Regulatory Guide 1.110
| ML003740332 | |
| Person / Time | |
|---|---|
| Issue date: | 03/31/1976 |
| From: | Office of Nuclear Regulatory Research |
| To: | |
| References | |
| RG-1.110 | |
| Download: ML003740332 (87) | |
U.S. NUCLEAR REGULATORY COMMISSION
REGULATORY GUIDE
OFFICE OF STANDARDS DEVELOPMENT
REGULATORY GUIDE 1.110
COST-BENEFIT ANALYSIS FOR RADWASTE S
LIGHT-WATER-COOLED NUCLEAR PDWE&
CRS'
March 1976
4 USNRC REGULATORY GUIDES
Commen.l shoutd be Sent to Rhe Secretary of the Comm,ssion U S Nuclea,
%equietoy Guido* ate issued to describe and meeks ovelablto
,he pubic Rogulstory Comminssion Washington. 0 C 2065. Attention Docketing end methods acceptable go the NRC staff of4 impementing specific pairt of the S
Commission'& fegulatione. to definetel technique mused by the state in evild The guides are issued in the following ten broad divisions at"ig *pecific problems or postulated accidents. 0r to provide guidance to eppli cents Regulatory Gudes am not substitutes for regulamons. end compliance I Power Reactors
5 Products with thenm ile rot reCed Methods end soutione diflerent fron those get out i I Research end Test Reactors
7 Tronsponstion Ihe guidell we be acceptable It they provide a bahis for lthe findings requrlit to
3 Fueuls and Materiels Facilities a Occupolionat 4palt h the mesnee
- l sentis*lnCe- of - permst of Scenes by the Commitssion
4 Environmental and Siting
2 Antitrust Review Commentd Isid uggestiOi$e
- 0F imPtoSetfitC it #hbae gtaldel We entcouraged S Materialt end Plant Protection
10 General ot anll.
end guidss Wil be Revised. a. a41pp1rop1riete.
to accommodate corn asmon ed ho wtc intormatiotn or e*perieot Ifowoer comments on Copies of published guides may be obtained by wistten .squett indicating Cth Ofu guide. A received within Oboins two month$ chatret. issuance. will be *at divisions desired to the U S Nuclear Regulators Commission Wshtington 0 C
ticfady orssIul Mt evaluating the teed
=
of an srly viision
20566. Attention Director. Office of Standerde Development
TABLE OF CONTENTS
Page
A. INTRODUCTION
.......................................................................
1.110-5
B. DISCUSSION
R .......................................................................
1.110-5
C. REGULATORY POSITION
.........................................................
1.110-6 D.
IMPLE14ENTATION ................................
..................................
1.110-6 APPENDIX A, PROCEDURES FOR PERFORMING COST-BENEFIT ANALYSES ...........................
1.110-7 APPENDIX B. BASES FOR PARAMETERS USED IN PERFORMING COST-BENEFIT
ANALYSES ..............................................................................
1.110-17 LIST OF APPENDIX B COST ESTIMATE SHEETS ...............................................
1.110-19 REFERENCES TO APPENDIX B ..............................................................
1.110-85 APPENDIX C, DATA NEEDED FOR RADWASTE TREATMENT SYSTEM COST-BENEFIT
ANALYSIS FOR LIGHT-WATER-COOLED NUCLEAR REACTORS ......................................
1.110-86 SAMPLE ESTIMATE SHEETS ................................................................
1.110-88
1.110-3
LIST OF TABLES
Table Page A-1 Direct Costs - Gaseous Radwaste Augments ................................
1.110-8 A-2 Annual Operating Costs - Gaseous Radwaste Augments; Liquid Radwaste Augments .....................................................
1.110-10
A-3 Annual Maintenance Costs - Gaseous Radwaste Augments; Liquid Radwaste Augments .....................................................
1.110-12 A-4 Labor Cost Correction Factors ...........................................
1.110-13 A-5 Indirect Cost Factors ...................................................
1.110-14 A-6 Capital Recovery Factors ................................................
1.110-15 B-1 Indirect Costs ..........................................................
1.110-18 LIST OF FIGURES
Figure Page A-1 Electric Power Supply Areas in the United States ........................
1.110-16
1.110-4
A.
INTRODUCTION
Section I1.D of Appendix I, "Numerical Guides for Design Objectives and Limiting Conditions for Operation to Meet the Criterion 'As Low As Is Reasonably Achievable' for Radioactive Material in Light-Water-Cooled Nuclear Power Reactor Effluents," to 10 CFR Part 50, "Licensing of Produc tion and Utilization Facilities," requires that liquid and gaseous radwaste systems for light water-cooled nuclear power reactors include all items of reasonably demonstrated technology that, when added to the system sequentially and in order of diminishing cost-benefit return, can, for a favorable cost-benefit ratio, effect reductions in dose to the population reasonably expected to be within 50 miles of the reactor.
Values of $1000 per man-rem and $1000 per man-thyroid-rem are given as interim criteria pending the development and establishment of better criteria.
Compliance with Section II.D of Appendix I to 10 CFR Part 50 (which specifically addresses doses to the population) and Sections IL.A,
11.8, and II.C (which address doses to nearby individuals)
is required to meet the criterion, "as low as is reasonably achievable."
To'implement the requirements of Appendix I, the NRC staff has developed a series of guides providing methods acceptable to the staff for the calculation of effluent releases, dispersion of effluents in the atmosphere and different water. bodies, associated radiation doses to man, and cost-benefit aspects of treating radwastes.
This regulatory guide describes a method for performing a cost-benefit analysis for liquid and gaseous radwaste system components.
The procedures and models provided in this guide will be subject to continuing review by the staff with the aim of providing greater flexibility to the applicant in meeting the require ments of Appendix I.
As a result of such reviews, it is expected that alternative acceptable methods for calculation will be made available to applicants and that calculational procedures found to be unnecessary will be eliminated.
B.
DISCUSSION
Each applicant for a permit to construct or a license to operate a light-water-cooled nuclear power reactor and each licensee with a license to operate a light-water-cooled nuclear power reactor is required to provide reasonable assurance that the design objectives for as low as is reasonably achievable effluent releases are satisfied by the liquid and gaseous radwaste system designs.
It is the objective of this guide to provide an acceptable method of performing cost-benefit analysis, in conformance with Section II.D of Appendix I, to demonstrate that the plant design includes all items of reasonably demonstrated technology for reducing the cumula tive population dose due to releases of radioactive materials from the reactor to levels as low as reasonably achievable.
As an interim measure the Conmnission chose values of $1000 per man rem and $1000 per man-thyroid-rem (or lesser values if demonstrated to be suitable for a particu lar site) to be used to implement the cost-benefit analysis.
Because the Commission has not outlined any procedures for including the effects of inflation in the analysis, the NRC staff's analysis is based on 1975 dollars; i.e., neither the costs nor the interim criteria are escalated for the predicted effects of inflation.
Since the worth of a man-rem or man-thyroid-rem to the public is subject to the same fluctuations in value as the cost of equipment to reduce radioactive emissions, the NRC staff believes this approach to be reasonable.
The NRC staff has outlined a method for performing the required cost-benefit analysis and has provided cost parameters for estimating the costs for the various radwaste treatment equip ment items in use, or proposed for use, at light-water-cooled nuclear power reactors.
The methodology and cost parameters are presented in Appendix A to this guide.
The costs presented.
consider the direct equipment cost and the costs of building space, supportive services, mainte nance, interest, and operating as well as other costs generally considered in analyzing capital and operating costs in power plant estimating.
The bases for the costs calculated by the NRC
staff are given in Appendix B.
1-110-5
C.
REGULATORY POSITION
1.
In accordance with Section II.D, Appendix I to 10 CFR Part 50, each applicant for a permit to construct a light-water-cooled nuclear power reactor should demonstrate by means of a cost benefit analysis that further reductions to the cumulative dose to the population within a
50-mile radius of the reactor site cannot be effected at an annual cost of $1000 per man-rem or
$1000 per man-thyroid-rem (or such lesser costs as demonstrated to be suitable for a particular case).
2.
The cost-benefit analysis should consider the reduction in releases of radioactive material from all effluent pathways.
Liquid and gaseous radwaste system augments considered in the analysis should be selected in order of diminishing cost-benefit returns.
3.
All costs should be given in terms of 1975 dollars (as is the $1000 per man-rem cost with which they are compared).
Allowances for Inflation after 1975 should not be factored into the cost estimates.
4.
The method of calculation described in Appendix A and the parameters presented in Appendix B of this guide are acceptable to the NRC staff for performing the cost-benefit analysis.
5.
In support of the cost-benefit analysis, the applicant should provide a complete evaluation including methodology used, components considered, and all assumptions and parameters used.
Information to be submitted by the applicant Is described in Appendix C to this guide.
Use of parameters, assumptions, and models different from those given in Appendices A and B to this guide may result in differences between the evaluations by applicants and those by the NRC staff.
Because of this, these parameters and assumptions should be clearly described and substantiated by the applicant.
0. IMPLEMENTATION
The purpose of this section is to provide information to license applicants and licensees regarding the NRC staff's plan for using this regulatory guide.
Except in those cases in which the applicant proposes an acceptable alternative method for complying with specified portions of the Commission's regulations, the method described herein will be used in the evaluation of construction permit applications docketed after June 4, 1976 unless this guide is revised as a result of suggestions from the public or additional staff review.
If an applicant wishes to use this regulatory guide in developing submittals for applications docketed on or before June 4, 1976, the pertinent portions of the application will be evaluated on the basis of this guide.
1.110-6
APPENDIX A
PROCEDURES FOR PERFORMING COST-BENEFIT ANALYSES
This appendix contains guidance for performing cost-benefit analyses on individual system augments, as well as the parameters needed for estimating costs.
The bases for the parameters and worksheets appropriate for use with the following cost-benefit procedure are given in Appendix B.
1.
The cumulative population man-rem exposure and man-thyroid-rem exposure should be determined for each effluent release source, e.g., liquid radwaste releases, ventilation releases, etc.
2. Potential reductions to the cumulative population exposure should be determined based on the addition of items of reasonably demonstrated technology which have the potential to reduce releases of radioactive materials.
3.
Acceptable methods for performing some of the calculations need for items 1 and 2 above are contained in Regulatory Guides 1.109, "Calculation of Annual Doses to.Man from Routine Releases of Reactor Effluents for the Purpose of Evaluating Compliance with 10 CFR Part 50, Appendix I,"
and 1.111,
"Methods for Estimating Atmospheric Transport and Dispersion for Gaseous Effluents in Routine Releases from Light-Water-Cooled Reactors," and in two regulatory guides now in prepara tion on the subjects of (1) calculation of releases of radioactive materials In liquid and gas eous effluents from light-water-cooled reactors and (2) methods for estimating aquatic dispersion of liquid effluents from routine reactor releases for the purpose of implementing Appendix I.
4.
The total annual cost of each augment considered in item 2 above should be determined as follows:
a.
The Total Direct Cost (TOC):
(1)
Obtain the direct cost of equipment and materials from Table A-1.
(2)
Multiply the direct labor cost obtained from Table A-1 by the appropriate labor cost correction factor from Table A-4 to obtain the corrected labor cost for the geographtcal area from Figure A-l, in which the plant is to be built.
