Regulatory Guide 1.110
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| Issue date: | 10/07/2013 |
| From: | Office of Nuclear Regulatory Research |
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| RG-1.110, Rev 1 | |
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U.S. NUCLEAR REGULATORY COMMISSION October 2013 OFFICE OF NUCLEAR REGULATORY RESEARCH Revision 1 REGULATORY GUIDE
REGULATORY GUIDE 1.110
COST-BENEFIT ANALYSIS FOR RADWASTE SYSTEMS FOR
LIGHT-WATER-COOLED NUCLEAR POWER REACTORS
A. INTRODUCTION
Purpose The U.S. Nuclear Regulatory Commission (NRC) staff has developed a series of guides that provide methods acceptable to the staff for calculating 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 methods and procedures that the staff of the NRC
considers acceptable for performing a cost-benefit analysis for liquid and gaseous radwaste system components for light-water-cooled nuclear power reactors.
Applicable Rules and RegulationsSection II.D of Appendix I, Numerical Guides for Design Objectives and Limiting Conditions for Operation to Meet the Criterion As Low As Is Reasonably Achievable for Radioactive Material in Light-Water-Cooled Nuclear Power Reactor Effluents, to part 50, Licensing of Production and Utilization Facilities, of Title 10 of the Code of Federal Regulations (10 CFR) (Ref. 1), 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, canfor a favorable cost-benefit ratiolead to reductions in dose to the population reasonably expected to be within an 80 kilometers (50 miles) of the reactor. Values of $1,000
per man-rem (roentgen equivalent man) and $1,000 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 II.A,
II.8, and II.C (which address doses to nearby individuals) is required to meet the criterion, as low as is reasonably achievable.
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 or licensee in meeting the requirements of Appendix I. As a result of such reviews, it is expected that alternative acceptable methods for Written suggestions regarding this guide or development of new guides may be submitted through the NRCs public Web site under the Regulatory Guides document collection of the NRC Library at http://www.nrc.gov/reading-rm/doc-collections/reg-guides/contactus.html.
Electronic copies of this regulatory guide, previous versions of this guide, and other recently issued guides are available through the NRCs public Web site under the Regulatory Guides document collection of the NRC Library at http://www.nrc.gov/reading-rm/doc-collections/.
The regulatory guide is also available through the NRCs Agencywide Documents Access and Management System (ADAMS) at http://www.nrc.gov/reading-rm/adams.html, under ADAMS Accession No. ML13241A052.
calculation will be made available to applicants or licensees, and that calculational procedures found to be unnecessary will be eliminated.
Related Guidance Regulatory Guide 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 (Ref. 2), describes methods for the calculation of preoperational estimates of effluents releases, dispersion of the effluent in the atmosphere and different water bodies, and estimation of the associated radiation doses to man.
It also suggests parameters for the estimation of radiation doses to man from effluent releases.
Regulatory Guide 1.111, Methods for Estimating Atmospheric Transport and Dispersion of Gaseous Effluents in Routine Releases from Light-Water-Cooled Reactors (Ref. 3), describes basic features of calculation models and assumptions for the estimation of atmospheric transport and dispersion of gaseous effluents in routine releases from land-based light-water-cooled reactors.
Regulatory Guide 1.112, Calculation of Releases of Radioactive Materials in Gaseous and Liquid Effluents from Light-Water-Cooled Power Reactors (Ref. 4), references NUREG-0016, Calculation of Releases of Radioactive Materials in Gaseous and Liquid Effluents from Boiling-Water Reactors (BWR-GALE Code), and NUREG-0017, Calculation of Releases of Radioactive Materials in Gaseous and Liquid Effluents from Pressurized-Water Reactors (PWR-GALE Code), to provide methods for calculating annual average expected releases of radioactive material in gaseous and liquid effluents from light-water-cooled nuclear power reactors.
Regulatory Guide 1.113, Estimating Aquatic Dispersion of Effluents from Accidental and Routine Reactor Releases for the Purpose of Implementing Appendix I (Ref. 5), describes basic features of calculational models and suggests methods of determining values of model parameters for the estimation of aquatic dispersion of both routine and accidental releases of liquid effluents.
Purpose of Regulatory Guides The NRC issues regulatory guides to describe to the public methods that the staff considers acceptable for use in implementing specific parts of the agencys regulations, to explain techniques that the staff uses in evaluating specific problems or postulated accidents, and to provide guidance to applicants and licensees. Regulatory guides are not substitutes for regulations and compliance with them is not required. Methods and solutions that differ from those set forth in regulatory guides will be deemed acceptable if they provide a basis for the findings required for the issuance or continuance of a permit or license by the Commission.
Paperwork Reduction Act This regulatory guide contains information collection requirements covered by 10 CFR Part 50
that the Office of Management and Budget (OMB) approved under OMB control number 3150-0011.
The NRC may neither conduct nor sponsor, and a person is not required to respond to, an information collection request or requirement unless the requesting document displays a currently valid OMB control number.
Rev. 1 of RG 1.110, Page 2
TABLE OF CONTENTS
Page
A. INTRODUCTION
................................................................................................................................... 1 Purpose......................................................................................................................................... 1 Applicable Rules and Regulations ............................................................................................... 1 Related Guidance ......................................................................................................................... 2 Purpose of Regulatory Guides ..................................................................................................... 2 Paperwork Reduction Act ............................................................................................................ 2
B. DISCUSSION
.......................................................................................................................................... 4 Reason for Revision ..................................................................................................................... 4 Background .................................................................................................................................. 4 Harmonization with International Standards ............................................................................... 4 C. STAFF REGULATORY GUIDANCE .................................................................................................... 4
D. IMPLEMENTATION
.............................................................................................................................. 5 Use by Applicants and Licensees................................................................................................. 5 Use by NRC Staff ........................................................................................................................ 6 REFERENCES ......................................................................................................................................... 7 Appendix A: Procedures for Performing Cost-Benefit Analyses ............................................................ A-1 Appendix B: Bases for Parameters Used in Performing Cost-Benefit Analysis....................................... B-1 Appendix C: Data Needed for Radwaste Treatment System Cost-Benefit Analysis for Light-Water- Cooled Nuclear Reactors .................................................................................................... C-1 LIST OF TABLES
Page A-1 Direct Costs-Gaseous Radwaste Augments, Liquid Radwaste Augments .................................. A-2 A-2 Annual Operating Costs-Gaseous Radwaste Augments, Liquid Radwaste Augments ............... A-4 A-3 Annual Maintenance Costs-Gaseous Radwaste Augments, Liquid Radwaste Augments .......... A-5 A-4 Labor Cost Correction Factors ..................................................................................................... A-7 A-5 Indirect Cost Factors .................................................................................................................... A-7 A-6 Capital Recovery Factors ............................................................................................................. A-8 B-1 Indirect Costs ............................................................................................................................... B-2 LIST OF FIGURES
Page A-1 Electric Power Supply Areas in the United States ....................................................................... A-9 Rev. 1 of RG 1.110, Page 3
B. DISCUSSION
Reason for Revision The NRC revised RG 1.110 to incorporate editorial changes and the current format for regulatory guides. These changes were intended to improve clarity and did not alter the staff regulatory guidance.
Background Each applicant for a permit to construct or a license to operate a light-water-cooled nuclear power reactor and each holder of 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 initial liquid and gaseous radwaste system designs at the time of licensing and, if these designs are subsequently modified, that the design objectives are reassessed to ensure that they are maintained. 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 10 CFR Part 50, to demonstrate that the plant design includes all items of reasonably demonstrated technology for reducing the cumulative population dose caused by releases of radioactive materials from the reactor to levels as low as reasonably achievable. As an interim measure, the Commission chose values of $1,000 per-man-rem and $1,000 per man-thyroid-rem (or lesser values if demonstrated to be suitable for a particular 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 staffs 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 equipment 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, maintenance, 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.
Harmonization with International Standards The NRC staff reviewed guidance from the International Atomic Energy Agency (IAEA) and did not identify any standards that provided useful guidance to NRC staff, applicants, or licensees.
C. STAFF REGULATORY GUIDANCE
1. In accordance with Section II.D, Appendix I, to 10 CFR Part 50, each applicant for a permit to construct or a license to operate a light-water-cooled nuclear power reactor and each holder of a license to operate 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 an
80-kilometer (50-mile) radius of the reactor site cannot be effected at an annual cost of $1,000 per man-rem or $1,000 per man-thyroid-rem (or such lesser costs as demonstrated to be suitable for a particular case).
Rev. 1 of RG 1.110, Page 4
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 $1,000 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 or licensee should provide a complete evaluation, including methodology used, components considered, and all assumptions and parameters used. Information to be submitted by the applicant or licensee 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 or licensees and those by the NRC staff. Because of this, these parameters and assumptions should be clearly described and substantiated by the applicant or licensee.
D. IMPLEMENTATION
The purpose of this section is to provide information on how applicants and licensees 1 may use this guide and information regarding the NRCs plans for using this regulatory guide. In addition, it describes how the NRC staff complies with 10 CFR 50.109, Backfitting, and any applicable finality provisions in 10 CFR Part 52, Licenses, Certifications, and Approvals for Nuclear Power Plants.
