Catalyst and a process for their preparation

Claim 2

Catalyst comprising in combination (1) a carrier formed of an intimate mixture of aluminum oxide and nickel oxide, said carrier having been obtained by co-precipitating a gel from a solution of an organic salt of aluminum and an aqueous solution containing nickel, said co-precipitation being followed by drying and by calcination of said gel, and (2) an active phase on said carrier comprising at least one metal selected from groups VIII and VIB of the Periodic Table of the elements.

Claim 3

Catalyst according to claim 1, wherein the content of said oxide of nickel in the carrier is from 0.1 to 20% by weight of the alumina.

Claim 4

Catalyst in accordance with claim 1, wherein the percentage of the active phase metals from groups VIII and VIB is comprised between 1 and 20%, calculated as an element of the total mass of the catalyst.

Claim 5

Catalyst according to claim 3, wherein said active phase metals from groups VIII and VIB are in the catalyst in the form of oxides.

Claim 6

Catalyst according to claim 3, wherein the active phase metals present on the carrier are cobalt and molybdenum.

Claim 7

Catalyst according to claim 4, wherein the active phase metals present on the carrier are cobalt and molybdenum.

Claim 8

Catalyst according to claim 6, wherein the weight percent, based on the oxide form and on the total weight of the catalyst, of the cobalt and of the molybdenum are between 1 and 5% and between 10 and 20% respectively.

Claim 9

Catalyst according to claim 6, wherein the weight percent, based on the oxide form and on the total weight of the catalyst, of the cobalt and of the molybdenum are between 2 and 4%, and between 12 and 18%, respectively.

Claim 10

Process of preparation of a catalyst according to claim 3 comprising said carrier being impregnated with said active phase from a solution containing salts of the metal comprising said active phase, drying the carrier so impregnated at between 70° and 140° C, and calcining the dried product at between 400° and 700° C.

Claim 11

Catalyst for desulfurization of a hydrocarbon charge consisting essentially of a carrier formed of an intimate mixture of aluminum oxide and cobalt oxide and obtained by coprecipitating a gel from a solution of an organic salt of aluminum and an aqueous solution of a cobalt salt with said gel being dried and calcined, said cobalt being present as an oxide in an amount of from 0.1 to 20% by weight of the alumina, and deposited on said carrier an active phase comprising between 1 and 20% of at least one metal selected from groups VIII and VIB of the Periodic Table.

Claim 12

Catalyst for desulfurization of a hydrocarbon charge consisting essentially of a carrier formed of an intimate mixture of aluminum oxide and cobalt oxide and obtained by coprecipitating a gel from a solution of an organic salt of aluminum and an aqueous solution of a cobalt salt with said gel being dried and calcined, said cobalt being present as an oxide in an amount of from 0.1 to 20% by weight of the alumina, and deposited on said carrier an active phase comprising between 1 and 20% of at least one metal selected from groups VIII and VIB of the Periodic Table.

Claim 13

Catalyst according to claim 10, wherein said active phase comprises the oxides of Co and Mo and the weight percent, based on the oxide form and on the total weight of the catalyst, of the cobalt and of the molybdenum are between 1 and 5% and between 10 and 20% respectively.

Claim 14

Process of preparation of a catalyst according to claim 10 comprising said carrier being impregnated with said active phase from a solution containing salts of the metal comprising said active phase, drying the carrier so impregnated at between 70° and 140° C, and calcining the dried product at between 400° and 700° C.

Claim 15

Process of preparation of a catalyst according to claim 3, comprising said carrier being impregnated with said active phase from a solution containing salts of the metal comprising said active phase, drying the carrier so impregnated at between 70° and 140° C.

Claim 16

Process according to claim 13, wherein the impregnated carrier is calcined between 400° and 600° C.

Claim 17

Process of preparation of a catalyst according to claim 14, wherein said carrier has been obtained by: (a) hydrolysis of a solution of an organic aluminum salt in an organic solvent by mixture with an aqueous solution of at least one water-soluble salt of nickel, producing a gel; (b) drying of the gel obtained at between 70° and 140° C; (c) steeping of the gel in a second organic solvent, and kneading of the paste obtained; (d) peptization with an acid solution, the amount of acid to be used being comprised between 0.5 and 10% by weight of the dry gel; (e) elimination of the second organic solvent; (f) forming of the paste obtained under (e) by extrusion or granulation; and (g) drying at between 70° and 140° C, followed by the calcination at between 400° and 700° C.

Claim 18

Process according to claim 15, wherein there is a calcination in (b) between 400° and 700° C.

Claim 19

Catalyst comprising in combination: (1) a carrier formed of an intimate mixture of aluminum oxide and at least one oxide of a second metal selected from the group consisting of nickel, tungsten, molybdenum and cobalt, said carrier having been obtained by a process comprising the following principal steps: (a) hydrolysis of a solution of an organic aluminum salt in a first organic solvent by mixture with an aqueous solution of at least one water-soluble salt of said second metal, producing a coprecipitated gel; (b) drying of the gel obtained between 70° and 140° C; (c) steeping and then kneading the gel in a second organic solvent; (d) peptizing with an acid solution, the amount of acid to be used being between 0.5 and 10% by weight of the dry gel; (e) eliminating said second organic solvent; (f) mechanical forming by extrusion or granulation of the paste so obtained; (g) drying at between 70° and 140° C; and (h) calcining at between 400° and 700° C.

