Characteristics of Fluidized Bed Type Gasification of Kideco Coal
Dal-Hee Bae, Sung-Ho Jo, Dowon Shun, Young-Sub Moon
Abstract
Dal-Hee Bae, Sung-Ho Jo, Dowon Shun, Young-Sub Moon
Abstract
Coal pyrolysis processes vary with the origin and rank of coal. It is difficult to generalize the characteristics of coal pyrolysis reaction because the process consists of numerous reactions including pyrolysis, gasification, and combustion. To find out the optimum process condition it is necessary to determine the condition fur each coal from the smatter scale experiment. In this study pressurized () fluidized bed, low temperature () gasification using Kideco coal was performed. The reaction condition and product gas composition were determined from the variables including steam flow rate, coal feed rate and air flow rate. Optimum reaction condition was determined from the concentrations of , and CO in the product gas. The ratio of air/coal was 4.45 and that of steam/coal was 0.21 respectively. The concentrations of CO and decreased with the increase of . It is important to control the feed rates of coal and steam because the reaction temperature rapidly increased when the combustion reaction dominates over the gasification reaction. The concentrations of CO and were 18%, 17% respectively from the continuous operating condition.
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Coal pyrolysis processes vary with the origin and rank of coal. It is difficult to generalize the characteristics of coal pyrolysis reaction because the process consists of numerous reactions including pyrolysis, gasification, and combustion. To find out the optimum process condition it is necessary to determine the condition fur each coal from the smatter scale experiment. In this study pressurized () fluidized bed, low temperature () gasification using Kideco coal was performed. The reaction condition and product gas composition were determined from the variables including steam flow rate, coal feed rate and air flow rate. Optimum reaction condition was determined from the concentrations of , and CO in the product gas. The ratio of air/coal was 4.45 and that of steam/coal was 0.21 respectively. The concentrations of CO and decreased with the increase of . It is important to control the feed rates of coal and steam because the reaction temperature rapidly increased when the combustion reaction dominates over the gasification reaction. The concentrations of CO and were 18%, 17% respectively from the continuous operating condition.
Key concepts: Coal, Pyrolysis, Fluidized bed, Coal gasification, Waste management, Dry distillation, Destructive distillation, Energy value of coal