Perovskite catalysts and process for their preparation

Claim 2

In a supported perovskite catalyst for hydrocarbon conversion and hydrocarbon treating processes which comprises a perovskite comprising at least one transition metal, the improvement which comprises: a support comprising a metal oxide and a spinel on the surface of said metal oxide, said spinel being selected from the group consisting of normal spinel and inverse spinel, said normal spinel having an empirical formula MY 2 O 4 wherein M and Y in said normal spinel formula are cations of different metals and wherein one of said cations of said normal spinel formula is the metal of said metal oxide, said inverse spinel having an empirical formula Y(XY)O 4 wherein Y and X in said inverse spinel formula are cations of different metals, and wherein one of said cations of said inverse spinel formula is the metal of said metal oxide, said supported catalyst having a surface area of at least 65 m 2 /g.

Claim 3

The supported perovskite catalyst of claim 1 wherein said metal oxide is a porous metal oxide.

Claim 4

The supported perovskite catalyst of claim 1 wherein said metal oxide is selected from the group consisting of Al 2 O 3 , MgO, TiO 2 , ZrO 2 , HfO 2 , WO 3 and mixtures thereof.

Claim 5

The supported catalyst of claim 1 wherein said metal oxide is alumina.

Claim 6

The supported perovskite catalyst of claim 1 wherein said perovskite is an oxide of at least two metals and wherein the sum of the ionic charges of the metals of the oxide equals six.

Claim 7

The supported perovskite catalyst of claim 1 wherein said perovskite is selected from the group consisting of LaCoO 3 , LaCrO 3 , CaThO 3 , AgNbO 3 and SrZrO 3 .

Claim 8

The supported perovskite catalyst of claim 1 wherein the surface area of the supported catalyst ranges from about 65 m 2 /g to about 250 m 2 /g.

Claim 9

The supported perovskite catalyst of claim 1 wherein the cations of said spinel are selected from the group consisting of Al, Mg, Fe, Co, Ni, Mn, Zn, Ti, Sn, Cu and Cr.

Claim 10

The catalyst of claim 1 wherein said metal oxide is alumina and wherein said spinel is MgAl 2 O 4 .

Claim 11

A supported perovskite catalyst which comprises a perovskite selected from the group consisting of LaCoO 3 , LaCrO 3 , CaThO 3 , AgNbO 3 and SrZrO 3 , said perovskite being composited with a support comprising alumina and a spinel on the surface of said alumina, said spinel being MgAl 2 O 4 .

Claim 12

A supported perovskite catalyst which comprises a perovskite selected from the group consisting of LaCoO 3 , LaCrO 3 , CaThO 3 , AgNbO 3 and SrZrO 3 , said perovskite being composited with a support comprising alumina and a spinel on the surface of said alumina, said spinel being MgAl 2 O 4 .

Claim 13

A process for the preparation of a supported perovskite catalyst for hydrocarbon conversion and hydrocarbon treating processes, which comprises: a. treating a metal oxide having an initial surface area ranging from about 50 to about 250 m 2 /g with at least one metal component such that the algebraic sum of the ionic charges of the metal of said metal oxide and the metal of said metal component corresponds to the algebraic sum of cations required for spinel formation, said spinel being selected from the group consisting of normal spinel and inverse spinel, said normal spinel having an empirical formula MY 2 O 4 , wherein M and Y in said normal spinel formula are cations of different metals, said inverse spinel having an empirical formula Y(XY)O 4 , wherein Y and X in said inverse spinel formula are cations of different metals; b. calcining the treated metal oxide resulting from step (a) at a temperature sufficient to produce a spinel on at least a portion of the surface of said treated metal oxide; c. treating the calcined metal oxide having said surface spinel thereon resulting from step (b) with perovskite precursor metal components comprising at least one transition metal component; d. calcining at a temperature of at least 540° C. the perovskite precursor treated-material resulting from step (c) to convert said perovskite precursors to a perovskite and thereby produce a supported perovskite catalyst.

