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


REGULATORY GUIDE 1.110  
anll.                                          to accommodate corn asmon ed                ho wtcintormatiotn or e*perieot    Ifowoer comments on  Copies of published guides may be obtained by wistten .squett indicating Cth Ofu guide. A received within Oboinstwo month$ chatret. issuance. will be *at      divisions desired to the U S Nuclear Regulators Commission Wshtington 0 C
COST-BENEFIT ANALYSIS FOR RADWASTE SYSTEMS FOR
ticfady orssIul Mtevaluating the =teed of an srly viision                        20566.Attention Director. Office of Standerde Development
LIGHT-WATER-COOLED NUCLEAR POWER REACTORS  
 
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==
==A. INTRODUCTION==
Purpose  The U.S. Nuclear Regulatory Commission (NRC) staff has developed a series of guides that provide methods acceptable to the staff for calculating effluent releases, dispersion of effluents in the atmosphere and different water bodies, associated radiation doses to man, and cost-benefit aspects of treating radwastes.  This regulatory guide describes methods and procedures that the staff of the NRC considers acceptable for performing a cost-benefit analysis for liquid and gaseous radwaste system components for light-water-cooled nuclear power reactors.
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.


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."  
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 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.
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.


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.
==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.


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.
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.


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.
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.


Purpose of Regulatory Guides
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.


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.
1-110-5


Paperwork Reduction Act This regulatory guide contains information collection requirements covered by 10 CFR Part 50  
==C. REGULATORY POSITION==
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.    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.


Rev. 1 of RG 1.110, Page 3 TABLE OF CONTENTS
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.
Page 


==A. INTRODUCTION==
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.
...............................................................................................................
 
.................... 1 Purpose .......................................................................................................................
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.
.................. 1 Applicable Rules and Regulations ............................................................................................... 1 Related Guidance ..............................................................................................................
 
........... 2 Purpose of Regulatory Guides ..................................................................................................
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.
... 2 Paperwork Reduction Act .......................................................................................................
 
..... 2
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.


==B. DISCUSSION==
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.
.................................................................................................................
......................... 4 Reason for Revision ...........................................................................................................
.......... 4 Background ....................................................................................................................
.............. 4 Harmonization with International Standards ............................................................................... 4 C. STAFF REGULATORY GUIDANCE ..................................................................................................
.. 4


==D. IMPLEMENTATION==
1.110-7
.............................................................................................................
................. 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
TABLE A-1 DIRECT COSTS -  GASEOUS RADWASTE AUGMENTS
Page A-1 Electric Power Supply Areas in the United States ....................................................................... A-
                                                        Direct- Costs
9 Rev. 1 of RG 1.110, Page 4
                                                                                  (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.


==B. DISCUSSION==
1.110-8
Reason for Revision The NRC revised RG 1.110 to incorporate editorial changes and the current format for regulatory guides.  These changes were intended to improve clarity and did not alter the staff regulatory guidance.


Background Each applicant for a permit to construct or a li cense to operate a light-water-cooled nuclear power reactor and each holder of a license to operate a light-water-cooled nuclear power reactor is required to provide reasonable assurance that the design objectives for as low as is reasonably achievable effluent releases are satisfied by the initial liquid and gaseous radwaste system designs at the time of licensing and, if these designs are subsequently modified, that the design objectives are reassessed to ensure that they are maintained.  It is the objective of this guide to provide an acceptable method of performing cost-benefit analysis, in conformance with Section II.D of Appendix I to 10 CFR Part 50, to demonstrate that the plant design includes all items of reasonably demonstrated technology for reducing the cumulative population dose caused by releases of radioactive materials from the reactor to levels as low as reasonably achievable.  As an interim measure, the Commission chose values of $1,000 per-man-rem and $1,000 per man-thyroid-rem (or lesser values if demonstrated to be suitable for a particular site) to be used to implement the cost-benefit analysis.
TABLE A-1 (Continued)
                          DIRECT COSTS - LIQUID RADWASTE AUGMENTS
                                                      Direct Costs
                                                                        (1975 $1000)
                                                                            Total Equipment/Material        Labor
                                                  386                201      587
15-gpm Evaporator
                                                  540                223      763
30-gpm Evaporator
                                                  655                233      888
50-gpm Evaporator
                                                  36                24      60
Evaporator Distillate Demineralizer
                                                  43                29      50
50-gpm Demineralizer
                                                  64                31      95
100-gpm Demineralizer
                                                  94                35      129
200-gpm Deminieralizer
                                                  102                44      146
400-gpm Demineralizer
                                                  108                56      164
100-gpm Precoat Filter
                                                  202                112      314
400-gpw Precoat Filter
                                                  13                11      24
20-gpm Cartridge Filter
                                                  100                38      138
2-gpm Reverse Osmosis
                                                  55                43      98
10,000-gal Tank
                                              1.110-9


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


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
1.110-10


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.
TABLE A-2 (Continued)
                        ANNUAL OPERATING COSTS - LIQUID RADWASTE AUGMENTS
                                                            Total Operating Cost (1975 $1000/yr)
                                                                            5 Demineralization - PWR Clean Waste Demineralization - BWR Dirty Waste                                          88
                                                                            18 Demineralization - PWR Dirty Waste
                                                                            95 Demineralization - PWR Turbine Bld


Harmonization with International Standards
====g. Drains====
                                                                            25 Desmineralization - PWR Steam Generator Blowdown
                                                                            53 Precoat Filter - BWR Dirty Waste Cartridge Filter                                                            7
                                                                            7 Reverse Osmosis - Detergent Waste
                                                                            1
10,000-gal Tank
                                                1.110-11


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.
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


C. STAFF REGULATORY GUIDANCE
TABLE A-4 LABOR COST CORRECTION FACTORS
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
                  FPC
              Geographic                            Labor Cost Correction Region                                        Factor I                                          1.6
                                                              1.5
                  1II
                                                              1.0
                  IV                                          1.4 V                                          1.1 VI                                          1.2 VII                                          1.3 Vlll                                          1.2 See Appendix B, "Labor Cost Correction Factors.'
See Figure A-1.


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). 
1.110-13
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.
TABLE A-5 INDIRECT COST FACTORS
    Type Radwaste System                          Indirect Cost Factor
"1.  Single unit site, unitized    radwaste system                                                    1.75
2.  Multi-unit site, shared radwaste system                                                    1.75
3.   Multi-unit site, unitized  radwaste system                                          1.75 + (n-1)1.5 n
                                                where n is the number of unitized radwaste systems at the site Each reactor has a separate, nonshared radwaste system.


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.
I..
                                      1.110-14


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


==D. IMPLEMENTATION==
LEGEND
The purpose of this section is to provide information on how applicants and licensees
                            ¶Im      REGIONAL GROUPING OF POWER SUPPLY AREAS
~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." 
  FIGURE A-1 ELECTRIC POWER SUPPLY AREAS IN THE UNITED STATES
Use by Applicants and Licensees Applicants and licensees may voluntarily
(                    C                                                        C
~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.
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 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.
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 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.
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.


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
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.


backfit consideration.
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.


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


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


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). 
Contingency onsite labor and process equipment and material are all based on-l0%.
Rev. 1 of RG 1.110, Page 7 REFERENCES
                                                1.110-17
~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.
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.


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


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


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.
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.


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


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


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


Appendix A to RG 1.110, Page A-1 APPENDIX A
1.110-18
  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.)
LIST OF APPENDIX B COST ESTIMATE SHEETS
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.
                                                                                                    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


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


4. The total annual cost of each augment considered in item 2 above should be determined as follows: a. The Total Direct Cost (TDC):
items 1 & 4 above SUBTOTAL                                  232                        503                                735
(1) Obtain the direct cost of equipment and materials from Table A-1.
  7.  CONTINGENCY                                        23                          50                                  73  10%
  8. TOTAL DIRECT COSTS                              2S5                        553                                808
(
                                                                                                                                                      r


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


(3) Add the costs obtained from steps (1) and (2) to obtain the TDC.
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
                                                                    FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
                                                                                                      m Description of Augment      3-ton Charcoal Adsorber (Sheet 1)
                                                                            DIRECT COST (1975 $1000)
                                                                                                                                BASIS FOR
                                !TFM                            LABOR            EOUIPMENTIMATERIALS          TOTAL          COST
                                                                                                                                - -
                                                                                                                                    ESTIMATF
                                                                                                                                      -- - - -
                                                                                                                                                      3
                  1. PROCESS EQUIPENT                              5                  44.0                    49.0    carbon steel, 350 psig, 200 ft volume (augment to existing train of beds)
                                                              4.        4.                                  4.      4
                  2. BUILDING ASSIGNMENT                            8                    4.5                    12.5    10' x 10' x 25' * $5/ft3 (turbine building shiel4ed area)
                  3. ASSOCIATED PIPING SYSTES                                                                      -    in item I
              a
                  4. INSTRUKENTATION AND CONTROLS                                                                neg S. ELECTRICAL SERVICE                                                                          neg
                  6. SPARE PARTS                                                                                none  existing SUBTOTAL                                13                  48.5                    61.5
                  7. CONTINGENCY                                    1                    5.0                      6.0  10%
                  8. TOTAL DIRECT COSTS                            14                  53.5                    67.5
. . .. . . . . r                                                                r                                                                  r


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


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


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


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


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


Table A-1.  Direct Costs-Gaseous Radwaste Augments, Liquid Radwaste Augments  DIRECT COSTS
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
-GASEOUS RADWASTE AUGMENTS
                                                          FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
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/  
        Description of Augment      Charcoal/HEPA Filtration System - Condenser Vacuum Pump (Sheet 1)
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)
                                                                                              i  n    *
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)  
                                                                  DIRECT COST (1975 $1000)
Turbine Bldg. Chilled Water HVAC System 614 374 988
                  ITE4                              I A*Q
600-ft 3 Gas Decay Tank 33 24 57 Appendix A to RG 1.110, Page A-3 DIRECT COSTS
                                                                                                                  BASIS FOR
-GASEOUS RADWASTE AUGMENTS
                                                    LABOR__        ~    LrILumLAL                IUIAL          COST ESTIMATE
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
    1.  PROCESS EQUIPMENT                              2                        32.5                34.5  2000 CFM preftlter/4" charcoal bed/HEPA @ S15/cfm, 10 kw heater @ $250/kw
    2.  BUILDING ASSIGNMENT                            3.1                      1.5                  4.6  Turbine building 8' x 16, x 12'
                                                                                                          @ $3/ft 3 (nonshielded area)
Nm
    3. ASSOCIATED PIPING' SYSTEMS                      1.3                      0,7                  2.0  allowance wO
  4.  INSTRUMENTATION AND CONTROLS
                                                                                                          in item 1
  5.  ELECTRICAL SERVICE                            1                          1.5                  2.5
  6.  SPARE PARTS                                                              0.5                0.5 SUBTOTAL                                7.4                      36.7                44.1
  7.  CONTINGENCY                                      .7                      3.7                  4.4  10%
  8.  TOTAL DIRECT COSTS                           8.1                      40.4                48.5
(                                                                                                                                     (


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


Appendix 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
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
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
                                                    FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
-GASEOUS RADWASTE AUGMENTS
    Description of Augment      Clean Steam to Turbine Glands (Sheot 1)
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
                                                            DIRECT COST (1975 $1000)
-GASEOUS RADWASTE AUGMENTS
                FM                                                FOIITDMFNTIMATPRTAI      STTTflTAI        BASIS FOR
TOTAL OPERATING COST (1975 $1,000/YR) 30,000-cfm Charcoal/HEPA Filtration System 18 Turbine Bldg. Chilled Water HVAC System 20
                                                                                                              *FnCT VCTttMATO
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
                                                I ARAR
~a FPC~b GEOGRAPHIC
                        ITEMP
REGION LABOR COST
  1. PROCESS EQUIPMENT                              15                   150                    165  25,000 lb/hr reboiler I $4/lb/hr I
CORRECTION FACTOR
                                                                                                      $25K/H.P. turbine glands
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."
  2. BUILDING ASSIGNMENT                            19                    10                      29 20' x 30' x 16' 6 $3/ft3
b. See Figure A-1. Table A-5.  Indirect Cost Factors TYPE RADWASTE SYSTEM INDIRECT COST FACTOR 
  3. ASSOCIATED PIPING SYSTEMS                      32                    18                      50  equiv 1000 ft 0 $50/ft
1. Single unit site, unitized
  4. INSTRUMENTATION AND CONTROLS                    8                    12                      20  in addition to Item I
~a radwaste system 1.75 2. Multiunit site, shared radwaste system  1.75
  5. ELECTRICAL SERVICE                                                                          nag
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.
  6. SPARE PARTS                                                          5                       5 SUBTOTAL                                  74                  195                    269
  7. CONTINGENCY                                    7                    20                      27 10%
  8. TOTAL DIRECT COSTS                            81                  215                    296 r                                                              r                                                              C


Appendix A to RG 1.110, Page A-8 Table A-6.  Capital Recovery Factors COST OF MONEY  (% PER YEAR, I) CAPITAL RECOVERY FACTOR
K                                                                                                                          K
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:
                                    ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
CRF = 1 30)i 1 (30)i 1 (i++ 
                                                SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
  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
      Description of Augment    Clean Steam to Turbine Glands (Sheet 2)
   BASES FOR PARAMETERS US
                                                                COST (1975 $1000)
ED IN PERFORMING COST-BENEFIT ANALYSIS
                1TR4                          LABOR          OTHER          TOTAL              BASIS FOR COST ESTIMATE
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.
  I. OPERATING LABOR, SUPERVISION,                                            3.3      15 min/shift AND OVERHEAD
  2. MAINTENANCE MATERIAL AND                                                  4.0       40 man-days LABOR
  3. CONSUMABLES, CHEMICALS, AND
      SUPPLIES
9'
  4. UTILITIES AND SERVICES
        Waste Disposal Water Steam                                                                21.0        10 Btu/kw-hr heat rate increase Electricity Building Services Other
   5. TOTAL 0 AND M ANNUAL COST                                               28.3


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


1. 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
K                                                                -\
~5 are included in the direct costs.  Total capital costs are obtained by multiplying direct costs by an indirect cost factor.
                                    ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
                                                SYSTEM1 FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
      Description of Augment    Clean Steam to Steam Valves 24" and Larger (Sheet 2)
                                                                COST (1975 $1000)
                TT!M                          LABOR          OTHER          TOTAL              BASIS FOR COST ESTIMATE
  1. OPERATING LABOR, SUPERVISION,                                           3.3        15 min/shift AND OVERHEAD
  2. MAINTENANCE MATERIAL AND                                                4.0        40 man-days LABOR
  3. CONSUMABLES, CHEMICALS, AND                                              neg SUPPLIES
w U,
  4. UTILITIES hND SERVICES
        Waste Disposal Water Steam                                                                  neg Electricity Building Services Other TOTAL 0 AND M ANNUAL COST                                                7.3


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


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


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


5 Contingency onsite labor and process equipment and material are all based on l0 percent.
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
                                                            FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
        Description of Augment        15,000-cfm HEPA Filtration System - Auxiliary Building (Sheet 1)
                                                                    DIRECT COST (1975 $1000)
                                                                                                                              BASIS FOR
                                                    I ADflD                £rI"TDUCMT MATrTAI C        TfllAI                rACT rCTTMATr I I~p~
                      ERq~
                      r.                              flTl II Anna                .r..
                                                                              X  rr...L./  - -. n nn.  .- v,    .            .,  .  L
                                                                                                                                      i-* ,
    1.  PROCESS EQUIPMENT                                    5                      40.0                  45.0    prefilter/HEPA @ $3/cfm, use existing fan BUILDING ASSIGNMENT                                  7                        4.5                11.5    16' x 12' x 12' @ $5/ft 3
    2.


Appendix B to RG 1.110, Page B-2  
(nonshielded area)
4. Indirect Cost Factor
    3. ASSOCIATED PIPING SYSTEMS                            3                        2.0                    5.0
,o L.


Indirect costs as a percentage of direct costs are calculated in Table B-1. Table B-
a'
    4.  INSTRUMENTATION AND CONTROLS                                                                                in item 1
    5.  ELECTRICAL SERVICE                                                                                          base
    6.  SPARE PARTS                                                                    0.5                    0.5 SUBTOTAL                                      15                        47.0                  62.0
    7. CONTINGENCY                                          1                          5.0                  6.0  10%
    8.  TOTAL DIRECT COSTS                                  16                        52.0                  68.0
(                                                                        (                                                                    (


===1. Indirect Costs  ===
K                                                                  T                                                                K !
1 ST UNIT, PERCENTAGE OF DIRECT COST SUBSEQUENT UNITS, PERCENTAGE OF DIRECT COST
                                            TOTAL DIRECT COST ESTIMATE SHEET OF RADWASrE TREATMENT SYSTEM
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.
                                                        FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
        Description of Augment      15,000-cfm HEPA Filtration System - Turbine Building (Sheet 2)
                                                                DIRECT COST (1975 $1000)
                                                                                                                      BASIS FOR
                                                                                                                        COST ESTIMATE
                                                                          lI TDMCWNT IMATrOAIC
                                                    I AflI                                        TflTAL
                    ITEM                                                !L___      f                      ______________
                                                      5                       40.0                45.0    skid mounted filter housing
    1. PROCESS EQUIPMENT                                                                                  w/o fans
                                                                                                                                      3
                                                                                2.3                  6.9  16' x 12' x 12' @ $3/ft
    2. BUILDING ASSIGNMENT                            4.6 (nonshielded area)
    3.                                                  3                        2.0                  5.0
        ASSOCIATED PIPING SYSTEMS
-I
    4.                                                                                                      in item 1 INSTRUMENTATION AND CONTROLS
    5.                                                                                                      base ELECTRICAL SERVICE
    6.                                                  0                      0.5                  0.5 SPARE PARTS
              SUBTOTAL                                12.6                    44.8                57.4
    7. CONTINGENCY                                    2                      4.0                  6.0    10l a.   TOTAL DIRECT COSTS                          14.6                    48.8                63.4


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.
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
                                                  SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
      Description of Augment    15,000-cfm HEPA Filtration System (Sheet 3)
                                                                COST (1975 $1000)
                ITEM                          LABOR          OTI4FR        TflTAI              RACTC Frn rncT FCTIMATC
  I. OPERATING LABOR, SUPERVISION,                                          3.8        15 min/shift + 40 hr annual test AND OVERHEAD
  2. MAINTENANCE MATERIAL AND                                                2.2        change every 2 yrs @ $150/filter element LABOR
      CONSUMABLES, CHEMICALS, AND
I
  3.                                                                                      in items 2 and 4 SUPPLIES
  4. UTILITIES AND SERVICES
        Waste Disposal                                                        0.8        $50/filter element Water Steam Electricity                                                            1.0        additional fan electrical load Building Services Other
  5. TOTAL 0 AND M ANNUAL COST                                                7.8 I_                                                                                                                                  (


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:
K                                                                                                                                K
1)i 1 ()i 1 (i n n++  
                                          TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
Appendix B to RG 1.110, Page B-3 Where: i = cost of borrowed money expressed as a decimal n = plant operating lifetime (yr)
                                                      FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
      Description of Augment      1000-cfm Charcoal/HEPA Filtration System (Sheet 1)
                                                              DIRECT COST (1975 $1000)
                                                                                                                BASIS FOR
                  I TEM                            LABOR              EOUIPMENT/MATERIALS        TOTAL        COST ESTIMATE
  I.  PROCESS EQUIPMENT                            2.0                  22.0                    24.0 prefllter/4" charcoal/HEPA
                                                                                                        @ $20/cfm, 5 kw htr @ $400/kw BUILDING ASSIGNMENT                          3.8                    2.0                    5.8 8' x 12' x 12' @ $5/ft 3
  2.


