Coal hydrogenation process with direct coal feed and improved residuum conversion

Claim 2

A process for hydrogenation of coal to produce hydrocarbon liquid and gaseous products, comprising: (a) pressurizing particulate coal which has been dried to a moisture content of less than about 5 W % and feeding it at temperature below about 600° F. directly, without further heating into a pressurized backmixed type reaction zone containing coal-derived liquid and hydrogen; (b) passing the coal along with said coal-derived liquid and hydrogen upwardly through said reaction zone which is maintained at 700°-975° F. temperature and 1000-5000 psig hydrogen partial pressure to rapidly heat the cool and convert it to hydrogenated coal-derived material; (c) heating recycle hydrogen and a recycle coal-derived hydrogen liquid normally boiling above about 550° F. to a temperature sufficient to maintain said reaction zone temperature and recycling the heated materials into the lower part of said reaction zone to maintain said temperature therein; (d) withdrawing said hydrogen coal-derived material containing gas and liquid fractions from the upper part of said reaction zone, and phase separating said material into gaseous and liquid fractions; (e) passing said liquid fraction from said phase separation to a liquid-solids separation step, from which an overhead liquid stream normally boiling above about 550° F. and containing a reduced concentration of particulate solids is heated to said temperature above the reaction zone before recycling said heated coal-derived liquid into the reaction zone; and (f) recovering hydrocarbon gas and increased yield of low boiling hydrocarbon liquid product from the process.

Claim 3

The process of claim 1, wherein the particulate coal feed is mixed with a coal-derived hydrocarbon slurrying liquid before pressurizing, and the resulting coal-liquid slurry mixture is fed without further heating directly into the lower of of said reaction zone.

Claim 4

The process of claim 2, wherein the coal-liquid slurry mixing temperature is 400°-575° F.

Claim 5

The process of claim 2, wherein the coal slurrying liquid has a normal boiling temperature range above about 600° F.

Claim 6

A process for catalytic hydrogenation of coal to produce hydrocarbon liquid and gaseous products, comprising: (a) pressurizing particulate coal and feeding it at temperature below about 600° F. directly without further heating into a pressurized catalytic reaction zone containing coal-derived liquid and hydrogen and an ebullated bed of particulate hydrogenation catalyst; (b) passing the coal along with said coal-derived liquid and hydrogen upwardly through said ebullated bed of particulate hydrocarbon catalyst, said bed being maintained at 700°-950° F. temperature and 1000-5000 psig hydrogen partial pressure to rapidly heat the coal and catalytically convert it to hydrogenated coal-derived material; (c) heating recycle hydrogen and a recycle coal-derived hydrocarbon liquid normally boiling above about 550° F. to a temperature sufficient to maintain said reaction zone temperature and recycling the heated materials into the lower part of said reaction zone to maintain said temperature therein; (d) withdrawing said hydrogenated coal-derived material containing gas and liquid fractions from the upper part of said reaction zone, and phase separating said material into gaseous and liquid fractions; (e) passing that liquid fraction from said phase separation to a liquid-solids separation step, from which an overflow liquid stream normally boiling above about 550°0 and containing a reduced concentration of particulate solids is heated to said temperature above the reaction zone temperature before recycling said heated coal-derived liquid into the reaction zone; and (f) recovering hydrocarbon gas and increased yield of low boiling hydrocarbon liquid product from the process.

