Patent US4665251A successfully refreshed from Google Patents.
US4665251A
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Aromatization reactions with zeolites containing phosphorus oxide
Assignee: Mobil Oil AS
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Filing: 1985-12-18
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Granted: 1987-05-12
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Expires: 2005-12-18
Abstract
Abstract There is provided a process for producing aromatic hydrocarbons. The process involves contacting one or more non-aromatic compounds, such as propane, propylene, or methanol, with a catalyst containing a zeolite, such as ZSM-5. The zeolite is modified with phosphorus oxide by impregnating the zeolite with a source of phosphate ions, such as an aqueous solution of an ammonium phosphate, followed by calcination.
Inventors
- 👤 Chin-Chiun Chu
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-05 23:40
CPC Classifications
C; C07; C07C; C07C1/00; C07C1/20; B; B01; B01J; B01J29/00; B01J29/04; B01J29/06; B01J29/40; C07C2/00; B01J2229/00; B01J2229/10; B01J2229/26; B01J2229/30; B01J2229/42; C07C2529/00; C07C2529/04; C07C2529/06; C07C2529/40; C07C2529/65; C07C2529/70
Claims Analysis
Total Claims: 11
Claim 1
Independent Claim
168 words
A process for producing aromatic hydrocarbons, said process comprising contacting a feedstock comprising one or more non-aromatic compounds selected from the group consisting of C 2 -C 12 alkanes and C 2 -C 12 alkenes with a catalyst comprising a crystalline zeolite material having the structure of ZSM-5 or ZSM-11, said contacting taking place under aromatization conditions including a temperature of from about 200° C. to about 700° C., a pressure of from about 0.1 atmosphere to about 60 atmospheres, a weight hourly space velocity (WHSV) of from about 0.1 to about 400 and a hydrogen/hydrocarbon mole ratio of from about 0 to about 20, said catalyst further comprising an oxide of phosphorus which has been incorporated into said catalyst by a process comprising the steps of: (i) impregnating said zeolite with a source of phosphate ions; and (ii) calcining the impregnated zeolite of step (i) at a temperature of at least 649° C. under conditions sufficient to convert said impregnated phosphate ions to said oxide of phosphorus.
Claim 2
Dependent Claim
168 words
A process for producing aromatic hydrocarbons, said process comprising contacting a feedstock comprising one or more non-aromatic compounds selected from the group consisting of C 2 -C 12 alkanes and C 2 -C 12 alkenes with a catalyst comprising a crystalline zeolite material having the structure of ZSM-5 or ZSM-11, said contacting taking place under aromatization conditions including a temperature of from about 200° C. to about 700° C., a pressure of from about 0.1 atmosphere to about 60 atmospheres, a weight hourly space velocity (WHSV) of from about 0.1 to about 400 and a hydrogen/hydrocarbon mole ratio of from about 0 to about 20, said catalyst further comprising an oxide of phosphorus which has been incorporated into said catalyst by a process comprising the steps of: (i) impregnating said zeolite with a source of phosphate ions; and (ii) calcining the impregnated zeolite of step (i) at a temperature of at least 649° C. under conditions sufficient to convert said impregnated phosphate ions to said oxide of phosphorus.
Claim 3
Dependent Claim
18 words
According to claim 1, wherein said source of phosphate ions is an aqueous solution of an ammonium phosphate.
Claim 4
Dependent Claim
31 words
A process according to claim 2, wherein said ammonium phosphate is selected from the group consisting of (NH 4 ) 2 HPO 4 and NH 4 H 2 PO 4 .
Claim 5
Dependent Claim
35 words
A process according to claim 3, wherein essentially all of the cationic exchange sites of said zeolites are occupied by ammonium ions prior to and during the impregnation of said zeolite with said ammonium phosphate.
Claim 6
Dependent Claim
23 words
A process according to claim 1, wherein said zeolite material is an aluminosilicate zeolite having a silica/alumina mole ratio of at least 12.
Claim 7
Dependent Claim
15 words
A process according to claim 2, wherein said zeolitc material has the structure of ZSM-5.
Claim 8
Dependent Claim
13 words
A process according to claim 1 wherein said catalyst further comprises a binder.
Claim 9
Dependent Claim
41 words
A process according to claim 1, wherein said feedstock comprises from about 1 to about 30 weight percent of ethylehe, from about 1 to about 30 weight percent of propylene and from about 1 to about 30 weight percent of propane.
Claim 10
Dependent Claim
14 words
A process according to claim 1, wherein said feedstock comprises a refinery off gas.
Claim 11
Dependent Claim
14 words
A process according to claim 1, wherein said feedstock comprises ethylene, propane or propylene.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1990-05-11 | 1990-11-10 | 1991-05-12 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1994-05-11 | 1994-11-10 | 1995-05-12 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1998-05-11 | 1998-11-10 | 1999-05-12 | $7700.00 | Window Closed / Lapsed |