Catalysts for hydrocarbon treating processes

Claim 2

A catalyst comprising a composition comprising a metal component, carbon and hydrogen deposited on a support, the metal constituent of said metal component of said composition being selected from the group consisting of metals of Groups II, III, IV, V, VIB, VIIB, VIII and mixtures thereof of the Periodic Table of Elements, said composition having a surface area of at least about 50 m 2 /g and said support being an aluminum alloy powder having a surface area of less than 5 square meters per gram, said alloy having been prepared by atomizing said aluminum alloy, in molten state, into a stream selected from the group consisting of water, a gas and mixtures thereof, said catalyst having been prepared by the steps which comprise: (a) dispersing in a hydrocarbon oil having a Conradson carbon content up to about 50 weight percent, (1) a thermally decomposable metal compound in an amount sufficient to provide a ratio of atoms of oil Conradson carbon to atom of metal constituent of said thermally decomposable metal compound of less than about 750 to 1, said metal constituent being selected from the group consisting of Group II, Group III, Group IV, Group V, Group VIB, Group VIIB, and Group VIII of the Periodic Table of Elements and mixtures thereof, and (2) said support; (b) heating the resulting mixture in the presence of a gas selected from the group consisting of a hydrogen-containing gas, a hydrogen sulfide-containing gas and a gas comprising hydrogen and hydrogen sulfide, and (c) recovering a supported catalyst.

Claim 3

The catalyst of claim 1 wherein said stream is water.

Claim 4

The catalyst of claim 1 wherein said gas is selected from the group consisting of hydrogen, argon, helium, nitrogen, steam, air, carbon dioxide and mixtures thereof.

Claim 5

The catalyst of claim 1 wherein said aluminum alloy powder comprises at leat one additional metal other than aluminum selected from the group consisting of IB, II, III, IV, VB, VIB, VIIB, VIII and mixtures thereof of the Periodic Table of Elements.

Claim 6

The catalyst of claim 1 wherein said aluminum alloy powder is a ferroaluminum alloy powder.

Claim 7

The catalyst of claim 1 or claim 5 wherein said aluminum alloy powder comprises from about 1 to about 59 weight percent aluminum.

Claim 8

The catalyst of claim 1 wherein said support is ferromagnetic.

Claim 9

The catalyst of claim 1 wherein said metal component of said composition, calculated as the elemental metal, comprises from about 0.01 to about 10 weight percent of said catalyst.

Claim 10

The catalyst of claim 1 wherein said metal component of said composition is selected from the group consisting of vanadium component, tungsten component, molybdenum component, nickel component, cobalt component, iron component and mixtures thereof.

Claim 11

The catalyst of claim 1 wherein said catalyst has a size ranging from about 0.5 micron to about 150 microns in diameter.

Claim 12

A process for the preparation of a supported catalyst which comprises, the steps of: (a) dispersing in a hydrocarbon oil having a Conradson content up to about 50 weight percent, (1) a thermally decomposable metal compound in an amount sufficient to provide a ratio of atoms of oil Conradson carbon to atom of metal constituent of said thermally decomposable compound of less than about 750 to 1, said metal constituent being selected from the group consisting of Group II, Group III, Group IV, Group V, Group VIB, Group VIIB, and Group VIII and mixtures thereof of the Periodic Table of Elements, and (2) an aluminum alloy powder support having a surface area of less than about 5 square meters per gram, said alloy support having been prepared by atomizing said aluminum alloy, in molten state, into a stream selected from the group consisting of water, a gas and mixtures thereof; (b) heating the resulting mixture in the presence of a gas selected from the group consisting of a hydrogen-containing gas, a hydrogen sulfide-containing gas, a gas comprising hydrogen and hydrogen sulfide, to produce a composition having a surface area of at least about 50 m 2 /g deposited on said support, and (c) recovering a supported catalyst.

Claim 13

A process for the preparation of a supported catalyst which comprises, the steps of: (a) dispersing in a hydrocarbon oil having a Conradson content up to about 50 weight percent, (1) a thermally decomposable metal compound in an amount sufficient to provide a ratio of atoms of oil Conradson carbon to atom of metal constituent of said thermally decomposable compound of less than about 750 to 1, said metal constituent being selected from the group consisting of Group II, Group III, Group IV, Group V, Group VIB, Group VIIB, and Group VIII and mixtures thereof of the Periodic Table of Elements, and (2) an aluminum alloy powder support having a surface area of less than about 5 square meters per gram, said alloy support having been prepared by atomizing said aluminum alloy, in molten state, into a stream selected from the group consisting of water, a gas and mixtures thereof; (b) heating the resulting mixture in the presence of a gas selected from the group consisting of a hydrogen-containing gas, a hydrogen sulfide-containing gas, a gas comprising hydrogen and hydrogen sulfide, to produce a composition having a surface area of at least about 50 m 2 /g deposited on said support, and (c) recovering a supported catalyst.

