Regulatory Guide 1.110: Difference between revisions

From kanterella
Jump to navigation Jump to search
(Created page by program invented by StriderTol)
(Created page by program invented by StriderTol)
Line 1: Line 1:
{{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 L
| 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 2013OFFICE OF NUCLEAR REGULATORY RESEARCH
{{#Wiki_filter:U.S. NUCLEAR REGULATORY  
Revision 1 REGULATORY GUIDE
COMMISSION  
    Written suggestions regarding this guide or development of new guides may be submitted through the NRC's public Web site under the Regulatory Guides document collection of the NRC Library at http://www.nrc.gov/reading-rm/doc-collections/reg-guides/contactus.html.  Electronic copies of this regulatory guide, previous versions of this guide, and other recently issued guides are available through the NRC's public Web site under the Regulatory Guides document collection of the NRC Library at http://www.nrc.gov/reading-rm/doc-collections/. The regulatory guide is also available through the NRC's Agencywide Documents Access and Management System (ADAMS) at http://www.nrc.gov/reading-rm/adams.html, under ADAMS Accession No. ML13241A052.
REGULATORY
GUIDE OFFICE OF STANDARDS
DEVELOPMENT
REGULATORY  
GUIDE 1.110 COST-BENEFIT
ANALYSIS FOR RADWASTE S LIGHT-WATER-COOLED
NUCLEAR PDWE& CRS'March 1976 4 USNRC REGULATORY
GUIDES Commen.l shoutd be Sent to Rhe Secretary of the Comm,ssion U S Nuclea, %equietoy Guido* ate issued to describe and meeks ovelablto ,he pubic Rogulstory Comminssion Washington.


REGULATORY GUIDE 1.110
0 C 2065. Attention Docketing end methods acceptable go the NRC staff of4 impementing specific pairt of the S Commission'&
COST-BENEFIT ANALYSIS FOR RADWASTE SYSTEMS FOR
fegulatione.
LIGHT-WATER-COOLED NUCLEAR POWER REACTORS


==A. INTRODUCTION==
to definetel technique mused by the state in evild The guides are issued in the following ten broad divisions at"ig *pecific problems or postulated accidents.
Purpose  The U.S. Nuclear Regulatory Commission (NRC) staff has developed a series of guides that provide methods acceptable to the staff for calculating effluent releases, dispersion of effluents in the atmosphere and different water bodies, associated radiation doses to man, and cost-benefit aspects of treating radwastes.  This regulatory guide describes methods and procedures that the staff of the NRC considers acceptable for performing a cost-benefit analysis for liquid and gaseous radwaste system components for light-water-cooled nuclear power reactors.


Applicable Rules and 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, can-for a favorable cost-benefit ratio-lead to reductions in dose to the population reasonably expected to be within an 80 kilometers (50 miles) of the reactor.  Values of $1,000 per man-rem (roentgen equivalent man) and $1,000 per man-thyroid-rem are given as interim criteria pending the development and establishment of better criteria.  Compliance with Section II.D of Appendix I to 10 CFR Part 50 (which specifically addresses doses to the population) and Sections II.A, II.8, and II.C (which address doses to nearby individuals) is required to meet the criterion, "as low as is reasonably achievable."
0r to provide guidance to eppli cents Regulatory Gudes am not substitutes for regulamons.


The procedures and models provided in this guide will be subject to continuing review by the staff with the aim of providing greater flexibility to the applicant or licensee in meeting the requirements of Appendix I.  As a result of such reviews, it is expected that alternative acceptable methods for Rev. 1 of RG 1.110, Page 2 calculation will be made available to applicants or licensees, and that calculational procedures found to be unnecessary will be eliminated. Related Guidance Regulatory Guide 1.109, "Calculation of Annual Doses to Man from Routine Releases of Reactor Effluents for the Purpose of Evaluating Compliance with 10 CFR Part 50, Appendix I" (Ref. 2), describes methods for the calculation of preoperational estimates of effluents releases, dispersion of the effluent in the atmosphere and different water bodies, and estimation of the associated radiation doses to man. It also suggests parameters for the estimation of radiation doses to man from effluent releases.
end compliance I Power Reactors 5 Products with thenm ile rot reCed Methods end soutione diflerent fron those get out i I Research end Test Reactors 7 Tronsponstion Ihe guidell we be acceptable It they provide a bahis for lthe findings requrlit to 3 Fueuls and Materiels Facilities a Occupolionat
4palt h the mesnee of -permst of Scenes by the Commitssion
4 Environmental and Siting 2 Antitrust Review Commentd Isid uggestiOi$e
#0F imPtoSetfitC
it #hbae gtaldel We entcouraged S Materialt end Plant Protection
10 General ot anll. end guidss Wil be Revised. a. a41pp1rop1riete.


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


Regulatory Guide 1.112, "Calculation of Releases of Radioactive Materials in Gaseous and Liquid Effluents from Light-Water-Cooled Power Reactors" (Ref. 4), references NUREG-0016, "Calculation of Releases of Radioactive Materials in Gaseous and Liquid Effluents from Boiling-Water Reactors (BWR-GALE Code)," and NUREG-0017, "Calcula tion of Releases of Radioactive Materials in Gaseous and Liquid Effluents from Pressurized-Water Reactors (PWR-GALE Code)," to provide methods for calculating annual average expected releases of radioactive material in gaseous and liquid effluents from light-water-cooled nuclear power reactors.
will be divisions desired to the U S Nuclear Regulators Commission Wshtington
0 C ticfady orssIul Mt evaluating the teed = of an srly viision 20566. Attention Director.


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.
Office of Standerde Development TABLE OF CONTENTS Page


Purpose of Regulatory Guides
==A. INTRODUCTION==
.......................................................................
1.110-5


The NRC issues regulatory guides to describe to the public methods that the staff considers acceptable for use in implementing specific parts of the agency's regulations, to explain techniques that the staff uses in evaluating specific problems or postulated accidents, and to provide guidance to applicants and licensees. Regulatory guides are not substitutes for regulations and compliance with them is not required. Methods and solutions that differ from those set forth in regulatory guides will be deemed acceptable if they provide a basis fo r the findings required for the issuance or continuance of a permit or license by the Commission.
==B. DISCUSSION==
 
R
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.
1.110-5 C. REGULATORY
 
POSITION .........................................................
Rev. 1 of RG 1.110, Page 3 TABLE OF CONTENTS
1.110-6 D. IMPLE14ENTATION
Page 
................................
..................................
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==
==A. INTRODUCTION==
...............................................................................................................
Section I1.D of Appendix I, "Numerical Guides for Design Objectives and Limiting Conditions for Operation to Meet the Criterion
.................... 1 Purpose .......................................................................................................................
'As Low As Is Reasonably Achievable'
.................. 1 Applicable Rules and Regulations ............................................................................................... 1 Related Guidance ..............................................................................................................
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.
........... 2 Purpose of Regulatory Guides ..................................................................................................
... 2 Paperwork Reduction Act .......................................................................................................
..... 2


==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 ...........................................................................................................
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.
.......... 4 Background ....................................................................................................................
.............. 4 Harmonization with International Standards ............................................................................... 4 C. STAFF REGULATORY GUIDANCE ..................................................................................................
.. 4


==D. IMPLEMENTATION==
This regulatory guide describes a method for performing a cost-benefit analysis for liquid and gaseous radwaste system components.
.............................................................................................................
................. 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
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.
Page A-1 Electric Power Supply Areas in the United States ....................................................................... A-
9 Rev. 1 of RG 1.110, Page 4


==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.


Background Each applicant for a permit to construct or a li cense to operate a light-water-cooled nuclear power reactor and each holder of a license to operate a light-water-cooled nuclear power reactor is required to provide reasonable assurance that the design objectives for as low as is reasonably achievable effluent releases are satisfied by the initial liquid and gaseous radwaste system designs at the time of licensing and, if these designs are subsequently modified, that the design objectives are reassessed to ensure that they are maintained.  It is the objective of this guide to provide an acceptable method of performing cost-benefit analysis, in conformance with Section II.D of Appendix I to 10 CFR Part 50, to demonstrate that the plant design includes all items of reasonably demonstrated technology for reducing the cumulative population dose caused by releases of radioactive materials from the reactor to levels as low as reasonably achievable.  As an interim measure, the Commission chose values of $1,000 per-man-rem and $1,000 per man-thyroid-rem (or lesser values if demonstrated to be suitable for a particular site) to be used to implement the cost-benefit analysis.
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 proce dures for including the effects of inflation in the analysis, the NRC staff's analysis is based on 1975 dollars; i.e., neither the costs nor the interim criteria are escalated for the predicted effects of inflation.  Since the worth of a man-rem or man-thyroid-rem to the public is subject to the same fluctuations in value as the cost of equipment to reduce radioactive emissions, the NRC staff believes this approach to be reasonable.
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.


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
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.


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.
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.


Harmonization with International Standards
The methodology and cost parameters are presented in Appendix A to this guide. The costs presented.


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.
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.


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


license to operate a light-water-cooled nuclear power reactor should demonstrate by means of a cost-benefit analysis that further reductions to the cumulative dose to the population within an 80-kilometer (50-mile) radius of the reactor site cannot be effected at an annual cost of $1,000 per man-rem or $1,000 per man-thyroid-rem (or such lesser costs as demonstrated to be suitable for a particular case). 
Liquid and gaseous radwaste system augments considered in the analysis should be selected in order of diminishing cost-benefit returns.
Rev. 1 of RG 1.110, Page 5
2. The cost-benefit analysis should consider the reduction in releases of radioactive material from all effluent pathways.  Liquid and gaseous radwaste system augments considered in the analysis should be selected in order of diminishing cost-benefit returns.


3. All costs should be given in terms of 1975 dollars (as is the $1,000 per man-rem cost with which they are compared). Allowances for inflation after 1975 should not be factored into the cost estimates.
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.
4. The method of calculation described in Appendix A and the parameters presented in Appendix B of this guide are acceptable to the NRC staff for performing the cost-benefit analysis.


5. In support of the cost-benefit analysis, the applicant or licensee should provide a complete evaluation, including methodology used, components considered, and all assumptions and parameters used.  Information to be submitted by the applicant or licensee is described in Appendix C to this guide. Use of parameters, assumptions, and models different from those given in Appendices A and B to this guide may result in differences between the evaluations by applicants or licensees and those by the NRC staff.  Because of this, these parameters and assumptions should be clearly described and substantiated by the applicant or licensee.
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.
 
==D. IMPLEMENTATION==
The purpose of this section is to provide information on how applicants and licensees
~1 may use this guide and information regarding the NRC's plans for using this regulatory guide.  In addition, it describes how the NRC staff complies with 10 CFR 50.109, "Backfitting," and any applicable finality provisions in 10 CFR Part 52, "Licenses, Certifications, and Approvals for Nuclear Power Plants." 
Use by Applicants and Licensees Applicants and licensees may voluntarily
~2 use the guidance in this document to demonstrate compliance with the underlying NRC regulations.  Methods or solutions that differ from those described in this regulatory guide may be deemed acceptable if they provide sufficient basis and information for the NRC staff to verify that the proposed alternative demonstrates compliance with the appropriate NRC regulations.  Current licensees may continue to use guidance the NRC found acceptable for complying with the identified regulations as long as their current licensing basis remains unchanged.
 
Licensees may use the information in this regulatory guide for actions that do not require NRC review and approval such as changes to a facility design under 10 CFR 50.59, "Changes, Tests, and Experiments."  Licensees may use the information in this regulatory guide or applicable parts to resolve regulatory or inspection issues.


1  In this section, "licensees" refers to licensees of nuclear power plants under 10 CFR Parts 50 and 52; and the term "applicants" refers to applicants for licenses and permits for (or relating to) nuclear power plants under 10 CFR Parts 50 and 52 and applicants for standard design approvals and standard design certifications under 10 CFR Part 52.
===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.


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.
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:  
Rev. 1 of RG 1.110, Page 6 Use by NRC Staff The NRC staff does not intend or approve any imposition or backfitting of the guidance in this regulatory guide.  The NRC staff does not expect any existing licensee to use or commit to using the guidance in this regulatory guide, unless the licensee makes a change to its licensing basis.  The NRC staff does not expect or plan to request licensees to voluntarily adopt this regulatory guide to resolve a generic regulatory issue.  The NRC staff does not expect or plan to initiate NRC regulatory action that would require the use of this regulatory guide.  Examples of such unplanned NRC regulatory actions include issuance of an order requiring the use of the regulatory guide, requests for information under 10 CFR 50.54(f) as to whether a licensee intends to commit to use of this regulatory guide, generic communication, or promulgation of a rule requiring the use of this regulatory guide without further
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.
 
backfit consideration.
 
During regulatory discussions on plant-specific operational issues, the staff may discuss with licensees various actions consistent with staff positions in this regulatory guide as one acceptable means of meeting the underlying NRC regulatory requirement.  Such discussions would not ordinarily be considered backfitting even if prior versions of this regulatory guide are part of the licensing basis of the facility.  However, unless this regulatory guide is part of the licensing basis for a facility, the staff may not represent to the licensee that the licensee's failure to comply with the positions in this regulatory guide constitutes a violation.
 
If an existing licensee voluntarily seeks a license amendment or change and (1) the NRC staff's consideration of the request involves a regulatory issue directly relevant to this new or revised regulatory guide and (2) the specific subject matter of this regulatory guide is an essential consideration in the staff's determination of the acceptability of the licensee's request, then the staff may request that the licensee either follow the guidance in this regulatory guide or provide an eq uivalent alternative process that demonstrates compliance with the underlying NRC regulatory requirements.  This is not considered backfitting as defined in 10 CFR 50.109(a)(1) or a violation of any of the issue finality provisions in 10 CFR Part 52.
 
If a licensee believes that the NRC is either using this regulatory guide or requesting or requiring the licensee to implement the methods or processes in this regulatory guide in a manner inconsistent with the discussion in this Implementation section, then the licensee may file a backfit appeal with the NRC in accordance with the guidance in NUREG-1409, "Backfitting Guidelines" (Ref. 6), and the NRC Management Directive 8.4, "Management of Facility-Specific Backfitting and Information Collection" (Ref. 7). 
Rev. 1 of RG 1.110, Page 7 REFERENCES
~3  1. Code of Federal Regulations (CFR), Title 10, "Energy," Part 50, "Domestic Licensing of Production and Utilization Facilities."
 
2. U.S. Nuclear Regulatory Commission (NRC), Regulatory Guide 1.109, "Calculation of Annual Doses to Man from Routine Releases of Reactor Effluents for the Purpose of Evaluating Compliance with 10 CFR Part 50, Appendix I," Washington, DC.
 
3. NRC, Regulatory Guide 1.111, "Methods for Estimating Atmospheric Transport and Dispersion of Gaseous Effluents in Routine Releases from Light-Water-Cooled Reactors," Washington, DC.
 
4. NRC, Regulatory Guide 1.112, "Calculation of Re leases of Radioactive Materials in Gaseous and Liquid Effluents from Light-Water-Cooled Power Reactors," Washington, DC.
 
5. NRC, Regulatory Guide 1.113, "Estimating Aquatic Dispersion of Effluents from Accidental and Routine Reactor Releases for the Purpose of Implementing Appendix I," Washington, DC.
 
6. NRC, NUREG-1409, "Backfitting Guidelines," Washington, DC.
 
7. NRC, Management Directive 8.4, "Management of Facility-specific Backfitting and Information Collection," Washington, DC.
 
3. Publicly available NRC-published documents are available electronically through the NRC Library on the NRC's public Web site at http://www.nrc.gov/reading-rm/doc-collections/ and through the NRC's Agencywide Documents Access and Management System (ADAMS) at http://www.nrc.gov/reading-rm/adams.html.  The documents can also be viewed online or printed for a fee in the NRC's Public Document Room (PDR) at 11555 Rockville Pike, Rockville, MD.  For problems with ADAMS, contact the PDR staff at 301-415-4737 or 800-397-4209; or e-mail pdr.resource@nrc.gov.
 
Appendix A to RG 1.110, Page A-1 APPENDIX A
  PROCEDURES FOR PERFORMING COST-BENEFIT ANALYSES
This appendix contains guidance for performing cost-benefit analyses on individual system augments, as well as the parameters needed for estimating costs.  The bases for the parameters and worksheets appropriate for use with the following cost-benefit procedure are given in Appendix B.
 
1. The cumulative population man-rem (roentgen equivalent man) exposure and man-thyroid-rem exposure should be determined for each effluent release source (e.g., liquid radwaste releases, ventilation releases, etc.)
2. Potential reductions to the cumulative population exposure should be determined based on the addition of items of reasonably demonstrated technology that have the potential to reduce releases of radioactive materials.
 
3. Acceptable methods for performing some of the cal culations needed for items 1 and 2 above are contained in Regulatory Guides 1.109, "Calculation of Annual Doses to Man from Routine Releases of Reactor Effluents for the Purpose of Evaluating Compliance with 10 CFR Part 50, Appendix I," and 1.111, "Methods for Estimating Atmospheric Transport and Dispersion for Gaseous Effluents in Routine Releases from Light-Water-Cooled Reactors." They are also included in two regulatory guides now in preparation on the subjects of (1) calculation of releases of radioactive materials in liquid and gaseous effluents from light-water-cooled reactors and (2) methods for estimating aquatic dispersion of liquid effluents from routine reactor releases for the purpose of implementing Appendix I.
 
4. The total annual cost of each augment considered in item 2 above should be determined as follows: a. The Total Direct Cost (TDC):  
(1) Obtain the direct cost of equipment and materials from Table A-1.
 
(2) Multiply the direct labor cost obtained from Table A-1 by the appropriate labor cost correction factor from Table A-4 to obtain the corrected labor cost for the geographical area (from Figure A-l) in which the plant is to be built.
 
(3) Add the costs obtained from steps (1) and (2) to obtain the TDC.
 
b. Obtain-the appropriate Indirect Cost Factor (ICF) from Table A-5.
 
c. Determine Total Capital Cost (TCC) by using the equation:  
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  
Appendix A to RG 1.110, Page A-2 f. Obtain the Annual Operating Cost (AOC) and the Annual Maintenance Cost (AMC) from Tables A-2 and A-3. Multiunit sites using shared radwaste systems should multiply the AOC by the number of reactors sharing the augment.


g. Determine the Total Annual Cost (TAC) by using the equation:  
g. Determine the Total Annual Cost (TAC) by using the equation:  
TAC = AFC + AOC + AMC  
TAC
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.
* 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.
6. The system should be augmented with any items for which the TAC from item 4.g above is less than the value calculated in item 5, in the order of diminishing cost-benefit.


Table A-1.  Direct Costs-Gaseous Radwaste Augments, Liquid Radwaste Augments  DIRECT COSTS
1.110-7 TABLE A-1 DIRECT COSTS -GASEOUS RADWASTE AUGMENTS Direct- Costs (1975 $1000) Equipment/Material Labor Total BWR Offgas Recombiner  
-GASEOUS RADWASTE AUGMENTS  
553 255 808 3-ton Charcoal Adsorber 53 14 67 Desiccant Dryer 218 176 394 Charcoal Vault Refrigeration  
EQUIPMENT/ MATERIAL LABOR (1975 $1,000)TOTAL BWR Offgas Recombiner 553 255 808 3-ton Charcoal Adsorber 53 14 67 Desiccant Dryer 218 176 394 Charcoal Vault Refrigeration 116 38 154 Main Condenser Vacuum Pump Charcoal/  
116 38 154 Main Condenser Vacuum Pump Charcoal/HEPA
HEPA Filtration System 40 8 48 Clean Steam to Turbine Glands 81 215 296 Clean Steam to Steam Valves, 24" and Larger 137 110 247 Clean Steam to Steam Valves, 21/2" and Less Than 24" 183 55 238 15,000-cfm HEPA Filtration System 52(49)
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  
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)  
Filtration System 28 10 38 15,000-cfm Charcoal/HEPA  
Turbine Bldg. Chilled Water HVAC System 614 374 988  
Filtration System 97(93) 31(26) 128(119) 30,000-cfm Charcoal/HEPA  
600-ft 3 Gas Decay Tank 33 24 57 Appendix A to RG 1.110, Page A-3 DIRECT COSTS
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  
-GASEOUS RADWASTE AUGMENTS
419 147 566 PWR Air Ejector Charcoal/HEPA  
EQUIPMENT/ MATERIAL LABOR (1975 $1,000)TOTAL PWR Hydrogen Recombiner 419 147 566 PWR Air Ejector Charcoal/HEPA Filtration Unit 14 10 24 Steam Generator Flash Tank Vent to Main  
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.
Condenser 19 14 33 a. In cases where the equipment may be located either in the auxiliary building or the turbine building and common usage does not indicate a definite preference of one location or the other, cost for both locations are listed with the turbine building location cost in parenthesis. Direct Costs-Liquid Radwaste Augments EQUIPMENT/ MATERIAL LABOR (1975 $1,000)TOTAL 15-gpm Evaporator 386 201 587 30-gpm Evaporator 540 223 763 50-gpm Evaporator  655 233 888 Evaporator Distillate Demineralizer  36 24 60 50-gpm Demineralizer  43 29 50 100-gpm Demineralizer  64 31 95 200-gpm Demineralizer  94 35 129 400-gpm Demineralizer  102 44 146 100-gpm Precoat Filter 108 56 164 400-gpm Precoat Filter 202 112 314 20-gpm Cartridge Filter  13 11 24 2-gpm Reverse Osmosis  100 38 138 10,000-gal Tank 55 43 98
 
Appendix A to RG 1.110, Page A-4 Table A-2.  Annual Operating Costs-Gaseous Radwaste Augments, Liquid Radwaste Augments Annual Operating Costs a-Gaseous Radwaste Augments TOTAL OPERATING COST (1975 $1,000/YR) BWR Offgas Recombiner  3 3-ton Charcoal Adsorber neg Desiccant Dryer 3 Charcoal Vault Refrigeration 4 Main Condenser Vacuum Pump Charcoal/HEPA Filtration System 0.4 Clean Steam to Turbine Glands 24 Clean Steam to Steam Valves, 24" and Larger 3 Clean Steam to Steam Valves, 2-1/2" and Less Than 24" 3 15,000-cfm HEPA Filtration System 6 1,000-cfm Charcoal/HEPA Filtration System 2 15,000-cfm Charcoal/HEPA Filtration System 7 30,000-cfm Charcoal/HEPA Filtration System 9 Turbine Bldg. Chilled Water HVAC System 49
600-ft 3 Gas Decay Tank neg PWR Hydrogen Recombiner 4 PWR Air Ejector Charcoal/HEPA Filtration Unit 4 Steam Generator Flash Tank Vent to Main Condenser 1 Annual Operating Costs-Liquid Radwaste Augments TOTAL OPERATING COST (1975 $1,000/YR) Evaporation-PWR Dirty Waste 50 Evaporation-BWR Dirty Waste 169 Evaporation-Condensate Polisher Chemical Waste 114  Evaporation-Detergent Waste 20  Demineralization-Evaporator Distillate  5 Appendix A to RG 1.110, Page A-5 Annual Operating Costs-Liquid Radwaste Augments TOTAL OPERATING COST (1975 $1,000/YR) Demineralization-BWR 2nd Waste Demineralizer in Series 15 Demineralization-PWR Clean Waste 5 Demineralization-BWR Dirty Waste 88 Demineralization-PWR Dirty Waste 18 Demineralization-PWR Turbine Bldg. Drains 95 Demineralization-PWR Steam Generator Blowdown 25 Precoat Filter-BWR Dirty Waste 53 Cartridge Filter  7 Reverse Osmosis-Detergent Waste  7 10,000-gal Tank 1 a. Operating costs are given for a single reactor.  Operating costs for augments in shared radwaste systems should be multiplied by the number of reactors serviced by the augment. Table A-3.  Annual Maintenance Costs-Gaseous Radwaste Augments, Liquid Radwaste Augments ANNUAL MAINTENANCE COSTS
-GASEOUS RADWASTE AUGMENTS
TOTAL OPERATING COST (1975 $1,000/YR) BWR Offgas Recombiner  20 3-ton Charcoal Adsorber neg Desiccant Dryer 6 Charcoal Vault Refrigeration 3 Main Condenser Vacuum Pump Charcoal/HEPA Filtration System 1 Clean Steam to Turbine Glands 4 Clean Steam to Steam Valves, 24" and Larger 4 Clean Steam to Steam Valves, 2-1/2" and Less Than 24" 12 15,000-cfm HEPA Filtration System 2 1,000-cfm Charcoal/HEPA Filtration System 0.6 15,000-cfm Charcoal/HEPA Filtration System  9 Appendix A to RG 1.110, Page A-6 ANNUAL MAINTENANCE COSTS
-GASEOUS RADWASTE AUGMENTS
TOTAL OPERATING COST (1975 $1,000/YR) 30,000-cfm Charcoal/HEPA Filtration System 18 Turbine Bldg. Chilled Water HVAC System 20
600-ft 3 Gas Decay Tank neg PWR Hydrogen Recombiner 10 PWR Air Ejector Charcoal/HEPA Filtration Unit 2 Steam Generator Flash Tank Vent to Main Condenser 1 Annual Maintenance Costs -Liquid Radwaste Augments 15-gpm Evaporator  30 30-gpm Evaporator 30 50-gpm Evaporator 30 Evaporator Distillate Demineralizer  2 50-gpm Demineralizer 5 100-gpm Demineralizer 5 200-gpm Demineralizer  5 100-gpm Precoat Filter  10 400-gpm Precoat Filter  10 20-gpm Cartridge Filter 1 2-gpm Reverse Osmosis  9 10,000-gal Tank 2 Appendix A to RG 1.110, Page A-7 Table A-4.  Labor Cost Correction Factors
~a FPC~b GEOGRAPHIC
REGION LABOR COST
CORRECTION FACTOR
I 1.6 II 1.5 III 1.0 IV 1.4 V 1.1 VI 1.2 VII 1.3 VIII 1.2 a. See Appendix B, "Labor Cost Correction Factors."
b. See Figure A-1. Table A-5.  Indirect Cost Factors TYPE RADWASTE SYSTEM INDIRECT COST FACTOR 
1. Single unit site, unitized
~a radwaste system  1.75 2. Multiunit site, shared radwaste system  1.75
3. Multiunit site, unitized a radwaste system n 5.1)1 n (75.1+ where n is the number of unitized radwaste systems at the site a. Each reactor has a separate, nonshared radwaste system.
 
