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Carbon combustion efficiency and sulfur dioxide emission in fluidized bed combustion of Texas lignite

Thesis/Dissertation ·
OSTI ID:6168239

This study is an effort to characterize the relationships between both the carbon efficiency and sulfur dioxide emission and the operating conditions of a pilot plant FBC (fluidized-bed combustion) unit. The design and instrumentation of the pilot plant FBC facility used in the experimental studies are described. The relevant operating parameters are identified and their influence on carbon efficiency and sulfur dioxide emission is determined experimentally. The effects of the operating parameters are then consolidated through use of the carbon residence time in the so-called emulsion-phase of the reactor as a single correlating parameter for the carbon efficiency. The variation in the sulfur retention by the lignite ash mineral matter with operating conditions is measured and the reduction in sulfur emission obtained with limestone sorbent addition is determined. The effects of staged combustion and recycle of the elutriated material are also studied. A model is developed to predict the carbon efficiency based on the residence time of the char in the bed. The char particle size distribution in the bed is calculated by use of a population balance assuming the rate of combustion to be controlled by diffusion of oxygen to the char particle surface. The predictions of the model show good agreement with the experimental pilot plant data.

Research Organization:
Texas Univ., Austin (USA)
OSTI ID:
6168239
Country of Publication:
United States
Language:
English

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