AIChE Journal · 1984 · 152 citations · 21 references
EngineeringChemical EngineeringProcess Systems EngineeringReaction EngineeringTransport PhenomenaBioreactor HydrodynamicsGas TransferHeat Transfer In ReactorsReactor DesignReactor ModelingChemical Treatment ProcessesGasificationHydrodynamicsInlet HydrodynamicsReactor HydrodynamicsReactor OperationSlurriesVelocity Profiles
Abstract A mathematical model has been developed to simulate the Texaco downflow entrained‐bed pilot‐plant gasifier using coal liquefaction residues and coal‐water slurries as feedstocks. This model describes the physical and chemical processes occurring in an entrained coal gasifier. The gasification kinetics describes different complex reactions occurring in the gasifier and the hydrodynamics describes mass, momentum and energy balances for solid and gas phases. Temperature, concentration and velocity profiles along the reactor height were obtained by solving the mass, momentum and energy balances. Parameter studies were made to provide a better understanding of the reactor performance for various inlet feed conditions utilizing the model.
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