JP6279255B2 - Coating composition and coated product using the coating composition - Google Patents
Coating composition and coated product using the coating composition Download PDFInfo
- Publication number
- JP6279255B2 JP6279255B2 JP2013175993A JP2013175993A JP6279255B2 JP 6279255 B2 JP6279255 B2 JP 6279255B2 JP 2013175993 A JP2013175993 A JP 2013175993A JP 2013175993 A JP2013175993 A JP 2013175993A JP 6279255 B2 JP6279255 B2 JP 6279255B2
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- Prior art keywords
- viscous material
- bubbles
- soluble gas
- gas
- coating composition
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- 239000008199 coating composition Substances 0.000 title claims description 60
- 239000011345 viscous material Substances 0.000 claims description 162
- 238000000034 method Methods 0.000 claims description 39
- 238000004090 dissolution Methods 0.000 claims description 36
- 230000008569 process Effects 0.000 claims description 34
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 25
- 238000004519 manufacturing process Methods 0.000 claims description 23
- 239000000203 mixture Substances 0.000 claims description 21
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims description 20
- 229920006395 saturated elastomer Polymers 0.000 claims description 18
- 230000005587 bubbling Effects 0.000 claims description 15
- 239000001569 carbon dioxide Substances 0.000 claims description 10
- 229910002092 carbon dioxide Inorganic materials 0.000 claims description 10
- GQPLMRYTRLFLPF-UHFFFAOYSA-N Nitrous Oxide Chemical compound [O-][N+]#N GQPLMRYTRLFLPF-UHFFFAOYSA-N 0.000 claims description 9
- 230000015572 biosynthetic process Effects 0.000 claims description 5
- 239000001272 nitrous oxide Substances 0.000 claims description 4
- 239000000463 material Substances 0.000 claims description 3
- 210000004761 scalp Anatomy 0.000 claims description 3
- 239000007789 gas Substances 0.000 description 180
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- 239000000047 product Substances 0.000 description 45
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Landscapes
- Cosmetics (AREA)
Description
本発明は、塗布用組成物に関する。さらに詳しくは、粘性物中に溶解性ガスの気泡が分散している塗布用組成物であって、塗布用組成物中に多量の小さな気泡が分散している塗布用組成物に関する。 The present invention relates to a coating composition. More specifically, the present invention relates to a coating composition in which bubbles of a soluble gas are dispersed in a viscous material, and a large amount of small bubbles are dispersed in the coating composition.
従来、ジェル状の整髪料などの塗布用組成物は、外観的な美しさの向上を目的として組成物中に気泡を分散させ、透明なチューブ容器に充填した製品として市販されている。そして、このような製品の改良を目的として、塗布用組成物中に気泡を分散させる技術や分散した気泡を保持する技術が種々提案されている。 Conventionally, a coating composition such as a gel-like hairdressing agent is commercially available as a product in which bubbles are dispersed in a composition for the purpose of improving the appearance beauty and filled in a transparent tube container. For the purpose of improving such products, various techniques for dispersing bubbles in the coating composition and techniques for holding the dispersed bubbles have been proposed.
例えば、特許文献1には泡入り粘性物の製造方法であって、所定の多孔板を用いることで直径が1〜10mmの泡を安定した状態で均一に混入させることのできる泡入り粘性物の製造方法が記載されている。しかしながら、特許文献1には混入させる気泡を溶解性ガスの気泡とすることについては考慮されておらず、また多量の気泡を混入することについても考慮されていない。 For example, Patent Document 1 discloses a method for producing a foamed viscous material, which is a foamed viscous material in which bubbles having a diameter of 1 to 10 mm can be uniformly mixed in a stable state by using a predetermined porous plate. A manufacturing method is described. However, Patent Document 1 does not take into consideration that bubbles to be mixed are bubbles of a soluble gas, and does not consider mixing a large amount of bubbles.
