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 2013OFFICE OF NUCLEAR REGULATORY RESEARCH
Revision 1 REGULATORY GUIDE
Written suggestions regarding this guide or development of new guides may be submitted through the NRC's 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 NRC's 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 NRC's Agencywide Documents Access and Management System (ADAMS) at http://www.nrc.gov/reading-rm/adams.html, under ADAMS Accession No. ML13241A052.
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, can-for a favorable cost-benefit ratio-lead 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 Rev. 1 of RG 1.110, Page 2 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, "Calcula tion 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 agency's 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 fo r 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 3 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 4
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 li cense 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 proce dures 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 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 5
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 NRC's 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 6 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 basis. 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 licensee's 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 staff's 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 staff's determination of the acceptability of the licensee's request, then the staff may request that the licensee either follow the guidance in this regulatory guide or provide an eq uivalent 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 10 CFR Part 52.
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 7 REFERENCES
~3 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 Re leases 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 NRC's public Web site at http://www.nrc.gov/reading-rm/doc-collections/ and through the NRC's 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 NRC's 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.
Appendix A to RG 1.110, Page A-1 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 cal culations 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-2 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 Costs-Gaseous Radwaste Augments, Liquid Radwaste Augments DIRECT COSTS
-GASEOUS RADWASTE AUGMENTS
EQUIPMENT/ MATERIAL LABOR (1975 $1,000)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, 21/2" and Less Than 24" 183 55 238 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-ft 3 Gas Decay Tank 33 24 57 Appendix A to RG 1.110, Page A-3 DIRECT COSTS
-GASEOUS RADWASTE AUGMENTS
EQUIPMENT/ MATERIAL LABOR (1975 $1,000)TOTAL 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 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 Costs-Liquid Radwaste Augments EQUIPMENT/ MATERIAL LABOR (1975 $1,000)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-4 Table A-2. Annual Operating Costs-Gaseous Radwaste Augments, Liquid Radwaste Augments Annual Operating Costs a-Gaseous 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-ft 3 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 TOTAL OPERATING COST (1975 $1,000/YR) Evaporation-PWR Dirty Waste 50 Evaporation-BWR Dirty Waste 169 Evaporation-Condensate Polisher Chemical Waste 114 Evaporation-Detergent Waste 20 Demineralization-Evaporator Distillate 5 Appendix A to RG 1.110, Page A-5 Annual Operating Costs-Liquid Radwaste Augments TOTAL OPERATING COST (1975 $1,000/YR) Demineralization-BWR 2nd Waste Demineralizer in Series 15 Demineralization-PWR Clean Waste 5 Demineralization-BWR Dirty Waste 88 Demineralization-PWR Dirty Waste 18 Demineralization-PWR Turbine Bldg. Drains 95 Demineralization-PWR Steam Generator Blowdown 25 Precoat Filter-BWR Dirty Waste 53 Cartridge Filter 7 Reverse Osmosis-Detergent Waste 7 10,000-gal Tank 1 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 Costs-Gaseous Radwaste Augments, Liquid Radwaste Augments ANNUAL MAINTENANCE COSTS
-GASEOUS 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-6 ANNUAL MAINTENANCE COSTS
-GASEOUS 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-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 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-7 Table A-4. Labor Cost Correction Factors
~a FPC~b GEOGRAPHIC
REGION LABOR COST
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 system 1.75 2. Multiunit site, shared radwaste system 1.75
