Regulatory Guide 1.110: Difference between revisions

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{{Adams
{{Adams
| number = ML13241A052
| number = ML003740332
| issue date = 10/07/2013
| issue date = 03/31/1976
| title = Cost Benefit Analysis for Radwaste Systems for Light-Water-Cooled Nuclear Power Reactors
| title = Cost-Benefit Analysis for Radwaste Systems for Light-Water-Cooled Nuclear Power Reactors
| author name =  
| author name =  
| author affiliation = NRC/RES
| author affiliation = NRC/RES
Line 9: Line 9:
| docket =  
| docket =  
| license number =  
| license number =  
| contact person = Rodriguez-Luccioni H
| contact person =  
| document report number = RG-1.110, Rev 1
| document report number = RG-1.110
| package number = ML13238A086
| document type = Regulatory Guide
| document type = Regulatory Guide
| page count = 88
| page count = 87
}}
}}
{{#Wiki_filter:U.S. NUCLEAR REGULATORY COMMISSION                                                               October 2013 OFFICE OF NUCLEAR REGULATORY RESEARCH                                                                  Revision 1 REGULATORY GUIDE
{{#Wiki_filter:U.S. NUCLEAR REGULATORY COMMISSION                                                                                             March 1976 REGULATORY GUIDE
                                        REGULATORY GUIDE 1.110
OFFICE OF STANDARDS DEVELOPMENT
  COST-BENEFIT ANALYSIS FOR RADWASTE SYSTEMS FOR
                                                                                                                                            4 REGULATORY GUIDE 1.110
      LIGHT-WATER-COOLED NUCLEAR POWER REACTORS
                        COST-BENEFIT ANALYSIS FOR RADWASTE S
                            LIGHT-WATER-COOLED NUCLEAR PDWE&                                    CRS'
                    USNRC REGULATORY GUIDES                                      Commen.l shoutd be Sent to Rhe Secretary of the Comm,ssion U S Nuclea,
%equietoy Guido* ate issued to describe and meeks ovelablto          ,he  pubic  Rogulstory Comminssion Washington. 0 C 2065. Attention Docketing end S
methods acceptable go the NRC staff of4 impementing specific pairt of the Commission'& fegulatione. to definetel techniquemused by the state in evild      The guides are issued in the following ten broaddivisions at"ig *pecific problems or postulated accidents. 0r to provide guidance to eppli cents Regulatory Gudes am not substitutes for regulamons. end compliance          I  Power Reactors                      5  Products with thenmilerot reCed Methods end soutione diflerent fron those get outi        I  Research end Test Reactors          7  Tronsponstion Ihe guidell we be acceptable It they provide a bahis for lthefindings requrlit to 3  Fueuls and Materiels Facilities    a  Occupolionat 4palt h themesnee
      *l          sentis*lnCe- of - permst of Scenes by the Commitssion          4  Environmental and Siting            2  Antitrust Review Commentd Isid uggestiOi$e        #0F imPtoSetfitC it #hbae gtaldel We entcouraged S Materialt end Plant Protection      10 General ot            end guidss Wil be Revised. a. a41pp1rop1riete.


==A. INTRODUCTION==
anll.                                          to accommodate corn asmon ed                ho wtcintormatiotn or e*perieot    Ifowoer comments on  Copies of published guides may be obtained by wistten .squett indicating Cth Ofu guide. A received within Oboinstwo month$ chatret. issuance. will be *at      divisions desired to the U S Nuclear Regulators Commission Wshtington 0 C
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
ticfady orssIul Mtevaluating the =teed of an srly viision                        20566.Attention Director. Office of Standerde Development
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 Regulations Section II.D of Appendix I, Numerical Guides for Design Objectives and Limiting Conditions for Operation to Meet the Criterion As Low As Is Reasonably Achievable for 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
TABLE OF CONTENTS
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,
                                                                                                                          Page
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.
==A. INTRODUCTION==
.......................................................................                                 1.110-5


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/.
==B. DISCUSSION==
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.
R .......................................................................                                   1.110-5


calculation will be made available to applicants or licensees, and that calculational procedures found to be unnecessary will be eliminated.
==C. REGULATORY POSITION==
.........................................................                                        1.110-6 D.    IMPLE14ENTATION ................................                                  .................................. 1.110-6 APPENDIX A, PROCEDURES FOR PERFORMING COST-BENEFIT ANALYSES ...........................                                    1.110-7 APPENDIX B. BASES FOR PARAMETERS USED IN PERFORMING COST-BENEFIT
ANALYSES ..............................................................................                                    1.110-17 LIST OF APPENDIX B COST ESTIMATE SHEETS ...............................................                                    1.110-19 REFERENCES TO APPENDIX B..............................................................                                    1.110-85 APPENDIX C, DATA NEEDED FOR RADWASTE TREATMENT SYSTEM COST-BENEFIT
ANALYSIS FOR LIGHT-WATER-COOLED NUCLEAR REACTORS ......................................                                    1.110-86 SAMPLE ESTIMATE SHEETS ................................................................                                    1.110-88
                                                                              1.110-3


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.
LIST OF TABLES
 
Table                                                                              Page A-1   Direct Costs - Gaseous Radwaste Augments ................................ 1.110-8 A-2  Annual Operating Costs - Gaseous Radwaste Augments; Liquid Radwaste Augments .....................................................  1.110-10
It also suggests parameters for the estimation of radiation doses to man from effluent releases.
A-3  Annual Maintenance Costs - Gaseous Radwaste Augments; Liquid Radwaste Augments ..................................................... 1.110-12 A-4  Labor Cost Correction Factors ........................................... 1.110-13 A-5  Indirect Cost Factors ................................................... 1.110-14 A-6  Capital Recovery Factors ................................................ 1.110-15 B-1  Indirect Costs .......................................................... 1.110-18 LIST OF FIGURES
 
Figure                                                                            Page A-1  Electric Power Supply Areas in the United States ........................ 1.110-16
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.
                                                        1.110-4
 
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==
==A. INTRODUCTION==
................................................................................................................................... 1 Purpose......................................................................................................................................... 1 Applicable Rules and Regulations ............................................................................................... 1 Related Guidance ......................................................................................................................... 2 Purpose of Regulatory Guides ..................................................................................................... 2 Paperwork Reduction Act ............................................................................................................ 2
Section I1.D of Appendix I, "Numerical Guides for Design Objectives and Limiting Conditions for Operation to Meet the Criterion 'As Low As Is Reasonably Achievable' for Radioactive Material in Light-Water-Cooled Nuclear Power Reactor Effluents," to 10 CFR Part 50, "Licensing of Produc tion and Utilization Facilities," requires that liquid and gaseous radwaste systems for light water-cooled nuclear power reactors include all items of reasonably demonstrated technology that, when added to the system sequentially and in order of diminishing cost-benefit return, can, for a favorable cost-benefit ratio, effect reductions in dose to the population reasonably expected to be within 50 miles of the reactor. Values of $1000 per man-rem and $1000 per man-thyroid-rem are given as interim criteria pending the development and establishment of better criteria.


==B. DISCUSSION==
Compliance with Section II.D of Appendix I to 10 CFR Part 50 (which specifically addresses doses to the population) and Sections IL.A, 11.8, and II.C (which address doses to nearby individuals)
.......................................................................................................................................... 4 Reason for Revision ..................................................................................................................... 4 Background .................................................................................................................................. 4 Harmonization with International Standards ............................................................................... 4 C. STAFF REGULATORY GUIDANCE .................................................................................................... 4
is required to meet the criterion, "as low as is reasonably achievable."
      To'implement the requirements of Appendix I, the NRC staff has developed a series of guides providing methods acceptable to the staff for the calculation of effluent releases, dispersion of effluents in the atmosphere and different water. bodies, associated radiation doses to man, and cost-benefit aspects of treating radwastes. This regulatory guide describes a method for performing a cost-benefit analysis for liquid and gaseous radwaste system components.


==D. IMPLEMENTATION==
The procedures and models provided in this guide will be subject to continuing review by the staff with the aim of providing greater flexibility to the applicant in meeting the require ments of Appendix I. As a result of such reviews, it is expected that alternative acceptable methods for calculation will be made available to applicants and that calculational procedures found to be unnecessary will be eliminated.
.............................................................................................................................. 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==
==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.
Each applicant for a permit to construct or a license to operate a light-water-cooled nuclear power reactor and each licensee with a license to operate a light-water-cooled nuclear power reactor is required to provide reasonable assurance that the design objectives for as low as is reasonably achievable effluent releases are satisfied by the liquid and gaseous radwaste system designs. It is the objective of this guide to provide an acceptable method of performing cost-benefit analysis, in conformance with Section II.D of Appendix I, to demonstrate that the plant design includes all items of reasonably demonstrated technology for reducing the cumula tive population dose due to releases of radioactive materials from the reactor to levels as low as reasonably achievable. As an interim measure the Conmnission chose values of $1000 per man rem and $1000 per man-thyroid-rem (or lesser values if demonstrated to be suitable for a particu lar site) to be used to implement the cost-benefit analysis.


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 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.


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 equip ment items in use, or proposed for use, at light-water-cooled nuclear power reactors. The methodology and cost parameters are presented in Appendix A to this guide. The costs presented.


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.
consider the direct equipment cost and the costs of building space, supportive services, mainte nance, interest, and operating as well as other costs generally considered in analyzing capital and operating costs in power plant estimating. The bases for the costs calculated by the NRC
  staff are given in Appendix B.


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.
1-110-5


C. STAFF REGULATORY GUIDANCE
==C. REGULATORY POSITION==
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
1.   In accordance with Section II.D, Appendix I to 10 CFR Part 50, each applicant for a permit to construct a light-water-cooled nuclear power reactor should demonstrate by means of a cost benefit analysis that further reductions to the cumulative dose to the population within a
        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).
50-mile radius of the reactor site cannot be effected at an annual cost of $1000 per man-rem or
                                              Rev. 1 of RG 1.110, Page 4
$1000 per man-thyroid-rem (or such lesser costs as demonstrated to be suitable for a particular case).
2.    The cost-benefit analysis should consider the reduction in releases of radioactive material from all effluent pathways. Liquid and gaseous radwaste system augments considered in the analysis should be selected in order of diminishing cost-benefit returns.


2.       The cost-benefit analysis should consider the reduction in releases of radioactive material from all effluent pathways. Liquid and gaseous radwaste system augments considered in the analysis should be selected in order of diminishing cost-benefit returns.
3.   All costs should be given in terms of 1975 dollars (as is the $1000 per man-rem cost with which they are compared). Allowances for Inflation after 1975 should not be factored into the cost estimates.


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.


4.       The method of calculation described in Appendix A and the parameters presented in Appendix B
5.   In support of the cost-benefit analysis, the applicant should provide a complete evaluation including methodology used, components considered, and all assumptions and parameters used.
        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.
Information to be submitted by the applicant Is described in Appendix C to this guide. Use of parameters, assumptions, and models different from those given in Appendices A and B to this guide may result in differences between the evaluations by applicants and those by the NRC staff.


==D. IMPLEMENTATION==
Because of this, these parameters and assumptions should be clearly described and substantiated by the applicant.
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
===0. IMPLEMENTATION===
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.
    The purpose of this section is to provide information to license applicants and licensees regarding the NRC staff's plan for using this regulatory guide.


Licensees may use the information in this regulatory guide for actions that do not require NRC
Except in those cases in which the applicant proposes an acceptable alternative method for complying with specified portions of the Commission's regulations, the method described herein will be used in the evaluation of construction permit applications docketed after June 4, 1976 unless this guide is revised as a result of suggestions from the public or additional staff review.
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
If an applicant wishes to use this regulatory guide in developing submittals for applications docketed on or before June 4, 1976, the pertinent portions of the application will be evaluated on the basis of this guide.
        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.
1.110-6


Rev. 1 of RG 1.110, Page 5
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.


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
1.    The cumulative population man-rem exposure and man-thyroid-rem exposure should be determined for each effluent release source, e.g., liquid radwaste releases, ventilation releases, etc.


====s. The NRC====
2. Potential reductions to the cumulative population exposure should be determined based on the addition of items of reasonably demonstrated technology which have the potential to reduce releases of radioactive materials.
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.
3.    Acceptable methods for performing some of the calculations need for items 1 and 2 above are contained in Regulatory Guides 1.109, "Calculation of Annual Doses to.Man from Routine Releases of Reactor Effluents for the Purpose of Evaluating Compliance with 10 CFR Part 50, Appendix I,"
and 1.111, "Methods for Estimating Atmospheric Transport and Dispersion for Gaseous Effluents in Routine Releases from Light-Water-Cooled Reactors," and in two regulatory guides now in prepara tion on the subjects of (1) calculation of releases of radioactive materials In liquid and gas eous effluents from light-water-cooled reactors and (2) methods for estimating aquatic dispersion of liquid effluents from routine reactor releases for the purpose of implementing Appendix I.


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
4.    The total annual cost of each augment considered in item 2 above should be determined as follows:
10 CFR Part 52.
      a.   The Total Direct Cost (TOC):
          (1) Obtain the direct cost of equipment and materials from Table A-1.


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
(2)  Multiply the direct labor cost obtained from Table A-1 by the appropriate labor cost correction factor from Table A-4 to obtain the corrected labor cost for the geographtcal area from Figure A-l, in which the plant is to be built.
Management Directive 8.4, Management of Facility-Specific Backfitting and Information Collection (Ref. 7).
                                              Rev. 1 of RG 1.110, Page 6


3 REFERENCES
(3)  Add the costs obtained from steps (1) and (2) to obtain the Total Direct Cost.
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.
b.   Obtain-the appropriate Indirect Cost Factor (ICF)   from Table A-S.


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


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


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.
g.  Determine the Total Annual Cost (TAC) by using the equation:
                          TAC
* AFC + AOC + AMC
5.   Determine the "benefit" of each augment by multiplying the dose reduction calculated in item 2 above by $1000 per man-rem and/or $1000 per man-thyroid-rem, as appropriate.


6. NRC, NUREG-1409, Backfitting Guidelines, Washington, DC.
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.


7. NRC, Management Directive 8.4, Management of Facility-specific Backfitting and Information Collection, Washington, DC.
1.110-7


3.
TABLE A-1 DIRECT COSTS -  GASEOUS RADWASTE AUGMENTS
                                                        Direct- Costs
                                                                                  (1975 $1000)
                                            Equipment/Material        Labor        Total BWR Offgas Recombiner                              553                  255          808
3-ton Charcoal Adsorber                              53                  14            67 Desiccant Dryer                                    218                  176          394 Charcoal Vault Refrigeration                        116                  38          154 Main Condenser Vacuum Pump Charcoal/HEPA
Filtration System                                    40                    8            48 Clean Steam to Turbine Glands                        81                  215          296 Clean Steam to Steam Valves. 24" and Larger                                              137                  110          247 Clean Steam to Steam Valves, 2-1/2"
and Less Than-24"                                  183                  55          238
15,000-cfm HEPA Filtration System                    52(49)*              16(14)*      68(63)*
1,000-cfm Charcoal/HEPA Filtration System            28                  10            38
15,000-cfm Charcoal/HEPA Filtration System          97(93)              31(26)      128(119)
30,000-cfm Charcoal/HEPA Filtration System          157(152)              51(41)      208(193)
Turbine Bldg. Chilled Water HVAC System            614                  374          988
600-ft 3 Gas Decay Tank                              33                  24            57 PWR Hydrogen Recombiner                            419                  147          566 PWR Air Ejector Charcoal/HEPA
Filtration Unit                                      14                  10            24 Steam Generator Flash Tank Vent to Main Condenser                                      19                  14            33 In cases where the equipment may be located either in the auxiliary building or the turbine building and common usage does not indicate a definite preference of one location or the other, cost for both locations are listed with the turbine building location cost in parenthesis.


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.
1.110-8


Rev. 1 of RG 1.110, Page 7
TABLE A-1 (Continued)
                          DIRECT COSTS - LIQUID RADWASTE AUGMENTS
                                                      Direct Costs
                                                                        (1975 $1000)
                                                                            Total Equipment/Material        Labor
                                                  386                201      587
15-gpm Evaporator
                                                  540                223      763
30-gpm Evaporator
                                                  655                233      888
50-gpm Evaporator
                                                  36                24      60
Evaporator Distillate Demineralizer
                                                  43                29      50
50-gpm Demineralizer
                                                  64                31      95
100-gpm Demineralizer
                                                  94                35      129
200-gpm Deminieralizer
                                                  102                44      146
400-gpm Demineralizer
                                                  108                56      164
100-gpm Precoat Filter
                                                  202                112      314
400-gpw Precoat Filter
                                                  13                11      24
20-gpm Cartridge Filter
                                                  100                38      138
2-gpm Reverse Osmosis
                                                  55                43      98
10,000-gal Tank
                                              1.110-9


APPENDIX A
TABLE A-2 ANNUAL OPERATING COSTST - GASEOUS RADWASTE AUGMENTS
    PROCEDURES FOR PERFORMING COST-BENEFIT ANALYSES
                                                              Total Operating Cost (1975 $lOOO/yr)
       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.
                                                                                    B        r m  m BWR Offgas Recoatbiner                                                          3
3-ton Charcoal Adsorber                                                      neg Desiccant Dryer                                                                3 Charcoal Vault Refrigeration                                                    4 Main Condenser Vacuum Pump Charcoal/HEPA
Filtration System                                                              0.4 Clean Steam to Turbine Glands                                                24 Clean Steam to Steam Valves, 24" and Larger                                    3 Clean Steam to Steam Valves, 2-1/2" and Less Than 24"                                                                  3
15,000-cfm HEPA Filtration System                                              6
1,000-cfm Charcoal/HEPA Filtration System                                      2
15,000-cfm Charcoal/HEPA Filtration System                                    7
30,000-cfm Charcoal/HEPA Filtration System                                    9 K
Turbine Bldg. Chilled Water HVAC System                                      49
       3
600-ft  Gas Decay Tank                                                      neg PWR Hydrogen Recombiner                                                        4 PWR Air Ejector Charcoal/HEPA Filtration Unit                                  4 Steam Generator Flash Tank Vent to Main Condenser                              1 ANNUAL OPERATING COSTS  - LIQUID RADWASTE AUGMENTS
Evaporation - PWR Dirty Waste                                                50
Evaporation - BWR Dirty Waste                                              169 Evaporation - Condensate Polisher Chemical Waste                            114 Evaporation - Detergent Waste                                                20
Demineralization - kvaporator Distillate                                      5 Demineralization - BWR 2nd Waste Demineralizer in Series                    15 Operating costs are given for a single reactor. Operating costs for augments in shared radwaste systems should be multiplied by the number of reactors serviced by the augment.


1.     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.)
1.110-10
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,
TABLE A-2 (Continued)
      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
                        ANNUAL OPERATING COSTS - LIQUID RADWASTE AUGMENTS
      (2) methods for estimating aquatic dispersion of liquid effluents from routine reactor releases for the purpose of implementing Appendix I.
                                                            Total Operating Cost (1975 $1000/yr)
                                                                            5 Demineralization - PWR Clean Waste Demineralization - BWR Dirty Waste                                          88
                                                                            18 Demineralization - PWR Dirty Waste
                                                                            95 Demineralization - PWR Turbine Bld


4.     The total annual cost of each augment considered in item 2 above should be determined as follows:
====g. Drains====
      a.      The Total Direct Cost (TDC):
                                                                            25 Desmineralization - PWR Steam Generator Blowdown
                (1)      Obtain the direct cost of equipment and materials from Table A-1.
                                                                            53 Precoat Filter - BWR Dirty Waste Cartridge Filter                                                            7
                                                                            7 Reverse Osmosis - Detergent Waste
                                                                            1
10,000-gal Tank
                                                1.110-11


(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.
TABLE A-3 ANNUAL MAINTENANCE COSTS-  GASEOUS RADWASTE AUGMENTS
                                                          Total Maintenance Cost (1975 $1O00/Yr)
BWR Offgas Recombiner                                                        20
3-ton Charcoal Adsorber                                                      neg Desiccant Dryer                                                              6 Charcoal Vault Refrigeration                                                  3 Main Condenser Vacuum Pump Charcoal/HEPA
  Filtration System                                                          1 Clean Steam to Turbine Glands                                                  4 Clean Steam to Steam Valves, 24" and Larger                                    4 Clean Steam to Steam Valves, 2-1/2" and Less Than 24"                                                            12
15,000-cfm HEPA Filtration System                                              2
1,000-cfm Charcoal/HEPA Filtration System                                      0.6
15,O00-cfm Charcoal/HEPA Filtration System                                    9
30,000-cfm Charcoal/HEPA Filtration System                                  18 Turbine Bldg. Chilled Water HVAC System                                      20
600-ft 3 Gas Decay Tank                                                      neg PWR Hydrogen "Recombiner                                                    10
PWR Air Ejector Charcoal/HEPA Filtration Unit                                2 Steam Generator Flash Tank Vent to Main Condenser                            1 ANNUAL MAINTENANCE COSTS - LIQUID RADWASTE AUGMENTS
15-gpm Evaporator                                                          30
30-gpm Evaporator                                                          30
50-gpm Evaporator                                                          30
Evaporator Distillate Demineralizer                                          2
50-gpm Demineral izer                                                        5 lO0-gpmi Demineralizer                                                        5
200-gpm Demineral izer                                                        S
100-gpm Precoat Filter                                                      10
400-gpm Precoat Filter                                                      10
20-gpm Cartridge Filter                                                      1
2-gpm Reverse Osmosis                                                        g
10.000-gal Tank                                                              2
                                                1.110-12


(3)      Add the costs obtained from steps (1) and (2) to obtain the TDC.
TABLE A-4 LABOR COST CORRECTION FACTORS
                  FPC
              Geographic                            Labor Cost Correction Region                                        Factor I                                          1.6
                                                              1.5
                  1II
                                                              1.0
                  IV                                          1.4 V                                          1.1 VI                                          1.2 VII                                          1.3 Vlll                                          1.2 See Appendix B, "Labor Cost Correction Factors.'
See Figure A-1.


b.       Obtain-the appropriate Indirect Cost Factor (ICF) from Table A-5.
1.110-13


c.      Determine Total Capital Cost (TCC) by using the equation:
TABLE A-5 INDIRECT COST FACTORS
                                            TCC = TDC x ICF
    Type Radwaste System                          Indirect Cost Factor
      d.       Obtain the appropriate Capital Recovery Factor (CRF) from Table A-6.
"1.  Single unit site, unitized    radwaste system                                                    1.75
2.  Multi-unit site, shared radwaste system                                                    1.75
3.  Multi-unit site, unitized  radwaste system                                          1.75 + (n-1)1.5 n
                                                where n is the number of unitized radwaste systems at the site Each reactor has a separate, nonshared radwaste system.


e.       Determine the Annual Fixed Cost (AFC) by using the equation:
I..
                                            AFC = TCC x CRF
                                       1.110-14
                                       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.
TABLE A-6 CAPITAL RECOVERY FACTORS
          Cost of Honey                                  Capital Recovery Factor
          (1 per year, i)
                5                                              0.0651
                                                              0.0726
                6
                                                              0.0806
                7
                                                              0.0888
                8
                                                              0.0973
                9
                                                              0.1061
              10
                                                              0.1150
              11
                                                              0.1241
              12
                                                              0.1334
              13
                                                              0.1428
              14
                                                              0.1523
              15
*
  Based on a service life of 30 years and the follwing equation:
                CRF    M + 1)3 (I + i)30-1
                                            1.110-15


g.     Determine the Total Annual Cost (TAC) by using the equation:
LEGEND
                                        TAC = AFC + AOC + AMC
                            ¶Im     REGIONAL GROUPING OF POWER SUPPLY AREAS
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.
  FIGURE A-1 ELECTRIC POWER SUPPLY AREAS IN THE UNITED STATES
(                    C                                                        C


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.
APPENDIX B
                    BASES FOR PARAMETERS USED IN PERFORMING COST-BENEFIT ANALYSIS
      This appendix contains detailed cost estimate sheets showing the methods and parameters used to obtain all costs associated with augments considered for the liquid and gaseous radwaste systems. The cost estimate sheets are grouped by radwaste system types. The first sheet in each case is an equipment cost worksheet for determining direct equipment costs. The second sheet is an operating cost worksheet. All costs are stated in terms of 1975 dollars. No attempt has been made to project the effect of inflation. Variations of labor costs and productivity with site locaticns are considered.* All costs are based on the assumption that the reactor is in the design stage and that augmentation of a radwaste system will not involve backfltting of an existing plant. Backfltttng costs should be determined on a case-by-case basis.


Table A-1. Direct CostsGaseous Radwaste Augments, Liquid Radwaste Augments DIRECT COSTSGASEOUS RADWASTE AUGMENTS
1.   Capital Costs Capital costs are reported by grouping items by system and by plant location, which gen erally follow the NRC (AEC) accounting system given in NUS-531 (Ref. 1). The direct costs considered to be applicable to radwaste systems are structures, electrical services, equipment, and instrumentation and controls. Spare parts and a contingency allowance** are included in the direct costs. Total capital costs are obtained by multiplying direct costs by an indirect cost factor.
                                                        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
2.    Direct Cost Direct costs for each augment include equipment, site labor, and site materials. Principal equipment designs and hardware costs were obtained from utility companies, architect-engineers, and vendors. Costs for building space, electrical services, piping, and instrumentation were estimated considering equipment functions and arrangements.
                                                            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)
Costs for electric services, piping, and instrumentation and controls were determined using judgment to estimate equipment layout, points of interface, and services required. The costs for equipment and building space are consistent with'NRC staff recommendations for radwaste sys tem quality assurance, materials, and seismic design. Space requirements were determined based on manufacturer's data or data from existing or proposed layout drawings.
                                                            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
3.    Labor Cost Correction Factors Labor cost adjustment factors were developed for each Of the eight FPC electric power supply areas shown in Figure A-I of Appendix A by calculiting the average labor cost-for selected cities (Ref. 2) in each area and adjusting this cost for estimated variations in labor productivity due only to differences In labor practices in the regions considered. Manpower costs were calcu lated by multiplying the estimated labor requirements in man-hours by the composite wage rate (Ref. 3). The calculated labor cost correction factors are tabulated in Table A-4 of Appendix A.
                                                                  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
4.   Indirect Cost Factor Indirect costs asa percentage of direct costs are calculated in Table B-1.
                                                                                      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.
Location effects of the eight FPC Power Supply areas are estimated and shown in Table A-4 of Appendix A.


Table A-3. Annual Maintenance CostsGaseous Radwaste Augments, Liquid Radwaste Augments ANNUAL MAINTENANCE COSTSGASEOUS RADWASTE AUGMENTS
Contingency onsite labor and process equipment and material are all based on-l0%.
                                                                                        TOTAL OPERATING
                                                1.110-17
                                                                                      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
TABLE 8-1                                          K..
                                                                    TOTAL OPERATING
                                          INDIRECT COSTS
                                                                    COST (1975 $1,000/YR)
                                                          1st Unit,          Subsequent Percentage of      Units. Percentage Direct Cost        of Direct Cost Construction facilities, equiment, and services                                                10                   5 Engineering and construction managment services                                         20                  10
30,000-cfm Charcoal/HEPA Filtration System                                  18 Turbine Bldg. Chilled Water HVAC System                                    20
Other owner s costs                                        10                   S
600-ft3 Gas Decay Tank                                                    neg PWR Hydrogen Recombiner                                                    10
Interest during construction                                3S                  35 Total                  75                  SS
PWR Air Ejector Charcoal/HEPA Filtration Unit                                2 Steam Generator Flash Tank Vent to Main Condenser                            1 Annual Maintenance Costs -Liquid Radwaste Augments
*Based on a lOs/yr interest rate and a 4-year construction time for radaste systems only.
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
Interest during construction Is estimated to be 25% of direct costs plus other indirect costs. This is equivalent to 351 of the direct costs.
                      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.
The Indirect escalators (factors) were estimated from preliminary architect/engineering data to be used to update the DOM concept and ORCOST computer codes.


b.
S.    Operation And Maintenance Costs Annual expenses for operation and maintenance (O&N) of the radwaste treatment systes were estimated for baseload power plants operating at 801 capacity factor. Manpower and supply costs were estimated by considering equipment functions it each case. Expenses for gases, steam, resins, auxiliary por. and other supplies and services were assessed individually. Maintenance costs were evaluated according to the type of service for which the equipment could be used.