Appendix A to RG 1.110, Page A-8 Table A-6.  Capital Recovery Factors COST OF MONEY  (% PER YEAR, I) CAPITAL RECOVERY FACTOR
a 5  0.0651 6  0.0726 7  0.0806 8  0.0888 9  0.0973 10  0.1061 11  0.1150 12  0.1241 13  0.1334 14  0.1428 15 0.1523 a. Based on a service life of 30 years and the following equation:
CRF = 1 30)i 1 (30)i 1 (i++ 
  Appendix A to RG 1.110, Page A-9 Figure A-1.  Electric Power Supply Areas in the United States Appendix B to RG 1.110, Page B-1 APPENDIX B
  BASES FOR PARAMETERS US
ED IN PERFORMING COST-BENEFIT ANALYSIS
This appendix contains detailed cost estimate sheets showing the methods and parameters used to obtain all costs associated with augments considered for the liquid and gaseous radwaste systems.  The cost estimate sheets are grouped by radwaste system types.  The first sheet in each case is an equipment cost worksheet for determining direct equipment costs.  The second sheet is an operating cost worksheet.  All costs are stated in terms of 1975 dollars.  No attempt has been made to project the effect of inflation.  Variations of labor costs and productivity with site locations are considered.
 
~4  All costs are based on the assumption that the reactor is in the design stage and that augmentation of a radwaste system will not involve backfitting of an existing plant.  Backfltttng costs should be determined on a case-by-case basis.
 
1. Capital Costs Capital costs are reported by grouping items by system and by plant location, which generally follow the U.S. Nuclear Regulatory Commission (NRC)/U.S. Atomic Energy Commission accounting system given in NUS-531 (Ref. 1).  The direct costs considered to be applicable to radwaste systems are structures, electrical services, equipment, and instrumentation and controls.  Spare parts and a contingency allowance
~5 are included in the direct costs.  Total capital costs are obtained by multiplying direct costs by an indirect cost factor.
 
2. Direct Costs Direct costs for each augment include equipment, site labor, and site materials.  Principal equipment designs and hardware costs were obtained from utility companies, architect-engineers, and vendors.  Costs for building space, electrical services, piping, and instrumentation were estimated considering equipment functions and arrangements. Costs for electric services, piping, and instrumentation and controls were determined using judgment to estimate equipment layout, points of interface, and services required.  The costs for equipment and building space are consistent with NRC staff recommendations for radwaste system quality assurance, materials, and seismic design.  Space requirements were determined based on manufacturer's data or data from existing or proposed layout drawings.
 
3. Labor Cost Correction Factors Labor cost adjustment factors were developed for each of the eight FPC electric power supply areas shown in Figure A-1 of Appendix A by calculating th e average labor cost for selected cities (Ref. 2) in each area and adjusting this cost for estimated variations in labor productivity due only to differences in labor practices in the regions considered.  Manpower costs were calculated by multiplying the estimated labor requirements in man-hours by the compos ite wage rate (Ref. 3).  The calculated labor cost correction factors are tabulated in Table A-4 of Appendix A.
 
4  Location effects of the eight FPC Power Supply areas are estimated and shown in Table A-4 of Appendix A.
 
5  Contingency onsite labor and process equipment and material are all based on l0 percent.
 
Appendix B to RG 1.110, Page B-2
4. Indirect Cost Factor
 
Indirect costs as a percentage of direct costs are calculated in Table B-1. Table B-
 
===1. Indirect Costs  ===
1 ST UNIT, PERCENTAGE OF DIRECT COST SUBSEQUENT UNITS, PERCENTAGE OF DIRECT COST
Construction facilities, equipment, and services  10 5 Engineering and construction management services  20 10 Other owners' costs  10 5 Interest during construction  35 a 35 a Total 75 55 a. Based on a 10 percent per year  interest rate and a 4-year construction time for radwaste systems only.  Interest during construction is estimated to be 25 percent of direct costs plus other indirect costs.  This is equivalent to 35 percent of the direct costs. The indirect escalators (factors) were estimated from preliminary architect and engineering data to be used to update the Oak Ridge National Laboratory concept and ORCOST computer codes.
 
5. Operation and Maintenance Costs Annual expenses for operation and maintenance (O&M) of the radwaste treatment systems were estimated for baseload power plants operating at 80 percent capacity factor.  Manpower and supply costs were estimated by considering equipment functions in each case.  Expenses for gases, steam, resins, auxiliary power, and other supplies and services were assessed individually.  Maintenance costs were evaluated according to the type of service for which the equipment could be used.  Operating costs include estimated manpower costs, costs of utilities and supplies, and effects on supporting plant systems interfacing with the augmented radwaste system (e.g., effect of an evaporator augment on the solid waste system).  Also included are costs of handling wastes such as spent resins, demineralizer regenerants, evaporator bottoms, and filter media, as well as offsite handling, transportation, and burial costs.
 
6. Capital Recovery Factor The capital recovery factor is a levelized annual charge that takes into account the cost of borrowed money and the depreciation of assets.  It is calculated from the expression:
1)i 1 ()i 1 (i n n++ 
Appendix B to RG 1.110, Page B-3 Where: i = cost of borrowed money expressed as a decimal n = plant operating lifetime (yr)
 
In calculating the values used in Table A-5 of Appendix A, a plant operating lifetime of 30 years was used.  The capital recovery factor multiplied by the total capital cost will give the annual dollar charges for capital and capital-related expenses.
 
LIST OF APPENDIX B COST ESTIMATE SHEETS  BWR Offgas Recombiner .........................................................................................................
... B-4 3-ton Charcoal Adsorber .......................................................................................................
....... B-6 Desiccant Dryer ...............................................................................................................
............ B-8 Charcoal Vault Refrigeration ..................................................................................................
... B-10 Charcoal/HEPA Filtration System - Condenser Vacuum Pump ............................................... B-12 Clean Steam to Turbine Glands ................................................................................................. B-14 Clean Steam to Steam Valves 24" and Larger ........................................................................... B-16 Clean Steam to Steam Valves 21/2" and less than 24\ ................................................................. B-18
15,000-cfm HEPA Filtration System ......................................................................................... B-2
0 1000-cfm Charcoal/HEPA Filtration System ............................................................................ B-23
15,000-cfm HEPA Filtration System ......................................................................................... B-2
5 30,000-cfm Charcoal/HEPA Filtration System ......................................................................... B-28 Turbine Building Chilled Water HVAC System ....................................................................... B-31
600-ft 3 Waste Gas Decay Tank .................................................................................................. B-33 PWR Hydrogen Recombiner ..................................................................................................... B
-35 PWR Air Ejector Charcoal/HEPA Filtration Unit ..................................................................... B-37 Steam Generator Flash Tank Vent to Main Condenser ............................................................. B-39 Evaporators ...................................................................................................................
............. B-41 Evaporator Distillate Demineralizer ..........................................................................................
B-48 Demineralizers ................................................................................................................
........... B-50
Cartridge Filter ..............................................................................................................
............. B-60
Precoat Filters ...............................................................................................................
............. B-62 Reverse Osmosis ...............................................................................................................
......... B-65
10,000-Gallon Tank ............................................................................................................
....... B-67
 
Appendix B to RG 1.110, Page B-4 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS Description of Augment BWR Offgas Recombiner (Sheet 1) DIRECT COST (1975 $1,000)  ITEM LABOR
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 90 260 350 single unit, catalytic type w/heater and condenser, w/o instrumentation and controls, stainless steel, ASME VIII
2. BUILDING ASSIGNMENT 100 50 150 30 x 40 x 25 @ $5/ft 3  (turbine building shielded area)
3. ASSOCIATED PIPING SYSTEMS 18 12 30 augment piping connections only 4. INSTRUMENTATION AND CONTROLS 24 96 120 allowance
5. ELECTRICAL SERVICE - - neg 4kw heaters on vessels neglected
6. SPARE PARTS - 85 85 75K for catalyst + 2% E/M in items 1 & 4 above  SUBTOTAL 232 503 735 
7. CONTINGENCY 23 50 73 10%
8. TOTAL DIRECT COSTS 255 553 808 
 
Appendix B to RG 1.110, Page B-5 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
TER-COOLED NUCLEAR REACTORS Description of Augment BWR Offgas Recombiner (Sheet 2) DIRECT COST (1975 $1,000)  ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD  3.3 15 min/shift
2. MAINTENANCE MATERIAL AND
LABOR  20.0 routine conditioning of catalyst and equipment upkeep; 5% of E/M including I&C
3. CONSUMABLES, CHEMICALS, AND
SUPPLIES  - in item 2
4. UTILITIES AND SERVICES      Waste Disposal      Water      Steam  neg intermittent; 4kw heater load is negligible  Electricity      Building Services      Other   
5. TOTAL O AND M ANNUAL COST  23.3 
 
Appendix B to RG 1.110, Page B-6 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS Description of Augment 3-ton Charcoal Adsorber (Sheet 1) DIRECT COST (1975 $1,000)  ITEM LABOR
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1.  PROCESS EQUIPMENT 5 44.0 49.0 carbon steel, 360 psig, 200 ft
3 volume (augment to existing train of beds)
2.  BUILDING ASSIGNMENT 8 4.5 12.5 10 x 10 x 25 @ $5/ft 3 (turbine building shielded area)
3.  ASSOCIATED PIPING SYSTEMS - - - in item 1
4.  INSTRUMENTATION AND CONTROLS - - neg 
5.  ELECTRICAL SERVICE - - neg 
6.  SPARE PARTS - - none existing  SUBTOTAL 13 48.5 61.5 
7.  CONTINGENCY 1 5.0 6.0 10%
8.  TOTAL DIRECT COSTS 14 53.5 67.5 
 
Appendix B to RG 1.110, Page B-7 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
TER-COOLED NUCLEAR REACTORS Description of Augment 3-ton Charcoal Adsorber (Sheet 2) DIRECT COST (1975 $1,000)  ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD  neg  2. MAINTENANCE MATERIAL AND
LABOR  neg allowance of 3% of equipment cost is negligible
3. CONSUMABLES, CHEMICALS, AND
SUPPLIES  neg lifetime use of charcoal assumed
4. UTILITIES AND SERVICES  neg  Waste Disposal      Water      Steam  neg  Electricity      Building Services      Other   
5. TOTAL O AND M ANNUAL COST  neg 
 
Appendix B to RG 1.110, Page B-8 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS Description of Augment Desiccant Dryer (Sheet 1) DIRECT COST (1975 $1,000)  ITEM LABOR
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 25 75 100 redundant dryer vessels with 1 regeneration skid
2. BUILDING ASSIGNMENT 95 50 145 40 x 36 x 20 @ $5/ft 3 turbine building (shielded area)
3. ASSOCIATED PIPING SYSTEMS 10 5 15 augment piping connections only 4. INSTRUMENTATION AND CONTROLS 12 48 60 allowance
5. ELECTRICAL SERVICE 18 17 35 service for heaters, blowers, pumps, and compressors
6. SPARE PARTS - 3 3  SUBTOTAL 160 198 358 
7. CONTINGENCY 16 20 36 10%
8. TOTAL DIRECT COSTS 176 218 394 
 
Appendix B to RG 1.110, Page B-9 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
TER-COOLED NUCLEAR REACTORS Description of Augment Desiccant Dryer (Sheet 2) DIRECT COST (1975 $1,000)  ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD  3.3 15 min/shift
2. MAINTENANCE MATERIAL AND
LABOR  6.1 5% of equipment including I&C
3. CONSUMABLES, CHEMICALS, AND
SUPPLIES  neg  4. UTILITIES AND SERVICES      Waste Disposal  neg operating time does not require significant utilities and services  Water  neg  Steam      Electricity  neg  Building Services      Other   
5. TOTAL O AND M ANNUAL COST  9.4 
 
Appendix B to RG 1.110, Page B-10 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS Description of Augment Charcoal Vault Refrigeration (Sheet 1) DIRECT COST (1975 $1,000)  ITEM LABOR
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 10 75 85 10-ton capacity, 3 refrigerators with drives, 32°F design
2. BUILDING ASSIGNMENT 9 3 12 20 x 10 x 20 @ $2/ft 3 turbine building (nonshielded area)
3. ASSOCIATED PIPING SYSTEMS    in item 1
4. INSTRUMENTATION AND CONTROLS 4 6 10 allowance
5. ELECTRICAL SERVICE 12 18 30 allowance
6. SPARE PARTS - 3 3  SUBTOTAL 35 105 140 
7. CONTINGENCY 3 11 14 10%
8. TOTAL DIRECT COSTS 38 116 154 
 
Appendix B to RG 1.110, Page B-11 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
TER-COOLED NUCLEAR REACTORS Description of Augment Charcoal Vault Refrigeration (Sheet 2) DIRECT COST (1975 $1,000)  ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD  3.3 15 min/shift
2. MAINTENANCE MATERIAL AND
LABOR  3.7 5% of equipment
3. CONSUMABLES, CHEMICALS, AND
SUPPLIES    in item 2
4. UTILITIES AND SERVICES      Waste Disposal      Water      Steam  0.5 electricity and cooling water  Electricity      Building Services      Other   
5. TOTAL O AND M ANNUAL COST  7.5 
 
Appendix B to RG 1.110, Page B-12 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS Description of Augment Charcoal/HEPA Filtration System - Condenser Vacuum Pump (Sheet 1) DIRECT COST (1975 $1,000)  ITEM LABOR
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 2 32.5 34.5 2,000 CFM prefilter/4" charcoal bed/HEPA @ $15/cfm, 10 kw heater @ $250/kw
2. BUILDING ASSIGNMENT 3.1 1.5 4.6 Turbine building 8 x 16 x 12 @ $3/ft 3 (nonshielded area)
3. ASSOCIATED PIPING SYSTEMS 1.3 0.7 2.0 allowance
4. INSTRUMENTATION AND CONTROLS    in item 1
5. ELECTRICAL SERVICE 1 1.5 2.5 
6. SPARE PARTS  0.5 0.5  SUBTOTAL 7.4 36.7 44.1 
7. CONTINGENCY 0.7 3.7 4.4 10%
8. TOTAL DIRECT COSTS 8.1 40.4 48.5 
 
Appendix B to RG 1.110, Page B-13 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
TER-COOLED NUCLEAR REACTORS Description of Augment Charcoal/HEPA Filtration System - Condenser Vacuum Pump (Sheet 2) DIRECT COST (1975 $1,000)  ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD  neg used only during startup and shutdown 2. MAINTENANCE MATERIAL AND
LABOR  1.2 4 HEPA filters @ $150 & 2 Charcoal filters @ $900, change every 2 years
3. CONSUMABLES, CHEMICALS, AND
SUPPLIES  - in items 2 and 4
4. UTILITIES AND SERVICES      Waste Disposal  0.2 $50/HEPA filter, $100/Charcoal filter  Water      Steam      Electricity      Building Services      Other   
5. TOTAL O AND M ANNUAL COST  1.4 
 
Appendix B to RG 1.110, Page B-14 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS Description of Augment Clean Steam to Turbine Glands (Sheet 1) DIRECT COST (1975 $1,000)  ITEM LABOR
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 9. PROCESS EQUIPMENT 15 150 165 25,000 lb/hr reboiler @ $4/lb/hr & $25K/H.P. turbine glands
10. BUILDING ASSIGNMENT 19 10 29 20 x 30 x 16 @ $3/ft 3 11. ASSOCIATED PIPING SYSTEMS 32 18 50 equiv 1,000 ft @ $50/ft
12. INSTRUMENTATION AND CONTROLS 8 12 20 in addition to item 1
13. ELECTRICAL SERVICE  neg 
14. SPARE PARTS - 5 5  SUBTOTAL 74 195 269 
15. CONTINGENCY 7 20 27 10%
16. TOTAL DIRECT COSTS 81 215 296 
 
Appendix B to RG 1.110, Page B-15 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
TER-COOLED NUCLEAR REACTORS Description of Augment Clean Steam to Turbine Glands (Sheet 2) DIRECT COST (1975 $1,000)  ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD  3.3 15 min/shift
2. MAINTENANCE MATERIAL AND
LABOR  4.0 40 man-days
3. CONSUMABLES, CHEMICALS, AND
SUPPLIES    4. UTILITIES AND SERVICES      Waste Disposal      Water      Steam  21.0 10 Btu/kw-hr heat rate increase  Electricity      Building Services      Other   
5. TOTAL O AND M ANNUAL COST  28.3 
 
Appendix B to RG 1.110, Page B-16 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS Description of Augment Clean Steam to Steam Valves 24" and Larger (Sheet 1) DIRECT COST (1975 $1,000)  ITEM LABOR
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 100 120 220 22 valves @ $1,0k/valve, use existing reboiler
2. BUILDING ASSIGNMENT  neg install in existing space
3. ASSOCIATED PIPING SYSTEMS  - in item 1
4. INSTRUMENTATION AND CONTROLS  - in item 1
5. ELECTRICAL SERVICE  neg 
6. SPARE PARTS - 5 5  SUBTOTAL 100 125 225 
7. CONTINGENCY 10 12 22 10%
8. TOTAL DIRECT COSTS 110 137 247 
 
Appendix B to RG 1.110, Page B-17 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
TER-COOLED NUCLEAR REACTORS Description of Augment Clean Steam to Steam Valves 24" and Larger (Sheet 2) DIRECT COST (1975 $1,000)  ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 6. OPERATING LABOR, SUPERVISION, AND OVERHEAD  3.3 15 min/shift
7. MAINTENANCE MATERIAL AND
LABOR  4.0 40 man-days
8. CONSUMABLES, CHEMICALS, AND
SUPPLIES  neg  9. UTILITIES AND SERVICES      Waste Disposal      Water      Steam  neg  Electricity      Building Services      Other   
1 0TOTAL O AND M ANNUAL COST  7.3 
 
Appendix B to RG 1.110, Page B-18 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS Description of Augment Clean Steam to Steam Valves 21/2" and less than 24" (Sheet 1) DIRECT COST (1975 $1,000)  ITEM LABOR
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 0 120 120 100 valves @ $1,200 each
2. BUILDING ASSIGNMENT - - neg 
3. ASSOCIATED PIPING SYSTEMS 40 20 60 
4. INSTRUMENTATION AND CONTROLS 10 20 30 allowance
5. ELECTRICAL SERVICE  - none
6. SPARE PARTS - 6 6  SUBTOTAL 50 166 216 
7. CONTINGENCY 5 17 22 10%
8. TOTAL DIRECT COSTS 55 183 238 
 
Appendix B to RG 1.110, Page B-19 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
TER-COOLED NUCLEAR REACTORS Description of Augment Clean Steam to Steam Valves 21/2" and less than 24" (Sheet 2) DIRECT COST (1975 $1,000)  ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD  3.3 15 min/shift
2. MAINTENANCE MATERIAL AND
LABOR  12.0 1% of direct cost of equipment
3. CONSUMABLES, CHEMICALS, AND
SUPPLIES  - in item 2
4. UTILITIES AND SERVICES      Waste Disposal      Water      Steam  neg  Electricity      Building Services      Other   
5. TOTAL O AND M ANNUAL COST  15.3 
 
Appendix B to RG 1.110, Page B-20 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS Description of Augment 15,000-cfm HEPA Filtration System - Auxiliary Building (Sheet 1) DIRECT COST (1975 $1,000)  ITEM LABOR
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 5 40.0 45.0 prefilter/HEPA @ $3/cfm, use existing fan
2. BUILDING ASSIGNMENT 7 4.5 11.5 16 x 12 x 12 @ $5/ft 3 (nonshielded area)
3. ASSOCIATED PIPING SYSTEMS 3 2.0 5.0 
4. INSTRUMENTATION AND CONTROLS    in item 1
5. ELECTRICAL SERVICE    base
6. SPARE PARTS  0.5 0.5  SUBTOTAL 15 47.0 62.0 
7. CONTINGENCY 1 5.0 6.0 10%
8. TOTAL DIRECT COSTS 16 52.0 68.0 
 
Appendix B to RG 1.110, Page B-21 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS Description of Augment 15,000-cfm HEPA Filtration System - Turbine Building (Sheet 2) DIRECT COST (1975 $1,000)  ITEM LABOR
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 5 40.0 45.0 skid mounted filter housing w/o fans 2. BUILDING ASSIGNMENT 4.6 2.3 6.9 16 x 12 x 12 @ $3/ft 3 (nonshielded area)
3. ASSOCIATED PIPING SYSTEMS 3 2.0 5.0 
4. INSTRUMENTATION AND CONTROLS    in item 1
5. ELECTRICAL SERVICE    base
6. SPARE PARTS 0 0.5 0.5  SUBTOTAL 12.6 44.8 57.4 
7. CONTINGENCY 2 4.0 6.0 10%
8. TOTAL DIRECT COSTS 14.6 48.8 63.4 
 
Appendix B to RG 1.110, Page B-22 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
TER-COOLED NUCLEAR REACTORS Description of Augment 15,000-cfm HEPA Filtration System (Sheet 3) DIRECT COST (1975 $1,000)  ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD  3.8 15 min/shift + 40 hr annual test
2. MAINTENANCE MATERIAL AND
LABOR  2.2 change every 2 yrs @ $150/filter element 3. CONSUMABLES, CHEMICALS, AND
SUPPLIES  - in items 2 and 4
4. UTILITIES AND SERVICES      Waste Disposal  0.8 $50/filter element  Water      Steam      Electricity  1.0 additional fan electrical load  Building Services      Other   
5. TOTAL O AND M ANNUAL COST  7.8 
 
