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Korean Journal of Chemical Engineering, Vol.18, No.5, 770-774, September, 2001
Gas Yields from Coal Devolatilization in a Bench-Scale Fluidized Bed Reactor
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Devolatilization behavior of Australian bituminous coal-gasification was determined in a 0.1 m diameter fluidized bed at 650-900 ℃. To predict gas yields from devolatilization, several correlations reported for gas yields were evaluated with the present experimental data. The correlation of Goyal and Rehmat [1993] was found to be good one. Also, a correlation for the product gas yields has been proposed from devolatilization of bituminous coals as a linear function of temperature with constants from the experiment. The experimental yields of product gas show good agreement with the values calculated by the proposed correlation.
- Fung DPC, Kim SD, Korean J. Chem. Eng., 7(2), 109 (1990)
- Goyal A, Rehmat A, Ind. Eng. Chem. Res., 32, 1396 (1993)
- Gururajan VS, Agarwal PK, Agnew JB, Chem. Eng. Res. Des., 70, 211 (1992)
- Lee JM, Kim YJ, Kim SD, HWAHAK KONGHAK, 38(2), 259 (2000)
- Lee JM, Kim YJ, Lee WJ, Kim SD, HWAHAK KONGHAK, 35(1), 121 (1997)
- Kim YJ, "Hydrodynamics, Heat Transfer and Coal Gasification Characteristics in a Downer Reactor," Ph. D. Thesis, KAIST (2000)
- Loison R, Chauvin R, Chimie Industrie, 91, 269 (1964)
- Ma RP, Felder RM, Ferrell JK, Ind. Eng. Chem. Res., 28, 27 (1989)
- Song BH, Watkinson AP, Can. J. Chem. Eng., 78(1), 143 (2000)
- Tsuji T, Watkinson AP, "Application of a Mixed Flow Reactor Model to a Coal Gasifier," Preprint, Canada-Japan joint Academic Research Program on Finding Efficient Uses for Coal, September, 101 (1990)
- Tyler RJ, Fuel, 58, 680 (1979)
- Yun Y, Lee GB, Korean J. Chem. Eng., 16(6), 798 (1999)