KR20180080126A - Availability Method of producing flavant extract - Google Patents

Abstract

A lyophilization step (40) of lyophilization of the placenta after the heating step (30) and the heating step (30) for heating the placenta after the sedimentation step (20) (50) for pulverizing the lyophilized placenta into a powder state after the lyophilization step (40), and an extraction for performing extraction by adding ether to the powdered placenta after the pulverization step (50) After the removing step (70) and the removing step (70) in which the etherified powder is excluded from the extraction liquid after the step (60) and the extracting step (60), the extract liquid is subjected to reduced pressure drying, And an oil dissolving step (90) for dissolving the dried material in oil after the reduced pressure drying step (80) for obtaining a dried material and the reduced pressure drying step (80). Thereby, it is possible to provide a method for producing a usable flavascent extract that contains a phosphorus-containing component and can be compounded in oily cosmetics or quasi-drugs.

Description

Availability Method of producing flavant extract

The present invention relates to a process for producing an oil-soluble flavant extract which can be formulated into oil-based cosmetics such as foundation, lipstick, oil and cleansing, or quasi-drugs.

Placental extract is widely used as a raw material for cosmetics originating from placenta. However, most of the Placental contained in quasi-drugs and cosmetics on the market is water-soluble extract. The water-soluble flavant extract can not be blended into oily form such as lip cream, foundation and oil cosmetic.

Here, Patent Document 1 discloses a non-rejuvenating nutritional supplement containing a placenta extract extracted from a placenta, fat and oil, and at least one additive selected from the group consisting of collagen, seaweed, plant extract, and royal jelly .

Patent Document 2 discloses a hair styling composition comprising hydrophobic silica, a dispersion liquid in which hydrophobic silica is dispersed, and a hair growth component, wherein a flavant extract can be used as a hair growth component, And is made of a material of oil-solubility.

Patent Document 3 discloses a method for producing a microorganism which comprises (A) a microorganism selected from the group consisting of Morus Nigra Leaf, Magnolia Biondii Flower, Trifolium Pratense, Lupinus Albus Seed, Hypericum One or two selected from the group consisting of Perforatum, Origanum Vulgare Flower, Viola Tricolor, Centaurea Cyanus Flower, Melissa Officinalis, Calendula Officinalis Flower, (B) an oil agent purified by column adsorption purification and / or (C) a whitening component, and olive oil can be used as an emulsion, and whitening component It is described that a flavin extract can be used.

Patent Document 4 discloses a transcutaneous absorption type pregnancy line formation inhibitor containing whey, a fibroblast formation promoting component, and an emulsion, and that a flavanal extract can be used as a fibroblast formation promoting component .

Japanese Laid-Open Patent Publication No. 2016-113442 International Publication No. 2012/105096 Japanese Laid-Open Patent Publication No. 2008-50292 Japanese Patent Application Laid-Open No. 2002-145788

In Patent Document 1, Patent Document 4 discloses that an oil and a plasticine extract are blended, but there is no description about the specific production method of the usable plasticine extract.

It is an object of the present invention to provide a process for producing a usable flavascent extract which contains a phosphorus-containing component and which can be blended with oily cosmetics or quasi-drugs.

A method for producing a usable plastender extract according to the present invention as set forth in claim 1 is characterized by comprising a cadaver step of cutting the placenta, a heating step of heating the placenta which has been sedimented after the cadavering step, A lyophilizing step of lyophilizing the placenta; a lyophilizing step of lyophilising the lyophilized placenta after the lyophilization step; and after the pulverizing step, adding the ether to the pulverized placenta And removing the ether fraction from the extract after the extracting step; and after the removing step, the extract is subjected to reduced-pressure drying to remove the phosphorus-containing component And an oil dissolving step of dissolving the dried material in the oil after the vacuum drying step The.

According to a second aspect of the present invention, in the method for producing an oil-soluble flavental extract according to the first aspect of the present invention, in the extraction step, the extraction temperature is 20 ° C or higher and 60 ° C or lower, The weight of the placenta is 5 times that of the placenta, and the weight is 10 times the weight of the placenta.

According to a third aspect of the present invention, in the method for producing an oil-soluble flavental extract according to the second aspect, in the extraction step, the extraction temperature is 40 ° C or more and 60 ° C or less and the extraction time is 2 hours or less .

The present invention according to claim 4 is characterized in that in the method for producing an oil-soluble flavental extract according to any one of claims 1 to 3, in the heating step, the heating temperature is 110 ° C or more and 135 ° C or less, , The ratio of the dried material dissolved in the oil is 0.1% or more and 5.0% or less.

