Control of Volatile Organic Compounds Emissions from Manufacturing

-___P___P_5-==-=-
Table E-11. CAPITAL AND OPERATIONG COST ESTIMATION FOR
CATALYTIC INCINERATOR SYSTEMS (Concluded)
P - - - - P - - r - - - - = - = 7 - ---
Item Value
Electricity ($0.312/scfm) x (Total gas volume
flow rate (Q4), scfm, Item 5 from
Table E-8) for units with no heat
recovery; and ($0.78/scfm) x (Total
gas volume flow rate (Q4), scfm,
Item 5 from Table E-8) for units with
heat recovery
Indi rect Costs
Capital recovery (0.1627) x (Total instal led capital
cost, $ from Figure E-5)
Taxes, insurance and (0.04) x (Total instal led capital
administrative charges cost, administrative charges
$ from Figure E-5)
Total Annualized Costs Sum of total direct costs and
total indi rect costs
aUpdated using Chemical Engineering Plant Cost Index from December 1979
(247.6) to June 1980 (259.2).
bpiping updated using Chemical Engineering Plant Cost pipes, val ves, and
fittings index from August 1978 (273.1) to June 1980 (329.3). Ducting
updated using Chemical Engineering Plant Cost fabricated equipment index
from December 1977 (226.2) to June 1980 (291.3).
%ee footnote c, Table E-7 for discussion on application of these costs
developed by Envi rosci ence (Reference 25).
d~pdated usi ng Chemical Engineering Plant Cost fabricated equipment index
from December 1979 (273,7) to June 1980 (291.3).
eTotal gas flow including waste gas and additional combustion air.