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US4157950A Expired / Lapsed US ⏱️ 0.0 years remaining

Conversion of hydrocarbons

Assignee: Mobil Oil AS
•
Filing: 1977-10-17
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Granted: 1979-06-12
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Expires: 1997-10-17
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Abstract

Abstract Crystalline aluminosilicate zeolites are used as catalysts for various hydrocarbon conversion processes and are particularly useful for conversion of paraffins in the presence of an alkylatable aromatic hydrocarbon such as benzene.

Inventors

  • 👤 Vincent J. Frilette
  • 👤 Mae K. Rubin

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-01 10:10
CPC Classifications
C; C10; C10G; C10G47/00; C10G47/02; C10G47/10; C10G47/12; C10G47/16; B; B01; B01J; B01J20/00; B01J20/02; B01J20/10; B01J20/16; B01J20/18; B01J20/186; B01J29/00; B01J29/04; B01J29/06; B01J29/18; C07; C07C; C07C2/00; C07C2/02; C07C2/04; C07C2/06; C07C2/08; C07C2/12; C07C2/54; C07C2/64; C07C2/66; C07C2/76; C07C4/00; C07C4/02; C07C4/06; C07C5/00; C07C5/22; C07C5/27; C07C5/29; C07C5/32; C07C5/367; C07C5/373; C07C5/393; C07C5/41; C07C6/00; C07C6/08; C07C6/12; C07C6/123; C10G11/00; C10G11/02; C10G11/04; C10G11/05; C10G35/00; C10G35/04; C10G35/06; C10G35/095; C07C2529/00; C07C2529/04; C07C2529/06; C07C2529/18; C07C2601/00; C07C2601/06; C07C2601/08; Y; Y02; Y02P; Y02P20/00; Y02P20/50; Y02P20/584

Claims Analysis

Total Claims: 11
Claim 1
Independent Claim 77 words
In a process for increasing the aromatic content of a liquid hydrocarbon charge comprising paraffins and cycloparaffins by contact with a solid catalyst under conversion temperatures of at least 180° C. and recovering from such conversion a liquid hydrocarbon product of greater aromatic content than said charge; the improvement consisting of conducting such conversion by contacting said charge with a catalyst comprising a crystalline aluminosilicate zeolite characterized by a silica to alumina ratio of at least 10.
Claim 2
Dependent Claim 77 words
In a process for increasing the aromatic content of a liquid hydrocarbon charge comprising paraffins and cycloparaffins by contact with a solid catalyst under conversion temperatures of at least 180° C. and recovering from such conversion a liquid hydrocarbon product of greater aromatic content than said charge; the improvement consisting of conducting such conversion by contacting said charge with a catalyst comprising a crystalline aluminosilicate zeolite characterized by a silica to alumina ratio of at least 10.
Claim 3
Dependent Claim 13 words
A process according to claim 1 wherein a petroleum naphtha is catalytically reformed.
Claim 4
Dependent Claim 47 words
A process for the alkylation of an aromatic hydrocarbon which comprises contacting said aromatic hydrocarbon with an alkylating agent in an alkylation reaction zone under alkylation conditions with a catalyst consisting essentially of a crystalline aluminosilicate zeolite having a silica to alumina ratio of at least 10.
Claim 5
Dependent Claim 47 words
A process for the alkylation of an aromatic hydrocarbon which comprises contacting said aromatic hydrocarbon with an alkylating agent in an alkylation reaction zone under alkylation conditions with a catalyst consisting essentially of a crystalline aluminosilicate zeolite having a silica to alumina ratio of at least 10.
Claim 6
Dependent Claim 17 words
The process of claim 1 wherein the aluminosilicate has been base exchanged with ammonium or hydrogen ions.
Claim 7
Dependent Claim 17 words
The process of claim 1 wherein the aluminosilicate is at least 50 percent in the hydrogen form.
Claim 8
Dependent Claim 11 words
The process of claim 3 wherein said aromatic hydrocarbon is benzene.
Claim 9
Dependent Claim 12 words
The process of claim 3 wherein said alkylating agent is an olefin.
Claim 10
Dependent Claim 10 words
The process of claim 7 wherein said olefin is ethylene.
Claim 11
Dependent Claim 10 words
The process of claim 7 wherein said olefin is propylene.

References Cited (Backward Citations)

US2904607A Cited
US3039953A Cited
US3114696A Cited
US3033778A Cited
US3140253A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1982-06-11 1982-12-11 1983-06-12 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1986-06-11 1986-12-11 1987-06-12 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1990-06-11 1990-12-11 1991-06-12 $7700.00 Window Closed / Lapsed

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