特許文献2には機能性ジェルの製造方法であって、低粘性の溶液中に微細気泡を送り込み、その後、ゲル化剤の添加によりゲル化せしめることで内部に微細気泡を保持させる製造方法が記載されている。しかしながら、特許文献2の製造方法では水または低粘性の溶液にガスを送り込んだ後でゲル化剤を添加してゲル化させているため、ガスは溶液中に飽和溶解していない。よって、二酸化炭素などの溶解性ガスを用いて機能性ジェルを製造した場合、しばらく静置しておくと微細気泡が水または低粘性の溶液に溶解し、気泡が消えてしまうという問題がある。さらに、微細気泡はナノバブルや、マイクロバブルであり、外観的な美しさの向上という点では問題がある。また、多量の気泡を保持させることは困難という問題がある。 Patent Document 2 describes a method for producing a functional gel, in which fine bubbles are fed into a low-viscosity solution and then gelled by the addition of a gelling agent to retain the fine bubbles inside. Has been. However, in the production method of Patent Document 2, since the gelling agent is added after the gas is fed into water or a low-viscosity solution to cause gelation, the gas is not saturated and dissolved in the solution. Therefore, when a functional gel is produced using a soluble gas such as carbon dioxide, there is a problem that if it is left standing for a while, fine bubbles dissolve in water or a low-viscosity solution, and the bubbles disappear. Furthermore, the fine bubbles are nanobubbles or microbubbles, and there is a problem in terms of improving the appearance beauty. There is also a problem that it is difficult to hold a large amount of bubbles.
特許文献3には粘性組成物を充填する容器として、内容物が接触する部分の酸素透過量を所定の範囲とすることで、粘性組成物中に混入させた気泡の安定性を向上させることが記載されている。しかしながら、特許文献3には気泡を溶解性ガスの気泡とすること、および混入させる気泡の量については考慮されていない。 In Patent Document 3, as a container filled with a viscous composition, the stability of bubbles mixed in the viscous composition can be improved by setting the oxygen permeation amount of the portion in contact with the contents within a predetermined range. Have been described. However, Patent Document 3 does not consider the bubbles to be dissolved gas bubbles and the amount of bubbles to be mixed.
また、特許文献4には水と増粘剤とからなる粘性物に、二酸化炭素が非気泡状態で溶解した二酸化炭素外用組成物およびその製造方法が記載されているが、粘性物に二酸化炭素が溶解しているだけであり二酸化炭素が気泡として分散している組成物については考慮されていない。 Patent Document 4 describes a composition for external use of carbon dioxide in which carbon dioxide is dissolved in a non-bubble state in a viscous material composed of water and a thickener, and a method for producing the same. No consideration is given to compositions that are only dissolved and in which carbon dioxide is dispersed as bubbles.
本発明は上記問題に鑑みてなされたものであり、粘性物中に溶解性ガスの小さな気泡が多量に分散しており、塗布用組成物の外観的な美しさの向上だけでなく、粘性物による効果および溶解性ガスの気泡による効果を有する塗布用組成物および塗布製品を提供することを目的とする。 The present invention has been made in view of the above problems, and a large amount of small bubbles of a soluble gas is dispersed in a viscous material. An object of the present invention is to provide a coating composition and a coated product having the effect of the above and the effect of bubbles of soluble gas.
本発明の塗布用組成物は、粘性物中に溶解性ガスの気泡が分散している塗布用組成物であって、25℃かつ大気圧下において、塗布用組成物1g中に溶解性ガスを含む気泡が0.02〜1.5ml分散していることを特徴とする。 The coating composition of the present invention is a coating composition in which bubbles of a soluble gas are dispersed in a viscous material, and the soluble gas is added to 1 g of the coating composition at 25 ° C. and atmospheric pressure. It is characterized in that 0.02 to 1.5 ml of contained bubbles are dispersed.
前記気泡の直径が0.01〜10mmであることが好ましい。 It is preferable that the bubble has a diameter of 0.01 to 10 mm.
