ML19199A442
| ML19199A442 | |
| Person / Time | |
|---|---|
| Site: | Crane  |
| Issue date: | 06/04/1976 |
| From: | NUCLEAR SAFETY ASSOCIATES |
| To: | |
| References | |
| ENVR-760604, NUDOCS 7905020190 | |
| Download: ML19199A442 (60) | |
Text
{{#Wiki_filter:.?F3L 50-3%0 'qg','[(n -- P. '. Evaluation of the Th'ree Mile Island Nuclear Station Unit 2 to Demonstrate Conformance to the Design Objectives of 10 CFR 50, Appendix 1. GE mia,Q.J5_ ?.h -. ~ METROPOLITON EDISON COMPANY Appendix 10.7-/. COST ESTIMATING METHODOLOGY AND DETAIL COST ESTL'4ATES 7905020GlRo 7D 4 f lC .,_ v prepared by Nuclear Safety Associates Bethesda, Md S 706 June, 1975
R ece'.o r : Three Mile Island-2 Appendix 10.7-A INDEX Pace Cost Estimating :.ethodology 10.7-Al Cost Multipli.:rs and Factors 10.7-14 Summary of Augment Costs 10.7-A5 DETAIL COST ESTIMATES Case Description C-1 Add one decay tank 10.7-A6 C-2 Delete HEPA from waste gas release 10.7-A9 C-3 Delete charcoal from easte gas release 10.7-All D-1 Delete HEPA -- Aux Bldg vent 10.7-A13 D-2 Delete charcoal -- Aux Bldg vent 10.7-A17 E-1 Add kidney 10.7-A21 E-2 Eliminate charcoal from high vol purge 10.7-A25 E-3 Eliminate EEPA from high voi purge 10.7-A29 F Eliminate charcoal from condenser air ejector off-gas 10.7-A33 G Delete demineralizer from CVCS condensate 10.7-A35 H-1 Remove first demineralizer from dirty waste system 10.7.38 H-2 Remove condensate demineralizers from dirty waste system 10.7-A42 H-3 Remove evaporator from dirty waste system 10.7-A46 H-4 Remove both demineralizers from dirty waste system 10.7-A51 H-5 Remove esaporator and both demineralizers from dirty waste system 10.7-A52 1-1 Remove first demineralizers from regen waste system 10.7-A53 1-2 Ramove condensate demineralizers frca regen waste system 10.7-A57 I-3 Remove both demineralizers fror regen waste system 10.7-A61 1-4 Delete both demineralizers and evaporstor from regen waste system 10.7-A62 6
g Cost Estimatine Methodolonv (1) The methods used in estimating the cost of the augments are outlined on the following paragraphs. (2) General Bases The cost estimates for the augments were prepared using wherever possible the cost bases and data presented in NRC Regulatory Guide 1.110* (3) Di_ rect Installed Costs In most of the augment cases studied for this application there were Reg Guide 1.110 unit cost values which could bm applied, with appropriate adjustments for size or capacity, to the augments considered. In many of the cases the unit values were used directly as outlined in the Reg Guide for the basic augment process systems. Support facilities such as building space, piping systems, electrical system and the like we e then applied at approximately the same percentage or at the same unit costs as stated in Reg Guide 1.110 cases. In some of the augments studied the equipment sizes or capacities were not sufficiently close to Reg Guide 1.110 typical equipaent to use the Reg Guide cost numbers directly.
- All references herein to " Reg Guide" cr " Reg Guide 1.110" refer to the United States Nuclear Regulatory Commission Regulatory Guide No. 1.110 dated March 1976 titled Cost-Benefit Anal" sis for Radwaste Systems for Light-Water-Cooled Nuclear Power Reactors 10.7-Al j
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In these cases the estimated costs of equipment were obtsined from curves or graphs which were constructed by using various Reg Guide 1.110 equipment cost / capacities as specific curve points. In other cases where only one Reg Guide 1.110 cost value was shown, estimated costs for the new equipment sizes were obtained by use of an exponential cost / size relationship (such as the "0.6 power curve") which engineering data or literature indicates to be appropriata for the type of equ.sment under consideration; these curves were projected using the Reg Guide 1.110 cost as the base point. In a few cases where there was either no Reg Guide 1.110 data available or no act'al construction cost data at hand the u costs were derived in a standard estimating manner using equipment costs obtained from equipment manufacturers or reliable engineering literature. In the above cases the same approxi= ate cost relationships of support facilities such as building space assignment, piping systems, electrical systems, etc as were used in the Reg Guide were then applied to arrive at the total estimated direct installed cost. The detail estimate sheet for each case shows the cost bases used for estimating the cost of the case. 10.7-A2 IL
e (4) Ocecating and Maintenance Costs The annual operating and maintenance costs for the various augments sere derived using Regulatory Guide 1.110 outlined costs for like equipment or systems. The same approximate equipment labor attention ranges were used as outlined in the Regulatory Guide. The amounts of the various maintenance materials, utilities and services were estimated using the augment requirements; the unit costs used for these are similar to those outlined in the Regulatory Guide. (5) Cost Multioliers and Factors The multipliers and f actors used to obtain the total capital cost of each augment, the annualized cost of capital and the appropria*.e geographical labor multiplier are shown on page 10.7-A4. (6) Cost Presentation Direct cost totals are rounded to the nearest whole number; operating and maintenance costs are rounded to the nearest tenth. All costs are expressed in year 1975. dollars. 10.7-A3 .-a gC
t Reactor: Three Mile Island -2 Cost Multioliers and Factors Indirect Cost Factor This is a two-unit site; per Regulatory Guide 1.110 page 14 the Indirect Cost Factor is 1.73. TP.e estimated installed direct cost of the augment is multiplied by this factor to obtain the total capital cost. Caoital Recoverv Factor General Public Utilities advises that the capital recovery factor to be used their nuclear facilities is 16.07. Labor Cost Correction Factor This facility is constructed in FFC Georgraphic Region I. Per Regulatoty Guide 1.110 page 13 the labor correction factor for this area is 1.6. 10.7-A4 IC Js
Reactor: Three Mile Island-2 Sucmarv of Augment Costs (1975 $1000) Inst Total Annual Oper-Maint-Total Direct Capital Fixed ating enance Annual Augment Cost Cost Charge Cost Case Description 0 16.07. C-1 Add one decay tank 156 273 43.7 neg neg 43.7 C-2 Delete HEPA from waste gas release 22 38 6.1 1.2 0.2 7.5 C-3 Lele' e charcoal from waste gas 22 38 6.1 0.8 0.4 7.3 release D-1 Delete HEPA--Aux Bldg vent 391 684 109.4 11.2 12.6 133.2 D-2 Delete charcoal--Aux Bldg vent 353 618 98.9 7.5 37.8 144.2 E-1 Add kidney 172 301 48.2 7.1 12.0 67.3 E-2 Eliminata. charcoal from high vol 209 366 58.6 0.5 2.2 61.3 purge E-3 Eliminate EEPA from high vol purge 242.. 423 67.7 0.8 0.7 69.2 F Eliminate charcoal from c,ndenser 30 52 8.3 3.8 2." 14.1 air ejector off-gas G Delete demineralizer from CVCS 98 171 27.4 2.9 2.0 32.3 condensate H-1 Remove first demineralizer from 37.6 66 10.6 7,5 12.0 30.1 dirty waste system H-2 Remove condensate demineralizers 19.6 34 5* 2.0 0.4 7.8 from dirty waste system H-3 Remove evsperator from dirty 132 231 37 63.2 9.9 110.1 waste system H-4 Remove both ?.emincralizers from 57 100 16 9.5 12.4 37.9 dirty waste system H-5 Remove evaporator and both demin-190 331 53 72.7 22.3 148.0 eralizers from dirty waste system (continuad next page) 10.7-A5
Reactor: Three Mile Irland-2 Summarv of Auenent Costs (1975 S1000) Inst Total Annual Opcr-t'.aia t - To t.ai Direct Capital Fixed ating enance Annual Augment Co c.u Cost Charge Cost Case Description 3 16.07 1-1 Remove first deminerali:ers from 105 184 29.4 52.1 3.0 84.5 regen waste system I-2 Remove condensate demineralizers 55 96 15.4 2.9 1.0 19.3 from regen waste system 1-3 Remove both demineralizers from 160 280 44.8 55.0 4.0 103.8 regen waste system I-4 Delete both demineralizers and 530 927 148.3 184.3 31.8 364.4 evaporator from regen waste system 10.7-A5.1 IC ,w
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Estimated Installed Direct Costa for Gas Decay Tanks Per Regulatory Guide 1.110 Values Without Contingency Reactor: Three Mile Island-2 Case: C-1 s 'O s _- .3 .m -. _. _, = N "; - -
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Reference:
Regulatory Guide 1.11' dated 3/76 p M Assign same labor / equipment / support-facility distribution as per Regulatory Guide 1.110 approximate values. \\,~ 5/76 lo.7-Aa
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6 7 / 5 0M1 8 2 es E T a M s C es TI tn S a e E e m l T e T S e c l N O E r C a /* a M l s T s R p o A O E a e p F R g r 2 s T S y i I E e a l s d S T t A d a m S s B / o e l A a n c a W D S w i r o A R m a c R O k h n r T F C n 0 c i a O A a 1 h E t c + T R E E R y l k H A a S E c L E C e L 5 T U d ) A 7 A N 0 T 4 1 2 e M I D m 0 O u 0 0 T 0 0 ? l T E o 1 S L r a E O f v O 5 T C 7 e S m 9 O R e 1 t C E ( t a T E A s T m C W y S R i N s O E x A T C i o l N H T E G n O r T I o p N I L i p A R t a M O a F r 0 DN M t 4 A E l T i p G S R N Y f O I S B 0 T l A 1 A L R a 1 E o P c 1 O r 2 L a e d 1 h d A M c i n N u a A e G l t N s e g 0 D I l 1 N e e 3 A T R e d D S N O r t t A S S C i n L E e + L A C L p l e I n A C I s A y I I V e U e o R M R c N s e A E E E l N t r k T H S a i A s v E AD f 0 A C s r h o B M D o y e M o T N p t S c T n ( LA E S A i c g N s i D e E C E r i GH N L S D i n A t NR A BS I e r m t d r 0 E r i o t ip IE N MI E TV E T t e a c l e c r AO TR UL I s t e e i h L a c R NO SP L a a t l u t A ED IB NP I W W S E B O T s e e PN AA OU T O R D OA ML CS U T 1 2 3 4 5 e( eD ~ s i 3 _ r 6 1
re i l p 6 i 7 t / 3 01 5 2 r 1 n C E T A = r e M o s Rl rb Oi a oa FS C e E t l S s 1 c IT a SS as s e AO m f e t BC e d s l e t r u o r i ol c b c s n an n a i l i o i g t M E e r o 2 2 39 0 9 0 9 T t L S p s A Y T S a O 2 2 1 0 79 2 1 w T 1 1 1 2 l T a N o k EM n c r T S a A R a t E O h R T c T C y A a E E S r c T R L o S e ) A A R l 0 I f e W A 0 R D E 0 E m d A L 1 T R C o A e U r M 0 0 5 2 0 3 3 s F N 5 / u f O 7 T 9 N 1 1 0 0 3 - l 4 D a 1 E 1 1 1 s T ( n E l ( M e e O P W u O t T I S C s S U l y O Q a E R C E v s T E A T T M A n C 9 W E IT o 3 R S T i I E H t D p G a T I r 0 S L O t 1 C R l 1 O R i T F O ) 39 6 0 7 1 C f B E A R L 1 1 0 46 0 7 e I 1 d D z = i o L c u A r G T O q! g 2 T l l e e d R n e a t f l e r o s l S e I e L l O l 04 d_ S R i 5A e M T l E N i t i T O - t y7 n S C l l M e Y m T S D u e0 e g N N E m S t 1 u T E G A C T n e A N M N I r S u e r E N I N V O h f M M G P O R o C i o E I S A S T Y C P I I I E Lb x. T T S P T S A a T op n I U l r o Q A D T L T O C E r i E E N A R T N I p R pr o G T E C A B t 6 E p S N A M I P U G D a 1 t i S I I U R S N c r E D C R T E 1 I A L a c C L O T C R T s O I S S E A x N T R D P B I e e R U N L P O O E S C T 1 2. 3 4 S 6 7 8 b O? l } 6 /
6 7 / 5 es E T a A C M I T 26 8 S E 1 2 3 T 1 1 2 T S N O E C N I R A O E F R T S I E S T A S B A W D S A R R 0 s F c Q a F T R ) E n E R i H A f S E c L E C L T U 0 ) A A N 0 0 T M 0 O 2 0, 6 2 0 8 I D 0 T T E 1 5 L 4 2 ~ 4 S 3 0 E ) 8 1 2 ( 5 T C ( 7 S 9 O R t 1 4 C E ( n T 1 E 4 e T A C M v S R N O E E Q in 7 A T C H N l T T I e O 0 l N L 1 b I A R M O u e F D x g N M a a A E l' T n G S r R N Y o 9 I S r B t T f A e A i R e E A h P P s O E 2 L l l n A o d U e i N n N t t a A e a l l l N s e u O D I d I N c S A T l M I e S a V O c l t R S S C i n E L E e P L A C L l M m U A CI V e U g S I I s A i e u R M R c N a e A E E E ) r R T H S s i N t v A e i f M O A C s r d l o E B M D o y e M T T AD N p i C t n LA E S A s r i GH N L S i D r o E C E o t NR A BS E ic g N e D n A r p p IE N AE I e r m t i r 0 d t_ i TV E MI T t e a c l h L e r AC TR UL I s t e e i c R NO SP L a a t l u t A s ED IB NP l W W S E B O T e PN AA OU i O D OA ML CS U T 1 2 3 4 S r, a