Use by Applicants and Licensees Applicants and licensees may voluntarily 2 use the guidance in this document to demonstrate compliance with the underlying NRC regulations. Methods or solutions that differ from those described in this regulatory guide may be deemed acceptable if they provide sufficient basis and information for the NRC staff to verify that the proposed alternative demonstrates compliance with the appropriate NRC
regulations. Current licensees may continue to use guidance the NRC found acceptable for complying with the identified regulations as long as their current licensing basis remains unchanged.
Licensees may use the information in this regulatory guide for actions that do not require NRC
review and approval such as changes to a facility design under 10 CFR 50.59, Changes, Tests, and Experiments. Licensees may use the information in this regulatory guide or applicable parts to resolve regulatory or inspection issues.
1 In this section, licensees refers to licensees of nuclear power plants under 10 CFR Parts 50 and 52; and the term applicants refers to applicants for licenses and permits for (or relating to) nuclear power plants under 10 CFR
Parts 50 and 52 and applicants for standard design approvals and standard design certifications under 10 CFR Part 52.
2 In this section, voluntary and voluntarily mean that the licensee is seeking the action of its own accord, without the force of a legally binding requirement or an NRC representation of further licensing or enforcement action.
Rev. 1 of RG 1.110, Page 5
Use by NRC Staff The NRC staff does not intend or approve any imposition or backfitting of the guidance in this regulatory guide. The NRC staff does not expect any existing licensee to use or commit to using the guidance in this regulatory guide, unless the licensee makes a change to its licensing basi
s. The NRC
staff does not expect or plan to request licensees to voluntarily adopt this regulatory guide to resolve a generic regulatory issue. The NRC staff does not expect or plan to initiate NRC regulatory action that would require the use of this regulatory guide. Examples of such unplanned NRC regulatory actions include issuance of an order requiring the use of the regulatory guide, requests for information under
10 CFR 50.54(f) as to whether a licensee intends to commit to use of this regulatory guide, generic communication, or promulgation of a rule requiring the use of this regulatory guide without further backfit consideration.
During regulatory discussions on plant-specific operational issues, the staff may discuss with licensees various actions consistent with staff positions in this regulatory guide as one acceptable means of meeting the underlying NRC regulatory requirement. Such discussions would not ordinarily be considered backfitting even if prior versions of this regulatory guide are part of the licensing basis of the facility. However, unless this regulatory guide is part of the licensing basis for a facility, the staff may not represent to the licensee that the licensees failure to comply with the positions in this regulatory guide constitutes a violation.
If an existing licensee voluntarily seeks a license amendment or change and (1) the NRC staffs consideration of the request involves a regulatory issue directly relevant to this new or revised regulatory guide and (2) the specific subject matter of this regulatory guide is an essential consideration in the staffs determination of the acceptability of the licensees request, then the staff may request that the licensee either follow the guidance in this regulatory guide or provide an equivalent alternative process that demonstrates compliance with the underlying NRC regulatory requirements. This is not considered backfitting as defined in 10 CFR 50.109(a)(1) or a violation of any of the issue finality provisions in
If a licensee believes that the NRC is either using this regulatory guide or requesting or requiring the licensee to implement the methods or processes in this regulatory guide in a manner inconsistent with the discussion in this Implementation section, then the licensee may file a backfit appeal with the NRC in accordance with the guidance in NUREG-1409, Backfitting Guidelines (Ref. 6), and the NRC
Management Directive 8.4, Management of Facility-Specific Backfitting and Information Collection (Ref. 7).
Rev. 1 of RG 1.110, Page 6
3 REFERENCES
1. Code of Federal Regulations (CFR), Title 10, Energy, Part 50, Domestic Licensing of Production and Utilization Facilities.
2. U.S. Nuclear Regulatory Commission (NRC), Regulatory Guide 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, Washington, DC.
3. NRC, Regulatory Guide 1.111, Methods for Estimating Atmospheric Transport and Dispersion of Gaseous Effluents in Routine Releases from Light-Water-Cooled Reactors, Washington, DC.
4. NRC, Regulatory Guide 1.112, Calculation of Releases of Radioactive Materials in Gaseous and Liquid Effluents from Light-Water-Cooled Power Reactors, Washington, DC.
5. NRC, Regulatory Guide 1.113, Estimating Aquatic Dispersion of Effluents from Accidental and Routine Reactor Releases for the Purpose of Implementing Appendix I, Washington, DC.
6. NRC, NUREG-1409, Backfitting Guidelines, Washington, DC.
7. NRC, Management Directive 8.4, Management of Facility-specific Backfitting and Information Collection, Washington, DC.
3.
Publicly available NRC-published documents are available electronically through the NRC Library on the NRCs public Web site at http://www.nrc.gov/reading-rm/doc-collections/ and through the NRCs Agencywide Documents Access and Management System (ADAMS) at http://www.nrc.gov/reading-rm/adams.html. The documents can also be viewed online or printed for a fee in the NRCs Public Document Room (PDR) at 11555 Rockville Pike, Rockville, MD. For problems with ADAMS, contact the PDR staff at 301-415-4737 or 800-397-4209; or e-mail pdr.resource@nrc.gov.
Rev. 1 of RG 1.110, Page 7
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 (roentgen equivalent man) 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 that have the potential to reduce releases of radioactive materials.
3. Acceptable methods for performing some of the calculations needed 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. They are also included in two regulatory guides now in preparation on the subjects of (1) calculation of releases of radioactive materials in liquid and gaseous 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 (TDC):
(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 geographical 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 TDC.
b. Obtain-the appropriate Indirect Cost Factor (ICF) from Table A-5.
c. Determine Total Capital Cost (TCC) by using the equation:
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
Appendix A to RG 1.110, Page A-1
f. Obtain the Annual Operating Cost (AOC) and the Annual Maintenance Cost (AMC) from Tables A-2 and A-3. Multiunit 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 $1,000 per-man-rem and/or $1,000 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.
Table A-1. Direct CostsGaseous Radwaste Augments, Liquid Radwaste Augments DIRECT COSTSGASEOUS RADWASTE AUGMENTS
EQUIPMENT/ (1975 $1,000)
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/ 40 8 48 HEPA Filtration System Clean Steam to Turbine Glands 81 215 296 Clean Steam to Steam Valves, 24" and Larger 137 110 247 Clean Steam to Steam Valves, 21/2" and 183 55 238 Less Than 24"
15,000-cfm HEPA Filtration System 52(49)a 16(14)a 68(63)a
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-ft3 Gas Decay Tank 33 24 57 Appendix A to RG 1.110, Page A-2
DIRECT COSTSGASEOUS RADWASTE AUGMENTS
EQUIPMENT/ (1975 $1,000)
MATERIAL LABOR TOTAL
PWR Hydrogen Recombiner 419 147 566 PWR Air Ejector Charcoal/HEPA Filtration Unit 14 10 24 Steam Generator Flash Tank Vent to Main 19 14 33 Condenser a. 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.
Direct CostsLiquid Radwaste Augments EQUIPMENT/ (1975 $1,000)
MATERIAL LABOR TOTAL
15-gpm Evaporator 386 201 587
30-gpm Evaporator 540 223 763
50-gpm Evaporator 655 233 888 Evaporator Distillate Demineralizer 36 24 60
50-gpm Demineralizer 43 29 50
100-gpm Demineralizer 64 31 95
200-gpm Demineralizer 94 35 129
400-gpm Demineralizer 102 44 146
100-gpm Precoat Filter 108 56 164
400-gpm Precoat Filter 202 112 314
20-gpm Cartridge Filter 13 11 24
2-gpm Reverse Osmosis 100 38 138
10,000-gal Tank 55 43 98 Appendix A to RG 1.110, Page A-3
Table A-2. Annual Operating CostsGaseous Radwaste Augments, Liquid Radwaste Augments Annual Operating CostsaGaseous Radwaste Augments TOTAL OPERATING
COST (1975 $1,000/YR)
BWR Offgas Recombiner 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 Turbine Bldg. Chilled Water HVAC System 49
600-ft3 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 CostsLiquid Radwaste Augments TOTAL OPERATING
COST (1975 $1,000/YR)
EvaporationPWR Dirty Waste 50
EvaporationBWR Dirty Waste 169 EvaporationCondensate Polisher Chemical Waste 114 EvaporationDetergent Waste 20
DemineralizationEvaporator Distillate 5 Appendix A to RG 1.110, Page A-4
Annual Operating CostsLiquid Radwaste Augments TOTAL OPERATING
COST (1975 $1,000/YR)
DemineralizationBWR 2nd Waste Demineralizer in Series 15 DemineralizationPWR Clean Waste 5 DemineralizationBWR Dirty Waste 88 DemineralizationPWR Dirty Waste 18 DemineralizationPWR Turbine Bldg. Drains 95 DemineralizationPWR Steam Generator Blowdown 25 Precoat FilterBWR Dirty Waste 53 Cartridge Filter 7 Reverse OsmosisDetergent Waste 7
10,000-gal Tank 1 a.
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.
