WO2010071095A1

WO2010071095A1 - Method for producing hydrogel particles

Info

Publication number: WO2010071095A1
Application number: PCT/JP2009/070801
Authority: WO
Inventors: 靖博志田原; 訓史上野; 浩二峯; 公一福田
Original assignee: 花王株式会社
Priority date: 2008-12-17
Filing date: 2009-12-14
Publication date: 2010-06-24
Also published as: CN102256694A; CN102256694B

Abstract

Disclosed is a method for producing hydrogel particles, which comprises a stirring step wherein a liquid dispersion is obtained by providing a mixture, which contains water and components (A)-(C), namely (A) a gelling agent wherein gelation is caused due to thermal reversibility of sol-gel transition, (B) an oily component and (C) a surfactant, with a stirring energy of 200-5,000 (kW × minutes/m³). The hydrogel particles obtained by this production method are suitable for use in toothpastes and the like.

Description

Method for producing hydrogel particles

The present invention relates to a method for producing hydrogel particles and hydrogel particles obtained by the method.

Hydrogel particles produced from a dispersion obtained by emulsifying and dispersing oily components or oily components and solid particles with a surfactant using a gelling agent that causes gelation due to thermoreversibility of the sol-gel include the following: The following are known.

In Patent Document 1, a surfactant such as sodium polyoxyethylene lauryl phosphate is used in an agar solution, and only an oil component or an oil component and talc are stirred by a homomixer (total amount of dispersion: 500 g, homomixer rotation speed: 8000 r). / M, treatment time 1 minute: a dispersion liquid is prepared by the following stirring energy amount = 67 [kW × min / m ³ ]) to form droplets, which are then cooled and solidified to form hydrogel particles Is manufacturing. In Patent Document 2, a hydrophobized powder and an oil component are mixed and dispersed in an agar solution using a surfactant such as polyoxyethylene sorbitan monostearate, and poured into a mold and cooled and solidified.

JP 2002-58990 A JP-A-8-208435

Summary of invention

That is, the gist of the present invention is as follows.
[1] The following components (A) to (C):
(A) a gelling agent in which gelation occurs due to thermoreversibility of the sol-gel;
(B) an oily component, and (C) a surfactant,
And a method for producing hydrogel particles, comprising a stirring treatment step of applying a stirring energy of 200 to 5000 [kW × min / m ³ ] to a mixture containing water to obtain a dispersion; and [2] [1] Hydrogel particles obtained by the production method described in 1. above.

Detailed Description of the Invention

In the above conventional technique, a surfactant is used in order to stably blend oily components and solid particles in an agar solution without causing creaming or sedimentation. However, when hydrogel particles are manufactured using a surfactant, if such a hydrogel particle is blended with an aqueous product, the oil component leaks out of the hydrogel particle during storage and distribution of the product. I understood that. Furthermore, when the hydrogel particles are intended to contain solid particles, the solid particles settle in the dispersion, and the product uniformity cannot be maintained. It has also been found that this causes a blockage.

The present invention relates to providing a method for producing hydrogel particles in which oily components do not leak out of the hydrogel particles even when the medium is blended with water-based products. Furthermore, the present invention relates to providing a method for producing hydrogel particles in which solid particles do not settle in the dispersion. Furthermore, the present invention relates to providing hydrogel particles obtained by such a production method, in which oily components do not leak out of the hydrogel particles and solid particles do not settle in the dispersion.

In view of the above circumstances, as a result of intensive studies by the present inventors, if the stirring energy at the time of preparation of the dispersion is insufficient, leakage of oily components to the outside and solid particles in the dispersion tend to settle. I found out. Furthermore, as a result of further investigations by the present inventors, the present invention was completed by setting the stirring energy at the time of preparation of the dispersion to a specific range.

According to the method for producing hydrogel particles of the present invention, it is possible to produce excellent hydrogel particles in which oily components of the obtained hydrogel particles are not leaked to the outside and solid particles are not precipitated in the dispersion. The excellent effect of being able to be exhibited. These and other advantages of the invention will be apparent from the description below.