INDUSTRIAL APPLICABILITY According to the present invention, it is possible to provide a process for producing an oil-soluble flavant extract which contains a phosphorus-containing component and can be incorporated in oily cosmetics.

FIG. 1 is a view showing a manufacturing process of the usability plasticine extract according to the present embodiment.
Fig. 2 is a graph showing the results obtained when the heating temperature in the heating step is 120 ° C and the heating time is 20 minutes to 30 minutes in the production process of the usable plasticine extract and diethyl ether is added to the lyophilized placenta in the extraction step Of phosphorus-containing components per extraction temperature and extraction time.
FIG. 3 is a graph showing the test results of inhibiting the evaporation of skin moisture when 3% of the above-described usable flavascent extract is blended into a gel.

A method of producing an oil-soluble plastender extract according to the first embodiment of the present invention is characterized in that it comprises a sedimentation step for sedimenting the placenta, a heating step for heating the sedimented placenta after the sedimentation step, A lyophilizing process for drying the lyophilized placenta, a lyophilizing process for lyophilizing the placenta after the lyophilization process, an extraction process for adding an ether to the powdered placenta after the powdering process, A step of removing the etherified product from the extract, a step of vacuum drying the extract to remove the etherified product, a step of vacuum drying to obtain a dried product containing the phosphorus containing component, and a step of vacuum drying, And an oil dissolving step of dissolving the oil in the oil.

According to this embodiment, an oil-soluble flavental extract containing a phosphorus-containing component in a predetermined amount or more can be produced. Further, by performing the heat treatment in the heating step before the freeze-drying step, the placental tissue is changed and the extraction efficiency of the phosphorus-containing component is improved.

A second embodiment of the present invention is the method for producing an oil-soluble plastender extract according to the first embodiment of the present invention, wherein in the extraction step, the extraction temperature is 20 ° C or higher and 60 ° C or lower, The weight of the placenta was 5 times the weight of the placenta and 10 times the weight of the placenta.

According to this embodiment, the phosphorus-containing component can be extracted more efficiently.

A third embodiment of the present invention is the method for producing an oil-soluble plastender extract according to the second embodiment, wherein the extraction temperature is 40 ° C or more and 60 ° C or less and the extraction time is 2 hours or less.

According to the present embodiment, it is possible to extract the phosphorus-containing component more efficiently and to avoid deterioration of the phosphorus-containing component.

In a fourth aspect of the present invention, in the method of manufacturing an oil-soluble flavental extract according to any one of the first to third aspects, in the heating step, the heating temperature is 110 ° C or more and 135 ° C or less, In the dissolving step, the ratio of the dried matter to be dissolved in the oil is 0.1% or more and 5.0% or less.

According to this embodiment, an oil-soluble flavental extract containing 0.1 to 0.6% of a phosphorus-containing component can be produced.

[Example]

Hereinafter, a method for producing a usable plastal extract according to an embodiment of the present invention will be described.

BRIEF DESCRIPTION OF THE DRAWINGS Fig. 1 is a process flow chart for producing an oil-soluble flavental extract according to the present embodiment. Fig. The method of manufacturing the usability plasticine extract according to the present embodiment is characterized in that the placenta selecting step 10, the sedimentation step 20, the heating step 30, the freeze-drying step 40, the pulverization step 50, An extraction step 60, a removal step 70, a reduced pressure drying step 80 and an oil dissolution step 90.

First, in the placenta selecting step (10), the placenta which is a raw material of the usable flavant extract is selected.

In the placenta, a placenta of a mammal such as pig, horse, sheep and the like can be used. Among them, a placenta of a pig is selected in this embodiment because the placenta of the pig is particularly excellent in safety.

Next, in the sedan step (20), the skin tissue is removed from the placenta selected in the placenta selecting step (10), and the villus tissue is cut into a mince state.

Next, in the heating step (30), the sedimented placenta is heated in the sedimentation step (20).

In the heating step (30), a high-pressure steam at a temperature of 110 ° C or more and 135 ° C or less under a high-pressure environment is used. For heating using such high-pressure steam, for example, an autoclave or the like can be used.

By the heat treatment in the heating step 30, the extraction efficiency of the phosphorus-containing component in the extraction step 60 is improved.