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Reactor Tw, e u n i,,, s. g Case D* HEPA/ Charcoal Filters for Ventilation System ESTIMATED ANNUAL OPEPATING AND PAINIENANCE COSTS Detail Calculation Sheet Description of Augment ( .ete HEPA frem aux bid 2 vent (84,000 cfm) I. COST BASES per Reg Guide 1.110 dated 3/76 (p 43 typical) 1. OPEPATING 1 ABOR, SUPERVISORY AND OVERHEAD a) 7 1/2 minutes / shift for HEPA bank = 136 hours / year b) 7 1/2 minutes shift for charcoal bank = KGE3h30tyJCDJJE c) 40 hours HEPA bank annual test = g hours,' year hours / year L' Total 2. MAINTENANCE FATERIAL AND IABOR a) HEPA: one change every 2 years @ $150/ unit b) prefilter; one change every 2 years @ S150/ unit c) charcoal: one change every 2 years @ $900/ unit 3. CONSUPABLES, CHEMICALS & SUPPLIES 4 UTILITIES & SERVICES a) Waste disposal: 1) per HEPA unit: $50
- 2) per prefilter unit: $50
- 3) per charcoal unit: $100 d)
Electricity Additional fan HP for filter @ 0.5 kv/1000 cfm @ $0.018/kwh $80 year */1000 cfm; allow = pro-rata $60/yr for HEPA, $20/yr for charcoal II. CALCULATIONS FOR ESTIFATE SHEET (per above bases) 1. ']PERATING IABOR, SUPERVISORY AND OVERHEAD 176 hours / year @ $12 =$ 2,112 /yr 2. MAINIENANCE MATERIAL AND IABOR 2a. As pref units x 0.5 unic/yr @ S150 ea =$ 6.,cn /yr 2b. 84 HEPA units x 0.5 unit /yr @ S150 ea =S 6,200 /yr 2c. XX char units x 0.5 unit /yr @ $900 ea =5 x /yr Total =S 12,600 /yr 3. CONSUMABLES, CHEMICALS & SUPPLIES 4 UTILITIES & SERVICES Waste Discosal pref units x 0.5 unir '. @ S 50 ea =$ 2,100 /yr 4al. or 4a2. d4 HEPA units x 0.5 unit /yr @ $ 50 ea. -S 2,100 /yr 4a3. X char units x 0.5 unit /y- @ S100 ea =S X /yr Total 4a =$ L,200 /yr Electricity 4d 84 kcfm @ $60 / year /kefm * =$ 5.cao lyr Notes: (1) HEPA unit = 1000 cfm unit; (2) Ciarcoal unit = 1000 cfm unit; (3) bank = entire group of filters for the total ventilatiot, stream; (4) dollars = year 1975; *(5) continuous operation basis @ 365 days /8760 hrs /yr; for 310 days /7440 hrs /yr operation 5/76 =ultiply by 0.85 ,6-4p 10.7-A14 e iU
r e i l p i t 6
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u / E 1 m 5 T A e M = r s RI o OT rb a FS oa C E S t l IT c SS as AO f e BC d r u ol b c an l i M E T L S A Y T 5 u 5 1 S O 2 4 8 1 2 5 3 9 T 5 6 33 3 T 2 N EM T S A R E O R T T CA ) E f S T R m L S f ) A A R c 0 I W A 0 R D E 0 E A L 0 1 T R C 0 A 2 3 1 3 7 0 U M 7 0, 7 - 2 0 F N 5 / 2 4 2 3 6 O 7 T D 4 9 N 2 1 T E 8 1 E A E t ( M ( E 0 P H 0 T S C t S I 7 U 1 n O Q 0 E R C E e 1 T E A T v T M A C E e I W g T R g S T d I a E H l D p G b T S t O x t C R u O R e a T F O 2 3 8 1 e C B 5 2 5 S8 9 h E a R t A 2 2 s o L I D r n f o At i T A t 2 O P a T E d l = l l u4 n cA a e l l t r a7 s e e c I l S 0 i e L l l 1 e d O S R p i l M T i ae i E N t t t g T O M n S C l e a e Y u d p e m T S D m e g N N C S r r u T E G A C I r A N M N I r S e e h E N I O R N V o O pp f M M G P T b C o I P I I I E L T I S P T S A a T n I U S A S Tl Y C o Q A D T L T 0 C E r it E E N A R T N IR o G T E C A B6 E t ip S N I M c r E I A I P U G D S U R S1 I L N D C R T E a c C L O T C R T A s O I S S E A x N T e e R U S N L P O O R D P B A I ( S C T 1 2 3 4 S 6 7 8 8L h h l C 6
k v Reactor Three Mile Island-2_ Case D-1 HEPA/01arcoal Filters For Ventilation Systems ESTIMATED DIRECT COSTS Detail Calculation Sheet Description of Augment delete HEPA from aux bida vent (84,000 cfm) Cost Bases Reference (1) Prefilter-HEPA-charcoal filter equipment = $5/cfm RG, p 41 $3/cfm RG, p 36 (2) Prefilter-HEPA filter equipment only (w/o = charcoal) (2) S2/cfm (1) (3) Charcoal filter equiptant value, therefore = (4) Heater for charcoal @ $400/1000 cfm = S0.40/cfm RG, p 41 (5) 3uilding space assignment: (6) Prefilter-HEPA-charcoal: for 15000 cfm = 16 ' : 20' x 12' soace = 3840 cu ft = 0.256 cu ft/cfm 0.256 cf/cfm RG, p 41 (7) Prefilter-HEPA (w/c charcoal); g for 15000 cfm = 16' x 12' x 12' space = 2304 cu f t = 0.154 cu f t/cfm 0.154 cf/cfm RG, p 36 (8) Bldg space assignment for charcoal (6) - (7) only, therefere, = 0.102 cu ft/cfm 0.102 cf/cfm # (9) Bldg space value: Auxiliary Bldg = $5/cu ft RG, p 36 $3/cu ft RG, p 41 Turbine Bldg = (10) CALCUIATIONS FOR ESTIM.lTE SHEEI (per above bases) # 1. PROCESS EQUIPMENT HEPA filter: 84,000 cfm @ $3/cfm = $252,000 2. BUILDING ASSIGNMENT 84,000 cfm 0 0.154 cu ft/cfm x S5/cu ft = $ 64,680 3. ASSOCIATED PIPING SYSTEMS $8000 allowar.ce 4. INSTRUMENTS AND CONIROLS in base 5. ELECTRICAL SERVICE in base 6. SPARE PARTS k h '. L .e1000 allowance Notes: (1) RG = Reg Guide 1.110 dated 3/76 (2) Dollars = year 1975 (3) I sign same labor /equipmene/ support-facility distributton as par Reg Guida 1.110 approximate values. 3/76 76 -4h 10.7-A16
6 7 / 5 2 D es E T a M C I 58 3 T S E 77 5 3 4 T T S N O E C M T R A O E F R T S I C S T A S B AW D S A R R O T ) F C O A m E f T R c E E R H A 0 S E 0 L 0, E C L T b ) A M N 4 0 T 1 0 O 6 8 7 2 3 t TI D 0 T E ( 1 S L 1 7 4 1 5 H E O t 3 4 1 O n A 5 T C 7 S e 9 7 O R v 1 C E ( T E A g 0 T C W d S R 1 N l O E A T C H N H b T e E G O g x a T I N I L u p A 9 a M 0 t n N M oi t D e A E r e T f i G S R ls N Y O TI S l B a A n A o L o R E c i P r t O a a 2 e l L A c u d U c N n e l N a A t a l e c N s l O D I e l I N d, i S A T e I D S a V N O t l t R A S S C e i n E L E H e P L A I s A C L d m U A C g S I I V e U r e u R M R c N e A E r R 1 E E l i N e H S a v A p i f M O A C s r l o E B M D o y e M T T AD N p t o E C E i s n I LA E S A s D r i GH N L S i c g N D i n E r i A t NR A BS I e r m t d r 0 o p IE K AE t i TV E MI T t e a c i h L l e c r AO TR UL I s t e l u t A e a c R NO SP I W W S E B O T L a a t s ED IB NP e e PN AA OU T O R D OA ML CS U T 1 2 3 4 5 a o
- ybC l
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O Reactor Three Mile Island-2 Case D-2 HEPA/ Charcoal Filters for Ventilation System ESTI?"ATED ANNUAL OPERATING AND MAINTENANCE COSTS Detail Calculation Sheet Description of Augment delete charcoal from aux blde vent (%.000 c f ) I. COST BASES per Reg Guide 1.110 approximate values (p 43 typical) 1. OPERATING IABOR, SUPERVISORY AND OVERHEAD a) 7 1/2 minutes / shift for HEPA bank = MbW6AlvW9Ne b) 7 1/2 minutes shift for charcoal bank = 136 hours / year c) 40 hours HEPA bank annual test = x'G0CtHEXUXXX Total = U hours / year 2. MAINTENANCE MATERIAL AND 1ABCR a) HEPA: one change every 2 years @ $150/ unit b) prefilter: cne change every 2 years @ $150/ unit c) charcoal: one change every 2 years @ $500/ unit 3. CONSUMABLES, CHDGCALS & SUPPLIES 4 UTILITIES & SERVICES a) Waste disposal: 1) per HEPA unit: $50
- 2) per prefilter unit: $50'
- 3) per charcoal unit: S100 d) Electricity
- Additional fan HP for filter @ 0.5 kw/1000 cfm
@ $0.018 kwh = $80 year */1000 cfm; allow pro-rata $60/yr for HEPA, S20/yr for charcoal II. CALCUIATIONS FCR ESTIMATF SHEET (per above bases) 1. OPERATI LABOR, SUPERVISORY AND OVERHEAD 136 hours / year @ $12 1.632 /yr = 2. MAINTENANCE MATERIAL AND LABOR 2a. x pref units x 0.5 unic/yr @ $150 ea =$ x /r 3 2b. I HEPA units x 0.5 unit /yr @ $150/ea =$ X /yr 2c. 84 char units x 0.5 unit /yr G $900 ea =$ 37,800 /yr Total =$ 37,800 /yr 3. CONSUMABLES, CHEMICALS & SUPPLIES 4. UTILITIES & SERVICES Waste Disposal 4al. x pref units x 0.5 unit /yr @ $ 50 ea =$ x lyr 4a2. Y HEPA units x 0.5 unit /yr @ $ 50 ea =$_ x /yr 4a3. u char units x 0.5 unic/yr @ $100 ea $ e,200 /yr = 4,200 /yr rotal 4a = Electricity 4d o* kefm @ $ 20 / year /kefs =$ 1.680 /yr Notes: (1) HEFA unit = 1000 cfm unis, (2) Clarcoal unit = 1000 cfm uni: (3) bank = entire group of filters for the total ventilation scream; (4) dollars = year 1975; (5)
- continuous operation basis 76-4 to,7.Atg 5/76
re
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1 p 6 i 7 2 = t / l S r u D E t su o T e M cr s RI ao OT a f b FS C E a S rl IT SS o AO b s BC ae l du hl t c i n wi M E T L S A 2 3 8 0 8 1 1 2 3 Y T S O 0 4 2 82 3 5 T 2 2 3 3 T N f H T S ) A R m E O R T f T C c A E E S T R 0 L S 0 ) A A R 0 0 I W A 0 R 1 0 E D E A L 4 1 T R C 8 A U M 2 4 3 7 8 4 1 5 ( F N 5 / O 7 T 8 1 1 2' 3 D t 9 N 1 2 2 T E E 0 n (1 M 2 E L E O e P S C S J A H O v T I g O 0 7 E R C E T E d T l T 0 W. A b C 1 I W E T R e S T x t I E H i D g G n a T I l p S L O m C R o O R t r O i T F C f B 0 9 5 3 77 1 t e E A 2 2 1 60 1 l e R L 1 I h I l D a s n n L e A T r o i O a 2 T h t c = a l dn o u4 a r cA e r l l s l S e a7 I e L i c t O l 0 e x_ M T S R p l 1 l E N i i t T O t ae i n S C l t g M e Y m T S D u ea g N N E m S d p e u T E G A C I e A N M N I S r rr N V r E N I O R o C e e C f M M G P I E Lb pp h o E P 1 I T T I P T S Aa T A-n I U S A S T W C o Q A D T L T Ol C E r it G T E C A D E E N A R I N IR E o h. c r E D I M t lp S I C R T E 1 A N A I P U S D S U R S N L a s C L O T C R s O I S S E A N T x e e R U S N L P O O R D P P A I E S C T 1 1 2. 3 4 5 6 6 7 8 ^, .u %7 ~ r, t ; e J
Reactor Three Mile Island-2 Case D-2 HEPA/ Charcoal Filters For Ventilation Systems ESTIMATED DIRECT COSTS Detail Calculation Sheet Description of Augment delete charcoal from aux b1dg vent (84,000 cfm) Cost Bases M erence (1) Prefilter-HEPA-charcoal filter equipment = $5/cfm RC, p 41 (2) Prefilter-HEPA filter equipment only (w/o = $3/cfm RG, p 36 charcoal) (3) Charcoal filter equipment value, therefore = $2/cfm (1) (2) (4) Heater for charcoal @ $400/1000 cfm = S0.40/cfm # RC, p 41 (5) Building space assigreent: (6) Prefilter-HEPA-charcoal: for 15000 c fm = lt ' x 20 ' x 12 ' spac e = 3840 cu ft = 0.256 cu ft/cfm 0.256 cf/cfm RG, p 41 (7) Prefilter-REPA (w/o charcoal): for 15000 cfm = 16 ' x 12' x 12 ' space = 2304 cu f t = 0.154 cu f t/cfm 0.154 cf/cfm RC, p 36 (8) Bldg space assignment for charcoal (6) - (7) only, therefore, = 0.102 cu f t/cfm 0.102 cf/cfm # (9) Bldg space value: Auxiliary Bldg = $5/cu ft RG, p 36 Turbine Bldg = $3/cu ft RC, p 41 (10) CALCUIATIONS FOR ESTIMATE SHELT (per above bases) # 1. PROCESS MUIPMENT Charcoal filter: 84,000 cfm @ $2/cfm = S168,000 Heater for cnarcoal: 84,000 cfm @ 40c/cfm 33,600 = 2. BUILDING ASSIGh> 7CE $201,600 84,000 cfm @ 0.102 cu f t/cfm x ?S/cu f t = $42,840 3. ASSOCIATED PIPING SYSTDG $8000 allowance 4 INSTRUMENIS AI' CONIROLS in item 1 5. ELECTRIO.AL SERVICE $20,000 allowance 6. SPARE PARTS $8000 allowance
- ~D Notes:
(1) RG = Reg Guide 1.110 dated 3/76 (2) Dollers = year 1975 (3) Assign same labor / equipment / support-facility distribution as per Reg Guide 1.110 approxi= ate values. 76-4h 10.7-A20 5/76
Reactor Three Mile Island-2 Case E-1 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIGHT-WATER-COOT ED NUCL EAR REACTORS Description of Augment add kidney (20,000 cfia) COST (1975 $1000) ITEM LABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPE 8tATING LABOR. SUPERVISION, 3.7 AND OVERHEAD 2. MAINTENANCE e'3TERIAL AND 12.0 LABOR g 3. CONSUMABLES, CHEMICALS, AND SUPPLIES wg O 4. UTILITIES AND SERVICES Waste Olsposal 2.0 Water Steam Electricity 1.4 Eullding Services Other c. 5. TOTAL 0 AND M ANNUAL C0'2T 19.I
- per detail calculation sheet, page 10.7-A22 s