Appendix B to RG 1.110, Page B-23 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS Description of Augment 1000-cfm Charcoal/HEPA Filtration System (Sheet 1) DIRECT COST (1975 $1,000)  ITEM LABOR
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 2.0 22.0 24.0 prefilter/4" charcoal/HEPA @ $20/cfm, 5 kw htr @ $400/kw
2. BUILDING ASSIGNMENT 3.8 2.0 5.8 8 x 12 x 12 @ $5/ft 3 (nonshielded area)
3. ASSOCIATED PIPING SYSTEMS 1.3 0.7 2.0 
4. INSTRUMENTATION AND CONTROLS  - in item 1
5. ELECTRICAL SERVICE 1.5 1.0 2.5 
6. SPARE PARTS  0.5 0.5  SUBTOTAL 8.6 26.2 34.8 
7. CONTINGENCY 1.0 2.0 3.0 10%
8. TOTAL DIRECT COSTS 9.6 28.2 37.8 
 
Appendix B to RG 1.110, Page B-24 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
TER-COOLED NUCLEAR REACTORS Description of Augment 1000-cfm Charcoal/HEPA Filtration System (Sheet 2) DIRECT COST (1975 $1,000)  ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD  1.9 20 min/day + 40 hr annual test
11. MAINTENANCE MATERIAL AND
LABOR  0.6 2 HEPA or prefilters @ $150
each and 1 charcoal @ $900 each every 2 years
12. CONSUMABLES, CHEMICALS, AND
SUPPLIES    in items 2 and 4
13. UTILITIES AND SERVICES      Waste Disposal  0.1 $50/HEPA or prefilter, $100/charcoal filter  Water      Steam      Electricity  neg  Building Services      Other   
14. TOTAL O AND M ANNUAL COST  2.6 


Appendix B to RG 1.110, Page B-25 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS Description of Augment 15,000-cfm HEPA Filtration System - Auxiliary Building (Sheet 1) DIRECT COST (1975 $1,000) ITEM LABOR
1.110-8 TABLE A-1 (Continued)
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 10 71 81 prefilter/4" charcoal/HEPA @ $5/cfm, 30kw htr @ $200/kw
DIRECT COSTS -LIQUID RADWASTE AUGMENTS Direct Costs 15-gpm Evaporator
2. BUILDING ASSIGNMENT 12 8 20 16 x 20 x 12 @ $5/ft 3 (nonshielded area)
30-gpm Evaporator
3. ASSOCIATED PIPING SYSTEMS 3 2 5
50-gpm Evaporator Evaporator Distillate Demineralizer
4. INSTRUMENTATION AND CONTROLS  - in item 1  
50-gpm Demineralizer
5. ELECTRICAL SERVICE 3 2 5 allowance
100-gpm Demineralizer
6. SPARE PARTS  5 5 4 elements of each type  SUBTOTAL 28 88 116 
200-gpm Deminieralizer
7. CONTINGENCY 3 9 12 10%
400-gpm Demineralizer
8. TOTAL DIRECT COSTS 31 97 128 
100-gpm Precoat Filter 400-gpw Precoat Filter 20-gpm Cartridge Filter 2-gpm Reverse Osmosis 10,000-gal Tank Equipment/Material
386 540 655 36 43 64 94 102 108 202 13 100 55 1.110-9 Labor 201 223 233 24 29 31 35 44 56 112 11 38 43 (1975 $1000) Total 587 763 888 60 50 95 129 146 164 314 24 138 98 TABLE A-2 T ANNUAL OPERATING
COSTS -GASEOUS RADWASTE AUGMENTS BWR Offgas Recoatbiner
3-ton Charcoal Adsorber Desiccant Dryer Charcoal Vault Refrigeration Main Condenser Vacuum Pump Charcoal/HEPA
Filtration System Clean Steam to Turbine Glands Clean Steam to Steam Valves, 24" and Larger Clean Steam to Steam Valves, 2-1/2" and Less Than 24" 15,000-cfm HEPA Filtration System 1,000-cfm Charcoal/HEPA
Filtration System 15,000-cfm Charcoal/HEPA
Filtration System 30,000-cfm Charcoal/HEPA  
Filtration System Turbine Bldg. Chilled Water HVAC System 600-ft 3 Gas Decay Tank PWR Hydrogen Recombiner PWR Air Ejector Charcoal/HEPA
Filtration Unit Steam Generator Flash Tank Vent to Main Condenser Total Operating Cost 3 (1975 $lOOO/yr)neg 3 4 0.4 24 3 3 6 2 7 9 49 neg 4 4 1 ANNUAL OPERATING
COSTS -LIQUID RADWASTE AUGMENTS Evaporation
-PWR Dirty Waste Evaporation
-BWR Dirty Waste Evaporation
-Condensate Polisher Chemical Waste Evaporation
-Detergent Waste Demineralization
-kvaporator Distillate Demineralization
-BWR 2nd Waste Demineralizer in Series 50 169 114 20 5 15 Operating costs are given for a single reactor. Operating costs for augments in shared radwaste systems should be multiplied by the number of reactors serviced by the augment.1.110-10 K B r m m TABLE A-2 (Continued)
ANNUAL OPERATING
COSTS -LIQUID RADWASTE AUGMENTS Total Operating Cost (1975 $1000/yr)5 Demineralization
-PWR Clean Waste Demineralization
-BWR Dirty Waste Demineralization
-PWR Dirty Waste Demineralization
-PWR Turbine Bldg. Drains Desmineralization
-PWR Steam Generator Blowdown Precoat Filter -BWR Dirty Waste Cartridge Filter Reverse Osmosis -Detergent Waste 10,000-gal Tank 88 18 95 25 53 7 7 1 1.110-11 TABLE A-3 ANNUAL MAINTENANCE
COSTS- GASEOUS RADWASTE AUGMENTS Total Maintenance Cost (1975 $1O00/Yr)  
BWR Offgas Recombiner
20 3-ton Charcoal Adsorber neg Desiccant Dryer 6 Charcoal Vault Refrigeration
3 Main Condenser Vacuum Pump Charcoal/HEPA
Filtration System 1 Clean Steam to Turbine Glands 4 Clean Steam to Steam Valves, 24" and Larger 4 Clean Steam to Steam Valves, 2-1/2" and Less Than 24" 12 15,000-cfm HEPA Filtration System 2 1,000-cfm Charcoal/HEPA
Filtration System 0.6 15,O00-cfm Charcoal/HEPA
Filtration System 9 30,000-cfm Charcoal/HEPA
Filtration System 18 Turbine Bldg. Chilled Water HVAC System 20 600-ft 3 Gas Decay Tank neg PWR Hydrogen "Recombiner
10 PWR Air Ejector Charcoal/HEPA
Filtration Unit 2 Steam Generator Flash Tank Vent to Main Condenser
1 ANNUAL MAINTENANCE
COSTS -LIQUID RADWASTE AUGMENTS 15-gpm Evaporator
30 30-gpm Evaporator
30 50-gpm Evaporator
30 Evaporator Distillate Demineralizer
2 50-gpm Demineral izer 5 lO0-gpmi Demineralizer
5 200-gpm Demineral izer S 100-gpm Precoat Filter 10 400-gpm Precoat Filter 10 20-gpm Cartridge Filter 1 2-gpm Reverse Osmosis g 10.000-gal Tank 2 1.110-12 TABLE A-4 LABOR COST CORRECTION
FACTORS Labor Cost Correction Factor 1.6 1.5 1.0 1.4 1.1 1.2 1.3 1.2 See Appendix B, "Labor See Figure A-1.Cost Correction Factors.'1.110-13 FPC Geographic Region I 1II IV V VI VII Vlll TABLE A-5 INDIRECT COST FACTORS Type Radwaste System "1. Single unit site, unitized radwaste system 2. Multi-unit site, shared radwaste system 3. Multi-unit site, unitized radwaste system Indirect Cost Factor 1.75 1.75 1.75 + (n-1)1.5 n where n is the number of unitized radwaste systems at the site Each reactor has a separate, nonshared radwaste system.I..1.110-14 TABLE A-6 CAPITAL RECOVERY FACTORS Cost of Honey (1 per year, i)5 6 7 8 9 10 11 12 13 14 15 Capital Recovery Factor 0.0651 0.0726 0.0806 0.0888 0.0973 0.1061 0.1150 0.1241 0.1334 0.1428 0.1523 service life of 30 years and the follwing equation:
CRF M + 1)3 (I + i)30-1 1.110-15*Based on a LEGEND ¶Im REGIONAL GROUPING OF POWER SUPPLY AREAS FIGURE A-1 ELECTRIC POWER SUPPLY AREAS IN THE UNITED STATES (C C
APPENDIX B BASES FOR PARAMETERS
USED IN PERFORMING
COST-BENEFIT
ANALYSIS This appendix contains detailed cost estimate sheets showing the methods and parameters used to obtain all costs associated with augments considered for the liquid and gaseous radwaste systems. The cost estimate sheets are grouped by radwaste system types. The first sheet in each case is an equipment cost worksheet for determining direct equipment costs. The second sheet is an operating cost worksheet.


Appendix B to RG 1.110, Page B-26 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS Description of Augment 15,000-cfm HEPA Filtration System - Turbine Building (Sheet 2) DIRECT COST (1975 $1,000)  ITEM LABOR
All costs are stated in terms of 1975 dollars. No attempt has been made to project the effect of inflation.
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 10.0 71.0 81.0 prefilter/4" charcoal/HEPA @ $5/cfm, 30 kw htr @ $200/kw
2. BUILDING ASSIGNMENT 7.7 3.8 11.5 16 x 20 x 12 @ $3/ft 3 (nonshielded area)
3. ASSOCIATED PIPING SYSTEMS 3.0 2.0 5.0 
4. INSTRUMENTATION AND CONTROLS    in item 1
5. ELECTRICAL SERVICE 3.0 2.0 5.0 allowance
6. SPARE PARTS - 5.0 5.0 4 elements each type  SUBTOTAL 23.7 83.8 107.5 
7. CONTINGENCY 2.0 9.0 11.0 10%
8. TOTAL DIRECT COSTS 25.7 92.8 118.5 


Appendix B to RG 1.110, Page B-27 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
Variations of labor costs and productivity with site locaticns are considered.*
TER-COOLED NUCLEAR REACTORS Description of Augment 15,000-cfm HEPA Filtration System (Sheet 3) DIRECT COST (1975 $1,000) ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD  3.8 15 min/shift & 40-hr annual test
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.
2. MAINTENANCE MATERIAL AND
LABOR  9.0 30 HEPA or prefilters @ $150 each & 15 charcoal filters @
$900 each every 2 years
3. CONSUMABLES, CHEMICALS, AND
SUPPLIES  - in items 2 and 4
4. UTILITIES AND SERVICES      Waste Disposal  1.5 $50/HEPA or prefilter, $100/charcoal  Water      Steam      Electricity  1.3 8kw additional fan power for filter P @ 0.018 $/kw-hr  Building Services      Other   
5. TOTAL O AND M ANNUAL COST  15.6 


Appendix B to RG 1.110, Page B-28 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS Description of Augment 30,000-cfm Charcoal/HEPA Filtration System - Auxiliary Building (Sheet 1) DIRECT COST (1975 $1,000)  ITEM LABOR
Spare parts and a contingency allowance**
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 15 117.0 132.0 prefilter/4" charcoal/HEPA @ $4/cfm, 60-kw htr @ $200/kw
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.
2. BUILDING ASSIGNMENT 20 13.6 33.6 28 x 20 x 12 @ $5/ft 3 (nonshielded area)
3. ASSOCIATED PIPING SYSTEMS 5 3.0 8.0 base
4. INSTRUMENTATION AND CONTROLS  - in item 1
5. ELECTRICAL SERVICE 6 4.0 10.0 allowance
6. SPARE PARTS - 5.0 5.0 4 elements each type  SUBTOTAL 46 142.6 188.6 
7. CONTINGENCY 5 14.0 19.0 10%
8. TOTAL DIRECT COSTS 51 156.6 207.6 


Appendix B to RG 1.110, Page B-29 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS Description of Augment 30,000-cfm Charcoal/HEPA Filtration System - Turbine Building (Sheet 2) DIRECT COST (1975 $1,000)  ITEM LABOR
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/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 15.0 117.0 132.0 prefilter/4" charcoal/HEPA @ $4/cfm, 60-kw htr @ $200/kw
2. BUILDING ASSIGNMENT 13.4 6.8 20.2 28 x 20 x 12 @ $3/ft 3 (nonshielded area)
3. ASSOCIATED PIPING SYSTEMS 3.0 5.0 8.0 base
4. INSTRUMENTATION AND CONTROLS    in item 1
5. ELECTRICAL SERVICE 6.0 4.0 10.0 allowance
6. SPARE PARTS - 5.0 5.0 4 elements each type  SUBTOTAL 37.4 137.8 175.2 
7. CONTINGENCY 4.0 14.0 18.0 10%
8. TOTAL DIRECT COSTS 41.4 151.8 193.2 


Appendix B to RG 1.110, Page B-30 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
Costs for electric services, piping, and instrumentation and controls were determined using judgment to estimate equipment layout, points of interface, and services required.
TER-COOLED NUCLEAR REACTORS Description of Augment 30,000-cfm Charcoal/HEPA Filtration System - Auxiliary Building (Sheet 3) DIRECT COST (1975 $1,000)  ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD  3.8 15 min/shift + 40 hr annual test
2. MAINTENANCE MATERIAL AND
LABOR  18.0 60 HEPA or prefilters @ $150 each & 30 charcoal filters @
$900 each every 2 years
3. CONSUMABLES, CHEMICALS, AND
SUPPLIES  - in items 2 and 4
4. UTILITIES AND SERVICES      Waste Disposal  3.0 $50/HEPA or prefilter, $100/charcoal filter  Water      Steam      Electricity  2.6 16 kw additional fan HP for filter @ 0.018 $/kw-hr  Building Services      Other   
5. TOTAL O AND M ANNUAL COST  27.4 


Appendix B to RG 1.110, Page B-31 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS Description of Augment Turbine Building Chilled Water HVAC System (Sheet 1) DIRECT COST (1975 $1,000)  ITEM LABOR
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.
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 300 500 800 500-ton capacity, w/o air filters
2. BUILDING ASSIGNMENT  - Coolers can be installed in existing space saved by deletion of ducting
3. ASSOCIATED PIPING SYSTEMS  - in item 1
4. INSTRUMENTATION AND CONTROLS  - in item 1
5. ELECTRICAL SERVICE 40 50 90 
6. SPARE PARTS - 8 8 1% item 1  SUBTOTAL 340 558 898 
7. CONTINGENCY 34 56 90 10%
8. TOTAL DIRECT COSTS 374 614 988 


Appendix B to RG 1.110, Page B-32 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
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.
TER-COOLED NUCLEAR REACTORS Description of Augment Turbine Building Chilled Water HVAC System (Sheet 2) DIRECT COST (1975 $1,000)  ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD  3.3 15 min/shift
2. MAINTENANCE MATERIAL AND
LABOR  20.0 21/2% of equipment costs
3. CONSUMABLES, CHEMICALS, AND
SUPPLIES  - in item 2
4. UTILITIES AND SERVICES      Waste Disposal      Water  13.0 500 gpm @ 10¢/1,000 gal &
50% load factor  Steam      Electricity  33.0 400 kw @ 0.018 $/kw-hr  Building Services      Other   
5. TOTAL O AND M ANNUAL COST  69.3 


Appendix B to RG 1.110, Page B-33 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS Description of Augment 600-ft
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
3 Waste Gas Decay Tank (Sheet 1) DIRECT COST (1975 $1,000)  ITEM LABOR
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)
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 2.5 20 22.5 600-ft
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.
3, 150 psig, C.S., ASME VIII 2. BUILDING ASSIGNMENT 18.0 9 27.0 15 x 15 x 20 @ $6/ft 3 (shielded area)
3. ASSOCIATED PIPING SYSTEMS 1.0 1 2.0 10% of item 1
4. INSTRUMENTATION AND CONTROLS  neg 
5. ELECTRICAL SERVICE  neg  
6. SPARE PARTS  neg  SUBTOTAL 21.5 30 51.5  
7. CONTINGENCY 2.0 3 5.0 10%
8. TOTAL DIRECT COSTS 23.5 33 56.5 


Appendix B to RG 1.110, Page B-34 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
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:
TER-COOLED NUCLEAR REACTORS Description of Augment 600-ft
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
3 Waste Gas Decay Tank (Sheet 2) DIRECT COST (1975 $1,000) ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD - - neg  2. MAINTENANCE MATERIAL AND  
.............................................................
LABOR - - neg  3. CONSUMABLES, CHEMICALS, AND  
1.110-20 3-ton Charcoal Adso r ...............................................................
SUPPLIES - - neg  4. UTILITIES AND SERVICES     Waste Disposal     Water     Steam   neg   Electricity     Building Services     Other    
1.110-22 Desiccant Dryer ..............................................................
5. TOTAL O AND M ANNUAL COST   neg  
1.110-24 Charcoal Vault Refrigeration
.........................................................
1.110-26 Charcoal/HEPA
Filtration System -Condenser Vacuun Pump ..............................
1.110-28 Clean Steam to Turbine Glands ........................................................
1.110-30 Clean Steam to Steam Valves 24- and Larger ...........................................
1.110-32 Clean Steam to Steam Valves 2-1/2' and Less Than 24" ................................
1.110-34 1S.000-cftm NEPA Filtration System ....................................................
1.110-36 1000-cfa Charcoal/HEPA
Filtration System .............................................
1.110-39 15.000-cfm Charcoal/HEPA
Filtration System ...........................................
1.110-41 30,000-cfm Charcoal/HEPA
Filtration System ..........................................
1.110-44 Turbine Building Chilled Mater HVAC System ...........................................
1.110-47 600-ft 3 Gas Decay Tank ...............................................................
1.110-49 PIW Hydrogen Recombiner
..............................................................
1.110-S1 PiW Air Ejector Charcoal/HEPA
Filtration Unit ........................................
1.110-53 Stem Generator Flash Tank Vent to rain Condenser
....................................
1.110-55 Evaporators
..........................................................................
1.110-57 Evaporator Distillate Demineralizer
..................................................
1.110-64 Demineralizers
.......................................................................
1.110-66 Cartridge Filter .....................................................................
1.110-76 Precoat Filters ......................................................................
.114 7R Reverse Osmosis .....................................................................
1.110-81 10.000-gal Tank ...........................................................
1.11" 1.110-19 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT
SYSTEM FOR LIGHT-WATER-COOLED
NUCLEAR REACTORS Description of Augment ITEM 1. PROCESS EQUIPMENT 2.  3.  4.  5.  6.  7.  8.RUD D r.mh4n.... 11 I___MIXL_
1 IVIML COST ESTIMATE DIRECT COST.(1975
$1000) r1 T DMUT'/MATrD
TAt BASIS FOR 90 260 350 single unit, catalytic type w/heater and condenser, w/o instrumentation and controls, stainless steel, ASME VIII BUILDING ASSIGNMENT
100 50 ISO 30' x 40' x 25' @ $5/ft 3 (turbine building shielded area) ASSOCIATED
PIPING SYSTEMS 18 12 30 augment piping connections only INSTRUM4ENTATION
AND CONTROLS 24 96 120 allowance ELECTRICAL
SERVICE neq 4kw heaters on vessels neglected SPARE PARTS 85 85 75K for catalyst + 2% E/M in items 1 & 4 above SUBTOTAL 232 503 735 CONTINGENCY
23 50 73 10% TOTAL DIRECT COSTS 2S5 553 808 r a O (S...... ..................
w BWR Off %e Darr-M---
Ick- a, I a W i IARND TflYAi K A ANNUAL OPERATING  
AND MAINTENANCE  
COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR-LIGHT-WATER-COOLED  
NUCLEAR REACTORS Description of Augment BWR Offgas Recombiner (Sheet 2) COST (1975 $1000)ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE OPERATING  
LABOR, SUPERVISION, 3.3 15 m.n/shift AND OVERHEAD MAINTENANCE  
MATERIAL AND. 20.0 routine conditioning of catalyst and LABOR equipment upkeep; 5% of E/M including I&C CONSUMBLES, CHEMICALS, AND -initem 2 SUPPLIES UTILITIES  
AND SERVICES Waste Disposal Water Steam neg intemittent;
4kw heater load is negligible Electricity Building Services Other TOTAL 0 AND M ANNUAL COST 23.3 1.  2.C2 ,01 3.  4. 5.I
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT
SYSTEM FOR LIGHT-WATER-COOLED
NUCLEAR REACTORS Description of Augment !TFM 1. PROCESS EQUIPENT


Appendix B to RG 1.110, Page B-35 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS Description of Augment PWR Hydrogen Recombiner (Sheet 1) DIRECT COST (1975 $1,000) ITEM LABOR
===2. BUILDING ASSIGNMENT===
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 50.0 300.0 350.0 skid mounted, catalytic type w/condenser, partial I&C single unit, ASME VIII
3.  4.  S.  6.  7.  8.3-ton Charcoal Adsorber (Sheet 1)LABOR 5 DIRECT COST (1975 $1000) EOUIPMENTIMATERIALS
2. BUILDING ASSIGNMENT 28.8 14.4 43.2 15 x 30 x 16 @ $6/ft 3 (shielded area)  
TOTAL-------44.0 49.0 BASIS FOR COST ESTIMATF carbon steel, 350 psig, 200 ft 3 volume (augment to existing train of beds)4. 4. 4. 4 8 4.5 12.5 10' x 10' x 25' * $5/ft 3 (turbine building shiel4ed area)ASSOCIATED
3. ASSOCIATED PIPING SYSTEMS 32.0 13.0 45.0 allowance
PIPING SYSTES -in item I INSTRUKENTATION
4. INSTRUMENTATION AND CONTROLS 10.0 40.0 50.0 allowance
AND CONTROLS neg ELECTRICAL
5. ELECTRICAL SERVICE 13.0 12.0 25.0 allowance
SERVICE neg SPARE PARTS none existing SUBTOTAL 13 48.5 61.5 CONTINGENCY
6. SPARE PARTS - 2.0 2.0  SUBTOTAL 133.8 381.4 515.2 
1 5.0 6.0 10% TOTAL DIRECT COSTS 14 53.5 67.5 r r a S.. .... ....r m K ANNUAL OPERATING
7. CONTINGENCY 13.0 38.0 51.0 10%
AND MAINTENANCE
8. TOTAL DIRECT COSTS 146.8 419.4 566.2 
COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED
NUCLEAR REACTORS Description of Augment 3-ton Charcoal Adsorber (Sheet 2) COST (1975 $1000)I TFM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE OPERATING
LABOR. SUPERVISION.


