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US3988334A Expired / Lapsed US ⏱️ 0.0 years remaining

Method for methanation

Assignee: Phillips Petroleum Co
•
Filing: 1975-05-16
•
Granted: 1976-10-26
•
Expires: 1995-05-16
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Abstract

Abstract A method is provided for producing methane in which hydrogen and carbon monoxide are contacted in the presence of a supported nickel or cobalt catalyst which is further promoted by a noble metal of Group VIII of the Periodic Table. In an embodiment of the invention a metal from Group VIB of the Periodic Table, preferably tungsten, is used along with the Group VIII noble metal to promote the methanation reaction.

Inventors

  • 👤 Jack N. Finch
  • 👤 Dennis L. Ripley

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-25 09:21
CPC Classifications
B; B01; B01J; B01J23/00; B01J23/70; B01J23/76; B01J23/84; B01J23/85; C; C07; C07C; C07C1/00; C07C1/02; C07C1/04; C07C1/0425; C07C1/043; C07C1/0435; C07C2521/00; C07C2521/02; C07C2521/04; C07C2521/06; C07C2521/08; C07C2521/12; C07C2523/00; C07C2523/16; C07C2523/24; C07C2523/26; C07C2523/28; C07C2523/30; C07C2523/38; C07C2523/40; C07C2523/42; C07C2523/44; C07C2523/46; C07C2523/70; C07C2523/74; C07C2523/75; C07C2523/755; C07C2523/89

Claims Analysis

Total Claims: 5
Claim 1
Independent Claim 115 words
A method for producing methane comprising contacting hydrogen and carbon monoxide within a temperature range of about 200° C to about 450° C in the presence of a supported catalyst composite comprising a metal chosen from nickel and cobalt in an amount in the range of about 5 to about 20 weight percent of the catalyst composite; with the catalyst further promoted by a noble metal of Group VIII of the Periodic Table in an amount in the range of about 0.05 to about 5 weight percent of the catalyst composite; and a Group VIB metal in an amount in the range of from about 10 to about 60 weight percent of the catalyst composite.
Claim 2
Independent Claim 115 words
A method for producing methane comprising contacting hydrogen and carbon monoxide within a temperature range of about 200° C to about 450° C in the presence of a supported catalyst composite comprising a metal chosen from nickel and cobalt in an amount in the range of about 5 to about 20 weight percent of the catalyst composite; with the catalyst further promoted by a noble metal of Group VIII of the Periodic Table in an amount in the range of about 0.05 to about 5 weight percent of the catalyst composite; and a Group VIB metal in an amount in the range of from about 10 to about 60 weight percent of the catalyst composite.
Claim 3
Dependent Claim 46 words
A method of claim 1 wherein the catalytic support is chosen from among alumina, silica, zirconia, silica-alumina, and mixtures thereof; the noble metals are chosen from ruthenium, rhodium, palladium, osmium, iridium, and platinum; and the Group VIB metal is chosen from among chromium, molybdenum, and tungsten.
Claim 4
Dependent Claim 27 words
The method of claim 2 wherein the ratio of hydrogen to carbon monoxide used in the reaction is in the range of about 2.8 to about 3.2.
Claim 5
Dependent Claim 12 words
The method of claim 3 wherein the Group VIB metal is tungsten.

References Cited (Backward Citations)

US2911357A Cited
US3267025A Cited
US3334055A Cited
US3271326A Cited
US3787468A Cited
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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) 1979-10-26 1980-04-26 1980-10-26 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1983-10-26 1984-04-26 1984-10-26 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1987-10-26 1988-04-26 1988-10-26 $7700.00 Window Closed / Lapsed

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