KR102680093B1 - cosmetic manufacturing apparatus - Google Patents

Abstract

The present invention provides an encapsulated channel portion comprising a flow channel; an enzyme supply unit that supplies water-soluble whitening enzyme to the tip of the flow channel; a fat-soluble supply unit disposed at a rear end of the enzyme supply unit and supplying a fat-soluble substance to the flow channel; an aqueous phase supply unit disposed at a rear end of the oil-soluble supply unit and supplying an aqueous substance to the flow channel; and a temperature control unit that supplies heat above the temperature at which the fat-soluble substance is liquefied to the flow channel.

Description

Cosmetic manufacturing apparatus {cosmetic manufacturing apparatus}

The present invention relates to a cosmetic manufacturing device.

In general, enzymes with a whitening effect are water-soluble, and when they come into contact with oxygen in the air, they usually lose their activity or have their activity reduced.

Therefore, it is necessary to block it from external oxygen through encapsulation. Existing cosmetic capsules include hard capsules, soft capsules, and bead-type capsules. However, these capsules have a problem in that the shell is thick, so it is difficult to rupture, and the shell remains on the skin after use, giving a foreign body sensation.

In addition, by using microfluidics to form a W/O/W multi-emulsion, water-soluble whitening enzymes are contained in the innermost water phase and encapsulated on the outside using biodegradable polymers such as PCL (Polycaprolactone) to create a uniform size and thin shell. It can be manufactured, but it is difficult to apply to cosmetics because it uses organic solvents.

There is a need for alternative capsules that do not use organic solvents and do not leave a wall substance on the skin but rather penetrate into the skin and do not cause a foreign body sensation. In addition, according to the previously published patent (application number: 10-2019-0035148), if fat-soluble animal-derived wax, semi-solid wax, and plant-derived semi-solid wax are present in a certain amount or more, the capsule may not be formed uniformly. , it is known that the size may also be non-uniform.

The purpose of the present invention is to provide a cosmetic manufacturing device capable of using a water-soluble whitening enzyme for cosmetics and a fat-soluble semi-solid oil widely used in cosmetics as a capsule wall material.

Meanwhile, the technical problems to be achieved in the present invention are not limited to the technical problems mentioned above, and other technical problems not mentioned will be clearly apparent to those skilled in the art from the description below. It will be understandable.

A cosmetic manufacturing apparatus according to an embodiment of the present invention includes an encapsulation channel portion including a flow channel; an enzyme supply unit that supplies water-soluble whitening enzyme to the tip of the flow channel; a fat-soluble supply unit disposed at a rear end of the enzyme supply unit and supplying a fat-soluble substance to the flow channel; an aqueous phase supply unit disposed at a rear end of the oil-soluble supply unit and supplying an aqueous substance to the flow channel; And it may include a temperature control unit that supplies heat above the temperature at which the fat-soluble material is liquefied to the flow channel.

Additionally, the fat-soluble substance may be maintained in a liquid state at skin temperature and in a semi-solid state at room temperature.

Additionally, the encapsulation channel portion may be disposed inside a body and have an open shape at the rear end, and may include a flow channel sequentially communicating with the enzyme supply portion, the fat-soluble supply portion, and the aqueous phase supply portion.

In addition, the flow channel communicates with the enzyme supply unit, a first channel that provides a flow path for the water-soluble whitening enzyme, and the fat-soluble supply unit communicates with the water-soluble whitening enzyme and the fat-soluble substance at a rear end of the first channel. A second channel providing a flow path and the aqueous phase supply unit communicate with each other, and may include a third channel providing a flow path for the water-soluble whitening enzyme, fat-soluble substances, and aqueous phase substances at a rear end of the second channel.

In addition, the temperature control unit may include a heat exchanger disposed within the body adjacent to the flow channel to exchange heat with the flow channel, and the encapsulation channel may further include a receiving unit for accommodating the heat exchanger.

In addition, the fat-soluble supply unit includes a fat-soluble substance transfer line that provides a path through which the fat-soluble substance is transferred to the flow channel, and the temperature control unit supplies heat above a temperature at which the fat-soluble substance is liquefied to the fat-soluble substance transfer line. It may further include a line heat exchange unit.

Additionally, the fat-soluble substance may include at least one of lanolin, orange wax, palm oil, and bees wax.