As used herein, “hydrogel particles” refers to one or more particles in which an oily component or an oily component and solid particles are dispersed in a hydrogel. Note that the concept of hydrogel particles does not include capsules in which the inner layer and the outer layer are concentric, each consisting of an outer layer that is an outer layer and a core component that is an inner layer.

As used herein, “hydrogel” refers to a gel obtained from a gelling agent using water as a solvent. In addition, “non-crosslinked hydrogel” as used in this specification means that gelation does not occur by reaction with ions, for example, potassium ions or calcium ions, but the gelling agent is agar. This refers to gelation caused by thermoreversibility of sol-gel. The melting temperature of agar in water is generally 75 ° C. or higher, and the main one is 75 to 90 ° C. The gelation temperature when agar is dissolved in water and then cooled is 30 to 45 ° C. .

<(A) component>
The component (A) is a gelling agent that causes gelation due to the thermoreversibility of the sol-gel. For example, agar, gelatin, gellan gum and the like can be mentioned. These can be used alone or in admixture of two or more. Of these, agar is preferred. The jelly strength of the agar used is preferably 68.6 kPa (700 g / cm ² ) or less from the viewpoint of feel during use, and 19.6 kPa (200 g / cm ² ) to 63.7 kPa (650 g / cm ² ). Is more preferable.

Here, the jelly strength is determined by the Nissho Water method. According to the Nissui water method, the jelly strength is determined by preparing a 1.5% by weight aqueous solution of a gelling agent and allowing the aqueous solution to stand for 15 hours at 20 ° C. to solidify the gel. The maximum weight [g] per surface area of 1 cm ² when a load is applied by (manufactured by Kiya Seisakusho Co., Ltd.) and the gel withstands the load for 20 seconds at 20 ° C.

The content of the component (A) in the hydrogel particles is preferably from 0.1 to 8.0% by weight, from the viewpoint of preventing breakage when the hydrogel particles are mixed with a water-based product. 5.0% by weight is more preferred.

<(B) component>
The component (B) is an oily component. The component (B) is preferably a solid fat having a melting point of 35 ° C. or higher and / or a liquid oil having a melting point of less than 35 ° C., for example, fragrances, fats and oils, waxes, hydrocarbons, higher fatty acids, higher alcohols. , One or more components selected from the group consisting of esters, oily medicinal components and silicone oils.

Perfumes include monoterpenes such as menthol or limonene, 1,8-cineole and linalool, citrus fruits such as orange, lemon and grapefruit, fruits such as apple, teas such as tea and green tea, and beans such as coffee Varieties of flavors, spices such as black pepper and curry, mint such as peppermint and spearmint, blended fragrances such as daily, vanilla and cola nuts, essential oils such as orange oil and eucalyptus oil, and extracts. Monoterpenes having high volatility and stability are preferable from the viewpoint of maintaining scent sustainability by preventing leakage from the hydrogel particles. Note that the fragrance is the component (b-1).

Examples of the fats and oils include soybean oil, nutka oil, avocado oil, almond oil, olive oil, cacao butter, sesame oil, persic oil, castor oil, coconut oil, mink oil, beef tallow, pork fat, and other natural fats and oils. Examples thereof include hardened oils obtained by hydrogenating natural fats and oils, and synthetic triglycerides such as myristic acid glyceride and 2-ethylhexanoic acid glyceride.

Examples of waxes include carnauba wax, whale wax, beeswax and lanolin.

Examples of hydrocarbons include liquid paraffin, solid paraffin, ceramide, petrolatum, paraffin, microcrystalline wax, ceresin, squalane and pristane. Hydrocarbons are used as component (b-2).

Examples of higher fatty acids include lauric acid, myristic acid, palmitic acid, stearic acid, behenic acid, oleic acid, linoleic acid, linolenic acid, lanolinic acid, and isostearic acid.

Examples of higher alcohols include lauryl alcohol, cetyl alcohol, stearyl alcohol, behenyl alcohol, oleyl alcohol, lanolin alcohol, cholesterol, isostearyl alcohol and the like.

Examples of the esters include cetyl octanoate, myristyl lactate, isopropyl myristate, octyldodecyl myristate, isopropyl palmitate, isopropyl adipate, butyl stearate, decyl oleate, and isostearyl isostearate.

