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Biomass as Fuel in Small Boilers (PDF 6.4 - APO Asian Productivity ...

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Solution:<br />

Step 1) F<strong>in</strong>d the theoretical air requirement<br />

- 33 -<br />

Performance Evaluation of <strong>Biom<strong>as</strong>s</strong> <strong>Boilers</strong><br />

- Ambient temperature - 30 ºC<br />

- Humidity of air - 0.018 kg/ kg of dry air<br />

[(11.43×C)+{34.5×(H2-02/8)+(4.32×S)}]/100kg/kg of fuel<br />

Step 2) F<strong>in</strong>d the percentage of excess air supplied<br />

Step 3) F<strong>in</strong>d the actual m<strong>as</strong>s of air supplied<br />

Actual m<strong>as</strong>s of Air supplied / Kg of fuel<br />

Note: In order to make the calculation simple, the flue g<strong>as</strong> m<strong>as</strong>s is taken <strong>as</strong><br />

actual m<strong>as</strong>s of air supplied for combustion.<br />

Step 4) F<strong>in</strong>d the losses<br />

i. Dry flue g<strong>as</strong> loss<br />

= [(11.43×38.5)+{34.5×(5.7-39.8/8)+(4.32×0)}]/100<br />

= 4.65kg of air / kg of rice husk<br />

=<br />

=<br />

% 02<br />

Excess Air Supplied(EA)=<br />

(21-%02)<br />

Excess Air Supplied(EA)=<br />

= 6.97 kg of Air/kg of R.H<br />

= 50%<br />

[1+EA/100]×Theoretical Air<br />

[1+50/100]×4.65<br />

% heat loss due to dry flue g<strong>as</strong> =<br />

% heat loss due to dry flue g<strong>as</strong> =<br />

=<br />

7<br />

(21-7)<br />

8.5 %<br />

×100<br />

×100<br />

m×Cp×(Tf-Ta)×100<br />

GCV of <strong>Fuel</strong><br />

6.97×0.23×(200-30)×100<br />

3200

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