Regulatory Guide 1.110

Cost-Benefit Analysis for Radwaste Systems for Light-Water-Cooled Nuclear Power Reactors

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Issue date:	03/31/1976
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U.S. NUCLEAR REGULATORY COMMISSION March 1976 REGULATORY GUIDE

OFFICE OF STANDARDS DEVELOPMENT

4 REGULATORY GUIDE 1.110

COST-BENEFIT ANALYSIS FOR RADWASTE S

LIGHT-WATER-COOLED NUCLEAR PDWE& CRS'

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 S

methods acceptable go the NRC staff of4 impementing specific pairt of the Commission'& fegulatione. to definetel techniquemused by the state in evild The guides are issued in the following ten broaddivisions 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 thenmilerot reCed Methods end soutione diflerent fron those get outi I Research end Test Reactors 7 Tronsponstion Ihe guidell we be acceptable It they provide a bahis for lthefindings requrlit to 3 Fueuls and Materiels Facilities a Occupolionat 4palt h themesnee

• l sentis*lnCe- of - permst of Scenes by the Commitssion 4 Environmental and Siting 2 Antitrust Review Commentd Isid uggestiOi$e #0F imPtoSetfitC it #hbae gtaldel We entcouraged S Materialt end Plant Protection 10 General ot end guidss Wil be Revised. a. a41pp1rop1riete.

anll. to accommodate corn asmon ed ho wtcintormatiotn or e*perieot Ifowoer comments on Copies of published guides may be obtained by wistten .squett indicating Cth Ofu guide. A received within Oboinstwo month$ chatret. issuance. will be *at divisions desired to the U S Nuclear Regulators Commission Wshtington 0 C

ticfady orssIul Mtevaluating 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

(1975 $1000)

Total Equipment/Material Labor

386 201 587

15-gpm Evaporator

540 223 763

30-gpm Evaporator

655 233 888

50-gpm Evaporator

36 24 60

Evaporator Distillate Demineralizer

43 29 50

50-gpm Demineralizer

64 31 95

100-gpm Demineralizer

94 35 129

200-gpm Deminieralizer

102 44 146

400-gpm Demineralizer

108 56 164

100-gpm Precoat Filter

202 112 314

400-gpw Precoat Filter

13 11 24

20-gpm Cartridge Filter

100 38 138

2-gpm Reverse Osmosis

55 43 98

10,000-gal Tank

1.110-9

TABLE A-2 ANNUAL OPERATING COSTST - GASEOUS RADWASTE AUGMENTS

Total Operating Cost (1975 $lOOO/yr)

B r m m BWR Offgas Recoatbiner 3

3-ton Charcoal Adsorber neg Desiccant Dryer 3 Charcoal Vault Refrigeration 4 Main Condenser Vacuum Pump Charcoal/HEPA

Filtration System 0.4 Clean Steam to Turbine Glands 24 Clean Steam to Steam Valves, 24" and Larger 3 Clean Steam to Steam Valves, 2-1/2" and Less Than 24" 3

15,000-cfm HEPA Filtration System 6

1,000-cfm Charcoal/HEPA Filtration System 2

15,000-cfm Charcoal/HEPA Filtration System 7

30,000-cfm Charcoal/HEPA Filtration System 9 K

Turbine Bldg. Chilled Water HVAC System 49

3

600-ft Gas Decay Tank neg PWR Hydrogen Recombiner 4 PWR Air Ejector Charcoal/HEPA Filtration Unit 4 Steam Generator Flash Tank Vent to Main Condenser 1 ANNUAL OPERATING COSTS - LIQUID RADWASTE AUGMENTS

Evaporation - PWR Dirty Waste 50

Evaporation - BWR Dirty Waste 169 Evaporation - Condensate Polisher Chemical Waste 114 Evaporation - Detergent Waste 20

Demineralization - kvaporator Distillate 5 Demineralization - BWR 2nd Waste Demineralizer in Series 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

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 88

18 Demineralization - PWR Dirty Waste

95 Demineralization - PWR Turbine Bld

g. Drains

25 Desmineralization - PWR Steam Generator Blowdown

53 Precoat Filter - BWR Dirty Waste Cartridge Filter 7

7 Reverse Osmosis - Detergent Waste

1

10,000-gal Tank

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

FPC

Geographic Labor Cost Correction Region Factor I 1.6

1.5

1II

1.0

IV 1.4 V 1.1 VI 1.2 VII 1.3 Vlll 1.2 See Appendix B, "Labor Cost Correction Factors.'

See Figure A-1.

1.110-13

TABLE A-5 INDIRECT COST FACTORS

Type Radwaste System Indirect Cost Factor

"1. Single unit site, unitized radwaste system 1.75

2. Multi-unit site, shared radwaste system 1.75

3. Multi-unit site, unitized radwaste system 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 Capital Recovery Factor

(1 per year, i)

5 0.0651

0.0726

6

0.0806

7

0.0888

8

0.0973

9

0.1061

10

0.1150

11

0.1241

12

0.1334

13

0.1428

14

0.1523

15

Based on a service life of 30 years and the follwing equation:

CRF M + 1)3 (I + i)30-1

1.110-15

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-COOLEDS...... NUCLEAR

.................. REACTORSw Description of Augment RUD flffn.e D r.mh4n.... iCk.e. 11 BWR Off a %e Darr-M--- Ick- Wa,Ii DIRECT COST.(1975 $1000)

ITEM IARND r1 T DMUT'/MATrD TAt TflYAi BASIS FOR

I___MIXL_ 1 IVIML COST ESTIMATE

1. PROCESS EQUIPMENT 90 260 350 single unit, catalytic type w/heater and condenser, w/o instrumentation and controls, stainless steel, ASME VIII

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

a ASSOCIATED PIPING SYSTEMS

3. 18 12 30 augment piping connections only O

4. INSTRUM4ENTATION AND CONTROLS 24 96 120 allowance

5. ELECTRICAL SERVICE neq 4kw heaters on vessels neglected SPARE PARTS 85 85 75K for catalyst + 2% E/M in

6.

items 1 & 4 above SUBTOTAL 232 503 735

7. CONTINGENCY 23 50 73 10%

8. TOTAL DIRECT COSTS 2S5 553 808

(

r

A K I

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

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

2. MAINTENANCE MATERIAL AND. 20.0 routine conditioning of catalyst and LABOR equipment upkeep; 5% of E/M including I&C

3. CONSUMBLES, CHEMICALS, AND - initem 2

,01 C2 SUPPLIES

4. UTILITIES AND 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

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

m Description of Augment 3-ton Charcoal Adsorber (Sheet 1)

DIRECT COST (1975 $1000)

BASIS FOR

!TFM LABOR EOUIPMENTIMATERIALS TOTAL COST

- -

ESTIMATF

-- - - -

3

1. PROCESS EQUIPENT 5 44.0 49.0 carbon steel, 350 psig, 200 ft volume (augment to existing train of beds)

4. 4. 4. 4

2. BUILDING ASSIGNMENT 8 4.5 12.5 10' x 10' x 25' * $5/ft3 (turbine building shiel4ed area)

3. ASSOCIATED PIPING SYSTES - in item I

a

4. INSTRUKENTATION AND CONTROLS neg S. ELECTRICAL SERVICE neg

6. SPARE PARTS none existing SUBTOTAL 13 48.5 61.5

7. CONTINGENCY 1 5.0 6.0 10%

8. TOTAL DIRECT COSTS 14 53.5 67.5

. . .. . . . . r r r

K 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

1. OPERATING LABOR. SUPERVISION. neg AND OVERHEAD

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

3. CONSUMABLES. CHEMICALS, AND

SUPPLIES neg lifetime use of charcoal assumed I..

