A one-dimensional transient mathematical model describing thermal and flow phenomena during coal coking in an oven chamber was studied in the paper. It also accounts for heat conduction in the ceramic oven wall when assuming a constant temperature at the heating channel side. The model was solved numerically using partly implicit methods for gas flow and heat transfer problems. The histories of temperature, gas evolution and internal pressure were presented and analysed. The theoretical predictions of temperature change in the centre plane of the coke oven were compared with industrialscale measurements. Both, the experimental data and obtained numerical results show that moisture content determines the coking process dynamics, lagging the temperature increase above the water steam evaporation temperature and in consequence the total coking time. The phenomenon of internal pressure generation in the context of overlapping effects of simultaneously occurring coal transitions - devolatilisation and coal permeability decrease under plastic stage - was also discussed.
Adesanya B.A., Pham H.N., 1995. Mathematical modelling of devolatilization of large coal particles in a convective environment. Fuel, 74, 896-902. DOI: 10.1016/0016-2361(95)00014-3.
Alvarez R., Pis J.J., Diez M.A., Barriocanal C., Menendez J.A., Casal M.D., Parra J.B., 1996. Carbonization of wet and preheated coal. Effect on coke quality and its relation with textural properties. J. Anal. Appl. Pyr., 38, 119-130. DOI: 10.1016/S0165-2370(96)00947-3.
Atkinson B., Merrick D., 1983. Mathematical models of the thermal decomposition of coal: 4. Heat transfer and temperature profiles in a coke-oven charge. Fuel, 62, 553-561. DOI: 10.1016/0016-2361(83)90225-9.
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