Examples of oily medicinal ingredients include tocopherol, retinol, ascorbyl palmitate, l-menthol, and triclosan.

Examples of silicone oils include dimethylpolysiloxane, decamethylcyclopentasiloxane, methylphenylpolysiloxane, alkyl acrylate copolymer methylpolysiloxane ester, and the like.

These oil components can be used alone or in admixture of two or more.

When the produced hydrogel particles are blended and stored in an aqueous medium containing a surfactant, it is preferable to include the above hydrocarbons as part of the oil component from the viewpoint of suppressing leakage of the oil component, More preferably, the hydrogen is ceresin, paraffin, or microcrystalline wax.

The content of the component (B) in the hydrogel particles is preferably 1 to 60% by weight, and more preferably 5 to 40% by weight. The content is preferably 1% by weight or more from the viewpoint of exhibiting the effect of the addition of the oil component, and the content is preferably 60% by weight or less from the viewpoint of suppressing the viscosity increase of the dispersion.

In one embodiment, when the fragrance of the component (b1) is used as the component (B), it is preferably used in combination with the hydrocarbon of the component (b2). In this case, the content weight ratio of the component (b2) to the component (b1) (the content weight of the component (b2) / the content weight of the component (b1)) is preferably 1/20 to 12/20, Is more preferably 7.5 / 20, more preferably 1.5 / 20 to 7/20, still more preferably 2/20 to 6.5 / 20, and 2/20 to 6 More preferably, it is / 20. By setting the content weight ratio to 1/20 or more, the fragrance can be held in a suitably sized hydrocarbon crystal, and the fragrance is prevented from flowing out (solubilizing) from the hydrogel particles. be able to. By making the said content weight ratio into 12/20 or less, it can suppress that a fragrance | flavor flows out from a hydrogel particle for the same reason as the above.

<(C) component>
The component (C) is a surfactant and is a component necessary for stably blending the component (B) in the dispersion. Examples of the component (C) include non-ionic surfactants such as polyglycerin fatty acid ester, sucrose fatty acid ester, polyoxyethylene alkyl ether, polyoxyethylene sorbitan fatty acid ester, tetraoleic acid polyoxyethylene sorbit and polyoxyethylene. Hardened castor oil, and anionic surfactants include alkyl sulfates, polyoxyethylene alkyl ether sulfates, polyoxyethylene alkyl acetates, polyoxyethylene alkyl ether phosphates, fatty acid salts, N-acyl taurine salts And cationic surfactants include alkylamine acetate, alkyltrimethylammonium chloride, dialkyldimethylammonium chloride and alkylbenzyldimethylammonium. Chloride and the like, in the zwitterionic surfactant alkyl dimethyl amino acetic acid betaine, alkyl dimethylamine oxide, alkyl carboxymethyl hydroxyethyl imidazolinium betaine, alkyl amidopropyl betaine and enzymatically decomposed lecithin.

(C) A component can be used individually or in mixture of 2 or more types. From the viewpoint of emulsion stability of the oil component and suppression of agar gel strength reduction, the component (C) is preferably an anionic surfactant, more preferably an N-acyl taurine salt, and more preferably sodium N-stearoylmethyl taurate. .

The content of the component (C) in the hydrogel particles is preferably 0.1 to 5.0% by weight, more preferably 0.15 to 3.0% by weight. From the viewpoint of maintaining stability in the dispersion of the component (B) and the component (D), the content is preferably 0.1% by weight or more, and from the viewpoint of avoiding the gel strength reduction of the agar, the content is 5.0. % By weight or less is preferred.

The hydrogel particles in the present invention contain water. The water content in the hydrogel particles is preferably 40 to 90% by weight, more preferably 50 to 80% by weight.

<(D) component>
The hydrogel particles in the present invention may contain solid particles as the component (D). Such solid particles are more preferably water-insoluble, where water-insoluble refers to those having a solubility in water at 25 ° C. of 0.1% by weight or less. The average particle size of the component (D) is preferably 50 μm or less, more preferably 0.01 to 50 μm, even more preferably 0.05 to 20 μm from the viewpoint of suppression of sedimentation. In the present specification, the average particle diameter of the component (D) is a value that can be measured by a laser diffraction / scattering formula unless otherwise specified. In the laser diffraction / scattering type, the median diameter obtained by measurement using a particle size distribution analyzer LA-920 (manufactured by Horiba, Ltd.) is defined as the average particle diameter. Further, the specific gravity of the component (D) with respect to water is preferably 1.1 to 8.0.