4. UTILITIES AND SERVICES

Waste Disposal Water Steam neg Electricity Building Services Other

5. TOTAL 0 AND M ANNUAL COST neg

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment Desiccant Drver fSheet !1 Desiccant Drver (Sheet I)

DIRECT COST (1975 $1000)

I TEN I ARflR T*TAI

BASIS FOR

1% IL COTETMT

1. PROCESS EQUIPMENT 25 75 100 redundant dryer vessels with

1 regeneration skid

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

3. ASSOCIATED PIPING SYSTEMS 10 5 15 augment piping connections only

8i

4. INSTRUMENTATION AND CONTROLS 12 48 60 allowance

5. ELECTRICAL SERVICE 18 17 35 service for heaters, blowers, pumps, and compressors

6. SPARE PARTS 3 3 SUBTOTAL 160 198 358

7. CONTINGENCY 16 20 36 10%

8. TOTAL DIRECT COSTS 176 218 394

( r r

K K 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)

Q*Pim I Ahfl flTIIP TflTAI BASIS FOR COST ESTIMATE

itri,,,

ITEM ........ . . . .

3.3 15 min/shift

1. OPERATING LABOR, SUPERVISION,

AND OVERHEAD

2. MAINTENANCE MATERIAL AND 6.1 5% of equipment including I&C

LABOR

3 CONSUMABLES, CHEMICALS, AND neg C SUPPLIES

U'

4. UTILITIES AND SERVICES

Waste Disposal neg operating time does not require neg significant utilities and services Water Steam Electricity neg Building Services Other S. TOTAL 0 AND M ANNUAL COST 9.4

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREAThENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment Charcoal Vault Refrigeration (Sheet 1)

DIRECT COST (1975 $1000)

BASIS FOR

ITEM TftTAI

LAORFlIITDUdCNT/UATCDTA1

10AM C YffASIfC et.V

1. PROCESS EQUIPMENT 10 75 85 10-ton capacity, 3 refrigerators with drives, 32°F design I t 4-4

2. BUILDING ASSIGNMENT 9 3 12 20' x 10' x 201 0 $2/ft 3 turbine building (nonshielded area)

0 3. ASSOCIATED PIPING SYSTEMS In item 1 N

14 Ch

4. INSTRUMENTATION AND CONTROLS 4 6 10 allowance

5. ELECTRICAL SERVICE 12 18 30 allowance

6. SPARE PARTS 3 3 SUBTOTAL 35 105 140

7. CONTINGENCY 3 11 14 10%

8. TOTAL DIRECT COSTS 38 116 154

(

K K 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)

COST (1975 $1000)

'TIn' rTeR TOTAL FOR COST !T1MATE

1. OPERATING LABOR, SUPERVISION. 3.3 15 min/shift AND OVERHEAD

2. MAINTENANCE MATERIAL AND

LABOR 3.7 51 of equlpemt

3. CONSUMABLES, CHEMICALS, AND in Item 2 SUPPLIES

4. UTILITIES AND SERVICES

Waste Disposal Water Steam 0.5 electricity and cooling water Electricity Building Services Other S. TOTAL 0 AND MANNUAL COST 7.5

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)

i n *

DIRECT COST (1975 $1000)

ITE4 I A*Q

BASIS FOR

LABOR__ ~ LrILumLAL IUIAL COST ESTIMATE

1. PROCESS EQUIPMENT 2 32.5 34.5 2000 CFM preftlter/4" charcoal bed/HEPA @ S15/cfm, 10 kw heater @ $250/kw

2. BUILDING ASSIGNMENT 3.1 1.5 4.6 Turbine building 8' x 16, x 12'

@ $3/ft 3 (nonshielded area)

Nm

3. ASSOCIATED PIPING' SYSTEMS 1.3 0,7 2.0 allowance wO

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%

8. TOTAL DIRECT COSTS 8.1 40.4 48.5

( (

K K K

ANNUAL OPERATING ANrMAINTENANCE 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 S...,iT*

RAmie FflQ tOI[IT F¢;TTMATF

I. OPERATING 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, CHEMICALS, AND initems 2 and 4 SUPPLIES

'.4

• 0

4. UTILITIES AND SERVICES

Waste Disposal 0.2 S50/HEPA filter, $100/Charcoal filter Water Steam Electricity Building Services Other

5. TOTAL 0 AND M ANNUAL COST 1.4

_______________________ I _________ ________ _______________________________

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment Clean Steam to Turbine Glands (Sheot 1)

DIRECT COST (1975 $1000)

FM FOIITDMFNTIMATPRTAI STTTflTAI BASIS FOR

• FnCT VCTttMATO

I ARAR

ITEMP

1. PROCESS EQUIPMENT 15 150 165 25,000 lb/hr reboiler I $4/lb/hr I

$25K/H.P. turbine glands

2. BUILDING ASSIGNMENT 19 10 29 20' x 30' x 16' 6 $3/ft3

3. ASSOCIATED PIPING SYSTEMS 32 18 50 equiv 1000 ft 0 $50/ft

4. INSTRUMENTATION AND CONTROLS 8 12 20 in addition to Item I

5. ELECTRICAL SERVICE nag

6. SPARE PARTS 5 5 SUBTOTAL 74 195 269

7. CONTINGENCY 7 20 27 10%

8. TOTAL DIRECT COSTS 81 215 296 r r C

K K

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT

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

I. OPERATING LABOR, SUPERVISION, 3.3 15 min/shift AND OVERHEAD

2. MAINTENANCE MATERIAL AND 4.0 40 man-days LABOR

3. CONSUMABLES, CHEMICALS, AND

SUPPLIES

9'

4. UTILITIES AND SERVICES

Waste Disposal Water Steam 21.0 10 Btu/kw-hr heat rate increase Electricity Building Services Other

5. TOTAL 0 AND M ANNUAL COST 28.3

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment Clean Steam to Steam Valves 24 " and Larger (Sheet 1)

DIRECT COST (1975 $1000)