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.
(nonshielded area)
  3.  ASSOCIATED PIPING SYSTEMS                    1.3                      .7                    2.0
0
  4.  INSTRUMENTATION AND CONTROLS                                                                      in item 1
  5.  ELECTRICAL SERVICE                            1.5                    1.0                    2.5
  6.  SPARE PARTS                                                          0.5                    0.5 SUBTOTAL                                8.6                    26.2                    34.8
    7. CONTINGENCY                                  1.0                    2.0                    3.0 10%
    8. TOTAL DIRECT COSTS                            9.6                    28.2                    37.8


LIST OF APPENDIX B COST ESTIMATE SHEETS  BWR Offgas Recombiner .........................................................................................................
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
... B-4 3-ton Charcoal Adsorber .......................................................................................................
                                                      SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
....... B-6 Desiccant Dryer ...............................................................................................................
        Description of Augment      1000-cfm Charcoal/HEPA Filtration System (Sheet 2)
............ B-8 Charcoal Vault Refrigeration ..................................................................................................
                                                                        COST (1975 $1000)
... 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
                        ITEM                      LABOR              OTHER          TOTAL          BASIS FOR COST £STII4ATF
15,000-cfm HEPA Filtration System ......................................................................................... B-2
    1. OPERATING LABOR, SUPERVISION,                                                  1.9    20 min/day + 40 hr annual test AND OVERHEAD
0 1000-cfm Charcoal/HEPA Filtration System ............................................................................ B-23
    2. MAINTENANCE 14ATERIAL AND                                                      .6    2 HEPA or prefilters @ $150 each and
15,000-cfm HEPA Filtration System ......................................................................................... B-2
                                                                                              1 charcoal @ $900 each every 2 yrs'
5 30,000-cfm Charcoal/HEPA Filtration System ......................................................................... B-28 Turbine Building Chilled Water HVAC System ....................................................................... B-31
-   3. CONSUMABLES, CHEMICALS, AND                                                            in items 2 and 4 SUPPLIES
600-ft 3 Waste Gas Decay Tank .................................................................................................. B-33 PWR Hydrogen Recombiner ..................................................................................................... B
0
-35 PWR Air Ejector Charcoal/HEPA Filtration Unit ..................................................................... B-37 Steam Generator Flash Tank Vent to Main Condenser ............................................................. B-39 Evaporators ...................................................................................................................
        UTILITIES AND SERVICES
............. B-41 Evaporator Distillate Demineralizer ..........................................................................................
            Waste Disposal                                                              .1    $50/HEPA or prefilter, $100/charcoal Water                                                                              filter Steam Electricity                                                                neg Building Services Other
B-48 Demineralizers ................................................................................................................
    5. TOTAL 0 AND M ANNUAL COST                                                      2.6
........... B-50
        ____________________________                          ____________      I        I
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  
K                                                              K
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
                                        TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
2. BUILDING ASSIGNMENT 100 50 150 30 x 40 x 25 @ $5/ft 3 (turbine building shielded area)
                                                    FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
3. ASSOCIATED PIPING SYSTEMS 18 12 30 augment piping connections only 4. INSTRUMENTATION AND CONTROLS 24 96 120 allowance
    Description of Augment       15,OOO-cfm Charcoal/HEPA Filtration System - Auxiliary Building (Sheet 1)
5. ELECTRICAL SERVICE - - neg 4kw heaters on vessels neglected
                                                            DIRECT COST (1975 $1000)
6. SPARE PARTS - 85 85 75K for catalyst + 2% E/M in items 1 & 4 above  SUBTOTAL 232 503 735 
                                                                                                              BASIS FOR
7. CONTINGENCY 23 50 73 10%
                TTVM                            LABOR             EQUIPMENT/MATERIALS         TOTAL           COST ESTIMATE
8. TOTAL DIRECT COSTS 255 553 808 
                ITE
                                                LABO.....
                                                                                                              COST ESTIMATE
  1. PROCESS EQUIPMENT                             10                    71                    81    prefilter/4" charcoal/HEPA
                                                                                                        @ $5/cfm, 30kw htr @ $200/kw BUILDING ASSIGNMENT                           12                    8                    20    16' x 20' x 12' @ $5/ft 3
  2.


Appendix B to RG 1.110, Page B-5 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
(nonshielded area)
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
   3. ASSOCIATED PIPING SYSTEMS                        3                   2                      5 a
2. MAINTENANCE MATERIAL AND  
  4. INSTRUMENTATION AND CONTROLS                                                                -    In Item 1
LABOR   20.0 routine conditioning of catalyst and equipment upkeep; 5% of E/M including I&C
   5. ELECTRICAL SERVICE                              3                    2                      5     allowance
3. CONSUMABLES, CHEMICALS, AND
  6. SPARE PARTS                                                          5                      5    4 elements of each type SUBTOTAL                                28                    88                    116
SUPPLIES   - in item 2
   7. CONTINGENCY                                      3                  9                    12     10%
4. UTILITIES AND SERVICES     Waste Disposal      Water      Steam   neg intermittent; 4kw heater load is negligible  Electricity      Building Services      Other   
   8. TOTAL DIRECT COSTS                            31                    97                    128
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
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1.  PROCESS EQUIPMENT 5 44.0 49.0 carbon steel, 360 psig, 200 ft
                                                          FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
3 volume (augment to existing train of beds)
        Description of Augment       15,000-cfm Charcoal/HEPA Filtration System - Turbine Building (Sheet 2)
2.  BUILDING ASSIGNMENT 8 4.5 12.5 10 x 10 x 25 @ $5/ft 3 (turbine building shielded area)
                                                                      DIRECT COST (1975 $1000)
3.  ASSOCIATED PIPING SYSTEMS - - - in item 1
                    I TEM                                                    CN "I lDMrLT    ATEDIlA1 C                BASIS FOR
4.  INSTRUMENTATION AND CONTROLS - - neg 
                                                    I fuND                                              T*TAi ITEM                I_____
5.  ELECTRICAL SERVICE - - neg 
                                                      ARAL?~urIIn~LJIUL      x         flMrnR                          UI
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
====t. IWUTflYAI====
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
                                                                                                                        1.3
LABOR  neg allowance of 3% of equipment cost is negligible
    1. PROCESS EQUIPMENT                            10.0                          71.0                81.0 prefilter/4* charcoal/HEPA
3. CONSUMABLES, CHEMICALS, AND
                                                                                                                @ $5/cfm, 30 kw htr
SUPPLIES  neg lifetime use of charcoal assumed
                                                                                                                @ $200/kw BUILDING ASSIGNMENT                              7.7                          3.8                11.5  16' x 20' x 121 @ $3/ft 3
4. UTILITIES AND SERVICES  neg  Waste Disposal     Water      Steam  neg  Electricity      Building Services      Other   
     2.
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
(nonshielded area)
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 25 75 100 redundant dryer vessels with 1 regeneration skid
    3. ASSOCIATED PIPING SYSTEMS                       3.0                          2.0                  5.0
2. BUILDING ASSIGNMENT 95 50 145 40 x 36 x 20 @ $5/ft 3 turbine building (shielded area)  
0
3. ASSOCIATED PIPING SYSTEMS 10 5 15 augment piping connections only 4. INSTRUMENTATION AND CONTROLS 12 48 60 allowance
.rg
5. ELECTRICAL SERVICE 18 17 35 service for heaters, blowers, pumps, and compressors
    4. INSTRUMENTATION AND CONTROLS                                                                           in item 1
6. SPARE PARTS - 3 3  SUBTOTAL 160 198 358 
    5. ELECTRICAL SERVICE                               3.0                          2.0                  5.0 allowance
7. CONTINGENCY 16 20 36 10%  
    6. SPARE PARTS                                                                   5.0                  5.0 4 elements each type SUBTOTAL                               23.7                          83.8                107.5
8. TOTAL DIRECT COSTS 176 218 394 
    7. CONTINGENCY                                     2.0                            9.0                11.0  10%
    8. TOTAL DIRECT COSTS                           25.7                          92.8                118.5
(                                                                        r                                                                (


Appendix B to RG 1.110, Page B-9 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
K                                                                                                                                K
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  
                                  ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREAThENT
2. MAINTENANCE MATERIAL AND  
                                                SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
LABOR  6.1 5% of equipment including I&C
    Description of Augment     15,O00-cfm Charcoal/HEPA Filtration System (Sheet 3)
3. CONSUMABLES, CHEMICALS, AND  
                                                                COST (1975 $1000)
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    
                ITEM                         LABOR           OTHER         TOTAL               BASIS FOR COST ESTIMATE
5. TOTAL O AND M ANNUAL COST   9.4 
  1. OPERATING LABOR. SUPERVISION,                                           3.8        15 min/shift & 40-hr annual test AND OVERHEAD
  2. MAINTENANCE MATERIAL AND                                                 9.0        30 HEPA or prefilters @ $150 each & 15 LABOR                                                                              charcoal filters @ $900 each every 2 yrs
  3. CONSUMABLES, CHEMICALS, AND                                                         in Items 2 and 4 SUPPLIES
0
   4. UTILITIES AND SERVICES
      Waste Disposal                                                         1.5        $S50/HEPA or prefilter, $100/charcoal Water Steam Electricity                                                             1.3      8kw additional fan power for filter aP
      Building Services                                                                   0.018.S/kw-hr Other
  5. TOTAL 0 AND M ANNUAL COST                                               15.6


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
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 10 75 85 10-ton capacity, 3 refrigerators with drives, 32°F design
                                                        FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
2. BUILDING ASSIGNMENT 9 3 12 20 x 10 x 20 @ $2/ft 3 turbine building (nonshielded area)  
      Description of Augment     30.00O-cfm Charcoal/HEPA Filtration System - Auxiliary Building (Sheet 1)
3. ASSOCIATED PIPING SYSTEMS   in item 1
                                                                DIRECT COST (1975 $1000)
4. INSTRUMENTATION AND CONTROLS 4 6 10 allowance
                                                                                                                BASIS FOR
5. ELECTRICAL SERVICE 12 18 30 allowance  
                  I ITU                            i ARng~
6. SPARE PARTS - 3 3  SUBTOTAL 35 105 140 
                                                                        FoII PI4FNTII4ATFRIALS  TOTAL            COST ESTIMATE
7. CONTINGENCY 3 11 14 10%  
                                                -¶  a        1n        FnrMN/AEIL
8. TOTAL DIRECT COSTS 38 116 154 
                                                      15                      117.0            132.0  pref1lter/4" charcoal/HEPA
    1. PROCESS EQUIPMENT                                                                                 @ $4/cfm, 60-kw htr @ $200/kw BUILDING ASSIGIMENT                            20                       13.6            33.6  28' x 20' x 12'    $S5/ft3
    2.                                                                                                    (nonshielded area)
    3. ASOCIATED PIPING SYSTEMS                         5                          3.0            8.0  base a
    4. INSTRUMENTATION AND CONTROLS                                                               -      in item I
    5. ELECTRICAL SERVICE                               6                          4.0          10.0    allowance
    6. SPARE PARTS                                                                 5.0            5.0    4 elements each type SUBTOTAL                                 46                      142.6            188.6
    7. CONTINGENCY                                       5                        14.0          19.0    10%
    8. TOTAL DIRECT COSTS                             51                      156.6            207.6
  (                                                                                                                                  C


Appendix B to RG 1.110, Page B-11 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
y                                                                                                                                      K
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
                                          TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
2. MAINTENANCE MATERIAL AND
                                                      FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
LABOR  3.7 5% of equipment
      Description of Augment       30,000-cfm Charcoal/HEPA Filtration System    - Turbine Building (Sheet 2)
3. CONSUMABLES, CHEMICALS, AND  
                                                              DIRECT COST (1975 $1000)
SUPPLIES    in item 2
                                                                    !OtITPHt¶!rT/ATrR TALS                          BASIS FOR
4. UTILITIES AND SERVICES      Waste Disposal      Water      Steam   0.5 electricity and cooling water Electricity      Building Services      Other      
                                                                                                                    t*nlT F*TTMATF
5. TOTAL O AND M ANNUAL COST  7.5 
                  ITEM                            LAROR                                            TflTA[
    1. PROCESS EQUIPMENT                            15.0                  117.0                    132.0    prefilter/4" charcoal/HEPA
                                                                                                              @ $4/cfm, 60kw htr
                                                                                                              @ $200/kw
    2. BUILDING ASSIGNMENT                          13.4                    6.8                      20.2   28' x 20' x 12' @ $3/ft3 (nonshielded area)
    3. ASSOCIATED PIPING SYSTEMS                    3.0                    5.0                        8.0  base me
    4. INSTRUMENTATION AND CONTROLS                                                                          in item 1
    5. ELECTRICAL SERVICE                            6.0                      4.0                      10.0   allowance
    6. SPARE PARTS                                                            5.0                       5.0 4 elements each type SUBTOTAL                              37.4                  137.8                    175.2
     7. CONTINGENCY                                  4.0                    14.0                      18.0  l0
    8. TOTAL DIRECT COSTS                          41.4                  151.8                    193.2


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  
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
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
                                                          SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
2. BUILDING ASSIGNMENT 3.1 1.5 4.6 Turbine building 8 x 16 x 12 @ $3/ft 3 (nonshielded area)
                Description of Augment     30.00O-cfm Charcoal/HEPA Filtration System - (Sheet 3)
3. ASSOCIATED PIPING SYSTEMS 1.3 0.7 2.0 allowance
                                                                          COST (1975 $1000)
4. INSTRUMENTATION AND CONTROLS    in item 1
                          ITEM                         LABOR         OTHER          TOTAL               BASIS FOR £OST FSTTMATF
5. ELECTRICAL SERVICE 1 1.5 2.5 
                OPERATING LABOR, SUPERVISION,                                          3.8        15 min/shift + 40 hr annual test AND OVERHEAD
6. SPARE PARTS  0.5 0.5  SUBTOTAL 7.4 36.7 44.1  
            2. MAINTENANCE MATERIAL AND                                              18.0        60 HEPA or prefilters @ $150 each & 30
7. CONTINGENCY 0.7 3.7 4.4 10%
                LABOR                                                                              charcoal filters @ $900 each every 2 yrs
8. TOTAL DIRECT COSTS 8.1 40.4 48.5 
          " 3. CONSUMABLES, CHEMICALS,  AND                                            -          in items 2 and 4 SUPPLIES
            4. UTILITIES AND SERVICES
                  Waste Disposal                                                        3.0        $50/HEPA or preftilter, $1007charcoal filter Water Steam Electricity                                                          2.6        16kw additional fan HP for filter @
                  Building Services                                                                0.018 S/ku-hr Other
            5. TOTAL 0 AND M ANNUAL COST                                              27.4
- :- t--.-J"
    ý:r                                                                                                                                __  C


Appendix B to RG 1.110, Page B-13 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
K                                                                  K
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
                                                                                                                                      11 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
LABOR  1.2 4 HEPA filters @ $150 & 2 Charcoal filters @ $900, change every 2 years
                                                        FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
3. CONSUMABLES, CHEMICALS, AND
      Description of Augment       Turbine Building Chilled Water HVAC System (Sheet 1)
SUPPLIES  - in items 2 and 4
                                                              DIRECT COST (1975 $1000)
4. UTILITIES AND SERVICES      Waste Disposal  0.2 $50/HEPA filter, $100/Charcoal filter Water      Steam      Electricity      Building Services      Other   
                                                                        EOUJIPMFNTIMATFRIALS                      BASIS FOR
5. TOTAL O AND M ANNUAL COST  1.4 
                  ITEM                            LABOR                                         TflTAI          rnCT  CTMATC
                                                                  TnIMNIAEIL                    1 nA
    1. PROCESS EQUIPMENT                            300                      500                  800    500-ton capacity, w/o air filters
                                                          -t                                  +        I
  2.  BUILDING ASSIG* *IENT                                                                              Coolers can be Installed in existing space saved by deletion of ducting.


