Numerical and experimental study for Datong coal gasification in entrained flow coal gasifier

  • Park, Y. C. (Energy Environment Research Department, Korea Institute of Energy Research(KIER)) ;
  • Park, T. J. (Energy Environment Research Department, Korea Institute of Energy Research(KIER)) ;
  • Kim, J. H. (Energy Environment Research Department, Korea Institute of Energy Research(KIER)) ;
  • Lee, J. G. (Energy Environment Research Department, Korea Institute of Energy Research(KIER))
  • Published : 2001.11.01

Abstract

The coal gasification process of a slurry feed type, entrained-flow coal gasifier was numerically predicted in this paper. By divding the complicated coal gasification process into several simplified stages suh as slurry evaporation, coal devolitilisation and two-phase reactions coupled with turbulent flow and two-phase heat transfer, a comprehensive numerical model was constructed to simulate the coal gasification process. The k-$\varepsilon$turbulence model was used for the gas phase flow while the Random-trajectory model was applied to describe the behavior of the coal slurry particles. The unreacted-core shrinking model and modified Eddy Break-Up(EBU) model were used to simulate the heterogeneous and homogeneous reactions, respectively. The simulation results obtained the detailed informations about the flow field, temperature inside the gasifier. Meanwhile, the simulation results were compared with the experimental data as function of $O_2$/coal ratio. It illustrated that the calculated carbon conversions agreed with the measured ones and that the measurd quality of the atngas was better than the calculated one when the $O_2$/coal ratio increases. The result was related with the total heat loss through the gasifier and uncertain kinetics for the heterogeneous reactions.

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