Claim 7

A process for catalytic hydrogenation of coal to produce hydrocarbon liquid and gaseous products, comprising: (a) pressurizing particulate coal and feeding it at temperature below about 600° F. directly without further heating into a pressurized catalytic reaction zone containing coal-derived liquid and hydrogen and an ebullated bed of particulate hydrogenation catalyst; (b) passing the coal along with said coal-derived liquid and hydrogen upwardly through said ebullated bed of particulate hydrocarbon catalyst, said bed being maintained at 700°-950° F. temperature and 1000-5000 psig hydrogen partial pressure to rapidly heat the coal and catalytically convert it to hydrogenated coal-derived material; (c) heating recycle hydrogen and a recycle coal-derived hydrocarbon liquid normally boiling above about 550° F. to a temperature sufficient to maintain said reaction zone temperature and recycling the heated materials into the lower part of said reaction zone to maintain said temperature therein; (d) withdrawing said hydrogenated coal-derived material containing gas and liquid fractions from the upper part of said reaction zone, and phase separating said material into gaseous and liquid fractions; (e) passing that liquid fraction from said phase separation to a liquid-solids separation step, from which an overflow liquid stream normally boiling above about 550°0 and containing a reduced concentration of particulate solids is heated to said temperature above the reaction zone temperature before recycling said heated coal-derived liquid into the reaction zone; and (f) recovering hydrocarbon gas and increased yield of low boiling hydrocarbon liquid product from the process.

Claim 8

The process of claim 5, wherein the particulate coal is dried to moisture content less than about 5 W % before pressurizing and the coal is then fed directly into said catalytic reaction zone at substantially the drying temperature.

Claim 9

The process of claim 5, wherein the particulate coal feed is mixed with a coal-derived hydrocarbon slurrying liquid before pressurizing, and the resulting coal-liquid slurry mixture is fed without further heating directly into the lower part of said reaction zone.

Claim 10

The process of claim 7, wherein the coal-liquid slurry mixing temperature is 400°-600° F.

Claim 11

The process of claim 7, wherein the coal slurrying liquid has a normal boiling temperature range above about 600° F.

Claim 12

The process of claim 5, wherein the reaction zone conditions are maintained at 750°-900° F. temperature and 1000-4000 psig hydrogen partial pressure.

Claim 13

The process of claim 5, wherein the particulate coal is pressurized to reaction zone pressure in a screw type feeder before introducing the coal into the reaction zone.

Claim 14

The process of claim 11, wherein the pressurized coal is mixed with a heated recycle hydrocarbon liquid and the mixture of coal-liquid is then introduced into the reaction zone.

Claim 15

The process of claim 5, wherein the coal is butuminous type.

Claim 16

The process of claim 5, wherein the coal is subbituminous type coal.

Claim 17

The process of claim 5, wherein the coal is pressurized to reaction zone pressure using a screw type feeder and the pressurized coal is mixed with recycle hydrogen and recycle coal-derived hydrocarbon liquid normally boiling above about 550° F. before feeding the coal-hydrocarbon liquid mixture into said reaction zone.

Claim 18

A process for catalytic hydrogenation of coal to produce hydrocarbon liquid and gaseous products, comprising: (a) mixing particulate coal with a hydrocarbon liquid to provide a flowable slurry and feeding the slurry at temperature of below about 600° F. directly without further heating into a pressurized catalytic reaction zone containing coal-derived liquid and hydrogen and an ebullated bed of particulate hydrogenation catalyst; (b) passing the coal along with said coal-derived liquid and hydrogen upwardly through said ebullated bed of particulate hydrogenation catalyst, said bed being maintained at 700°-950° F. temperature and 1000-5000 psig hydrogen partial pressure to rapidly heat the coal and catalytically convert it to a hydrogenated coal-derived material; (c) heating recycle hydrogen and a coal-derived hydrocarbon liquid normally boiling above about 600° F. to temperatures about 10° F.-100° F. above the reaction zone temperature and introducing the heated materials into the lower part of said reaction zone to maintain said temperature therein; (d) withdrawing said hydrogenated coal-derived material containing gas and liquid fractions from the upper part of said reaction zone, and phase separating said material into gaseous and liquid fractions; (e) passing said liquid fraction from said phase separation to a liquid-solids separation step, from which an overhead liquid stream normally boiling above about 650° F. and containing a reduced concentration of particulate solids is heated to said temperature above the reaction zone temperature before recycling the heated coal-derived liquid into the reaction zone; and (f) recovering hydrocarbon gas and increased yields of low boiling hydrocarbon liquid products from the process.