前記粘性物中に溶解性ガスが飽和溶解していることが好ましい。 It is preferable that a soluble gas is saturated and dissolved in the viscous material.
前記溶解性ガスが二酸化炭素ガスであることが好ましい。 The soluble gas is preferably carbon dioxide gas.
前記溶解性ガスが亜酸化窒素ガスであることが好ましい。 The soluble gas is preferably nitrous oxide gas.
前記粘性物の25℃における粘度が1,000〜200,000mPa・sであることが好ましい。 The viscosity of the viscous material at 25 ° C. is preferably 1,000 to 200,000 mPa · s.
また、本発明は前記の塗布用組成物が容器に充填された塗布製品に関する。 The present invention also relates to a coated product in which the coating composition is filled in a container.
さらに、本発明は前記塗布製品の製造方法であって、粘性物に溶解性ガスを大気圧以上の圧力下で溶解させる溶解工程と、圧力を大気圧に戻し、粘性物に溶解した溶解性ガスの一部を気泡化させる気泡化工程とを有することを特徴とする製造方法に関する。 Furthermore, the present invention is a method for producing the coated product, comprising: a dissolving step in which a soluble gas is dissolved in a viscous material under a pressure equal to or higher than atmospheric pressure; and a soluble gas in which the pressure is returned to atmospheric pressure and dissolved in the viscous material And a bubbling step for bubbling a part of the film.
前記気泡化工程を容器内で行うことが好ましい。 It is preferable to perform the aeration process in a container.
本発明によれば、粘性物中に溶解性ガスの小さな気泡が多量に分散しているため、外観的な美しさに優れるだけでなく、粘性物による効果および溶解性ガスの気泡による効果を有する塗布用組成物および塗布製品を提供することができる。 According to the present invention, since small bubbles of soluble gas are dispersed in a large amount in the viscous material, not only is the appearance beautiful, but also the effect of the viscous material and the effect of the bubbles of the soluble gas are obtained. Coating compositions and coated products can be provided.
気泡の直径を0.01〜10mmとすることで、外観的な美しさに一層優れ、粘性物を塗り伸ばしやすい塗布用組成物を提供することができる。 By setting the diameter of the bubbles to 0.01 to 10 mm, it is possible to provide a coating composition that is more excellent in appearance and easily spreads a viscous material.
粘性物中に溶解性ガスが飽和溶解していることで、気泡状態にある溶解性ガスによる効果と合わせて溶解性ガスの効果が最大限得られる塗布用組成物を提供することができる。 Since the soluble gas is saturated and dissolved in the viscous material, it is possible to provide a coating composition that can obtain the maximum effect of the soluble gas in combination with the effect of the soluble gas in the bubble state.
溶解性ガスとして二酸化炭素ガスを使用することにより、外観的な美しさ、粘性物による効果、ならびに二酸化炭素ガスによるマッサージ効果および血行促進効果を有する塗布用組成物を提供することができる。 By using carbon dioxide gas as the soluble gas, it is possible to provide a coating composition having an external beauty, an effect of a viscous material, and a massage effect and blood circulation promoting effect by carbon dioxide gas.
溶解性ガスとして亜酸化窒素ガスを使用することにより、外観的な美しさ、粘性物による効果、ならびに粘性物に含まれる成分に影響されることなく気泡が安定して分散する塗布用組成物を提供することができる。 By using nitrous oxide gas as a soluble gas, it is possible to obtain a coating composition in which bubbles are stably dispersed without being affected by the beauty of the appearance, the effects of viscous materials, and the components contained in the viscous materials. Can be provided.
粘性物の25℃における粘度を1,000〜200,000mPa・sとすることで、静置状態における気泡の移動を防止し、安定して分散させることができるため、外観的な美しさに一層優れた塗布用組成物を提供することができる。 By setting the viscosity of the viscous material at 25 ° C. to 1,000 to 200,000 mPa · s, it is possible to prevent the movement of bubbles in a stationary state and stably disperse, so that the appearance is further improved. An excellent coating composition can be provided.