ITEM I AMII n:*.:TDAACLIMATDTai BASIS FOR

TnTAI

I. PROCESS EQUIPMENT 100 120 220 22 valves @ $1OK/valve, use existing reboiler

2. BUILDING ASSIGNMENT neg install in existing space

3. ASSOCIATED PIPING SYSTEMS - in item 1

0

i%1J

4. INSTRUMENTATION AND CONTROLS - in Item 1 S. ELECTRICAL SERVICE neg

6. SPARE PARTS 5 SUBTOTAL 100 125 225

7. CONTINGENCY 10 12 22 10%

8. TOTAL DIRECT COSTS 110 137 247

( r

K -\

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

1. OPERATING LABOR, SUPERVISION, 3.3 15 min/shift AND OVERHEAD

2. MAINTENANCE MATERIAL AND 4.0 40 man-days LABOR

3. CONSUMABLES, CHEMICALS, AND neg SUPPLIES

w U,

4. UTILITIES hND SERVICES

Waste Disposal Water Steam neg Electricity Building Services Other TOTAL 0 AND M ANNUAL COST 7.3

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment Clean Steam to Steam Valves 2-1/2N and Less Than 24" (Sheet 1)

DIRECT COST (1975 $1000)

BASIS FOR

ITEM LAB OR EQUIPMENT/MATERIALS TOTAl_ (*fl[T F*TIUATF

COS ESTIMATE

TOTAL

1. PROCESS EQUIPMENT 0 120 120 100 valves 0 $1200 each

2. BUILDING ASSIGNMENT - - neg

-* 3. ASSOCIATED PIPING SYSTEMS 40 20 60

.

w

.h 4.6.

INSTRUMENTATION AND CONTROLS 10 20 30 allowance

5. ELECTRICAL SERVICE - none

7.e

6. SPARE PARTS - 6 6 SUBTOTAL 50 166 216

7. CONTINGENCY 5 17 22 10%

8. TOTAL DIRECT COSTS 55 183 238 I (

K A K

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT

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 TNTAI DA*f* *R r*eT r*w*a*P

1. OPERATING LABOR, SUPERVISION, 3.3 15 min/shift AND OVERHEAD

2. MAINTENANCE MATERIAL AND 12.0 1% of direct cost of equipment LABOR

3. CONSUMABLES, CHEMICALS, AND - in item 2 a SUPPLIES

-a U'

4. UTILITIES AND SERVICES

Waste Disposal Water Steam neg Electricity Building Services Other S. TOTAL 0 AND H ANNUAL COST 15.3

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment 15,000-cfm HEPA Filtration System - Auxiliary Building (Sheet 1)

DIRECT COST (1975 $1000)

BASIS FOR

I ADflD £rI"TDUCMT MATrTAI C TfllAI rACT rCTTMATr I I~p~

ERq~

r. flTl II Anna .r..

X rr...L./ - -. n nn. .- v, . ., . L

i-* ,

1. PROCESS EQUIPMENT 5 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

2.

(nonshielded area)

3. ASSOCIATED PIPING SYSTEMS 3 2.0 5.0

,o L.

a'

4. INSTRUMENTATION AND CONTROLS in item 1

5. ELECTRICAL SERVICE base

6. SPARE PARTS 0.5 0.5 SUBTOTAL 15 47.0 62.0

7. CONTINGENCY 1 5.0 6.0 10%

8. TOTAL DIRECT COSTS 16 52.0 68.0

( ( (

K T K !

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASrE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment 15,000-cfm HEPA Filtration System - Turbine Building (Sheet 2)

DIRECT COST (1975 $1000)

BASIS FOR

COST ESTIMATE

lI TDMCWNT IMATrOAIC

I AflI TflTAL

ITEM !L___ f ______________

5 40.0 45.0 skid mounted filter housing

1. PROCESS EQUIPMENT w/o fans

3

2.3 6.9 16' x 12' x 12' @ $3/ft

2. BUILDING ASSIGNMENT 4.6 (nonshielded area)

3. 3 2.0 5.0

ASSOCIATED PIPING SYSTEMS

-I

4. in item 1 INSTRUMENTATION AND CONTROLS

5. base ELECTRICAL SERVICE

6. 0 0.5 0.5 SPARE PARTS

SUBTOTAL 12.6 44.8 57.4

7. CONTINGENCY 2 4.0 6.0 10l a. TOTAL DIRECT COSTS 14.6 48.8 63.4

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 System (Sheet 3)

COST (1975 $1000)

ITEM LABOR OTI4FR TflTAI RACTC Frn rncT FCTIMATC

I. OPERATING LABOR, SUPERVISION, 3.8 15 min/shift + 40 hr annual test AND OVERHEAD

2. MAINTENANCE MATERIAL AND 2.2 change every 2 yrs @ $150/filter element LABOR

CONSUMABLES, CHEMICALS, AND

I

3. in items 2 and 4 SUPPLIES

4. UTILITIES AND SERVICES

Waste Disposal 0.8 $50/filter element Water Steam Electricity 1.0 additional fan electrical load Building Services Other

5. TOTAL 0 AND M ANNUAL COST 7.8 I_ (

K 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)

DIRECT COST (1975 $1000)

BASIS FOR

I TEM LABOR EOUIPMENT/MATERIALS TOTAL COST ESTIMATE

I. 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

2.

(nonshielded area)

3. ASSOCIATED PIPING SYSTEMS 1.3 .7 2.0

0

4. INSTRUMENTATION AND CONTROLS in item 1

5. ELECTRICAL SERVICE 1.5 1.0 2.5

6. SPARE PARTS 0.5 0.5 SUBTOTAL 8.6 26.2 34.8

7. CONTINGENCY 1.0 2.0 3.0 10%

8. TOTAL DIRECT COSTS 9.6 28.2 37.8

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

1. OPERATING LABOR, SUPERVISION, 1.9 20 min/day + 40 hr annual test AND OVERHEAD

2. MAINTENANCE 14ATERIAL AND .6 2 HEPA or prefilters @ $150 each and

1 charcoal @ $900 each every 2 yrs'

- 3. CONSUMABLES, CHEMICALS, AND in items 2 and 4 SUPPLIES

0

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

• ( --

__ (

K 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)

DIRECT COST (1975 $1000)

BASIS FOR

TTVM LABOR EQUIPMENT/MATERIALS TOTAL COST ESTIMATE

ITE

LABO.....

COST ESTIMATE

1. PROCESS EQUIPMENT 10 71 81 prefilter/4" charcoal/HEPA

@ $5/cfm, 30kw htr @ $200/kw BUILDING ASSIGNMENT 12 8 20 16' x 20' x 12' @ $5/ft 3

2.

