CN107189849A - A kind of production method of the cosmetic oil based on kardiseed - Google Patents
A kind of production method of the cosmetic oil based on kardiseed Download PDFInfo
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- CN107189849A CN107189849A CN201710250919.XA CN201710250919A CN107189849A CN 107189849 A CN107189849 A CN 107189849A CN 201710250919 A CN201710250919 A CN 201710250919A CN 107189849 A CN107189849 A CN 107189849A
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- ethanol
- extraction
- ethyl acetate
- kardiseed
- seed oil
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K8/00—Cosmetics or similar toiletry preparations
- A61K8/18—Cosmetics or similar toiletry preparations characterised by the composition
- A61K8/30—Cosmetics or similar toiletry preparations characterised by the composition containing organic compounds
- A61K8/31—Hydrocarbons
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K8/00—Cosmetics or similar toiletry preparations
- A61K8/18—Cosmetics or similar toiletry preparations characterised by the composition
- A61K8/30—Cosmetics or similar toiletry preparations characterised by the composition containing organic compounds
- A61K8/49—Cosmetics or similar toiletry preparations characterised by the composition containing organic compounds containing heterocyclic compounds
- A61K8/4973—Cosmetics or similar toiletry preparations characterised by the composition containing organic compounds containing heterocyclic compounds with oxygen as the only hetero atom
- A61K8/498—Cosmetics or similar toiletry preparations characterised by the composition containing organic compounds containing heterocyclic compounds with oxygen as the only hetero atom having 6-membered rings or their condensed derivatives, e.g. coumarin
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K8/00—Cosmetics or similar toiletry preparations
- A61K8/18—Cosmetics or similar toiletry preparations characterised by the composition
- A61K8/30—Cosmetics or similar toiletry preparations characterised by the composition containing organic compounds
- A61K8/64—Proteins; Peptides; Derivatives or degradation products thereof
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K8/00—Cosmetics or similar toiletry preparations
- A61K8/18—Cosmetics or similar toiletry preparations characterised by the composition
- A61K8/92—Oils, fats or waxes; Derivatives thereof, e.g. hydrogenation products thereof
- A61K8/922—Oils, fats or waxes; Derivatives thereof, e.g. hydrogenation products thereof of vegetable origin
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K8/00—Cosmetics or similar toiletry preparations
- A61K8/18—Cosmetics or similar toiletry preparations characterised by the composition
- A61K8/96—Cosmetics or similar toiletry preparations characterised by the composition containing materials, or derivatives thereof of undetermined constitution
- A61K8/97—Cosmetics or similar toiletry preparations characterised by the composition containing materials, or derivatives thereof of undetermined constitution from algae, fungi, lichens or plants; from derivatives thereof
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- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
- C11B1/00—Production of fats or fatty oils from raw materials
- C11B1/02—Pretreatment
- C11B1/04—Pretreatment of vegetable raw material
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
- C11B1/00—Production of fats or fatty oils from raw materials
- C11B1/10—Production of fats or fatty oils from raw materials by extracting
- C11B1/104—Production of fats or fatty oils from raw materials by extracting using super critical gases or vapours
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
- C11B3/00—Refining fats or fatty oils
- C11B3/12—Refining fats or fatty oils by distillation
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- Life Sciences & Earth Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical & Material Sciences (AREA)
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- Epidemiology (AREA)
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- General Health & Medical Sciences (AREA)
- Public Health (AREA)
- Veterinary Medicine (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Wood Science & Technology (AREA)
- Organic Chemistry (AREA)
- Microbiology (AREA)
- Biotechnology (AREA)
- Botany (AREA)
- Mycology (AREA)
- Cosmetics (AREA)
- Fats And Perfumes (AREA)
Abstract
A kind of production method of the cosmetic oil based on kardiseed, belongs to cosmetics processing technique field.The inventive method by kardiseed by drying, be crushed to certain particle size;Add after ethanol and the pretreatment of ethyl acetate microwave radiation technology, supercritical CO is carried out using ethanol and ethyl acetate as entrainer2Extraction, pressure is extraction under the conditions of 20~30MPa, 45~50 DEG C of temperature;Then separated in knockout drum at pressure 3MPa~6MPa, 25~30 DEG C of temperature.After reclaiming ethanol and ethyl acetate through vacuum distillation, extraction oil obtains anti-oxidant safflower seed oil by adding carnosine, Tea Polyphenols and lycopene composite antioxidant after solubilising.This method extraction rate is fast, recovery rate is high, no solvent residue, and the high quality oils water activity of acquisition is low, with anti-oxidant and vegetative cell function, and water retention property and Storage are all good, can be used as in cosmetics of super quality base starting material.