Claim 14

The process of claim 11 wherein said aluminum alloy powder comprises at least one additional metal other than aluminum selected from the group consisting of Groups, IB, II, III, IV, VB, VIB, VIIB, VIII and mixtures thereof of the Periodic Table of Elements.

Claim 15

The process of claim 11 wherein said aluminum alloy powder is a ferroaluminum alloy powder.

Claim 16

The process of claim 11 wherein said aluminum alloy powder comprises from about 1 to about 59 weight percent aluminum.

Claim 17

The process of claim 11 wherein said thermally decomposable metal compound is selected from the group consisting of inorganic metal compounds, salts of organic acids, organometallic compounds and salts of organic amines.

Claim 18

The process of claim 11 wherein said thermally decomposable metal compound is a metal naphthenate.

Claim 19

The process of claim 11 wherein said thermally decomposable metal compound is phosphomolybdic acid.

Claim 20

The process of claim 11 wherein said metal constituent of said thermally decomposable metal compound is selected from the group consisting of vanadium, tungsten, molybdenum, nickel, cobalt, iron and mixtures thereof.

Claim 21

The process of claim 11 wherein said support has a surface area of less than about 1 square meter per gram.

Claim 22

The process of claim 11, wherein said heating of step (b) is conducted at a temperature ranging from about 199° C. to about 571° C.

Claim 23

A process for the preparation of a supported catalyst which comprises the steps of: (a) dispersing in a hydrocarbon oil having a Conradson carbon content up to about 50 weight percent, a thermally decomposable compound in an amount sufficient to provide a ratio of atoms of oil Conradson carbon to atom of metal constituent of said thermally decomposable compounds of less than about 750 to 1, said metal constituent of said thermally decomposable compound being selected from the group consisting of Group II, Group III, Group IV, Group V, Group VIB, Group VIIB, Group VIII and mixtures thereof of the Periodic Table of Elements; (b) heating the resulting mixture in the presence of a gas selected from the group consisting of a hydrogen-containing gas, a hydrogen sulfide-containing gas, and a gas comprising hydrogen and hydrogen sulfide, to form a catalytic composition comprising a metal component, carbon and hydrogen; (c) contacting the resulting composition with an aluminum alloy powder support having a surface area of less than about 5 square meters per gram, said support having been prepared by atomizing said alloy, in molten state, into a stream selected from the group consisting of water, a gas and mixtures thereof, said contacting being in the presence of a hydrocarbon oil having a Conradson carbon content up to about 50 weight percent; (d) heating the resulting mixture in the presence of a gas selected from the group consisting of a hydrogen-containing gas, a hydrogen sulfide-containing gas and a gas comprising hydrogen and hydrogen sulfide, for a time sufficient to deposit said composition on said support, said composition having a surface area of at least about 50 m 2 /g, and (e) recovering a supported catalyst.

Claim 24

A process for the preparation of a supported catalyst which comprises the steps of: (a) dispersing in a hydrocarbon oil having a Conradson carbon content up to about 50 weight percent, a thermally decomposable compound in an amount sufficient to provide a ratio of atoms of oil Conradson carbon to atom of metal constituent of said thermally decomposable compounds of less than about 750 to 1, said metal constituent of said thermally decomposable compound being selected from the group consisting of Group II, Group III, Group IV, Group V, Group VIB, Group VIIB, Group VIII and mixtures thereof of the Periodic Table of Elements; (b) heating the resulting mixture in the presence of a gas selected from the group consisting of a hydrogen-containing gas, a hydrogen sulfide-containing gas, and a gas comprising hydrogen and hydrogen sulfide, to form a catalytic composition comprising a metal component, carbon and hydrogen; (c) contacting the resulting composition with an aluminum alloy powder support having a surface area of less than about 5 square meters per gram, said support having been prepared by atomizing said alloy, in molten state, into a stream selected from the group consisting of water, a gas and mixtures thereof, said contacting being in the presence of a hydrocarbon oil having a Conradson carbon content up to about 50 weight percent; (d) heating the resulting mixture in the presence of a gas selected from the group consisting of a hydrogen-containing gas, a hydrogen sulfide-containing gas and a gas comprising hydrogen and hydrogen sulfide, for a time sufficient to deposit said composition on said support, said composition having a surface area of at least about 50 m 2 /g, and (e) recovering a supported catalyst.