(nonshielded area)

3. ASSOCIATED PIPING SYSTEMS 3 2 5 a

4. INSTRUMENTATION AND CONTROLS - In Item 1

5. ELECTRICAL SERVICE 3 2 5 allowance

6. SPARE PARTS 5 5 4 elements of each type SUBTOTAL 28 88 116

7. CONTINGENCY 3 9 12 10%

8. TOTAL DIRECT COSTS 31 97 128

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment 15,000-cfm Charcoal/HEPA Filtration System - Turbine Building (Sheet 2)

DIRECT COST (1975 $1000)

I TEM CN "I lDMrLT ATEDIlA1 C BASIS FOR

I fuND T*TAi ITEM I_____

ARAL?~urIIn~LJIUL x flMrnR UI

t. IWUTflYAI

1.3

1. PROCESS EQUIPMENT 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

2.

(nonshielded area)

3. ASSOCIATED PIPING SYSTEMS 3.0 2.0 5.0

0

.rg

4. INSTRUMENTATION AND CONTROLS in item 1

5. ELECTRICAL SERVICE 3.0 2.0 5.0 allowance

6. SPARE PARTS 5.0 5.0 4 elements each type SUBTOTAL 23.7 83.8 107.5

7. CONTINGENCY 2.0 9.0 11.0 10%

8. TOTAL DIRECT COSTS 25.7 92.8 118.5

( r (

K K

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

1. OPERATING LABOR. SUPERVISION, 3.8 15 min/shift & 40-hr annual test AND OVERHEAD

2. MAINTENANCE MATERIAL AND 9.0 30 HEPA or prefilters @ $150 each & 15 LABOR charcoal filters @ $900 each every 2 yrs

3. CONSUMABLES, CHEMICALS, AND in Items 2 and 4 SUPPLIES

0

4. 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

5. TOTAL 0 AND M ANNUAL COST 15.6

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment 30.00O-cfm Charcoal/HEPA Filtration System - Auxiliary Building (Sheet 1)

DIRECT COST (1975 $1000)

BASIS FOR

I ITU i ARng~

FoII PI4FNTII4ATFRIALS TOTAL COST ESTIMATE

-¶ a 1n FnrMN/AEIL

15 117.0 132.0 pref1lter/4" charcoal/HEPA

1. PROCESS EQUIPMENT @ $4/cfm, 60-kw htr @ $200/kw BUILDING ASSIGIMENT 20 13.6 33.6 28' x 20' x 12' $S5/ft3

2. (nonshielded area)

3. ASOCIATED PIPING SYSTEMS 5 3.0 8.0 base a

4. INSTRUMENTATION AND CONTROLS - in item I

5. ELECTRICAL SERVICE 6 4.0 10.0 allowance

6. SPARE PARTS 5.0 5.0 4 elements each type SUBTOTAL 46 142.6 188.6

7. CONTINGENCY 5 14.0 19.0 10%

8. TOTAL DIRECT COSTS 51 156.6 207.6

( C

y 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)

DIRECT COST (1975 $1000)

!OtITPHt¶!rT/ATrR TALS BASIS FOR

t*nlT F*TTMATF

ITEM LAROR TflTA[

1. PROCESS EQUIPMENT 15.0 117.0 132.0 prefilter/4" charcoal/HEPA

@ $4/cfm, 60kw htr

@ $200/kw

2. BUILDING ASSIGNMENT 13.4 6.8 20.2 28' x 20' x 12' @ $3/ft3 (nonshielded area)

3. ASSOCIATED PIPING SYSTEMS 3.0 5.0 8.0 base me

4. INSTRUMENTATION AND CONTROLS in item 1

5. ELECTRICAL SERVICE 6.0 4.0 10.0 allowance

6. SPARE PARTS 5.0 5.0 4 elements each type SUBTOTAL 37.4 137.8 175.2

7. CONTINGENCY 4.0 14.0 18.0 l0

8. TOTAL DIRECT COSTS 41.4 151.8 193.2

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

2. MAINTENANCE MATERIAL AND 18.0 60 HEPA or prefilters @ $150 each & 30

LABOR charcoal filters @ $900 each every 2 yrs

" 3. CONSUMABLES, CHEMICALS, AND - in items 2 and 4 SUPPLIES

4. 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

5. TOTAL 0 AND M ANNUAL COST 27.4

- :- t--.-J"

ý:r __ C

K K

11 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment Turbine Building Chilled Water HVAC System (Sheet 1)

DIRECT COST (1975 $1000)

EOUJIPMFNTIMATFRIALS BASIS FOR

ITEM LABOR TflTAI rnCT CTMATC

TnIMNIAEIL 1 nA

1. PROCESS EQUIPMENT 300 500 800 500-ton capacity, w/o air filters

-t + I

2. BUILDING ASSIG* *IENT Coolers can be Installed in existing space saved by deletion of ducting.

0

3. ASSOCIATED PIPING SYSTEM; - in item 1

-J

4. INSTRUMENTATION AND CONTROLS - in item 1

5. ELECTRICAL SERVICE 40 so 90

6. SPARE PARTS - 8 8 1%item 1 SUBTOTAL 340 558 898

7. CONTINGENCY 34 56 90 10l

8. TOTAL DIRECT COSTS 374 614 988

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

I. OPERATING LABOR, SUPERVISION, 3.3 15 min/shift AND OVERHEAD

2. MAINTENANCE MATERIAL AND 20.0 2-1/2% of equipment costs LABOR

.0

3. CONSUMABLES, CHEMICALS, AND - initem 2 SUPPLIES

0

4. 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 S. TOTAL 0 AND M ANNUAL COST 69.3 C C r

K

I

K K

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT. SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

3 Description of Augment 600-ft Waste Gas Decay Tank' (Sheet 1)

DIRECT COST (1975 $1000)

EOUIPMENT/MATERIALS BASIS FOR

I TFM LABOR TOTAL 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

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)

ITEM LABOR OTHER TOTAL RA;T* FflR i*lT r*T1MATr I. OPERATING LABOR, SUPERVISION,

AND OVERHEAD neg

2. MAINTENANCE MATERIAL AND

LABOR neg

3. CONSUMABLES, CHEMICALS, AND

0

SUPPLIES neg U'

0~e

4. UTILITIES AND SERVICES

Waste Disposal Water Steam neg Electricity Building Services Other

5. TOTAL 0 AND N ANNUAL COST neg

(

K K

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment PWR Hydrogen Recombiner (Sheet 1)

DIRECT COST (1975 $1000)

rflIITPMPINIMAT*RTAI

BASIS FOR

IT"M IARno TflTAI rnqT vtTTMATF

I l VT :fTI b V nA. I

1. PROCESS EQUIPMENT 50.0 300.0 350.0 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/ft3

2.