S/76 7.1 12.0 19.1 76-3a
Reactor Three Mi!_ Island-2 Case E-1 HEPA/Clarcoal Filters for Ventilation System ESTIMATED ANNUAL OPERATING AND MAINTENANCE COSTS Detail Calculation Sheet Description of Augment add kidnev (20,000 cfm) I. COST SASES per Reg Guide 1.110 dated 3/76 (p 43 typical) 1. OPERATING LABOR, SUPERVISORY AND OVERHEAD a) 7 1/2 minutes / shift for HEPA bank = 136 hours / year b) 7 1/2 minutee shift for charcoal bank = 136 hours / year c) 40 hours HEPA bank annual test = J hours / year Total 2 hours / year = 2. MAINTENANCE MATERIAL AND IlBOR a) HEPA: one change every 2 years @ $150/ unit b) prefilter. one change every 2 years @ $150/ unit c) chcrcoal: one change every 2 years @ $900/ unit 3. CONSUMABLES, CHEMICALS & SUPPLIES 4 UTILITIES & SERVICES a) Waste di.e.posal: 1) per HEPA unit: $50
- 2) per prefilter unit: $50
- 3) per charcoal unit: $100 d)
Electricity
- Additional fan HP for filter
@ 0.5 kw/1000 cfm @ $0.018/kwh $80 year */iOOO cfm; allow = pro-rata $60/yr for HEPA, $20/yr for charconi II. CALCUIATIONS oa. ESTIMATE SHEET (per above bases) 1. OPERATING LABOR, SUPERVISORY AND OVERHEAD 312 hours / year @ $12 1.7c4 /yr 2. MAINIENANCE MATERIAL AND LABOR 2a. 20 pref units x 0.5 unit /yr @ $150 ea =$ 1,500 fyr 2b. 20 HEPA units x 0.5 unit /yr G $150 ea =$ t,500 /yr 2c. 20 _ char units x 0.5 unit /yr G $900 ea =S o coo /yr Total = $ 12,000 /yr 3. CCNSUMABLES, CHEMICALS & SUPPLIES 4. UTILITIES & SERVICES Waste Disposal 4al. 20 pref units x 0.5 unit /yr G $ 50 ea =$ 500 _/ yr 4a2. 20 HEPA units x 0.5 unit /yr @ $ 50 ea. =$ 500 /yr 4a3. 20 char units x 0.5 unit /yr @ S100 ea =$ L,000 /yr Total 4a =$ 2,000 /yr Electricity 4d 20 kcfm @ $80 / year /kefm =$ L,360 /yr Notes: (1) HEPA unit = 1000 cfm unit; (2) diarcoal unit = 1000 cfm unit; (3) bank = entire group of filters for the total ventilation stream; (4) dollars = year 1975; *(5) continu. s operation basis @ 365 days /8760 hrs /yr; for 310 da,3/7440 hrs /yr operation 3/76 multiply by 0.85 76-4P 10.7-A22 1 i L, J;
r e i l p 6 i 7 1 t / 5
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E 1 m E T s r A o e M s RI rb a oa OT FS t l C E c S T as ISS f e AO d BC r u ol b c a n l i M 6 8 0 0 0 O. 2, E T L S A Y T 0 5 1 66 5 1 S O 4 45 1 7 T 1 1 1 1 T u N m EH T S 4 R i O R T T CA E E 5 T R L S ) A A R 0 I W A 0 R D E 0 E 0 0 0 0 9 A L 1 T R C 4 U K F N 5 / 6 2 1 9 2 1 O 7 T 2 2 - 1 4 4 D 9 N 1 1 1 2 T E 1 E E L ( M A E O P H O T I 7 S C S U O Q E R C E O T E I A T T I A C M e W E T R g a S T I ) E H D p G m T I f S L c O t C R e 02 7 9 0 0 O 0 R e T F 0 O B 4 3 77 2 9 h C 0, A E 1 1 2 2 s R L I 0 D = n 2 o L ( i A t T y O a e T l 2 n d u4 d i cA n k l a a7 l d r c S e 0 s d L i l 1 I a O S R l i M T n ae e E N l t g i l t T O i e a i n S C e Y l d p M m T S D n g N N E S u r r e u T E G A C e A N M N I r T S e e E N I N V r O pp r f M M G P O R C h o E P I I I E L o A T I S P T S Ab T T n I U S A S T a Y C o Q A D T L T O C E l_ N R r i E E N A P. T t G T E C A B E Sd G I o N A N U D t ip S I C R T E I A I P N c r E D l R S I L i T O T C R a c C l S S E A N T s O l e e R u N L P x O O R D P B I E S C T i 2 3 4. S 6 7 8 .Y>y 6 s 2 . s 7 ~ O h (
O Reactor Three Mile Island-2 Case E-1 HEPA/ Charcoal Filters For Ventilation Syste=s ESTIMATED DIRECT COSTS Detail Calculation Sheet Description of Augment add kidney to containment (20,000 cfm) Cost Bases Reference (1) Prefilter-HEPA-charcoal filter equipment $5/cfm RG, p 41 = (2) Prefilter-REPA filter equipment only (w/o $3/cfm RG, p 36 = charcoal) (3) Charcoal filter equipment value, therefore $2/cfm (1) - (2) = (4) Heater for charcoal @ $400/1000 cfm S0.40/cfm RG, p 41 = (S) Building space assignment: (6) Prefilter-REPA-charcoal: for 15000 c fm = 16 ' x 20 ' x 12 ' spac e = 3640 cu ft = 0.256 cu ft/cfm 0.256 cf/cfm RG, p 41 (7) Prefilter-REPA (w/o charcoal): for 15000 cfm = 16' x 12' x 12' space = 2304 cu ft = 0.154 cu ft/cfm 0.154 cf/cfm RC, p 36 (8) Bldg space assignment for charcoal (6) - (7) only, theref ore, = 0.102 cu f t/cEn 0.102 c.. am (9) Bldg space value: Auxiliary Bldg = $5/cu ft RG, p 36 Turbine Bldg $3/cu ft RG, p 41 = (10) CALCUIATICNS FCR ESTIMATE SHEEI (per above bases) 1. PROCESS EQUIPMENI allow 47/cfm for REPA & charcoal filter equipment plus bicwers, mounta, ductwork and containment penetrations. 2. BUILDING ASSIGNMENT 20,000 cfm 0 $7/cfm = $ 140,000 none required; equipment located in existing space 3. ASSOCIATED PIPING SYSTD'.S allow $5000 4 INSTRUMENIS AND CONIROLS in item 1 5. ELECTRICAL SERVICE in item 1 6. SPARE PARTS alicw $1000 C ~) ', e Notes: (1) RG = Reg Guide 1.110 dated 3/76 (2) Dollars = yeae 1975 (3) Assign same labar/egoipment/ support-facility distribution as par Reg Guide 1.110 approximate valt es. 5/76 76 -4h 10.7-A24
Reactor Three Mile Island-2 Case E-2 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RA0 WASTE TREATMENT SYSTEM FOR LIGHT-u TER-C00tED NUCLEAR REACTORS Description of Augment delete charcoal from high volume purge (50,000 cfm) COST (1975 $1000) ITEM LAB 0k OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR. SUPERVISION. 1.6 AND DVERHEAD 2. MAINTENANCE MATERIAL AND 22.5 charcoal replacements LABOR o 3. C0hSUMABLES CHEMICALS. AND 7 $UPPLIES U 4. UTILITIES AND SERVICES 2.5 da m at m pmal Waste Disposal Water Steam 1.0 Electricity Building Services Other ns ~ 27.6 conUnuous operaFI5irTanirs* S. TOTAL 0 AND M ANNUAL COST 2.7 assignment for infrequent use basis ** x 107. = Jl t't llotes:
- per detail calculation sheet, page 10.7-A26 AASince this purge system is operated at infrequent intervals, the annual o & H costs are taken at approximately 107. of continuous operation costs.
5/76 0.5 M 2.7 16-la
Reactor Three Mile Islard-2 Case E-2 HEPA/ Charcoal Filters for Ventilation System ESTIMATED ANNUAL OPERATING AND MAINIENANCE COSTS Detail Calculation Sheet Description of Augment delete charcoal from hizh vol ource ( 50.000 cfm) I. COST BASES per Reg Guide 1.110 approximate values (p 43 typical) 1. OPERATING IABOR, SUPERVISORY AND OVERHEAD a) 7 1/2 minutes / shift for HEPA bank = 32EC.LXICC$X:Ct-b) 7 1/2 minutes shift for charcoal bank = 136 hours / year c) 40 hours HEPA bank annual test = 7J.EutCCCC$X!EtX Total = @ hours / year 2. MAINTENANCE MATERIAL AND LABCR a) HEPA: one change every 2 years @ $150/ unit b) prefilter: one change every 2 years @ $150/ unit c) charcoal: one change every 2 years @ $900/unic 3. CONSUMA3LES, CHDiICALS & SUPPLIES 4 UTILITIES & bERVICES a) Waste disposal: 1) per HEPA unit: $50
- 2) per prefilter unit: $50
- 3) per charcoal unit: $100 d)
Electricity
- Additional fan 3P for filter @ 0.5 kv/1000 cfm
@ $0.018 kwh = $80 year */1000 cfm; alice pro-rata $60/yr for HEPA. $20/yr for charcoal II. CALCULATIONS FOR ESTIMATE SHErr (per above bases)* 1. OPERATING LABOR, SUP'tRVISORY AND OVERHEAD 126 hours / year @ $12 = $ y 1' /yr 2. MAINTENANCE MA*.'ERIAL AND LABOR 2a. x pref units x 0.5 unic/yr @ $150 ea x /yr = 2b. x HEPA units x 0.5 unit /yr @ $150/ea x / ~r = $ 22, #00 /yr 2<, 50 cher t. nits x 0.5 unit /yr @ $900 ea = $ 22,500 /yr Total = 3. CONSUMABLES, 3Df1CALS S SUPPLIES 4. UTILITIES & SERVICL3 Waste Discosal v /yr 4al. Y _ pref units x 0.5 unit /yr @ $ 50 ea = 4a2. x _ HEPA unita x 0.5 unit /yr @ $ 50 ea v /yr = ,.cno /yr 4a3. cn char units x 0.5 unit 'yr @ $100 ea = Total 4a $ 2,500 /yr = Electru ity / year /kefm $ J,000 /yr 4d 50 kcfm @ $ on = Notes: (1) HEPA unit = 1000 cfm unit; (2) Charcoal unit = 1000 cfm unit ; (3) bank = entire group of filters for; the total ventilation stream; (4) dollars = year 1975; (5) *continuot s operation basis; (6) Since this purge system is operated at ineermittent intervals, the annual 0 & M costs are taken Tt approximately 107, of :entinuous operation costs. .-/ 5/76 76-4s 10.7-A26 j G sJv
r e
- 0. i 6
l 7 1 p / i S =t 2 l r u E o E m t T A c r e M a o s Rl f Oi b a FS a C E r l S o IT SS b s AO a e BC l d h u l t e i wp M E T L S A 0 5 5 2 S 7 0 9 9 Y T 2 2 1 69 1 0 S O 1 1 1 2 T T N m ) u i S R f '.n.O c I T' CA 0 E 0 S U' R 0, L ) A A R 0 I W A 0 0 R D E 5 0 E A 1 T l ( R C A U M F N e 6 / O g 7 T 8 9 2 4 S 8 3 1 D 9 N r 0 2 - 1 4 T t 1 E u ( M 1 1 1 E t E o p P H u T I S C S U l O Q E R o C E 6 T E v A T T 2 M A i C A I W l E T g R 7 S T I i E H D C h 0 T I 1 S t m O C R o O r R e T F f O 2 6 3 4 2 6 8 g ) t C B E A 36 6 a 1 1 R l p t I a =- D o L c t A r e a e I O 2 h h T c s d _n n e a t o l e r i s l e t S I e i a L d O l l e S R p u4 l M T i cA E N i t T O t l M n S C l a7 e Y u c m T S D e g N N E m 0 S e u T E G A C I l 1 r A N M I O R C N I r S i E N N V h f M M G I I E L o O ae P T o E I I P T S Aa T e a P b t g T S n I U S A S Tl Y C d p o Q A D T L T O C E r i E E N A R I N I r r R o G T E I P J G D e e t C A B6 I t ip S N I L R S S I A E N pp c r E D C R T E I A 1 L a c C L O T C R T e O I s S S i A x N T e R U S N t P O O R D P B A I E S C T 1 2 3 4 F 6 7 8 1 1 b 8,s3 - n 'C-l' 6 1
Reactor Three Mile Island-? Case E-2 HEPA/Garcoal Filters For Ventilation Systems ESTIMATED DIRECT COSTS Detail Calculation Sheet Description of Augment delete charcoal frco high vol purge (50,000 cfm) Cost Ba e e s_ Reference (1) Prefilter-HEPA-charcoal filter equipment = $5/cfn RC, p 41 (2) Prefilter-HEPA filter equipment only (w/o S3/cfm RG, p 36 = charcoal) (3) Garcoal filter equipment value, therefore $2/cfm (1) - (2) = (4) Heater for charcoal @ $400/1000 cfm = $0.40/cfm # RC, p 41 (5) Building space assignstme: (6) Prefilter-HEPA-charcoal: for 15000 cfm = 16' x 20 ' x 12' space = 3840 cu ft = 0.256 cu ft/cfm 0.256 cf/cfm RC, p 41 (7) Prefilter-REPA (w/o charcoal): for 15000 cfm = 16' x 12' x 12' space = 2304 cu ft = 0.154 cu ft/cfm 0.154 cf/cfm RG, p 36 (8) Bldg space assign =ent for charcoal (6) - (7) only, therefore, = 0.102 cu ft/cfm 0.102 c f / cfm # (9) Bldg space value: Auxiliary Bldg $5/cu ft RG, p 36 = Turbine Bldg = $3/cu ft RG, p 41 (10) CALC"IATICNS FCR ESTIMATE SHEER (per above bases) # 1. PROCESS AUIPMENT charcoal filter: 50,000 cfm 3 $2/cfm = $ 100,000 heater for charcoal: 50,000 cfm 3 $0.40/cfm 20, ^g = 2. BUILDING ASSIGNMEyr $ 120,000 50,000 cfm x 0.102 cu ft/ cfm 3 $5/cu f t = $ 25,500 3. ASSOCIATED PIPING SYSTD'S $5000 allowance 4 INSTRUMENIS AND CONIROLS in item 1 5. ELECTRICAL SERVICE $ 12,000 allowance 6. SPARE PARTS $5000 allowance Notes: (1) RG = Reg Guidt 1.110 dated 3/76 (2) Dollars = year 1975 (3) Assign same labor /cquipment/ support-facility distribution 3/76 as par Reg Guide 1.110 approximate values. 76-4h 10.7-A28
Reactor Three Mile Island-2 Case ANNUAt OPERATING AND HAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR LIQtT. WATER-COOLED NUCLEAR REACTORS Description of Augment nielete IlEPA from liiph vol purge (50,000 cfm) COST (1975 $1000) ITEM TABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION, AND OVERHEAD 2.1 2. MAINTENANCE MA!ERIAL AND LABOR 7.5 IIEPA replacements 3. CONSUMABLLS, CHEMICALS, AND P SUPPLIES l'>y 4. UTILITIES AND SERVICES Waste Disposal 2.5 IIEPA disposal Water Steam Electricity 3.0 Building Services Other 15.1 continuous operation basisT 5. TOTAL 0 AND M ANNUAL COST x 107. 1.5 assignment for infrequent use basis ** = Notes:
- per detail calculation sheet, page IO.7-A30
- Since this purge system is operated at infrequent intervals, the annual O 6 H costs are taken at approxinuitely 107. of cont.inuous operation costs.
