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US4609679A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for producing methane from hydrogen and carbon monoxide

Assignee: Dow Chemical Co
•
Filing: 1985-05-31
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Granted: 1986-09-02
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Expires: 2005-05-31
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Abstract

Abstract Selectively produce methane under Fischer-Tropsch conditions using a catalyst consisting essentially of ruthenium supported on an oxide of tantalum, niobium, vanadium or mixtures thereof, the support preparation including calcination at a temperature such that essentially no crystalline metal oxide is detectable by X-ray diffraction prior to deposition of the catalytic metal.

Inventors

  • 👤 Clayton D. Wood
  • 👤 Edward F. Gleason

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-23 15:09
CPC Classifications
C; C07; C07C; C07C1/00; C07C1/02; C07C1/04; C07C1/0425; C07C1/043; C07C1/0435; B; B01; B01J; B01J23/00; B01J23/38; B01J23/54; B01J23/56; B01J23/64; B01J23/648; C07C2523/00; C07C2523/16; C07C2523/20; C07C2523/22; C07C2523/38; C07C2523/40; C07C2523/46; C07C2523/54; C07C2523/56; C07C2523/64; C07C2523/648

Claims Analysis

Total Claims: 14
Claim 1
Independent Claim 110 words
In a process for producing hydrocarbons by contacting carbon monoxide and hydrogen at reactive conditions, the improvement comprising increasing the yield of methane by contacting the carbon monoxide and hydrogen with a catalyst consisting essentially of: (a) a catalytic metal component which is from about 0.1 to about 10 percent by weight, based on the weight of the catalyst, of ruthenium; and the balance being (b) a support component which is at least one oxide of tantalum, niobium, vanadium or mixtures thereof, the support preparation including calcination at a temperature such that essentially no crystalline metal oxide is detectable by X-ray diffraction prior to deposition of the catalytic metal thereon.
Claim 2
Dependent Claim 110 words
In a process for producing hydrocarbons by contacting carbon monoxide and hydrogen at reactive conditions, the improvement comprising increasing the yield of methane by contacting the carbon monoxide and hydrogen with a catalyst consisting essentially of: (a) a catalytic metal component which is from about 0.1 to about 10 percent by weight, based on the weight of the catalyst, of ruthenium; and the balance being (b) a support component which is at least one oxide of tantalum, niobium, vanadium or mixtures thereof, the support preparation including calcination at a temperature such that essentially no crystalline metal oxide is detectable by X-ray diffraction prior to deposition of the catalytic metal thereon.
Claim 3
Dependent Claim 14 words
The process of claim 1 wherein the support component is an oxide of tantalum.
Claim 4
Dependent Claim 20 words
The process of claim 2 wherein the ratio of hydrogen to carbon monoxide ranges from about 1 to about 3.
Claim 5
Dependent Claim 20 words
The process of claim 2 wherein the support component has a surface area greater than about 10 m 2 /g.
Claim 6
Dependent Claim 13 words
The process of claim 1 wherein the yield is at least 25 percent.
Claim 7
Dependent Claim 20 words
The process of claim 4 wherein the catalytic metal component is from about 0.5 to about 5 percent by weight.
Claim 8
Dependent Claim 21 words
The process of claim 1 wherein the contacting is at a temperature of from about 200° C. to about 400° C.
Claim 9
Dependent Claim 19 words
The process of claim 3 wherein the hydrogen to carbon monoxide ratio is 2 and the pressure is ambient.
Claim 10
Dependent Claim 13 words
The process of claim 1 wherein the yield is at least 55 percent.
Claim 11
Dependent Claim 14 words
The process of claim 2 wherein the yield is at least about 85 percent.
Claim 12
Dependent Claim 19 words
The process of claim 1 wherein the support is calcined at from about 100° C. to about 550° C.
Claim 13
Dependent Claim 109 words
In a process for producing methane by contacting carbon monoxide and hydrogen at reactive conditions, the improvement comprising contacting the carbon monoxide and hydrogen with a catalyst composition consisting essentially of: (a) from about 0.1 to about 10 percent by weight, based on the weight of the composition, ruthenium; and (b) a support component which is at least one non-crystalline oxide of tantalum, niobium, vanadium or mixtures thereof, the support preparation including calcination at a temperature such that essentially no crystalline metal oxide is detectable by X-ray diffraction prior to deposition of the catalytic metal thereon under conditions sufficient to produce a yield of at least about 25 percent.
Claim 14
Dependent Claim 109 words
In a process for producing methane by contacting carbon monoxide and hydrogen at reactive conditions, the improvement comprising contacting the carbon monoxide and hydrogen with a catalyst composition consisting essentially of: (a) from about 0.1 to about 10 percent by weight, based on the weight of the composition, ruthenium; and (b) a support component which is at least one non-crystalline oxide of tantalum, niobium, vanadium or mixtures thereof, the support preparation including calcination at a temperature such that essentially no crystalline metal oxide is detectable by X-ray diffraction prior to deposition of the catalytic metal thereon under conditions sufficient to produce a yield of at least about 25 percent.

References Cited (Backward Citations)

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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) 1989-09-01 1990-03-03 1990-09-02 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1993-09-01 1994-03-03 1994-09-02 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1997-09-01 1998-03-03 1998-09-02 $7700.00 Window Closed / Lapsed

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