Coal liquefaction

Claim 2

A process for separating insoluble material from a coal liquefaction product, produced from a coal feed, comprised of carbonaceous matter dissolved in a coal liquefaction solvent and insoluble material, comprising: separating from the coal liquefaction product an essentially solid free stream and a solid containing liquid stream, including coal ash; hydrotreating the solid containing liquid stream at hydrogenation conditions in the absence of extraneous catalyst; and stripping the hydrotreated solid containing liquid stream to strip clean fuel components therefrom and produce a stripped flowable solid containing liquid stream having a reduced quantity of combustible products.

Claim 3

The process of claim 1 wherein the stripping is effected to provide a stripped flowable solid containing liquid stream, having at least 35% Benzene solubles and less than 70%, Benzene solubles.

Claim 4

The process of claim 2 wherein the stripping is effected to strip components boiling at no greater than 900° F

Claim 5

The process of claim 3 wherein the hydrotreating is effected at a temperature from 600° F to 900° F and at pressures from 500 to 3000 psig.

Claim 6

The process of claim 4 wherein the coal liquefaction product is subjected to gravity settling to separate said essentially solid free and said solid containing stream.

Claim 7

The process of claim 5 wherein said gravity settling is effected in the presence of a promoter liquid, said promoter liquid having a characterization factor of at least 9.75, a 5 volume percent distillation temperature of at least about 250° F and a 95 volume percent distillation temperature of at least about 350° F and no greater than about 750° F.

Claim 8

A process for producing clean fuel from coal, comprising: hydrotreating coal dissolved and dispersed in a liquefaction solvent to produce a coal liquefaction product comprised of carbonaceous matter dissolved in the coal liquefaction solvent and insoluble material; separating from the coal liquefaction product, by gravity settling, an essentially solids free stream, as overflow and, as underflow, a solid containing liquid stream, said gravity settling being effected in the presence of a promoter liquid having a characterization factor of at least about 9.75, a 5 volume percent distillation temperature of at least about 250° F, and a 95 volume percent distillation temperature of at least about 350° F and no greater than about 750° F, hydrotreating said solid containing liquid stream at hydrogenation conditions in the absence of extraneous catalyst; stripping the hydrotreated solid containing liquid stream to strip clean fuel components from the hydrotreated stream and provide a flowable stripped solid containing liquid stream; and recovering clean fuel product from the overflow from the gravity settling zone and the clean fuel components recovered in the stripping.

Claim 9

A process for producing clean fuel from coal, comprising: hydrotreating coal dissolved and dispersed in a liquefaction solvent to produce a coal liquefaction product comprised of carbonaceous matter dissolved in the coal liquefaction solvent and insoluble material; separating from the coal liquefaction product, by gravity settling, an essentially solids free stream, as overflow and, as underflow, a solid containing liquid stream, said gravity settling being effected in the presence of a promoter liquid having a characterization factor of at least about 9.75, a 5 volume percent distillation temperature of at least about 250° F, and a 95 volume percent distillation temperature of at least about 350° F and no greater than about 750° F, hydrotreating said solid containing liquid stream at hydrogenation conditions in the absence of extraneous catalyst; stripping the hydrotreated solid containing liquid stream to strip clean fuel components from the hydrotreated stream and provide a flowable stripped solid containing liquid stream; and recovering clean fuel product from the overflow from the gravity settling zone and the clean fuel components recovered in the stripping.

Claim 10

The process of claim 7 wherein the stripping is effected to provide a stripped flowable solid containing liquid stream, having at least 35% Benzene solubles and less than 70%, Benzene solubles.

Claim 11

The process of claim 8 wherein the stripping is effected to strip components boiling at no greater than 900° F.

Claim 12

The process of claim 9 wherein the hydrotreating is effected at a temperature from 600° F to 900° F and at pressures from 500 to 3000 psig.

Claim 13

The process of claim 10 wherein the liquid promoter is at least one member selected from the group consisting of kerosene, kerosene fractions, middle distillates, light gas oils, gas oil fractions, heavy naphthas, white oils and white oil fractions, all from crude oils.