Process for the production of alcohol
First Claim
1. A process for the production of a residue containing sugars from a cellulosic material, said process comprising the steps of:
- (i) hydrolyzing said cellulosic material with an aqueous acid to produce a hydrolysate;
(ii) extracting acid and water from said hydrolysate with a water-miscible organic extraction solvent to yield (a) a first aqueous acidic solution containing said extraction solvent and (b) the residue containing sugars;
(iii) evaporating said extraction solvent from said first solution to yield (a) a second aqueous acid solution containing no more than 10% wt. of said extraction solvent and (b) gaseous extraction solvent;
(iv) condensing said gaseous extraction solvent for recycling; and
, optionally,(v) concentrating said second aqueous acid solution for recycling;
wherein said extraction solvent is liquid at the temperature and pressure of step (ii), has a boiling point of from 25 to 60°
C. at a pressure in the range 1 to 8 bar, comprises a solvent having a boiling point at 1 bar of below 20°
C., and is such that water-soluble oligosaccharides are precipitated from solution by its addition in step (ii).
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Abstract
The invention provides a process for producing alcohol from a cellulosic material, said process comprising the steps of: (i) hydrolyzing said cellulosic material with an aqueous acid to produce a hydrolysate; (ii) extracting acid and water from said hydrolysate with a water-miscible organic extraction solvent to yield (a) a first aqueous acidic solution containing said extraction solvent and (b) a residue containing sugars, —(iii) subjecting said residue to an oligosaccharide cleavage reaction to yield an aqueous solution of fermentable sugars; (iv) fermenting said fermentable sugars and distilling alcohol from the resulting fermented mixture; (v) evaporating said extraction solvent from said first solution to yield (a) a second aqueous acid solution containing no more than 10% wt., preferably no more than 5% wt., of said extraction solvent and (b) gaseous extraction solvent; (vi) condensing said gaseous extraction solvent for recycling; and, optionally, (vii) concentrating said second aqueous acid solution for recycling; wherein said extraction solvent is liquid at the temperature and pressure of step (ii), has a boiling point of from 25 to 60° C. at a pressure in the range 1 to 8 bar, and is such that water-soluble oligosaccharides are precipitated from solution by its addition in step (ii).
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Citations
17 Claims
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1. A process for the production of a residue containing sugars from a cellulosic material, said process comprising the steps of:
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(i) hydrolyzing said cellulosic material with an aqueous acid to produce a hydrolysate; (ii) extracting acid and water from said hydrolysate with a water-miscible organic extraction solvent to yield (a) a first aqueous acidic solution containing said extraction solvent and (b) the residue containing sugars; (iii) evaporating said extraction solvent from said first solution to yield (a) a second aqueous acid solution containing no more than 10% wt. of said extraction solvent and (b) gaseous extraction solvent; (iv) condensing said gaseous extraction solvent for recycling; and
, optionally,(v) concentrating said second aqueous acid solution for recycling; wherein said extraction solvent is liquid at the temperature and pressure of step (ii), has a boiling point of from 25 to 60°
C. at a pressure in the range 1 to 8 bar, comprises a solvent having a boiling point at 1 bar of below 20°
C., and is such that water-soluble oligosaccharides are precipitated from solution by its addition in step (ii). - View Dependent Claims (2, 3, 4, 8, 9, 10, 15, 16, 17)
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5. A process for the production of a residue containing sugars from a cellulosic material, said process comprising the steps of:
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(i) hydrolyzing said cellulosic material with an aqueous acid to produce a hydrolysate; (ii) extracting acid and water from said hydrolysate with a water-miscible organic extraction solvent comprising a C2-3 ether to yield (a) a first aqueous acidic solution containing said extraction solvent and (b) the residue containing sugars; (iii) evaporating said extraction solvent from said first solution to yield (a) a second aqueous acid solution containing no more than 10% wt. of said extraction solvent and (b) gaseous extraction solvent; (iv) condensing said gaseous extraction solvent for recycling; and
, optionally,(v) concentrating said second aqueous acid solution for recycling; wherein said extraction solvent is liquid at the temperature and pressure of step (ii) and is such that water-soluble oligosaccharides are precipitated from solution by its addition in step (ii). - View Dependent Claims (6, 7)
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11. A process for the production of a residue containing sugars from a cellulosic material, said process comprising the steps of:
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(i) hydrolyzing said cellulosic material with an aqueous acid to produce a hydrolysate; (ii) extracting acid and water from said hydrolysate with a water-miscible organic extraction solvent to yield (a) a first aqueous acidic solution containing said extraction solvent and (b) the residue containing sugars; (iii) evaporating said extraction solvent from said first solution to yield (a) a second aqueous acid solution containing no more than 10% wt. of said extraction solvent and (b) gaseous extraction solvent; (iv) condensing said gaseous extraction solvent for recycling; and
, optionally,(v) concentrating said second aqueous acid solution for recycling; wherein said extraction solvent is liquid at the temperature and pressure of step (ii), has a boiling point of from 25 to 60°
C. at a pressure in the range 1 to 8 bar, and is such that water-soluble oligosaccharides are precipitated from solution by its addition in step (ii), wherein extraction step (ii) is performed at a temperature within 15°
C. and a pressure within 1 bar of the temperature and pressure of hydrolysis step (i), wherein evaporation step (iii) is performed at a temperature within 15°
C. and a pressure within 5 bar of the temperature and pressure of extraction step (ii), and wherein condensation step (iv) is performed at a temperature within 15°
C. and a pressure within 1 bar of the temperature and pressure of extraction step (ii). - View Dependent Claims (12, 13, 14)
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Specification