Claim 14

A process for the preparation of a supported perovskite catalyst for hydrocarbon conversion and hydrocarbon treating processes, which comprises: a. treating a metal oxide having an initial surface area ranging from about 50 to about 250 m 2 /g with at least one metal component such that the algebraic sum of the ionic charges of the metal of said metal oxide and the metal of said metal component corresponds to the algebraic sum of cations required for spinel formation, said spinel being selected from the group consisting of normal spinel and inverse spinel, said normal spinel having an empirical formula MY 2 O 4 , wherein M and Y in said normal spinel formula are cations of different metals, said inverse spinel having an empirical formula Y(XY)O 4 , wherein Y and X in said inverse spinel formula are cations of different metals; b. calcining the treated metal oxide resulting from step (a) at a temperature sufficient to produce a spinel on at least a portion of the surface of said treated metal oxide; c. treating the calcined metal oxide having said surface spinel thereon resulting from step (b) with perovskite precursor metal components comprising at least one transition metal component; d. calcining at a temperature of at least 540° C. the perovskite precursor treated-material resulting from step (c) to convert said perovskite precursors to a perovskite and thereby produce a supported perovskite catalyst.

Claim 15

The process of claim 11 wherein said oxide is a porous inorganic metal oxide or a porous inorganic metal oxide gel.

Claim 16

The process of claim 11 wherein said metal oxide is selected from the group consisting of Al 2 O 3 ; MgO; TiO 2 , ZrO 2 ; HfO 2 ; WO 3 and mixtures thereof.

Claim 17

The process of claim 11 wherein said metal oxide comprises alumina.

Claim 18

The process of claim 11 wherein said perovskite precursor metal components are selected from components having cationic charges such that the algebraic sum of said cations equals six.

Claim 19

The process of claim 11 wherein said perovskite precursor metal components are two metal components, the sum of the cationic charges of which equals six.

Claim 20

The process of claim 11 wherein said perovskite precursor metal components are selected from the group consisting of metals, metal oxides, metal hydroxides, metal salts and mixtures thereof of metals having a valence ranging from 1 to 5.

Claim 21

The process of claim 11 wherein said perovskite of step (d) is an oxide of two or more metals, the sum of the ionic charges of which equals six.

Claim 22

The process of claim 11 wherein additional catalytic active metal components are composited with said supported perovskite catalyst.

Claim 23

A process for the preparation of a supported LaCoO 3 persovkite catalyst which comprises: a. impregnating a gamma alumina gel having a surface area of about 185 m 2 /g with Mg(NO 2 ) 2 ; b. calcining the impregnated alumina alumina gel at a temperature of about 540° C., thereby producing a surface coating of MgAl 2 O 4 spinel on said gamma alumina; c. impregnating the spinel-coated alumina resulting from step (b) with an equimolar solution of La(NO 3 ) 3 .6H 2 O and Co(NO 3 ) 2 .6H 2 0; d. calcining at a temperature of at least 540° C. the impregnated material resulting from step (c) and e. recovering a supported LaCoO 3 catalyst.

Claim 24

A process for the preparation of a supported LaCoO 3 persovkite catalyst which comprises: a. impregnating a gamma alumina gel having a surface area of about 185 m 2 /g with Mg(NO 2 ) 2 ; b. calcining the impregnated alumina alumina gel at a temperature of about 540° C., thereby producing a surface coating of MgAl 2 O 4 spinel on said gamma alumina; c. impregnating the spinel-coated alumina resulting from step (b) with an equimolar solution of La(NO 3 ) 3 .6H 2 O and Co(NO 3 ) 2 .6H 2 0; d. calcining at a temperature of at least 540° C. the impregnated material resulting from step (c) and e. recovering a supported LaCoO 3 catalyst.

Claim 25

The process of claim 20 wherein said supported LaCoO 3 catalyst has a surface area of at least about 65 m 2 /g.

Claim 26

The process of claim 11 wherein said metal oxide resulting from step (a) is calcined at a temperature ranging from about 500° C to about 1000° C. to produce said spinel.