Table A-3. Annual Maintenance CostsGaseous Radwaste Augments, Liquid Radwaste Augments ANNUAL MAINTENANCE COSTSGASEOUS RADWASTE AUGMENTS
TOTAL OPERATING
COST (1975 $1,000/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
15,000-cfm Charcoal/HEPA Filtration System 9 Appendix A to RG 1.110, Page A-5
ANNUAL MAINTENANCE COSTSGASEOUS RADWASTE AUGMENTS
TOTAL OPERATING
COST (1975 $1,000/YR)
30,000-cfm Charcoal/HEPA Filtration System 18 Turbine Bldg. Chilled Water HVAC System 20
600-ft3 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 Demineralizer 5
100-gpm Demineralizer 5
200-gpm Demineralizer 5
100-gpm Precoat Filter 10
400-gpm Precoat Filter 10
20-gpm Cartridge Filter 1
2-gpm Reverse Osmosis 9
10,000-gal Tank 2 Appendix A to RG 1.110, Page A-6
a Table A-4. Labor Cost Correction Factors FPC b GEOGRAPHIC LABOR COST
REGION CORRECTION FACTOR
I 1.6 II 1.5 III 1.0
IV 1.4 V 1.1 VI 1.2 VII 1.3 VIII 1.2 a.
See Appendix B, Labor Cost Correction Factors.
b.
See Figure A-1.
Table A-5. Indirect Cost Factors TYPE RADWASTE SYSTEM INDIRECT COST FACTOR
1. Single unit site, unitized a radwaste 1.75 system
2. Multiunit site, shared radwaste system 1.75
3. Multiunit site, unitizeda radwaste system 1.75 + ( n 1)1.5 n
where n is the number of unitized radwaste systems at the site a.
Each reactor has a separate, nonshared radwaste system.
Appendix A to RG 1.110, Page A-7
Table A-6. Capital Recovery Factors COST OF MONEY
(% PER YEAR, I) CAPITAL RECOVERY FACTORa
5 0.0651
6 0.0726
7 0.0806
8 0.0888
9 0.0973
10 0.1061
11 0.1150
12 0.1241
13 0.1334
14 0.1428
15 0.1523 a.
Based on a service life of 30 years and the following equation:
i(1 + i )30
CRF =
(1 + i)30 1 Appendix A to RG 1.110, Page A-8
Appendix A to RG 1.110, Page A-9 Figure A-1. Electric Power Supply Areas in the United States
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 locations are considered. 4 All costs are based on the assumption that the reactor is in the design stage and that augmentation of a radwaste system will not involve backfitting of an existing plant. 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 generally follow the U.S. Nuclear Regulatory Commission (NRC)/U.S. Atomic Energy Commission 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 5 are included in the direct costs. Total capital costs are obtained by multiplying direct costs by an indirect cost factor.
2. Direct Costs 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 system quality assurance, materials, and seismic design. Space requirements were determined based on manufacturers 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-1 of Appendix A by calculating the average labor cost for selected cities (Ref. 2)
in each area and adjusting this cost for estimated variations in labor productivity due only to differences in labor practices in the regions considered. Manpower costs were calculated 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 Location effects of the eight FPC Power Supply areas are estimated and shown in Table A-4 of Appendix A.
5 Contingency onsite labor and process equipment and material are all based on l0 percent.
Appendix B to RG 1.110, Page B-1
4. Indirect Cost Factor Indirect costs as a percentage of direct costs are calculated in Table B-1.
Table B-
1. Indirect Costs
1ST UNIT, PERCENTAGE SUBSEQUENT UNITS,
OF DIRECT COST PERCENTAGE OF DIRECT COST
Construction facilities, 10 5 equipment, and services Engineering and construction 20 10
management services Other owners costs 10 5 Interest during construction 35a 35a Total 75 55 a.
Based on a 10 percent per year interest rate and a 4-year construction time for radwaste systems only. Interest during construction is estimated to be 25 percent of direct costs plus other indirect costs. This is equivalent to
35 percent of the direct costs.
The indirect escalators (factors) were estimated from preliminary architect and engineering data to be used to update the Oak Ridge National Laboratory concept and ORCOST computer codes.
5. Operation and Maintenance Costs Annual expenses for operation and maintenance (O&M) of the radwaste treatment systems were estimated for baseload power plants operating at 80 percent capacity factor. Manpower and supply costs were estimated by considering equipment functions in each case. Expenses for gases, steam, resins, auxiliary power, 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 radwaste system (e.g., effect of an evaporator augment on the solid waste system). 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 that takes into account the cost of borrowed money and the depreciation of assets. It is calculated from the expression:
i(1 + i) n
(1 + i) n 1 Appendix B to RG 1.110, Page B-2
Where:
i = cost of borrowed money expressed as a decimal n = plant operating lifetime (yr)
In calculating the values used in Table A-5 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.
LIST OF APPENDIX B COST ESTIMATE SHEETS
BWR Offgas Recombiner ............................................................................................................ B-4
3-ton Charcoal Adsorber .............................................................................................................. B-6 Desiccant Dryer ........................................................................................................................... B-8 Charcoal Vault Refrigeration ..................................................................................................... B-10
Charcoal/HEPA Filtration System - Condenser Vacuum Pump ............................................... B-12 Clean Steam to Turbine Glands ................................................................................................. B-14 Clean Steam to Steam Valves 24" and Larger ........................................................................... B-16 Clean Steam to Steam Valves 21/2" and less than 24\ ................................................................. B-18
15,000-cfm HEPA Filtration System ......................................................................................... B-20
1000-cfm Charcoal/HEPA Filtration System ............................................................................ B-23
15,000-cfm HEPA Filtration System ......................................................................................... B-25
30,000-cfm Charcoal/HEPA Filtration System ......................................................................... B-28 Turbine Building Chilled Water HVAC System ....................................................................... B-31
600-ft3 Waste Gas Decay Tank .................................................................................................. B-33 PWR Hydrogen Recombiner ..................................................................................................... B-35 PWR Air Ejector Charcoal/HEPA Filtration Unit ..................................................................... B-37 Steam Generator Flash Tank Vent to Main Condenser ............................................................. B-39 Evaporators ................................................................................................................................ B-41 Evaporator Distillate Demineralizer .......................................................................................... B-48 Demineralizers ........................................................................................................................... B-50
Cartridge Filter ........................................................................................................................... B-60
