US4483764A
Expired / Lapsed
US
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Hydrocarbon conversion process
Assignee: BP Corp North America Inc
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Filing: 1983-10-27
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Granted: 1984-11-20
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Expires: 2003-10-27
Abstract
Abstract Hydrocarbon conversion process catalyst comprising an active metallic component comprising at least one metal having hydrocarbon conversion activity and at least one oxygenated phosphorus component, and a support component comprising at least one porous refractory inorganic oxide matrix component and at least one crystalline molecular sieve zeolite component.
Inventors
- 👤 Albert L. Hensley, Jr.
- 👤 Jeffrey T. Miller
- 👤 Thomas D. Nevitt
- 👤 A. Martin Tait
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-28 16:49
CPC Classifications
B; B01; B01J; B01J27/00; B01J27/14; B01J27/186; B01J29/00; B01J29/04; B01J29/06; B01J29/061; C; C10; C10G; C10G49/00; C10G49/02; C10G49/08
Claims Analysis
Total Claims: 4
Claim 1
Independent Claim
145 words
A hydrocarbon conversion process comprising contacting a chargestock comprising whole petroleum, shale oil, tar sand oil, coal and biomass liquids and fractions thereof, under hydrocarbon conversion conditions comprising a temperature of 350° F. to 850° F., a hydrogen pressure of 100 to 3,000 psig and a space velocity of 0.1 to 10 volumes of feed per volume of catalyst per hour, in the presence of a catalytic composition comprising (1) an active metallic component comprising at least one metal having hydrocarbon conversion activity and at least one oxygenated phosphorus component, and (2) a support component comprising at least one non-zeolitic, porous refractory inorganic matrix component and at least one crystalline molecular sieve zeolite component comprising a crystalline borosilicate zeolite or a crystalline aluminosilicate zeolite selected from the group consisting of ultrastable Y crystalline aluminosilicate zeolites and Y crustalline aluminosilicates in acid form or mixtures thereof.
Claim 2
Dependent Claim
145 words
A hydrocarbon conversion process comprising contacting a chargestock comprising whole petroleum, shale oil, tar sand oil, coal and biomass liquids and fractions thereof, under hydrocarbon conversion conditions comprising a temperature of 350° F. to 850° F., a hydrogen pressure of 100 to 3,000 psig and a space velocity of 0.1 to 10 volumes of feed per volume of catalyst per hour, in the presence of a catalytic composition comprising (1) an active metallic component comprising at least one metal having hydrocarbon conversion activity and at least one oxygenated phosphorus component, and (2) a support component comprising at least one non-zeolitic, porous refractory inorganic matrix component and at least one crystalline molecular sieve zeolite component comprising a crystalline borosilicate zeolite or a crystalline aluminosilicate zeolite selected from the group consisting of ultrastable Y crystalline aluminosilicate zeolites and Y crustalline aluminosilicates in acid form or mixtures thereof.
Claim 3
Dependent Claim
146 words
A hydrogen processing process comprising contacting a whole petroleum or synthetic crude oil, coal or biomass liquid, or a fraction thereof with hydrogen under hydrogen processing conditions comprising a temperature of 350° F. to 850° F., a hydrogen pressure of 100 to 3,000 psig and a space velocity of 0.1 to 10 volumes of feed per volume of catalyst per hour, in the presence of a catalytic composition comprising (1) an active metallic oomponent comprising at least one metal having hydrogenation activity and at least one oxygenated phosphorus component, and (2) a support component comprising at least one non-zeolitic, porous refractory inorganic oxide matrix component and at least one crystalline molecular sieve zeolite component comprising a crystalline borosilicate zeolite or a crystalline aluminosilicate zeolite selected from the group consisting of ultrastable Y crystalline aluminosilicate zeolites and Y crystalline aluminosilite zeolites in acid form or mixtures therof.
Claim 4
Dependent Claim
146 words
A hydrogen processing process comprising contacting a whole petroleum or synthetic crude oil, coal or biomass liquid, or a fraction thereof with hydrogen under hydrogen processing conditions comprising a temperature of 350° F. to 850° F., a hydrogen pressure of 100 to 3,000 psig and a space velocity of 0.1 to 10 volumes of feed per volume of catalyst per hour, in the presence of a catalytic composition comprising (1) an active metallic oomponent comprising at least one metal having hydrogenation activity and at least one oxygenated phosphorus component, and (2) a support component comprising at least one non-zeolitic, porous refractory inorganic oxide matrix component and at least one crystalline molecular sieve zeolite component comprising a crystalline borosilicate zeolite or a crystalline aluminosilicate zeolite selected from the group consisting of ultrastable Y crystalline aluminosilicate zeolites and Y crystalline aluminosilite zeolites in acid form or mixtures therof.
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) | 1987-11-20 | 1988-05-21 | 1988-11-20 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1991-11-20 | 1992-05-21 | 1992-11-20 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1995-11-20 | 1996-05-21 | 1996-11-20 | $7700.00 | Window Closed / Lapsed |