(3)
Add the costs obtained from steps (1) and (2) to obtain the Total Direct Cost.
b.
Obtain-the appropriate Indirect Cost Factor (ICF)
from Table A-S.
c.
Determine Total Capital Cost (TCC)
by using the equation:
TCC -
TDC x ICF
d.
Obtain the appropriate Capital Recovery Factor (CRF) from Table A-6.
e.
Determine the Annual Fixed Cost (AFC) by using the equation:
AFC = TCC x CRF
f.
Obtain the Annual Operating Cost (AOC) and the Annual Maintenance Cost (AMC)
from Tables A-2 and A-3.
Multi-unit sites using shared radwaste systems should multiply the AOC by the number of reactors sharing the augment.
g.
Determine the Total Annual Cost (TAC) by using the equation:
- 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
419
147
566 PWR Air Ejector Charcoal/HEPA
Filtration Unit
14
10
24 Steam Generator Flash Tank Vent to Main Condenser
19
14
33 In cases where the equipment may be located either in the auxiliary building or the turbine building and common usage does not indicate a definite preference of one location or the other, cost for both locations are listed with the turbine building location cost in parenthesis.
1.110-8
TABLE A-1 (Continued)
DIRECT COSTS - LIQUID RADWASTE AUGMENTS
Direct Costs
15-gpm Evaporator
30-gpm Evaporator
50-gpm Evaporator Evaporator Distillate Demineralizer
50-gpm Demineralizer
100-gpm Demineralizer
200-gpm Deminieralizer
400-gpm Demineralizer
100-gpm Precoat Filter
400-gpw Precoat Filter
20-gpm Cartridge Filter
2-gpm Reverse Osmosis
10,000-gal Tank Equipment/Material
386
540
655
36
43
64
94
102
108
202
13
100
55
1.110-9 Labor
201
223
233
24
29
31
35
44
56
112
11
38
43
(1975 $1000)
Total
587
763
888
60
50
95
129
146
164
314
24
138
98
TABLE A-2 T
ANNUAL OPERATING COSTS
-
GASEOUS RADWASTE AUGMENTS
BWR Offgas Recoatbiner
3-ton Charcoal Adsorber Desiccant Dryer Charcoal Vault Refrigeration Main Condenser Vacuum Pump Charcoal/HEPA
Filtration System Clean Steam to Turbine Glands Clean Steam to Steam Valves, 24" and Larger Clean Steam to Steam Valves, 2-1/2" and Less Than 24"
15,000-cfm HEPA Filtration System
1,000-cfm Charcoal/HEPA Filtration System
15,000-cfm Charcoal/HEPA Filtration System
30,000-cfm Charcoal/HEPA Filtration System Turbine Bldg. Chilled Water HVAC System
600-ft 3 Gas Decay Tank PWR Hydrogen Recombiner PWR Air Ejector Charcoal/HEPA Filtration Unit Steam Generator Flash Tank Vent to Main Condenser Total Operating Cost
3
(1975 $lOOO/yr)
neg
3
4
0.4
24
3
3
6
2
7
9
49 neg
4
4
1 ANNUAL OPERATING COSTS
- LIQUID RADWASTE AUGMENTS
Evaporation -
PWR Dirty Waste Evaporation -
BWR Dirty Waste Evaporation - Condensate Polisher Chemical Waste Evaporation - Detergent Waste Demineralization - kvaporator Distillate Demineralization - BWR 2nd Waste Demineralizer in Series
50
169
114
20
5
15 Operating costs are given for a single reactor.
Operating costs for augments in shared radwaste systems should be multiplied by the number of reactors serviced by the augment.
1.110-10
K
B
r m m
TABLE A-2 (Continued)
ANNUAL OPERATING COSTS - LIQUID RADWASTE AUGMENTS
Total Operating Cost (1975 $1000/yr)
5 Demineralization - PWR Clean Waste Demineralization - BWR Dirty Waste Demineralization - PWR Dirty Waste Demineralization - PWR Turbine Bldg. Drains Desmineralization - PWR Steam Generator Blowdown Precoat Filter -
BWR Dirty Waste Cartridge Filter Reverse Osmosis - Detergent Waste
10,000-gal Tank
88
18
95
25
53
7
7
1
1.110-11
TABLE A-3 ANNUAL MAINTENANCE COSTS-
GASEOUS RADWASTE AUGMENTS
Total Maintenance Cost (1975 $1O00/Yr)
BWR Offgas Recombiner
20
3-ton Charcoal Adsorber neg Desiccant Dryer
6 Charcoal Vault Refrigeration
3 Main Condenser Vacuum Pump Charcoal/HEPA
Filtration System
1 Clean Steam to Turbine Glands
4 Clean Steam to Steam Valves, 24" and Larger
4 Clean Steam to Steam Valves, 2-1/2" and Less Than 24"
12
15,000-cfm HEPA Filtration System
2
1,000-cfm Charcoal/HEPA Filtration System
0.6
15,O00-cfm Charcoal/HEPA Filtration System
9
30,000-cfm Charcoal/HEPA Filtration System
18 Turbine Bldg. Chilled Water HVAC System
20
600-ft 3 Gas Decay Tank neg PWR Hydrogen "Recombiner
10
PWR Air Ejector Charcoal/HEPA Filtration Unit
2 Steam Generator Flash Tank Vent to Main Condenser
1 ANNUAL MAINTENANCE COSTS - LIQUID RADWASTE AUGMENTS
15-gpm Evaporator
30
30-gpm Evaporator
30
50-gpm Evaporator
30
Evaporator Distillate Demineralizer
2
50-gpm Demineral izer
5 lO0-gpmi Demineralizer
5
200-gpm Demineral izer S
100-gpm Precoat Filter
10
400-gpm Precoat Filter
10
20-gpm Cartridge Filter
1
2-gpm Reverse Osmosis g
10.000-gal Tank
2
1.110-12
TABLE A-4 LABOR COST CORRECTION FACTORS
Labor Cost Correction Factor
1.6
1.5
1.0
1.4
1.1
1.2
1.3
1.2 See Appendix B, "Labor See Figure A-1.
Cost Correction Factors.'
1.110-13 FPC
Geographic Region I
1II
IV
V
VI
VII
Vlll
TABLE A-5 INDIRECT COST FACTORS
Type Radwaste System
"1. Single unit site, unitized radwaste system
2.
Multi-unit site, shared radwaste system
3.
Multi-unit site, unitized radwaste system Indirect Cost Factor
1.75
1.75
1.75 + (n-1)1.5 n
where n is the number of unitized radwaste systems at the site Each reactor has a separate, nonshared radwaste system.
I..
1.110-14
TABLE A-6 CAPITAL RECOVERY FACTORS
Cost of Honey
(1 per year, i)
5
6
7
8
9
10
11
12
13
14
15 Capital Recovery Factor
0.0651
0.0726
0.0806
0.0888
0.0973
0.1061
0.1150
0.1241
0.1334
0.1428
0.1523 service life of 30 years and the follwing equation:
CRF
M + 1)3 (I + i)30-1
1.110-15
Based on a
LEGEND
¶Im REGIONAL GROUPING OF POWER SUPPLY AREAS
FIGURE A-1 ELECTRIC POWER SUPPLY AREAS IN THE UNITED STATES
(
C
C
APPENDIX B
BASES FOR PARAMETERS USED IN PERFORMING COST-BENEFIT ANALYSIS
This appendix contains detailed cost estimate sheets showing the methods and parameters used to obtain all costs associated with augments considered for the liquid and gaseous radwaste systems.
The cost estimate sheets are grouped by radwaste system types.
The first sheet in each case is an equipment cost worksheet for determining direct equipment costs.
The second sheet is an operating cost worksheet.
All costs are stated in terms of 1975 dollars.
No attempt has been made to project the effect of inflation.
Variations of labor costs and productivity with site locaticns are considered.*
All costs are based on the assumption that the reactor is in the design stage and that augmentation of a radwaste system will not involve backfltting of an existing plant.
Backfltttng costs should be determined on a case-by-case basis.
1.
Capital Costs Capital costs are reported by grouping items by system and by plant location, which gen erally follow the NRC (AEC)
accounting system given in NUS-531 (Ref. 1).
The direct costs considered to be applicable to radwaste systems are structures, electrical services, equipment, and instrumentation and controls.
Spare parts and a contingency allowance** are included in the direct costs.
Total capital costs are obtained by multiplying direct costs by an indirect cost factor.
2.
Direct Cost Direct costs for each augment include equipment, site labor, and site materials.
Principal equipment designs and hardware costs were obtained from utility companies, architect-engineers, and vendors.
Costs for building space, electrical services, piping, and instrumentation were estimated considering equipment functions and arrangements.
Costs for electric services, piping, and instrumentation and controls were determined using judgment to estimate equipment layout, points of interface, and services required.
The costs for equipment and building space are consistent with'NRC staff recommendations for radwaste sys tem quality assurance, materials, and seismic design.
Space requirements were determined based on manufacturer's data or data from existing or proposed layout drawings.
3.
Labor Cost Correction Factors Labor cost adjustment factors were developed for each Of the eight FPC electric power supply areas shown in Figure A-I of Appendix A by calculiting the average labor cost-for selected cities (Ref. 2) in each area and adjusting this cost for estimated variations in labor productivity due only to differences In labor practices in the regions considered.
Manpower costs were calcu lated by multiplying the estimated labor requirements in man-hours by the composite wage rate (Ref.
3).
The calculated labor cost correction factors are tabulated in Table A-4 of Appendix A.
4.
Indirect Cost Factor Indirect costs asa percentage of direct costs are calculated in Table B-1.
Location effects of the eight FPC Power Supply areas are estimated and shown in Table A-4 of Appendix A.
Contingency onsite labor and process equipment and material are all based on-l0%.
1.110-17
TABLE 8-1 K..
INDIRECT COSTS
1st Unit, Subsequent Percentage of Units. Percentage Direct Cost of Direct Cost Construction facilities, equiment, and services
10
5 Engineering and construction managment services
20
10
Other owner s costs
10
S
Interest during construction
3S
35 Total
75 SS
- Based on a lOs/yr interest rate and a 4-year construction time for radaste systems only.
Interest during construction Is estimated to be 25% of direct costs plus other indirect costs.
This is equivalent to 351 of the direct costs.
The Indirect escalators (factors) were estimated from preliminary architect/engineering data to be used to update the DOM concept and ORCOST computer codes.
S.
Operation And Maintenance Costs Annual expenses for operation and maintenance (O&N) of the radwaste treatment systes were estimated for baseload power plants operating at 801 capacity factor.
Manpower and supply costs were estimated by considering equipment functions it each case.
Expenses for gases, steam, resins, auxiliary por. and other supplies and services were assessed individually.
Maintenance costs were evaluated according to the type of service for which the equipment could be used.
Operating costs include estimated manpower costs, costs of utilities and supplies, and effects on supporting plant systems Interfacing with the augmented radmste system (e.g., effect of an evaporator augment on the solid waste syste).
Also included are costs of handling wastes such as spent resins, demineralizer regenerants, evaporator bottoms, and filter media, as well as offsite handling, transportation, and burial costs.