Appendix B to RG 1.110, Page B-36 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
neg AND OVERHEAD MAINTENANCE  
TER-COOLED NUCLEAR REACTORS Description of Augment PWR Hydrogen Recombiner (Sheet 2) DIRECT COST (1975 $1,000)  ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD  3.3 15 min/shift
MATERIAL AND allowance of 3% of equipment cost LABOR neg is negligible CONSUMABLES.
2. MAINTENANCE MATERIAL AND  
LABOR  10.0 3% of equipment cost  
3. CONSUMABLES, CHEMICALS, AND
SUPPLIES  1.0 oxygen @ $2.5/10
3 cf & .25 cfm @ 7,000 hrs
4. UTILITIES AND SERVICES      Waste Disposal      Water      Steam  neg  Electricity      Building Services      Other   
5. TOTAL O AND M ANNUAL COST  14.3 


Appendix B to RG 1.110, Page B-37 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS Description of Augment PWR Air Ejector Charcoal/HEPA Filtration Unit (Sheet 1) DIRECT COST (1975 $1,000)  ITEM LABOR
CHEMICALS, AND SUPPLIES neg lifetime use of charcoal assumed UTILITIES
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 3.0 7.5 10.5 chiller, heater, charcoal HEPA
AND SERVICES Waste Disposal Water Steam neg Electricity Building Services Other TOTAL 0 AND M ANNUAL COST neg K 1. 2. 3. 4.I..5.
2. BUILDING ASSIGNMENT 3.0 1.5 4.5 10 x 10 x 15 @ $3/ft 3 (unshielded turbine building)
3. ASSOCIATED PIPING SYSTEMS 2.0 1.0 3.0 allowance
4. INSTRUMENTATION AND CONTROLS 0.5 1.5 2.0 allowance
5. ELECTRICAL SERVICE 0.5 0.5 1.0 allowance
6. SPARE PARTS - 1.0 1.0  SUBTOTAL 9.0 13.0 22.0 
7. CONTINGENCY 1.0 1.0 2.0 10%
8. TOTAL DIRECT COSTS 10.0 14.0 24.0 


Appendix B to RG 1.110, Page B-38 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT
TER-COOLED NUCLEAR REACTORS Description of Augment PWR Air Ejector Charcoal/HEPA Filtration Unit (Sheet 2) DIRECT COST (1975 $1,000) ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD  3.8 15 min/shift + 40 hr annual test
SYSTEM FOR LIGHT-WATER-COOLED
2. MAINTENANCE MATERIAL AND  
NUCLEAR REACTORS Description of Augment Desiccant Drver fSheet !1 I TEN I ARflR DIRECT COST (1975 $1000)IL 1% COTETMT BASIS FOR 1. PROCESS EQUIPMENT 25 75 100 redundant dryer vessels with 1 regeneration skid BUILDING ASSIGNMENT
LABOR   2.0 includes replacement filter
95 50 145 40' x 36' x 20' @ $5/ft 3 turbine building (shielded area) ASSOCIATED
3. CONSUMABLES, CHEMICALS, AND  
PIPING SYSTEMS 10 5 15 augment piping connections only INSTRUMENTATION
SUPPLIES   - in item 2
AND CONTROLS 12 48 60 allowance ELECTRICAL
4. UTILITIES AND SERVICES     Waste Disposal   neg   Water     Steam     Electricity     Building Services     Other    
SERVICE 18 17 35 service for heaters, blowers, pumps, and compressors SPARE PARTS 3 3 SUBTOTAL 160 198 358 CONTINGENCY
5. TOTAL O AND M ANNUAL COST   5.8  
16 20 36 10% TOTAL DIRECT COSTS 176 218 394 r 2.8i 3.  4.  5.6.  7.  8.(r Desiccant Drver (Sheet I)
K ANNUAL CPERATING
AND MAINTENANCE  
COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED  
NUCLEAR REACTORS Description of Augment Desiccant Dryer (Sheet 2) COST (1975 $1000)I Ahfl flTIIP TflTAI BASIS FOR COST ESTIMATE ITEM itri,,, ........ .... OPERATING  
LABOR, SUPERVISION, 3.3 15 min/shift AND OVERHEAD MAINTENANCE
MATERIAL AND 6.1 5% of equipment including I&C LABOR CONSUMABLES, CHEMICALS, AND neg SUPPLIES UTILITIES
AND SERVICES Waste Disposal neg operating time does not require Water neg significant utilities and services Steam Electricity neg Building Services Other TOTAL 0 AND M ANNUAL COST 9.4 K K 1.  2.  3 4.C U'S.


Appendix B to RG 1.110, Page B-39 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS Description of Augment Steam Generator Flash Tank Vent to Main Condenser (Sheet 1) DIRECT COST (1975 $1,000) ITEM LABOR
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREAThENT
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT   - no equipment required
SYSTEM FOR LIGHT-WATER-COOLED  
2. BUILDING ASSIGNMENT  neg install in existing space
NUCLEAR REACTORS Description of Augment ITEM Charcoal Vault Refrigeration (Sheet 1)10AM DIRECT COST (1975 $1000)LAORFlIITDUdCNT/UATCDTA1 C YffAS IfC et.V BASIS FOR 1. PROCESS EQUIPMENT  
3. ASSOCIATED PIPING SYSTEMS 13 7 20 200 ft of 10-in pipe with 2 valves 4. INSTRUMENTATION AND CONTROLS 4 6 10 allowance
5. ELECTRICAL SERVICE  neg 
6. SPARE PARTS  neg  SUBTOTAL 17 13 30 
7. CONTINGENCY 2 1 3 10%
8. TOTAL DIRECT COSTS 19 14 33 


Appendix B to RG 1.110, Page B-40 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
===2. BUILDING ASSIGNMENT===
TER-COOLED NUCLEAR REACTORS Description of Augment Steam Generator Flash Tank Vent to Main Condenser (Sheet 2) DIRECT COST (1975 $1,000) ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD  1 allowance
3.  4.  5.  6.  7.  8.10 75 85 10-ton capacity, 3 refrigerators with drives, 32°F design I t 4-4 9 3 12 20' x 10' x 201 0 $2/ft 3 turbine building (nonshielded area)ASSOCIATED
2. MAINTENANCE MATERIAL AND
PIPING SYSTEMS In item 1 INSTRUMENTATION
LABOR  1 2% Total Direct Cost
AND CONTROLS 4 6 10 allowance ELECTRICAL
3. CONSUMABLES, CHEMICALS, AND
SERVICE 12 18 30 allowance SPARE PARTS 3 3 SUBTOTAL 35 105 140 CONTINGENCY
SUPPLIES  neg  4. UTILITIES AND SERVICES      Waste Disposal      Water  neg  Steam      Electricity      Building Services      Other   
3 11 14 10% TOTAL DIRECT COSTS 38 116 154 0 N 14 Ch (TftTAI
5. TOTAL O AND M ANNUAL COST  2 
K ANNUAL OPERATING  
AND MAINTENANCE  
COST ESTIMATE SHEET OF RADWASTE TREATMENT  
SYSTEM FOR LIGHT-WATER-COO.EO
NUCLEAR REACTORS Description of Augment Charcoal Vault Refriceration (Sheet 2)'TIn'COST (1975 $1000) rTeR TOTAL FOR COST OPERATING  
LABOR, SUPERVISION.


Appendix B to RG 1.110, Page B-41 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS Description of Augment 15-gpm Evaporator (Sheet 1) DIRECT COST (1975 $1,000)  ITEM LABOR
3.3 15 min/shift AND OVERHEAD MAINTENANCE
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 30 225 255 skid mounted, submerged tube bundle, ASME VIII, Incoloy in
MATERIAL AND LABOR 3.7 51 of equlpemt CONSUMABLES, CHEMICALS, AND in Item 2 SUPPLIES UTILITIES
AND SERVICES Waste Disposal Water Steam 0.5 electricity and cooling water Electricity Building Services Other TOTAL 0 AND M ANNUAL COST 7.5 K K 1. 2.  3.  4.  S.


contact with process fluid
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT
2. BUILDING ASSIGNMENT 68 34 102 evap & services 25 x 30 x 20 @ $6/ft 3 plus 2,000 ft
SYSTEM FOR LIGHT-WATER-COOLED
3 increase in solid waste storage area
NUCLEAR REACTORS Description of Augment Charcoal/HEPA
3. ASSOCIATED PIPING SYSTEMS 35 30 65 includes service piping
Filtration System -Condenser Vacuum Pump (Sheet 1)ITE4 1. PROCESS EQUIPMENT 2.  3.  4.  5.  6.  7.  8.LABOR__ ~ LrILumLAL
4. INSTRUMENTATION AND CONTROLS 10 10 20 allowance
IUIAL COST ESTIMATE D IRECT COST (1975 $1000)2 32.5 34.5 2000 CFM preftlter/4" charcoal bed/HEPA @ S15/cfm, 10 kw heater @ $250/kw BUILDING ASSIGNMENT  
5. ELECTRICAL SERVICE 40 25 65 allowance
3.1 1.5 4.6 Turbine building 8' x 16, x 12' @ $3/ft 3 (nonshielded area) ASSOCIATED
6. SPARE PARTS - 27 27 2% of item 1 plus tube bundle SUBTOTAL 183 351 534  
PIPING' SYSTEMS 1.3 0,7 2.0 allowance INSTRUMENTATION
7. CONTINGENCY 18 35 53 10%
AND CONTROLS in item 1 ELECTRICAL
8. TOTAL DIRECT COSTS 201 386 587 
SERVICE 1 1.5 2.5 SPARE PARTS 0.5 0.5 SUBTOTAL 7.4 36.7 44.1 CONTINGENCY
.7 3.7 4.4 10% TOTAL DIRECT COSTS 8.1 40.4 48.5 (Nm wO (i n *BASIS FOR I 
K K ANNUAL OPERATING
ANr MAINTENANCE
COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED
NUCLEAR REACTORS Description of Augment Charcoal/HEPA
Filtration System -Condenser Vacuum Pump (Sheet 2) COST (1975 $1000) 'ueD TfllhI RAmie FflQ tOI[IT F¢;TTMATF OPERATING
LABOR, SUPERVISION, neg used only during startup and shutdown AND OVERHEAD MAINTENANCE
MATERIAL AND 1.2 4 HEPA filters @ $150 & 2 Charcoal filters LABOR @ $900, change every 2 years CONSUMABLES, CHEMICALS, AND in items 2 and 4 SUPPLIES UTILITIES
AND SERVICES Waste Disposal 0.2 S50/HEPA filter, $100/Charcoal filter Water Steam Electricity Building Services Other 1.4 5. TOTAL 0 AND M ANNUAL COST_______________________
I _________
________ _______________________________
K I.2.  3.  4.'.4 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT
SYSTEM FOR LIGHT-WATER-COOLED
NUCLEAR REACTORS Description of Augment STT F M 1. PROCESS EQUIPMENT 2.  3. 4.  5.  6. 7. 8.Clean Steam to Turbine Glands (Sheot 1)I ARAR DIRECT COST (1975 $1000) FOIITDMFNTIMATPRTAI
ITEMP 15 150 TflTAI 165 BASIS FOR VCTttMATO 25,000 lb/hr reboiler I $4/lb/hr I $25K/H.P.


Appendix B to RG 1.110, Page B-42 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS Description of Augment 30-gpm Evaporator (Sheet 2) DIRECT COST (1975 $1,000) ITEM LABOR  
turbine glands BUILDING ASSIGNMENT
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 30 350 380 ASME VIII skid mounted, submerged, tube bundle, Incoloy in contact with process fluid
19 10 29 20' x 30' x 16' 6 $3/ft 3 ASSOCIATED
2. BUILDING ASSIGNMENT 88 44 132 evap + services - 25 x 40 x 20 @ $6/ft 3 plus 2,000 ft
PIPING SYSTEMS 32 18 50 equiv 1000 ft 0 $50/ft INSTRUMENTATION
3 increase in solid waste storage area
AND CONTROLS 8 12 20 in addition to Item I ELECTRICAL
3. ASSOCIATED PIPING SYSTEMS 35 35 70 includes service piping
SERVICE nag SPARE PARTS 5 5 SUBTOTAL 74 195 269 CONTINGENCY
4. INSTRUMENTATION AND CONTROLS 10 10 20 allowance
7 20 27 10% TOTAL DIRECT COSTS 81 215 296 r C r K K SYSTEM FOR LIGHT-WATER-COOLED  
5. ELECTRICAL SERVICE 40 25 65 allowance
NUCLEAR REACTORS Description of Augment Clean Steam to Turbine Glands (Sheet 2) COST (1975 $1000)1TR4 LABOR OTHER TOTAL BASIS FOR COST ESTIMATE OPERATING
6. SPARE PARTS - 27 27 2% of item 1 plus tube bundle SUBTOTAL 203 491 694  
LABOR, SUPERVISION, 3.3 15 min/shift AND OVERHEAD MAINTENANCE
7. CONTINGENCY 20 49 69 10%
MATERIAL AND 4.0 40 man-days LABOR CONSUMABLES, CHEMICALS, AND SUPPLIES UTILITIES
8. TOTAL DIRECT COSTS 223 540 763 
AND SERVICES Waste Disposal Water Steam 21.0 10 Btu/kw-hr heat rate increase Electricity Building Services Other TOTAL 0 AND M ANNUAL COST 28.3 ANNUAL OPERATING
AND MAINTENANCE
COST ESTIMATE SHEET OF RADWASTE TREATMENT 9'I. 2.  3. 4. 5.


Appendix B to RG 1.110, Page B-43 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS Description of Augment 50-gpm Evaporator (Sheet 3) DIRECT COST (1975 $1,000)  ITEM LABOR  
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 30 450 480 ASME VIII skid mounted, submerged, tube bundle, Incoloy in contact with
SYSTEM FOR LIGHT-WATER-COOLED
NUCLEAR REACTORS Description of Augment Clean Steam to Steam Valves 2 4" and Larger (Sheet 1)ITEM I AMII DIRECT COST (1975 $1000) n:*.:TDAACLIMATDTai PROCESS EQUIPMENT
100 120 220 22 valves @ $1OK/valve, use existing reboiler BUILDING ASSIGNMENT
neg install in existing space ASSOCIATED
PIPING SYSTEMS -in item 1 INSTRUMENTATION
AND CONTROLS -in Item 1 ELECTRICAL
SERVICE neg SPARE PARTS 5 SUBTOTAL 100 125 225 CONTINGENCY
10 12 22 10% TOTAL DIRECT COSTS 110 137 247 BASIS FOR 0 i%1J I.  2.  3.  4.  S.  6.  7.  8.(r TnTAI
-\ANNUAL OPERATING
AND MAINTENANCE
COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM1 FOR LIGHT-WATER-COOLED
NUCLEAR REACTORS Description of Augment Clean Steam to Steam Valves 24" and Larger (Sheet 2) COST (1975 $1000)TT!M LABOR OTHER TOTAL BASIS FOR COST ESTIMATE OPERATING
LABOR, SUPERVISION, 3.3 15 min/shift AND OVERHEAD MAINTENANCE
MATERIAL AND 4.0 40 man-days LABOR CONSUMABLES, CHEMICALS, AND neg SUPPLIES UTILITIES
hND SERVICES Waste Disposal Water Steam neg Electricity Building Services Other TOTAL 0 AND M ANNUAL COST 7.3 K 1.  2.  3.  4.w U,
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT  
SYSTEM FOR LIGHT-WATER-COOLED  
NUCLEAR REACTORS Description of Augment ITEM 1. PROCESS EQUIPMENT 2.  6.  3.  7.e .  w .h 4.  5.  6.  7.  8.Clean Steam to Steam Valves 2-1/2N and Less Than 24" (Sheet 1)LAB 0 DIRECT COST (1975 $1000) OR EQUIPMENT/MATERIALS
120 TOTAl_120 BASIS FOR  100 valves 0 $1200 each BUILDING ASSIGNMENT
--neg ASSOCIATED
PIPING SYSTEMS 40 20 60 INSTRUMENTATION
AND CONTROLS 10 20 30 allowance ELECTRICAL
SERVICE -none SPARE PARTS -6 6 SUBTOTAL 50 166 216 CONTINGENCY
5 17 22 10% TOTAL DIRECT COSTS 55 183 238 I (TOTAL COS ESTIMATE
K SYSTEM FOR LIGHT-WATER-COOLED
NUCLEAR REACTORS Description of Augment Clean Steam to Steam Valves 2-1/2" and Less Than 24" (Sheet 2)COST (1975 $1000)ITEM LABOR OTN!R OPERATING
LABOR, SUPERVISION, 3.3 15 min/shift AND OVERHEAD MAINTENANCE
MATERIAL AND 12.0 1% of direct cost of equipment LABOR CONSUMABLES, CHEMICALS, AND -in item 2 SUPPLIES UTILITIES
AND SERVICES Waste Disposal Water Steam neg Electricity Building Services Other TOTAL 0 AND H ANNUAL COST 15.3 A ANNUAL OPERATING
AND MAINTENANCE
COST ESTIMATE SHEET OF RADWASTE TREATMENT K-a a U'1.  2.  3.  4.  S.TNTAI
Description of Augment TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT
SYSTEM FOR LIGHT-WATER-COOLED
NUCLEAR REACTORS 15,000-cfm HEPA Filtration System -Auxiliary Building (Sheet 1)BASIS FOR rACT rCTTMATr II Anna flTl .r.. --.n .- L , I r. I~p~ ERq~ X rr...L./ n n. v, .., .1. PROCESS EQUIPMENT 40.0 45.0 prefilter/HEPA
@ $3/cfm, use existing fan BUILDING ASSIGNMENT
7 4.5 11.5 16' x 12' x 12' @ $5/ft 3 (nonshielded area) ASSOCIATED
PIPING SYSTEMS 3 2.0 5.0 INSTRUMENTATION
AND CONTROLS in item 1 ELECTRICAL
SERVICE base SPARE PARTS 0.5 0.5 SUBTOTAL 15 47.0 62.0 CONTINGENCY
1 5.0 6.0 10% TOTAL DIRECT COSTS 16 52.0 68.0 ((I ADflD DIRECT COST (1975 $1000) £rI"TDUCMT
MATrTAI C 5 TfllAI ,o L.  a'2.  3.  4.  5.  6.  7.  8.(
K FOR LIGHT-WATER-COOLED
NUCLEAR REACTORS Description of Augment 15,000-cfm HEPA Filtration System -Turbine Building (Sheet 2)I AflI DIRECT COST (1975 $1000) lI TDMCWNT IMATrOAIC TflTAL BASIS FOR COST ESTIMATE ITEM !L___ f ______________
PROCESS EQUIPMENT
5 40.0 45.0 skid mounted filter housing w/o fans BUILDING ASSIGNMENT
4.6 2.3 6.9 16' x 12' x 12' @ $3/ft 3 (nonshielded area) ASSOCIATED
PIPING SYSTEMS 3 2.0 5.0 INSTRUMENTATION
AND CONTROLS in item 1 ELECTRICAL
SERVICE base SPARE PARTS 0 0.5 0.5 SUBTOTAL 12.6 44.8 57.4 CONTINGENCY
2 4.0 6.0 10l TOTAL DIRECT COSTS 14.6 48.8 63.4 T TOTAL DIRECT COST ESTIMATE SHEET OF RADWASrE TREATMENT
SYSTEM K-I 1. 2.  3.  4.  5.  6.  7.  a.!
ANNUAL OPERATING
AND MAINTENANCE
COST ESTIMATE SHEET OF RADWASTE TREATMENT
SYSTEM FOR LIGHT-WATER-COOLED
NUCLEAR REACTORS Description of Augment 15,000-cfm HEPA Filtration ITEM LABOR System (Sheet 3) COST (1975 $1000)OTI4FR TflTAI OPERATING
LABOR, SUPERVISION, 3.8 15 min/shift
+ 40 hr annual test AND OVERHEAD MAINTENANCE
MATERIAL AND 2.2 change every 2 yrs @ $150/filter element LABOR CONSUMABLES, CHEMICALS, AND in items 2 and 4 SUPPLIES UTILITIES
AND SERVICES Waste Disposal 0.8 $50/filter element Water Steam Electricity
1.0 additional fan electrical load Building Services Other TOTAL 0 AND M ANNUAL COST 7.8 (I.  2.  3.I RACTC Frn rncT FCTIMATC 4.  5.I_
K TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT
SYSTEM FOR LIGHT-WATER-COOLED
NUCLEAR REACTORS Description of Augment 1000-cfm Charcoal/HEPA
Filtration System (Sheet 1)I TEM LABOR DIRECT COST (1975 $1000) EOUIPMENT/MATERIALS
TOTAL BASIS FOR COST ESTIMATE PROCESS EQUIPMENT  
2.0 22.0 24.0 prefllter/4" charcoal/HEPA
@ $20/cfm, 5 kw htr @ $400/kw BUILDING ASSIGNMENT
3.8 2.0 5.8 8' x 12' x 12' @ $5/ft 3 (nonshielded area) ASSOCIATED
PIPING SYSTEMS 1.3 .7 2.0 INSTRUMENTATION
AND CONTROLS in item 1 ELECTRICAL
SERVICE 1.5 1.0 2.5 SPARE PARTS 0.5 0.5 SUBTOTAL 8.6 26.2 34.8 CONTINGENCY
1.0 2.0 3.0 10% TOTAL DIRECT COSTS 9.6 28.2 37.8 K 0 I.  2.  3.  4.  5.  6.  7.  8.


process fluid
ANNUAL OPERATING
2. BUILDING ASSIGNMENT 97 48 145 10% more than 30 gpm
AND MAINTENANCE
3. ASSOCIATED PIPING SYSTEMS 35 35 70 allowance
COST ESTIMATE SHEET OF RADWASTE TREATMENT
4. INSTRUMENTATION AND CONTROLS 10 10 20 allowance
SYSTEM FOR LIGHT-WATER-COOLED
5. ELECTRICAL SERVICE 40 25 65 allowance  
NUCLEAR REACTORS Description of Augment 1000-cfm Charcoal/HEPA
6. SPARE PARTS - 27 27 2% of item 1 plus tube bundle  SUBTOTAL 212 595 807 
Filtration System (Sheet 2) COST (1975 $1000) ITEM LABOR OTHER TOTAL BASIS FOR COST £STII4ATF OPERATING
7. CONTINGENCY 21 60 81 10%  
LABOR, SUPERVISION, 1.9 20 min/day + 40 hr annual test AND OVERHEAD MAINTENANCE
8. TOTAL DIRECT COSTS 233 655 888  
14ATERIAL
AND .6 2 HEPA or prefilters
@ $150 each and 1 charcoal @ $900 each every 2 yrs' CONSUMABLES, CHEMICALS, AND in items 2 and 4 SUPPLIES UTILITIES
AND SERVICES Waste Disposal .1 $50/HEPA or prefilter, $100/charcoal Water filter Steam Electricity neg Building Services Other 5. TOTAL 0 AND M ANNUAL COST 2.6____________________________
____________
I I ( __ (1.  2.  -3.  0--
K TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT
SYSTEM FOR LIGHT-WATER-COOLED
NUCLEAR REACTORS Description of Augment 15,OOO-cfm Charcoal/HEPA
Filtration System -Auxiliary Building (Sheet 1)TTVM 1. PROCESS EQUIPMENT 2. 3.  4.  5.  6.  7.  8.LABOR 10 DIRECT COST (1975 $1000) EQUIPMENT/MATERIALS
71 TOTAL 81 BASIS FOR COST ESTIMATE prefilter/4" charcoal/HEPA
@ $5/cfm, 30kw htr @ $200/kw BUILDING ASSIGNMENT  
12 8 20 16' x 20' x 12' @ $5/ft 3 (nonshielded area) ASSOCIATED
PIPING SYSTEMS 3 2 5 INSTRUMENTATION
AND CONTROLS -In Item 1 ELECTRICAL
SERVICE 3 2 5 allowance SPARE PARTS 5 5 4 elements of each type SUBTOTAL 28 88 116 CONTINGENCY
3 9 12 10% TOTAL DIRECT COSTS 31 97 128 K a COST ESTIMATE ITE LABO.....
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT
SYSTEM FOR LIGHT-WATER-COOLED
NUCLEAR REACTORS Description of Augment I TEM 1. PROCESS EQUIPMENT 2.  3.  4.  5.  6.  7.  8.15,000-cfm Charcoal/HEPA
Filtration System -Turbine Building (Sheet 2)I fuND DIRECT COST (1975 $1000) CN "I lDMrLT ATEDIlA1 C ITEM x flMrnR 1.3 UTflYAI I_____ ARAL?~urIIn~LJIUL
UIt.IW BASIS FOR 10.0 71.0 81.0 prefilter/4*
charcoal/HEPA
@ $5/cfm, 30 kw htr @ $200/kw BUILDING ASSIGNMENT
7.7 3.8 11.5 16' x 20' x 121 @ $3/ft 3 (nonshielded area) ASSOCIATED  
PIPING SYSTEMS 3.0 2.0 5.0 INSTRUMENTATION  
AND CONTROLS in item 1 ELECTRICAL
SERVICE 3.0 2.0 5.0 allowance SPARE PARTS 5.0 5.0 4 elements each type SUBTOTAL 23.7 83.8 107.5 CONTINGENCY  
2.0 9.0 11.0 10% TOTAL DIRECT COSTS 25.7 92.8 118.5 r (0 .rg (
ANNUAL OPERATING
AND MAINTENANCE
COST ESTIMATE SHEET OF RADWASTE TREAThENT SYSTEM FOR LIGHT-WATER-COOLED
NUCLEAR REACTORS Description of Augment 15,O00-cfm Charcoal/HEPA
Filtration System (Sheet 3)COST (1975 $1000)ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE OPERATING
LABOR. SUPERVISION, 3.8 15 min/shift
& 40-hr annual test AND OVERHEAD MAINTENANCE
MATERIAL AND 9.0 30 HEPA or prefilters
@ $150 each & 15 LABOR charcoal filters @ $900 each every 2 yrs CONSUMABLES, CHEMICALS, AND in Items 2 and 4 SUPPLIES UTILITIES
AND SERVICES Waste Disposal 1.5 $S50/HEPA
or prefilter, $100/charcoal Water Steam Electricity
1.3 8kw additional fan power for filter aP Building Services 0.018.S/kw-hr Other TOTAL 0 AND M ANNUAL COST 15.6 K K 1.  2.  3. 4.0 5.