See Figure A-1.
Operating costs include estimated manpower costs, costs of utilities and supplies, and effects on supporting plant systems Interfacing with the augmented radmste system (e.g., effect of an evaporator augment on the solid waste syste). Also included are costs of handling wastes such as spent resins, demineralizer regenerants, evaporator bottoms, and filter media, as well as offsite handling, transportation, and burial costs.


Table A-5. Indirect Cost Factors TYPE RADWASTE SYSTEM                          INDIRECT COST FACTOR
6.   Capital Recovery Factor The capital recovery factor Is a levelized annual charge which takes into account the cost of borroved money and the depreciation of assets. It Is calculated from the expression:
1. Single unit site, unitized a radwaste                          1.75 system
                I(1 #)o (I + ~
2. Multiunit site, shared radwaste system                        1.75
where i a cost of borrowed money expressed as a decimal P - plant operating lifetime (yr)
3. Multiunit site, unitizeda radwaste system                1.75 + ( n  1)1.5 n
In calculating the values used in Table A-S of Appendix A. a plant operating lifetime of 30
                                                    where n is the number of unitized radwaste systems at the site a.
years was used.


Each reactor has a separate, nonshared radwaste system.
The capital recovery factor multiplied by the total capital cost will give the annual dollar charges for capital and capital-related expenses.


Appendix A to RG 1.110, Page A-7
1.110-18


Table A-6. Capital Recovery Factors COST OF MONEY
LIST OF APPENDIX B COST ESTIMATE SHEETS
(% PER YEAR, I)                  CAPITAL RECOVERY FACTORa
                                                                                                    Page Numiber BW Offgas Recmbiner .............................................................                1.110-20
           5                                          0.0651
3-ton Charcoal Adso            r ............................................................... 1.110-22 Desiccant Dryer ..............................................................                    1.110-24 Charcoal Vault Refrigeration .........................................................            1.110-26 Charcoal/HEPA Filtration System - Condenser Vacuun Pump ..............................            1.110-28 Clean Steam to Turbine Glands ........................................................            1.110-30
          6                                          0.0726
Clean Steam to Steam Valves 24- and Larger ...........................................            1.110-32 Clean Steam to Steam Valves 2-1/2' and Less Than 24" ................................            1.110-34
          7                                          0.0806
1S.000-cftm NEPA Filtration System ....................................................           1.110-36
           8                                          0.0888
1000-cfa Charcoal/HEPA Filtration System .............................................            1.110-39
          9                                          0.0973
15.000-cfm Charcoal/HEPA Filtration System ...........................................            1.110-41
        10                                         0.1061
30,000-cfm Charcoal/HEPA Filtration System ..........................................            1.110-44 Turbine Building Chilled Mater HVAC System ...........................................            1.110-47
        11                                          0.1150
600-ft 3 Gas Decay Tank ...............................................................           1.110-49 PIW Hydrogen Recombiner ..............................................................            1.110-S1 PiW Air Ejector Charcoal/HEPA Filtration Unit ........................................            1.110-53 Stem Generator Flash Tank Vent to rain Condenser ....................................            1.110-55 Evaporators ..........................................................................            1.110-57 Evaporator Distillate Demineralizer ..................................................            1.110-64 Demineralizers .......................................................................            1.110-66 Cartridge Filter .....................................................................            1.110-76 Precoat Filters ......................................................................            .114  7R
        12                                          0.1241
Reverse Osmosis .....................................................................            1.110-81
        13                                          0.1334
10.000-gal Tank ...........................................................                     1.11"
        14                                          0.1428
                                                                          1.110-19
        15                                          0.1523 a.


Based on a service life of 30 years and the following equation:
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
                                        i(1 + i )30
                                                          FOR LIGHT-WATER-COOLEDS...... NUCLEAR
                               CRF =
                                                                                        .................. REACTORSw Description of Augment        RUD flffn.e  D  r.mh4n.... iCk.e.    11 BWR Off a %e Darr-M--- Ick- Wa,Ii DIRECT COST.(1975 $1000)
                                      (1 + i)30  1 Appendix A to RG 1.110, Page A-8
                  ITEM                                IARND                  r1 T DMUT'/MATrD TAt                    TflYAi BASIS FOR
                                                                I___MIXL_                                  1        IVIML        COST ESTIMATE
  1.  PROCESS EQUIPMENT                                  90                        260                                350  single unit, catalytic type w/heater and condenser, w/o instrumentation and controls, stainless steel, ASME VIII
  2.  BUILDING ASSIGNMENT                              100                          50                                ISO  30' x 40' x 25' @ $5/ft 3 (turbine building shielded area)
a    ASSOCIATED PIPING SYSTEMS
  3.                                                    18                          12                                  30 augment piping connections only O
  4.  INSTRUM4ENTATION AND CONTROLS                    24                          96                               120  allowance
  5.  ELECTRICAL SERVICE                                                                                              neq  4kw heaters on vessels neglected SPARE PARTS                                                                    85                                  85  75K for catalyst + 2% E/M in
  6.


Appendix A to RG 1.110, Page A-9 Figure A-1. Electric Power Supply Areas in the United States
items 1 & 4 above SUBTOTAL                                  232                        503                                735
  7. CONTINGENCY                                        23                          50                                  73  10%
  8. TOTAL DIRECT COSTS                              2S5                        553                                808
(
                                                                                                                                                      r


APPENDIX B
A                                                                K  I
                BASES FOR PARAMETERS USED IN PERFORMING
                                    ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
                                        COST-BENEFIT ANALYSIS
                                                  SYSTEM FOR-LIGHT-WATER-COOLED NUCLEAR REACTORS
         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.
      Description of Augment    BWR Offgas Recombiner (Sheet 2)
                                                                  COST (1975 $1000)
                  ITEM                          LABOR          OTHER         TOTAL              BASIS FOR COST ESTIMATE
    1. OPERATING LABOR, SUPERVISION,                                            3.3        15 m.n/shift AND OVERHEAD
    2. MAINTENANCE MATERIAL AND.                                              20.0        routine conditioning of catalyst and LABOR                                                                              equipment upkeep; 5% of E/M including I&C
    3. CONSUMBLES, CHEMICALS, AND                                              -            initem 2
,01 C2    SUPPLIES
    4. UTILITIES AND SERVICES
        Waste Disposal Water Steam                                                                  neg        intemittent; 4kw heater load is negligible Electricity Building Services Other
    5. TOTAL 0 AND M ANNUAL COST                                              23.3


All costs are stated in terms of 1975 dollars. No attempt has been made to project the effect of inflation.
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
                                                                    FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                                                                                      m Description of Augment      3-ton Charcoal Adsorber (Sheet 1)
                                                                            DIRECT COST (1975 $1000)
                                                                                                                                BASIS FOR
                                !TFM                            LABOR            EOUIPMENTIMATERIALS          TOTAL          COST
                                                                                                                                - -
                                                                                                                                    ESTIMATF
                                                                                                                                      -- - - -
                                                                                                                                                      3
                  1. PROCESS EQUIPENT                              5                  44.0                    49.0    carbon steel, 350 psig, 200 ft volume (augment to existing train of beds)
                                                              4.        4.                                  4.      4
                  2. BUILDING ASSIGNMENT                            8                    4.5                    12.5    10' x 10' x 25' * $5/ft3 (turbine building shiel4ed area)
                  3. ASSOCIATED PIPING SYSTES                                                                      -    in item I
              a
                  4. INSTRUKENTATION AND CONTROLS                                                                neg S. ELECTRICAL SERVICE                                                                          neg
                  6. SPARE PARTS                                                                                none  existing SUBTOTAL                                13                  48.5                    61.5
                  7. CONTINGENCY                                    1                    5.0                      6.0  10%
                  8. TOTAL DIRECT COSTS                            14                  53.5                    67.5
. . .. . . . . r                                                                r                                                                  r


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.
K                                                                  K
                                      ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
                                                  SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
        Description of Augment    3-ton Charcoal Adsorber (Sheet 2)
                                                                  COST (1975 $1000)
                  I TFM                        LABOR          OTHER          TOTAL              BASIS FOR COST ESTIMATE
    1. OPERATING LABOR. SUPERVISION.                                            neg AND OVERHEAD
    2.  MAINTENANCE MATERIAL AND                                                            allowance of 3% of equipment cost LABOR                                                                    neg        is negligible
    3.  CONSUMABLES. CHEMICALS, AND
        SUPPLIES                                                                neg        lifetime use of charcoal assumed I..
    4. UTILITIES AND SERVICES
          Waste Disposal Water Steam                                                                  neg Electricity Building Services Other
    5. TOTAL 0 AND M ANNUAL COST                                                neg


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.
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
                                                          FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
        Description of Augment      Desiccant Drver  fSheet !1 Desiccant Drver (Sheet I)
                                                                DIRECT COST (1975 $1000)
                  I TEN                            I ARflR                                      T*TAI
                                                                                                                  BASIS FOR
                                                              1%                  IL                              COTETMT
    1. PROCESS EQUIPMENT                                25                    75                  100  redundant dryer vessels with
                                                                                                          1 regeneration skid
    2. BUILDING ASSIGNMENT                              95                    50                  145  40' x 36' x 20' @ $5/ft 3 turbine building (shielded area)
    3. ASSOCIATED PIPING SYSTEMS                        10                      5                    15  augment piping connections only
8i
  4.   INSTRUMENTATION AND CONTROLS                    12                    48                    60  allowance
  5. ELECTRICAL SERVICE                              18                    17                    35  service for heaters, blowers, pumps, and compressors
  6. SPARE PARTS                                                              3                      3 SUBTOTAL                                  160                  198                    358
  7. CONTINGENCY                                      16                    20                    36  10%
  8. TOTAL DIRECT COSTS                            176                    218                  394
(                                                                  r                                                              r


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.
K                                                                  K                                                            K
                                    ANNUAL CPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
                                                  SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
      Description of Augment    Desiccant Dryer (Sheet 2)
                                                                  COST (1975 $1000)
                  Q*Pim I Ahfl          flTIIP          TflTAI              BASIS FOR COST ESTIMATE
                    itri,,,
                  ITEM                                            ........                              .  .  .  .
                                                                                3.3        15 min/shift
  1.  OPERATING LABOR, SUPERVISION,
      AND OVERHEAD
  2.  MAINTENANCE MATERIAL AND                                                  6.1        5% of equipment including I&C
      LABOR
  3  CONSUMABLES, CHEMICALS, AND                                                neg C      SUPPLIES
U'
  4.  UTILITIES AND SERVICES
          Waste Disposal                                                          neg        operating time does not require neg        significant utilities and services Water Steam Electricity                                                            neg Building Services Other S. TOTAL 0 AND M ANNUAL COST                                                  9.4


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.
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREAThENT SYSTEM
                                                      FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
        Description of Augment      Charcoal Vault Refrigeration (Sheet 1)
                                                              DIRECT COST (1975 $1000)
                                                                                                                  BASIS FOR
                  ITEM                                                                          TftTAI
                                                        LAORFlIITDUdCNT/UATCDTA1
                                                      10AM                            C          YffASIfC              et.V
    1.  PROCESS EQUIPMENT                            10                    75                      85    10-ton capacity, 3 refrigerators with drives, 32°F design I          t                                  4-4
    2. BUILDING ASSIGNMENT                            9                    3                      12    20' x 10' x 201 0 $2/ft 3 turbine building (nonshielded area)
0  3.  ASSOCIATED PIPING SYSTEMS                                                                          In item 1 N
14 Ch
  4.  INSTRUMENTATION AND CONTROLS                  4                      6                      10    allowance
  5.  ELECTRICAL SERVICE                            12                    18                      30    allowance
  6.  SPARE PARTS                                                          3                        3 SUBTOTAL                              35                    105                      140
  7. CONTINGENCY                                    3                    11                      14    10%
  8. TOTAL DIRECT COSTS                          38                    116                      154
                                                                                                                                      (


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)
K                                                              K                                                      K
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.
                                  ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
                                              SYSTEM FOR LIGHT-WATER-COO.EO NUCLEAR REACTORS
    Description of Augment    Charcoal Vault Refriceration (Sheet 2)
                                                              COST (1975 $1000)
                'TIn'                                        rTeR          TOTAL                    FOR COST !T1MATE
  1. OPERATING LABOR, SUPERVISION.                                          3.3        15 min/shift AND OVERHEAD
  2. MAINTENANCE MATERIAL AND
    LABOR                                                                  3.7        51 of equlpemt
  3. CONSUMABLES, CHEMICALS, AND                                                        in Item 2 SUPPLIES
  4. UTILITIES AND SERVICES
      Waste Disposal Water Steam                                                                0.5        electricity and cooling water Electricity Building Services Other S. TOTAL 0 AND MANNUAL COST                                                7.5


4 Location effects of the eight FPC Power Supply areas are estimated and shown in Table A-4 of Appendix A.
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
                                                          FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
        Description of Augment      Charcoal/HEPA Filtration System - Condenser Vacuum Pump (Sheet 1)
                                                                                              i  n    *
                                                                  DIRECT COST (1975 $1000)
                  ITE4                              I A*Q
                                                                                                                  BASIS FOR
                                                    LABOR__        ~    LrILumLAL                IUIAL          COST ESTIMATE
    1.  PROCESS EQUIPMENT                              2                        32.5                34.5  2000 CFM preftlter/4" charcoal bed/HEPA @ S15/cfm, 10 kw heater @ $250/kw
    2.  BUILDING ASSIGNMENT                            3.1                      1.5                  4.6  Turbine building 8' x 16, x 12'
                                                                                                          @ $3/ft 3 (nonshielded area)
Nm
    3. ASSOCIATED PIPING' SYSTEMS                      1.3                      0,7                  2.0  allowance wO
  4.  INSTRUMENTATION AND CONTROLS
                                                                                                          in item 1
  5.  ELECTRICAL SERVICE                            1                          1.5                  2.5
  6.  SPARE PARTS                                                              0.5                0.5 SUBTOTAL                                7.4                      36.7                44.1
  7.  CONTINGENCY                                      .7                      3.7                  4.4  10%
  8.  TOTAL DIRECT COSTS                            8.1                      40.4                 48.5
(                                                                                                                                    (


5 Contingency onsite labor and process equipment and material are all based on l0 percent.
K                                                                      K                                                                    K
                                      ANNUAL OPERATING ANrMAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
                                                  SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
        Description of Augment    Charcoal/HEPA Filtration System - Condenser Vacuum Pump (Sheet 2)
                                                                      COST (1975 $1000)
                                                                    'ueD            TfllhI          S...,iT*
                                                                                                            RAmie    FflQ tOI[IT F¢;TTMATF
    I.  OPERATING LABOR, SUPERVISION,                                                  neg      used only during startup and shutdown AND OVERHEAD
    2.  MAINTENANCE MATERIAL AND                                                        1.2      4 HEPA filters @ $150 & 2 Charcoal filters LABOR                                                                                    @ $900, change every 2 years
    3.  CONSUMABLES, CHEMICALS, AND                                                              initems 2 and 4 SUPPLIES
'.4
*0
    4.  UTILITIES AND SERVICES
          Waste Disposal                                                              0.2      S50/HEPA filter, $100/Charcoal filter Water Steam Electricity Building Services Other
    5.  TOTAL 0 AND M ANNUAL COST                                                      1.4
        _______________________                I            _________          ________    _______________________________


Appendix B to RG 1.110, Page B-1
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
                                                    FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
    Description of Augment      Clean Steam to Turbine Glands (Sheot 1)
                                                            DIRECT COST (1975 $1000)
                FM                                                FOIITDMFNTIMATPRTAI      STTTflTAI        BASIS  FOR
                                                                                                              *FnCT VCTttMATO
                                                I ARAR
                        ITEMP
  1. PROCESS EQUIPMENT                              15                  150                    165  25,000 lb/hr reboiler I $4/lb/hr I
                                                                                                      $25K/H.P. turbine glands
  2. BUILDING ASSIGNMENT                            19                    10                      29  20' x 30' x 16' 6 $3/ft3
  3. ASSOCIATED PIPING SYSTEMS                      32                    18                      50  equiv 1000 ft 0 $50/ft
  4. INSTRUMENTATION AND CONTROLS                    8                    12                      20  in addition to Item I
  5. ELECTRICAL SERVICE                                                                          nag
  6. SPARE PARTS                                                          5                        5 SUBTOTAL                                  74                  195                    269
  7. CONTINGENCY                                    7                    20                      27  10%
  8. TOTAL DIRECT COSTS                            81                  215                    296 r                                                              r                                                              C


4.      Indirect Cost Factor Indirect costs as a percentage of direct costs are calculated in Table B-1.
K                                                                                                                          K
                                    ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
                                                SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
      Description of Augment    Clean Steam to Turbine Glands (Sheet 2)
                                                                COST (1975 $1000)
                1TR4                          LABOR          OTHER          TOTAL              BASIS FOR COST ESTIMATE
  I. OPERATING LABOR, SUPERVISION,                                            3.3      15 min/shift AND OVERHEAD
  2. MAINTENANCE MATERIAL AND                                                  4.0      40 man-days LABOR
  3. CONSUMABLES, CHEMICALS, AND
       SUPPLIES
9'
  4. UTILITIES AND SERVICES
        Waste Disposal Water Steam                                                                21.0        10 Btu/kw-hr heat rate increase Electricity Building Services Other
  5. TOTAL 0 AND M ANNUAL COST                                                28.3


Table B-
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
                                                        FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
        Description of Augment      Clean Steam to Steam Valves 24 " and Larger (Sheet 1)
                                                                DIRECT COST (1975 $1000)
                    ITEM                            I AMII            n:*.:TDAACLIMATDTai BASIS FOR
                                                                                                  TnTAI
      I. PROCESS EQUIPMENT                            100                    120                  220    22 valves @ $1OK/valve, use existing reboiler
    2.  BUILDING ASSIGNMENT                                                                        neg    install in existing space
    3.  ASSOCIATED PIPING SYSTEMS                                                                  -    in item 1
0
i%1J
    4.  INSTRUMENTATION AND CONTROLS                                                                -    in Item 1 S.  ELECTRICAL SERVICE                                                                        neg
    6.  SPARE PARTS                                                            5 SUBTOTAL                                  100                  125                  225
    7.  CONTINGENCY                                    10                    12                    22    10%
    8.  TOTAL DIRECT COSTS                            110                  137                  247
(                                                                                                                                    r


===1. Indirect Costs===
K                                                                -\
                                    1ST UNIT, PERCENTAGE                        SUBSEQUENT UNITS,
                                    ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
                                        OF DIRECT COST                  PERCENTAGE OF DIRECT COST
                                                SYSTEM1 FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Construction facilities,                         10                                            5 equipment, and services Engineering and construction                      20                                          10
      Description of Augment    Clean Steam to Steam Valves 24" and Larger (Sheet 2)
management services Other owners costs                              10                                            5 Interest during construction                      35a                                          35a Total                                            75                                          55 a.
                                                                COST (1975 $1000)
                TT!M                          LABOR          OTHER          TOTAL              BASIS FOR COST ESTIMATE
  1. OPERATING LABOR, SUPERVISION,                                           3.3        15 min/shift AND OVERHEAD
  2. MAINTENANCE MATERIAL AND                                                4.0        40 man-days LABOR
  3. CONSUMABLES, CHEMICALS, AND                                              neg SUPPLIES
w U,
  4. UTILITIES hND SERVICES
        Waste Disposal Water Steam                                                                  neg Electricity Building Services Other TOTAL 0 AND M ANNUAL COST                                                7.3


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
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
    35 percent of the direct costs.
                                                        FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
        Description of Augment      Clean Steam to Steam Valves 2-1/2N and Less Than 24" (Sheet 1)
                                                              DIRECT COST (1975 $1000)
                                                                                                                  BASIS FOR
                    ITEM                            LAB OR            EQUIPMENT/MATERIALS        TOTAl_        (*fl[T F*TIUATF
                                                                                                                COS    ESTIMATE
                                                                                                  TOTAL
    1.  PROCESS EQUIPMENT                            0                    120                    120  100 valves 0 $1200 each
    2.  BUILDING ASSIGNMENT                          -                      -                    neg
-*  3. ASSOCIATED PIPING SYSTEMS                    40                      20                      60
      .
w
.h 4.6.


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.
INSTRUMENTATION AND CONTROLS                10                      20                      30  allowance
  5.  ELECTRICAL SERVICE                                                                          -    none
  7.e
  6.  SPARE PARTS                                  -                        6                      6 SUBTOTAL                              50                    166                    216
  7.  CONTINGENCY                                  5                      17                      22  10%
  8.  TOTAL DIRECT COSTS                          55                    183                    238 I                                                                                                                                (


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.
K                                                                  A                                                      K
                                      ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
                                                  SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
      Description of Augment    Clean Steam to Steam Valves 2-1/2" and Less Than 24" (Sheet 2)
                                                                  COST (1975 $1000)
                  ITEM                          LABOR          OTN!R          TNTAI              DA*f* *R  r*eT r*w*a*P
    1. OPERATING LABOR, SUPERVISION,                                             3.3      15 min/shift AND OVERHEAD
    2. MAINTENANCE MATERIAL AND                                                12.0        1% of direct cost of equipment LABOR
    3. CONSUMABLES, CHEMICALS, AND                                                -        in item 2 a    SUPPLIES
-a U'
    4. UTILITIES AND SERVICES
        Waste Disposal Water Steam                                                                  neg Electricity Building Services Other S. TOTAL 0 AND H ANNUAL COST                                                15.3


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:
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
                                                      i(1 + i) n
                                                            FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                                    (1 + i) n  1 Appendix B to RG 1.110, Page B-2
        Description of Augment        15,000-cfm HEPA Filtration System - Auxiliary Building (Sheet 1)
                                                                    DIRECT COST (1975 $1000)
                                                                                                                              BASIS FOR
                                                    I ADflD                £rI"TDUCMT MATrTAI C        TfllAI                rACT rCTTMATr I I~p~
                      ERq~
                      r.                              flTl II Anna                .r..
                                                                              X  rr...L./  - -. n nn. .- v,    .            .,  .  L
                                                                                                                                      i-* ,
    1. PROCESS EQUIPMENT                                    5                      40.0                  45.0    prefilter/HEPA @ $3/cfm, use existing fan BUILDING ASSIGNMENT                                  7                        4.5                11.5    16' x 12' x 12' @ $5/ft 3
    2.


Where:
(nonshielded area)
        i = cost of borrowed money expressed as a decimal n = plant operating lifetime (yr)
    3.  ASSOCIATED PIPING SYSTEMS                            3                        2.0                    5.0
        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.
,o L.


LIST OF APPENDIX B COST ESTIMATE SHEETS
a'
        BWR Offgas Recombiner ............................................................................................................ B-4
    4.   INSTRUMENTATION AND CONTROLS                                                                                in item 1
        3-ton Charcoal Adsorber .............................................................................................................. B-6 Desiccant Dryer ........................................................................................................................... B-8 Charcoal Vault Refrigeration ..................................................................................................... B-10
    5. ELECTRICAL SERVICE                                                                                          base
        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
    6. SPARE PARTS                                                                    0.5                    0.5 SUBTOTAL                                      15                       47.0                  62.0
        15,000-cfm HEPA Filtration System ......................................................................................... B-20
    7. CONTINGENCY                                          1                          5.0                  6.0  10%
        1000-cfm Charcoal/HEPA Filtration System ............................................................................ B-23
    8. TOTAL DIRECT COSTS                                  16                        52.0                  68.0
        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
K                                                                  T                                                                K !
                                                         LIGHT-WATER-COOLED NUCLEAR REACTORS
                                            TOTAL DIRECT COST ESTIMATE SHEET OF RADWASrE TREATMENT SYSTEM
                                  Description of Augment             BWR Offgas Recombiner (Sheet 1)
                                                         FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                                                        DIRECT COST (1975 $1,000)
        Description of Augment       15,000-cfm HEPA Filtration System - Turbine Building (Sheet 2)
                                                                                  EQUIPMENT/                          BASIS FOR COST
                                                                DIRECT COST (1975 $1000)
                                                            ITEM       LABOR      MATERIALS            TOTAL          ESTIMATE
                                                                                                                      BASIS FOR
                                    1. PROCESS EQUIPMENT               90            260              350    single unit, catalytic type w/heater and condenser, w/o instrumentation and controls, stainless steel, ASME VIII
                                                                                                                        COST ESTIMATE
                                    2. BUILDING ASSIGNMENT            100              50              150    30 x 40 x 25 @ $5/ft3 (turbine building shielded area)
                                                                          lI TDMCWNT IMATrOAIC
                                    3. ASSOCIATED PIPING SYSTEMS       18              12              30    augment piping connections Appendix B to RG 1.110, Page B-4                                                                                only
                                                    I AflI                                        TflTAL
                                    4. INSTRUMENTATION AND CONTROLS    24              96              120    allowance
                    ITEM                                                 !L___      f                      ______________
                                    5. ELECTRICAL SERVICE               -                -              neg    4kw heaters on vessels neglected
                                                      5                      40.0                45.0    skid mounted filter housing
                                    6. SPARE PARTS                       -              85              85    75K for catalyst + 2% E/M in items 1 & 4 above SUBTOTAL                232            503              735
    1. PROCESS EQUIPMENT                                                                                   w/o fans
                                    7. CONTINGENCY                     23              50              73   10%
                                                                                                                                      3
                                    8. TOTAL DIRECT COSTS             255            553              808
                                                                                2.3                  6.9  16' x 12' x 12' @ $3/ft
    2.  BUILDING ASSIGNMENT                            4.6 (nonshielded area)
    3.                                                 3                        2.0                  5.0
        ASSOCIATED PIPING SYSTEMS
-I
    4.                                                                                                       in item 1 INSTRUMENTATION AND CONTROLS
     5.                                                                                                       base ELECTRICAL SERVICE
    6.                                                 0                      0.5                  0.5 SPARE PARTS
              SUBTOTAL                                12.6                    44.8                57.4
    7. CONTINGENCY                                     2                      4.0                  6.0   10l a.   TOTAL DIRECT COSTS                           14.6                    48.8                63.4


ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
                                            TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                                  SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                  Description of Augment               BWR Offgas Recombiner (Sheet 2)
      Description of Augment     15,000-cfm HEPA Filtration System (Sheet 3)
                                                                        DIRECT COST (1975 $1,000)
                                                                COST (1975 $1000)
                                                                                                                        BASIS FOR COST
                ITEM                           LABOR          OTI4FR        TflTAI              RACTC Frn rncT FCTIMATC
                                                            ITEM       LABOR          OTHER              TOTAL          ESTIMATE
  I. OPERATING LABOR, SUPERVISION,                                           3.8        15 min/shift + 40 hr annual test AND OVERHEAD
                                    1. OPERATING LABOR, SUPERVISION,                                       3.3  15 min/shift AND OVERHEAD
  2. MAINTENANCE MATERIAL AND                                                 2.2        change every 2 yrs @ $150/filter element LABOR
                                    2. MAINTENANCE MATERIAL AND                                           20.0  routine conditioning of catalyst LABOR                                                                     and equipment upkeep; 5% of E/M including I&C
      CONSUMABLES, CHEMICALS, AND
                                    3. CONSUMABLES, CHEMICALS, AND                                         -    in item 2 SUPPLIES
I
                                    4. UTILITIES AND SERVICES
  3.                                                                                      in items 2 and 4 SUPPLIES
Appendix B to RG 1.110, Page B-5 Waste Disposal Water Steam                                                           neg    intermittent; 4kw heater load is negligible Electricity Building Services Other
  4. UTILITIES AND SERVICES
                                    5. TOTAL O AND M ANNUAL COST                                         23.3
        Waste Disposal                                                         0.8        $50/filter element Water Steam Electricity                                                            1.0        additional fan electrical load Building Services Other
  5. TOTAL 0 AND M ANNUAL COST                                               7.8 I_                                                                                                                                  (


TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-
K                                                                                                                                K
                                                        WATER-COOLED NUCLEAR REACTORS
                                          TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
                                  Description of Augment             3-ton Charcoal Adsorber (Sheet 1)
                                                      FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                                                        DIRECT COST (1975 $1,000)
      Description of Augment       1000-cfm Charcoal/HEPA Filtration System (Sheet 1)
                                                                                    EQUIPMENT/                          BASIS FOR COST
                                                              DIRECT COST (1975 $1000)
                                                            ITEM      LABOR       MATERIALS             TOTAL           ESTIMATE
                                                                                                                BASIS FOR
                                  1.   PROCESS EQUIPMENT               5                44.0             49.0   carbon steel, 360 psig, 200 ft3 volume (augment to existing train of beds)
                  I TEM                            LABOR             EOUIPMENT/MATERIALS         TOTAL         COST ESTIMATE
                                  2.  BUILDING ASSIGNMENT               8                 4.5             12.5  10 x 10 x 25 @ $5/ft3 (turbine building shielded area)
  I. PROCESS EQUIPMENT                             2.0                  22.0                   24.0 prefllter/4" charcoal/HEPA
                                  3.  ASSOCIATED PIPING SYSTEMS        -                -                -    in item 1
                                                                                                        @ $20/cfm, 5 kw htr @ $400/kw BUILDING ASSIGNMENT                           3.8                     2.0                    5.8 8' x 12' x 12' @ $5/ft 3
                                  4.  INSTRUMENTATION AND CONTROLS      -                -              neg Appendix B to RG 1.110, Page B-6
   2.
                                  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
(nonshielded area)
                                            TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
  3.  ASSOCIATED PIPING SYSTEMS                    1.3                      .7                    2.0
                                  Description of Augment              3-ton Charcoal Adsorber (Sheet 2)
0
                                                                        DIRECT COST (1975 $1,000)
  4.  INSTRUMENTATION AND CONTROLS                                                                      in item 1
                                                                                                                          BASIS FOR COST
  5.  ELECTRICAL SERVICE                            1.5                    1.0                    2.5
                                                            ITEM        LABOR          OTHER              TOTAL          ESTIMATE
   6.  SPARE PARTS                                                          0.5                    0.5 SUBTOTAL                                8.6                    26.2                    34.8
                                    1. OPERATING LABOR, SUPERVISION,                                        neg AND OVERHEAD
    7. CONTINGENCY                                  1.0                    2.0                    3.0 10%
                                    2. MAINTENANCE MATERIAL AND                                            neg   allowance of 3% of equipment LABOR                                                                      cost is negligible
    8. TOTAL DIRECT COSTS                            9.6                    28.2                    37.8
                                    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-
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
                                                        WATER-COOLED NUCLEAR REACTORS
                                                      SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                  Description of Augment                 Desiccant Dryer (Sheet 1)
        Description of Augment       1000-cfm Charcoal/HEPA Filtration System (Sheet 2)
                                                                        DIRECT COST (1975 $1,000)
                                                                        COST (1975 $1000)
                                                                                  EQUIPMENT/                      BASIS FOR COST
                        ITEM                     LABOR             OTHER          TOTAL          BASIS FOR COST £STII4ATF
                                                            ITEM       LABOR       MATERIALS          TOTAL          ESTIMATE
    1. OPERATING LABOR, SUPERVISION,                                                  1.9    20 min/day + 40 hr annual test AND OVERHEAD
                                    1. PROCESS EQUIPMENT              25                75          100    redundant dryer vessels with
    2. MAINTENANCE 14ATERIAL AND                                                      .6     2 HEPA or prefilters @ $150 each and
                                                                                                              1 regeneration skid
                                                                                              1 charcoal @ $900 each every 2 yrs'
                                    2. BUILDING ASSIGNMENT              95              50          145    40 x 36 x 20 @ $5/ft3 turbine building (shielded area)
-   3. CONSUMABLES, CHEMICALS, AND                                                            in items 2 and 4 SUPPLIES
                                    3. ASSOCIATED PIPING SYSTEMS      10                5            15    augment piping connections only
0
                                    4. INSTRUMENTATION AND CONTROLS     12              48          60    allowance Appendix B to RG 1.110, Page B-8
        UTILITIES AND SERVICES
                                    5. ELECTRICAL SERVICE              18                17            35    service for heaters, blowers, pumps, and compressors
             Waste Disposal                                                              .1   $50/HEPA or prefilter, $100/charcoal Water                                                                              filter Steam Electricity                                                                neg Building Services Other
                                    6. SPARE PARTS                      -                3             3 SUBTOTAL                160              198          358
    5. TOTAL 0 AND M ANNUAL COST                                                      2.6
                                    7. CONTINGENCY                      16              20            36   10%
        ____________________________                          ____________      I        I
                                    8. TOTAL DIRECT COSTS              176              218          394
  *                                        (                                                                                --
                                                                                                                                __  (


ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE
K                                                              K
                                            TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                        TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
                                  Description of Augment                 Desiccant Dryer (Sheet 2)
                                                    FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                                                        DIRECT COST (1975 $1,000)
    Description of Augment       15,OOO-cfm Charcoal/HEPA Filtration System - Auxiliary Building (Sheet 1)
                                                                                                                    BASIS FOR COST
                                                            DIRECT COST (1975 $1000)
                                                            ITEM        LABOR         OTHER          TOTAL          ESTIMATE
                                                                                                              BASIS FOR
                                    1. OPERATING LABOR, SUPERVISION,                                    3.3  15 min/shift AND OVERHEAD
                TTVM                            LABOR             EQUIPMENT/MATERIALS        TOTAL          COST ESTIMATE
                                    2. MAINTENANCE MATERIAL AND                                        6.1  5% of equipment including I&C
                ITE
                                        LABOR
                                                LABO.....
                                    3. CONSUMABLES, CHEMICALS, AND                                    neg SUPPLIES
                                                                                                              COST  ESTIMATE
                                    4. UTILITIES AND SERVICES
  1. PROCESS EQUIPMENT                              10                    71                    81    prefilter/4" charcoal/HEPA
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/cfm, 30kw htr @ $200/kw BUILDING ASSIGNMENT                            12                    8                    20    16' x 20' x 12' @ $5/ft 3
                                    5. TOTAL O AND M ANNUAL COST                                        9.4
  2.


TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-
(nonshielded area)
                                                          WATER-COOLED NUCLEAR REACTORS
  3. ASSOCIATED PIPING SYSTEMS                       3                    2                      5 a
                                    Description of Augment              Charcoal Vault Refrigeration (Sheet 1)
  4. INSTRUMENTATION AND CONTROLS                                                                 -     In Item 1
                                                                          DIRECT COST (1975 $1,000)
  5. ELECTRICAL SERVICE                               3                    2                      5    allowance
                                                                                        EQUIPMENT/                            BASIS FOR COST
  6. SPARE PARTS                                                           5                      5    4 elements of each type SUBTOTAL                                 28                    88                    116
                                                            ITEM      LABOR          MATERIALS                TOTAL          ESTIMATE
  7. CONTINGENCY                                       3                  9                    12      10%
                                      1. PROCESS EQUIPMENT                10                75                  85    10-ton capacity, 3 refrigerators with drives, 32°F design
  8. TOTAL DIRECT COSTS                             31                    97                    128
                                      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
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
                                            TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                                          FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                    Description of Augment               Charcoal Vault Refrigeration (Sheet 2)
        Description of Augment       15,000-cfm Charcoal/HEPA Filtration System - Turbine Building (Sheet 2)
                                                                            DIRECT COST (1975 $1,000)
                                                                      DIRECT COST (1975 $1000)
                                                                                                                                BASIS FOR COST
                    I TEM                                                    CN "I lDMrLT    ATEDIlA1 C                BASIS FOR
                                                            ITEM       LABOR              OTHER                 TOTAL          ESTIMATE
                                                    I fuND                                              T*TAi ITEM                I_____
                                      1. OPERATING LABOR, SUPERVISION,                                              3.3  15 min/shift AND OVERHEAD
                                                      ARAL?~urIIn~LJIUL      x          flMrnR                          UI
                                      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-
====t. IWUTflYAI====
                                                          WATER-COOLED NUCLEAR REACTORS
                                                                                                                        1.3
                                    Description of Augment          Charcoal/HEPA Filtration System - Condenser Vacuum Pump (Sheet 1)
    1. PROCESS EQUIPMENT                            10.0                          71.0                81.0  prefilter/4* charcoal/HEPA
                                                                                      DIRECT COST (1975 $1,000)
                                                                                                                @ $5/cfm, 30 kw htr
                                                                                                EQUIPMENT/                              BASIS FOR COST
                                                                                                                @ $200/kw BUILDING ASSIGNMENT                             7.7                           3.8                11.5 16' x 20' x 121 @ $3/ft 3
                                                            ITEM                  LABOR        MATERIALS            TOTAL                ESTIMATE
    2.
                                      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
(nonshielded area)
                                            TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
    3. ASSOCIATED PIPING SYSTEMS                        3.0                          2.0                  5.0
                                    Description of Augment          Charcoal/HEPA Filtration System - Condenser Vacuum Pump (Sheet 2)
0
                                                                                      DIRECT COST (1975 $1,000)
.rg
                                                                                                                                          BASIS FOR COST
    4. INSTRUMENTATION AND CONTROLS                                                                          in item 1
                                                            ITEM                  LABOR            OTHER            TOTAL                ESTIMATE
    5. ELECTRICAL SERVICE                              3.0                          2.0                  5.0 allowance
                                      1. OPERATING LABOR, SUPERVISION,                                                  neg        used only during startup and AND OVERHEAD                                                                              shutdown
    6.  SPARE PARTS                                                                    5.0                  5.0 4 elements each type SUBTOTAL                                23.7                          83.8                107.5
                                      2. MAINTENANCE MATERIAL AND                                                         1.2      4 HEPA filters @ $150 &
    7.  CONTINGENCY                                    2.0                            9.0               11.0  10%
                                        LABOR                                                                                      2 Charcoal filters @ $900,
    8. TOTAL DIRECT COSTS                            25.7                          92.8                118.5
                                                                                                                                    change every 2 years
(                                                                        r                                                                (
                                      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-
K                                                                                                                                K
                                                          WATER-COOLED NUCLEAR REACTORS
                                  ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREAThENT
                                    Description of Augment           Clean Steam to Turbine Glands (Sheet 1)
                                                SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                                                          DIRECT COST (1975 $1,000)
    Description of Augment     15,O00-cfm Charcoal/HEPA Filtration System (Sheet 3)
                                                                                      EQUIPMENT/                            BASIS FOR COST
                                                                COST (1975 $1000)
                                                            ITEM     LABOR          MATERIALS            TOTAL             ESTIMATE
                ITEM                         LABOR           OTHER         TOTAL               BASIS FOR COST ESTIMATE
                                      9.   PROCESS EQUIPMENT              15               150                165  25,000 lb/hr reboiler @ $4/lb/hr
  1. OPERATING LABOR. SUPERVISION,                                            3.8        15 min/shift & 40-hr annual test AND OVERHEAD
                                                                                                                      & $25K/H.P. turbine glands
  2. MAINTENANCE MATERIAL AND                                                9.0        30 HEPA or prefilters @ $150 each & 15 LABOR                                                                              charcoal filters @ $900 each every 2 yrs
                                      10. BUILDING ASSIGNMENT            19                10                  29   20 x 30 x 16 @ $3/ft3
   3. CONSUMABLES, CHEMICALS, AND                                                        in Items 2 and 4 SUPPLIES
                                      11. ASSOCIATED PIPING SYSTEMS      32                18                  50  equiv 1,000 ft @ $50/ft
0
                                      12. INSTRUMENTATION AND               8                12                  20  in addition to item 1 CONTROLS
  4. UTILITIES AND SERVICES
Appendix B to RG 1.110, Page B-14
      Waste Disposal                                                          1.5        $S50/HEPA or prefilter, $100/charcoal Water Steam Electricity                                                            1.3      8kw additional fan power for filter aP
                                      13. ELECTRICAL SERVICE                                                    neg
      Building Services                                                                    0.018.S/kw-hr Other
                                      14. SPARE PARTS                      -                 5                  5 SUBTOTAL                74                195                269
   5. TOTAL 0 AND M ANNUAL COST                                              15.6
                                      15. CONTINGENCY                      7                20                  27   10%
                                      16. TOTAL DIRECT COSTS              81                215                296


ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
                                            TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                                        FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                    Description of Augment               Clean Steam to Turbine Glands (Sheet 2)
      Description of Augment     30.00O-cfm Charcoal/HEPA Filtration System - Auxiliary Building (Sheet 1)
                                                                            DIRECT COST (1975 $1,000)
                                                                DIRECT COST (1975 $1000)
                                                                                                                                BASIS FOR COST
                                                                                                                BASIS FOR
                                                            ITEM        LABOR            OTHER              TOTAL             ESTIMATE
                  I ITU                            i ARng~
                                      1. OPERATING LABOR, SUPERVISION,                                              3.3   15 min/shift AND OVERHEAD
                                                                        FoII PI4FNTII4ATFRIALS  TOTAL           COST ESTIMATE
                                      2. MAINTENANCE MATERIAL AND                                                  4.0  40 man-days LABOR
                                                -¶  a        1n        FnrMN/AEIL
                                      3. CONSUMABLES, CHEMICALS, AND
                                                      15                      117.0            132.0  pref1lter/4" charcoal/HEPA
                                        SUPPLIES
    1. PROCESS EQUIPMENT                                                                                @ $4/cfm, 60-kw htr @ $200/kw BUILDING ASSIGIMENT                            20                        13.6            33.6   28' x 20' x 12'    $S5/ft3
                                      4. UTILITIES AND SERVICES
    2.                                                                                                   (nonshielded area)
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
    3. ASOCIATED PIPING SYSTEMS                          5                          3.0            8.0  base a
                                       5. TOTAL O AND M ANNUAL COST                                                28.3
    4. INSTRUMENTATION AND CONTROLS                                                                -      in item I
    5. ELECTRICAL SERVICE                                6                          4.0          10.0    allowance
    6. SPARE PARTS                                                                 5.0           5.0    4 elements each type SUBTOTAL                                  46                      142.6            188.6
    7. CONTINGENCY                                       5                         14.0          19.0    10%
    8. TOTAL DIRECT COSTS                            51                      156.6            207.6
  (                                                                                                                                  C


TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-
y                                                                                                                                      K
                                                          WATER-COOLED NUCLEAR REACTORS
                                          TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
                                    Description of Augment           Clean Steam to Steam Valves 24" and Larger (Sheet 1)
                                                      FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                                                                DIRECT COST (1975 $1,000)
      Description of Augment       30,000-cfm Charcoal/HEPA Filtration System    - Turbine Building (Sheet 2)
                                                                                            EQUIPMENT/                           BASIS FOR COST
                                                              DIRECT COST (1975 $1000)
                                                            ITEM           LABOR          MATERIALS            TOTAL              ESTIMATE
                                                                    !OtITPHt¶!rT/ATrR TALS                          BASIS FOR
                                      1. PROCESS EQUIPMENT                    100              120              220      22 valves @ $1,0k/valve, use existing reboiler
                                                                                                                    t*nlT F*TTMATF
                                      2. BUILDING ASSIGNMENT                                                       neg     install in existing space
                  ITEM                             LAROR                                            TflTA[
                                      3. ASSOCIATED PIPING SYSTEMS                                                   -     in item 1
    1. PROCESS EQUIPMENT                           15.0                  117.0                     132.0    prefilter/4" charcoal/HEPA
                                      4. INSTRUMENTATION AND CONTROLS                                                 -    in item 1 Appendix B to RG 1.110, Page B-16
                                                                                                              @ $4/cfm, 60kw htr
                                      5. ELECTRICAL SERVICE                                                         neg
                                                                                                              @ $200/kw
                                      6. SPARE PARTS                             -                  5                 5 SUBTOTAL                     100              125              225
    2. BUILDING ASSIGNMENT                         13.4                    6.8                      20.2  28' x 20' x 12' @ $3/ft3 (nonshielded area)
                                      7. CONTINGENCY                           10                12                22     10%
     3. ASSOCIATED PIPING SYSTEMS                     3.0                    5.0                        8.0  base me
                                      8. TOTAL DIRECT COSTS                   110              137              247
     4. INSTRUMENTATION AND CONTROLS                                                                           in item 1
    5. ELECTRICAL SERVICE                           6.0                      4.0                      10.0  allowance
    6. SPARE PARTS                                                           5.0                        5.0  4 elements each type SUBTOTAL                               37.4                  137.8                    175.2
    7. CONTINGENCY                                   4.0                    14.0                      18.0  l0
     8. TOTAL DIRECT COSTS                           41.4                  151.8                    193.2


ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
                                            TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                                          SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                    Description of Augment               Clean Steam to Steam Valves 24" and Larger (Sheet 2)
                Description of Augment     30.00O-cfm Charcoal/HEPA Filtration System - (Sheet 3)
                                                                                    DIRECT COST (1975 $1,000)
                                                                          COST (1975 $1000)
                                                                                                                                      BASIS FOR COST
                          ITEM                         LABOR         OTHER         TOTAL               BASIS FOR £OST FSTTMATF
                                                            ITEM               LABOR             OTHER             TOTAL             ESTIMATE
                OPERATING LABOR, SUPERVISION,                                           3.8        15 min/shift + 40 hr annual test AND OVERHEAD
                                      6. OPERATING LABOR, SUPERVISION,                                                   3.3  15 min/shift AND OVERHEAD
            2. MAINTENANCE MATERIAL AND                                               18.0         60 HEPA or prefilters @ $150 each & 30
                                      7. MAINTENANCE MATERIAL AND                                                         4.0   40 man-days LABOR
                LABOR                                                                               charcoal filters @ $900 each every 2 yrs
                                      8. CONSUMABLES, CHEMICALS, AND                                                   neg SUPPLIES
          " 3. CONSUMABLES, CHEMICALS, AND                                             -          in items 2 and 4 SUPPLIES
                                      9. UTILITIES AND SERVICES
            4. UTILITIES AND SERVICES
Appendix B to RG 1.110, Page B-17 Waste Disposal Water Steam                                                                       neg Electricity Building Services Other
                  Waste Disposal                                                        3.0        $50/HEPA or preftilter, $1007charcoal filter Water Steam Electricity                                                           2.6        16kw additional fan HP for filter @
                                      10 TOTAL O AND M ANNUAL COST                                                       7.3
                  Building Services                                                                 0.018 S/ku-hr Other
            5. TOTAL 0 AND M ANNUAL COST                                             27.4
- :-  t--.-J"
    ý:r                                                                                                                                __  C


TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-
K                                                                  K
                                                          WATER-COOLED NUCLEAR REACTORS
                                                                                                                                      11 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
                                    Description of Augment           Clean Steam to Steam Valves 21/2" and less than 24" (Sheet 1)
                                                        FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                                                                  DIRECT COST (1975 $1,000)
      Description of Augment       Turbine Building Chilled Water HVAC System (Sheet 1)
                                                                                              EQUIPMENT/                                BASIS FOR COST
                                                              DIRECT COST (1975 $1000)
                                                            ITEM               LABOR         MATERIALS            TOTAL                  ESTIMATE
                                                                        EOUJIPMFNTIMATFRIALS                      BASIS FOR
                                      1. PROCESS EQUIPMENT                           0              120              120        100 valves @ $1,200 each
                  ITEM                             LABOR                                         TflTAI          rnCT  CTMATC
                                      2. BUILDING ASSIGNMENT                        -                -              neg
                                                                  TnIMNIAEIL                    1  nA
                                      3. ASSOCIATED PIPING SYSTEMS                40                20                60
    1. PROCESS EQUIPMENT                             300                      500                  800    500-ton capacity, w/o air filters
                                      4. INSTRUMENTATION AND CONTROLS              10                20                30        allowance
                                                          -t                                  +       I
                                      5. ELECTRICAL SERVICE                                                              -        none Appendix B to RG 1.110, Page B-18
  2. BUILDING ASSIG* *IENT                                                                              Coolers can be Installed in existing space saved by deletion of ducting.
                                      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
0
                                            TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
  3.  ASSOCIATED PIPING SYSTEM;                                                                    -     in item 1
                                    Description of Augment          Clean Steam to Steam Valves 21/2" and less than 24" (Sheet 2)
-J
                                                                                  DIRECT COST (1975 $1,000)
  4. INSTRUMENTATION AND CONTROLS                                                                  -    in item 1
                                                                                                                                        BASIS FOR COST
  5. ELECTRICAL SERVICE                            40                      so                    90
                                                            ITEM              LABOR            OTHER              TOTAL                ESTIMATE
  6. SPARE PARTS                                    -                        8                      8  1%item 1 SUBTOTAL                                340                      558                  898
                                      1. OPERATING LABOR, SUPERVISION,                                                    3.3      15 min/shift AND OVERHEAD
  7. CONTINGENCY                                    34                      56                    90    10l
                                      2. MAINTENANCE MATERIAL AND                                                      12.0      1% of direct cost of equipment LABOR
  8. TOTAL DIRECT COSTS                            374                      614                  988
                                      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-
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
                                                          WATER-COOLED NUCLEAR REACTORS
                                                SYSTE14 FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                    Description of Augment         15,000-cfm HEPA Filtration System - Auxiliary Building (Sheet 1)
      Description of Augment     Turbine Building Chilled Water HVAC System (Sheet 2)
                                                                                    DIRECT COST (1975 $1,000)
                                                                COST (1975 $1000)
                                                                                                EQUIPMENT/                                  BASIS FOR COST
                ITEM                         LABOR           OTHER         TOTAL                 BASIS FOR COST ESTIMATE
                                                            ITEM                 LABOR          MATERIALS            TOTAL                     ESTIMATE
  I. OPERATING LABOR, SUPERVISION,                                            3.3         15 min/shift AND OVERHEAD
                                      1. PROCESS EQUIPMENT                            5                40.0              45.0         prefilter/HEPA @ $3/cfm, use existing fan
  2. MAINTENANCE MATERIAL AND                                                20.0         2-1/2% of equipment costs LABOR
                                      2. BUILDING ASSIGNMENT                          7                4.5              11.5         16 x 12 x 12 @ $5/ft3 (nonshielded area)
.0
                                      3. ASSOCIATED PIPING SYSTEMS                    3                2.0                5.0
  3. CONSUMABLES, CHEMICALS, AND                                              -              initem 2 SUPPLIES
                                      4. INSTRUMENTATION AND CONTROLS                                                                  in item 1 Appendix B to RG 1.110, Page B-20
0
                                      5. ELECTRICAL SERVICE                                                                            base
  4. UTILITIES AND SERVICES
                                      6. SPARE PARTS                                                    0.5                0.5 SUBTOTAL                            15                47.0               62.0
        Waste Disposal Water                                                                13.0         500 gpm @ 104/1000 gal & 50% load factor Steam Electricity                                                          33.0         400 kw @ 0.018 $/kw hr Building Services Other S. TOTAL 0 AND M ANNUAL COST                                              69.3 C                                                                C                                                                r
                                      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-
K
                                                          WATER-COOLED NUCLEAR REACTORS
                                                                                                                                    I
                                    Description of Augment           15,000-cfm HEPA Filtration System - Turbine Building (Sheet 2)
                                                              K                                                                  K
                                                                                    DIRECT COST (1975 $1,000)
                                        TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT. SYSTEM
                                                                                                EQUIPMENT/                                 BASIS FOR COST
                                                    FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                                            ITEM                LABOR         MATERIALS           TOTAL                    ESTIMATE
                                      3 Description of Augment       600-ft    Waste Gas Decay Tank' (Sheet 1)
                                      1. PROCESS EQUIPMENT                           5               40.0              45.0        skid mounted filter housing w/o fans
                                                          DIRECT COST (1975 $1000)
                                      2. BUILDING ASSIGNMENT                         4.6              2.3                6.9        16 x 12 x 12 @ $3/ft3 (nonshielded area)
                                                                  EOUIPMENT/MATERIALS                          BASIS FOR
                                      3. ASSOCIATED PIPING SYSTEMS                   3                2.0               5.0
            I TFM                              LABOR                                         TOTAL           COST ESTIMATE
                                      4. INSTRUMENTATION AND CONTROLS                                                                 in item 1 Appendix B to RG 1.110, Page B-21
  PROCESS EQUIPMENT                               2.5                  20                      22.5   600-ft 3 , 150 pslgo C.S.,
                                      5. ELECTRICAL SERVICE                                                                           base
                                                                                                      ASME VIII
                                      6. SPARE PARTS                                  0                0.5               0.5 SUBTOTAL                            12.6              44.8              57.4
  BUILDING ASSIGNMENT                           18.0                    9                      27.0  15' x 15' x 20' @ S6/ft 3 (shielded area)
                                      7. CONTINGENCY                                 2                 4.0               6.0       10%
  ASSOCIATED PIPING SYSTEMS                       1.0                   1                        2.0 10% of item 1 INSTRUMENTATION AND CONTROLS                                                                 neg ELECTRICAL SERVICE                                                                           neg SPARE PARTS                                                                                   neg SUBTOTAL                                 21.5                 30                      51.5 CONTINGENCY                                     2.0                   3                        5.0 10%
                                      8. TOTAL DIRECT COSTS                         14.6              48.8              63.4
  TOTAL DIRECT COSTS                             23.5                  33                      56.5


ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
                                            TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                                      SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                    Description of Augment               15,000-cfm HEPA Filtration System (Sheet 3)
                                            3 Description of Augment     600-ft  Waste Gas Decay Tank (Sheet 2)
                                                                                DIRECT COST (1975 $1,000)
                                                                    COST (1975 $1000)
                                                                                                                                  BASIS FOR COST
                    ITEM                           LABOR         OTHER         TOTAL             RA;T* FflR i*lT r*T1MATr I. OPERATING LABOR, SUPERVISION,
                                                            ITEM           LABOR           OTHER              TOTAL              ESTIMATE
        AND OVERHEAD                                                             neg
                                      1. OPERATING LABOR, SUPERVISION,                                                 3.8  15 min/shift + 40 hr annual test AND OVERHEAD
    2. MAINTENANCE MATERIAL AND
                                      2. MAINTENANCE MATERIAL AND                                                     2.2  change every 2 yrs @ $150/filter LABOR                                                                               element
        LABOR                                                                     neg
                                      3. CONSUMABLES, CHEMICALS, AND                                                   -    in items 2 and 4 SUPPLIES
    3. CONSUMABLES,   CHEMICALS, AND
                                      4. UTILITIES AND SERVICES
0
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
        SUPPLIES                                                                 neg U'
                                      5. TOTAL O AND M ANNUAL COST                                                     7.8
0~e
    4. UTILITIES AND SERVICES
          Waste Disposal Water Steam                                                                   neg Electricity Building Services Other
    5. TOTAL 0 AND N  ANNUAL COST                                               neg
                                                                                                                              (


TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-
K                                                                K
                                                          WATER-COOLED NUCLEAR REACTORS
                                          TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
                                    Description of Augment           1000-cfm Charcoal/HEPA Filtration System (Sheet 1)
                                                      FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                                                              DIRECT COST (1975 $1,000)
      Description of Augment       PWR Hydrogen Recombiner (Sheet 1)
                                                                                          EQUIPMENT/                          BASIS FOR COST
                                                              DIRECT COST (1975 $1000)
                                                            ITEM          LABOR          MATERIALS            TOTAL            ESTIMATE
                                                                    rflIITPMPINIMAT*RTAI
                                      1. PROCESS EQUIPMENT                     2.0             22.0             24.0  prefilter/4" charcoal/HEPA @
                                                                                                                BASIS FOR
                                                                                                                          $20/cfm, 5 kw htr @ $400/kw
                IT"M                              IARno                                        TflTAI        rnqT vtTTMATF
                                      2. BUILDING ASSIGNMENT                    3.8               2.0              5.8  8 x 12 x 12 @ $5/ft3 (nonshielded area)
                                                            I  l        VT  :fTI    b    V      nA. I
                                      3. ASSOCIATED PIPING SYSTEMS              1.3              0.7              2.0
  1. PROCESS EQUIPMENT                             50.0                   300.0               350.0  skid mounted, catalytic type w/condenser, partial I&C
                                      4. INSTRUMENTATION AND CONTROLS                                              -    in item 1 Appendix B to RG 1.110, Page B-23
                                                                                                        single unit, ASME VIII
                                      5. ELECTRICAL SERVICE                    1.5              1.0              2.5
      BUILDING ASSIGNM4ENT                          28.8                   14.4                  43.2  15' x 30' x 16' 0 $6/ft3
                                      6. SPARE PARTS                                              0.5              0.5 SUBTOTAL                      8.6              26.2              34.8
  2.
                                      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
(shielded area)
                                              TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
  3. ASSOCIATED PIPING SYSTEMS                      32.0                    13.0                  45.0  allowance a
                                    Description of Augment                1000-cfm Charcoal/HEPA Filtration System (Sheet 2)
Ue
                                                                                    DIRECT COST (1975 $1,000)
  4. INSTRUMENTATION AND CONTROLS                  10.0                    40.0                  50.0  allowance
                                                                                                                                      BASIS FOR COST
  5. ELECTRICAL SERVICE                            13.0                    12.0                 25.0  allowance
                                                            ITEM                LABOR            OTHER            TOTAL            ESTIMATE
  6. SPARE PARTS                                    -                        2.0                  2.0
                                      1.   OPERATING LABOR, SUPERVISION,                                                  1.9  20 min/day + 40 hr annual test AND OVERHEAD
            SUBTOTAL                                133.8                  381.4                515.2
                                      11. MAINTENANCE MATERIAL AND                                                        0.6   2 HEPA or prefilters @ $150
  7. CONTINGENCY                                    13.0                    38.0                 51.0  101
                                          LABOR                                                                                each and 1 charcoal @ $900
  8. TOTAL DIRECT COSTS                            146.8                  419.4                566.2
                                                                                                                                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-
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADtWASTE TREAThENT
                                                          WATER-COOLED NUCLEAR REACTORS
                                                SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                    Description of Augment         15,000-cfm HEPA Filtration System - Auxiliary Building (Sheet 1)
      Description of Augment     PUR Hydrogen Recombiner (Sheet 2)
                                                                                    DIRECT COST (1975 $1,000)
                                                                COST (1975 $1000)
                                                                                                EQUIPMENT/                                  BASIS FOR COST
                ITEM                           LABOR          OTHER          TOTAL               BASIS FOR COST ESTIMATE
                                                            ITEM                 LABOR          MATERIALS            TOTAL                   ESTIMATE
  1. OPERATING LABOR, SUPERVISION,                                           3.3        15 min/shift AND OVERHEAD
                                      1. PROCESS EQUIPMENT                          10                71                81          prefilter/4" charcoal/HEPA @
  2. MAINTENANCEMATERIAL AND.                                                10.0        3% of equipment cost LABOR
                                                                                                                                      $5/cfm, 30kw htr @ $200/kw
  3. CONSUMABLES, CHEMICALS, AND                                             1.0        oxygen @.S2.5/103 cf & .25 cfm 0
                                      2. BUILDING ASSIGNMENT                        12                  8                20          16 x 20 x 12 @ $5/ft3 (nonshielded area)
      SUPPLIES                                                                            7000 hrs Ca I
                                      3. ASSOCIATED PIPING SYSTEMS                    3                 2                5
U'
                                      4. INSTRUMENTATION AND CONTROLS                                                      -          in item 1 Appendix B to RG 1.110, Page B-25
  4. UTILITIES AND SERVICES
                                      5. ELECTRICAL SERVICE                          3                  2                5          allowance
        Waste Disposal Water Steam                                                                  neg Electricity Building Services Other S. TOTAL 0 AND M ANNUAL COST                                              14.3 K                                                                                                                          C
                                      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-
K*
                                                          WATER-COOLED NUCLEAR REACTORS
                                          TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
                                    Description of Augment           15,000-cfm HEPA Filtration System - Turbine Building (Sheet 2)
                                                      FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                                                                    DIRECT COST (1975 $1,000)
      Description of Augment       PWR Air EJector      Charcoal/HEPA Filtration Unit (Sheet 1)
                                                                                                EQUIPMENT/                                BASIS FOR COST
                                                              DIRECT COST (1975 $1000)
                                                            ITEM                 LABOR         MATERIALS           TOTAL                   ESTIMATE
                                                                                                                  BASIS FOR
                                      1. PROCESS EQUIPMENT                           10.0             71.0              81.0        prefilter/4" charcoal/HEPA @
                ITEM                               LABOR             EOUIPMENT/MATERIALS       TOTAL             COST ESTIMATE
                                                                                                                                      $5/cfm, 30 kw htr @ $200/kw
                                                                                                        1*
                                      2. BUILDING ASSIGNMENT                         7.7              3.8              11.5         16 x 20 x 12 @ $3/ft3 (nonshielded area)
    1. PROCESS EQUIPMENT                             3.0                   7.5                  10.5    chiller, heater, charcoal HEPA
                                      3. ASSOCIATED PIPING SYSTEMS                   3.0               2.0               5.0
                                                                                                                                  3
                                      4. INSTRUMENTATION AND CONTROLS                                                                 in item 1 Appendix B to RG 1.110, Page B-26
    2. BUILDING ASSIGNMENT                           3.0                    1.5                    4.5     10' x 10' x 15' @ $3/ft (unshielded turbine bldg)
                                      5. ELECTRICAL SERVICE                           3.0               2.0                5.0       allowance
    3. ASSOCIATED PIPING SYSTEMS                     2.0                   1.0                   3.0     allowance L*a
                                      6. SPARE PARTS                                 -                5.0               5.0       4 elements each type SUBTOTAL                           23.7              83.8            107.5
    4. INSTRUMENTATION AND CONTROLS                 0.5                    1.5                    2.0    allowance
                                      7. CONTINGENCY                                 2.0               9.0               11.0       10%
    5. ELECTRICAL SERVICE                           0.5                  0.5                     1.0     allowance
                                      8. TOTAL DIRECT COSTS                         25.7              92.8            118.5
    6. SPARE PARTS                                                         1.0                   1.0
            SUBTOTAL                                 9.0                  13.0                    22.0
    7. CONTINGENCY                                   1.0                   1.0                   2.0     1O0
    8. TOTAL DIRECT COSTS                           10.0                  14.0                    24.0


ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
                                            TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                                          SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                    Description of Augment              15,000-cfm HEPA Filtration System (Sheet 3)
          Description of Augnent          PWR Air EJector    Charcoal/HEPA Filtration Unit (Sheet 2)
                                                                                DIRECT COST (1975 $1,000)
                                                                            COST (1975 $1000)
                                                                                                                                    BASIS FOR COST
                    ITEM                               LARAR           flTIFD          TnTAI            DAete  *  *    rP*eUA*
                                                            ITEM            LABOR            OTHER              TOTAL                ESTIMATE
                    .....________________
                                      1. OPERATING LABOR, SUPERVISION,                                                 3.8   15 min/shift & 40-hr annual test AND OVERHEAD
                    ___                                                      I*          ,    L          ueA5  rwK Guil r.4IrMIE
                                      2. MAINTENANCE MATERIAL AND                                                       9.0   30 HEPA or prefilters @ $150
      l. OPERATING LABOR, SUPERVISION,                                                     3.8     15 min/shift + 40 hr annual test AND OVERHEAD
                                        LABOR                                                                               each & 15 charcoal filters @
      2. MAINTENANCE MATERIAL AND                                                         2.0     includes replacement filter LABOR
                                                                                                                              $900 each every 2 years
    3. CONSUMABLES,       CHEMICALS, AND                                                   -       in item 2 EP
                                      3. CONSUMABLES, CHEMICALS, AND                                                   -     in items 2 and 4 SUPPLIES
        SUPPLIES
                                      4. UTILITIES AND SERVICES
U'
Appendix B to RG 1.110, Page B-27 Waste Disposal                                                             1.5  $50/HEPA or prefilter,
    4. UTILITIES AND SERViCES
                                                                                                                              $100/charcoal Water Steam Electricity                                                                 1.3  8kw additional fan power for filter P @ 0.018 $/kw-hr Building Services Other
            Waste Disposal                                                                 neg Water Steam Electricity Building Services Other
                                      5. TOTAL O AND M ANNUAL COST                                                     15.6
    5. TOTAL 0 AND M ANNUAL COST                                                         5.8 K


TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-
K                                                                                                                              K
                                                          WATER-COOLED NUCLEAR REACTORS
                                            TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
                                    Description of Augment         30,000-cfm Charcoal/HEPA Filtration System - Auxiliary Building (Sheet 1)
                                                      FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                                                                        DIRECT COST (1975 $1,000)
        Description of Augment       Steam Generator Flash Tank Vent to Main Condenser (Sheet 1)
                                                                                                    EQUIPMENT/                                BASIS FOR COST
                                                              DIRECT COST (1975 $1000)
                                                            ITEM                     LABOR          MATERIALS            TOTAL                 ESTIMATE
                                                                                                                  BASIS FOR
                                      1. PROCESS EQUIPMENT                               15              117.0            132.0      prefilter/4" charcoal/HEPA @
                  ITEM                             LABOR           EQUIPMENT/MATERIALS         TOTAL         COST ESTIMATE
                                                                                                                                        $4/cfm, 60-kw htr @ $200/kw
    I. PROCESS EQUIPMENT                                                                           -     no equipment required
                                      2. BUILDING ASSIGNMENT                             20                13.6              33.6      28 x 20 x 12 @ $5/ft3 (nonshielded area)
    2. BUILDING ASSIGNMENT                                                                       neg    install In existing space
                                      3. ASSOCIATED PIPING SYSTEMS                         5                3.0              8.0      base
    3. ASSOCIATED PIPING SYSTEMS                     13                      7                    20    200 ft of 10-in pipe with
                                      4. INSTRUMENTATION AND CONTROLS                                                         -        in item 1 Appendix B to RG 1.110, Page B-28
                                                                                                          2 valves U't ull
                                      5. ELECTRICAL SERVICE                               6                4.0              10.0      allowance
    4. INSTRUMENTATION AND CONTROLS                   4                      6                      10  allowance
                                      6. SPARE PARTS                                       -                5.0              5.0      4 elements each type SUBTOTAL                                 46              142.6            188.6
    5. ELECTRICAL SERVICE                                                                         neg
                                      7. CONTINGENCY                                       5                14.0              19.0      10%
    6. SPARE PARTS                                                                               neg SUBTOTAL                               17,,                  13                      30
                                      8. TOTAL DIRECT COSTS                               51              156.6            207.6
    7. CONTINGENCY                                   2                      1                      3  10%
    8. TOTAL DIRECT COSTS                           19                    14                      33


TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREAThENT
                                                          WATER-COOLED NUCLEAR REACTORS
                                                  SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                    Description of Augment         30,000-cfm Charcoal/HEPA Filtration System - Turbine Building (Sheet 2)
      Description of Augment   Steam.Generator Flash Tank Vent to Main Condenser (Sheet 2)
                                                                                        DIRECT COST (1975 $1,000)
                                                                  COST (1975 $1000)
                                                                                                    EQUIPMENT/                                BASIS FOR COST
                  ITEM                         LABOR           OTHER         TOTAL               BASIS FOR COST ESTIMATE
                                                            ITEM                   LABOR          MATERIALS            TOTAL                 ESTIMATE
    1. OPERATING LABOR, SUPERVISION,                                             1          allowance AND OVERHEAD
                                      1. PROCESS EQUIPMENT                              15.0            117.0            132.0      prefilter/4" charcoal/HEPA @
    2. MAINTENANCE MATERIAL AND                                                  1        2% Total Direct Cost LABOR
                                                                                                                                        $4/cfm, 60-kw htr @ $200/kw
    3. CONSUHABLES, CHEMICALS, AND                                              neg
                                      2. BUILDING ASSIGNMENT                            13.4              6.8              20.2       28 x 20 x 12 @ $3/ft3 (nonshielded area)
.a    SUPPLIES
                                      3. ASSOCIATED PIPING SYSTEMS                        3.0              5.0              8.0      base
U'
                                      4. INSTRUMENTATION AND CONTROLS                                                                  in item 1 Appendix B to RG 1.110, Page B-29
    4. UTILITIES AND SERVICES
                                      5. ELECTRICAL SERVICE                              6.0              4.0              10.0      allowance
        Waste Disposal Water                                                                  neg Steam Electricity Building Services Other
                                      6. SPARE PARTS                                      -                5.0               5.0      4 elements each type SUBTOTAL                                37.4            137.8            175.2
    5. TOTAL 0 AND H ANNUAL COST                                                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
K
                                            TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                        TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
                                    Description of Augment         30,000-cfm Charcoal/HEPA Filtration System - Auxiliary Building (Sheet 3)
                                                      FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                                                                        DIRECT COST (1975 $1,000)
      Description of Augment       lSqpm Evaporator (Sheet 1)
                                                                                                                                                BASIS FOR COST
                                                            DIRECT COST (1975 $1000)
                                                            ITEM                    LABOR            OTHER              TOTAL                 ESTIMATE
                                                                                                              BASIS FOR
                                      1. OPERATING LABOR, SUPERVISION,                                                         3.8       15 min/shift + 40 hr annual test AND OVERHEAD
                 ITI'N                          I AnRO                                        T*TA!
                                      2. MAINTENANCE MATERIAL AND                                                            18.0      60 HEPA or prefilters @ $150
  1. PROCESS EQUIPMENT                            30                  225                    255    skid mounted, bundle,        submerged ASME VIII,      tubein Incoloy contact with process fluid
                                        LABOR                                                                                          each & 30 charcoal filters @
  2. BUILDING ASSIGNMENT                          68                    34                  102    evap & services 25' x 301 x 20'
                                                                                                                                        $900 each every 2 years
                                                                                                      @ $6/ft3 plus 2,000 ft3 increase in solid waste storage area a. 3. ASSOCIATED PIPING SYSTEMS                    35                    30                    65  inludes service piping
                                      3. CONSUMABLES, CHEMICALS, AND                                                          -        in items 2 and 4 SUPPLIES
  4. INSTRUMENTATION AND CONTROLS                  10                    10                    20  allowance
                                      4. UTILITIES AND SERVICES
  5. ELECTRICAL SERVICE                            40                    25                    65  allowance
Appendix B to RG 1.110, Page B-30
  6. SPARE PARTS                                  -                      27                    27  2% of item 1 plus tube bundle SUBTOTAL                              183                  351                    534
                                            Waste Disposal                                                                    3.0      $50/HEPA or prefilter,
  7. CONTINGENCY                                  18                    35                    53  10%
                                                                                                                                        $100/charcoal filter Water Steam Electricity                                                                        2.6      16 kw additional fan HP for filter @ 0.018 $/kw-hr Building Services Other
  8. TOTAL DIRECT COSTS                          201                    386                    587
                                      5. TOTAL O AND M ANNUAL COST                                                            27.4


TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREAThENT'SYSTEM
                                                          WATER-COOLED NUCLEAR REACTORS
                                                        FOR LIGHT-WdATER-COOLED NUCLEAR REACTORS
                                    Description of Augment           Turbine Building Chilled Water HVAC System (Sheet 1)
      Description of Augment       30-gpm Evaporator (Sheet 2)     ,
                                                                                DIRECT COST (1975 $1,000)
                                                                DIRECT COST (1975 $1000)
                                                                                            EQUIPMENT/                            BASIS FOR COST
                  tTrW                                                                                              BASIS   FOR
                                                            ITEM           LABOR         MATERIALS            TOTAL              ESTIMATE
                                                                                                                      rncT rCY?UAYT
                                      1. PROCESS EQUIPMENT                     300              500              800      500-ton capacity, w/o air filters
                                                  I AfPtflD           rfIITDfMlrTIMATrDTAI        TnTA,
                                      2. BUILDING ASSIGNMENT                                                        -     Coolers can be installed in existing space saved by deletion of ducting
                  *.-                            -..rw-f              .dV..r  b.r I  ... u snlrl.# ,nI    .         bl    r~l) I lruI
                                      3. ASSOCIATED PIPING SYSTEMS                                                   -      in item 1
    1. PROCESS EQUIPMENT                               30                      350                  380    ASME VIII
                                      4. INSTRUMENTATION AND CONTROLS                                               -      in item 1 Appendix B to RG 1.110, Page B-31
                                                                                                              skid mounted, submerged,
                                      5. ELECTRICAL SERVICE                     40               50                90
                                                                                                            'tube bundle, Incoloy in contact with process fluid t
                                      6. SPARE PARTS                             -                8                8      1% item 1 SUBTOTAL                      340              558              898
  2. BUILDING ASSIGNMgNT                            88                        44                  132    evap + services - 25' x 40' x 20'
                                      7. CONTINGENCY                             34              56                90      10%
                                                                                                              @ $6/ft3 plus 2,000 ft 3 Increase In solid waste storage area
                                      8. TOTAL DIRECT COSTS                   374              614              988
  3. ASSOCIATED PIPING SYSTEMS                       35                        35                    70    includes service piping CO
  4. INSTRUMENTATION AND CONTROLS                   10                        10                    20    allowance
  5. ELECTRICAL SERVICE                             40                       25                    65    allowance
  6. SPARE PARTS                                                               27                    27    2% of Item 1 plus tube bundle SUBTOTAL                                 203                     491                  694
  7. CONTINGENCY                                     20                        49                    69    1O0
  8. TOTAL DIRECT COSTS                           223                      540                  763 C                                                                  C


ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE
K
                                            TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                                                                                                                      'III
                                    Description of Augment             Turbine Building Chilled Water HVAC System (Sheet 2)
                                                                    T
                                                                                  DIRECT COST (1975 $1,000)
                                                              3)
                                                                                                                                    BASIS FOR COST
                                          TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMErNT SYSTEM
                                                            ITEM             LABOR            OTHER            TOTAL             ESTIMATE
                                                        (Sheet
                                      1. OPERATING LABOR, SUPERVISION,                                                 3.3   15 min/shift AND OVERHEAD
                                                50-gpmFOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                      2. MAINTENANCE MATERIAL AND                                                    20.0   21/2% of equipment costs LABOR
                                            Augment of Evaporator Description Description of Augment       50-qpm Evaporator (Sheet 3)
                                      3. CONSUMABLES, CHEMICALS, AND                                                  -      in item 2 SUPPLIES
                                                              DIRECT COST (1975 $1000)
                                      4. UTILITIES AND SERVICES
                                                                                                                BASIS FOR
Appendix B to RG 1.110, Page B-32 Waste Disposal Water                                                                    13.0   500 gpm @ 10¢/1,000 gal &
                ITEM                               LABOR            EOUIPMENT/MATERIALS        TOTAL         COST ESTIMATE
                                                                                                                              50% load factor Steam Electricity                                                              33.0   400 kw @ 0.018 $/kw-hr Building Services Other
  1. PROCESS EQUIPMENT                                30                  450                    480    ASME VIII
                                      5. TOTAL O AND M ANNUAL COST                                                    69.3
                                                                                                        skid mounted, submerged, tube bundle, Incoloy In contact with process fluid
   2. BUILDING ASSIGNMENT                              97                  48                    145   10% more than 30 gpm
  3. ASSOCIATED PIPING SYSTEMS                        35                  35                    70    allowance a
*0 4. INSTRUMENTATION AND CONTROLS                    10                  10                    20    allowance S. ELECTRICAL SERVICE                              40                  25                    65    allowance
  6. SPARE PARTS.                                                         27                    27   2% of Item 1 plus tube bundle SUBTOTAL                                  212                  595                    807
  7. CONTINGENCY                                      21                  60                    81   10%
  8. TOTAL- DIRECT COSTS                            233                  655                    888


TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
                                                          WATER-COOLED NUCLEAR REACTORS
                                              SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                    Description of Augment             600-ft3 Waste Gas Decay Tank (Sheet 1)
  Description of Augment   FuannAtnY  - RUR Dirty Ua~tm - Finn, fl,.n1,, (k..t £1 COST (1975 $1000)
                                                                            DIRECT COST (1975 $1,000)
              ITEM                         LABOR          OT14ER          TOTAL             BASIS FOR LOST FSTIMATF
                                                                                        EQUIPMENT/                            BASIS FOR COST
1. OPERATING LABOR, SUPERVISION,                                             12      2.6 x 106 gpy; 1000 hrs/yr labor AND OVERHEAD
                                                            ITEM       LABOR          MATERIALS            TOTAL             ESTIMATE
2. MAINTENANCE MATERIAL AND                                                  30      7-1/2% of equipment cost LABOR
                                      1. PROCESS EQUIPMENT                  2.5              20                22.5  600-ft3, 150 psig, C.S., ASME
3. CONSUMABLES, CHEMICALS, AND                                              neg      concentrate solidification chemicats SUPPLIES                                                                            in item 4
                                                                                                                        VIII
4. UTILITIES AND SERVICES                                                                                                      3 Waste Disposal                                                          70      100:1 feed to concentrate ratio @ 20/ft disposal cost Water                                                                    27      1000 gpm @ 1500 hrs @ 30t/1000 gal Steam                                                                    60      1500 hrs steaw @ 20,000 lb/hr @ $2/1000 lbs Electricity Building Services Other
                                      2. BUILDING ASSIGNMENT                18.0              9                27.0  15 x 15 x 20 @ $6/ft3 (shielded area)
5. TOTAL 0 AND M ANNUAL COST                                                199 C                                                                C
                                      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
K*                                                                                                                                  K
                                            TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                    ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
                                    Description of Augment               600-ft3 Waste Gas Decay Tank (Sheet 2)
                                                SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                                                            DIRECT COST (1975 $1,000)
      Description of Augment     Evaporator PWR Dirty Waste (Sheet 5)
                                                                                                                        BASIS FOR COST
                                                                COST (1975 $1000)
                                                            ITEM        LABOR            OTHER            TOTAL      ESTIMATE
                lTYM                          [AROR          OTHER          TOTAL              BASIS FOR COST ESTTMATE
                                      1. OPERATING LABOR, SUPERVISION,       -                -                neg AND OVERHEAD
  I. OPERATING LABOR, SUPERVISION,
                                      2. MAINTENANCE MATERIAL AND             -                 -                neg LABOR
      AND OVERHEAD                                                             6.0        500,000 gpy; 500 hrs/yr labor
                                      3. CONSUMABLES, CHEMICALS, AND          -                -                neg SUPPLIES
  2. MAINTENANCE MATERIAL AND
                                      4. UTILITIES AND SERVICES
      LABOR                                                                  30.0        7-1/2% of equipment cost
Appendix B to RG 1.110, Page B-34 Waste Disposal Water Steam                                                                neg Electricity Building Services Other
  3. CONSUMABLES, CHEMICALS, AND                                             -         concentrate solidification chemicals
                                      5. TOTAL O AND M ANNUAL COST                                                neg
0'
      SUPPLIES                                                                           in item 4
  4. UTILITIES AND SERVICES                                                                                                       3
                                                                                          50:1  feed to concentrate ratio @ $20/ft Waste Disposal                                                       27.0        disposal cost Water                                                                 5.0        1000 gpm @.277 hrs @ 30t/1000 gal Steam                                                                12.0        277 hrs steam @S20,000 4bs/hr @$2/1000 lbs Electricity Building Services Other
  5. TOTAL 0 AND MANNUAL COST                                                80.0


TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
                                                          WATER-COOLED NUCLEAR REACTORS
                                                    SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                    Description of Augment             PWR Hydrogen Recombiner (Sheet 1)
        Description of Augment v
                                                                          DIRECT COST (1975 $1,000)
                                  EvaDorator
                                                                                    EQUIPMENT/                            BASIS FOR COST
                                              - Condenser Polisher Chemical IaCto Ih    +0A
                                                            ITEM       LABOR        MATERIALS              TOTAL            ESTIMATE
                                                                  COST (1975 $1000)
                                      1. PROCESS EQUIPMENT                50.0           300.0              350.0  skid mounted, catalytic type w/condenser, partial I&C single unit, ASME VIII
                    ITEM                        LAI*R          NTH*D          T*TAI
                                      2. BUILDING ASSIGNMENT              28.8            14.4              43.2   15 x 30 x 16 @ $6/ft3 (shielded area)
                                                LABOR      0ATD    AU       .,* TC4TAI                  FRUK CS
                                      3. ASSOCIATED PIPING SYSTEMS        32.0           13.0              45.0  allowance
                                                                                                              LU  ETIMATE
                                      4. INSTRUMENTATION AND CONTROLS      10.0           40.0              50.0  allowance Appendix B to RG 1.110, Page B-35
    1. OPERATING LABOR, SUPERVISION,
                                      5. ELECTRICAL SERVICE                13.0           12.0              25.0  allowance
        AND OVERHEAD                                                                6.0     650.000 gpy; 500 hr/yr labor
                                      6. SPARE PARTS                        -                2.0               2.0
  2.  MAINTENANCE MATERIAL AND
                                                SUBTOTAL                133.8          381.4             515.2
        LABOR                                                                    30.0      7-1/2% of equipment cost
                                      7. CONTINGENCY                      13.0           38.0              51.0  10%
  3.   CONSUMABLES, CHEMICALS. AND                                                        concentrate solidification chemicals
                                      8. TOTAL DIRECT COSTS              146.8          419.4              566.2
0       SUPPLIES                                                                            In item 4
  4. UTILITIES  AND SERVICES
          Waste Disposal
                                                                                  87.0     20:1 feed to concentrate ratio @ $20/ft 3 Wl7.0     disposal cost Water                                                                    6.5      1000 gpm 0 360 hrs @ 30/10OO gal Steam                                                                  14.4     360 hrs steam @ 20,000 lb/hr @ $2/1000 lbs Electricity Building Services Other
  5.   TOTAL 0 AND M ANNUAL COST                                                143.9
(                                                                                                                                    C


ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE
K                                                                                                                                      K
                                            TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                    ANNUAL OPERATING AND MAI[NTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
                                    Description of Augment               PWR Hydrogen Recombiner (Sheet 2)
                                                  SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                                                            DIRECT COST (1975 $1,000)
      Description of Augment       .an    - hla~aum*., Um.4.a Iqkaa÷ 7*
                                                                                                                          BASIS FOR COST
                                                                  COST (1975. $1000)
                                                            ITEM        LABOR          OTHER              TOTAL          ESTIMATE
                  TT!M                          LABOR            OTHER          TOTAL              BASIS FOR COST ESTIMATE
                                      1. OPERATING LABOR, SUPERVISION,                                         3.3  15 min/shift AND OVERHEAD
    I. OPERATING LABOR, SUPERVISION,
                                      2. MAINTENANCE MATERIAL AND                                             10.0   3% of equipment cost LABOR
      AND OVERHEAD                                                                6.0    160,000 gpy; 500 hrs/yr
                                      3. CONSUMABLES, CHEMICALS, AND                                           1.0  oxygen @ $2.5/103 cf & .25 cfm SUPPLIES                                                                   @ 7,000 hrs
    2. MAINTENANCE MATERIAL AND
                                      4. UTILITIES AND SERVICES
      LABOR                                                                      30.0       7-1/25 of equipment cost
Appendix B to RG 1.110, Page B-36 Waste Disposal Water Steam                                                            neg Electricity Building Services Other
    3. CONSUMABLES, CHEMICALS, AND                                                 -        concentrate solidification chemicals In ad    SUPPLIES                                                                             item 4 a,     UTILITIES AND SERVICES
                                      5. TOTAL O AND M ANNUAL COST                                           14.3
LeD
    4.  WasteITsposal                                                              8.6      50:1 feed to concentrate ratio 0 $20/ft 3 disposal cost Water                                                                      1.6      1000 gpm 0 90 hrs 0 30t/1000 gal Steam                                                                      3.6      90 hrs steam 0 20,000 lb/hr 1 $2/1000 lbs Electricity Building Services Other
    5. TOTAL 0 AND MANNUAL COST                                                   49.8


TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
                                                          WATER-COOLED NUCLEAR REACTORS
                                                        FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                    Description of Augment           PWR Air Ejector Charcoal/HEPA Filtration Unit (Sheet 1)
        Description of Augment       Evaporator Distillate Demineralizer (Sheet 1)
                                                                                DIRECT COST (1975 $1,000)
                                                                DIRECT COST (1975 $1000)
                                                                                            EQUIPMENT/                              BASIS FOR COST
                  TTIrM                            I anAD            EniI nlrT IUA?~nAi    e    qrft*IrA I
                                                            ITEM            LABOR          MATERIALS            TOTAL              ESTIMATE
                                                                                                                      BASIS FOR
                                      1. PROCESS EQUIPMENT                         3.0              7.5              10.5    chiller, heater, charcoal HEPA
                    *,-.                          I.rluvn            Iuu~rnllu~r'¶l  KhMiLR      IJI/L              W,5MIIEIHMAIT
                                      2. BUILDING ASSIGNMENT                       3.0              1.5              4.5    10 x 10 x 15 @ $3/ft3 (unshielded turbine building)
    1. PROCESS EQUIPMENT                             4.0                      20.0              24.0    30 ft 3 , SS. ASME VIII, 150 psi nonregenerative, w/resin
                                      3. ASSOCIATED PIPING SYSTEMS                 2.0               1.0               3.0    allowance
    2. BUILDING ASSIGNMENT                           6.4                        3.2                9.6  10' x 10' x 16' @ $6/ft3 (shielded area)
                                      4. INSTRUMENTATION AND CONTROLS             0.5               1.5              2.0     allowance Appendix B to RG 1.110, Page B-37
    3. ASSOCIATED PIPING SYSTEMS                       9.0                         6.0             15.0    2" piping i
                                      5. ELECTRICAL SERVICE                       0.5              0.5              1.0    allowance
Ot
                                      6. SPARE PARTS                               -                1.0               1.0
  4.   INSTRUMENTATION AND CONTROLS                   2.0                         3.0                5.0   remote conductivity readout
                                                SUBTOTAL                         9.0              13.0              22.0
  5. ELECTRICAL SERVICE                                                                           neg
                                      7. CONTINGENCY                               1.0               1.0               2.0     10%
  6. SPARE PARTS                                                                 1.0                 1.0
                                      8. TOTAL DIRECT COSTS                       10.0              14.0              24.0
            SUBTOTAL                               21.4                        33.2              54.6
  7. CONTINGENCY                                     2.0                         3.0               5.0   10%
  8. TOTAL DIRECT COSTS                           23.4                        36.2              59.6
(                                                                  C                                                                  (


ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE
)
                                            TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
K
                                    Description of Augment           PWR Air Ejector Charcoal/HEPA Filtration Unit (Sheet 2)
                                    ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
                                                                                DIRECT COST (1975 $1,000)
                                                      SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                                                                                                                    BASIS FOR COST
      Description of Augment     Evaporator Distillate Demineralizer (Sheet 2)
                                                            ITEM            LABOR            OTHER              TOTAL              ESTIMATE
                                                                    COST (1975 $1000)
                                      1. OPERATING LABOR, SUPERVISION,                                                3.8     15 min/shift + 40 hr annual test AND OVERHEAD
                  YtM                              I ARnlQ        OTHER          TOTAL                BASIS FOR COST ESTIMATE
                                      2. MAINTENANCE MATERIAL AND                                                     2.0    includes replacement filter LABOR
                  aI1II                    ____________
                                      3. CONSUMABLES, CHEMICALS, AND                                                   -      in item 2 SUPPLIES
    I. OPERATING LABOR, SUPERVISION.                                              1.8         1500 hrs operation @ 10% attendance AND OVERHEAD
                                      4. UTILITIES AND SERVICES
    2. MAINTENANCE MATERIAL AND
Appendix B to RG 1.110, Page B-38 Waste Disposal                                                           neg Water Steam Electricity Building Services Other
      LABOR                                                                      2.0         allowance
                                      5. TOTAL O AND M ANNUAL COST                                                     5.8
     3. CONSUMABLES, CHEMICALS, AND
,ap    SUPPLIES                                                                    2.3        1 change per yr @ $75/ft 3
    4. UTILITIES AND SERVICES
        Waste Disposal                                                           0.6          30 ft 3
                                                                                                        @ $20/ft 3 disposal cost Water Steam Electricity Building Services Other
    5. TOTAL 0 AND M ANNUAL COST                                                   6.7


TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
                                                          WATER-COOLED NUCLEAR REACTORS
                                                      FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                    Description of Augment           Steam Generator Flash Tank Vent to Main Condenser (Sheet 1)
      Description of Augment     50-opDemintralzer Sh t 1)
                                                                                    DIRECT COST (1975 $1,000)
                                                          {Sheet 1)
                                                                                              EQUIPMENT/                                BASIS FOR COST
                                  SO-gin  .D*l.n.fraltzer DIRECT COST (1975 $1000)
                                                            ITEM               LABOR        MATERIALS            TOTAL                ESTIMATE
                                                                                                                BASIS FOR
                                      1. PROCESS EQUIPMENT                                                              -        no equipment required
                ITEM                             LAROR              1ITOM    AUIFRAI It    TIhTAI              CflCY
                                      2. BUILDING ASSIGNMENT                                                           neg        install in existing space
                                                                                                                      1T
                                      3. ASSOCIATED PIPING SYSTEMS                  13                7                20        200 ft of 10-in pipe with 2 valves
                                                                                                                        tMAr"
                                      4. INSTRUMENTATION AND CONTROLS               4                 6               10         allowance Appendix B to RG 1.110, Page B-39
  1. PROCESS EQUIP4ENT                              5                  20.0                  25.0  30 ft 3. SS, A*NE VIII. 150 psi, nonreganerative, with resin
                                      5. ELECTRICAL SERVICE                                                           neg
  2. BUILDING ASSIGNMENT                             9                    4.8                  13.8  12' x 12' x 16' 0 $6/ft3 (shielded ar*)
                                      6. SPARE PARTS                                                                   neg SUBTOTAL                           17                13                30
  3. ASSOCIATED PIPING SYSTEMS                       9                    6.0                 15.0  2" piping
                                      7. CONTINGENCY                                 2                 1                3        10%
  4. INSTRUMENTATION AND CONTROLS                     4                   6.0                  10.0
                                      8. TOTAL DIRECT COSTS                         19                14                33
  5. ELECTRICAL SERVICE                                                                         No
  6. SPARE PARTS                                                           2.0                  2.0    miscellaneous supplies SUBTOTAL                                 27                  38.8                  66.8
  7. CONTINGENCY                                     2                   4.0                  6.0    10%
  8. TOTAL DIRECT COSTS                             29                  42.8        -        71.8
(                                                                C                                                              C


ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE
K                                                                K
                                            TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                          TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
                                    Description of Augment           Steam Generator Flash Tank Vent to Main Condenser (Sheet 2)
                                                      FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                                                                    DIRECT COST (1975 $1,000)
      Description of Augment       1O0-9pm Deminerallizer (Sheet 2)
                                                                                                                                        BASIS FOR COST
                                                              DIRECT COST (1975 $1000)
                                                            ITEM                LABOR           OTHER              TOTAL                ESTIMATE
                                                                    FO*l PMFNT/MATFRTALS                        BASIS FOR
                                      1. OPERATING LABOR, SUPERVISION,                                                   1        allowance AND OVERHEAD
                  tT*M                            LANOR                                        TOTAL           COST FSTTMATF
                                      2. MAINTENANCE MATERIAL AND                                                        1        2% Total Direct Cost LABOR
  I.  PROCESS EQUIPMENT                              5                  35.0                  40.0  60 ft 3 , SS, ASME VIII, 150 psi, nonregenerative, with resin
                                      3. CONSUMABLES, CHEMICALS, AND                                                   neg SUPPLIES
  2. BUILDING ASSIGNMENT                            9                    4.8                  13.8  12' x 12' x 16' 0 $6/ft3 (shielded area)
                                      4. UTILITIES AND SERVICES
  3." ASSOCIATED PIPING SYSTEMS                      10                  10.0                  20.0  2-1/21 piping a, 4.  INSTRUMENTATION AND CONTROLS                    4                   6.0                  10.0
Appendix B to RG 1.110, Page B-40
.1
                                            Waste Disposal Water                                                                      neg Steam Electricity Building Services Other
  5.  ELECTRICAL SERVICE                                                                        neg
                                      5. TOTAL O AND M ANNUAL COST                                                      2
  6.  SPARE PARTS                                                          2.0                    2.0  miscellaneous supplies SUBTOTAL                                28                  57.8                  85.8
  7.  CONTINGENCY                                    3                    6.0                    9.0
  B. TOTAL DIRECT COSTS                            31                  63.8                  94.8


TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-
TOTAL DIRECT COST ESTIMATE SHEET OF RADWAST!E TREATMENT SYSTEM
                                                          WATER-COOLED NUCLEAR REACTORS
                                                    FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                    Description of Augment               15-gpm Evaporator (Sheet 1)
      Description of Augment         20-plDmneralizer(Sheet 3)  3)__
                                                                        DIRECT COST (1975 $1,000)
                                                        (Sheet
                                                                                    EQUIPMENT/                       BASIS FOR COST
                                  200-gpm Oemtneraltzer DIRECT COST (1975 $1000)
                                                            ITEM       LABOR       MATERIALS           TOTAL          ESTIMATE
                                                                  EflUIPI4FNTII4ATFRTAL *                       BASIS FOR
                                      1. PROCESS EQUIPMENT               30              225            255    skid mounted, submerged tube bundle, ASME VIII, Incoloy in contact with process fluid
                ITEM                             LABOR                                         TflTAI           rnCT r~tTuATr
                                      2. BUILDING ASSIGNMENT             68              34            102    evap & services 25 x 30 x 20
                                                                  1T                  A
                                                                                                                @ $6/ft3 plus 2,000 ft3 increase in solid waste storage area
  1. PROCESS EQUIPMENT                             5                    60.0                    65.0  120 ft 3 , SS, ASME VIII, i50 psi, nonregenerative, with resin
                                      3. ASSOCIATED PIPING SYSTEMS       35                30            65    includes service piping
  2. BUILDING ASSIGNMENT                           11                      5.2                    16.2  13' x 13' x 16' 0 $6/ft 3
                                      4. INSTRUMENTATION AND CONTROLS     10              10             20    allowance Appendix B to RG 1.110, Page B-41
                ___(shielded                                                                                        area)
                                      5. ELECTRICAL SERVICE               40              25            65    allowance
  3. ASSOCIATED PIPING SYSTEMS                     12                    12.0                    24.0  4" piping
                                      6. SPARE PARTS                       -              27            27    2% of item 1 plus tube bundle SUBTOTAL               183              351            534
  4. INSTRUMENTATION AND CONTROLS                   4                    6.0                    10.0
                                      7. CONTINGENCY                     18              35            53    10%
  5. ELECTRICAL SERVICE                                                                         neg
                                      8. TOTAL DIRECT COSTS             201              386            587
  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-
K
                                                          WATER-COOLED NUCLEAR REACTORS
                                          TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
                                    Description of Augment               30-gpm Evaporator (Sheet 2)
                                                      FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                                                        DIRECT COST (1975 $1,000)
      Description of Augment       400-gpm Demineralizer  -  Steam Generator Blowdown Service (Sheet 4)
                                                                                    EQUIPMENT/                        BASIS FOR COST
                                                              DIRECT COST (1975 $1000)
                                                             ITEM      LABOR      MATERIALS          TOTAL          ESTIMATE
                                                                                                                  BASIS FOR
                                      1. PROCESS EQUIPMENT               30              350            380    ASME VIII
                  I TrM                            lAROR              EOUJIPMNT/MATERjALS          TOTAL          COST ESTIMATE
                                                                                                                skid mounted, submerged, tube bundle, Incoloy in contact with process fluid
                                  T                                                             I                COST ESTIMATE
                                      2. BUILDING ASSIGNMENT              88              44            132    evap + services - 25 x 40 x 20
                                                                                                                3
                                                                                                                @ $6/ft3 plus 2,000 ft3 increase in solid waste storage area
  1. PROCESS EQUIPMENT                               5                    60.0                  65.0  120 ft , SS. ASME VIII, 150 psi, nonregenerative. with resin BUILDING ASSIGNMENT                            11                      5.2                   16.2  ,3' x 13' x 16' @ $6/ft 3
                                      3. ASSOCIATED PIPING SYSTEMS      35                35            70    includes service piping Appendix B to RG 1.110, Page B-42
   2.
                                      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-
(shielded area)
                                                          WATER-COOLED NUCLEAR REACTORS
   3. ASSOCIATED PIPING SYSTEMS                     20                      20.0                  40.0  6" piping a,
                                    Description of Augment                50-gpm Evaporator (Sheet 3)
'a
                                                                        DIRECT COST (1975 $1,000)
   4. INSTRUMENTATION AND CONTROLS                   4                      6.0                    10.0 allowance
                                                                                    EQUIPMENT/                        BASIS FOR COST
  5. ELECTRICAL SERVICE                                                                           neg
                                                            ITEM      LABOR      MATERIALS          TOTAL          ESTIMATE
   6. SPARE PARTS                                                           2.0                    2.0 miscellaneous supplies SUBTOTAL                                 40                    93.2                  133.2
                                      1. PROCESS EQUIPMENT                30              450            480   ASME VIII
    7. CONTINGENCY                                     4                    9.0                    13.0
                                                                                                                skid mounted, submerged, tube bundle, Incoloy in contact with process fluid
   8. TOTAL DIRECT COSTS                             44                    102.2                  146.2
                                      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
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
                                            TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                                                SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                    Description of Augment             Evaporator - BWR Dirty Waste - Floor Drains (Sheet 4)
        Description of Augment     BWR  - 2nd Waste Demineralizer In Serf es (Sheet El COST (1975 $1000)
                                                                                  DIRECT COST (1975 $1,000)
                    ITEM                                   lABOR             NTNrD          TJlTA!
                                                                                                                                    BASIS FOR COST
                                              _...._-_....__,,__                            ,v-n  -
                                                            ITEM             LABOR             OTHER              TOTAL              ESTIMATE
                                                                                                                  aAeT*
                                      1. OPERATING LABOR, SUPERVISION,                                                 12      2.6 x 106 gpy; 1000 hrs/yr labor AND OVERHEAD
                                                                                                                  DROIO
                                      2. MAINTENANCE MATERIAL AND                                                     30      71/2% of equipment costs LABOR
                                                                                                                          *n*  *
                                      3. CONSUMABLES, CHEMICALS, AND                                                 neg      concentrate solidification SUPPLIES                                                                             chemicals in item 4
                                                                                                                          rvr uK    EV)lr.1~PY.I
                                      4. UTILITIES AND SERVICES
                                                                                                                                      PP*guA*P
                                            Waste Disposal                                                             70      100:1 feed to concentrate ratio Appendix B to RG 1.110, Page B-44
    1. OPERATING LABOR, SUPERVISION,                                                         3.3      15 min/shift AND OVERHEAD
                                                                                                                              @ $20/ft3 disposal cost Water                                                                     27      1,000 gpm @ 1,500 hrs @
    2. MAINTENANCE MATERIAL AND
                                                                                                                              30¢/1000 gal Steam                                                                     60      1,500 hrs steam @ 20,000 lb/hr
        LABOR                                                                                 5.0      allowance
                                                                                                                              @ $2/1,000 lbs Electricity Building Services Other
    3. CONSUMABLES,   CHEMICALS, AND                                                         9.0      1 change per year @ 120 ft 3 0 $75/ft 3 (one a      SUPPLIES                                                                                         vessel change per year. regardless of size)
                                      5. TOTAL O AND M ANNUAL COST                                                   199
-.J
a
    4. UTILITIES AND SERVICES
          Waste Disposal                                                                     2.4      120 ft 3 lyr    * $20/ft 3 disposal cost Water Steam Electricity Building Services Other
    5. TOTAL 0 AND M ANNUAL COST                                                           19.7 C


ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE
K                                                                                                                              I
                                            TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                    ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
                                    Description of Augment               Evaporator PWR Dirty Waste (Sheet 5)
                                                  SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                                                            DIRECT COST (1975 $1,000)
    Description of Augment       Demineralizer - PWR Clean Wastes (Sheet 6)
                                                                                                                              BASIS FOR COST
                                                                    COST (197k.$1000)
                                                            ITEM        LABOR            OTHER                TOTAL          ESTIMATE
                YYIPLu AILr nV                  IlV%
                                      1. OPERATING LABOR, SUPERVISION,                                           6.0  500,000 gpy; 500 hrs/yr labor AND OVERHEAD
                                                I am*o    -
                                      2. MAINTENANCE MATERIAL AND                                               30.0  71/2% of equipment costs LABOR
                                                                flTurD
                                      3. CONSUMABLES, CHEMICALS, AND                                             -     concentrate solidification SUPPLIES                                                                      chemicals in item 4
                                                                  lll_ __ _
                                      4. UTILITIES AND SERVICES
                                                                                ?linI
                                            Waste Disposal                                                       27.0  50:1 feed to concentrate ratio @
                                                                                  Ifl, matie fflS EflM? rCTTMATe
Appendix B to RG 1.110, Page B-45
                                                                                                      &'flC I  l      bl  *fll
                                                                                                                        $20/ft3 disposal cost Water                                                                 5.0  1,000 gpm @ 277 hrs @
  1. OPERATING LABOR, SUPERVISION,                                                 1.8    10% of DRS shim bleed (50,000 gpy),
                                                                                                                        30¢/1,000 gal Steam                                                               12.0  277 hrs steam @ 20,000 lbs/hr
    AND OVERHEAD                                                                           30 min/day
                                                                                                                        @ $2/1,000 lbs Electricity Building Services Other
  2. MAINTENANCE MATERIAL AND
                                      5. TOTAL O AND M ANNUAL COST                                               80.0
    LABOR                                                                          5.0     allowance
                                                                                                                3
   3. CONSUMABLES,
    SUPPLIES        CHEMICALS, AND                                                 2.3     30 3ft /yr @ $75/ft3 a
  4. UTILITIES AND SERVICES
      Waste Disposal                                                               0.6      30 ft 3/yr @ $20/ft3 disposal cost Water Steam Electricity Building Services Other S. TOTAL 0 AND M ANNUAL COST                                                     9.7


ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADIASTE TREATMENT
                                            TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                                      SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                    Description of Augment           Evaporator - Condenser Polisher Chemical Waste (Sheet 6)
          Description of Augment     Demineralizer - BWR Dirty Waste (Sheet 7)
                                                                                  DIRECT COST (1975 $1,000)
                                                                      COST (1975 $1000)
                                                                                                                                      BASIS FOR COST
                    JTFN                          [ABDR            nlTHVg          TNlT61             DACIC mnD r.ncT  reTvUnt I. OPERATING LABOR, SUPERVISION,
                                                            ITEM              LABOR             OTHER            TOTAL                ESTIMATE
          AND OVERHEAD                                                                6.5      2.6 x 106 gpy, 30 min/shift
                                      1. OPERATING LABOR, SUPERVISION,                                                 6.0    650,000 gpy; 500 hr/yr labor AND OVERHEAD
      2. MAINTENANCE MATERIAL AND
                                      2. MAINTENANCE MATERIAL AND                                                     30.0      71/2% of equipment costs LABOR
          LABOR                                                                      5.0      allowance CONSUNABLES,  CHEMICALS, AND33
                                      3. CONSUMABLES, CHEMICALS, AND                                                            concentrate solidification SUPPLIES                                                                              chemicals in item 4
      3.   SUPALES                                                                  64.5      860 ft 3 resin 0 $75/ft 3 N
                                      4. UTILITIES AND SERVICES
      4. UTILITIES AND SERVICES
                                            Waste Disposal                                                           87.0     20:1 feed to concentrate ratio @
            Waste Disposal                                                           17.2     860 ft 3 @ $20/ft 3 disposal cost Water Steam Electricity Building Services Other S. TOTAL 0 AND N ANNUAL COST                                                 93.2
Appendix B to RG 1.110, Page B-46
--- I                                                                C                                                          C
                                                                                                                                $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
                                                                K
                                    Description of Augment               Evaporator - Detergent Waste (Sheet 7)
                                    ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
                                                                            DIRECT COST (1975 $1,000)
                                                  SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                                                                                                                BASIS FOR COST
      Description of Augment     Demineraltzer - PWR Dirty. Wastes (w/o turbine building) (Sheet 8)
                                                            ITEM         LABOR             OTHER                TOTAL          ESTIMATE
                                                                  COST (1975 $1000)
                                      1. OPERATING LABOR, SUPERVISION,                                             6.0  160,000 gpy; 500 hrs/yr AND OVERHEAD
                ITEM                           LABOR         OTHER           TOTAL                 BASIS FOR COST ESTIMATE
                                      2. MAINTENANCE MATERIAL AND                                                 30.0  71/2% of equipment costs LABOR
  l. OPERATING LABOR, SUPERVISION,
                                      3. CONSUMABLES, CHEMICALS, AND                                               -    concentrate solidification SUPPLIES                                                                         chemicals in item 4
      AND OVERHEAD                                                                3.3      500,000 gpy; 15 min/shift
                                      4. UTILITIES AND SERVICES
  2. MAINTENANCE MATERIAL AND
                                            Waste Disposal                                                         8.6  50:1 feed to concentrate ration Appendix B to RG 1.110, Page B-47
      LABOR                                                                      5.0       allowance
                                                                                                                          @ $20/ft3 disposal cost Water                                                                  1.6  1,000 gpm @ 90 hrs @
   3. CONSUMABLES, CHEMICALS, AND
                                                                                                                          30¢/1,000 gal Steam                                                                   3.6  90 hrs steam @ 20,000 lb/hr @
      SUPPLIES                                                                 12.0        160 ft 3 /yr @ $75/ft 3 a
                                                                                                                          $2/1,000 lbs Electricity Building Services Other
  4. UTILITIES AND SERVICES
                                      5. TOTAL O AND M ANNUAL COST                                                49.8
        Waste Disposal                                                           3.2      160 ft 3 /yr @ $20/ft 3 disposal cost water Steam Electricity Building Services Other
  5. TOTAL 0 AND M ANNUAL COST                                                23.5


TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-
ANNUAL OPERATIN AND MAINTE*ANCE COST ESTIMTE SHEET OF RADWASTE TREATMENT
                                                          WATER-COOLED NUCLEAR REACTORS
                                                            SYSTEM FOR L.IGHT,oWATER-COOLEO NUCL..EAR,, REACTORS
                                    Description of Augment             Evaporator Distillate Demineralizer (Sheet 1)
      D*crlrintinn      of Aujnmant flminapA147AP      .  DUo
                                                                              DIRECT COST (1975 $1,000)
             *7m,
                                                                                          EQUIPMENT/                                BASIS FOR COST
              *  **,*,-*      pww-                      -  .  T. *    a w,*g uu,,*U-I
                                                            ITEM          LABOR          MATERIALS              TOTAL                ESTIMATE
                                                                        *fm          rC1      uVfm "a 1.411W4b  7I
                                      1. PROCESS EQUIPMENT                      4.0              20.0                  24.0  30 ft3, SS, ASME VIII, 150 psi nonregenerative, w/resin
                                                                                COST (1975 $1000)
                                      2. BUILDING ASSIGNMENT                    6.4                3.2                  9.6  10 x 10 x 16 @ $6/ft3 (shielded area)
                      ITEM                               I ARMR            flTIIFA         Ti*TAI                      oAeTe *    *Ae*  rPgvu4*
                                      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
                                                                                              ..-.                       urwl, rvuK I.UF)I LtIY:llrl
                                      5. ELECTRICAL SERVICE                                                        neg
  1. OPERATING LABOR, SUPERVISION.
                                      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
AND OVERHEAD                                                                              13.1            1 hr/shift, 2.6 x 106 opy
                                            TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
   2. MAINTENANCE MATERIAL AND
                                    Description of Augment                Evaporator Distillate Demineralizer (Sheet 2)
      LABOR                                                                                        5.0         allowance
                                                                                DIRECT COST (1975 $1,000)
  3. CONSUMABLES, CHEMICALS, AND
                                                                                                                                      BASIS FOR COST
a SUPPLIES                                                                                64.5            660 ft 3 resin 0 $75/ft 3
                                                            ITEM           LABOR              OTHER              TOTAL              ESTIMATE
  4. UTILITIES AND SERVICES
                                      15. OPERATING LABOR, SUPERVISION,                                                  1.8   1,500 hrs operation @
        Waste Disposal                                                                         17.2            860 ft 3/yr 9 $20/ft 3 disposal cost Water Steam Electricity Building Services Other S. TOTAL 0 AND N ANNUAL COST                                                               99.8
                                          AND OVERHEAD                                                                          10% attendance
(                                                                      .-."(
                                      16. MAINTENANCE MATERIAL AND                                                       2.0   allowance LABOR
                                                                -1-:j:.1i-:i...-
                                      17. CONSUMABLES, CHEMICALS, AND                                                     2.3   1 change per yr @ $75/ft3 SUPPLIES
                                                                              ........                                                               r
                                      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-
K
                                                          WATER-COOLED NUCLEAR REACTORS
                                  A..UAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
                                    Description of Augment               50-gpm Demineralizer (Sheet 1)
                                                SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                                                        DIRECT COST (1975 $1,000)
    Description of Augment   Demineralizer - PIER Steam Generator Blowdomn (Sheet 10)
                                                                                    EQUIPMENT/                        BASIS FOR COST
                                                                COST (1975 $1000)
                                                            ITEM      LABOR        MATERIALS            TOTAL          ESTIMATE
                 tim                          I alLfl9       nyu,..O        inaI               ma*tt  ens rtnt ReTtMAta OPERATING LABOR, SUPERVISION.
                                      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-
AND OVERHEAD                                                              3.3      15 min/shift
                                                          WATER-COOLED NUCLEAR REACTORS
  2. MAINTENANCE MATERIAL AND
                                    Description of Augment              100-gpm Demineralizer (Sheet 2)
    LABOR                                                                     5.0       allowance
                                                                          DIRECT COST (1975 $1,000)
  3. CONSUMABLES, CHEMICALS, AN"
                                                                                    EQUIPMENT/                          BASIS FOR COST
a    SUPPLIES                                                                  16.9       225 ft 3 resin/yr @$75/ft3
                                                            ITEM      LABOR       MATERIALS            TOTAL          ESTIMATE
   4. UTILITIES AND SERVICES
                                      1. PROCESS EQUIPMENT                5               35.0           40.0  60 ft3, SS, ASME VIII, 150 psi, nonregenerative, with resin
      Waste Disposal                                                          4.5      225 ft 3 /Yr I $20/ft 3 disposal cost Water Stem Electricity Building Services Other S. TOTAL 0 AND M ANNUAL COST                                                 29.7
                                      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-
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
                                                          WATER-COOLED NUCLEAR REACTORS
                                                            FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                    Description of Augment               200-gpm Demineralizer (Sheet 3)
          Description of Augment     20-qp Cartridge Filter (Sheet 1)  1)
                                                                          DIRECT COST (1975 $1,000)
                                                        Ftlter (Sheet
                                                                                    EQUIPMENT/                          BASIS FOR COST
                                      20-qm Cartrtd9e DIRECT COST (1975 $1000)
                                                            ITEM       LABOR        MATERIALS            TOTAL            ESTIMATE
                    TTFM                            I AI*fl2            vN  Itur
                                      1. PROCESS EQUIPMENT                 5               60.0             65.0   120 ft3, SS, ASME VIII, 150 psi, nonregenerative, with resin
                                                                                ¶      u'IIAqr rD lr e                BASIS FOR
                                      2. BUILDING ASSIGNMENT             11                5.2            16.2  13 x 13 x 16 @ $6/ft3 (shielded area)
                                          ...                            t.J       ~vrl.rnlr.lL*nL    T*Ai UIhLU                11MAT
                                      3. ASSOCIATED PIPING SYSTEMS        12                12.0             24.0  4" piping
      1. PROCESS EQUIPMENT                             2.0                        5.0                   7.0 SS, ASME VIII, 150 psi BUILDING ASSIGNMENT                             5.6                       3.0                   8.6 16' x 12' x 20' S $6/ft 3
                                      4. INSTRUMENTATION AND CONTROLS      4                6.0            10.0
      2.
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-
(shielded area)
                                                          WATER-COOLED NUCLEAR REACTORS
      3. ASSOCIATED PIPING SYSTEMS                      1.5'                      1.0                   2.5 allowance
                                    Description of Augment          400-gpm Demineralizer - Steam Generator Blowdown Service (Sheet 4)
-. 4 Q
                                                                                      DIRECT COST (1975 $1,000)
at    4. INSTRUMENTATION AND CONTROLS                   0.6                       2.4                    3.0 allowance
                                                                                                  EQUIPMENT/                              BASIS FOR COST
      5. ELECTRICAL SERVICE                                                                               neg
                                                            ITEM                  LABOR          MATERIALS            TOTAL                ESTIMATE
    6. SPARE PARTS                                                               0.5                    0.5 SUBTOTAL                                 9.7                      11.9                  21.6
                                      1. PROCESS EQUIPMENT                              5               60.0              65.0       120 ft3, SS, ASME VIII, 150 psi, nonregenerative, with resin
    7. CONTINGENCY                                     1.0                        1.0                   2.0 10%
                                      2. BUILDING ASSIGNMENT                          11                5.2              16.2      13 x 13 x 16 @ $6/ft3 (shielded area)
    8. TOTAL DIRECT COSTS                            10.7                        12.9                  23.6
                                      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
                                            TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                  ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE
                                    Description of Augment               BWR - 2nd Waste Demineralizer in Series (Sheet 5)
                                              SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                                                                  DIRECT COST (1975 $1,000)
    Description of Augment   Cartridge Filter (Sheet 2)
                                                                                                                                    BASIS FOR COST
                                                                COST (1975 $1000)
                                                            ITEM             LABOR            OTHER              TOTAL            ESTIMATE
                                                            A'1JCDl        T*TAI              RAM!S FOR COST ESTIMATE
                                      1. OPERATING LABOR, SUPERVISION,                                                 3.3  15 min/shift AND OVERHEAD
              ITEM                         LADUK          uini n          ,    -... .        .....    .... ...  ..
                                      2. MAINTENANCE MATERIAL AND                                                       5.0   allowance LABOR
                                                                                4.5      10 changes @ 10 man-hrs/change
                                      3. CONSUMABLES, CHEMICALS, AND                                                   9.0   1 change per year @ 120 ft3 @
1. OPERATING LABOR. SUPERVISION,                                                         @ $12/hr + 15 min/shift AND OVERHEAD
                                        SUPPLIES                                                                             $75/ft3 (one vessel change per year, regardless of size)
2. MAINTENANCE MATERIAL AND                                                             allowance
                                      4. UTILITIES AND SERVICES
                                                                                1.0
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
    LABOR
                                      5. TOTAL O AND M ANNUAL COST                                                     19.7
3. CONSUMABLES. CHEMICALS, AND                                                           10 changes/yr @$100/change
                                                                                1.0
    SUPPLIES
4. UTILITIES AND SERVICES                                                                                         3
                                                                                1.5      10 drums/yr @$20/ft Waste Disposal Water Steam Electricity Building Services Other
                                                                                8.0
5. TOTAL 0 AND MANNUAL COST


ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREAT1ENT SYSTEM
                                            TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                                                                                        i FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                    Description of Augment               Demineralizer - PWR Clean Wastes (Sheet 6)
        Description of Augment     100-gpim Precoat Filter (Shoot 1)
                                                                              DIRECT COST (1975 $1,000)
                                                                    1)
                                                                                                                                  BASIS FOR COST
                                                      Ftlter (Sheet lO0-gpm Precoat            DIRECT COST (1975 $1000)
                                                            ITEM           LABOR            OTHER            TOTAL              ESTIMATE
                                                                        fIW01T
                                      1. OPERATING LABOR, SUPERVISION,                                                1.8   10% of BRS shim bleed AND OVERHEAD                                                                      (50,000 gpy), 30 min/day
                                                                            P~NT uI~dTIDTAI                        BASIS FOR
                                      2. MAINTENANCE MATERIAL AND                                                    5.0  allowance LABOR
                  ITEM                             LARnR                                        T*TAI
                                      3. CONSUMABLES, CHEMICALS, AND                                                  2.3  30 ft3/yr @ $75/ft3 SUPPLIES
    1. PROCESS EQUIPMENT                              10                      65.0                  75   automated system 1 gpm/ft 2 ,
                                      4. UTILITIES AND SERVICES
                                                                                                          ASM4E VIII
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
        BUILDING ASSIGNMENT                            18                      9.0                   27   15' x 15' x 20' 0 $6/ft 3
                                      5. TOTAL O AND M ANNUAL COST                                                    9.7
  2.


ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE
(shielded area)
                                            TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
  3.  ASSOCIATED PIPING SYSTEM4S                      16                      9.0                  25  35% of equipment cost
                                    Description of Augment              Demineralizer - BWR Dirty Waste (Sheet 7)
0
                                                                              DIRECT COST (1975 $1,000)
   4.   INSTRUMENTATION AND CONTROLS                                                                      in item 1
                                                                                                                                  BASIS FOR COST
  5.   ELECTRICAL SERVICE                              7                      13.0                 20    allowance
                                                            ITEM          LABOR            OTHER            TOTAL                ESTIMATE
  6.   SPARE PARTS                                                              2.0                    2   2% of item 1 SUBTOTAL                                51                      98.0                  149
                                      1. OPERATING LABOR, SUPERVISION,                                                6.5   2.6 x 106 gpy, 30 min/shift AND OVERHEAD
  7.   CONTINGENCY                                      5                    10.0                  15    10%
                                      2. MAINTENANCE MATERIAL AND                                                    5.0   allowance LABOR
   8.   TOTAL DIRECT COSTS                            56                    108.0                164
                                      3. CONSUMABLES, CHEMICALS, AND                                                64.5   860 ft3 resin @ $75/ft3 SUPPLIES
(                                                                                                                                    r
                                      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
K                                                                                                                                    K
                                            TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                          TOTAL DIRECT COST ESTIMATE     SHEET OF RADWASTE TREATMENT SYSTEM
                                    Description of Augment         Demineralizer - PWR Dirty Wastes (w/o turbine building) (Sheet 8)
                                                                    2)
                                                                                    DIRECT COST (1975 $1,000)
                                                        FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                                                                                                                              BASIS FOR COST
      Description of Augment     400-oam Precoat Filter (Sheet 2)
                                                            ITEM                LABOR            OTHER              TOTAL                   ESTIMATE
                                    -vT
                                      1. OPERATING LABOR, SUPERVISION,                                                      3.3        500,000 gpy; 15 min/shift AND OVERHEAD
                                                            (Sheet DIRECT COST (1975 $1000)
                                      2. MAINTENANCE MATERIAL AND                                                          5.0        allowance LABOR
                                                                                                                  BASIS FOR
                                      3. CONSUMABLES, CHEMICALS, AND                                                      12.0          160 ft3/yr @ $75/ft3 SUPPLIES
                  TT*M                            LAROR              EOUIPMENT/MATERIALS          TOTAL         COST ESTIMATE
                                      4. UTILITIES AND SERVICES
      PROCESS EQUIPMENT                            35                      135.0                  170    automated system; 1 gpm/ft 2
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
===1. ASME Viii===
                                            TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                                                                                                                    3 BUILDING ASSIGNMENT                            24                      12.0                    36  15' x 20' x 20' @ $6/ft
                                    Description of Augment          Demineralizer - PWR Turbine Building Floor Drains (Sheet 9)
    2.                                                                                                      (shielded area)
                                                                                  DIRECT COST (1975 $1,000)
    3. ASSOCIATED PIPING SYSTEMS                      31                      16.0                    47  35% of equipment cost
                                                                                                                                        BASIS FOR COST
-J
                                                            ITEM              LABOR            OTHER              TOTAL                ESTIMATE
    4. INSTRUMENTATION AND CONTROLS                  -                                                -    item I
                                      1. OPERATING LABOR, SUPERVISION,                                                  13.1      1 hr/shift, 2.6 x 106 gpy AND OVERHEAD
    5. ELECTRICAL SERVICE                            12                      18.0                     30  allowance
                                      2. MAINTENANCE MATERIAL AND                                                        5.0       allowance LABOR
    6. SPARE PARTS                                    -                        3.0                      3 SUBTOTAL                                102                    184.0                    286
                                      3. CONSUMABLES, CHEMICALS, AND                                                    64.5      860 ft3 resin @ 75/ft3 SUPPLIES
    7. CONTINGENCY                                    10                      18.0                    28    10%
                                      4. UTILITIES AND SERVICES
    8. TOTAL DIRECT COSTS                            112                    202.0                    314
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
ANNUAL OPERATING AND MAINTENANCE COST ESTI1ATE SHEET OF RADWASTE TREATMENT
                                            TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                                SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                    Description of Augment           Demineralizer - PWR Steam Generator Blowdown (Sheet 10)
    Description of Augment     Precoat Filter - BWR Dirty Waste (Sheet 3)
                                                                                  DIRECT COST (1975 $1,000)
                                                                COST (1975 $1000)
                                                                                                                                    BASIS FOR COST
                ITEM                         LABOR         OTHER           TOTAL                BASIS FOR COST !STTI4ATF
                                                            ITEM             LABOR           OTHER             TOTAL                ESTIMATE
  1. OPERATING LABOR, SUPERVISION,
                                      1. OPERATING LABOR, SUPERVISION,                                               3.3      15 min/shift AND OVERHEAD
    AND OVERHEAD                                                              6.6      2 x 106 gpy, 30 min/shift
                                      2. MAINTENANCE MATERIAL AND                                                     5.0     allowance LABOR
  2. MAINTENANCE MATERIAL AND
                                      3. CONSUMABLES, CHEMICALS, AND                                                 16.9      225 ft3 resin/yr @ $75/ft3 SUPPLIES
    LABOR                                                                    10.0       allowance
                                      4. UTILITIES AND SERVICES
  3. CONSUMABLES, CHEMICALS, AND                                               6.0      10 lbs precoat @ lOt/lb per 1000 gal SUPPLIES                                                                           processed
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
  4. UTILITIES AND SERVICES                                                                                                           3 Waste Disposal                                                         40.0      1 ft 3/sludge per 1000 qal processed @ $30/ft disposal cost Water Steam Electricity Building Services Other S. TOTAL 0 AND M ANNUAL COST         j[                                    62.6
                                      5. TOTAL O AND M ANNUAL COST                                                   29.7
(                                                                                                                              C


TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-
T                                                                K
                                                          WATER-COOLED NUCLEAR REACTORS
                                          TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
                                    Description of Augment               20-gpm Cartridge Filter (Sheet 1)
                                                      FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                                                          DIRECT COST (1975 $1,000)
      Description of Augment       2-com Reverse Osmosis (Sheet 1)
                                                                                      EQUIPMENT/                          BASIS FOR COST
                                                            DIRECT COST (1975 $1000)
                                                            ITEM      LABOR        MATERIALS              TOTAL           ESTIMATE
                                                                                                              BASIS FOR
                                      1. PROCESS EQUIPMENT                2.0               5.0             7.0   SS, ASME VIII, 150 psi
                TTIFM                            LABOR             FOUlPMENTIMATFRIALS         TOTAL         COST ESTIMATF
                                      2. BUILDING ASSIGNMENT               5.6               3.0              8.6  16 x 12 x 20 @ $6/ft3 (shielded area)
  1. PROCESS EQUIPIENT                              6.0                 60.0                   66.0 skid mounted w/500-gal SS
                                      3. ASSOCIATED PIPING SYSTEMS         1.5                1.0             2.5   allowance
                                                                                                        feed tank, ASME VIII
                                      4. INSTRUMENTATION AND CONTROLS     0.6                2.4              3.0   allowance Appendix B to RG 1.110, Page B-60
  2. BUILDING ASSIGNMENT                           19.2                  9.6                   28.8 12' x 25' x 16' @ $6/ft 3
                                      5. ELECTRICAL SERVICE                                                  neg
  3. ASSOCIATED PIPING SYSTEMS                     3.0                   2.0                    5.0  allowance
                                      6. SPARE PARTS                       -                  0.5              0.5 SUBTOTAL                 9.7              11.9            21.6
0
                                      7. CONTINGENCY                       1.0               1.0             2.0  10%
  4. INSTRUMENTATION AND CONTROLS                                                                     in item I
                                      8. TOTAL DIRECT COSTS               10.7              12.9            23.6
  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
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
                                            TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                                  SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                    Description of Augment                 Cartridge Filter (Sheet 2)
        Description of Augment     Reverse Osmosis - Detergent Wastes COST (1975 $1000)
                                                                          DIRECT COST (1975 $1,000)
                  ITEM                         LABOR         OTHER         TOTAL               BASIS FOR COST ESTIMATE
                                                                                                                      BASIS FOR COST
    1. OPERATING LABOR, SUPERVISION,
                                                            ITEM       LABOR           OTHER           TOTAL         ESTIMATE
        AND OVERHEAD                                                             3.1      160.000 gpy, 1300 hrs/yr @ 20% attendance
                                      1. OPERATING LABOR, SUPERVISION,                                     4.5  10 changes @ 10
    2. MAINTENANCE MATERIAL AND                                                 8.8      4% less bldg + 24 module with 3-yr life LABOR                                                                               @ $600 each
                                        AND OVERHEAD                                                           man-hrs/change @ $12/hr +
    3. CONSUMABLES, CHEMICALS. AND
                                                                                                                15 min/shift
        SUPPLIES                                                                 neg No
                                      2. MAINTENANCE MATERIAL AND                                         1.0  allowance LABOR
    4. UTILITIES AND SERVICES
                                      3. CONSUMABLES, CHEMICALS, AND                                       1.0  10 changes/yr @ $100/change SUPPLIES
          Waste Disposal                                                         4.3      100:1 vol reduction @ $20/ft 3 disposal cost Water Steam Electricity                                                             neg Building Services Other
Appendix B to RG 1.110, Page B-61
    5. TOTAL 0 AND MANNUAL COST                                                 16.2
                                      4. UTILITIES AND SERVICES
(                                                              r                                                                  C
                                            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-
1)
                                                          WATER-COOLED NUCLEAR REACTORS
                                        TOTAL DIRECT (Sheet  COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
                                    Description of Augment               100-gpm Precoat Filter (Sheet 1)
                                                          FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                                                        DIRECT COST (1975 $1,000)
                                        10tOOO-GallonTapk Description of Augment       1O,000-Gallon Tank__(Sheet 1)
                                                                                      EQUIPMENT/                         BASIS FOR COST
                                                                  DIRECT COST (1975 $1000)
                                                            ITEM      LABOR        MATERIALS            TOTAL          ESTIMATE
                                                                          !0IJ!P?4fNT/MATERIALS                      BASIS FOR
                                      1. PROCESS EQUIPMENT                10                65.0              75    automated system 1 gpm/ft2, ASME VIII
                ?tTrM                                I AROR                                          TOTAL          COST ESTIMATE
                                      2. BUILDING ASSIGNMENT              18                  9.0            27    15 x 15 x 20 @ $6/ft3 (shielded area)
                T -
                                      3. ASSOCIATED PIPING SYSTEMS        16                  9.0            25    35% of equipment cost
                                                          3                      28                    31  SS, ASME VIII, atmospheric
                                      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-
===1. PROCESS EQUIPMENT===
                                                          WATER-COOLED NUCLEAR REACTORS
                                                                                                              service, 200°F
                                    Description of Augment              400-gpm Precoat Filter (Sheet 2)
    BUILDING ASSIGNMENT                                 30                        15                    45   15' x 20' x 25' @ $6/ft3
                                                                        DIRECT COST (1975 $1,000)
   2.
                                                                                      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
(shielded area)
                                            TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
  3. ASSOCIATED PIPING SYSTEMS                              2                        1                     3   10% of item 1 C
                                    Description of Augment              Reverse Osmosis - Detergent Wastes DIRECT COST (1975 $1,000)
w 4. INSTRUMENTATION AND CONTROLS                          4                        6                    10   allowance
                                                                                                                            BASIS FOR COST
  5. ELECTRICAL SERVICE                                                                                  neg
                                                            ITEM        LABOR            OTHER              TOTAL          ESTIMATE
  6. SPARE PARTS                                                                                        neg SUBTOTAL                                       39                        s0                    89
                                      1. OPERATING LABOR, SUPERVISION,                                          3.1  160,000 gpy, 1300 hrs/yr @
  7. CONTINGENCY                                            4                         5                    9   10%
                                        AND OVERHEAD                                                                20% attendance
  8. TOTAL DIRECT COSTS                                    43                      55                    98
                                      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-
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREAThENT
                                                          WATER-COOLED NUCLEAR REACTORS
                                              SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                    Description of Augment                 10,000-Gallon Tank (Sheet 1)
    Description of Augment   10000-Gallon Tank (Sheet 2)
                                                                          DIRECT COST (1975 $1,000)
                                                              COST (1975 $1000)
                                                                                      EQUIPMENT/                        BASIS FOR COST
              ITEM                         LABOR         OTHER           TOTAL              RA~l  flD rfl*T r*TUATr
                                                            ITEM       LABOR       MATERIALS           TOTAL           ESTIMATE
1. OPERATING LABOR, SUPERVISION.
                                      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
AND OVERHEAD                                                             1.1       5 min/shift - log level readings
                                              TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
2. MAINTENANCE MATERIAL AND
                                    Description of Augment                  10,000-Gallon Tank (Sheet 2)
    LABOR                                                                    1.6       1/2% of equipment
                                                                          DIRECT COST (1975 $1,000)
3. CONSUMABLES. CHEMICALS, AND                                             neg SUPPLIES
                                                                                                                        BASIS FOR COST
4. UTILITIES AND SERVICES
                                                             ITEM        LABOR          OTHER            TOTAL          ESTIMATE
      Waste Disposal Water Steam                                                                 neg Electricity Building Services Other
                                      1. OPERATING LABOR, SUPERVISION,                                      1.1   5 min/shift - log level readings AND OVERHEAD
5. TOTAL 0 AND N ANNUAL COST                                               2.7
                                      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
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.
                                                                                  NUS-531,
1. "Guide for Economic Evaluation of Nuclear Reactor Plant Oesigns," USAEC Report NUS Corporation, January 1969.


2. Wage Rates for Key Construction Trades, Engineering News Record, pp. 36-37, January 2, 1975.
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,
- 2000,"
  1974-2000, USAEC Report WASH-1334, Washington, DC, August 1974.
3. "Projections of Labor Requirements for Electric Power Plants Construction, 1974 USAEC Report WASH-1334, Washington, D.C., August 1974.


Appendix B to RG 1.110, Page B-69
1.110-85


APPENDIX C
APPENDIX C
          DATA NEEDED FOR RADWASTE TREATMENT SYSTEM
                            DATA NEEDED FOR RADIIASTE TREATMENT SYSTEM
          COST-BENEFIT ANALYSIS FOR LIGHT-WATER-COOLED
                              COST-BENEFIT ANALYSIS FOR LIGHT-WATER
                                    NUCLEAR REACTORS
                                      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:
      This appendix describes information that should be submitted in support of radwaste treat ment system cost-benefit analyses for light-water-cooled nuclear reactors. The information should be consistent with the contents of the Safety Analysis Report (SAR) and Environmental Report (ER) for the proposed reactor. Appropriate sections of the SAR and ER containing more detailed discussions of the required information should be referenced as appropriate. Each response, however, should be Independent of the ER and SAR. All responses should be on a per reactor basis and should provide the following information:
1.     Detailed cost estimate sheets similar to those shown on the following pages listing all parameters (and their bases) used in determining capital, operating, and maintenance costs associated with all augments considered in the cost-benefit analysis. All costs should be stated in terms of
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.
        1975 dollars.
 
2.    The cost of borrowed money used in the cost analysis and the method of arriving at this cost.


2.     The cost of borrowed money used in the cost analysis and the method of arriving at this cost.
3.   If methods and parameters used in the cost-benefit analysis are different from those aiven in this guide, describe the methods used in detail and provide bases for all parameters.    Include the following information:
      a.  Decontamination factors assigned to each augment and fraction of "on-line" time assumed, i.e., hours per year used.


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:
b.   Parameters and method used to determine the Indirect Cost Factor and the Capital Recovery Factor.
        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
1.110-87


TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE'TREATMENT-SYSTEH
                                                      LIGHT-WATER-COOLED NUCLEAR REACTORS
                                                                          FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                  Description of Augment DIRECT COST (1975 $1,000)
    Description of Augment DIRECT COST (1975 $1000)
                                                                                EQUIPMENT/                BASIS FOR COST
                                                                                                                                                                  BASIS FOR
                                                            ITEM      LABOR    MATERIALS          TOTAL     ESTIMATE
                    i Tru                                            1 AflfD
                                                                                                FflIIIPMFNT/MATFRlALS                    TOTAL                   COST ESTIMATE
                                                                    i aunD                    EnUTPMENTIMATERIALS


===1. PROCESS EQUIPMENT===
===1. PROCESS EQUIPMENT===
                                                              t                  I                                                    1              I


===2. BUILDING ASSIGNMENT===
===2. BUILDING ASSIGNMENT===
                                    3. ASSOCIATED PIPING SYSTEMS
                                                              I                  I                                                    I              I
                                    4. INSTRUMENTATION AND CONTROLS
0 3. ASSOCIATED PIPING SYSTEMS
 
                                                              I                  I                                                    I              I                                          --
===5. ELECTRICAL SERVICE===
  4. INSTRUMENTATION AND CONTROLS
Appendix C to RG-1.110, Page C-2
                                                              I                  I                                                    I              I
  S. ELECTRICAL SERVICE
                                                              I                  I                                                    I              I


===6. SPARE PARTS===
===6. SPARE PARTS===
                                                SUBTOTAL
                  ______________________I                                      i                                                    mI
            SUBTOTAL
    ________________________________________________________ 1            -I                                                        I              I


===7. CONTINGENCY===
===7. CONTINGENCY===
                                                              I                  I                                                    I


===8. TOTAL DIRECT COSTS===
===8. TOTAL DIRECT COSTS===
    ________________________________________________________  ________________ I __________________________________________________  _____________  _______________________________________________
(                                                                                          C                                                                                                  C
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2                                        ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
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  9 COST (1975 $1000)
  9 I TIFM                          LABOR          OTHER          TOTAL              BASIS FOR COST ESTIMATE
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      2.  MAINTENANCE MATERIAL AND
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ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE
CONSUMABLES,
                                                                                                  TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
          SUPPLIES
                                                                                          Description of Augment DIRECT COST (1975 $1,000)
                            CHEMICALS, AND
                                                                                                                                                                    BASIS FOR COST
          UTILITIES AND SERVICES
                                                                                                                  ITEM        LABOR        OTHER          TOTAL    ESTIMATE
              Waste Disposal Water Steam Electricity Building Services Other
*U.S. Government Printing Office: 1987-202-292:60255
        5. TOTAL 0 AND M ANNUAL COST}}
                                                                                            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}}


{{RG-Nav}}
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Latest revision as of 10:13, 28 March 2020

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


U.S. NUCLEAR REGULATORY COMMISSION March 1976 REGULATORY GUIDE

OFFICE OF STANDARDS DEVELOPMENT

4 REGULATORY GUIDE 1.110

COST-BENEFIT ANALYSIS FOR RADWASTE S

LIGHT-WATER-COOLED NUCLEAR PDWE& CRS'

USNRC REGULATORY GUIDES Commen.l shoutd be Sent to Rhe Secretary of the Comm,ssion U S Nuclea,

%equietoy Guido* ate issued to describe and meeks ovelablto ,he pubic Rogulstory Comminssion Washington. 0 C 2065. Attention Docketing end S

methods acceptable go the NRC staff of4 impementing specific pairt of the Commission'& fegulatione. to definetel techniquemused by the state in evild The guides are issued in the following ten broaddivisions at"ig *pecific problems or postulated accidents. 0r to provide guidance to eppli cents Regulatory Gudes am not substitutes for regulamons. end compliance I Power Reactors 5 Products with thenmilerot reCed Methods end soutione diflerent fron those get outi I Research end Test Reactors 7 Tronsponstion Ihe guidell we be acceptable It they provide a bahis for lthefindings requrlit to 3 Fueuls and Materiels Facilities a Occupolionat 4palt h themesnee

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

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

ticfady orssIul Mtevaluating the =teed of an srly viision 20566.Attention Director. Office of Standerde Development

TABLE OF CONTENTS

Page

A. INTRODUCTION

....................................................................... 1.110-5

B. DISCUSSION

R ....................................................................... 1.110-5

C. REGULATORY POSITION

......................................................... 1.110-6 D. IMPLE14ENTATION ................................ .................................. 1.110-6 APPENDIX A, PROCEDURES FOR PERFORMING COST-BENEFIT ANALYSES ........................... 1.110-7 APPENDIX B. BASES FOR PARAMETERS USED IN PERFORMING COST-BENEFIT

ANALYSES .............................................................................. 1.110-17 LIST OF APPENDIX B COST ESTIMATE SHEETS ............................................... 1.110-19 REFERENCES TO APPENDIX B.............................................................. 1.110-85 APPENDIX C, DATA NEEDED FOR RADWASTE TREATMENT SYSTEM COST-BENEFIT

ANALYSIS FOR LIGHT-WATER-COOLED NUCLEAR REACTORS ...................................... 1.110-86 SAMPLE ESTIMATE SHEETS ................................................................ 1.110-88

1.110-3

LIST OF TABLES

Table Page A-1 Direct Costs - Gaseous Radwaste Augments ................................ 1.110-8 A-2 Annual Operating Costs - Gaseous Radwaste Augments; Liquid Radwaste Augments ..................................................... 1.110-10

A-3 Annual Maintenance Costs - Gaseous Radwaste Augments; Liquid Radwaste Augments ..................................................... 1.110-12 A-4 Labor Cost Correction Factors ........................................... 1.110-13 A-5 Indirect Cost Factors ................................................... 1.110-14 A-6 Capital Recovery Factors ................................................ 1.110-15 B-1 Indirect Costs .......................................................... 1.110-18 LIST OF FIGURES

Figure Page A-1 Electric Power Supply Areas in the United States ........................ 1.110-16

1.110-4

A. INTRODUCTION

Section I1.D of Appendix I, "Numerical Guides for Design Objectives and Limiting Conditions for Operation to Meet the Criterion 'As Low As Is Reasonably Achievable' for Radioactive Material in Light-Water-Cooled Nuclear Power Reactor Effluents," to 10 CFR Part 50, "Licensing of Produc tion and Utilization Facilities," requires that liquid and gaseous radwaste systems for light water-cooled nuclear power reactors include all items of reasonably demonstrated technology that, when added to the system sequentially and in order of diminishing cost-benefit return, can, for a favorable cost-benefit ratio, effect reductions in dose to the population reasonably expected to be within 50 miles of the reactor. Values of $1000 per man-rem and $1000 per man-thyroid-rem are given as interim criteria pending the development and establishment of better criteria.

Compliance with Section II.D of Appendix I to 10 CFR Part 50 (which specifically addresses doses to the population) and Sections IL.A, 11.8, and II.C (which address doses to nearby individuals)

is required to meet the criterion, "as low as is reasonably achievable."

To'implement the requirements of Appendix I, the NRC staff has developed a series of guides providing methods acceptable to the staff for the calculation of effluent releases, dispersion of effluents in the atmosphere and different water. bodies, associated radiation doses to man, and cost-benefit aspects of treating radwastes. This regulatory guide describes a method for performing a cost-benefit analysis for liquid and gaseous radwaste system components.

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

B. DISCUSSION

Each applicant for a permit to construct or a license to operate a light-water-cooled nuclear power reactor and each licensee with a license to operate a light-water-cooled nuclear power reactor is required to provide reasonable assurance that the design objectives for as low as is reasonably achievable effluent releases are satisfied by the liquid and gaseous radwaste system designs. It is the objective of this guide to provide an acceptable method of performing cost-benefit analysis, in conformance with Section II.D of Appendix I, to demonstrate that the plant design includes all items of reasonably demonstrated technology for reducing the cumula tive population dose due to releases of radioactive materials from the reactor to levels as low as reasonably achievable. As an interim measure the Conmnission chose values of $1000 per man rem and $1000 per man-thyroid-rem (or lesser values if demonstrated to be suitable for a particu lar site) to be used to implement the cost-benefit analysis.

Because the Commission has not outlined any procedures for including the effects of inflation in the analysis, the NRC staff's analysis is based on 1975 dollars; i.e., neither the costs nor the interim criteria are escalated for the predicted effects of inflation. Since the worth of a man-rem or man-thyroid-rem to the public is subject to the same fluctuations in value as the cost of equipment to reduce radioactive emissions, the NRC staff believes this approach to be reasonable.

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

consider the direct equipment cost and the costs of building space, supportive services, mainte nance, interest, and operating as well as other costs generally considered in analyzing capital and operating costs in power plant estimating. The bases for the costs calculated by the NRC

staff are given in Appendix B.

1-110-5

C. REGULATORY POSITION

1. In accordance with Section II.D, Appendix I to 10 CFR Part 50, each applicant for a permit to construct a light-water-cooled nuclear power reactor should demonstrate by means of a cost benefit analysis that further reductions to the cumulative dose to the population within a

50-mile radius of the reactor site cannot be effected at an annual cost of $1000 per man-rem or

$1000 per man-thyroid-rem (or such lesser costs as demonstrated to be suitable for a particular case).

