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Condensation of natural gas or methane into gasoline-range hydrocarbons

Assignee: Individual
•
Filing: 1983-06-16
•
Granted: 1984-08-21
•
Expires: 2003-06-16
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Abstract

Abstract This invention relates to a new process for the direct conversion of natural gas or methane into gasoline-range hydrocarbons (i.e., synthetic transportation fuels or lower olefins) via catalytic condensation using superacid catalysts.

Inventors

  • 👤 George A. Olah

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-08 16:41
CPC Classifications
C; C07; C07C; C07C17/00; C07C17/093; C07C17/10; C07C17/26; C07C17/263; C07C2/00; C07C2/76; C07C2/82; C07C2/84; C07C2521/00; C07C2521/16; C07C2521/18; C07C2527/00; C07C2527/02; C07C2527/03; C07C2527/06; C07C2527/08; C07C2527/12; C07C2527/1206; C07C2527/125; C07C2531/00; C07C2531/02; C07C2531/025; C07C2531/06; C07C2531/08; C07C2531/10; Y; Y10; Y10S; Y10S585/00; Y10S585/929; Y10S585/943

Claims Analysis

Total Claims: 5
Claim 1
Independent Claim 62 words
A process for the heterogeneous gas-phase condensation of natural gas or methane into gasoline-range hydrocarbons comprising the steps of: (a) thermally pretreating the natural gas or methane to form an acetylene-containing mixture; (b) condensing the resulting methane-acetylene-containing mixture in the presence of a superacid catalyst having a Hammett acidity function H o less than -11.9 to hydrocarbon mixtures in the gasoline range.
Claim 2
Dependent Claim 62 words
A process for the heterogeneous gas-phase condensation of natural gas or methane into gasoline-range hydrocarbons comprising the steps of: (a) thermally pretreating the natural gas or methane to form an acetylene-containing mixture; (b) condensing the resulting methane-acetylene-containing mixture in the presence of a superacid catalyst having a Hammett acidity function H o less than -11.9 to hydrocarbon mixtures in the gasoline range.
Claim 3
Dependent Claim 40 words
The process of claim 1 carried out utilizing solid superacid catalysts of strong Lewis acid fluorides of metals of Groups IV, V or VI of the Periodic Table, deposited on a chalconide carrier including alumina, silica, alumina-silica, or floridated alumina.
Claim 4
Dependent Claim 69 words
The process of claim 1 carried out utilizing a conjugate solid superacid catalyst composed of a strong Bronsted acid component selected from fluorosulfuric acid, perfluoroalkanesulfonic acids of 1 to 18 carbon atoms deposited on a suitable carrier, perfluorinated polymeric resinsulfonic acids or co-polymers of perfluorovinylsulfonic acid and tetrafluoroethylene or trifluorochloroethylene complexed with a Lewis acid fluoride of a metal of Groups IV, V or VI of the Periodic Table.
Claim 5
Dependent Claim 23 words
The process of claim 1 carried out at a temperature between 50° to 250° C. and a pressure of 1 to 150 atmospheres.

References Cited (Backward Citations)

US3678120A Cited
US3636129A Cited
US4035286A Cited
US3809728A Cited
US3979476A Cited
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US3960764A Cited
US4044069A Cited
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FR2372133A1 Cited
US4065381A Cited
US4162233A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1987-08-21 1988-02-20 1988-08-21 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1991-08-21 1992-02-20 1992-08-21 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1995-08-21 1996-02-20 1996-08-21 $7700.00 Window Closed / Lapsed

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