Method for recovering acid from an acid-sugar hydrolyzate
AssigneeNorth Carolina State University
InventorIrving S. Goldstein
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Abstract
The invention discloses a method for separating acid from an acid-sugar hydrolyzate in an electrodialysis apparatus comprising the steps of continuously passing the hydrolyzate through a diluate compartment of the electrodialysis apparatus, continuously passing a carrier fluid through a concentrate compartment of the electrodialysis apparatus, and maintaining a current between the anode-cathode pair of the electrodialysis apparatus that forces the anions and cations of the acid to migrate from the diluate compartment into a concentrate compartment.
Claims39
A method for recovering the acid component of an acid-sugar hydrolyzate in an electrodialysis apparatus including at least one acid concentrate compartment, at least one acid concentrate compartment, at least one diluate compartment and an anode-cathode pair across said electrodialysis apparatus, said method comprising the steps of:
- (a) continuously passing said acid-sugar hydrolyzate through said diluate compartment, said hydrolyzate including cellulose hydrolysis products and at least one of the group consisting of hydrochloric acid having an initial concentration of between 14 and 17 percent and sulfuric acid having an initial concentration of between 9 and 11 percent;
- (b) continuously passing a carrier fluid through said acid concentrate compartment;
- and
- (c) maintaining a current between said anode-cathode pair which forces anions and cations of said acid component to separate from said hydrolyzate and migrate into said concentrate within said at least one acid concentrate compartment, with the proviso that if hydrochloric acid is the acid passed through the diluate compartment in step (a), the current efficiency resulting from the maintenance of said current is between 0.45 and 0.75 Moles/F/Cell.
A method for recovering the acid component of an acid-sugar hydrolyzate in an electrodialysis apparatus including at least one acid concentrate compartment, at least one diluate compartment, and an anode-cathode pair for providing current across said electrodialysis apparatus, said method comprising the steps of:
- (a) continuously passing said acid-sugar hydrolyzate through said diluate compartment, said hydrolyzate including cellulose hydrolysis products and at least one of the group consisting of hydrochloric acid and sulfuric acid;
- (b) continuously passing a carrier fluid through said acid concentrate compartment;
- (c) maintaining a current between said anode-cathode pair which forces anions and cations of said acid component to separate from said hydrolyzate and migrate into said concentrate within said at least one acid concentrate compartments;
- and
- (d) ceasing steps (a)-(c) when acid concentration of said concentrate reaches a predetermined level, said predetermined level being between 15 and 25 percent for recovery of hydrochloric acid and being between 18 and 28 percent for recovery of sulfuric acid.
A method for recovering the acid component of an acid-sugar hydrolyzate in an electrodialysis apparatus including at least one acid concentrate compartment, at least one diluate compartment, and an anode and cathode pair for providing electric current across said electrodialysis apparatus, said method comprising the steps of:
- (a) continuously passing said acid-sugar hydrolyzate through said diluate compartment, said hydrolyzate including hydrochloric acid in concentration of between 14 and 17 percent and sugar concentration of between 3.25 and 4.25 parts sugar to one part hydrochloric acid;
- (b) continuously passing a hydrochloric acid solution through said acid concentration compartment;
- and
- (c) maintaining a current between said anode-cathode pair which forces anions and cations of said acid component to separate from said hydrolyzate and migrate into said concentrate within said at least one acid concentrate compartments, said current producing a current efficiency across said electrodialysis apparatus of between 0.57 and 0.63 Moles/F/Cell and resulting in a power/acid transport ratio of between 0.47 and 0.53 KWhr/lbHCl.
Dependencies are inferred from the claim text.