Description
Technical field
The present invention relates to the production method of cosmetic oil, belong to cosmetics processing technique field.
Background technology
General principle:There are a variety of aliphatic acid in kardiseed fat oil about oil-containing 20-45%, oil, importantly linoleic acid, oil
Acid and palmitic acid.Containing saturated fatty acid, linoleic acid, and multivitamin, also containing sterol, flavones, chlorogenic acid, neochlorogenic acid, with
And olefine aldehydr, alkene -1- alcohol, linalool, tetradecanoic acid etc..Simultaneously as containing abundant carrotene, preventing free radical
Invasion cell, the effect with pre- preventing tumor.Therefore, multiple biological activities composition is contained in safflower seed oil, for cosmetics energy
Make soft lubrication, the effect of skin nutrition cell.Lycopene can promote the growth and regeneration of cell, and beauty Eradicates wrinkles maintain skin
The effects such as skin health, anti-aging, skin allergy can be substantially improved, eliminate dry skin and scabies because caused by allergic
Gargalesthesia, makes us feeling relaxed happy.Carnosine can remove the aliphatic acid over oxidation for making cell membrane during oxidative stress and shape
Into active oxygen radical(ROS)And alpha-beta unsaturated aldehyde.The effect that the aging and skin that skin can be prevented are brightened, carnosine
It can prevent free radical from producing, repair skin injury, the function with vegetative cell.
The principle of microwave treatment is to penetrate spe medium using frequency electromagnetic waves, reaches the inside for being extracted material, microwave
Heat energy can be quickly converted to and make the temperature rapid increase of cell interior.When the pressure of cell interior exceedes the ability to bear of cell
When, cell will rupture, and active ingredient is i.e. from intracellular outflow, and be dissolved in spe medium at a lower temperature.
Supercritical CO2The principle of fluid extraction separation is the relation of the solvability using supercritical fluid and its density,
Influence i.e. using pressure and temperature to supercritical fluid solvability and extract.In the supercritical state, will be overcritical
Fluid is contacted with material to be separated, make its selectively polarity size, boiling point height it is different with molecular size range into
Divide and extract successively.Certainly, the extract obtained by each pressure limit of correspondence is unlikely to be single, but can be with control condition
The blending constituent of optimal proportion is obtained, then supercritical fluid is become common gases by the method for decompression, heating, is extracted
Material is then wholly or substantially separated out, so that the purpose of separating-purifying is reached, so supercritical CO2Fluid extraction process is by extracting
Combined with separation process.Supercritical CO2The sharpest edges of fluid extraction are no solvent residues, and natural active matter is obtained
It is effectively maintained.In the present invention, ethanol and ethyl acetate are in supercritical CO2Play entrainer during fluid extraction,
Extraction efficiency can be improved.And different from general organic solvent, provide that ethanol and ethyl acetate are fair according to GB 2760-96
Perhaps the flavorant used, for cosmetics more without toxic side effect.Extraction under the conditions of 45-60 DEG C, high vacuum carry out
The recyclable ethanol of vacuum distillation and ethyl acetate obtain product.The grease extracted at the process conditions has the same of bioactivity
When, its antioxidation activity is low, easy oxidation deterioration.Carnosine, Tea Polyphenols and tomato red have extraordinary antioxygenic property, three
Also there is synergy in the presence of simultaneously, antioxidation activity is greatly improved.But carnosine and Tea Polyphenols do not dissolve in grease, kind
Lycopene is water insoluble, it is impossible to which three is directly added into grease, finds carnosine and Tea Polyphenols being dissolved in after water by studying, plus
The binary compound emulsifying agent for entering HLB value 5-6 monoglyceride and HLB value 12-15 nonionic polyoxyethylene monolaurate can
To promote lycopene to dissolve, add in grease and form the particulate of Water-In-Oil and dispersed, effect very well, then uses ultrasonic wave
Concussion is uniformly mixed so as to obtain the safflower seed oil with antioxidation activity high bioactivity, and it contains abundant nutriment, can be used as
The matrix of cosmetic.
The content of the invention
It is an object of the invention to provide a kind of production method of the cosmetic oil based on kardiseed, for producing cosmetics
Matrix oil.Supercritical CO after being pre-processed by microwave radiation technology2Liquid extraction of safflower oil, addition carnosine, Tea Polyphenols and kind
Lycopene improves antioxidation activity, obtains the active safflower seed oil of antioxidation biology of functionalization.
