GH5 and GH30 in Wet Milling
US-2020140909-A1 · May 7, 2020 · US
US12005456B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12005456-B2 |
| Application number | US-201716326952-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 15, 2017 |
| Priority date | Sep 16, 2016 |
| Publication date | Jun 11, 2024 |
| Grant date | Jun 11, 2024 |
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The present invention provides to a fiber washing system, optimized for the use of hydrolytic enzymes in the system. Furthermore, the present invention provides to a method for improving starch and gluten yield in a wet milling process, preferably comprising the optimized fiber washing system.
Opening claim text (preview).
The invention claimed is: 1. A fiber washing system in a corn kernel wet milling system comprising a plurality of screen units being fluidly connected in a counter current washing configuration from a most upstream screen unit to a most downstream screen unit; each screen unit is configured for separating a stream of corn kernel mass and liquid into two fractions: a first fraction (s) and a second fraction (f), said second fraction (f) containing a higher amount measured in wt % fiber than the first fraction (s); a space (V) is a separate container being fluidly connected with one or more screen units to receive one of said first fraction (s), one of said second fraction (f), or a mixed first and second fraction (s,f), and wherein the space (V) is configured to provide an incubation time in which the first fraction (s), the second fraction (f), or the mixed first and second fraction (s,f) received in the space (V) are contacted with one or more hydrolytic enzymes to produce incubated fractions; and outletting the incubated fractions to a downstream screen unit, wherein the system is configured for inletting the corn kernel mass and the liquid to the most upstream screen unit, outletting the first fraction (s) from the most upstream screen unit as a product stream containing starch, inletting process water, outletting the second fraction (f) from the most downstream screen unit as a washed corn kernel mass containing a lower amount of starch and gluten than the corn kernel mass, and introducing the one or more hydrolytic enzymes into the first fraction (s), the second fraction (f), the mixed first and second fraction (s,f), or the process water, wherein an incubation time in the space (V) is from 0.5 to 3 hours and a total retention time in which one or more fractions of the corn kernel mass is contacted with an effective amount of the one or more hydrolytic enzymes in the fiber-washing system is from 90 minutes to 5 hours. 2. The system according to claim 1 , wherein one or more screen units are hydro-cyclones ( 16 ). 3. The system according to claim 1 wherein the system is configured to introduce the one or more hydrolytic enzymes into said first fraction (s) and/or into said second fraction (f) and/or into said mixed first and second fraction (s,f) and/or into the process water, by means of a dosing device ( 10 ). 4. The system according to claim 3 , wherein said dosing device ( 10 ) is adapted to provide a controllable dosing of a quantity of the one or more hydrolytic enzymes according to a predetermined specific ratio between an amount of the one or more hydrolytic enzymes and an infeed of the corn kernel mass to the system. 5. The system according to claim 3 , wherein the dosing device ( 10 ) is a metering pump. 6. The system according to claim 3 , wherein the dosing device ( 10 ) is a gravity flow dispenser having a controllable outflow valve configured for controlling an amount of one or more hydrolytic enzymes flowing through a flow valve. 7. The system according to claim 1 , wherein the second fraction (f) of the corn kernel mass contacted with the one or more hydrolytic enzymes in the space (V) has a fiber content, which corresponds to 5-15% (w/w) dry solids (DS). 8. The system according to claim 1 , wherein the second fraction (f) of the corn kernel mass contacted with the one or more hydrolytic enzymes in the space (V) has a fiber content, which corresponds to 5-12% (w/w) dry solids (DS). 9. The system according to claim 1 , wherein the second fraction (f) of the corn kernel mass contacted with the one or more hydrolytic enzymes in the space (V) has a fiber content, which corresponds to 5-10% (w/w) dry solids (DS). 10. The system according to claim 1 , wherein the second fraction (f) of the corn kernel mass contacted with the one or more hydrolytic enzymes in the space (V) has a fiber content, which corresponds to 7.5-12.5% (w/w) dry solids (DS). 11. The system according to claim 1 , wherein the second fraction (f) of the corn kernel mass contacted with the one or more hydrolytic enzymes in the space (V) has a fiber content, which corresponds to 8-12% (w/w) dry solids (DS). 12. The system according to claim 1 , wherein the second fraction (f) of the corn kernel mass contacted with the one or more hydrolytic enzymes in the space (V) has a fiber content, which corresponds to 8-11% (w/w) dry solids (DS). 13. A method to improve starch yield and/or gluten yield from corn kernels in a wet milling process, comprising the steps of: a) soaking the kernels in water to produce soaked kernels; b) grinding the soaked kernels; c) separating germs from the ground and soaked kernels to produce a corn kernel mass comprising fiber, starch and gluten; and d) subjecting the resultant corn kernel mass, to a fiber washing procedure; wherein during step d) one or more fractions of the corn kernel mass is contacted with an effective amount of one or more hydrolytic enzymes, and wherein the fiber washing procedure is performed with a fiber washing system in a corn kernel wet milling system comprising a plurality of screen units being fluidly connected in a counter current washing configuration from a most upstream screen unit to a most downstream screen unit; each screen unit is configured for separating a stream of corn kernel mass and liquid into two fractions: a first fraction (s) and a second fraction (f), said second fraction (f) containing a higher amount measured in wt % fiber than the first fraction (s); a space (V) is a separate container being fluidly connected with one or more screen units to receive one of said first fraction (s), one of said second fraction (f), or a mixed first and second fraction (s,f), and wherein the space (V) is configured to provide an incubation time in which the first fraction (s), the second fraction (f), or the mixed first and second fraction (s,f) received in the space (V) are contacted with the one or more hydrolytic enzymes to produce incubated fractions; and outletting the incubated fractions to a downstream screen unit, wherein the system is configured for inletting the corn kernel mass and the liquid to the most upstream screen unit, outletting the first fraction (s) from the most upstream screen unit as a product stream containing starch, inletting process water, outletting the second fraction (f) from the most downstream screen unit as a washed corn kernel mass containing a lower amount of starch and gluten than the corn kernel mass, and introducing the one or more hydrolytic enzymes into the first fraction (s), the second fraction (f), the mixed first and second fraction (s,f), or the process water, wherein an incubation time in the space (V) is from 0.5 to 3 hours and a total retention time in which one or more fractions of the corn kernel mass is contacted with an effective amount of the one or more hydrolytic enzymes in the fiber-washing system is from 90 minutes to 5 hours. 14. The method according to claim 13 , wherein the one or more of said hydrolytic enzymes is/are selected from the group consisting of cellulases (EC 3.2.1.4), xylanases (EC 3.2.1.8) arabinofuranosidases (EC 3.2.1.55 (Non-reducing end alpha-L-arabinofuranosidases); EC 3.2.1.185 (Non-reducing end beta-L-arabinofuranosidases) cellobiohydrolase I (EC 3.2.1.150), cellobiohydrolase II (E.C. 3.2.1.91), cellobiosidase (E.C. 3.2.1.176), beta-glucosidase (E.C. 3.2.1.21), beta-xylosidases (EC 3.2.1.37). 15. The method according to claim 13 , wherein the one or more of said hydrolytic enzymes is expressed in an organism with a cellulase background. 16. The method accord
Apparatus therefor · CPC title
Concentration of starch suspensions · CPC title
from corn or maize · CPC title
Preparatory treatment, e.g. crushing of raw materials {or steeping process (machines for preliminary washing A23N)} · CPC title
for washing or blanching (A23N12/06 takes precedence; blanching methods A23B7/06) · CPC title
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