3. Multiunit site, unitized a radwaste system n 5.1)1 n (75.1+ 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-8 Table A-6. Capital Recovery Factors COST OF MONEY (% PER YEAR, I) CAPITAL RECOVERY FACTOR
a 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:
CRF = 1 30)i 1 (30)i 1 (i++
Appendix A to RG 1.110, Page A-9 Figure A-1. Electric Power Supply Areas in the United States Appendix B to RG 1.110, Page B-1 APPENDIX B
BASES FOR PARAMETERS US
ED 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 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-1 of Appendix A by calculating th e 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 compos ite 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-2
4. Indirect Cost Factor
Indirect costs as a percentage of direct costs are calculated in Table B-1. Table B-
1. Indirect Costs
1 ST UNIT, PERCENTAGE OF DIRECT COST SUBSEQUENT UNITS, PERCENTAGE OF DIRECT COST
Construction facilities, equipment, and services 10 5 Engineering and construction management services 20 10 Other owners' costs 10 5 Interest during construction 35 a 35 a 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:
1)i 1 ()i 1 (i n n++
Appendix B to RG 1.110, Page B-3 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-2
0 1000-cfm Charcoal/HEPA Filtration System ............................................................................ B-23
15,000-cfm HEPA Filtration System ......................................................................................... B-2
5 30,000-cfm Charcoal/HEPA Filtration System ......................................................................... B-28 Turbine Building Chilled Water HVAC System ....................................................................... B-31
600-ft 3 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-4 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) ITEM LABOR
EQUIPMENT/ MATERIALS TOTAL BASIS FOR 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 50 150 30 x 40 x 25 @ $5/ft 3 (turbine building shielded area)
3. ASSOCIATED PIPING SYSTEMS 18 12 30 augment piping connections only 4. INSTRUMENTATION AND CONTROLS 24 96 120 allowance
5. ELECTRICAL SERVICE - - neg 4kw heaters on vessels neglected
6. SPARE PARTS - 85 85 75K for catalyst + 2% E/M in items 1 & 4 above SUBTOTAL 232 503 735
7. CONTINGENCY 23 50 73 10%
8. TOTAL DIRECT COSTS 255 553 808
Appendix B to RG 1.110, Page B-5 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
TER-COOLED NUCLEAR REACTORS Description of Augment BWR Offgas Recombiner (Sheet 2) DIRECT COST (1975 $1,000) ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD 3.3 15 min/shift
2. MAINTENANCE MATERIAL AND
LABOR 20.0 routine conditioning of catalyst and equipment upkeep; 5% of E/M including I&C
3. CONSUMABLES, CHEMICALS, AND
SUPPLIES - in item 2
4. UTILITIES AND SERVICES Waste Disposal Water Steam neg intermittent; 4kw heater load is negligible Electricity Building Services Other
5. TOTAL O AND M ANNUAL COST 23.3
Appendix B to RG 1.110, Page B-6 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) ITEM LABOR
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 5 44.0 49.0 carbon steel, 360 psig, 200 ft
3 volume (augment to existing train of beds)
2. BUILDING ASSIGNMENT 8 4.5 12.5 10 x 10 x 25 @ $5/ft 3 (turbine building shielded area)
3. ASSOCIATED PIPING SYSTEMS - - - in item 1
4. INSTRUMENTATION AND CONTROLS - - neg
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
Appendix B to RG 1.110, Page B-7 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
TER-COOLED NUCLEAR REACTORS Description of Augment 3-ton Charcoal Adsorber (Sheet 2) DIRECT COST (1975 $1,000) ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD neg 2. MAINTENANCE MATERIAL AND
LABOR neg allowance of 3% of equipment cost is negligible
3. CONSUMABLES, CHEMICALS, AND
SUPPLIES neg lifetime use of charcoal assumed
4. UTILITIES AND SERVICES neg Waste Disposal Water Steam neg Electricity Building Services Other
5. TOTAL O AND M ANNUAL COST neg
Appendix B to RG 1.110, Page B-8 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) ITEM LABOR
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST 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/ft 3 turbine building (shielded area)
3. ASSOCIATED PIPING SYSTEMS 10 5 15 augment piping connections only 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
Appendix B to RG 1.110, Page B-9 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
TER-COOLED NUCLEAR REACTORS Description of Augment Desiccant Dryer (Sheet 2) DIRECT COST (1975 $1,000) ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD 3.3 15 min/shift
2. MAINTENANCE MATERIAL AND
