Hydrocarbon-conversion catalyst and its method of preparation

Claim 2

A process for the conversion of a hydrocarbon stream, which process comprises contacting said stream at conversion conditions with a catalytic composition comprising a crystalline borosilicate and a porous refractory inorganic oxide, said borosilicate and said inorganic oxide having been intimately admixed with one another, said borosilicate comprising a molecular sieve material providing an X-ray diffraction pattern comprising the following X-ray diffraction lines and assigned strengths: ______________________________________ d(A) Assigned Strength ______________________________________ 11.2 ± 0.2 W- VS 10.0 ± 0.2 W-MS 5.97 ± 0.07 W-M 3.82 ± 0.05 VS 3.70 ± 0.05 MS 3.62 ± 0.05 M-MS 2.97 ± 0.02 W-M 1.99 ± 0.02 VW-M ______________________________________ and having the following composition in terms of mole ratios of oxides: 0.9±0.2M.sub.2/n O:B.sub.2 O.sub.3 :YSiO.sub.2 :ZH.sub.2 O wherein M is at least one cation having a valence of n, Y is between 4 and about 600, and Z is between 0 and about 160.

Claim 3

A process for the conversion of a hydrocarbon stream, which process comprises contacting said stream at conversion conditions with a catalytic composition comprising at least one catalytically-active metal and a catalytic support comprising a crystalline borosilicate suspended in and distributed throughout a matrix of a refractory inorganic oxide, which composition has been prepared by the method which comprises: (1) admixing said crystalline borosilicate in a finely-divided state with a hydrosol, sol, or hydrogel of said inorganic oxide in order to uniformly disperse said borosilicate in said hydrosol, sol, or hydrogel of said inorganic oxide to form an admixture, said borosilicate comprising a molecular sieve material providing an X-ray diffraction pattern comprising the following X-ray diffraction lines and assigned strengths: ______________________________________ d(A) Assigned Strength ______________________________________ 11.2 ± 0.2 W- VS 10.0 ± 0.2 W-MS 5.97 ± 0.07 W-M 3.82 ± 0.05 VS 3.70 ± 0.05 MS 3.62 ± 0.05 M-MS 2.97 ± 0.02 W-M 1.99 ± 0.02 VW-M ______________________________________ and having the following composition in terms of mole ratios of oxides: 0.9±0.2M.sub.2/n O:B.sub.2 O.sub.3 :YSiO.sub.2 :ZH.sub.2 O wherein M is at least one cation, n is the valence of the cation, Y is a value within the range of 4 to about 600, and Z is a value within the range of 0 to about 160; (2) while continually stirring the admixture, adding a gelling medium to promote gellation and to form a gel; (3) drying said gel at a temperature of about 77° F. (25° C.) to about 392° F. (200° C.) for a period of about 10 minutes to about 100 hours in the presence of air to form a dried mixture; (4) calcining said dried mixture by heating said dried mixture in air at a maximum rate of 200° F. per hour (111° C. per hour) to a calcination temperature within the range of about 752° F. (400° C.) to about 1,112° F. (600° C.) and maintaining said dried material at said calcination temperature for a period of about 30 minutes to about 20 hours to provide a calcined catalytic support material; (5) impregnating said calcined catalytic support material with a solution of a heat-decomposable compound of said catalytically-active metal to provide an impregnated material; (6) drying said impregnated material at a temperature of about 77° F. (25° C.) to about 392° F. (200° C.) for a period of about 10 minutes to about 100 hours in air to obtain a dried impregnated material; and (7) calcining said dried impregnated material by heating said dried impregnated material in air at a maximum rate of 200° F. per hour (111° C. per hour) to a calcination temperature within the range of about 752° F. (400° C.) to about 1,112° F. (600° C.) and maintaining said dried impregnated material at said calcination temperature for a period of about 30 minutes to about 20 hours to provide said catalytic composition.