本発明の塗布製品は、溶解性ガスが気泡状態で分散した塗布用組成物を指先や手のひらなどにとって直接対象物に塗布することができるため、溶解性ガスの効果が得られやすい。 In the coated product of the present invention, since the coating composition in which the soluble gas is dispersed in a bubble state can be directly applied to an object for a fingertip or a palm, the effect of the soluble gas is easily obtained.
本発明の塗布製品の製造方法は、粘性物に溶解性ガスを大気圧以上の圧力で溶解させ、その後、圧力を大気圧に戻し、粘性物に溶解した溶解性ガスの一部を気泡化させることにより、溶解性ガスを粘性物中に容易に飽和溶解させることができ、さらに、均等な大きさの気泡を分散させやすい。 In the method for producing a coated product of the present invention, a soluble gas is dissolved in a viscous material at a pressure higher than atmospheric pressure, and then the pressure is returned to atmospheric pressure, and a part of the dissolved gas dissolved in the viscous material is bubbled. Thus, the soluble gas can be easily saturated and dissolved in the viscous material, and the air bubbles of equal size can be easily dispersed.
また気泡化工程を容器内で行うことにより、気泡が分散した塗布用組成物を容易に製造することができる。 In addition, by performing the bubble forming process in a container, a coating composition in which bubbles are dispersed can be easily produced.
本発明の塗布用組成物は粘性物中に溶解性ガスの気泡が分散している塗布用組成物であって、25℃かつ大気圧下において、塗布用組成物1g中に溶解性ガスを含む気泡が0.02〜1.5ml分散していることを特徴とする。 The coating composition of the present invention is a coating composition in which bubbles of a soluble gas are dispersed in a viscous material, and contains a soluble gas in 1 g of the coating composition at 25 ° C. and atmospheric pressure. It is characterized in that 0.02 to 1.5 ml of bubbles are dispersed.
前記粘性物は、粘性調整剤を基剤に溶解または分散させることで調製することができる。 The viscous material can be prepared by dissolving or dispersing a viscosity modifier in a base.
前記粘性調整剤としては、例えば、水溶性高分子や、固形油分、高粘度の油分などが挙げられる。 Examples of the viscosity modifier include water-soluble polymers, solid oils, and oils with high viscosity.
前記水溶性高分子としては、例えば、キサンタンガム、デキストラン、サクシノグルカン、カードラン、ヒアルロン酸などの微生物系多糖類;カルボキシビニルポリマー、(アクリル酸/イタコン酸ステアレス)コポリマー、(アクリル酸/イタコン酸セテス)コポリマー、(アクリル酸/アミノアクリレート/C10−30アルキルPEG−20イタコン酸)コポリマーなどのアクリル酸とイタコン酸エステルからなる共重合体などの架橋型アクリル系高分子;カラギーナン、グアーガム、ローカストビンガム、クインスシード、ガラクタン、アラビアガム、トラガカントガム、ペクチン、マンナン、デンプンなどの植物系多糖類;メチルセルロース、エチルセルロース、ヒドロキシメチルセルロース、ヒドロキシエチルセルロース、ヒドロキシプロピルセルロース、メチルヒドロキシプロピルセルロース、カルボキシメチルセルロースなどのセルロース系高分子;ゼラチンなどが挙げられる。特に、粘性物中に分散している気泡を安定して保持できる点からは微生物系多糖類、架橋型アクリル系高分子を用いることが好ましく、発泡性が高く粘性物中に気泡を多量に含有させやすいという点からはセルロース系高分子、植物系多糖類を用いることが好ましい。 Examples of the water-soluble polymer include microbial polysaccharides such as xanthan gum, dextran, succinoglucan, curdlan, and hyaluronic acid; carboxyvinyl polymer, (acrylic acid / itaconate steareth) copolymer, (acrylic acid / itaconic acid). Cross-linked acrylic polymers such as copolymers of acrylic acid and itaconic acid esters such as (ceteth) copolymer, (acrylic acid / amino acrylate / C10-30 alkyl PEG-20 itaconic acid) copolymer; carrageenan, guar gum, locust bin gum Plant polysaccharides such as quince seed, galactan, gum arabic, gum tragacanth, pectin, mannan, starch; methylcellulose, ethylcellulose, hydroxymethylcellulose, hydroxyethylcellulose, hydride Hydroxypropyl cellulose, methyl hydroxypropyl cellulose, cellulose polymers such as carboxymethylcellulose; and gelatin. In particular, it is preferable to use microbial polysaccharides and cross-linked acrylic polymers from the viewpoint of stably holding bubbles dispersed in the viscous material, and it has high foamability and contains a large amount of bubbles in the viscous material. It is preferable to use a cellulosic polymer or a plant-based polysaccharide from the viewpoint that it can be easily formed.