'-I' 5/76 -J
- 0. ti M
1.5 16-h
Reactor Ts oo v4to ist,-a_o E-3 Case HEPA/ Charcoal Filters for Ventilation System ESTIMATED ANNUAL OPERATING AND MAINIENANCE COSTS Detail Calculation Sheet Description of Augment delete HEPA from hich vol ource (50,000 cfm) I. COST BASES per Reg Guide 1.110 approximate values (p 43 typical) 1. OPERATING IABOR, SUPERVISORY AND OVERHEAD a) 7 1/2 minutes / shift for HEPA bank = 136 hours / year b) 7 1/2 minutes shifc for charcoal bank = 4X36%Gi7d9ihnitK 40 hours /vear c) 40 hours HEPA bank annual test = ~ Total = 17 hours / year 2. MAINIENANCE MATERIAL AND IABOR a) HEPA: one change every 2 years @ $150/ unit b) prefilt:r: one change every 2 years @ S150/ unit c) charcoal: one change every 2 years @ $900/ unit 3. CONSUMABLES, CHEMICALS & SUPPLIES 4 ITIILITIES & SERVICES a) Waste disposal: 1) per HEI'A unit: $50
- 2) per prefilter unit: $50
- 3) per charcoal unit: S:.00 Additional fan HP for filter @ 0.5 kv/1000 cfm d) Electricity
@ $0.013 kvh = $80 year */1000 cfm; allow pro-rata $60/yr for HEPA, S20/yr for charcoal II. CALCULATIONS FOR ESTIMATE SHEET (per above bases)* 1. OPERATING LABOR, SUPERVISORY AND OVERHEAD 176 hours / year @ S12 =$ 2.112 /yr 2. MAINTENANCE MATERIAL AND LABOR 2a. 50 prof units x 0.5 unit /yr @ S150 ea =S 3.750 /yr 2b. 50 HEPA units x 0.5 unit /yr @ S150/ea =S 3,750 /yr 2c. x char units x 0.5 unit /yr @ $900 ea =S X /yr Total =S 7,500 /yr 3. CONSUMABLES, CHDfICALS & SUPPLIES 4. UTILITIES & SERVICES Waste Discosal 4al. _ 50 pref units x 0.5 unit /yr @ S 50 ea =S 1,250 lyr 4a2. 5c HEPA units x 0.5 unit /yr @ S 50 ea =$ 1,250 _/yr / 4a3. X char units x 0.5 unit /yr @ $100 ea =S X _ yr Total 4a =S
- 2. 500_ / yr Electricity 4d 50 kcfm @ $
60 / year /kcfm =S 3,000 /yr Notes: (1) HEPA unit = 1000 cfm unit; (2) Curcoal unit = 1000 cfm unit; (3) bank = entire group of filters for the total ventilation stream; (4) dollars = year 1975; (5)
- continuous operation basis; (6) Since this purge system is operated at intermittent intervals, the annual 0 & M costs are taken at approximately 10~.
of continuous operation 5/76 p costs. 10.7-A30 76-4s l( Cv
Reactor Titree Mile Island-2 E-3 TOTAL DIRECT COST 15TIMATE SHEET OF RADWASTE TREAIMfNT SYSTfM FOR LIGHT-WATER-C00tED NUCtfAR REACTORS Description of Augment delete llEPA f roin liigh vol purge ( 50,000 cfin) DIRECT COST (1975 $1000) BASIS FOR ITEM (ABOR EQt]IPMENT/ MATERIALS TOTAL COST ESTIMATE 1. PROCESS EQUIPMENT 15 135 150 2. BUILDING ASSILNMENT 25 13 33 3. SOCIAIED PIPING SYSTEMS 3 2 5 ?> 4. INSTRUMENTATION AND CONIROLS 5. ELECTRICAL SERVICE 6. SPARE PARTS 1 1 SUBIOTAL 43 151 194* willi lain >r factor - 1.0 69 220 includes t al>or mul t iplier 1,6 labor !nti tigjhp A A l = x 7. CONTINGENCY 7 15 22 8. TOTAL DIRECT COSTS 76 166 242 e-, Aper detail calculat. ton - '. page 10.7-A32 per page IO.7-A4 J
- A 5/76 s
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Reactor Three Mile Island-2 Case E-3 HEPA/ciarcoal Filters For Ventilation Systems ESTDMTED DIRECT COSTS Detail calculation Sheet Description of Augment _, delete HEPA from iiigh vol purge (50,000 cfm) Cost Bases Reference (1) Prefilter-HEPA-charcoal filter equipment $5/cfm RG, p 41 = (2) Prefilter-HEPA filter equipment only (w/o $3/cfm 5/ RG, p 36 = charcoal) (3) Ciarcoal filter equipment value, therefore S2/cfm (1) - (2) = (4) Heater for charcoal @ $400/1000'cfm $0.40/cfm RG, p 41 = (5) Building space assignment: (6) Prefilter-HEPA-charcoal: for 15000 cfm = 16' x 20' x 12' space = 3840 cu ft = 0.256 cu ft/cfm 0.256 ef/cfm RG, p 41 (7) Prefilter-HEPA (w/o charcoal): for 15000 cfm = 16' x 12' x 12' space = 23G4 cu f t = 0.154 cu f t/cfm 0.154 cf/cfm f/ RG, p 36 (8) Bldg space assignment for charcoal (6) - (7) only, therefore, = 0.102 cu ft/cfm 0.102 cf/cfm (9) Bldg space value: Auxiliary Bldg = $5/cu ft gj RG, p 36 Turbine Bldg $3/cu ft RG, p 41 = (10) CALC 1'IATIONS FOR ESTIMATE SHEET (per above bases) 7p 1. PROCESS @UIPMENI 50,000 cfm G S3/cfm = $150,000 2. BUILDING ASSIGRfENT 50,000 cfm x 0.154 cu ft/cfm G SS/cu ft = $38,500 3. ASSOCIATED PIPING SYSTD'.S $5000 allowance 4 INSTRUMENIS AND CONIROLS in item 1 i 5. ELECTRICAL SERVICE j, vU-in base 5. SPARE PARTS a, c allow $1000 Notes: (1) RG = Reg Guide 1.110 dated 3/76 (2) Dollars = year 1975 (3) Assign same labor / equipment / support-facility distribution as per Reg Guide 1.110 approximate values. 5/76 76-4h 10.7-A32
7 6 /, t F se t e l r s E a e T a A u t C I n i M n l
- 8. M 5 8
T a f S 3 E r t T h n T S N O en E C 0 i M 4 c T R c A O E F + a R l T S t p I E S f e T A i r S B h 2 A W s s n D S / e i A R r n d e R O o i u t T F C t m l i O A c c E e 5 n n T R E j 1 i i E R e H A S E r L E C i L T U a 8 8 0 ) A A N 0 T g M 0 O D r 0 T 3 2 e 5 I n T E e 1 S L s E OO n 5 T C e 7 s S d 9 e O R 1 n u C E ( T o l E A c T a C W S R v N O E n A Tl oi C H N T e Q r O t E T I N f a I L n r A R r i M 0 x e f D t o N M l r A E i p T G S f p R N Y O a I S l B T A 4 A a L R o 5 E c P r p O a 2 L h I 0 A c 1 U d N 1 n N e a A t 1 l e N e s l O D I N d I e S A T i d I D S u e V N O G l t R A S S C i n E L E e P L A I s A e C L g M m U A I V e U C g S I e u R M R iv A r c N R e A E E E l N R T H S a r f M O A C s r h o E B M D o y e M e T AD N p t S p T n I LA E S A is i D o E C E c g N r i GH N L $ D i n A t NR A BS l e r m t d r 0 o [ r i p IE N AE t i TV E MI T t e a c l e c r AO TR UL I s t e le i h L a c R NO SP I W W S E B O T L a a t u t A s ED IB NP e e PN AA OU T O - U T R D OA M1 CS 1 2 3 4 S a 'c>r_ 3 s .>u 6 7
Reactor _Il ree Mile Island-2 f Case 10TAL DIRECT COST ESTIMATE SHEET OF_RADWASTE TREA1Hf NT SYSTEM ~ IOR t IGifT-WATER-CO0l ED MfCLEAR Rf ACTORS Description of Augment Alet e charcoal filter from condenser air elector DIRICT COST (1975 $1000) BASIS FOR ITEM LED EQUIPMENTfMAT AIALS _ TOTAL COST ESTIMATE 1. PROCESS EQUIPMENT 3.0 7.5 10.5 chiller. heater, charcoal 2. BUILDING ASSIGNMENT 3.0 1.5 4.S 5 2.0 1.0 3.0 allowance J 3. ASSOCIATED PIPING SYSTEMS 5-o u 4. INUS*:dTATION AND CONTROLS 0.5 1.5 2.0 allowance S. ELECTRICAL SERVICE 0.5 0.5 1.0 allowance 6. SPARE PARTS 1.0 1.0 9.0 13.0 22.0A With labor factor " 1.0 SUBIOTAL 1.6 laboc multiplier ** = 14 27 includes labor multiplier x 7. CONTINGENCY 1.5 1.5 3 8. I0f f L DIRECT C0515 15.5 14.5 30 r-, C. f.
- per Reg Guide 1.110 p 53 approximate values
- per page to.7-A4 S/76 7 6 - 313
Reactor Three Mile Island-2 Case G ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET CS RADWASTE TREATMf NT SYSTEM FOR llGIT-WATER-000t f D NtlCLEAR REA! TORS Description of Augment remove evaporator distillate demineralizers from CVCS condensate circuit COST (1975 $1000) ITIM TABOR OTHER TOTAL BAS 15 FOR COST E*TIMATE 1. OPERATING LABOR SUPERVISION
- 1.H 1500 hrs operatio< - 107. attendance AND OVERHEAD 2.
MAINTENANCE MATERIAL AND 2.0 allowance iABOR 3. CONSUMABL ES, CitLMICALS, AND O.9 12 f t. per yr O $75/ft ,y SUPPLIES [ 4. LTILITifS AND SERVICES 0.2 12 ft U $20/ft disposal cost Waste Disposal Water Steam Electricity Building Services Other 09 5. 10iAl. O AND M ANNtlAL COST
- per Reg Guide 1.110 p 65 approximate vs. l u e s
$/76 2.9 2d 4.9 / t - i.i
) i e s r p ap 0 s 5 1 r I e
- 0. l i
f I I 1 p r I i e V t p 6 l o 7 E r u / E om l 5 T t A S t ( e i M A c r s u RI ao s OT a c FS f b t t C r E S a i i i S S rl nn IT c o iu SS n AO ,n b s e BC i ae eo t t s l d nw a f e i u ot s r t l n 2/ t c r r e 1 w i n oo d wi f f n M o 0 _ 4 0 0 _ 0 40 t i c g L S A e Y S T 6 6 H 5 n 1 6 5 98 S O C T 34 4 49 1 i V h i C = M n T S i A R o E O r R I f T CA E r S T R e L S ) A A R z 0 I W A i 0 R D E 0 E l A 1 T t a 0 2 0 0 0 0 2 2 R C A U r M F N e 5 / 3 2 3 3 1 2 - 2 4 O n 1 2 2 7 T D 9 N i T E 1 E m ( M E L E O e P i O T I t S C d S U O Q E R e C E T l t A l T M A a C I W l E T l R S T I E i i t D T I t G s S t i O C R d O R 0 2 0 0 28 0 t. 1 7 T F r O 3 C B E o A 3 4 5 2 42 4 A R DI t L 1 2 2 a 7 r L o o A p t T O a T v e 2 e = g a d e p4 n v A a o r t l m e e7 S s e L i ei I r O l l 0 S R p s 1 e M T N i l t T O t t e i n S C l s g e Y M m T S D u o a g N N E m S c p e u T E G A C T c A N M N I r S r r E N I h V O r f M M G P O R o e e i C l o l P 1 I I E b p p l I P T S T T n I U S A S T Y C o Q A D T L I C E r l E E N A R N IR i o G T E C A 0 E t ip S N A M P G D S I I U 'R N c r E C C R T E l L 1 a c C l O T C R i A s O e e R l S S E A x N T u S N L P O O R D P B A I E S C T 1 2 3 4 5 6 7 8 ,1 [ r o'u w 6 7
Estimated ..ect Installed Costs for Process .aineralizers Per Regulatory Guide 1.110 Values Without Contingency Reactor: Three Mile Island-2 Case: G G 'o : ,-.c- _3 g .v E. _; r ' E- _l 'i i-_ q = ' ~ 4.: i'c H ._-l- '_- si :_ g :q
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- -d121
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-+ i=-r=?aH i=*=m:H =:iEEEEiEID sa- =izEm EI M =L 1;21===st=M =E= =:+s;p J-- IE==e== =+g+=#es=22=,=+i =. ;= 1:=apg = , N_5 MN-25I~25.'--Di[5-iE.[U N 2--[ ~ L-----E - '"^5'_~i'f'- 53did-~' M I T.#' ;I'_T-:=_i.s Q' j ' "_--'--9;:--j
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Reference:
Regulatory Guide 1.110 dated 3/76 pp 64-68 Assign same labor / equipment / support-facility distribution as per Regulatory Guide 1.110 approximate values. 5/76 10.7-A37 n f (j -t Uv
Reactor Three Mile Island-2 11 - 1 Case ANNUAL OPERATING AND MAINTENANCE COST ESTIMAIE SHEET OF RADWASTE TREATHENT SYSTEM FOR LIGHT-WATER-COOLED NUCL EAR RE ACIORS Description of Augment reinove first detaineralizer from dirty waste system COST (1975 $1000) ITEM 1 ABOR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR. SUPERVISION
- 3.3 nll 2 dirty waste AND DVERHEAD 3
558 x 10 gg>y 2. MAINTENEE MATERIAL AND 1.0 allowance LABOR ,8 3. CONSI LES, CilEMICALS. AND 12.0 160 ft [>er yr 0 $75/f t y for Ull-2 dirty waste b a> 4. UTILITIES AND SERVICES 3 Waste Olsposal 3.2 160 ft 0 $20/ft disgiosal cost for Water THI-2 dirty waste Steam Electricity Building Services Other S. 10TAL 0 AND M ANNUAL COST 19.5
- cost bases tier RG 1.110 l>. 73 alii >roxinate valines 5/76 s
7.5 12.0 19.5 ~ cn - 1 76 - 3:n
Reactor Thrae Mile Is12nd-2 Case H-1 Description of Augment remove first demineralizer syctem from dirty was :e TOTAL DIRECT COST Detail Calculation Sheet Item Direct installed Cost First Demineralizer Base $188,000 = direct installed cost for two Cost demineralizer units (1 oper & 1 spare) per detail estimate sheet, page 10.7-A40 Cost Assignment for For Case H-1, multiply the above cost by 207 Case H-1 to obtain Eh!I-2 dirty waste cost assign =ent* Cost for Case H-1 20" x 5188,000 = S 37,600
- TMI-1 E IMI-2 misc wastes are both processed in the TMI-1 misc waste system.
