Patent US4116996A successfully refreshed from Google Patents.
US4116996A
Expired / Lapsed
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Catalyst for methane production
Assignee: Albemarle Corp
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Filing: 1977-06-06
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Granted: 1978-09-26
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Expires: 1997-06-06
Abstract
Abstract A process for selectively converting a gaseous mixture of carbon monoxide and hydrogen to methane, which comprises contacting the gases with a catalyst at elevated temperature. The catalyst consists essentially of alkali metal, activated carbon and at least one halide of a transition metal selected from Group VIII of the Periodic Table. This catalyst has good activity at temperatures between about 250° C. and about 350° C.
Inventors
- 👤 Yun-Yang Huang
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-05 20:47
CPC Classifications
B; B01; B01J; B01J27/00; B01J27/06; B01J27/08; B01J27/10; C; C07; C07C; C07C1/00; C07C1/02; C07C1/04; C07C1/0425; C07C1/043; C07C1/0435; C07C2521/00; C07C2521/18; C07C2523/00; C07C2523/02; C07C2523/04; C07C2527/00; C07C2527/06; C07C2527/128
Claims Analysis
Total Claims: 11
Claim 1
Independent Claim
96 words
A process for the conversion of a gaseous reactant mixture comprising carbon monoxide and hydrogen to methane, comprising contacting said gaseous mixture with a catalyst at an elevated temperature sufficient to convert said mixture to methane, said catalyst consisting essentially of (i) an alkali metal, (ii) activated carbon, and (iii) at least one halide of a transition metal selected from Group VIII of the Periodic Table, wherein the weight ratio of said transition metal halide to activated carbon is approximately 0.01-1.0:1, and of said alkali metal to activated carbon and transition metal halide is approximately 0.1-0.5:1.
Claim 2
Dependent Claim
96 words
A process for the conversion of a gaseous reactant mixture comprising carbon monoxide and hydrogen to methane, comprising contacting said gaseous mixture with a catalyst at an elevated temperature sufficient to convert said mixture to methane, said catalyst consisting essentially of (i) an alkali metal, (ii) activated carbon, and (iii) at least one halide of a transition metal selected from Group VIII of the Periodic Table, wherein the weight ratio of said transition metal halide to activated carbon is approximately 0.01-1.0:1, and of said alkali metal to activated carbon and transition metal halide is approximately 0.1-0.5:1.
Claim 3
Dependent Claim
12 words
A process according to claim 1 wherein said alkali metal is potassium.
Claim 4
Dependent Claim
14 words
A process according to claim 1 wherein said transition metal halide is ferric chloride.
Claim 5
Dependent Claim
26 words
A process according to claim 1 wherein said hydrogen and said carbon monoxide are contacted at a temperature between about 250° C. to about 350° C.
Claim 6
Dependent Claim
26 words
A process according to claim 4 wherein said hydrogen and said carbon monoxide are contacted at a temperature between about 275° C. and about 325°° C.
Claim 7
Dependent Claim
18 words
A process according to claim 1 wherein the mole ratio of hydrogen to carbon monoxide is approximately 1.5:1.
Claim 8
Dependent Claim
100 words
A process according to claim 1 wherein said catalyst is formed by (a) preparing an aqueous solution of a halide of a transition metal selected from Group VIII of the Periodic Table, (b) impregnating finely divided particles of activated carbon with the resulting aqueous solution, (c) isolating and drying the resultant mixture, (d) heating the dried mixture to an elevated temperature, (e) adding an alkali metal to the activated carbon-metal halide mixture, and (f) heating the resultant mixture at a temperature above the melting point of the alkali metal under reduced pressure to form said alkali metal-activated carbon-metal halide catalyst.
Claim 9
Dependent Claim
113 words
A process according to claim 7 wherein said catalyst is formed by (a) preparing an aqueous solution of a halide of a transition metal selected from Group VIII of the Periodic Table, (b) impregnating finely divided particles of activated carbon with the resulting aqueous solution, (c) isolating and drying the resultant mixture (d) heating the dried mixture to an elevated temperature between about 100° C. and about 300° C., (e) adding an alkali metal to the activated carbon-metal halide mixture, and (f) heating the resultant mixture at a temperature to about 350° C. and at a pressure of less than about 10 -3 mm Hg to form said alkali metal-activated carbon-metal halide catalyst.
Claim 10
Dependent Claim
12 words
A process according to claim 8 wherein said alkali metal is potassium.
Claim 11
Dependent Claim
14 words
A process according to claim 7 wherein said transition metal halide is ferric chloride.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1981-09-25 | 1982-03-27 | 1982-09-26 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1985-09-25 | 1986-03-27 | 1986-09-26 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1989-09-25 | 1990-03-27 | 1990-09-26 | $7700.00 | Window Closed / Lapsed |