U.S. patents available from 1976 to present.
U.S. patent applications available from 2005 to present.

Process for producing fuel grade ethanol by continuous fermentation, solvent extraction and alcohol separation

Patent 4517298 Issued on May 14, 1985. Estimated Expiration Date: Icon_subject September 21, 2003. Estimated Expiration Date is calculated based on simple USPTO term provisions. It does not account for terminal disclaimers, term adjustments, failure to pay maintenance fees, or other factors which might affect the term of a patent.

Patent References

Production of ethanol from cellulose using a thermophilic mixed culture
Patent #: 4094742
Issued on: 06/13/1978
Inventor: Bellamy

Process for the acid hydrolysis of carbohydrate polymers and the continuous fermentation of the sugars _obtained therefrom to provide ethanol
Patent #: 4242455
Issued on: 12/30/1980
Inventor: Muller ,   et al.

Direct process for the production of gasohol from fermentation mixtures
Patent #: 4251231
Issued on: 02/17/1981
Inventor: Baird

Alcohol and fuel production Patent #: 4306884
Issued on: 12/22/1981
Inventor: Roth

Inventor

Assignee

Application

No. 06/534262 filed on 09/21/1983

US Classes:

435/160, Butanol435/161, Ethanol435/162, Multiple stages of fermentation; multiple types of micro-organisms or reuse of micro-organisms435/165, Substrate contains cellulosic material435/813, CONTINUOUS FERMENTATION44/453, Dehydration processes, and products thereof568/920Alkali or alkaline earth metal containing compound utilized

Examiners

Primary: Yoncoskie, Robert A.

Attorney, Agent or Firm

International Classes

C12P 7/02 (20060101)
C12P 7/06 (20060101)

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.

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