Precoat Filters ............................................................................................................................ B-62 Reverse Osmosis ........................................................................................................................ B-65
10,000-Gallon Tank ................................................................................................................... B-67 Appendix B to RG 1.110, Page B-3
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR
LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment BWR Offgas Recombiner (Sheet 1)
DIRECT COST (1975 $1,000)
EQUIPMENT/ BASIS FOR COST
ITEM LABOR MATERIALS TOTAL 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 50 150 30 x 40 x 25 @ $5/ft3 (turbine building shielded area)
3. ASSOCIATED PIPING SYSTEMS 18 12 30 augment piping connections Appendix B to RG 1.110, Page B-4 only
4. INSTRUMENTATION AND CONTROLS 24 96 120 allowance
5. ELECTRICAL SERVICE - - neg 4kw heaters on vessels neglected
6. SPARE PARTS - 85 85 75K for catalyst + 2% E/M in items 1 & 4 above SUBTOTAL 232 503 735
7. CONTINGENCY 23 50 73 10%
8. TOTAL DIRECT COSTS 255 553 808
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)
DIRECT COST (1975 $1,000)
BASIS FOR COST
ITEM LABOR OTHER TOTAL ESTIMATE
1. OPERATING LABOR, SUPERVISION, 3.3 15 min/shift AND OVERHEAD
2. MAINTENANCE MATERIAL AND 20.0 routine conditioning of catalyst LABOR and equipment upkeep; 5% of E/M including I&C
3. CONSUMABLES, CHEMICALS, AND - in item 2 SUPPLIES
4. UTILITIES AND SERVICES
Appendix B to RG 1.110, Page B-5 Waste Disposal Water Steam neg intermittent; 4kw heater load is negligible Electricity Building Services Other
5. TOTAL O AND M ANNUAL COST 23.3
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-
WATER-COOLED NUCLEAR REACTORS
Description of Augment 3-ton Charcoal Adsorber (Sheet 1)
DIRECT COST (1975 $1,000)
EQUIPMENT/ BASIS FOR COST
ITEM LABOR MATERIALS TOTAL ESTIMATE
1. PROCESS EQUIPMENT 5 44.0 49.0 carbon steel, 360 psig, 200 ft3 volume (augment to existing train of beds)
2. BUILDING ASSIGNMENT 8 4.5 12.5 10 x 10 x 25 @ $5/ft3 (turbine building shielded area)
3. ASSOCIATED PIPING SYSTEMS - - - in item 1
4. INSTRUMENTATION AND CONTROLS - - neg Appendix B to RG 1.110, Page B-6
5. 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
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)
DIRECT COST (1975 $1,000)
BASIS FOR COST
ITEM LABOR OTHER TOTAL ESTIMATE
1. OPERATING LABOR, SUPERVISION, neg AND OVERHEAD
2. MAINTENANCE MATERIAL AND neg allowance of 3% of equipment LABOR cost is negligible
3. CONSUMABLES, CHEMICALS, AND neg lifetime use of charcoal assumed SUPPLIES
4. UTILITIES AND SERVICES neg Appendix B to RG 1.110, Page B-7 Waste Disposal Water Steam neg Electricity Building Services Other
5. TOTAL O AND M ANNUAL COST neg
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-
WATER-COOLED NUCLEAR REACTORS
Description of Augment Desiccant Dryer (Sheet 1)
DIRECT COST (1975 $1,000)
EQUIPMENT/ BASIS FOR COST
ITEM LABOR MATERIALS TOTAL ESTIMATE
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/ft3 turbine building (shielded area)
3. ASSOCIATED PIPING SYSTEMS 10 5 15 augment piping connections only
4. INSTRUMENTATION AND CONTROLS 12 48 60 allowance Appendix B to RG 1.110, Page B-8
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
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE
TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment Desiccant Dryer (Sheet 2)
DIRECT COST (1975 $1,000)
BASIS FOR COST
ITEM LABOR OTHER TOTAL ESTIMATE
1. OPERATING LABOR, SUPERVISION, 3.3 15 min/shift AND OVERHEAD
2. MAINTENANCE MATERIAL AND 6.1 5% of equipment including I&C
LABOR
3. CONSUMABLES, CHEMICALS, AND neg SUPPLIES
4. UTILITIES AND SERVICES
Appendix B to RG 1.110, Page B-9 Waste Disposal neg operating time does not require significant utilities and services Water neg Steam Electricity neg Building Services Other
5. TOTAL O AND M ANNUAL COST 9.4
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-
WATER-COOLED NUCLEAR REACTORS
Description of Augment Charcoal Vault Refrigeration (Sheet 1)
DIRECT COST (1975 $1,000)
EQUIPMENT/ BASIS FOR COST
ITEM LABOR MATERIALS TOTAL ESTIMATE
1. PROCESS EQUIPMENT 10 75 85 10-ton capacity, 3 refrigerators with drives, 32°F design
2. BUILDING ASSIGNMENT 9 3 12 20 x 10 x 20 @ $2/ft3 turbine building (nonshielded area)
3. ASSOCIATED PIPING SYSTEMS in item 1
4. INSTRUMENTATION AND CONTROLS 4 6 10 allowance Appendix B to RG 1.110, Page B-10
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
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE
TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment Charcoal Vault Refrigeration (Sheet 2)
DIRECT COST (1975 $1,000)
BASIS FOR COST
ITEM LABOR OTHER TOTAL ESTIMATE
1. OPERATING LABOR, SUPERVISION, 3.3 15 min/shift AND OVERHEAD
2. MAINTENANCE MATERIAL AND 3.7 5% of equipment LABOR
3. CONSUMABLES, CHEMICALS, AND in item 2 SUPPLIES
4. UTILITIES AND SERVICES
Appendix B to RG 1.110, Page B-11 Waste Disposal Water Steam 0.5 electricity and cooling water Electricity Building Services Other
5. TOTAL O AND M ANNUAL 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)
DIRECT COST (1975 $1,000)
EQUIPMENT/ BASIS FOR COST
ITEM LABOR MATERIALS TOTAL ESTIMATE
1. PROCESS EQUIPMENT 2 32.5 34.5 2,000 CFM prefilter/4" charcoal bed/HEPA @ $15/cfm, 10 kw heater @ $250/kw
2. BUILDING ASSIGNMENT 3.1 1.5 4.6 Turbine building 8 x 16 x 12
@ $3/ft3 (nonshielded area)
3. ASSOCIATED PIPING SYSTEMS 1.3 0.7 2.0 allowance
4. INSTRUMENTATION AND CONTROLS in item 1 Appendix B to RG 1.110, Page B-12
5. ELECTRICAL SERVICE 1 1.5 2.5
6. SPARE PARTS 0.5 0.5 SUBTOTAL 7.4 36.7 44.1
7. CONTINGENCY 0.7 3.7 4.4 10%
8. TOTAL DIRECT COSTS 8.1 40.4 48.5
ANNUAL OPERATING AND 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)
DIRECT COST (1975 $1,000)
BASIS FOR COST
ITEM LABOR OTHER TOTAL ESTIMATE
1. OPERATING LABOR, SUPERVISION, neg used only during startup and AND OVERHEAD shutdown
2. MAINTENANCE MATERIAL AND 1.2 4 HEPA filters @ $150 &
LABOR 2 Charcoal filters @ $900,
change every 2 years
3. CONSUMABLES, CHEMICALS, AND - in items 2 and 4 SUPPLIES
4. UTILITIES AND SERVICES
Appendix B to RG 1.110, Page B-13 Waste Disposal 0.2 $50/HEPA filter, $100/Charcoal filter Water Steam Electricity Building Services Other
5. TOTAL O AND M ANNUAL COST 1.4
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-
WATER-COOLED NUCLEAR REACTORS
Description of Augment Clean Steam to Turbine Glands (Sheet 1)
DIRECT COST (1975 $1,000)
EQUIPMENT/ BASIS FOR COST
ITEM LABOR MATERIALS TOTAL ESTIMATE
9. PROCESS EQUIPMENT 15 150 165 25,000 lb/hr reboiler @ $4/lb/hr
& $25K/H.P. turbine glands
10. BUILDING ASSIGNMENT 19 10 29 20 x 30 x 16 @ $3/ft3
11. ASSOCIATED PIPING SYSTEMS 32 18 50 equiv 1,000 ft @ $50/ft
12. INSTRUMENTATION AND 8 12 20 in addition to item 1 CONTROLS
Appendix B to RG 1.110, Page B-14
13. ELECTRICAL SERVICE neg
14. SPARE PARTS - 5 5 SUBTOTAL 74 195 269
15. CONTINGENCY 7 20 27 10%
16. TOTAL DIRECT COSTS 81 215 296
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)
DIRECT COST (1975 $1,000)
BASIS FOR COST
ITEM LABOR OTHER TOTAL 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
SUPPLIES
4. UTILITIES AND SERVICES
Appendix B to RG 1.110, Page B-15 Waste Disposal Water Steam 21.0 10 Btu/kw-hr heat rate increase Electricity Building Services Other
5. TOTAL O 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 $1,000)
EQUIPMENT/ BASIS FOR COST
ITEM LABOR MATERIALS TOTAL ESTIMATE
1. PROCESS EQUIPMENT 100 120 220 22 valves @ $1,0k/valve, use existing reboiler
2. BUILDING ASSIGNMENT neg install in existing space
