S/kw-hr Other TOTAL 0 AND M ANNUAL COST 15.6 K K 1. 2. 3. 4.0 5.

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS 30.00O-cfm Charcoal/HEPA

Filtration System -Auxiliary Building (Sheet 1)i ARng~DIRECT COST (1975 $1000) FoII PI4FNTII4ATFRIALS

-¶ a 1n FnrMN/AEIL

1. PROCESS EQUIPMENT 15 117.0 TOTAL 132.0 BASIS FOR COST ESTIMATE pref1lter/4" charcoal/HEPA

@ $4/cfm, 60-kw htr @ $200/kw BUILDING ASSIGIMENT

20 13.6 33.6 28' x 20' x 12' $S5/ft 3 (nonshielded area) ASOCIATED

PIPING SYSTEMS 5 3.0 8.0 base INSTRUMENTATION

AND CONTROLS -in item I ELECTRICAL

SERVICE 6 4.0 10.0 allowance SPARE PARTS 5.0 5.0 4 elements each type SUBTOTAL 46 142.6 188.6 CONTINGENCY

5 14.0 19.0 10% TOTAL DIRECT COSTS 51 156.6 207.6 C Description of Augment I ITU a 2. 3. 4. 5. 6. 7. 8.(

K TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment 30,000-cfm Charcoal/HEPA

Filtration System -Turbine Building (Sheet 2)ITEM LAROR DIRECT COST (1975 $1000) !OtITPHt¶!rT/ATrR

TALS TflTA[BASIS FOR PROCESS EQUIPMENT

15.0 117.0 132.0 prefilter/4" charcoal/HEPA

@ $4/cfm, 60kw htr @ $200/kw BUILDING ASSIGNMENT

13.4 6.8 20.2 28' x 20' x 12' @ $3/ft 3 (nonshielded area) ASSOCIATED

PIPING SYSTEMS 3.0 5.0 8.0 base INSTRUMENTATION

AND CONTROLS in item 1 ELECTRICAL

SERVICE 6.0 4.0 10.0 allowance SPARE PARTS 5.0 5.0 4 elements each type SUBTOTAL 37.4 137.8 175.2 CONTINGENCY

4.0 14.0 18.0 l0 TOTAL DIRECT COSTS 41.4 151.8 193.2 y me 1. 2. 3. 4. 5. 6. 7. 8.

ANNUAL OPERATING

AND MAINTENANCE

COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment 30.00O-cfm Charcoal/HEPA

Filtration System -(Sheet 3)COST (1975 $1000)ITEM LABOR OTHER TOTAL BASIS FOR £OST FSTTMATF OPERATING

LABOR, SUPERVISION, 3.8 15 min/shift

+ 40 hr annual test AND OVERHEAD MAINTENANCE

MATERIAL AND 18.0 60 HEPA or prefilters

@ $150 each & 30 LABOR charcoal filters @ $900 each every 2 yrs CONSUMABLES, CHEMICALS, AND -in items 2 and 4 SUPPLIES UTILITIES

AND SERVICES Waste Disposal 3.0 $50/HEPA or preftilter, $1007charcoal filter Water Steam Electricity

2.6 16kw additional fan HP for filter @ Building Services 0.018 S/ku-hr Other TOTAL 0 AND M ANNUAL COST 27.4__ C 2. " 3. 4. 5.-: -ý:r t- -.-J"

K TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment ITEM 1. PROCESS EQUIPMENT 2. BUILDING 3. 4. 5. 6. 7. 8.Turbine Building Chilled Water HVAC System (Sheet 1) LABOR 300 DIRECT COST (1975 $1000) EOUJIPMFNTIMATFRIALS

TnIMNIAEIL

1 nA 500 TflTAI 800 BASIS FOR rnCT CTMATC 500-ton capacity, w/o air filters-t + I Coolers can be Installed in existing space saved by deletion of ductin

g. ASSOCIATED

PIPING SYSTEM; -in item 1 INSTRUMENTATION

AND CONTROLS -in item 1 ELECTRICAL

SERVICE 40 so 90 SPARE PARTS -8 8 1% item 1 SUBTOTAL 340 558 898 CONTINGENCY

34 56 90 10l TOTAL DIRECT COSTS 374 614 988 K 11 0 -J

ANNUAL OPERATING

AND MAINTENANCE

COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTE14 FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment Turbine Building Chilled Water HVAC System (Sheet 2)COST (1975 $1000)ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE OPERATING

LABOR, SUPERVISION, 3.3 15 min/shift AND OVERHEAD MAINTENANCE

MATERIAL AND 20.0 2-1/2% of equipment costs LABOR CONSUMABLES, CHEMICALS, AND -initem 2 SUPPLIES UTILITIES

AND SERVICES Waste Disposal Water 13.0 500 gpm @ 104/1000 gal & 50% load factor Steam Electricity

33.0 400 kw @ 0.018 $/kw hr Building Services Other TOTAL 0 AND M ANNUAL COST 69.3 C r I. 2. 3. 4..0 0 S.C

K Description of Augment K TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT.

SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS 600-ft 3 Waste Gas Decay Tank' (Sheet 1)I TFM LABOR DIRECT COST (1975 $1000) EOUIPMENT/MATERIALS

TOTAL BASIS FOR COST ESTIMATE PROCESS EQUIPMENT

2.5 20 22.5 600-ft 3 , 150 pslgo C.S., ASME VIII BUILDING ASSIGNMENT

18.0 9 27.0 15' x 15' x 20' @ S6/ft 3 (shielded area) ASSOCIATED

PIPING SYSTEMS 1.0 1 2.0 10% of item 1 INSTRUMENTATION

AND CONTROLS neg ELECTRICAL

SERVICE neg SPARE PARTS neg SUBTOTAL 21.5 30 51.5 CONTINGENCY

2.0 3 5.0 10% TOTAL DIRECT COSTS 23.5 33 56.5 K I

ANNUAL OPERATING

AND MAINTENANCE

COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment 600-ft 3 Waste Gas Decay ITEM LABOR Tank (Sheet 2) COST (1975 $1000)OTHER TOTAL OPERATING

LABOR, SUPERVISION, AND OVERHEAD neg MAINTENANCE

MATERIAL AND LABOR neg CONSUMABLES, CHEMICALS, AND SUPPLIES neg UTILITIES

AND SERVICES Waste Disposal Water Steam neg Electricity Building Services Other TOTAL 0 AND N ANNUAL COST neg I. 2. 3. 4.FflR 0 U' 0~e 5.(

K TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM Description of Augment IT"M 1. PROCESS EQUIPMENT 2. 3. 4. 5. 6. 7. 8.FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS PWR Hydrogen Recombiner (Sheet 1)IARno 50.0 DIRECT COST (1975 $1000)

TAI TflTAI I l :fTI b V VT nA. I 300.0 350.0 BASIS FOR rnqT vtTTMATF skid mounted, catalytic type w/condenser, partial I&C single unit, ASME VIII BUILDING ASSIGNM4ENT

28.8 14.4 43.2 15' x 30' x 16' 0 $6/ft 3 (shielded area) ASSOCIATED

PIPING SYSTEMS 32.0 13.0 45.0 allowance INSTRUMENTATION

AND CONTROLS 10.0 40.0 50.0 allowance ELECTRICAL

SERVICE 13.0 12.0 25.0 allowance SPARE PARTS -2.0 2.0 SUBTOTAL 133.8 381.4 515.2 CONTINGENCY

13.0 38.0 51.0 101 TOTAL DIRECT COSTS 146.8 419.4 566.2 K a Ue ANNUAL OPERATING

AND MAINTENANCE

COST ESTIMATE SHEET OF RADtWASTE

TREAThENT

SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment PUR Hydrogen Recombiner (Sheet 2) COST (1975 $1000)ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE OPERATING

LABOR, SUPERVISION, 3.3 15 min/shift AND OVERHEAD MAINTENANCEMATERIAL

AND. 10.0 3% of equipment cost LABOR CONSUMABLES, CHEMICALS, AND 1.0 oxygen @.S2.5/103 cf & .25 cfm 0 SUPPLIES 7000 hrs UTILITIES

AND SERVICES Waste Disposal Water Steam neg Electricity Building Services Other TOTAL 0 AND M ANNUAL COST 14.3 1. 2. 3. 4.Ca I U'S.K C

Description of Augment ITEM 1. PROCESS EQUIPMENT 2. 3. 4. 5. 6. 7. 8.TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS PWR Air EJector Charcoal/HEPA

Filtration Unit (Sheet 1)LABOR 3.0 DIRECT COST (1975 $1000) EOUIPMENT/MATERIALS

7.5 TOTAL 10.5 1*BASIS FOR COST ESTIMATE chiller, heater, charcoal HEPA BUILDING ASSIGNMENT

3.0 1.5 4.5 10' x 10' x 15' @ $3/ft 3 (unshielded turbine bldg) ASSOCIATED

PIPING SYSTEMS 2.0 1.0 3.0 allowance INSTRUMENTATION

AND CONTROLS 0.5 1.5 2.0 allowance ELECTRICAL

SERVICE 0.5 0.5 1.0 allowance SPARE PARTS 1.0 1.0 SUBTOTAL 9.0 13.0 22.0 CONTINGENCY

1.0 1.0 2.0 1O0 TOTAL DIRECT COSTS 10.0 14.0 24.0

ANNUAL OPERATING

AND MAINTENANCE

COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augnent PWR Air EJector Charcoal/HEPA

Filtration Unit (Sheet 2)COST (1975 $1000)ITEM LARAR___ .....________________

I , L ueA5 rwK Guil r.4IrMIE OPERATING

LABOR, SUPERVISION, 3.8 15 min/shift

+ 40 hr annual test AND OVERHEAD MAINTENANCE

MATERIAL AND 2.0 includes replacement filter LABOR CONSUMABLES, CHEMICALS, AND -in item 2 SUPPLIES UTILITIES

AND SERViCES Waste Disposal neg Water Steam Electricity Building Services Other TOTAL 0 AND M ANNUAL COST 5.8 flTIFD TnTAI l. 2. 3. 4.EP U'5.K DAete K K TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment ITEM Steam Generator Flash LABOR Tank Vent to Main Condenser (Sheet DIRECT COST (1975 $1000) EQUIPMENT/MATERIALS

1)TOTAL BASIS FOR COST ESTIMATE PROCESS EQUIPMENT

-no equipment required BUILDING ASSIGNMENT

neg install In existing space ASSOCIATED

PIPING SYSTEMS 13 7 20 200 ft of 10-in pipe with 2 valves INSTRUMENTATION

AND CONTROLS 4 6 10 allowance ELECTRICAL

SERVICE neg SPARE PARTS neg SUBTOTAL 17,, 13 30 CONTINGENCY

2 1 3 10% TOTAL DIRECT COSTS 19 14 33 I.U't ull 2. 3. 4. 5. 6.7. 8.