6.
Capital Recovery Factor The capital recovery factor Is a levelized annual charge which takes into account the cost of borroved money and the depreciation of assets.
It Is calculated from the expression:
I(1 #)o (I + ~
where i a cost of borrowed money expressed as a decimal P - plant operating lifetime (yr)
In calculating the values used in Table A-S of Appendix A. a plant operating lifetime of 30
years was used.
The capital recovery factor multiplied by the total capital cost will give the annual dollar charges for capital and capital-related expenses.
1.110-18
LIST OF APPENDIX B COST ESTIMATE SHEETS
Page Numiber BW Offgas Recmbiner .............................................................
1.110-20
3-ton Charcoal Adso r ...............................................................
1.110-22 Desiccant Dryer ..............................................................
1.110-24 Charcoal Vault Refrigeration .........................................................
1.110-26 Charcoal/HEPA Filtration System - Condenser Vacuun Pump ..............................
1.110-28 Clean Steam to Turbine Glands ........................................................
1.110-30
Clean Steam to Steam Valves 24- and Larger ...........................................
1.110-32 Clean Steam to Steam Valves 2-1/2' and Less Than 24" ................................
1.110-34
1S.000-cftm NEPA Filtration System ....................................................
1.110-36
1000-cfa Charcoal/HEPA Filtration System .............................................
1.110-39
15.000-cfm Charcoal/HEPA Filtration System ...........................................
1.110-41
30,000-cfm Charcoal/HEPA Filtration System ..........................................
1.110-44 Turbine Building Chilled Mater HVAC System ...........................................
1.110-47
600-ft 3 Gas Decay Tank ...............................................................
1.110-49 PIW Hydrogen Recombiner ..............................................................
1.110-S1 PiW Air Ejector Charcoal/HEPA Filtration Unit ........................................
1.110-53 Stem Generator Flash Tank Vent to rain Condenser ....................................
1.110-55 Evaporators ..........................................................................
1.110-57 Evaporator Distillate Demineralizer ..................................................
1.110-64 Demineralizers .......................................................................
1.110-66 Cartridge Filter .....................................................................
1.110-76 Precoat Filters ......................................................................
.114
7R
Reverse Osmosis .....................................................................
1.110-81
10.000-gal Tank ...........................................................
1.11"
1.110-19
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment ITEM
1.
PROCESS EQUIPMENT
2.
3.
4.
5.
6.
7.
8.
RUD flffn.e D
r.mh4n.... iCk.e.
11 I___MIXL_
1 IVIML
COST ESTIMATE
DIRECT COST.(1975 $1000)
r1 T DMUT'/MATrD TAt BASIS FOR
90
260
350
single unit, catalytic type w/heater and condenser, w/o instrumentation and controls, stainless steel, ASME VIII
BUILDING ASSIGNMENT
100
50
30' x 40' x 25' @ $5/ft 3 (turbine building shielded area)
ASSOCIATED PIPING SYSTEMS
18
12
30
augment piping connections only INSTRUM4ENTATION AND CONTROLS
24
96
120
allowance ELECTRICAL SERVICE
neq
4kw heaters on vessels neglected SPARE PARTS
85
85
75K for catalyst + 2% E/M in items 1 & 4 above SUBTOTAL
232
503
735 CONTINGENCY
23
50
73
10%
TOTAL DIRECT COSTS
2S5
553
808 r
a O
(
S......
..................
w BWR Off %e Darr-M--- Ick- a, I
a W
i IARND
TflYAi
K
A
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
SYSTEM FOR-LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment BWR Offgas Recombiner (Sheet 2)
COST (1975 $1000)
ITEM
LABOR
OTHER
TOTAL
BASIS FOR COST ESTIMATE
OPERATING LABOR,
SUPERVISION,
3.3
15 m.n/shift AND OVERHEAD
MAINTENANCE MATERIAL AND.
20.0
routine conditioning of catalyst and LABOR
equipment upkeep; 5% of E/M including I&C
CONSUMBLES, CHEMICALS, AND
-
initem 2 SUPPLIES
UTILITIES AND SERVICES
Waste Disposal Water Steam neg intemittent; 4kw heater load is negligible Electricity Building Services Other TOTAL 0 AND M ANNUAL COST
23.3
1.
2.
C2
,01
3.
4.
5.
I
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment
!TFM
1.
PROCESS EQUIPENT
2.
BUILDING ASSIGNMENT
3.
4.
S.
6.
7.
8.
3-ton Charcoal Adsorber (Sheet 1)
LABOR
5 DIRECT COST (1975 $1000)
EOUIPMENTIMATERIALS
TOTAL
- -
- -
-
-
-
44.0
49.0
BASIS FOR
COST ESTIMATF
carbon steel, 350 psig, 200 ft 3 volume (augment to existing train of beds)
4.
4.
4.
4
8
4.5
12.5
10' x 10' x 25' * $5/ft3 (turbine building shiel4ed area)
ASSOCIATED PIPING SYSTES
-
in item I
INSTRUKENTATION AND CONTROLS
neg ELECTRICAL SERVICE
neg SPARE PARTS
none existing SUBTOTAL
13
48.5
61.5 CONTINGENCY
1
5.0
6.0
10%
TOTAL DIRECT COSTS
14
53.5
67.5 r
r a
.
. .. . . .
. r m
K
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment
3-ton Charcoal Adsorber (Sheet 2)
COST (1975 $1000)
I TFM
LABOR
OTHER
TOTAL
BASIS FOR COST ESTIMATE
OPERATING LABOR.
SUPERVISION.
neg AND OVERHEAD
MAINTENANCE MATERIAL AND
allowance of 3% of equipment cost LABOR
neg is negligible CONSUMABLES.
CHEMICALS,
AND
SUPPLIES
neg lifetime use of charcoal assumed UTILITIES AND SERVICES
Waste Disposal Water Steam neg Electricity Building Services Other TOTAL 0 AND M ANNUAL COST
neg K
1.
2.
3.
4.
I..
5.
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment Desiccant Drver fSheet !1 I TEN
I ARflR
DIRECT COST (1975 $1000)
IL
1%
COTETMT
BASIS FOR
1.
PROCESS EQUIPMENT
25
75
100
redundant dryer vessels with
1 regeneration skid BUILDING ASSIGNMENT
95
50
145
40' x 36' x 20' @ $5/ft3 turbine building (shielded area)
ASSOCIATED PIPING SYSTEMS
10
5
15 augment piping connections only INSTRUMENTATION AND CONTROLS
12
48
60
allowance ELECTRICAL SERVICE
18
17
35 service for heaters, blowers, pumps, and compressors SPARE PARTS
3
3 SUBTOTAL
160
198
358 CONTINGENCY
16
20
36
10%
TOTAL DIRECT COSTS
176
218
394 r
2.
8i
3.
4.
5.
6.
7.
8.
(
r Desiccant Drver (Sheet I)
T*TAI
K
ANNUAL CPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment Desiccant Dryer (Sheet 2)
COST (1975 $1000)
I Ahfl flTIIP
TflTAI
BASIS FOR COST ESTIMATE
ITEM
itri,,,
........
.
.
.
.
OPERATING LABOR,
SUPERVISION,
3.3
15 min/shift AND OVERHEAD
MAINTENANCE MATERIAL AND
6.1
5% of equipment including I&C
LABOR
CONSUMABLES,
CHEMICALS,
AND
neg SUPPLIES
UTILITIES AND SERVICES
Waste Disposal neg operating time does not require Water neg significant utilities and services Steam Electricity neg Building Services Other TOTAL 0 AND M ANNUAL COST
9.4 K
K
1.
2.
3
4.
C
U'
S.
Q*Pim
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREAThENT SYSTEM
FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment ITEM
Charcoal Vault Refrigeration (Sheet 1)
10AM
DIRECT COST (1975 $1000)
LAORFlIITDUdCNT/UATCDTA1 C
YffAS IfC
et.V
BASIS FOR
1.
PROCESS EQUIPMENT
2.
BUILDING ASSIGNMENT
3.
4.
5.
6.
7.
8.
10
75
85
10-ton capacity, 3 refrigerators with drives, 32°F design I
t
4-4
9
3
12
20' x 10' x 201 0 $2/ft3 turbine building (nonshielded area)
ASSOCIATED PIPING SYSTEMS
In item 1 INSTRUMENTATION AND CONTROLS
4
6
10
allowance ELECTRICAL SERVICE
12
18
30
allowance SPARE PARTS
3
3 SUBTOTAL
35
105
140
CONTINGENCY
3
11
14
10%
TOTAL DIRECT COSTS
38
116
154
0 N
14 Ch
(
TftTAI
K
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
SYSTEM FOR LIGHT-WATER-COO.EO NUCLEAR REACTORS
Description of Augment Charcoal Vault Refriceration (Sheet 2)
'TIn'
COST (1975 $1000)
rTeR
TOTAL
FOR COST !T1MATE
OPERATING LABOR, SUPERVISION.
3.3
15 min/shift AND OVERHEAD
MAINTENANCE MATERIAL AND
LABOR
3.7
51 of equlpemt CONSUMABLES, CHEMICALS,
AND
in Item 2 SUPPLIES
UTILITIES AND SERVICES
Waste Disposal Water Steam
0.5 electricity and cooling water Electricity Building Services Other TOTAL 0 AND M ANNUAL COST
7.5 K
K
1.
2.
3.
4.
S.
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment Charcoal/HEPA Filtration System - Condenser Vacuum Pump (Sheet 1)
ITE4
1.
PROCESS EQUIPMENT
2.
3.
4.
5.
6.
7.
8.
LABOR__
~
LrILumLAL
IUIAL
COST ESTIMATE
D IRECT COST (1975 $1000)
2
32.5
34.5
2000 CFM preftlter/4" charcoal bed/HEPA @ S15/cfm, 10 kw heater @ $250/kw BUILDING ASSIGNMENT
3.1
1.5
4.6 Turbine building 8' x 16, x 12'
@ $3/ft3 (nonshielded area)
ASSOCIATED PIPING' SYSTEMS
1.3
0,7
2.0
allowance INSTRUMENTATION AND CONTROLS
in item 1 ELECTRICAL SERVICE
1
1.5
2.5 SPARE PARTS
0.5
0.5 SUBTOTAL
7.4
36.7
44.1 CONTINGENCY
.7
3.7
4.4
10%
TOTAL DIRECT COSTS 8.1
40.4
48.5
(
Nm wO
(
i n
BASIS FOR
I A*Q
K
K
ANNUAL OPERATING ANr MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment Charcoal/HEPA Filtration System - Condenser Vacuum Pump (Sheet 2)
COST (1975 $1000)
S...,iT*
'ueD
TfllhI
RAmie FflQ tOI[IT F¢;TTMATF
OPERATING LABOR, SUPERVISION,
neg used only during startup and shutdown AND OVERHEAD
MAINTENANCE MATERIAL AND
1.2
4 HEPA filters @ $150 & 2 Charcoal filters LABOR
@ $900, change every 2 years CONSUMABLES, CHEMICALS, AND
in items 2 and 4 SUPPLIES
UTILITIES AND SERVICES
Waste Disposal
0.2 S50/HEPA filter, $100/Charcoal filter Water Steam Electricity Building Services Other
1.4
5.