LABOR 6.1 5% of equipment including I&C
3. CONSUMABLES, CHEMICALS, AND
SUPPLIES neg 4. UTILITIES AND SERVICES 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
Appendix B to RG 1.110, Page B-10 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) ITEM LABOR
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST 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/ft 3 turbine building (nonshielded area)
3. ASSOCIATED PIPING SYSTEMS in item 1
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
Appendix B to RG 1.110, Page B-11 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
TER-COOLED NUCLEAR REACTORS Description of Augment Charcoal Vault Refrigeration (Sheet 2) DIRECT COST (1975 $1,000) ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD 3.3 15 min/shift
2. MAINTENANCE MATERIAL AND
LABOR 3.7 5% of equipment
3. CONSUMABLES, CHEMICALS, AND
SUPPLIES in item 2
4. UTILITIES AND SERVICES Waste Disposal Water Steam 0.5 electricity and cooling water Electricity Building Services Other
5. TOTAL O AND M ANNUAL COST 7.5
Appendix B to RG 1.110, Page B-12 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) ITEM LABOR
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST 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/ft 3 (nonshielded area)
3. ASSOCIATED PIPING SYSTEMS 1.3 0.7 2.0 allowance
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 0.7 3.7 4.4 10%
8. TOTAL DIRECT COSTS 8.1 40.4 48.5
Appendix B to RG 1.110, Page B-13 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
TER-COOLED NUCLEAR REACTORS Description of Augment Charcoal/HEPA Filtration System - Condenser Vacuum Pump (Sheet 2) DIRECT COST (1975 $1,000) ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD neg used only during startup and shutdown 2. MAINTENANCE MATERIAL AND
LABOR 1.2 4 HEPA filters @ $150 & 2 Charcoal filters @ $900, change every 2 years
3. CONSUMABLES, CHEMICALS, AND
SUPPLIES - in items 2 and 4
4. UTILITIES AND SERVICES 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
Appendix B to RG 1.110, Page B-14 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) ITEM LABOR
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST 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/ft 3 11. ASSOCIATED PIPING SYSTEMS 32 18 50 equiv 1,000 ft @ $50/ft
12. INSTRUMENTATION AND CONTROLS 8 12 20 in addition to item 1
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
Appendix B to RG 1.110, Page B-15 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
TER-COOLED NUCLEAR REACTORS Description of Augment Clean Steam to Turbine Glands (Sheet 2) DIRECT COST (1975 $1,000) ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD 3.3 15 min/shift
2. MAINTENANCE MATERIAL AND
LABOR 4.0 40 man-days
3. CONSUMABLES, CHEMICALS, AND
SUPPLIES 4. UTILITIES AND SERVICES 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
Appendix B to RG 1.110, Page B-16 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) ITEM LABOR
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST 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
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
Appendix B to RG 1.110, Page B-17 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
TER-COOLED NUCLEAR REACTORS Description of Augment Clean Steam to Steam Valves 24" and Larger (Sheet 2) DIRECT COST (1975 $1,000) ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 6. OPERATING LABOR, SUPERVISION, AND OVERHEAD 3.3 15 min/shift
7. MAINTENANCE MATERIAL AND
LABOR 4.0 40 man-days
8. CONSUMABLES, CHEMICALS, AND
SUPPLIES neg 9. UTILITIES AND SERVICES Waste Disposal Water Steam neg Electricity Building Services Other
1 0TOTAL O AND M ANNUAL COST 7.3
Appendix B to RG 1.110, Page B-18 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) ITEM LABOR
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST 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
6. SPARE PARTS - 6 6 SUBTOTAL 50 166 216
7. CONTINGENCY 5 17 22 10%
8. TOTAL DIRECT COSTS 55 183 238
Appendix B to RG 1.110, Page B-19 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
TER-COOLED NUCLEAR REACTORS Description of Augment Clean Steam to Steam Valves 21/2" and less than 24" (Sheet 2) DIRECT COST (1975 $1,000) ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD 3.3 15 min/shift
2. MAINTENANCE MATERIAL AND
LABOR 12.0 1% of direct cost of equipment
3. CONSUMABLES, CHEMICALS, AND
SUPPLIES - in item 2
4. UTILITIES AND SERVICES Waste Disposal Water Steam neg Electricity Building Services Other
5. TOTAL O AND M ANNUAL COST 15.3
Appendix B to RG 1.110, Page B-20 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) ITEM LABOR