ANNUAL OPERATING

AND MAINTENANCE

COST ESTIMATE SHEET OF RADWASTE TREAThENT SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment Steam.Generator Flash Tank Vent to Main Condenser (Sheet 2) COST (1975 $1000)ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE OPERATING

LABOR, SUPERVISION, 1 allowance AND OVERHEAD MAINTENANCE

MATERIAL AND 1 2% Total Direct Cost LABOR CONSUHABLES, CHEMICALS, AND neg SUPPLIES UTILITIES

AND SERVICES Waste Disposal Water neg Steam Electricity Building Services Other TOTAL 0 AND H ANNUAL COST 2 1. 2. 3. 4..a U'5.((

K TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment lSqpm Evaporator (Sheet 1)I AnRO DIRECT COST (1975 $1000)PROCESS EQUIPMENT

30 225 255 skid mounted, submerged tube bundle, ASME VIII, Incoloy in contact with process fluid BASIS FOR

2. BUILDING ASSIGNMENT

68 34 102 evap & services 25' x 301 x 20' @ $6/ft3 plus 2,000 ft3 increase in solid waste storage area ASSOCIATED

PIPING SYSTEMS 35 30 65 inludes service piping INSTRUMENTATION

AND CONTROLS 10 10 20 allowance ELECTRICAL

SERVICE 40 25 65 allowance SPARE PARTS -27 27 2% of item 1 plus tube bundle SUBTOTAL 183 351 534 CONTINGENCY

18 35 53 10% TOTAL DIRECT COSTS 201 386 587 ITI'N 1.a.3. 4. 5. 6. 7. 8.

Description of Augment tTrW TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREAThENT'SYSTEM

FOR LIGHT-WdATER-COOLED

NUCLEAR REACTORS 30-gpm Evaporator (Sheet 2) , BASIS FOR rncT rCY?UAYT*.- -..rw-f .dV..r b.r ...I u snlrl.# ,nI .bl r~l) I lruI 1. PROCESS EQUIPMENT

2. BUILDING ASSIGNMgNT

30 t 88 350 44 380 132 ASME VIII skid mounted, submerged, 'tube bundle, Incoloy in contact with process fluid evap + services -25' x 40' x 20' @ $6/ft 3 plus 2,000 ft 3 Increase In solid waste storage area ASSOCIATED

PIPING SYSTEMS 35 35 70 includes service piping INSTRUMENTATION

AND CONTROLS 10 10 20 allowance ELECTRICAL

SERVICE 40 25 65 allowance SPARE PARTS 27 27 2% of Item 1 plus tube bundle SUBTOTAL 203 491 694 CONTINGENCY

20 49 69 1O0 TOTAL DIRECT COSTS 223 540 763 C C I AfPtflD DIRECT COST (1975 $1000) rfIITDfMlrTIMATrDTAI

TnTA, CO 3. 4. 5. 6. 7. 8.

K FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment 50-qpm Evaporator (Sheet 3)ITEM 1. PROCESS EQUIPMENT 2. 3. 4. S. 6. 7. 8.LABOR 30 DIRECT COST (1975 $1000) EOUIPMENT/MATERIALS

450 TOTAL 480 BASIS FOR COST ESTIMATE ASME VIII skid mounted, submerged, tube bundle, Incoloy In contact with process fluid BUILDING ASSIGNMENT

97 48 145 10% more than 30 gpm ASSOCIATED

PIPING SYSTEMS 35 35 70 allowance INSTRUMENTATION

AND CONTROLS 10 10 20 allowance ELECTRICAL

SERVICE 40 25 65 allowance SPARE PARTS. 27 27 2% of Item 1 plus tube bundle SUBTOTAL 212 595 807 CONTINGENCY

21 60 81 10% TOTAL- DIRECT COSTS 233 655 888 T TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMErNT

SYSTEM'III a Description of Augment 50-gpm Evaporator (Sheet 3)

ANNUAL OPERATING

AND MAINTENANCE

COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment

-RUR Dirty Ua~tm-Finn, £1 COST (1975 $1000)ITEM LABOR OT14ER TOTAL BASIS FOR LOST FSTIMATF OPERATING

LABOR, SUPERVISION, 12 2.6 x 106 gpy; 1000 hrs/yr labor AND OVERHEAD MAINTENANCE

MATERIAL AND 30 7-1/2% of equipment cost LABOR CONSUMABLES, CHEMICALS, AND neg concentrate solidification chemicats SUPPLIES in item 4 UTILITIES

AND SERVICES Waste Disposal 70 100:1 feed to concentrate ratio @ 20/ft 3 disposal cost Water 27 1000 gpm @ 1500 hrs @ 30t/1000 gal Steam 60 1500 hrs steaw @ 20,000 lb/hr @ $2/1000 lbs Electricity Building Services Other TOTAL 0 AND M ANNUAL COST 199 C C 1. 2. 3. 4. 5.

SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment Evaporator PWR DirtylT YM[AROR Waste (Sheet 5) COST (1975 $1000)OTHER TOTAL BASIS FOR COST ESTTMATE OPERATING

LABOR, SUPERVISION, AND OVERHEAD 6.0 500,000 gpy; 500 hrs/yr labor MAINTENANCE

MATERIAL AND LABOR 30.0 7-1/2% of equipment cost CONSUMABLES, CHEMICALS, AND -concentrate solidification chemicals SUPPLIES in item 4 UTILITIES

AND SERVICES 50:1 feed to concentrate ratio @ $20/ft 3 Waste Disposal 27.0 disposal cost Water 5.0 1000 gpm @.277 hrs @ 30t/1000 gal Steam 12.0 277 hrs steam @S 20,000 4bs/hr @ $2/1000 lbs Electricity Building Services Other TOTAL 0 AND M ANNUAL COST 80.0 ANNUAL OPERATING

AND MAINTENANCE

COST ESTIMATE SHEET OF RADWASTE TREATMENT K I. 2. 3. 4.0'5.

ANNUAL OPERATING

AND MAINTENANCE

COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment EvaDorator

-Condenser Polisher Chemical IaCto Ih +0 A COST (1975 $1000)ITEMFR CS UK LU ETIMATE OPERATING

LABOR, SUPERVISION, AND OVERHEAD 6.0 650.000 gpy; 500 hr/yr labor MAINTENANCE

MATERIAL AND LABOR 30.0 7-1/2% of equipment cost CONSUMABLES, CHEMICALS.

AND concentrate solidification chemicals SUPPLIES In item 4 UTILITIES

AND SERVICES Waste Disposal 87.0 20:1 feed to concentrate ratio @ $20/ft 3 Wl7.0 disposal cost Water 6.5 1000 gpm 0 360 hrs @ 30*/10OO gal Steam 14.4 360 hrs steam @ 20,000 lb/hr @ $2/1000 lbs Electricity Building Services Other LABOR 0ATD AU TC4TAI TOTAL 0 AND M ANNUAL COST 143.9 C 0 1. 2. 3. 4. 5.(v K SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment-hla~aum*., Um.4.a Iqkaa÷ COST (1975. $1000)TT!M LABOR OTHER TOTAL BASIS FOR COST ESTIMATE OPERATING

LABOR, SUPERVISION, AND OVERHEAD 6.0 160,000 gpy; 500 hrs/yr MAINTENANCE

MATERIAL AND LABOR 30.0 7-1/25 of equipment cost CONSUMABLES, CHEMICALS, AND -concentrate solidification chemicals In SUPPLIES item 4 UTILITIES

AND SERVICES Waste ITsposal 8.6 50:1 feed to concentrate ratio 0 $20/ft 3 disposal cost Water 1.6 1000 gpm 0 90 hrs 0 30t/1000 gal Steam 3.6 90 hrs steam 0 20,000 lb/hr 1 $2/1000 lbs Electricity Building Services Other TOTAL 0 AND M ANNUAL COST 49.8 ANNUAL OPERATING

AND MAI[NTENANCE

COST ESTIMATE SHEET OF RADWASTE TREATMENT K I. 2. 3. 4.ad a, LeD 5.

Description of Augment TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Evaporator Distillate Demineralizer (Sheet 1)TTIrM I anAD DIRECT COST (1975 $1000) EniI nlrT IUA?~nAi e*,-. I.rluvn Iuu~rnllu~r'¶l KhMiLR IJI/L W,5MII EIHMAIT PROCESS EQUIPMENT

4.0 20.0 24.0 30 ft 3 , SS. ASME VIII, 150 psi nonregenerative, w/resin BUILDING ASSIGNMENT

6.4 3.2 9.6 10' x 10' x 16' @ $6/ft 3 (shielded area) ASSOCIATED

PIPING SYSTEMS 9.0 6.0 15.0 2" piping INSTRUMENTATION

AND CONTROLS 2.0 3.0 5.0 remote conductivity readout ELECTRICAL

SERVICE neg SPARE PARTS 1.0 1.0 SUBTOTAL 21.4 33.2 54.6 CONTINGENCY

2.0 3.0 5.0 10% TOTAL DIRECT COSTS 23.4 36.2 59.6 BASIS FOR C (1. 2.i Ot 3. 4. 5. 6. 7. 8.(qrft*IrA I

)K SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment Evaporator Distillate Demineralizer (Sheet 2) COST (1975 $1000)YtM I ARnlQ OTHER TOTAL BASIS FOR COST ESTIMATE aI1II ____________

OPERATING

LABOR, SUPERVISION.

1.8 1500 hrs operation

@ 10% attendance AND OVERHEAD MAINTENANCE

MATERIAL AND LABOR 2.0 allowance CONSUMABLES, CHEMICALS, AND SUPPLIES 2.3 1 change per yr @ $75/ft 3 UTILITIES

AND SERVICES Waste Disposal 0.6 30 ft 3 @ $20/ft 3 disposal cost Water Steam Electricity Building Services Other TOTAL 0 AND M ANNUAL COST 6.7 ANNUAL OPERATING

AND MAINTENANCE

COST ESTIMATE SHEET OF RADWASTE TREATMENT I. 2. 3. 4.,ap 5.

