Apparatus and method for the gasification of solid carbonaceous material

Claim 2

A process for promoting gasification reaction between an oxygen-rich gas and particulate carbonaceous solids to produce a combustible effluent gas and a residue which comprises, continuously feeding particulate carbonaceous fuel solids to a closed bottom jet-fluidized reactor, said reactor having a roof enclosure, directing an oxygen-rich gaseous jet stream into said reactor by means of a lance passing axially through said roof enclosure to fluidize said carbonaceous solids and to effect gasification reactions, said oxygen-rich gas and said particulate carbonaceous solids being fed to the reactor at rates proportioned to effect exothermic reaction and provide reactor temperatures of at least about 1600° F, discharging said gaseous jet stream into said reactor at a nozzle velocity sufficient to form a highly turbulent and rapidly circulating suspension of particulate solids deflecting substantially radially outwardly on the bottom, upwardly on the outside and then inwardly and downwardly below the jet, said circulating suspension defining a reaction zone adjacent to the bottom of said reactor, maintaining total feed rates of said oxygen-rich gas and carbonaceous solids to provide an average upward velocity of effluent gas substantially above the minimum fluidization velocity for said particulate solids, and removing said effluent gas and residue formed by said gasification from said reactor.

Claim 3

The process of claim 1, wherein said particulate carbonaceous solids are partially gasified to form said combustible gas and a residue comprising char and ash.

Claim 4

The process of claim 1, wherein said particulate carbonaceous solids are substantially completely gasified to form said combustible gas and a residue comprising ash.

Claim 5

The process of claim 1, wherein said gasification is carried out in the presence of steam continuously fed to said reactor in an amount sufficient to provide an endothermic production of hydrogen by reaction with carbonaceous solids in said reactor.

Claim 6

The process of claim 3, wherein slag-forming constituents are fed to the reactor with said carbonaceous solids to form a liquid slag with said ash, wherein a layer of liquid slag is maintained at the bottom of said reactor, and wherein said jet-fluidized reaction is further augmented at the gas-liquid interface of said slag, any excess slag formed being withdrawn from said reactor.

Claim 7

The process of claim 3, wherein solids entrained in said effluent gas are separated therefrom and returned to the reactor.

Claim 8

The process of claim 3, wherein the particulate carbonaceous solids is high-sulfur coal, and wherein the particulate coal fed to the reactor is blended with an amount of a solid particulate sulfur combining material at least stoichiometrically sufficient to fix said sulfur and to remove it from the combustible effluent gas.

Claim 9

A process for promoting gasification reaction between an oxygen-rich gas and particulate carbonaceous coal to produce a combustible effluent gas and a residue which comprises, continuously feeding particulate coal and slag-forming constitutents to a closed bottom jet-fluidized reactor, said reactor having a roof enclosure, directing an oxygen-rich gaseous jet stream into said reactor by means of a lance passing axially through said roof enclosure to fluidize said coal and to effect gasification reactions and form an ash-containing residue, said oxygen-rich gas and particulate coal being fed to the reactor at rates proportioned to effect exothermic reaction and provide reactor temperatures of about 1800° to 2700° F, discharging said gaseous jet stream into said reactor at a nozzle velocity sufficient to form a highly turbulent and rapidly circulating suspension of particulate solids deflecting substantially radially outwardly on the bottom, upwardly on the outside and then inwardly and downwardly below the jet, said circulating suspension defining a reaction zone adjacent to the bottom of said reactor, maintaining total feed rates of said oxygen-rich gas and said particulate coal to provide an average upward velocity of effluent gas substantially above the minimum fluidization velocity for said particulate coal, forming a molten slag layer at the bottom of said reactor with said slag-forming constituents and ash as it forms, and removing said combustible effluent gas and excess slag from said reactor while maintaining said slag layer during said gasification reaction.

Claim 10

A process for promoting gasification reaction between an oxygen-rich gas and particulate carbonaceous coal to produce a combustible effluent gas and a residue which comprises, continuously feeding particulate coal and slag-forming constitutents to a closed bottom jet-fluidized reactor, said reactor having a roof enclosure, directing an oxygen-rich gaseous jet stream into said reactor by means of a lance passing axially through said roof enclosure to fluidize said coal and to effect gasification reactions and form an ash-containing residue, said oxygen-rich gas and particulate coal being fed to the reactor at rates proportioned to effect exothermic reaction and provide reactor temperatures of about 1800° to 2700° F, discharging said gaseous jet stream into said reactor at a nozzle velocity sufficient to form a highly turbulent and rapidly circulating suspension of particulate solids deflecting substantially radially outwardly on the bottom, upwardly on the outside and then inwardly and downwardly below the jet, said circulating suspension defining a reaction zone adjacent to the bottom of said reactor, maintaining total feed rates of said oxygen-rich gas and said particulate coal to provide an average upward velocity of effluent gas substantially above the minimum fluidization velocity for said particulate coal, forming a molten slag layer at the bottom of said reactor with said slag-forming constituents and ash as it forms, and removing said combustible effluent gas and excess slag from said reactor while maintaining said slag layer during said gasification reaction.