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST 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/ft 3 (nonshielded area)
3. ASSOCIATED PIPING SYSTEMS 3 2.0 5.0
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
Appendix B to RG 1.110, Page B-21 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) ITEM LABOR
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST 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/ft 3 (nonshielded area)
3. ASSOCIATED PIPING SYSTEMS 3 2.0 5.0
4. INSTRUMENTATION AND CONTROLS in item 1
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
Appendix B to RG 1.110, Page B-22 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
TER-COOLED NUCLEAR REACTORS Description of Augment 15,000-cfm HEPA Filtration System (Sheet 3) DIRECT COST (1975 $1,000) ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD 3.8 15 min/shift + 40 hr annual test
2. MAINTENANCE MATERIAL AND
LABOR 2.2 change every 2 yrs @ $150/filter element 3. CONSUMABLES, CHEMICALS, AND
SUPPLIES - in items 2 and 4
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 O AND M ANNUAL COST 7.8
Appendix B to RG 1.110, Page B-23 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) ITEM LABOR
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST 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/ft 3 (nonshielded area)
3. ASSOCIATED PIPING SYSTEMS 1.3 0.7 2.0
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
Appendix B to RG 1.110, Page B-24 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
TER-COOLED NUCLEAR REACTORS Description of Augment 1000-cfm Charcoal/HEPA Filtration System (Sheet 2) DIRECT COST (1975 $1,000) ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD 1.9 20 min/day + 40 hr annual test
11. MAINTENANCE MATERIAL AND
LABOR 0.6 2 HEPA or prefilters @ $150
each and 1 charcoal @ $900 each every 2 years
12. CONSUMABLES, CHEMICALS, AND
SUPPLIES in items 2 and 4
13. UTILITIES AND SERVICES 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
Appendix B to RG 1.110, Page B-25 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) ITEM LABOR
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST 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/ft 3 (nonshielded area)
3. ASSOCIATED PIPING SYSTEMS 3 2 5
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
Appendix B to RG 1.110, Page B-26 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) ITEM LABOR
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST 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/ft 3 (nonshielded area)
3. ASSOCIATED PIPING SYSTEMS 3.0 2.0 5.0
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
Appendix B to RG 1.110, Page B-27 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
TER-COOLED NUCLEAR REACTORS Description of Augment 15,000-cfm HEPA Filtration System (Sheet 3) DIRECT COST (1975 $1,000) ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD 3.8 15 min/shift & 40-hr annual test
2. MAINTENANCE MATERIAL AND
LABOR 9.0 30 HEPA or prefilters @ $150 each & 15 charcoal filters @
$900 each every 2 years
3. CONSUMABLES, CHEMICALS, AND
SUPPLIES - in items 2 and 4
4. UTILITIES AND SERVICES 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
Appendix B to RG 1.110, Page B-28 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) ITEM LABOR
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST 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/ft 3 (nonshielded area)
3. ASSOCIATED PIPING SYSTEMS 5 3.0 8.0 base
4. INSTRUMENTATION AND CONTROLS - in item 1
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
Appendix B to RG 1.110, Page B-29 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) ITEM LABOR
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST 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/ft 3 (nonshielded area)
3. ASSOCIATED PIPING SYSTEMS 3.0 5.0 8.0 base
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 10%
8. TOTAL DIRECT COSTS 41.4 151.8 193.2
Appendix B to RG 1.110, Page B-30 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
TER-COOLED NUCLEAR REACTORS Description of Augment 30,000-cfm Charcoal/HEPA Filtration System - Auxiliary Building (Sheet 3) DIRECT COST (1975 $1,000) ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD 3.8 15 min/shift + 40 hr annual test
2. MAINTENANCE MATERIAL AND
LABOR 18.0 60 HEPA or prefilters @ $150 each & 30 charcoal filters @
$900 each every 2 years
3. CONSUMABLES, CHEMICALS, AND
SUPPLIES - in items 2 and 4
4. UTILITIES AND SERVICES 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
Appendix B to RG 1.110, Page B-31 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) ITEM LABOR
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST 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