Appendix B to RG 1.110, Page B-44 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT  
TER-COOLED NUCLEAR REACTORS Description of Augment Evaporator - BWR Dirty Waste - Floor Drains (Sheet 4) DIRECT COST (1975 $1,000)  ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD  12 2.6 x 10
SYSTEM FOR LIGHT-WATER-COOLED  
6 gpy; 1000 hrs/yr labor
NUCLEAR REACTORS 30.00O-cfm Charcoal/HEPA
2. MAINTENANCE MATERIAL AND
Filtration System -Auxiliary Building (Sheet 1)i ARng~DIRECT COST (1975 $1000) FoII PI4FNTII4ATFRIALS
LABOR  30 71/2% of equipment costs
-¶ a 1n FnrMN/AEIL
3. CONSUMABLES, CHEMICALS, AND  
1. PROCESS EQUIPMENT 15 117.0 TOTAL 132.0 BASIS FOR COST ESTIMATE pref1lter/4" charcoal/HEPA
SUPPLIES  neg concentrate solidification chemicals in item 4  
@ $4/cfm, 60-kw htr @ $200/kw BUILDING ASSIGIMENT
4. UTILITIES AND SERVICES      Waste Disposal  70 100:1 feed to concentrate ratio
20 13.6 33.6 28' x 20' x 12' $S5/ft 3 (nonshielded area) ASOCIATED
@ $20/ft 3 disposal cost Water  27 1,000 gpm @ 1,500 hrs @ 30¢/1000 gal Steam  60 1,500 hrs steam @ 20,000 lb/hr @ $2/1,000 lbs  Electricity      Building Services      Other   
PIPING SYSTEMS 5 3.0 8.0 base INSTRUMENTATION
5. TOTAL O AND M ANNUAL COST  199  
AND CONTROLS -in item I ELECTRICAL
SERVICE 6 4.0 10.0 allowance SPARE PARTS 5.0 5.0 4 elements each type SUBTOTAL 46 142.6 188.6 CONTINGENCY
5 14.0 19.0 10% TOTAL DIRECT COSTS 51 156.6 207.6 C Description of Augment I ITU a 2.  3.  4.  5.  6. 7.  8.(
K TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT
SYSTEM FOR LIGHT-WATER-COOLED
NUCLEAR REACTORS Description of Augment 30,000-cfm Charcoal/HEPA
Filtration System -Turbine Building (Sheet 2)ITEM LAROR DIRECT COST (1975 $1000) !OtITPHt¶!rT/ATrR
TALS TflTA[BASIS FOR PROCESS EQUIPMENT
15.0 117.0 132.0 prefilter/4" charcoal/HEPA
@ $4/cfm, 60kw htr @ $200/kw BUILDING ASSIGNMENT
13.4 6.8 20.2 28' x 20' x 12' @ $3/ft 3 (nonshielded area) ASSOCIATED
PIPING SYSTEMS 3.0 5.0 8.0 base INSTRUMENTATION
AND CONTROLS in item 1 ELECTRICAL
SERVICE 6.0 4.0 10.0 allowance SPARE PARTS 5.0 5.0 4 elements each type SUBTOTAL 37.4 137.8 175.2 CONTINGENCY
4.0 14.0 18.0 l0 TOTAL DIRECT COSTS 41.4 151.8 193.2 y me 1.  2.  3.  4.  5.  6.  7. 8.


Appendix B to RG 1.110, Page B-45 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
ANNUAL OPERATING  
TER-COOLED NUCLEAR REACTORS Description of Augment Evaporator PWR Dirty Waste (Sheet 5) DIRECT COST (1975 $1,000) ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD  6.0 500,000 gpy; 500 hrs/yr labor
AND MAINTENANCE  
2. MAINTENANCE MATERIAL AND  
COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED  
LABOR   30.0 71/2% of equipment costs
NUCLEAR REACTORS Description of Augment 30.00O-cfm Charcoal/HEPA
3. CONSUMABLES, CHEMICALS, AND  
Filtration System -(Sheet 3)COST (1975 $1000)ITEM LABOR OTHER TOTAL BASIS FOR £OST FSTTMATF OPERATING  
SUPPLIES  - concentrate solidification chemicals in item 4  
LABOR, SUPERVISION, 3.8 15 min/shift
4. UTILITIES AND SERVICES     Waste Disposal   27.0 50:1 feed to concentrate ratio @  
+ 40 hr annual test AND OVERHEAD MAINTENANCE  
$20/ft 3 disposal cost Water  5.0 1,000 gpm @ 277 hrs @ 30¢/1,000 gal Steam  12.0 277 hrs steam @ 20,000 lbs/hr @ $2/1,000 lbs Electricity      Building Services      Other   
MATERIAL AND 18.0 60 HEPA or prefilters
5. TOTAL O AND M ANNUAL COST  80.0  
@ $150 each & 30 LABOR charcoal filters @ $900 each every 2 yrs CONSUMABLES, CHEMICALS, AND -in items 2 and 4 SUPPLIES UTILITIES
AND SERVICES Waste Disposal 3.0 $50/HEPA or preftilter, $1007charcoal filter Water Steam Electricity
2.6 16kw additional fan HP for filter @ Building Services 0.018 S/ku-hr Other TOTAL 0 AND M ANNUAL COST 27.4__ C 2.  " 3.  4. 5.-: -ý:r t- -.-J"
K TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT
SYSTEM FOR LIGHT-WATER-COOLED
NUCLEAR REACTORS Description of Augment ITEM 1. PROCESS EQUIPMENT 2. BUILDING 3. 4.  5. 6.  7.  8.Turbine Building Chilled Water HVAC System (Sheet 1) LABOR 300 DIRECT COST (1975 $1000) EOUJIPMFNTIMATFRIALS
TnIMNIAEIL
1 nA 500 TflTAI 800 BASIS FOR rnCT CTMATC 500-ton capacity, w/o air filters-t + I Coolers can be Installed in existing space saved by deletion of ductin


Appendix B to RG 1.110, Page B-46 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
====g. ASSOCIATED ====
TER-COOLED NUCLEAR REACTORS Description of Augment Evaporator - Conde nser Polisher Chemical Waste (Sheet 6) DIRECT COST (1975 $1,000) ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD   6.0 650,000 gpy; 500 hr/yr labor
PIPING SYSTEM; -in item 1 INSTRUMENTATION
2. MAINTENANCE MATERIAL AND  
AND CONTROLS -in item 1 ELECTRICAL
LABOR  30.0 71/2% of equipment costs  
SERVICE 40 so 90 SPARE PARTS -8 8 1% item 1 SUBTOTAL 340 558 898 CONTINGENCY
3. CONSUMABLES, CHEMICALS, AND  
34 56 90 10l TOTAL DIRECT COSTS 374 614 988 K 11 0 -J
SUPPLIES   concentrate solidification chemicals in item 4
ANNUAL OPERATING  
4. UTILITIES AND SERVICES     Waste Disposal   87.0 20:1 feed to concentrate ratio @
AND MAINTENANCE  
$20/ft 3 disposal cost  Water  6.5 1,000 gpm @ 360 hrs @ 30¢/1,000 gal Steam   14.4 360 hrs steam @ 20,000 lbs/hr @ $2/1,000 lbs  Electricity      Building Services     Other    
COST ESTIMATE SHEET OF RADWASTE TREATMENT  
5. TOTAL O AND M ANNUAL COST   143.9  
SYSTE14 FOR LIGHT-WATER-COOLED  
NUCLEAR REACTORS Description of Augment Turbine Building Chilled Water HVAC System (Sheet 2)COST (1975 $1000)ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE OPERATING  
LABOR, SUPERVISION, 3.3 15 min/shift AND OVERHEAD MAINTENANCE
MATERIAL AND 20.0 2-1/2% of equipment costs LABOR CONSUMABLES, CHEMICALS, AND -initem 2 SUPPLIES UTILITIES
AND SERVICES Waste Disposal Water 13.0 500 gpm @ 104/1000 gal & 50% load factor Steam Electricity
33.0 400 kw @ 0.018 $/kw hr Building Services Other TOTAL 0 AND M ANNUAL COST 69.3 C r I.  2.  3.  4..0 0 S.C
K Description of Augment K TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT.


Appendix B to RG 1.110, Page B-47 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
SYSTEM FOR LIGHT-WATER-COOLED
TER-COOLED NUCLEAR REACTORS Description of Augment Evaporator - Detergent Waste (Sheet 7) DIRECT COST (1975 $1,000) ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD   6.0 160,000 gpy; 500 hrs/yr
NUCLEAR REACTORS 600-ft 3 Waste Gas Decay Tank' (Sheet 1)I TFM LABOR DIRECT COST (1975 $1000) EOUIPMENT/MATERIALS
2. MAINTENANCE MATERIAL AND  
TOTAL BASIS FOR COST ESTIMATE PROCESS EQUIPMENT
LABOR  30.0 71/2% of equipment costs
2.5 20 22.5 600-ft 3 , 150 pslgo C.S., ASME VIII BUILDING ASSIGNMENT
3. CONSUMABLES, CHEMICALS, AND  
18.0 9 27.0 15' x 15' x 20' @ S6/ft 3 (shielded area) ASSOCIATED
SUPPLIES   - concentrate solidification chemicals in item 4
PIPING SYSTEMS 1.0 1 2.0 10% of item 1 INSTRUMENTATION
4. UTILITIES AND SERVICES     Waste Disposal   8.6 50:1 feed to concentrate ration
AND CONTROLS neg ELECTRICAL
@ $20/ft 3 disposal cost  Water  1.6 1,000 gpm @ 90 hrs @ 30¢/1,000 gal  Steam  3.6 90 hrs steam @ 20,000 lb/hr @ $2/1,000 lbs  Electricity     Building Services     Other    
SERVICE neg SPARE PARTS neg SUBTOTAL 21.5 30 51.5 CONTINGENCY
5. TOTAL O AND M ANNUAL COST   49.8   
2.0 3 5.0 10% TOTAL DIRECT COSTS 23.5 33 56.5 K I
ANNUAL OPERATING  
AND MAINTENANCE  
COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED  
NUCLEAR REACTORS Description of Augment 600-ft 3 Waste Gas Decay ITEM LABOR Tank (Sheet 2) COST (1975 $1000)OTHER TOTAL OPERATING  
LABOR, SUPERVISION, AND OVERHEAD neg MAINTENANCE
MATERIAL AND LABOR neg CONSUMABLES, CHEMICALS, AND SUPPLIES neg UTILITIES
AND SERVICES Waste Disposal Water Steam neg Electricity Building Services Other TOTAL 0 AND N ANNUAL COST neg I.  2.  3.  4.FflR  0 U' 0~e 5.(
K TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT
SYSTEM Description of Augment IT"M 1. PROCESS EQUIPMENT 2.  3.  4.  5.  6.  7.  8.FOR LIGHT-WATER-COOLED
NUCLEAR REACTORS PWR Hydrogen Recombiner (Sheet 1)IARno 50.0 DIRECT COST (1975 $1000)
TAI TflTAI I l :fTI b V VT nA. I 300.0 350.0 BASIS FOR rnqT vtTTMATF skid mounted, catalytic type w/condenser, partial I&C single unit, ASME VIII BUILDING ASSIGNM4ENT
28.8 14.4 43.2 15' x 30' x 16' 0 $6/ft 3 (shielded area) ASSOCIATED
PIPING SYSTEMS 32.0 13.0 45.0 allowance INSTRUMENTATION
AND CONTROLS 10.0 40.0 50.0 allowance ELECTRICAL
SERVICE 13.0 12.0 25.0 allowance SPARE PARTS -2.0 2.0 SUBTOTAL 133.8 381.4 515.2 CONTINGENCY
13.0 38.0 51.0 101 TOTAL DIRECT COSTS 146.8 419.4 566.2 K a Ue ANNUAL OPERATING
AND MAINTENANCE
COST ESTIMATE SHEET OF RADtWASTE
TREAThENT
SYSTEM FOR LIGHT-WATER-COOLED
NUCLEAR REACTORS Description of Augment PUR Hydrogen Recombiner (Sheet 2) COST (1975 $1000)ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE OPERATING
LABOR, SUPERVISION, 3.3 15 min/shift AND OVERHEAD MAINTENANCEMATERIAL
AND. 10.0 3% of equipment cost LABOR CONSUMABLES, CHEMICALS, AND 1.0 oxygen @.S2.5/103 cf & .25 cfm 0 SUPPLIES 7000 hrs UTILITIES
AND SERVICES Waste Disposal Water Steam neg Electricity Building Services Other TOTAL 0 AND M ANNUAL COST 14.3 1.  2.  3.  4.Ca I U'S.K C
Description of Augment ITEM 1. PROCESS EQUIPMENT 2.  3.  4.  5.  6.  7.  8.TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT
SYSTEM FOR LIGHT-WATER-COOLED
NUCLEAR REACTORS PWR Air EJector Charcoal/HEPA
Filtration Unit (Sheet 1)LABOR 3.0 DIRECT COST (1975 $1000) EOUIPMENT/MATERIALS
7.5 TOTAL 10.5 1*BASIS FOR COST ESTIMATE chiller, heater, charcoal HEPA BUILDING ASSIGNMENT
3.0 1.5 4.5 10' x 10' x 15' @ $3/ft 3 (unshielded turbine bldg) ASSOCIATED
PIPING SYSTEMS 2.0 1.0 3.0 allowance INSTRUMENTATION
AND CONTROLS 0.5 1.5 2.0 allowance ELECTRICAL
SERVICE 0.5 0.5 1.0 allowance SPARE PARTS 1.0 1.0 SUBTOTAL 9.0 13.0 22.0 CONTINGENCY
1.0 1.0 2.0 1O0 TOTAL DIRECT COSTS 10.0 14.0 24.0
ANNUAL OPERATING
AND MAINTENANCE
COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED
NUCLEAR REACTORS Description of Augnent PWR Air EJector Charcoal/HEPA
Filtration Unit (Sheet 2)COST (1975 $1000)ITEM LARAR___ .....________________
I , L ueA5 rwK Guil r.4IrMIE OPERATING
LABOR, SUPERVISION, 3.8 15 min/shift
+ 40 hr annual test AND OVERHEAD MAINTENANCE
MATERIAL AND 2.0 includes replacement filter LABOR CONSUMABLES, CHEMICALS, AND -in item 2 SUPPLIES UTILITIES
AND SERViCES Waste Disposal neg Water Steam Electricity Building Services Other TOTAL 0 AND M ANNUAL COST 5.8 flTIFD TnTAI l. 2.  3.  4.EP U'5.K DAete K K TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT
SYSTEM FOR LIGHT-WATER-COOLED
NUCLEAR REACTORS Description of Augment ITEM Steam Generator Flash LABOR Tank Vent to Main Condenser (Sheet DIRECT COST (1975 $1000) EQUIPMENT/MATERIALS
1)TOTAL BASIS FOR COST ESTIMATE PROCESS EQUIPMENT
-no equipment required BUILDING ASSIGNMENT
neg install In existing space ASSOCIATED
PIPING SYSTEMS 13 7 20 200 ft of 10-in pipe with 2 valves INSTRUMENTATION
AND CONTROLS 4 6 10 allowance ELECTRICAL
SERVICE neg SPARE PARTS neg SUBTOTAL 17,, 13 30 CONTINGENCY
2 1 3 10% TOTAL DIRECT COSTS 19 14 33 I.U't ull 2.  3.  4.  5.  6.7.  8.


Appendix B to RG 1.110, Page B-48 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS Description of Augment Evaporator Distillate Demineralizer (Sheet 1) DIRECT COST (1975 $1,000) ITEM LABOR  
ANNUAL OPERATING
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 4.0 20.0 24.0 30 ft
AND MAINTENANCE
3 , SS, ASME VIII, 150 psi nonregenerative, w/resin
COST ESTIMATE SHEET OF RADWASTE TREAThENT SYSTEM FOR LIGHT-WATER-COOLED  
2. BUILDING ASSIGNMENT 6.4 3.2 9.6 10 x 10 x 16 @ $6/ft 3 (shielded area)
NUCLEAR REACTORS Description of Augment Steam.Generator Flash Tank Vent to Main Condenser (Sheet 2) COST (1975 $1000)ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE OPERATING
3. ASSOCIATED PIPING SYSTEMS 9.0 6.0 15.0 2" piping
LABOR, SUPERVISION, 1 allowance AND OVERHEAD MAINTENANCE
4. INSTRUMENTATION AND CONTROLS 2.0 3.0 5.0 remote conductivity readout
MATERIAL AND 1 2% Total Direct Cost LABOR CONSUHABLES, CHEMICALS, AND neg SUPPLIES UTILITIES
5. ELECTRICAL SERVICE  neg 
AND SERVICES Waste Disposal Water neg Steam Electricity Building Services Other TOTAL 0 AND H ANNUAL COST 2 1. 2.  3. 4..a U'5.((
6. SPARE PARTS - 1.0 1.0  SUBTOTAL 21.4 33.2 54.6 
K TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT
7. CONTINGENCY 2.0 3.0 5.0 10%
SYSTEM FOR LIGHT-WATER-COOLED
8. TOTAL DIRECT COSTS 23.4 36.2 59.6 
NUCLEAR REACTORS Description of Augment lSqpm Evaporator (Sheet 1)I AnRO DIRECT COST (1975 $1000)PROCESS EQUIPMENT
30 225 255 skid mounted, submerged tube bundle, ASME VIII, Incoloy in contact with process fluid BASIS FOR


Appendix B to RG 1.110, Page B-49 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
===2. BUILDING ASSIGNMENT===
TER-COOLED NUCLEAR REACTORS Description of Augment Evaporator Distillate Demineralizer (Sheet 2) DIRECT COST (1975 $1,000)  ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 15. OPERATING LABOR, SUPERVISION, AND OVERHEAD  1.8 1,500 hrs operation @ 10% attendance
68 34 102 evap & services 25' x 301 x 20' @ $6/ft3 plus 2,000 ft3 increase in solid waste storage area ASSOCIATED
16. MAINTENANCE MATERIAL AND
PIPING SYSTEMS 35 30 65 inludes service piping INSTRUMENTATION
LABOR  2.0 allowance  
AND CONTROLS 10 10 20 allowance ELECTRICAL
17. CONSUMABLES, CHEMICALS, AND
SERVICE 40 25 65 allowance SPARE PARTS -27 27 2% of item 1 plus tube bundle SUBTOTAL 183 351 534 CONTINGENCY
SUPPLIES  2.3 1 change per yr @ $75/ft
18 35 53 10% TOTAL DIRECT COSTS 201 386 587 ITI'N 1.a.3.  4. 5. 6. 7. 8.
3 18. UTILITIES AND SERVICES      Waste Disposal  0.6 30 ft
3 @ $20/ft 3 disposal cost Water      Steam      Electricity      Building Services      Other   
19. TOTAL O AND M ANNUAL COST  6.7   


Appendix B to RG 1.110, Page B-50 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS Description of Augment 50-gpm Demineralizer (Sheet 1) DIRECT COST (1975 $1,000)  ITEM LABOR
Description of Augment tTrW TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREAThENT'SYSTEM  
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 5 20.0 25.0 30 ft
FOR LIGHT-WdATER-COOLED  
3 , SS, ASME VIII, 150 psi, nonregenerative, with resin
NUCLEAR REACTORS 30-gpm Evaporator (Sheet 2) , BASIS FOR rncT rCY?UAYT*.- -..rw-f .dV..r b.r ...I u snlrl.# ,nI .bl r~l) I lruI 1. PROCESS EQUIPMENT
2. BUILDING ASSIGNMENT 9 4.8 13.8 12 x 12 x 16 @ $6/ft 3  (shielded area)
3. ASSOCIATED PIPING SYSTEMS 9 6.0 15.0 2" piping
4. INSTRUMENTATION AND CONTROLS 4 6.0 10.0 
5. ELECTRICAL SERVICE  neg 
6. SPARE PARTS - 2.0 2.0 miscellaneous supplies  SUBTOTAL 27 38.8 65.8 
7. CONTINGENCY 2 4.0 6.0 10%
8. TOTAL DIRECT COSTS 29 42.8 71.8 


Appendix B to RG 1.110, Page B-51 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS Description of Augment 100-gpm Demineralizer (Sheet 2) DIRECT COST (1975 $1,000)  ITEM LABOR
===2. BUILDING ASSIGNMgNT===
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 5 35.0 40.0 60 ft
30 t 88 350 44 380 132 ASME VIII skid mounted, submerged, 'tube bundle, Incoloy in contact with process fluid evap + services -25' x 40' x 20' @ $6/ft 3 plus 2,000 ft 3 Increase In solid waste storage area ASSOCIATED
3 , SS, ASME VIII, 150 psi, nonregenerative, with resin
PIPING SYSTEMS 35 35 70 includes service piping INSTRUMENTATION
2. BUILDING ASSIGNMENT 9 4.8 13.8 12 x 12 x 16 @ $6/ft 3 (shielded area)
AND CONTROLS 10 10 20 allowance ELECTRICAL
3. ASSOCIATED PIPING SYSTEMS 10 10.0 20.0 21/2" piping  
SERVICE 40 25 65 allowance SPARE PARTS 27 27 2% of Item 1 plus tube bundle SUBTOTAL 203 491 694 CONTINGENCY
4. INSTRUMENTATION AND CONTROLS 4 6.0 10.0 
20 49 69 1O0 TOTAL DIRECT COSTS 223 540 763 C C I AfPtflD DIRECT COST (1975 $1000) rfIITDfMlrTIMATrDTAI
5. ELECTRICAL SERVICE   neg 
TnTA, CO 3. 4.  5. 6.  7.  8.
6. SPARE PARTS - 2.0 2.0 miscellaneous supplies SUBTOTAL 28 57.8 85.8  
7. CONTINGENCY 3 6.0 9.0  
8. TOTAL DIRECT COSTS 31 63.8 94.8 


Appendix B to RG 1.110, Page B-52 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS Description of Augment 200-gpm Demineralizer (Sheet 3) DIRECT COST (1975 $1,000) ITEM LABOR
K FOR LIGHT-WATER-COOLED  
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 5 60.0 65.0 120 ft
NUCLEAR REACTORS Description of Augment 50-qpm Evaporator (Sheet 3)ITEM 1. PROCESS EQUIPMENT 2.  3.  4.  S.  6.  7.  8.LABOR 30 DIRECT COST (1975 $1000) EOUIPMENT/MATERIALS
3 , SS, ASME VIII, 150 psi, nonregenerative, with resin
450 TOTAL 480 BASIS FOR COST ESTIMATE ASME VIII skid mounted, submerged, tube bundle, Incoloy In contact with process fluid BUILDING ASSIGNMENT  
2. BUILDING ASSIGNMENT 11 5.2 16.2 13 x 13 x 16 @ $6/ft 3  (shielded area)
97 48 145 10% more than 30 gpm ASSOCIATED  
3. ASSOCIATED PIPING SYSTEMS 12 12.0 24.0 4" piping
PIPING SYSTEMS 35 35 70 allowance INSTRUMENTATION
4. INSTRUMENTATION AND CONTROLS 4 6.0 10.0 
AND CONTROLS 10 10 20 allowance ELECTRICAL
5. ELECTRICAL SERVICE   neg 
SERVICE 40 25 65 allowance SPARE PARTS. 27 27 2% of Item 1 plus tube bundle SUBTOTAL 212 595 807 CONTINGENCY
6. SPARE PARTS - 2.0 2.0 miscellaneous supplies SUBTOTAL 32 85.2 117.2
21 60 81 10% TOTAL- DIRECT COSTS 233 655 888 T TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMErNT
7. CONTINGENCY 3 9.0 12.0  
SYSTEM'III a Description of Augment 50-gpm Evaporator (Sheet 3)
8. TOTAL DIRECT COSTS 35 94.2 129.2  
ANNUAL OPERATING
AND MAINTENANCE
COST ESTIMATE SHEET OF RADWASTE TREATMENT
SYSTEM FOR LIGHT-WATER-COOLED
NUCLEAR REACTORS Description of Augment
-RUR Dirty Ua~tm-Finn, £1 COST (1975 $1000)ITEM LABOR OT14ER TOTAL BASIS FOR LOST FSTIMATF OPERATING
LABOR, SUPERVISION, 12 2.6 x 106 gpy; 1000 hrs/yr labor AND OVERHEAD MAINTENANCE
MATERIAL AND 30 7-1/2% of equipment cost LABOR CONSUMABLES, CHEMICALS, AND neg concentrate solidification chemicats SUPPLIES in item 4 UTILITIES
AND SERVICES Waste Disposal 70 100:1 feed to concentrate ratio @ 20/ft 3 disposal cost Water 27 1000 gpm @ 1500 hrs @ 30t/1000 gal Steam 60 1500 hrs steaw @ 20,000 lb/hr @ $2/1000 lbs Electricity Building Services Other TOTAL 0 AND M ANNUAL COST 199 C C 1.  2. 3. 4.  5.