According to an embodiment of the present invention, by manufacturing W/O/W multi-capsules using fat-soluble semi-solid oil, which is widely used in cosmetics, as a wall material, there is little irritation to the skin, and when applied to the skin, the capsules are quickly liquefied and do not stick to the skin. It can be easily absorbed, and it is also possible to make capsules that can be applied to cosmetics without using organic solvents. The capsules exist in a solid or semi-solid form at room temperature, so the water-soluble whitening enzyme does not escape to the external water phase and oxygen By blocking contact with the enzyme, the activity of the enzyme can be maintained for a long period of time and the effects of external pH, surfactants, etc. can be minimized.

Meanwhile, the effects that can be obtained from the present invention are not limited to the effects mentioned above, and other effects not mentioned will be clearly understood by those skilled in the art from the description below. You will be able to.

1 is an exemplary diagram schematically showing a cosmetics manufacturing apparatus according to an embodiment of the present invention;
Figure 2 is a cross-sectional view schematically showing the configuration of an encapsulation channel portion in a cosmetics manufacturing device according to an embodiment of the present invention;
Figure 3 is a diagram showing the final W/O/W emulsion made through the first channel (151a), second channel (151b), and third channel (151c) in Figure 2.
Figure 4 is a photograph showing the form of cosmetics manufactured through a cosmetics manufacturing device according to an embodiment of the present invention;
Figure 5 is a cross-sectional view schematically showing the shape of Figure 4,
Figure 6 is an image of cosmetics manufactured through a cosmetics manufacturing device according to an embodiment of the present invention analyzed by Cryo-SEM.
Figure 7 is a graph showing the change in absorbance seen through the reaction between melanin and a capsule contained in a cosmetic manufactured using a cosmetic manufacturing device according to an embodiment of the present invention.
Figure 8 is a photograph analyzing the change in phase of a W/O/W emulsion produced through a cosmetics manufacturing device according to an embodiment of the invention at room temperature (indoor standard) and body temperature range.

Hereinafter, embodiments of the present invention will be described in more detail with reference to the attached drawings. Embodiments of the present invention may be modified in various forms, and the scope of the present invention should not be construed as being limited to the following embodiments. This example is provided to more completely explain the present invention to those skilled in the art. Therefore, the shapes of elements in the drawings are exaggerated to emphasize clearer explanation.

The configuration of the invention to clarify the solution to the problem to be solved by the present invention will be described in detail with reference to the accompanying drawings based on preferred embodiments of the present invention, and the reference numbers to the components in the drawings will be the same. Components are given the same reference numbers even if they are in different drawings, and it is stated in advance that components of other drawings can be cited when necessary when explaining the relevant drawings.

FIG. 1 is an exemplary diagram schematically showing a cosmetics manufacturing device according to an embodiment of the present invention, FIG. 2 is a cross-sectional view schematically showing the configuration of an encapsulation channel portion in a cosmetics manufacturing device according to an embodiment of the present invention, and FIG. 3 is a FIG. 2 is a diagram showing the final W/O/W emulsion made through the first channel (151a), the second channel (151b), and the third channel (151c).

1 to 3, the cosmetics manufacturing apparatus according to an embodiment of the present invention includes an enzyme supply unit 110, a fat-soluble supply unit 120, an aqueous phase supply unit 130, a temperature control unit 140, and an encapsulation channel unit 150. ) may include.

The enzyme supply unit 110 communicates with a pump (pump1) for injecting water-soluble whitening enzyme, etc., and an injection unit (111) disposed at the end of the pump (pump1), and a channel unit ( It may include a whitening enzyme transfer line 112 that transfers up to 150).

Here, the pump (pump1) is preferably 0.01 to 100 μL/min.

Additionally, the diameter of the whitening enzyme transfer line 112 is preferably 1 to 3 mm.

Meanwhile, the diameter of one end of the transfer line (Micro capillary glass tubes) used to send the whitening enzyme to the second channel 151b is 1 to 100 μm, preferably 80 μm. Additionally, the diameter of the other end is 1.1 to 1.2 mm, preferably 1.1 mm.

Here, the water-soluble whitening enzyme may include one of Lignin Peroxidase, Manganese Peroxidase, Versatile Peroxidase, laccase, and Horseradish Peroxidase, which have whitening function.

Meanwhile, in the present invention, various water-soluble substances such as water-soluble fragrances and water-soluble proteins can be supplied and encapsulated through the enzyme supply unit 110, and the substances injected into the core are not limited to whitening enzymes.