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
Appendix B to RG 1.110, Page B-32 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
TER-COOLED NUCLEAR REACTORS Description of Augment Turbine Building Chilled Water HVAC System (Sheet 2) DIRECT COST (1975 $1,000) ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD 3.3 15 min/shift
2. MAINTENANCE MATERIAL AND
LABOR 20.0 21/2% of equipment costs
3. CONSUMABLES, CHEMICALS, AND
SUPPLIES - in item 2
4. UTILITIES AND SERVICES 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
Appendix B to RG 1.110, Page B-33 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS Description of Augment 600-ft
3 Waste Gas Decay Tank (Sheet 1) DIRECT COST (1975 $1,000) ITEM LABOR
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 2.5 20 22.5 600-ft
3, 150 psig, C.S., ASME VIII 2. BUILDING ASSIGNMENT 18.0 9 27.0 15 x 15 x 20 @ $6/ft 3 (shielded area)
3. ASSOCIATED PIPING SYSTEMS 1.0 1 2.0 10% of item 1
4. INSTRUMENTATION AND CONTROLS neg
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
Appendix B to RG 1.110, Page B-34 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
TER-COOLED NUCLEAR REACTORS Description of Augment 600-ft
3 Waste Gas Decay Tank (Sheet 2) DIRECT COST (1975 $1,000) ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD - - neg 2. MAINTENANCE MATERIAL AND
LABOR - - neg 3. CONSUMABLES, CHEMICALS, AND
SUPPLIES - - neg 4. UTILITIES AND SERVICES Waste Disposal Water Steam neg Electricity Building Services Other
5. TOTAL O AND M ANNUAL COST neg
Appendix B to RG 1.110, Page B-35 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) ITEM LABOR
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST 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/ft 3 (shielded area)
3. ASSOCIATED PIPING SYSTEMS 32.0 13.0 45.0 allowance
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 10%
8. TOTAL DIRECT COSTS 146.8 419.4 566.2
Appendix B to RG 1.110, Page B-36 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
TER-COOLED NUCLEAR REACTORS Description of Augment PWR Hydrogen Recombiner (Sheet 2) DIRECT COST (1975 $1,000) ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD 3.3 15 min/shift
2. MAINTENANCE MATERIAL AND
LABOR 10.0 3% of equipment cost
3. CONSUMABLES, CHEMICALS, AND
SUPPLIES 1.0 oxygen @ $2.5/10
3 cf & .25 cfm @ 7,000 hrs
4. UTILITIES AND SERVICES Waste Disposal Water Steam neg Electricity Building Services Other
5. TOTAL O AND M ANNUAL COST 14.3
Appendix B to RG 1.110, Page B-37 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) ITEM LABOR
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST 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/ft 3 (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
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
Appendix B to RG 1.110, Page B-38 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
TER-COOLED NUCLEAR REACTORS Description of Augment PWR Air Ejector Charcoal/HEPA Filtration Unit (Sheet 2) DIRECT COST (1975 $1,000) ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD 3.8 15 min/shift + 40 hr annual test
2. MAINTENANCE MATERIAL AND
LABOR 2.0 includes replacement filter
3. CONSUMABLES, CHEMICALS, AND
SUPPLIES - in item 2
4. UTILITIES AND SERVICES Waste Disposal neg Water Steam Electricity Building Services Other
5. TOTAL O AND M ANNUAL COST 5.8
Appendix B to RG 1.110, Page B-39 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) ITEM LABOR
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST 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
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
Appendix B to RG 1.110, Page B-40 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
TER-COOLED NUCLEAR REACTORS Description of Augment Steam Generator Flash Tank Vent to Main Condenser (Sheet 2) DIRECT COST (1975 $1,000) ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD 1 allowance
2. MAINTENANCE MATERIAL AND
LABOR 1 2% Total Direct Cost
3. CONSUMABLES, CHEMICALS, AND
SUPPLIES neg 4. UTILITIES AND SERVICES Waste Disposal Water neg Steam Electricity Building Services Other
5. TOTAL O AND M ANNUAL COST 2
Appendix B to RG 1.110, Page B-41 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) ITEM LABOR
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST 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/ft 3 plus 2,000 ft
3 increase in solid waste storage area
3. ASSOCIATED PIPING SYSTEMS 35 30 65 includes 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
Appendix B to RG 1.110, Page B-42 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) ITEM LABOR
