Process
US-2015299612-A1 · Oct 22, 2015 · US
US10975244B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10975244-B2 |
| Application number | US-201716328195-A |
| Country | US |
| Kind code | B2 |
| Filing date | Aug 17, 2017 |
| Priority date | Aug 26, 2016 |
| Publication date | Apr 13, 2021 |
| Grant date | Apr 13, 2021 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
The present invention relates to a valuable product in the form of a flavonoid-containing phenol mixture having intense red coloration and to a method for obtaining a valuable-substance phase, more particularly a red-colored phase, from a native substance mixture.
Opening claim text (preview).
The invention claimed is: 1. A method for obtaining a valuable-substance phase comprising the following steps: Step A: providing a native substance mixture composed of seeds and/or fruits from the cabbage family Brassicaceae, having comminuted as a proportion of hard, breakable shells or in shelled form, wherein the native substance mixture is rapeseeds composed of complete seeds or composed of partially deoiled seeds; Step B: if the native substance mixture from step A) is not completely comminuted, further comminuting the native substance mixture from step A) to break up the shells; Step C: dispersing and/or mixing the comminuted substance mixture from step A) or B) with water, with addition of up to a maximum of 8 parts water to one part comminuted substance mixture and with stirring of the water and the comminuted substance mixture to yield a flowable slurry or a dispersion; Step D: adjusting the pH of the slurry from step C) into an alkaline range of pH>9.5; Step E: adding a water-soluble organic solvent to the slurry from step D) following the adjustment of the pH of the slurry in step D); in such a way that an alcohol concentration of less than 30% by volume is reached in order to detach the shells from the endosperm of the seeds/fruits; Step F: separating off a solid phase comprising the overwhelming proportion of any shells still present, wherein the separation is performed in the centrifugal field in a centrifuge; Step G: shifting the pH of the solid phase-cleared slurry from step F) into the pH range of from pH=4.5 to pH=7.2; and Step H: separating the shell-free slurry, the pH of which was shifted into the acidic range in step G), wherein the separation is performed in a centrifuge into multiple phases, wherein at least one of said phases is a sinapinic acid-containing phase; Step I: adding laccase to the sinapinic acid-containing phase of step H), wherein the phase separation is performed in step H) in one or two steps, into two valuable-substance phases, with at least one aqueous phase comprising an albumin content and a sinapinic acid content and a residual-oil content. 2. The method as claimed in claim 1 , characterized in that the native substance mixture is processed in the form of a recently produced intermediate product not more than 31 days after a preliminary stage. 3. The method as claimed in claim 1 , characterized in that the native substance mixture is processed in the form of a fresh intermediate product not more than 3 days after a preliminary stage. 4. The method as claimed in claim 1 , characterized in that the native substance mixture used in step A) is a cold-pressed material, which was pressed at a temperature of less than 70° C. 5. The method as claimed in claim 1 , characterized in that one or more of the separation steps in step F) or H) is/are carried out in a 3-phase decanter or in at least two steps in 2-phase decanters. 6. The method as claimed in claim 1 , characterized in that one or more of the separation steps in step F) or H) is/are carried out in a nozzle separator. 7. The method as claimed in claim 1 , wherein the water-soluble organic solvent is a linear aliphatic alcohol. 8. The method as claimed in claim 1 , wherein the content of the water-soluble organic solvent in the aqueous part of the slurry in step E) after the addition of the water-soluble organic solvent is 20% by volume or less. 9. The method as claimed in claim 1 , wherein all the method steps are performed at a temperature below 60° C. 10. The method as claimed in claim 1 , wherein all the method steps are performed at a temperature below 50° C. 11. A method for obtaining a valuable-substance phase comprising the following steps: Step A: providing a native substance mixture composed of seeds and/or fruits from the cabbage family Brassicaceae, having comminuted as a proportion of hard, breakable shells or in shelled form, wherein the native substance mixture is rapeseeds composed of complete seeds or composed of partially deoiled seeds; Step B: if the native substance mixture from step A) is not completely comminuted, further comminuting the native substance mixture from step A) to break up the shells; Step C: dispersing and/or mixing the comminuted substance mixture from step A) or B) with water, with addition of up to a maximum of 8 parts water to one part comminuted substance mixture and with stirring of the water and the comminuted substance mixture to yield a flowable slurry or a dispersion; Step D: adjusting the pH of the slurry from step C) into an alkaline range of pH>9.5; Step E: adding a water-soluble organic solvent to the slurry from step D) following the adjustment of the pH of the slurry in step D); in such a way that an alcohol concentration of less than 30% by volume is reached in order to detach the shells from the endosperm of the seeds/fruits; Step F: separating off a solid phase comprising the overwhelming proportion of any shells still present, wherein the separation is performed in the centrifugal field in a centrifuge; Step G: shifting the pH of the solid phase-cleared slurry from step F) into the pH range of from pH=4.5 to pH=7.2; Step H: separating the shell-free slurry, the pH of which was shifted into the acidic range in step G), wherein the separation is performed in a decanter into multiple phases, wherein at least one of said phases is a sinapinic acid-containing phase; and Step I: adding laccase to the sinapinic acid-containing phase of step H), wherein the phase separation is performed in step H) in one or two steps, into two valuable-substance phases, with at least one aqueous phase comprising an albumin content and a sinapinic acid content and a residual-oil content. 12. The method as claimed in claim 3 , wherein the native substance mixture is processed in the form of a fresh intermediate product less than 48 hours after the preliminary stage. 13. The method as claimed in claim 3 , wherein the native substance mixture is processed in the form of a fresh intermediate product less than 24 hours after the preliminary stage. 14. The method as claimed in claim 4 , wherein the cold pressed material is a cold pressed rape cake. 15. The method as claimed in claim 4 , wherein the cold-pressed material was pressed at a temperature of less than 60° C. 16. The method as claimed in claim 1 , wherein in step C), the dispersing and/or mixing of the comminuted substance mixture from step A) or B) with water is with the addition of up to a maximum of 6 parts water to one part comminuted substance mixture. 17. The method as claimed in claim 1 , wherein in step C), the dispersing and/or mixing of the comminuted substance mixture from step A) or B) with water is with the addition of up to a maximum of 5 parts water to one part comminuted substance mixture. 18. The method as claimed in claim 1 , wherein in step E), the water-soluble organic solvent is ethanol and is in water diluted form. 19. The method as claimed in claim 1 , wherein the content of the water-soluble organic solvent added to the slurry in step E) is 30 to 60% by volume.
Laccase (1.10.3.2) · CPC title
Oxidoreductases (1.) · CPC title
Removing undesirable substances, e.g. bitter substances · CPC title
from waste material (from hydrolysates of wood or straw A23K10/32; from molasses A23K10/33) · CPC title
from leguminous or other vegetable seeds; from press-cake or oil-bearing seeds · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.