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment 50-opDemintralzer Sh t 1)ITEM LAROR DIRECT COST (1975 $1000) 1ITOM AUIFRAI It TIhTAI BASIS FOR CflCY 1T tMAr" PROCESS EQUIP4ENT

5 20.0 25.0 30 ft 3.SS, VIII. 150 psi, nonreganerative, with resin BUILDING ASSIGNMENT

9 4.8 13.8 12' x 12' x 16' 0 $6/ft 3 (shielded ASSOCIATED

PIPING SYSTEMS 9 6.0 15.0 2" piping INSTRUMENTATION

AND CONTROLS 4 6.0 10.0 ELECTRICAL

SERVICE No SPARE PARTS 2.0 2.0 miscellaneous supplies SUBTOTAL 27 38.8 66.8 CONTINGENCY

2 4.0 6.0 10% TOTAL DIRECT COSTS 29 42.8 -71.8 C 1. 2. 3. 4. 5. 6. 7. 8.(C SO-gin

{Sheet 1)

K Description of Augment K TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS 1O0-9pm Deminerallizer (Sheet 2) LANOR DIRECT COST (1975 $1000) PMFNT/MATFRTALS

TOTAL BASIS FOR COST FSTTMATF PROCESS EQUIPMENT

5 35.0 40.0 60 ft 3 , SS, ASME VIII, 150 psi, nonregenerative, with resin BUILDING ASSIGNMENT

9 4.8 13.8 12' x 12' x 16' 0 $6/ft 3 (shielded area) ASSOCIATED

PIPING SYSTEMS 10 10.0 20.0 2-1/21 piping INSTRUMENTATION

AND CONTROLS 4 6.0 10.0 ELECTRICAL

SERVICE neg SPARE PARTS 2.0 2.0 miscellaneous supplies SUBTOTAL 28 57.8 85.8 CONTINGENCY

3 6.0 9.0 TOTAL DIRECT COSTS 31 63.8 94.8 I. 2. 3." 4. 5.a, 6. 7. B.

TOTAL DIRECT COST ESTIMATE SHEET OF RADWAST!E

TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment 20-plDmneralizer(Sheet

3)__ITEM 1. PROCESS EQUIPMENT 2. 3. 4. 5. 6. 7. 8.LABOR 5 1T A DIRECT COST (1975 $1000) EflUIPI4FNTII4ATFRTAL 60.0 TflTAI 65.0 BASIS FOR rnCT r~tTuATr 120 ft 3 , SS, ASME VIII, i50 psi, nonregenerative, with resin BUILDING ASSIGNMENT

11 5.2 16.2 13' x 13' x 16' 0 $6/ft 3 ___(shielded area) ASSOCIATED

PIPING SYSTEMS 12 12.0 24.0 4" piping INSTRUMENTATION

AND CONTROLS 4 6.0 10.0 ELECTRICAL

SERVICE neg SPARE PARTS 2.0 2.0 miscellaneous supplies SUBTOTAL 32 85.2 117.2 CONTINGENCY

3 9.0 12.0 TOTAL DIRECT COSTS 35 94.2 129.2 ((200-gpm Oemtneraltzer (Sheet 3)

K Description of Augment 400-gpm Demineralizer

-Steam Generator Blowdown Service (Sheet 4)I TrM 1. PROCESS EQUIPMENT 2. 3. 4. 5. 6. 7. 8.lAROR DIRECT COST (1975 $1000) EOUJIPMNT/MATERjALS

TOTAL BASIS FOR COST ESTIMATE T I COST ESTIMATE 5 60.0 65.0 120 ft 3 , SS. ASME VIII, 150 psi, nonregenerative.

with resin BUILDING ASSIGNMENT

11 5.2 16.2 ,3' x 13' x 16' @ $6/ft 3 (shielded area) ASSOCIATED

PIPING SYSTEMS 20 20.0 40.0 6" piping INSTRUMENTATION

AND CONTROLS 4 6.0 10.0 allowance ELECTRICAL

SERVICE neg SPARE PARTS 2.0 2.0 miscellaneous supplies SUBTOTAL 40 93.2 133.2 CONTINGENCY

4 9.0 13.0 TOTAL DIRECT COSTS 44 102.2 146.2 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS a, 'a ANNUAL OPERATING

AND MAINTENANCE

COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment BWR-2nd Waste Demineralizer In Serf es (Sheet El COST (1975 $1000)ITEM_...._-_....__,,__ ,v-n -DROIO rvr uK EV)lr.1 ~PY.I OPERATING

LABOR, SUPERVISION, 3.3 15 min/shift AND OVERHEAD MAINTENANCE

MATERIAL AND LABOR 5.0 allowance CONSUMABLES, CHEMICALS, AND 9.0 1 change per year @ 120 ft 3 0 $75/ft 3 (one SUPPLIES vessel change per year. regardless of size) UTILITIES

AND SERVICES Waste Disposal 2.4 120 ft 3 lyr * $20/ft 3 disposal cost Water Steam Electricity Building Services Other TOTAL 0 AND M ANNUAL COST 19.7 1. 2. 3. 4.a -.J a 5.C lABOR NTNrD TJlTA!