Specific examples of the component (D) include pigments, cosmetic powders, and natural polymer powders. These are coloring agents for hydrogel particles, and those in which hydrogel particles are blended in cosmetics are used on the skin. When used, it can function as a feeling-improving agent such as improving the smooth feeling. Examples of pigments include inorganic pigments such as carbon black, talc, kaolin, mica, mica titanium, iron oxide (bengal), yellow iron oxide, black iron oxide, bismuth oxychloride, magnesium silicate, titanium oxide, and calcium carbonate, red Organic pigments such as No. 202, Red No. 204, Red No. 205, Red No. 206, Red No. 219, Red No. 228, Red No. 404, Yellow No. 205, Yellow No. 401, Orange No. 401 and Blue No. 404 are listed. . Examples of the cosmetic powder include talc, kaolin, sericite, calcium carbonate, magnesium carbonate, magnesium silicate, calcium silicate, anhydrous silicic acid, titanium oxide, zinc oxide, titanium mica, silica, zeolite, barium sulfate, calcium phosphate. , Hydroxyapatite, metal soap, polyethylene powder, polystyrene powder and the like. Examples of the natural polymer powder include cellulose powder, chitosan powder, starch powder, silk powder, and crystalline cellulose powder. (D) component can be used individually or in mixture of 2 or more types. Among these, calcium carbonate is more preferable from the viewpoint of foam suppression. Further, the specific gravity of each solid particle with respect to water is in the range of 1.1 to 8.0.

In the dispersion, it is presumed that the (B) component and the (D) component interact with each other. It was considered that a stable dispersion liquid in which neither creaming nor sedimentation occurs can be obtained by balancing the force that the component (B) tries to cream with the force that the component (D) tries to settle. From this viewpoint, the weight ratio of the component (B) / the component (D) is preferably 3/1 to 20/1, more preferably 4/1 to 18/1, and particularly preferably 5/1 to 15/1.

<Other ingredients>
In addition to (A) component, (B) component, (C) component, (D) component, and water, the hydrogel particles in the present invention may contain other substances as necessary. . Examples of such other substances include water-soluble organic compounds such as saccharides, polyhydric alcohols, and water-soluble polymer compounds, preservatives, water-soluble colorants, and antioxidants.

<Method for producing hydrogel particles>
The manufacturing method of the hydrogel particle of this invention has the stirring process process which provides a specific stirring energy to the mixture containing (A) component, (B) component, (C) component, and water, and obtains a dispersion liquid. The dispersion is subjected to a general method such as a dropping method, a spraying method, or a stirring method to form droplets, and then the droplets are cooled and solidified to produce hydrogel particles.

When stirring the mixture, in the present invention, it is essential to apply stirring energy of 200 to 5000 [kW × min / m ³ ] to the mixture. A preferable range of the stirring energy is 230 to 4500 [kW × min / m ³ ], and a more preferable range is 250 to 4200 [kW × min / m ³ ]. The stirring energy is 200 [kW × min / m ³ ] from the viewpoint of suppressing sedimentation of the solid particles in the dispersion and preventing leakage of the oil component when the hydrogel particles are blended into the aqueous medium. Preferably, the stirring energy is 5000 [kW × min / m ³ ] or less from the viewpoint of maintaining the stability of the dispersion, suppressing the increase in viscosity, and avoiding prolonging the production time. Preferably there is. When the viscosity of the dispersion is high, for example, when it exceeds 600 mPa · s, it tends to be difficult to form hydrogel particles.

Further, the apparatus for applying stirring energy to the mixture is not particularly limited, and a known stirring apparatus can be used. However, in order to give such stirring energy, a device capable of exhibiting a high shearing force is required. Therefore, the device is preferably a homomixer, a line mixer, a disper, or the like, and more preferably a homomixer in terms of operation.

