System and method 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 biochemical production. In particular, after saccharification and prior to a sugar conversion process, a sugar/carbohydrate stream is removed from a saccharified stream. The sugar/carbohydrate stream includes a desired Dextrose Equivalent (DE) where DE describes the degree of conversion of starch to dextrose can be produced, with the such sugar stream being available for biochemical 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 and/or fiber. Sugar stream production occurs on the front end of the system and method.
1 . A system for producing a sugar stream, the system comprising:
a slurry tank in which ground grain particles mix with a liquid to produce a slurry including starch;
a liquefaction system that receives the slurry and provides a liquefied starch solution, and whereat the starch begins to convert to oligosaccharides;
a solid/liquid separation device that is situated after the liquefaction system and that receives the liquefied starch solution, wherein the solid/liquid separation device separates out a solids portion from the liquefied starch solution including the starch;
a saccharification system that is situated after the solid/liquid separation device and that receives at least a portion of the liquefied starch solution therefrom, wherein the saccharification system converts the oligosaccharides to simple sugars thereby producing a saccharified stream including the simple sugars; and
a first separation device that receives and separates the saccharified stream into a first solids portion and a first liquid portion including the simple sugars, wherein the first liquid portion defines a sugar stream having a dextrose equivalent of at least 20 DE and a total unfermentable solids fraction that is less than or equal to 30% of the total solids content, the first separation device situated prior to any sugar conversion device that receives and processes the simple sugars to produce a biochemical.
2 . The system of claim 1 further comprising a biochemical conversion device that receives the first solids portion and the separated solids portion from the solid/liquid separation device.
3 . The system of claim 2 wherein the biochemical conversion device comprises a fermentation device and a distillation device to produce an alcohol.
4 . The system of claim 1 further comprising, after the slurry tank and prior to the liquefaction system, a grinding device that receives and grinds the slurry.
5 . The system of claim 4 further comprising, after the slurry tank and prior to the grinding device, a liquid/solid separation device that receives and separates the slurry into a solids portion and a liquid portion including the starch, wherein the grinding device receives and grinds the solids portion to produce a ground solids portion, and wherein the liquefaction system receives the ground solids portion and the separated liquid portion, which together define the slurry.
6 . The system of claim 1 further comprising a sugar conversion device that receives the sugar stream to produce a biochemical.
7 . The system of claim 6 wherein the sugar conversion device is a fermenter, or a catalytic or chemical reactor.