2. The cost-benefit analysis should consider the reduction in releases of radioactive material from all effluent pathways. Liquid and gaseous radwaste system augments considered in the analysis should be selected in order of diminishing cost-benefit returns.

3. All costs should be given in terms of 1975 dollars (as is the $1000 per man-rem cost with which they are compared). Allowances for Inflation after 1975 should not be factored into the cost estimates.

4. The method of calculation described in Appendix A and the parameters presented in Appendix B of this guide are acceptable to the NRC staff for performing the cost-benefit analysis.

5. In support of the cost-benefit analysis, the applicant should provide a complete evaluation including methodology used, components considered, and all assumptions and parameters used.

Information to be submitted by the applicant Is described in Appendix C to this guide. Use of parameters, assumptions, and models different from those given in Appendices A and B to this guide may result in differences between the evaluations by applicants and those by the NRC staff.

Because of this, these parameters and assumptions should be clearly described and substantiated by the applicant.

0. IMPLEMENTATION

The purpose of this section is to provide information to license applicants and licensees regarding the NRC staff's plan for using this regulatory guide.

Except in those cases in which the applicant proposes an acceptable alternative method for complying with specified portions of the Commission's regulations, the method described herein will be used in the evaluation of construction permit applications docketed after June 4, 1976 unless this guide is revised as a result of suggestions from the public or additional staff review.

If an applicant wishes to use this regulatory guide in developing submittals for applications docketed on or before June 4, 1976, the pertinent portions of the application will be evaluated on the basis of this guide.

1.110-6

APPENDIX A

PROCEDURES FOR PERFORMING COST-BENEFIT ANALYSES

This appendix contains guidance for performing cost-benefit analyses on individual system augments, as well as the parameters needed for estimating costs. The bases for the parameters and worksheets appropriate for use with the following cost-benefit procedure are given in Appendix B.

1. The cumulative population man-rem exposure and man-thyroid-rem exposure should be determined for each effluent release source, e.g., liquid radwaste releases, ventilation releases, etc.

2. Potential reductions to the cumulative population exposure should be determined based on the addition of items of reasonably demonstrated technology which have the potential to reduce releases of radioactive materials.

3. Acceptable methods for performing some of the calculations need for items 1 and 2 above are contained in Regulatory Guides 1.109, "Calculation of Annual Doses to.Man from Routine Releases of Reactor Effluents for the Purpose of Evaluating Compliance with 10 CFR Part 50, Appendix I,"

and 1.111, "Methods for Estimating Atmospheric Transport and Dispersion for Gaseous Effluents in Routine Releases from Light-Water-Cooled Reactors," and in two regulatory guides now in prepara tion on the subjects of (1) calculation of releases of radioactive materials In liquid and gas eous effluents from light-water-cooled reactors and (2) methods for estimating aquatic dispersion of liquid effluents from routine reactor releases for the purpose of implementing Appendix I.

4. The total annual cost of each augment considered in item 2 above should be determined as follows:

a. The Total Direct Cost (TOC):

(1) Obtain the direct cost of equipment and materials from Table A-1.

(2) Multiply the direct labor cost obtained from Table A-1 by the appropriate labor cost correction factor from Table A-4 to obtain the corrected labor cost for the geographtcal area from Figure A-l, in which the plant is to be built.

(3) Add the costs obtained from steps (1) and (2) to obtain the Total Direct Cost.

b. Obtain-the appropriate Indirect Cost Factor (ICF) from Table A-S.

c. Determine Total Capital Cost (TCC) by using the equation:

TCC - TDC x ICF

d. Obtain the appropriate Capital Recovery Factor (CRF) from Table A-6.

e. Determine the Annual Fixed Cost (AFC) by using the equation:

AFC = TCC x CRF

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

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

TAC

  • AFC + AOC + AMC

5. Determine the "benefit" of each augment by multiplying the dose reduction calculated in item 2 above by $1000 per man-rem and/or $1000 per man-thyroid-rem, as appropriate.

6. The system should be augmented with any items for which the TAC from item 4.g above is less than the value calculated in item 5, in the order of diminishing cost-benefit.

1.110-7

TABLE A-1 DIRECT COSTS - GASEOUS RADWASTE AUGMENTS

Direct- Costs

(1975 $1000)

Equipment/Material Labor Total BWR Offgas Recombiner 553 255 808

3-ton Charcoal Adsorber 53 14 67 Desiccant Dryer 218 176 394 Charcoal Vault Refrigeration 116 38 154 Main Condenser Vacuum Pump Charcoal/HEPA

Filtration System 40 8 48 Clean Steam to Turbine Glands 81 215 296 Clean Steam to Steam Valves. 24" and Larger 137 110 247 Clean Steam to Steam Valves, 2-1/2"

and Less Than-24" 183 55 238

15,000-cfm HEPA Filtration System 52(49)* 16(14)* 68(63)*

1,000-cfm Charcoal/HEPA Filtration System 28 10 38

15,000-cfm Charcoal/HEPA Filtration System 97(93) 31(26) 128(119)

30,000-cfm Charcoal/HEPA Filtration System 157(152) 51(41) 208(193)

Turbine Bldg. Chilled Water HVAC System 614 374 988

600-ft 3 Gas Decay Tank 33 24 57 PWR Hydrogen Recombiner 419 147 566 PWR Air Ejector Charcoal/HEPA

Filtration Unit 14 10 24 Steam Generator Flash Tank Vent to Main Condenser 19 14 33 In cases where the equipment may be located either in the auxiliary building or the turbine building and common usage does not indicate a definite preference of one location or the other, cost for both locations are listed with the turbine building location cost in parenthesis.

1.110-8

TABLE A-1 (Continued)

DIRECT COSTS - LIQUID RADWASTE AUGMENTS

Direct Costs

(1975 $1000)

Total Equipment/Material Labor

386 201 587

15-gpm Evaporator

540 223 763

30-gpm Evaporator

655 233 888

50-gpm Evaporator

36 24 60

Evaporator Distillate Demineralizer

43 29 50

50-gpm Demineralizer

64 31 95

100-gpm Demineralizer

94 35 129

200-gpm Deminieralizer

102 44 146

400-gpm Demineralizer

108 56 164

100-gpm Precoat Filter

202 112 314

400-gpw Precoat Filter

13 11 24

20-gpm Cartridge Filter

100 38 138

2-gpm Reverse Osmosis

55 43 98

10,000-gal Tank

1.110-9

TABLE A-2 ANNUAL OPERATING COSTST - GASEOUS RADWASTE AUGMENTS

Total Operating Cost (1975 $lOOO/yr)

B r m m BWR Offgas Recoatbiner 3

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

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

15,000-cfm HEPA Filtration System 6

1,000-cfm Charcoal/HEPA Filtration System 2

15,000-cfm Charcoal/HEPA Filtration System 7

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

Turbine Bldg. Chilled Water HVAC System 49

3

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

Evaporation - PWR Dirty Waste 50

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

Demineralization - kvaporator Distillate 5 Demineralization - BWR 2nd Waste Demineralizer in Series 15 Operating costs are given for a single reactor. Operating costs for augments in shared radwaste systems should be multiplied by the number of reactors serviced by the augment.

1.110-10

TABLE A-2 (Continued)

ANNUAL OPERATING COSTS - LIQUID RADWASTE AUGMENTS

Total Operating Cost (1975 $1000/yr)

5 Demineralization - PWR Clean Waste Demineralization - BWR Dirty Waste 88

18 Demineralization - PWR Dirty Waste

95 Demineralization - PWR Turbine Bld

g. Drains

25 Desmineralization - PWR Steam Generator Blowdown

53 Precoat Filter - BWR Dirty Waste Cartridge Filter 7

7 Reverse Osmosis - Detergent Waste

1

10,000-gal Tank

1.110-11

TABLE A-3 ANNUAL MAINTENANCE COSTS- GASEOUS RADWASTE AUGMENTS

Total Maintenance Cost (1975 $1O00/Yr)

BWR Offgas Recombiner 20

3-ton Charcoal Adsorber neg Desiccant Dryer 6 Charcoal Vault Refrigeration 3 Main Condenser Vacuum Pump Charcoal/HEPA

Filtration System 1 Clean Steam to Turbine Glands 4 Clean Steam to Steam Valves, 24" and Larger 4 Clean Steam to Steam Valves, 2-1/2" and Less Than 24" 12

15,000-cfm HEPA Filtration System 2

1,000-cfm Charcoal/HEPA Filtration System 0.6

15,O00-cfm Charcoal/HEPA Filtration System 9

30,000-cfm Charcoal/HEPA Filtration System 18 Turbine Bldg. Chilled Water HVAC System 20

600-ft 3 Gas Decay Tank neg PWR Hydrogen "Recombiner 10

PWR Air Ejector Charcoal/HEPA Filtration Unit 2 Steam Generator Flash Tank Vent to Main Condenser 1 ANNUAL MAINTENANCE COSTS - LIQUID RADWASTE AUGMENTS

15-gpm Evaporator 30

30-gpm Evaporator 30

50-gpm Evaporator 30

Evaporator Distillate Demineralizer 2

50-gpm Demineral izer 5 lO0-gpmi Demineralizer 5

200-gpm Demineral izer S

100-gpm Precoat Filter 10

400-gpm Precoat Filter 10

20-gpm Cartridge Filter 1

2-gpm Reverse Osmosis g

10.000-gal Tank 2

1.110-12

TABLE A-4 LABOR COST CORRECTION FACTORS

FPC

Geographic Labor Cost Correction Region Factor I 1.6

1.5

1II

1.0

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

See Figure A-1.

1.110-13

TABLE A-5 INDIRECT COST FACTORS

Type Radwaste System Indirect Cost Factor

"1. Single unit site, unitized radwaste system 1.75

2. Multi-unit site, shared radwaste system 1.75

3. Multi-unit site, unitized radwaste system 1.75 + (n-1)1.5 n

where n is the number of unitized radwaste systems at the site Each reactor has a separate, nonshared radwaste system.

I..

1.110-14

TABLE A-6 CAPITAL RECOVERY FACTORS

Cost of Honey Capital Recovery Factor

(1 per year, i)

5 0.0651

0.0726

6

0.0806

7

0.0888

8

0.0973

9

0.1061

10

0.1150

11

0.1241

12

0.1334

13

0.1428

14

0.1523

15

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

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

1.110-15

LEGEND

¶Im REGIONAL GROUPING OF POWER SUPPLY AREAS

FIGURE A-1 ELECTRIC POWER SUPPLY AREAS IN THE UNITED STATES

( C C

APPENDIX B

BASES FOR PARAMETERS USED IN PERFORMING COST-BENEFIT ANALYSIS

This appendix contains detailed cost estimate sheets showing the methods and parameters used to obtain all costs associated with augments considered for the liquid and gaseous radwaste systems. The cost estimate sheets are grouped by radwaste system types. The first sheet in each case is an equipment cost worksheet for determining direct equipment costs. The second sheet is an operating cost worksheet. All costs are stated in terms of 1975 dollars. No attempt has been made to project the effect of inflation. Variations of labor costs and productivity with site locaticns are considered.* All costs are based on the assumption that the reactor is in the design stage and that augmentation of a radwaste system will not involve backfltting of an existing plant. Backfltttng costs should be determined on a case-by-case basis.

1. Capital Costs Capital costs are reported by grouping items by system and by plant location, which gen erally follow the NRC (AEC) accounting system given in NUS-531 (Ref. 1). The direct costs considered to be applicable to radwaste systems are structures, electrical services, equipment, and instrumentation and controls. Spare parts and a contingency allowance** are included in the direct costs. Total capital costs are obtained by multiplying direct costs by an indirect cost factor.

2. Direct Cost Direct costs for each augment include equipment, site labor, and site materials. Principal equipment designs and hardware costs were obtained from utility companies, architect-engineers, and vendors. Costs for building space, electrical services, piping, and instrumentation were estimated considering equipment functions and arrangements.

Costs for electric services, piping, and instrumentation and controls were determined using judgment to estimate equipment layout, points of interface, and services required. The costs for equipment and building space are consistent with'NRC staff recommendations for radwaste sys tem quality assurance, materials, and seismic design. Space requirements were determined based on manufacturer's data or data from existing or proposed layout drawings.

3. Labor Cost Correction Factors Labor cost adjustment factors were developed for each Of the eight FPC electric power supply areas shown in Figure A-I of Appendix A by calculiting the average labor cost-for selected cities (Ref. 2) in each area and adjusting this cost for estimated variations in labor productivity due only to differences In labor practices in the regions considered. Manpower costs were calcu lated by multiplying the estimated labor requirements in man-hours by the composite wage rate (Ref. 3). The calculated labor cost correction factors are tabulated in Table A-4 of Appendix A.

4. Indirect Cost Factor Indirect costs asa percentage of direct costs are calculated in Table B-1.

Location effects of the eight FPC Power Supply areas are estimated and shown in Table A-4 of Appendix A.

Contingency onsite labor and process equipment and material are all based on-l0%.

1.110-17

TABLE 8-1 K..

INDIRECT COSTS

1st Unit, Subsequent Percentage of Units. Percentage Direct Cost of Direct Cost Construction facilities, equiment, and services 10 5 Engineering and construction managment services 20 10

Other owner s costs 10 S

Interest during construction 3S 35 Total 75 SS

  • Based on a lOs/yr interest rate and a 4-year construction time for radaste systems only.

Interest during construction Is estimated to be 25% of direct costs plus other indirect costs. This is equivalent to 351 of the direct costs.

The Indirect escalators (factors) were estimated from preliminary architect/engineering data to be used to update the DOM concept and ORCOST computer codes.

S. Operation And Maintenance Costs Annual expenses for operation and maintenance (O&N) of the radwaste treatment systes were estimated for baseload power plants operating at 801 capacity factor. Manpower and supply costs were estimated by considering equipment functions it each case. Expenses for gases, steam, resins, auxiliary por. and other supplies and services were assessed individually. Maintenance costs were evaluated according to the type of service for which the equipment could be used.

Operating costs include estimated manpower costs, costs of utilities and supplies, and effects on supporting plant systems Interfacing with the augmented radmste system (e.g., effect of an evaporator augment on the solid waste syste). Also included are costs of handling wastes such as spent resins, demineralizer regenerants, evaporator bottoms, and filter media, as well as offsite handling, transportation, and burial costs.

6. Capital Recovery Factor The capital recovery factor Is a levelized annual charge which takes into account the cost of borroved money and the depreciation of assets. It Is calculated from the expression:

I(1 #)o (I + ~

where i a cost of borrowed money expressed as a decimal P - plant operating lifetime (yr)

In calculating the values used in Table A-S of Appendix A. a plant operating lifetime of 30

years was used.

The capital recovery factor multiplied by the total capital cost will give the annual dollar charges for capital and capital-related expenses.

1.110-18

LIST OF APPENDIX B COST ESTIMATE SHEETS

Page Numiber BW Offgas Recmbiner ............................................................. 1.110-20

3-ton Charcoal Adso r ............................................................... 1.110-22 Desiccant Dryer .............................................................. 1.110-24 Charcoal Vault Refrigeration ......................................................... 1.110-26 Charcoal/HEPA Filtration System - Condenser Vacuun Pump .............................. 1.110-28 Clean Steam to Turbine Glands ........................................................ 1.110-30

Clean Steam to Steam Valves 24- and Larger ........................................... 1.110-32 Clean Steam to Steam Valves 2-1/2' and Less Than 24" ................................ 1.110-34

1S.000-cftm NEPA Filtration System .................................................... 1.110-36

1000-cfa Charcoal/HEPA Filtration System ............................................. 1.110-39

15.000-cfm Charcoal/HEPA Filtration System ........................................... 1.110-41

30,000-cfm Charcoal/HEPA Filtration System .......................................... 1.110-44 Turbine Building Chilled Mater HVAC System ........................................... 1.110-47

600-ft 3 Gas Decay Tank ............................................................... 1.110-49 PIW Hydrogen Recombiner .............................................................. 1.110-S1 PiW Air Ejector Charcoal/HEPA Filtration Unit ........................................ 1.110-53 Stem Generator Flash Tank Vent to rain Condenser .................................... 1.110-55 Evaporators .......................................................................... 1.110-57 Evaporator Distillate Demineralizer .................................................. 1.110-64 Demineralizers ....................................................................... 1.110-66 Cartridge Filter ..................................................................... 1.110-76 Precoat Filters ...................................................................... .114 7R

Reverse Osmosis ..................................................................... 1.110-81

10.000-gal Tank ........................................................... 1.11"

1.110-19

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLEDS...... NUCLEAR

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

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

I___MIXL_ 1 IVIML COST ESTIMATE

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

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

a ASSOCIATED PIPING SYSTEMS

3. 18 12 30 augment piping connections only O

4. INSTRUM4ENTATION AND CONTROLS 24 96 120 allowance

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

6.

items 1 & 4 above SUBTOTAL 232 503 735

7. CONTINGENCY 23 50 73 10%

8. TOTAL DIRECT COSTS 2S5 553 808

(

r

A K I

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR-LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment BWR Offgas Recombiner (Sheet 2)

COST (1975 $1000)

ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE

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

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

3. CONSUMBLES, CHEMICALS, AND - initem 2

,01 C2 SUPPLIES

4. UTILITIES AND SERVICES

Waste Disposal Water Steam neg intemittent; 4kw heater load is negligible Electricity Building Services Other

5. TOTAL 0 AND M ANNUAL COST 23.3

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

DIRECT COST (1975 $1000)

BASIS FOR

!TFM LABOR EOUIPMENTIMATERIALS TOTAL COST

- -

ESTIMATF

-- - - -

3

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

4. 4. 4. 4

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

3. ASSOCIATED PIPING SYSTES - in item I

a

4. INSTRUKENTATION AND CONTROLS neg S. ELECTRICAL SERVICE neg

6. SPARE PARTS none existing SUBTOTAL 13 48.5 61.5

7. CONTINGENCY 1 5.0 6.0 10%

8. TOTAL DIRECT COSTS 14 53.5 67.5

. . .. . . . . r r r

K K

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment 3-ton Charcoal Adsorber (Sheet 2)

COST (1975 $1000)

I TFM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE

1. OPERATING LABOR. SUPERVISION. neg AND OVERHEAD

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

3. CONSUMABLES. CHEMICALS, AND

SUPPLIES neg lifetime use of charcoal assumed I..

4. UTILITIES AND SERVICES

Waste Disposal Water Steam neg Electricity Building Services Other

5. TOTAL 0 AND M ANNUAL COST neg

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

DIRECT COST (1975 $1000)

I TEN I ARflR T*TAI

BASIS FOR

1% IL COTETMT

1. PROCESS EQUIPMENT 25 75 100 redundant dryer vessels with

1 regeneration skid

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

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

8i

4. INSTRUMENTATION AND CONTROLS 12 48 60 allowance

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

6. SPARE PARTS 3 3 SUBTOTAL 160 198 358

7. CONTINGENCY 16 20 36 10%

8. TOTAL DIRECT COSTS 176 218 394

( r r

K K K

ANNUAL CPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment Desiccant Dryer (Sheet 2)

COST (1975 $1000)

Q*Pim I Ahfl flTIIP TflTAI BASIS FOR COST ESTIMATE

itri,,,

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

3.3 15 min/shift

1. OPERATING LABOR, SUPERVISION,

AND OVERHEAD

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

LABOR

3 CONSUMABLES, CHEMICALS, AND neg C SUPPLIES

U'

4. UTILITIES AND SERVICES

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

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREAThENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment Charcoal Vault Refrigeration (Sheet 1)

DIRECT COST (1975 $1000)

BASIS FOR

ITEM TftTAI

LAORFlIITDUdCNT/UATCDTA1

10AM C YffASIfC et.V

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

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

0 3. ASSOCIATED PIPING SYSTEMS In item 1 N

14 Ch

4. INSTRUMENTATION AND CONTROLS 4 6 10 allowance

5. ELECTRICAL SERVICE 12 18 30 allowance

6. SPARE PARTS 3 3 SUBTOTAL 35 105 140

7. CONTINGENCY 3 11 14 10%

8. TOTAL DIRECT COSTS 38 116 154

(

K K K

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COO.EO NUCLEAR REACTORS

Description of Augment Charcoal Vault Refriceration (Sheet 2)

COST (1975 $1000)

'TIn' rTeR TOTAL FOR COST !T1MATE

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

2. MAINTENANCE MATERIAL AND

LABOR 3.7 51 of equlpemt

3. CONSUMABLES, CHEMICALS, AND in Item 2 SUPPLIES

4. UTILITIES AND SERVICES

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

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment Charcoal/HEPA Filtration System - Condenser Vacuum Pump (Sheet 1)

i n *

DIRECT COST (1975 $1000)

ITE4 I A*Q

BASIS FOR

LABOR__ ~ LrILumLAL IUIAL COST ESTIMATE

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

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

@ $3/ft 3 (nonshielded area)

Nm

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

4. INSTRUMENTATION AND CONTROLS

in item 1

5. ELECTRICAL SERVICE 1 1.5 2.5

6. SPARE PARTS 0.5 0.5 SUBTOTAL 7.4 36.7 44.1

7. CONTINGENCY .7 3.7 4.4 10%

8. TOTAL DIRECT COSTS 8.1 40.4 48.5

( (

K K K

ANNUAL OPERATING ANrMAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment Charcoal/HEPA Filtration System - Condenser Vacuum Pump (Sheet 2)

COST (1975 $1000)

'ueD TfllhI S...,iT*

RAmie FflQ tOI[IT F¢;TTMATF

I. OPERATING LABOR, SUPERVISION, neg used only during startup and shutdown AND OVERHEAD

2. MAINTENANCE MATERIAL AND 1.2 4 HEPA filters @ $150 & 2 Charcoal filters LABOR @ $900, change every 2 years

3. CONSUMABLES, CHEMICALS, AND initems 2 and 4 SUPPLIES

'.4

  • 0

4. UTILITIES AND SERVICES

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

5. TOTAL 0 AND M ANNUAL COST 1.4

_______________________ I _________ ________ _______________________________

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

DIRECT COST (1975 $1000)

FM FOIITDMFNTIMATPRTAI STTTflTAI BASIS FOR

  • FnCT VCTttMATO

I ARAR

ITEMP

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

$25K/H.P. turbine glands

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

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

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

5. ELECTRICAL SERVICE nag

6. SPARE PARTS 5 5 SUBTOTAL 74 195 269

7. CONTINGENCY 7 20 27 10%

8. TOTAL DIRECT COSTS 81 215 296 r r C

K K

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment Clean Steam to Turbine Glands (Sheet 2)

COST (1975 $1000)

1TR4 LABOR OTHER TOTAL BASIS FOR COST ESTIMATE

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

2. MAINTENANCE MATERIAL AND 4.0 40 man-days LABOR

3. CONSUMABLES, CHEMICALS, AND

SUPPLIES

9'

4. UTILITIES AND SERVICES

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

5. TOTAL 0 AND M ANNUAL COST 28.3

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

DIRECT COST (1975 $1000)

ITEM I AMII n:*.:TDAACLIMATDTai BASIS FOR

TnTAI

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

2. BUILDING ASSIGNMENT neg install in existing space

3. ASSOCIATED PIPING SYSTEMS - in item 1

0

i%1J

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

6. SPARE PARTS 5 SUBTOTAL 100 125 225

7. CONTINGENCY 10 12 22 10%

8. TOTAL DIRECT COSTS 110 137 247

( r

K -\

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM1 FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment Clean Steam to Steam Valves 24" and Larger (Sheet 2)

COST (1975 $1000)

TT!M LABOR OTHER TOTAL BASIS FOR COST ESTIMATE

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

2. MAINTENANCE MATERIAL AND 4.0 40 man-days LABOR

3. CONSUMABLES, CHEMICALS, AND neg SUPPLIES

w U,

4. UTILITIES hND SERVICES

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

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

DIRECT COST (1975 $1000)

BASIS FOR

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

COS ESTIMATE

TOTAL

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

2. BUILDING ASSIGNMENT - - neg

-* 3. ASSOCIATED PIPING SYSTEMS 40 20 60

.

w

.h 4.6.

INSTRUMENTATION AND CONTROLS 10 20 30 allowance

5. ELECTRICAL SERVICE - none

7.e

6. SPARE PARTS - 6 6 SUBTOTAL 50 166 216

7. CONTINGENCY 5 17 22 10%

8. TOTAL DIRECT COSTS 55 183 238 I (

K A K

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

COST (1975 $1000)

ITEM LABOR OTN!R TNTAI DA*f* *R r*eT r*w*a*P

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

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

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

-a U'

4. UTILITIES AND SERVICES

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

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

DIRECT COST (1975 $1000)

BASIS FOR

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

ERq~

r. flTl II Anna .r..

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

i-* ,

1. PROCESS EQUIPMENT 5 40.0 45.0 prefilter/HEPA @ $3/cfm, use existing fan BUILDING ASSIGNMENT 7 4.5 11.5 16' x 12' x 12' @ $5/ft 3

2.

(nonshielded area)

3. ASSOCIATED PIPING SYSTEMS 3 2.0 5.0

,o L.

a'

4. INSTRUMENTATION AND CONTROLS in item 1

5. ELECTRICAL SERVICE base

6. SPARE PARTS 0.5 0.5 SUBTOTAL 15 47.0 62.0

7. CONTINGENCY 1 5.0 6.0 10%

8. TOTAL DIRECT COSTS 16 52.0 68.0

( ( (

K T K !

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASrE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

DIRECT COST (1975 $1000)

BASIS FOR

COST ESTIMATE

lI TDMCWNT IMATrOAIC

I AflI TflTAL

ITEM !L___ f ______________

5 40.0 45.0 skid mounted filter housing

1. PROCESS EQUIPMENT w/o fans

3

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

2. BUILDING ASSIGNMENT 4.6 (nonshielded area)

3. 3 2.0 5.0

ASSOCIATED PIPING SYSTEMS

-I

4. in item 1 INSTRUMENTATION AND CONTROLS

5. base ELECTRICAL SERVICE

6. 0 0.5 0.5 SPARE PARTS

SUBTOTAL 12.6 44.8 57.4

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

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment 15,000-cfm HEPA Filtration System (Sheet 3)

COST (1975 $1000)

ITEM LABOR OTI4FR TflTAI RACTC Frn rncT FCTIMATC

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

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

CONSUMABLES, CHEMICALS, AND

I

3. in items 2 and 4 SUPPLIES

4. UTILITIES AND SERVICES

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

5. TOTAL 0 AND M ANNUAL COST 7.8 I_ (

K K

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment 1000-cfm Charcoal/HEPA Filtration System (Sheet 1)

DIRECT COST (1975 $1000)

BASIS FOR

I TEM LABOR EOUIPMENT/MATERIALS TOTAL COST ESTIMATE

I. PROCESS EQUIPMENT 2.0 22.0 24.0 prefllter/4" charcoal/HEPA

@ $20/cfm, 5 kw htr @ $400/kw BUILDING ASSIGNMENT 3.8 2.0 5.8 8' x 12' x 12' @ $5/ft 3

2.

(nonshielded area)

3. ASSOCIATED PIPING SYSTEMS 1.3 .7 2.0

0

4. INSTRUMENTATION AND CONTROLS in item 1

5. ELECTRICAL SERVICE 1.5 1.0 2.5

6. SPARE PARTS 0.5 0.5 SUBTOTAL 8.6 26.2 34.8

7. CONTINGENCY 1.0 2.0 3.0 10%

8. TOTAL DIRECT COSTS 9.6 28.2 37.8

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment 1000-cfm Charcoal/HEPA Filtration System (Sheet 2)

COST (1975 $1000)

ITEM LABOR OTHER TOTAL BASIS FOR COST £STII4ATF

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

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

1 charcoal @ $900 each every 2 yrs'

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

0

UTILITIES AND SERVICES

Waste Disposal .1 $50/HEPA or prefilter, $100/charcoal Water filter Steam Electricity neg Building Services Other

5. TOTAL 0 AND M ANNUAL COST 2.6

____________________________ ____________ I I

  • ( --

__ (

K K

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

DIRECT COST (1975 $1000)

BASIS FOR

TTVM LABOR EQUIPMENT/MATERIALS TOTAL COST ESTIMATE

ITE

LABO.....

