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PROFITABILITY ANALYSIS (2008 prices)
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A.
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Direct Fixed Capital
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188524000.00 $
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B.
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Working Capital
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4087000.00 $
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C.
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Startup Cost
|
11311000.00 $
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D.
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Up-Front R&D
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0.00 $
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E.
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Up-Front Royalties
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4000000.00 $
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F.
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Total Investment (A+B+C+D+E)
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207923000.00 $
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G.
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Investment Charged to This Project
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207923000.00 $
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H.
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Revenue Stream Flowrates
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|
|
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Total Flow of Stream EtOH
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119454958.00 kg/yr
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|
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Total Flow in Steam
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10153761372.00 kg/yr
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|
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Total Production of Recovered Steam
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9,999,000,000 kg/yr
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|
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Total Energy Content of Recovered Steam
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2,844,215,150,040 kJ/yr
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|
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Total Requirements of Steam (High P)
|
652,362,126 kg/yr
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|
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Total Energy Content of Steam (High P)
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1,130,708,220,559 kJ/yr
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|
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Total Energy Left over for Electricity
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1,713,506,929,481 kJ/yr
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I.
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Production Unit Cost
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|
|
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EtOH
|
0.68 $/kg
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J.
|
Selling / Processing Price
|
|
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Total Flow of Stream EtOH
|
0.84 $/kg
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|
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Total Flow in Steam
|
1.60 $/1000 kg
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K.
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Revenues
|
|
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EtOH
|
99833000.00 $/yr
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|
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Steam
|
16199000.00 $/yr
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|
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Total Revenues
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116032000.00 $/yr
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L.
|
Annual Operating Cost
|
81119000.00 $/yr
|
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M.
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Gross Profit (K-L)
|
34913000.00 $/yr
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N.
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Taxes (35%)
|
12220000.00 $/yr
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O.
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Net Profit (M-N)
|
22694000.00 $/yr
|
|
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Gross Margin
|
30.09%
|
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Return on Investment
|
10.91%
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Payback Time
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9.16 years
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