Control of Volatile Organic Compounds Emissions from Manufacturing

Table E-3. CAPITAL AND ANNUAL OPERATING COST ESTIMATION PROCEDURE FOR'
STEAM-ASSISTED SMOKELESS FLARES
- - Y 1 l I _ l - r - - - - - P m - - - - - - - - - --=,,----~.--=d?lr;a---=
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Item Val ue
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Capital Costs
Flare- ourchase cost. C1 ' ~1 Select from Table E-2 if val ue given'
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(Oct. 1982 $)
or use equations:
(3905.7) + (35#.054) H x D + (900.36) D.
- (126.08)~2, fair 20 ( H 5 40 ft and D < 8 in.
(6275.6) + (2214.10) H -i-(12.782) H x D
+ (24.856)~2, for 50 5 H 5 200 ft.
or from Figure E:-2 if H = 40 ft and D > 8 in.
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Fluidic seal purchase cost, C1 'fl.s. See footnote a.
(Oct. 1982 $)
Flare system purchase cost, C1'fl C"lf1 + C1"fl ,,s.
Flare installed cost, ~ . ' . ~ 1 - C1 ' fl x 2.65
(Oct. 1982 $1
Total installed piping costs, C', Method of Appendix E .6
(Aug. 1978 $)-
Total instal 1 ed ducting costs, C1d Method of Appendix E .6 - *
(Dec. 1977 $)
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June 1980 Installed costs
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Total flare system cost, (Cp + cd + cfl)
Csvs
~Ill
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