Claim 4

A process for the conversion of a hydrocarbon stream, which process comprises contacting said stream at conversion conditions with a catalytic composition comprising at least one catalytically-active metal and a catalytic support comprising a crystalline borosilicate suspended in and distributed throughout a matrix of a refractory inorganic oxide, which composition has been prepared by the method which comprises: (1) admixing said crystalline borosilicate in a finely-divided state with a hydrosol, sol, or hydrogel of said inorganic oxide in order to uniformly disperse said borosilicate in said hydrosol, sol, or hydrogel of said inorganic oxide to form an admixture, said borosilicate comprising a molecular sieve material providing an X-ray diffraction pattern comprising the following X-ray diffraction lines and assigned strengths: ______________________________________ d(A) Assigned Strength ______________________________________ 11.2 ± 0.2 W- VS 10.0 ± 0.2 W-MS 5.97 ± 0.07 W-M 3.82 ± 0.05 VS 3.70 ± 0.05 MS 3.62 ± 0.05 M-MS 2.97 ± 0.02 W-M 1.99 ± 0.02 VW-M ______________________________________ and having the following composition in terms of mole ratios of oxides: 0.9±0.2M.sub.2/n O:B.sub.2 O.sub.3 :YSiO.sub.2 :ZH.sub.2 O wherein M is at least one cation, n is the valence of the cation, Y is a value within the range of 4 to about 600, and Z is a value within the range of 0 to about 160; (2) while continually stirring the admixture, adding a gelling medium to promote gellation and to form a gel; (3) drying said gel at a temperature of about 77° F. (25° C.) to about 392° F. (200° C.) for a period of about 10 minutes to about 100 hours in the presence of air to form a dried mixture; (4) calcining said dried mixture by heating said dried mixture in air at a maximum rate of 200° F. per hour (111° C. per hour) to a calcination temperature within the range of about 752° F. (400° C.) to about 1,112° F. (600° C.) and maintaining said dried material at said calcination temperature for a period of about 30 minutes to about 20 hours to provide a calcined catalytic support material; (5) impregnating said calcined catalytic support material with a solution of a heat-decomposable compound of said catalytically-active metal to provide an impregnated material; (6) drying said impregnated material at a temperature of about 77° F. (25° C.) to about 392° F. (200° C.) for a period of about 10 minutes to about 100 hours in air to obtain a dried impregnated material; and (7) calcining said dried impregnated material by heating said dried impregnated material in air at a maximum rate of 200° F. per hour (111° C. per hour) to a calcination temperature within the range of about 752° F. (400° C.) to about 1,112° F. (600° C.) and maintaining said dried impregnated material at said calcination temperature for a period of about 30 minutes to about 20 hours to provide said catalytic composition.

Claim 5

A process for the catalytic isomerization of a xylene feed, which process comprises contacting said feed at isomerization conditions with a catalytic composition comprising a crystalline borosilicate and a porous refractory inorganic oxide, said borosilicate and said inorganic oxide having been intimately admixed with one another, said borosilicate comprising a molecular sieve material providing an X-ray diffraction pattern comprising the following X-ray diffraction lines and assigned strengths: ______________________________________ d(A) Assigned Strength ______________________________________ 11.2 ± 0.2 W- VS 10.0 ± 0.2 W-MS 5.97 ± 0.07 W-M 3.82 ± 0.05 VS 3.70 ± 0.05 MS 3.62 ± 0.05 M-MS 2.97 ± 0.02 W-M 1.99 ± 0.02 VW-M ______________________________________ and having the following composition in terms of mole ratios of oxides: 0.9±0.2M.sub.2/n O:B.sub.2 O.sub.3 :YSiO.sub.2 :ZH.sub.2 O wherein M is at least one cation having a valence of n, Y is between 4 and about 600, and Z is between 0 and about 160.

Claim 6

A process for the catalytic isomerization of a xylene feed, which process comprises contacting said feed at isomerization conditions with a catalytic composition comprising a crystalline borosilicate and a porous refractory inorganic oxide, said borosilicate and said inorganic oxide having been intimately admixed with one another, said borosilicate comprising a molecular sieve material providing an X-ray diffraction pattern comprising the following X-ray diffraction lines and assigned strengths: ______________________________________ d(A) Assigned Strength ______________________________________ 11.2 ± 0.2 W- VS 10.0 ± 0.2 W-MS 5.97 ± 0.07 W-M 3.82 ± 0.05 VS 3.70 ± 0.05 MS 3.62 ± 0.05 M-MS 2.97 ± 0.02 W-M 1.99 ± 0.02 VW-M ______________________________________ and having the following composition in terms of mole ratios of oxides: 0.9±0.2M.sub.2/n O:B.sub.2 O.sub.3 :YSiO.sub.2 :ZH.sub.2 O wherein M is at least one cation having a valence of n, Y is between 4 and about 600, and Z is between 0 and about 160.

