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insufficient to produce complete combustion and the presence of water as steam favors the reactions that yield fuel-gas However, to raise the efficiency of a power plant, commercial gasifiers must recover the heat released during gasification Most designs do this by cooling the gasifier with water, to produce steam and fuel-gas The fuel-gas itself may have to be cooled and reheating reduces the overall efficiency of the plant The countercurrent fixed bed (up draft) gasifier consists of a fixed bed of carbonaceous fuel (eg, coal or biomass) through which the gasification agent (steam, oxygen, and/or air) flows in countercurrent configuration The ash is either removed dry or as a slag The slagging gasifiers require a higher ratio of steam and oxygen to carbon in order to reach temperatures higher than the ash fusion temperature.

1 Right-click the domain or OU, and select Properties. In the Group Policy tab of the Properties dialog box, click Properties. 2 To disable the policy entirely, select the policy, and then click Options. In the Options dialog box, select Disabled, and then click OK. If you later want to enable the policy, you would repeat this process and clear the Disabled option. 3 To disable the policy partially, select the policy, and then click Properties. In the Properties dialog box, select or clear Disable Computer Configuration Settings and Disable User Configuration Settings as necessary.

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The nature of the gasifier means that the fuel must have high mechanical strength and must be noncaking so that it will form a permeable bed, although recent developments have reduced these restrictions to some extent The throughput for this type of gasifier is relatively low Thermal efficiency is high as the gas exit temperatures are relatively low However, this means that tar and methane production is significant at typical operation temperatures, so product gas must be extensively cleaned before use or recycled to the reactor The major advantages of this type of gasifier are its simplicity, high charcoal burnout, and internal heat exchange leading to low gas exit temperatures and high gasification efficiency In this way, also fuels with high moisture content (up to 50 percent by weight) can be used.

Major drawbacks are the high amounts of tar and pyrolysis products, because the pyrolysis gas is not led through the oxidation zone This is of minor importance if the gas is used for direct heat applications, in which the tars are simply burnt In case the gas is used for engines, gas cleaning is required, resulting in problems of tar-containing condensates The cocurrent fixed bed (down draft) gasifier is similar to the countercurrent type, but the gasification agent gas flows in cocurrent configuration with the fuel (downward, hence the name down draft gasifier) Heat needs to be added to the upper part of the bed, either by combusting small amounts of the fuel or from external heat sources.

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The produced gas leaves the gasifier at a high temperature, and most of this heat is often transferred to the gasification agent added in the top of the bed, resulting in energy efficiency on level with the countercurrent type Since all tars must pass through a hot bed of char in this configuration, tar levels are much lower than the countercurrent type.

Drawbacks of the downdraft gasifier are: (a) the high amounts of ash and dust particles in the gas, (b) the inability to operate on a number of unprocessed fuels, often pelletization or briquetting of the biomass is necessary (c) the outlet gas has a high temperature leading to a lower gasification efficiency, (d) the moisture content of the biomass must be less than 25 percent to maintain the high temperature and the mineral content (ash yield) should also be low and nonslagging, and (e) the feed must have uniform particle size In the fluid bed gasifier, the fuel is fluidized in oxygen (or air) and steam The ash is removed dry or as heavy agglomerates that defluidize The temperatures are relatively low in dry ash gasifiers, so the fuel must be highly reactive; low-grade coals are particularly suitable.

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