The fat-soluble supply part 120 is a pump (pump2) for injecting a fat-soluble semi-solid oily substance, etc., and an injection part (121) disposed at the end of the pump (pump2), and a channel part that communicates with the injection part (121) to encapsulate the fat-soluble substance. It may include a fat-soluble material transfer line 122 that transfers up to 150.

Here, the pump (pump2) is preferably 0.01 to 0.8 mL/min.

In addition, the diameter of the oil-soluble material transfer line 122 is preferably 1 to 3 mm.

Meanwhile, the diameter of both ends of the transfer line (Micro capillary glass tubes) for moving to the third channel 151c through which the aqueous material is supplied is 1.1 to 1.2 mm, preferably 1.1 mm.

Here, the fat-soluble substance may include at least one of animal-derived fat-soluble solid wax, semi-solid wax, liquid oil, and semi-solid plant-derived oil, and specifically, lanolin, orange wax, and palm oil. ) and bees wax.

Meanwhile, these fat-soluble substances may dissolve and exist in a liquid state at around 32°C to 36.5°C, which is the human body temperature, and may exist in a semi-solid state at room temperature.

Here, a semi-solid state refers to a state that appears solid at a certain temperature, but becomes a substance close to a liquid due to a change in molecular structure as the temperature changes, and also refers to a state that melts or softens due to body temperature. The meaning of the present invention is not limited to the above-mentioned invention.

These fat-soluble substances can be transferred in liquid form by the temperature control unit 140, discharged to the outside, and can perform the function of a shell that holds enzymes inside, and when applied to the skin from the outside, the capsule is quickly liquefied and easily applied to the skin. can be absorbed.

The aqueous phase supply unit 130 includes a pump (pump3) for injecting the aqueous phase surrounding the outside of the capsule in which the oil-soluble semi-solid oily substance forms the shell, and injection units (131, 133) disposed at the end of the pump (pump3) and an injection unit ( It may include aqueous material transfer lines 132 and 134 that communicate with the aqueous material 131 and 133 to transport the aqueous material to the encapsulation channel portion 150.

Here, the pump (pump3) is preferably 1mL/min. Meanwhile, the diameter of both ends of the transfer line (Micro capillary glass tubes) for transporting the whitening enzyme core (1) and the shell (2) surrounding the whitening enzyme core (1) is 1.1 to 1.2 mm, preferably 1.1 mm. mm. Additionally, the angle at one end is 1 to 60 degrees, preferably 55 degrees. Here, the water-soluble material consists of a water-soluble solvent, such as purified water, propylene glycol (propylene-8-glycol), and polyethylene glycol. , diphosphoglycerate and glycerin, Sepimaxzen, a type of thickening agent, Carbomer 980 Diglycerin and 1,3-butylene glycol, Tromethamine, 1,2-Hexanediol, It may contain at least one of Butylene Glycol, PEG-60 Hydrogenated Castor Oil, and Phenoxyethanol.

The temperature control unit 140 allows fat-soluble substances to flow in a liquid state to function as a wall agent surrounding the whitening enzyme.

That is, the temperature control unit 140 is connected to the encapsulation channel unit 150 and the fat-soluble substance transfer line 122, and provides a constant temperature to the fat-soluble substance flowing in the encapsulation channel unit 150 and the fat-soluble substance transfer line 122. Thus, it functions to suppress fat-soluble substances from solidifying and maintain a liquid state.

Meanwhile, the temperature control unit 140 may transfer heat to the encapsulation channel unit 150 and the fat-soluble material transfer line 122 in the range of 32°C to 45°C. Through this, the fat-soluble substance is completely liquefied and the whitening enzyme is not denatured.

Referring to FIG. 1, in one example, the temperature control unit 140 may circulate the fruit and transfer heat to the encapsulation channel unit 150 and the fat-soluble material transfer line 122.

In this case, the temperature control unit 140 is a heat exchange unit 141 that provides fruit having a temperature in a set range (32 ℃ to 45 ℃) to the encapsulation channel portion 150, and heat-exchanged fruit in the encapsulation channel portion 150. A recovery unit 142 for recovering, a line heat exchange unit 143, 145 for providing fruit having a temperature in a set range (32 ℃ to 45 ℃) to the fat-soluble material transfer line 122, and a pump 144 (pump4) , It may include a recovery unit 146 that recovers the fruit that has undergone heat exchange in the fat-soluble material transfer line 122.