Claim 19

A process for catalytic hydrogenation of coal to produce hydrocarbon liquid and gaseous products, comprising: (a) mixing particulate coal with a hydrocarbon liquid to provide a flowable slurry and feeding the slurry at temperature of below about 600° F. directly without further heating into a pressurized catalytic reaction zone containing coal-derived liquid and hydrogen and an ebullated bed of particulate hydrogenation catalyst; (b) passing the coal along with said coal-derived liquid and hydrogen upwardly through said ebullated bed of particulate hydrogenation catalyst, said bed being maintained at 700°-950° F. temperature and 1000-5000 psig hydrogen partial pressure to rapidly heat the coal and catalytically convert it to a hydrogenated coal-derived material; (c) heating recycle hydrogen and a coal-derived hydrocarbon liquid normally boiling above about 600° F. to temperatures about 10° F.-100° F. above the reaction zone temperature and introducing the heated materials into the lower part of said reaction zone to maintain said temperature therein; (d) withdrawing said hydrogenated coal-derived material containing gas and liquid fractions from the upper part of said reaction zone, and phase separating said material into gaseous and liquid fractions; (e) passing said liquid fraction from said phase separation to a liquid-solids separation step, from which an overhead liquid stream normally boiling above about 650° F. and containing a reduced concentration of particulate solids is heated to said temperature above the reaction zone temperature before recycling the heated coal-derived liquid into the reaction zone; and (f) recovering hydrocarbon gas and increased yields of low boiling hydrocarbon liquid products from the process.

Claim 20

A process for catalytic hydrogenation of coal to product hydrocarbon liquid and gaseous products, comprising: (a) pressurizing particulate coal in an extruder type feeder at temperature below about 600° F. and feeding the coal along with a hydrocarbon liquid directly into a pressurized catalytic reaction zone containing coal-derived liquid and hydrogen and an ebullated bed of particulate hydrogenation catalyst; (b) passing the coal along with said coal-derived liquid and hydrogen upwardly through said ebullated bed of particulate hydrogenation catalyst, said bed being maintained at 700°-950° F. temperature and 1000-5000 psig hydrogen partial pressure to rapidly heat the coal and catalytically convert it to a hydrogenated coal-derived material; (c) heating recycling hydrogen and a coal-derived hydrocarbon liquid normally boiling above about 650° F. to temperatures about 10° F.-100° F. above the reaction zone temperature and introducing the heated materials into the lower part of said reaction zone to maintain the desired temperature therein; (d) withdrawing said hydrogenated coal-derived material containing gas and liquid fractions from the upper part of said reaction zone, and phase separating said material into gaseous and liquid fractions; (e) passing said liquid fraction from said phase separation to a liquid-solids separation step, from which an overhead liquid stream normally boiling above about 550° F. and containing a reduced concentration of particulate solids is heated to said temperature above the reaction zone temperature before recycling the heated coal-derived liquid into the reaction zone; and (f) recovering hydrocarbon gas and increased yields of low boiling hydrocarbon liquid product from the process.

