Non-crystallisable D-allulose syrups
US-11439168-B2 · Sep 13, 2022 · US
US11980206B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11980206-B2 |
| Application number | US-202016749438-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jan 22, 2020 |
| Priority date | Jun 18, 2014 |
| Publication date | May 14, 2024 |
| Grant date | May 14, 2024 |
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The present invention provides a method for forming caramels having reduced low molecular weight species such as 4-MeI. The low-4-MeI caramels produced by this method have improved stability and taste relative to those known in the art. The invention also extends to the caramels produced by the disclosed methods and the use of such caramels in food and beverages.
Opening claim text (preview).
We claim: 1. A method of reducing the low molecular weight component of a caramel solution, comprising: (i) adding a caramel selected from a class III or class IV caramel and water to a feed tank to provide a caramelized solution, said caramel comprising low molecular weight species and high molecular weight species; (ii) adjusting the pH of the caramelized solution in the feed tank to greater than 7.5; (iii) subjecting the caramelized solution to diafiltration to provide a retained fraction and a permeated fraction, said retained fraction comprising high molecular weight species and water; (iv) subjecting the permeate fraction to reverse osmosis to provide a recycle water stream and a permeate concentrate stream; (v) adding the retained fraction and recycle water stream to the feed tank in (i); (vi) repeating steps (iii)-(vi) one or more times to provide a concentrated, purified class III or class IV caramel that has less than about 10 ppm 4 -methylimidazole (4-MeI), wherein the pH is not adjusted when the retained fraction and recycle water stream are added to the feed tank; and, (vii) adjusting the pH of the concentrated, purified class III or class IV caramel from step (vi) to between about 2.4-3.25; and wherein the diafiltration comprises a molecular weight cutoff (MWCO) of about 600 to 800 Dalton. 2. The method of claim 1 , wherein the purified class III or IV caramel has a reduced amount of species selected from the group consisting of 2-methylimidazole, 5-hydroxy methyl furfural, 5-hydroxy 2-methyl pyridine, 2-hydroxy pyridine and 2-hydroxy-6methylpyridine carboxylic acid. 3. The method of claim 1 , wherein the purified class III or IV caramel has less than about 5 ppm 4-methylimidzaole. 4. The method of claim 3 , wherein the purified class III or IV caramel has less than 1 ppm 4-methylimidazole. 5. The method of claim 1 , wherein the diafiltration is nano-filtration. 6. The method of claim 1 , wherein the diafiltration is carried out in constant flux mode, constant pressure mode or a combination thereof. 7. The method of claim 1 , wherein the method is carried out at a temperature from about 60° F. to about 95° F. 8. The method of claim 1 , wherein the method is carried out at a constant pressure in the range of about 50 to about 55 psi. 9. The method of claim 1 , wherein the process time for the method is from about 2 hours to about 10 hours. 10. The method of claim 1 , wherein the pH adjustment in step (vii) is adjusted by addition of 75% food grade phosphoric acid. 11. The method of claim 1 , further comprising collecting and storing the purified class III or class IV caramel. 12. The method of claim 1 , further comprising spray-drying the purified class III or class IV caramel to provide a powder.
Processes for preparing caramel or sugar colours · CPC title
Compounds of unspecified constitution characterised by the chemical process for their preparation · CPC title
heated in the presence of reducing sugars, e.g. Maillard's non-enzymatic browning · CPC title
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