Claim 7

The process of claim 3, wherein said isomerization conditions comprise a temperature of about 200° F. (93° C.) to about 1,000° F. (538° C.), a hydrogen-to-hydrocarbon mole ratio of about 0 to about 20, a weight hourly space velocity (WHSV) of about 0.01 weight unit of feed per hour per weight unit of catalyst (hr -1 ) to about 90 hr -1 , and a pressure of about 0 psig (101 KPa) to about 1,000 psig (6,998 KPa).

Claim 8

A process for the catalytic isomerization of a xylene feed, which process comprises contacting said feed at isomerization conditions with a catalytic composition comprising at least one catalytically-active metal and a catalytic support comprising a crystalline borosilicate suspended in and distributed throughout a matrix of a refractory inorganic oxide, which composition has been prepared by the method which comprises: (1) admixing said crystalline borosilicate in a finely-divided state with a hydrosol, sol, or hydrogel of said inorganic oxide in order to uniformly disperse said borosilicate in said hydrosol, sol, or hydrogel of said inorganic oxide to form an admixture, said borosilicate comprising a molecular sieve material providing an X-ray diffraction pattern comprising the following X-ray diffraction lines and assigned strengths: ______________________________________ d(A) Assigned Strength ______________________________________ 11.2 ± 0.2 W- VS 10.0 ± 0.2 W-MS 5.97 ± 0.07 W-M 3.82 ± 0.05 VS 3.70 ± 0.05 MS 3.62 ± 0.05 M-MS 2.97 ± 0.02 W-M 1.99 ± 0.02 VW-M ______________________________________ and having the following composition in terms of mole ratios of oxides: 0.9±0.2M.sub.2/n O:B.sub.2 O.sub.3 :YSiO.sub.2 :ZH.sub.2 O wherein M is at least one cation, n is the valence of the cation, Y is a value within the range of 4 to about 600, and Z is a value within the range of 0 to about 160; (2) while continually stirring the admixture, adding a gelling medium to promote gellation and to form a gel; (3) drying said gel at a temperature of about 77° F. (25° C.) to about 392° F. (200° C.) for a period of about 10 minutes to about 100 hours in the presence of air to form a dried mixture; (4) calcining said dried mixture by heating said dried mixture in air at a maximum rate of 200° F. per hour (111° C. per hour) to a calcination temperature within the range of about 752° F. (400° C.) to about 1,112° F. (600° C.) and maintaining said dried material at said calcination temperature for a period of about 30 minutes to about 20 hours to provide a calcined catalytic support material; (5) impregnating said calcined catalytic support material with a solution of a heat-decomposable compound of said catalytically-active metal to provide an impregnated material; (6) drying said impregnated material at a temperature of about 77° F. (25° C.) to about 392° F. (200° C.) for a period of about 10 minutes to about 100 hours in air to obtain a dried impregnated material; and (7) calcining said dried impregnated material by heating said dried impregnated material in air at a maximum rate of 200° F. per hour (111° C. per hour) to a calcination temperature within the range of about 752° F. (400° C.) to about 1,112° F. (600° C.) and maintaining said dried impregnated material at said calcination temperature for a period of about 30 minutes to about 20 hours to provide said catalytic composition.

