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US4452908A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for the production of catalysts based on crystalline aluminosilicates

Assignee: BP PLC
•
Filing: 1982-07-08
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Granted: 1984-06-05
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Expires: 2002-07-08
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Abstract

Abstract A process for the production of a catalyst based on a crystalline aluminosilicate having a silica to alumina molar ratio greater than 12:1 which is obtained by mixing a source of silica, a source of alumina, a source of alkali metal, water and a source of ammonium ions in defined proportions, crystallizing the mixture, recovering the crystalline aluminosilicate so-formed, cation-exchanging and/or impregnating the recovered crystalline aluminosilicate and finally calcining, wherein either the recovered crystalline aluminosilicate or the cation-exchanged aluminosilicate or the impregnated aluminosilicate is washed with a solution containing either an organic base, a carboxylic acid, an alcohol, a glycol, a phenol or an ester. The washing treatment results in a reduction in the rate of decline in catalytic activity in reactions such as the conversion of aliphatic to aromatic hydrocarbons.

Inventors

  • 👤 William J. Ball
  • 👤 David G. Stewart

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-25 19:48
CPC Classifications
B; B01; B01J; B01J29/00; B01J29/87; B01J29/04; B01J29/06; B01J29/40; C; C07; C07C; C07C2/00; C07C2529/00; C07C2529/04; C07C2529/06

Claims Analysis

Total Claims: 15
Claim 1
Independent Claim 252 words
A process for the production of a catalyst based on a crystalline aluminosilicate having a silica to alumina molar ratio greater than 12:1 which crystalline aluminosilicate is obtained by mixing a source of silica, a source of alumina, a source of alkali metal, water and a source of ammonium ions in the absence of an alcohol or an alkylene oxide in the molar proportions (expressed in the case of the silica and alumina sources in terms of the equivalent moles of the oxide, in the case of the alkali metal source in terms of the equivalent moles of the hydroxide [MOH] and in the case of the source of ammonium ions in terms of free ammonia): SiO 2 :Al 2 O 3 greater than 12:1 MOH:Al 2 O 3 in the range from 1:1 to 20:1 SiO 2 :NH 3 in the range from 1:1 to 200:1, and H 2 O:MOH in the range from 30:1 to 300:1, maintaining the mixture at elevated temperature for a period such that crystallisation occurs, recovering the crystalline aluminosilicate so-formed, cation-exchanging the recovered crystalline aluminosilicate with either gallium or aluminum cations and/or impregnating the recovered crystalline aluminosilicate with a solution of a gallium or aluminum compound and finally calcining the exchanged and/or impregnated crystalline aluminosilicate characterised in that either the recovered crystalline aluminosilicate or the cation-exchanged crystalline aluminosilicate or the metal impregnated crystalline aluminosilicate is washed with a solution containing either an organic base, a carboxylic acid, an alcohol, a glycol, a phenol or an ester.
Claim 2
Dependent Claim 252 words
A process for the production of a catalyst based on a crystalline aluminosilicate having a silica to alumina molar ratio greater than 12:1 which crystalline aluminosilicate is obtained by mixing a source of silica, a source of alumina, a source of alkali metal, water and a source of ammonium ions in the absence of an alcohol or an alkylene oxide in the molar proportions (expressed in the case of the silica and alumina sources in terms of the equivalent moles of the oxide, in the case of the alkali metal source in terms of the equivalent moles of the hydroxide [MOH] and in the case of the source of ammonium ions in terms of free ammonia): SiO 2 :Al 2 O 3 greater than 12:1 MOH:Al 2 O 3 in the range from 1:1 to 20:1 SiO 2 :NH 3 in the range from 1:1 to 200:1, and H 2 O:MOH in the range from 30:1 to 300:1, maintaining the mixture at elevated temperature for a period such that crystallisation occurs, recovering the crystalline aluminosilicate so-formed, cation-exchanging the recovered crystalline aluminosilicate with either gallium or aluminum cations and/or impregnating the recovered crystalline aluminosilicate with a solution of a gallium or aluminum compound and finally calcining the exchanged and/or impregnated crystalline aluminosilicate characterised in that either the recovered crystalline aluminosilicate or the cation-exchanged crystalline aluminosilicate or the metal impregnated crystalline aluminosilicate is washed with a solution containing either an organic base, a carboxylic acid, an alcohol, a glycol, a phenol or an ester.
Claim 3
Dependent Claim 32 words
A process according to claim 1 wherein the source of ammonium is ammonium hydroxide, either added as an aqueous solution or formed "in situ" by passing gaseous ammonia into the aqueous mixture.
Claim 4
Dependent Claim 60 words
A process according to claim 1 wherein the molar composition of the initial mixture is: SiO 2 :Al 2 O 3 in the range from 25:1 to 45:1 MOH:Al 2 O 3 in the range from 3:1 to 7:1 SiO 2 :NH 3 in the range from 25:1 to 40:1 H 2 O:MOH in the range from 40:1 to 60:1
Claim 5
Dependent Claim 32 words
A process according to claim 1, 2 or 3 wherein the washing is effected with a solution of an organic base which is either an amine, an alkanolamine or a tetraalkylammonium compound.
Claim 6
Dependent Claim 35 words
A process according to claim 1, 2 or 3 wherein the washing is effected with a solution of a carboxylic acid which is either formic acid, acetic acid, propionic acid, butyric acid or benzoic acid.
Claim 7
Dependent Claim 29 words
A process according to claim 1, 2 or 3 wherein the washing is effected with a solution of an alcohol which is a C 1 to C 4 alkanol.
Claim 8
Dependent Claim 27 words
A process according to claim 1, 2 or 3 wherein the washing is effected with a solution of a glycol which is ethylene glycol or propylene glycol.
Claim 9
Dependent Claim 24 words
A process according to claim 1, 2 or 3 wherein the washing is effected with a solution of an ester which is methyl acetate.
Claim 10
Dependent Claim 28 words
A process according to claim 1, 2 or 3 wherein the washing is effected with a solution of a phenol which is either phenol or an alkyl phenol.
Claim 11
Dependent Claim 36 words
A process according to claim 1, 2 or 3 wherein the organic base, the carboxylic acid, the alcohol, the glycol, the ester or the phenol comprises from 5 to 15 percent by weight of the solution.
Claim 12
Dependent Claim 34 words
A process according to claim 1, 2 or 3 wherein the organic base, the carboxylic acid, the alcohol, the glycol, the ester or the phenol are employed in the form of an aqueous solution.
Claim 13
Dependent Claim 20 words
A process according to claim 1, 2 or 3 wherein the washing step is effected on the recovered crystalline aluminosilicate.
Claim 14
Dependent Claim 22 words
A process according to claim 1, 2 or 3 wherein the washing step is effected on an aluminum or gallium-exchanged crystalline aluminosilicate.
Claim 15
Dependent Claim 26 words
A process according to claim 1, 2 or 3 wherein the washing step is effected on a crystalline aluminosilicate impregnated with an aluminum or gallium compound.

References Cited (Backward Citations)

US3509042A Cited
US3213013A Cited
US3264208A Cited
US3360484A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1987-06-05 1987-12-05 1988-06-05 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1991-06-05 1991-12-05 1992-06-05 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1995-06-05 1995-12-05 1996-06-05 $7700.00 Window Closed / Lapsed

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