(shielded area)

3. ASSOCIATED PIPING SYSTEMS 32.0 13.0 45.0 allowance a

Ue

4. INSTRUMENTATION AND CONTROLS 10.0 40.0 50.0 allowance

5. ELECTRICAL SERVICE 13.0 12.0 25.0 allowance

6. SPARE PARTS - 2.0 2.0

SUBTOTAL 133.8 381.4 515.2

7. CONTINGENCY 13.0 38.0 51.0 101

8. TOTAL DIRECT COSTS 146.8 419.4 566.2

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

1. OPERATING LABOR, SUPERVISION, 3.3 15 min/shift AND OVERHEAD

2. MAINTENANCEMATERIAL AND. 10.0 3% of equipment cost LABOR

3. CONSUMABLES, CHEMICALS, AND 1.0 oxygen @.S2.5/103 cf & .25 cfm 0

SUPPLIES 7000 hrs Ca I

U'

4. UTILITIES AND SERVICES

Waste Disposal Water Steam neg Electricity Building Services Other S. TOTAL 0 AND M ANNUAL COST 14.3 K C

K*

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment PWR Air EJector Charcoal/HEPA Filtration Unit (Sheet 1)

DIRECT COST (1975 $1000)

BASIS FOR

ITEM LABOR EOUIPMENT/MATERIALS TOTAL COST ESTIMATE

1*

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 15' @ $3/ft (unshielded turbine bldg)

3. ASSOCIATED PIPING SYSTEMS 2.0 1.0 3.0 allowance L*a

4. INSTRUMENTATION AND CONTROLS 0.5 1.5 2.0 allowance

5. ELECTRICAL SERVICE 0.5 0.5 1.0 allowance

6. SPARE PARTS 1.0 1.0

SUBTOTAL 9.0 13.0 22.0

7. CONTINGENCY 1.0 1.0 2.0 1O0

8. 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 flTIFD TnTAI DAete * * rP*eUA*

.....________________

___ I* , L ueA5 rwK Guil r.4IrMIE

l. OPERATING LABOR, 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 EP

SUPPLIES

U'

4. UTILITIES AND SERViCES

Waste Disposal neg Water Steam Electricity Building Services Other

5. TOTAL 0 AND M ANNUAL COST 5.8 K

K K

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment Steam Generator Flash Tank Vent to Main Condenser (Sheet 1)

DIRECT COST (1975 $1000)

BASIS FOR

ITEM LABOR EQUIPMENT/MATERIALS TOTAL COST ESTIMATE

I. PROCESS EQUIPMENT - no equipment required

2. BUILDING ASSIGNMENT neg install In existing space

3. ASSOCIATED PIPING SYSTEMS 13 7 20 200 ft of 10-in pipe with

2 valves U't ull

4. INSTRUMENTATION AND CONTROLS 4 6 10 allowance

5. ELECTRICAL SERVICE neg

6. SPARE PARTS neg SUBTOTAL 17,, 13 30

7. CONTINGENCY 2 1 3 10%

8. TOTAL DIRECT COSTS 19 14 33

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

1. OPERATING LABOR, SUPERVISION, 1 allowance AND OVERHEAD

2. MAINTENANCE MATERIAL AND 1 2% Total Direct Cost LABOR

3. CONSUHABLES, CHEMICALS, AND neg

.a SUPPLIES

U'

4. UTILITIES AND SERVICES

Waste Disposal Water neg Steam Electricity Building Services Other

5. TOTAL 0 AND H ANNUAL COST 2

( (

K

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment lSqpm Evaporator (Sheet 1)

DIRECT COST (1975 $1000)

BASIS FOR

ITI'N I AnRO T*TA!

1. PROCESS EQUIPMENT 30 225 255 skid mounted, bundle, submerged ASME VIII, tubein Incoloy contact with process fluid

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 a. 3. ASSOCIATED PIPING SYSTEMS 35 30 65 inludes service 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 SUBTOTAL 183 351 534

7. CONTINGENCY 18 35 53 10%

8. TOTAL DIRECT COSTS 201 386 587

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREAThENT'SYSTEM

FOR LIGHT-WdATER-COOLED NUCLEAR REACTORS

Description of Augment 30-gpm Evaporator (Sheet 2) ,

DIRECT COST (1975 $1000)

tTrW BASIS FOR

rncT rCY?UAYT

I AfPtflD rfIITDfMlrTIMATrDTAI TnTA,

• .- -..rw-f .dV..r b.r I ... u snlrl.# ,nI . bl r~l) I lruI

1. PROCESS EQUIPMENT 30 350 380 ASME VIII

skid mounted, submerged,

'tube bundle, Incoloy in contact with process fluid t

2. BUILDING ASSIGNMgNT 88 44 132 evap + services - 25' x 40' x 20'

@ $6/ft3 plus 2,000 ft 3 Increase In solid waste storage area

3. ASSOCIATED PIPING SYSTEMS 35 35 70 includes service piping CO

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 SUBTOTAL 203 491 694

7. CONTINGENCY 20 49 69 1O0

8. TOTAL DIRECT COSTS 223 540 763 C C

K

'III

T

3)

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMErNT SYSTEM

(Sheet

50-gpmFOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Augment of Evaporator Description Description of Augment 50-qpm Evaporator (Sheet 3)

DIRECT COST (1975 $1000)

BASIS FOR

ITEM LABOR EOUIPMENT/MATERIALS TOTAL COST ESTIMATE

1. PROCESS EQUIPMENT 30 450 480 ASME VIII

skid mounted, submerged, tube bundle, Incoloy In contact with process fluid

2. BUILDING ASSIGNMENT 97 48 145 10% more than 30 gpm

3. ASSOCIATED PIPING SYSTEMS 35 35 70 allowance a

• 0 4. INSTRUMENTATION AND CONTROLS 10 10 20 allowance S. ELECTRICAL SERVICE 40 25 65 allowance

6. SPARE PARTS. 27 27 2% of Item 1 plus tube bundle SUBTOTAL 212 595 807

7. CONTINGENCY 21 60 81 10%

8. TOTAL- DIRECT COSTS 233 655 888

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment FuannAtnY - RUR Dirty Ua~tm - Finn, fl,.n1,, (k..t £1 COST (1975 $1000)

ITEM LABOR OT14ER TOTAL BASIS FOR LOST FSTIMATF

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

2. MAINTENANCE MATERIAL AND 30 7-1/2% of equipment cost LABOR

3. CONSUMABLES, CHEMICALS, AND neg concentrate solidification chemicats SUPPLIES in item 4

4. UTILITIES AND SERVICES 3 Waste Disposal 70 100:1 feed to concentrate ratio @ 20/ft 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

5. TOTAL 0 AND M ANNUAL COST 199 C C

K* K

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment Evaporator PWR Dirty Waste (Sheet 5)

COST (1975 $1000)

lTYM [AROR OTHER TOTAL BASIS FOR COST ESTTMATE

I. OPERATING LABOR, SUPERVISION,

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

2. MAINTENANCE MATERIAL AND

LABOR 30.0 7-1/2% of equipment cost

3. CONSUMABLES, CHEMICALS, AND - concentrate solidification chemicals

0'

