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US4564595A Expired / Lapsed US ⏱️ 0.0 years remaining

Alcohol manufacturing process

Assignee: BIOMASS INTERNATIONAL Inc A CORP OF
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Filing: 1984-01-09
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Granted: 1986-01-14
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Expires: 2004-01-09
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Abstract

Abstract A continuous process for the production of alcohol, preferably ethanol, from cellulosic materials. The cellulosic materials are delignified such that the hemicellulose and the cellulose can be subsequently acid hydrolyzed into simple sugars. These sugars are fermented in the presence of yeast to yield ethanol and carbon dioxide. The alcohol vapor is removed from the fermentation solution under a reduced pressure and subsequently distilled. Carbon dioxide gas may be sparged throughout the fermenting solution in order to aid in the removal of the alcohol from the fermenting solution. The gaseous carbon dioxide is captured and utilized in the manufacture of additional quantities of ethanol or other basic chemicals.

Inventors

  • 👤 Alan M. Neves

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-05 10:49
CPC Classifications
C; C12; C12P; C12P7/00; C12P7/02; C12P7/04; C12P7/06; C12P7/08; C12P7/10; Y; Y02; Y02E; Y02E50/00; Y02E50/10; Y02P; Y02P20/00; Y02P20/50; Y02P20/582

Claims Analysis

Total Claims: 16
Claim 1
Independent Claim 111 words
A process for the conversion of cellulosic material into fermentable sugars, the process consisting essentially of the following steps: obtaining a feedstock, at least a portion of which is a cellulosic material; contacting the cellulosic material with a concentrated delignifying acid said concentrated delignifying acid being in a liquid phase and having a temperature of less than about 60° F. and having a concentration of from about 60% to about 90% acid by volume, thereby producing a cellulose-containing solution and a solid residue; removing the solid residue from the cellulose-containing solution; precipitating cellulose from the cellulose-containing solution; and hydrolyzing the precipitated cellulose with a dilute hydrolyzing acid, thereby producing fermentable sugars.
Claim 2
Dependent Claim 111 words
A process for the conversion of cellulosic material into fermentable sugars, the process consisting essentially of the following steps: obtaining a feedstock, at least a portion of which is a cellulosic material; contacting the cellulosic material with a concentrated delignifying acid said concentrated delignifying acid being in a liquid phase and having a temperature of less than about 60° F. and having a concentration of from about 60% to about 90% acid by volume, thereby producing a cellulose-containing solution and a solid residue; removing the solid residue from the cellulose-containing solution; precipitating cellulose from the cellulose-containing solution; and hydrolyzing the precipitated cellulose with a dilute hydrolyzing acid, thereby producing fermentable sugars.
Claim 3
Dependent Claim 30 words
A process as defined in claim 1 wherein the cellulosic material is a waste material selected from the group consisting of corn residue, forestry, feedlot, crop, urban, and industrial wastes.
Claim 4
Dependent Claim 15 words
A process as defined in claim 1 wherein the concentrated acid is concentrated sulfuric acid.
Claim 5
Dependent Claim 24 words
A process as defined in claim 1 wherein the dilute hydrolyzing acid has a concentration of about 0.5% to about 10% acid by volume.
Claim 6
Dependent Claim 16 words
A process as defined in claim 4 wherein the dilute hydrolyzing acid is dilute sulfuric acid.
Claim 7
Dependent Claim 53 words
A process as defined in claim 4 wherein during the hydrolyzing step the precipitated cellulose is hydrolyzed at a temperature within the range of about 200° F. to about 400° F. at a pressure from about 15 psi to about 200 psi for a period of about two minutes to about ten minutes.
Claim 8
Dependent Claim 23 words
A process as defined in claim 1 wherein the cellulose is precipitated from the cellulose-containing solution by diluting the cellulose-containing solution with methanol.
Claim 9
Dependent Claim 78 words
A process as defined in claim 1 wherein the cellulosic material comprises cellulose and hemicellulose and wherein the process further comprises the steps of: dissolving at least a portion of the hemicellulose in the cellulosic material with a dilute hemicellulose-dissolving acid prior to treating the cellulosic material in the contacting step, thereby producing a hemicellulose-containing solution and leaving undissolved cellulosic material to be treated in the contacting step; and separating the hemicellulose-containing solution from the undissolved cellulosic material.
Claim 10
Dependent Claim 25 words
A process as defined in claim 8 wherein the concentration of the dilute hemicellulose-dissolving acid is from about 0.5% to about 2.0% acid by volume.
Claim 11
Dependent Claim 17 words
A process as defined in claim 9 wherein the the dilute hemicellulose-dissolving acid is dilute sulfuric acid.
Claim 12
Dependent Claim 58 words
A process as defined in claim 9 wherein during the dissolving step the cellulosic material and the dilute hemicellulose-dissolving acid are heated to a temperature within the range of about 200° F. to about 300° F. at a pressure of about 5 psi to about 50 psi for a period of about two minutes to about ten minutes.
Claim 13
Dependent Claim 236 words
