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As we saw in Figures 6.4 and 6.6, the cross-sectional area of a downdraft gasifier may be nonuniform; it is narrowest at the throat. The hearth load is, therefore, based on the cross-sectional area of the throat for a throated gasifier, and for a throatless or stratified downdraft gasifier, it is based on the gasifier crosssectional area. The actual velocity of gas is, however, significantly higher than the designed space velocity because much of the flow passage is occupied by fuel particles. The velocity is higher in the throat also because of the higher temperature there. Table 6.6 gives some characteristic values of these parameters.
In a downdraft gasifer, the gasification air is injected by a number of nozzles from the periphery (refer to Figure 6.6). The total nozzle area is typically 7 to 4% of the throat area. The number of nozzles should be an odd number so that the jet from one nozzle does not hit a jet from the opposite side, leaving a dead space in between. To ensure adequate penetration of nozzle air into the hearth, the diameter of a downdraft gasifier is generally limited to 1.5 m. This naturally restricts the size and capacity of a downdraft gasifier.
TABLE 6.6 Hearth Load for Downdraft Gasifiers Maximum Values Based on Throat Area |
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Plant |
Gasifier Type |
Medium |
Superficial Velocity at Throat (m/s) |
Hearth Load* (MW/m2) |
||
Gengas |
Imbert |
Air |
0.15 |
0.3 |
2.5 |
15 |
Biomass Corp. |
Imbert |
Air |
0.3 |
0.61 |
0.95 |
5.7 |
SERI |
Throatless |
Air |
0.15 |
0.28 |
1.67 |
|
Buck Rogers |
Throatless |
Air |
0.61 |
0.23 |
1.35 |
|
Buck Rogers |
Throatless |
Air |
0.61 |
0.13 |
0.788 |
|
Syngas |
Throatless |
Air |
0.76 |
1.71 |
10.28 |
|
Syngas |
Throatless |
Oxygen |
0.76 |
1.07 |
12.84 |
|
SERI |
Throatless |
Oxygen |
0.15 |
0.24 |
1.42 |
|
area. |
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Source: Data compiled from Reed and Das, 1988, p. 36. |
Table 6.7 lists typical sizes for the Imbert-type downdraft gasifier and shows the relation between throat size and air nozzle diameter. |