3. ASSOCIATED PIPING SYSTEMS - in item 1
4. INSTRUMENTATION AND CONTROLS - in item 1 Appendix B to RG 1.110, Page B-16
5. ELECTRICAL SERVICE neg
6. SPARE PARTS - 5 5 SUBTOTAL 100 125 225
7. CONTINGENCY 10 12 22 10%
8. TOTAL DIRECT COSTS 110 137 247
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 24" and Larger (Sheet 2)
DIRECT COST (1975 $1,000)
BASIS FOR COST
ITEM LABOR OTHER TOTAL ESTIMATE
6. OPERATING LABOR, SUPERVISION, 3.3 15 min/shift AND OVERHEAD
7. MAINTENANCE MATERIAL AND 4.0 40 man-days LABOR
8. CONSUMABLES, CHEMICALS, AND neg SUPPLIES
9. UTILITIES AND SERVICES
Appendix B to RG 1.110, Page B-17 Waste Disposal Water Steam neg Electricity Building Services Other
10 TOTAL O 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 21/2" and less than 24" (Sheet 1)
DIRECT COST (1975 $1,000)
EQUIPMENT/ BASIS FOR COST
ITEM LABOR MATERIALS TOTAL ESTIMATE
1. PROCESS EQUIPMENT 0 120 120 100 valves @ $1,200 each
2. BUILDING ASSIGNMENT - - neg
3. ASSOCIATED PIPING SYSTEMS 40 20 60
4. INSTRUMENTATION AND CONTROLS 10 20 30 allowance
5. ELECTRICAL SERVICE - none Appendix B to RG 1.110, Page B-18
6. SPARE PARTS - 6 6 SUBTOTAL 50 166 216
7. CONTINGENCY 5 17 22 10%
8. TOTAL DIRECT COSTS 55 183 238
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 21/2" and less than 24" (Sheet 2)
DIRECT COST (1975 $1,000)
BASIS FOR COST
ITEM LABOR OTHER TOTAL ESTIMATE
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 SUPPLIES
4. UTILITIES AND SERVICES
Appendix B to RG 1.110, Page B-19 Waste Disposal Water Steam neg Electricity Building Services Other
5. TOTAL O AND M 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 $1,000)
EQUIPMENT/ BASIS FOR COST
ITEM LABOR MATERIALS TOTAL ESTIMATE
1. PROCESS EQUIPMENT 5 40.0 45.0 prefilter/HEPA @ $3/cfm, use existing fan
2. BUILDING ASSIGNMENT 7 4.5 11.5 16 x 12 x 12 @ $5/ft3 (nonshielded area)
3. ASSOCIATED PIPING SYSTEMS 3 2.0 5.0
4. INSTRUMENTATION AND CONTROLS in item 1 Appendix B to RG 1.110, Page B-20
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
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-
WATER-COOLED NUCLEAR REACTORS
Description of Augment 15,000-cfm HEPA Filtration System - Turbine Building (Sheet 2)
DIRECT COST (1975 $1,000)
EQUIPMENT/ BASIS FOR COST
ITEM LABOR MATERIALS TOTAL ESTIMATE
1. PROCESS EQUIPMENT 5 40.0 45.0 skid mounted filter housing w/o fans
2. BUILDING ASSIGNMENT 4.6 2.3 6.9 16 x 12 x 12 @ $3/ft3 (nonshielded area)
3. ASSOCIATED PIPING SYSTEMS 3 2.0 5.0
4. INSTRUMENTATION AND CONTROLS in item 1 Appendix B to RG 1.110, Page B-21
5. ELECTRICAL SERVICE base
6. SPARE PARTS 0 0.5 0.5 SUBTOTAL 12.6 44.8 57.4
7. CONTINGENCY 2 4.0 6.0 10%
8. 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)
DIRECT COST (1975 $1,000)
BASIS FOR COST
ITEM LABOR OTHER TOTAL ESTIMATE
1. 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 LABOR element
3. CONSUMABLES, CHEMICALS, AND - in items 2 and 4 SUPPLIES
4. UTILITIES AND SERVICES
Appendix B to RG 1.110, Page B-22 Waste Disposal 0.8 $50/filter element Water Steam Electricity 1.0 additional fan electrical load Building Services Other
5. TOTAL O AND M ANNUAL COST 7.8
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 $1,000)
EQUIPMENT/ BASIS FOR COST
ITEM LABOR MATERIALS TOTAL ESTIMATE
1. PROCESS EQUIPMENT 2.0 22.0 24.0 prefilter/4" charcoal/HEPA @
$20/cfm, 5 kw htr @ $400/kw
2. BUILDING ASSIGNMENT 3.8 2.0 5.8 8 x 12 x 12 @ $5/ft3 (nonshielded area)
3. ASSOCIATED PIPING SYSTEMS 1.3 0.7 2.0
4. INSTRUMENTATION AND CONTROLS - in item 1 Appendix B to RG 1.110, Page B-23
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)
DIRECT COST (1975 $1,000)
BASIS FOR COST
ITEM LABOR OTHER TOTAL ESTIMATE
1. OPERATING LABOR, SUPERVISION, 1.9 20 min/day + 40 hr annual test AND OVERHEAD
11. MAINTENANCE MATERIAL AND 0.6 2 HEPA or prefilters @ $150
LABOR each and 1 charcoal @ $900
each every 2 years
12. CONSUMABLES, CHEMICALS, AND in items 2 and 4 SUPPLIES
13. UTILITIES AND SERVICES
Appendix B to RG 1.110, Page B-24 Waste Disposal 0.1 $50/HEPA or prefilter,
$100/charcoal filter Water Steam Electricity neg Building Services Other
14. TOTAL O AND M ANNUAL COST 2.6
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 $1,000)
EQUIPMENT/ BASIS FOR COST
ITEM LABOR MATERIALS TOTAL ESTIMATE
1. PROCESS EQUIPMENT 10 71 81 prefilter/4" charcoal/HEPA @
$5/cfm, 30kw htr @ $200/kw
2. BUILDING ASSIGNMENT 12 8 20 16 x 20 x 12 @ $5/ft3 (nonshielded area)
3. ASSOCIATED PIPING SYSTEMS 3 2 5
4. INSTRUMENTATION AND CONTROLS - in item 1 Appendix B to RG 1.110, Page B-25
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 HEPA Filtration System - Turbine Building (Sheet 2)
DIRECT COST (1975 $1,000)
EQUIPMENT/ BASIS FOR COST
ITEM LABOR MATERIALS TOTAL ESTIMATE
1. PROCESS EQUIPMENT 10.0 71.0 81.0 prefilter/4" charcoal/HEPA @
$5/cfm, 30 kw htr @ $200/kw
2. BUILDING ASSIGNMENT 7.7 3.8 11.5 16 x 20 x 12 @ $3/ft3 (nonshielded area)
3. ASSOCIATED PIPING SYSTEMS 3.0 2.0 5.0
4. INSTRUMENTATION AND CONTROLS in item 1 Appendix B to RG 1.110, Page B-26
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
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)
DIRECT COST (1975 $1,000)
BASIS FOR COST
ITEM LABOR OTHER TOTAL 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
LABOR each & 15 charcoal filters @
$900 each every 2 years
3. CONSUMABLES, CHEMICALS, AND - in items 2 and 4 SUPPLIES
4. UTILITIES AND SERVICES
Appendix B to RG 1.110, Page B-27 Waste Disposal 1.5 $50/HEPA or prefilter,
$100/charcoal Water Steam Electricity 1.3 8kw additional fan power for filter P @ 0.018 $/kw-hr Building Services Other
5. TOTAL O AND M ANNUAL COST 15.6
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-
WATER-COOLED NUCLEAR REACTORS
Description of Augment 30,000-cfm Charcoal/HEPA Filtration System - Auxiliary Building (Sheet 1)
DIRECT COST (1975 $1,000)
EQUIPMENT/ BASIS FOR COST
ITEM LABOR MATERIALS TOTAL ESTIMATE
1. PROCESS EQUIPMENT 15 117.0 132.0 prefilter/4" charcoal/HEPA @
$4/cfm, 60-kw htr @ $200/kw
2. BUILDING ASSIGNMENT 20 13.6 33.6 28 x 20 x 12 @ $5/ft3 (nonshielded area)
3. ASSOCIATED PIPING SYSTEMS 5 3.0 8.0 base
4. INSTRUMENTATION AND CONTROLS - in item 1 Appendix B to RG 1.110, Page B-28
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
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 $1,000)
EQUIPMENT/ BASIS FOR COST
ITEM LABOR MATERIALS TOTAL ESTIMATE
1. PROCESS EQUIPMENT 15.0 117.0 132.0 prefilter/4" charcoal/HEPA @
$4/cfm, 60-kw 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
4. INSTRUMENTATION AND CONTROLS in item 1 Appendix B to RG 1.110, Page B-29
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 10%
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 30,000-cfm Charcoal/HEPA Filtration System - Auxiliary Building (Sheet 3)
DIRECT COST (1975 $1,000)
BASIS FOR COST
ITEM LABOR OTHER TOTAL ESTIMATE
1. 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
LABOR each & 30 charcoal filters @
$900 each every 2 years
3. CONSUMABLES, CHEMICALS, AND - in items 2 and 4 SUPPLIES
4. UTILITIES AND SERVICES
Appendix B to RG 1.110, Page B-30
Waste Disposal 3.0 $50/HEPA or prefilter,
$100/charcoal filter Water Steam Electricity 2.6 16 kw additional fan HP for filter @ 0.018 $/kw-hr Building Services Other
5. TOTAL O AND M ANNUAL COST 27.4
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 $1,000)
EQUIPMENT/ BASIS FOR COST
ITEM LABOR MATERIALS TOTAL ESTIMATE
1. PROCESS EQUIPMENT 300 500 800 500-ton capacity, w/o air filters
2. BUILDING ASSIGNMENT - Coolers can be installed in existing space saved by deletion of ducting
3. ASSOCIATED PIPING SYSTEMS - in item 1
4. INSTRUMENTATION AND CONTROLS - in item 1 Appendix B to RG 1.110, Page B-31
