Training Manual on Energy Efficiency - APO Asian Productivity ...
Training Manual on Energy Efficiency - APO Asian Productivity ...
Training Manual on Energy Efficiency - APO Asian Productivity ...
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Table 4-1 Radiant heat loss comparis<strong>on</strong> at various temperatures<br />
C1<br />
( º C)<br />
C2<br />
( º C)<br />
K1<br />
(C1 +273)<br />
K2<br />
(C2 +273)<br />
- 37 -<br />
(K1/K2) 4<br />
Relative<br />
Radiant Heat Transfer<br />
700 20 973 293 122 1.0 (baseline value)<br />
900 20 1173 293 255 2.1<br />
1100 20 1373 293 482 3.96<br />
1300 20 1573 293 830 6.83<br />
1500 20 1773 293 1340 11.02<br />
1700 20 1973 293 2056 16.91<br />
(Note: C1 is hot body temperature and C2 is ambient air temperature)<br />
<strong>Energy</strong> <strong>Efficiency</strong> in Furnaces<br />
In other words, the radiati<strong>on</strong> losses from an open furnace door at 1500 º C<br />
are 11 times greater than the losses of the same furnace at 700 º C. A good<br />
practice for ir<strong>on</strong> and steel melters is to keep the furnace lid closed at all times<br />
and maintain a c<strong>on</strong>tinuous feed of cold charge <strong>on</strong>to the molten bath.<br />
4.7.3 Determining black body radiati<strong>on</strong> at a particular temperature<br />
If a furnace body has an opening, the heat in the furnace escapes to the<br />
outside as radiant heat. Heat loss due to openings can be calculated by<br />
computing black body radiati<strong>on</strong> at furnace temperature, and multiplying these<br />
values by emissivity (usually 0.8 for furnace brick work), and the factor of<br />
radiati<strong>on</strong> through openings. The black body radiati<strong>on</strong> losses can be directly<br />
computed from the curves as given in Figure 4-4.<br />
Figure 4-4 Black body radiati<strong>on</strong>