TOTAL 0 AND M ANNUAL COST
_______________________
I
_________
________
_______________________________
K
I.
2.
3.
4.
'.4
- 0
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment STT
F M
1.
PROCESS EQUIPMENT
2.
3.
4.
5.
6.
7.
8.
Clean Steam to Turbine Glands (Sheot 1)
I ARAR
DIRECT COST (1975 $1000)
FOIITDMFNTIMATPRTAI
ITEMP
15
150
TflTAI
165 BASIS FOR
- FnCT VCTttMATO
25,000 lb/hr reboiler I $4/lb/hr I
$25K/H.P. turbine glands BUILDING ASSIGNMENT
19
10
29
20' x 30' x 16' 6 $3/ft3 ASSOCIATED PIPING SYSTEMS
32
18
50
equiv 1000 ft 0 $50/ft INSTRUMENTATION AND CONTROLS
8
12
20
in addition to Item I
ELECTRICAL SERVICE
nag SPARE PARTS
5
5 SUBTOTAL
74
195
269 CONTINGENCY
7
20
27
10%
TOTAL DIRECT COSTS
81
215
296 r
C
r
K
K
SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment Clean Steam to Turbine Glands (Sheet 2)
COST (1975 $1000)
1TR4 LABOR
OTHER
TOTAL
BASIS FOR COST ESTIMATE
OPERATING LABOR,
SUPERVISION,
3.3
15 min/shift AND OVERHEAD
MAINTENANCE MATERIAL AND
4.0
40 man-days LABOR
CONSUMABLES,
CHEMICALS,
AND
SUPPLIES
UTILITIES AND SERVICES
Waste Disposal Water Steam
21.0
10 Btu/kw-hr heat rate increase Electricity Building Services Other TOTAL 0 AND M ANNUAL COST
28.3 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
9'
I.
2.
3.
4.
5.
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment Clean Steam to Steam Valves 24" and Larger (Sheet 1)
ITEM
I AMII
DIRECT COST (1975 $1000)
n:*.:TDAACLIMATDTai PROCESS EQUIPMENT
100
120
220
22 valves @ $1OK/valve, use existing reboiler BUILDING ASSIGNMENT
neg install in existing space ASSOCIATED PIPING SYSTEMS
-
in item 1 INSTRUMENTATION AND CONTROLS
-
in Item 1 ELECTRICAL SERVICE
neg SPARE PARTS
5 SUBTOTAL
100
125
225 CONTINGENCY
10
12
22
10%
TOTAL DIRECT COSTS
110
137
247 BASIS FOR
0
i%1J
I.
2.
3.
4.
S.
6.
7.
8.
(
r TnTAI
-\\
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
SYSTEM1 FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment Clean Steam to Steam Valves 24" and Larger (Sheet 2)
COST (1975 $1000)
TT!M
LABOR
OTHER
TOTAL
BASIS FOR COST ESTIMATE
OPERATING LABOR,
SUPERVISION,
3.3
15 min/shift AND OVERHEAD
MAINTENANCE MATERIAL AND
4.0
40 man-days LABOR
CONSUMABLES,
CHEMICALS,
AND
neg SUPPLIES
UTILITIES hND SERVICES
Waste Disposal Water Steam neg Electricity Building Services Other TOTAL 0 AND M ANNUAL COST
7.3 K
1.
2.
3.
4.
w U,
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment ITEM
1.
PROCESS EQUIPMENT
2.
6.
-*
3.
7.e
.
w
.h
4.
5.
6.
7.
8.
Clean Steam to Steam Valves 2-1/2N and Less Than 24" (Sheet 1)
LAB
0
DIRECT COST (1975 $1000)
EQUIPMENT/MATERIALS
120
TOTAl_
120
BASIS FOR
(*fl[T F*TIUATF
100 valves 0 $1200 each BUILDING ASSIGNMENT
-
-
neg ASSOCIATED PIPING SYSTEMS
40
20
60
INSTRUMENTATION AND CONTROLS
10
20
30
allowance ELECTRICAL SERVICE
-
none SPARE PARTS
-
6
6 SUBTOTAL
50
166
216 CONTINGENCY
5
17
22
10%
TOTAL DIRECT COSTS
55
183
238 I
(
TOTAL
COS
ESTIMATE
K
SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment Clean Steam to Steam Valves 2-1/2" and Less Than 24" (Sheet 2)
COST (1975 $1000)
ITEM
LABOR
OTN!R
OPERATING LABOR,
SUPERVISION,
3.3
15 min/shift AND OVERHEAD
MAINTENANCE MATERIAL AND
12.0
1% of direct cost of equipment LABOR
CONSUMABLES,
CHEMICALS, AND
-
in item 2 SUPPLIES
UTILITIES AND SERVICES
Waste Disposal Water Steam neg Electricity Building Services Other TOTAL 0 AND H ANNUAL COST
15.3 A
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
K
-a a
U'
1.
2.
3.
4.
S.
TNTAI
DA*f*
- R
r*eT
r*w*a*P
Description of Augment TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
15,000-cfm HEPA Filtration System - Auxiliary Building (Sheet 1)
BASIS FOR
rACT rCTTMATr II Anna flTl
.r..
-
-.
n
.-
L
,
I
r.
I~p~
ERq~
X
rr...L./
n n.
v,
.
.,
.
i-*
1.
PROCESS EQUIPMENT
40.0
45.0
prefilter/HEPA @ $3/cfm, use existing fan BUILDING ASSIGNMENT
7
4.5
11.5
16' x 12' x 12' @ $5/ft3 (nonshielded area)
ASSOCIATED PIPING SYSTEMS
3
2.0
5.0
INSTRUMENTATION AND CONTROLS
in item 1 ELECTRICAL SERVICE
base SPARE PARTS
0.5
0.5 SUBTOTAL
15
47.0
62.0
CONTINGENCY
1
5.0
6.0
10%
TOTAL DIRECT COSTS
16
52.0
68.0
(
(
I ADflD
DIRECT COST (1975 $1000)
£rI"TDUCMT MATrTAI C
5 TfllAI
,o L.
a'
2.
3.
4.
5.
6.
7.
8.
(
K
FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment
15,000-cfm HEPA Filtration System - Turbine Building (Sheet 2)
I AflI
DIRECT COST (1975 $1000)
lI TDMCWNT IMATrOAIC
TflTAL
BASIS FOR
COST ESTIMATE
ITEM
!L___
f
______________
PROCESS EQUIPMENT
5
40.0
45.0
skid mounted filter housing w/o fans BUILDING ASSIGNMENT
4.6
2.3
6.9
16' x 12'
x 12' @ $3/ft3 (nonshielded area)
ASSOCIATED PIPING SYSTEMS
3
2.0
5.0
INSTRUMENTATION AND CONTROLS
in item 1 ELECTRICAL SERVICE
base SPARE PARTS
0
0.5
0.5 SUBTOTAL
12.6
44.8
57.4 CONTINGENCY
2
4.0
6.0
10l TOTAL DIRECT COSTS
14.6
48.8
63.4 T
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASrE TREATMENT SYSTEM
K
-I
1.
2.
3.
4.
5.
6.
7.
a.
!
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment
15,000-cfm HEPA Filtration ITEM
LABOR
System (Sheet 3)
COST (1975 $1000)
OTI4FR
TflTAI
OPERATING LABOR,
SUPERVISION,
3.8
15 min/shift + 40 hr annual test AND OVERHEAD
MAINTENANCE MATERIAL AND
2.2 change every 2 yrs @ $150/filter element LABOR
CONSUMABLES,
CHEMICALS,
AND
in items 2 and 4 SUPPLIES
UTILITIES AND SERVICES
Waste Disposal
0.8
$50/filter element Water Steam Electricity
1.0
additional fan electrical load Building Services Other TOTAL 0 AND M ANNUAL COST
7.8
(
I.
2.
3.I
RACTC Frn rncT FCTIMATC
4.
5.
I_
K
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment
1000-cfm Charcoal/HEPA Filtration System (Sheet 1)
I TEM
LABOR
DIRECT COST (1975 $1000)
EOUIPMENT/MATERIALS
TOTAL
BASIS FOR
COST ESTIMATE
PROCESS EQUIPMENT
2.0
22.0
24.0
prefllter/4" charcoal/HEPA
@ $20/cfm, 5 kw htr @ $400/kw BUILDING ASSIGNMENT
3.8
2.0
5.8
8' x 12'
x 12' @ $5/ft3 (nonshielded area)
ASSOCIATED PIPING SYSTEMS
1.3
.7
2.0
INSTRUMENTATION AND CONTROLS
in item 1 ELECTRICAL SERVICE
1.5
1.0
2.5 SPARE PARTS
0.5
0.5 SUBTOTAL
8.6
26.2
34.8 CONTINGENCY
1.0
2.0
3.0
10%
TOTAL DIRECT COSTS 9.6
28.2
37.8 K
0
I.
2.
3.
4.
5.
6.
7.
8.
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment
1000-cfm Charcoal/HEPA Filtration System (Sheet 2)
COST (1975 $1000)
ITEM
LABOR
OTHER
TOTAL
BASIS FOR COST £STII4ATF
OPERATING LABOR,
SUPERVISION,
1.9
20 min/day + 40 hr annual test AND OVERHEAD
MAINTENANCE 14ATERIAL AND
.6
2 HEPA or prefilters @ $150 each and
1 charcoal @ $900 each every 2 yrs'
CONSUMABLES,
CHEMICALS,
AND
in items 2 and 4 SUPPLIES
UTILITIES AND SERVICES
Waste Disposal
.1
$50/HEPA or prefilter, $100/charcoal Water filter Steam Electricity neg Building Services Other
5.
TOTAL 0 AND M ANNUAL COST
2.6
____________________________
____________
I
I
(
__ (
1.
2.
-
3.
0
--
K
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment
15,OOO-cfm Charcoal/HEPA Filtration System - Auxiliary Building (Sheet 1)
TTVM
1.
PROCESS EQUIPMENT
2.
3.
4.
5.
6.
7.
8.
LABOR
10
DIRECT COST (1975 $1000)
EQUIPMENT/MATERIALS
71 TOTAL
81 BASIS FOR
COST ESTIMATE
prefilter/4" charcoal/HEPA
@ $5/cfm, 30kw htr @ $200/kw BUILDING ASSIGNMENT
12
8
20
16' x 20' x 12' @ $5/ft3 (nonshielded area)
ASSOCIATED PIPING SYSTEMS
3
2
5 INSTRUMENTATION AND CONTROLS
-
In Item 1 ELECTRICAL SERVICE
3
2
5 allowance SPARE PARTS
5
5
4 elements of each type SUBTOTAL
28
88
116 CONTINGENCY
3
9
12
10%
TOTAL DIRECT COSTS
31
97
128 K
a COST ESTIMATE
ITE
LABO.....
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment I TEM
1.
PROCESS EQUIPMENT
2.
3.
4.
5.
6.
7.
8.
