US4517298A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for producing fuel grade ethanol by continuous fermentation, solvent extraction and alcohol separation
Assignee: Georgia Tech Research Corp
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Filing: 1983-09-21
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Granted: 1985-05-14
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Expires: 2003-09-21
Abstract
Abstract Alcohol substantially free of water is prepared by continuously fermenting a fermentable biomass feedstock in a fermentation unit, thereby forming an aqueous fermentation liquor containing alcohol and microorganisms. Continuously extracting a portion of alcohol from said fermentation liquor with an organic solvent system containing an extractant for said alcohol, thereby forming an alcohol-organic solvent extract phase and an aqueous raffinate. Said alcohol is separated from said alcohol-organic solvent phase. A raffinate comprising microorganisms and unextracted alcohol is returned to the fermentation unit.
Inventors
- 👤 Daniel W. Tedder
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-02 17:14
CPC Classifications
C; C12; C12P; C12P7/00; C12P7/02; C12P7/04; C12P7/06; Y; Y02; Y02E; Y02E50/00; Y02E50/10; Y10; Y10S; Y10S435/00; Y10S435/813
Claims Analysis
Total Claims: 15
Claim 1
Independent Claim
176 words
A continuous method of preparing alcohol, comprising: continuously fermenting with fermentation microorganisms a fermentable biomass feedstock in water in a fermentation unit, thereby forming an aqueous fermentation liquor containing alcohol; withdrawing a sludge waste and fermentation liquor comprising microorganisms and alcohol obtained during the processing of the biomass in the processing unit; supplying additional feedstock and microorganisms to said fermentation unit; continuously extracting a low-level alcohol from said fermentation liquor with a chemically stable organic solvent system containing an extractant for said alcohol and a hydrocarbon solvent for said extractant, said hydrocarbon solvent having ten or more carbons in its atom, thereby forming an alcohol-organic solvent extract phase and an aqueous raffinate; separating said alcohol from said alcohol-organic solvent phase; wherein said low-level alcohol-organic solvent extract phase from the fermentation liquor is such that the alcohol content in the remaining fermentation liquor is maintained sufficiently low so that it does not destroy the microorganisms in the fermentation liquor; and returning all material components of said aqueous raffinate comprising microorganisms and unextracted alcohol to said fermentation unit.
Claim 2
Dependent Claim
176 words
A continuous method of preparing alcohol, comprising: continuously fermenting with fermentation microorganisms a fermentable biomass feedstock in water in a fermentation unit, thereby forming an aqueous fermentation liquor containing alcohol; withdrawing a sludge waste and fermentation liquor comprising microorganisms and alcohol obtained during the processing of the biomass in the processing unit; supplying additional feedstock and microorganisms to said fermentation unit; continuously extracting a low-level alcohol from said fermentation liquor with a chemically stable organic solvent system containing an extractant for said alcohol and a hydrocarbon solvent for said extractant, said hydrocarbon solvent having ten or more carbons in its atom, thereby forming an alcohol-organic solvent extract phase and an aqueous raffinate; separating said alcohol from said alcohol-organic solvent phase; wherein said low-level alcohol-organic solvent extract phase from the fermentation liquor is such that the alcohol content in the remaining fermentation liquor is maintained sufficiently low so that it does not destroy the microorganisms in the fermentation liquor; and returning all material components of said aqueous raffinate comprising microorganisms and unextracted alcohol to said fermentation unit.
Claim 3
Dependent Claim
39 words
The method of claim 1, which further comprises conducting said fermentation by continuously admitting fermentable biomass feedstock and fermenting microorganisms into said fermentation unit and continuously withdrawing portions of fermentation liquor for extraction and sludge wastes from said unit.
Claim 4
Dependent Claim
31 words
The method of claim 1, which further comprises: adding absolute alcohol obtained from said separation step to said extraction step to facilitate drying of the alcohol in the solvent-alcohol extract phase.
Claim 5
Dependent Claim
32 words
The method of claim 1, which further comprises: separating said alcohol from said alcohol-solvent phase by vacuum distillation; condensing the absolute alcohol distillate; and returning the solvent phase to said extraction step.
Claim 6
Dependent Claim
29 words
The method of claim 1, wherein said biomass feedstock is molasses, sugar cane or sugar beets or a grain selected from the group consisting of corn, barley and wheat.
Claim 7
Dependent Claim
18 words
The method of claim 1, wherein said fermentation is conducted at a temperature from 25° to 35° C.
Claim 8
Dependent Claim
21 words
The method of claim 1, wherein said fermentation is conducted at a temperature as high as 75° C. to 95° C.
Claim 9
Dependent Claim
22 words
The method of claim 1, wherein said solvent system contains an extractant which is capable of hydrogen bonding with water or alcohol.
Claim 10
Dependent Claim
20 words
The method of claim 8, wherein said extractant is an alkyl or aromatic alcohol, an ether or a carboxylic acid.
Claim 11
Dependent Claim
35 words
the method of claim 9, wherein said alcohol extractant is a high boiling alcohol having an alkyl group of at least ten carbon atoms, said high boiling alcohol not being combined with a hydrophobic solvent.
Claim 12
Dependent Claim
25 words
The method of claim 9, wherein said extractant is a solvent selected from the group consisting of isodecanol, 2-ethylhexanol, 2-methyl-2-pentanol, 4-heptanol, 3-ethyl-3-pentanol and mixtures thereof.
Claim 13
Dependent Claim
29 words
The method of claim 1, wherein the solvent component of said organic solvent system is a hydrocarbon material selected from the group consisting of dodecane, kerosene, gasoline and diisopropylbenzene.
Claim 14
Dependent Claim
51 words
The method of claim 1, wherein the extractant of said solvent system is a solvent selected from the group consisting of a symmetric or unsymmetric alkyl or aryl phosphate, phosphonate, phosphine oxide, sulfoxide, sulfone and an amine oxide or a quarternary ammonium or phosphonium salt of a sterically hindered carboxylic acid.
Claim 15
Dependent Claim
15 words
The method of claim 1, wherein the alcohol product of fermentation is ethanol or butanol.
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) | 1988-05-13 | 1988-11-12 | 1989-05-14 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1992-05-13 | 1992-11-12 | 1993-05-14 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1996-05-13 | 1996-11-12 | 1997-05-14 | $7700.00 | Window Closed / Lapsed |