T:: fMI-1 misc waste sy stem components prorata assignable to each waste are k'a s t e cal /dav davs/vr cal /vr x 10 ". of total TM1-1 equip drain waste 200 310 62 2 ". TMI-1 clean waste 0 TMI-1 dirty waste 1800 310 558 207. IMI-1 regen easte 0 TMI-2 a~ vip drain waste 200 310 62 2 ?. IMI-2 9 waste 0
- TMI-2
- -. vaste 1800 310 558 207.
- TMI ca waste 5000 310 1,550 26" Total misc waste 2,790 100".
5/76 10.7-A39 o 76-4d 'i \\l s
) era 6 p 7 s / r S e 1
- 0. l i
6 p 1 r n i. i a t e s l p e r u o r om E / t 1 T A w c r ( e M ao s RI t f b a OT a FS i a t t C E n rl i i S u o nn IT b s uu SS AO i ae BC s l d eo p u nw hl ot 0 t c 5 i n r r 1 wi oo f f M E 0 T L S A g 8 Y T 5 S 0 c 2 96 8 48 S O T 1 I 1 n 68 91 T N e = IH t T S s A R a E O w R T T CA y t 5 E E T R 1 S r ) A A R i 0 I W A d 0 R D E 0 E A L 1 T R C m A i o M l F N r 5 / O 7 T AM S 6 6 2 1 4 5 D f 9 4 4 T E 1 m E t ( E 0 P e H 0 T S C t S l 0 s O 0 E R y C E T E s T A T M A C I W r E T R e S T I E H z D G i T I l S 1 O a C R r 1 O e R 4 T I O C n B A E i A o 9 4 85 4 9 R m t t 24 4 7 I e D d = 0 L 1 A t T O s e T r g 2 i a f p4 d A n e t - a v r e7 l o e
- e. 0 S
s m L i I e O l 1 S R p r M T e E N i t e l t T O t s g n S C l o a i e Y M m T S D u c p g N N E m S e u T E G A C T r r A N M N r S e e e E N I N V O r f M M G P O R o C pp h o I P 1 I I E ka> T I P T S T T n I U S A S N. Y C o Q A D T L T C E r i E E N A R N R o G T E I P t C A E I t ip S I C R T E 1 N A N G D S I t R N c r E D I L O T C R T A a c C l s O l S S E A x N T e e R u S N L P O O R D P B A I E S C T 1 2, 3 4 5 6 7 8 -. >)_ o ' a Lb c". h 3 6 1
Estimat irect Installed Costs for Proce emineralizers Per Regulatory Guide 1.110 Values Without Contingency Reactor: Three Mile Island-2 Case: H-1 6 ' j_e=y 17-t t t.=p cy .,. g-p = =--r
- r=.
- g gg1:gg3-1 g ; si- ,==- =m_ y, _ -.g .wi=+:- v .= ggg =-i g&y 3=, m =g-
- =.
mig- =,gsy _ gi
- -ii + :q
_ _. =.g (.g = =. = = = = =_= 5g_ az = - _ 3-5,-_
- _: = = =
7 5 555 g',_5.^ :- 3=--g: .=:.- __5 5._-_zy - 5_5 - ;555 5 _ g_5_ __._5 3._ _ 3 5 =; 3 .._3; j'_L.__ zz. _ ((gg z _1 g.1 r :1
- gg --g___---_ gi g_-
~ =?hE? L-D':d:m2a 3 -~-f 2 =? M'
- 6-r; V+~hE== E~=-;-U i =? i W - M= = = E' i~
^ = = = - 't~ =# ^
== ='
= -+- - r rE = =
=_
=
n=E r !!=
- 2
- 4=_
w= g + _ = _ i:3 ~== M mi--;(- i+5 n r=-5.3.. J=b:-- NNI-5. bE :;dii5 b:~ I --5: $ -5 r-3@-I-N5 =~}fN=NN^5-5-55sfi5 d-=i^_' ii -N 'j-_t=- -i=21:1-_- E = I:-5b5}~._Q -- : =--E EE$ g= =-- 5- -- - - - - - -_,__.._a----._=t-=.-.- = -. - - - - - - - - - - - - - - - _ -- g 5-- _5._= - =:: ---- - - - - - - - - ----~----=.g a O 5 a
- .4 2s
/ / Qg l ,f U* m I y _2==g_-_._ tc wj -_ 2-3-4. - =Z--P .=. = ? = 1== O O= 3 33.=J- :t I - li:-i-i 15.Ef
- - --: = - p - -3 :1 ; =?i = 25 ';,.& -: - -
_ 4 =ig_ u_: d:=-rJ3 _;=--{=3:r.Ei : 3 3
- F m_g+_=g g=4:=g _ _ _, _,_ __ _ =,__
3,3 g==q g_ - -. _m g 3_t : _2-;g=gg_ g 3,;.,7g__77gg;
_ __=__g
=;j g _g ., = = = _,_ ._g j __ =i 7= ,E Wisk. _~ _:hU kE=- hi.[.Eb _ 2 -[iSUUE=bN -khii-2. M165li=-hb.bi b5--i--Ei =NMig-ihEi[Mii!UUA:h=-j m__..___ ,M M-Ehk!N*-iM__ Ni 5_? ~_--N. " If:f=~i-!M d -E=ss9= N = l"9E jd_!.=3.9 =M E =4+W *V-132 ~~=7 -* E==E i = i =i ~~ , t=: w-- - :-- =m=== = ---~ = = =r= = = 1 ---g==== g-- = i=== m -ni=--tg_=r.x-il=;= z =. = = - = u i== w=.=ipp. = #-4.iii ; -. d yl_5_-5 st"__sh.!!E!M ~- "_LM=d"_"_- =."- "._'_ _---=8".=ii-i s=9 E==* mmh.__. -.----- i=i_'s ".=__' _i'._ f =M i--EM '== s,-. '.. _".. tmh t: =-i+_r=3_ 3] 3; ~ R 2 IDa' ' a- { _1 i a 2 2 5 -d cu e i
- !b
- ' E P-@=: : -
- =. i=
=. 's - si'E-Esit E-+;qsg:ra :-: : [pbb
==- _zz== 1 - r=g = = #= _ 2 ___=;_- 83" i M =i= +=m== r M==;s==_ im 3E-:==-i +E- =B=t=E =+* ir= H:"ir li==H = -
- 1'=E-i=-t-! = = i-EE=e+i =
==si--i-----=='====1=.: }2) g _l_i"=ititi!"=i=_i=i"-~ ~ " iWi "_i= ~ __M = "= ~i ;i='== ~ 'i _M; 3hb =- bd =i-!=.+N=5iMN_: ._________'5--iih[==d 5-k---h ,a. y.g
- P' N
U [ m F_; =5 ETsE2 -=ti! M_1Ji-j = #sE #:"Ephi-i 1.- h==11-ir+;3ri--51_ =pe=V;g=ggiy3 _ =3 wgiiM:n-p E+n=_=i=sgg =rm:;=gggy a M , F =.,*I = -I '--i-- E i En--
- s-Z.T iif""==
==t=. =_===i EItEl Edi===="V=iff=ii:r-;'-E5"EEi?gi= i = = - ~ =- M=-r = " - = - '=
== 0
- ==m = E __C r a== --
- ====2 x;n _ i
- x__ _a_ur r.;3e sdaMPjjjdu.4= =E =iE- =--i?i=-._f_wu_(_ _g,g..a i mgg3gg=: m=? g===== -- 3
- -- a
' ~ -i ^M DT- "H'_- a.- L ;be?--r'ete2er ~ ;.' h, a a 2 = 10 10 0 DEMINERALI2R SIE, CU. Pr. RESIN
Reference:
Regulatory Guide 1.110 dated 3/76 pp 64-6a Assign same labor / support-facility / equipment distribution I, s as per Regulatory Guide 1.110 approximate values. 5 g \\i 10.7-A41
I 6 2 7 / 1 e S 1 t t s s a t o w f c / es E y 5 l T t 7 t a a A r $ n o" e s C M t I d G m p" i e s T E" 0 1_ 4 a S n s E w 2 r g i i T yi dI 2S2 T y S 1 s 8 N O 1 t rs 3 E C T H r 1 e a T i R p f A d O y e / # E F R p nt 0 I n S g i s 2 " T r I s a o E S r 3 e ew T A S f B g c r O A g n y Y W a t 3 D S A R x w t r t o fi f R O g l d T s F C O A y l 2 2 E s S a 1 x 1
- T R
E r E R H A e s S E z e L i u E C L l 8 5 l T U ) A 4 0 4 N a 0 T g 1 a M r 0 O v I D e 0 T g 0 O O 2 T E 1 e n S L E O i t O m 5 a T C 7 i e n S 9 O R d 1 i C E ( x T e o E A T C W t S R r N a O E p A T C H p l N H T E G O a l T I i N L t 5 I A R s 6 M O i F d p DN M r 0 A E T o 1 G S t R 1 Ni S a B Y O r A 1 A o L R p e E P a d O v i 2 e u L A G d U e n N v g N a A o e m R l s e N I r O D r I N e S A T e I D S p V N O l t R A S S C s i n E L E e M e P L A C L m U A C I s A s g S I I V e U a e u R M R r R T H S a ic N E E E l N b e A v A f M O A C s r t h o E B M D o y e M s T T AD N p t n I LA E S A s i S D o o E C E i c g N c r i GH N L S D i n t NR A BS E r i A o t ip IE N AE I e r m t d r 0 TV E Ml T t e a c l e c r AD TR Ui I s t e e i h L a c R INO SP L a a t l u t A s ED B NP I W W S E B O T e e PN AA OU T O R D OA Mi CS U T 1 2 3 4 5 h. 5 e ? 6 7
Reactor Three Mile I nd-2 Case H-2 Description of Augment remove evaporator distillate o minerali:er system from dirty waste TOTAL DIRECT COST Detail Calculation Sheet Item Direct Ins:alled Cost Evaporator $98,000 = direct installed cost for two Condensate demineralizers ( l oper & 1 spare) per detail Demineralizers estimate sheet, page 10.7-A04 Base Cost Cost Assignment for For Case H-2, multiply the above cost by 207. Case H-2 to obtain TMI-2 dirty waste t Cost for Case H-2 207. x $98,000 = $ 19,600 TMI-l & TMI-2 misc wastes are both precessed in the TMI-l misc waste system. The TMI-1 misc waste system components prorata assignable to each waste are 'Jaste cal / day davs/vr gal /vr x 10 ". of total TMI-l equip drain waste 200 310 62 27. TMI-l clean waste 0 TMI-l dirty wacte 1800 310 558 207.* TMI-1 regen waste 0 TMI-2 equit drain waste 200 310 62 27. TMI-2 cles; wast 0 TMI-2 dirty <ast, 1800 310 558 207. -te 5000 310 1,550 567 TMI-2 regen wu Total misc was..e 2,790 1007. 10.7-A43 5/76 76-4d , n q' G \\n
) erap s r I e 6 i 7
- 0. l I
/ I 1 p r 5 2 I i e 1 V = t p l o 1 E r im E l M n oi T A Si t ( e M A s c r s RI e ao s a OT , r f b t t FS i C E S/ a i e S S w rl n n IT o u u t SS .i b s s AO a BC s ae e o w t p l d nw f u ot y 0 hl oo_ r r t 2 5 t c r 1 1 i n f f i wi d M E m 4 0 4 0 0 0 L. T L g S o A Y r T 6 6 P e 1 65 9 H S f O 1 n 34 4 4 )' T T N m E e H T S t l A R s O y R T s T C A E E r 5 T R e L S ) A A R z 0 I W A i 0 R D E l 0 E 7_ A L 1 T a R C A 0 2 0 0 u 2 U r M 0 2 F N e 5 / O n 7 T 3 2 3 3 I 2 4 D 9 N i 1 / 2 E E 1 E m E L ( M E O e P f O T I i d S C S U O Q E R e C I = T E t A T T M A a C I W l E T l R S T I i E H D G t T I s S L i O C R d 0 2 0 0 2 8 0 8 O R 5 T F r 0 4 C 8 o 3 4 5 2 42 2 4 A E A R t 1 2 2 t I a 7 D r L o = O A p g I T a O T v e 2 e g a d e p4 n v A a o r r - l m e e7 s e S i p L I r O l 0 S R p s1 e M T i e E N t s e l t T O i n S C l ag e Y u b a M m T S D m p g N N E 5 e t T E G A C 1 t e A N M N I r S s r E N N V o O oe I r f M M G P O R i C c p h o E I I I I E b P T T S P T S T N n I U S A S Y C o Q A D T L I C E r i E E N A R N IR 3 o G T E C A t E p S N A N G D I P t i S I I I R N c r E D C R T E l A L a c C L O T C R i s O I S S E A x N T e e R U S L P O O R D P B A I E S L T I 2 3. 7 8 4 S 6 Lb 6 7
Estimated Direct Installed Costs for Process Demineralizers Per Regulatory Guide 1.110 Values Without Contingency Reactor: Three Mile Island-2 Case: H-2 0 19 m =.-mz#g _ - - g _p w r_ r.-71 = r--m m g_q r =_-- w g c._E===-g;7-.p p g iiir4-
- m.=.4-
. ; =q
== =fI-iz-4i Eit=:1EE i=t 3-- =:1 = ?==-f--i -==lerEiE + H-!!i i "i"=+J-+ 1 %=- = i= !-'i-i== - -- = E i-14= i' = 'i = = n - t=- = -i =_==wd l , ; ~ = = = 'T==2 ===EMiF=_= N=.=.=.= 5'.-ME= 3=+==_:_ -...54==- i= 9=i- !=#=.+=_=-FE:frE+ i= =-M+-i--i = =-#'= E 'mM f-i=i= d4Mi==i = g_._---.-__--_- n ' n =3 . c=.E = = a== ?=- z= a-v = <= =2 ~21 = _ t= =t= _ 35;i=in=.US=n _ ~i =m = = - - =... :==n a i=u - .=vzu
==v = = - i=- UM$NUM-E=i-U Eai~iM ~l-U M ;" 5 55-E==3=-O5-i=ME==in I - = Mi=-d-EEis=7i:rl c
- fr Q'=== q = :=25=h=i= = --f +=== =_=t =hti=E =i=ui=t== m=': _ q -== -E==fz '-i^y =Q ' 42?-2Q=
_+=== ,=_% . _ _ _ _ _ _ _ _ _ = = _ _ _ _. -. _ _ _ =, z ~ 0 a 4 U t ne u E3 / c pe _ e U* c y i e z3 ud,- *% n ti 0; a= ~-i =1:g rw21-h- =M
==== =e a - 1 - =r== r rE- =nes w 4= =+ - = = i. t:% . =i== *===i =ril r=-
=