In the stirring treatment step, a preferable temperature range is 60 to 90 ° C., and a preferable pH of the dispersion liquid is pH 5.5 to 8.5 (80 ° C.).

The “stirring energy” defined in this specification is stirring power P / V [kW / m ³ ] × time [minutes], and a detailed calculation formula is described in Japanese Patent Application Laid-Open No. 2007-161683. ing. The formula for calculating the stirring energy when using a homomixer is shown in (I).

Stirring energy [kW × min / m ³ ] = [stirring power P (kW)] / [treatment liquid volume V (m ³ )] × stirring time (min) (I)

In the above formula (I), the stirring power P (kW) is calculated by the following experimental formula 1.
Stirring power P (kW) = Np x n ³ x d ⁵ x ρ / 1000 (empirical formula 1)
Here, Np is the power number. When the stirring device is a homomixer, the stirring tank capacity is less than 10L: 1.5, 10L or more: 1.3
n: Stirring speed [-/ sec]
d: Diameter of stirring blade [m]
ρ: Content density [kg / m ³ ]

The dropping method uses the property that a dispersion liquid is discharged from a hole and the discharged dispersion liquid becomes a droplet by its surface tension or interfacial tension, and the droplet is cooled in a gas phase such as air or in a liquid phase. It is a method of forming hydrogel particles by solidifying. In addition, from the viewpoint of forming hydrogel particles having a uniform particle size, it is preferable to vibrate the dispersion discharged from the holes.

The spraying method uses a spray nozzle and discharges (sprays) the dispersion liquid into the gas phase from the spray nozzle, forms droplets by the surface tension, and cools and solidifies the droplets in the gas phase to form hydrogel particles. It is a method of forming.

In the stirring method, the dispersion is poured into a liquid that has a property that does not substantially mix with the dispersion and is adjusted to a temperature equal to or higher than the gelling temperature, and the dispersion is atomized by a shearing force by stirring. This is a method of forming hydrogel particles by utilizing the property of forming droplets and cooling and solidifying the droplets in a liquid that does not substantially mix with the dispersion.

In any of the dropping method, the spraying method, and the stirring method, it is preferable that the temperature of the dispersion at the time of discharging, spraying, or charging is set to a temperature not lower than the gelling temperature and not higher than 100 ° C. Further, from the viewpoint that spherical particles having excellent aesthetics can be easily produced, the temperature of the dispersion is preferably set to a gelling temperature + 10 ° C. or higher, and to a gelling temperature + 20 ° C. or higher. More preferred. The upper limit of this temperature is 100 ° C., which is the boiling point of water. Specifically, the temperature of the dispersion is preferably in the range of 60 to 90 ° C, more preferably in the range of 70 to 80 ° C.

The hydrogel particles formed as described above may be further made into fine hydrogel particles by pulverization or the like, if necessary.

In the production method of the present invention, almost all the components constituting the dispersion form the hydrogel particles as they are, so the content of each component in the dispersion is the content of each component in the hydrogel particles. Can be considered.

<Hydrogel particles>
In the hydrogel particles obtained by the production method of the present invention, the component (B) is dispersed and encapsulated in the continuous phase containing the component (A) and water. The structure of such hydrogel particles can be confirmed, for example, by analyzing an SEM photograph of the hydrogel particles.

The shape of the hydrogel particles obtained by the production method of the present invention is not particularly limited, but preferably has a shape of a rotating body constituted by a curved surface. Here, the “rotary body constituted by a curved surface” means a closed figure constituted by a virtual axis and a continuous curve, rotated by the virtual axis, and has a shape such as a triangular pyramid or a cylinder. Is not included. The shape of the hydrogel particles is more preferably spherical or elliptical from the viewpoint of aesthetics.

The average particle diameter of the hydrogel particles produced according to the present invention and the emulsified diameter of the oil component can be measured by a laser diffraction / scattering method. In the laser diffraction / scattering method, the median diameter measured using a particle size distribution analyzer LA-920 (manufactured by Horiba, Ltd.) is defined as the average particle diameter. The average particle size of the hydrogel particles is preferably 5 to 10,000 μm, more preferably 30 to 3000 μm, and particularly preferably 50 to 1000 μm. The emulsified diameter of the oil component is preferably 0.01 to 20 μm, more preferably 0.02 to 15 μm, and particularly preferably 0.03 to 10 μm.