15,000-cfm Charcoal/HEPA Filtration System - Turbine Building (Sheet 2)
I fuND
DIRECT COST (1975 $1000)
CN "I lDMrLT
ATEDIlA1 C
ITEM
x flMrnR
1.3 UTflYAI
I_____
ARAL?~urIIn~LJIUL
UIt.IW
BASIS FOR
10.0
71.0
81.0
prefilter/4* charcoal/HEPA
@ $5/cfm, 30 kw htr
@ $200/kw BUILDING ASSIGNMENT
7.7
3.8
11.5
16' x 20' x 121 @ $3/ft3 (nonshielded area)
ASSOCIATED PIPING SYSTEMS
3.0
2.0
5.0
INSTRUMENTATION AND CONTROLS
in item 1 ELECTRICAL SERVICE
3.0
2.0
5.0
allowance SPARE PARTS
5.0
5.0
4 elements each type SUBTOTAL
23.7
83.8
107.5 CONTINGENCY
2.0
9.0
11.0
10%
TOTAL DIRECT COSTS
25.7
92.8
118.5 r
(
0
.rg
(
T*TAi
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREAThENT
SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment
15,O00-cfm Charcoal/HEPA Filtration System (Sheet 3)
COST (1975 $1000)
ITEM
LABOR
OTHER
TOTAL
BASIS FOR COST ESTIMATE
OPERATING LABOR.
SUPERVISION,
3.8
15 min/shift & 40-hr annual test AND OVERHEAD
MAINTENANCE MATERIAL AND
9.0
30 HEPA or prefilters @ $150 each & 15 LABOR
charcoal filters @ $900 each every 2 yrs CONSUMABLES,
CHEMICALS,
AND
in Items 2 and 4 SUPPLIES
UTILITIES AND SERVICES
Waste Disposal
1.5
$S50/HEPA or prefilter, $100/charcoal Water Steam Electricity
1.3
8kw additional fan power for filter aP
Building Services
0.018.S/kw-hr Other TOTAL 0 AND M ANNUAL COST
15.6 K
K
1.
2.
3.
4.
0
5.
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
30.00O-cfm Charcoal/HEPA Filtration System - Auxiliary Building (Sheet 1)
i ARng~
DIRECT COST (1975 $1000)
FoII PI4FNTII4ATFRIALS
-¶
a
1n FnrMN/AEIL
1.
PROCESS EQUIPMENT
15
117.0
TOTAL
132.0
BASIS FOR
COST ESTIMATE
pref1lter/4" charcoal/HEPA
@ $4/cfm, 60-kw htr @ $200/kw BUILDING ASSIGIMENT
20
13.6
33.6
28' x 20' x 12'
$S5/ft3 (nonshielded area)
ASOCIATED PIPING SYSTEMS
5
3.0
8.0
base INSTRUMENTATION AND CONTROLS
-
in item I
ELECTRICAL SERVICE
6
4.0
10.0
allowance SPARE PARTS
5.0
5.0
4 elements each type SUBTOTAL
46
142.6
188.6 CONTINGENCY
5
14.0
19.0
10%
TOTAL DIRECT COSTS
51
156.6
207.6 C
Description of Augment I ITU
a
2.
3.
4.
5.
6.
7.
8.
(
K
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment
30,000-cfm Charcoal/HEPA Filtration System - Turbine Building (Sheet 2)
ITEM
LAROR
DIRECT COST (1975 $1000)
!OtITPHt¶!rT/ATrR TALS
TflTA[
BASIS FOR
t*nlT F*TTMATF
PROCESS EQUIPMENT
15.0
117.0
132.0
prefilter/4" charcoal/HEPA
@ $4/cfm, 60kw htr
@ $200/kw BUILDING ASSIGNMENT
13.4
6.8
20.2
28' x 20' x 12' @ $3/ft3 (nonshielded area)
ASSOCIATED PIPING SYSTEMS
3.0
5.0
8.0
base INSTRUMENTATION AND CONTROLS
in item 1 ELECTRICAL SERVICE
6.0
4.0
10.0
allowance SPARE PARTS
5.0
5.0
4 elements each type SUBTOTAL
37.4
137.8
175.2 CONTINGENCY
4.0
14.0
18.0
l0
TOTAL DIRECT COSTS
41.4
151.8
193.2 y
me
1.
2.
3.
4.
5.
6.
7.
8.
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment
30.00O-cfm Charcoal/HEPA Filtration System - (Sheet 3)
COST (1975 $1000)
ITEM
LABOR
OTHER
TOTAL
BASIS FOR £OST FSTTMATF
OPERATING LABOR,
SUPERVISION,
3.8
15 min/shift + 40 hr annual test AND OVERHEAD
MAINTENANCE MATERIAL AND
18.0
60 HEPA or prefilters @ $150 each & 30
LABOR
charcoal filters @ $900 each every 2 yrs CONSUMABLES,
CHEMICALS,
AND
-
in items 2 and 4 SUPPLIES
UTILITIES AND SERVICES
Waste Disposal
3.0
$50/HEPA or preftilter, $1007charcoal filter Water Steam Electricity
2.6
16kw additional fan HP for filter @
Building Services
0.018 S/ku-hr Other TOTAL 0 AND M ANNUAL COST
27.4
__
C
2.
"
3.
4.
5.
- : -ý:r t- -.-J"
K
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment ITEM
1.
PROCESS EQUIPMENT
2.
BUILDING ASSIG*
3.
4.
5.
6.
7.
8.
Turbine Building Chilled Water HVAC System (Sheet 1)
- IENT
LABOR
300
DIRECT COST (1975 $1000)
EOUJIPMFNTIMATFRIALS
TnIMNIAEIL
1 nA
500
TflTAI
800
BASIS FOR
rnCT CTMATC
500-ton capacity, w/o air filters
-t
+
I
Coolers can be Installed in existing space saved by deletion of ducting.
ASSOCIATED PIPING SYSTEM;
-
in item 1 INSTRUMENTATION AND CONTROLS
-
in item 1 ELECTRICAL SERVICE
40
so
90
SPARE PARTS
-
8
8
1% item 1 SUBTOTAL
340
558
898 CONTINGENCY
34
56
90
10l TOTAL DIRECT COSTS
374
614
988 K
11
0
-J
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
SYSTE14 FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment Turbine Building Chilled Water HVAC System (Sheet 2)
COST (1975 $1000)
ITEM
LABOR
OTHER
TOTAL
BASIS FOR COST ESTIMATE
OPERATING LABOR, SUPERVISION,
3.3
15 min/shift AND OVERHEAD
MAINTENANCE MATERIAL AND
20.0
2-1/2% of equipment costs LABOR
CONSUMABLES, CHEMICALS,
AND
-
initem 2 SUPPLIES
UTILITIES AND SERVICES
Waste Disposal Water
13.0
500 gpm @ 104/1000 gal & 50% load factor Steam Electricity
33.0
400 kw @ 0.018 $/kw hr Building Services Other TOTAL 0 AND M ANNUAL COST
69.3 C
r I.
2.
3.
4.
.0
0
S.
C
K
Description of Augment K
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT. SYSTEM
FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
600-ft 3 Waste Gas Decay Tank' (Sheet 1)
I TFM
LABOR
DIRECT COST (1975 $1000)
EOUIPMENT/MATERIALS
TOTAL
BASIS FOR
COST ESTIMATE
PROCESS EQUIPMENT
2.5
20
22.5
600-ft 3, 150 pslgo C.S.,
ASME VIII
BUILDING ASSIGNMENT
18.0
9
27.0
15' x 15' x 20' @ S6/ft 3 (shielded area)
ASSOCIATED PIPING SYSTEMS
1.0
1
2.0
10% of item 1 INSTRUMENTATION AND CONTROLS
neg ELECTRICAL SERVICE
neg SPARE PARTS
neg SUBTOTAL
21.5
30
51.5 CONTINGENCY
2.0
3
5.0
10%
TOTAL DIRECT COSTS
23.5
33
56.5 K
I
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment
600-ft 3 Waste Gas Decay ITEM
LABOR
Tank (Sheet 2)
COST (1975 $1000)
OTHER
TOTAL
OPERATING LABOR,
SUPERVISION,
AND OVERHEAD
neg MAINTENANCE MATERIAL AND
LABOR
neg CONSUMABLES,
CHEMICALS,
AND
SUPPLIES
neg UTILITIES AND SERVICES
Waste Disposal Water Steam neg Electricity Building Services Other TOTAL 0 AND N ANNUAL COST
neg I.
2.
3.
4.
RA;T* FflR i*lT r*T1MATr
0
U'
0~e
5.
(
K
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
Description of Augment IT"M
1.
PROCESS EQUIPMENT
2.
3.
4.
5.
6.
7.
8.
FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
PWR Hydrogen Recombiner (Sheet 1)
IARno
50.0
DIRECT COST (1975 $1000)
rflIITPMPINIMAT*R TAI
TflTAI
I
l
- fTI
b V
nA. I
300.0
350.0
BASIS FOR
rnqT vtTTMATF
skid mounted, catalytic type w/condenser, partial I&C
single unit, ASME VIII
BUILDING ASSIGNM4ENT
28.8
14.4
43.2
15' x 30' x 16' 0 $6/ft3 (shielded area)
ASSOCIATED PIPING SYSTEMS
32.0
13.0
45.0
allowance INSTRUMENTATION AND CONTROLS
10.0
40.0
50.0
allowance ELECTRICAL SERVICE
13.0
12.0
25.0
allowance SPARE PARTS
-
2.0
2.0
SUBTOTAL
133.8
381.4
515.2 CONTINGENCY
13.0
38.0
51.0
101 TOTAL DIRECT COSTS
146.8
419.4
566.2 K
a Ue
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADtWASTE TREAThENT
SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment PUR Hydrogen Recombiner (Sheet 2)
COST (1975 $1000)
ITEM
LABOR
OTHER
TOTAL
BASIS FOR COST ESTIMATE
OPERATING LABOR,
SUPERVISION,
3.3
15 min/shift AND OVERHEAD
MAINTENANCEMATERIAL AND.
10.0
3% of equipment cost LABOR
CONSUMABLES,
CHEMICALS,
AND
1.0
oxygen @.S2.5/103 cf & .25 cfm 0
SUPPLIES
7000 hrs UTILITIES AND SERVICES
Waste Disposal Water Steam neg Electricity Building Services Other TOTAL 0 AND M ANNUAL COST
14.3
1.
2.
3.
4.
Ca I
U'
S.
K
C
K*
Description of Augment ITEM
1.
PROCESS EQUIPMENT
2.
3.
4.
5.
6.
7.
8.