Claim 21

A process for catalytic hydrogenation of coal to product hydrocarbon liquid and gaseous products, comprising: (a) pressurizing particulate coal in an extruder type feeder at temperature below about 600° F. and feeding the coal along with a hydrocarbon liquid directly into a pressurized catalytic reaction zone containing coal-derived liquid and hydrogen and an ebullated bed of particulate hydrogenation catalyst; (b) passing the coal along with said coal-derived liquid and hydrogen upwardly through said ebullated bed of particulate hydrogenation catalyst, said bed being maintained at 700°-950° F. temperature and 1000-5000 psig hydrogen partial pressure to rapidly heat the coal and catalytically convert it to a hydrogenated coal-derived material; (c) heating recycling hydrogen and a coal-derived hydrocarbon liquid normally boiling above about 650° F. to temperatures about 10° F.-100° F. above the reaction zone temperature and introducing the heated materials into the lower part of said reaction zone to maintain the desired temperature therein; (d) withdrawing said hydrogenated coal-derived material containing gas and liquid fractions from the upper part of said reaction zone, and phase separating said material into gaseous and liquid fractions; (e) passing said liquid fraction from said phase separation to a liquid-solids separation step, from which an overhead liquid stream normally boiling above about 550° F. and containing a reduced concentration of particulate solids is heated to said temperature above the reaction zone temperature before recycling the heated coal-derived liquid into the reaction zone; and (f) recovering hydrocarbon gas and increased yields of low boiling hydrocarbon liquid product from the process.

Claim 22

The process of claim 17, wherein a minor amount of coal-derived liquid is introduced into the extruder feeder at near its inlet end to provide a seal.

Claim 23

A process for hydrogenation of coal to produce hydrocarbon liquid and gaseous products; comprising: (a) pressurizing particulate coal and feeding it at temperature below about 600° F. directly without further heating into a pressurized backmixed type reaction zone containing coal-derived liquid and hydrogen; (b) passing the coal along with said coal-derived liquid and hydrogen upwardly through said reaction zone which is maintained at 700°-950° F. temperature and 1000-5000 psig hydrogen partial pressure to rapidly heat the coal and convert it to hydrogenated coal-derived material; (c) heating recycle hydrogen and a recycle coal-derived hydrocarbon liquid normally boiling above about 550° F. to a temperature sufficient to maintain said reaction zone temperature and recycling the heated materials into the lower part of said reaction zone to maintain said temperature therein, said recycled hydrogen and coal-derived hydrocarbon liquid being heated separately before being introduced in separate streams into said lower part of said reaction zone; (d) withdrawing said hydrogenated coal-derived material containing gas and liquid fractions from the upper part of said reaction zone, and phase separating said material into gaseous and liquid fractions; (e) passing said liquid fraction from said phase separation to a liquid-solids separation step, from which an over-heat liquid stream normally boiling above about 550° F. and containing a reduced concentration of particulate solids is heated to said temperature above the reaction zone temperature before recycling said heated coal-derived liquid into the reaction zone; and (f) recovering hydrocarbon gas and increased yield of low boiling hydrocarbon liquid product from the process.

Claim 24

A process for hydrogenation of coal to produce hydrocarbon liquid and gaseous products; comprising: (a) pressurizing particulate coal and feeding it at temperature below about 600° F. directly without further heating into a pressurized backmixed type reaction zone containing coal-derived liquid and hydrogen; (b) passing the coal along with said coal-derived liquid and hydrogen upwardly through said reaction zone which is maintained at 700°-950° F. temperature and 1000-5000 psig hydrogen partial pressure to rapidly heat the coal and convert it to hydrogenated coal-derived material; (c) heating recycle hydrogen and a recycle coal-derived hydrocarbon liquid normally boiling above about 550° F. to a temperature sufficient to maintain said reaction zone temperature and recycling the heated materials into the lower part of said reaction zone to maintain said temperature therein, said recycled hydrogen and coal-derived hydrocarbon liquid being heated separately before being introduced in separate streams into said lower part of said reaction zone; (d) withdrawing said hydrogenated coal-derived material containing gas and liquid fractions from the upper part of said reaction zone, and phase separating said material into gaseous and liquid fractions; (e) passing said liquid fraction from said phase separation to a liquid-solids separation step, from which an over-heat liquid stream normally boiling above about 550° F. and containing a reduced concentration of particulate solids is heated to said temperature above the reaction zone temperature before recycling said heated coal-derived liquid into the reaction zone; and (f) recovering hydrocarbon gas and increased yield of low boiling hydrocarbon liquid product from the process.

