High efficiency organosolv saccharification process

Claim 2

In a process for the production of carbohydrate hydrolysates as sugars from a comminuted cellulosic material which can contain lignin by treating the material in a pressure vessel with a solvent mixture of acetone and water containing a small amount of an acidic compound at elevated temperatures to form reducing sugars in a liquor, the improvement which comprises: (a) providing mixtures of acetone and water containing greater than 70 volume percent acetone and the catalytic acidic compound as the solvent mixture in the pressure vessel at the elevated temperatures with the cellulosic material; (b) repeatedly treating the cellulosic material in the solvent mixture for a limited period of time at the elevated temperatures until the cellulosic material is at least partially dissolved and such that at least 90 percent of the solubilized sugars from the cellulosic material are recovered without degradation to non-sugars in the liquor; and (c) rapidly cooling the liquor as it is removed from the pressure vessel after each treatment, wherein the cellulosic material is treated on a batch or continuous basis in the pressure vessel using successive amounts of the solvent mixture thereby defining successive stages of treatment at the elevated temperatures, wherein less than 50 percent by weight of the cellulosic material is dissolved in each stage of treatment and wherein in each stage the cellulosic material is treated for a limited period of time in the pressure vessel and then the withdrawn liquor is rapidly cooled when removed from the pressure vessel so as to achieve the sugar recovery.

Claim 3

The process of claim 1 wherein the concentration of acetone in the acetone and water mixture is between 80 to 90 volume percent.

Claim 4

The process of claim 2 wherein the acidic compound is sulfuric acidic and the concentration is less than 2 percent per weight of the acetone-water mixture.

Claim 5

The process of claim 3 wherein the acidic compound is hydrochloric acid and the concentration is less than 1 percent per weight of the acetone-water mixture.

Claim 6

The process of claim 1 wherein the elevated temperatures are between 145° C. to 230° C.

Claim 7

The process of claim 1 wherein the addition the liquor is further hydrolyzed at elevated temperatures and dilute acid solutions to produce essentially monomeric sugars.

Claim 8

The process of claim 1 wherein the liquor is subjected to distillation whereby pentoses are volatilized from the liquor.

Claim 9

The process of claims 1, 6 or 7 wherein the aqueous solution contains dissolved sugars in excess of 15 percent solids.

Claim 10

The process of claim 3 or 4 wherein the concentration of the acid is between 0.10 Normal and 0.001 Normal with respect to the acetone-water mixture.

Claim 11

The process of claim 1 wherein the volatiles in the liquor are distilled at reduced pressures to leave an aqueous solution in which lignin is precipitated and is separated.

Claim 12

In a process for the production of carbohydrate hydrolysates as sugars and lignin from comminuted cellulosic material which can contain lignin by treating the material in a pressure vessel with a solvent mixture of acetone and water containing a small amount of an acidic compound at elevated temperatures to solubilize any lignin and to form reducing sugars in a liquor, the improvement which comprises: (a) providing mixtures of acetone and water containing greater than 70 volume percent acetone and the catalytic acid compound as the solvent mixture in the pressure vessel at the elevated temperatures with the cellulosic material; (b) repeatedly treating the cellulosic material in the solvent mixture for limited periods of time at the elevated temperatures until the cellulosic material is at least partially dissolved and such that at least 90 percent of the solubilized sugars from the cellulosic material are recovered without degradation to non-sugars wherein the carbohydrates in the cellulosic material are dissolved and hydrolyzed partially or substantially completely; (c) continuously removing the liquor from the pressure vessel; (d) rapidly cooling the liquor by controlled flash evaporation of acetone to form a residual aqueous solution after each treatment, wherein the cellulosic material is treated in the pressure vessel using successive amounts of the solvent mixture thereby defining successive stages of treatment at the elevated temperatures, wherein less than 50 percent of the cellulosic material is dissolved in each stage and wherein in each stage the cellulosic material is treated for a limited period of time in the pressure vessel and then the withdrawn liquor is rapidly cooled when removed from the pressure vessel so as to achieve the sugar recovery.

Claim 13

In a process for the production of carbohydrate hydrolysates as sugars and lignin from comminuted cellulosic material which can contain lignin by treating the material in a pressure vessel with a solvent mixture of acetone and water containing a small amount of an acidic compound at elevated temperatures to solubilize any lignin and to form reducing sugars in a liquor, the improvement which comprises: (a) providing mixtures of acetone and water containing greater than 70 volume percent acetone and the catalytic acid compound as the solvent mixture in the pressure vessel at the elevated temperatures with the cellulosic material; (b) repeatedly treating the cellulosic material in the solvent mixture for limited periods of time at the elevated temperatures until the cellulosic material is at least partially dissolved and such that at least 90 percent of the solubilized sugars from the cellulosic material are recovered without degradation to non-sugars wherein the carbohydrates in the cellulosic material are dissolved and hydrolyzed partially or substantially completely; (c) continuously removing the liquor from the pressure vessel; (d) rapidly cooling the liquor by controlled flash evaporation of acetone to form a residual aqueous solution after each treatment, wherein the cellulosic material is treated in the pressure vessel using successive amounts of the solvent mixture thereby defining successive stages of treatment at the elevated temperatures, wherein less than 50 percent of the cellulosic material is dissolved in each stage and wherein in each stage the cellulosic material is treated for a limited period of time in the pressure vessel and then the withdrawn liquor is rapidly cooled when removed from the pressure vessel so as to achieve the sugar recovery.

Claim 14

The process of claim 11 wherein the cellulosic material is lignocellulosic and wherein the volatiles in the liquor are distilled at reduced pressure to leave the residual aqueous solution and precipitated lignin and wherein the residual aqueous solution is neutralized prior to recovering the sugars.

Claim 15

The process of claim 11 wherein the concentration of acetone and water is between 80 to 90 percent.

Claim 16

The process of claim 11 wherein the pentose sugars are volatilized from the residual aqueous solution as acetone complexes to separate them from the hexose sugars.

Claim 17

The process of claim 14 wherein the sugar-acetone complexes are each broken by contacting the complexes with aqueous acid at elevated temperature.

Claim 18

The process of claim 15 wherein the complexes are continuously treated with aqueous acid at elevated temperature until sugar dehydration products are formed.

Claim 19

The method of claim 11 wherein the cellulosic material is treated in a batch or continuous manner and the recovered solvent fractions are worked up separately or in unison.

Claim 20

The method of claim 11 wherein hydrolysis of the cellulosic material is stopped at a point where essentially pure crystalline cellulose is recovered as solid residue from the reactor.