US4443560A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Adiabatically reforming a reformed gas for producing methanol
Assignee: MW KELLOGG COMPANY (A DE CORP FORMED IN 1987)
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Filing: 1982-07-28
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Granted: 1984-04-17
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Expires: 2002-07-28
Abstract
Abstract The present invention is an improvement to a process for producing methanol which uses both steam reforming and partial oxidation by adiabatically reforming with substantially pure oxygen the reformed gas to produce the maximum amount of hydrogen for the synthesis of methanol.
Inventors
- 👤 Joseph R. Le Blanc, Jr.
- 👤 Dewey O. Moore
- 👤 Robert V. Schneider, III
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-04 17:10
CPC Classifications
C; C07; C07C; C07C29/00; C07C29/15; C07C29/151; C07C29/1516; C07C29/1518; C01; C01B; C01B3/00; C01B3/02; C01B3/32; C01B3/34; C01B3/50; C01B3/52; C01B2203/00; C01B2203/04; C01B2203/0415; C01B2203/0465; C01B2203/0475
Claims Analysis
Total Claims: 2
Claim 1
Independent Claim
144 words
In a process for producing methanol and purge gas in a first methanol plant and a second methanol plant wherein methanol from the first methanol plant is synthesized from a reformed gas mixture comprising hydrogen, methane, and carbon oxides produced by steam reforming C 1 to C 4 hydrocarbons and wherein methanol from the second methanol plant is synthesized from a clean synthesis gas comprising hydrogen and carbon monoxide produced by partial oxidation with substantially pure oxygen of a heavy carbonaceous material, the improvement which comprises: (a) recovering purge gas containing hydrogen, methane, and carbon monoxide from the first methanol plant; (b) adiabatically reforming the recovered purge gas to produce adiabatically reformed purge gas; and (c) mixing adiabatically reformed purge gas with clean synthesis gas from the heavy carbonaceous material partial oxidation step and introducing the resulting mixed gas to the second methanol plant.
Claim 2
Dependent Claim
144 words
In a process for producing methanol and purge gas in a first methanol plant and a second methanol plant wherein methanol from the first methanol plant is synthesized from a reformed gas mixture comprising hydrogen, methane, and carbon oxides produced by steam reforming C 1 to C 4 hydrocarbons and wherein methanol from the second methanol plant is synthesized from a clean synthesis gas comprising hydrogen and carbon monoxide produced by partial oxidation with substantially pure oxygen of a heavy carbonaceous material, the improvement which comprises: (a) recovering purge gas containing hydrogen, methane, and carbon monoxide from the first methanol plant; (b) adiabatically reforming the recovered purge gas to produce adiabatically reformed purge gas; and (c) mixing adiabatically reformed purge gas with clean synthesis gas from the heavy carbonaceous material partial oxidation step and introducing the resulting mixed gas to the second methanol plant.
References Cited (Backward Citations)
US3598527A
Cited
US4277416A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1987-04-17 | 1987-10-17 | 1988-04-17 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1991-04-17 | 1991-10-17 | 1992-04-17 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1995-04-17 | 1995-10-17 | 1996-04-17 | $7700.00 | Window Closed / Lapsed |