SUPPLIES in item 4

4. UTILITIES AND SERVICES 3

50:1 feed to concentrate ratio @ $20/ft Waste Disposal 27.0 disposal cost Water 5.0 1000 gpm @.277 hrs @ 30t/1000 gal Steam 12.0 277 hrs steam @S20,000 4bs/hr @$2/1000 lbs Electricity Building Services Other

5. TOTAL 0 AND MANNUAL COST 80.0

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment v

EvaDorator

- Condenser Polisher Chemical IaCto Ih +0A

COST (1975 $1000)

ITEM LAI*R NTH*D T*TAI

LABOR 0ATD AU .,* TC4TAI FRUK CS

LU ETIMATE

1. OPERATING LABOR, SUPERVISION,

AND OVERHEAD 6.0 650.000 gpy; 500 hr/yr labor

2. MAINTENANCE MATERIAL AND

LABOR 30.0 7-1/2% of equipment cost

3. CONSUMABLES, CHEMICALS. AND concentrate solidification chemicals

0 SUPPLIES In item 4

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

5. TOTAL 0 AND M ANNUAL COST 143.9

( C

K K

ANNUAL OPERATING AND MAI[NTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment .an - hla~aum*., Um.4.a Iqkaa÷ 7*

COST (1975. $1000)

TT!M LABOR OTHER TOTAL BASIS FOR COST ESTIMATE

I. OPERATING LABOR, SUPERVISION,

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

2. MAINTENANCE MATERIAL AND

LABOR 30.0 7-1/25 of equipment cost

3. CONSUMABLES, CHEMICALS, AND - concentrate solidification chemicals In ad SUPPLIES item 4 a, UTILITIES AND SERVICES

LeD

4. WasteITsposal 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

5. TOTAL 0 AND MANNUAL COST 49.8

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment Evaporator Distillate Demineralizer (Sheet 1)

DIRECT COST (1975 $1000)

TTIrM I anAD EniI nlrT IUA?~nAi e qrft*IrA I

BASIS FOR

• ,-. I.rluvn Iuu~rnllu~r'¶l KhMiLR IJI/L W,5MIIEIHMAIT

1. PROCESS EQUIPMENT 4.0 20.0 24.0 30 ft 3 , SS. ASME VIII, 150 psi nonregenerative, w/resin

2. BUILDING ASSIGNMENT 6.4 3.2 9.6 10' x 10' x 16' @ $6/ft3 (shielded area)

3. ASSOCIATED PIPING SYSTEMS 9.0 6.0 15.0 2" piping i

Ot

4. INSTRUMENTATION AND CONTROLS 2.0 3.0 5.0 remote conductivity readout

5. ELECTRICAL SERVICE neg

6. SPARE PARTS 1.0 1.0

SUBTOTAL 21.4 33.2 54.6

7. CONTINGENCY 2.0 3.0 5.0 10%

8. TOTAL DIRECT COSTS 23.4 36.2 59.6

( C (

)

K

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT

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 ____________

I. OPERATING LABOR, SUPERVISION. 1.8 1500 hrs operation @ 10% attendance AND OVERHEAD

2. MAINTENANCE MATERIAL AND

LABOR 2.0 allowance

3. CONSUMABLES, CHEMICALS, AND

,ap SUPPLIES 2.3 1 change per yr @ $75/ft 3

4. UTILITIES AND SERVICES

Waste Disposal 0.6 30 ft 3

@ $20/ft 3 disposal cost Water Steam Electricity Building Services Other

5. TOTAL 0 AND M ANNUAL COST 6.7

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment 50-opDemintralzer Sh t 1)

{Sheet 1)

SO-gin .D*l.n.fraltzer DIRECT COST (1975 $1000)

BASIS FOR

ITEM LAROR 1ITOM AUIFRAI It TIhTAI CflCY

1T

tMAr"

1. PROCESS EQUIP4ENT 5 20.0 25.0 30 ft 3. SS, A*NE VIII. 150 psi, nonreganerative, with resin

2. BUILDING ASSIGNMENT 9 4.8 13.8 12' x 12' x 16' 0 $6/ft3 (shielded ar*)

3. ASSOCIATED PIPING SYSTEMS 9 6.0 15.0 2" piping

4. INSTRUMENTATION AND CONTROLS 4 6.0 10.0

5. ELECTRICAL SERVICE No

6. SPARE PARTS 2.0 2.0 miscellaneous supplies SUBTOTAL 27 38.8 66.8

7. CONTINGENCY 2 4.0 6.0 10%

8. TOTAL DIRECT COSTS 29 42.8 - 71.8

( C C

K K

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment 1O0-9pm Deminerallizer (Sheet 2)

DIRECT COST (1975 $1000)

FO*l PMFNT/MATFRTALS BASIS FOR

tT*M LANOR TOTAL COST FSTTMATF

I. PROCESS EQUIPMENT 5 35.0 40.0 60 ft 3 , SS, ASME VIII, 150 psi, nonregenerative, with resin

2. BUILDING ASSIGNMENT 9 4.8 13.8 12' x 12' x 16' 0 $6/ft3 (shielded area)

3." ASSOCIATED PIPING SYSTEMS 10 10.0 20.0 2-1/21 piping a, 4. INSTRUMENTATION AND CONTROLS 4 6.0 10.0

.1

5. ELECTRICAL SERVICE neg

6. SPARE PARTS 2.0 2.0 miscellaneous supplies SUBTOTAL 28 57.8 85.8

7. CONTINGENCY 3 6.0 9.0

B. TOTAL DIRECT COSTS 31 63.8 94.8

TOTAL DIRECT COST ESTIMATE SHEET OF RADWAST!E TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment 20-plDmneralizer(Sheet 3) 3)__

(Sheet

200-gpm Oemtneraltzer DIRECT COST (1975 $1000)

EflUIPI4FNTII4ATFRTAL * BASIS FOR

ITEM LABOR TflTAI rnCT r~tTuATr

1T A

1. PROCESS EQUIPMENT 5 60.0 65.0 120 ft 3 , SS, ASME VIII, i50 psi, nonregenerative, with resin

2. BUILDING ASSIGNMENT 11 5.2 16.2 13' x 13' x 16' 0 $6/ft 3

___(shielded area)

3. ASSOCIATED PIPING SYSTEMS 12 12.0 24.0 4" piping

4. INSTRUMENTATION AND CONTROLS 4 6.0 10.0

5. ELECTRICAL SERVICE neg

6. SPARE PARTS 2.0 2.0 miscellaneous supplies SUBTOTAL 32 85.2 117.2

7. CONTINGENCY 3 9.0 12.0

8. TOTAL DIRECT COSTS 35 94.2 129.2

( (

K

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment 400-gpm Demineralizer - Steam Generator Blowdown Service (Sheet 4)

DIRECT COST (1975 $1000)

BASIS FOR

I TrM lAROR EOUJIPMNT/MATERjALS TOTAL COST ESTIMATE

T I COST ESTIMATE

3

1. PROCESS EQUIPMENT 5 60.0 65.0 120 ft , SS. ASME VIII, 150 psi, nonregenerative. with resin BUILDING ASSIGNMENT 11 5.2 16.2 ,3' x 13' x 16' @ $6/ft 3

2.

