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Received March 12, 2001
Accepted May 24, 2001
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Prediction of Gaseous Pollutants and Heavy Metals during Fluidized Bed Incineration of Dye Sludge
Dept. of Environ. Eng., Dongseo University, Busan 617-716, Korea 1Dept. of Environ. Eng., Pukyong National University, Busan 608-737, Korea 2Dept. of Chem. Eng., Korea University, Seoul 136-701, Korea
leejk@pknu.ac.kr
Korean Journal of Chemical Engineering, July 2001, 18(4), 506-511(6), 10.1007/BF02698298
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Abstract
This research provides an equilibrium model for predicting both the emission of gaseous pollutants and the fate of heavy metals during incineration of biologically treated dye sludge in a bench-scale fluidized bed incinerator. Major gaseous pollutants and hazardous trace heavy metals have been also measured under various operating conditions. The predicted values, which were derived by using a thermodynamic equilibrium model, can be used to determine the optimum operating parameters and the risk associated with hazardous waste incineration by means of verifying experimental data. However, prediction of NOx emission using a thermodynamic equilibrium model during incineration of waste was not simple. The reason is that the variation of NOx emission during incineration of waste was affected by the various operating parameters, such as air-fuel ratio (λ(T)), primary air factor (λ(1)/λ(T)), combustor geometry, method of heat release, and preheating of combustion air. According to the distributions of Cr and Pb simulated by the equilibrium model, all of the Cr in the feed was retained in the ash as the solid phase of Cr2CO3. However, most Pb was retained in the ash during incineration as the solid phase of PbSO4, or heterogeneously deposited onto the fly ash as PbO(g) when the combustion gas becomes cool.
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References
Baeyens J, Geldart D, "Fluidized Bed Incineration," A Design Approach for Complete Combustion of Gydrocarbons, Proc. 2nd Eng. Found. Conf., Cambridge, England, 264 (1978)
Dewling RT, Manganelli RM, J. WPCF, 52, 2552 (1980)
Gibbs BM, Hampartsoumian E, "In Fluidized Bed Boilers; Design and Application," Basu, P., Ed., Pergamon Press, Toronto (1984)
Gordon S, McBride BT, "Computer Program for Calculation of Complex Chemical Equilibrium Compositional, Rocket Performance, Incident and Reflected Shecks, and Chapman-Jouguet Detonations," NASA Lewers Research Center, NASA SP-273 (1971)
Hughes ISC, Littlejohn RF, "Trace Element Emissions from AFBC," Proc. 9th Int. Conf. on FBC, ASME, Boston, 2, 906 (1987)
Kawaguchi M, J. Environ. Pollut. Contr. Japan, 21, 853 (1985)
Lee CC, JAPCA, 38, 941 (1988)
Lee JK, Lee KH, Jang JG, Lee NS, Lim JS, Chun HS, HWAHAK KONGHAK, 30(2), 228 (1992)
U.S. EPA, EPA 625/8-81-006 (1981)
U.S. EPA, EPA/625/4-85/015 (1985)
Valk M, Bramer EA, Toissant HHJ, "Effect of Staged Combustion of Coal on Emission Levels NO(x) and SO2 in a Fluidized Bed," Proceedings of the 9th International Conference on Fluidized Bed Combustion, ASME, Boston, MA, 2, 784 (1987)
Yaverbaum L, "Fluidized Bed Combustion of Coal and Waste Materials," Noyes Data Corp., New Jerey, 87 (1977)
Dewling RT, Manganelli RM, J. WPCF, 52, 2552 (1980)
Gibbs BM, Hampartsoumian E, "In Fluidized Bed Boilers; Design and Application," Basu, P., Ed., Pergamon Press, Toronto (1984)
Gordon S, McBride BT, "Computer Program for Calculation of Complex Chemical Equilibrium Compositional, Rocket Performance, Incident and Reflected Shecks, and Chapman-Jouguet Detonations," NASA Lewers Research Center, NASA SP-273 (1971)
Hughes ISC, Littlejohn RF, "Trace Element Emissions from AFBC," Proc. 9th Int. Conf. on FBC, ASME, Boston, 2, 906 (1987)
Kawaguchi M, J. Environ. Pollut. Contr. Japan, 21, 853 (1985)
Lee CC, JAPCA, 38, 941 (1988)
Lee JK, Lee KH, Jang JG, Lee NS, Lim JS, Chun HS, HWAHAK KONGHAK, 30(2), 228 (1992)
U.S. EPA, EPA 625/8-81-006 (1981)
U.S. EPA, EPA/625/4-85/015 (1985)
Valk M, Bramer EA, Toissant HHJ, "Effect of Staged Combustion of Coal on Emission Levels NO(x) and SO2 in a Fluidized Bed," Proceedings of the 9th International Conference on Fluidized Bed Combustion, ASME, Boston, MA, 2, 784 (1987)
Yaverbaum L, "Fluidized Bed Combustion of Coal and Waste Materials," Noyes Data Corp., New Jerey, 87 (1977)