Alcoholic nitrogenized coffee product, system, and method
US-2024423408-A1 · Dec 26, 2024 · US
US10058113B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10058113-B2 |
| Application number | US-201715588950-A |
| Country | US |
| Kind code | B2 |
| Filing date | May 8, 2017 |
| Priority date | Oct 4, 2012 |
| Publication date | Aug 28, 2018 |
| Grant date | Aug 28, 2018 |
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Disclosed herein are shelf-stable, clear liquid nutritional compositions having a pH ranging from 2.5 to 4.6 and comprising water; at least one source of EGCg in an amount sufficient to provide 200-1700 mg/L of EGCg; and at least one source of protein in an amount sufficient to provide 25-45 g/L of total protein. The shelf-stable, clear liquid nutritional compositions lose no more than 20% by weight solids of the EGCg content present in the initial formulation of the compositions to epimerization, degradation, or both epimerization and degradation during heat sterilization. In certain embodiments, the loss of EGCg is exhibited by the amount of epimerization product GCg present in the shelf-stable, clear liquid nutritional composition following heat sterilization. Methods for preparing the shelf-stable, clear liquid nutritional compositions are also disclosed herein.
Opening claim text (preview).
What is claimed is: 1. A method for preparing a sterilized, clear liquid nutritional composition, the method comprising: heating an unsterilized liquid nutritional composition having a pH ranging from 2.5 to 4.6 to a temperature ranging from 85° C. (185° F.) to 152° C. (306° F.) for a period of time sufficient to produce a sterilized liquid nutritional composition, thereby producing a sterilized liquid nutritional composition comprising: water; at least one source of epigallocatechin gallate (EGCg) in an amount sufficient to provide 200-1700 g/L of EGCg; and one or more sources of protein in an amount sufficient to provide 25-45 g/L of total protein, wherein the one or more sources of protein comprise whey protein concentrate, whey protein isolates; and/or whey protein hydrosylates; wherein: the whey protein concentrate, whey protein isolates, and/or whey protein hydrosylates comprise β-lactoglobulin; the sterilized liquid nutritional composition contains no more than 340 mg/L of gallocatechin gallate (GCg), and the sterilized liquid nutritional composition is clear. 2. The method of claim 1 further comprising adjusting the pH of the unsterilized liquid nutritional composition to a level ranging from 2.5 to 4.6 prior to the heating. 3. The method of claim 1 , wherein the whey protein concentrate, whey protein isolates, and/or whey protein hydrosylates comprise β-lactoglobulin in an amount sufficient to provide a molar ratio of EGCg to β-lactoglobulin of 1:1 to 11:1 prior to sterilization. 4. The method of claim 1 , wherein the at least one source of EGCg is a green tea-based source of EGCg. 5. The method of claim 1 , wherein the at least one source of EGCg comprises 45% to 100% by weight solids of EGCg based on the weight of the at least one source of EGCg. 6. The method of claim 1 , wherein the sterilized liquid nutritional composition further comprises acidified soy protein isolates, soy protein hydrolysates, casein hydrolysates, or pea hydrolysates. 7. The method of claim 1 , wherein the one or more sources of protein comprise whey-based protein containing 20% to 95% of β-lactoglobulin by weight of the solids of the whey-based protein. 8. The method of claim 1 , wherein no more than 170 mg/L of GCg is present in the sterilized liquid nutritional composition. 9. The method of claim 1 , wherein the heating occurs at a temperature of at least 105° C. (221° F.) for a period of time sufficient to sterilize the composition. 10. The method claim 1 , wherein the heating occurs at a temperature of at least 126° C. (259° F.) for a period of time sufficient to sterilize the composition. 11. The method of claim 1 , further comprising adjusting the pH level of the sterilized liquid nutritional composition to a range of 2.5 to 3.5. 12. The method of claim 1 , further comprising admixing at least a portion of the at least one source of EGCg with the one or more sources of protein, wherein the step of admixing occurs at a pH ranging from 2.5 to 4.6 and occurs prior to the heating of the unsterilized liquid nutritional composition. 