Method and system for removing insoluble solids mid-evaporation from a corn dry milling process
The present invention relates generally to corn dry-milling, and more specifically, to a method and system for removing insoluble solids mid-evaporation in a corn (or similar carbohydrate-containing grain) dry milling process for making alcohol, such as ethanol, and/or other biofuels/biochemicals. In one example, the method for removing residual insoluble solids in a grain dry milling process includes separating a whole stillage byproduct into an insoluble solids portion and a solubles portion, which includes residual insoluble solids. Then, the solubles portion is subjected to a first evaporation, via one or more evaporators, to remove liquid from the solubles portion to define a concentrated solubles portion. After the first evaporation, the residual insoluble solids are separated from the concentrated solubles portion. And thereafter, the concentrated solubles portion is subjected to a second evaporation, via one or more evaporators, to remove additional liquid from the concentrated solubles portion.
1. A method for removing residual insoluble solids in a grain dry milling process, the method comprising:
separating a whole stillage byproduct into an insoluble solids portion and a solubles portion, which includes residual insoluble solids;
subjecting the solubles portion to a first evaporation, via one or more first evaporators, to remove liquid from the solubles portion to define a concentrated solubles portion;
after the first evaporation, separating the concentrated solubles portion into only a first stream and a second stream, wherein the first stream includes residual insoluble solids, and wherein the second stream includes free oil and soluble solids;
thereafter, separating the second stream into a free oil stream and a soluble solids stream, wherein the free oil stream defines an oil product; and
thereafter, subjecting the soluble solids stream to a second evaporation, via one or more second evaporators, which are different than the one or more first evaporators, to remove additional liquid from the soluble solids stream,
wherein the first stream including the residual insoluble solids is not subjected to the second evaporation.
2. The method of claim 1 further comprising, prior to separating the concentrated solubles portion into the first stream and the second stream, adding a flocculent and/or surfactant to the concentrated solubles portion.
3. The method of claim 1 further comprising, prior to the first evaporation, separating a solids portion, including protein, from the soluble solids portion, including residual insoluble solids.
4. The method of claim 3 further comprising, prior to separating the concentrated solubles portion into the first stream, including the residual insoluble solids, and the second stream, adding a flocculent and/or surfactant to the concentrated solubles portion.
5. The method of claim 3 further comprising drying the solids portion, including the protein, to define a grain meal that includes at least 40 wt % protein on a dry basis.
6. The method of claim 3 further comprising dewatering the solids portion, including the protein, and drying the dewatered solids portion, including the protein, to define a grain meal that includes at least 40 wt % protein on a dry basis.
7. A method for removing residual insoluble solids in a grain dry milling process, the method comprising:
separating a whole stillage byproduct into an insoluble solids portion and a solubles portion, which includes residual insoluble solids;
subjecting the solubles portion to a first evaporation, via one or more first evaporators, to remove liquid from the solubles portion to define a concentrated solubles portion;
after the first evaporation, separating the concentrated solubles portion into only a first stream and a second stream, wherein the first stream includes free oil and defines an oil product, and wherein the second stream includes the residual insoluble solids and soluble solids;
thereafter, separating the second stream into a residual insoluble solids stream and a soluble solids stream; and
thereafter, subjecting the soluble solids stream to a second evaporation, via one or more second evaporators, which are different than the one or more first evaporators, to remove additional liquid from the soluble solids stream,
wherein the residual insoluble solids stream is not subjected to the second evaporation.
8. The method of claim 7 further comprising, prior to separating the second stream into the residual insoluble solids stream and the soluble solids stream, adding a flocculent and/or surfactant to the second stream.
9. The method of claim 7 further comprising, prior to the first evaporation, separating a solids portion, including protein, from the soluble solids portion, including residual insoluble solids.
10. The method of claim 9 further comprising, prior to separating the second stream into the residual insoluble solids stream and the soluble solids stream, adding a flocculent and/or surfactant to the second stream.
11. The method of claim 9 further comprising drying the solids portion, including the protein, to define a grain meal that includes at least 40 wt % protein on a dry basis.
12. The method of claim 9 further comprising:
drying the solids portion, including the protein, to define a dewatered solids portion, including the protein; and
drying the dewatered solids portion, including the protein, to define a grain meal that includes at least 40 wt % protein on a dry basis.