PROCESS FOR THE RECOVERY OF HCL FROM A DILUTE SOLUTION THEREOF
The invention provides a process for the recovery of HCl from a dilute solution thereof, comprising: a) bringing a dilute aqueous HCl solution into contact with a substantially immiscible extractant, said extractant comprising: 1) an oil soluble amine which amine is substantially water insoluble both in free and in salt form; 2) an oil soluble organic acid which acid is substantially water insoluble both in free and in salt form; and 3) a solvent for the amine and organic acid; whereupon HCl selectively transfers to said extractant to form an HCl-carrying extractant; and b) treating said HCl-carrying extractant to obtain gaseous HCl.
1 . A process for the recovery of gaseous HCl from a dilute solution thereof, comprising:
a) bringing a dilute aqueous HCl solution Into contact with a substantially Immiscible extractant, said extractant comprising;
1) an oil soluble amine, which amine is substantially water Insoluble both in free and in salt form;
2) an oil soluble organic acid, which acid is substantially water Insoluble both in free and In salt form; and
3) a solvent for the amine and organic acid;
whereupon HCl selectively transfers to said extractant to form an HCl-carrying extractant; and
b) distilling MCI from said HCl-carrying extractant to form gaseous HCl and HCl-depleted extractant.
2 . A process according to claim 1 , further comprising
c) absorbing the gaseous HCl produced in step b In a part of said dilute solution or in water, to provide hydrochloric acid of a higher concentration than that of the HCl In said dilute aqueous HCl solution of step a.
3 . A process according to claim 1 , wherein said distilling comprises heating.
4 . A process according to claim 3 , wherein said heating is to a temperature of up to 260° C.
5 . A process according to claim 4 , wherein said heating is to a temperature of up to 200° C.
6 . A process according to claim 1 , wherein said distilling comprises introducing a stream of an Inert gas for conveying the MCI from said extraotant phase.
7 . A process according to claim 1 , wherein said distilling comprises a combination of heating and Introducing a stream of an inert gas.
8 . A process according to claim 6 , wherein said inert gas is a superheated steam.
9 . A process according to claim 1 , wherein said extractant is characterized by a pHhn of less than 3.
10 . A process for the production of carbohydrates, comprising:
a) providing a polysaccharide
b) hydrolyzing said polysaccharide in an HCl-containing hydrolysis medium to form a carbohydrate-containing, dilute aqueous HCl solution;
a) bringing said dilute aqueous HCl solution Into contact with a substantially immiscible extractant, said extractant comprising;
1) an oil-soluble amine, which amine is substantially water-insoluble, in both free and salt forms;
2) an oil-soluble organic acid, which acid is substantially water-insoluble, in both free and salt forms; and
3) a solvent for the amine and organic acid,
whereupon HCl selectively transfers to said extractant to form an HCl-carrying extractant and an HCl-depleted carbohydrate-containing solution;
d) distilling HCl from said HCl-carrying extractant to form gaseous 1101 and HCl-depleted extractant and
e) using said gaseous HCl for hydrolysis of a polysaccharide.
11 . A process according to claim 10 wherein said polysaccharide is provided in a polysaccharide-containing material.
12 . A process according to claim 11 further comprising a step of comminuting said material to form an aqueous slurry.
13 . A process according to claim 11 , wherein said polysaccharide-containing material is a lignocellulosic material
14 . A process according to claim 10 , wherein said HCl-depleted carbohydrate-containing solution provides a feedstock for fermentation to generate a fermentation product.
15 . A process according to claim 10 , wherein said fermentation product is ethanol.
16 . A process) according to claim 10 , wherein the amount of HCl in said gaseous HCl is at least 70% of the amount of HCl in said dilute aqueous HCl solution.
17 . A process according to claim 11 , wherein at least 70% of the polysaccharide in said polysaccharide-containing material is hydrolyzed to carbohydrates,
18 . A process according to claim 10 , wherein carbohydrate concentration in said HCl-depleted carbohydrate-containing solution is at least 15%.
19 . A process according to claim 10 , wherein said polysaccharide is provided in a polysaccharide-containing material, said process further comprising a step of comminuting said material to form a slurry, wherein said provided polysaccharide material has not been dried prior to said forming of said slurry.
20 . A process according to claim 19 , further comprising a step wherein said gaseous HCl is directly absorbed into a slurry of a comminuted polysaccharide-containing material to generate said HCl-containing hydrolysis medium.
21 . A process according to claim 10 , wherein said extractant is characterized by a pHhn of less than 3.