Method for separation and purification of zeaxanthin from capsanthin

A technology for the separation and purification of zeaxanthin, which is applied in the direction of organic chemistry, can solve the problems of low yield, high cost, and high price, and achieve the effects of improving purity, safe and reliable use and consumption, and high purity

Active Publication Date: 2019-12-20
山东天音生物科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] The applicant found in the research: first, there is an urgent need for a method that can efficiently extract natural zeaxanthin; with the continuous development of toxicology and analysis techniques, studies have shown that although the purity of chemically synthesized zeaxanthin is relatively high , the production cost is low, but the product is easily mixed with a small amount of toxic chemicals, which can cause chromosomal mutation and carcinogenesis, so with the continuous improvement of awareness, naturally extracted zeaxanthin will occupy an active position in the market
Second, the natural zeaxanthin obtained by the existing separation method has low purity and high price; in the field of extracts, the purity is directly proportional to the price. When the purity of a single component reaches more than 80%, as the purity of a single component of the extract increases Increasing its selling price will increase exponentially; in order to obtain high-purity natural zeaxanthin, the existing methods are mostly supercritical extraction and subcritical fluid extraction. This method is extremely expensive and low in output, and cannot be applied to large-scale industrial production However, the relatively low-cost analytical column adsorption separation method has unsatisfactory purity and low yield.
Third, due to the problem of impurities, in the prior art, it is necessary to separate and remove impurities multiple times to obtain high-purity zeaxanthin, and there must be a loss of zeaxanthin in each separation, which leads to an unsatisfactory yield and causes raw material loss. waste, increased cost

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0032] 1) Carry out saponification reaction of capsanthin, ethanol, potassium hydroxide and vitamin E under nitrogen gas, saponify at 40°C for 8 hours to obtain saponified product; the mass ratio of capsanthin, ethanol, potassium hydroxide and vitamin E is 1: 0.25:0.75:0.05; Potassium hydroxide is added in the form of 45% potassium hydroxide aqueous solution;

[0033] 2) Add hydrochloric acid to the saponified product to adjust the pH to 7, and dilute it with a mixture of n-hexane-acetone-ethyl acetate (V / V, 8.5:1.5:0.15) that is 3 times the mass of capsanthin to obtain a saponified product dilution ;

[0034] 3) Pass the diluent of the saponified matter into the analysis column with 6 kg of XR15C macroporous adsorption resin inside, and the adsorption flow rate is 2BV / h; after the adsorption is completed, wash it with deionized water until it is colorless; Esters mixture solution (V / V, 8.5:1.5:0.15) was analyzed, the analysis flow rate was 1BV / h, and the zeaxanthin analysis ...

Embodiment 2

[0038] 1) Saponification reaction of capsanthin, ethanol, sodium hydroxide, and tert-butylhydroquinone under nitrogen gas, saponification at 45°C for 8.5 hours, to obtain saponified product; capsanthin, ethanol, sodium hydroxide, tert-butyl The mass ratio of hydroquinone is 1:0.2:0.8:0.04; sodium hydroxide is added in the form of an aqueous solution of sodium hydroxide with a mass percentage of 40%;

[0039] 2) Add acetic acid to the saponified product to adjust the pH between 7, and dilute it with a mixture of n-hexane-acetone-ethyl acetate (V / V, 8:1.7:0.13) that is 4 times the mass of capsanthin to obtain a diluted saponified product liquid;

[0040] 3) Pass the diluent of the saponified matter into the analysis column with 6 kg of XR919LZ macroporous adsorption resin inside, and the adsorption flow rate is 1.5BV / h; after the adsorption is completed, wash it with deionized water until it is colorless; Ethyl ester mixture (V / V, 8:1.7:0.13) was analyzed at an analysis flow ra...

Embodiment 3

[0044] 1) Saponification reaction of capsanthin, ethanol, potassium hydroxide, and vitamin E under the condition of nitrogen gas, saponification at 55°C for 8 hours, to obtain saponified product; the mass ratio of capsanthin, ethanol, potassium hydroxide, and vitamin E is 1: 0.3:0.7:0.06; Potassium hydroxide is added in the form of an aqueous solution of potassium hydroxide with a mass percentage of 50%;

[0045] 2) Add oxalic acid to the saponified product to adjust the pH between 7.5, and dilute it with a mixture of n-hexane-acetone-ethyl acetate (V / V, 9:1.3:0.17) that is 5 times the mass of capsanthin to obtain saponified product. liquid;

[0046] 3) Pass the diluent of the saponified substance into the analytical column with 6 kg of XR921H macroporous adsorption resin inside, and the adsorption flow rate is 2BV / h; after the adsorption is completed, wash it with deionized water until it is colorless; The ester mixture (V / V, 9:1.3:0.17) was analyzed at a flow rate of 1.5BV / ...

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Abstract

Belonging to the technical field of carotenoid preparation, the invention discloses a method for separation and purification of zeaxanthin from capsanthin. The method is characterized by including thepreparation steps of: subjecting capsanthin, alcohol, alkali and an antioxidant to saponification reaction; adjusting the pH value of the saponification product to 7-8, performing diluting a n-hexane-acetone-ethyl acetate mixed solution, carrying out desorption, and collecting a zeaxanthin desorption solution; recovering the solvent, and conducting cooling and crystallizing; and carrying out filtering, washing and drying to obtain zeaxanthin crystals. The method provided by the invention directly adopts capsanthin as the raw material, performs saponification treatment to obtain a zeaxanthin monomer, and then separate zeaxanthin with a content of 90% or above. The product is convenient for large-scale production.

Description

technical field [0001] The invention discloses a method for separating and purifying zeaxanthin from capsanthin, which belongs to the technical field of carotenoid preparation. Background technique [0002] Capsanthin, or capsanthin, is a tetraterpenoid orange-red pigment present in ripe red pepper fruits, which belongs to carotenoid pigments. Among them, the more polar red components are capsanthin and capsanthin, accounting for 50%~60% of the total, and the other is the less polar yellow component, the main components are zeaxanthin and carrot white. [0003] Zeaxanthin (Zeaxanthin, 3,3'-dihydroxy-β-carotene), also known as zeaxanthin, has a molecular formula of C40H56O2 and a molecular weight of 566.88. It belongs to the isoprene class and is an oxygen-containing carotenoid. It is isomer with lutein. With good antioxidant properties, it has unique functions in relieving visual fatigue, preventing age-related macular degeneration, protecting skin, enhancing immunity and...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C403/24
CPCC07C403/24
Inventor 刘温来李勇田芸赵辰光于正毅
Owner 山东天音生物科技有限公司
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