Industrial production method of lycopene microemulsion

A technology of lycopene and production method, which is applied in the field of industrial production of lycopene microemulsion, can solve the problems of lycopene application limitation, microemulsion solvent residue, microemulsion process complexity, etc., and achieve reduction of emulsifier consumption, production The effect of low process temperature and avoiding the increase of emulsifier dosage

Active Publication Date: 2017-01-25
CHENGUANG BIOTECH GRP CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Due to the water insolubility of lycopene, the application of lycopene is greatly limited
At present, in order to improve the hydrophobicity of lycopene, the main methods are: 1) Microcapsule technology: However, due to its insufficient particle size, after the wall material is dissolved, lycopene cannot be well suspended in the aqueous solution, and will soon occur. settlement
2) Microemulsion technology: In the prior art, the preparation of lycopene microemulsion mainly relies on dissolving lycopene crystals in oil or solvent. The process is relatively cumbersome, and high temperature melting or The way of solvent dissolution will not only cause the loss of lycopene, but also the risk of solvent residue
For example, the patent with publication number CN 101991175 A provides a lycopene microemulsion product with high cis-isomer content and its preparation method, which dissolves lycopene in vegetable oil at high temperature (about 150°C) , and then add co-emulsifier, emulsifier and water at 100°C to make a microemulsion; this method is not only cumbersome, but also uses high temperature many times, which can easily cause the loss of lycopene
The patent application with the publication number CN200710024111.6 provides a water-soluble lycopene nano-dispersion product and its preparation method, which dissolves lycopene in an organic solvent, and then adds co-emulsifiers and emulsifiers, through high-pressure The microemulsion is prepared in a homogeneous manner, and then the solvent residue is removed by rotary evaporation; the microemulsion prepared by this method is not only complicated in process, but also has the risk of solvent residue in the obtained microemulsion

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0020] Embodiment 1: The specific process of the industrialized production method of this lycopene microemulsion is as follows.

[0021] Lycopene crystals with a lycopene content of 90wt% are used as raw materials; 30g lycopene crystals, 450g glycerin, 50g lecithin and 9g tea polyphenols are evenly mixed, and then ground in a nano grinder; the grinding speed is 1700r / min, the grinding temperature is 20°C, and the nano-grinding is 60 min; a uniform and fine oil phase is obtained. 234g of water and 117g of Tween 20 were stirred at a speed of 80r / min for 15min at a temperature of 40°C, and mixed uniformly to obtain an aqueous phase. The above-mentioned water phase: oil phase = 1:1.54; slowly add the oil phase to the water phase at 40°C and a rotation speed of 100r / min, then adjust the rotation speed to 600r / min, and stir for 20min to obtain In the lycopene microemulsion, the content of lycopene in the obtained lycopene microemulsion is 3.01wt%, and the loss rate of lycopene is ...

Embodiment 2

[0022] Embodiment 2: The specific process of the industrialized production method of the lycopene microemulsion is as follows.

[0023] Lycopene crystals with a lycopene content of 85wt% are used as raw materials; 50g lycopene crystals, 500g sorbitol, 150g Span 60 and 10g hesperidin are mixed evenly, and then ground in a nano grinder; the grinding speed is 2000r / min, the grinding temperature is 30°C, and the nano-grinding is 30min; a uniform and fine oil phase is obtained. 150 g of water and 75 g of sucrose stearate were stirred at a speed of 100 r / min for 12 min at a temperature of 50° C., and mixed uniformly to obtain an aqueous phase. The above-mentioned water phase: oil phase = 1:3.16; slowly add the oil phase to the water phase at 30°C and a rotation speed of 150r / min, then adjust the rotation speed to 700r / min, and stir for 30min to obtain the obtained Described lycopene microemulsion, the content of lycopene in the gained lycopene microemulsion is 4.53wt%; Wherein the...

Embodiment 3

[0024] Embodiment 3: The specific process of the industrialized production method of the lycopene microemulsion is as follows.

[0025] Lycopene crystals with a lycopene content of 92wt% are used as raw materials; after mixing 90g lycopene crystals, 500g glycerol, 90g lecithin and 20g resveratrol, grind them in a nano grinder; the grinding speed 2500r / min, the grinding temperature is 25°C, nano-grinding for 20min; a uniform and fine oil phase is obtained. 300 g of water and 180 g of Tween 80 were stirred at a speed of 70 r / min for 20 min at a temperature of 45° C., and mixed uniformly to obtain an aqueous phase. The above-mentioned water phase: oil phase = 1:1.46; slowly add the oil phase to the water phase at 50°C and a rotating speed of 120r / min, then adjust the rotating speed to 800r / min, and stir for 25min to obtain the obtained Described lycopene microemulsion, the content of lycopene in the gained lycopene microemulsion is 7.00wt%; Wherein the loss rate of lycopene is 0...

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PUM

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Abstract

The invention discloses an industrial production method of a lycopene microemulsion. The method comprises the following steps: uniformly mixing a lycopene crystal, a co-emulsifier, an oil-soluble emulsifier and an antioxidant to obtain a suspension; carrying out nano grinding on the suspension to obtain an oil phase; uniformly mixing water with a water-soluble emulsifier to obtain a water phase; and finally, uniformly mixing the water phase and oil phase, thereby obtaining the lycopene microemulsion. According to the method, the co-emulsifier and oil-soluble emulsifier are added into the raw material lycopene crystal and subjected to nano grinding to obtain the nano oil suspension, and the nano oil suspension is mixed with the water and water-soluble emulsifier to obtain the lycopene microemulsion. The material treatment capacity is increased, and the industrial production efficiency is enhanced only by grinding the oil phase without using vegetable oil or organic solvent to dissolve the lycopene. The method has the advantages of simple technique and high product safety, can prepare the high-content lycopene microemulsion, is suitable for industrialized continuous production, and has obvious economic benefits.

Description

technical field [0001] The invention belongs to the technical field of natural pigment application, in particular to an industrial production method of lycopene microemulsion. Background technique [0002] Lycopene is one of the carotenoids. There are many double bonds in the lycopene molecule, which has strong physiological functions. For example: lycopene has a strong antioxidant activity, which can avoid the antioxidant damage of cells and prevent the occurrence of cancer. Secondly, lycopene can also prevent the occurrence of cardiovascular and cerebrovascular diseases, and delay aging. [0003] Lycopene is a fat-soluble pigment, easily soluble in lipids and non-polar solvents, insoluble in water, hardly soluble in strong polar solvents such as methanol, ethanol, etc., soluble in aliphatic hydrocarbons, aromatic hydrocarbons and chlorinated hydrocarbons such as Organic solvents such as ethane, benzene, and chloroform. Due to the water insolubility of lycopene, the appl...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): A61K9/107A61K31/01A61K47/10A61K47/22A61K47/26A61K47/46A61P35/00A61P9/10A61P9/00A61P39/06
CPCA61K9/1075A61K31/01A61K47/10A61K47/22A61K47/26A61K47/46
Inventor 张志明安晓东杨丽微李乾丽温盼来
Owner CHENGUANG BIOTECH GRP CO LTD
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