COST ESTIMATE

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

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

2.

(nonshielded area)

3. ASSOCIATED PIPING SYSTEMS 3 2 5 a

4. INSTRUMENTATION AND CONTROLS - In Item 1

5. ELECTRICAL SERVICE 3 2 5 allowance

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

7. CONTINGENCY 3 9 12 10%

8. TOTAL DIRECT COSTS 31 97 128

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

DIRECT COST (1975 $1000)

I TEM CN "I lDMrLT ATEDIlA1 C BASIS FOR

I fuND T*TAi ITEM I_____

ARAL?~urIIn~LJIUL x flMrnR UI

t. IWUTflYAI

1.3

1. PROCESS EQUIPMENT 10.0 71.0 81.0 prefilter/4* charcoal/HEPA

@ $5/cfm, 30 kw htr

@ $200/kw BUILDING ASSIGNMENT 7.7 3.8 11.5 16' x 20' x 121 @ $3/ft 3

2.

(nonshielded area)

3. ASSOCIATED PIPING SYSTEMS 3.0 2.0 5.0

0

.rg

4. INSTRUMENTATION AND CONTROLS in item 1

5. ELECTRICAL SERVICE 3.0 2.0 5.0 allowance

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

7. CONTINGENCY 2.0 9.0 11.0 10%

8. TOTAL DIRECT COSTS 25.7 92.8 118.5

( r (

K K

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREAThENT

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment 15,O00-cfm Charcoal/HEPA Filtration System (Sheet 3)

COST (1975 $1000)

ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE

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

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

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

0

4. UTILITIES AND SERVICES

Waste Disposal 1.5 $S50/HEPA or prefilter, $100/charcoal Water Steam Electricity 1.3 8kw additional fan power for filter aP

Building Services 0.018.S/kw-hr Other

5. TOTAL 0 AND M ANNUAL COST 15.6

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

DIRECT COST (1975 $1000)

BASIS FOR

I ITU i ARng~

FoII PI4FNTII4ATFRIALS TOTAL COST ESTIMATE

-¶ a 1n FnrMN/AEIL

15 117.0 132.0 pref1lter/4" charcoal/HEPA

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

2. (nonshielded area)

3. ASOCIATED PIPING SYSTEMS 5 3.0 8.0 base a

4. INSTRUMENTATION AND CONTROLS - in item I

5. ELECTRICAL SERVICE 6 4.0 10.0 allowance

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

7. CONTINGENCY 5 14.0 19.0 10%

8. TOTAL DIRECT COSTS 51 156.6 207.6

( C

y K

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment 30,000-cfm Charcoal/HEPA Filtration System - Turbine Building (Sheet 2)

DIRECT COST (1975 $1000)

!OtITPHt¶!rT/ATrR TALS BASIS FOR

t*nlT F*TTMATF

ITEM LAROR TflTA[

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

@ $4/cfm, 60kw htr

@ $200/kw

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

3. ASSOCIATED PIPING SYSTEMS 3.0 5.0 8.0 base me

4. INSTRUMENTATION AND CONTROLS in item 1

5. ELECTRICAL SERVICE 6.0 4.0 10.0 allowance

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

7. CONTINGENCY 4.0 14.0 18.0 l0

8. TOTAL DIRECT COSTS 41.4 151.8 193.2

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment 30.00O-cfm Charcoal/HEPA Filtration System - (Sheet 3)

COST (1975 $1000)

ITEM LABOR OTHER TOTAL BASIS FOR £OST FSTTMATF

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

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

LABOR charcoal filters @ $900 each every 2 yrs

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

4. UTILITIES AND SERVICES

Waste Disposal 3.0 $50/HEPA or preftilter, $1007charcoal filter Water Steam Electricity 2.6 16kw additional fan HP for filter @

Building Services 0.018 S/ku-hr Other

5. TOTAL 0 AND M ANNUAL COST 27.4

- :- t--.-J"

ý:r __ C

K K

11 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

DIRECT COST (1975 $1000)

EOUJIPMFNTIMATFRIALS BASIS FOR

ITEM LABOR TflTAI rnCT CTMATC

TnIMNIAEIL 1 nA

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

-t + I

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

0

3. ASSOCIATED PIPING SYSTEM; - in item 1

-J

4. INSTRUMENTATION AND CONTROLS - in item 1

5. ELECTRICAL SERVICE 40 so 90

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

7. CONTINGENCY 34 56 90 10l

8. TOTAL DIRECT COSTS 374 614 988

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTE14 FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment Turbine Building Chilled Water HVAC System (Sheet 2)

COST (1975 $1000)

ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE

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

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

.0

3. CONSUMABLES, CHEMICALS, AND - initem 2 SUPPLIES

0

4. UTILITIES AND SERVICES

Waste Disposal Water 13.0 500 gpm @ 104/1000 gal & 50% load factor Steam Electricity 33.0 400 kw @ 0.018 $/kw hr Building Services Other S. TOTAL 0 AND M ANNUAL COST 69.3 C C r

K

I

K K

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT. SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

DIRECT COST (1975 $1000)

EOUIPMENT/MATERIALS BASIS FOR

I TFM LABOR TOTAL COST ESTIMATE

PROCESS EQUIPMENT 2.5 20 22.5 600-ft 3 , 150 pslgo C.S.,

ASME VIII

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

ASSOCIATED PIPING SYSTEMS 1.0 1 2.0 10% of item 1 INSTRUMENTATION AND CONTROLS neg ELECTRICAL SERVICE neg SPARE PARTS neg SUBTOTAL 21.5 30 51.5 CONTINGENCY 2.0 3 5.0 10%

TOTAL DIRECT COSTS 23.5 33 56.5

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

3 Description of Augment 600-ft Waste Gas Decay Tank (Sheet 2)

COST (1975 $1000)

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

AND OVERHEAD neg

2. MAINTENANCE MATERIAL AND

LABOR neg

3. CONSUMABLES, CHEMICALS, AND

0

SUPPLIES neg U'

0~e

4. UTILITIES AND SERVICES

Waste Disposal Water Steam neg Electricity Building Services Other

5. TOTAL 0 AND N ANNUAL COST neg

(

K K

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment PWR Hydrogen Recombiner (Sheet 1)

DIRECT COST (1975 $1000)

rflIITPMPINIMAT*RTAI

BASIS FOR

IT"M IARno TflTAI rnqT vtTTMATF

I l VT :fTI b V nA. I

1. PROCESS EQUIPMENT 50.0 300.0 350.0 skid mounted, catalytic type w/condenser, partial I&C

single unit, ASME VIII

BUILDING ASSIGNM4ENT 28.8 14.4 43.2 15' x 30' x 16' 0 $6/ft3

2.

(shielded area)

3. ASSOCIATED PIPING SYSTEMS 32.0 13.0 45.0 allowance a

Ue

4. INSTRUMENTATION AND CONTROLS 10.0 40.0 50.0 allowance

5. ELECTRICAL SERVICE 13.0 12.0 25.0 allowance

6. SPARE PARTS - 2.0 2.0

SUBTOTAL 133.8 381.4 515.2

7. CONTINGENCY 13.0 38.0 51.0 101

8. TOTAL DIRECT COSTS 146.8 419.4 566.2

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADtWASTE TREAThENT

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment PUR Hydrogen Recombiner (Sheet 2)

COST (1975 $1000)

ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE

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

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

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

SUPPLIES 7000 hrs Ca I

U'

4. UTILITIES AND SERVICES

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

K*

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

DIRECT COST (1975 $1000)

BASIS FOR

ITEM LABOR EOUIPMENT/MATERIALS TOTAL COST ESTIMATE

1*

1. PROCESS EQUIPMENT 3.0 7.5 10.5 chiller, heater, charcoal HEPA

3

2. BUILDING ASSIGNMENT 3.0 1.5 4.5 10' x 10' x 15' @ $3/ft (unshielded turbine bldg)

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

4. INSTRUMENTATION AND CONTROLS 0.5 1.5 2.0 allowance

5. ELECTRICAL SERVICE 0.5 0.5 1.0 allowance

6. SPARE PARTS 1.0 1.0

SUBTOTAL 9.0 13.0 22.0

7. CONTINGENCY 1.0 1.0 2.0 1O0

8. TOTAL DIRECT COSTS 10.0 14.0 24.0

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augnent PWR Air EJector Charcoal/HEPA Filtration Unit (Sheet 2)

COST (1975 $1000)

ITEM LARAR flTIFD TnTAI DAete * * rP*eUA*

.....________________

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

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

2. MAINTENANCE MATERIAL AND 2.0 includes replacement filter LABOR

3. CONSUMABLES, CHEMICALS, AND - in item 2 EP

SUPPLIES

U'

4. UTILITIES AND SERViCES

Waste Disposal neg Water Steam Electricity Building Services Other

5. TOTAL 0 AND M ANNUAL COST 5.8 K

K K

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

DIRECT COST (1975 $1000)

BASIS FOR

ITEM LABOR EQUIPMENT/MATERIALS TOTAL COST ESTIMATE

I. PROCESS EQUIPMENT - no equipment required

2. BUILDING ASSIGNMENT neg install In existing space

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

2 valves U't ull

4. INSTRUMENTATION AND CONTROLS 4 6 10 allowance

5. ELECTRICAL SERVICE neg

6. SPARE PARTS neg SUBTOTAL 17,, 13 30

7. CONTINGENCY 2 1 3 10%

8. TOTAL DIRECT COSTS 19 14 33

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREAThENT

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment Steam.Generator Flash Tank Vent to Main Condenser (Sheet 2)

COST (1975 $1000)

ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE

1. OPERATING LABOR, SUPERVISION, 1 allowance AND OVERHEAD

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

3. CONSUHABLES, CHEMICALS, AND neg

.a SUPPLIES

U'

4. UTILITIES AND SERVICES

Waste Disposal Water neg Steam Electricity Building Services Other

5. TOTAL 0 AND H ANNUAL COST 2

( (

K

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment lSqpm Evaporator (Sheet 1)

DIRECT COST (1975 $1000)

BASIS FOR

ITI'N I AnRO T*TA!

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

2. BUILDING ASSIGNMENT 68 34 102 evap & services 25' x 301 x 20'

@ $6/ft3 plus 2,000 ft3 increase in solid waste storage area a. 3. ASSOCIATED PIPING SYSTEMS 35 30 65 inludes service piping

4. INSTRUMENTATION AND CONTROLS 10 10 20 allowance

5. ELECTRICAL SERVICE 40 25 65 allowance

6. SPARE PARTS - 27 27 2% of item 1 plus tube bundle SUBTOTAL 183 351 534

7. CONTINGENCY 18 35 53 10%

8. TOTAL DIRECT COSTS 201 386 587

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREAThENT'SYSTEM

FOR LIGHT-WdATER-COOLED NUCLEAR REACTORS

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

DIRECT COST (1975 $1000)

tTrW BASIS FOR

rncT rCY?UAYT

I AfPtflD rfIITDfMlrTIMATrDTAI TnTA,

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

1. PROCESS EQUIPMENT 30 350 380 ASME VIII

skid mounted, submerged,

'tube bundle, Incoloy in contact with process fluid t

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

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

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

4. INSTRUMENTATION AND CONTROLS 10 10 20 allowance

5. ELECTRICAL SERVICE 40 25 65 allowance

6. SPARE PARTS 27 27 2% of Item 1 plus tube bundle SUBTOTAL 203 491 694

7. CONTINGENCY 20 49 69 1O0

8. TOTAL DIRECT COSTS 223 540 763 C C

K

'III

T

3)

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMErNT SYSTEM

(Sheet

50-gpmFOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

DIRECT COST (1975 $1000)

BASIS FOR

ITEM LABOR EOUIPMENT/MATERIALS TOTAL COST ESTIMATE

1. PROCESS EQUIPMENT 30 450 480 ASME VIII

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

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

3. ASSOCIATED PIPING SYSTEMS 35 35 70 allowance a

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

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

7. CONTINGENCY 21 60 81 10%

8. TOTAL- DIRECT COSTS 233 655 888

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

ITEM LABOR OT14ER TOTAL BASIS FOR LOST FSTIMATF

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

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

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

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

5. TOTAL 0 AND M ANNUAL COST 199 C C

K* K

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment Evaporator PWR Dirty Waste (Sheet 5)

COST (1975 $1000)

lTYM [AROR OTHER TOTAL BASIS FOR COST ESTTMATE

I. OPERATING LABOR, SUPERVISION,

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

2. MAINTENANCE MATERIAL AND

LABOR 30.0 7-1/2% of equipment cost

3. CONSUMABLES, CHEMICALS, AND - concentrate solidification chemicals

0'

SUPPLIES in item 4

4. UTILITIES AND SERVICES 3

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

5. TOTAL 0 AND MANNUAL COST 80.0

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment v

EvaDorator

- Condenser Polisher Chemical IaCto Ih +0A

COST (1975 $1000)

ITEM LAI*R NTH*D T*TAI

LABOR 0ATD AU .,* TC4TAI FRUK CS

LU ETIMATE

1. OPERATING LABOR, SUPERVISION,

AND OVERHEAD 6.0 650.000 gpy; 500 hr/yr labor

2. MAINTENANCE MATERIAL AND

LABOR 30.0 7-1/2% of equipment cost

3. CONSUMABLES, CHEMICALS. AND concentrate solidification chemicals

0 SUPPLIES In item 4

4. UTILITIES AND SERVICES

Waste Disposal

87.0 20:1 feed to concentrate ratio @ $20/ft 3 Wl7.0 disposal cost Water 6.5 1000 gpm 0 360 hrs @ 30/10OO gal Steam 14.4 360 hrs steam @ 20,000 lb/hr @ $2/1000 lbs Electricity Building Services Other

5. TOTAL 0 AND M ANNUAL COST 143.9

( C

K K

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

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

COST (1975. $1000)

TT!M LABOR OTHER TOTAL BASIS FOR COST ESTIMATE

I. OPERATING LABOR, SUPERVISION,

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

2. MAINTENANCE MATERIAL AND

LABOR 30.0 7-1/25 of equipment cost

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

LeD

4. WasteITsposal 8.6 50:1 feed to concentrate ratio 0 $20/ft 3 disposal cost Water 1.6 1000 gpm 0 90 hrs 0 30t/1000 gal Steam 3.6 90 hrs steam 0 20,000 lb/hr 1 $2/1000 lbs Electricity Building Services Other

5. TOTAL 0 AND MANNUAL COST 49.8

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment Evaporator Distillate Demineralizer (Sheet 1)

DIRECT COST (1975 $1000)

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

BASIS FOR

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

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

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

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

Ot

4. INSTRUMENTATION AND CONTROLS 2.0 3.0 5.0 remote conductivity readout

5. ELECTRICAL SERVICE neg

6. SPARE PARTS 1.0 1.0

SUBTOTAL 21.4 33.2 54.6

7. CONTINGENCY 2.0 3.0 5.0 10%

8. TOTAL DIRECT COSTS 23.4 36.2 59.6

( C (

)

K

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment Evaporator Distillate Demineralizer (Sheet 2)

COST (1975 $1000)

YtM I ARnlQ OTHER TOTAL BASIS FOR COST ESTIMATE

aI1II ____________

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

2. MAINTENANCE MATERIAL AND

LABOR 2.0 allowance

3. CONSUMABLES, CHEMICALS, AND

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

4. UTILITIES AND SERVICES

Waste Disposal 0.6 30 ft 3

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

5. TOTAL 0 AND M ANNUAL COST 6.7

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment 50-opDemintralzer Sh t 1)

{Sheet 1)

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

BASIS FOR

ITEM LAROR 1ITOM AUIFRAI It TIhTAI CflCY

1T

tMAr"

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

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

3. ASSOCIATED PIPING SYSTEMS 9 6.0 15.0 2" piping

4. INSTRUMENTATION AND CONTROLS 4 6.0 10.0

5. ELECTRICAL SERVICE No

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

7. CONTINGENCY 2 4.0 6.0 10%

8. TOTAL DIRECT COSTS 29 42.8 - 71.8

( C C

K K

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

DIRECT COST (1975 $1000)

FO*l PMFNT/MATFRTALS BASIS FOR

tT*M LANOR TOTAL COST FSTTMATF

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

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

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

.1

5. ELECTRICAL SERVICE neg

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

7. CONTINGENCY 3 6.0 9.0

B. TOTAL DIRECT COSTS 31 63.8 94.8

TOTAL DIRECT COST ESTIMATE SHEET OF RADWAST!E TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

(Sheet

200-gpm Oemtneraltzer DIRECT COST (1975 $1000)

EflUIPI4FNTII4ATFRTAL * BASIS FOR

ITEM LABOR TflTAI rnCT r~tTuATr

1T A

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

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

___(shielded area)

3. ASSOCIATED PIPING SYSTEMS 12 12.0 24.0 4" piping

4. INSTRUMENTATION AND CONTROLS 4 6.0 10.0

5. ELECTRICAL SERVICE neg

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

7. CONTINGENCY 3 9.0 12.0

8. TOTAL DIRECT COSTS 35 94.2 129.2

( (

K

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

DIRECT COST (1975 $1000)

BASIS FOR

I TrM lAROR EOUJIPMNT/MATERjALS TOTAL COST ESTIMATE

T I COST ESTIMATE

3

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

2.

(shielded area)

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

'a

4. INSTRUMENTATION AND CONTROLS 4 6.0 10.0 allowance

5. ELECTRICAL SERVICE neg

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

7. CONTINGENCY 4 9.0 13.0

8. TOTAL DIRECT COSTS 44 102.2 146.2

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment BWR - 2nd Waste Demineralizer In Serf es (Sheet El COST (1975 $1000)

ITEM lABOR NTNrD TJlTA!

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

aAeT*

DROIO

  • n* *

rvr uK EV)lr.1~PY.I

PP*guA*P

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

2. MAINTENANCE MATERIAL AND

LABOR 5.0 allowance

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

-.J

a

4. UTILITIES AND SERVICES

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

5. TOTAL 0 AND M ANNUAL COST 19.7 C

K I

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment Demineralizer - PWR Clean Wastes (Sheet 6)

COST (197k.$1000)

YYIPLu AILr nV IlV%

I am*o -

flTurD

lll_ __ _

?linI

Ifl, matie fflS EflM? rCTTMATe

&'flC I l bl *fll

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

AND OVERHEAD 30 min/day

2. MAINTENANCE MATERIAL AND

LABOR 5.0 allowance

3

3. CONSUMABLES,

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

4. UTILITIES AND SERVICES

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

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADIASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment Demineralizer - BWR Dirty Waste (Sheet 7)

COST (1975 $1000)

JTFN [ABDR nlTHVg TNlT61 DACIC mnD r.ncT reTvUnt I. OPERATING LABOR, SUPERVISION,

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

2. MAINTENANCE MATERIAL AND

LABOR 5.0 allowance CONSUNABLES, CHEMICALS, AND33

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

4. UTILITIES AND SERVICES

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

--- I C C

/

K

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment Demineraltzer - PWR Dirty. Wastes (w/o turbine building) (Sheet 8)

COST (1975 $1000)

ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE

l. OPERATING LABOR, SUPERVISION,

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

2. MAINTENANCE MATERIAL AND

LABOR 5.0 allowance

3. CONSUMABLES, CHEMICALS, AND

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

4. UTILITIES AND SERVICES

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

5. TOTAL 0 AND M ANNUAL COST 23.5

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

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

D*crlrintinn of Aujnmant flminapA147AP . DUo

  • 7m,
  • **,*,-* pww- - . T. * a w,*g uu,,*U-I
  • fm rC1 uVfm "a 1.411W4b 7I

COST (1975 $1000)

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

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

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

1. OPERATING LABOR, SUPERVISION.

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

2. MAINTENANCE MATERIAL AND

LABOR 5.0 allowance

3. CONSUMABLES, CHEMICALS, AND

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

4. UTILITIES AND SERVICES

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

( .-."(

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

........ r

K

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

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

COST (1975 $1000)

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

AND OVERHEAD 3.3 15 min/shift

2. MAINTENANCE MATERIAL AND

LABOR 5.0 allowance

3. CONSUMABLES, CHEMICALS, AN"

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

4. UTILITIES AND SERVICES

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

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

Ftlter (Sheet

20-qm Cartrtd9e DIRECT COST (1975 $1000)

TTFM I AI*fl2 vN Itur

¶ u'IIAqr rD lr e BASIS FOR

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

1. PROCESS EQUIPMENT 2.0 5.0 7.0 SS, ASME VIII, 150 psi BUILDING ASSIGNMENT 5.6 3.0 8.6 16' x 12' x 20' S $6/ft 3

2.

(shielded area)

3. ASSOCIATED PIPING SYSTEMS 1.5' 1.0 2.5 allowance

-. 4 Q

at 4. INSTRUMENTATION AND CONTROLS 0.6 2.4 3.0 allowance

5. ELECTRICAL SERVICE neg

6. SPARE PARTS 0.5 0.5 SUBTOTAL 9.7 11.9 21.6

7. CONTINGENCY 1.0 1.0 2.0 10%

8. TOTAL DIRECT COSTS 10.7 12.9 23.6

(

TREATMENT

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment Cartridge Filter (Sheet 2)

COST (1975 $1000)

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

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

4.5 10 changes @ 10 man-hrs/change

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

2. MAINTENANCE MATERIAL AND allowance

1.0

LABOR

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

1.0

SUPPLIES

4. UTILITIES AND SERVICES 3

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

8.0

5. TOTAL 0 AND MANNUAL COST

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREAT1ENT SYSTEM

i FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

1)

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

fIW01T

P~NT uI~dTIDTAI BASIS FOR

ITEM LARnR T*TAI

1. PROCESS EQUIPMENT 10 65.0 75 automated system 1 gpm/ft 2 ,

ASM4E VIII

BUILDING ASSIGNMENT 18 9.0 27 15' x 15' x 20' 0 $6/ft 3

2.

(shielded area)

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

0

4. INSTRUMENTATION AND CONTROLS in item 1

5. ELECTRICAL SERVICE 7 13.0 20 allowance

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

7. CONTINGENCY 5 10.0 15 10%

8. TOTAL DIRECT COSTS 56 108.0 164

( r

K K

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

2)

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

-vT

(Sheet DIRECT COST (1975 $1000)

BASIS FOR

TT*M LAROR EOUIPMENT/MATERIALS TOTAL COST ESTIMATE

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

1. ASME Viii

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

2. (shielded area)

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

-J

4. INSTRUMENTATION AND CONTROLS - - item I

5. ELECTRICAL SERVICE 12 18.0 30 allowance

6. SPARE PARTS - 3.0 3 SUBTOTAL 102 184.0 286

7. CONTINGENCY 10 18.0 28 10%

8. TOTAL DIRECT COSTS 112 202.0 314

ANNUAL OPERATING AND MAINTENANCE COST ESTI1ATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment Precoat Filter - BWR Dirty Waste (Sheet 3)

COST (1975 $1000)

ITEM LABOR OTHER TOTAL BASIS FOR COST !STTI4ATF

1. OPERATING LABOR, SUPERVISION,

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

2. MAINTENANCE MATERIAL AND

LABOR 10.0 allowance

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

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

( C

T K

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

DIRECT COST (1975 $1000)

BASIS FOR

TTIFM LABOR FOUlPMENTIMATFRIALS TOTAL COST ESTIMATF

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

feed tank, ASME VIII

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

3. ASSOCIATED PIPING SYSTEMS 3.0 2.0 5.0 allowance

0

4. INSTRUMENTATION AND CONTROLS in item I

5. ELECTRICAL SERVICE 7.0 13.0 20.0 allowance

6. SPARE PARTS 6.0 6.0

SUBTOTAL 35.2 90.6 125.8

7. CONTINGENCY 3.0 9.0 12.0 10%

8. TOTAL DIRECT COSTS 38.2 99.6 137.8

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment Reverse Osmosis - Detergent Wastes COST (1975 $1000)

ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE

1. OPERATING LABOR, SUPERVISION,

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

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

3. CONSUMABLES, CHEMICALS. AND

SUPPLIES neg No

4. UTILITIES AND SERVICES

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

5. TOTAL 0 AND MANNUAL COST 16.2

( r C

1)

TOTAL DIRECT (Sheet COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

DIRECT COST (1975 $1000)

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

?tTrM I AROR TOTAL COST ESTIMATE

T -

3 28 31 SS, ASME VIII, atmospheric

1. PROCESS EQUIPMENT

service, 200°F

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

2.

(shielded area)

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

w 4. INSTRUMENTATION AND CONTROLS 4 6 10 allowance

5. ELECTRICAL SERVICE neg

6. SPARE PARTS neg SUBTOTAL 39 s0 89

7. CONTINGENCY 4 5 9 10%

8. TOTAL DIRECT COSTS 43 55 98

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREAThENT

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment 10000-Gallon Tank (Sheet 2)

COST (1975 $1000)

ITEM LABOR OTHER TOTAL RA~l flD rfl*T r*TUATr

1. OPERATING LABOR, SUPERVISION.

AND OVERHEAD 1.1 5 min/shift - log level readings

2. MAINTENANCE MATERIAL AND

LABOR 1.6 1/2% of equipment

3. CONSUMABLES. CHEMICALS, AND neg SUPPLIES

4. UTILITIES AND SERVICES

Waste Disposal Water Steam neg Electricity Building Services Other

5. TOTAL 0 AND N ANNUAL COST 2.7

(

REFERENCES TO APPENDIX B

NUS-531,

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

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

- 2000,"

3. "Projections of Labor Requirements for Electric Power Plants Construction, 1974 USAEC Report WASH-1334, Washington, D.C., August 1974.

1.110-85

APPENDIX C

DATA NEEDED FOR RADIIASTE TREATMENT SYSTEM

COST-BENEFIT ANALYSIS FOR LIGHT-WATER

COOLED NUCLEAR REACTORS

This appendix describes information that should be submitted in support of radwaste treat ment system cost-benefit analyses for light-water-cooled nuclear reactors. The information should be consistent with the contents of the Safety Analysis Report (SAR) and Environmental Report (ER) for the proposed reactor. Appropriate sections of the SAR and ER containing more detailed discussions of the required information should be referenced as appropriate. Each response, however, should be Independent of the ER and SAR. All responses should be on a per reactor basis and should provide the following information:

1. Detailed cost estimate sheets similar to those shown on the following pages listing all parameters (and their bases) used in determining capital, operating, and maintenance costs associated with all augments considered in the cost-benefit analysis. All costs should be stated in terms of 1975 dollars.

2. The cost of borrowed money used in the cost analysis and the method of arriving at this cost.

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

a. Decontamination factors assigned to each augment and fraction of "on-line" time assumed, i.e., hours per year used.

b. Parameters and method used to determine the Indirect Cost Factor and the Capital Recovery Factor.

1.110-87

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE'TREATMENT-SYSTEH

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment DIRECT COST (1975 $1000)

BASIS FOR

i Tru 1 AflfD

FflIIIPMFNT/MATFRlALS TOTAL COST ESTIMATE

i aunD EnUTPMENTIMATERIALS

1. PROCESS EQUIPMENT

t I 1 I

2. BUILDING ASSIGNMENT

I I I I

0 3. ASSOCIATED PIPING SYSTEMS

I I I I --

4. INSTRUMENTATION AND CONTROLS

I I I I

S. ELECTRICAL SERVICE

I I I I

6. SPARE PARTS

______________________I i mI

SUBTOTAL

________________________________________________________ 1 -I I I

7. CONTINGENCY

I I I

8. TOTAL DIRECT COSTS

________________________________________________________ ________________ I __________________________________________________ _____________ _______________________________________________

( C C

K

0

"I

U

2 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT

2

-4 SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

U

2

2 Description of Augment C,

a

9 COST (1975 $1000)

9 I TIFM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE

'a ITEM

w

-J

04

1. OPERATING LABOR, SUPERVISION,

AND OVERHEAD

0.j

'a

"4 a.

0

"4

2. MAINTENANCE MATERIAL AND

LABOR

U3.

4.

CONSUMABLES,

SUPPLIES

CHEMICALS, AND

UTILITIES AND SERVICES

Waste Disposal Water Steam Electricity Building Services Other

5. TOTAL 0 AND M ANNUAL COST


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