Claim 20

Catalyst comprising in combination: (1) a carrier formed of an intimate mixture of aluminum oxide and at least one oxide of a second metal selected from the group consisting of nickel, tungsten, molybdenum and cobalt, said carrier having been obtained by a process comprising the following principal steps: (a) hydrolysis of a solution of an organic aluminum salt in a first organic solvent by mixture with an aqueous solution of at least one water-soluble salt of said second metal, producing a coprecipitated gel; (b) drying of the gel obtained between 70° and 140° C; (c) steeping and then kneading the gel in a second organic solvent; (d) peptizing with an acid solution, the amount of acid to be used being between 0.5 and 10% by weight of the dry gel; (e) eliminating said second organic solvent; (f) mechanical forming by extrusion or granulation of the paste so obtained; (g) drying at between 70° and 140° C; and (h) calcining at between 400° and 700° C.

Claim 21

Catalyst according to claim 17, wherein said second metal oxide is present in said intimate mixture in an amount from about 0.1 to 20% by weight of the aluminum oxide.

Claim 22

Catalyst according to claim 18, wherein said second metal is nickel.

Claim 23

Catalyst according to claim 18, wherein said active phase metals from groups VIII and VIB are in the catalyst in the form of oxides.

Claim 24

Catalyst according to claim 20, wherein said active phase metals present on the carrier are cobalt and molybdenum.

Claim 25

Catalyst according to claim 21, wherein the weight percent, based on the oxide form and on the total weight of the catalyst, of the cobalt and of the molybdenum are between 1 and 5% and between 10 and 20%, respectively.

Claim 26

Catalyst according to claim 22, wherein said percentages are between 2 and 4%, and 12 and 18%, respectively.

Claim 27

Catalyst according to claim 22, wherein said second metal is nickel.

Claim 28

Catalyst according to claim 18, wherein between steps (b) and (c) said gel is calcined between 400° and 700° C.

Claim 29

Catalyst according to claim 18, wherein between steps (c) and (d) said gel is moistened with water in a proportion which may be as high as 70 wt. % based on the dry gel.

Claim 30

Catalyst according to claim 25, wherein between steps (c) and (d) said gel is moistened with water in a proportion which may be as high as 70 wt. %, based on the dry gel.

Claim 31

Process of preparation of a catalyst according to claim 18, comprising said carrier being impregnated with said active phase from a solution containing salts of the metal comprising said active phase, drying the carrier so impregnated at between 70° and 140° C, and calcining the dried product at between 400° and 600° C.

Claim 32

Catalyst for desulfurization of a hydrocarbon charge consisting essentially of a carrier formed of an intimate mixture of aluminum oxide and tungsten oxide and obtained by coprecipitating a gel from a solution of an organic salt of aluminum and an aqueous solution of a tungsten salt with said gel being dried and calcined, said tungsten being present as an oxide in an amount of from 0.1 to 20% by weight of the alumina, and deposited on said carrier an active phase comprising between 1 and 20% of at least one metal selected from groups VIII and VIB of the Periodic Table.

Claim 33

Catalyst for desulfurization of a hydrocarbon charge consisting essentially of a carrier formed of an intimate mixture of aluminum oxide and tungsten oxide and obtained by coprecipitating a gel from a solution of an organic salt of aluminum and an aqueous solution of a tungsten salt with said gel being dried and calcined, said tungsten being present as an oxide in an amount of from 0.1 to 20% by weight of the alumina, and deposited on said carrier an active phase comprising between 1 and 20% of at least one metal selected from groups VIII and VIB of the Periodic Table.

Claim 34

Catalyst according to claim 29, wherein said active phase comprises the oxides of Co and Mo and the weight percent, based on the oxide form and on the total weight of the catalyst, of the cobalt and of the molybdenum are between 1 and 5% and between 10 and 20% respectively.

Claim 35

Process of preparation of a catalyst according to claim 29, comprising said carrier being impregnated with said active phase from a solution, containing salts of the metal comprising said active phase, drying the carrier so impregnated at between 70° and 140° C.

Claim 36

Process of preparation of a catalyst according to claim 31, wherein said carrier has been obtained by: (a) hydrolysis of a solution of an organic aluminum salt in an organic solvent by mixture with an aqueous solution of at least one water-soluble salt of tungsten, producing a gel; (b) drying of the gel obtained at between 70° and 140° C; (c) steeping of the gel in a second organic solvent, and kneading of the paste obtained. (d) peptization with an acid solution, the amount of acid to be used being comprised between 0.5 and 10% by weight of the dry gel; (e) elimination of the second organic solvent; (f) forming of the paste obtained under (e) by extrusion or granulation; and (g) drying at between 70° and 140° C, followed by the calcination at between 400° and 700° C.

Claim 37

Process of preparation of a catalyst according to claim 12, wherein said carrier has been obtained by: (a) hydrolysis of a solution of an organic aluminum salt in an organic solvent by mixture with an aqueous solution of at least one water-soluble salt of cobalt, producing a gel; (b) drying of the gel obtained at between 70° and 140° C; (c) steeping of the gel in a second organic solvent, and kneading of the paste obtained; (d) peptization with an acid solution, the amount of acid to be used being comprised between 0.5 and 10% by weight of the dry gel; (e) elimination of the second organic solvent; (f) forming of the paste obtained under (e) by extrusion or granulation; and (g) drying at between 70° and 140° C, followed by the calcination at between 400° and 700° C.