Appendix B to RG 1.110, Page B-53 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS Description of Augment 400-gpm Demineralizer - Steam Generator Blowdown Service (Sheet 4) DIRECT COST (1975 $1,000) ITEM LABOR
SYSTEM FOR LIGHT-WATER-COOLED  
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 5 60.0 65.0 120 ft
NUCLEAR REACTORS Description of Augment Evaporator PWR DirtylT YM[AROR Waste (Sheet 5) COST (1975 $1000)OTHER TOTAL BASIS FOR COST ESTTMATE OPERATING
3 , SS, ASME VIII, 150 psi, nonregenerative, with resin
LABOR, SUPERVISION, AND OVERHEAD 6.0 500,000 gpy; 500 hrs/yr labor MAINTENANCE
2. BUILDING ASSIGNMENT 11 5.2 16.2 13 x 13 x 16 @ $6/ft 3 (shielded area)
MATERIAL AND LABOR 30.0 7-1/2% of equipment cost CONSUMABLES, CHEMICALS, AND -concentrate solidification chemicals SUPPLIES in item 4 UTILITIES
3. ASSOCIATED PIPING SYSTEMS 20 20.0 40.0 6" piping
AND SERVICES 50:1 feed to concentrate ratio @ $20/ft 3 Waste Disposal 27.0 disposal cost Water 5.0 1000 gpm @.277 hrs @ 30t/1000 gal Steam 12.0 277 hrs steam @S 20,000 4bs/hr @ $2/1000 lbs Electricity Building Services Other TOTAL 0 AND M ANNUAL COST 80.0 ANNUAL OPERATING
4. INSTRUMENTATION AND CONTROLS 4 6.0 10.0 allowance
AND MAINTENANCE
5. ELECTRICAL SERVICE  neg  
COST ESTIMATE SHEET OF RADWASTE TREATMENT K I.  2.  3.  4.0'5.
6. SPARE PARTS - 2.0 2.0 miscellaneous supplies SUBTOTAL 40 93.2 133.2  
7. CONTINGENCY 4 9.0 13.0 
8. TOTAL DIRECT COSTS 44 102.2 146.2 


Appendix B to RG 1.110, Page B-54 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
ANNUAL OPERATING  
TER-COOLED NUCLEAR REACTORS Description of Augment BWR - 2nd Waste Demineralizer in Series (Sheet 5) DIRECT COST (1975 $1,000) ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD   3.3 15 min/shift
AND MAINTENANCE  
2. MAINTENANCE MATERIAL AND  
COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED  
LABOR   5.0 allowance
NUCLEAR REACTORS Description of Augment EvaDorator
3. CONSUMABLES, CHEMICALS, AND
-Condenser Polisher Chemical IaCto Ih +0 A COST (1975 $1000)ITEMFR CS UK LU ETIMATE OPERATING  
SUPPLIES  9.0 1 change per year @ 120 ft
LABOR, SUPERVISION, AND OVERHEAD 6.0 650.000 gpy; 500 hr/yr labor MAINTENANCE
3 @ $75/ft 3 (one vessel change per year, regardless of size)
MATERIAL AND LABOR 30.0 7-1/2% of equipment cost CONSUMABLES, CHEMICALS.
4. UTILITIES AND SERVICES      Waste Disposal  2.4 120 ft
3/yr @ $20/ft
3 disposal cost Water      Steam      Electricity      Building Services      Other   
5. TOTAL O AND M ANNUAL COST  19.7 


Appendix B to RG 1.110, Page B-55 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
AND concentrate solidification chemicals SUPPLIES In item 4 UTILITIES
TER-COOLED NUCLEAR REACTORS Description of Augment Demineralizer - PWR Clean Wastes (Sheet 6) DIRECT COST (1975 $1,000) ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD   1.8 10% of BRS shim bleed (50,000 gpy), 30 min/day
AND SERVICES Waste Disposal 87.0 20:1 feed to concentrate ratio @ $20/ft 3 Wl7.0 disposal cost Water 6.5 1000 gpm 0 360 hrs @ 30*/10OO gal Steam 14.4 360 hrs steam @ 20,000 lb/hr @ $2/1000 lbs Electricity Building Services Other LABOR 0ATD AU TC4TAI TOTAL 0 AND M ANNUAL COST 143.9 C 0 1.  2.  3.  4.  5.(v K SYSTEM FOR LIGHT-WATER-COOLED  
2. MAINTENANCE MATERIAL AND  
NUCLEAR REACTORS Description of Augment-hla~aum*., Um.4.a Iqkaa÷ COST (1975. $1000)TT!M LABOR OTHER TOTAL BASIS FOR COST ESTIMATE OPERATING  
LABOR   5.0 allowance
LABOR, SUPERVISION, AND OVERHEAD 6.0 160,000 gpy; 500 hrs/yr MAINTENANCE
3. CONSUMABLES, CHEMICALS, AND  
MATERIAL AND LABOR 30.0 7-1/25 of equipment cost CONSUMABLES, CHEMICALS, AND -concentrate solidification chemicals In SUPPLIES item 4 UTILITIES  
SUPPLIES   2.3 30 ft
AND SERVICES Waste ITsposal 8.6 50:1 feed to concentrate ratio 0 $20/ft 3 disposal cost Water 1.6 1000 gpm 0 90 hrs 0 30t/1000 gal Steam 3.6 90 hrs steam 0 20,000 lb/hr 1 $2/1000 lbs Electricity Building Services Other TOTAL 0 AND M ANNUAL COST 49.8 ANNUAL OPERATING
3/yr @ $75/ft
AND MAI[NTENANCE
3 4. UTILITIES AND SERVICES     Waste Disposal  0.6 30 ft3/yr @ $20/ft
COST ESTIMATE SHEET OF RADWASTE TREATMENT K I.  2.  3.  4.ad a, LeD 5.
3 disposal cost Water     Steam     Electricity     Building Services     Other    
5. TOTAL O AND M ANNUAL COST   9.7  


Appendix B to RG 1.110, Page B-56 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
Description of Augment TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT  
TER-COOLED NUCLEAR REACTORS Description of Augment Demineralizer - BWR Dirty Waste (Sheet 7) DIRECT COST (1975 $1,000)  ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD  6.5 2.6 x 10
SYSTEM FOR LIGHT-WATER-COOLED  
6 gpy, 30 min/shift
NUCLEAR REACTORS Evaporator Distillate Demineralizer (Sheet 1)TTIrM I anAD DIRECT COST (1975 $1000) EniI nlrT IUA?~nAi e*,-. I.rluvn Iuu~rnllu~r'¶l KhMiLR IJI/L W,5MII EIHMAIT PROCESS EQUIPMENT
2. MAINTENANCE MATERIAL AND
4.0 20.0 24.0 30 ft 3 , SS. ASME VIII, 150 psi nonregenerative, w/resin BUILDING ASSIGNMENT
LABOR  5.0 allowance
6.4 3.2 9.6 10' x 10' x 16' @ $6/ft 3 (shielded area) ASSOCIATED
3. CONSUMABLES, CHEMICALS, AND
PIPING SYSTEMS 9.0 6.0 15.0 2" piping INSTRUMENTATION
SUPPLIES  64.5 860 ft
AND CONTROLS 2.0 3.0 5.0 remote conductivity readout ELECTRICAL
3 resin @ $75/ft
SERVICE neg SPARE PARTS 1.0 1.0 SUBTOTAL 21.4 33.2 54.6 CONTINGENCY
3 4. UTILITIES AND SERVICES      Waste Disposal  17.2 860 ft
2.0 3.0 5.0 10% TOTAL DIRECT COSTS 23.4 36.2 59.6 BASIS FOR C (1. 2.i Ot 3.  4. 5. 6.  7.  8.(qrft*IrA I
3 @ $20/ft 3 disposal cost Water      Steam      Electricity      Building Services      Other   
)K SYSTEM FOR LIGHT-WATER-COOLED
5. TOTAL O AND M ANNUAL COST   93.2 
NUCLEAR REACTORS Description of Augment Evaporator Distillate Demineralizer (Sheet 2) COST (1975 $1000)YtM I ARnlQ OTHER TOTAL BASIS FOR COST ESTIMATE aI1II ____________
OPERATING
LABOR, SUPERVISION.


Appendix B to RG 1.110, Page B-57 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
1.8 1500 hrs operation
TER-COOLED NUCLEAR REACTORS Description of Augment Demineralizer - PWR Dirty Wastes (w/o turbine building) (Sheet 8) DIRECT COST (1975 $1,000)  ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD   3.3 500,000 gpy; 15 min/shift
@ 10% attendance AND OVERHEAD MAINTENANCE
2. MAINTENANCE MATERIAL AND  
MATERIAL AND LABOR 2.0 allowance CONSUMABLES, CHEMICALS, AND SUPPLIES 2.3 1 change per yr @ $75/ft 3 UTILITIES  
LABOR   5.0 allowance  
AND SERVICES Waste Disposal 0.6 30 ft 3 @ $20/ft 3 disposal cost Water Steam Electricity Building Services Other TOTAL 0 AND M ANNUAL COST 6.7 ANNUAL OPERATING
3. CONSUMABLES, CHEMICALS, AND  
AND MAINTENANCE
SUPPLIES   12.0 160 ft
COST ESTIMATE SHEET OF RADWASTE TREATMENT I.  2.  3.  4.,ap 5.
3/yr @ $75/ft
3 4. UTILITIES AND SERVICES     Waste Disposal   3.2 160 ft
3/yr @ $20/ft
3 disposal cost Water     Steam     Electricity     Building Services     Other    
5. TOTAL O AND M ANNUAL COST   23.5


Appendix B to RG 1.110, Page B-58 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT  
TER-COOLED NUCLEAR REACTORS Description of Augment Demineralizer - PWR Turbine Building Floor Drains (Sheet 9) DIRECT COST (1975 $1,000) ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD  13.1 1 hr/shift, 2.6 x 10
SYSTEM FOR LIGHT-WATER-COOLED  
6 gpy 2. MAINTENANCE MATERIAL AND
NUCLEAR REACTORS Description of Augment 50-opDemintralzer Sh t 1)ITEM LAROR DIRECT COST (1975 $1000) 1ITOM AUIFRAI It TIhTAI BASIS FOR CflCY 1T tMAr" PROCESS EQUIP4ENT
LABOR  5.0 allowance
5 20.0 25.0 30 ft 3.SS, VIII. 150 psi, nonreganerative, with resin BUILDING ASSIGNMENT
3. CONSUMABLES, CHEMICALS, AND
9 4.8 13.8 12' x 12' x 16' 0 $6/ft 3 (shielded ASSOCIATED
SUPPLIES  64.5 860 ft
PIPING SYSTEMS 9 6.0 15.0 2" piping INSTRUMENTATION
3 resin @ 75/ft
AND CONTROLS 4 6.0 10.0 ELECTRICAL
3 4. UTILITIES AND SERVICES      Waste Disposal  17.2 860 ft
SERVICE No SPARE PARTS 2.0 2.0 miscellaneous supplies SUBTOTAL 27 38.8 66.8 CONTINGENCY
3/yr @ $20/ft
2 4.0 6.0 10% TOTAL DIRECT COSTS 29 42.8 -71.8 C 1.  2. 3.  4.  5.  6.  7.  8.(C SO-gin
3 disposal cost Water      Steam      Electricity      Building Services      Other   
{Sheet 1)
5. TOTAL O AND M ANNUAL COST  99.8  
K Description of Augment K TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT
SYSTEM FOR LIGHT-WATER-COOLED
NUCLEAR REACTORS 1O0-9pm Deminerallizer (Sheet 2) LANOR DIRECT COST (1975 $1000) PMFNT/MATFRTALS
TOTAL BASIS FOR COST FSTTMATF PROCESS EQUIPMENT
5 35.0 40.0 60 ft 3 , SS, ASME VIII, 150 psi, nonregenerative, with resin BUILDING ASSIGNMENT
9 4.8 13.8 12' x 12' x 16' 0 $6/ft 3 (shielded area) ASSOCIATED
PIPING SYSTEMS 10 10.0 20.0 2-1/21 piping INSTRUMENTATION
AND CONTROLS 4 6.0 10.0 ELECTRICAL
SERVICE neg SPARE PARTS 2.0 2.0 miscellaneous supplies SUBTOTAL 28 57.8 85.8 CONTINGENCY
3 6.0 9.0 TOTAL DIRECT COSTS 31 63.8 94.8 I.  2.  3." 4. 5.a,  6.  7.  B.


Appendix B to RG 1.110, Page B-59 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
TOTAL DIRECT COST ESTIMATE SHEET OF RADWAST!E
TER-COOLED NUCLEAR REACTORS Description of Augment Demineralizer - PWR Steam Generator Blowdown (Sheet 10) DIRECT COST (1975 $1,000) ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD  3.3 15 min/shift
TREATMENT  
2. MAINTENANCE MATERIAL AND  
SYSTEM FOR LIGHT-WATER-COOLED  
LABOR  5.0 allowance
NUCLEAR REACTORS Description of Augment 20-plDmneralizer(Sheet  
3. CONSUMABLES, CHEMICALS, AND
3)__ITEM 1. PROCESS EQUIPMENT 2.  3.  4.  5.  6.  7.  8.LABOR 5 1T A DIRECT COST (1975 $1000) EflUIPI4FNTII4ATFRTAL 60.0 TflTAI 65.0 BASIS FOR rnCT r~tTuATr 120 ft 3 , SS, ASME VIII, i50 psi, nonregenerative, with resin BUILDING ASSIGNMENT
SUPPLIES  16.9 225 ft
11 5.2 16.2 13' x 13' x 16' 0 $6/ft 3 ___(shielded area) ASSOCIATED
3 resin/yr @ $75/ft
PIPING SYSTEMS 12 12.0 24.0 4" piping INSTRUMENTATION
3 4. UTILITIES AND SERVICES      Waste Disposal  4.5 225 ft
AND CONTROLS 4 6.0 10.0 ELECTRICAL
3/yr @ $20/ft
SERVICE neg SPARE PARTS 2.0 2.0 miscellaneous supplies SUBTOTAL 32 85.2 117.2 CONTINGENCY
3 disposal cost  Water      Steam      Electricity      Building Services      Other   
3 9.0 12.0 TOTAL DIRECT COSTS 35 94.2 129.2 ((200-gpm Oemtneraltzer (Sheet 3)
5. TOTAL O AND M ANNUAL COST  29.7 
K Description of Augment 400-gpm Demineralizer
-Steam Generator Blowdown Service (Sheet 4)I TrM 1. PROCESS EQUIPMENT 2.  3. 4. 5.  6.  7.  8.lAROR DIRECT COST (1975 $1000) EOUJIPMNT/MATERjALS
TOTAL BASIS FOR COST ESTIMATE T I COST ESTIMATE 5 60.0 65.0 120 ft 3 , SS. ASME VIII, 150 psi, nonregenerative.


Appendix B to RG 1.110, Page B-60 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS Description of Augment 20-gpm Cartridge Filter (Sheet 1) DIRECT COST (1975 $1,000) ITEM LABOR
with resin BUILDING ASSIGNMENT
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 2.0 5.0 7.0 SS, ASME VIII, 150 psi
11 5.2 16.2 ,3' x 13' x 16' @ $6/ft 3 (shielded area) ASSOCIATED
2. BUILDING ASSIGNMENT 5.6 3.0 8.6 16 x 12 x 20 @ $6/ft 3 (shielded area)  
PIPING SYSTEMS 20 20.0 40.0 6" piping INSTRUMENTATION
3. ASSOCIATED PIPING SYSTEMS 1.5 1.0 2.5 allowance
AND CONTROLS 4 6.0 10.0 allowance ELECTRICAL
4. INSTRUMENTATION AND CONTROLS 0.6 2.4 3.0 allowance
SERVICE neg SPARE PARTS 2.0 2.0 miscellaneous supplies SUBTOTAL 40 93.2 133.2 CONTINGENCY
5. ELECTRICAL SERVICE  neg  
4 9.0 13.0 TOTAL DIRECT COSTS 44 102.2 146.2 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT
6. SPARE PARTS - 0.5 0.5  SUBTOTAL 9.7 11.9 21.6  
SYSTEM FOR LIGHT-WATER-COOLED
7. CONTINGENCY 1.0 1.0 2.0 10%
NUCLEAR REACTORS a, 'a ANNUAL OPERATING
8. TOTAL DIRECT COSTS 10.7 12.9 23.6  
AND MAINTENANCE
COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED  
NUCLEAR REACTORS Description of Augment BWR-2nd Waste Demineralizer In Serf es (Sheet El COST (1975 $1000)ITEM_...._-_....__,,__ ,v-n -DROIO rvr uK EV)lr.1 ~PY.I OPERATING
LABOR, SUPERVISION, 3.3 15 min/shift AND OVERHEAD MAINTENANCE
MATERIAL AND LABOR 5.0 allowance CONSUMABLES, CHEMICALS, AND 9.0 1 change per year @ 120 ft 3 0 $75/ft 3 (one SUPPLIES vessel change per year. regardless of size) UTILITIES
AND SERVICES Waste Disposal 2.4 120 ft 3 lyr * $20/ft 3 disposal cost Water Steam Electricity Building Services Other TOTAL 0 AND M ANNUAL COST 19.7 1. 2. 3.  4.a -.J a 5.C lABOR NTNrD TJlTA!
K ANNUAL OPERATING
AND MAINTENANCE
COST ESTIMATE SHEET OF RADWASTE TREATMENT
SYSTEM FOR LIGHT-WATER-COOLED
NUCLEAR REACTORS Description of Augment Demineralizer
-PWR Clean Wastes (Sheet 6) COST (197k. $1000)YY IPLu I flTurD?linI matie fflS EflM? rCTTMATe AILr IlV% -lll_ __ _ Ifl, &'flC I l nV bl *fll OPERATING
LABOR, SUPERVISION, 1.8 10% of DRS shim bleed (50,000 gpy), AND OVERHEAD 30 min/day MAINTENANCE
MATERIAL AND LABOR 5.0 allowance CONSUMABLES, CHEMICALS, AND 3 3 SUPPLIES 2.3 30 ft /yr @ $75/ft3 UTILITIES
AND SERVICES Waste Disposal 0.6 30 ft 3/yr @ $20/ft 3 disposal cost Water Steam Electricity Building Services Other TOTAL 0 AND M ANNUAL COST 9.7 I 1. 2.  3.  4.a S.


Appendix B to RG 1.110, Page B-61 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
ANNUAL OPERATING
TER-COOLED NUCLEAR REACTORS Description of Augment Cartridge Filter (Sheet 2) DIRECT COST (1975 $1,000) ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD   4.5 10 changes @ 10 man-hrs/change @ $12/hr + 15 min/shift  
AND MAINTENANCE
2. MAINTENANCE MATERIAL AND  
COST ESTIMATE SHEET OF RADIASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED
LABOR   1.0 allowance  
NUCLEAR REACTORS Description of Augment Demineralizer
3. CONSUMABLES, CHEMICALS, AND  
-BWR Dirty Waste (Sheet 7)COST (1975 $1000)JTFN[ABDR nlTHVg TNlT61 DACIC mnD r.ncT reTvUnt OPERATING
SUPPLIES   1.0 10 changes/yr @ $100/change
LABOR, SUPERVISION, AND OVERHEAD 6.5 2.6 x 106 gpy, 30 min/shift MAINTENANCE
4. UTILITIES AND SERVICES     Waste Disposal   1.5 10 drums/yr @ $20/ft
MATERIAL AND LABOR 5.0 allowance CONSUNABLES, CHEMICALS, AND33 SUPALES 64.5 860 ft 3 resin 0 $75/ft 3 UTILITIES
3 Water      Steam     Electricity     Building Services     Other    
AND SERVICES Waste Disposal 17.2 860 ft 3 @ $20/ft 3 disposal cost Water Steam Electricity Building Services Other TOTAL 0 AND N ANNUAL COST 93.2 C I.  2.  3.  4.N S.---I C
5. TOTAL O AND M ANNUAL COST   8.0  
K ANNUAL OPERATING  
AND MAINTENANCE  
COST ESTIMATE SHEET OF RADWASTE TREATMENT  
SYSTEM FOR LIGHT-WATER-COOLED  
NUCLEAR REACTORS Description of Augment Demineraltzer
-PWR Dirty.Wastes (w/o turbine building) (Sheet 8) COST (1975 $1000)ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE OPERATING  
LABOR, SUPERVISION, AND OVERHEAD 3.3 500,000 gpy; 15 min/shift MAINTENANCE
MATERIAL AND LABOR 5.0 allowance CONSUMABLES, CHEMICALS, AND SUPPLIES 12.0 160 ft 3/yr @ $75/ft 3 UTILITIES
AND SERVICES Waste Disposal 3.2 160 ft 3/yr @ $20/ft 3 disposal cost water Steam Electricity Building Services Other TOTAL 0 AND M ANNUAL COST 23.5 l.  2.  3.  4.a 5./
ANNUAL OPERATIN AND
COST ESTIMTE SHEET OF RADWASTE TREATMENT
of Aujnmant flminapA147AP
.DUo*7m,
* pww-ITEM T. -a .* C1 *fm r uVfm "a 1.411W4b 7I COST (1975 $1000)--______ .... ..-. ",,' ,,,. urwl, rvuK I.UF)I LtIY:llrl OPERATING
LABOR, SUPERVISION.