K ANNUAL OPERATING

AND MAINTENANCE

COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment Demineralizer

-PWR Clean Wastes (Sheet 6) COST (197k. $1000)YY IPLu I flTurD?linI matie fflS EflM? rCTTMATe AILr IlV% -lll_ __ _ Ifl, &'flC I l nV bl *fll OPERATING

LABOR, SUPERVISION, 1.8 10% of DRS shim bleed (50,000 gpy), AND OVERHEAD 30 min/day MAINTENANCE

MATERIAL AND LABOR 5.0 allowance CONSUMABLES, CHEMICALS, AND 3 3 SUPPLIES 2.3 30 ft /yr @ $75/ft3 UTILITIES

AND SERVICES Waste Disposal 0.6 30 ft 3/yr @ $20/ft 3 disposal cost Water Steam Electricity Building Services Other TOTAL 0 AND M ANNUAL COST 9.7 I 1. 2. 3. 4.a S.

ANNUAL OPERATING

AND MAINTENANCE

COST ESTIMATE SHEET OF RADIASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment Demineralizer

-BWR Dirty Waste (Sheet 7)COST (1975 $1000)JTFN[ABDR nlTHVg TNlT61 DACIC mnD r.ncT reTvUnt OPERATING

LABOR, SUPERVISION, AND OVERHEAD 6.5 2.6 x 106 gpy, 30 min/shift MAINTENANCE

MATERIAL AND LABOR 5.0 allowance CONSUNABLES, CHEMICALS, AND33 SUPALES 64.5 860 ft 3 resin 0 $75/ft 3 UTILITIES

AND SERVICES Waste Disposal 17.2 860 ft 3 @ $20/ft 3 disposal cost Water Steam Electricity Building Services Other TOTAL 0 AND N ANNUAL COST 93.2 C I. 2. 3. 4.N S.---I C

K ANNUAL OPERATING

AND MAINTENANCE

COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment Demineraltzer

-PWR Dirty.Wastes (w/o turbine building) (Sheet 8) COST (1975 $1000)ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE OPERATING

LABOR, SUPERVISION, AND OVERHEAD 3.3 500,000 gpy; 15 min/shift MAINTENANCE

MATERIAL AND LABOR 5.0 allowance CONSUMABLES, CHEMICALS, AND SUPPLIES 12.0 160 ft 3/yr @ $75/ft 3 UTILITIES

AND SERVICES Waste Disposal 3.2 160 ft 3/yr @ $20/ft 3 disposal cost water Steam Electricity Building Services Other TOTAL 0 AND M ANNUAL COST 23.5 l. 2. 3. 4.a 5./

ANNUAL OPERATIN AND

COST ESTIMTE SHEET OF RADWASTE TREATMENT

of Aujnmant flminapA147AP

.DUo*7m,

  • pww-ITEM T. -a .* C1 *fm r uVfm "a 1.411W4b 7I COST (1975 $1000)--______ .... ..-. ",,' ,,,. urwl, rvuK I.UF)I LtIY:llrl OPERATING

LABOR, SUPERVISION.

AND OVERHEAD 13.1 1 hr/shift, 2.6 x 106 opy MAINTENANCE

MATERIAL AND LABOR 5.0 allowance CONSUMABLES, CHEMICALS, AND SUPPLIES 64.5 660 ft 3 resin 0 $75/ft 3 UTILITIES

AND SERVICES Waste Disposal 17.2 860 ft 3/yr 9 $20/ft 3 disposal cost Water Steam Electricity Building Services Other TOTAL 0 AND N ANNUAL COST 99.8 I ARMR flTIIFA 1. 2. 3. 4.a S.(r SYSTEM FOR L.IGHT, oWATER-COOLEO

NUCL..EAR,, REACTORS oAeTe -1-:j:.1i-:i...-

..........

-."(

K Description of Augment Demineralizer

-PIER tim Steam Generator Blowdomn (Sheet 10) COST (1975 $1000)nyu,..O inaI OPERATING

LABOR, SUPERVISION.

AND OVERHEAD 3.3 15 min/shift MAINTENANCE

MATERIAL AND LABOR 5.0 allowance CONSUMABLES, CHEMICALS, AN" SUPPLIES 16.9 225 ft 3 resin/yr @ $75/ft 3 UTILITIES

AND SERVICES Waste Disposal 4.5 225 ft 3/Yr I $20/ft 3 disposal cost Water Stem Electricity Building Services Other TOTAL 0 AND M ANNUAL COST 29.7 A..UAL OPERATING

AND MAINTENANCE

COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS 2. 3. 4.ens rtnt ReTtMAta a I alLfl9 S.