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST 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/ft 3 plus 2,000 ft
3 increase in solid waste storage area
3. ASSOCIATED PIPING SYSTEMS 35 35 70 includes 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 203 491 694
7. CONTINGENCY 20 49 69 10%
8. TOTAL DIRECT COSTS 223 540 763
Appendix B to RG 1.110, Page B-43 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) ITEM LABOR
EQUIPMENT/ MATERIALS TOTAL BASIS FOR 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
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 212 595 807
7. CONTINGENCY 21 60 81 10%
8. TOTAL DIRECT COSTS 233 655 888
Appendix B to RG 1.110, Page B-44 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
TER-COOLED NUCLEAR REACTORS Description of Augment Evaporator - BWR Dirty Waste - Floor Drains (Sheet 4) DIRECT COST (1975 $1,000) ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD 12 2.6 x 10
6 gpy; 1000 hrs/yr labor
2. MAINTENANCE MATERIAL AND
LABOR 30 71/2% of equipment costs
3. CONSUMABLES, CHEMICALS, AND
SUPPLIES neg concentrate solidification chemicals in item 4
4. UTILITIES AND SERVICES Waste Disposal 70 100:1 feed to concentrate ratio
@ $20/ft 3 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
Appendix B to RG 1.110, Page B-45 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
TER-COOLED NUCLEAR REACTORS Description of Augment Evaporator PWR Dirty Waste (Sheet 5) DIRECT COST (1975 $1,000) ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD 6.0 500,000 gpy; 500 hrs/yr labor
2. MAINTENANCE MATERIAL AND
LABOR 30.0 71/2% of equipment costs
3. CONSUMABLES, CHEMICALS, AND
SUPPLIES - concentrate solidification chemicals in item 4
4. UTILITIES AND SERVICES Waste Disposal 27.0 50:1 feed to concentrate ratio @
$20/ft 3 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
Appendix B to RG 1.110, Page B-46 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
TER-COOLED NUCLEAR REACTORS Description of Augment Evaporator - Conde nser Polisher Chemical Waste (Sheet 6) DIRECT COST (1975 $1,000) ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD 6.0 650,000 gpy; 500 hr/yr labor
2. MAINTENANCE MATERIAL AND
LABOR 30.0 71/2% of equipment costs
3. CONSUMABLES, CHEMICALS, AND
SUPPLIES concentrate solidification chemicals in item 4
4. UTILITIES AND SERVICES Waste Disposal 87.0 20:1 feed to concentrate ratio @
$20/ft 3 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
Appendix B to RG 1.110, Page B-47 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
TER-COOLED NUCLEAR REACTORS Description of Augment Evaporator - Detergent Waste (Sheet 7) DIRECT COST (1975 $1,000) ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD 6.0 160,000 gpy; 500 hrs/yr
2. MAINTENANCE MATERIAL AND
LABOR 30.0 71/2% of equipment costs
3. CONSUMABLES, CHEMICALS, AND
SUPPLIES - concentrate solidification chemicals in item 4
4. UTILITIES AND SERVICES Waste Disposal 8.6 50:1 feed to concentrate ration
@ $20/ft 3 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
Appendix B to RG 1.110, Page B-48 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) ITEM LABOR
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 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/ft 3 (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
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
Appendix B to RG 1.110, Page B-49 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
TER-COOLED NUCLEAR REACTORS Description of Augment Evaporator Distillate Demineralizer (Sheet 2) DIRECT COST (1975 $1,000) ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 15. OPERATING LABOR, SUPERVISION, AND OVERHEAD 1.8 1,500 hrs operation @ 10% attendance
16. MAINTENANCE MATERIAL AND
LABOR 2.0 allowance
17. CONSUMABLES, CHEMICALS, AND
SUPPLIES 2.3 1 change per yr @ $75/ft
3 18. UTILITIES AND SERVICES Waste Disposal 0.6 30 ft
3 @ $20/ft 3 disposal cost Water Steam Electricity Building Services Other
19. TOTAL O AND M ANNUAL COST 6.7
Appendix B to RG 1.110, Page B-50 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) ITEM LABOR
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 5 20.0 25.0 30 ft
3 , SS, ASME VIII, 150 psi, nonregenerative, with resin
2. BUILDING ASSIGNMENT 9 4.8 13.8 12 x 12 x 16 @ $6/ft 3 (shielded area)
3. ASSOCIATED PIPING SYSTEMS 9 6.0 15.0 2" piping
4. INSTRUMENTATION AND CONTROLS 4 6.0 10.0
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
Appendix B to RG 1.110, Page B-51 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) ITEM LABOR
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. 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 @ $6/ft 3 (shielded area)