This method by kardiseed by drying, being crushed to after certain particle size;Add ethanol and ethyl acetate microwave radiation technology is pre-
Processing, uses supercritical CO under certain process conditions afterwards2Second is reclaimed in fluid extraction vegetable oil and active ingredient, vacuum distillation
After alcohol and ethyl acetate, then using raising antioxidation activities such as certain method addition Tea Polyphenols, obtain high with antioxidation activity
The safflower seed oil of bioactivity.The major advantage of this method is red obtained by supercritical carbon dioxide extraction at the process conditions
Flower seed oil, bioactive substance content is high, loses small.Adding has well anti-oxidant after carnosine, Tea Polyphenols and lycopene
Characteristic, the grease produced with this method can make the matrix oil of cosmetics, contain a large amount of bioactivity and nutriment.
The present invention is achieved in that step is as follows.
1)By kardiseed by drying, be crushed to certain particle size.
2)Ethanol and the pretreatment of ethyl acetate microwave radiation technology.
3)Using ethanol and ethyl acetate as entrainer supercritical CO2Fluid extraction.
4)Ethanol and ethyl acetate are reclaimed in vacuum distillation.
5)Add carnosine, Tea Polyphenols and lycopene and improve anti-oxidation characteristics.
The microwave radiation technology pretreatment, refers to and is handled 5-10 minutes in 2450MHz with Microwave Extraction reaction system.
The supercritical CO2Fluid extraction, refers in extractor under the conditions of pressure is 20~30MPa, 45~50 DEG C of temperature
Extraction;Separated in knockout drum at pressure 3MPa~5MPa, 25~30 DEG C of temperature.
The raising inoxidizability.Refer to and carnosine and Tea Polyphenols are dissolved in distilled water, add HLB value 5-6 monoglyceride and HLB
The binary compound emulsifying agent of value 12-15 nonionic polyoxyethylene monolaurate, adds lycopene and heats 30-40 DEG C,
It is allowed to be completely dissolved, above-mentioned solution is slowly added dropwise into the 4th)Walk in the safflower seed oil obtained by extraction and quickly stir, be dispersed into
Uniform single-phase oily liquids, is mixed with ultrasonic oscillation;Carnosine, Tea Polyphenols and the lycopene total content in grease(Quality
Than)It is not less than 0.01%, obtains the active safflower seed oil of antioxidation biology of functionalization.
Its main principle steps:1. by kardiseed by drying, be crushed to certain particle size;2. ethanol and ethyl acetate are micro-
Ripple auxiliary pretreatment;3. carry out supercritical CO using ethanol and ethyl acetate as entrainer in certain process conditions2Fluid extraction.
4. ethanol and ethyl acetate are reclaimed in vacuum distillation;5. adding carnosine, Tea Polyphenols and lycopene improves anti-oxidation characteristics.Use the party
The major advantage of method is supercritical CO at the process conditions2Safflower seed oil obtained by fluid extraction, bioactive substance content
Height, loses small, adding has high anti-oxidation characteristic after carnosine, Tea Polyphenols and lycopene, improves storage phase, prevent from going bad.Should
The grease of method production can make the matrix oil of cosmetics, contain a large amount of bioactivity and nutriment.
Beneficial effects of the present invention:The present invention provides a kind of objectively high bioactivity cosmetics with antioxidation activity
With the production method of oil.This method can efficiently extract high activity safflower seed oil with objective, have compared to solvent extraction without molten
The characteristic of agent residual, has high anti-oxidation activity by adding composite antioxidant, can be used for the life of cosmetic base oil
Production.
Embodiment
The present invention will be described further by following examples.
Embodiment 1.
1)By kardiseed by drying, be crushed to 30 mesh sieve.
2)Ethanol and ethyl acetate submergence are added, Microwave Extraction reaction system is used(Such as the SOS- of French PR OLABO companies
1100 series of products)Handled 5-10 minutes in 2450MHz.
3)Then by said mixture supercritical CO 2 equipment(Such as the U.S. morning 300L type in Guangzhou)Extract 3h, extraction conditions:Extraction
It is extraction under the conditions of 25MPa, 45~50 DEG C of temperature to take pressure in tank;Separated in knockout drum at pressure 3MPa, 25 DEG C of temperature.
4)The lipidic compounds that 3) step is obtained, are vacuumized at 40-50 DEG C, and ethanol and ethyl acetate are reclaimed in vacuum distillation.
