Process for hydroliquefying coal or like carbonaceous solid materials

Claim 2

In a process for producing hydrocarbons by hydroliquefaction of coal, comprising passing the coal feed into a coal dissolution-hydrogenation zone wherein subjecting the coal under an operating pressure in the range of 1000 to 3000 PSIA and an operating temperature in the range of 700° to 900° F to reactions with hydrogen for yielding desired hydrocarbons in a mixture of gasiform and slurryform hydrogenated coal products containing asphaltenes, the improvement consisting in admixing to these slurryform products, after the gasiform part of said mixture of products leaving said coal dissolution-hydrogenation zone has been taken-off, an alkali selected from the group consisting of alkali metal hydroxides, alkaline earth metal hydroxides, alkali metal carbonates, ammonium hydroxide, in an amount necessary to break, at least partly, the acid-base type structures of asphaltenes present in said slurryform products, subjecting the latter to react with the admixed said alkali at an operating temperature in the range of 200° F to 900° F and under an operating pressure up to 3000 PSIA, and subjecting the treated slurryform products to reactions with hydrogen in a rehydrogenation zone different from said coal dissolution-hydrogenation zone under an operating pressure and temperature in the range of 1050 PSIA to 3100 PSIA and 650° to 900° F respectively, to yield a mixture of a hydrogen containing rehydrogenation product gas with slurryform rehydrogenation products, and separating the hydrogen containing gas product from said slurryform products of the rehydrogenation.

Claim 3

The process of the claim 1, wherein said alkali for breaking the acid-base structures of asphaltenes is in a water diluted form and in this form it is being admixed to said slurryform products.

Claim 4

The process of claim 1, comprising admixing, with the said alkali, a carboxylic salt of calcium to said slurryform products.

Claim 5

The process of claim 1, wherein said hydrogen with which the coal is subjected to reactions in said dissolution-hydrogenation zone is constituted by the hydrogen contained in said gas product separated from the slurryform products of said rehydrogenation, and directed to said coal dissolution-hydrogenation zone.

Claim 6

In a process for producing hydrocarbons by hydroliquefaction of coal, comprising passing hydrogen and coal feed being preheated into a coal dissolution-hydrogenation zone wherein subjecting the coal under an operating pressure in the range of 1000 to 3000 PSIA and an operating temperature in the range of 700° to 900° F to react with hydrogen for yielding desired hydrocarbons in a mixture of gasiform and slurryform hydrogenated coal products containing asphaltenes, the improvement consisting in admixing to these slurryform products, after the gasiform part of said mixture of products leaving said coal dissolution-hydrogenation zone has been taken-off, an alkali selected from the group consisting of alkali metal hydroxides, alkaline earth metal hydroxides, alkali metal carbonates, ammonium hydroxide, in an amount necessary to break, at least partly, the acid-base type structures of asphaltenes present in said slurryform products, subjecting the latter to react with the admixed said alkali at an operating temperature in the range of 200° to 900° F and under an operating pressure up to 3000 PSIA, supplying the treated slurryform products with hydrogen, and subjecting said products to react with the hydrogen in a rehydrogenation zone different from said coal dissolution-hydrogenation zone under an operating pressure and temperature in the range of 1050 PSIA to 3100 PSIA and 650° to 900° F respectively, to yield a mixture of a hydrogen containing rehydrogenation product gas with slurryform rehydrogenation products, and separating the hydrogen containing gas product from said slurryform products of the rehydrogenation.

Claim 7

In a process for producing hydrocarbons by hydroliquefaction of coal, comprising passing hydrogen and coal feed being preheated into a coal dissolution-hydrogenation zone wherein subjecting the coal under an operating pressure in the range of 1000 to 3000 PSIA and an operating temperature in the range of 700° to 900° F to react with hydrogen for yielding desired hydrocarbons in a mixture of gasiform and slurryform hydrogenated coal products containing asphaltenes, the improvement consisting in admixing to these slurryform products, after the gasiform part of said mixture of products leaving said coal dissolution-hydrogenation zone has been taken-off, an alkali selected from the group consisting of alkali metal hydroxides, alkaline earth metal hydroxides, alkali metal carbonates, ammonium hydroxide, in an amount necessary to break, at least partly, the acid-base type structures of asphaltenes present in said slurryform products, subjecting the latter to react with the admixed said alkali at an operating temperature in the range of 200° to 900° F and under an operating pressure up to 3000 PSIA, supplying the treated slurryform products with hydrogen, and subjecting said products to react with the hydrogen in a rehydrogenation zone different from said coal dissolution-hydrogenation zone under an operating pressure and temperature in the range of 1050 PSIA to 3100 PSIA and 650° to 900° F respectively, to yield a mixture of a hydrogen containing rehydrogenation product gas with slurryform rehydrogenation products, and separating the hydrogen containing gas product from said slurryform products of the rehydrogenation.

Claim 8

The process of claim 5, wherein said alkali for breaking the acid-base structures of asphaltenes is in a water diluted form, and in this form it is being admixed to said slurryform products.

Claim 9

The process of claim 5, comprising admixing, with said alkali, a carboxylic salt of calcium to said slurryform products.

Claim 10

The process of claim 5, wherein said hydrogen with which the coal is subjected to react in said dissolution-hydrogenation zone is constituted by the hydrogen contained in said gas product separated from the slurryform products of said rehydrogenation, and directed to said coal feed and into the coal dissolution-hydrogenation zone.

Claim 11

The process of claim 5, comprising passing said hydrogen and coal feed being preheated into the coal dissolution-hydrogenation zone through a preheater.

Claim 12

The process of claim 1, wherein said alkali for breaking the acid-base structures of asphaltenes comprises sodium hydroxide.

Claim 13

The process of claim 1, wherein said alkali for breaking the acid-base structures of asphaltenes comprises ammonium hydroxide.

Claim 14

The process of claim 5, wherein said alkali for breaking the acid-base structures of asphaltenes comprises sodium hydroxide.

Claim 15

The process of claim 5, wherein said alkali for breaking the acid-base structures of asphaltenes comprises ammonium hydroxide.