Isolation and purification of cartenoids from marigold flowers

a technology of marigold flowers and crystals, which is applied in the direction of biocide, plant growth regulators, plant ingredients, etc., can solve the problems of promoting the formation of oxidative degenerative products, unable to synthesize animals, and exposure of products for a longer time under heat and air, so as to achieve the effect of realizing and effective processes, facilitating better extraction of carotenoid esters, and convenient size, density and hardness

Active Publication Date: 2010-04-01
KATRA PHYTOCHEM PRIVATE
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

This patented technology allows for efficient separation of luteins that can be used as feedstock or medicine. It uses natural gases such as propane or butane with minimal harmful emissions during production. Dryed mealt obtained through this method has good extraction properties because it contains only small amounts of impurities.

Problems solved by technology

Technologies described involve producing high amounts of carboxylic compounds called beta -tocopherols (C24oceritrienols) alongwith various types of pharmaceutical agents including alpha steranes, retinoids, flavonoids, lyrosine, melanotropins, neurotransmitters, etc. These substances help maintain good health during life when taken through food sources without causing harmful side effects.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

example 1

[0071]25 Kgs of Marigold Oleoresin having 92.19 gm / Kg or 9.22% of Xanthophylls is taken in 100 litres capacity reactor with an agitator. The Oleoresin is homogenised for 10 minutes under stirring at a temperature of about 40° C. with either steam or hot water in the jacket of the reactor as heating medium. Ethanolic KOH is prepared by taking 5 Kgs of KOH with purity of 95% and dissolving it in 35 litres of Ethyl alcohol (1:1.4 volumes). The prepared ethanolic KOH is added into reaction vessel slowly, containing the homogenised mass. The saponification reaction is carried out at a temperature of about 75° C. for 30 minutes. After ensuring the degree of saponification to be more than 99% by HPLC, 40 litres of demineralised hot water maintained at a temperature of 70° C. is added to the reacted mass and the stirring is continued for 10 minutes. The diluted mass with carotenoid crystals is then pumped into a filter press to recover the crystals. Around 250 litres of additional hot water

example 2

[0074]25.5 Kgs of Marigold Oleoresin having 102.18 gm / Kg or 10.22% of Xanthophylls is taken in 100 litres capacity reactor with an agitator.

[0075]The Oleoresin is homogenised for 10 minutes under stirring at a temperature of about 45° C. with either steam or hot water in the jacket of the reactor as heating medium. Ethanolic KOH is prepared by taking 5.1 Kgs of KOH with purity of 95% and dissolving it 40 litres of Ethyl alcohol (1:1.56 volumes).

[0076]The prepared Ethanolic KOH is added into reaction vessel slowly, containing the homogenised mass. The saponification reaction is carried out at a temperature of 73° C. for 30 minutes. After ensuring the degree of saponification to be more than 99% by HPLC, 45 litres of demineralised hot water maintained at a temperature of about 65° C. is added to the reacted mass and the stirring is continued for 10 minutes. The diluted mass with carotenoid crystals is then pumped into a filter press to recover the crystals. Around 275 litres of additio

example 3

[0080]20 kg of lutein rich Marigold meal having 8.99 gm / Kg (0.89%) of total carotenoids (with a carotenoids profile of 74.58% trans-lutein (T-lutein), 4.28% trans-zeaxanthin, 1.94% of beta-carotene, 1.02% of cryptoxanthin and 18.08% cis-isomers & epoxides measured by HPLC) was taken in a 200 Litres capacity extractor with circulation facility. 120 Litres of Food grade hexane with a Gas chromatographic purity of more than 98%, was added to the extractor and circulated. The temperature was raised to about 55° C. and maintained for 1 hour, under circulation. After 1 hour the extract was drained and collected in a miscela tank. The extraction was repeated for two more times each with 120 Litres of Hexane under the same conditions of temperature and time. The extracts obtained were collected in the miscela tank. The fourth and fifth extractions were carried out using 100 Litres of hexane in each extraction under circulation and at a temperature of 58° C. 512 Litres of miscela collected fr

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Abstract

A process for isolation of carotenoids crystals having lutein and zeaxanthin in a weight ratio of about 10:1, 5:1 or 1:1. The process comprises contacting a plant source rich in lutein with hexane and extracting at a temperature of about 40° C. to 60° C. to obtain an oleoresin rich in lutein; contacting a plant source rich in zeaxanthin with hexane and extracting at a temperature of about 40° C. to 60° C. to obtain an oleoresin rich in zeaxanthin. The oleoresin rich in lutein and the oleoresin rich in zeaxanthin are mixed separately in a ratios ranging from about 80:20(w/w) to 90:10(w/w) or about 70:30(w/w) to 30:70(w/w) or about 10:90(w/w) to 20:80(w/w) and homogenized to obtain a mixed oleoresin. The mixed oleoresin is hydrolyzed with an alcoholic alkali at a temperature of about 70° C. to 80° C. to obtain a reaction mixture. The carotenoids crystals are precipitated by adding hot water to the reaction mixture to form a precipitate. Carotenoids crystals having lutein and zeaxanthin in a ratio of about 10:1 or 5:1 or 1:1 respectively are obtained by filtering, washing and drying the precipitate.

Description

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Claims

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Application Information

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Owner KATRA PHYTOCHEM PRIVATE
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