US3271418A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Catalytic conversion of hydrocarbons with a crystalline alumino-silicate in a silica-alumina matrix
Assignee: Mobil Oil AS
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Filing: 1965-06-22
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Granted: 1966-09-06
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Expires: 1985-06-22
Abstract
No abstract record available.
Inventors
- 👤 Charles J Plank
- 👤 Edward J Rosinski
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-25 10:51
CPC Classifications
B; B01; B01J; B01J29/00; B01J29/04; B01J29/06; B01J29/08; C; C10; C10G; C10G11/00; C10G11/02; C10G11/04; C10G11/05
Claims Analysis
Total Claims: 2
Claim 1
Independent Claim
293 words
IN A CONTINUOUS CYCLIC PROCESS OF CRACKING A PETROLEUM GAS OIL TO PRODUCE A SELECTIVELY LARGE YIELD OF HIGH OCTANE GASOLINE, AND SELECTIVELY SMALL YIELDS OF DRY GAS AND COKE, THE STEPS OF: (A) CONTINUOUSLY PASSING A GAS OIL THROUGH A CRACKING ZONE MAINTAINED UNDER CATALYTIC CRACKING CONDITIONS; (B) IN CONTACT WITH A COMPOSITION CATALYST IN SAID CRACKING ZONE; (C) SAID COMPOSITE CATALYST COMPRISING AS A MAJOR PROPORTION POROUS SILICA-ALUMINA; (D) WHICH SILICA-ALUMINA IS CAPABLE, AS A CATALYST, OF EFFECTING AT LEAST 15 PERCENT CONVERSION OF MID-CONTIENT GAS OIL HAVING A BOILING RANGE OF 450* TO 950*F. AT A LIQUID HOURLY SPACE VELOCITY OF 2, A CATALYST TO OIL VOLUME RATIO OF 3, A TEMPERATURE OF 900*F. AND SUBSTANTIALLY ATMOSPHERIC PRESSURE; (E) AND NOT MORE THAN ABOUT 25 PERCENT BY WEIGHT OF A FINELY DIVIDED CRYSTALLINE ALUMINOSILICATE INTERMIXED OF RIGID THREE-DIMENSIONAL NETWORKS CHARACTERIZED BY TION OF THE ORIGINAL ALKALI METAL CONTENT OF SAID CRYSTALLINE ALUMINOSILICATE HAVING BEEN REPLACED BY ION EXCHANGE; (F) SAID CRYSTALLINE ALUMINOSILICATE HAVING A STRUCTURE OF RIGID THREE-DIMENSIONAL NEWTWORKS CHARACTERIZED BY A SYSTEM OF CAVITIES WITH INTERCONNECTING PORE OPENINGS HAVING MINIMUM DIAMETERS OF GREATER THAN 4 ANGSTROMS AND LESS THAN 15 AMGSTROMS, THE CAVITIES BEING CONNECTED WITH EACH OTHER IN THREE DEEMENSIONS BY SAID PORE OPENINGS; (B) SAID CRYSTALLINE ALUMINOSILICATE HAVING A CATALYTIC ACTIVITY WHICH IS SUBSTANTIALLY GREATER THAN THAT OF SAID SILICA-ALUMINA; (H) THE EXCHANGEABLE SODIUM CONTENT OF SAID COMPOSITE CATALYST BEING LESS THAN ABOUT 1% BY WEIGHT; (I) CONTINUOUSLY RECOVERING A LIQUID FRACTION RICH IN HIGH OCTANE GASOLINE; (J) CONTINUOUSLY WITHDRAWING SPENT COMPOSITE CATALYST FROM THE CRACKING ZONE; (K) SUBJECTING SAID WITHDRAWN SPENT CATALYST TO AN OPERATION TO REGENERATE CATALYTIC ACTIVITY OF BOTH SAID SILICA-ALUMINA AND SAID ZEOLITE; (L) AND RETURNING REGENERATED COMPOSITE CATALYST TO SAID CRACKING ZONE.
Claim 2
Dependent Claim
293 words
IN A CONTINUOUS CYCLIC PROCESS OF CRACKING A PETROLEUM GAS OIL TO PRODUCE A SELECTIVELY LARGE YIELD OF HIGH OCTANE GASOLINE, AND SELECTIVELY SMALL YIELDS OF DRY GAS AND COKE, THE STEPS OF: (A) CONTINUOUSLY PASSING A GAS OIL THROUGH A CRACKING ZONE MAINTAINED UNDER CATALYTIC CRACKING CONDITIONS; (B) IN CONTACT WITH A COMPOSITION CATALYST IN SAID CRACKING ZONE; (C) SAID COMPOSITE CATALYST COMPRISING AS A MAJOR PROPORTION POROUS SILICA-ALUMINA; (D) WHICH SILICA-ALUMINA IS CAPABLE, AS A CATALYST, OF EFFECTING AT LEAST 15 PERCENT CONVERSION OF MID-CONTIENT GAS OIL HAVING A BOILING RANGE OF 450* TO 950*F. AT A LIQUID HOURLY SPACE VELOCITY OF 2, A CATALYST TO OIL VOLUME RATIO OF 3, A TEMPERATURE OF 900*F. AND SUBSTANTIALLY ATMOSPHERIC PRESSURE; (E) AND NOT MORE THAN ABOUT 25 PERCENT BY WEIGHT OF A FINELY DIVIDED CRYSTALLINE ALUMINOSILICATE INTERMIXED OF RIGID THREE-DIMENSIONAL NETWORKS CHARACTERIZED BY TION OF THE ORIGINAL ALKALI METAL CONTENT OF SAID CRYSTALLINE ALUMINOSILICATE HAVING BEEN REPLACED BY ION EXCHANGE; (F) SAID CRYSTALLINE ALUMINOSILICATE HAVING A STRUCTURE OF RIGID THREE-DIMENSIONAL NEWTWORKS CHARACTERIZED BY A SYSTEM OF CAVITIES WITH INTERCONNECTING PORE OPENINGS HAVING MINIMUM DIAMETERS OF GREATER THAN 4 ANGSTROMS AND LESS THAN 15 AMGSTROMS, THE CAVITIES BEING CONNECTED WITH EACH OTHER IN THREE DEEMENSIONS BY SAID PORE OPENINGS; (B) SAID CRYSTALLINE ALUMINOSILICATE HAVING A CATALYTIC ACTIVITY WHICH IS SUBSTANTIALLY GREATER THAN THAT OF SAID SILICA-ALUMINA; (H) THE EXCHANGEABLE SODIUM CONTENT OF SAID COMPOSITE CATALYST BEING LESS THAN ABOUT 1% BY WEIGHT; (I) CONTINUOUSLY RECOVERING A LIQUID FRACTION RICH IN HIGH OCTANE GASOLINE; (J) CONTINUOUSLY WITHDRAWING SPENT COMPOSITE CATALYST FROM THE CRACKING ZONE; (K) SUBJECTING SAID WITHDRAWN SPENT CATALYST TO AN OPERATION TO REGENERATE CATALYTIC ACTIVITY OF BOTH SAID SILICA-ALUMINA AND SAID ZEOLITE; (L) AND RETURNING REGENERATED COMPOSITE CATALYST TO SAID CRACKING ZONE.
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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) | 1969-09-05 | 1970-03-07 | 1970-09-06 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1973-09-05 | 1974-03-07 | 1974-09-06 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1977-09-05 | 1978-03-07 | 1978-09-06 | $7700.00 | Window Closed / Lapsed |