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment 20-qp Cartridge Filter (Sheet 1)TTFM I DIRECT COST (1975 $1000) vN Itur ¶ u'IIAqr rD lr e... t.J UIhLU 11MAT PROCESS EQUIPMENT

2.0 5.0 7.0 SS, ASME VIII, 150 psi BUILDING ASSIGNMENT

5.6 3.0 8.6 16' x 12' x 20' S $6/ft 3 (shielded area) ASSOCIATED

PIPING SYSTEMS 1.5' 1.0 2.5 allowance INSTRUMENTATION

AND CONTROLS 0.6 2.4 3.0 allowance ELECTRICAL

SERVICE neg SPARE PARTS 0.5 0.5 SUBTOTAL 9.7 11.9 21.6 CONTINGENCY

1.0 1.0 2.0 10% TOTAL DIRECT COSTS 10.7 12.9 23.6 BASIS FOR-.4 Q at 1. 2. 3. 4. 5. 6. 7. 8.(20-qm Cartrtd9e Ftlter (Sheet 1)

ANNUAL OPERATING

AND MAINTENANCE

COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment Cartridge Filter (Sheet 2) COST (1975 $1000)A'1JCDl RAM!S FOR COST ESTIMATE ITEM LADUK uini n , -... ...... .... ... .. OPERATING

LABOR. SUPERVISION, 4.5 10 changes @ 10 man-hrs/change AND OVERHEAD @ $12/hr + 15 min/shift MAINTENANCE

MATERIAL AND LABOR 1.0 allowance CONSUMABLES.

CHEMICALS, AND SUPPLIES 1.0 10 changes/yr

@ $100/change UTILITIES

AND SERVICES Waste Disposal 1.5 10 drums/yr @ $20/ft 3 Water Steam Electricity Building Services Other TOTAL 0 AND M ANNUAL COST 8.0 1. 2. 3. 4. 5.

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREAT1ENT

SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment 100-gpim Precoat Filter (Shoot 1)ITEM LARnR DIRECT COST (1975 $1000) fIW01T P~NT uI~dTIDTAI

PROCESS EQUIPMENT

10 65.0 75 automated system 1 gpm/ft 2 , ASM4E VIII BUILDING ASSIGNMENT

18 9.0 27 15' x 15' x 20' 0 $6/ft 3 (shielded area) ASSOCIATED

PIPING SYSTEM4S 16 9.0 25 35% of equipment cost INSTRUMENTATION

AND CONTROLS in item 1 ELECTRICAL

SERVICE 7 13.0 20 allowance SPARE PARTS 2.0 2 2% of item 1 SUBTOTAL 51 98.0 149 CONTINGENCY

5 10.0 15 10% TOTAL DIRECT COSTS 56 108.0 164 BASIS FOR 0 1. 2. 3. 4. 5. 6. 7. 8.(r i lO0-gpm Precoat Ftlter (Sheet 1)

K FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment 400-oam Precoat Filter T LAROR DIRECT COST (1975 $1000) EOUIPMENT/MATERIALS

TOTAL BASIS FOR COST ESTIMATE PROCESS EQUIPMENT

35 135.0 170 automated system; 1 gpm/ft 2 ASME Viii BUILDING ASSIGNMENT

24 12.0 36 15' x 20' x 20' @ $6/ft 3 (shielded area) ASSOCIATED

PIPING SYSTEMS 31 16.0 47 35% of equipment cost INSTRUMENTATION

AND CONTROLS --item I ELECTRICAL

SERVICE 12 18.0 30 allowance SPARE PARTS -3.0 3 SUBTOTAL 102 184.0 286 CONTINGENCY

10 18.0 28 10% TOTAL DIRECT COSTS 112 202.0 314 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM K (Sheet 2)-J 1. 2. 3. 4. 5. 6. 7. 8.(Sheet 2)-vT

ANNUAL OPERATING

AND MAINTENANCE

COST ESTI1ATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment Precoat Filter -BWR Dirty Waste (Sheet 3) COST (1975 $1000)ITEM LABOR OTHER TOTAL BASIS FOR COST !STTI4ATF OPERATING

LABOR, SUPERVISION, AND OVERHEAD 6.6 2 x 106 gpy, 30 min/shift MAINTENANCE

MATERIAL AND LABOR 10.0 allowance CONSUMABLES, CHEMICALS, AND 6.0 10 lbs precoat @ lOt/lb per 1000 gal SUPPLIES processed

4. UTILITIES

AND SERVICES Waste Disposal Water Steam Electricity Building Services Other 40.0 TOTAL 0 AND M ANNUAL COST j[ 62.6 1 ft 3/sludge per disposal cost 1000 qal processed

@ $30/ft 3 C 1. 2. 3.S.(

T TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment 2-com Reverse TTIFM LABOR DIRECT COST (1975 $1000) FOUlPMENTIMATFRIALS

TOTAL BASIS FOR COST ESTIMATF PROCESS EQUIPIENT

6.0 60.0 66.0 skid mounted w/500-gal SS feed tank, ASME VIII BUILDING ASSIGNMENT

19.2 9.6 28.8 12' x 25' x 16' @ $6/ft 3 ASSOCIATED

PIPING SYSTEMS 3.0 2.0 5.0 allowance INSTRUMENTATION

AND CONTROLS in item I ELECTRICAL

SERVICE 7.0 13.0 20.0 allowance SPARE PARTS 6.0 6.0 SUBTOTAL 35.2 90.6 125.8 CONTINGENCY

3.0 9.0 12.0 10% TOTAL DIRECT COSTS 38.2 99.6 137.8 K 0 1. 2. 3. 4. 5. 6. 7. 8.Osmosis (Sheet 1)

ANNUAL OPERATING

AND MAINTENANCE

COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment Reverse Osmosis -Detergent Wastes COST (1975 $1000)ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE OPERATING

LABOR, SUPERVISION, AND OVERHEAD 3.1 160.000 gpy, 1300 hrs/yr @ 20% attendance MAINTENANCE

MATERIAL AND 8.8 4% less bldg + 24 module with 3-yr life LABOR @ $600 each CONSUMABLES, CHEMICALS.

