Processes for recovering products from a corn fermentation mash
Processes and systems for recovering products from a corn fermentation mash. In one example, a process for recovering products from a corn fermentation mash can include separating ethanol from a fermentation mash to produce a whole stillage. The fermentation mash can be derived from a ground corn product milled from a plurality of corn pieces. The plurality of corn pieces can include whole corn kernels, fragmented corn kernels, size-reduced corn kernels, milled corn kernels, or a mixture thereof. Greater than 25 wt % of the ground corn product can have a particle size of greater than 105 μm and greater than 80 wt % of the ground corn product can have a particle size of 425 μm or less, as measured according to AOAC 965.22-1966. The process can also include separating the whole stillage to produce a fiber rich portion and a filtrate.
1. A process for recovering products from a corn fermentation mash, comprising:
separating ethanol from a fermentation mash to produce a whole stillage, wherein the fermentation mash is derived from a ground corn product milled from a plurality of corn pieces, wherein the plurality of corn pieces comprises whole corn kernels, fragmented corn kernels, size-reduced corn kernels, milled corn kernels, or any mixture thereof, wherein greater than 30 wt % of the ground corn product has a particle size of 105 μm or less, wherein greater than 25 wt % of the ground corn product has a particle size of greater than 105 μm, wherein greater than 80 wt % of the ground corn product has a particle size of 425 μm or less, as measured according to AOAC 965.22-1966, and wherein the ground corn product has a crystallinity that is more than 75% of a crystallinity of the corn pieces; and
separating the whole stillage with one or more fiber filters to produce a fiber rich portion and a filtrate, wherein the fiber filter comprises a filter sleeve and a rotor disposed within the filter sleeve, wherein the filter sleeve comprises a woven polymer fabric and has openings of about 10 μm to less than 400 μm.
2. The process of claim 1 , further comprising:
separating the filtrate to produce a protein rich portion and a clarified stillage; and
removing water from the protein rich portion to produce a protein rich product.
3. The process of claim 2 , further comprising:
removing water from the clarified stillage to produce an evaporated clarified stillage; and
separating the evaporated clarified stillage to produce an oil product and a stillage with reduced oil.
4. The process of claim 1 , wherein the ground corn product has a d 50 by volume percent of 100 μm to 400 μm, as measured according to ISO 13320:2009.
5. The process of claim 1 , wherein greater than 85 wt % of the ground corn product has a particle size of 425 μm or less, as measured according to AOAC 965.22-1966.
6. The process of claim 1 , wherein greater than 85 wt % of the ground corn product has a particle size of 425 μm or less, as measured according to AOAC 965.22-1966, and wherein the ground corn product has a d 50 by volume percent of 100 μm to 400 μm, as measured according to ISO 13320:2009.
7. A process for recovering products from a corn fermentation mash, comprising:
separating ethanol from a fermentation mash to produce a whole stillage, wherein the fermentation mash is derived from a ground corn product milled from a plurality of corn pieces, wherein the plurality of corn pieces comprises whole corn kernels, fragmented corn kernels, size-reduced corn kernels, milled corn kernels, or any mixture thereof, wherein greater than 30 wt % of the ground corn product has a particle size of 105 μm or less, wherein greater than 25 wt % of the ground corn product has a particle size of greater than 105 μm, and wherein greater than 80 wt % of the ground corn product has a particle size of 425 μm or less, as measured according to AOAC 965.22-1966, and wherein the ground corn product has a crystallinity that is more than 75% of a crystallinity of the corn pieces; and
separating the whole stillage with one or more fiber filters to produce a fiber rich portion and a filtrate.
8. The process of claim 7 , wherein the fiber filter comprises a filter sleeve having openings of 500 μm or less, and wherein the filter sleeve is tensioned with a pair of springs.
9. The process of claim 7 , wherein the fiber filter comprises a filter sleeve having openings of about 12 μm to about 200 μm.
10. The process of claim 7 , further comprising:
separating the filtrate to produce a protein rich portion and a clarified stillage; and
removing water from the protein rich portion to produce a protein rich product.
11. A process for recovering products from a corn fermentation mash, comprising:
separating ethanol from a fermentation mash to produce a whole stillage, wherein the fermentation mash is derived from a ground corn product milled from a plurality of corn pieces, wherein the plurality of corn pieces comprises whole corn kernels, fragmented corn kernels, size-reduced corn kernels, milled corn kernels, or any mixture thereof, wherein the ground corn product has a crystallinity that is more than 75% of a crystallinity of the corn pieces;
separating the whole stillage with one or more fiber filters to produce a fiber rich portion and a filtrate;
separating the filtrate to produce a protein rich portion and a clarified stillage;
removing water from the clarified stillage to produce an evaporated clarified stillage; and
separating the evaporated clarified stillage to produce an oil product and a stillage with reduced oil.
12. The process of claim 7 , wherein the fiber filter comprises a filter sleeve and a rotor disposed within the filter sleeve, and wherein the filter sleeve comprises a woven polymer fabric.
13. The process of claim 11 , wherein greater than 30 wt % of the ground corn product has a particle size of 105 μm or less, wherein greater than 30 wt % of the ground corn product has a particle size of greater than 105 μm, and wherein greater than 80 wt % of the ground corn product has a particle size of 425 μm or less, as measured according to AOAC 965.22-1966.
14. The process of claim 7 , wherein greater than 94 wt % of the ground corn product has a particle size of 425 μm or less, as measured according to AOAC 965.22-1966, and wherein the ground corn product has a d 50 by volume percent of 120 μm to 350 μm, as measured according to ISO 13320:2009.
15. The process of claim 7 , wherein the whole stillage is separated with the one or more fiber filters in combination with at least one separator to produce the fiber rich portion and a filtrate, the separator selected from the group consisting of: a rotary drum screen, a rotary vacuum drum filter, a brush strainer, a vibratory separator, a linear motion screen, and a vacu-deck screen.
16. The process of claim 7 , wherein:
greater than 35 wt % of the ground corn product has a particle size of 105 μm or less and greater than 94 wt % of the ground corn product has a particle size of 425 μm or less, as measured according to AOAC 965.22-1966.
17. The process of claim 1 , wherein:
greater than 35 wt % of the ground corn product has a particle size of 105 μm or less and greater than 94 wt % of the ground corn product has a particle size of 425 μm or less, as measured according to AOAC 965.22-1966, and
the ground corn product has a d 50 by volume percent of 120 μm to 350 μm, as measured according to ISO 13320:2009.
18. The process of claim 7 , wherein:
greater than 35 wt % of the ground corn product has a particle size of 105 μm or less and greater than 94 wt % of the ground corn product has a particle size of 425 μm or less, as measured according to AOAC 965.22-1966,
the ground corn product has a d 50 by volume percent of 120 μm to 350 μm, as measured according to ISO 13320:2009, and
the fiber filter comprises a filter sleeve having openings of about 12 μm to about 200 μm.
19. The process of claim 1 , wherein the filter sleeve is tensioned with a pair of springs.