The viscosity of the dispersion can be measured with a B-type viscometer. The viscosity of the dispersion is not particularly limited, but it is usually 0.1 to 700 mPa · s, preferably 1 to 500 mPa · s at the temperature at the time of discharging, spraying or charging.

Hereinafter, aspects of the present invention will be further described and disclosed by way of examples. This example is merely illustrative of the invention and is not meant to be limiting in any way. The% used in the following examples is% by weight unless otherwise specified.

The viscosity of the dispersion was obtained by measuring the dispersion at 80 ° C. with a B-type viscometer. The average particle diameter of the hydrogel particles was defined as the median diameter measured using a laser diffraction / scattering particle size distribution analyzer LA-920 (manufactured by Horiba, Ltd.).

As a device for mixing and stirring, a homomixer (TK Robotics: manufactured by Primics) was used. The wing diameter was 2.5 cm.

Examples 1 to 4 and Comparative Examples 1 to 5
Solution A and an oil component were prepared as follows. Specific components and blending ratios are shown in Tables 1 and 2. Solution A was prepared by blending each component in ion-exchanged water at room temperature, heating and mixing at 90 ° C. for 30 minutes, and then cooling to 80 ° C. The oil component was prepared by heating and mixing each component at 80 ° C.

Thereafter, an oily component was added to Solution A to obtain a mixture. This mixture was adjusted to 800 g and then charged into a homomixer. By carrying out stirring treatment under the conditions shown in Table 2, stirring energy was applied to each mixture to prepare each dispersion.

A portion of each dispersion obtained was transferred to a transparent container and stored at 80 ° C., and the state of the dispersion after 12 hours was observed. The observation results are shown in Table 2.

On the other hand, while maintaining the temperature of the dispersion liquid at 80 ° C., the remaining amount of each dispersion liquid was measured using a one-fluid nozzle having a pore diameter of 0.9 mm, a flow rate of 18 to 20 L / hr, and a spray pressure of 0.45 to 0. The dispersion was sprayed into cooling air at .75 MPa to form hydrogel particles. Here, the dispersion of Comparative Example 5 had a very high viscosity of 720 mPas, and it was difficult to form particles by the spray method.

3 g of the obtained hydrogel particles were dispersed in 30 g of an aqueous sodium alkyl sulfate solution having a concentration of 1% by weight, and then transferred to a transparent container and left to stand at 50 ° C. for 24 hours to obtain oily components from the hydrogel particles. The presence or absence of leakage was observed. The observation results are shown in Table 2.

The state of the dispersion after 12 hours was evaluated as follows.
Stability: Neither sedimentation of solid particles (pigments) nor separation of oily components was observed in the dispersion.
Pigment sedimentation: In the dispersion liquid, separation of oily components was not observed, but sedimentation of solid particles (pigments) was observed.
Oil separation: In the dispersion liquid, no precipitation of solid particles (pigments) was observed, but separation of oily components was observed.

The presence or absence of leakage of the oil component from the hydrogel particles was evaluated as follows.
Yes: In the aqueous solution containing hydrogel particles, many oily components were observed floating on the water surface.
None: In the aqueous solution containing hydrogel particles, there was almost no floating oily component on the water surface.

As described above, the dispersion liquid containing predetermined components is treated with a stirring energy of 200 to 5000 [kW × min / m ³ ], and then the hydrogel particles are produced from the dispersion liquid. Even when the hydrogel particles were stored in an aqueous solution, it was possible to prevent leakage of oily components, and the stability of the dispersion was excellent (Examples 1 to 4). On the other hand, in the case where the stirring energy during the treatment is outside the range of the present invention, leakage of the oil component from the hydrogel particles cannot be prevented (Comparative Examples 1, 2 and 4), or the stability of the dispersion is poor (Comparative Example 3). Furthermore, in Comparative Example 5, since the amount of stirring energy applied is too much, not only the energy consumption increases, but also the viscosity of the mixture (dispersion) rapidly increases during the stirring process, and it is extremely difficult to continue the stirring process. It became. Due to such an increase in viscosity, hydrogel particles could not be formed in Comparative Example 5.

