Coal gasification process utilizing waste water from an external process

Claim 1

A process for gasifying feed ashcontaining solid carbonaceous particulates comprising passing a first feed stream comprising an aqueous mixture of carbonaceous particulates together with an oxygen-containing gas to a combustion zone to provide heat and reactants for said process, passing a second feed stream comprising carbonaceous particulates to a fluidized bed gasifier zone disposed upon grate means with said second feed stream entering said gasifier zone above said grate means, said aqueous mixture comprising at least in part waste water containing at least one member selected from the group consisting of combustible pollutants and slag-forming salts, maintaining said combustion zone under exothermic oxidation reaction conditions including a temperature between 2200° and 3300°F. and a residence time of up to 30 seconds to produce hot combustion gases and steam and to convert ash into molten slag, passing said hot combustion gases and steam upwardly from said combustion zone through said grate means into said fluidized gasifier zone to form a fluidized bed of said second feed stream particulates having a pseudo-liquid level, injecting at least one coolant selected from the group consisting of water and steam into said hot combustion gases between said combustion zone and said grate means to solidify molten slag in said hot combustion gases, maintaining said gasifier zone under endothermic reducing conditions including a temperature between 1400° and 2000°F., an average particle residence time of 5 to 60 minutes, and a pressure of at least 10 psi at which carbon dioxide and water vapor react with carbon to produce carbon monoxide and hydrogen, withdrawing an overhead stream from said gasifier zone comprising carbon monoxide, hydrogen and water vapor, said overhead stream containing elutriated solid particulates from said fluid bed, said elutriated solid particulates having a lower carbon-to-ash weight ratio than the average carbon-to-ash weight ratio of the particles in said fluid bed, said elutriated solid particulates comprising substantially all the fluidized solid particulates removed from said gasifier zone, said process essentially avoiding removal of a stream of average carbon-to-ash weight ratio fluidized solid particulates from said fluid bed.