US5070016A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Integrated process for producing ethanol, methanol and butyl ethers
Assignee: BIOCLEAN FUELS Inc
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Filing: 1991-03-28
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Granted: 1991-12-03
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Expires: 2011-03-28
Abstract
Abstract A methanol synthesis and an ethanol synthesis are integrated into a single continuous process with the by-product carbon dioxide generated in the ethanol synthesis being utilized in the methanol synthesis. The methanol synthesis and ethanol synthesis can be further integrated with isobutylene synthesis with by-product hydrogen formed during isobutylene synthesis being used as a raw material in the methanol synthesis. In the preferred embodiments the ethanol synthesis utilizes Zymomonas mobilis bacteria in anaerobic fermentation in order to maximize the amount of carbon dioxide produced in a form which can be utilized in the methanol synthesis, to reduce carbon dioxide emissions and to provide an ethnaol product which is highly suitable for reaction with the isobutylene to form ethyl tertiary butyl ether.
Inventors
- 👤 David E. Hallberg
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-24 15:09
CPC Classifications
C; C12; C12P; C12P7/00; C12P7/02; C12P7/04; C07; C07C; C07C29/00; C07C29/15; C07C29/151; C07C29/1516; C07C29/1518; C07C41/00; C07C41/01; C07C41/05; C07C41/06; C12P7/06; C12P7/065; C12P7/14; Y; Y02; Y02E; Y02E50/00; Y02E50/10; Y02P; Y02P20/00; Y02P20/10; Y10; Y10S; Y10S435/00; Y10S435/813; Y10S435/8215; Y10S435/822
Claims Analysis
Total Claims: 17
Claim 1
Independent Claim
73 words
An integrated continuous process for the production of ethanol and methanol comprising: (a) fermenting a vegetable material anaerobically in an aqueous medium to produce ethanol in said medium and by-product carbon dioxide containing less than 1% by volume air; (b) recovering said ethanol from said aqueous medium; (c) reacting said by-product carbon dioxide containing less than 1% by volume air with hydrogen in a methanol reactor to form a gas stream containing methanol.
Claim 2
Dependent Claim
73 words
An integrated continuous process for the production of ethanol and methanol comprising: (a) fermenting a vegetable material anaerobically in an aqueous medium to produce ethanol in said medium and by-product carbon dioxide containing less than 1% by volume air; (b) recovering said ethanol from said aqueous medium; (c) reacting said by-product carbon dioxide containing less than 1% by volume air with hydrogen in a methanol reactor to form a gas stream containing methanol.
Claim 3
Dependent Claim
12 words
The integrated process of claim 1 wherein said fermenting is by bacteria.
Claim 4
Dependent Claim
12 words
The integrated process of claim 2 wherein said bacteria are Zymomonas mobilis.
Claim 5
Dependent Claim
58 words
The integrated process of claim 3 wherein said fermenting is conducted in at least one fermenter on a continuous basis, with continuous addition of a carbon source and continuous removal of medium, and wherein the removed medium is filtered to separate out said bacteria leaving an ethanol product stream, and said separated bacteria are returned to said fermenter.
Claim 6
Dependent Claim
33 words
The integrated process of claim 1 wherein the ethanol is recovered from the aqueous medium by distillation and at least a portion of the heat used for said distillation is the generated steam.
Claim 7
Dependent Claim
57 words
The integrated process of claim 1 further comprising: (d) reacting methane and steam in a steam reformer to form carbon oxides and at least a portion of said hydrogen and wherein said carbon oxides and said hydrogen portion are reacted in admixture with said by-product carbon dioxide in step (c) to form said gas stream containing methanol.
Claim 8
Dependent Claim
57 words
The integrated process of claim 3 further comprising: (d) reacting methane and steam in a steam reformer to form carbon oxides and at least a portion of said hydrogen and wherein said carbon oxides and said hydrogen portion are reacted in admixtures with said by-product carbon dioxzide in step (c) to form said gas stream containing methanol.
Claim 9
Dependent Claim
26 words
The integrated process of claim 6 wherein said by-product carbon dioxide is fed to said steam reformer for admixture with carbon oxides and hydrogen produced therein.
Claim 10
Dependent Claim
36 words
The integrated process of claim 6 wherein said by-product carbon dioxide is admixed with said carbon oxides and portion of said hydrogen exiting said steam reformer and wherein the admixture is fed to the methanol reactor.
Claim 11
Dependent Claim
36 words
The integrated process of claim 7 wherein said by-product carbon dioxide is admixed with said carbon oxides and portion of said hydrogen exiting said steam reformer and wherein the admixture is fed to the methanol reactor.
Claim 12
Dependent Claim
38 words
The integrated process of claim 9 further comprising: dehydrogenating isobutane to make by-product hydrogen and isobutylene; and admixing said by-product hydrogen with said admixture for reaction with said carbon oxides and by-product carbon dioxide in said methanol reactor.
Claim 13
Dependent Claim
38 words
The integrated process of claim 10 further comprising: dehydrogenating isobutane to make by-product hydrogen and isobutylene; and admixing said by-product hydrogen with said admixture for reaction with said carbon oxides and by-product carbon dioxide in said methanol reactor.
Claim 14
Dependent Claim
22 words
The integrated process of claim 11 further comprising: reacting said ethanol and/or methanol with said isobutylene to produce a tertiary butyl ether.
Claim 15
Dependent Claim
22 words
The integrated process of claim 12 further comprising: reacting said ethanol and/or methanol with said isobutylene to produce a tertiary butyl ether.
Claim 16
Dependent Claim
21 words
The integrated process of claim 1 further comprising: dehydrogenating isobutane to make at least a portion of said hydrogen and isobutylene.
Claim 17
Dependent Claim
22 words
The integrated process of claim 1, further comprising: contacting said gas stream with water in a heat exchange relationship to generate steam.
References Cited (Backward Citations)
US4118425A
Cited
US4425433A
Cited
US4334026A
Cited
US4731329A
Cited
US4413150A
Cited
US4680263A
Cited
US4617270A
Cited
US4476334A
Cited
US4816607A
Cited
US4894394A
Cited
US4885241A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1994-12-02 | 1995-06-03 | 1995-12-03 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1998-12-02 | 1999-06-03 | 1999-12-03 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2002-12-02 | 2003-06-03 | 2003-12-03 | $7700.00 | Window Closed / Lapsed |