US3230164A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Hydrocracking process to produce gasoline and turbine fuels
Assignee: Shell USA Inc
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Filing: 1963-06-13
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Granted: 1966-01-18
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Expires: 1983-06-13
Abstract
No abstract record available.
Inventors
- 👤 Iii Curtis C Williams
- 👤 Mortimer D Abbott
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-30 22:57
CPC Classifications
C; C10; C10G; C10G45/00; C10G45/44; C10G2400/00; C10G2400/08
Claims Analysis
Total Claims: 2
Claim 1
Independent Claim
186 words
A PROCESS FOR CONVERTING A HIGH BOILING MINERAL OIL INTO GASOLINE AND AVIATION TURBINE FUEL WHICH COMPRISES CONTACTING SAID MINERAL OIL AND HYDROGEN WITH A HYDROFINING CATALYST AT HYDROFINING CONDITIONS TO REMOVE ORGANIC NITROGEN COMPOUNDS FROM THE OIL, CONTACTING THE HYDROFINED OIL AND HYDROGEN IN A HYDROCRACKING ZONE WITH A HYDROCRACKING CATALYST COMPRISING A HYDROGENATING-DEHYDROGENATING COMPONENT IN ASSOCIATION WITH AN ACTIVE ACID-ACTING CRACKING CATALYST AT HYDROCRACKING CONDITIONS, PARTIALLY COOLING EFFUENT FROM THE HYDROCRACKING ZONE, SEPARATING THE PARTIALLY COOLED EFFLUENT INTO A GASEOUS PHASE CONTAINING HYDROCARBONS IN THE GASOLINE BOILING RANGE AND A LIQUID PHASE CONTAINING HYDROCARBONS IN THE AVIATION TURBINE FUEL BOILING RANGE, CONTACTING THE LIQUID PHASE AND HYDROGEN WITH AN ACTIVE HYDROGENATION CATALYST ON A SUBSTANTIALLY INERT POROUS SUPPORT AT CONDITIONS INCLUDING A TEMPERATURE IN THE RANGE FROM ABOUT 250* TO 600*F. TO HYDROGENATE AROMATIC HYDROCARBONS TO NAPHTHENES, COOLING THE GASEOUS PHASE AND RECOVERING A NORMALLY LIQUID HYDROCARBON OIL, RECOVERING A NORMALLY LIQUID HYDROCARBON OIL AND THE HYDROGENATED LIQUID A HEAVY GASOLINE FRACTION AND AN AVIATION TURBINE FUEL FRACTION HAVING AN AROMATIC CONTENT LESS THAN 20% BY VOLUME, AND CATALYTICALLY REFORMING THE HEAVY GASOLINE FRACTION.
Claim 2
Dependent Claim
186 words
A PROCESS FOR CONVERTING A HIGH BOILING MINERAL OIL INTO GASOLINE AND AVIATION TURBINE FUEL WHICH COMPRISES CONTACTING SAID MINERAL OIL AND HYDROGEN WITH A HYDROFINING CATALYST AT HYDROFINING CONDITIONS TO REMOVE ORGANIC NITROGEN COMPOUNDS FROM THE OIL, CONTACTING THE HYDROFINED OIL AND HYDROGEN IN A HYDROCRACKING ZONE WITH A HYDROCRACKING CATALYST COMPRISING A HYDROGENATING-DEHYDROGENATING COMPONENT IN ASSOCIATION WITH AN ACTIVE ACID-ACTING CRACKING CATALYST AT HYDROCRACKING CONDITIONS, PARTIALLY COOLING EFFUENT FROM THE HYDROCRACKING ZONE, SEPARATING THE PARTIALLY COOLED EFFLUENT INTO A GASEOUS PHASE CONTAINING HYDROCARBONS IN THE GASOLINE BOILING RANGE AND A LIQUID PHASE CONTAINING HYDROCARBONS IN THE AVIATION TURBINE FUEL BOILING RANGE, CONTACTING THE LIQUID PHASE AND HYDROGEN WITH AN ACTIVE HYDROGENATION CATALYST ON A SUBSTANTIALLY INERT POROUS SUPPORT AT CONDITIONS INCLUDING A TEMPERATURE IN THE RANGE FROM ABOUT 250* TO 600*F. TO HYDROGENATE AROMATIC HYDROCARBONS TO NAPHTHENES, COOLING THE GASEOUS PHASE AND RECOVERING A NORMALLY LIQUID HYDROCARBON OIL, RECOVERING A NORMALLY LIQUID HYDROCARBON OIL AND THE HYDROGENATED LIQUID A HEAVY GASOLINE FRACTION AND AN AVIATION TURBINE FUEL FRACTION HAVING AN AROMATIC CONTENT LESS THAN 20% BY VOLUME, AND CATALYTICALLY REFORMING THE HEAVY GASOLINE FRACTION.
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) | 1969-01-17 | 1969-07-19 | 1970-01-18 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1973-01-17 | 1973-07-19 | 1974-01-18 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1977-01-17 | 1977-07-19 | 1978-01-18 | $7700.00 | Window Closed / Lapsed |