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
0
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
  3. ASSOCIATED PIPING SYSTEM;                                                                    -    in item 1
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
-J
12. INSTRUMENTATION AND CONTROLS 8 12 20 in addition to item 1  
  4. INSTRUMENTATION AND CONTROLS                                                                 -    in item 1
13. ELECTRICAL SERVICE   neg 
  5. ELECTRICAL SERVICE                             40                      so                    90
14. SPARE PARTS - 5 5   SUBTOTAL 74 195 269 
  6. SPARE PARTS                                   -                         8                      8   1%item 1 SUBTOTAL                               340                      558                  898
15. CONTINGENCY 7 20 27 10%
  7. CONTINGENCY                                   34                      56                    90    10l
16. TOTAL DIRECT COSTS 81 215 296 
  8. TOTAL DIRECT COSTS                           374                      614                  988


Appendix B to RG 1.110, Page B-15 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
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  
                                                SYSTE14 FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
2. MAINTENANCE MATERIAL AND  
      Description of Augment     Turbine Building Chilled Water HVAC System (Sheet 2)
LABOR  4.0 40 man-days
                                                                COST (1975 $1000)
3. CONSUMABLES, CHEMICALS, AND  
                ITEM                         LABOR           OTHER         TOTAL                 BASIS FOR COST ESTIMATE
SUPPLIES    4. UTILITIES AND SERVICES     Waste Disposal     Water     Steam   21.0 10 Btu/kw-hr heat rate increase  Electricity      Building Services     Other    
  I. OPERATING LABOR, SUPERVISION,                                           3.3         15 min/shift AND OVERHEAD
5. TOTAL O AND M ANNUAL COST   28.3
  2. MAINTENANCE MATERIAL AND                                               20.0        2-1/2% of equipment costs LABOR
.0
  3. CONSUMABLES, CHEMICALS, AND                                             -              initem 2 SUPPLIES
0
  4. UTILITIES AND SERVICES
        Waste Disposal Water                                                                 13.0        500 gpm @ 104/1000 gal & 50% load factor Steam Electricity                                                          33.0         400 kw @ 0.018 $/kw hr Building Services Other S. TOTAL 0 AND M ANNUAL COST                                               69.3 C                                                                C                                                                r


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
K
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 100 120 220 22 valves @ $1,0k/valve, use existing reboiler
                                                                                                                                    I
2. BUILDING ASSIGNMENT  neg install in existing space
                                                              K                                                                  K
3. ASSOCIATED PIPING SYSTEMS   - in item 1  
                                        TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT. SYSTEM
4. INSTRUMENTATION AND CONTROLS   - in item 1
                                                    FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
5. ELECTRICAL SERVICE   neg
                                      3 Description of Augment       600-ft    Waste Gas Decay Tank' (Sheet 1)
6. SPARE PARTS - 5 5   SUBTOTAL 100 125 225  
                                                          DIRECT COST (1975 $1000)
7. CONTINGENCY 10 12 22 10%  
                                                                  EOUIPMENT/MATERIALS                           BASIS FOR
8. TOTAL DIRECT COSTS 110 137 247 
            I TFM                              LABOR                                          TOTAL            COST ESTIMATE
  PROCESS EQUIPMENT                               2.5                  20                      22.5  600-ft 3 , 150 pslgo C.S.,
                                                                                                      ASME VIII
  BUILDING ASSIGNMENT                           18.0                    9                      27.0   15' x 15' x 20' @ S6/ft 3 (shielded area)
  ASSOCIATED PIPING SYSTEMS                       1.0                  1                        2.0  10% of item 1 INSTRUMENTATION AND CONTROLS                                                                 neg ELECTRICAL SERVICE                                                                           neg SPARE PARTS                                                                                   neg SUBTOTAL                                  21.5                 30                      51.5 CONTINGENCY                                      2.0                  3                        5.0 10%
  TOTAL DIRECT COSTS                             23.5                  33                      56.5


Appendix B to RG 1.110, Page B-17 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
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
                                                      SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
7. MAINTENANCE MATERIAL AND  
                                            3 Description of Augment     600-ft  Waste Gas Decay Tank (Sheet 2)
LABOR   4.0 40 man-days
                                                                    COST (1975 $1000)
8. CONSUMABLES, CHEMICALS, AND  
                    ITEM                           LABOR         OTHER         TOTAL             RA;T* FflR i*lT r*T1MATr I. OPERATING LABOR, SUPERVISION,
SUPPLIES   neg  9. UTILITIES AND SERVICES     Waste Disposal     Water     Steam   neg   Electricity     Building Services     Other    
        AND OVERHEAD                                                             neg
1 0TOTAL O AND M ANNUAL COST   7.3 
    2. MAINTENANCE MATERIAL AND
        LABOR                                                                     neg
    3. CONSUMABLES,   CHEMICALS, AND
0
        SUPPLIES                                                                 neg U'
0~e
    4. UTILITIES AND SERVICES
          Waste Disposal Water Steam                                                                   neg Electricity Building Services Other
    5.  TOTAL 0 AND N  ANNUAL COST                                               neg
                                                                                                                              (


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
K                                                                K
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 0 120 120 100 valves @ $1,200 each
                                          TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
2. BUILDING ASSIGNMENT - - neg 
                                                      FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
3. ASSOCIATED PIPING SYSTEMS 40 20 60 
      Description of Augment       PWR Hydrogen Recombiner (Sheet 1)
4. INSTRUMENTATION AND CONTROLS 10 20 30 allowance
                                                              DIRECT COST (1975 $1000)
5. ELECTRICAL SERVICE  - none
                                                                    rflIITPMPINIMAT*RTAI
6. SPARE PARTS - 6 6  SUBTOTAL 50 166 216 
                                                                                                                BASIS FOR
7. CONTINGENCY 5 17 22 10%
                IT"M                              IARno                                        TflTAI        rnqT vtTTMATF
8. TOTAL DIRECT COSTS 55 183 238 
                                                            I  l        VT  :fTI    b    V      nA. I
  1. PROCESS EQUIPMENT                             50.0                   300.0                350.0  skid mounted, catalytic type w/condenser, partial I&C
                                                                                                        single unit, ASME VIII
      BUILDING ASSIGNM4ENT                          28.8                    14.4                 43.2  15' x 30' x 16' 0 $6/ft3
  2.


Appendix B to RG 1.110, Page B-19 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
(shielded area)
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
  3. ASSOCIATED PIPING SYSTEMS                      32.0                    13.0                  45.0 allowance a
2. MAINTENANCE MATERIAL AND
Ue
LABOR  12.0 1% of direct cost of equipment
  4. INSTRUMENTATION AND CONTROLS                  10.0                    40.0                  50.0  allowance
3. CONSUMABLES, CHEMICALS, AND
  5. ELECTRICAL SERVICE                            13.0                    12.0                 25.0  allowance
SUPPLIES  - in item 2  
  6. SPARE PARTS                                    -                       2.0                  2.0
4. UTILITIES AND SERVICES      Waste Disposal      Water      Steam  neg  Electricity      Building Services      Other   
            SUBTOTAL                                133.8                  381.4               515.2
5. TOTAL O AND M ANNUAL COST  15.3 
  7. CONTINGENCY                                    13.0                    38.0                  51.0  101
  8. TOTAL DIRECT COSTS                            146.8                  419.4                566.2


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  
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADtWASTE TREAThENT
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 5 40.0 45.0 prefilter/HEPA @ $3/cfm, use existing fan
                                                SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
2. BUILDING ASSIGNMENT 7 4.5 11.5 16 x 12 x 12 @ $5/ft 3 (nonshielded area)
      Description of Augment     PUR Hydrogen Recombiner (Sheet 2)
3. ASSOCIATED PIPING SYSTEMS 3 2.0 5.0 
                                                                COST (1975 $1000)
4. INSTRUMENTATION AND CONTROLS    in item 1  
                ITEM                           LABOR         OTHER          TOTAL               BASIS FOR COST ESTIMATE
5. ELECTRICAL SERVICE    base
  1. OPERATING LABOR, SUPERVISION,                                            3.3       15 min/shift AND OVERHEAD
6. SPARE PARTS  0.5 0.5   SUBTOTAL 15 47.0 62.0 
  2. MAINTENANCEMATERIAL AND.                                               10.0        3% of equipment cost LABOR
7. CONTINGENCY 1 5.0 6.0 10%
  3. CONSUMABLES, CHEMICALS, AND                                             1.0       oxygen @.S2.5/103 cf & .25 cfm 0
8. TOTAL DIRECT COSTS 16 52.0 68.0 
      SUPPLIES                                                                            7000 hrs Ca I
U'
  4. UTILITIES AND SERVICES
        Waste Disposal Water Steam                                                                  neg Electricity Building Services Other S. TOTAL 0 AND M ANNUAL COST                                              14.3 K                                                                                                                          C


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  
K*
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)  
                                          TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
3. ASSOCIATED PIPING SYSTEMS 3 2.0 5.0
                                                      FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
4. INSTRUMENTATION AND CONTROLS   in item 1  
      Description of Augment       PWR Air EJector      Charcoal/HEPA Filtration Unit (Sheet 1)
5. ELECTRICAL SERVICE   base
                                                              DIRECT COST (1975 $1000)
6. SPARE PARTS 0 0.5 0.5  SUBTOTAL 12.6 44.8 57.4 
                                                                                                                  BASIS FOR
7. CONTINGENCY 2 4.0 6.0 10%
                ITEM                               LABOR             EOUIPMENT/MATERIALS       TOTAL             COST ESTIMATE
8. TOTAL DIRECT COSTS 14.6 48.8 63.4 
                                                                                                        1*
    1. PROCESS EQUIPMENT                             3.0                   7.5                  10.5    chiller, heater, charcoal HEPA
                                                                                                                                  3
    2. BUILDING ASSIGNMENT                           3.0                    1.5                    4.5    10' x 10' x 15' @ $3/ft (unshielded turbine bldg)
    3. ASSOCIATED PIPING SYSTEMS                     2.0                   1.0                    3.0     allowance L*a
    4. INSTRUMENTATION AND CONTROLS                 0.5                    1.5                    2.0    allowance
    5. ELECTRICAL SERVICE                           0.5                  0.5                    1.0    allowance
    6. SPARE PARTS                                                         1.0                   1.0
            SUBTOTAL                                 9.0                  13.0                    22.0
    7. CONTINGENCY                                   1.0                    1.0                   2.0     1O0
    8. TOTAL DIRECT COSTS                           10.0                  14.0                    24.0


Appendix B to RG 1.110, Page B-22 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
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  
                                                          SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
2. MAINTENANCE MATERIAL AND  
          Description of Augnent          PWR Air EJector    Charcoal/HEPA Filtration Unit (Sheet 2)
LABOR  2.2 change every 2 yrs @ $150/filter element 3. CONSUMABLES, CHEMICALS, AND  
                                                                            COST (1975 $1000)
SUPPLIES  - in items 2 and 4
                    ITEM                                LARAR            flTIFD          TnTAI            DAete *  *    rP*eUA*
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
                    ___                                                      I*          ,    L          ueA5  rwK Guil r.4IrMIE
      l. OPERATING LABOR, SUPERVISION,                                                     3.8     15 min/shift + 40 hr annual test AND OVERHEAD
      2. MAINTENANCE MATERIAL AND                                                         2.0      includes replacement filter LABOR
    3. CONSUMABLES,       CHEMICALS, AND                                                   -       in item 2 EP
        SUPPLIES
U'
    4. UTILITIES AND SERViCES
            Waste Disposal                                                                 neg Water Steam Electricity Building Services Other
    5. TOTAL 0 AND M ANNUAL COST                                                         5.8 K


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  
K                                                                                                                              K
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
                                            TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
2. BUILDING ASSIGNMENT 3.8 2.0 5.8 8 x 12 x 12 @ $5/ft 3 (nonshielded area)
                                                      FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
3. ASSOCIATED PIPING SYSTEMS 1.3 0.7 2.0 
        Description of Augment       Steam Generator Flash Tank Vent to Main Condenser (Sheet 1)
4. INSTRUMENTATION AND CONTROLS  - in item 1
                                                              DIRECT COST (1975 $1000)
5. ELECTRICAL SERVICE 1.5 1.0 2.5 
                                                                                                                  BASIS FOR
6. SPARE PARTS 0.5 0.5  SUBTOTAL 8.6 26.2 34.8 
                  ITEM                             LABOR           EQUIPMENT/MATERIALS         TOTAL         COST ESTIMATE
7. CONTINGENCY 1.0 2.0 3.0 10%  
    I. PROCESS EQUIPMENT                                                                           -    no equipment required
8. TOTAL DIRECT COSTS 9.6 28.2 37.8 
    2. BUILDING ASSIGNMENT                                                                       neg    install In existing space
    3. ASSOCIATED PIPING SYSTEMS                     13                      7                     20    200 ft of 10-in pipe with
                                                                                                          2 valves U't ull
    4. INSTRUMENTATION AND CONTROLS                   4                      6                      10   allowance
    5. ELECTRICAL SERVICE                                                                         neg
    6. SPARE PARTS                                                                               neg SUBTOTAL                               17,,                  13                      30
    7. CONTINGENCY                                   2                      1                       3   10%
    8. TOTAL DIRECT COSTS                           19                    14                      33


Appendix B to RG 1.110, Page B-24 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREAThENT
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
                                                  SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
11. MAINTENANCE MATERIAL AND  
      Description of Augment   Steam.Generator Flash Tank Vent to Main Condenser (Sheet 2)
LABOR  0.6 2 HEPA or prefilters @ $150
                                                                  COST (1975 $1000)
each and 1 charcoal @ $900 each every 2 years
                  ITEM                         LABOR           OTHER         TOTAL               BASIS FOR COST ESTIMATE
12. CONSUMABLES, CHEMICALS, AND  
    1. OPERATING LABOR, SUPERVISION,                                             1          allowance AND OVERHEAD
SUPPLIES   in items 2 and 4  
    2. MAINTENANCE MATERIAL AND                                                 1         2% Total Direct Cost LABOR
13. UTILITIES AND SERVICES     Waste Disposal   0.1 $50/HEPA or prefilter, $100/charcoal filter  Water     Steam     Electricity   neg  Building Services     Other     
    3. CONSUHABLES, CHEMICALS, AND                                             neg
14. TOTAL O AND M ANNUAL COST  2.6 
.a    SUPPLIES
U'
    4. UTILITIES AND SERVICES
        Waste Disposal Water                                                                 neg Steam Electricity Building Services Other
     5. TOTAL 0 AND H ANNUAL COST                                                 2
   (                                                                                                                        (


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
K
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 10 71 81 prefilter/4" charcoal/HEPA @ $5/cfm, 30kw htr @ $200/kw
                                        TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
2. BUILDING ASSIGNMENT 12 8 20 16 x 20 x 12 @ $5/ft 3 (nonshielded area)
                                                      FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
3. ASSOCIATED PIPING SYSTEMS 3 2 5 
      Description of Augment       lSqpm Evaporator (Sheet 1)
4. INSTRUMENTATION AND CONTROLS  - in item 1
                                                            DIRECT COST (1975 $1000)
5. ELECTRICAL SERVICE 3 2 5 allowance  
                                                                                                              BASIS FOR
6. SPARE PARTS 5 5 4 elements of each type  SUBTOTAL 28 88 116 
                ITI'N                          I AnRO                                        T*TA!
7. CONTINGENCY 3 9 12 10%  
  1. PROCESS EQUIPMENT                             30                  225                    255    skid mounted, bundle,        submerged ASME VIII,       tubein Incoloy contact with process fluid
8. TOTAL DIRECT COSTS 31 97 128 
  2. BUILDING ASSIGNMENT                           68                    34                  102    evap & services 25' x 301 x 20'
                                                                                                      @ $6/ft3 plus 2,000 ft3 increase in solid waste storage area a. 3. ASSOCIATED PIPING SYSTEMS                     35                    30                    65  inludes service piping
  4. INSTRUMENTATION AND CONTROLS                 10                    10                    20   allowance
  5. ELECTRICAL SERVICE                           40                    25                    65  allowance
  6. SPARE PARTS                                   -                      27                    27  2% of item 1 plus tube bundle SUBTOTAL                               183                  351                    534
  7. CONTINGENCY                                   18                    35                    53  10%
  8. TOTAL DIRECT COSTS                         201                    386                    587


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
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREAThENT'SYSTEM
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
                                                        FOR LIGHT-WdATER-COOLED NUCLEAR REACTORS
2. BUILDING ASSIGNMENT 7.7 3.8 11.5 16 x 20 x 12 @ $3/ft 3 (nonshielded area)
      Description of Augment       30-gpm Evaporator (Sheet 2)     ,
3. ASSOCIATED PIPING SYSTEMS 3.0 2.0 5.0 
                                                                DIRECT COST (1975 $1000)
4. INSTRUMENTATION AND CONTROLS    in item 1
                  tTrW                                                                                              BASIS   FOR
5. ELECTRICAL SERVICE 3.0 2.0 5.0 allowance  
                                                                                                                      rncT rCY?UAYT
6. SPARE PARTS - 5.0 5.0 4 elements each type  SUBTOTAL 23.7 83.8 107.5  
                                                  I AfPtflD            rfIITDfMlrTIMATrDTAI        TnTA,
7. CONTINGENCY 2.0 9.0 11.0 10%
                  *.-                            -..rw-f              .dV..r  b.r I  ... u snlrl.# ,nI    .          bl    r~l) I lruI
8. TOTAL DIRECT COSTS 25.7 92.8 118.5 
    1. PROCESS EQUIPMENT                              30                       350                  380    ASME VIII
                                                                                                              skid mounted, submerged,
                                                                                                            'tube bundle, Incoloy in contact with process fluid t
  2. BUILDING ASSIGNMgNT                            88                        44                  132    evap + services - 25' x 40' x 20'
                                                                                                              @ $6/ft3 plus 2,000 ft 3 Increase In solid waste storage area
  3. ASSOCIATED PIPING SYSTEMS                       35                        35                    70    includes service piping CO
  4. INSTRUMENTATION AND CONTROLS                   10                        10                    20   allowance
  5. ELECTRICAL SERVICE                             40                        25                    65    allowance
  6. SPARE PARTS                                                               27                    27    2% of Item 1 plus tube bundle SUBTOTAL                                 203                      491                  694
  7.  CONTINGENCY                                     20                        49                    69    1O0
  8. TOTAL DIRECT COSTS                           223                      540                  763 C                                                                  C


Appendix B to RG 1.110, Page B-27 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
K
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
                                                                                                                                      'III
2. MAINTENANCE MATERIAL AND
                                                                    T
LABOR  9.0 30 HEPA or prefilters @ $150 each & 15 charcoal filters @
                                                              3)
$900 each every 2 years
                                          TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMErNT SYSTEM
3. CONSUMABLES, CHEMICALS, AND
                                                        (Sheet
SUPPLIES  - in items 2 and 4  
                                                50-gpmFOR LIGHT-WATER-COOLED NUCLEAR REACTORS
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   
                                            Augment of Evaporator Description Description of Augment       50-qpm Evaporator (Sheet 3)
5. TOTAL O AND M ANNUAL COST  15.6 
                                                              DIRECT COST (1975 $1000)
                                                                                                                BASIS FOR
                ITEM                               LABOR             EOUIPMENT/MATERIALS        TOTAL         COST ESTIMATE
  1. PROCESS EQUIPMENT                                30                  450                    480    ASME VIII
                                                                                                        skid mounted, submerged, tube bundle, Incoloy In contact with process fluid
  2. BUILDING ASSIGNMENT                              97                  48                    145    10% more than 30 gpm
  3. ASSOCIATED PIPING SYSTEMS                        35                  35                    70    allowance a
*0 4. INSTRUMENTATION AND CONTROLS                    10                  10                    20    allowance S. ELECTRICAL SERVICE                              40                  25                    65    allowance
  6. SPARE PARTS.                                                         27                    27    2% of Item 1 plus tube bundle SUBTOTAL                                  212                  595                    807
  7. CONTINGENCY                                      21                  60                    81    10%
  8. TOTAL- DIRECT COSTS                            233                  655                    888


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  
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
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
                                              SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
2. BUILDING ASSIGNMENT 20 13.6 33.6 28 x 20 x 12 @ $5/ft 3 (nonshielded area)
  Description of Augment   FuannAtnY  - RUR Dirty Ua~tm - Finn, fl,.n1,, (k..t £1 COST (1975 $1000)
3. ASSOCIATED PIPING SYSTEMS 5 3.0 8.0 base
              ITEM                         LABOR         OT14ER          TOTAL             BASIS FOR LOST FSTIMATF
4. INSTRUMENTATION AND CONTROLS  - in item 1
1. OPERATING LABOR, SUPERVISION,                                             12      2.6 x 106 gpy; 1000 hrs/yr labor AND OVERHEAD
5. ELECTRICAL SERVICE 6 4.0 10.0 allowance
2. MAINTENANCE MATERIAL AND                                                  30      7-1/2% of equipment cost LABOR
6. SPARE PARTS - 5.0 5.0 4 elements each type  SUBTOTAL 46 142.6 188.6 
3. CONSUMABLES, CHEMICALS, AND                                               neg      concentrate solidification chemicats SUPPLIES                                                                            in item 4
7. CONTINGENCY 5 14.0 19.0 10%
4. UTILITIES AND SERVICES                                                                                                      3 Waste Disposal                                                          70      100:1 feed to concentrate ratio @ 20/ft disposal cost Water                                                                    27      1000 gpm @ 1500 hrs @ 30t/1000 gal Steam                                                                    60      1500 hrs steaw @ 20,000 lb/hr @ $2/1000 lbs Electricity Building Services Other
8. TOTAL DIRECT COSTS 51 156.6 207.6 
5. TOTAL 0 AND M ANNUAL COST                                                199 C                                                                C


