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Synthesis gas from biomass: operating data on a 1-ton/day oxygen gasifier

Conference ·
OSTI ID:5355002
A 1 ton/day (900 kg/day), downdraft, oxygen biomass gasifier has been built and operated on wood chips and densified biomass for one year. The gasifier, which is a modification of the small gasifiers widely used in the past, has an extended char bed and staged oxygen injection designed to crack all the pyrolysis tars to eliminate downstream gas cleanup requirements. The gasifier is fed continuously, which allows high temperature combustion of the tars above the pyrolysis section. This in turn provides heat for the pyrolysis reaction. Actual feed rates varied up to 62 lb/h (28 kg/h), or 314 lb/ft/sup 2/ h (1533 kg/m/sup 2/ h) with measured oxygen/fuel ratios varying between 0.42 and 0.44. A typical gas has a composition of 48% CO, 15% CO/sub 2/, 32% H/sub 2/, 3% N/sub 2/, and 2% CH/sub 4/. Organic content in the gas quench water is typically 0.02% to 0.1% of the feed. Heat losses through the insulation and grate are typically 6% to 8% of the throughput energy in the 6-in. (150-mm)-diameter bed. The downdraft gasifier produces a gas close to that predicted by the equilibrium between C, H/sub 2/, CO, CO/sub 2/, and H/sub 2/O at temperatures between 700/sup 0/ and 900/sup 0/C and is therefore particularly suited to producing synthesis gas for synthetic fuels. Two liters of methanol were synthesized from the gas using the liquid-phase process. The gas was found to be similar to synthesis gas from coal and presented no difficulty in synthesis.
Research Organization:
Solar Energy Research Inst., Golden, CO (USA); Colorado School of Mines, Golden (USA)
DOE Contract Number:
AC02-77CH00178
OSTI ID:
5355002
Report Number(s):
SERI/TP-234-1455; CONF-820324-1; ON: DE82008185
Country of Publication:
United States
Language:
English