Method of treating ethanol production byproducts
View Patent ↗A method of treating ethanol production byproduct is provided by treating wet distillers grain or stillage with a solution containing at least one α-hydroxysulfonic acid to produce at least one fermentable sugar containing product. Fermentable sugar useful for the production of biofuels or ethanol can be produced from such methods. The α-hydroxysulfonic acid can be easily removed from the product and recycled.
1. A method of treating ethanol production byproduct comprising: (a) providing a wet distillers grain containing moisture; (b) contacting the wet distillers grain with a solution comprising at least one α-hydroxysulfonic acid thereby hydrolyzing the wet distillers grain to produce at least one fermentable sugar containing product; and (c) removing at least a portion of said α-hydroxysulfonic acid in its component form from said fermentable sugar containing product by a process consisting of heating and/or reducing pressure to produce an acid-removed product containing at least one fermentable sugar.
2. The method of claim 1 , further comprising recycling the removed α-hydroxysulfonic acid obtained in step (c) to step (b) as components or in its recombined form.
3. The method of claim 1 , further comprising fermenting said acid-removed product to produce at least one alcohol.
4. The method of claim 1 , further comprising hydrolyzing said acid-removed product to produce a hydrolyzed product.
5. The method of claim 4 , further comprising fermenting said hydrolyzed product to produce at least one alcohol.
6. The method of claim 1 , wherein said α-hydroxysulfonic acid is present in an amount of 1% wt. to 55% wt., based on the solution.
7. The method of claim 1 , wherein said α-hydroxysulfonic acid is produced from a carbonyl compound or a precursor to a carbonyl compound combined with sulfur dioxide and water.
8. The method of claim 1 , wherein said α-hydroxysulfonic acid is in-situ generated.
9. The method of claim 1 , wherein step (b) is carried out at a temperature within the range of 50° C. to 150° C. and a pressure within the range of 1 barg to 10 barg.
10. A method comprising: (a) providing grain; (b) grinding said grain to produce ground grain; (c) treating said ground grain to produce a fermentable sugar mixture; (d) fermenting the fermentable sugar mixture to produce a fermented product containing ethanol, solids and water; (e) separating said fermented product to produce ethanol and stillage containing water; (f) contacting at least a portion of said stillage containing water with a solution comprising at least one α-hydroxysulfonic acid thereby hydrolyzing said stillage to produce at least one fermentable sugar containing product; and (g) removing at least a portion of said α-hydroxysulfonic acid in its component form from said fermentable sugar containing product by a process consisting of heating and/or reducing pressure to produce an acid-removed product containing at least one fermentable sugar.
11. The method of claim 10 , further comprising recycling the removed α-hydroxysulfonic acid obtained in step (g) to step (f) as components or in its recombined form.
12. The method of claim 10 , further comprising fermenting said acid-removed product to produce at least one alcohol.
13. The method of claim 10 , further comprising hydrolyzing said acid-removed product to produce a hydrolyzed product.
14. The method of claim 13 , further comprising fermenting said hydrolyzed product to produce at least one alcohol.
15. The method of claim 10 , wherein said α-hydroxysulfonic acid is present in an amount of 1% wt. to 55% wt., based on the solution.
16. The method of claim 10 , wherein said α-hydroxysulfonic acid is produced from a carbonyl compound or a precursor to a carbonyl compound combined with sulfur dioxide and water.
17. The method of claim 10 , wherein said α-hydroxysulfonic acid is in-situ generated.
18. The method of claim 10 , wherein step (f) is carried out at a temperature within the range of 50° C. to 150° C. and a pressure within the range of 1 barg to 10 barg.
19. A method comprising: (a) providing grain; (b) grinding said grain to produce ground grain; (c) treating said ground grain to produce fermentable sugar mixture; (d) fermenting said fermentable sugar mixture to produce a fermented product containing ethanol, solids and water; (e) separating said fermented product to produce ethanol and stillage; (f) separating said stillage to produce thin stillage and wet distillers grain containing moisture; and (g) contacting at least a portion of said wet distillers grain containing moisture with a solution comprising at least one α-hydroxysulfonic acid thereby hydrolyzing said wet distillers grain to produce at least one fermentable sugar containing product; and (h) removing at least a portion of said α-hydroxysulfonic acid in its component form from said fermentable sugar containing product by a process consisting of heating and/or reducing pressure to produce an acid-removed product containing at least one fermentable sugar.
20. The method of claim 19 , further comprising recycling the removed α-hydroxysulfonic acid obtained in step (h) to step (g) as components or in its recombined form.
21. The method of claim 19 , further comprising fermenting said acid-removed product to produce at least one alcohol.
22. The method of claim 19 , further comprising hydrolyzing said acid-removed product to produce a hydrolyzed product.
23. The method of claim 22 , further comprising fermenting said hydrolyzed product to produce at least one alcohol.
24. The method of claim 19 , wherein said α-hydroxysulfonic acid is present in an amount of 1% wt. to 55% wt., based on the solution.
25. The method of claim 19 , wherein said α-hydroxysulfonic acid is produced from a carbonyl compound or a precursor to a carbonyl compound combined with sulfur dioxide and water.
26. The method of claim 19 , wherein said α-hydroxysulfonic acid is in-situ generated.
27. The method of claim 19 , wherein step (g) is carried out at a temperature within the range of 50° C. to about 150° C. and a pressure within the range of 1 barg to 10 barg.