US4609679A
Expired / Lapsed
US
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Process for producing methane from hydrogen and carbon monoxide
Assignee: Dow Chemical Co
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Filing: 1985-05-31
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Granted: 1986-09-02
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Expires: 2005-05-31
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.
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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 |