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
K*                                                                                                                                  K
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
                                    ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
2. BUILDING ASSIGNMENT 13.4 6.8 20.2 28 x 20 x 12 @ $3/ft 3 (nonshielded area)
                                                SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
3. ASSOCIATED PIPING SYSTEMS 3.0 5.0 8.0 base
      Description of Augment     Evaporator PWR Dirty Waste (Sheet 5)
4. INSTRUMENTATION AND CONTROLS    in item 1
                                                                COST (1975 $1000)
5. ELECTRICAL SERVICE 6.0 4.0 10.0 allowance
                lTYM                          [AROR          OTHER          TOTAL               BASIS FOR COST ESTTMATE
6. SPARE PARTS - 5.0 5.0 4 elements each type  SUBTOTAL 37.4 137.8 175.2
  I. OPERATING LABOR, SUPERVISION,
7. CONTINGENCY 4.0 14.0 18.0 10%
      AND OVERHEAD                                                            6.0       500,000 gpy; 500 hrs/yr labor
8. TOTAL DIRECT COSTS 41.4 151.8 193.2 
  2. MAINTENANCE MATERIAL AND
      LABOR                                                                  30.0        7-1/2% of equipment cost
  3. CONSUMABLES, CHEMICALS, AND                                              -          concentrate solidification chemicals
0'
      SUPPLIES                                                                            in item 4
  4. UTILITIES AND SERVICES                                                                                                      3
                                                                                          50:1  feed to concentrate ratio @ $20/ft Waste Disposal                                                        27.0       disposal cost Water                                                                  5.0         1000 gpm @.277 hrs @ 30t/1000 gal Steam                                                                12.0        277 hrs steam @S20,000 4bs/hr @$2/1000 lbs Electricity Building Services Other
  5. TOTAL 0 AND MANNUAL COST                                                80.0


Appendix B to RG 1.110, Page B-30 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
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
                                                    SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
2. MAINTENANCE MATERIAL AND  
        Description of Augment v
LABOR   18.0 60 HEPA or prefilters @ $150 each & 30 charcoal filters @
                                  EvaDorator
$900 each every 2 years
                                              - Condenser Polisher Chemical IaCto Ih    +0A
3. CONSUMABLES, CHEMICALS, AND  
                                                                  COST (1975 $1000)
SUPPLIES   - in items 2 and 4  
                    ITEM                         LAI*R          NTH*D          T*TAI
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    
                                                LABOR     0ATD    AU      .,* TC4TAI                  FRUK CS
5. TOTAL O AND M ANNUAL COST   27.4 
                                                                                                              LU  ETIMATE
    1. OPERATING LABOR, SUPERVISION,
        AND OVERHEAD                                                               6.0      650.000 gpy; 500 hr/yr labor
  2.   MAINTENANCE MATERIAL AND
        LABOR                                                                     30.0       7-1/2% of equipment cost
  3.   CONSUMABLES, CHEMICALS. AND                                                         concentrate solidification chemicals
0      SUPPLIES                                                                           In item 4
  4. UTILITIES   AND SERVICES
          Waste Disposal
                                                                                  87.0     20:1 feed to concentrate ratio @ $20/ft 3 Wl7.0      disposal cost Water                                                                   6.5     1000 gpm 0 360 hrs @ 30/10OO gal Steam                                                                   14.4     360 hrs steam @ 20,000 lb/hr @ $2/1000 lbs Electricity Building Services Other
  5.   TOTAL 0 AND M ANNUAL COST                                               143.9
(                                                                                                                                    C


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  
K                                                                                                                                      K
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 300 500 800 500-ton capacity, w/o air filters
                                    ANNUAL OPERATING AND MAI[NTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
2. BUILDING ASSIGNMENT  - Coolers can be installed in existing space saved by deletion of ducting
                                                  SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
3. ASSOCIATED PIPING SYSTEMS  - in item 1
      Description of Augment       .an    - hla~aum*., Um.4.a Iqkaa÷ 7*
4. INSTRUMENTATION AND CONTROLS   - in item 1
                                                                  COST (1975. $1000)
5. ELECTRICAL SERVICE 40 50 90 
                  TT!M                          LABOR           OTHER          TOTAL             BASIS FOR COST ESTIMATE
6. SPARE PARTS - 8 8 1% item 1 SUBTOTAL 340 558 898 
    I. OPERATING LABOR, SUPERVISION,
7. CONTINGENCY 34 56 90 10%
      AND OVERHEAD                                                                6.0    160,000 gpy; 500 hrs/yr
8. TOTAL DIRECT COSTS 374 614 988 
    2. MAINTENANCE MATERIAL AND
      LABOR                                                                      30.0      7-1/25 of equipment cost
    3. CONSUMABLES, CHEMICALS, AND                                                  -       concentrate solidification chemicals In ad    SUPPLIES                                                                              item 4 a,    UTILITIES AND SERVICES
LeD
    4.  WasteITsposal                                                              8.6      50:1 feed to concentrate ratio 0 $20/ft 3 disposal cost Water                                                                      1.6      1000 gpm 0 90 hrs 0 30t/1000 gal Steam                                                                      3.6      90 hrs steam 0 20,000 lb/hr 1 $2/1000 lbs Electricity Building Services Other
    5. TOTAL 0 AND MANNUAL COST                                                    49.8


Appendix B to RG 1.110, Page B-32 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
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
                                                        FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
2. MAINTENANCE MATERIAL AND
        Description of Augment       Evaporator Distillate Demineralizer (Sheet 1)
LABOR  20.0 21/2% of equipment costs
                                                                DIRECT COST (1975 $1000)
3. CONSUMABLES, CHEMICALS, AND
                  TTIrM                            I anAD            EniI nlrT IUA?~nAi    e    qrft*IrA I
SUPPLIES   - in item 2  
                                                                                                                      BASIS FOR
4. UTILITIES AND SERVICES      Waste Disposal      Water   13.0 500 gpm @ 10¢/1,000 gal &
                    *,-.                           I.rluvn            Iuu~rnllu~r'¶l  KhMiLR      IJI/L              W,5MIIEIHMAIT
50% load factor Steam      Electricity  33.0 400 kw @ 0.018 $/kw-hr  Building Services      Other   
    1.  PROCESS EQUIPMENT                              4.0                      20.0               24.0    30 ft 3 , SS. ASME VIII, 150 psi nonregenerative, w/resin
5. TOTAL O AND M ANNUAL COST  69.3 
    2.  BUILDING ASSIGNMENT                            6.4                        3.2                9.6   10' x 10' x 16' @ $6/ft3 (shielded area)
    3. ASSOCIATED PIPING SYSTEMS                      9.0                        6.0              15.0    2" piping i
Ot
  4.   INSTRUMENTATION AND CONTROLS                  2.0                        3.0                5.0   remote conductivity readout
  5.  ELECTRICAL SERVICE                                                                          neg
  6.  SPARE PARTS                                                                1.0                 1.0
            SUBTOTAL                                21.4                        33.2              54.6
  7. CONTINGENCY                                    2.0                         3.0               5.0    10%
  8. TOTAL DIRECT COSTS                            23.4                        36.2              59.6
(                                                                  C                                                                  (


Appendix B to RG 1.110, Page B-33 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS Description of Augment 600-ft
)
3 Waste Gas Decay Tank (Sheet 1) DIRECT COST (1975 $1,000) ITEM LABOR
K
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 2.5 20 22.5 600-ft
                                    ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
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)
                                                      SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
3. ASSOCIATED PIPING SYSTEMS 1.0 1 2.0 10% of item 1
      Description of Augment     Evaporator Distillate Demineralizer (Sheet 2)
4. INSTRUMENTATION AND CONTROLS  neg 
                                                                    COST (1975 $1000)
5. ELECTRICAL SERVICE  neg 
                  YtM                              I ARnlQ        OTHER          TOTAL                 BASIS FOR COST ESTIMATE
6. SPARE PARTS  neg  SUBTOTAL 21.5 30 51.5 
                  aI1II                    ____________
7. CONTINGENCY 2.0 3 5.0 10%
    I. OPERATING LABOR, SUPERVISION.                                              1.8        1500 hrs operation @ 10% attendance AND OVERHEAD
8. TOTAL DIRECT COSTS 23.5 33 56.5 
    2. MAINTENANCE MATERIAL AND
      LABOR                                                                      2.0        allowance
    3. CONSUMABLES, CHEMICALS, AND
,ap    SUPPLIES                                                                    2.3        1 change per yr @ $75/ft 3
    4. UTILITIES AND SERVICES
        Waste Disposal                                                            0.6         30 ft 3
                                                                                                        @ $20/ft 3 disposal cost Water Steam Electricity Building Services Other
    5. TOTAL 0 AND M ANNUAL COST                                                    6.7


Appendix B to RG 1.110, Page B-34 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
TER-COOLED NUCLEAR REACTORS Description of Augment 600-ft
                                                      FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
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
      Description of Augment     50-opDemintralzer Sh t 1)
LABOR - - neg  3. CONSUMABLES, CHEMICALS, AND
                                                          {Sheet 1)
SUPPLIES - - neg 4. UTILITIES AND SERVICES      Waste Disposal      Water      Steam   neg   Electricity      Building Services      Other   
                                  SO-gin  .D*l.n.fraltzer DIRECT COST (1975 $1000)
5. TOTAL O AND M ANNUAL COST   neg  
                                                                                                                BASIS FOR
                ITEM                              LAROR              1ITOM    AUIFRAI It    TIhTAI              CflCY
                                                                                                                      1T
                                                                                                                        tMAr"
  1. PROCESS EQUIP4ENT                              5                  20.0                  25.0  30 ft 3. SS, A*NE VIII. 150 psi, nonreganerative, with resin
  2. BUILDING ASSIGNMENT                              9                    4.8                  13.8  12' x 12' x 16' 0 $6/ft3 (shielded ar*)
  3. ASSOCIATED PIPING SYSTEMS                        9                    6.0                  15.0  2" piping
  4. INSTRUMENTATION AND CONTROLS                    4                   6.0                  10.0
   5.  ELECTRICAL SERVICE                                                                        No
   6.  SPARE PARTS                                                          2.0                  2.0    miscellaneous supplies SUBTOTAL                                  27                  38.8                  66.8
  7.  CONTINGENCY                                    2                    4.0                  6.0    10%
   8. TOTAL DIRECT COSTS                            29                  42.8        -        71.8
(                                                                C                                                              C


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
K                                                                K
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  
                                          TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
2. BUILDING ASSIGNMENT 28.8 14.4 43.2 15 x 30 x 16 @ $6/ft 3  (shielded area)  
                                                      FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
3. ASSOCIATED PIPING SYSTEMS 32.0 13.0 45.0 allowance
      Description of Augment       1O0-9pm Deminerallizer (Sheet 2)
4. INSTRUMENTATION AND CONTROLS 10.0 40.0 50.0 allowance
                                                              DIRECT COST (1975 $1000)
5. ELECTRICAL SERVICE 13.0 12.0 25.0 allowance
                                                                    FO*l PMFNT/MATFRTALS                        BASIS FOR
6. SPARE PARTS - 2.0 2.0  SUBTOTAL 133.8 381.4 515.2 
                  tT*M                            LANOR                                        TOTAL            COST FSTTMATF
7. CONTINGENCY 13.0 38.0 51.0 10%
  I. PROCESS EQUIPMENT                               5                  35.0                   40.0   60 ft 3 , SS, ASME VIII, 150 psi, nonregenerative, with resin
8. TOTAL DIRECT COSTS 146.8 419.4 566.2 
  2. BUILDING ASSIGNMENT                             9                    4.8                   13.8  12' x 12' x 16' 0 $6/ft3 (shielded area)
  3." ASSOCIATED PIPING SYSTEMS                     10                  10.0                   20.0   2-1/21 piping a, 4. INSTRUMENTATION AND CONTROLS                   4                    6.0                   10.0
.1
  5. ELECTRICAL SERVICE                                                                         neg
  6. SPARE PARTS                                                         2.0                   2.0  miscellaneous supplies SUBTOTAL                                 28                  57.8                   85.8
  7. CONTINGENCY                                     3                    6.0                   9.0
  B. TOTAL DIRECT COSTS                             31                  63.8                   94.8


Appendix B to RG 1.110, Page B-36 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
TOTAL DIRECT COST ESTIMATE SHEET OF RADWAST!E TREATMENT SYSTEM
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
                                                    FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
2. MAINTENANCE MATERIAL AND
      Description of Augment         20-plDmneralizer(Sheet 3)  3)__
LABOR   10.0 3% of equipment cost
                                                        (Sheet
3. CONSUMABLES, CHEMICALS, AND
                                  200-gpm Oemtneraltzer DIRECT COST (1975 $1000)
SUPPLIES   1.0 oxygen @ $2.5/10
                                                                  EflUIPI4FNTII4ATFRTAL *                        BASIS FOR
3 cf & .25 cfm @ 7,000 hrs
                ITEM                             LABOR                                         TflTAI          rnCT r~tTuATr
4. UTILITIES AND SERVICES      Waste Disposal      Water      Steam  neg   Electricity      Building Services      Other   
                                                                  1T                  A
5. TOTAL O AND M ANNUAL COST  14.3 
  1. PROCESS EQUIPMENT                              5                    60.0                    65.0  120 ft 3 , SS, ASME VIII, i50 psi, nonregenerative, with resin
   2.  BUILDING ASSIGNMENT                          11                      5.2                    16.2  13' x 13' x 16' 0 $6/ft 3
                ___(shielded                                                                                        area)
  3.  ASSOCIATED PIPING SYSTEMS                    12                    12.0                    24.0  4" piping
   4.  INSTRUMENTATION AND CONTROLS                  4                    6.0                    10.0
  5. ELECTRICAL SERVICE                                                                          neg
   6.  SPARE PARTS                                                          2.0                      2.0 miscellaneous supplies SUBTOTAL                                32                    85.2                   117.2
  7.  CONTINGENCY                                    3                     9.0                    12.0
   8. TOTAL DIRECT COSTS                            35                    94.2                  129.2
(                                                                                                                                  (


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
K
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 3.0 7.5 10.5 chiller, heater, charcoal HEPA
                                          TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
2. BUILDING ASSIGNMENT 3.0 1.5 4.5 10 x 10 x 15 @ $3/ft 3 (unshielded turbine building)
                                                      FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
3. ASSOCIATED PIPING SYSTEMS 2.0 1.0 3.0 allowance
      Description of Augment       400-gpm Demineralizer  -  Steam Generator Blowdown Service (Sheet 4)
4. INSTRUMENTATION AND CONTROLS 0.5 1.5 2.0 allowance
                                                              DIRECT COST (1975 $1000)
5. ELECTRICAL SERVICE 0.5 0.5 1.0 allowance
                                                                                                                  BASIS FOR
6. SPARE PARTS - 1.0 1.0  SUBTOTAL 9.0 13.0 22.0 
                  I TrM                            lAROR              EOUJIPMNT/MATERjALS          TOTAL           COST ESTIMATE
7. CONTINGENCY 1.0 1.0 2.0 10%
                                  T                                                              I                COST ESTIMATE
8. TOTAL DIRECT COSTS 10.0 14.0 24.0 
                                                                                                                3
  1. PROCESS EQUIPMENT                               5                    60.0                   65.0  120 ft , SS. ASME VIII, 150 psi, nonregenerative. with resin BUILDING ASSIGNMENT                           11                      5.2                    16.2  ,3' x 13' x 16' @ $6/ft 3
  2.


Appendix B to RG 1.110, Page B-38 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
(shielded area)
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
  3. ASSOCIATED PIPING SYSTEMS                    20                      20.0                  40.0  6" piping a,
2. MAINTENANCE MATERIAL AND
'a
LABOR  2.0 includes replacement filter
  4.  INSTRUMENTATION AND CONTROLS                    4                      6.0                    10.0 allowance
3. CONSUMABLES, CHEMICALS, AND
  5. ELECTRICAL SERVICE                                                                            neg
SUPPLIES  - in item 2  
  6.  SPARE PARTS                                                            2.0                    2.0 miscellaneous supplies SUBTOTAL                                40                    93.2                  133.2
4. UTILITIES AND SERVICES      Waste Disposal  neg  Water      Steam      Electricity      Building Services      Other   
    7. CONTINGENCY                                      4                     9.0                    13.0
5. TOTAL O AND M ANNUAL COST  5.8 
  8. TOTAL DIRECT COSTS                            44                    102.2                  146.2


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
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT  - no equipment required
                                                                SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
2. BUILDING ASSIGNMENT  neg install in existing space
        Description of Augment     BWR  - 2nd Waste Demineralizer In Serf es (Sheet El COST (1975 $1000)
3. ASSOCIATED PIPING SYSTEMS 13 7 20 200 ft of 10-in pipe with 2 valves 4. INSTRUMENTATION AND CONTROLS 4 6 10 allowance  
                    ITEM                                   lABOR            NTNrD          TJlTA!
5. ELECTRICAL SERVICE   neg 
                                              _...._-_....__,,__                            ,v-n  -
6. SPARE PARTS  neg  SUBTOTAL 17 13 30  
                                                                                                                  aAeT*
7. CONTINGENCY 2 1 3 10%
                                                                                                                  DROIO
8. TOTAL DIRECT COSTS 19 14 33 
                                                                                                                          *n*  *
                                                                                                                          rvr uK    EV)lr.1~PY.I
                                                                                                                                      PP*guA*P
    1.  OPERATING LABOR, SUPERVISION,                                                        3.3      15 min/shift AND OVERHEAD
    2. MAINTENANCE MATERIAL AND
        LABOR                                                                                5.0      allowance
    3. CONSUMABLES,   CHEMICALS, AND                                                          9.0      1 change per year @ 120 ft 3 0 $75/ft 3 (one a      SUPPLIES                                                                                        vessel change per year. regardless of size)
-.J
a
    4.  UTILITIES AND SERVICES
          Waste Disposal                                                                      2.4      120 ft 3 lyr    * $20/ft 3 disposal cost Water Steam Electricity Building Services Other
    5. TOTAL 0 AND M ANNUAL COST                                                            19.7 C