A process for the conversion of cellulosic material to fermentable sugars, the process consisting essentially of the following steps: obtaining a feedstock, at least a portion of which is a cellulosic material; dissolving at least a portion of the cellulosic material with a first dilute sulfuric acid having a concentration of from about 0.5% to about 2.0% sulfuric acid by volume at a temperature of from about 200° F. to about 300° F. at a pressure of about 5 psi to about 50 psi for a period of about two minutes to about ten minutes, thereby producing a hemicellulose-containing solution and leaving undissolved cellulosic material; separating the hemicellulose-containing solution from the undissolved cellulosic material; contacting the undissolved cellulosic material with concentrated sulfuric acid cooled to a temperature of about 30° F. to about 60° F. for a period of about one minute to about ten minutes, thereby producing a cellulose-containing solution and a solid residue; removing the solid residue from the cellulose-containing solution; precipitating cellulose from the cellulose-containing solution by diluting the cellulose-containing solution with methanol; and hydrolyzing the hemicellulose and the precipitated cellulose with a second dilute sulfuric acid having a concentration of about 0.5% to about 10% sulfuric acid by volume at a temperature of about 200° F. to about 400° F. at a pressure of about 15 psi to about 200 psi for a period of about two minutes to about ten minutes.
Claim 14
Dependent Claim 236 words
A process for the conversion of cellulosic material to fermentable sugars, the process consisting essentially of the following steps: obtaining a feedstock, at least a portion of which is a cellulosic material; dissolving at least a portion of the cellulosic material with a first dilute sulfuric acid having a concentration of from about 0.5% to about 2.0% sulfuric acid by volume at a temperature of from about 200° F. to about 300° F. at a pressure of about 5 psi to about 50 psi for a period of about two minutes to about ten minutes, thereby producing a hemicellulose-containing solution and leaving undissolved cellulosic material; separating the hemicellulose-containing solution from the undissolved cellulosic material; contacting the undissolved cellulosic material with concentrated sulfuric acid cooled to a temperature of about 30° F. to about 60° F. for a period of about one minute to about ten minutes, thereby producing a cellulose-containing solution and a solid residue; removing the solid residue from the cellulose-containing solution; precipitating cellulose from the cellulose-containing solution by diluting the cellulose-containing solution with methanol; and hydrolyzing the hemicellulose and the precipitated cellulose with a second dilute sulfuric acid having a concentration of about 0.5% to about 10% sulfuric acid by volume at a temperature of about 200° F. to about 400° F. at a pressure of about 15 psi to about 200 psi for a period of about two minutes to about ten minutes.
Claim 15
Dependent Claim 246 words
A process for the production of alcohol from cellulosic material, the process comprising the steps of: obtaining a feedstock, at least a portion of which is a cellulosic material; contacting the cellulosic material with concentrated delignifying acid said concentrated delignifying acid being in a liquid phase and having a temperature of less than about 60° F. and having a concentration of from about 60% to about 90% acid by volume, thereby producing a cellulose-containing solution and a solid residue; removing the solid residue from the cellulose-containing solution; precipitating cellulose from the cellulose-containing solution; hydrolyzing the precipitated cellulose with a dilute hydrolyzing acid, thereby producing fermentable sugars; introducing the fermentable sugars into a vessel; mixing yeast with the fermentable sugars and fermenting the fermentable sugars to produce alcohol and carbon dioxide; removing alcohol vapor and carbon dioxide from the vessel under a partial vacuum, said removal being aided by sparging a gas throughout the fermentable sugars in the vessel at a rate of about 0.01 to about 0.5 cubic feet per minute per gallon of fermentable sugars in the vessel; concentrating the alcohol vapor by passing the alcohol vapor and carbon dioxide through a distillation column under the partial vacuum while refluxing liquid alcohol through the distillation column, the vessel being in gaseous communication with the distillation column; and condensing the alcohol vapor which has passed through the distillation column, producing liquid alcohol and thereby creating at least a portion of the partial vacuum in the vessel.
Claim 16
Dependent Claim 246 words
A process for the production of alcohol from cellulosic material, the process comprising the steps of: obtaining a feedstock, at least a portion of which is a cellulosic material; contacting the cellulosic material with concentrated delignifying acid said concentrated delignifying acid being in a liquid phase and having a temperature of less than about 60° F. and having a concentration of from about 60% to about 90% acid by volume, thereby producing a cellulose-containing solution and a solid residue; removing the solid residue from the cellulose-containing solution; precipitating cellulose from the cellulose-containing solution; hydrolyzing the precipitated cellulose with a dilute hydrolyzing acid, thereby producing fermentable sugars; introducing the fermentable sugars into a vessel; mixing yeast with the fermentable sugars and fermenting the fermentable sugars to produce alcohol and carbon dioxide; removing alcohol vapor and carbon dioxide from the vessel under a partial vacuum, said removal being aided by sparging a gas throughout the fermentable sugars in the vessel at a rate of about 0.01 to about 0.5 cubic feet per minute per gallon of fermentable sugars in the vessel; concentrating the alcohol vapor by passing the alcohol vapor and carbon dioxide through a distillation column under the partial vacuum while refluxing liquid alcohol through the distillation column, the vessel being in gaseous communication with the distillation column; and condensing the alcohol vapor which has passed through the distillation column, producing liquid alcohol and thereby creating at least a portion of the partial vacuum in the vessel.

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1989-01-13 1989-07-15 1990-01-14 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1993-01-13 1993-07-15 1994-01-14 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1997-01-13 1997-07-15 1998-01-14 $7700.00 Window Closed / Lapsed

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