Claim 25

The process of claim 19, wherein the recycled hydrogen and coal-derived hydrocarbon liquid are mixed together and then heated before introducing the mixed heated streams into the lower part of said reaction zone to maintain said temperature therein.

Claim 26

A process for catalytic hydrogenation of coal to produce hydrocarbon liquid and gaseous products, comprising: (a) pressurizing particulate coal and feeding it at temperature below about 600° F. directly, without further heating, into a pressurized catalytic reaction zone containing coal-derived liquid and hydrogen and an ebullated bed of particulate hydrogenation catalyst; (b) passing the coal along with said coal-derived liquid and hydrogen upwardly through said ebullated bed of particulate hydrogenation catalyst, said bed being maintained at 700°-950° F. temperature and 1000-5000 psig hydrogen partial pressure to rapidly heat the coal and catalytically convert it to hydrogenated coal-derived material; (c) heating recycle hydrogen and a recycle coal-derived hydrocarbon liquid normally boiling above about 500° F. to a temperature sufficient to maintain said reaction zone temperature and recycling the heated materials into the lower part of said reaction zone to maintain said temperature therein, said recycled hydrogen and coal-derived hydrocarbon liquid being heated separately before being introduced in separate streams into said lower part of said reaction zone; (d) withdrawing said hydrogenated coal-derived material containing gas and liquid fractions from the upper part of said reaction zone, and phase separating said material into gaseous and liquid fractions; (e) passing said liquid fraction from said phase separation to a liquid-solids separation step, from which an overhead liquid stream normally boiling above about 550° F. and containing a reduced concentration of particulate solids is heated to said temperature above the reaction zone temperature before recycling said heated coal-derived liquid into the reaction zone; and (f) recovering hydrocarbon gas and increased yield of low boiling hydrocarbon liquid product from the process.

Claim 27

A process for catalytic hydrogenation of coal to produce hydrocarbon liquid and gaseous products, comprising: (a) pressurizing particulate coal and feeding it at temperature below about 600° F. directly, without further heating, into a pressurized catalytic reaction zone containing coal-derived liquid and hydrogen and an ebullated bed of particulate hydrogenation catalyst; (b) passing the coal along with said coal-derived liquid and hydrogen upwardly through said ebullated bed of particulate hydrogenation catalyst, said bed being maintained at 700°-950° F. temperature and 1000-5000 psig hydrogen partial pressure to rapidly heat the coal and catalytically convert it to hydrogenated coal-derived material; (c) heating recycle hydrogen and a recycle coal-derived hydrocarbon liquid normally boiling above about 500° F. to a temperature sufficient to maintain said reaction zone temperature and recycling the heated materials into the lower part of said reaction zone to maintain said temperature therein, said recycled hydrogen and coal-derived hydrocarbon liquid being heated separately before being introduced in separate streams into said lower part of said reaction zone; (d) withdrawing said hydrogenated coal-derived material containing gas and liquid fractions from the upper part of said reaction zone, and phase separating said material into gaseous and liquid fractions; (e) passing said liquid fraction from said phase separation to a liquid-solids separation step, from which an overhead liquid stream normally boiling above about 550° F. and containing a reduced concentration of particulate solids is heated to said temperature above the reaction zone temperature before recycling said heated coal-derived liquid into the reaction zone; and (f) recovering hydrocarbon gas and increased yield of low boiling hydrocarbon liquid product from the process.

Claim 28

The process of claim 21, wherein the particulate hydrogenation catalyst is selected from the group consisting of oxides of cobalt, iron, molybdenum, nickel, tin and mixtures thereof, deposited on a base material selected from the group consisting of alumina, magnesia, silica and combination thereof.

Claim 29

The process of claim 21, wherein the overflow liquid containing reduced solids concentration from said liquid-solids separation is heated to a temperature 10°-100° F. above the reaction zone temperature before introducing the heated coal-derived liquid into said reaction zone to help maintain said reaction zone temperature.