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

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Summary <strong>of</strong> country study – Bangladesh 143<br />

3.3 Pre-feasibility Studies at Selected Industrial <strong>and</strong> Commercial Sites<br />

For the purpose <strong>of</strong> economic analysis, the total <strong>in</strong>stalled costs <strong>of</strong> the <strong>cogeneration</strong> plants<br />

were assumed as follows: steam turb<strong>in</strong>es: US$ 1,200/kWe; gas turb<strong>in</strong>es: US$ 1,000/kWe;<br />

<strong>and</strong> reciprocat<strong>in</strong>g eng<strong>in</strong>es: US$ 900/kWe. Some common f<strong>in</strong>ancial data gathered or<br />

assumed before conduct<strong>in</strong>g the pre-feasibility studies are summarized <strong>in</strong> Table 3.4.<br />

Table 3.4 F<strong>in</strong>ancial data used for the pre-feasibility study<br />

Parameters Unit Value<br />

Exchange rate Taka/US$ 48.00<br />

Tax rate Per cent/year 35.00<br />

Discount rate Per cent/year 15.00<br />

Cogeneration plant service life Year 15.00<br />

Electricity purchase price Taka/kWh 3.60<br />

Electricity buy-back rate Per cent <strong>of</strong> purchase price 80 per cent<br />

Fuel price escalation rate Per cent/year 5.00<br />

Electricity price escalation rate Per cent/year 6.00<br />

Electricity st<strong>and</strong>-by rate Taka/kW.month 80.00<br />

Fuel purchase price (natural gas) Taka/m 3<br />

1.68<br />

3.3.1 Recycled paper mill<br />

This factory operates 24 hours a day <strong>and</strong> 350 days a year. Natural gas is used <strong>in</strong> boiler<br />

furnace for steam generation. The electrical energy is required to drive the motors. The rate<br />

<strong>of</strong> production is ma<strong>in</strong>ta<strong>in</strong>ed up to the target level.<br />

Analysis <strong>of</strong> the monthly electricity <strong>and</strong> steam consumption <strong>in</strong> 1997 led to the follow<strong>in</strong>g:<br />

• Total Electricity Consumption <strong>in</strong> 1997: 23,412 MWh<br />

• Maximum Electricity Dem<strong>and</strong>: 3,100 kW<br />

• M<strong>in</strong>imum Electricity Dem<strong>and</strong>: 2,750 kW<br />

• Total Steam Consumption <strong>in</strong> 1997: 69,386 tons<br />

• Maximum Steam Dem<strong>and</strong>: 9.65 ton/hr<br />

• M<strong>in</strong>imum Steam Dem<strong>and</strong>: 7.15 ton/hr<br />

The average power-to-heat ratios were found to be 0.52 <strong>in</strong> 1997. Typical <strong>cogeneration</strong><br />

system for this site would be based on steam turb<strong>in</strong>e. However, reciprocat<strong>in</strong>g eng<strong>in</strong>e, gas<br />

turb<strong>in</strong>e <strong>cogeneration</strong> systems were also considered as potential alternatives. Results <strong>of</strong> the<br />

feasibility study are summarized <strong>in</strong> Table 3.5.<br />

Obviously, the steam turb<strong>in</strong>e option does not seem feasible: (i) with steam turb<strong>in</strong>e thermal<br />

match (STTM), less than 25 per cent <strong>of</strong> the power requirement is generated; (ii) with steam<br />

turb<strong>in</strong>e power match (STPM), too much excess heat is generated.<br />

With the reciprocat<strong>in</strong>g eng<strong>in</strong>e thermal match (RETM) option, 200 per cent excess power is<br />

generated. The project pr<strong>of</strong>itability will depend on the buy-back rate. This may not be a good<br />

option as the purpose is not to earn from electricity sale. Reciprocat<strong>in</strong>g eng<strong>in</strong>e power match<br />

(REPM) option seems feasible as almost all the power needed can be met though an<br />

auxiliary boiler will be necessary to make up for the 30 per cent shortfall <strong>in</strong> the heat supply.

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