5. ELECTRICAL SERVICE 40 50 90
6. SPARE PARTS - 8 8 1% item 1 SUBTOTAL 340 558 898
7. CONTINGENCY 34 56 90 10%
8. TOTAL DIRECT COSTS 374 614 988
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE
TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment Turbine Building Chilled Water HVAC System (Sheet 2)
DIRECT COST (1975 $1,000)
BASIS FOR COST
ITEM LABOR OTHER TOTAL ESTIMATE
1. OPERATING LABOR, SUPERVISION, 3.3 15 min/shift AND OVERHEAD
2. MAINTENANCE MATERIAL AND 20.0 21/2% of equipment costs LABOR
3. CONSUMABLES, CHEMICALS, AND - in item 2 SUPPLIES
4. UTILITIES AND SERVICES
Appendix B to RG 1.110, Page B-32 Waste Disposal Water 13.0 500 gpm @ 10¢/1,000 gal &
50% load factor Steam Electricity 33.0 400 kw @ 0.018 $/kw-hr Building Services Other
5. TOTAL O AND M ANNUAL COST 69.3
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-
WATER-COOLED NUCLEAR REACTORS
Description of Augment 600-ft3 Waste Gas Decay Tank (Sheet 1)
DIRECT COST (1975 $1,000)
EQUIPMENT/ BASIS FOR COST
ITEM LABOR MATERIALS TOTAL ESTIMATE
1. PROCESS EQUIPMENT 2.5 20 22.5 600-ft3, 150 psig, C.S., ASME
VIII
2. BUILDING ASSIGNMENT 18.0 9 27.0 15 x 15 x 20 @ $6/ft3 (shielded area)
3. ASSOCIATED PIPING SYSTEMS 1.0 1 2.0 10% of item 1
4. INSTRUMENTATION AND CONTROLS neg Appendix B to RG 1.110, Page B-33
5. ELECTRICAL SERVICE neg
6. SPARE PARTS neg SUBTOTAL 21.5 30 51.5
7. CONTINGENCY 2.0 3 5.0 10%
8. 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
Description of Augment 600-ft3 Waste Gas Decay Tank (Sheet 2)
DIRECT COST (1975 $1,000)
BASIS FOR COST
ITEM LABOR OTHER TOTAL ESTIMATE
1. OPERATING LABOR, SUPERVISION, - - neg AND OVERHEAD
2. MAINTENANCE MATERIAL AND - - neg LABOR
3. CONSUMABLES, CHEMICALS, AND - - neg SUPPLIES
4. UTILITIES AND SERVICES
Appendix B to RG 1.110, Page B-34 Waste Disposal Water Steam neg Electricity Building Services Other
5. TOTAL O AND M ANNUAL COST neg
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 $1,000)
EQUIPMENT/ BASIS FOR COST
ITEM LABOR MATERIALS TOTAL ESTIMATE
1. PROCESS EQUIPMENT 50.0 300.0 350.0 skid mounted, catalytic type w/condenser, partial I&C single unit, ASME VIII
2. BUILDING ASSIGNMENT 28.8 14.4 43.2 15 x 30 x 16 @ $6/ft3 (shielded area)
3. ASSOCIATED PIPING SYSTEMS 32.0 13.0 45.0 allowance
4. INSTRUMENTATION AND CONTROLS 10.0 40.0 50.0 allowance Appendix B to RG 1.110, Page B-35
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 10%
8. TOTAL DIRECT COSTS 146.8 419.4 566.2
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE
TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment PWR Hydrogen Recombiner (Sheet 2)
DIRECT COST (1975 $1,000)
BASIS FOR COST
ITEM LABOR OTHER TOTAL ESTIMATE
1. OPERATING LABOR, SUPERVISION, 3.3 15 min/shift AND OVERHEAD
2. MAINTENANCE MATERIAL AND 10.0 3% of equipment cost LABOR
3. CONSUMABLES, CHEMICALS, AND 1.0 oxygen @ $2.5/103 cf & .25 cfm SUPPLIES @ 7,000 hrs
4. UTILITIES AND SERVICES
Appendix B to RG 1.110, Page B-36 Waste Disposal Water Steam neg Electricity Building Services Other
5. TOTAL O AND M ANNUAL COST 14.3
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 $1,000)
EQUIPMENT/ BASIS FOR COST
ITEM LABOR MATERIALS TOTAL ESTIMATE
1. PROCESS EQUIPMENT 3.0 7.5 10.5 chiller, heater, charcoal HEPA
2. BUILDING ASSIGNMENT 3.0 1.5 4.5 10 x 10 x 15 @ $3/ft3 (unshielded turbine building)
3. ASSOCIATED PIPING SYSTEMS 2.0 1.0 3.0 allowance
4. INSTRUMENTATION AND CONTROLS 0.5 1.5 2.0 allowance Appendix B to RG 1.110, Page B-37
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 10%
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 Augment PWR Air Ejector Charcoal/HEPA Filtration Unit (Sheet 2)
DIRECT COST (1975 $1,000)
BASIS FOR COST
ITEM LABOR OTHER TOTAL ESTIMATE
1. 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 SUPPLIES
4. UTILITIES AND SERVICES
Appendix B to RG 1.110, Page B-38 Waste Disposal neg Water Steam Electricity Building Services Other
5. TOTAL O AND M ANNUAL COST 5.8
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 $1,000)
EQUIPMENT/ BASIS FOR COST
ITEM LABOR MATERIALS TOTAL ESTIMATE
1. 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
4. INSTRUMENTATION AND CONTROLS 4 6 10 allowance Appendix B to RG 1.110, Page B-39
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
TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment Steam Generator Flash Tank Vent to Main Condenser (Sheet 2)
DIRECT COST (1975 $1,000)
BASIS FOR COST
ITEM LABOR OTHER TOTAL ESTIMATE
1. OPERATING LABOR, SUPERVISION, 1 allowance AND OVERHEAD
2. MAINTENANCE MATERIAL AND 1 2% Total Direct Cost LABOR
3. CONSUMABLES, CHEMICALS, AND neg SUPPLIES
4. UTILITIES AND SERVICES
Appendix B to RG 1.110, Page B-40
Waste Disposal Water neg Steam Electricity Building Services Other
5. TOTAL O AND M ANNUAL COST 2
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-
WATER-COOLED NUCLEAR REACTORS
Description of Augment 15-gpm Evaporator (Sheet 1)
DIRECT COST (1975 $1,000)
EQUIPMENT/ BASIS FOR COST
ITEM LABOR MATERIALS TOTAL ESTIMATE
1. PROCESS EQUIPMENT 30 225 255 skid mounted, submerged tube bundle, ASME VIII, Incoloy in contact with process fluid
2. BUILDING ASSIGNMENT 68 34 102 evap & services 25 x 30 x 20
@ $6/ft3 plus 2,000 ft3 increase in solid waste storage area
3. ASSOCIATED PIPING SYSTEMS 35 30 65 includes service piping
4. INSTRUMENTATION AND CONTROLS 10 10 20 allowance Appendix B to RG 1.110, Page B-41
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 TREATMENT SYSTEM FOR LIGHT-
WATER-COOLED NUCLEAR REACTORS
Description of Augment 30-gpm Evaporator (Sheet 2)
DIRECT COST (1975 $1,000)
EQUIPMENT/ BASIS FOR COST
ITEM LABOR MATERIALS TOTAL ESTIMATE
1. PROCESS EQUIPMENT 30 350 380 ASME VIII
skid mounted, submerged, tube bundle, Incoloy in contact with process fluid
2. BUILDING ASSIGNMENT 88 44 132 evap + services - 25 x 40 x 20
@ $6/ft3 plus 2,000 ft3 increase in solid waste storage area
3. ASSOCIATED PIPING SYSTEMS 35 35 70 includes service piping Appendix B to RG 1.110, Page B-42
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 10%
8. TOTAL DIRECT COSTS 223 540 763
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-
WATER-COOLED NUCLEAR REACTORS
Description of Augment 50-gpm Evaporator (Sheet 3)
DIRECT COST (1975 $1,000)
EQUIPMENT/ BASIS FOR COST
ITEM LABOR MATERIALS TOTAL 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
4. INSTRUMENTATION AND CONTROLS 10 10 20 allowance Appendix B to RG 1.110, Page B-43
5. 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 Evaporator - BWR Dirty Waste - Floor Drains (Sheet 4)
DIRECT COST (1975 $1,000)
BASIS FOR COST
ITEM LABOR OTHER TOTAL ESTIMATE
1. OPERATING LABOR, SUPERVISION, 12 2.6 x 106 gpy; 1000 hrs/yr labor AND OVERHEAD
2. MAINTENANCE MATERIAL AND 30 71/2% of equipment costs LABOR
3. CONSUMABLES, CHEMICALS, AND neg concentrate solidification SUPPLIES chemicals in item 4
4. UTILITIES AND SERVICES
Waste Disposal 70 100:1 feed to concentrate ratio Appendix B to RG 1.110, Page B-44
@ $20/ft3 disposal cost Water 27 1,000 gpm @ 1,500 hrs @
30¢/1000 gal Steam 60 1,500 hrs steam @ 20,000 lb/hr
@ $2/1,000 lbs Electricity Building Services Other
5. TOTAL O AND M ANNUAL COST 199
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)
DIRECT COST (1975 $1,000)
BASIS FOR COST
ITEM LABOR OTHER TOTAL ESTIMATE
1. OPERATING LABOR, SUPERVISION, 6.0 500,000 gpy; 500 hrs/yr labor AND OVERHEAD
2. MAINTENANCE MATERIAL AND 30.0 71/2% of equipment costs LABOR
3. CONSUMABLES, CHEMICALS, AND - concentrate solidification SUPPLIES chemicals in item 4
4. UTILITIES AND SERVICES
Waste Disposal 27.0 50:1 feed to concentrate ratio @
Appendix B to RG 1.110, Page B-45
$20/ft3 disposal cost Water 5.0 1,000 gpm @ 277 hrs @