Usability Although the flavant extract is an extract from a natural product, the sterilization process such as heating or filtration can not be set in a subsequent process such as a water soluble flavor extract in terms of its nature. Here, it is preferable that the heating temperature in the heating step (30) is 110 占 폚 or more and 135 占 폚 or less, and the heating time is 15 minutes or more and 1 hour or less so as to combine the sterilization treatment suitable for the placenta. From the viewpoint of the efficiency of the heat treatment, it is more preferable to set the heating temperature to not less than 120 ° C and not more than 122 ° C, and the heating time to not less than 20 minutes and not more than 30 minutes.

Next, in the freeze-drying step (40), the placenta heated in the heating step (30) is freeze-dried.

By freeze drying, the water content of the placenta is lowered. By reducing the water content of the placenta before the extraction step (60), the separation step other than the etherified part in the removal step (70) is facilitated.

Next, in the pulverization step (50), the lyophilized placenta in the freeze-drying step (40) is pulverized or the like.

By placing the placenta in a powder state, the contact efficiency with the ether can be increased.

Next, in the extraction step (60), ether is added to the powdered placenta in the pulverization step (50) to perform extraction. As the ether, diethyl ether is preferably used from the viewpoint of extractability of the phosphorus-containing component.

In this example, extraction was carried out under the following conditions with respect to each of the case of adding 5 times by weight of diethyl ether to the lyophilized placenta and the case of adding 10 times by weight of diethyl ether to the lyophilized placenta.

[Condition 1] Weight 5 times, extraction temperature: room temperature (25 占 폚), extraction time: 2 hours

[Condition 2] Weight 5 times, extraction temperature: room temperature (25 占 폚), extraction time: 16 hours

[Condition 3] Weight 5 times, extraction temperature: heating (55 占 폚), extraction time: 2 hours

[Condition 4] Weight 10 times, extraction temperature: room temperature (25 占 폚), extraction time: 2 hours

[Condition 5] Weight 10 times, extraction temperature: room temperature (25 占 폚), extraction time: 16 hours

[Condition 6] Weight 10 times, extraction temperature: heating (55 占 폚), extraction time: 2 hours

Since diethyl ether has a boiling point of 36.4 占 폚 at atmospheric pressure, when the temperature is higher than the above, diethyl ether is maintained in a liquid state by blowing nitrogen gas into a pressurized state.

Heating is performed by indirect heating using steam. In order to avoid discoloration and deterioration of the phosphorus-containing component, when the temperature is raised, the extraction time is set to 2 hours or less. Further, although it depends on the extraction temperature and the amount of diethyl ether to be added, the lower limit of the extraction time is preferably 30 minutes or more, more preferably 1 hour or more. When the extraction temperature is high, the extraction efficiency is high. However, if the extraction temperature is too high, the phosphorus-containing component is discolored or deteriorated. Therefore, the extraction temperature in the case of heating is preferably 40 ° C or more and 60 ° C or less, Deg.] C or lower.

Next, in the removing step (70), other than the diethyl etherified powder fraction is removed from the extract liquid extracted in the extracting step (60).

In the freeze-drying step (40), the placenta is lyophilized to reduce the water content of the placenta in advance, whereby other than the diethyl ether powder can be removed by a simple method such as filtration.

Next, in the reduced pressure drying step (80), the filtrate obtained by the filtration in the removal step (70) is subjected to reduced pressure drying.

Thereby, diethyl ether is removed and a dried product containing a phosphorus-containing component is obtained in a paste state.

Fig. 2 (a) is a graph showing the results obtained when the heating temperature in the heating step was 120 캜, the heating time was 20 minutes or more and 30 minutes or less, and 5 times by weight diethyl ether was added to the lyophilized placenta in the extraction step. Fig. 5 is a graph showing the amounts of phosphorus-containing components per extraction temperature and extraction time. Fig. Fig. 2 (b) shows the results obtained when the heating temperature in the heating step was 120 캜, the heating time was 20 minutes or more and 30 minutes or less, and diethyl ether 10 times by weight in the extraction step was added to the lyophilized placenta. Fig. 5 is a graph showing the amounts of phosphorus-containing components per extraction temperature and extraction time. Fig.

In Fig. 2, the highest value is indicated as " 100 " with respect to the amount of the phosphorus-containing component of the dried product obtained in the reduced-pressure drying step.

2, in the case of extracting at room temperature (25 ° C), the condition (condition 5) in which diethyl ether 10 times by weight was added to the lyophilized placenta for extraction for 16 hours was the most efficient, (Condition 3) in which 5 times by weight of diethyl ether is added to the lyophilized placenta and extraction is performed for 2 hours is the most efficient.

Further, under a warming condition, since it can be extracted with a small amount of solvent (diethyl ether), it can be said that it is a very good condition in terms of worker health and environmental load.