5) inoxidizability will be improved.Carnosine and Tea Polyphenols are dissolved in distilled water, HLB value 5-6 monoglyceride and HLB value is added
The binary compound emulsifying agent of 12-15 nonionic polyoxyethylene monolaurate, adds lycopene and heats 30-40 DEG C, make
Be completely dissolved, above-mentioned solution is slowly added dropwise into the 3rd)Walk in the safflower seed oil obtained by extraction and quickly stir, be dispersed into
Even single-phase oily liquids, is mixed with ultrasonic oscillation;Carnosine, Tea Polyphenols and the lycopene total content in grease(Mass ratio)
It is not less than 0.01%, obtains the active safflower seed oil of antioxidation biology of functionalization.
Embodiment 2
1)By kardiseed by drying, be crushed to 30 mesh sieve.
2)Ethanol and ethyl acetate submergence are added, Microwave Extraction reaction system is used(Such as the SOS- of French PR OLABO companies
1100 series of products)Handled 8 minutes in 2450MHz.
3)Then by said mixture supercritical CO 2 equipment(Such as the U.S. morning 300L type in Guangzhou)Extract 2h, extraction conditions:Extraction
It is extraction under the conditions of 25MPa, temperature 45 C to take pressure in tank;Separated in knockout drum at pressure 3MPa, 25 DEG C of temperature.
4)The lipidic compounds that 3) step is obtained, are vacuumized at 50 DEG C, and ethanol and ethyl acetate are reclaimed in vacuum distillation.
5) inoxidizability will be improved.Carnosine and Tea Polyphenols are dissolved in distilled water, HLB value 5-6 monoglyceride and HLB value is added
The binary compound emulsifying agent of 12-15 nonionic polyoxyethylene monolaurate, adds lycopene and heats 40 DEG C, be allowed to
Fully dissolved, above-mentioned solution is slowly added dropwise into the 4th)Walk in the safflower seed oil obtained by extraction and quickly stir, be dispersed into uniform
Single-phase oily liquids, is mixed with ultrasonic oscillation;Carnosine, Tea Polyphenols and the lycopene total content in grease(Mass ratio)It is not low
In 0.3%, the active safflower seed oil of antioxidation biology of functionalization is obtained.
Claims (1)
1. a kind of production method of the cosmetic oil based on kardiseed, its characterization step is as follows:
(1)By kardiseed by drying, be crushed to certain particle size;
(2)Ethanol and the pretreatment of ethyl acetate microwave radiation technology;Appropriate ethanol and ethyl acetate is added in the kardiseed of crushing,
Microwave Pretreatment 3-10 minutes, makes breaking-wall cell:
(3)Supercritical safflower extracting seed oil:By step(2)The mixture of gained is using ethanol and ethyl acetate as entrainer, with super
Critical CO2With extraction under the conditions of 20~30MPa of pressure, 45~50 DEG C of temperature in extractor;Then with pressure in knockout drum
Separated at power 3MPa~4MPa, 25~30 DEG C of temperature;
(4)By step(3)Grease is obtained, at 45-60 DEG C, pumping high vacuum carries out vacuum distillation and reclaims removing ethanol and acetic acid second
Ester, obtains safflower seed oil;
(5)Improve inoxidizability:Carnosine and Tea Polyphenols are dissolved in distilled water, HLB value 5-6 monoglyceride and HLB value 12-15 is added
Nonionic polyoxyethylene monolaurate binary compound emulsifying agent, add lycopene heat 30-40 DEG C, be allowed to complete
Dissolving, above-mentioned solution is slowly added dropwise into step(4)Stir in safflower seed oil obtained by extraction and quickly, be dispersed into uniform list
Phase oily liquids, is mixed with ultrasonic oscillation;Carnosine, Tea Polyphenols and the lycopene mass ratio of total content in grease are not less than
0.01%, obtain the active safflower seed oil of antioxidation biology of functionalization.
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CN201710250919.XA CN107189849A (en) | 2017-04-18 | 2017-04-18 | A kind of production method of the cosmetic oil based on kardiseed |
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CN201710250919.XA CN107189849A (en) | 2017-04-18 | 2017-04-18 | A kind of production method of the cosmetic oil based on kardiseed |
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CN107189849A true CN107189849A (en) | 2017-09-22 |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112545914A (en) * | 2020-12-14 | 2021-03-26 | 刘袭文 | Safflower rich velvet nourishing lipstick |
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2017
- 2017-04-18 CN CN201710250919.XA patent/CN107189849A/en not_active Withdrawn
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112545914A (en) * | 2020-12-14 | 2021-03-26 | 刘袭文 | Safflower rich velvet nourishing lipstick |
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Application publication date: 20170922 |