Meanwhile, although not shown, the temperature control unit 140 may be implemented in a form that transfers heat generated using resistance heat to the encapsulation channel unit 150 and the oil-soluble material transfer line 122.

Each substance transferred from the whitening enzyme transfer line 112, the fat-soluble substance transfer line 122, and the aqueous substance transfer line 132 and 134 sequentially flows into the encapsulation channel unit 150, creating a capsule with a core-shell structure. can be created.

Referring to FIG. 2, the encapsulation channel portion 150 may include a body 151, flow channels 151a, 151b, and 151c, sealing portions 152, 153, and 154, and a receiving portion 155.

The body 151 facilitates internal heat transfer and is preferably made of a lightweight, hard material.

The flow channels (151a, 151b, 151c) have an open rear end shape inside the body 151, and include a whitening enzyme transfer line 112, a fat-soluble substance transfer line 122, and an aqueous substance transfer line 132, 133. These are connected sequentially.

Here, the flow channels 151a, 151b, and 151c may include a first channel 151a, a second channel 151b, and a third channel 151c.

The first channel (151a) is connected to the whitening enzyme transfer line 112 and provides a flow path for the injected water-soluble whitening enzyme, and the second channel (151b) is connected to the fat-soluble substance transfer line 122 to provide a flow path for the injected fat-soluble substance. It provides a flow path for the water-soluble whitening enzyme, and the third channel 151c is connected to the aqueous material transfer lines 132 and 133 to provide a flow path for the injected aqueous material, fat-soluble material, and water-soluble whitening enzyme.

Figure 4 is a photograph showing the form of cosmetics manufactured through a cosmetics manufacturing apparatus according to an embodiment of the present invention, and Figure 5 is a cross-sectional view schematically showing the form of Figure 4. In addition, Figure 6 is an image of cosmetics manufactured through a cosmetics manufacturing device according to an embodiment of the present invention analyzed by Cryo-SEM.

Meanwhile, referring to FIGS. 1 to 6 together, in the process of the whitening enzyme first flowing through the first channel (151a), when a fat-soluble substance is injected into the second channel (151b), the whitening enzyme is injected into the core (1). Clumped into a structure, the fat-soluble substance may have the structure of a shell (2) surrounding the core (1).

In particular, referring to FIGS. 1 to 3, the fat-soluble material is distributed in the whitening enzyme core ( The size of the shell (2) surrounding 1), a capsule with a size of 1 to 1000 μm can be made.

Meanwhile, referring to FIG. 6, the average size of capsules made by the cosmetics manufacturing device according to the above embodiment may be 761.52 μm. However, this is only the average particle size according to the preferred embodiment, which can be changed depending on the flow rate and temperature value of the pump, and is not limited to the present invention.

Thereafter, when the aqueous phase material is injected into the third channel 151c, the plurality of capsules 1 and 2 generated in the second channel 151b may be distributed and arranged within the aqueous phase material 3.

The sealing parts (152, 153, 154) seal between the flow channels (151a, 151b, 151c) and each transfer line (112, 122, 132, 133) to prevent liquid from leaking from the connection part and to prevent air from leaking from the outside. It can prevent foreign substances such as inflow.

The receiving portion 155 secures the heat exchanger 141 to the body 151 so that the heat provided to the heat exchanger 141 can be continuously transferred to the flow channels 151a, 151b, and 151c.

<Example>

1. Manufacturing and method of cosmetics manufacturing equipment

In the present invention, the cosmetic manufacturing device is manufactured by cutting a modern acrylic 3P plate using a laser cutting machine (STCC-460), and then using a UV curing ability tester (SP-V, USHIO) with NOA 65, respectively. Acrylic 3P Plate was attached. In addition, NOA 65, rather than PDMS (polydimethylsiloxane), was used to produce a sturdy cosmetics manufacturing device. In particular, a sturdy cosmetics manufacturing device was manufactured using bolts and nuts (length 30mm × diameter 3mm) to prevent deformation from external forces. .

In the above, the power of the UV curing ability tester is set to 100%, and when bonding one plate, the minimum curing time is 10 minutes and the maximum is 60 minutes, and the appropriate curing time is 30 minutes. Also, when cutting an acrylic 3P plate with a laser cutting machine, set the power to 50~99.9%, and the appropriate cutting power is 85%.