30¢/1,000 gal Steam 12.0 277 hrs steam @ 20,000 lbs/hr
@ $2/1,000 lbs Electricity Building Services Other
5. TOTAL O AND M ANNUAL COST 80.0
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE
TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment Evaporator - Condenser Polisher Chemical Waste (Sheet 6)
DIRECT COST (1975 $1,000)
BASIS FOR COST
ITEM LABOR OTHER TOTAL ESTIMATE
1. OPERATING LABOR, SUPERVISION, 6.0 650,000 gpy; 500 hr/yr labor AND OVERHEAD
2. MAINTENANCE MATERIAL AND 30.0 71/2% of equipment costs LABOR
3. CONSUMABLES, CHEMICALS, AND concentrate solidification SUPPLIES chemicals in item 4
4. UTILITIES AND SERVICES
Waste Disposal 87.0 20:1 feed to concentrate ratio @
Appendix B to RG 1.110, Page B-46
$20/ft3 disposal cost Water 6.5 1,000 gpm @ 360 hrs @
30¢/1,000 gal Steam 14.4 360 hrs steam @ 20,000 lbs/hr
@ $2/1,000 lbs Electricity Building Services Other
5. TOTAL O AND M ANNUAL COST 143.9
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE
TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment Evaporator - Detergent Waste (Sheet 7)
DIRECT COST (1975 $1,000)
BASIS FOR COST
ITEM LABOR OTHER TOTAL ESTIMATE
1. OPERATING LABOR, SUPERVISION, 6.0 160,000 gpy; 500 hrs/yr AND OVERHEAD
2. MAINTENANCE MATERIAL AND 30.0 71/2% of equipment costs LABOR
3. CONSUMABLES, CHEMICALS, AND - concentrate solidification SUPPLIES chemicals in item 4
4. UTILITIES AND SERVICES
Waste Disposal 8.6 50:1 feed to concentrate ration Appendix B to RG 1.110, Page B-47
@ $20/ft3 disposal cost Water 1.6 1,000 gpm @ 90 hrs @
30¢/1,000 gal Steam 3.6 90 hrs steam @ 20,000 lb/hr @
$2/1,000 lbs Electricity Building Services Other
5. TOTAL O AND M ANNUAL 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 $1,000)
EQUIPMENT/ BASIS FOR COST
ITEM LABOR MATERIALS TOTAL ESTIMATE
1. PROCESS EQUIPMENT 4.0 20.0 24.0 30 ft3, 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
4. INSTRUMENTATION AND CONTROLS 2.0 3.0 5.0 remote conductivity readout Appendix B to RG 1.110, Page B-48
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
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)
DIRECT COST (1975 $1,000)
BASIS FOR COST
ITEM LABOR OTHER TOTAL ESTIMATE
15. OPERATING LABOR, SUPERVISION, 1.8 1,500 hrs operation @
AND OVERHEAD 10% attendance
16. MAINTENANCE MATERIAL AND 2.0 allowance LABOR
17. CONSUMABLES, CHEMICALS, AND 2.3 1 change per yr @ $75/ft3 SUPPLIES
18. UTILITIES AND SERVICES
Appendix B to RG 1.110, Page B-49 Waste Disposal 0.6 30 ft3 @ $20/ft3 disposal cost Water Steam Electricity Building Services Other
19. TOTAL O 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-gpm Demineralizer (Sheet 1)
DIRECT COST (1975 $1,000)
EQUIPMENT/ BASIS FOR COST
ITEM LABOR MATERIALS TOTAL ESTIMATE
1. PROCESS EQUIPMENT 5 20.0 25.0 30 ft3, SS, ASME VIII, 150 psi, nonregenerative, with resin
2. BUILDING ASSIGNMENT 9 4.8 13.8 12 x 12 x 16 @ $6/ft3 (shielded area)
3. ASSOCIATED PIPING SYSTEMS 9 6.0 15.0 2" piping
4. INSTRUMENTATION AND CONTROLS 4 6.0 10.0
Appendix B to RG 1.110, Page B-50
5. ELECTRICAL SERVICE neg
6. SPARE PARTS - 2.0 2.0 miscellaneous supplies SUBTOTAL 27 38.8 65.8
7. CONTINGENCY 2 4.0 6.0 10%
8. TOTAL DIRECT COSTS 29 42.8 71.8
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-
WATER-COOLED NUCLEAR REACTORS
Description of Augment 100-gpm Demineralizer (Sheet 2)
DIRECT COST (1975 $1,000)
EQUIPMENT/ BASIS FOR COST
ITEM LABOR MATERIALS TOTAL ESTIMATE
1. PROCESS EQUIPMENT 5 35.0 40.0 60 ft3, SS, ASME VIII, 150 psi, nonregenerative, with resin
2. BUILDING ASSIGNMENT 9 4.8 13.8 12 x 12 x 16 @ $6/ft3 (shielded area)
3. ASSOCIATED PIPING SYSTEMS 10 10.0 20.0 21/2" piping
4. INSTRUMENTATION AND CONTROLS 4 6.0 10.0
Appendix B to RG 1.110, Page B-51
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
8. TOTAL DIRECT COSTS 31 63.8 94.8
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-
WATER-COOLED NUCLEAR REACTORS
Description of Augment 200-gpm Demineralizer (Sheet 3)
DIRECT COST (1975 $1,000)
EQUIPMENT/ BASIS FOR COST
ITEM LABOR MATERIALS TOTAL ESTIMATE
1. PROCESS EQUIPMENT 5 60.0 65.0 120 ft3, SS, ASME VIII, 150 psi, nonregenerative, with resin
2. BUILDING ASSIGNMENT 11 5.2 16.2 13 x 13 x 16 @ $6/ft3 (shielded area)
3. ASSOCIATED PIPING SYSTEMS 12 12.0 24.0 4" piping
4. INSTRUMENTATION AND CONTROLS 4 6.0 10.0
Appendix B to RG 1.110, Page B-52
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
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 $1,000)
EQUIPMENT/ BASIS FOR COST
ITEM LABOR MATERIALS TOTAL ESTIMATE
1. PROCESS EQUIPMENT 5 60.0 65.0 120 ft3, SS, ASME VIII, 150 psi, nonregenerative, with resin
2. BUILDING ASSIGNMENT 11 5.2 16.2 13 x 13 x 16 @ $6/ft3 (shielded area)
3. ASSOCIATED PIPING SYSTEMS 20 20.0 40.0 6" piping
4. INSTRUMENTATION AND CONTROLS 4 6.0 10.0 allowance Appendix B to RG 1.110, Page B-53
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 Series (Sheet 5)
DIRECT COST (1975 $1,000)
BASIS FOR COST
ITEM LABOR OTHER TOTAL ESTIMATE
1. OPERATING LABOR, SUPERVISION, 3.3 15 min/shift AND OVERHEAD
2. MAINTENANCE MATERIAL AND 5.0 allowance LABOR
3. CONSUMABLES, CHEMICALS, AND 9.0 1 change per year @ 120 ft3 @
SUPPLIES $75/ft3 (one vessel change per year, regardless of size)
4. UTILITIES AND SERVICES
Appendix B to RG 1.110, Page B-54 Waste Disposal 2.4 120 ft3/yr @ $20/ft3 disposal cost Water Steam Electricity Building Services Other
5. TOTAL O AND M ANNUAL COST 19.7
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)
DIRECT COST (1975 $1,000)
BASIS FOR COST
ITEM LABOR OTHER TOTAL ESTIMATE
1. OPERATING LABOR, SUPERVISION, 1.8 10% of BRS shim bleed AND OVERHEAD (50,000 gpy), 30 min/day
2. MAINTENANCE MATERIAL AND 5.0 allowance LABOR
3. CONSUMABLES, CHEMICALS, AND 2.3 30 ft3/yr @ $75/ft3 SUPPLIES
4. UTILITIES AND SERVICES
Appendix B to RG 1.110, Page B-55 Waste Disposal 0.6 30 ft3/yr @ $20/ft3 disposal cost Water Steam Electricity Building Services Other
5. TOTAL O AND M ANNUAL COST 9.7
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE
TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment Demineralizer - BWR Dirty Waste (Sheet 7)
DIRECT COST (1975 $1,000)
BASIS FOR COST
ITEM LABOR OTHER TOTAL ESTIMATE
1. OPERATING LABOR, SUPERVISION, 6.5 2.6 x 106 gpy, 30 min/shift AND OVERHEAD
2. MAINTENANCE MATERIAL AND 5.0 allowance LABOR
3. CONSUMABLES, CHEMICALS, AND 64.5 860 ft3 resin @ $75/ft3 SUPPLIES
4. UTILITIES AND SERVICES
Appendix B to RG 1.110, Page B-56 Waste Disposal 17.2 860 ft3 @ $20/ft3 disposal cost Water Steam Electricity Building Services Other
5. TOTAL O AND M ANNUAL COST 93.2
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE
TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment Demineralizer - PWR Dirty Wastes (w/o turbine building) (Sheet 8)
DIRECT COST (1975 $1,000)
BASIS FOR COST
ITEM LABOR OTHER TOTAL ESTIMATE
1. OPERATING LABOR, SUPERVISION, 3.3 500,000 gpy; 15 min/shift AND OVERHEAD
2. MAINTENANCE MATERIAL AND 5.0 allowance LABOR
3. CONSUMABLES, CHEMICALS, AND 12.0 160 ft3/yr @ $75/ft3 SUPPLIES
4. UTILITIES AND SERVICES
Appendix B to RG 1.110, Page B-57 Waste Disposal 3.2 160 ft3/yr @ $20/ft3 disposal cost Water Steam Electricity Building Services Other
5. TOTAL O AND M ANNUAL COST 23.5
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE
TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment Demineralizer - PWR Turbine Building Floor Drains (Sheet 9)
DIRECT COST (1975 $1,000)
BASIS FOR COST
ITEM LABOR OTHER TOTAL ESTIMATE
1. OPERATING LABOR, SUPERVISION, 13.1 1 hr/shift, 2.6 x 106 gpy AND OVERHEAD
2. MAINTENANCE MATERIAL AND 5.0 allowance LABOR
3. CONSUMABLES, CHEMICALS, AND 64.5 860 ft3 resin @ 75/ft3 SUPPLIES
4. UTILITIES AND SERVICES
