US4534772A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process of ether synthesis
Assignee: Consolidation Coal Co
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Filing: 1983-10-28
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Granted: 1985-08-13
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Expires: 2003-10-28
Abstract
Abstract A method for producing fuel comprised of gasoline rich in methanol and methyl ethers derived from coal, which process comprises gasifying the coal to produce carbon monoxide and hydrogen, steam shifting the gasification product to produce additional hydrogen, cleaning up the shifted product, catalytically converting the cleaned shifted gas to a mixture of alcohols, separating a methanol fraction from the mixture of alcohols, dehydrating the remaining alcohols to olefins, etherifying the olefin mixture with a portion of the removed methanol fraction, and blending into gasoline the resulting ether mixture and a second portion of the removed methanol fraction.
Inventors
- 👤 Eric H. Reichl
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-25 15:05
CPC Classifications
C; C10; C10L; C10L1/00; C10L1/02; C10L1/023; C07; C07C; C07C29/00; C07C29/15; C07C29/151; C07C29/1516; C07C29/1518; C07C41/00; C07C41/01; C07C41/05; C07C41/06
Claims Analysis
Total Claims: 3
Claim 1
Independent Claim
393 words
A process for producing a high octane liquid gasoline fuel product mixture rich in methanol and methyl ethers from coal consisting of the sequence of steps as follows: (a) gasifying coal to form a coal gasification product gas mixture comprising hydrogen and carbon monoxide, (b) contacting said coal gasification product gas with water and a shift conversion catalyst to catalytically react said water with said carbon monoxide of said gasification product gas to form a shift product gas mixture comprising carbon dioxide and hydrogen, (c) subjecting said shift product gas mixture to a clean-up step to produce a cleaned shift product gas mixture, (d) contacting said cleaned shift product gas mixture with an alcohol synthesis catalyst to form a synthesis product mixture of alcohols, said synthesis product mixture of alcohols comprising methanol, and said alcohol synthesis catalyst comprising alkali modified zinc oxide and chromium oxide, (e) separating said synthesis product mixture of alcohols into a methyl alcohol separation product mixture and a higher alcohol separation product mixture, said methyl alcohol separation product mixture comprising a substantially larger proportion of methanol than said synthesis product mixture of alcohols, and said higher alcohol separation product mixture further comprising substantially all of the alcohols other than methanol from said synthesis product mixture of alcohols, (f) dehydrating said higher alcohol separation product mixture with a catalyst to form a dehydration product mixture and water, said dehydration product mixture comprising olefins, and said catalyst comprising alumina, (g) catalytically reacting said olefins of said dehydration product mixture with a portion of said methyl alcohol separation product mixture in the presence of an ether synthesis catalyst at about 125° F. and 300 psig to form a methyl ether product mixture, said ether synthesis catalyst comprising acidic ion exchange resin, (h) mixing the remainder of said methyl alcohol separation product with said methyl ether product mixture to form a methyl alcohol and methyl ether product mixture as substantially the only liquid product of said coal gasified in step (a), and (i) mixing gasoline with said methyl alcohol and methyl ether product mixture to form a high octane fuel product, whereby substantially all of the alcohols formed in step (d) are formed into a mixture of methyl alcohol and methyl ethers and are mixed with gasoline to produce a high octane liquid gasoline fuel product rich in methyl alcohol and methyl ethers.
Claim 2
Dependent Claim
393 words
A process for producing a high octane liquid gasoline fuel product mixture rich in methanol and methyl ethers from coal consisting of the sequence of steps as follows: (a) gasifying coal to form a coal gasification product gas mixture comprising hydrogen and carbon monoxide, (b) contacting said coal gasification product gas with water and a shift conversion catalyst to catalytically react said water with said carbon monoxide of said gasification product gas to form a shift product gas mixture comprising carbon dioxide and hydrogen, (c) subjecting said shift product gas mixture to a clean-up step to produce a cleaned shift product gas mixture, (d) contacting said cleaned shift product gas mixture with an alcohol synthesis catalyst to form a synthesis product mixture of alcohols, said synthesis product mixture of alcohols comprising methanol, and said alcohol synthesis catalyst comprising alkali modified zinc oxide and chromium oxide, (e) separating said synthesis product mixture of alcohols into a methyl alcohol separation product mixture and a higher alcohol separation product mixture, said methyl alcohol separation product mixture comprising a substantially larger proportion of methanol than said synthesis product mixture of alcohols, and said higher alcohol separation product mixture further comprising substantially all of the alcohols other than methanol from said synthesis product mixture of alcohols, (f) dehydrating said higher alcohol separation product mixture with a catalyst to form a dehydration product mixture and water, said dehydration product mixture comprising olefins, and said catalyst comprising alumina, (g) catalytically reacting said olefins of said dehydration product mixture with a portion of said methyl alcohol separation product mixture in the presence of an ether synthesis catalyst at about 125° F. and 300 psig to form a methyl ether product mixture, said ether synthesis catalyst comprising acidic ion exchange resin, (h) mixing the remainder of said methyl alcohol separation product with said methyl ether product mixture to form a methyl alcohol and methyl ether product mixture as substantially the only liquid product of said coal gasified in step (a), and (i) mixing gasoline with said methyl alcohol and methyl ether product mixture to form a high octane fuel product, whereby substantially all of the alcohols formed in step (d) are formed into a mixture of methyl alcohol and methyl ethers and are mixed with gasoline to produce a high octane liquid gasoline fuel product rich in methyl alcohol and methyl ethers.
Claim 3
Dependent Claim
11 words
The process of claim 1 wherein said clean-up step comprises scrubbing.
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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) | 1988-08-12 | 1989-02-11 | 1989-08-13 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1992-08-12 | 1993-02-11 | 1993-08-13 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1996-08-12 | 1997-02-11 | 1997-08-13 | $7700.00 | Window Closed / Lapsed |