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part 1: overview of cogeneration and its status in asia - Fire

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Sample case study <strong>in</strong> a pulp <strong>and</strong> paper mill 111<br />

2.3 Calculation <strong>of</strong> Costs <strong>and</strong> Benef<strong>its</strong><br />

After evaluat<strong>in</strong>g the technical potential <strong>of</strong> the alternative <strong>cogeneration</strong> systems, the different<br />

sources <strong>of</strong> revenues <strong>and</strong> expenses <strong>of</strong> the systems are determ<strong>in</strong>ed so that the evaluation <strong>of</strong><br />

the economic potential <strong>of</strong> each system could be followed.<br />

Table 2.7 Summary <strong>of</strong> the results for the gas turb<strong>in</strong>e<br />

Thermal Match<strong>in</strong>g<br />

5,000 kg/hr 13,000 kg/hr<br />

Power Generat<strong>in</strong>g Capacity, kW 2,493 6,482<br />

Power Generation, MWh/year 18,673 48,550<br />

Excess(+)/Deficit(-) Power, MWh/year 5,958 35,835<br />

Excess(+)/Deficit(-) Heat, TJ/year -55 111<br />

Fuel Consumption, TJ/year 269 699<br />

Power Match<strong>in</strong>g<br />

1,500 kW 2,430 kW<br />

Heat Generat<strong>in</strong>g Capacity, kJ/kg 3,008 4,873<br />

Heat Generation, TJ/year 62 101<br />

Excess(+)/Deficit(-) Heat, TJ/year -96 -57<br />

Excess(+)/Deficit(-) Power, MWh/year -1,480 5,485<br />

Fuel Consumption, TJ/year 162 262<br />

2.3.1 Costs<br />

(a) Total <strong>in</strong>stallation cost<br />

The <strong>in</strong>stallation cost <strong>of</strong> each <strong>cogeneration</strong> system can be roughly estimated by the formula<br />

taken from the report on “Industrial <strong>and</strong> Commercial Cogeneration”, Office <strong>of</strong> Technology<br />

Assessment, Wash<strong>in</strong>gton D.C., U.S.A.:<br />

• Steam Turb<strong>in</strong>e (Oil-<strong>Fire</strong>d):<br />

C = [962.761- (9.119 x10 -3 x M) - (1.314 x 10 -7 x M 2 ) + (2.782 x 10 -11 x M 3 )] x M x E<br />

• Diesel Eng<strong>in</strong>e:<br />

C = [915.14 - (6.531 x 10 -2 x M) + (4.56 x 10 -6 x M 2 ) - (1.424 x 10 -10 x M 3 )] x M x E<br />

Where, C = <strong>in</strong>stallation cost, Peso<br />

M = <strong>in</strong>stalled capacity, kW<br />

E = peso - dollar exchange rate, assumed 26 Peso/$ <strong>in</strong> 1996<br />

(b) Operat<strong>in</strong>g costs<br />

The operat<strong>in</strong>g costs <strong>in</strong> this case study <strong>in</strong>clude:<br />

• Fuel Costs: cost <strong>of</strong> fuel consumed by the <strong>cogeneration</strong> unit.<br />

• Operat<strong>in</strong>g <strong>and</strong> Ma<strong>in</strong>tenance Costs: These are taken as 2.5 per cent <strong>of</strong> the total <strong>in</strong>stallation<br />

cost <strong>of</strong> the <strong>cogeneration</strong> unit.

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