Further, Table 3 shows the content of each component in the obtained hydrogel particles.

The physical property values and the like of each component used in Examples etc. were as follows:
Bengala Cloisonne average particle size and specific gravity (against water): 1.6 μm, 5.2
Yellow LLXLO average particle size and specific gravity (against water): 1.8 μm, 5.2
Average particle diameter and specific gravity (to water) of Toyo White: 7.0 μm, 2.7.

Examples 5-7
<Example 5>
(A) Component Agar (Ina Food Industries, trade name: AX-200), (C) Component N-stearoylmethyl taurine sodium (Nikko Chemicals, trade name: SMT), and (D) The component calcium carbonate (product name: Toyo White, manufactured by Toyo Denka Kogyo Co., Ltd.) is added to room temperature ion-exchanged water, heated and mixed at 90 ° C. for 30 minutes, and then cooled to 80 ° C. to prepare an aqueous solution A (aqueous) Ingredient) was prepared.

In addition, ceresin (B2) component (manufactured by Nikko Rica Co., Ltd., trade name: ceresin 810K (melting point: 74.1 ° C.)) and l-menthol (b1) component (trade name menthol crystal, manufactured by Takasago Inc.) ) And essential oil (trade name: orange oil manufactured by Ogawa Fragrance Co., Ltd.) were heated and mixed at 80 ° C. to prepare an oil component. The melting point of ceresin is the endothermic peak temperature when DSC (Differential Scanning Calorimeter: Rigaku Co., Ltd., ThermoCplus DSC8230) is used and the heating rate of the sample is 2 ° C./min (the following microscopic temperature). The same applies to crystallin wax and behenyl alcohol).

The amount of each component is 3.00% by weight of the agar component (A), 0.38% by weight of stearoylmethyltaurine Na (C) component, and 4.00% by weight of calcium carbonate (D) component. %, (B2) component ceresin 2.50% by weight, component (b1) l-menthol 10.00% by weight and essential oil 10.00% by weight, and ion-exchanged water was set as the balance. Therefore, the content weight of the component (b2) / the content weight of the component (b1) (content weight ratio) is 2.5 / 20.

An oily component was added to the aqueous solution A to obtain 800 g of a mixture. The mixture was homomixer (manufactured by Primics, trade name: TK Robotics, power number Np = 1.5, stirring blade diameter d = 0. And a stirring blade was rotated at a stirring speed n = 250 times / sec for a stirring time t = 1.5 minutes to prepare a dispersion. Content density of (mixtures) ρ = 950kg / m ^3, and the treatment liquid has a volume V = 0.00084m ^3. Therefore, the stirring power P = 0.217 kW, and the stirring energy is 387 kW × min / m ³ .

Then, the obtained dispersion is sprayed into cooling air at a flow rate of 30 L / hr and a spraying pressure of 1.1 to 1.3 MPa using a one-fluid nozzle having a pore diameter of 0.9 mm, whereby droplets of the dispersion are obtained. Produced hydrogel particles which were cooled and solidified.

<Example 6>
A dispersion was prepared and hydrogel particles were prepared in the same manner as in Example 5 except that the blending amount of ceresin as the component (b2) was 5.00% by weight of the dispersion. (B2) Component weight / (b1) Component weight (content weight ratio) is 5/20.

<Example 7>
A dispersion was prepared and hydrogel particles were prepared in the same manner as in Example 5 except that the blending amount of ceresin as the component (b2) was 10.00% by weight of the dispersion. (B2) Component weight / (b1) Component weight (content weight ratio) is 10/20.

<Example 8>
Instead of ceresin as the component (b2), the microcrystalline wax (product name: Multiwax W-835 (melting point: 77.8 ° C.) manufactured by Sonneborn, Inc.) as the component (b2) has a content of 5.00. A dispersion was prepared and hydrogel particles were prepared in the same manner as in Example 5 except that it was blended so as to be in wt%. (B2) Component weight / (b1) Component weight (content weight ratio) is 5/20.