Appendix B to RG 1.110, Page B-40 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
K                                                                                                                              I
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
                                    ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
2. MAINTENANCE MATERIAL AND  
                                                  SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
LABOR  1 2% Total Direct Cost
    Description of Augment       Demineralizer - PWR Clean Wastes (Sheet 6)
3. CONSUMABLES, CHEMICALS, AND  
                                                                    COST (197k.$1000)
SUPPLIES   neg  4. UTILITIES AND SERVICES     Waste Disposal      Water   neg  Steam     Electricity     Building Services     Other    
                YYIPLu AILr nV                  IlV%
5. TOTAL O AND M ANNUAL COST   2 
                                                I am*o    -
                                                                flTurD
                                                                  lll_ __ _
                                                                                ?linI
                                                                                  Ifl, matie fflS EflM? rCTTMATe
                                                                                                      &'flC I  l      bl *fll
  1. OPERATING LABOR, SUPERVISION,                                                 1.8    10% of DRS shim bleed (50,000 gpy),
    AND OVERHEAD                                                                           30 min/day
   2. MAINTENANCE MATERIAL AND
    LABOR                                                                         5.0    allowance
                                                                                                                3
   3. CONSUMABLES,
    SUPPLIES        CHEMICALS, AND                                                 2.3    30 3ft /yr @ $75/ft3 a
   4. UTILITIES AND SERVICES
      Waste Disposal                                                               0.6     30 ft 3/yr @ $20/ft3 disposal cost Water Steam Electricity Building Services Other S. TOTAL 0 AND M ANNUAL COST                                                     9.7


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  
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADIASTE TREATMENT
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 30 225 255 skid mounted, submerged tube bundle, ASME VIII, Incoloy in
                                                      SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
          Description of Augment     Demineralizer - BWR Dirty Waste (Sheet 7)
                                                                      COST (1975 $1000)
                    JTFN                          [ABDR            nlTHVg          TNlT61            DACIC mnD r.ncT reTvUnt I. OPERATING LABOR, SUPERVISION,
          AND OVERHEAD                                                                6.5      2.6 x 106 gpy, 30 min/shift
      2. MAINTENANCE MATERIAL AND
          LABOR                                                                      5.0      allowance CONSUNABLES,  CHEMICALS, AND33
      3.  SUPALES                                                                  64.5      860 ft 3 resin 0 $75/ft 3 N
      4. UTILITIES AND SERVICES
            Waste Disposal                                                          17.2      860 ft 3 @ $20/ft 3 disposal cost Water Steam Electricity Building Services Other S. TOTAL 0 AND N ANNUAL COST                                                 93.2
--- I                                                                C                                                          C


contact with process fluid
/
2. BUILDING ASSIGNMENT 68 34 102 evap & services 25 x 30 x 20 @ $6/ft 3 plus 2,000 ft
                                                                K
3 increase in solid waste storage area
                                    ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
3. ASSOCIATED PIPING SYSTEMS 35 30 65 includes service piping
                                                  SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
4. INSTRUMENTATION AND CONTROLS 10 10 20 allowance
      Description of Augment      Demineraltzer - PWR Dirty. Wastes (w/o turbine building) (Sheet 8)
5. ELECTRICAL SERVICE 40 25 65 allowance  
                                                                  COST (1975 $1000)
6. SPARE PARTS - 27 27 2% of item 1 plus tube bundle SUBTOTAL 183 351 534  
                ITEM                          LABOR          OTHER          TOTAL                BASIS FOR COST ESTIMATE
7. CONTINGENCY 18 35 53 10%
  l.  OPERATING LABOR,  SUPERVISION,
8. TOTAL DIRECT COSTS 201 386 587 
      AND OVERHEAD                                                                3.3       500,000 gpy; 15 min/shift
  2. MAINTENANCE MATERIAL AND
      LABOR                                                                      5.0      allowance
  3.  CONSUMABLES, CHEMICALS, AND
      SUPPLIES                                                                  12.0        160 ft 3 /yr @ $75/ft 3 a
  4. UTILITIES AND SERVICES
        Waste Disposal                                                          3.2      160 ft 3 /yr @ $20/ft 3 disposal cost water Steam Electricity Building Services Other
  5. TOTAL 0 AND M ANNUAL COST                                                23.5


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
ANNUAL OPERATIN AND MAINTE*ANCE COST ESTIMTE SHEET OF RADWASTE TREATMENT
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
                                                            SYSTEM FOR L.IGHT,oWATER-COOLEO NUCL..EAR,, REACTORS
2. BUILDING ASSIGNMENT 88 44 132 evap + services - 25 x 40 x 20 @ $6/ft 3 plus 2,000 ft
      D*crlrintinn      of Aujnmant flminapA147AP      .  DUo
3 increase in solid waste storage area
            *7m,
3. ASSOCIATED PIPING SYSTEMS 35 35 70 includes service piping
              *  **,*,-*      pww-                      -  .  T. *    a w,*g uu,,*U-I
4. INSTRUMENTATION AND CONTROLS 10 10 20 allowance
                                                                        *fm          rC1      uVfm "a 1.411W4b  7I
5. ELECTRICAL SERVICE 40 25 65 allowance
                                                                                COST (1975 $1000)
6. SPARE PARTS - 27 27 2% of item 1 plus tube bundle  SUBTOTAL 203 491 694 
                      ITEM                               I ARMR            flTIIFA          Ti*TAI                      oAeTe *    *Ae*  rPgvu4*
7. CONTINGENCY 20 49 69 10%
                      --                    .... ______                      ",,'          ,,,.
8. TOTAL DIRECT COSTS 223 540 763 
                                                                                              ..-.                      urwl, rvuK I.UF)I LtIY:llrl
  1. OPERATING LABOR, SUPERVISION.


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
AND OVERHEAD                                                                              13.1           1 hr/shift, 2.6 x 106 opy
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 30 450 480 ASME VIII skid mounted, submerged, tube bundle, Incoloy in contact with
  2.  MAINTENANCE MATERIAL AND
      LABOR                                                                                        5.0          allowance
  3.  CONSUMABLES, CHEMICALS, AND
a SUPPLIES                                                                                64.5            660 ft 3 resin 0 $75/ft 3
  4. UTILITIES AND SERVICES
        Waste Disposal                                                                        17.2            860 ft 3/yr 9 $20/ft 3 disposal cost Water Steam Electricity Building Services Other S.  TOTAL 0 AND N ANNUAL COST                                                               99.8
(                                                                      .-."(
                                                                -1-:j:.1i-:i...-
                                                                              ........                                                              r


process fluid
K
2. BUILDING ASSIGNMENT 97 48 145 10% more than 30 gpm
                                  A..UAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
3. ASSOCIATED PIPING SYSTEMS 35 35 70 allowance
                                                SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
4. INSTRUMENTATION AND CONTROLS 10 10 20 allowance
    Description of Augment    Demineralizer - PIER Steam Generator Blowdomn (Sheet 10)
5. ELECTRICAL SERVICE 40 25 65 allowance
                                                                COST (1975 $1000)
6. SPARE PARTS - 27 27 2% of item 1 plus tube bundle  SUBTOTAL 212 595 807 
                tim                          I alLfl9        nyu,..O        inaI                ma*tt ens rtnt ReTtMAta OPERATING LABOR, SUPERVISION.
7. CONTINGENCY 21 60 81 10%
8. TOTAL DIRECT COSTS 233 655 888  


Appendix B to RG 1.110, Page B-44 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
AND OVERHEAD                                                               3.3      15 min/shift
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
  2. MAINTENANCE MATERIAL AND
6 gpy; 1000 hrs/yr labor
    LABOR                                                                     5.0      allowance
2. MAINTENANCE MATERIAL AND  
   3. CONSUMABLES, CHEMICALS, AN"
LABOR  30 71/2% of equipment costs
a    SUPPLIES                                                                 16.9      225 ft 3 resin/yr @$75/ft3
3. CONSUMABLES, CHEMICALS, AND
   4. UTILITIES AND SERVICES
SUPPLIES  neg concentrate solidification chemicals in item 4
      Waste Disposal                                                           4.5      225 ft 3 /Yr I $20/ft 3 disposal cost Water Stem Electricity Building Services Other S. TOTAL 0 AND M ANNUAL COST                                                 29.7
4. UTILITIES AND SERVICES     Waste Disposal   70 100:1 feed to concentrate ratio
@ $20/ft 3 disposal cost Water   27 1,000 gpm @ 1,500 hrs @ 30¢/1000 gal  Steam  60 1,500 hrs steam @ 20,000 lb/hr @ $2/1,000 lbs  Electricity     Building Services     Other    
5. TOTAL O AND M ANNUAL COST   199 


Appendix B to RG 1.110, Page B-45 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
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
                                                            FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
2. MAINTENANCE MATERIAL AND
          Description of Augment     20-qp Cartridge Filter (Sheet 1)  1)
LABOR  30.0 71/2% of equipment costs
                                                        Ftlter (Sheet
3. CONSUMABLES, CHEMICALS, AND
                                      20-qm Cartrtd9e DIRECT COST (1975 $1000)
SUPPLIES  - concentrate solidification chemicals in item 4
                    TTFM                            I AI*fl2            vN Itur
4. UTILITIES AND SERVICES      Waste Disposal  27.0 50:1 feed to concentrate ratio @
                                                                                ¶      u'IIAqr rD lr e                BASIS FOR
$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   
                                          ...                            t.J      ~vrl.rnlr.lL*nL    T*Ai UIhLU                11MAT
5. TOTAL O AND M ANNUAL COST  80.0 
      1.  PROCESS EQUIPMENT                              2.0                        5.0                   7.0  SS, ASME VIII, 150 psi BUILDING ASSIGNMENT                            5.6                        3.0                   8.6 16' x 12' x 20' S $6/ft 3
      2.


Appendix B to RG 1.110, Page B-46 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
(shielded area)
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
      3. ASSOCIATED PIPING SYSTEMS                      1.5'                      1.0                    2.5  allowance
2. MAINTENANCE MATERIAL AND
-. 4 Q
LABOR  30.0 71/2% of equipment costs
at    4. INSTRUMENTATION AND CONTROLS                    0.6                        2.4                    3.0  allowance
3. CONSUMABLES, CHEMICALS, AND
      5. ELECTRICAL SERVICE                                                                                neg
SUPPLIES    concentrate solidification chemicals in item 4
    6. SPARE PARTS                                                                0.5                    0.5 SUBTOTAL                                  9.7                      11.9                  21.6
4. UTILITIES AND SERVICES      Waste Disposal  87.0 20:1 feed to concentrate ratio @
    7. CONTINGENCY                                    1.0                        1.0                    2.0 10%
$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   
     8. TOTAL DIRECT COSTS                            10.7                        12.9                 23.6
5. TOTAL O AND M ANNUAL COST  143.9
(


Appendix B to RG 1.110, Page B-47 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
TREATMENT
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
                                  ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE
2. MAINTENANCE MATERIAL AND  
                                              SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
LABOR  30.0 71/2% of equipment costs
    Description of Augment   Cartridge Filter (Sheet 2)
3. CONSUMABLES, CHEMICALS, AND  
                                                                COST (1975 $1000)
SUPPLIES   - concentrate solidification chemicals in item 4
                                                            A'1JCDl        T*TAI              RAM!S FOR COST ESTIMATE
4. UTILITIES AND SERVICES     Waste Disposal  8.6 50:1 feed to concentrate ration
              ITEM                          LADUK          uini n          ,    -... .        .....    .... ...  ..
@ $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    
                                                                                4.5      10 changes @ 10 man-hrs/change
5. TOTAL O AND M ANNUAL COST   49.8 
1. OPERATING LABOR. SUPERVISION,                                                         @ $12/hr + 15 min/shift AND OVERHEAD
2. MAINTENANCE MATERIAL AND                                                             allowance
                                                                                1.0
    LABOR
3. CONSUMABLES. CHEMICALS, AND                                                           10 changes/yr @$100/change
                                                                                1.0
    SUPPLIES
4. UTILITIES AND SERVICES                                                                                         3
                                                                                1.5      10 drums/yr @$20/ft Waste Disposal Water Steam Electricity Building Services Other
                                                                                8.0
5. TOTAL 0 AND MANNUAL COST


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
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREAT1ENT SYSTEM
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 4.0 20.0 24.0 30 ft
                                                                                                        i FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
3 , SS, ASME VIII, 150 psi nonregenerative, w/resin
        Description of Augment     100-gpim Precoat Filter (Shoot 1)
2. BUILDING ASSIGNMENT 6.4 3.2 9.6 10 x 10 x 16 @ $6/ft 3 (shielded area)
                                                                    1)
3. ASSOCIATED PIPING SYSTEMS 9.0 6.0 15.0 2" piping
                                                      Ftlter (Sheet lO0-gpm Precoat            DIRECT COST (1975 $1000)
4. INSTRUMENTATION AND CONTROLS 2.0 3.0 5.0 remote conductivity readout
                                                                        fIW01T
5. ELECTRICAL SERVICE  neg 
                                                                            P~NT uI~dTIDTAI                        BASIS FOR
6. SPARE PARTS - 1.0 1.0  SUBTOTAL 21.4 33.2 54.6 
                  ITEM                              LARnR                                        T*TAI
7. CONTINGENCY 2.0 3.0 5.0 10%
    1. PROCESS EQUIPMENT                             10                      65.0                   75  automated system 1 gpm/ft 2 ,
8. TOTAL DIRECT COSTS 23.4 36.2 59.6 
                                                                                                          ASM4E VIII
        BUILDING ASSIGNMENT                           18                      9.0                  27  15' x 15' x 20' 0 $6/ft 3
  2.


Appendix B to RG 1.110, Page B-49 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
(shielded area)
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
  3. ASSOCIATED PIPING SYSTEM4S                      16                      9.0                  25   35% of equipment cost
16. MAINTENANCE MATERIAL AND  
0
LABOR   2.0 allowance  
  4.   INSTRUMENTATION AND CONTROLS                                                                      in item 1
17. CONSUMABLES, CHEMICALS, AND
   5.  ELECTRICAL SERVICE                              7                      13.0                 20    allowance
SUPPLIES   2.3 1 change per yr @ $75/ft
  6.  SPARE PARTS                                                              2.0                    2  2% of item 1 SUBTOTAL                                51                      98.0                  149
3 18. UTILITIES AND SERVICES      Waste Disposal   0.6 30 ft
  7.  CONTINGENCY                                      5                    10.0                   15    10%
3 @ $20/ft 3 disposal cost  Water      Steam      Electricity      Building Services      Other   
  8.   TOTAL DIRECT COSTS                            56                    108.0                164
19. TOTAL O AND M ANNUAL COST  6.7 
(                                                                                                                                    r


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
K                                                                                                                                    K
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 5 20.0 25.0 30 ft
                                          TOTAL DIRECT COST ESTIMATE     SHEET OF RADWASTE TREATMENT SYSTEM
3 , SS, ASME VIII, 150 psi, nonregenerative, with resin
                                                                    2)
2. BUILDING ASSIGNMENT 9 4.8 13.8 12 x 12 x 16 @ $6/ft 3  (shielded area)
                                                        FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
3. ASSOCIATED PIPING SYSTEMS 9 6.0 15.0 2" piping
      Description of Augment     400-oam Precoat Filter (Sheet 2)
4. INSTRUMENTATION AND CONTROLS 4 6.0 10.0 
                                    -vT
5. ELECTRICAL SERVICE  neg 
                                                            (Sheet DIRECT COST (1975 $1000)
6. SPARE PARTS - 2.0 2.0 miscellaneous supplies  SUBTOTAL 27 38.8 65.8 
                                                                                                                  BASIS FOR
7. CONTINGENCY 2 4.0 6.0 10%
                  TT*M                            LAROR              EOUIPMENT/MATERIALS         TOTAL         COST ESTIMATE
8. TOTAL DIRECT COSTS 29 42.8 71.8 
      PROCESS EQUIPMENT                             35                      135.0                   170    automated system; 1 gpm/ft 2


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
===1. ASME Viii===
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 5 35.0 40.0 60 ft
                                                                                                                                    3 BUILDING ASSIGNMENT                           24                      12.0                    36  15' x 20' x 20' @ $6/ft
3 , SS, ASME VIII, 150 psi, nonregenerative, with resin
    2.                                                                                                      (shielded area)
2. BUILDING ASSIGNMENT 9 4.8 13.8 12 x 12 x 16 @ $6/ft 3  (shielded area)  
    3. ASSOCIATED PIPING SYSTEMS                     31                      16.0                     47  35% of equipment cost
3. ASSOCIATED PIPING SYSTEMS 10 10.0 20.0 21/2" piping
-J
4. INSTRUMENTATION AND CONTROLS 4 6.0 10.0 
    4. INSTRUMENTATION AND CONTROLS                   -                                                -    item I
5. ELECTRICAL SERVICE  neg 
    5. ELECTRICAL SERVICE                             12                      18.0                    30   allowance
6. SPARE PARTS - 2.0 2.0 miscellaneous supplies  SUBTOTAL 28 57.8 85.8 
    6. SPARE PARTS                                   -                       3.0                       3 SUBTOTAL                                102                    184.0                   286
7. CONTINGENCY 3 6.0 9.0 
    7. CONTINGENCY                                   10                      18.0                     28    10%
8. TOTAL DIRECT COSTS 31 63.8 94.8 
    8. TOTAL DIRECT COSTS                           112                    202.0                    314


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  
ANNUAL OPERATING AND MAINTENANCE COST ESTI1ATE SHEET OF RADWASTE TREATMENT
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 5 60.0 65.0 120 ft
                                                SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
3 , SS, ASME VIII, 150 psi, nonregenerative, with resin
    Description of Augment     Precoat Filter - BWR Dirty Waste (Sheet 3)
2. BUILDING ASSIGNMENT 11 5.2 16.2 13 x 13 x 16 @ $6/ft 3  (shielded area)
                                                                COST (1975 $1000)
3. ASSOCIATED PIPING SYSTEMS 12 12.0 24.0 4" piping
                ITEM                         LABOR         OTHER          TOTAL               BASIS FOR COST !STTI4ATF
4. INSTRUMENTATION AND CONTROLS 4 6.0 10.0 
  1. OPERATING LABOR, SUPERVISION,
5. ELECTRICAL SERVICE   neg 
    AND OVERHEAD                                                              6.6      2 x 106 gpy, 30 min/shift
6. SPARE PARTS - 2.0 2.0 miscellaneous supplies  SUBTOTAL 32 85.2 117.2 
  2. MAINTENANCE MATERIAL AND
7. CONTINGENCY 3 9.0 12.0 
    LABOR                                                                    10.0       allowance
8. TOTAL DIRECT COSTS 35 94.2 129.2 
  3. CONSUMABLES, CHEMICALS, AND                                               6.0       10 lbs precoat @ lOt/lb per 1000 gal SUPPLIES                                                                            processed
   4. UTILITIES AND SERVICES                                                                                                            3 Waste Disposal                                                        40.0       1 ft 3/sludge per 1000 qal processed @ $30/ft disposal cost Water Steam Electricity Building Services Other S. TOTAL 0 AND M ANNUAL COST          j[                                    62.6
(                                                                                                                              C