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
PWR Air EJector Charcoal/HEPA Filtration Unit (Sheet 1)
LABOR
3.0
DIRECT COST (1975 $1000)
EOUIPMENT/MATERIALS
7.5 TOTAL
10.5
1*
BASIS FOR
COST ESTIMATE
chiller, heater, charcoal HEPA
BUILDING ASSIGNMENT
3.0
1.5
4.5
10' x 10' x 15' @ $3/ft3 (unshielded turbine bldg)
ASSOCIATED PIPING SYSTEMS
2.0
1.0
3.0
allowance INSTRUMENTATION AND CONTROLS
0.5
1.5
2.0
allowance ELECTRICAL SERVICE
0.5
0.5
1.0
allowance SPARE PARTS
1.0
1.0
SUBTOTAL
9.0
13.0
22.0
CONTINGENCY
1.0
1.0
2.0
1O0
TOTAL DIRECT COSTS
10.0
14.0
24.0
L*a
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augnent PWR Air EJector Charcoal/HEPA Filtration Unit (Sheet 2)
COST (1975 $1000)
ITEM
LARAR
___
.....________________
I *
,
L
ueA5 rwK Guil r.4IrMIE
OPERATING LABOR,
SUPERVISION,
3.8
15 min/shift + 40 hr annual test AND OVERHEAD
MAINTENANCE MATERIAL AND
2.0
includes replacement filter LABOR
CONSUMABLES,
CHEMICALS,
AND
-
in item 2 SUPPLIES
UTILITIES AND SERViCES
Waste Disposal neg Water Steam Electricity Building Services Other TOTAL 0 AND M ANNUAL COST
5.8 flTIFD
TnTAI
l.
2.
3.
4.
U'
5.
K
DAete
rP*eUA*
K
K
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment ITEM
Steam Generator Flash LABOR
Tank Vent to Main Condenser (Sheet DIRECT COST (1975 $1000)
EQUIPMENT/MATERIALS
1)
TOTAL
BASIS FOR
COST ESTIMATE
PROCESS EQUIPMENT
-
no equipment required BUILDING ASSIGNMENT
neg install In existing space ASSOCIATED PIPING SYSTEMS
13
7
20
200 ft of 10-in pipe with
2 valves INSTRUMENTATION AND CONTROLS
4
6
10
allowance ELECTRICAL SERVICE
neg SPARE PARTS
neg SUBTOTAL
17,,
13
30
CONTINGENCY
2
1
3
10%
TOTAL DIRECT COSTS
19
14
33 I.
U't ull
2.
3.
4.
5.
6.
7.
8.
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREAThENT
SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment Steam.Generator Flash Tank Vent to Main Condenser (Sheet 2)
COST (1975 $1000)
ITEM
LABOR
OTHER
TOTAL
BASIS FOR COST ESTIMATE
OPERATING LABOR,
SUPERVISION,
1 allowance AND OVERHEAD
MAINTENANCE MATERIAL AND
1
2% Total Direct Cost LABOR
CONSUHABLES,
CHEMICALS,
AND
neg SUPPLIES
UTILITIES AND SERVICES
Waste Disposal Water neg Steam Electricity Building Services Other TOTAL 0 AND H ANNUAL COST
2
1.
2.
3.
4.
.a U'
5.
(
(
K
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment lSqpm Evaporator (Sheet 1)
I AnRO
DIRECT COST (1975 $1000)
PROCESS EQUIPMENT
30
225
255 skid mounted, submerged tube bundle, ASME VIII, Incoloy in contact with process fluid BASIS FOR
2.
BUILDING ASSIGNMENT
68
34
102 evap & services 25' x 301 x 20'
@ $6/ft3 plus 2,000 ft3 increase in solid waste storage area ASSOCIATED PIPING SYSTEMS
35
30
65 inludes service piping INSTRUMENTATION AND CONTROLS
10
10
20
allowance ELECTRICAL SERVICE
40
25
65 allowance SPARE PARTS
-
27
27
2% of item 1 plus tube bundle SUBTOTAL
183
351
534 CONTINGENCY
18
35
53
10%
TOTAL DIRECT COSTS
201
386
587 ITI'N
1.
a.
3.
4.
5.
6.
7.
8.
T*TA!
Description of Augment tTrW
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREAThENT'SYSTEM
FOR LIGHT-WdATER-COOLED NUCLEAR REACTORS
30-gpm Evaporator (Sheet 2)
,
BASIS FOR
rncT rCY?UAYT
- .-
-..rw-f
.dV..r b.r
...
I
u snlrl.#
,nI
.
bl r~l) I lruI
1.
PROCESS EQUIPMENT
2.
BUILDING ASSIGNMgNT
30
t
88
350
44
380
132 ASME VIII
skid mounted, submerged,
'tube bundle, Incoloy in contact with process fluid evap + services - 25' x 40' x 20'
@ $6/ft3 plus 2,000 ft 3 Increase In solid waste storage area ASSOCIATED PIPING SYSTEMS
35
35
70
includes service piping INSTRUMENTATION AND CONTROLS
10
10
20
allowance ELECTRICAL SERVICE
40
25
65 allowance SPARE PARTS
27
27
2% of Item 1 plus tube bundle SUBTOTAL
203
491
694 CONTINGENCY
20
49
69
1O0
TOTAL DIRECT COSTS
223
540
763 C
C
I AfPtflD
DIRECT COST (1975 $1000)
rfIITDfMlrTIMATrDTAI
TnTA,
CO
3.
4.
5.
6.
7.
8.
K
FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment
50-qpm Evaporator (Sheet 3)
ITEM
1.
PROCESS EQUIPMENT
2.
3.
4.
S.
6.
7.
8.
LABOR
30
DIRECT COST (1975 $1000)
EOUIPMENT/MATERIALS
450
TOTAL
480
BASIS FOR
COST ESTIMATE
ASME VIII
skid mounted, submerged, tube bundle, Incoloy In contact with process fluid BUILDING ASSIGNMENT
97
48
145
10% more than 30 gpm ASSOCIATED PIPING SYSTEMS
35
35
70
allowance INSTRUMENTATION AND CONTROLS
10
10
20
allowance ELECTRICAL SERVICE
40
25
65 allowance SPARE PARTS.
27
27
2% of Item 1 plus tube bundle SUBTOTAL
212
595
807 CONTINGENCY
21
60
81
10%
TOTAL- DIRECT COSTS
233
655
888 T
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMErNT SYSTEM
'III
a
- 0
Description of Augment
50-gpm Evaporator (Sheet
3)
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment FuannAtnY
-
RUR Dirty Ua~tm
-
Finn, fl,.n1,,
(k..t £1 COST (1975 $1000)
ITEM
LABOR
OT14ER
TOTAL
BASIS FOR LOST FSTIMATF
OPERATING LABOR, SUPERVISION,
12
2.6 x 106 gpy; 1000 hrs/yr labor AND OVERHEAD
MAINTENANCE MATERIAL AND
30
7-1/2% of equipment cost LABOR
CONSUMABLES,
CHEMICALS,
AND
neg concentrate solidification chemicats SUPPLIES
in item 4 UTILITIES AND SERVICES
Waste Disposal
70
100:1 feed to concentrate ratio @ 20/ft 3 disposal cost Water
27
1000 gpm @ 1500 hrs @ 30t/1000 gal Steam
60
1500 hrs steaw @ 20,000 lb/hr @ $2/1000 lbs Electricity Building Services Other TOTAL 0 AND M ANNUAL COST
199 C
C
1.
2.
3.
4.
5.
K*
SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment Evaporator PWR Dirty lT YM
[AROR
Waste (Sheet 5)
COST (1975 $1000)
OTHER
TOTAL
BASIS FOR COST ESTTMATE
OPERATING LABOR, SUPERVISION,
AND OVERHEAD
6.0
500,000 gpy; 500 hrs/yr labor MAINTENANCE MATERIAL AND
LABOR
30.0
7-1/2% of equipment cost CONSUMABLES, CHEMICALS, AND
-
concentrate solidification chemicals SUPPLIES
in item 4 UTILITIES AND SERVICES
50:1 feed to concentrate ratio @ $20/ft 3 Waste Disposal
27.0
disposal cost Water
5.0
1000 gpm @.277 hrs @ 30t/1000 gal Steam
12.0
277 hrs steam @S
20,000 4bs/hr @ $2/1000 lbs Electricity Building Services Other TOTAL 0 AND
M ANNUAL COST
80.0
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
K
I.
2.
3.
4.
0'
5.
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment EvaDorator
- Condenser Polisher Chemical IaCto Ih
+0 A
COST (1975 $1000)
ITEM
.,*
FR CS
UK LU
ETIMATE
OPERATING LABOR,
SUPERVISION,
AND OVERHEAD
6.0
650.000 gpy; 500 hr/yr labor MAINTENANCE MATERIAL AND
LABOR
30.0
7-1/2% of equipment cost CONSUMABLES, CHEMICALS. AND
concentrate solidification chemicals SUPPLIES
In item 4 UTILITIES AND SERVICES
Waste Disposal
87.0
20:1 feed to concentrate ratio @ $20/ft 3 Wl7.0
disposal cost Water
6.5
1000 gpm 0 360 hrs @ 30/10OO gal Steam
14.4
360 hrs steam @ 20,000 lb/hr @ $2/1000 lbs Electricity Building Services Other LABOR
0ATD
TC4TAI
TOTAL 0 AND M ANNUAL COST
143.9 C
0
1.
2.
3.
4.
5.
(
v LAI*R
NTH*D
T*TAI
K
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
OPERATING LABOR,
SUPERVISION,
AND OVERHEAD
6.0
160,000 gpy; 500 hrs/yr MAINTENANCE MATERIAL AND
LABOR
30.0
7-1/25 of equipment cost CONSUMABLES, CHEMICALS,
AND
-
concentrate solidification chemicals In SUPPLIES
item 4 UTILITIES AND SERVICES
Waste ITsposal
8.6
50:1 feed to concentrate ratio 0 $20/ft3 disposal cost Water
1.6
1000 gpm 0 90 hrs 0 30t/1000 gal Steam
3.6
90 hrs steam 0 20,000 lb/hr 1 $2/1000 lbs Electricity Building Services Other TOTAL 0 AND M ANNUAL COST
49.8 ANNUAL OPERATING AND MAI[NTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
K
I.
2.
3.
4.
ad a,
LeD
5.
Description of Augment TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Evaporator Distillate Demineralizer (Sheet 1)
TTIrM
I anAD
DIRECT COST (1975 $1000)
EniI nlrT
IUA?~nAi e
- ,-.
I.rluvn Iuu~rnllu~r'¶l KhMiLR
IJI/L
W,5MII
EIHMAIT
PROCESS EQUIPMENT
4.0
20.0
24.0
30 ft 3 , SS. ASME VIII, 150 psi nonregenerative, w/resin BUILDING ASSIGNMENT
6.4
3.2
9.6
10' x 10' x 16' @ $6/ft3 (shielded area)
ASSOCIATED PIPING SYSTEMS
9.0
6.0
15.0
2" piping INSTRUMENTATION AND CONTROLS
2.0
3.0
5.0
remote conductivity readout ELECTRICAL SERVICE
neg SPARE PARTS
1.0
1.0
SUBTOTAL
21.4
33.2
54.6 CONTINGENCY
2.0
3.0
5.0
10%
TOTAL DIRECT COSTS
23.4
36.2
59.6 BASIS FOR
C
(
1.
2.
i Ot
3.
4.
5.
6.
7.
8.
(
qrft*IrA I
)
K
SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment Evaporator Distillate Demineralizer (Sheet 2)
COST (1975 $1000)
YtM
I ARnlQ
OTHER
TOTAL
BASIS FOR COST ESTIMATE
aI1II
____________
OPERATING LABOR, SUPERVISION.