2. Production of Microcapillary Glass Tubes for cosmetics manufacturing equipment

To manufacture Microcapillary Glass Tubes, which are the core of cosmetics manufacturing equipment, Microcapillary Tubes with one end of 1~100μm can be made using Micorhaematocrit capillary tubes (length 75mm×int1.1×ext1.5mm) using an alcohol lamp. Here, the diameter of one end of the Microcapillary Glass Tubes is 1 to 100 μm, preferably 80 μm. Additionally, to make Microcapillary Tubes with one end measuring 80μm, they are pulled out using an alcohol lamp and then processed using sand paper. Sand paper is used from CC-300 to CC-1500. Preferably, Microcapillary Glass Tubes capable of supplying whitening enzyme were manufactured by using CC-800 sand paper and then gradually using CC-1500 sand paper. In particular, the appropriate length after processing the Micorhaematocrit capillary tubes of the whitening enzyme transfer line is 28mm.

In addition, the oil-soluble material transfer line was processed using Micorhaematocrit capillary tubes (length 75mm × int1.1mm × ext1.5mm) using the above sand paper, and the length after processing is preferably 35mm. Here, both ends of the Microcapillary Glass Tubes, the transfer line for oil-soluble substances, are 1.1 mm.

In addition, it was manufactured using Micorhaematocrit capillary tubes (length 75mm × int1.1 × ext1.5mm), a transfer line through which aqueous substances are supplied, and the length after processing is preferably 30mm. In particular, it is desirable to process the angle of one end of the Microcapillary Glass Tubes through which the aqueous material is supplied to 55°.

3. Manufacturing of aqueous substance (solubilized essence)

The winning substance was a solubilized essence formulation among cosmetic formulations.

First, in order to manufacture solubilized essence, which is an aqueous substance, Carbomer 980 and Water (DW) in Table 1 below were measured and mixed using an Azimixer (HS-100D, Daehan Science) at 200 to 1000 RPM for a minimum of 10 minutes and a maximum of 10 minutes. Stir at 60 min, preferably at 500 RPM for 40 min.

Second, measure Tromethamine, 1,2-Hexanediol, Glycerin, and Water (DW) using a homogenizer (POONG LIM Co.) at 100 to 1000 RPM for a minimum of 5 minutes to a maximum of 20 minutes, preferably at 900 RPM for 15 minutes. Stir.

Third, the stirred aqueous solution of cabomer 980 is slowly added to the aqueous solution prepared in the second step and stirred. Since the viscosity increases here, the stirring speed of the homogenizer is 100 to 500 RPM and stirred for at least 10 to 30 min, and preferably 450 RPM for 20 min.

Finally, measure Butylene Glycol, PEG-60 Hydrogenated Castor Oil, and Phenoxyethanol as shown in [Table 1] below, add them to the aqueous solution prepared in the third step above, and stir at a minimum of 3000 to 7000 RPM for 30 minutes. Preferably, stir for 20 minutes at 5000RP.

Finally, degassing is performed using a vacuum pump (GAST Manufacturing lnc.) for a minimum of 1 hour and a maximum of 4 hours. Preferably, degassing is performed for 2.5 hours.

Composition of solubilized essence Country of manufacture, manufacturer INCI wt% Water 74.24 D.W. Glycerin 2 Korea, LG Household & Health Care 1,2-Hexanediol One Korea, Shinan Corporation Tromethamine 0.16 Korea, Goldleben Co., Ltd. 　 　 Water 19.8 D.W. Carbomer 980 0.2 Korea, Goldleben Co., Ltd. 　 　 Butylene Glycol 2 Korea, Wemeco PEG-60 Hydrogenated Castor Oil 0.3 China, Jinlan Pharm-Drugs Technology Co. Phenoxyethanol 0.3 China, Hangzhou Keying Chem Co. 　 　 　 25.76 Total amount (wt%) 100

4. Characteristic evaluation

Figure 7 is a graph showing the change in absorbance seen through the reaction between melanin and a capsule contained in a cosmetic manufactured through a cosmetics manufacturing device according to an embodiment of the present invention, and Figure 8 is a cosmetics manufacturing device according to an embodiment of the invention. This is a photo analyzing the change in phase of the W/O/W emulsion prepared through room temperature (indoor standard) and body temperature range.