(shielded area)

3. ASSOCIATED PIPING SYSTEMS 20 20.0 40.0 6" piping a,

'a

4. INSTRUMENTATION AND CONTROLS 4 6.0 10.0 allowance

5. ELECTRICAL SERVICE neg

6. SPARE PARTS 2.0 2.0 miscellaneous supplies SUBTOTAL 40 93.2 133.2

7. CONTINGENCY 4 9.0 13.0

8. TOTAL DIRECT COSTS 44 102.2 146.2

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 lABOR NTNrD TJlTA!

_...._-_....__,,__ ,v-n -

aAeT*

DROIO

• n* *

rvr uK EV)lr.1~PY.I

PP*guA*P

1. OPERATING LABOR, SUPERVISION, 3.3 15 min/shift AND OVERHEAD

2. MAINTENANCE MATERIAL AND

LABOR 5.0 allowance

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

-.J

a

4. UTILITIES AND SERVICES

Waste Disposal 2.4 120 ft 3 lyr * $20/ft 3 disposal cost Water Steam Electricity Building Services Other

5. TOTAL 0 AND M ANNUAL COST 19.7 C

K I

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)

YYIPLu AILr nV IlV%

I am*o -

flTurD

lll_ __ _

?linI

Ifl, matie fflS EflM? rCTTMATe

&'flC I l bl *fll

1. OPERATING LABOR, SUPERVISION, 1.8 10% of DRS shim bleed (50,000 gpy),

AND OVERHEAD 30 min/day

2. MAINTENANCE MATERIAL AND

LABOR 5.0 allowance

3

3. CONSUMABLES,

SUPPLIES CHEMICALS, AND 2.3 30 3ft /yr @ $75/ft3 a

4. UTILITIES AND SERVICES

Waste Disposal 0.6 30 ft 3/yr @ $20/ft3 disposal cost Water Steam Electricity Building Services Other S. TOTAL 0 AND M ANNUAL COST 9.7

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 I. OPERATING LABOR, SUPERVISION,

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

2. MAINTENANCE MATERIAL AND

LABOR 5.0 allowance CONSUNABLES, CHEMICALS, AND33

3. SUPALES 64.5 860 ft 3 resin 0 $75/ft 3 N

4. UTILITIES AND SERVICES

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

--- I C 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

l. OPERATING LABOR, SUPERVISION,

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

2. MAINTENANCE MATERIAL AND

LABOR 5.0 allowance

3. CONSUMABLES, CHEMICALS, AND

SUPPLIES 12.0 160 ft 3 /yr @ $75/ft 3 a

4. UTILITIES AND SERVICES

Waste Disposal 3.2 160 ft 3 /yr @ $20/ft 3 disposal cost water Steam Electricity Building Services Other

5. TOTAL 0 AND M ANNUAL COST 23.5

ANNUAL OPERATIN AND MAINTE*ANCE COST ESTIMTE SHEET OF RADWASTE TREATMENT

SYSTEM FOR L.IGHT,oWATER-COOLEO NUCL..EAR,, REACTORS

D*crlrintinn of Aujnmant flminapA147AP . DUo

• 7m,

• **,*,-* pww- - . T. * a w,*g uu,,*U-I

• fm rC1 uVfm "a 1.411W4b 7I

COST (1975 $1000)

ITEM I ARMR flTIIFA Ti*TAI oAeTe * *Ae* rPgvu4*

-- .... ______ ",,' ,,,.

..-. urwl, rvuK I.UF)I LtIY:llrl

1. OPERATING LABOR, SUPERVISION.

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

2. MAINTENANCE MATERIAL AND

LABOR 5.0 allowance

3. CONSUMABLES, CHEMICALS, AND

a SUPPLIES 64.5 660 ft 3 resin 0 $75/ft 3

4. UTILITIES AND SERVICES

Waste Disposal 17.2 860 ft 3/yr 9 $20/ft 3 disposal cost Water Steam Electricity Building Services Other S. TOTAL 0 AND N ANNUAL COST 99.8

( .-."(

-1-:j:.1i-:i...-

........ r

K

A..UAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment Demineralizer - PIER Steam Generator Blowdomn (Sheet 10)

COST (1975 $1000)

tim I alLfl9 nyu,..O inaI ma*tt ens rtnt ReTtMAta OPERATING LABOR, SUPERVISION.

AND OVERHEAD 3.3 15 min/shift

2. MAINTENANCE MATERIAL AND

LABOR 5.0 allowance

3. CONSUMABLES, CHEMICALS, AN"

a SUPPLIES 16.9 225 ft 3 resin/yr @$75/ft3

4. UTILITIES AND SERVICES

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

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment 20-qp Cartridge Filter (Sheet 1) 1)

Ftlter (Sheet

20-qm Cartrtd9e DIRECT COST (1975 $1000)

TTFM I AI*fl2 vN Itur

¶ u'IIAqr rD lr e BASIS FOR

... t.J ~vrl.rnlr.lL*nL T*Ai UIhLU 11MAT

1. 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

2.

(shielded area)

3. ASSOCIATED PIPING SYSTEMS 1.5' 1.0 2.5 allowance

-. 4 Q

at 4. INSTRUMENTATION AND CONTROLS 0.6 2.4 3.0 allowance

5. ELECTRICAL SERVICE neg

6. SPARE PARTS 0.5 0.5 SUBTOTAL 9.7 11.9 21.6

7. CONTINGENCY 1.0 1.0 2.0 10%

8. TOTAL DIRECT COSTS 10.7 12.9 23.6

(

TREATMENT

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment Cartridge Filter (Sheet 2)

COST (1975 $1000)

A'1JCDl T*TAI RAM!S FOR COST ESTIMATE

ITEM LADUK uini n , -... . ..... .... ... ..

4.5 10 changes @ 10 man-hrs/change

1. OPERATING LABOR. SUPERVISION, @ $12/hr + 15 min/shift AND OVERHEAD

2. MAINTENANCE MATERIAL AND allowance

1.0

LABOR

3. CONSUMABLES. CHEMICALS, AND 10 changes/yr @$100/change

1.0

SUPPLIES

4. UTILITIES AND SERVICES 3

1.5 10 drums/yr @$20/ft Waste Disposal Water Steam Electricity Building Services Other

8.0

5. TOTAL 0 AND MANNUAL COST

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREAT1ENT SYSTEM

i FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment 100-gpim Precoat Filter (Shoot 1)

1)

Ftlter (Sheet lO0-gpm Precoat DIRECT COST (1975 $1000)

fIW01T

P~NT uI~dTIDTAI BASIS FOR

ITEM LARnR T*TAI

1. 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

2.