<Example 9>
(B2) In place of ceresin as component, behenyl alcohol (trade name: Calcoal 220-80 (melting point: 72.0 ° C.) manufactured by Kao Corporation) was blended so that the content in the dispersion was 5.00% by weight. Except for this, a dispersion was prepared in the same manner as in Example 5, and hydrogel particles were prepared.

(Test evaluation method)
<Average particle size of oil component in dispersion>
For the dispersions prepared in each of Examples 5 to 9, the median diameter was measured using a laser diffraction / scattering particle size distribution analyzer LA-920 (manufactured by Horiba, Ltd.), and the oiliness in the dispersion was measured. It was set as the average particle diameter of the component. The average particle size of the oil component is approximately equal to the average particle size of the oil component in the hydrogel particles.

<Average particle size of hydrogel particles>
For the hydrogel particles produced in each of Examples 5 to 9, the median diameter was measured using a laser diffraction / scattering particle size distribution analyzer LA-920 (manufactured by Horiba, Ltd.), and the hydrogel particles were measured. The average particle size was taken.

<Perfume extraction rate>
3 g of the hydrogel particles produced in each of Examples 5 to 9 were collected, dispersed in 27 g of a sodium alkylsulfate aqueous solution having a concentration of 1% by weight, transferred to a screw tube and allowed to stand at 50 ° C. for 24 hours. saved. Then, after separating hydrogel particles and sodium alkyl sulfate aqueous solution with a syringe filter, 10 g of the separated aqueous solution was weighed, 0.5 g of calcium chloride was added and stirred with a stirrer for 10 minutes, and then 10 mL of diethyl ether and an internal standard were added. 1 mL of 1% ethanol solution as a substance was added and stirred with a stirrer for 10 minutes, the ether layer was analyzed by gas chromatography, and the amount of limonene, which is the main component of orange oil, was solubilized on the aqueous solution side was measured.

(Test evaluation results)
Table 4 shows the test results. It can be understood that the hydrogel particles obtained from Examples 5 to 9 can suppress the perfume contained in the hydrogel particles from being solubilized outside the particles even when blended in a product containing a surfactant. .

The present invention described above clearly has many things in the range of identity. Such diversity is not to be considered as departing from the spirit and scope of the invention, and all such modifications that are obvious to those skilled in the art are included within the scope of the following claims.

Claims

The following components (A) to (C):
(A) a gelling agent in which gelation occurs due to thermoreversibility of the sol-gel;
(B) an oily component, and (C) a surfactant,
And a method of producing hydrogel particles, comprising a stirring treatment step of applying a stirring energy of 200 to 5000 [kW × min / m 3 ] to a mixture containing water to obtain a dispersion.
Further, the mixture is
(D) solid particles,
The manufacturing method of Claim 1 containing this.
The component (A) is one or more components selected from the group consisting of agar, gelatin and gellan gum, and the content of the component (A) in the hydrogel particles is 0.1 to 8.0% by weight. The manufacturing method of Claim 1 or 2.
The production method according to any one of claims 1 to 3, wherein the content of the component (B) in the hydrogel particles is 1 to 60% by weight.
The component (C) contains an anionic surfactant, and the content of the component (C) in the hydrogel particles is 0.1 to 5.0% by weight. Manufacturing method.
The production method according to claim 5, wherein the anionic surfactant is an N-acyl taurine salt.
The production method according to any one of claims 2 to 6, wherein the specific gravity of the component (D) with respect to water is 1.1 to 8.0.
The production method according to any one of claims 2 to 7, wherein the component (D) is at least one component selected from the group consisting of pigments, cosmetic powders and natural polymer powders.
The manufacturing method of Claim 8 whose pigment of (D) component is calcium carbonate.
The production method according to any one of claims 2 to 8, wherein the weight ratio of the (B) component / (D) component in the hydrogel particles is 3/1 to 20/1.
A step of discharging the dispersion obtained by the stirring treatment step from the spray nozzle to form droplets, and then cooling and solidifying the droplets;
The production method according to any one of claims 1 to 10, further comprising:
Hydrogel particles obtained by the production method according to any one of claims 1 to 11.