Appendix B to RG 1.110, Page B-58 Waste Disposal 17.2 860 ft3/yr @ $20/ft3 disposal cost Water Steam Electricity Building Services Other
5. TOTAL O AND M ANNUAL COST 99.8
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE
TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment Demineralizer - PWR Steam Generator Blowdown (Sheet 10)
DIRECT COST (1975 $1,000)
BASIS FOR COST
ITEM LABOR OTHER TOTAL ESTIMATE
1. OPERATING LABOR, SUPERVISION, 3.3 15 min/shift AND OVERHEAD
2. MAINTENANCE MATERIAL AND 5.0 allowance LABOR
3. CONSUMABLES, CHEMICALS, AND 16.9 225 ft3 resin/yr @ $75/ft3 SUPPLIES
4. UTILITIES AND SERVICES
Appendix B to RG 1.110, Page B-59 Waste Disposal 4.5 225 ft3/yr @ $20/ft3 disposal cost Water Steam Electricity Building Services Other
5. TOTAL O 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-gpm Cartridge Filter (Sheet 1)
DIRECT COST (1975 $1,000)
EQUIPMENT/ BASIS FOR COST
ITEM LABOR MATERIALS TOTAL ESTIMATE
1. PROCESS EQUIPMENT 2.0 5.0 7.0 SS, ASME VIII, 150 psi
2. BUILDING ASSIGNMENT 5.6 3.0 8.6 16 x 12 x 20 @ $6/ft3 (shielded area)
3. ASSOCIATED PIPING SYSTEMS 1.5 1.0 2.5 allowance
4. INSTRUMENTATION AND CONTROLS 0.6 2.4 3.0 allowance Appendix B to RG 1.110, Page B-60
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
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE
TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment Cartridge Filter (Sheet 2)
DIRECT COST (1975 $1,000)
BASIS FOR COST
ITEM LABOR OTHER TOTAL ESTIMATE
1. OPERATING LABOR, SUPERVISION, 4.5 10 changes @ 10
AND OVERHEAD man-hrs/change @ $12/hr +
15 min/shift
2. MAINTENANCE MATERIAL AND 1.0 allowance LABOR
3. CONSUMABLES, CHEMICALS, AND 1.0 10 changes/yr @ $100/change SUPPLIES
Appendix B to RG 1.110, Page B-61
4. UTILITIES AND SERVICES
Waste Disposal 1.5 10 drums/yr @ $20/ft3 Water Steam Electricity Building Services Other
5. TOTAL O AND M ANNUAL COST 8.0
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-
WATER-COOLED NUCLEAR REACTORS
Description of Augment 100-gpm Precoat Filter (Sheet 1)
DIRECT COST (1975 $1,000)
EQUIPMENT/ BASIS FOR COST
ITEM LABOR MATERIALS TOTAL ESTIMATE
1. PROCESS EQUIPMENT 10 65.0 75 automated system 1 gpm/ft2, ASME VIII
2. BUILDING ASSIGNMENT 18 9.0 27 15 x 15 x 20 @ $6/ft3 (shielded area)
3. ASSOCIATED PIPING SYSTEMS 16 9.0 25 35% of equipment cost
4. INSTRUMENTATION AND CONTROLS in item 1 Appendix B to RG 1.110, Page B-62
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
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-
WATER-COOLED NUCLEAR REACTORS
Description of Augment 400-gpm Precoat Filter (Sheet 2)
DIRECT COST (1975 $1,000)
EQUIPMENT/ BASIS FOR COST
ITEM LABOR MATERIALS TOTAL ESTIMATE
1. PROCESS EQUIPMENT 35 135.0 170 automated system; 1 gpm/ft2 ASME VIII
2. BUILDING ASSIGNMENT 24 12.0 36 15 x 20 x 20 @ $6/ft3 (shielded area)
3. ASSOCIATED PIPING SYSTEMS 31 16.0 47 35% of equipment cost
4. INSTRUMENTATION AND CONTROLS - - - item 1 Appendix B to RG 1.110, Page B-63
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 ESTIMATE SHEET OF RADWASTE
TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment Precoat Filter - BWR Dirty Waste (Sheet 3)
DIRECT COST (1975 $1,000)
BASIS FOR COST
ITEM LABOR OTHER TOTAL ESTIMATE
1. OPERATING LABOR, SUPERVISION, 6.6 2 x 106 gpy, 30 min/shift AND OVERHEAD
2. MAINTENANCE MATERIAL AND 10.0 allowance LABOR
3. CONSUMABLES, CHEMICALS, AND 6.0 10 lbs precoat @ 10¢/lb per SUPPLIES 1,000 gal processed
4. UTILITIES AND SERVICES
Appendix B to RG 1.110, Page B-64 Waste Disposal 40.0 1 ft3/sludge per 1,000 gal processed @ $30/ft3 disposal cost Water Steam Electricity Building Services Other
5. TOTAL O AND M ANNUAL COST 62.6
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-
WATER-COOLED NUCLEAR REACTORS
Description of Augment 2-gpm Reverse Osmosis (Sheet 1)
DIRECT COST (1975 $1,000)
EQUIPMENT/ BASIS FOR COST
ITEM LABOR MATERIALS TOTAL ESTIMATE
1. PROCESS EQUIPMENT 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/ft3
3. ASSOCIATED PIPING SYSTEMS 3.0 2.0 5.0 allowance
4. INSTRUMENTATION AND CONTROLS - in item 1 Appendix B to RG 1.110, Page B-65
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 DIRECT COST (1975 $1,000)
BASIS FOR COST
ITEM LABOR OTHER TOTAL ESTIMATE
1. OPERATING LABOR, SUPERVISION, 3.1 160,000 gpy, 1300 hrs/yr @
AND OVERHEAD 20% attendance
2. MAINTENANCE MATERIAL AND 8.8 4% less bldg + 24 module with LABOR 3-yr life @ $600 each
3. CONSUMABLES, CHEMICALS, AND neg SUPPLIES
4. UTILITIES AND SERVICES
Appendix B to RG 1.110, Page B-66 Waste Disposal 4.3 100:1 vol reduction @ $20/ft3 disposal cost Water Steam Electricity neg Building Services Other
5. TOTAL O AND M ANNUAL COST 16.2
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-
WATER-COOLED NUCLEAR REACTORS
Description of Augment 10,000-Gallon Tank (Sheet 1)
DIRECT COST (1975 $1,000)
EQUIPMENT/ BASIS FOR COST
ITEM LABOR MATERIALS TOTAL ESTIMATE
1. PROCESS EQUIPMENT 3 28 31 SS, ASME VIII, atmospheric service, 200°F
2. BUILDING ASSIGNMENT 30 15 45 15 x 20 x 25 @ $6/ft3 (shielded area)
3. ASSOCIATED PIPING SYSTEMS 2 1 3 10% of item 1
4. INSTRUMENTATION AND CONTROLS 4 6 10 allowance Appendix B to RG 1.110, Page B-67
5. ELECTRICAL SERVICE neg
6. SPARE PARTS - - neg SUBTOTAL 39 50 89
7. CONTINGENCY 4 5 9 10%
8. TOTAL DIRECT COSTS 43 55 98
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE
TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment 10,000-Gallon Tank (Sheet 2)
DIRECT COST (1975 $1,000)
BASIS FOR COST
ITEM LABOR OTHER TOTAL ESTIMATE
1. OPERATING LABOR, SUPERVISION, 1.1 5 min/shift - log level readings AND OVERHEAD
2. MAINTENANCE MATERIAL AND 1.6 1/2% of equipment LABOR
3. CONSUMABLES, CHEMICALS, AND neg SUPPLIES
4. UTILITIES AND SERVICES
Appendix B to RG 1.110, Page B-68 Waste Disposal Water Steam neg Electricity Building Services Other
5. TOTAL O AND M ANNUAL COST 2.7
REFERENCES TO APPENDIX B
1. U.S. Atomic Energy Commission (USAEC), Guide for Economic Evaluation of Nuclear Reactor Plant Designs, USAEC Report NUS-531, NUS Corporation, January 1969.
2. Wage Rates for Key Construction Trades, Engineering News Record, pp. 36-37, January 2, 1975.
3. USAEC, Projections of Labor Requirements for Electric Power Plants Construction,
1974-2000, USAEC Report WASH-1334, Washington, DC, August 1974.
Appendix B to RG 1.110, Page B-69
APPENDIX C
DATA NEEDED FOR RADWASTE TREATMENT SYSTEM
COST-BENEFIT ANALYSIS FOR LIGHT-WATER-COOLED
NUCLEAR REACTORS
This appendix describes information that should be submitted in support of radwaste treatment 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 SAR and ER. 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 given 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.
Appendix C to RG 1.110, Page C-1
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR
LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment DIRECT COST (1975 $1,000)
EQUIPMENT/ BASIS FOR COST
ITEM LABOR MATERIALS TOTAL ESTIMATE
1. PROCESS EQUIPMENT
2. BUILDING ASSIGNMENT
3. ASSOCIATED PIPING SYSTEMS
4. INSTRUMENTATION AND CONTROLS
5. ELECTRICAL SERVICE
Appendix C to RG-1.110, Page C-2
6. SPARE PARTS
SUBTOTAL
7. CONTINGENCY
8. TOTAL DIRECT COSTS
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE
TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment DIRECT COST (1975 $1,000)
BASIS FOR COST
ITEM LABOR OTHER TOTAL ESTIMATE
- U.S. Government Printing Office: 1987-202-292:60255
1. OPERATING LABOR, SUPERVISION,
AND OVERHEAD
2. MAINTENANCE MATERIAL AND
LABOR
3. CONSUMABLES, CHEMICALS, AND
SUPPLIES
4. UTILITIES AND SERVICES
Appendix C to RG-1.110, Page C-3 Waste Disposal Water Steam Electricity Building Services Other
5. TOTAL O AND M ANNUAL COST