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
T                                                                K
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 5 60.0 65.0 120 ft
                                          TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
3 , SS, ASME VIII, 150 psi, nonregenerative, with resin
                                                      FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
2. BUILDING ASSIGNMENT 11 5.2 16.2 13 x 13 x 16 @ $6/ft 3 (shielded area)
      Description of Augment       2-com Reverse Osmosis (Sheet 1)
3. ASSOCIATED PIPING SYSTEMS 20 20.0 40.0 6" piping
                                                            DIRECT COST (1975 $1000)
4. INSTRUMENTATION AND CONTROLS 4 6.0 10.0 allowance  
                                                                                                              BASIS FOR
5. ELECTRICAL SERVICE   neg 
                TTIFM                            LABOR            FOUlPMENTIMATFRIALS        TOTAL          COST ESTIMATF
6. SPARE PARTS - 2.0 2.0 miscellaneous supplies  SUBTOTAL 40 93.2 133.2 
  1. PROCESS EQUIPIENT                              6.0                  60.0                   66.0 skid mounted w/500-gal SS
7. CONTINGENCY 4 9.0 13.0
                                                                                                        feed tank, ASME VIII
8. TOTAL DIRECT COSTS 44 102.2 146.2 
  2. BUILDING ASSIGNMENT                           19.2                   9.6                    28.8  12' x 25' x 16' @ $6/ft 3
  3. ASSOCIATED PIPING SYSTEMS                     3.0                  2.0                     5.0 allowance
0
  4. INSTRUMENTATION AND CONTROLS                                                                     in item I
  5.  ELECTRICAL SERVICE                            7.0                  13.0                   20.0 allowance
   6. SPARE PARTS                                                         6.0                     6.0
            SUBTOTAL                               35.2                 90.6                  125.8
  7. CONTINGENCY                                   3.0                  9.0                   12.0   10%
  8. TOTAL DIRECT COSTS                           38.2                 99.6                  137.8


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 AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
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
                                                  SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
2. MAINTENANCE MATERIAL AND  
        Description of Augment     Reverse Osmosis - Detergent Wastes COST (1975 $1000)
LABOR   5.0 allowance
                  ITEM                         LABOR         OTHER         TOTAL               BASIS FOR COST ESTIMATE
3. CONSUMABLES, CHEMICALS, AND  
    1. OPERATING LABOR, SUPERVISION,
SUPPLIES   9.0 1 change per year @ 120 ft
        AND OVERHEAD                                                             3.1      160.000 gpy, 1300 hrs/yr @ 20% attendance
3 @ $75/ft 3 (one vessel change per year, regardless of size)
    2. MAINTENANCE MATERIAL AND                                                 8.8      4% less bldg + 24 module with 3-yr life LABOR                                                                               @ $600 each
4. UTILITIES AND SERVICES     Waste Disposal   2.4 120 ft
    3. CONSUMABLES, CHEMICALS. AND
3/yr @ $20/ft
        SUPPLIES                                                                 neg No
3 disposal cost Water     Steam     Electricity     Building Services     Other    
    4. UTILITIES AND SERVICES
5. TOTAL O AND M ANNUAL COST   19.7 
          Waste Disposal                                                         4.3       100:1 vol reduction @ $20/ft 3 disposal cost Water Steam Electricity                                                             neg Building Services Other
    5. TOTAL 0 AND MANNUAL COST                                                 16.2
(                                                              r                                                                  C


Appendix B to RG 1.110, Page B-55 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
1)
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
                                        TOTAL DIRECT (Sheet  COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
2. MAINTENANCE MATERIAL AND
                                                          FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
LABOR   5.0 allowance
                                        10tOOO-GallonTapk Description of Augment       1O,000-Gallon Tank__(Sheet 1)
3. CONSUMABLES, CHEMICALS, AND
                                                                  DIRECT COST (1975 $1000)
SUPPLIES  2.3 30 ft
                                                                          !0IJ!P?4fNT/MATERIALS                      BASIS FOR
3/yr @ $75/ft
                ?tTrM                                I AROR                                          TOTAL          COST ESTIMATE
3 4. UTILITIES AND SERVICES      Waste Disposal  0.6 30 ft3/yr @ $20/ft
                T -
3 disposal cost  Water      Steam      Electricity      Building Services      Other   
                                                          3                      28                    31   SS, ASME VIII, atmospheric
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
===1. PROCESS EQUIPMENT===
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
                                                                                                              service, 200°F
6 gpy, 30 min/shift
    BUILDING ASSIGNMENT                                30                         15                    45   15' x 20' x 25' @ $6/ft3
2. MAINTENANCE MATERIAL AND
   2.
LABOR   5.0 allowance
3. CONSUMABLES, CHEMICALS, AND
SUPPLIES  64.5 860 ft
3 resin @ $75/ft
3 4. UTILITIES AND SERVICES      Waste Disposal   17.2 860 ft
3 @ $20/ft 3 disposal cost  Water      Steam      Electricity      Building Services      Other   
5. TOTAL O AND M ANNUAL COST  93.2 


Appendix B to RG 1.110, Page B-57 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
(shielded area)
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
   3. ASSOCIATED PIPING SYSTEMS                              2                        1                    3   10% of item 1 C
2. MAINTENANCE MATERIAL AND  
w 4. INSTRUMENTATION AND CONTROLS                          4                        6                    10  allowance
LABOR   5.0 allowance
   5. ELECTRICAL SERVICE                                                                                  neg
3. CONSUMABLES, CHEMICALS, AND
  6. SPARE PARTS                                                                                        neg SUBTOTAL                                      39                        s0                    89
SUPPLIES   12.0 160 ft
   7. CONTINGENCY                                            4                         5                    9   10%
3/yr @ $75/ft
  8. TOTAL DIRECT COSTS                                    43                      55                    98
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
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREAThENT
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 NUCLEAR REACTORS
6 gpy 2. MAINTENANCE MATERIAL AND
    Description of Augment   10000-Gallon Tank (Sheet 2)
LABOR  5.0 allowance
                                                              COST (1975 $1000)
3. CONSUMABLES, CHEMICALS, AND
              ITEM                         LABOR         OTHER           TOTAL             RA~l  flD rfl*T r*TUATr
SUPPLIES  64.5 860 ft
1. OPERATING LABOR, SUPERVISION.
3 resin @ 75/ft
3 4. UTILITIES AND SERVICES      Waste Disposal  17.2 860 ft
3/yr @ $20/ft
3 disposal cost  Water      Steam      Electricity      Building Services      Other   
5. TOTAL O AND M ANNUAL COST  99.8 


Appendix B to RG 1.110, Page B-59 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
AND OVERHEAD                                                              1.1       5 min/shift - log level readings
TER-COOLED NUCLEAR REACTORS Description of Augment Demineralizer - PWR Steam Generator Blowdown (Sheet 10) DIRECT COST (1975 $1,000)  ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD  3.3 15 min/shift  
2. MAINTENANCE MATERIAL AND
2. MAINTENANCE MATERIAL AND  
    LABOR                                                                     1.6      1/2% of equipment
LABOR   5.0 allowance
3. CONSUMABLES. CHEMICALS, AND                                             neg SUPPLIES
3. CONSUMABLES, CHEMICALS, AND  
4. UTILITIES AND SERVICES
SUPPLIES   16.9 225 ft
      Waste Disposal Water Steam                                                                 neg Electricity Building Services Other
3 resin/yr @ $75/ft
5. TOTAL 0 AND N ANNUAL COST                                               2.7
3 4. UTILITIES AND SERVICES     Waste Disposal   4.5 225 ft
                                                                                                                        (
3/yr @ $20/ft
3 disposal cost  Water     Steam     Electricity     Building Services     Other    
5. TOTAL O AND M ANNUAL COST   29.7


Appendix B to RG 1.110, Page B-60 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS Description of Augment 20-gpm Cartridge Filter (Sheet 1) DIRECT COST (1975 $1,000)  ITEM LABOR
REFERENCES TO APPENDIX B
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 2.0 5.0 7.0 SS, ASME VIII, 150 psi
                                                                                  NUS-531,
2. BUILDING ASSIGNMENT 5.6 3.0 8.6 16 x 12 x 20 @ $6/ft 3  (shielded area)
1. "Guide for Economic Evaluation of Nuclear Reactor Plant Oesigns," USAEC Report NUS Corporation, January 1969.
3. ASSOCIATED PIPING SYSTEMS 1.5 1.0 2.5 allowance
4. INSTRUMENTATION AND CONTROLS 0.6 2.4 3.0 allowance
5. ELECTRICAL SERVICE  neg 
6. SPARE PARTS - 0.5 0.5  SUBTOTAL 9.7 11.9 21.6 
7. CONTINGENCY 1.0 1.0 2.0 10%
8. TOTAL DIRECT COSTS 10.7 12.9 23.6 


Appendix B to RG 1.110, Page B-61 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
2. "Wage Rates for Key Construction Trades," Engineering News Record, pp. 36-37, January 2, 1975.
TER-COOLED NUCLEAR REACTORS Description of Augment Cartridge Filter (Sheet 2) DIRECT COST (1975 $1,000)  ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD  4.5 10 changes @ 10 man-hrs/change @ $12/hr + 15 min/shift
2. MAINTENANCE MATERIAL AND
LABOR  1.0 allowance
3. CONSUMABLES, CHEMICALS, AND
SUPPLIES  1.0 10 changes/yr @ $100/change
4. UTILITIES AND SERVICES      Waste Disposal  1.5 10 drums/yr @ $20/ft
3  Water      Steam      Electricity      Building Services      Other   
5. TOTAL O AND M ANNUAL COST  8.0 


Appendix B to RG 1.110, Page B-62 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS Description of Augment 100-gpm Precoat Filter (Sheet 1) DIRECT COST (1975 $1,000)  ITEM LABOR
- 2000,"
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 10 65.0 75 automated system 1 gpm/ft
3. "Projections of Labor Requirements for Electric Power Plants Construction, 1974 USAEC Report WASH-1334, Washington, D.C., August 1974.
2 , ASME VIII
2. BUILDING ASSIGNMENT 18 9.0 27 15 x 15 x 20 @ $6/ft 3  (shielded area)
3. ASSOCIATED PIPING SYSTEMS 16 9.0 25 35% of equipment cost
4. INSTRUMENTATION AND CONTROLS    in item 1
5. ELECTRICAL SERVICE 7 13.0 20 allowance
6. SPARE PARTS - 2.0 2 2% of item 1  SUBTOTAL 51 98.0 149 
7. CONTINGENCY 5 10.0 15 10%
8. TOTAL DIRECT COSTS 56 108.0 164 


Appendix B to RG 1.110, Page B-63 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS Description of Augment 400-gpm Precoat Filter (Sheet 2) DIRECT COST (1975 $1,000)  ITEM LABOR
1.110-85
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 35 135.0 170 automated system; 1 gpm/ft
2 ASME VIII
2. BUILDING ASSIGNMENT 24 12.0 36 15 x 20 x 20 @ $6/ft 3  (shielded area)
3. ASSOCIATED PIPING SYSTEMS 31 16.0 47 35% of equipment cost
4. INSTRUMENTATION AND CONTROLS - - - item 1
5. ELECTRICAL SERVICE 12 18.0 30 allowance
6. SPARE PARTS - 3.0 3  SUBTOTAL 102 184.0 286 
7. CONTINGENCY 10 18.0 28 10%
8. TOTAL DIRECT COSTS 112 202.0 314 


Appendix B to RG 1.110, Page B-64 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
APPENDIX C
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
                            DATA NEEDED FOR RADIIASTE TREATMENT SYSTEM
6 gpy, 30 min/shift
                              COST-BENEFIT ANALYSIS FOR LIGHT-WATER
2. MAINTENANCE MATERIAL AND
                                      COOLED NUCLEAR REACTORS
LABOR  10.0 allowance
      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:
3. CONSUMABLES, CHEMICALS, AND
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.
SUPPLIES  6.0 10 lbs precoat @ 10¢/lb per 1,000 gal processed
4. UTILITIES AND SERVICES      Waste Disposal  40.0 1 ft
3/sludge per 1,000 gal processed @ $30/ft
3 disposal cost Water      Steam      Electricity      Building Services      Other   
5. TOTAL O AND M ANNUAL COST  62.6 


Appendix B to RG 1.110, Page B-65 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS Description of Augment 2-gpm Reverse Osmosis (Sheet 1) DIRECT COST (1975 $1,000)  ITEM LABOR
2.   The cost of borrowed money used in the cost analysis and the method of arriving at this cost.
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 6.0 60.0 66.0 skid mounted w/500-gal SS feed tank, ASME VIII
2. BUILDING ASSIGNMENT 19.2 9.6 28.8 12 x 25 x 16 @ $6/ft 3 3. ASSOCIATED PIPING SYSTEMS 3.0 2.0 5.0 allowance
4. INSTRUMENTATION AND CONTROLS  - in item 1
5. ELECTRICAL SERVICE 7.0 13.0 20.0 allowance
6. SPARE PARTS - 6.0 6.0  SUBTOTAL 35.2 90.6 125.8 
7. CONTINGENCY 3.0 9.0 12.0 10%
8. TOTAL DIRECT COSTS 38.2 99.6 137.8 


Appendix B to RG 1.110, Page B-66 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
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:
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
      a.  Decontamination factors assigned to each augment and fraction of "on-line" time assumed, i.e., hours per year used.
2. MAINTENANCE MATERIAL AND
LABOR   8.8 4% less bldg + 24 module with 3-yr life @ $600 each
3. CONSUMABLES, CHEMICALS, AND
SUPPLIES  neg  4. UTILITIES AND SERVICES      Waste Disposal  4.3 100:1 vol reduction @ $20/ft
3 disposal cost  Water      Steam      Electricity  neg  Building Services      Other   
5. TOTAL O AND M ANNUAL COST  16.2 


Appendix B to RG 1.110, Page B-67 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS Description of Augment 10,000-Gallon Tank (Sheet 1) DIRECT COST (1975 $1,000)  ITEM LABOR
b.  Parameters and method used to determine the Indirect Cost Factor and the Capital Recovery Factor.
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT 3 28 31 SS, ASME VIII, atmospheric service, 200°F
2. BUILDING ASSIGNMENT 30 15 45 15 x 20 x 25 @ $6/ft 3  (shielded area)
3. ASSOCIATED PIPING SYSTEMS 2 1 3 10% of item 1
4. INSTRUMENTATION AND CONTROLS 4 6 10 allowance
5. ELECTRICAL SERVICE   neg 
6. SPARE PARTS - - neg  SUBTOTAL 39 50 89 
7. CONTINGENCY 4 5 9 10%
8. TOTAL DIRECT COSTS 43 55 98 


Appendix B to RG 1.110, Page B-68 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
1.110-87
TER-COOLED NUCLEAR REACTORS Description of Augment 10,000-Gallon Tank (Sheet 2) DIRECT COST (1975 $1,000)  ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD  1.1 5 min/shift - log level readings
2. MAINTENANCE MATERIAL AND
LABOR  1.6 1/2% of equipment
3. CONSUMABLES, CHEMICALS, AND
SUPPLIES  neg  4. UTILITIES AND SERVICES      Waste Disposal      Water      Steam  neg  Electricity      Building Services      Other   
5. TOTAL O AND M ANNUAL COST  2.7 


Appendix B to RG 1.110, Page B-69 REFERENCES TO APPENDIX B
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE'TREATMENT-SYSTEH
1. U.S. Atomic Energy Commission (USAEC), "Guide for Economic Evaluation of Nuclear Reactor Plant Designs," USAEC Report NUS-531, NUS Corporation, January 1969.
                                                                          FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
    Description of Augment DIRECT COST (1975 $1000)
                                                                                                                                                                  BASIS FOR
                    i Tru                                            1 AflfD
                                                                                                FflIIIPMFNT/MATFRlALS                    TOTAL                  COST ESTIMATE
                                                                    i aunD                    EnUTPMENTIMATERIALS


2. "Wage Rates for Key Construction Trades,"
===1. PROCESS EQUIPMENT===
Engineering News Record, pp. 36-37, January 2, 1975.
                                                              t                  I                                                    1              I


3. USAEC, "Projections of Labor Requirements for Electric Power Plants Construction,  1974-2000," USAEC Report WASH-1334, Washington, DC, August 1974.
===2. BUILDING ASSIGNMENT===
                                                              I                  I                                                    I              I
0 3. ASSOCIATED PIPING SYSTEMS
                                                              I                  I                                                    I              I                                          --
  4. INSTRUMENTATION AND CONTROLS
                                                              I                  I                                                    I              I
  S. ELECTRICAL SERVICE
                                                              I                  I                                                    I              I


Appendix C to RG 1.110, Page C-1 APPENDIX C
===6. SPARE PARTS===
  DATA NEEDED FOR RADWASTE TREATMENT SYSTEM  COST-BENEFIT ANALYSIS FOR LIGHT-WATER-COOLED 
                  ______________________I                                      i                                                    mI
NUCLEAR REACTORS
            SUBTOTAL
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           -I                                                        I              I
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.
===7. CONTINGENCY===
                                                              I                  I                                                    I


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:
===8. TOTAL DIRECT COSTS===
    ________________________________________________________  ________________ I __________________________________________________  _____________ _______________________________________________
(                                                                                          C                                                                                                  C


a. Decontamination factors assigned to each augment and fraction of "on-line" time assumed (i.e., hours per year used).  
K
b. Parameters and method used to determine th e Indirect Cost Factor and the Capital Recovery Factor.
  0
"I
U
2                                        ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
2
-4                                                    SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
U
2
2 Description of Augment C,
a
  9 COST (1975 $1000)
  9 I TIFM                          LABOR          OTHER          TOTAL              BASIS FOR COST ESTIMATE
'a                  ITEM
w
  -J
  04
      1. OPERATING LABOR, SUPERVISION,
          AND OVERHEAD
  0.j
  'a
"4 a.


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
0
EQUIPMENT/ MATERIALS TOTAL BASIS FOR COST ESTIMATE 1. PROCESS EQUIPMENT   
  "4
2. BUILDING ASSIGNMENT   
      2. MAINTENANCE MATERIAL AND
3. ASSOCIATED PIPING SYSTEMS   
          LABOR
4. INSTRUMENTATION AND CONTROLS   
      U3.
5. ELECTRICAL SERVICE   
6. SPARE PARTS      SUBTOTAL   


===7. CONTINGENCY    ===
4.
8. TOTAL DIRECT COSTS   


Appendix C to RG-1.110, Page C-3 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WA
CONSUMABLES,
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
          SUPPLIES
LABOR    3. CONSUMABLES, CHEMICALS, AND  
                            CHEMICALS, AND
SUPPLIES    4. UTILITIES AND SERVICES     Waste Disposal     Water     Steam     Electricity     Building Services     Other    
          UTILITIES AND SERVICES
5. TOTAL O AND M ANNUAL COST    
              Waste Disposal Water Steam Electricity Building Services Other
*U.S. Government Printing Office:  1987-202-292:60255}}
        5. TOTAL 0 AND M ANNUAL COST}}


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

Latest revision as of 10:13, 28 March 2020

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


U.S. NUCLEAR REGULATORY COMMISSION March 1976 REGULATORY GUIDE

OFFICE OF STANDARDS DEVELOPMENT

4 REGULATORY GUIDE 1.110

COST-BENEFIT ANALYSIS FOR RADWASTE S

LIGHT-WATER-COOLED NUCLEAR PDWE& CRS'

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

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

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

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

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

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

TABLE OF CONTENTS

Page

A. INTRODUCTION

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

B. DISCUSSION

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

C. REGULATORY POSITION

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

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

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

1.110-3

LIST OF TABLES

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

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

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

1.110-4

A. INTRODUCTION

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

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

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

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

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

B. DISCUSSION

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

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

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

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

staff are given in Appendix B.