1.8
1500 hrs operation @ 10% attendance AND OVERHEAD
MAINTENANCE MATERIAL AND
LABOR
2.0
allowance CONSUMABLES,
CHEMICALS,
AND
SUPPLIES
2.3
1 change per yr @ $75/ft3 UTILITIES AND SERVICES
Waste Disposal
0.6
30 ft 3 @ $20/ft 3 disposal cost Water Steam Electricity Building Services Other TOTAL 0 AND M ANNUAL COST
6.7 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
I.
2.
3.
4.
,ap
5.
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment
50-opDemintralzer Sh t 1)
ITEM
LAROR
DIRECT COST (1975 $1000)
1ITOM
AUIFRAI It TIhTAI
BASIS FOR
CflCY
1T tMAr"
PROCESS EQUIP4ENT
5
20.0
25.0
30 ft 3.
SS, A*NE VIII. 150 psi, nonreganerative, with resin BUILDING ASSIGNMENT
9
4.8
13.8
12' x 12' x 16' 0 $6/ft3 (shielded ar*)
ASSOCIATED PIPING SYSTEMS
9
6.0
15.0
2" piping INSTRUMENTATION AND CONTROLS
4
6.0
10.0
ELECTRICAL SERVICE
No SPARE PARTS
2.0
2.0
miscellaneous supplies SUBTOTAL
27
38.8
66.8 CONTINGENCY
2
4.0
6.0
10%
TOTAL DIRECT COSTS
29
42.8
-
71.8 C
1.
2.
3.
4.
5.
6.
7.
8.
(
C
SO-gin
.D*l.n.fraltzer {Sheet 1)
K
Description of Augment K
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
1O0-9pm Deminerallizer (Sheet 2)
tT*M
LANOR
DIRECT COST (1975 $1000)
FO*l PMFNT/MATFRTALS
TOTAL
BASIS FOR
COST FSTTMATF
PROCESS EQUIPMENT
5
35.0
40.0
60 ft 3 , SS, ASME VIII, 150 psi, nonregenerative, with resin BUILDING ASSIGNMENT
9
4.8
13.8
12' x 12' x 16' 0 $6/ft3 (shielded area)
ASSOCIATED PIPING SYSTEMS
10
10.0
20.0
2-1/21 piping INSTRUMENTATION AND CONTROLS
4
6.0
10.0
ELECTRICAL SERVICE
neg SPARE PARTS
2.0
2.0
miscellaneous supplies SUBTOTAL
28
57.8
85.8 CONTINGENCY
3
6.0
9.0
TOTAL DIRECT COSTS
31
63.8
94.8 I.
2.
3."
4.
5.
a,
.1
6.
7.
B.
TOTAL DIRECT COST ESTIMATE SHEET OF RADWAST!E TREATMENT SYSTEM
FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment
20-plDmneralizer(Sheet 3)__
ITEM
1.
PROCESS EQUIPMENT
2.
3.
4.
5.
6.
7.
8.
LABOR
5
1T
A
DIRECT COST (1975 $1000)
EflUIPI4FNTII4ATFRTAL *
60.0
TflTAI
65.0
BASIS FOR
rnCT r~tTuATr
120 ft3 , SS, ASME VIII, i50 psi, nonregenerative, with resin BUILDING ASSIGNMENT
11
5.2
16.2
13' x 13' x 16' 0 $6/ft 3
___(shielded area)
ASSOCIATED PIPING SYSTEMS
12
12.0
24.0
4" piping INSTRUMENTATION AND CONTROLS
4
6.0
10.0
ELECTRICAL SERVICE
neg SPARE PARTS
2.0
2.0
miscellaneous supplies SUBTOTAL
32
85.2
117.2 CONTINGENCY
3
9.0
12.0
TOTAL DIRECT COSTS
35
94.2
129.2
(
(
200-gpm Oemtneraltzer (Sheet 3)
K
Description of Augment
400-gpm Demineralizer
- Steam Generator Blowdown Service (Sheet 4)
I TrM
1.
PROCESS EQUIPMENT
2.
3.
4.
5.
6.
7.
8.
lAROR
DIRECT COST (1975 $1000)
EOUJIPMNT/MATERjALS
TOTAL
BASIS FOR
COST ESTIMATE
T
I
COST ESTIMATE
5
60.0
65.0
150 psi, nonregenerative. with resin BUILDING ASSIGNMENT
11
5.2
16.2
,3'
x 13' x 16' @ $6/ft3 (shielded area)
ASSOCIATED PIPING SYSTEMS
20
20.0
40.0
6" piping INSTRUMENTATION AND CONTROLS
4
6.0
10.0
allowance ELECTRICAL SERVICE
neg SPARE PARTS
2.0
2.0
miscellaneous supplies SUBTOTAL
40
93.2
133.2 CONTINGENCY
4
9.0
13.0
TOTAL DIRECT COSTS
44
102.2
146.2 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
a,
'a
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment BWR
- 2nd Waste Demineralizer In Serf es (Sheet El COST (1975 $1000)
ITEM
_...._-_....__,,__
,v-n
-
DROIO rvr uK
EV)lr.1 ~PY.I
OPERATING LABOR,
SUPERVISION,
3.3
15 min/shift AND OVERHEAD
MAINTENANCE MATERIAL AND
LABOR
5.0
allowance CONSUMABLES,
CHEMICALS, AND
9.0
1 change per year @ 120 ft 3 0 $75/ft 3 (one SUPPLIES
vessel change per year. regardless of size)
UTILITIES AND SERVICES
Waste Disposal
2.4
120 ft 3lyr * $20/ft3 disposal cost Water Steam Electricity Building Services Other TOTAL 0 AND M ANNUAL COST
19.7
1.
2.
3.
4.
a
-.J
a
5.
C
lABOR
NTNrD
TJlTA!
aAeT*
- n*
PP*guA*P
K
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment Demineralizer - PWR Clean Wastes (Sheet 6)
COST (197k. $1000)
YY
IPLu I am*o flTurD
?linI
matie fflS EflM? rCTTMATe AILr IlV%
-
lll_
__
_
Ifl,
&'flC
I
l nV
bl
- fll OPERATING LABOR, SUPERVISION,
1.8
10% of DRS shim bleed (50,000 gpy),
AND OVERHEAD
30 min/day MAINTENANCE MATERIAL AND
LABOR
5.0
allowance CONSUMABLES,
CHEMICALS,
AND
3
3 SUPPLIES
2.3
30 ft /yr @ $75/ft3 UTILITIES AND SERVICES
Waste Disposal
0.6
30 ft 3/yr @ $20/ft3 disposal cost Water Steam Electricity Building Services Other TOTAL 0 AND M ANNUAL COST
9.7 I
1.
2.
3.
4.
a S.
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADIASTE TREATMENT
SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment Demineralizer - BWR Dirty Waste (Sheet 7)
COST (1975 $1000)
JTFN
[ABDR
nlTHVg TNlT61 DACIC
mnD r.ncT reTvUnt OPERATING LABOR, SUPERVISION,
AND OVERHEAD
6.5
2.6 x 106 gpy, 30 min/shift MAINTENANCE MATERIAL AND
LABOR
5.0
allowance CONSUNABLES,
CHEMICALS, AND33 SUPALES
64.5
860 ft 3 resin 0 $75/ft 3 UTILITIES AND SERVICES
Waste Disposal
17.2
860 ft 3 @ $20/ft 3 disposal cost Water Steam Electricity Building Services Other TOTAL 0 AND N ANNUAL COST
93.2 C
I.
2.
3.
4.
N
S.
--- I
C
K
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment Demineraltzer - PWR Dirty. Wastes (w/o turbine building) (Sheet 8)
COST (1975 $1000)
ITEM
LABOR
OTHER
TOTAL
BASIS FOR COST ESTIMATE
OPERATING LABOR,
SUPERVISION,
AND OVERHEAD
3.3
500,000 gpy; 15 min/shift MAINTENANCE MATERIAL AND
LABOR
5.0
allowance CONSUMABLES,
CHEMICALS,
AND
SUPPLIES
12.0
160 ft 3 /yr @ $75/ft 3 UTILITIES AND SERVICES
Waste Disposal
3.2
160 ft 3/yr @ $20/ft 3 disposal cost water Steam Electricity Building Services Other TOTAL 0 AND M ANNUAL COST
23.5 l.
2.
3.
4.
a
5.
/
ANNUAL OPERATIN
AND MAINTE*ANCE COST ESTIMTE SHEET OF RADWASTE TREATMENT
D*crlrintinn of Aujnmant flminapA147AP
.
DUo
- 7m,
- ,*,-*
pww- ITEM
T.
-
a
.
C1
- fm w,*g uu,,*U-I
r uVfm
"a
1.411W4b
7I
COST (1975 $1000)
--
______
....
..-.
",,'
,,,.
urwl, rvuK I.UF)I LtIY:llrl OPERATING LABOR,
SUPERVISION.
AND OVERHEAD
13.1
1 hr/shift, 2.6 x 106 opy MAINTENANCE MATERIAL AND
LABOR
5.0
allowance CONSUMABLES,
CHEMICALS, AND
SUPPLIES
64.5
660 ft 3 resin 0 $75/ft3 UTILITIES AND SERVICES
Waste Disposal
17.2
860 ft 3/yr 9 $20/ft 3 disposal cost Water Steam Electricity Building Services Other TOTAL 0 AND N ANNUAL COST
99.8 I ARMR
flTIIFA
1.
2.
3.
4.
a S.
(
r SYSTEM FOR L.IGHT, oWATER-COOLEO NUCL..EAR,, REACTORS
Ti*TAI
oAeTe
- Ae*
rPgvu4*
-1-:j:.1i-:i...-
..........
-."(
K
Description of Augment Demineralizer - PIER
tim Steam Generator Blowdomn (Sheet 10)
COST (1975 $1000)
nyu,..O
inaI
OPERATING LABOR, SUPERVISION.
AND OVERHEAD
3.3
15 min/shift MAINTENANCE MATERIAL AND
LABOR
5.0
allowance CONSUMABLES, CHEMICALS, AN"
SUPPLIES
16.9
225 ft 3 resin/yr @ $75/ft3 UTILITIES AND SERVICES
Waste Disposal
4.5
225 ft 3/Yr I $20/ft 3 disposal cost Water Stem Electricity Building Services Other TOTAL 0 AND M ANNUAL COST
29.7 A..UAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
2.
3.
4.
ma*tt ens rtnt ReTtMAta a
I alLfl9 S.
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment
20-qp Cartridge Filter (Sheet 1)
TTFM
I AI*fl2 DIRECT COST (1975 $1000)
vN Itur
¶
u'IIAqr rD lr e
...
t.J
~vrl.rnl r.lL*nL
UIhLU
11MAT
PROCESS EQUIPMENT
2.0
5.0
7.0
SS, ASME VIII, 150 psi BUILDING ASSIGNMENT
5.6
3.0
8.6
16' x 12' x 20' S $6/ft 3 (shielded area)
ASSOCIATED PIPING SYSTEMS
1.5'
1.0
2.5 allowance INSTRUMENTATION AND CONTROLS
0.6
2.4
3.0
allowance ELECTRICAL SERVICE
neg SPARE PARTS
0.5
0.5 SUBTOTAL
9.7
11.9
21.6 CONTINGENCY
1.0
1.0
2.0
10%
TOTAL DIRECT COSTS
10.7
12.9
23.6 BASIS FOR
-. 4 Q
at
1.