3. ASSOCIATED PIPING SYSTEMS 10 10.0 20.0 21/2" piping
4. INSTRUMENTATION AND CONTROLS 4 6.0 10.0
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
Appendix B to RG 1.110, Page B-52 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) ITEM LABOR
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 5 60.0 65.0 120 ft
3 , SS, ASME VIII, 150 psi, nonregenerative, with resin
2. BUILDING ASSIGNMENT 11 5.2 16.2 13 x 13 x 16 @ $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
Appendix B to RG 1.110, Page B-53 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) ITEM LABOR
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 5 60.0 65.0 120 ft
3 , SS, ASME VIII, 150 psi, nonregenerative, with resin
2. BUILDING ASSIGNMENT 11 5.2 16.2 13 x 13 x 16 @ $6/ft 3 (shielded area)
3. ASSOCIATED PIPING SYSTEMS 20 20.0 40.0 6" piping
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
Appendix B to RG 1.110, Page B-54 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
TER-COOLED NUCLEAR REACTORS Description of Augment BWR - 2nd Waste Demineralizer in Series (Sheet 5) DIRECT COST (1975 $1,000) ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD 3.3 15 min/shift
2. MAINTENANCE MATERIAL AND
LABOR 5.0 allowance
3. CONSUMABLES, CHEMICALS, AND
SUPPLIES 9.0 1 change per year @ 120 ft
3 @ $75/ft 3 (one vessel change per year, regardless of size)
4. UTILITIES AND SERVICES Waste Disposal 2.4 120 ft
3/yr @ $20/ft
3 disposal cost Water Steam Electricity Building Services Other
5. TOTAL O AND M ANNUAL COST 19.7
Appendix B to RG 1.110, Page B-55 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
TER-COOLED NUCLEAR REACTORS Description of Augment Demineralizer - PWR Clean Wastes (Sheet 6) DIRECT COST (1975 $1,000) ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD 1.8 10% of BRS shim bleed (50,000 gpy), 30 min/day
2. MAINTENANCE MATERIAL AND
LABOR 5.0 allowance
3. CONSUMABLES, CHEMICALS, AND
SUPPLIES 2.3 30 ft
3/yr @ $75/ft
3 4. UTILITIES AND SERVICES Waste Disposal 0.6 30 ft3/yr @ $20/ft
3 disposal cost Water Steam Electricity Building Services Other
5. TOTAL O AND M ANNUAL COST 9.7
Appendix B to RG 1.110, Page B-56 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
TER-COOLED NUCLEAR REACTORS Description of Augment Demineralizer - BWR Dirty Waste (Sheet 7) DIRECT COST (1975 $1,000) ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD 6.5 2.6 x 10
6 gpy, 30 min/shift
2. MAINTENANCE MATERIAL AND
LABOR 5.0 allowance
3. CONSUMABLES, CHEMICALS, AND
SUPPLIES 64.5 860 ft
3 resin @ $75/ft
3 4. UTILITIES AND SERVICES Waste Disposal 17.2 860 ft
3 @ $20/ft 3 disposal cost Water Steam Electricity Building Services Other
5. TOTAL O AND M ANNUAL COST 93.2
Appendix B to RG 1.110, Page B-57 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
TER-COOLED NUCLEAR REACTORS Description of Augment Demineralizer - PWR Dirty Wastes (w/o turbine building) (Sheet 8) DIRECT COST (1975 $1,000) ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. 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 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 O AND M ANNUAL COST 23.5
Appendix B to RG 1.110, Page B-58 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
TER-COOLED NUCLEAR REACTORS Description of Augment Demineralizer - PWR Turbine Building Floor Drains (Sheet 9) DIRECT COST (1975 $1,000) ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD 13.1 1 hr/shift, 2.6 x 10
6 gpy 2. MAINTENANCE MATERIAL AND
LABOR 5.0 allowance
3. CONSUMABLES, CHEMICALS, AND
SUPPLIES 64.5 860 ft
3 resin @ 75/ft
3 4. UTILITIES AND SERVICES Waste Disposal 17.2 860 ft
3/yr @ $20/ft
3 disposal cost Water Steam Electricity Building Services Other
5. TOTAL O AND M ANNUAL COST 99.8
Appendix B to RG 1.110, Page B-59 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
TER-COOLED NUCLEAR REACTORS Description of Augment Demineralizer - PWR Steam Generator Blowdown (Sheet 10) DIRECT COST (1975 $1,000) ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD 3.3 15 min/shift
2. MAINTENANCE MATERIAL AND
LABOR 5.0 allowance
3. CONSUMABLES, CHEMICALS, AND
SUPPLIES 16.9 225 ft
3 resin/yr @ $75/ft
3 4. UTILITIES AND SERVICES Waste Disposal 4.5 225 ft
3/yr @ $20/ft
3 disposal cost Water Steam Electricity Building Services Other
5. TOTAL O AND M ANNUAL COST 29.7
Appendix B to RG 1.110, Page B-60 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) ITEM LABOR
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST 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/ft 3 (shielded area)
3. ASSOCIATED PIPING SYSTEMS 1.5 1.0 2.5 allowance
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
Appendix B to RG 1.110, Page B-61 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