1-110-5

C. REGULATORY POSITION

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

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

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

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

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

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

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

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

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

0. IMPLEMENTATION

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

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

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

1.110-6

APPENDIX A

PROCEDURES FOR PERFORMING COST-BENEFIT ANALYSES

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

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

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

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

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

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

a. The Total Direct Cost (TOC):

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

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

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

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

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

TCC - TDC x ICF

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

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

AFC = TCC x CRF

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

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

TAC

  • AFC + AOC + AMC

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

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

1.110-7

TABLE A-1 DIRECT COSTS - GASEOUS RADWASTE AUGMENTS

Direct- Costs

(1975 $1000)

Equipment/Material Labor Total BWR Offgas Recombiner 553 255 808

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

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

and Less Than-24" 183 55 238

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

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

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

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

Turbine Bldg. Chilled Water HVAC System 614 374 988

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

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

1.110-8

TABLE A-1 (Continued)

DIRECT COSTS - LIQUID RADWASTE AUGMENTS

Direct Costs

(1975 $1000)

Total Equipment/Material Labor

386 201 587

15-gpm Evaporator

540 223 763

30-gpm Evaporator

655 233 888

50-gpm Evaporator

36 24 60

Evaporator Distillate Demineralizer

43 29 50

50-gpm Demineralizer

64 31 95

100-gpm Demineralizer

94 35 129

200-gpm Deminieralizer

102 44 146

400-gpm Demineralizer

108 56 164

100-gpm Precoat Filter

202 112 314

400-gpw Precoat Filter

13 11 24

20-gpm Cartridge Filter

100 38 138

2-gpm Reverse Osmosis

55 43 98

10,000-gal Tank

1.110-9

TABLE A-2 ANNUAL OPERATING COSTST - GASEOUS RADWASTE AUGMENTS

Total Operating Cost (1975 $lOOO/yr)

B r m m BWR Offgas Recoatbiner 3

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

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

15,000-cfm HEPA Filtration System 6

1,000-cfm Charcoal/HEPA Filtration System 2

15,000-cfm Charcoal/HEPA Filtration System 7

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

Turbine Bldg. Chilled Water HVAC System 49

3

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

Evaporation - PWR Dirty Waste 50

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

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

1.110-10

TABLE A-2 (Continued)

ANNUAL OPERATING COSTS - LIQUID RADWASTE AUGMENTS

Total Operating Cost (1975 $1000/yr)

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

18 Demineralization - PWR Dirty Waste

95 Demineralization - PWR Turbine Bld

g. Drains

25 Desmineralization - PWR Steam Generator Blowdown

53 Precoat Filter - BWR Dirty Waste Cartridge Filter 7

7 Reverse Osmosis - Detergent Waste

1

10,000-gal Tank

1.110-11

TABLE A-3 ANNUAL MAINTENANCE COSTS- GASEOUS RADWASTE AUGMENTS

Total Maintenance Cost (1975 $1O00/Yr)

BWR Offgas Recombiner 20

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

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

15,000-cfm HEPA Filtration System 2

1,000-cfm Charcoal/HEPA Filtration System 0.6

15,O00-cfm Charcoal/HEPA Filtration System 9

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

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

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

15-gpm Evaporator 30

30-gpm Evaporator 30

50-gpm Evaporator 30

Evaporator Distillate Demineralizer 2

50-gpm Demineral izer 5 lO0-gpmi Demineralizer 5

200-gpm Demineral izer S

100-gpm Precoat Filter 10

400-gpm Precoat Filter 10

20-gpm Cartridge Filter 1

2-gpm Reverse Osmosis g

10.000-gal Tank 2

1.110-12

TABLE A-4 LABOR COST CORRECTION FACTORS

FPC

Geographic Labor Cost Correction Region Factor I 1.6

1.5

1II

1.0

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

See Figure A-1.

1.110-13

TABLE A-5 INDIRECT COST FACTORS

Type Radwaste System Indirect Cost Factor

"1. Single unit site, unitized radwaste system 1.75

2. Multi-unit site, shared radwaste system 1.75

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

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

I..

1.110-14

TABLE A-6 CAPITAL RECOVERY FACTORS

Cost of Honey Capital Recovery Factor

(1 per year, i)

5 0.0651

0.0726

6

0.0806

7

0.0888

8

0.0973

9

0.1061

10

0.1150

11

0.1241

12

0.1334

13

0.1428

14

0.1523

15

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

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

1.110-15

LEGEND

¶Im REGIONAL GROUPING OF POWER SUPPLY AREAS

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

( C C

APPENDIX B

BASES FOR PARAMETERS USED IN PERFORMING COST-BENEFIT ANALYSIS

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

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

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

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

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

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

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

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

1.110-17

TABLE 8-1 K..

INDIRECT COSTS

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

Other owner s costs 10 S

Interest during construction 3S 35 Total 75 SS

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

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

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

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

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

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

I(1 #)o (I + ~

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

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

years was used.

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

1.110-18

LIST OF APPENDIX B COST ESTIMATE SHEETS

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

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

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

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

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

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

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

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

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

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

1.110-19

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

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

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

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

I___MIXL_ 1 IVIML COST ESTIMATE

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

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

a ASSOCIATED PIPING SYSTEMS

3. 18 12 30 augment piping connections only O

4. INSTRUM4ENTATION AND CONTROLS 24 96 120 allowance

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

6.

items 1 & 4 above SUBTOTAL 232 503 735

7. CONTINGENCY 23 50 73 10%

8. TOTAL DIRECT COSTS 2S5 553 808

(

r

A K I

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR-LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment BWR Offgas Recombiner (Sheet 2)

COST (1975 $1000)

ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE

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

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

3. CONSUMBLES, CHEMICALS, AND - initem 2

,01 C2 SUPPLIES

4. UTILITIES AND SERVICES

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

5. TOTAL 0 AND M ANNUAL COST 23.3

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

DIRECT COST (1975 $1000)

BASIS FOR

!TFM LABOR EOUIPMENTIMATERIALS TOTAL COST

- -

ESTIMATF

-- - - -

3

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

4. 4. 4. 4

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

3. ASSOCIATED PIPING SYSTES - in item I

a

4. INSTRUKENTATION AND CONTROLS neg S. ELECTRICAL SERVICE neg

6. SPARE PARTS none existing SUBTOTAL 13 48.5 61.5

7. CONTINGENCY 1 5.0 6.0 10%

8. TOTAL DIRECT COSTS 14 53.5 67.5

. . .. . . . . r r r

K K

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

COST (1975 $1000)

I TFM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE

1. OPERATING LABOR. SUPERVISION. neg AND OVERHEAD

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

3. CONSUMABLES. CHEMICALS, AND

SUPPLIES neg lifetime use of charcoal assumed I..

4. UTILITIES AND SERVICES

Waste Disposal Water Steam neg Electricity Building Services Other

5. TOTAL 0 AND M ANNUAL COST neg

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

DIRECT COST (1975 $1000)

I TEN I ARflR T*TAI

BASIS FOR

1% IL COTETMT

1. PROCESS EQUIPMENT 25 75 100 redundant dryer vessels with

1 regeneration skid

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

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

8i

4. INSTRUMENTATION AND CONTROLS 12 48 60 allowance

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

6. SPARE PARTS 3 3 SUBTOTAL 160 198 358

7. CONTINGENCY 16 20 36 10%

8. TOTAL DIRECT COSTS 176 218 394

( r r

K K K

ANNUAL CPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment Desiccant Dryer (Sheet 2)

COST (1975 $1000)

Q*Pim I Ahfl flTIIP TflTAI BASIS FOR COST ESTIMATE

itri,,,

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

3.3 15 min/shift

1. OPERATING LABOR, SUPERVISION,

AND OVERHEAD

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

LABOR

3 CONSUMABLES, CHEMICALS, AND neg C SUPPLIES

U'

4. UTILITIES AND SERVICES

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

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREAThENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment Charcoal Vault Refrigeration (Sheet 1)

DIRECT COST (1975 $1000)

BASIS FOR

ITEM TftTAI

LAORFlIITDUdCNT/UATCDTA1

10AM C YffASIfC et.V

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

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

0 3. ASSOCIATED PIPING SYSTEMS In item 1 N

14 Ch

4. INSTRUMENTATION AND CONTROLS 4 6 10 allowance

5. ELECTRICAL SERVICE 12 18 30 allowance

6. SPARE PARTS 3 3 SUBTOTAL 35 105 140

7. CONTINGENCY 3 11 14 10%

8. TOTAL DIRECT COSTS 38 116 154

(

K K K

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COO.EO NUCLEAR REACTORS

Description of Augment Charcoal Vault Refriceration (Sheet 2)

COST (1975 $1000)

'TIn' rTeR TOTAL FOR COST !T1MATE

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

2. MAINTENANCE MATERIAL AND

LABOR 3.7 51 of equlpemt

3. CONSUMABLES, CHEMICALS, AND in Item 2 SUPPLIES

4. UTILITIES AND SERVICES

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

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

i n *

DIRECT COST (1975 $1000)

ITE4 I A*Q

BASIS FOR

LABOR__ ~ LrILumLAL IUIAL COST ESTIMATE

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

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

@ $3/ft 3 (nonshielded area)

Nm

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

4. INSTRUMENTATION AND CONTROLS

in item 1

5. ELECTRICAL SERVICE 1 1.5 2.5

6. SPARE PARTS 0.5 0.5 SUBTOTAL 7.4 36.7 44.1

7. CONTINGENCY .7 3.7 4.4 10%

8. TOTAL DIRECT COSTS 8.1 40.4 48.5

( (

K K K

ANNUAL OPERATING ANrMAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

COST (1975 $1000)

'ueD TfllhI S...,iT*

RAmie FflQ tOI[IT F¢;TTMATF

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

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

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

'.4

  • 0

4. UTILITIES AND SERVICES

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

5. TOTAL 0 AND M ANNUAL COST 1.4

_______________________ I _________ ________ _______________________________

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

DIRECT COST (1975 $1000)

FM FOIITDMFNTIMATPRTAI STTTflTAI BASIS FOR

  • FnCT VCTttMATO

I ARAR

ITEMP

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

$25K/H.P. turbine glands

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

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

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

5. ELECTRICAL SERVICE nag

6. SPARE PARTS 5 5 SUBTOTAL 74 195 269

7. CONTINGENCY 7 20 27 10%

8. TOTAL DIRECT COSTS 81 215 296 r r C

K K

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

COST (1975 $1000)

1TR4 LABOR OTHER TOTAL BASIS FOR COST ESTIMATE

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

2. MAINTENANCE MATERIAL AND 4.0 40 man-days LABOR

3. CONSUMABLES, CHEMICALS, AND

SUPPLIES

9'

4. UTILITIES AND SERVICES

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

5. TOTAL 0 AND M ANNUAL COST 28.3

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

DIRECT COST (1975 $1000)

ITEM I AMII n:*.:TDAACLIMATDTai BASIS FOR

TnTAI

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

2. BUILDING ASSIGNMENT neg install in existing space

3. ASSOCIATED PIPING SYSTEMS - in item 1

0

i%1J

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

6. SPARE PARTS 5 SUBTOTAL 100 125 225

7. CONTINGENCY 10 12 22 10%

8. TOTAL DIRECT COSTS 110 137 247

( r

K -\

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM1 FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

COST (1975 $1000)

TT!M LABOR OTHER TOTAL BASIS FOR COST ESTIMATE

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

2. MAINTENANCE MATERIAL AND 4.0 40 man-days LABOR

3. CONSUMABLES, CHEMICALS, AND neg SUPPLIES

w U,

4. UTILITIES hND SERVICES

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

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

DIRECT COST (1975 $1000)

BASIS FOR

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

COS ESTIMATE

TOTAL

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

2. BUILDING ASSIGNMENT - - neg

-* 3. ASSOCIATED PIPING SYSTEMS 40 20 60

.

w

.h 4.6.

INSTRUMENTATION AND CONTROLS 10 20 30 allowance

5. ELECTRICAL SERVICE - none

7.e

6. SPARE PARTS - 6 6 SUBTOTAL 50 166 216

7. CONTINGENCY 5 17 22 10%

8. TOTAL DIRECT COSTS 55 183 238 I (

K A K

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

COST (1975 $1000)

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

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

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

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

-a U'

4. UTILITIES AND SERVICES

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

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

DIRECT COST (1975 $1000)

BASIS FOR

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

ERq~

r. flTl II Anna .r..

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

i-* ,

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

2.

(nonshielded area)

3. ASSOCIATED PIPING SYSTEMS 3 2.0 5.0

,o L.

a'

4. INSTRUMENTATION AND CONTROLS in item 1

5. ELECTRICAL SERVICE base

6. SPARE PARTS 0.5 0.5 SUBTOTAL 15 47.0 62.0

7. CONTINGENCY 1 5.0 6.0 10%

8. TOTAL DIRECT COSTS 16 52.0 68.0

( ( (

K T K !

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASrE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

DIRECT COST (1975 $1000)

BASIS FOR

COST ESTIMATE

lI TDMCWNT IMATrOAIC

I AflI TflTAL

ITEM !L___ f ______________

5 40.0 45.0 skid mounted filter housing

1. PROCESS EQUIPMENT w/o fans

3

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

2. BUILDING ASSIGNMENT 4.6 (nonshielded area)

3. 3 2.0 5.0

ASSOCIATED PIPING SYSTEMS

-I

4. in item 1 INSTRUMENTATION AND CONTROLS

5. base ELECTRICAL SERVICE

6. 0 0.5 0.5 SPARE PARTS

SUBTOTAL 12.6 44.8 57.4

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

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

COST (1975 $1000)

ITEM LABOR OTI4FR TflTAI RACTC Frn rncT FCTIMATC

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

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

CONSUMABLES, CHEMICALS, AND

I

3. in items 2 and 4 SUPPLIES

4. UTILITIES AND SERVICES

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

5. TOTAL 0 AND M ANNUAL COST 7.8 I_ (

K K

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

DIRECT COST (1975 $1000)

BASIS FOR

I TEM LABOR EOUIPMENT/MATERIALS TOTAL COST ESTIMATE

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

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

2.

(nonshielded area)

3. ASSOCIATED PIPING SYSTEMS 1.3 .7 2.0

0

4. INSTRUMENTATION AND CONTROLS in item 1

5. ELECTRICAL SERVICE 1.5 1.0 2.5

6. SPARE PARTS 0.5 0.5 SUBTOTAL 8.6 26.2 34.8

7. CONTINGENCY 1.0 2.0 3.0 10%

8. TOTAL DIRECT COSTS 9.6 28.2 37.8

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

COST (1975 $1000)

ITEM LABOR OTHER TOTAL BASIS FOR COST £STII4ATF

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

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

1 charcoal @ $900 each every 2 yrs'

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

0

UTILITIES AND SERVICES

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

5. TOTAL 0 AND M ANNUAL COST 2.6

____________________________ ____________ I I

  • ( --

__ (

K K

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

DIRECT COST (1975 $1000)

BASIS FOR

TTVM LABOR EQUIPMENT/MATERIALS TOTAL COST ESTIMATE

ITE

LABO.....

COST ESTIMATE

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

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

2.

(nonshielded area)

3. ASSOCIATED PIPING SYSTEMS 3 2 5 a

4. INSTRUMENTATION AND CONTROLS - In Item 1

5. ELECTRICAL SERVICE 3 2 5 allowance

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

7. CONTINGENCY 3 9 12 10%

8. TOTAL DIRECT COSTS 31 97 128

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

DIRECT COST (1975 $1000)

I TEM CN "I lDMrLT ATEDIlA1 C BASIS FOR

I fuND T*TAi ITEM I_____

ARAL?~urIIn~LJIUL x flMrnR UI

t. IWUTflYAI

1.3

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

@ $5/cfm, 30 kw htr

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

2.

(nonshielded area)

3. ASSOCIATED PIPING SYSTEMS 3.0 2.0 5.0

0

.rg

4. INSTRUMENTATION AND CONTROLS in item 1

5. ELECTRICAL SERVICE 3.0 2.0 5.0 allowance

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

7. CONTINGENCY 2.0 9.0 11.0 10%

8. TOTAL DIRECT COSTS 25.7 92.8 118.5

( r (

K K

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREAThENT

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

COST (1975 $1000)

ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE

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

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

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

0

4. UTILITIES AND SERVICES

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

Building Services 0.018.S/kw-hr Other

5. TOTAL 0 AND M ANNUAL COST 15.6

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

DIRECT COST (1975 $1000)

BASIS FOR

I ITU i ARng~

FoII PI4FNTII4ATFRIALS TOTAL COST ESTIMATE

-¶ a 1n FnrMN/AEIL

15 117.0 132.0 pref1lter/4" charcoal/HEPA

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

2. (nonshielded area)

3. ASOCIATED PIPING SYSTEMS 5 3.0 8.0 base a

4. INSTRUMENTATION AND CONTROLS - in item I

5. ELECTRICAL SERVICE 6 4.0 10.0 allowance

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

7. CONTINGENCY 5 14.0 19.0 10%

8. TOTAL DIRECT COSTS 51 156.6 207.6

( C

y K

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

DIRECT COST (1975 $1000)

!OtITPHt¶!rT/ATrR TALS BASIS FOR

t*nlT F*TTMATF

ITEM LAROR TflTA[

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

@ $4/cfm, 60kw htr

@ $200/kw

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

3. ASSOCIATED PIPING SYSTEMS 3.0 5.0 8.0 base me

4. INSTRUMENTATION AND CONTROLS in item 1

5. ELECTRICAL SERVICE 6.0 4.0 10.0 allowance

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

7. CONTINGENCY 4.0 14.0 18.0 l0

8. TOTAL DIRECT COSTS 41.4 151.8 193.2

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

COST (1975 $1000)

ITEM LABOR OTHER TOTAL BASIS FOR £OST FSTTMATF

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

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

LABOR charcoal filters @ $900 each every 2 yrs

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

4. UTILITIES AND SERVICES

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

Building Services 0.018 S/ku-hr Other

5. TOTAL 0 AND M ANNUAL COST 27.4

- :- t--.-J"

ý:r __ C

K K

11 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

DIRECT COST (1975 $1000)

EOUJIPMFNTIMATFRIALS BASIS FOR

ITEM LABOR TflTAI rnCT CTMATC

TnIMNIAEIL 1 nA

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

-t + I

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

0

3. ASSOCIATED PIPING SYSTEM; - in item 1

-J

4. INSTRUMENTATION AND CONTROLS - in item 1

5. ELECTRICAL SERVICE 40 so 90

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

7. CONTINGENCY 34 56 90 10l

8. TOTAL DIRECT COSTS 374 614 988

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTE14 FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

COST (1975 $1000)

ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE

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

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

.0

3. CONSUMABLES, CHEMICALS, AND - initem 2 SUPPLIES

0

4. UTILITIES AND SERVICES

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

K

I

K K

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT. SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

DIRECT COST (1975 $1000)

EOUIPMENT/MATERIALS BASIS FOR

I TFM LABOR TOTAL COST ESTIMATE

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

ASME VIII

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

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

TOTAL DIRECT COSTS 23.5 33 56.5

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

COST (1975 $1000)

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

AND OVERHEAD neg

2. MAINTENANCE MATERIAL AND

LABOR neg

3. CONSUMABLES, CHEMICALS, AND

0

SUPPLIES neg U'

0~e

4. UTILITIES AND SERVICES

Waste Disposal Water Steam neg Electricity Building Services Other

5. TOTAL 0 AND N ANNUAL COST neg

(

K K

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment PWR Hydrogen Recombiner (Sheet 1)

DIRECT COST (1975 $1000)

rflIITPMPINIMAT*RTAI

BASIS FOR

IT"M IARno TflTAI rnqT vtTTMATF

I l VT :fTI b V nA. I

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

single unit, ASME VIII

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

2.