Appendix B to RG 1.110, Page B-62 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS Description of Augment 100-gpm Precoat Filter (Sheet 1) DIRECT COST (1975 $1,000)  ITEM LABOR  
AND OVERHEAD 13.1 1 hr/shift, 2.6 x 106 opy MAINTENANCE
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 10 65.0 75 automated system 1 gpm/ft
MATERIAL AND LABOR 5.0 allowance CONSUMABLES, CHEMICALS, AND SUPPLIES 64.5 660 ft 3 resin 0 $75/ft 3 UTILITIES
2 , ASME VIII
AND SERVICES Waste Disposal 17.2 860 ft 3/yr 9 $20/ft 3 disposal cost Water Steam Electricity Building Services Other TOTAL 0 AND N ANNUAL COST 99.8 I ARMR flTIIFA 1.  2. 3. 4.a S.(r SYSTEM FOR L.IGHT, oWATER-COOLEO
2. BUILDING ASSIGNMENT 18 9.0 27 15 x 15 x 20 @ $6/ft 3  (shielded area)
NUCL..EAR,, REACTORS oAeTe -1-:j:.1i-:i...-
3. ASSOCIATED PIPING SYSTEMS 16 9.0 25 35% of equipment cost
..........
4. INSTRUMENTATION AND CONTROLS    in item 1  
-."(
5. ELECTRICAL SERVICE 7 13.0 20 allowance
K Description of Augment Demineralizer
6. SPARE PARTS - 2.0 2 2% of item 1  SUBTOTAL 51 98.0 149 
-PIER tim Steam Generator Blowdomn (Sheet 10) COST (1975 $1000)nyu,..O inaI OPERATING
7. CONTINGENCY 5 10.0 15 10%
LABOR, SUPERVISION.
8. TOTAL DIRECT COSTS 56 108.0 164 


Appendix B to RG 1.110, Page B-63 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS Description of Augment 400-gpm Precoat Filter (Sheet 2) DIRECT COST (1975 $1,000)  ITEM LABOR
AND OVERHEAD 3.3 15 min/shift MAINTENANCE
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 35 135.0 170 automated system; 1 gpm/ft
MATERIAL AND LABOR 5.0 allowance CONSUMABLES, CHEMICALS, AN" SUPPLIES 16.9 225 ft 3 resin/yr @ $75/ft 3 UTILITIES
2 ASME VIII
AND SERVICES Waste Disposal 4.5 225 ft 3/Yr I $20/ft 3 disposal cost Water Stem Electricity Building Services Other TOTAL 0 AND M ANNUAL COST 29.7 A..UAL OPERATING
2. BUILDING ASSIGNMENT 24 12.0 36 15 x 20 x 20 @ $6/ft 3 (shielded area)
AND MAINTENANCE
3. ASSOCIATED PIPING SYSTEMS 31 16.0 47 35% of equipment cost
COST ESTIMATE SHEET OF RADWASTE TREATMENT  
4. INSTRUMENTATION AND CONTROLS - - - item 1
SYSTEM FOR LIGHT-WATER-COOLED  
5. ELECTRICAL SERVICE 12 18.0 30 allowance
NUCLEAR REACTORS 2.  3. 4.ens rtnt ReTtMAta a I alLfl9 S.
6. SPARE PARTS - 3.0 3  SUBTOTAL 102 184.0 286 
7. CONTINGENCY 10 18.0 28 10%
8. TOTAL DIRECT COSTS 112 202.0 314 


Appendix B to RG 1.110, Page B-64 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT  
TER-COOLED NUCLEAR REACTORS Description of Augment Precoat Filter - BWR Dirty Waste (Sheet 3) DIRECT COST (1975 $1,000) ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD  6.6 2 x 10
SYSTEM FOR LIGHT-WATER-COOLED  
6 gpy, 30 min/shift
NUCLEAR REACTORS Description of Augment 20-qp Cartridge Filter (Sheet 1)TTFM I  DIRECT COST (1975 $1000) vN Itur ¶ u'IIAqr rD lr e... t.J UIhLU 11MAT PROCESS EQUIPMENT
2. MAINTENANCE MATERIAL AND  
2.0 5.0 7.0 SS, ASME VIII, 150 psi BUILDING ASSIGNMENT
LABOR  10.0 allowance  
5.6 3.0 8.6 16' x 12' x 20' S $6/ft 3 (shielded area) ASSOCIATED
3. CONSUMABLES, CHEMICALS, AND
PIPING SYSTEMS 1.5' 1.0 2.5 allowance INSTRUMENTATION
SUPPLIES  6.0 10 lbs precoat @ 10¢/lb per 1,000 gal processed
AND CONTROLS 0.6 2.4 3.0 allowance ELECTRICAL
4. UTILITIES AND SERVICES      Waste Disposal  40.0 1 ft
SERVICE neg SPARE PARTS 0.5 0.5 SUBTOTAL 9.7 11.9 21.6 CONTINGENCY
3/sludge per 1,000 gal processed @ $30/ft
1.0 1.0 2.0 10% TOTAL DIRECT COSTS 10.7 12.9 23.6 BASIS FOR-.4 Q at 1.  2.  3.  4. 5.  6.  7.  8.(20-qm Cartrtd9e Ftlter (Sheet 1)
3 disposal cost  Water      Steam      Electricity      Building Services      Other   
ANNUAL OPERATING
5. TOTAL O AND M ANNUAL COST  62.6 
AND MAINTENANCE
COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED
NUCLEAR REACTORS Description of Augment Cartridge Filter (Sheet 2) COST (1975 $1000)A'1JCDl RAM!S FOR COST ESTIMATE ITEM LADUK uini n , -... ...... .... ... .. OPERATING
LABOR. SUPERVISION, 4.5 10 changes @ 10 man-hrs/change AND OVERHEAD @ $12/hr + 15 min/shift MAINTENANCE
MATERIAL AND LABOR 1.0 allowance CONSUMABLES.


Appendix B to RG 1.110, Page B-65 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS Description of Augment 2-gpm Reverse Osmosis (Sheet 1) DIRECT COST (1975 $1,000)  ITEM LABOR
CHEMICALS, AND SUPPLIES 1.0 10 changes/yr
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 6.0 60.0 66.0 skid mounted w/500-gal SS feed tank, ASME VIII
@ $100/change UTILITIES
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
AND SERVICES Waste Disposal 1.5 10 drums/yr @ $20/ft 3 Water Steam Electricity Building Services Other TOTAL 0 AND M ANNUAL COST 8.0 1. 2.  3. 4. 5.
4. INSTRUMENTATION AND CONTROLS  - in item 1  
5. ELECTRICAL SERVICE 7.0 13.0 20.0 allowance
6. SPARE PARTS - 6.0 6.0  SUBTOTAL 35.2 90.6 125.8  
7. CONTINGENCY 3.0 9.0 12.0 10%
8. TOTAL DIRECT COSTS 38.2 99.6 137.8 


Appendix B to RG 1.110, Page B-66 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREAT1ENT
TER-COOLED NUCLEAR REACTORS Description of Augment Reverse Osmosis - Detergent Wastes DIRECT COST (1975 $1,000) ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD   3.1 160,000 gpy, 1300 hrs/yr @ 20% attendance
SYSTEM FOR LIGHT-WATER-COOLED
2. MAINTENANCE MATERIAL AND  
NUCLEAR REACTORS Description of Augment 100-gpim Precoat Filter (Shoot 1)ITEM LARnR DIRECT COST (1975 $1000) fIW01T P~NT uI~dTIDTAI
LABOR   8.8 4% less bldg + 24 module with 3-yr life @ $600 each
PROCESS EQUIPMENT
3. CONSUMABLES, CHEMICALS, AND  
10 65.0 75 automated system 1 gpm/ft 2 , ASM4E VIII BUILDING ASSIGNMENT
SUPPLIES  neg  4. UTILITIES AND SERVICES      Waste Disposal  4.3 100:1 vol reduction @ $20/ft
18 9.0 27 15' x 15' x 20' 0 $6/ft 3 (shielded area) ASSOCIATED
3 disposal cost  Water      Steam      Electricity  neg  Building Services      Other   
PIPING SYSTEM4S 16 9.0 25 35% of equipment cost INSTRUMENTATION
5. TOTAL O AND M ANNUAL COST  16.2 
AND CONTROLS in item 1 ELECTRICAL
SERVICE 7 13.0 20 allowance SPARE PARTS 2.0 2 2% of item 1 SUBTOTAL 51 98.0 149 CONTINGENCY
5 10.0 15 10% TOTAL DIRECT COSTS 56 108.0 164 BASIS FOR 0 1.  2.  3.  4.  5.  6.  7.  8.(r i lO0-gpm Precoat Ftlter (Sheet 1)
K FOR LIGHT-WATER-COOLED
NUCLEAR REACTORS Description of Augment 400-oam Precoat Filter T  LAROR DIRECT COST (1975 $1000) EOUIPMENT/MATERIALS
TOTAL BASIS FOR COST ESTIMATE PROCESS EQUIPMENT
35 135.0 170 automated system; 1 gpm/ft 2 ASME Viii BUILDING ASSIGNMENT
24 12.0 36 15' x 20' x 20' @ $6/ft 3 (shielded area) ASSOCIATED
PIPING SYSTEMS 31 16.0 47 35% of equipment cost INSTRUMENTATION
AND CONTROLS --item I ELECTRICAL
SERVICE 12 18.0 30 allowance SPARE PARTS -3.0 3 SUBTOTAL 102 184.0 286 CONTINGENCY
10 18.0 28 10% TOTAL DIRECT COSTS 112 202.0 314 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT
SYSTEM K (Sheet 2)-J 1.  2.  3.  4.  5.  6.  7.  8.(Sheet 2)-vT 
ANNUAL OPERATING  
AND MAINTENANCE  
COST ESTI1ATE SHEET OF RADWASTE TREATMENT  
SYSTEM FOR LIGHT-WATER-COOLED  
NUCLEAR REACTORS Description of Augment Precoat Filter -BWR Dirty Waste (Sheet 3) COST (1975 $1000)ITEM LABOR OTHER TOTAL BASIS FOR COST !STTI4ATF OPERATING  
LABOR, SUPERVISION, AND OVERHEAD 6.6 2 x 106 gpy, 30 min/shift MAINTENANCE
MATERIAL AND LABOR 10.0 allowance CONSUMABLES, CHEMICALS, AND 6.0 10 lbs precoat @ lOt/lb per 1000 gal SUPPLIES processed


Appendix B to RG 1.110, Page B-67 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS Description of Augment 10,000-Gallon Tank (Sheet 1) DIRECT COST (1975 $1,000) ITEM LABOR
===4. UTILITIES ===
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 3 28 31 SS, ASME VIII, atmospheric service, 200°F
AND SERVICES Waste Disposal Water Steam Electricity Building Services Other 40.0 TOTAL 0 AND M ANNUAL COST j[ 62.6 1 ft 3/sludge per disposal cost 1000 qal processed
2. BUILDING ASSIGNMENT 30 15 45 15 x 20 x 25 @ $6/ft 3 (shielded area)
@ $30/ft 3 C 1. 2.  3.S.(
3. ASSOCIATED PIPING SYSTEMS 2 1 3 10% of item 1  
T TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT  
4. INSTRUMENTATION AND CONTROLS 4 6 10 allowance
SYSTEM FOR LIGHT-WATER-COOLED  
5. ELECTRICAL SERVICE  neg  
NUCLEAR REACTORS Description of Augment 2-com Reverse TTIFM LABOR DIRECT COST (1975 $1000) FOUlPMENTIMATFRIALS
6. SPARE PARTS - - neg  SUBTOTAL 39 50 89 
TOTAL BASIS FOR COST ESTIMATF PROCESS EQUIPIENT
7. CONTINGENCY 4 5 9 10%  
6.0 60.0 66.0 skid mounted w/500-gal SS feed tank, ASME VIII BUILDING ASSIGNMENT
8. TOTAL DIRECT COSTS 43 55 98 
19.2 9.6 28.8 12' x 25' x 16' @ $6/ft 3 ASSOCIATED
PIPING SYSTEMS 3.0 2.0 5.0 allowance INSTRUMENTATION
AND CONTROLS in item I ELECTRICAL
SERVICE 7.0 13.0 20.0 allowance SPARE PARTS 6.0 6.0 SUBTOTAL 35.2 90.6 125.8 CONTINGENCY
3.0 9.0 12.0 10% TOTAL DIRECT COSTS 38.2 99.6 137.8 K 0 1.  2.  3.  4. 5.  6. 7.  8.Osmosis (Sheet 1)
ANNUAL OPERATING
AND MAINTENANCE
COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED
NUCLEAR REACTORS Description of Augment Reverse Osmosis -Detergent Wastes COST (1975 $1000)ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE OPERATING
LABOR, SUPERVISION, AND OVERHEAD 3.1 160.000 gpy, 1300 hrs/yr @ 20% attendance MAINTENANCE
MATERIAL AND 8.8 4% less bldg + 24 module with 3-yr life LABOR @ $600 each CONSUMABLES, CHEMICALS.


Appendix B to RG 1.110, Page B-68 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
AND SUPPLIES neg UTILITIES
TER-COOLED NUCLEAR REACTORS Description of Augment 10,000-Gallon Tank (Sheet 2) DIRECT COST (1975 $1,000) ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD  1.1 5 min/shift - log level readings
AND SERVICES Waste Disposal 4.3 100:1 vol reduction
2. MAINTENANCE MATERIAL AND
@ $20/ft 3 disposal cost Water Steam Electricity neg Building Services Other TOTAL 0 AND M ANNUAL COST 16.2 r C 1.  2.  3.  4.No 5.(
LABOR  1.6 1/2% of equipment
FOR LIGHT-WATER-COOLED  
3. CONSUMABLES, CHEMICALS, AND  
NUCLEAR REACTORS Description of Augment 1O,000-Gallon Tank__(Sheet  
SUPPLIES  neg 4. UTILITIES AND SERVICES      Waste Disposal      Water      Steam  neg   Electricity      Building Services      Other   
1)?tTrM 1. PROCESS EQUIPMENT 2.  3.  4.  5.  6.  7.  8.I AROR 3 DIRECT COST (1975 $1000) !0IJ!P?4fNT/MATERIALS
5. TOTAL O AND M ANNUAL COST   2.7 
TOTAL T -28 31 BASIS FOR COST ESTIMATE SS, ASME VIII, atmospheric service, 200°F BUILDING ASSIGNMENT
30 15 45 15' x 20' x 25' @ $6/ft 3 (shielded area) ASSOCIATED
PIPING SYSTEMS 2 1 3 10% of item 1 INSTRUMENTATION
AND CONTROLS 4 6 10 allowance ELECTRICAL
SERVICE neg SPARE PARTS neg SUBTOTAL 39 s0 89 CONTINGENCY
4 5 9 10% TOTAL DIRECT COSTS 43 55 98 C w 10tOOO-GallonTapk (Sheet 1)TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT
SYSTEM
ANNUAL OPERATING
AND MAINTENANCE
COST ESTIMATE SHEET OF RADWASTE TREAThENT
SYSTEM FOR LIGHT-WATER-COOLED
NUCLEAR REACTORS Description of Augment 10000-Gallon Tank (Sheet 2) COST (1975 $1000)ITEM LABOR OTHER TOTAL RA~l flD  OPERATING
LABOR, SUPERVISION.


Appendix B to RG 1.110, Page B-69 REFERENCES TO APPENDIX B
AND OVERHEAD 1.1 5 min/shift
1. U.S. Atomic Energy Commission (USAEC), "Guide for Economic Evaluation of Nuclear Reactor Plant Designs," USAEC Report NUS-531, NUS Corporation, January 1969.
-log level readings MAINTENANCE
MATERIAL AND LABOR 1.6 1/2% of equipment CONSUMABLES.


2. "Wage Rates for Key Construction Trades,"  
CHEMICALS, AND neg SUPPLIES UTILITIES
Engineering News Record, pp. 36-37, January 2, 1975.
AND SERVICES Waste Disposal Water Steam neg Electricity Building Services Other TOTAL 0 AND N ANNUAL COST 2.7 1.  2.  3.  4.  5.(
REFERENCES
TO APPENDIX B 1. "Guide for Economic Evaluation of Nuclear Reactor Plant Oesigns," USAEC Report NUS-531, NUS Corporation, January 1969.  2. "Wage Rates for Key Construction Trades," Engineering News Record, pp. 36-37, January 2, 1975.  3. "Projections of Labor Requirements for Electric Power Plants Construction, 1974 -2000," USAEC Report WASH-1334, Washington, D.C., August 1974.1.110-85 APPENDIX C DATA NEEDED FOR RADIIASTE
TREATMENT
SYSTEM COST-BENEFIT
ANALYSIS FOR LIGHT-WATER
COOLED NUCLEAR REACTORS This appendix describes information that should be submitted in support of radwaste treat ment system cost-benefit analyses for light-water-cooled nuclear reactors.


3. USAEC, "Projections of Labor Requirements for Electric Power Plants Construction,  1974-2000," USAEC Report WASH-1334, Washington, DC, August 1974.
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.


Appendix C to RG 1.110, Page C-1 APPENDIX C
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:  
  DATA NEEDED FOR RADWASTE TREATMENT SYSTEM  COST-BENEFIT ANALYSIS FOR LIGHT-WATER-COOLED 
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.
NUCLEAR REACTORS
This appendix describes information that should be submitted in support of radwaste treatment system cost-benefit analyses for light-water-cooled nuclear reactors.  The information should be consistent with the contents of the safety analysis report (SAR) and environmental report (ER) for the proposed reactor.  Appropriate sections of the SAR and ER containing more detailed discussions of the required information should be referenced as appropriate.  Each response, however, should be independent of the SAR and ER. All responses should be on a per reactor basis and should provide the following information:  
1. Detailed cost estimate sheets similar to those shown on the following pages listing all parameters (and their bases) used in determining capital, operating, and maintenance costs associated with all augments considered in the cost-benefit analysis.  All costs should be stated in terms of 1975 dollars.


2. The cost of borrowed money used in the cost analysis and the method of arriving at this cost.
All costs should be stated in terms of 1975 dollars.


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:
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.


a. Decontamination factors assigned to each augment and fraction of "on-line" time assumed (i.e., hours per year used).  
Include the following information:
b. Parameters and method used to determine th e 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.1.110-87 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE'TREATMENT-SYSTEH
FOR LIGHT-WATER-COOLED
NUCLEAR REACTORS Description of Augment i Tru 1 AflfD DIRECT COST (1975 $1000) FflIIIPMFNT/MATFRlALS


Appendix C to RG-1.110, Page C-2 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS Description of Augment  DIRECT COST (1975 $1,000)  ITEM LABOR
===1. PROCESS EQUIPMENT ===
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT    
2. BUILDING ASSIGNMENT   
3. ASSOCIATED PIPING SYSTEMS   
4. INSTRUMENTATION AND CONTROLS   
5. ELECTRICAL SERVICE   
6. SPARE PARTS      SUBTOTAL   


===7. CONTINGENCY    ===
===2. BUILDING ASSIGNMENT===
8. TOTAL DIRECT COSTS   
t I 1 I I I I I ASSOCIATED
PIPING SYSTEMS BASIS FOR COST ESTIMATE I I I I --INSTRUMENTATION
AND CONTROLS I I I I ELECTRICAL
SERVICE I I I I 6. SPARE PARTS______________________I
i mI SUBTOTAL________________________________________________________
1 -I I I CONTINGENCY
I I I TOTAL DIRECT COSTS________________________________________________________
________________
I __________________________________________________
_____________
_______________________________________________
C TOTAL 0 3.  4.  S.7.  8.(C i aunD EnUTPMENTIMATERIALS
ANNUAL OPERATING
AND MAINTENANCE
COST ESTIMATE SHEET OF RADWASTE TREATMENT
SYSTEM FOR LIGHT-WATER-COOLED
NUCLEAR REACTORS 0 "I U 2 2 -4 U 2 2 C, a 9 9 'a w -J 04 0.j 'a "4 a.  0 "4 COST (1975 $1000)I TIFM


Appendix C to RG-1.110, Page C-3 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
===1. OPERATING ===
TER-COOLED NUCLEAR REACTORS Description of Augment  DIRECT COST (1975 $1,000)  ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD     2. MAINTENANCE MATERIAL AND  
LABOR, SUPERVISION, AND OVERHEAD MAINTENANCE  
LABOR     3. CONSUMABLES, CHEMICALS, AND  
MATERIAL AND LABOR CONSUMABLES, CHEMICALS, AND SUPPLIES UTILITIES  
SUPPLIES     4. UTILITIES AND SERVICES     Waste Disposal     Water     Steam     Electricity     Building Services     Other    
AND SERVICES Waste Disposal Water Steam Electricity Building Services Other TOTAL 0 AND M ANNUAL COST LABOR OTHER TOTAL BASIS FOR COST ESTIMATE Description of Augment U K 2. 3.  4.  5.ITEM}}
5. TOTAL O AND M ANNUAL COST    
*U.S. Government Printing Office: 1987-202-292:60255}}


{{RG-Nav}}
{{RG-Nav}}

Revision as of 03:29, 21 September 2018

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

REGULATORY

GUIDE OFFICE OF STANDARDS

DEVELOPMENT

REGULATORY

GUIDE 1.110 COST-BENEFIT

ANALYSIS FOR RADWASTE S LIGHT-WATER-COOLED

NUCLEAR PDWE& CRS'March 1976 4 USNRC REGULATORY

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

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

fegulatione.

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

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

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

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

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

  1. 0F imPtoSetfitC

it #hbae gtaldel We entcouraged S Materialt end Plant Protection

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

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

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

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

Office of Standerde Development TABLE OF CONTENTS Page

A. INTRODUCTION

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

1.110-5

B. DISCUSSION

R

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

1.110-5 C. REGULATORY

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

1.110-6 D. IMPLE14ENTATION

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

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

1.110-6 APPENDIX A, PROCEDURES

FOR PERFORMING

COST-BENEFIT

ANALYSES ...........................

1.110-7 APPENDIX B. BASES FOR PARAMETERS

USED IN PERFORMING

COST-BENEFIT

ANALYSES ..............................................................................

1.110-17 LIST OF APPENDIX B COST ESTIMATE SHEETS ...............................................

1.110-19 REFERENCES

TO APPENDIX B ..............................................................

1.110-85 APPENDIX C, DATA NEEDED FOR RADWASTE TREATMENT

SYSTEM COST-BENEFIT

ANALYSIS FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS ......................................

1.110-86 SAMPLE ESTIMATE SHEETS ................................................................

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

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

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

1.110-10 A-3 Annual Maintenance Costs -Gaseous Radwaste Augments;

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

1.110-12 A-4 Labor Cost Correction Factors ...........................................

1.110-13 A-5 Indirect Cost Factors ...................................................

1.110-14 A-6 Capital Recovery Factors ................................................

1.110-15 B-1 Indirect Costs ..........................................................

1.110-18 LIST OF FIGURES Figure Page A-1 Electric Power Supply Areas in the United States ........................

1.110-16 1.110-4

A. INTRODUCTION

Section I1.D of Appendix I, "Numerical Guides for Design Objectives and Limiting Conditions for Operation to Meet the Criterion

'As Low As Is Reasonably Achievable'

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

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

and Sections IL.A, 11.8, and II.C (which address doses to nearby individuals)

is required to meet the criterion, "as low as is reasonably achievable." To'implement the requirements of Appendix I, the NRC staff has developed a series of guides providing methods acceptable to the staff for the calculation of effluent releases, dispersion of effluents in the atmosphere and different water. bodies, associated radiation doses to man, and cost-benefit aspects of treating radwastes.

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

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

B. DISCUSSION

Each applicant for a permit to construct or a license to operate a light-water-cooled nuclear power reactor and each licensee with a license to operate a light-water-cooled nuclear power reactor is required to provide reasonable assurance that the design objectives for as low as is reasonably achievable effluent releases are satisfied by the liquid and gaseous radwaste system designs. It is the objective of this guide to provide an acceptable method of performing cost-benefit analysis, in conformance with Section II.D of Appendix I, to demonstrate that the plant design includes all items of reasonably demonstrated technology for reducing the cumula tive population dose due to releases of radioactive materials from the reactor to levels as low as reasonably achievable.

As an interim measure the Conmnission chose values of $1000 per man rem and $1000 per man-thyroid-rem (or lesser values if demonstrated to be suitable for a particu lar site) to be used to implement the cost-benefit analysis.

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

Since the worth of a man-rem or man-thyroid-rem to the public is subject to the same fluctuations in value as the cost of equipment to reduce radioactive emissions, the NRC staff believes this approach to be reasonable.

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

The methodology and cost parameters are presented in Appendix A to this guide. The costs presented.

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

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

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

Liquid and gaseous radwaste system augments considered in the analysis should be selected in order of diminishing cost-benefit returns.

