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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
•
Filing: 1965-06-22
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Granted: 1966-09-06
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Expires: 1985-06-22
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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NETWORKS CHARACTERIZED BY TION OF THE ORIGINAL ALKALI METAL CONTENT OF SAID CRYSTALLINE ALUMINOSILICATE HAVING BEEN REPLACED BY ION EXCHANGE; (F) SAID CRYSTALLINE ALUMINOSILICATE HAVING A STRUCTURE OF RIGID THREE-DIMENSIONAL NEWTWORKS CHARACTERIZED BY A SYSTEM OF CAVITIES WITH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.

References Cited (Backward Citations)

US2962435A Cited
US2971903A Cited
US2971904A Cited
US2983670A Cited
US3130006A Cited
US3140249A Cited

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

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