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US4239499A Expired / Lapsed US ⏱️ 0.0 years remaining

Production of a fuel gas and synthetic natural gas from methanol

Assignee: BASF Catalysts LLC
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Filing: 1977-11-15
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Granted: 1980-12-16
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Expires: 1997-11-15
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Abstract

Abstract Methanol is passed over a catalyst at an elevated temperature and pressure to produce a fuel gas containing a high proportion of methane in a one-step catalytic conversion process. Removal of water and carbon dioxide from the fuel gas produces a synthetic natural gas. For example, methanol with water is passed over a precious metal catalyst such as ruthenium on alumina at a temperature in the range of about 350° C. to 500° C. and a pressure in the range of about 800 to 2500 psig to produce a gaseous mixture comprising methane, carbon dioxide, minor amounts of hydrogen and essentially no carbon monoxide. Upon condensing the water vapor and scrubbing out the carbon dioxide, synthetic natural gas is obtained having a methane content above 90% by volume.

Inventors

  • 👤 William C. Pfefferle

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-30 02:53
CPC Classifications
C; C10; C10L; C10L3/00; C10L3/06; C10L3/08

Claims Analysis

Total Claims: 11
Claim 1
Independent Claim 112 words
A single-stage catalytic process for making a fuel gas, said process comprising passing a gaseous feed comprised of methanol and steam, in a reactor, over a catalyst comprised of Group VIII metal on a support at a pressure in the range of from about 800 psig to about 2500 psig and a temperature in the range of from about 350° C. to about 500° C., maintaining said gaseous feed in a completely vaporized state while passing said gaseous feed through said reactor whereby said gaseous feed is reformed entirely in the vapor phase to a gaseous product mixture containing at least about 90% methane by volume on a dry carbon dioxide-free basis.
Claim 2
Dependent Claim 112 words
A single-stage catalytic process for making a fuel gas, said process comprising passing a gaseous feed comprised of methanol and steam, in a reactor, over a catalyst comprised of Group VIII metal on a support at a pressure in the range of from about 800 psig to about 2500 psig and a temperature in the range of from about 350° C. to about 500° C., maintaining said gaseous feed in a completely vaporized state while passing said gaseous feed through said reactor whereby said gaseous feed is reformed entirely in the vapor phase to a gaseous product mixture containing at least about 90% methane by volume on a dry carbon dioxide-free basis.
Claim 3
Dependent Claim 29 words
The process of claim 1 wherein said catalyst is selected from the group consisting of nickel, platinum, palladium, rhodium, ruthenium and mixtures thereof on a refractory inorganic oxide support.
Claim 4
Dependent Claim 10 words
The process of claim 2 wherein said catalyst comprises ruthenium.
Claim 5
Dependent Claim 10 words
The process of claim 2 wherein said catalyst comprises nickel.
Claim 6
Dependent Claim 30 words
The process of claim 2 wherein said steam is present in a ratio in the range of from about 0.5 to about 1.5 moles steam for each mole of methanol.
Claim 7
Dependent Claim 30 words
The processs of claim 1 wherein said steam is present in a ratio in the range of from about 0.5 to about 1.5 moles steam for each mole of methanol.
Claim 8
Dependent Claim 21 words
The process of claim 1 wherein said gaseous feed contains at least a portion of said gaseous product mixture recycled thereto.
Claim 9
Dependent Claim 17 words
The process of claim 7 wherein steam is first removed from said portion of gaseous product mixture.
Claim 10
Dependent Claim 21 words
The process of claim 1 wherein said temperature is in the range of from about 380° C. to about 420° C.
Claim 11
Dependent Claim 21 words
The process of claim 1 wherein said pressure is in the range of from about 1100 psig to about 1600 psig.

References Cited (Backward Citations)

GB798741A Cited
US3379505A Cited
US3429679A Cited
US3511624A Cited
BE787137A Cited
GB1408134A Cited
US3915670A Cited
US3898057A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1983-12-16 1984-06-16 1984-12-16 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1987-12-16 1988-06-16 1988-12-16 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1991-12-16 1992-06-16 1992-12-16 $7700.00 Window Closed / Lapsed

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