First, referring to FIG. 7, the degree of melanin decolorization was measured to verify the whitening effect of a capsule containing the water-soluble whitening enzyme Laccase manufactured through a cosmetic manufacturing device according to an embodiment of the present invention, and specifically, using a UV-vis spectrometer. The absorbance in the range of 400 nm to 700 nm was measured using . Because melanin absorbs all wavelengths, it is difficult to observe specific peaks, but when comparing 0h and 14h after reacting melanin with the capsule, it can be seen that the melanin color decreased by about 15%. Through this, it was proven that the laccase whitening enzyme capsule prepared above has a whitening effect. Here, the concentration of 1.8 mL of melanin solution was 100 ppm, and the absorbance was measured after mixing 50 ppm vanillin solution with the solution and then mixing 1.2 mL of the filtered solution.

In addition, referring to Figure 8, it can be seen that although it maintains a semi-solid form at room temperature (26.42 ℃ based on room temperature), the capsule melts and becomes a single capsule at the human body temperature (32 ~ 36.5 ℃).

In particular, when applying cosmetics to the skin, friction and body temperature are added, so they easily melt and are absorbed into the skin. Here, a temperature control device and a fluorescence microscope were used to confirm that the capsule melts within the human body temperature range. Meanwhile, the Fluorescent lamp of the fluorescence microscope was not used.

In other words, referring to Figure 8, the fact that three capsules melt to form one capsule at 36.5 degrees, which is the body temperature of a person, is to show that melting begins at body temperature, and that the pressure and friction heat used when using cosmetics As a result, the entire capsule is primarily destroyed, and the surface area is expanded, so it can be sufficiently dissolved and absorbed into the skin even at the skin surface temperature.

The above detailed description is illustrative of the present invention. Additionally, the foregoing is intended to illustrate preferred embodiments of the present invention, and the present invention can be used in various other combinations, modifications, and environments. That is, changes or modifications are possible within the scope of the inventive concept disclosed in this specification, the scope equivalent to the written disclosure, and/or the technology or knowledge in the art. The written examples illustrate the best state for implementing the technical idea of the present invention, and various changes required for specific application fields and uses of the present invention are also possible. Accordingly, the detailed description of the invention above is not intended to limit the invention to the disclosed embodiments. Additionally, the appended claims should be construed to include other embodiments as well.

110: Enzyme supply unit
120: Fat-soluble supply unit
130: Water supply department
140: Temperature control unit
150: Encapsulation channel part

Claims (7)

an encapsulated channel portion comprising a flow channel;
an enzyme supply unit that supplies water-soluble whitening enzyme to the tip of the flow channel;
a fat-soluble supply unit disposed at a rear end of the enzyme supply unit and supplying a fat-soluble substance to the flow channel;
an aqueous phase supply unit disposed at a rear end of the oil-soluble supply unit and supplying an aqueous substance to the flow channel; and
It includes a temperature control unit that supplies heat above the temperature at which the fat-soluble material is liquefied to the flow channel,
The fat-soluble substance is maintained in a liquid state at the temperature of human skin and in a semi-solid state at room temperature,
The fat-soluble supply part
comprising a fat-soluble material transfer line that provides a path for the fat-soluble material to be transported to the flow channel;
The temperature control unit
A cosmetics manufacturing device that supplies heat above the temperature at which the fat-soluble material is liquefied to the oil-soluble material transfer line.
delete According to clause 1,
The encapsulation channel unit
body and
A cosmetics manufacturing apparatus disposed inside the body, having an open shape at a rear end, and including a flow channel sequentially communicating with the enzyme supply unit, the fat-soluble supply unit, and the aqueous phase supply unit.
According to clause 3,
The flow channel is,
A first channel communicating with the enzyme supply unit to provide a flow path for the water-soluble whitening enzyme,
a second channel communicating with the fat-soluble supply unit and providing a flow path for the water-soluble whitening enzyme and fat-soluble material at a rear end of the first channel; and
A cosmetics manufacturing apparatus comprising a third channel communicating with the aqueous phase supply unit and providing a flow path for the water-soluble whitening enzyme, fat-soluble substance, and aqueous substance at a rear end of the second channel.
According to clause 3,
The temperature control unit includes a heat exchanger disposed within the body adjacent to the flow channel and exchanging heat with the flow channel,
The cosmetics manufacturing device wherein the encapsulation channel portion further includes a receiving portion that accommodates the heat exchange portion.
According to clause 5,
The temperature control unit
A cosmetics manufacturing device further comprising a line heat exchanger that supplies heat above a temperature at which the oil-soluble material is liquefied to the oil-soluble material transfer line.
According to clause 1,
The oil-soluble substance is a cosmetics manufacturing device comprising at least one of lanolin, orange wax, palm oil, and bees wax.