(shielded area)

3. ASSOCIATED PIPING SYSTEM4S 16 9.0 25 35% of equipment cost

0

4. INSTRUMENTATION AND CONTROLS in item 1

5. ELECTRICAL SERVICE 7 13.0 20 allowance

6. SPARE PARTS 2.0 2 2% of item 1 SUBTOTAL 51 98.0 149

7. CONTINGENCY 5 10.0 15 10%

8. TOTAL DIRECT COSTS 56 108.0 164

( r

K K

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

2)

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment 400-oam Precoat Filter (Sheet 2)

-vT

(Sheet DIRECT COST (1975 $1000)

BASIS FOR

TT*M LAROR EOUIPMENT/MATERIALS TOTAL COST ESTIMATE

PROCESS EQUIPMENT 35 135.0 170 automated system; 1 gpm/ft 2

1. ASME Viii

3 BUILDING ASSIGNMENT 24 12.0 36 15' x 20' x 20' @ $6/ft

2. (shielded area)

3. ASSOCIATED PIPING SYSTEMS 31 16.0 47 35% of equipment cost

-J

4. INSTRUMENTATION AND CONTROLS - - item I

5. ELECTRICAL SERVICE 12 18.0 30 allowance

6. SPARE PARTS - 3.0 3 SUBTOTAL 102 184.0 286

7. CONTINGENCY 10 18.0 28 10%

8. TOTAL DIRECT COSTS 112 202.0 314

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

1. OPERATING LABOR, SUPERVISION,

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

2. MAINTENANCE MATERIAL AND

LABOR 10.0 allowance

3. CONSUMABLES, CHEMICALS, AND 6.0 10 lbs precoat @ lOt/lb per 1000 gal SUPPLIES processed

4. UTILITIES AND SERVICES 3 Waste Disposal 40.0 1 ft 3/sludge per 1000 qal processed @ $30/ft disposal cost Water Steam Electricity Building Services Other S. TOTAL 0 AND M ANNUAL COST j[ 62.6

( C

T K

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment 2-com Reverse Osmosis (Sheet 1)

DIRECT COST (1975 $1000)

BASIS FOR

TTIFM LABOR FOUlPMENTIMATFRIALS TOTAL COST ESTIMATF

1. PROCESS EQUIPIENT 6.0 60.0 66.0 skid mounted w/500-gal SS

feed tank, ASME VIII

2. BUILDING ASSIGNMENT 19.2 9.6 28.8 12' x 25' x 16' @ $6/ft 3

3. ASSOCIATED PIPING SYSTEMS 3.0 2.0 5.0 allowance

0

4. INSTRUMENTATION AND CONTROLS in item I

5. ELECTRICAL SERVICE 7.0 13.0 20.0 allowance

6. SPARE PARTS 6.0 6.0

SUBTOTAL 35.2 90.6 125.8

7. CONTINGENCY 3.0 9.0 12.0 10%

8. TOTAL DIRECT COSTS 38.2 99.6 137.8

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

1. OPERATING LABOR, SUPERVISION,

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

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

3. CONSUMABLES, CHEMICALS. AND

SUPPLIES neg No

4. UTILITIES AND SERVICES

Waste Disposal 4.3 100:1 vol reduction @ $20/ft 3 disposal cost Water Steam Electricity neg Building Services Other

5. TOTAL 0 AND MANNUAL COST 16.2

( r C

1)

TOTAL DIRECT (Sheet COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

10tOOO-GallonTapk Description of Augment 1O,000-Gallon Tank__(Sheet 1)

DIRECT COST (1975 $1000)

!0IJ!P?4fNT/MATERIALS BASIS FOR

?tTrM I AROR TOTAL COST ESTIMATE

T -

3 28 31 SS, ASME VIII, atmospheric

1. PROCESS EQUIPMENT

service, 200°F

BUILDING ASSIGNMENT 30 15 45 15' x 20' x 25' @ $6/ft3

2.

(shielded area)

3. ASSOCIATED PIPING SYSTEMS 2 1 3 10% of item 1 C

w 4. INSTRUMENTATION AND CONTROLS 4 6 10 allowance

5. ELECTRICAL SERVICE neg

6. SPARE PARTS neg SUBTOTAL 39 s0 89

7. CONTINGENCY 4 5 9 10%

8. TOTAL DIRECT COSTS 43 55 98

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 rfl*T r*TUATr

1. OPERATING LABOR, SUPERVISION.

AND OVERHEAD 1.1 5 min/shift - log level readings

2. MAINTENANCE MATERIAL AND

LABOR 1.6 1/2% of equipment

3. CONSUMABLES. CHEMICALS, AND neg SUPPLIES

4. UTILITIES AND SERVICES

Waste Disposal Water Steam neg Electricity Building Services Other

5. TOTAL 0 AND N ANNUAL COST 2.7

(

REFERENCES TO APPENDIX B

NUS-531,

1. "Guide for Economic Evaluation of Nuclear Reactor Plant Oesigns," USAEC Report NUS Corporation, January 1969.

2. "Wage Rates for Key Construction Trades," Engineering News Record, pp. 36-37, January 2, 1975.

- 2000,"

3. "Projections of Labor Requirements for Electric Power Plants Construction, 1974 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 DIRECT COST (1975 $1000)

BASIS FOR

i Tru 1 AflfD

FflIIIPMFNT/MATFRlALS TOTAL COST ESTIMATE

i aunD EnUTPMENTIMATERIALS

1. PROCESS EQUIPMENT

t I 1 I

2. BUILDING ASSIGNMENT

I I I I

0 3. ASSOCIATED PIPING SYSTEMS

I I I I --

4. INSTRUMENTATION AND CONTROLS

I I I I

S. ELECTRICAL SERVICE

I I I I

6. SPARE PARTS

______________________I i mI

SUBTOTAL

________________________________________________________ 1 -I I I

7. CONTINGENCY

I I I

8. TOTAL DIRECT COSTS

________________________________________________________ ________________ I __________________________________________________ _____________ _______________________________________________

( C C

K

0

"I

U

2 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT

2

-4 SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

U

2

2 Description of Augment C,

a

9 COST (1975 $1000)

9 I TIFM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE

'a ITEM

w

-J

04

1. OPERATING LABOR, SUPERVISION,

AND OVERHEAD

0.j

'a

"4 a.

0

"4

2. MAINTENANCE MATERIAL AND

LABOR

U3.

4.

CONSUMABLES,

SUPPLIES

CHEMICALS, AND

UTILITIES AND SERVICES

Waste Disposal Water Steam Electricity Building Services Other

5. TOTAL 0 AND M ANNUAL COST