(shielded area)

3. ASSOCIATED PIPING SYSTEMS 32.0 13.0 45.0 allowance a

Ue

4. INSTRUMENTATION AND CONTROLS 10.0 40.0 50.0 allowance

5. ELECTRICAL SERVICE 13.0 12.0 25.0 allowance

6. SPARE PARTS - 2.0 2.0

SUBTOTAL 133.8 381.4 515.2

7. CONTINGENCY 13.0 38.0 51.0 101

8. TOTAL DIRECT COSTS 146.8 419.4 566.2

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADtWASTE TREAThENT

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment PUR Hydrogen Recombiner (Sheet 2)

COST (1975 $1000)

ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE

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

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

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

SUPPLIES 7000 hrs Ca I

U'

4. UTILITIES AND SERVICES

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

K*

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

DIRECT COST (1975 $1000)

BASIS FOR

ITEM LABOR EOUIPMENT/MATERIALS TOTAL COST ESTIMATE

1*

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

3

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

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

4. INSTRUMENTATION AND CONTROLS 0.5 1.5 2.0 allowance

5. ELECTRICAL SERVICE 0.5 0.5 1.0 allowance

6. SPARE PARTS 1.0 1.0

SUBTOTAL 9.0 13.0 22.0

7. CONTINGENCY 1.0 1.0 2.0 1O0

8. TOTAL DIRECT COSTS 10.0 14.0 24.0

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

COST (1975 $1000)

ITEM LARAR flTIFD TnTAI DAete * * rP*eUA*

.....________________

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

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

2. MAINTENANCE MATERIAL AND 2.0 includes replacement filter LABOR

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

SUPPLIES

U'

4. UTILITIES AND SERViCES

Waste Disposal neg Water Steam Electricity Building Services Other

5. TOTAL 0 AND M ANNUAL COST 5.8 K

K K

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

DIRECT COST (1975 $1000)

BASIS FOR

ITEM LABOR EQUIPMENT/MATERIALS TOTAL COST ESTIMATE

I. PROCESS EQUIPMENT - no equipment required

2. BUILDING ASSIGNMENT neg install In existing space

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

2 valves U't ull

4. INSTRUMENTATION AND CONTROLS 4 6 10 allowance

5. ELECTRICAL SERVICE neg

6. SPARE PARTS neg SUBTOTAL 17,, 13 30

7. CONTINGENCY 2 1 3 10%

8. TOTAL DIRECT COSTS 19 14 33

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREAThENT

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

COST (1975 $1000)

ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE

1. OPERATING LABOR, SUPERVISION, 1 allowance AND OVERHEAD

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

3. CONSUHABLES, CHEMICALS, AND neg

.a SUPPLIES

U'

4. UTILITIES AND SERVICES

Waste Disposal Water neg Steam Electricity Building Services Other

5. TOTAL 0 AND H ANNUAL COST 2

( (

K

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment lSqpm Evaporator (Sheet 1)

DIRECT COST (1975 $1000)

BASIS FOR

ITI'N I AnRO T*TA!

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

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

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

4. INSTRUMENTATION AND CONTROLS 10 10 20 allowance

5. ELECTRICAL SERVICE 40 25 65 allowance

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

7. CONTINGENCY 18 35 53 10%

8. TOTAL DIRECT COSTS 201 386 587

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREAThENT'SYSTEM

FOR LIGHT-WdATER-COOLED NUCLEAR REACTORS

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

DIRECT COST (1975 $1000)

tTrW BASIS FOR

rncT rCY?UAYT

I AfPtflD rfIITDfMlrTIMATrDTAI TnTA,

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

1. PROCESS EQUIPMENT 30 350 380 ASME VIII

skid mounted, submerged,

'tube bundle, Incoloy in contact with process fluid t

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

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

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

4. INSTRUMENTATION AND CONTROLS 10 10 20 allowance

5. ELECTRICAL SERVICE 40 25 65 allowance

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

7. CONTINGENCY 20 49 69 1O0

8. TOTAL DIRECT COSTS 223 540 763 C C

K

'III

T

3)

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMErNT SYSTEM

(Sheet

50-gpmFOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

DIRECT COST (1975 $1000)

BASIS FOR

ITEM LABOR EOUIPMENT/MATERIALS TOTAL COST ESTIMATE

1. PROCESS EQUIPMENT 30 450 480 ASME VIII

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

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

3. ASSOCIATED PIPING SYSTEMS 35 35 70 allowance a

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

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

7. CONTINGENCY 21 60 81 10%

8. TOTAL- DIRECT COSTS 233 655 888

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

ITEM LABOR OT14ER TOTAL BASIS FOR LOST FSTIMATF

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

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

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

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

5. TOTAL 0 AND M ANNUAL COST 199 C C

K* K

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment Evaporator PWR Dirty Waste (Sheet 5)

COST (1975 $1000)

lTYM [AROR OTHER TOTAL BASIS FOR COST ESTTMATE

I. OPERATING LABOR, SUPERVISION,

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

2. MAINTENANCE MATERIAL AND

LABOR 30.0 7-1/2% of equipment cost

3. CONSUMABLES, CHEMICALS, AND - concentrate solidification chemicals

0'

SUPPLIES in item 4

4. UTILITIES AND SERVICES 3

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

5. TOTAL 0 AND MANNUAL COST 80.0

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment v

EvaDorator

- Condenser Polisher Chemical IaCto Ih +0A

COST (1975 $1000)

ITEM LAI*R NTH*D T*TAI

LABOR 0ATD AU .,* TC4TAI FRUK CS

LU ETIMATE

1. OPERATING LABOR, SUPERVISION,

AND OVERHEAD 6.0 650.000 gpy; 500 hr/yr labor

2. MAINTENANCE MATERIAL AND

LABOR 30.0 7-1/2% of equipment cost

3. CONSUMABLES, CHEMICALS. AND concentrate solidification chemicals

0 SUPPLIES In item 4

4. UTILITIES AND SERVICES

Waste Disposal

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

5. TOTAL 0 AND M ANNUAL COST 143.9

( C

K K

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

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

COST (1975. $1000)

TT!M LABOR OTHER TOTAL BASIS FOR COST ESTIMATE

I. OPERATING LABOR, SUPERVISION,

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

2. MAINTENANCE MATERIAL AND

LABOR 30.0 7-1/25 of equipment cost

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

LeD

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

5. TOTAL 0 AND MANNUAL COST 49.8

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment Evaporator Distillate Demineralizer (Sheet 1)

DIRECT COST (1975 $1000)

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

BASIS FOR

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

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

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

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

Ot

4. INSTRUMENTATION AND CONTROLS 2.0 3.0 5.0 remote conductivity readout

5. ELECTRICAL SERVICE neg

6. SPARE PARTS 1.0 1.0

SUBTOTAL 21.4 33.2 54.6

7. CONTINGENCY 2.0 3.0 5.0 10%

8. TOTAL DIRECT COSTS 23.4 36.2 59.6

( C (

)

K

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment Evaporator Distillate Demineralizer (Sheet 2)

COST (1975 $1000)

YtM I ARnlQ OTHER TOTAL BASIS FOR COST ESTIMATE

aI1II ____________

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

2. MAINTENANCE MATERIAL AND

LABOR 2.0 allowance

3. CONSUMABLES, CHEMICALS, AND

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

4. UTILITIES AND SERVICES

Waste Disposal 0.6 30 ft 3

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

5. TOTAL 0 AND M ANNUAL COST 6.7

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment 50-opDemintralzer Sh t 1)

{Sheet 1)

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

BASIS FOR

ITEM LAROR 1ITOM AUIFRAI It TIhTAI CflCY

1T

tMAr"

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

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

3. ASSOCIATED PIPING SYSTEMS 9 6.0 15.0 2" piping

4. INSTRUMENTATION AND CONTROLS 4 6.0 10.0

5. ELECTRICAL SERVICE No

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

7. CONTINGENCY 2 4.0 6.0 10%

8. TOTAL DIRECT COSTS 29 42.8 - 71.8

( C C

K K

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

DIRECT COST (1975 $1000)

FO*l PMFNT/MATFRTALS BASIS FOR

tT*M LANOR TOTAL COST FSTTMATF

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

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

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

.1

5. ELECTRICAL SERVICE neg

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

7. CONTINGENCY 3 6.0 9.0

B. TOTAL DIRECT COSTS 31 63.8 94.8

TOTAL DIRECT COST ESTIMATE SHEET OF RADWAST!E TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

(Sheet

200-gpm Oemtneraltzer DIRECT COST (1975 $1000)

EflUIPI4FNTII4ATFRTAL * BASIS FOR

ITEM LABOR TflTAI rnCT r~tTuATr

1T A

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

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

___(shielded area)

3. ASSOCIATED PIPING SYSTEMS 12 12.0 24.0 4" piping

4. INSTRUMENTATION AND CONTROLS 4 6.0 10.0

5. ELECTRICAL SERVICE neg

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

7. CONTINGENCY 3 9.0 12.0

8. TOTAL DIRECT COSTS 35 94.2 129.2

( (

K

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

DIRECT COST (1975 $1000)

BASIS FOR

I TrM lAROR EOUJIPMNT/MATERjALS TOTAL COST ESTIMATE

T I COST ESTIMATE

3

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

2.

(shielded area)

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

'a

4. INSTRUMENTATION AND CONTROLS 4 6.0 10.0 allowance

5. ELECTRICAL SERVICE neg

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

7. CONTINGENCY 4 9.0 13.0

8. TOTAL DIRECT COSTS 44 102.2 146.2

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

ITEM lABOR NTNrD TJlTA!

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

aAeT*

DROIO

  • n* *

rvr uK EV)lr.1~PY.I

PP*guA*P

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

2. MAINTENANCE MATERIAL AND

LABOR 5.0 allowance

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

-.J

a

4. UTILITIES AND SERVICES

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

5. TOTAL 0 AND M ANNUAL COST 19.7 C

K I

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

COST (197k.$1000)

YYIPLu AILr nV IlV%

I am*o -

flTurD

lll_ __ _

?linI

Ifl, matie fflS EflM? rCTTMATe

&'flC I l bl *fll

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

AND OVERHEAD 30 min/day

2. MAINTENANCE MATERIAL AND

LABOR 5.0 allowance

3

3. CONSUMABLES,

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

4. UTILITIES AND SERVICES

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

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADIASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

COST (1975 $1000)

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

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

2. MAINTENANCE MATERIAL AND

LABOR 5.0 allowance CONSUNABLES, CHEMICALS, AND33

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

4. UTILITIES AND SERVICES

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

--- I C C

/

K

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

COST (1975 $1000)

ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE

l. OPERATING LABOR, SUPERVISION,

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

2. MAINTENANCE MATERIAL AND

LABOR 5.0 allowance

3. CONSUMABLES, CHEMICALS, AND

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

4. UTILITIES AND SERVICES

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

5. TOTAL 0 AND M ANNUAL COST 23.5

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

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

D*crlrintinn of Aujnmant flminapA147AP . DUo

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

COST (1975 $1000)

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

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

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

1. OPERATING LABOR, SUPERVISION.

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

2. MAINTENANCE MATERIAL AND

LABOR 5.0 allowance

3. CONSUMABLES, CHEMICALS, AND

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

4. UTILITIES AND SERVICES

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

( .-."(

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

........ r

K

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

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

COST (1975 $1000)

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

AND OVERHEAD 3.3 15 min/shift

2. MAINTENANCE MATERIAL AND

LABOR 5.0 allowance

3. CONSUMABLES, CHEMICALS, AN"

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

4. UTILITIES AND SERVICES

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

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

Ftlter (Sheet

20-qm Cartrtd9e DIRECT COST (1975 $1000)

TTFM I AI*fl2 vN Itur

¶ u'IIAqr rD lr e BASIS FOR

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

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

2.

(shielded area)

3. ASSOCIATED PIPING SYSTEMS 1.5' 1.0 2.5 allowance

-. 4 Q

at 4. INSTRUMENTATION AND CONTROLS 0.6 2.4 3.0 allowance

5. ELECTRICAL SERVICE neg

6. SPARE PARTS 0.5 0.5 SUBTOTAL 9.7 11.9 21.6

7. CONTINGENCY 1.0 1.0 2.0 10%

8. TOTAL DIRECT COSTS 10.7 12.9 23.6

(

TREATMENT

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment Cartridge Filter (Sheet 2)

COST (1975 $1000)

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

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

4.5 10 changes @ 10 man-hrs/change

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

2. MAINTENANCE MATERIAL AND allowance

1.0

LABOR

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

1.0

SUPPLIES

4. UTILITIES AND SERVICES 3

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

8.0

5. TOTAL 0 AND MANNUAL COST

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREAT1ENT SYSTEM

i FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

1)

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

fIW01T

P~NT uI~dTIDTAI BASIS FOR

ITEM LARnR T*TAI

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

ASM4E VIII

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

2.

(shielded area)

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

0

4. INSTRUMENTATION AND CONTROLS in item 1

5. ELECTRICAL SERVICE 7 13.0 20 allowance

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

7. CONTINGENCY 5 10.0 15 10%

8. TOTAL DIRECT COSTS 56 108.0 164

( r

K K

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

2)

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

-vT

(Sheet DIRECT COST (1975 $1000)

BASIS FOR

TT*M LAROR EOUIPMENT/MATERIALS TOTAL COST ESTIMATE

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

1. ASME Viii

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

2. (shielded area)

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

-J

4. INSTRUMENTATION AND CONTROLS - - item I

5. ELECTRICAL SERVICE 12 18.0 30 allowance

6. SPARE PARTS - 3.0 3 SUBTOTAL 102 184.0 286

7. CONTINGENCY 10 18.0 28 10%

8. TOTAL DIRECT COSTS 112 202.0 314

ANNUAL OPERATING AND MAINTENANCE COST ESTI1ATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

COST (1975 $1000)

ITEM LABOR OTHER TOTAL BASIS FOR COST !STTI4ATF

1. OPERATING LABOR, SUPERVISION,

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

2. MAINTENANCE MATERIAL AND

LABOR 10.0 allowance

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

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

( C

T K

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

DIRECT COST (1975 $1000)

BASIS FOR

TTIFM LABOR FOUlPMENTIMATFRIALS TOTAL COST ESTIMATF

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

feed tank, ASME VIII

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

3. ASSOCIATED PIPING SYSTEMS 3.0 2.0 5.0 allowance

0

4. INSTRUMENTATION AND CONTROLS in item I

5. ELECTRICAL SERVICE 7.0 13.0 20.0 allowance

6. SPARE PARTS 6.0 6.0

SUBTOTAL 35.2 90.6 125.8

7. CONTINGENCY 3.0 9.0 12.0 10%

8. TOTAL DIRECT COSTS 38.2 99.6 137.8

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE

1. OPERATING LABOR, SUPERVISION,

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

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

3. CONSUMABLES, CHEMICALS. AND

SUPPLIES neg No

4. UTILITIES AND SERVICES

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

5. TOTAL 0 AND MANNUAL COST 16.2

( r C

1)

TOTAL DIRECT (Sheet COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

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

DIRECT COST (1975 $1000)

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

?tTrM I AROR TOTAL COST ESTIMATE

T -

3 28 31 SS, ASME VIII, atmospheric

1. PROCESS EQUIPMENT

service, 200°F

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

2.

(shielded area)

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

w 4. INSTRUMENTATION AND CONTROLS 4 6 10 allowance

5. ELECTRICAL SERVICE neg

6. SPARE PARTS neg SUBTOTAL 39 s0 89

7. CONTINGENCY 4 5 9 10%

8. TOTAL DIRECT COSTS 43 55 98

ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREAThENT

SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment 10000-Gallon Tank (Sheet 2)

COST (1975 $1000)

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

1. OPERATING LABOR, SUPERVISION.

AND OVERHEAD 1.1 5 min/shift - log level readings

2. MAINTENANCE MATERIAL AND

LABOR 1.6 1/2% of equipment

3. CONSUMABLES. CHEMICALS, AND neg SUPPLIES

4. UTILITIES AND SERVICES

Waste Disposal Water Steam neg Electricity Building Services Other

5. TOTAL 0 AND N ANNUAL COST 2.7

(

REFERENCES TO APPENDIX B

NUS-531,

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

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

- 2000,"

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

1.110-85

APPENDIX C

DATA NEEDED FOR RADIIASTE TREATMENT SYSTEM

COST-BENEFIT ANALYSIS FOR LIGHT-WATER

COOLED NUCLEAR REACTORS

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

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

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

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

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

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

1.110-87

TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE'TREATMENT-SYSTEH

FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

Description of Augment DIRECT COST (1975 $1000)

BASIS FOR

i Tru 1 AflfD

FflIIIPMFNT/MATFRlALS TOTAL COST ESTIMATE

i aunD EnUTPMENTIMATERIALS

1. PROCESS EQUIPMENT

t I 1 I

2. BUILDING ASSIGNMENT

I I I I

0 3. ASSOCIATED PIPING SYSTEMS

I I I I --

4. INSTRUMENTATION AND CONTROLS

I I I I

S. ELECTRICAL SERVICE

I I I I

6. SPARE PARTS

______________________I i mI

SUBTOTAL

________________________________________________________ 1 -I I I

7. CONTINGENCY

I I I

8. TOTAL DIRECT COSTS

________________________________________________________ ________________ I __________________________________________________ _____________ _______________________________________________

( C C

K

0

"I

U

2 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT

2

-4 SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS

U

2

2 Description of Augment C,

a

9 COST (1975 $1000)

9 I TIFM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE

'a ITEM

w

-J

04

1. OPERATING LABOR, SUPERVISION,

AND OVERHEAD

0.j

'a

"4 a.

0

"4

2. MAINTENANCE MATERIAL AND

LABOR

U3.

4.

CONSUMABLES,

SUPPLIES

CHEMICALS, AND

UTILITIES AND SERVICES

Waste Disposal Water Steam Electricity Building Services Other

5. TOTAL 0 AND M ANNUAL COST


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