AND SUPPLIES neg UTILITIES

AND SERVICES Waste Disposal 4.3 100:1 vol reduction

@ $20/ft 3 disposal cost Water Steam Electricity neg Building Services Other TOTAL 0 AND M ANNUAL COST 16.2 r C 1. 2. 3. 4.No 5.(

FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment 1O,000-Gallon Tank__(Sheet

1)?tTrM 1. PROCESS EQUIPMENT 2. 3. 4. 5. 6. 7. 8.I AROR 3 DIRECT COST (1975 $1000) !0IJ!P?4fNT/MATERIALS

TOTAL T -28 31 BASIS FOR COST ESTIMATE SS, ASME VIII, atmospheric service, 200°F BUILDING ASSIGNMENT

30 15 45 15' x 20' x 25' @ $6/ft 3 (shielded area) ASSOCIATED

PIPING SYSTEMS 2 1 3 10% of item 1 INSTRUMENTATION

AND CONTROLS 4 6 10 allowance ELECTRICAL

SERVICE neg SPARE PARTS neg SUBTOTAL 39 s0 89 CONTINGENCY

4 5 9 10% TOTAL DIRECT COSTS 43 55 98 C w 10tOOO-GallonTapk (Sheet 1)TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM

ANNUAL OPERATING

AND MAINTENANCE

COST ESTIMATE SHEET OF RADWASTE TREAThENT

SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment 10000-Gallon Tank (Sheet 2) COST (1975 $1000)ITEM LABOR OTHER TOTAL RA~l flD OPERATING

LABOR, SUPERVISION.

AND OVERHEAD 1.1 5 min/shift

-log level readings MAINTENANCE

MATERIAL AND LABOR 1.6 1/2% of equipment CONSUMABLES.

CHEMICALS, AND neg SUPPLIES UTILITIES

AND SERVICES Waste Disposal Water Steam neg Electricity Building Services Other TOTAL 0 AND N ANNUAL COST 2.7 1. 2. 3. 4. 5.(

REFERENCES

TO APPENDIX B 1. "Guide for Economic Evaluation of Nuclear Reactor Plant Oesigns," USAEC Report NUS-531, NUS Corporation, January 1969. 2. "Wage Rates for Key Construction Trades," Engineering News Record, pp. 36-37, January 2, 1975. 3. "Projections of Labor Requirements for Electric Power Plants Construction, 1974 -2000," USAEC Report WASH-1334, Washington, D.C., August 1974.1.110-85 APPENDIX C DATA NEEDED FOR RADIIASTE

TREATMENT

SYSTEM COST-BENEFIT

ANALYSIS FOR LIGHT-WATER

COOLED NUCLEAR REACTORS This appendix describes information that should be submitted in support of radwaste treat ment system cost-benefit analyses for light-water-cooled nuclear reactors.

The information 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 more detailed discussions of the required information should be referenced as appropriate.

Each response, however, should be Independent of the ER and SAR. All responses should be on a per reactor basis and should provide the following information:

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. 3. If methods and parameters used in the cost-benefit analysis are different from those aiven in this guide, describe the methods used in detail and provide bases for all parameters.

Include the following information:

a. Decontamination factors assigned to each augment and fraction of "on-line" time assumed, i.e., hours per year used. b. Parameters and method used to determine the Indirect Cost Factor and the Capital Recovery Factor.1.110-87 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE'TREATMENT-SYSTEH

FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment i Tru 1 AflfD DIRECT COST (1975 $1000) FflIIIPMFNT/MATFRlALS

1. PROCESS EQUIPMENT

2. BUILDING ASSIGNMENT

t I 1 I I I I I ASSOCIATED

PIPING SYSTEMS BASIS FOR COST ESTIMATE I I I I --INSTRUMENTATION

AND CONTROLS I I I I ELECTRICAL

SERVICE I I I I 6. SPARE PARTS______________________I

i mI SUBTOTAL________________________________________________________

1 -I I I CONTINGENCY

I I I TOTAL DIRECT COSTS________________________________________________________

________________

I __________________________________________________

_____________

_______________________________________________

C TOTAL 0 3. 4. S.7. 8.(C i aunD EnUTPMENTIMATERIALS

ANNUAL OPERATING

AND MAINTENANCE

COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS 0 "I U 2 2 -4 U 2 2 C, a 9 9 'a w -J 04 0.j 'a "4 a. 0 "4 COST (1975 $1000)I TIFM

1. OPERATING

LABOR, SUPERVISION, AND OVERHEAD MAINTENANCE

MATERIAL AND LABOR CONSUMABLES, CHEMICALS, AND SUPPLIES UTILITIES

AND SERVICES Waste Disposal Water Steam Electricity Building Services Other TOTAL 0 AND M ANNUAL COST LABOR OTHER TOTAL BASIS FOR COST ESTIMATE Description of Augment U K 2. 3. 4. 5.ITEM


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