Claim 9

A process for the catalytic isomerization of a xylene feed, which process comprises contacting said feed at isomerization conditions with a catalytic composition comprising at least one catalytically-active metal and a catalytic support comprising a crystalline borosilicate suspended in and distributed throughout a matrix of a refractory inorganic oxide, which composition has been prepared by the method which comprises: (1) admixing said crystalline borosilicate in a finely-divided state with a hydrosol, sol, or hydrogel of said inorganic oxide in order to uniformly disperse said borosilicate in said hydrosol, sol, or hydrogel of said inorganic oxide to form an admixture, said borosilicate comprising a molecular sieve material providing an X-ray diffraction pattern comprising the following X-ray diffraction lines and assigned strengths: ______________________________________ d(A) Assigned Strength ______________________________________ 11.2 ± 0.2 W- VS 10.0 ± 0.2 W-MS 5.97 ± 0.07 W-M 3.82 ± 0.05 VS 3.70 ± 0.05 MS 3.62 ± 0.05 M-MS 2.97 ± 0.02 W-M 1.99 ± 0.02 VW-M ______________________________________ and having the following composition in terms of mole ratios of oxides: 0.9±0.2M.sub.2/n O:B.sub.2 O.sub.3 :YSiO.sub.2 :ZH.sub.2 O wherein M is at least one cation, n is the valence of the cation, Y is a value within the range of 4 to about 600, and Z is a value within the range of 0 to about 160; (2) while continually stirring the admixture, adding a gelling medium to promote gellation and to form a gel; (3) drying said gel at a temperature of about 77° F. (25° C.) to about 392° F. (200° C.) for a period of about 10 minutes to about 100 hours in the presence of air to form a dried mixture; (4) calcining said dried mixture by heating said dried mixture in air at a maximum rate of 200° F. per hour (111° C. per hour) to a calcination temperature within the range of about 752° F. (400° C.) to about 1,112° F. (600° C.) and maintaining said dried material at said calcination temperature for a period of about 30 minutes to about 20 hours to provide a calcined catalytic support material; (5) impregnating said calcined catalytic support material with a solution of a heat-decomposable compound of said catalytically-active metal to provide an impregnated material; (6) drying said impregnated material at a temperature of about 77° F. (25° C.) to about 392° F. (200° C.) for a period of about 10 minutes to about 100 hours in air to obtain a dried impregnated material; and (7) calcining said dried impregnated material by heating said dried impregnated material in air at a maximum rate of 200° F. per hour (111° C. per hour) to a calcination temperature within the range of about 752° F. (400° C.) to about 1,112° F. (600° C.) and maintaining said dried impregnated material at said calcination temperature for a period of about 30 minutes to about 20 hours to provide said catalytic composition.

Claim 10

The process of claim 5, wherein said isomerization conditions comprise a temperature of about 200° F. (93° C.) to about 1,000° F. (538° C.), a hydrogen-to-hydrocarbon mole ratio of about 0 to about 20, a weight hourly space velocity (WHSV) of about 0.01 weight unit of feed per hour per weight unit of catalyst (hr -1 ) to about 90 hr -1 , and a pressure of about 0 psig (101 KPa) to about 1,000 psig (6,998 KPa).

Claim 11

The process of claim 1, wherein at least one catalytically-active metal has been cation-exchanged onto said borosilicate.

Claim 12

The process of claim 7, wherein said at least one catalytically-active metal is nickel.

Claim 13

The process of claim 2, wherein at least one catalytically-active metal has been cation-exchanged onto said borosilicate.

Claim 14

The process of claim 2, wherein the impregnated catalytically-active metal is molybdenum, tungsten, cobalt, or nickel.

Claim 15

The process of claim 9, wherein the impregnated catalytically-active metal is molybdenum, tungsten, cobalt, or nickel.

Claim 16

The process of claim 4, wherein at least one catalytically-active metal has been cation-exchanged onto said borosilicate.

Claim 17

The process of claim 12, wherein said at least one catalytically-active metal is nickel.

Claim 18

The process of claim 5, wherein at least one catalytically-active metal has been cation-exchanged onto said borosilicate.

Claim 19

The process of claim 5, wherein the impregnated catalytically-active metal is molybdenum, tungsten, cobalt, or nickel.

Claim 20

The process of claim 6, wherein at least one catalytically-active metal has been cation-exchanged onto said borosilicate.

Claim 21

The process of claim 6, wherein the impregnated catalytically-active metal is molybdenum, tungsten, cobalt, or nickel.

Claim 22

The process of claim 14, wherein the impregnated catalytically-active metal is molybdenum, tungsten, cobalt, or nickel.

Claim 23

The process of claim 15, wherein the impregnated catalytically-active metal is molybdenum.

Claim 24

The process of claim 16, wherein the impregnated catalytically-active metal is molybdenum, tungsten, cobalt, or nickel.

Claim 25

The process of claim 17, wherein the impregnated catalytically-active metal is molybdenum.

Claim 26

The process of claim 18, wherein the cation-exchanged metal is nickel.

Claim 27

The process of claim 20, wherein the cation-exchanged metal is nickel.