b++E31 iiEii= Miirs_-7=iisifiE4sii=E5 1_ __ S--ti!Mk =--Ei i=Hi-i=!i EEfM=====i+ is f-' i-E= f ri i==Ij k' -t- '- - 7=ri- - =
==i=1 g % =~~"' = E=E- =.= =~ - ^' =
=='tf t.T 2 ^: T=== EG=.=_ =~-f_f_ _=_=_-.=_: -3 i=_ 4Ki * --9t ~K=;;er=_=-E Eib==E=:=5=i=^i =:= _ a __ _ _ _ _.._ =., m.=_.. ___--__.__-3 ._ p ,w n_.,,.,_-- .. y _ _ p _.__n ' !21-.*'* TH EC+ i _ MEf E==" . f it 15= fi=+i E'_E;_ t+-- d="' bb .h 1 ; =+nf.4F@i :=lii.-i-;iipj i= M FMil: i_=i-E4; tt==tPE==+p=+E=-i3=i-fiift M=i .} E_:=E 4 E - ;;=.e =.=i E i: -: =i = t= i 5 ? E-bi-i=J3= % i=ii:9:1E=i= ="=EiME!!Ei'i!E'=sil ~E~r== _4 n=rn-s==.i =2=U -fiE
- -+-M4
- ?id:dx.Et hi-'E::i. -.._.. _ -. ~ ~.i~.3M-~ !"==
== -, #.--=-r-~ x x. - xx x x_ : r-- ~ x__.n__ _zr.. _a ^.r"_".k= =E!-&i5i ~ _ =- !== r -~ x x x- - - X: ~~====A^- "= i-i=5hi.-h ^ ' =:=~ = = bia'~;.3 s-s t4 2 a g z I d g muos cm . a r 2 I UE !. ! $. [. M =f 9 M i .=m=maniczn== =D=== -=W. = T ndMIH=P- - - - =
====s=-. - = =. =--=======-..---:=-=--- . = = = - - _ iM N ' "M ~F +E 'i i"*" M <- " * -~4~' E -" ~ = rw n = = = === = - , w =h_,==-===- T :==.::===_ - - - =. ~. = -= = = = - _ ~ .. - - -. - _ - _ _. - - -. -==r
- =-
==t====-*"-- _=r.-.-... = z, a --_:rn---.-.=.==--=__=:=.=-===r=-" .,-'.=-a. - - - - = - - - - y,. = :. w_ a g, r '- --.__---_=_.;_____., 3*> t-P n c SENEi~i_3 = i=_ =E Ei t:5+JiEi'IrQiili i=E
== #_-'iiTiW'-i i E 2EN-Ei==. * =.5-45i'5Ei l'=F = E i--ib M
- E P= E--==EE =M F !Ni -55*E hh?]iiE==h =%-I-MIdE i
^ E J E=- va_ =E E +=1-5== ---=-in
==r= 2 -55:=Ezr 22:g==t=c=== =si =t =_r5:=-22-i.=-i=4=-- = ===-- =._iz_=En =-s p - ~--21 ret=== =E ihb
==-
=
=- v mr =.==_-_=.:===--z.n ;=. n;_== :; M s a_; m i m.= a =2- = - - n==a=_.p- -- a a =*;m:1== -n c= = =..._. _
-r :
. = =-- -z==-a===. . _ = - - - - =- = - - - = = = = =... a e__ __ 3' ~ ~ - ~ ~ ' ~ ~ ' ~ ' EN " ~ ~ --*"-~ ~ ='~s w = m rrm_ m - tr n--' _mw '] - 5ver-dic iHeeemervica-~ ,._r m fe r = uu i ( i a a a e e 7 eoe a s s e 7 e e, a a 4 s e 7 e e ' 10 100 i ? DEMINERALIZER SIZE, CU. ET. RESIN i i \\t
Reference:
Regulatory Guide 1.110 dated 3/76 pp 64-68 Assign same labor / equipment / support-facility distribution as per Regulatory Guide 1.110 approximate values. 96 10.7-A45
Reactor Tlaree Mile Island-2 Case 11 - 3 ANNUAL OPERATING AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSTEM FOR E!QlT-WATER-COOLED NUCLEAR REACTORS Description of Augment remove evaporator from dirty waste sys teia COST (1975 $1000) ITEM LABOR OT11ER TOTAL BASl$ FOR COLT ESTIMATE 1. OPERATING LABOR, SUPERVISION' 6.7 THI-2 dirty waste SSti x 10 gpy AND OVERHEAD 2. MAINTENANCE MATERIAL AND 9.9 THI-2 dirty waste assignment LABOR 3. CONSUMABLES. CHEMICALS, AND ,o SUPPLIES Y 4. UTILITIES AND SERVICES 29.8 Waste Disposal Water 10.0 Steam 16.7 Electricity ne8 Building Services Other 73*I 5. TOTAL 0 AND M ANNUAL COST
- per detail calculation slieet, page 5/76 63.2 c-;
9.9 t'T 73.1 76-la
Reactor Three Mile Isicad-2 Case H-3 EVAPORATOR SYSTDiS ESTIMATED ANNUAL OPERATING AND MAINTENANCE COSTS Detail Calculation Sheet Description of Augment remove evaporator from dirty waste system I. COST BASES (per Reg Guide 1.110 dated 3/76, pp 60-63 approximate values)
- 1. OPERATING LABOR, SUPERVISORY AND OVERHEAD a) dirty waste volu=e:
1800 gpd x 310 days /yr 558,000 gpy = b) Use 1 hr labor per 1000 gal waste handled (approx Reg Guide basis).
- 2. MAINTENANCE MATERIAL AND LABOR a) Use 7%
- 7. of estimated equipment cost
- 3. CONSUMA3LES, CHEMICALS & SUPPLIES
- 4. UTILITIES & SERVICES a) Waste disposal: clean waste; use 100:1 feed / conc ratio dirty waste; use 50:1 feed / conc ratio disposal cost = $20/ft3 concentrate b) Water:
Use 4 gal cooling water per lb steam used (= about 30 F rise) Use water cost = $0.30/1000 gal c) Steam: Use 10 lb steam per gal waste processed x 1.5 for heat losses, start-up,3 idling time allowances, etc. Use steam cost @ $2/10 lbs II. CALCULATIONS FOR ESTIMATE SHEET (per above bases)
- 1. OPERATING LABOR, SUPERVISORY AND OVERHEAD b) Operating labor hours:
558 hours @ $12/hr =$ 6.696 /yr
- 2. MAINTENANCE MATERIAL AND LABOR a) 7 1/27. x $ 661,000 x TMI-2 dirty waste assign =est @ 20*. = $ 9,900
/yr
- 3. CONSUMA3LES, C3DiICALS & SUPPLIESb
- 4. UTILITIES & SERVICES a) Waste generated @
50:1 ratio = 11,160 gal /yr + 7.5 3 1488 ft /yr = @ $20/ft3 dispc -1 = $ 29,760 /yr. 3 b) Cooling water @ 4 gal /lb of steam used = 4 x 8370 x 10 lb steam /yr 33.480 x 103 gal water / year G $0.30/103 = gal =S lo.Osa /yr c) Steam = 15 x 358 x 103 gal waste /yr 8370 x 103 lb steam /yr @ $2/103 = lb =$ 16,740 /yr III. NOTES
- (1) the TMI-2 dirty waste portion = approx 20
- 7. of the total waste handled.
(2) concentrate solidification chemicals are in item 4. (3) dollars = year 1975. 10.7-A47 5/76 76-4k il
Reactor Three Mile Isi-ad-? Case H-3 Description of Augment re=ove evaporator from dirty waste system TOTAL DIRECT COST Detail Calculation Sheet Item Direct Installed Cost Evaporator $ 661,000 = direct installed cost for Base Cost evaporator per detail estimate sheet, page 10.7-A49 Cost Assignment for For Case H-3 =ultiply the above cost by Case H-3 207. to obtain TMI 2 dirty waste cost assignment
- Cost for Case H-3 207. x $661,000 = $132,200
- TMI-1 & TMI-2 misc wastes are both processed in the TMI-1 mise waste system.
The TMI-1 misc waste system components prorata assignable to each waste are Waste gal /dav days /vr zal/vr x 10
- of total TMI-1 equip drain waste 200 310 62 27.
TMI-1 clean waste 0 TMI-1 dirty waste 1800 310 558 207. TMI-1 regen waste 0 TMI. equip drain waste 200 310 62 27. TMI-2 clean waste 0
- ?MI-2 dirty waste 1800 310 558 207.*
TMI-2 regen waste 5000 310 1,550 567 Total misc weste 2,790 1007. ,4 4 \\j s, 76-ad 10.7-A48 5/76
6 7 / S re
- 0. l i
3 1 p r i 3 o = t 1 t l n r u E r om T A o t e M p c r s RI a s o OT a ES v fb C E e a S rl IT SS m o AO p b s BC g ae l d 5 u hl = 2 t c 1 i n wi M f i L S A 0 5 0 0 0 5 01 0 1 Y I 4 9 6 2 6 2 00 6 6 S O T 2 56 6 T N fM T S A R E O R T T C A E E S T R I S ) A A R m 0 I W A e 0 R 0 E 0 E t A L 1 T R C s A, l y M i F M s 5 / 4 2 0 0 0 5 1 3 4 O 7 T 1 3 3 1 2 2 3 - 3 6 D 9 N T I e 1 E 2 3 3 E t t ( M E 0 P s H 0 T I S 0 a S U w O Q E R C E T E y T A T M A t C I W r E T R i S T I E H d D G T I m S L O o C R r O f R 90 7 7 T F O C B 6 3 0 0 0 67 2 9 O E r A 2 6 3 1 4 1 2 2 S R o ( A I D t a = 7 L r A o o T O p t 2 T a v e d e g n a a e r p4 l v e A s o S i t I m L l e 7 e O p e S R e r i h 0 M T E N t s 1 l i t T O l n S C a t e M e Y m T S D u s g e g N N E S o a u T E G A C r T e c p A N M N I o S r L N I N V O h f M M I I I E b e e G P O R b C r r T o E P T I S P T S T p p n I U S A S Y C o Q A D T L T C E r i E E N A R d. I N R o G T I I A t C I t ip S I I L T E I L N A F P G D Y S R N c r E D C R a c C L e e R I O T C R x T A s O S S E A N T U N L P O O R D P B I E S C T I 2 3 4 S 6 7. 8 y ?>$ b l 6 1
Estimated Installed Direct Costs for Process Evaporators Per Regulatory Guide 1.110 Values Without Contingency Reactor: Three Mile Island-2 Case: H-3 L_._...--_.-....._..-_ _ = _ _ _ =_. = =. _. _ _ =_ .__,_,. = _ _ _ _ _ = _ _. - _ = -__.E_. o E- - -- -~ - -.
- : ^. :- M - -
-_T-~ 1' T1' 1..T. ~E:--..--~
- ~-
_,.___-___._...._-1_.. _ a: : :Tr: _ :: n: :.1. _._ c __: ::r---
- - _ 1_..____- - - - - - - -: : - -
- -- - - --- r:-. n:: _--ui : J. 1.- 1 -
A C -^~=:: r ^ :.=r:-~ ~; v. -~ :: '-'~~ _ :~_ ~~J : Y' T ~ - ~~ -~ _~2 L : : T TX._._L. _ -.- - - - - - - - - - - - - - - - ~ - - -
- ---=====
= = _.. _ _ _. z=-_ ^ : 2^^
- ^~ - _ I :-~'~ L : :
' h = 1 =-sikiv =k = u=1====BK-~2= 1E++==t
rs;- i=-wi=-L-5+1 i =J W+= a -iM- =-E i- -m a = i=+ t -== = + - W = = = L = L=M=bi
=- .. n L =:==E*=-~==C- ~=&iit EH;E EW-L=Ei=^E ?##-i ===--E-E~23=1-~ =t E =Ei=-if==-R==i=Eli=i-i 4= iXMr =-uE1.=+uit^= iM- =; iWi=-n=? N ' p-E==+ = = +=+= 21_. unq r= =
== =_=_ _'====, =_= i= 5 =-;; g=E== = ~ - - ! ---; =ggg ; W:.-_ E- - _ z =_= =f -.=+g-i::-[=+ =~=~ = ". imil-1-j ._... -.. = = - - - -. - - -. r__..._. --=-_.-. 3- _ _. m.- z Q k -c
- i I-23 o:
i u-;f W = v% ./ i 9 i 3; .L ....-.. x - = =ar =- at= = =-== ++= w = r -- Y= -=--+++'= r= Ee; =n== M i=m-+s== =au-=== m ',2-4_1 *L ~ _ s-u,==-l'=X : _. _. - M@-"--~"t'=..._.-~=+-_"E=i-- -----6%L*"'" =M' ,-~' al " = ='Mi+ =K=iE =~ = ="-M *"'5W-# [ M=='6.- =E _= ~ 5 = "="" Z - . _. ~ _Z "t"_~= _T Tiii=_J -M-'-W d-E T ~~ =.-~ " "_ _ti 4 _-- _~ - ____. E -~9 =M&-d3~ m._. 3 -s ' ?O= ~ =E-=== =iiiM='%2W=-l==u =rti.==. A15 M*ti2'=pS-M=#E=ii-E!E= i- =2T=i=E EEf= -EU I19 I=i-===-~ H=iE I+-E==_ =i V=EEE5=!!=EuR&E =ii= Ediliide 9=Eii+=t=*= ='ENE-i-43 2-ni^-== =2 - i
"f= r-i e -'E T
fi-i Mi E' MEE n 4 y_ 1.i =i=E9=3= E==- =~E==="===~. -.. - - ~.- __.=...._=._..=_=_,_g... - - -. - _. - - _ - _ _ _ E-i- = =__ _-. , _=. _g_.g_g- -. _ = _ - _ g m 2 {N .a-4 a, 1 I m 2 =, y 1 0 u0 1 s i i
- 33-4 -15=r i-- II
s uibi~=
E=itiHr=E-
==-- ~~ =M2=n14 -2=M-iE = e-i eei"fi-J=:Ej E 29=is=='id I Esi+-iiiiisii;i=ii=-!=Ei!5 iI:ihiciM -=' 2 = = - = d,E[{l-M._-.=..E -- =- = = === i =- ===== ===1_.z i 3Eisg
- _m ihr
^- T6 ~ T 3=== iM== _EMHE--i-iEEiE=-g==-r;x ~ ' ~ ' ~ - __-_-_---_-_-.._.._y.2==.-_..m. _ = - - o :.e,,r.._,__--__.____..._.. _ - - ~ _ _. - - - - -o e N*> Z4 a u
- ___Ni_- E===+i1Ei =+Ei i rile =~ Es ?
