A numerical simulation study was conducted for a jetting fluidized bed
coal gasifier with a conical distributor. It was based on a steady-st
ate model which took account of hydrodynamics, mass heat transfer and
reactions in the grid zone, bubble zone and freeboard zone of the gasi
fier. Temperature of the particles and gas in the jet, compositions in
the dilute phase and the dense phase, and some hydrodynamic character
istics were calculated. Effects of some operating conditions such as o
xygen and steam flow rates, bed temperature and bed pressure on the te
mperatures in the jet and gas compositions in the gasifier were numeri
cally investigated. (C) 1997 Elsevier Science Ltd.