2.
3.
4.
5.
6.
7.
8.
(
20-qm Cartrtd9e Ftlter (Sheet 1)
T*Ai
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment Cartridge Filter (Sheet 2)
COST (1975 $1000)
A'1JCDl RAM!S FOR COST ESTIMATE
ITEM
LADUK
uini n
,
-...
.
.....
....
...
..
OPERATING LABOR. SUPERVISION,
4.5
10 changes @ 10 man-hrs/change AND OVERHEAD
@ $12/hr + 15 min/shift MAINTENANCE MATERIAL AND
LABOR
1.0
allowance CONSUMABLES. CHEMICALS, AND
SUPPLIES
1.0
10 changes/yr @ $100/change UTILITIES AND SERVICES
Waste Disposal
1.5
10 drums/yr @ $20/ft 3 Water Steam Electricity Building Services Other TOTAL 0 AND M ANNUAL COST
8.0
1.
2.
3.
4.
5.
T*TAI
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREAT1ENT SYSTEM
FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment
100-gpim Precoat Filter (Shoot 1)
ITEM
LARnR
DIRECT COST (1975 $1000)
fIW01T
P~NT uI~dTIDTAI
PROCESS EQUIPMENT
10
65.0
75 automated system 1 gpm/ft 2 ,
ASM4E VIII
BUILDING ASSIGNMENT
18
9.0
27
15' x 15' x 20' 0 $6/ft3 (shielded area)
ASSOCIATED PIPING SYSTEM4S
16
9.0
25
35% of equipment cost INSTRUMENTATION AND CONTROLS
in item 1 ELECTRICAL SERVICE
7
13.0
20
allowance SPARE PARTS
2.0
2
2% of item 1 SUBTOTAL
51
98.0
149 CONTINGENCY
5
10.0
15
10%
TOTAL DIRECT COSTS
56
108.0
164 BASIS FOR
0
1.
2.
3.
4.
5.
6.
7.
8.
(
r i
lO0-gpm Precoat Ftlter (Sheet 1)
T*TAI
K
FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment
400-oam Precoat Filter T T*M
LAROR
DIRECT COST (1975 $1000)
EOUIPMENT/MATERIALS
TOTAL
BASIS FOR
COST ESTIMATE
PROCESS EQUIPMENT
35
135.0
170
automated system; 1 gpm/ft 2 ASME Viii BUILDING ASSIGNMENT
24
12.0
36
15' x 20' x 20' @ $6/ft3 (shielded area)
ASSOCIATED PIPING SYSTEMS
31
16.0
47
35% of equipment cost INSTRUMENTATION AND CONTROLS
-
-
item I
ELECTRICAL SERVICE
12
18.0
30
allowance SPARE PARTS
-
3.0
3 SUBTOTAL
102
184.0
286 CONTINGENCY
10
18.0
28
10%
TOTAL DIRECT COSTS
112
202.0
314 TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
K
(Sheet 2)
-J
1.
2.
3.
4.
5.
6.
7.
8.
(Sheet
2)
-vT
[
ANNUAL OPERATING AND MAINTENANCE COST ESTI1ATE SHEET OF RADWASTE TREATMENT
SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment Precoat Filter - BWR Dirty Waste (Sheet 3)
COST (1975 $1000)
ITEM
LABOR
OTHER
TOTAL
BASIS FOR COST !STTI4ATF
OPERATING LABOR,
SUPERVISION,
AND OVERHEAD
6.6
2 x 106 gpy, 30 min/shift MAINTENANCE MATERIAL AND
LABOR
10.0
allowance CONSUMABLES,
CHEMICALS,
AND
6.0
10 lbs precoat @ lOt/lb per 1000 gal SUPPLIES
processed
4.
UTILITIES AND SERVICES
Waste Disposal Water Steam Electricity Building Services Other
40.0
TOTAL 0 AND M ANNUAL COST
j[
62.6
1 ft 3/sludge per disposal cost
1000 qal processed @ $30/ft 3 C
1.
2.
3.
S.
(
T
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
FOR LIGHT-WATER-COOLED
NUCLEAR REACTORS
Description of Augment
2-com Reverse TTIFM
LABOR
DIRECT COST (1975 $1000)
FOUlPMENTIMATFRIALS
TOTAL
BASIS FOR
COST ESTIMATF
PROCESS EQUIPIENT
6.0
60.0
66.0
feed tank, ASME VIII
BUILDING ASSIGNMENT
19.2
9.6
28.8
12' x 25' x 16' @ $6/ft3 ASSOCIATED PIPING SYSTEMS
3.0
2.0
5.0
allowance INSTRUMENTATION AND CONTROLS
in item I
ELECTRICAL SERVICE
7.0
13.0
20.0
allowance SPARE PARTS
6.0
6.0
SUBTOTAL
35.2
90.6
125.8 CONTINGENCY
3.0
9.0
12.0
10%
TOTAL DIRECT COSTS
38.2
99.6
137.8 K
0
1.
2.
3.
4.
5.
6.
7.
8.
Osmosis (Sheet 1)
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment Reverse Osmosis - Detergent Wastes COST (1975 $1000)
ITEM
LABOR
OTHER
TOTAL
BASIS FOR COST ESTIMATE
OPERATING LABOR, SUPERVISION,
AND OVERHEAD
3.1
160.000 gpy, 1300 hrs/yr @ 20% attendance MAINTENANCE MATERIAL AND
8.8
4% less bldg + 24 module with 3-yr life LABOR
@ $600 each CONSUMABLES,
CHEMICALS.
AND
SUPPLIES
neg UTILITIES AND SERVICES
Waste Disposal
4.3
100:1 vol reduction @ $20/ft 3 disposal cost Water Steam Electricity neg Building Services Other TOTAL 0 AND M ANNUAL COST
16.2 r
C
1.
2.
3.
4.
No
5.
(
FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment
1O,000-Gallon Tank__(Sheet 1)
?tTrM
1.
PROCESS EQUIPMENT
2.
3.
4.
5.
6.
7.
8.
I AROR
3 DIRECT COST (1975 $1000)
!0IJ!P?4fNT/MATERIALS
TOTAL
T -
28
31 BASIS FOR
COST ESTIMATE
SS, ASME VIII, atmospheric service, 200°F
BUILDING ASSIGNMENT
30
15
45
15' x 20' x 25' @ $6/ft3 (shielded area)
ASSOCIATED PIPING SYSTEMS
2
1
3
10% of item 1 INSTRUMENTATION AND CONTROLS
4
6
10
allowance ELECTRICAL SERVICE
neg SPARE PARTS
neg SUBTOTAL
39 s0
89 CONTINGENCY
4
5
9
10%
TOTAL DIRECT COSTS
43
55
98 C
w
10tOOO-GallonTapk (Sheet
1)
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREAThENT
SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment
10000-Gallon Tank (Sheet 2)
COST (1975 $1000)
ITEM
LABOR
OTHER
TOTAL
RA~l flD rfl*T r*TUATr OPERATING LABOR, SUPERVISION.
AND OVERHEAD
1.1
5 min/shift - log level readings MAINTENANCE MATERIAL AND
LABOR
1.6
1/2% of equipment CONSUMABLES. CHEMICALS,
AND
neg SUPPLIES
UTILITIES AND SERVICES
Waste Disposal Water Steam neg Electricity Building Services Other TOTAL 0 AND N ANNUAL COST
2.7
1.
2.
3.
4.
5.
(
REFERENCES TO APPENDIX B
1.
"Guide for Economic Evaluation of Nuclear Reactor Plant Oesigns," USAEC Report NUS-531, NUS Corporation, January 1969.
2.
"Wage Rates for Key Construction Trades," Engineering News Record, pp. 36-37, January 2, 1975.
3.
"Projections of Labor Requirements for Electric Power Plants Construction, 1974 - 2000,"
USAEC Report WASH-1334, Washington, D.C., August 1974.
1.110-85
APPENDIX C
DATA NEEDED FOR RADIIASTE TREATMENT SYSTEM
COST-BENEFIT ANALYSIS FOR LIGHT-WATER
COOLED NUCLEAR REACTORS
This appendix describes information that should be submitted in support of radwaste treat ment system cost-benefit analyses for light-water-cooled nuclear reactors.
The information should be consistent with the contents of the Safety Analysis Report (SAR) and Environmental Report (ER) for the proposed reactor.
Appropriate sections of the SAR and ER containing more detailed discussions of the required information should be referenced as appropriate.
Each response, however, should be Independent of the ER and SAR.
All responses should be on a per reactor basis and should provide the following information:
1.
Detailed cost estimate sheets similar to those shown on the following pages listing all parameters (and their bases) used in determining capital, operating, and maintenance costs associated with all augments considered in the cost-benefit analysis.
All costs should be stated in terms of 1975 dollars.
2.
The cost of borrowed money used in the cost analysis and the method of arriving at this cost.
3.
If methods and parameters used in the cost-benefit analysis are different from those aiven in this guide, describe the methods used in detail and provide bases for all parameters.
Include the following information:
a.
Decontamination factors assigned to each augment and fraction of "on-line" time assumed, i.e., hours per year used.
b.
Parameters and method used to determine the Indirect Cost Factor and the Capital Recovery Factor.
1.110-87
TOTAL DIRECT COST ESTIMATE SHEET OF RADWASTE'TREATMENT-SYSTEH
FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
Description of Augment i Tru
1 AflfD
DIRECT COST (1975 $1000)
FflIIIPMFNT/MATFRlALS
1.
PROCESS EQUIPMENT
2.
BUILDING ASSIGNMENT
t I
1 I
I
I
I
I
ASSOCIATED PIPING SYSTEMS
BASIS FOR
COST ESTIMATE
I
I
I
I
--
INSTRUMENTATION AND CONTROLS
I
I
I
I
ELECTRICAL SERVICE
I
I
I
I
6.
SPARE PARTS
______________________I
i mI
SUBTOTAL
________________________________________________________ 1
-I
I
I
CONTINGENCY
I
I
I
TOTAL DIRECT COSTS
________________________________________________________
________________ I __________________________________________________
_____________
_______________________________________________
C
TOTAL
0
3.
4.
S.
7.
8.
(
C
i aunD
EnUTPMENTIMATERIALS
ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT
SYSTEM FOR LIGHT-WATER-COOLED NUCLEAR REACTORS
0
"I
U
2
2
-4 U
2
2 C,
a
9
9
'a w
-J
04
0.j
'a
"4 a.
0
"4 COST (1975 $1000)
I TIFM
1.
OPERATING LABOR,
SUPERVISION,
AND OVERHEAD
MAINTENANCE MATERIAL AND
LABOR
CONSUMABLES,
CHEMICALS,
AND
SUPPLIES
UTILITIES AND SERVICES
Waste Disposal Water Steam Electricity Building Services Other TOTAL 0 AND M ANNUAL COST
LABOR
OTHER
TOTAL
BASIS FOR COST ESTIMATE
Description of Augment U
K
2.
3.
4.
5.
ITEM