Z_-n.E6=. =i*Fiii E E =E5-#Esie=iiiii==:==i--t-- i-i= _~i-AM *i=ti=Hs = E=ii+2isabki-Efi =d a = ni "I I . Eff-J,=._EksliiE=EEEE-fif'E--._M. m.. __T-~~~=~~=.=_-_ ._"_= 95_4~ ;...~=M -.. Wii. = =T=ET= I ~5"= ~ - =T E.- _~~A J.:-s EE; 5- = z g _ _. _ _ _ _.. _ _ _. _ _ _ _ _. _ _ .==z;-___. _u = _2;_ __3 g S 8~ L,u e--w m i n w m -_ ~~ ~_ ___ A d., u & ~.~a-.~~L
- b3
~ ~ i 7 4 i i i i g a 3 4 s. - r. i a a 4 s. 7 e e i a s 4 e
- 7 e e i 10 10 0 EVAPORATCR SIZE, CFM c1 O
Reference:
Regulatory Guide 1.110 dated 3/76 pp 57-59 (l s Assign same labor / equipment / support-facility distributien as per Regulatory Guide 1.110 approxi= ate values. 5d 10.7 A50
B Reactor Three Mile Island-2 Case H-4 COMBI!iATION OF AUCME!CS Detail Calculation Sheet Description of Augment: delete both demineralizers from TMI-2 dirty waste system Annual Cost (1975 S1000) r Installed Total Capital Operat-Maint. Total Item Direct Capital Cost ing Annual (ref: note 1) Cost Cost Fixed Cost Charge 9 16.07. Case F-1 37 66 10.6 7.5 12.0 30.1 First demineralizers (Cost ref: p 10.7-A38) Case H-2 20 34 3.4 2.0 0.4 7.8 Evap cond desineralizers (Cost ref: p 10.7-A42) sum of the above = 57 100 16 9.5 12.4 37.9 Case H-4 f NOTES: (1) This case H-4 is a summation of the costs of cases H-1 plus H-2 (2) The costs of these cases are as shown on individual calculation sheets for these cases. 76-4f ( ) = saving for additive /suttractive type combination cases -p 10.7-A51 5/76
Reactor Three Mile Island-2 Case H-5 COMBINATION OF AUGMENTS Detail Calculation Sheet Description of Augment: remove evaporator and both demineralizers from dirty waste system Annual Cost (1975 $1000) Installed Total Capital Operat-Maint. Total Item Direct Capital Cost ing Annual (ref: note 1) Cost Cost Fixed Cast Charge 3 16". Case H-3 132 231 37 63.2 9.9 110.1 Evaporator (cost ref: p 10.7-A40) Case H-4 57 100 16 9.5 12.4 37.9 Both demineralizers (cost ref: p 10.7-A51) i sum of the above = 189 331 53 72.7 22.3 148.0 Case H-5 NOTES: (1) This case H-5 is a summation of the costs of cases H-3 plus H-4 (2) The costs of these cases are as shown on individual calculation sheets for these cases. 76-4f ( ) = saving for additive /subtractive type combination cases 10.7-A52 5/76
y 6 3 1 l t 7 g s / o 5 c 0 e 1 l s E a T a x s A C M 3 o I 5 t 0I T 5 f s[ I S / i 2 3 5 E 1 5 d 5 5 T 7 T S e 3 N e t t E L M s G f T R a / A O w n 0 E F R i 2 T S n s I e e E S T A g e r O S B e c AW m r n 3 D S e a t t A R t 2 w f f R O s o T f C y T l 0 0 O A s l l 8 8 U a 4 4 E T R e E E R t s l i A s e S E a u L E C w l L T U ) A a A N n 0 T M 5 0 0 6 1 v TI D e 0 O 0 T E g 6 3 6 9 5 e 1 S L e 3 5 t E O r a O 5 T C 7 m m 9 i S O R o 1 x C E ( r T o E A f T r C W S R g i N O E A i C H N i r ai T Q e O E T I z N 3 I L i 7 A R l M O a F [ D r N i e 0 A tt n 1 i i 1 G S R N Y m O I S e B 1 T d A A t R e E t d P s i 2 O r u L i G d A f n UN g a N e e l A v R s o m N I r O D e I e N e r S A T g 1 I J S V N 1 t R A S S O s 1 C n E L E e 1 e P L A C L s m U A C e g S I V e U b e u R I I s A a M R h R T i S a ic N r A E E E l N l v A t f M O A C s r T o I B M D o y e M s T N p t S o n I E S A s r i C E i i D c o c g N N L S D i n A o t A BS E r t ip N AE I e r mt i r 0 d T E MI T t e a c l e c r TR l t I s t e e i h L a c e INO SP L a a t l u t A s B hP W W S E B O T e AA 0U I O R D ML 0S U T 1 2 3 4 S ) ) y e, ol i a 3 M
Reactor Three Mile Island-2 Case I-1 Description of Augment remove first demineralizer from recen waste system TOTAL DIRECT COST Detail Calculation Sheet Item Direct Installed Cost First demineralizers Base Cos $ 188,000 ' direct installed cost for two Cost decineralizers ( l oper & 1 spare) per detail estimate sheet page 10.7-A55 Cost assignment for For case 1-1 =ultiply the above cost by 567. Case 1-1 to obtain TMI-2 regen waste cost assig:. ment. ' Cost for Case 1-1 567. x $ 188,000 = $ 105,300
- TMI-l & TMI-2 misc wastes are both processed in the TMI-1 misc waste system.
The TMI-1 mi.c waste system components prorata assignable to each waste are Waste gal /dav davs/vr cal /vr x 10 ". of total TMI-1 equip drain waste 200 310 62 27. TMI-l clean waste 0 TMI-l dirty waste 1800 310 558 207. 1D11-1 regen waste 0 TMI-2 equip drain waste 200 310 62 27 TMI-2 clean waste 0 TMI-2 dirty waste 1800 310 558 207.
- TM I - 2 regen waste 5000 310 1,550 5 6 ".x Tctal misc waste 2,790 1007.
A 76-ad 10.7-A54 5/76
r e
- 0. l i
6 1 p 7 gn i / g i c t 5 y s l 1 e r u g/ r o m 1 E t T w cr A e M ao s RI t f b OT a FS i a t C E ,. n rl i S 3 u o n IT SS b s u AO i ae BC 3 s l d e p u n hl o 0 t c 5 i n r 1 wi o f M E T L S A 8 0 Y T 5 5 o e 96 8 4 S O 1 1 t e H 2 6 8 9 T T t N s fM a T S w A R E O n R T T C e A n E E e S T R L S r ) A A R 0 I W A m 0 R D E 0 E o A L 1 T E R C r J f a F 5 / 5 O l 7 T D m 5 6 6 2 1 4 5 9 N T E e 1 E 4 - 4 E L t ( M E O s P H O T S C y S I U s O Q E R C E T E r A T T M A e C I W z E T R i S T E H ) 0 G n T I r S L O n C R n O i R T F g O 0 9 4 85 4 9 C g L E i A 1 24 4 R I d L 6 D 5 t A L s A r 7 T f O 2 T f 0 1 d e r n Y e t a o i g m l l i< s e S p p4 I r L i A O t t - e S R l e7 M T E N u e. l i t T O m hO n M S C sI e Y m T S D r e g N N E o S t e; c u T E G A I b T s g C A N M N S r N V a oa i E N I O R l O l f M M G I T S P C c p T o E P I I E T I S P d. T r r n I U S A S Y C e e o Q A D T L T C E r i E E N A R f N R pp o G T E I A E I t C
- ~
- p S
N I R A P G D Y t ir E D C R' T E I L S I N ca c C l O T C R T A s O S S E A N T e e R l I E S C T u S N L P O O R D P B A 1 \\ r 1 2 3 4 S 6 7 8 b 7> l 6 7
Estimated Direct Installed Costs for Process Demineralizers Per Regulatory Guide 1.110 Values, Without Contingency Reactor: Three Mile Island-2 Case: 1-1 Id = =m=z v==n~=ui--'=-42:==+w ti--mzwx r cr = =-z = 1 u ir s=i^ i-e==-mw= =s=wirrm=a += - -+1 =-i V = + =:= = = -=.==r m = a ~ ---i.E-2 h-- t!! -l i_L.+ --i= -i==-i= --
- --4=. _ I i__
== - l_;
iH i 1 : = i --'--El-d'hi--===-i-'t.-
=- % _ r u =9 _ =- '-' i n=. --i..-ir = ?._ _ 5=A A_N=I55lNy-i$.? _ :. 2-Ys =.d = i-b_!=kSW..=l_5i--I V=i II_--d-?.. _ _ _ -.=lI=II=_5-b -i I-
- W. a ii=a -Eweima:
z 1:a
==L Erietz;W 2= pi= =-1 niera a1H= =pi ;q- ;=== =ft-= = > -r+=---+-+- :== = M A=+:mm-%s = w = -
^E
M==:== 2=ita=-:-;=;
==t== m==:u = = i_==22=- at= ' 2= := _=--y=E E y= i=%: = i2--- n==z= 8 - q= =i =5=E=.i-Ez==.:EukE =4,E ^ i-== _~= =_-_ - +H b =^===.L.L6-- -== : ~
==&- ___-.EH=2#h =.== Z- -~ =E =EE =-- . = _-zzsit a =z=: ___Q.K._. _ _._ _ _ __ __-L=, _3--k s = _. __. ny _ = z a E a ~ C
- 4 e
2 22 i - e j o r u-7 x1 w} d=h ir--La=-+ E= =+u- -
; =--+==
==
Rr3_~ =- =+2e=1 zun=we=z==-t wi i = u====2, " = =
La= gau = u-;-m=-=aau=m= a =w+w==; / l M=G EEm t%=aEE-. __ : ~~ Iia =-lExt= E='EniE _E =*E= = - i=-== h=- K=iMWw=s=2-M =a + i+ L 3 A =- =a=4 2=t =L=rn_=+Ei 2 ,E-I_4====.._ Z _~--- ~TZZ =~ ~ =~;~ZZZZ_ T -~ : =E=T~,6z:W=96 ~ l=s--P#2=t= 1 1M== ._=T. 3+3E=-Eg5ME 3 o f ' ;=gg =- - g=- =:= = = :=g- = y_g==.- m a.mg wgwwmmgmu-wm=g;g = = - =__ u = = - = - .b55- -l_9-5-~-~ ~55 5~-E=U ~555-fD_Y._ FE hif=5[ M @ M M E ? 5 M !iM-l5=5 EE== EE 2 -'==-____= _ - - - - __: -.-- = =_ _ ______ _. _ _ _.. _ - - - - ____ _.-._____.-._.__. _ _.. = = _ = _ =. = = f.----__ =# s w M 24 a, - 2 4 e 2 i a d -2, 4-u u
- E ' *_ L
%== r+m1= =m======im+==== =i=2 zi=5 Ea==M =m==um=u?=8 = a-+ x = gam-i== z=-11=# u uzm=in-u-- ;=a = =miM^= = =-i
- i ~ " ! P35 = =-i =5tii=n== = _ - _=- - ===iE===i =-
. -e-_---eeu=;==;Gi _a=i==cta: -uJ.;9 =- -- =a--; ardi-i=E;=+I="=5% ?- -45s'E#d
== u 1 [, 595 r====== _====_- =z ---
==-------_-;m 2R
_3---;---_3----------3;---___-
0 5c m m, _-~ u
- pi-2n w 8241 n 2=uty waga=qit=---
m m 1 =r- . - - = = =
===m--- =g- + me-+ im=.__=. _=;- nez=u:=za.+m=3=w-,=;- -m
- =
2 3g_==_g-------_--_--- -_ 3p_=====gy.
- -----______-g-_;____,_;
4 .E=E~21._Z--_'-'-".'^."_--.~~:'l--'- --~'--Z_-~_~T_-'N -~ ~~ 1.Z
- T_ _ -' _ ~1_'
i.- '- ~ ZZ - ~_ .__:---_..'C.;Z'--Z.'~~T.-'~_-_T~~ .====h=======m m
- =_-
~--- y , c- ~ ~~e x mm; n,. - - he= 5N M iew , < r - 13 5 t^ i a a ..,..i a 3 .7 e e i a 3 s e 7 =a i l0 10 0 Demineralizer Site, cu. ft. Resin -C
Reference:
Regulatory Guide 1.110 dated 3/76 pp 64-68 ., j (,,.; Assign same labor / equipment / support-facility distribution \\' as per Regulatory Guide 1.110 approximate values. ~ i N~ 10.7-A56
Heactor Three title Island-2 Case 1-2 ANNUAL GPERA!!NG AND MAINTENANCE COST ESTIMATE SHEET OF RADWASTE TREATMENT SYSfEM FOR LIGHT-WATER-COOLED NUCLEAR Rf ACIORS Description of Augment remove evap cond demineralizers from regen waste system COST (1975 $1' 3) ITEM IABDR OTHER TOTAL BASIS FOR COST ESTIMATE 1. OPERATING LABOR, SUPERVISION. 1.8 THI-2 regen waste 1.55 x in gpy AND OVERIIEAD 2. MAINTENANCE MATERIAL AND 1.0 allowance 1 ABOR ~4 h 3. CDNSUMABLES. CHIMICAli, AND O.9 12 ft. per yr O $75/ft ~J SUPPL IES 4. UTILITIES AND SERVICES 3 3 Waste Disposal O.2 12 ft 9 $20/ft dit,posal cost hter Steam Electricity Building Services Other S. AL 0 AND M ANNUAL COST 39
- cost bases per RG 1.110 p 65 approximate values S/76 2.9 10 3.9
/6-3a b
Reactor Three Mile Island-2 Case I-2 Description of Augment remove evap cond demineralizers from regen waste system TOTAL DIRECT COST Detail C. .ulation Sheet Item Direct Installed Cast Evaporator $98,000 = direct installed cost for two Condensate demineralizers (1 oper 6 1 spare) per Demineralizers detail estimate sheet, page 10. 7-A 59 Base Cose Cost Assignment for For case I-2, multiply the above cost by 56", Case 1-2 to obtain TMI-2 regen waste ecst a;s i gnmen t e Cost for Case I-2 567. x S98,000 = $54,880
- 1311-1 & TMI-2 misc wastes are both processed in the TMI-1 misc waste system.
The TMI-1 misc waste system components prorata assignable to each waste are 'Ja s t e gal /dav days /vr cal /vr x 10
- 7. of total TMI-1 equip drain waste 200 310 62 27.
241-1 clean waste 0 TMI-1 dirty waste 1800 310 558 207 TMI-1 regen waste 0 TMI-2 equip drain waste 200 310 62 27. TMI-2 clean waste 0 TMI-2 dirty waste 1800 310 558 207.
