Hydroconversion of an oil-coal mixture

Claim 2

A process for simultaneously hydroconverting a non-hydrogen donor heavy hydrocarbon oil and coal in admixture, which comprises: (a) forming a mixture of said heavy hydrocarbon oil, coal and an added thermally decomposable metal compound, in an amount ranging from about 10 to about 950 weight parts per million, calculated as the elemental metal, based on said oil-coal mixture, said metal being selected from the group consisting of Groups IVB, VB, VIB, VIIB and VIII of the Periodic Table of Elements and mixtures thereof; (b) converting said thermally decomposable metal compound to a catalyst within said mixture in the presence of a hydrogen-containing gas by heating said mixture to an elevated temperature; (c) reacting the resulting mixture containing said catalyst with hydrogen under oil and coal hydroconversion conditions, such that at least 50 weight percent of said heavy oil has a boiling point below the initial boiling point of said heavy oil, in a hydroconversion zone, said catalyst being the sole catalyst in said hydroconversion zone, and (d) recovering a hydroconverted normally liquid hydrocarbon product.

Claim 3

The process of claim 1 wherein said coal comprises from 2 to 50 weight percent of said mixture of step (a).

Claim 4

The process of claim 1 wherein said coal comprises from about 3 to 20 weight percent of said mixture of step (a).

Claim 5

The process of claim 1 wherein said thermally decomposable metal compound is selected from the group consisting of inorganic metal compounds, salts of organic acids, organometallic compounds and salts or organic amines.

Claim 6

The process of claim 1 wherein said thermally decomposable metal compound is selected from the group consisting of salts of acyclic aliphatic carboxylic acids and salts of alicyclic aliphatic carboxylic acids.

Claim 7

The process of claim 1 wherein said thermally decomposable metal compound is a salt of napthenic acid.

Claim 8

The process of claim 1 wherein the metal constituent of said thermally decomposable metal compound is selected from the group consisting of molybdenum, chromium and vanadium.

Claim 9

The process of claim 1 wherein said thermally decomposable metal compound is molybdenum naphthenate.

Claim 10

The process of claim 1 wherein said thermally decomposable metal compound is a phosphomolybdic acid.

Claim 11

The process of claim 1 wherein said hydrogen-containing gas of step (b) comprises from about 1 to about 90 mole percent hydrogen sulfide.

Claim 12

The process of claim 1 wherein said thermally decomposable metal compound is converted by first heating the mixture of thermally decomposable metal compound, oil and coal to a temperature ranging from about 325° C. to about 415° C. in the presence of said hydrogen-containing gas to form a catalyst within said mixture and subsequently reacting the resulting mixture containing the catalyst with hydrogen under hydroconversion conditions.

Claim 13

The process of claim 12 wherein said hydrogen-containing gas also contains hydrogen sulfide.

Claim 14

The process of claim 1 wherein said thermally decomposable metal compound is converted in the presence of a hydrogen-containing gas at hydroconversion conditions thereby forming said catalyst in situ within said mixture in said hydroconversion zone and producing a hydroconverted oil.

Claim 15

The process of claim 1 wherein said hydroconversion conditions include a temperature ranging from about 416° to about 538° C. (780.8° to 1000° F.) and a hydrogen pressure of at least 500 psig.

Claim 16

In the process of claim 1 wherein the reaction product of step (c) comprises a hydroconverted oil containing catalytic solids, the additional steps which comprise separating at least a portion of said catalytic solids from the hydroconverted oil and recycling at least a portion of said solids to step (a) or to step (c).

Claim 17

A process for simultaneously hydroconverting a non-hydrogen donor heavy hydrocarbon oil and coal in admixture, which comprises: (a) forming a mixture of said heavy hydrocarbon oil, coal and an added thermally decomposable metal compound, said metal compound being added in an amount ranging from about 10 to about 950 weight parts per million, calculated as the elemental metal, based on said oil-coal mixture, said metal being selected from the group consisting of Groups IVB, VB, VIB, VIIB and VIII of the Periodic Table of Elements and mixtures thereof; (b) heating the mixture resulting from step (a) to a temperature ranging from 325° C. to about 415° C. in the presence of a hydrogen-containing gas to form a catalyst within said mixture, said catalyst comprising from about 10 to about 950 wppm of said metal, calculated as the elemental metal, based on said oil-coal mixture; (c) reacting the resulting mixture containing said catalyst with hydrogen under hydroconversion conditions in a hydroconversion zone including a temperature ranging from about 416° C. to about 538° C. (780.8° to 1000° F.) and a hydrogen pressure ranging from about 500 to about 5000 psig, said catalyst being the sole catalyst in said hydroconversion zone, and (d) recovering a hydroconverted oil.

Claim 18

A process for simultaneously hydroconverting a non-hydrogen donor heavy hydrocarbon oil and coal in admixture, which comprises: (a) forming a mixture of said heavy hydrocarbon oil, coal and an added thermally decomposable metal compound, said metal compound being added in an amount ranging from about 10 to about 950 weight parts per million, calculated as the elemental metal, based on said oil-coal mixture, said metal being selected from the group consisting of Groups IVB, VB, VIB, VIIB and VIII of the Periodic Table of Elements and mixtures thereof; (b) heating the mixture resulting from step (a) to a temperature ranging from 325° C. to about 415° C. in the presence of a hydrogen-containing gas to form a catalyst within said mixture, said catalyst comprising from about 10 to about 950 wppm of said metal, calculated as the elemental metal, based on said oil-coal mixture; (c) reacting the resulting mixture containing said catalyst with hydrogen under hydroconversion conditions in a hydroconversion zone including a temperature ranging from about 416° C. to about 538° C. (780.8° to 1000° F.) and a hydrogen pressure ranging from about 500 to about 5000 psig, said catalyst being the sole catalyst in said hydroconversion zone, and (d) recovering a hydroconverted oil.

Claim 19

The process of claim 16 wherein said hydrogen-containing gas of step (b) comprises from about 1 to about 90 mole percent hydrogen sulfide.

Claim 20

The process of claim 16 wherein said thermally decomposable metal compound is a molybdenum compound.

Claim 21

The process of claim 16 wherein said thermally decomposable metal compound is molybdenum naphthenate.

Claim 22

The process of claim 16 wherein said thermally decomposable metal compound is a phosphomolybdic acid.

Claim 23

The process of claim 16 wherein said metal compound in step (a) is added in an amount ranging from about 25 to about 300 weight parts per million.

Claim 24

In the process of claim 16 wherein the reaction product of step (c) comprises a hydroconverted oil containing catalytic solids, the additional steps which comprise separating at least a portion of said catalytic solids from the hydroconverted oil and recycling at least a portion of said catalytic solids to step (a) or to step (c).

Claim 25

The process of claim 16 wherein said heavy oil is hydroconverted in step (c) so that at least 50 weight percent thereof has a boiling point below the initial boiling point of said heavy oil.