Claim 11

The process of claim 8, wherein said particulate coal is partially gasified to form a residue containing char in addition to said ash, said ash being removed in the slag, and said char being recycled to said reactor.

Claim 12

The process of claim 8, wherein said particulate coal is substantially completely gasified to form said combustible gas, the ash residue being removed from the zone of reaction by slagging with said slag-forming constitutents.

Claim 13

The process of claim 10, wherein said gasification reaction is carried out in the presence of steam continuously fed to said reactor in an amount sufficient to provide an endothermic production of combustible gas comprising hydrogen by reaction with said particulate coal in said reactor.

Claim 14

The process of claim 8, wherein said coal is a high-sulfur coal, and wherein the particulate coal fed to the reactor is blended with an amount of particulate iron-containing sulfur-fixing material selected from the group consisting of metallic iron and iron oxide at least stoichiometrically sufficient to form a molten iron-containing layer disposed below said slag layer and containing a substantial amount of said sulfur.

Claim 15

A continuous process for converting particulate high-sulfur coal by gasification into a low-sulfur combustible effluent gas and a residue which comprises, continuously feeding particulate high-sulfur coal and slag-forming constitutents to a closed bottom jet-fluidized reactor together with particulate sulfur-fixing material selected from the group consisting of metallic iron and iron oxide, said reactor having a roof enclosure, directing an oxygen-rich gaseous jet stream into said reactor by means of a lance passing axially through said roof enclosure to fluidize said particulate coal and form a low-sulfur combustible gas and an ash-containing residue, said oxygen-rich gas and said particulate coal being fed to the reactor at rates proportioned to effect exothermic reaction and provide reactor temperatures ranging from about 1800° to 2700° F, discharging said gaseous jet stream into said reactor at a nozzle velocity sufficient to form a highly turbulent and rapidly circulating suspension of particulate solids deflecting substantially radially outwardly on the bottom and upwardly on the outside and then inwardly and downwardly below the jet, said circulating suspension defining a reaction zone adjacent to the bottom of said reactor, maintaining total feed rates of said oxygen-rich gas and said particulate coal to provide an average upward velocity of effluent gas substantially above the minimum fluidization velocity for said particulate coal, continuing said gasification to form a first molten layer of slag at the bottom of said reactor with said slag-forming constituents and the ash as it forms and a second molten layer below said slag layer comprising iron and containing sulfur fixed as iron sulfide, and removing said combustible effluent gas, excess slag and excess iron-containing layer from said reactor while maintaining a slag layer during said gasification reaction.

Claim 16

A continuous process for converting particulate high-sulfur coal by gasification into a low-sulfur combustible effluent gas and a residue which comprises, continuously feeding particulate high-sulfur coal and slag-forming constitutents to a closed bottom jet-fluidized reactor together with particulate sulfur-fixing material selected from the group consisting of metallic iron and iron oxide, said reactor having a roof enclosure, directing an oxygen-rich gaseous jet stream into said reactor by means of a lance passing axially through said roof enclosure to fluidize said particulate coal and form a low-sulfur combustible gas and an ash-containing residue, said oxygen-rich gas and said particulate coal being fed to the reactor at rates proportioned to effect exothermic reaction and provide reactor temperatures ranging from about 1800° to 2700° F, discharging said gaseous jet stream into said reactor at a nozzle velocity sufficient to form a highly turbulent and rapidly circulating suspension of particulate solids deflecting substantially radially outwardly on the bottom and upwardly on the outside and then inwardly and downwardly below the jet, said circulating suspension defining a reaction zone adjacent to the bottom of said reactor, maintaining total feed rates of said oxygen-rich gas and said particulate coal to provide an average upward velocity of effluent gas substantially above the minimum fluidization velocity for said particulate coal, continuing said gasification to form a first molten layer of slag at the bottom of said reactor with said slag-forming constituents and the ash as it forms and a second molten layer below said slag layer comprising iron and containing sulfur fixed as iron sulfide, and removing said combustible effluent gas, excess slag and excess iron-containing layer from said reactor while maintaining a slag layer during said gasification reaction.

Claim 17

The process of claim 13, wherein said particulate coal is partially gasified to form a residue-containing char in addition to said ash, said ash being removed in the slag, and said char being recycled to said reactor.

Claim 18

The process of claim 13, wherein said particulate coal is substantially completely gasified to form a medium BTU combustible gas.

Claim 19

The process of claim 13, wherein said gasification reaction is carried out in the presence of steam continuously fed to said reactor in an amount sufficient to provide an endothermic production of combustible gas comprising hydrogen by reaction with said particulate coal in said reactor.