US4677239A
Expired / Lapsed
US
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Toluene disproportionation with a surface dealuminated zeolite
Assignee: Imperial Chemical Industries Ltd
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Filing: 1985-02-19
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Granted: 1987-06-30
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Expires: 2005-02-19
Abstract
Abstract Selective and controlled dealumination of an aluminosilicate zeolite is achieved by filling the pore system of the zeolite with a foreign material, for example coke, removing part of the foreign material from the outer portion of the zeolite, for example by heating in a gas stream comprising oxygen, dealuminating the outer portion, and then removing the remainder of the foreign material. Use of such a partially dealuminated zeolite as catalyst in a toluene disproportionation reaction leads to greater selectivity to paraxylene.
Inventors
- 👤 John Dewing
- 👤 Philip J. Hogan
- 👤 Allan Stewart
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-29 19:46
CPC Classifications
C; C07; C07C; C07C6/00; C07C6/08; C07C6/12; C07C6/123; C01; C01B; C01B39/00; C01B39/02; C01B39/026; B; B01; B01J; B01J2229/00; B01J2229/10; B01J2229/16; C07C2529/00; C07C2529/04; C07C2529/06; Y; Y10; Y10S; Y10S423/00; Y10S423/22
Claims Analysis
Total Claims: 4
Claim 1
Independent Claim
198 words
A process for the disproportionation of toluene to benzene and xylene which comprises reacting toluene under disproportionation conditions using a catalyst which comprises a zeolite prepared by the process of controlled removal of aluminum from a crystalline aluminosilicate zeolite material which comprises: (a) subjecting the zeolite material to a treatment whereby the pore system of the zeolite material is filled substantially completely with a foreign material; (b) selectively removing a portion of said foreign material from an outer zone of the zeolite crystal structure; (c) contacting the zeolite from step (b) with a dealuminating agent to which the said foreign material is substantially inert under the process conditions for a sufficient time and under suitable process conditions as to remove at least some of the aluminum from the zeolite; and (d) subjecting the thus partially de-aluminated zeolite to further treatment whereby to remove substantially the remainder of said foreign material, said de-aluminated zeolite being further characterized as comprising an inner core having silica to alumina mole ratio substantially characteristic of the untreated zeolite and an outer skin which has been at least partially dealuminated and which has a higher silica to alumina mole ratio than said inner core.
Claim 2
Dependent Claim
198 words
A process for the disproportionation of toluene to benzene and xylene which comprises reacting toluene under disproportionation conditions using a catalyst which comprises a zeolite prepared by the process of controlled removal of aluminum from a crystalline aluminosilicate zeolite material which comprises: (a) subjecting the zeolite material to a treatment whereby the pore system of the zeolite material is filled substantially completely with a foreign material; (b) selectively removing a portion of said foreign material from an outer zone of the zeolite crystal structure; (c) contacting the zeolite from step (b) with a dealuminating agent to which the said foreign material is substantially inert under the process conditions for a sufficient time and under suitable process conditions as to remove at least some of the aluminum from the zeolite; and (d) subjecting the thus partially de-aluminated zeolite to further treatment whereby to remove substantially the remainder of said foreign material, said de-aluminated zeolite being further characterized as comprising an inner core having silica to alumina mole ratio substantially characteristic of the untreated zeolite and an outer skin which has been at least partially dealuminated and which has a higher silica to alumina mole ratio than said inner core.
Claim 3
Dependent Claim
42 words
A process according to claim 1 wherein the zeolite is from a crystalline aluminosilicate zeolite selected from the group consisting of mordenites, ferrierites, FU-1, FU-9, Nu-1, Nu-2, Nu-3, Nu-4, Nu-5, Nu-6, Nu-10, EU-1, EU-2, EU-4, ZSM-5, 11, 12, 35, 38 and 48.
Claim 4
Dependent Claim
12 words
A process according to claim 1 wherein the aluminosilicate zeolite is ZSM-5.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1990-06-29 | 1990-12-29 | 1991-06-30 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1994-06-29 | 1994-12-29 | 1995-06-30 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1998-06-29 | 1998-12-29 | 1999-06-30 | $7700.00 | Window Closed / Lapsed |