13. The method of claim 12 , wherein at least a portion of the β-lactoglobulin is denatured upon admixing. 14. The method of claim 12 , further comprising denaturing at least a portion of the β-lactoglobulin prior to admixing. 15. The method of claim 14 , wherein the step of denaturing the at least a portion of the β-lactoglobulin includes heating the one or more sources of protein containing β-lactoglobulin to a temperature ranging from 50° C. (122° F.) to 90° C. (194° F.) for a period of time sufficient to denature the at least a portion of the β-lactoglobulin. 16. The method of claim 12 , wherein the one or more sources of protein containing β-lactoglobulin is at a temperature ranging from 15° C. (59° F.) to 35° C. (95° F.) prior to admixing with the at least one source of EGCg. 17. The method of claim 1 , wherein the sterilized composition has a pH at a level ranging from 2.5 to 4. 18. The method of claim 1 , wherein the sterilized composition further comprises at least one source of carbohydrate, and the at least one source of carbohydrate is present in an amount sufficient to provide 30-200 g/L of carbohydrate. 19. The method of claim 1 , further comprising admixing at least a portion of the at least one source of EGCg with the one or more sources of protein prior to the heating step and denaturing at least a portion of the β-lactoglobulin prior to the admixing. 20. The method of claim 1 , further comprising: admixing, prior to the step of heating, the at least one source of epigallocatechin gallate (EGCg) and the one or more sources of protein comprising β-lactoglobulin to form an admixture; and forming an unsterilized liquid nutritional composition by combining the admixture with at least one of the following ingredients: water; an additional source of EGCg; and an additional source of protein selected from the group consisting of acidified soy protein isolates, soy protein hydrolysates, casein hydrolysates, pea hydrolysates, and a combination thereof. 21. A method for preparing a sterilized, clear liquid nutritional composition, the method comprising: admixing at least one source of epigallocatechin gallate (EGCg) and at least one source of whey-based protein containing β-lactoglobulin to form an admixture, wherein the admixture comprises EGCg and β-lactoglobulin in amounts sufficient to provide a molar ratio of EGCg to β-lactoglobulin of 1:1 to 11:1 in the admixture, and wherein the admixing occurs at a pH of 2.5 to 4.6; forming an unsterilized liquid nutritional composition by combining the admixture with at least one of the following ingredients: water; an additional source of EGCg; and an additional source of protein selected from the group consisting of whey-based proteins, acidified soy protein isolates, soy protein hydrolysates, casein hydrolysates, pea hydrolysates, and combinations thereof; adjusting the pH of the unsterilized nutritional composition to obtain a pH ranging from 2.5 to 4.6 if necessary; and heating the unsterilized liquid nutritional composition to a temperature ranging from 85° C. (185° F.) to 152° C. (306° F.) for a period of time sufficient to produce a sterilized liquid nutritional composition comprising: water, 200-1700 mg/L of total EGCg, 25-45 g/L of total protein, and no more than 340 mg/L of gallocatechin gallate (GCg), wherein the sterilized liquid nutritional composition is clear. 22. The method of claim 21 , wherein at least a portion of the at least one source of whey-based protein containing β-lactoglobulin in the admixture includes denatured β-lactoglobulin. 23. The method of claim 21 further comprising denaturing at least a portion of the at least one source of whey-based protein containing β-lactoglobulin by heating the at least one source of whey-based protein containing β-lactoglobulin to a temperature ranging from 50° C. (122° F.) to 90° C. (194° F.) prior to the admixing for a period of time sufficient to denature at least a portion of the β-lactoglobulin. 24. The method of claim 23 , wherein the at least one source of protein containing β-lactoglobulin is at a temperature ranging from 15° C. (59° F.) to 35° C. (95° F.) prior to admixing. 25. The method of claim 21 , wherein the sterilized liquid nutritional composition further comprises at least one source of carbohydrate in an amount sufficient to provide 30-200
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