US4093029A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Utilization of low BTU natural gas
Assignee: Mobil Oil AS
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Filing: 1977-03-24
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Granted: 1978-06-06
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Expires: 1997-03-24
Abstract
Abstract Natural gas having a high CO2 content and low heating value is converted to useful and valuable products by the extensive removal of CO2 followed by conversion of the residue to a liquid product useful as fuel (e.g. methanol) through a process combining steam reforming and conversion of the resultant reformer stream, which contains CO, CO2 and H2 to liquid products. The CO2 removed from the natural gas feed is used, in a preferred embodiment, in tertiary methods of recovery of petroleum from natural reservoirs in which primary and secondary methods are no longer viable.
Inventors
- 👤 Paul Burg Weisz
- 👤 John Clarence Zahner
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-27 10:36
CPC Classifications
C; C10; C10G; C10G2/00; C10G2/30; C10G2/32; C01; C01B; C01B3/00; C01B3/02; C01B3/32; C01B3/34; C01B3/38; C01B3/48; C07; C07C; C07C1/00; C07C1/02; C07C29/00; C07C29/15; C07C29/151; C07C29/1516; C07C29/1518; E; E21; E21B; E21B43/00; E21B43/16; E21B43/164; E21B43/34; E21B43/40; C01B2203/00; C01B2203/02; C01B2203/0205; C01B2203/0227; C01B2203/0233; C01B2203/0283; C01B2203/04; C01B2203/0465; C01B2203/0475; C01B2203/0495; C01B2203/06; C01B2203/061; C01B2203/062; C01B2203/08; C01B2203/0872; C01B2203/0883; C01B2203/10; C01B2203/1041; C01B2203/1047; C01B2203/1052; C01B2203/1076; C01B2203/1082; C01B2203/1094; C01B2203/12; C01B2203/1205; C01B2203/1211; C01B2203/1235; C01B2203/1241; C01B2203/1258; C01B2203/1264; C01B2203/127
Claims Analysis
Total Claims: 6
Claim 1
Independent Claim
186 words
A process for economic utilization of natural gas, having low heating value by reason of containing carbon dioxide in admixture with the methane content thereof, which process comprises subjecting a natural gas having substantial methane content in admixture with at least 50 volume percent of carbon dioxide based on total volume of said gas to the following steps in the sequence recited: (a) removing a substantial portion of the acid gases from said natural gas to leave a reformer feed gas containing 20-40 mol percent carbon dioxide; (b) mixing said reformer feed gas with water and reacting the mixture in contact with a catalyst to promote the reforming reaction of methane and water to produce carbon monoxide and hydrogen under temperature and pressure conditions conducive to said reforming reaction; and (c) reacting the product of step (b) in contact with a carbon monoxide reduction catalyst for promotion of synthesis reaction between carbon dioxide, carbon monoxide and hydrogen to produce methanol or hydrocarbons, which are liquid at normal temperature of 21° C (70° F) and atmospheric pressure, under conditions of temperature and pressure conducive of said synthesis.
Claim 2
Dependent Claim
186 words
A process for economic utilization of natural gas, having low heating value by reason of containing carbon dioxide in admixture with the methane content thereof, which process comprises subjecting a natural gas having substantial methane content in admixture with at least 50 volume percent of carbon dioxide based on total volume of said gas to the following steps in the sequence recited: (a) removing a substantial portion of the acid gases from said natural gas to leave a reformer feed gas containing 20-40 mol percent carbon dioxide; (b) mixing said reformer feed gas with water and reacting the mixture in contact with a catalyst to promote the reforming reaction of methane and water to produce carbon monoxide and hydrogen under temperature and pressure conditions conducive to said reforming reaction; and (c) reacting the product of step (b) in contact with a carbon monoxide reduction catalyst for promotion of synthesis reaction between carbon dioxide, carbon monoxide and hydrogen to produce methanol or hydrocarbons, which are liquid at normal temperature of 21° C (70° F) and atmospheric pressure, under conditions of temperature and pressure conducive of said synthesis.
Claim 3
Dependent Claim
24 words
The process of claim 1 wherein said reformer feed gas consists essentially of 1.5 to 4 moles of methane per mole of carbon dioxide.
Claim 4
Dependent Claim
40 words
The process of claim 1 wherein said acid gases removed from said natural gas feed are further processed to separate the sulfur-containing component therefrom and provide a gaseous by-product stream enriched in carbon dioxide as compared with said natural gas.
Claim 5
Dependent Claim
22 words
The process of claim 3 wherein said by-product stream is injected into a subterranean oil-bearing formation to enhance production of oil therefrom.
Claim 6
Dependent Claim
43 words
The process of claim 1 wherein said acid gases removed from said natural gas feed, comprising a gaseous by-product stream enriched in carbon dioxide as compared with said natural gas, are injected into a subterranean oil-bearing formation to enhance production of oil therefrom.
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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) | 1981-06-05 | 1981-12-05 | 1982-06-06 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1985-06-05 | 1985-12-05 | 1986-06-06 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1989-06-05 | 1989-12-05 | 1990-06-06 | $7700.00 | Window Closed / Lapsed |