Remediation of toxins in biorefinery process streams

1. A process for remediating mycotoxin in one or more biorefinery process streams, wherein the process comprises:

introducing one or more treatment compounds into at least one biorefinery process stream to form a treated biorefinery process stream, wherein the at least one biorefinery process stream is chosen from thin stillage, syrup and combinations thereof, wherein the one or more treatment compounds comprises one or more sulfur-containing compounds, wherein the at least one biorefinery process stream comprises one or more mycotoxins, wherein the one or more treatment compounds react with the one or more mycotoxins in the at least one biorefinery process stream to form the treated biorefinery process stream, and wherein the treated biorefinery process stream is less toxic than the at least one biorefinery process stream.

2. The process of claim 1 , wherein the at least one biorefinery process stream is produced in a grain-to-ethanol conversion process that also includes the steps of:

i. milling grain to provide a milled grain;

ii. mixing the milled grain with water to form a slurry;

iii. saccharifying the slurry;

iv. fermenting the saccharified slurry with a yeast to produce a beer;

v. separating the beer to produce an ethanol stream and whole stillage; and

vi. separating the whole stillage into thin stillage and wet cake; and

vii. concentrating thin stillage into syrup.

3. The process of claim 2 , wherein the one or more treatment compounds react with the one or more mycotoxins in the at least one biorefinery process stream for a dwell time from 1 hour to 24 hours.

4. The process of claim 1 , wherein the at least one biorefinery process stream is a syrup stream.

5. The process of claim 1 , wherein the one or more mycotoxins comprises at least one of zearalenone, deoxynivalenol, and fumonisin.

6. The process of claim 1 , wherein the treatment compound is chosen from a sulfate, a sulfite, a bisulfite, a metabisulfite and combinations thereof.

7. The process of claim 1 , wherein the treatment compound is chosen from ammonium bisulfite, potassium bisulfite, sodium bisulfite and combinations thereof.

8. The process of claim 1 , wherein the treatment compound amount is between 0.05% to about 5% weight of the at least one biorefinery process stream.

9. The process of claim 1 , wherein the introducing the one or more treatment compounds into the at least one biorefinery process stream occurs while the at least one biorefinery process stream is at temperatures from 30° C. to 120° C.

10. The process of claim 1 , wherein the at least one or more biorefinery process stream comprises 5 to 60% solids by weight.

11. The process of claim 1 , wherein the one or more mycotoxins comprises deoxynivalenol.

12. The process of claim 11 , wherein the one or more treatment compounds react with the deoxynivalenol in the at least one biorefinery process stream to form deoxynivalenol sulfonate wherein the deoxynivalenol the treated biorefinery process stream is reduced by 30% or more as compared to the deoxynivalenol in the at least one biorefinery process stream.

13. The process of claim 1 , wherein the one or more mycotoxins in the treated biorefinery process stream is less than 5 ppm.

14. The process of claim 1 , wherein the one or more treatment compounds is introduced into the at least one biorefinery process stream in a tank.

15. The process of claim 1 , wherein the treated biorefinery process stream is combined with wet cake.

16. The process of claim 15 , wherein the treated biorefinery process stream combined with wet cake is dried to form dried distillers grain with solubles (DDGS).

17. The process of claim 1 , wherein the introducing the one or more treatment compounds into the at least one biorefinery process stream occurs while the at least one biorefinery process stream is at temperatures from 55° C. to 120° C.

18. The process of claim 1 , wherein the one or more treatment compounds are introduced into the thin stillage stream, wherein a portion of the thin stillage stream is recycled to fermentation, saccharification or both before introducing one or more treatment compounds into the thin stillage stream.