US4448673A
Expired / Lapsed
US
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Aging resistance shape selective catalyst with enhanced activity
Assignee: Mobil Oil AS
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Filing: 1982-09-28
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Granted: 1984-05-15
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Expires: 2002-09-28
Abstract
Abstract A shape selective catalyst useful in a variety of hydrocarbon conversion processes such as cracking, hydrocracking, hydrofining, isomerization, dewaxing, and the like, is obtained from the process which comprises steaming a precursor crystalline aluminosilicate in the hydrogen or ammonium form having a silica-alumina ratio greater than 12, a constraint index between about 1 and about 12 and an alpha value greater than about 20 in the presence of ammonia to provide a crystalline aluminosilicate having an alpha value of from about 10 to about 150 and thereafter ion-exchanging the steamed precursor with an alkali metal cation under conditions effective to further reduce the alpha value of the crystalline aluminosilicate to less than about 10.
Inventors
- 👤 David S. Shihabi
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-03 21:56
CPC Classifications
B; B01; B01J; B01J37/00; B01J37/08; B01J37/10; B01J29/00; B01J29/04; B01J29/06; B01J29/40; B01J2229/00; B01J2229/30; B01J2229/36
Claims Analysis
Total Claims: 5
Claim 1
Independent Claim
118 words
In a process for the catalytic dewaxing of a hydrocarbon fraction under catalytic dewaxing conditions wherein the improvement comprises employing as catalyst for said dewaxing a composition obtained from the process which comprises steaming a precursor crystalline aluminosilicate in the hydrogen or ammonium form having a silica-alumina ratio greater than 12, a constraint index between about 1 and about 12 and an alpha value greater than about 20 in the presence of ammonia to provide a crystalline aluminosilicate having an alpha value of from about 10 to about 150 and thereafter ion-exchanging the steamed precursor with an alkali metal cation under conditions effective to further reduce the alpha value of the crystalline aluminosilicate to less than about 10.
Claim 2
Dependent Claim
118 words
In a process for the catalytic dewaxing of a hydrocarbon fraction under catalytic dewaxing conditions wherein the improvement comprises employing as catalyst for said dewaxing a composition obtained from the process which comprises steaming a precursor crystalline aluminosilicate in the hydrogen or ammonium form having a silica-alumina ratio greater than 12, a constraint index between about 1 and about 12 and an alpha value greater than about 20 in the presence of ammonia to provide a crystalline aluminosilicate having an alpha value of from about 10 to about 150 and thereafter ion-exchanging the steamed precursor with an alkali metal cation under conditions effective to further reduce the alpha value of the crystalline aluminosilicate to less than about 10.
Claim 3
Dependent Claim
128 words
In a process for the catalytic hydrocracking of a hydrocarbon oil under catalytic hydrocracking conditions wherein the improvement comprises employing as catalyst for said hydrocracking a composition obtained from the process which comprises steaming a precursor crystalline aluminosilicate in the hydrogen or ammonium form having a silica-alumina ratio greater than 12, a constraint index between about 1 and about 12 and an alpha value greater than about 20 in the presence of ammonia to provide a crystalline aluminosilicate having an alpha value of from about 10 to about 150 and thereafter ion-exchanging the steamed precursor with an alkali metal cation under conditions effective to further reduce the alpha value of the crystalline aluminosilicate to less than about 10, said composition being present in association with a hydrogenation component.
Claim 4
Dependent Claim
128 words
In a process for the catalytic hydrocracking of a hydrocarbon oil under catalytic hydrocracking conditions wherein the improvement comprises employing as catalyst for said hydrocracking a composition obtained from the process which comprises steaming a precursor crystalline aluminosilicate in the hydrogen or ammonium form having a silica-alumina ratio greater than 12, a constraint index between about 1 and about 12 and an alpha value greater than about 20 in the presence of ammonia to provide a crystalline aluminosilicate having an alpha value of from about 10 to about 150 and thereafter ion-exchanging the steamed precursor with an alkali metal cation under conditions effective to further reduce the alpha value of the crystalline aluminosilicate to less than about 10, said composition being present in association with a hydrogenation component.
Claim 5
Dependent Claim
22 words
The process claimed in claim 2, wherein said hydrogenation component consists of metals of group VI and VIII of the Periodic Table.
References Cited (Backward Citations)
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US4263129A
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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) | 1987-05-15 | 1987-11-14 | 1988-05-15 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1991-05-15 | 1991-11-14 | 1992-05-15 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1995-05-15 | 1995-11-14 | 1996-05-15 | $7700.00 | Window Closed / Lapsed |