Further, since the extraction time under normal temperature conditions is long, the amount of the phosphorus-containing component which is not substantially different from that under the heating condition can be obtained. Therefore, depending on the production environment of the production facility or the like, the extraction under the heating condition or the extraction under the room temperature condition is selected It is possible to do.

In this case, as a comparative example, after the culling step 20, the heating step 30 is omitted, the process proceeds to the freeze-drying step 40, ether is added to the powdered placenta through the powdering step 50, . The extraction conditions were condition 5 (weight 10 times, extraction temperature: room temperature (25 占 폚), extraction time: 16 hours).

As a result, the amount of the phosphorus-containing component in the above-mentioned Examples was set to a heating step (30) in which the heating temperature was 120 ° C and the heating time was 20 minutes or more and 30 minutes or less, The highest value obtained when 10-fold extraction of diethyl ether was carried out in the extraction step 60 through the pulverization step 50 was "100", and it was "64".

In the embodiment, the heating process is performed in the heating process 30 at a heating temperature of 120 ° C and a heating time of 20 minutes or more and 30 minutes or less. After the freeze-drying process 40 and the pulverization process 50, The extraction efficiency of the phosphorus-containing component is about 1.5 times as high as that of the phosphorus-containing component extraction by the heating step (30) because the phosphorus-containing component amount is the result of "97" .

Next, in the oil dissolving step (90), the dried paste obtained in the reduced pressure drying step (80) is dissolved in oil.

As the oil, it is preferable to use olive oil or sesame oil, but other oils may also be used.

The dried paste in paste form is dissolved in olive oil, and if there is a precipitate, it is appropriately removed by filtration or the like to complete the useful plasticine extract.

In the oil dissolving step (90), the ratio of the dried matter to be dissolved in the oil is preferably 0.1% or more and 5.0% or less. As a result, the amount of the phosphorus-containing component contained in the usable flavascent extract can be made 0.1 to 0.6%.

In addition, when the ratio of the dried matter to be dissolved in the oil is 0.5% or more and 2.0% or less, the amount of the phosphorus-containing component contained in the oiliness flavascent extract can be adjusted to 0.2 to 0.5%.

Further, for the analysis of the phosphorus-containing component, the sample was dry-painted (ashed) using an ICP emission spectrochemical analyzer (manufactured by AGILENT TECHNOLOGIES) and then extracted with diluted hydrochloric acid.

To examine the moisturizing effect, the effect of inhibiting the evaporation of skin moisture when 3% of the gel was blended was tested for the usable flavascent extract obtained by the above production method. The results are shown in Fig. At this time, the skin moisture amount at the normal time (when nothing is applied) was set to 0 μS. The test conditions were a temperature of 25 占 폚 and a humidity of 30%. For measurement, a moisture content measuring apparatus SKICON-200EX was used.

As shown in Fig. 3, the oiliness flavascent extract shows higher moisture-holding power than glycerin, squalene, and water-soluble flavant extract.

The usability plasticine extract according to the production method of the present invention can be compounded in oily cosmetics such as foundation, lipstick, oil, cleansing, and the like.

10: Placenta selection process
20: Sedan process
30: Heating process
40: Freeze-drying process
50: Powdering process
60: Extraction process
70: Removal process
80: Vacuum drying process
90: Oil dissolution process

Claims (4)

A sedan process in which the placenta is cut,
A heating step of heating the laid placenta after the sediment step,
A freeze-drying step of freeze-drying the placenta after the heating step;
A lyophilization step of lyophilising the placenta after the lyophilization step,
An extraction step of adding ether to the powdered placenta to perform extraction after the pulverization step,
A removing step of removing, after the extracting step, the etherified powder from the extract,
A reduced pressure drying step of performing reduced pressure drying on the extracted liquid after the removing step to obtain a dried product containing the phosphorus containing component,
Characterized by having an oil dissolving step of dissolving the dried material in an oil after the reduced-pressure drying step. The method according to claim 1,
Wherein the extraction temperature is set to 20 ° C or higher and 60 ° C or lower and the amount of the added ether is changed from 5 times the weight of the powdered placenta to 10 times the weight of the powdered placenta extract . 3. The method of claim 2,
Wherein the extraction temperature is in the range of 40 占 폚 to 60 占 폚 and the extraction time is 2 hours or less in the extraction step. 4. The method according to any one of claims 1 to 3,
In the heating step, the heating temperature is set to 110 ° C or more and 135 ° C or less,
Wherein the ratio of the dried matter dissolved in the oil is 0.1% or more and 5.0% or less in the oil dissolving step.

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