Refined chlorogenic acid-containing composition manufacturing method
US-2019274985-A1 · Sep 12, 2019 · US
US11771670B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11771670-B2 |
| Application number | US-201716345194-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 28, 2017 |
| Priority date | Oct 26, 2016 |
| Publication date | Oct 3, 2023 |
| Grant date | Oct 3, 2023 |
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Provided is a method of producing a purified chlorogenic acid-containing composition, including a contact step of bringing a chlorogenic acid-containing composition having solids concentration of from 1.5 mass % to 4.7 mass % and a “caffeine/chlorogenic acid” mass ratio of 5 or less into contact with a porous adsorbent.
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The invention claimed is: 1. A method of producing a purified chlorogenic acid-containing composition, comprising: providing a chlorogenic acid-containing composition comprising chlorogenic acid and caffeine, wherein the chlorogenic acid-containing composition has a solids concentration of from 1.5 mass % to 4.7 mass % and a mass ratio of caffeine to chlorogenic acid is from 0.001 to 0.4; and contacting the chlorogenic acid-containing composition with a porous adsorbent at a temperature of from 50° C. to 100° C.; wherein the change ratio of caffeine to chlorogenic acid before and after purification is 89% or more, wherein the change ratio of caffeine to chlorogenic acid (%)=100−(C/D)/(E/F)×100, wherein C represents the mass of caffeine after contact with the porous adsorbent, D represents the mass of the chlorogenic acid after contact with the porous adsorbent, E represents the mass of caffeine before contact with the porous adsorbent, and F represents the mass of the chlorogenic acid before contact with the porous adsorbent. 2. The method of producing a purified chlorogenic acid-containing composition according to claim 1 , wherein the porous adsorbent comprises activated carbon. 3. The method of producing a purified chlorogenic acid-containing composition according to claim 2 , wherein a pore radius of the activated carbon is from 0.1 nm to 1.0 nm. 4. The method of producing a purified chlorogenic acid-containing composition according to claim 2 , wherein an average particle size of the activated carbon is from 0.01 mm to 2.0 mm. 5. The method of producing a purified chlorogenic acid-containing composition according to claim 1 , wherein the method of contacting the chlorogenic acid-containing composition with the porous adsorbent is a continuous method. 6. The method of producing a purified chlorogenic acid-containing composition according to claim 1 , wherein the porous adsorbent is used in an amount from 50 mass % to 400 mass % with respect to the solids concentration of the chlorogenic acid-containing composition. 7. The method of producing a purified chlorogenic acid-containing composition according to claim 1 , further comprising a step of subjecting a solution treated with the porous adsorbent to solid-liquid separation after the contact with the porous adsorbent. 8. The method of producing a purified chlorogenic acid-containing composition according to claim 7 , wherein the solid-liquid separation comprises one or two or more selected from the group consisting of paper filtration, centrifugal separation and membrane filtration. 9. The method of producing a purified chlorogenic acid-containing composition according to claim 1 , further comprising, before the contact step, a step of obtaining the chlorogenic acid-containing composition having solids concentration of from 1.5 mass % to 4.7 mass % and a mass ratio of caffeine to chlorogenic acid is from 0.001 to 0.4 through a step comprising an extraction step of subjecting at least one selected from the group consisting of green coffee beans, decaffeinated green coffee beans, roasted coffee beans having an L value of 30 or more, and decaffeinated roasted coffee beans having an L value of 25 or more, to column extraction using an aqueous solvent. 10. The method of producing a purified chlorogenic acid-containing composition according to claim 9 , wherein an extraction temperature in the extraction step is from 75° C. to 98° C. 11. The method of producing a purified chlorogenic acid-containing composition according to claim 9 , wherein the aqueous solvent comprises water. 12. The method of producing a purified chlorogenic acid-containing composition according to claim 1 , wherein the chlorogenic acid is selectively recovered. 13. The method of producing a purified chlorogenic acid-containing composition according to claim 12 , wherein caffeine is removed through a porous adsorbent treatment. 14. The method of producing a purified chlorogenic acid-containing composition according to claim 1 , wherein a value of G×H/I is >1.3, wherein G represents a mass of the recovered solution, H represents the solids concentration (mass %) of the chlorogenic acid-containing composition before contact with the porous adsorbent, and I represents the mass (g) of the porous adsorbent used. 15. The method of producing a purified chlorogenic acid-containing composition according to claim 1 , wherein the porous adsorbent is used in an amount from 80 mass % to 370 mass % with respect to the solids concentration of the chlorogenic acid-containing composition. 16. The method of producing a purified chlorogenic acid-containing composition according to claim 1 , wherein the porous adsorbent is used in an amount from 150 mass % to 350 mass % with respect to the solids concentration of the chlorogenic acid-containing composition.
Coffea, e.g. coffee · CPC title
having two or more carboxyl groups, e.g. succinic, maleic or phthalic acid · CPC title
Coffee; Coffee substitutes; Preparations thereof (preservation of coffee or coffee substitutes A23B90/00) · CPC title
Plant extracts, their artificial duplicates or their derivatives · CPC title
of acids having aromatic rings, e.g. benactizyne, clofibrate · CPC title
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