US3943236A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Reforming process for carbon monoxide
Assignee: EIDP Inc
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Filing: 1973-10-17
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Granted: 1976-03-09
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Expires: 1993-10-17
Abstract
Abstract Hydrocarbons are reformed with steam to produce synthesis gas or hydrogen and carbon monoxide. This reforming process can be improved if after the carbon monoxide in the reformer effluent is removed, the remaining effluent, essentially hydrogen, is recycled to the reformer. Carbon dioxide must be added to the reformer inlet in an amount to balance the hydrogen present in the recycle. By this process larger quantities of carbon monoxide relative to the hydrogen produced can be realized.
Inventors
- 👤 Ralph V. Green
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-03 06:39
CPC Classifications
C; C01; C01B; C01B3/00; C01B3/50; C01B3/02; C01B3/32; C01B3/34; C01B3/38; C01B32/00; C01B32/40; C01B2203/00; C01B2203/04; C01B2203/0465; C01B2203/047
Claims Analysis
Total Claims: 4
Claim 1
Independent Claim
130 words
In the manufacture of carbon monoxide by the steam reforming of hydrocarbons in the presence of a nickel catalyst under pressures of 20 to 500 psig at temperatures of 650° to 1000°C. to produce a reformer effluent which contains hydrogen, carbon dioxide, and carbon monoxide, and thereafter compressing said reformer effluent and first separating the carbon dioxide from the reformer effluent and then separating and recovering the carbon monoxide from the reformer effluent, the improvement comprising recycling and preheating at least a portion of the reformer effluent remaining after the carbon monoxide has been separated to the feed to the reformer inlet and adding carbon dioxide to the reformer feed in an amount of at least one mole of carbon dioxide for every mole of hydrogen in the recycle stream.
Claim 2
Dependent Claim
130 words
In the manufacture of carbon monoxide by the steam reforming of hydrocarbons in the presence of a nickel catalyst under pressures of 20 to 500 psig at temperatures of 650° to 1000°C. to produce a reformer effluent which contains hydrogen, carbon dioxide, and carbon monoxide, and thereafter compressing said reformer effluent and first separating the carbon dioxide from the reformer effluent and then separating and recovering the carbon monoxide from the reformer effluent, the improvement comprising recycling and preheating at least a portion of the reformer effluent remaining after the carbon monoxide has been separated to the feed to the reformer inlet and adding carbon dioxide to the reformer feed in an amount of at least one mole of carbon dioxide for every mole of hydrogen in the recycle stream.
Claim 3
Dependent Claim
17 words
The process of claim 1 wherein the recycle stream is purified such that it is essentially hydrogen.
Claim 4
Dependent Claim
21 words
The process of claim 1 wherein the ratio of hydrogen to carbon monoxide in the reformer effluent is less than 2:1.
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) | 1979-03-09 | 1979-09-08 | 1980-03-09 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1983-03-09 | 1983-09-08 | 1984-03-09 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1987-03-09 | 1987-09-08 | 1988-03-09 | $7700.00 | Window Closed / Lapsed |