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Mathematical model for a fluidized-bed coal gasifier. Final report August 1980-August 1983

Technical Report ·
OSTI ID:6524904
The report gives results of gasifying four fuels--a devolatilized Kentucky bituminous coal, a New Mexico subbituminous coal, a North Carolina peat, and a Texas lignite--with steam and oxygen in a pilot-scale fluidized-bed reactor. Experimental results were used to provide an evaluation of mathematical models developed for the gasifier. A simple three-stage gasifier model and a two-phase bubbling-bed model were developed. Model options include allowance for a jetting region at the gas inlet of the bed and elutriation of fines. Gasification reactions in both models are described by Johnson kinetics. The models were applied to the gasification of the devolatilized Kentucky bituminous coal and the New Mexico subbituminous coal. Parameter optimizations were performed with each model for each feedstock. The main difference in the optimal values was in char reactivity, for which that of the New Mexico coal was roughly an order of magnitude greater than that for the Kentucky char. Using the optimal values, the models were applied to all experimental runs with these two coals. The resulting model predictions and experimental results showed reasonably good agreement in all cases.
Research Organization:
North Carolina State Univ., Raleigh (USA). Dept. of Chemical Engineering
OSTI ID:
6524904
Report Number(s):
PB-84-209469
Country of Publication:
United States
Language:
English