3. All costs should be given in terms of 1975 dollars (as is the $1000 per man-rem cost with which they are compared).

Allowances for Inflation after 1975 should not be factored into the cost estimates.

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

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

0. IMPLEMENTATION

The purpose of this section is to provide information to license applicants and licensees regarding the NRC staff's plan for using this regulatory guide. Except in those cases in which the applicant proposes an acceptable alternative method for complying with specified portions of the Commission's regulations, the method described herein will be used in the evaluation of construction permit applications docketed after June 4, 1976 unless this guide is revised as a result of suggestions from the public or additional staff review. If an applicant wishes to use this regulatory guide in developing submittals for applications docketed on or before June 4, 1976, the pertinent portions of the application will be evaluated on the basis of this guide.1.110-6 APPENDIX A PROCEDURES

FOR PERFORMING

COST-BENEFIT

ANALYSES This appendix contains guidance for performing cost-benefit analyses on individual system augments, as well as the parameters needed for estimating costs. The bases for the parameters and worksheets appropriate for use with the following cost-benefit procedure are given in Appendix B. 1. The cumulative population man-rem exposure and man-thyroid-rem exposure should be determined for each effluent release source, e.g., liquid radwaste releases, ventilation releases, etc. 2. Potential reductions to the cumulative population exposure should be determined based on the addition of items of reasonably demonstrated technology which have the potential to reduce releases of radioactive materials.

3. Acceptable methods for performing some of the calculations need for items 1 and 2 above are contained in Regulatory Guides 1.109, "Calculation of Annual Doses to.Man from Routine Releases of Reactor Effluents for the Purpose of Evaluating Compliance with 10 CFR Part 50, Appendix I," and 1.111, "Methods for Estimating Atmospheric Transport and Dispersion for Gaseous Effluents in Routine Releases from Light-Water-Cooled Reactors," and in two regulatory guides now in prepara tion on the subjects of (1) calculation of releases of radioactive materials In liquid and gas eous effluents from light-water-cooled reactors and (2) methods for estimating aquatic dispersion of liquid effluents from routine reactor releases for the purpose of implementing Appendix I. 4. The total annual cost of each augment considered in item 2 above should be determined as follows: a. The Total Direct Cost (TOC): (1) Obtain the direct cost of equipment and materials from Table A-1. (2) Multiply the direct labor cost obtained from Table A-1 by the appropriate labor cost correction factor from Table A-4 to obtain the corrected labor cost for the geographtcal area from Figure A-l, in which the plant is to be built. (3) Add the costs obtained from steps (1) and (2) to obtain the Total Direct Cost. b. Obtain-the appropriate Indirect Cost Factor (ICF) from Table A-S. c. Determine Total Capital Cost (TCC) by using the equation:

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

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

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

TAC

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

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

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

553 255 808 3-ton Charcoal Adsorber 53 14 67 Desiccant Dryer 218 176 394 Charcoal Vault Refrigeration

116 38 154 Main Condenser Vacuum Pump Charcoal/HEPA

Filtration System 40 8 48 Clean Steam to Turbine Glands 81 215 296 Clean Steam to Steam Valves. 24" and Larger 137 110 247 Clean Steam to Steam Valves, 2-1/2" and Less Than-24" 183 55 238 15,000-cfm HEPA Filtration System 52(49)* 16(14)* 68(63)* 1,000-cfm Charcoal/HEPA

Filtration System 28 10 38 15,000-cfm Charcoal/HEPA

Filtration System 97(93) 31(26) 128(119) 30,000-cfm Charcoal/HEPA

Filtration System 157(152) 51(41) 208(193) Turbine Bldg. Chilled Water HVAC System 614 374 988 600-ft 3 Gas Decay Tank 33 24 57 PWR Hydrogen Recombiner

419 147 566 PWR Air Ejector Charcoal/HEPA

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

19 14 33 In cases where the equipment may be located either in the auxiliary building or the turbine building and common usage does not indicate a definite preference of one location or the other, cost for both locations are listed with the turbine building location cost in parenthesis.

1.110-8 TABLE A-1 (Continued)

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

30-gpm Evaporator

50-gpm Evaporator Evaporator Distillate Demineralizer

50-gpm Demineralizer

100-gpm Demineralizer

200-gpm Deminieralizer

400-gpm Demineralizer

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

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

COSTS -GASEOUS RADWASTE AUGMENTS BWR Offgas Recoatbiner

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

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

Filtration System 15,000-cfm Charcoal/HEPA

Filtration System 30,000-cfm Charcoal/HEPA

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

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

COSTS -LIQUID RADWASTE AUGMENTS Evaporation

-PWR Dirty Waste Evaporation

-BWR Dirty Waste Evaporation

-Condensate Polisher Chemical Waste Evaporation

-Detergent Waste Demineralization

-kvaporator Distillate Demineralization

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

ANNUAL OPERATING

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

-PWR Clean Waste Demineralization

-BWR Dirty Waste Demineralization

-PWR Dirty Waste Demineralization

-PWR Turbine Bldg. Drains Desmineralization

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

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

BWR Offgas Recombiner

20 3-ton Charcoal Adsorber neg Desiccant Dryer 6 Charcoal Vault Refrigeration

3 Main Condenser Vacuum Pump Charcoal/HEPA

Filtration System 1 Clean Steam to Turbine Glands 4 Clean Steam to Steam Valves, 24" and Larger 4 Clean Steam to Steam Valves, 2-1/2" and Less Than 24" 12 15,000-cfm HEPA Filtration System 2 1,000-cfm Charcoal/HEPA

Filtration System 0.6 15,O00-cfm Charcoal/HEPA

Filtration System 9 30,000-cfm Charcoal/HEPA

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

10 PWR Air Ejector Charcoal/HEPA

Filtration Unit 2 Steam Generator Flash Tank Vent to Main Condenser

1 ANNUAL MAINTENANCE

COSTS -LIQUID RADWASTE AUGMENTS 15-gpm Evaporator

30 30-gpm Evaporator

30 50-gpm Evaporator

30 Evaporator Distillate Demineralizer

2 50-gpm Demineral izer 5 lO0-gpmi Demineralizer

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

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

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

APPENDIX B BASES FOR PARAMETERS

USED IN PERFORMING

COST-BENEFIT

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

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

Variations of labor costs and productivity with site locaticns are considered.*

All costs are based on the assumption that the reactor is in the design stage and that augmentation of a radwaste system will not involve backfltting of an existing plant. Backfltttng costs should be determined on a case-by-case basis. 1. Capital Costs Capital costs are reported by grouping items by system and by plant location, which gen erally follow the NRC (AEC) accounting system given in NUS-531 (Ref. 1). The direct costs considered to be applicable to radwaste systems are structures, electrical services, equipment, and instrumentation and controls.

Spare parts and a contingency allowance**

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

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

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

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

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

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

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

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

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

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

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

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

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

1.110-24 Charcoal Vault Refrigeration

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

1.110-26 Charcoal/HEPA

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

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

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

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

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

1.110-36 1000-cfa Charcoal/HEPA

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

1.110-39 15.000-cfm Charcoal/HEPA

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

1.110-41 30,000-cfm Charcoal/HEPA

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

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

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

1.110-49 PIW Hydrogen Recombiner

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

1.110-S1 PiW Air Ejector Charcoal/HEPA

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

1.110-53 Stem Generator Flash Tank Vent to rain Condenser

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

1.110-55 Evaporators

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

1.110-57 Evaporator Distillate Demineralizer

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

1.110-64 Demineralizers

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

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

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

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

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

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

SYSTEM FOR LIGHT-WATER-COOLED

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

1 IVIML COST ESTIMATE DIRECT COST.(1975

$1000) r1 T DMUT'/MATrD

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

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

PIPING SYSTEMS 18 12 30 augment piping connections only INSTRUM4ENTATION

AND CONTROLS 24 96 120 allowance ELECTRICAL

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

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

w BWR Off %e Darr-M---

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

AND MAINTENANCE

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

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

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

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

AND SERVICES Waste Disposal Water Steam neg intemittent;

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

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment !TFM 1. PROCESS EQUIPENT

2. BUILDING ASSIGNMENT

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

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

PIPING SYSTES -in item I INSTRUKENTATION

AND CONTROLS neg ELECTRICAL

SERVICE neg SPARE PARTS none existing SUBTOTAL 13 48.5 61.5 CONTINGENCY

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

AND MAINTENANCE

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

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

LABOR. SUPERVISION.

neg AND OVERHEAD MAINTENANCE

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

CHEMICALS, AND SUPPLIES neg lifetime use of charcoal assumed UTILITIES

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

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

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

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

PIPING SYSTEMS 10 5 15 augment piping connections only INSTRUMENTATION

AND CONTROLS 12 48 60 allowance ELECTRICAL

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

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

K ANNUAL CPERATING

AND MAINTENANCE

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

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

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

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

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

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREAThENT

SYSTEM FOR LIGHT-WATER-COOLED

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

2. BUILDING ASSIGNMENT

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

PIPING SYSTEMS In item 1 INSTRUMENTATION

AND CONTROLS 4 6 10 allowance ELECTRICAL

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

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

K ANNUAL OPERATING

AND MAINTENANCE

COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COO.EO

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

LABOR, SUPERVISION.

3.3 15 min/shift AND OVERHEAD MAINTENANCE

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

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

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment Charcoal/HEPA

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

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

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

PIPING' SYSTEMS 1.3 0,7 2.0 allowance INSTRUMENTATION

AND CONTROLS in item 1 ELECTRICAL

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

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

K K ANNUAL OPERATING

ANr MAINTENANCE

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

NUCLEAR REACTORS Description of Augment Charcoal/HEPA

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

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

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

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

I _________

________ _______________________________

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

SYSTEM FOR LIGHT-WATER-COOLED

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

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

turbine glands BUILDING ASSIGNMENT

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

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

AND CONTROLS 8 12 20 in addition to Item I ELECTRICAL

SERVICE nag SPARE PARTS 5 5 SUBTOTAL 74 195 269 CONTINGENCY

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

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

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

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

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

AND MAINTENANCE

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

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

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

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

neg install in existing space ASSOCIATED

PIPING SYSTEMS -in item 1 INSTRUMENTATION

AND CONTROLS -in Item 1 ELECTRICAL

SERVICE neg SPARE PARTS 5 SUBTOTAL 100 125 225 CONTINGENCY

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

-\ANNUAL OPERATING

AND MAINTENANCE

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

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

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

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

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

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

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

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

--neg ASSOCIATED

PIPING SYSTEMS 40 20 60 INSTRUMENTATION

AND CONTROLS 10 20 30 allowance ELECTRICAL

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

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

K SYSTEM FOR LIGHT-WATER-COOLED

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

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

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

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

AND MAINTENANCE

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

Description of Augment TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

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

@ $3/cfm, use existing fan BUILDING ASSIGNMENT

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

PIPING SYSTEMS 3 2.0 5.0 INSTRUMENTATION

AND CONTROLS in item 1 ELECTRICAL

SERVICE base SPARE PARTS 0.5 0.5 SUBTOTAL 15 47.0 62.0 CONTINGENCY

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

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

K FOR LIGHT-WATER-COOLED

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

PROCESS EQUIPMENT

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

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

PIPING SYSTEMS 3 2.0 5.0 INSTRUMENTATION

AND CONTROLS in item 1 ELECTRICAL

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

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

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

ANNUAL OPERATING

AND MAINTENANCE

COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

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

LABOR, SUPERVISION, 3.8 15 min/shift

+ 40 hr annual test AND OVERHEAD MAINTENANCE

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

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

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

K TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment 1000-cfm Charcoal/HEPA

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

TOTAL BASIS FOR COST ESTIMATE PROCESS EQUIPMENT

2.0 22.0 24.0 prefllter/4" charcoal/HEPA

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

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

PIPING SYSTEMS 1.3 .7 2.0 INSTRUMENTATION

AND CONTROLS in item 1 ELECTRICAL

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

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

ANNUAL OPERATING

AND MAINTENANCE

COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment 1000-cfm Charcoal/HEPA

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

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

14ATERIAL

AND .6 2 HEPA or prefilters

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

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

____________

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

K TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

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

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

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

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

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

PIPING SYSTEMS 3 2 5 INSTRUMENTATION

AND CONTROLS -In Item 1 ELECTRICAL

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

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

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

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

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

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

charcoal/HEPA

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

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

PIPING SYSTEMS 3.0 2.0 5.0 INSTRUMENTATION

AND CONTROLS in item 1 ELECTRICAL

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

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

ANNUAL OPERATING

AND MAINTENANCE

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

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

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

LABOR. SUPERVISION, 3.8 15 min/shift

& 40-hr annual test AND OVERHEAD MAINTENANCE

MATERIAL AND 9.0 30 HEPA or prefilters

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

AND SERVICES Waste Disposal 1.5 $S50/HEPA

or prefilter, $100/charcoal Water Steam Electricity

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

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS 30.00O-cfm Charcoal/HEPA

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

-¶ a 1n FnrMN/AEIL

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

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

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

PIPING SYSTEMS 5 3.0 8.0 base INSTRUMENTATION

AND CONTROLS -in item I ELECTRICAL

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

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

K TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

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

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

TALS TflTA[BASIS FOR PROCESS EQUIPMENT

15.0 117.0 132.0 prefilter/4" charcoal/HEPA

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

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

PIPING SYSTEMS 3.0 5.0 8.0 base INSTRUMENTATION

AND CONTROLS in item 1 ELECTRICAL

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

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

ANNUAL OPERATING

AND MAINTENANCE

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

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

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

LABOR, SUPERVISION, 3.8 15 min/shift

+ 40 hr annual test AND OVERHEAD MAINTENANCE

MATERIAL AND 18.0 60 HEPA or prefilters

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

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

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

K TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

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

TnIMNIAEIL

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

g. ASSOCIATED

PIPING SYSTEM; -in item 1 INSTRUMENTATION

AND CONTROLS -in item 1 ELECTRICAL

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

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

ANNUAL OPERATING

AND MAINTENANCE

COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTE14 FOR LIGHT-WATER-COOLED

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

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

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

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

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

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

SYSTEM FOR LIGHT-WATER-COOLED

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

TOTAL BASIS FOR COST ESTIMATE PROCESS EQUIPMENT

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

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

PIPING SYSTEMS 1.0 1 2.0 10% of item 1 INSTRUMENTATION

AND CONTROLS neg ELECTRICAL

SERVICE neg SPARE PARTS neg SUBTOTAL 21.5 30 51.5 CONTINGENCY

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

ANNUAL OPERATING

AND MAINTENANCE

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

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

LABOR, SUPERVISION, AND OVERHEAD neg MAINTENANCE

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

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

K TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT

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

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

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

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

PIPING SYSTEMS 32.0 13.0 45.0 allowance INSTRUMENTATION

AND CONTROLS 10.0 40.0 50.0 allowance ELECTRICAL

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

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

AND MAINTENANCE

COST ESTIMATE SHEET OF RADtWASTE

TREAThENT

SYSTEM FOR LIGHT-WATER-COOLED

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

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

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

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

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

SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS PWR Air EJector Charcoal/HEPA

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

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

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

PIPING SYSTEMS 2.0 1.0 3.0 allowance INSTRUMENTATION

AND CONTROLS 0.5 1.5 2.0 allowance ELECTRICAL

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

1.0 1.0 2.0 1O0 TOTAL DIRECT COSTS 10.0 14.0 24.0

ANNUAL OPERATING

AND MAINTENANCE

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

NUCLEAR REACTORS Description of Augnent PWR Air EJector Charcoal/HEPA

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

I , L ueA5 rwK Guil r.4IrMIE OPERATING

LABOR, SUPERVISION, 3.8 15 min/shift

+ 40 hr annual test AND OVERHEAD MAINTENANCE

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

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

SYSTEM FOR LIGHT-WATER-COOLED

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

1)TOTAL BASIS FOR COST ESTIMATE PROCESS EQUIPMENT

-no equipment required BUILDING ASSIGNMENT

neg install In existing space ASSOCIATED

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

AND CONTROLS 4 6 10 allowance ELECTRICAL

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

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

ANNUAL OPERATING

AND MAINTENANCE

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

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

LABOR, SUPERVISION, 1 allowance AND OVERHEAD MAINTENANCE

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

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

K TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

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

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

2. BUILDING ASSIGNMENT

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

PIPING SYSTEMS 35 30 65 inludes service piping INSTRUMENTATION

AND CONTROLS 10 10 20 allowance ELECTRICAL

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

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

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

FOR LIGHT-WdATER-COOLED

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

2. BUILDING ASSIGNMgNT

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

PIPING SYSTEMS 35 35 70 includes service piping INSTRUMENTATION

AND CONTROLS 10 10 20 allowance ELECTRICAL

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

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

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

K FOR LIGHT-WATER-COOLED

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

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

97 48 145 10% more than 30 gpm ASSOCIATED

PIPING SYSTEMS 35 35 70 allowance INSTRUMENTATION

AND CONTROLS 10 10 20 allowance ELECTRICAL

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

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

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

ANNUAL OPERATING

AND MAINTENANCE

COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment

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

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

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

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

SYSTEM FOR LIGHT-WATER-COOLED

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

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

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

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

AND MAINTENANCE

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

ANNUAL OPERATING

AND MAINTENANCE

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

NUCLEAR REACTORS Description of Augment EvaDorator

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

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

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

AND concentrate solidification chemicals SUPPLIES In item 4 UTILITIES

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

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

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

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

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

AND MAI[NTENANCE

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

Description of Augment TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

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

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

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

PIPING SYSTEMS 9.0 6.0 15.0 2" piping INSTRUMENTATION

AND CONTROLS 2.0 3.0 5.0 remote conductivity readout ELECTRICAL

SERVICE neg SPARE PARTS 1.0 1.0 SUBTOTAL 21.4 33.2 54.6 CONTINGENCY

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

)K SYSTEM FOR LIGHT-WATER-COOLED

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

OPERATING

LABOR, SUPERVISION.

1.8 1500 hrs operation

@ 10% attendance AND OVERHEAD MAINTENANCE

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

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

AND MAINTENANCE

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

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

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

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

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

PIPING SYSTEMS 9 6.0 15.0 2" piping INSTRUMENTATION

AND CONTROLS 4 6.0 10.0 ELECTRICAL

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

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

{Sheet 1)

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

SYSTEM FOR LIGHT-WATER-COOLED

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

TOTAL BASIS FOR COST FSTTMATF PROCESS EQUIPMENT

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

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

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

AND CONTROLS 4 6.0 10.0 ELECTRICAL

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

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

TOTAL DIRECT COST ESTIMATE SHEET OF RADWAST!E

TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment 20-plDmneralizer(Sheet

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

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

PIPING SYSTEMS 12 12.0 24.0 4" piping INSTRUMENTATION

AND CONTROLS 4 6.0 10.0 ELECTRICAL

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

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

K Description of Augment 400-gpm Demineralizer

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

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

with resin BUILDING ASSIGNMENT

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

PIPING SYSTEMS 20 20.0 40.0 6" piping INSTRUMENTATION

AND CONTROLS 4 6.0 10.0 allowance ELECTRICAL

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

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

SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS a, 'a ANNUAL OPERATING

AND MAINTENANCE

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

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

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

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

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

K ANNUAL OPERATING

AND MAINTENANCE

COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment Demineralizer

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

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

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

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

ANNUAL OPERATING

AND MAINTENANCE

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

NUCLEAR REACTORS Description of Augment Demineralizer

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

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

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

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

K ANNUAL OPERATING

AND MAINTENANCE

COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

NUCLEAR REACTORS Description of Augment Demineraltzer

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

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

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

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

ANNUAL OPERATIN AND

COST ESTIMTE SHEET OF RADWASTE TREATMENT

of Aujnmant flminapA147AP

.DUo*7m,

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

LABOR, SUPERVISION.

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

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

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

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

..........

-."(

K Description of Augment Demineralizer

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

LABOR, SUPERVISION.

AND OVERHEAD 3.3 15 min/shift MAINTENANCE

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

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

AND MAINTENANCE

COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

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

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

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

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

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

PIPING SYSTEMS 1.5' 1.0 2.5 allowance INSTRUMENTATION

AND CONTROLS 0.6 2.4 3.0 allowance ELECTRICAL

SERVICE neg SPARE PARTS 0.5 0.5 SUBTOTAL 9.7 11.9 21.6 CONTINGENCY

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

ANNUAL OPERATING

AND MAINTENANCE

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

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

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

MATERIAL AND LABOR 1.0 allowance CONSUMABLES.

CHEMICALS, AND SUPPLIES 1.0 10 changes/yr

@ $100/change UTILITIES

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

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREAT1ENT

SYSTEM FOR LIGHT-WATER-COOLED

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

PROCESS EQUIPMENT

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

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

PIPING SYSTEM4S 16 9.0 25 35% of equipment cost INSTRUMENTATION

AND CONTROLS in item 1 ELECTRICAL

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

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

K FOR LIGHT-WATER-COOLED

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

TOTAL BASIS FOR COST ESTIMATE PROCESS EQUIPMENT

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

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

PIPING SYSTEMS 31 16.0 47 35% of equipment cost INSTRUMENTATION

AND CONTROLS --item I ELECTRICAL

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

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

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

ANNUAL OPERATING

AND MAINTENANCE

COST ESTI1ATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

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

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

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

4. UTILITIES

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

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

T TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

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

TOTAL BASIS FOR COST ESTIMATF PROCESS EQUIPIENT

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

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

PIPING SYSTEMS 3.0 2.0 5.0 allowance INSTRUMENTATION

AND CONTROLS in item I ELECTRICAL

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

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

ANNUAL OPERATING

AND MAINTENANCE

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

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

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

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

AND SUPPLIES neg UTILITIES

AND SERVICES Waste Disposal 4.3 100:1 vol reduction

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

FOR LIGHT-WATER-COOLED

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

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

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

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

PIPING SYSTEMS 2 1 3 10% of item 1 INSTRUMENTATION

AND CONTROLS 4 6 10 allowance ELECTRICAL

SERVICE neg SPARE PARTS neg SUBTOTAL 39 s0 89 CONTINGENCY

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

SYSTEM

ANNUAL OPERATING

AND MAINTENANCE

COST ESTIMATE SHEET OF RADWASTE TREAThENT

SYSTEM FOR LIGHT-WATER-COOLED

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

LABOR, SUPERVISION.

AND OVERHEAD 1.1 5 min/shift

-log level readings MAINTENANCE

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

CHEMICALS, AND neg SUPPLIES UTILITIES

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

REFERENCES

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

TREATMENT

SYSTEM COST-BENEFIT

ANALYSIS FOR LIGHT-WATER

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

The information should be consistent with the contents of the Safety Analysis Report (SAR) and Environmental Report (ER) for the proposed reactor. Appropriate sections of the SAR and ER containing more detailed discussions of the required information should be referenced as appropriate.

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

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

All costs should be stated in terms of 1975 dollars.

2. The cost of borrowed money used in the cost analysis and the method of arriving at this cost. 3. If methods and parameters used in the cost-benefit analysis are different from those aiven in this guide, describe the methods used in detail and provide bases for all parameters.

Include the following information:

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

FOR LIGHT-WATER-COOLED

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

1. PROCESS EQUIPMENT

2. BUILDING ASSIGNMENT

t I 1 I I I I I ASSOCIATED

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

AND CONTROLS I I I I ELECTRICAL

SERVICE I I I I 6. SPARE PARTS______________________I

i mI SUBTOTAL________________________________________________________

1 -I I I CONTINGENCY

I I I TOTAL DIRECT COSTS________________________________________________________

________________

I __________________________________________________

_____________

_______________________________________________

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

ANNUAL OPERATING

AND MAINTENANCE

COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED

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

1. OPERATING

LABOR, SUPERVISION, AND OVERHEAD MAINTENANCE

MATERIAL AND LABOR CONSUMABLES, CHEMICALS, AND SUPPLIES UTILITIES

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


Retrieved from "https://kanterella.com/w/index.php?title=Regulatory_Guide_1.110&oldid=1062659"