Systems and methods for producing a sugar stream
An improved dry grind system and method for producing a sugar stream from grains or similar carbohydrate sources and/or residues, such as for biofuel production. In particular, a sugar/carbohydrate stream, which includes a desired Dextrose Equivalent (DE) where DE describes the degree of conversion of starch to dextrose (aka glucose) and/or has had removed therefrom an undesirable amount of unfermentable components, can be produced after saccharification and prior to fermentation (or other sugar conversion process), with such sugar stream being available for biofuel production, e.g., alcohol production, or other processes. In addition, the systems and methods also can involve the removal of certain grain components, e.g., corn kernel components, including protein, oil and/or fiber, prior to fermentation or other conversion systems. In other words, sugar stream production and/or grain component separation occurs on the front end of the system and method.
1. A method for producing a sugar stream comprising:
mixing ground grain and/or grain components with a liquid to produce a slurry including starch and unfermentable components;
subjecting the slurry to liquefaction followed by saccharification to convert the starch to simple sugars and produce a stream including the simple sugars and unfermentable components; and
directly after saccharification, separating the stream, via particle sizes with a paddle screen, into only a solids portion including unfermentable components and a liquid portion including the simple sugars, followed by separating out free oil from the liquid portion, via density with a centrifuge, followed by separating out residual protein from the liquid portion, via density with a centrifuge, wherein the liquid portion, after separating out the residual protein, has a dextrose equivalent of at least 20 D.E. and a total unfermentable solids fraction that is less than or equal to 30% of the total solids content, and thereafter microfiltering the liquid portion to filter out additional insoluble components, via particle sizes, wherein the liquid portion, after microfiltering, defines a sugar stream that remains separate from the solids portion and that has a total unfermentable solids fraction that is less than or equal to 10% of the totals solids content.
2. A method for producing a sugar stream comprising:
mixing ground grain and/or grain components with a liquid to produce a slurry including starch and unfermentable components;
subjecting the slurry to liquefaction followed by saccharification to convert the starch to simple sugars and produce a stream including the simple sugars and unfermentable components;
directly after saccharification, separating the stream, via particle sizes with a paddle screen, into only a solids portion including unfermentable components and a liquid portion including the simple sugars, followed by separating out free oil from the liquid portion, via density with a centrifuge, followed by separating out residual protein from the liquid portion, via density with a centrifuge, wherein the liquid portion, after separating out the residual protein, has a dextrose equivalent of at least 20 D.E. and a total unfermentable solids fraction that is less than or equal to 30% of the total solids content, and thereafter microfiltering the liquid portion to filter out additional insoluble components, via particle sizes, wherein the liquid portion, after microfiltering, defines a sugar stream that remains separate from the solids portion and that has a total unfermentable solids fraction that is less than or equal to 10% of the totals solids content; and
subjecting the sugar stream, which remains separate from the solids portion, to a sugar utilization process to produce a biofuel and/or biochemical.
3. The method of claim 2 further comprising grinding grain and/or grain components into the ground grain and/or grain components.
4. The method of claim 2 wherein subjecting the sugar stream to a sugar utilization process comprises subjecting the sugar stream to fermentation to produce the biofuel and/or biochemical.
5. The method of claim 4 further comprising recovering a fermentation agent used in fermentation to produce the biofuel and/or biochemical.
6. The method of claim 2 further comprising recovering the free oil to yield an oil co-product.
7. The method of claim 2 wherein the unfermentable components of the solids portion includes protein and further comprising separating and recovering the protein pre-fermentation to yield a protein co-product.
8. The method of claim 2 wherein the unfermentable components of the solids portion includes fiber and further comprising recovering the fiber to yield a fiber co-product.
9. The method of claim 2 wherein after mixing the ground grain and/or grain component with the liquid to produce the slurry including starch and unfermentable components and prior to subjecting the slurry to liquefaction followed by saccharification, milling the slurry of ground grain and/or grain component.
10. The method of claim 2 wherein the liquid portion, after separating out the residual protein, has a dextrose equivalent of at least 40 D.E.
11. The method of claim 2 wherein the liquid portion, after separating out the residual protein, has a total unfermentable solids fraction that is less than or equal to 20% of the total solids content.
12. The method of claim 2 wherein the liquid portion, after microfiltering, defines a sugar stream having a total unfermentable solids fraction that is less than 5% of the total solids content.
13. The method of claim 2 further comprising separating the separated solids portion into a second solids portion including unfermentable components and a second liquid portion including simple sugars.
14. The method of claim 2 wherein the grain and/or grain component are one or more selected from the group consisting of corn, wheat, barley, sorghum, rye, rice, oats, sugar cane, tapioca, and cassava.