TER-COOLED NUCLEAR REACTORS Description of Augment Cartridge Filter (Sheet 2) DIRECT COST (1975 $1,000) ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD 4.5 10 changes @ 10 man-hrs/change @ $12/hr + 15 min/shift
2. MAINTENANCE MATERIAL AND
LABOR 1.0 allowance
3. CONSUMABLES, CHEMICALS, AND
SUPPLIES 1.0 10 changes/yr @ $100/change
4. UTILITIES AND SERVICES Waste Disposal 1.5 10 drums/yr @ $20/ft
3 Water Steam Electricity Building Services Other
5. TOTAL O AND M ANNUAL COST 8.0
Appendix B to RG 1.110, Page B-62 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) ITEM LABOR
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 10 65.0 75 automated system 1 gpm/ft
2 , ASME VIII
2. BUILDING ASSIGNMENT 18 9.0 27 15 x 15 x 20 @ $6/ft 3 (shielded area)
3. ASSOCIATED PIPING SYSTEMS 16 9.0 25 35% of equipment cost
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
Appendix B to RG 1.110, Page B-63 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) ITEM LABOR
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 35 135.0 170 automated system; 1 gpm/ft
2 ASME VIII
2. BUILDING ASSIGNMENT 24 12.0 36 15 x 20 x 20 @ $6/ft 3 (shielded area)
3. ASSOCIATED PIPING SYSTEMS 31 16.0 47 35% of equipment cost
4. INSTRUMENTATION AND CONTROLS - - - item 1
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
Appendix B to RG 1.110, Page B-64 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
TER-COOLED NUCLEAR REACTORS Description of Augment Precoat Filter - BWR Dirty Waste (Sheet 3) DIRECT COST (1975 $1,000) ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD 6.6 2 x 10
6 gpy, 30 min/shift
2. MAINTENANCE MATERIAL AND
LABOR 10.0 allowance
3. CONSUMABLES, CHEMICALS, AND
SUPPLIES 6.0 10 lbs precoat @ 10¢/lb per 1,000 gal processed
4. UTILITIES AND SERVICES Waste Disposal 40.0 1 ft
3/sludge per 1,000 gal processed @ $30/ft
3 disposal cost Water Steam Electricity Building Services Other
5. TOTAL O AND M ANNUAL COST 62.6
Appendix B to RG 1.110, Page B-65 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) ITEM LABOR
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST 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/ft 3 3. ASSOCIATED PIPING SYSTEMS 3.0 2.0 5.0 allowance
4. INSTRUMENTATION AND CONTROLS - in item 1
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
Appendix B to RG 1.110, Page B-66 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
TER-COOLED NUCLEAR REACTORS Description of Augment Reverse Osmosis - Detergent Wastes DIRECT COST (1975 $1,000) 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
LABOR 8.8 4% less bldg + 24 module with 3-yr life @ $600 each
3. CONSUMABLES, CHEMICALS, AND
SUPPLIES neg 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 O AND M ANNUAL COST 16.2
Appendix B to RG 1.110, Page B-67 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) ITEM LABOR
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST 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/ft 3 (shielded area)
3. ASSOCIATED PIPING SYSTEMS 2 1 3 10% of item 1
4. INSTRUMENTATION AND CONTROLS 4 6 10 allowance
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
Appendix B to RG 1.110, Page B-68 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
TER-COOLED NUCLEAR REACTORS Description of Augment 10,000-Gallon Tank (Sheet 2) DIRECT COST (1975 $1,000) ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 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
SUPPLIES neg 4. UTILITIES AND SERVICES Waste Disposal Water Steam neg Electricity Building Services Other
5. TOTAL O AND M ANNUAL COST 2.7
Appendix B to RG 1.110, Page B-69 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 C to RG 1.110, Page C-1 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 th e Indirect Cost Factor and the Capital Recovery Factor.
Appendix C to RG-1.110, Page C-2 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS Description of Augment DIRECT COST (1975 $1,000) ITEM LABOR
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT
2. BUILDING ASSIGNMENT
3. ASSOCIATED PIPING SYSTEMS
4. INSTRUMENTATION AND CONTROLS
5. ELECTRICAL SERVICE
6. SPARE PARTS SUBTOTAL
7. CONTINGENCY
8. TOTAL DIRECT COSTS
Appendix C to RG-1.110, Page C-3 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
TER-COOLED NUCLEAR REACTORS Description of Augment DIRECT COST (1975 $1,000) ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD 2. MAINTENANCE MATERIAL AND
LABOR 3. CONSUMABLES, CHEMICALS, AND
SUPPLIES 4. UTILITIES AND SERVICES Waste Disposal Water Steam Electricity Building Services Other
5. TOTAL O AND M ANNUAL COST
- U.S. Government Printing Office: 1987-202-292:60255