- TMI-2 regen waste 5000 310 1 550 563*
Total misc waste 2,790 1007 m \\i 76-ad 10.7-A58 5/'6
) erap s 1 r e 6 0i l l r_ p y l 1 2 i i p 6 V - t o 7 1 l / I 5 E r u E M n o m ( T A Si t e M A s c r s s R! e ao t t 0! , r f b a ii S C 1E S/ a nn e S S w rl uu II t o SS is e o s AO ,i l a BC s ae nw w t p t d ot f u n 0 i l rr e 25 dc o o g 1 1 i n f f e wi r M E T m L g 0 4 o, 0 0 l.0 S o A l Y r T _ 9 e 4 9' S O f 6 6 g 5 n 1 6 5 4 T T 1 34 N m tM e I S t A R s O y I T R s T C A E E r s T R e t S ) A A R z 0 I W A i 0 R D E 0 E l 1 A A L T a R C 0 o, 0 0 0 U r M 2 2 2 F N e 5 / O n 3 2 3 3 1 2 - 2 4 7 T D 9 N i 1 2 2 T E 1 E E L m ( M E O e P H O T I S C d S U O Q E R e C E I E t M T T I A a C W l E T R l S T I i E H D 0 G t T I s 6 S L i A O C R d O R 7 T F r O 8 0 _ H. 0 o, 0 2 2 C B o f o A I t L 3 4 S 2 42 2 4 R l a 1 2 2 D r e L o = g A p a T O a p4 T v A 2 e r r - e e7 d e i p O n v l a o p sI m i e l S s e L t s e I r O l a g S R u b a M T e E N m p l t T O t n S C r s r i e Y M m T S D o o e g N N E b S c p e u T E G A I l C a T A N M N S e E N I N V O r f M M G I I E F O R C h o E I S A S T Y C P I b. T S P T S A T T n I U o Q A D T L T 3 C E r i E E N A R 1 N R t G T E C A 8x E o t ip S N A F I P U G I D S I I l R S N c r E D C R T E I L L O T C R T A a c C I S S E A N T s O e e R U S N L P O O R D P B A I E S C T I 2 3 4 S 6 7 8 s e h ? g t 6 7
Estimatec installed Direct Costs for Process demineralizers Per Regulatory Guide 1.110 Values '41thout Centingency Reactor: Three Mile Island -2 Case: 1-2 6 , o r-- y .p.
- --.i:
,u. =. .4n .t-qj - mp..
- n; p-m:
- _a ; -.3-_ r g _ =p ir i ' :-- i+;=_- ;3p - =c;:- = rg =-p =-g--g--;-g=g.- ;=ieg.= _i=-- _-4-- - zw 3.z;,4 m_y-e y, _. - - - - - - = _ _ _.. _ _ _,. _ _ _ _ _ _. - _ _ _..:._.rx = = ~ = i W+ = - : ---++H--- ,-+--$:---_d--~= k -- -l---~ 3 --+ ~- ~ & 5-- ~'- h- - ----+-, = "-H m d s 4.
- x ra m
.- L -
- == =.
.._. m ,=it -......= _,.. = = iF= : =_ :. -_.. n.- :.u : - _1: _ 1_ : -- ;_ _ r__x : - ...... :. ; a===- F - = = 5=.. - - - 2- += =1 , F3 - :y= = := r = -- - -. _.. _ _ _F-i== = s3 =a===__.=__.-I= ---- _ - :. 3 u c =ur- - _ _ _ _.___.._=..=_.==_=____=_:n:=:
- === = i - - q = -- - a H =-
7 = c-- i ( 2 - o* -C n* 23 0 I u-r-- i. z % ".,- f .i j! 10--u _ , g 8 y~~ . ~? .. ~ ~ ~. .7 4 ~~ ~ _ ' ~_. s . mL - ~y . I g g._'.... - - -.
- =1
_ ;_ - p _ _ m yrg,c p g 7 4 M = - - _ , s '; =i=E-- MR=f=:-?===iM:E=_ i==:-Mi=5-i =#i&E_:#WMi : si-MMsg _=i=e + _=-iEi:ssisr=i#= =_i '.--=__;i 3 =_7- - -- .pf--- n _ =~ + .-,-p t =+ ' = t'-5 ~ ._. Rh.. _.. -ij.. _ _j. _ j-Y. --- _0. -+f^ in~ f..__. m-s' _ gf.4-]+i k. __ = g } - =- Y '.... W& - i_ ~. _ _. _-- +-b =_k -h-j l. _. _. _.
- i. J j. _ _ ; :t
. _ n = :.. -.. i:= 2 7-- is"'i u : -... r-- -L ;, j = E i i:1.1-11 t_ :H _ ; _; ; - d -_.r-~i !-NN-kbiiHE-lEih=b 5--$ 1Wh?ibi=._Et id[ :U. 3__.5Uh!95 EU-_-Mi.-!skb=-ib_ b 5MNi=_$= _ _5_. r= 3 zD I a 4 1 n ar i r. .m 1 5 a x.
- u5 4.- r
- i. 0.C
.o. 2 , n . _j_- :-
- t,_
=--nr m.: _
- q 7_-
g _ :.
- :3 -._::_-_
. : n_;:_ m., w q ,7 fm,h ' IN f5- - - M -- ;----$. ' N. 15-NTS-- 9 :: R-Ni 5@ = $ =i' l ' -i'd ~= i. i;t a=t[= : :.dN':~M ' i m i =-'-] s S. },, W _'-Ei2:! =! !+=f._.. Z '.__~EZ l i _;=_i6.l Mf== ~ ~.. '~ ~ ~ ~~ 5 Z -~1==-iMM := =-iW1.._.. M 2 -E -M-d E 3 " n=-*" . ' l O - - ' 'C-I '+L" -%-- dbiH l b
- = mm-m k= g w~ ~ n~ =w' E
II ' UI:~ '~^ U'i <IJ ^~ -I~ ~ ~~5-d ~~ '3 =r m: g =r _ w a=1 m e:. - ;=<. =- + =m - 5 't -& E +=i = 5 # --tt=it= D =..-s-tisMnit=h=n5Maipre=t=a-2==ei=-5 +=f =+a M--i :== a=&4=w---h;_=_. i.,. t =_M.=_r=nr=n:: MUin =g/n f =n=n..5. _ g=;p - - = = = - s-- w.3,. __._ =_ :7._.=__gg-_---_____-__.____=r=-- __. _ _ = _ _ - - - - - _,_ Re u w: s----- ap.m - a - QWT DW~ 2=c%. _, m ii_ w m. i u%r ra w = _a ( 10 too DEMINERALIZER SIZE C". FT. RESIN ~ D
Reference:
Regulatory Guide 1.110 dated 3/76 pp64-68 II Assign same labor /equiprant/ support-facility Cist"ibution as per Regulatory Guide 1.110 appron s "e values. 5/76 10.7-A60
Reactor Three Mile Island-2 Case I-3 COMBINATION OF AUGME!rrS Detail Calculation Sheet Description of Augment: remove both decineralizers from regen waste system Annual Cost (1975 S1000) Installed Total rapital Operat-Maint. Total Item Direct Capftal Cost ing Annual (ref: note 1) Cost Cost Fixed Cast Chirge3 16. 0". Case I-1 105 184 29.4 52.1 3.0 84.5 First demineralizers (costs per page 10.7-A53) Case I-2 55 96 15.4 2.9 1.0 19.3 Condensate demineralizers (costs per page 10.7-A57) Sum of the above = 160 280 44.8 55.0 4.0 103.8 Case I-3 NOTES: (1) This case 1-3 is a summation of the costs of cases 1-1 plus 1-2 (2) The costs of these cases are as shown on individual calculation shests for these cases. 76-4f ( ) -' saving for additive /subtractive type combination cases 5/76 10.7-A61 f U s
Reactor Three Mile Island-2 Case I-4 CC".BINATION OF ACCMENTS Detail Calculation Sheet Description of Augment: Discard regen vaste without trea tment Equipment change: Delete both deminerali:ers and evaporator from regen vaste system Annual Cost (1975 $1CCO) Installed Total Capital Operat-Maint. Total Direct Capital Cost ing Annual " ** l' Cost Cost Fixed Cost Charge 3 16.07 t Case I-3 160 280 44.8 55.0 4.0 103.8 Both deciperalizers (cost ref: page 10.7-A61) Evaporator 370 647 103.5 129.3 27.8 260.6 (cost ref: page 10.7-A63) Sum of the above = 530 927 148.3 184.3 31.8 364.4 Case I-4 l NOTES: (1) This case I-4 is a su==ation of the costs of case I-3 and the evaporator (2) The costs of these cases are as shown on individual calculation sheets for these cases. 'l r a ' 76-ef ( ) saving for additive /subtractive type combin_ 'es = 5i76 10.7-A62
Reactor Three Mile I s l anti-2 Case 1-4 ANNUAL OPERATINC. AND MINTENANCE COST ISTIMATE SHEET OF RADWASTE TREATHINT SYSTEM f0R IIQtT-kATER-000ifD NUCLEAR REACTORS Description of AugmentThis sheet covers the evaporator removal portion only of this augment equipment change. COST (1975 11000) ITIM LABOR OTifE R TOTAL BASIS FOR COST ESTIMATE I. OPERATING LABOR, SUPERVISION, 6 18.0 regen waste 1.55 x 10 gg>y AND OVERHEAD Evaporator 2. MAINTENANCE MATERIAL AND 2 7. tl regen waste atsignment LABOR Evaporator g 3. CONSUMA2LES, CHLMICALS, AND SUPPLIES sJ Evaporator O' 4. UTILITIES AND SERVICES Waste Disposal 41.3 Water 27.0 Steam 43.0 Electricity Building Services Other 5. TOTAL 0 AND M ANNUAL LOST 157.I Evaporator
- per aletail calculation sheet page 10.7-A 64 5/76 129.3 27.8
~~' 157.1 ? 76-la )
Reactor Three Mile Island-2 Case I-A EVAPORATCR SYSTDiS ESTIFATED ANNUAL OPERATING AND MAINTENANCE COSTS Detail Calculation Sheet Description of Augment Thie sheet covers the evaporator removal portion only of this aug=ent equipment cnange. I. COST BASES (per Reg Guide 1.110 dated 3/76, pp 60-63 approximate values)
- 1. OPERATING 1A30R, SUPERVISORY AND OVGHEAD 6
a) regen vaste valu=e: 5,000 gpd x 310 days /yr = 1.55 x 10 gpy b) Use 1 hr labor per 1000 gal waste handled (approx Reg Guide basis).
- 2. MAINTENANCE MATERIAL AND LABOR a) Use 7
- of estimated equipment cost x regen vaste percentage of total waste stream
- 3. C0b5UMABLES, CHEMICALS & SUPPLIES
- 4. UTILITIES & SERVICES a) Waste disposal:
clean vaste; use 100:1 feed / conc ratio dirty waste; use 50 1 feed / conc ratio disposal cost = $20/ft3 concentrate b) Water: Use 4 gal cooling water per Ib steam used (= about 30 F rise) Use water cost = $0.30/1000 gal c) Steam: Use 10 lb steam per gal waste processed x 1.5 for heat losses, start-up,3 idling time allowances, etc. Use sees, coat @ $2/10 lbs II. CALCUIATIONS FOR ESTIMATE SHEET (per above bases)
- 1. OPERATING IABOR, SUPGVISORY AND OVERHEAD b) Operating labor hours: 1500 hours @ $12/hr
= $18,000 !yr
- 2. MAINTENANCE MATERIAL AND IABOR a) 7 1/2" x $ 661,000 x
56
- ('
= $ 27,762 /yr b
- 3. CCNSUMABLES, CHDtICALS & SUPPLIES
- 4. UTILITIES & SERVICES 3
a) Waste generated @ 100:1 ratio = y,500 gal /yr + 7.5 2066 ft /yr @ $20/ft3 disposal = $ 41,320 /yr. 3 b) Cooling water @ 4 gal /lb of steam used = 4 x 22500 x 10 lb steam /yr 90.000 x 103 gal water / year @ $0.30/103 gal =S 27,000 !yr = c) Steam = 15 x 1.500 x 103 gal waste /yr 3 22.500 x 103 lb steam /yr @ $2/10 lb = $ 43,000 /yr = III. NOTES (1) the recen vaste portion = approx 56
- 7. of the total waste handled.
(2) concentrate solidification chemicals are in item 4 (3) dollars = year 1975. .o 76-4k 10.7-A64 {/
- i. M 6
Reactor Three Mile Island-2 Case I-4 Description of Augment This sheet covers the evaporator removal portion only of this augment equipment change. TOTAL DIRECT COST Detail Calculation Sneet Item Direct Installed Cost Evaporator Base Cost $661,000 = evaporator total direct installed cost per detail estimate sheet page 10.7-A66 Cost Assignment for Case I-4 For Case I-4 =ultiply the above evaporator cost by l 567. to obtain its TM'. 2 regen waste cost assignment
- Cost for Case 1-4 56" x $661,]00 = $370,000
- TMI-1 & TMI-2 misc wastes are both processed in the TMI-1 mise waste system.
The TMI-1 misc waste system components prorata assignable to each waste are Waste gal /dav davs/vr cal /vr x 1.0 . of total TMI-1 equip drain vaste 200 310 62 2" TMI-1 clean waste 0 TMI-1 dirty waste 1800 310 558 207 TMI-1 regen waste 0 TMI-2 equip drain waste 200 310 62 2" TMI 2 clean waste 0 TMI-2 dirty waste 1800 310 558 207. 5i" "
- TMI-2 regen waste 5000 310 1,550 3
Total misc waste 2,790 1007. 10.7-A65 1/ 76 76-4d {[
e 6 r 7 e / i S l p i 0 r t o l I t u E a " m T r A o r e M p " o s RI OT a b a FS v a C E e l S IT SS m s AO p l e BC g t u 5 lc 2 n 1 i_ M f i L S A Y T 0 1 S O 0 5 0 0 0 5 1 T 4 9 6 2 6 2 0 6 6 T 2 6 6 N fM T S A R E O R T T CA E E S I R L S ) A A R 0 I W A 0 R D E 0 E A L 1 T R C A ) M L F N 5 / 4 2 0 0 0 5 3 4 O 7 T D 9 N 1 3 3 1 2 2 3 6 T E 1 E 2 3 E L ( M E O P H O T I S C S U O Q E R C I T E A T T I A S M W E T R S T I E H D G 5 I l T a I 0 v C R o O R m T F O C e B r A 6 3 0 0 0 0 7 7 7 E R I 1 2 6 3 1 4 7 2 9 6 D r 2 2 A o = L t 7 A T a 2 O r 0 T o 1 d p r n a e e a v i g l e l a s p p4 I S i A L t t - O e S R l e7 u e M T l i E N m h0 t T O M n S C s1 e Y r e m T S D o t e g N N E b 5 s g e u T E G A C 1 r A N H N I a aa 5 i E N I N V l 0 cp lT f M H 1 P T S A G P O R C o E P I I E L T l 6 rr i T n I t S A S T Y C e e o Q A D T L I O1 C E pp r i E E N A R T N I R o G T E I A 8 E t C i 5 I I N P Ux G D p 5 N A t I R 5 N c r L D C R T E I L L O T C R T A a c C I I E S C 1 s O S S E A N i e e R U S N L P O 0 R D P B A I 2 3 4 5 6 7 8 I 7' i e ? ?,$ l 6 7
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Reference:
Regulatary Guide 1.110 dated 3/76 pp 57-59 Assign same labor / equipment / support-facility distribution as per Regulatory Guide 1.110 approximate values. - - 7 5/76 lO.7-A67 [ s., v}}