また、ゼラチンが溶解した粘性物は温度に依存して粘度が変化する特性、つまり高温で粘度が低く、低温では粘度が高いという特性を有する。そのため、水溶性高分子としてゼラチンを使用する場合は、粘性物の粘度が低く流動性を有する状態で後述する溶解工程および気泡化工程を行い、その後低温にして粘性物の粘度を高くすることで溶解性ガスの気泡の保持性を向上させることができる。 Further, a viscous material in which gelatin is dissolved has a characteristic that the viscosity changes depending on temperature, that is, a viscosity is low at a high temperature and a viscosity is high at a low temperature. Therefore, when gelatin is used as the water-soluble polymer, the viscosity and viscosity of the viscous material are low, the dissolution process and the bubbling process described below are performed, and then the viscosity of the viscous material is increased by lowering the temperature. It is possible to improve the retention of bubbles of the soluble gas.
前記固形油分としては、例えば、ラウリルアルコール、ミリスチルアルコール、セチルアルコール、ステアリルアルコール、アラキルアルコール、ベヘニルアルコール、ラノリンアルコールなどの高級アルコール;ラウリン酸、ミリスチン酸、パルミチン酸、ステアリン酸、ベヘニン酸などの脂肪酸;ワセリン、パラフィンなどの炭化水素;ミツロウ、カルナウバロウ、カンデリラロウなどのロウ類;などが挙げられる。 Examples of the solid oil include higher alcohols such as lauryl alcohol, myristyl alcohol, cetyl alcohol, stearyl alcohol, aralkyl alcohol, behenyl alcohol, and lanolin alcohol; fatty acids such as lauric acid, myristic acid, palmitic acid, stearic acid, and behenic acid. Hydrocarbons such as petrolatum and paraffin; waxes such as beeswax, carnauba wax and candelilla wax; and the like.
また、前記高粘度の油分としては、25℃における粘度が100mPa・s以上のものが挙げられ、例えば、ジメチルポリシロキサン、流動パラフィンなどが挙げられる。 Examples of the high-viscosity oil include those having a viscosity at 25 ° C. of 100 mPa · s or more, such as dimethylpolysiloxane and liquid paraffin.
前記粘性調整剤の含有量は、粘性物中0.1〜20質量%が好ましく、0.5〜15質量%がより好ましい。粘性調整剤の含有量が0.1質量%未満の場合は粘性物を増粘させる効果が得られにくく、粘性物中に溶解性ガスを気泡状態で保持しにくくなる傾向がある。また、20質量%を超える場合はべたつきやすくなり使用感が低下する傾向がある。 The content of the viscosity modifier is preferably from 0.1 to 20 mass%, more preferably from 0.5 to 15 mass% in the viscous material. When the content of the viscosity modifier is less than 0.1% by mass, it is difficult to obtain the effect of thickening the viscous material, and it tends to be difficult to hold the soluble gas in the viscous material in a bubble state. Moreover, when it exceeds 20 mass%, it will become sticky and there exists a tendency for a usability | use_condition to fall.
前記基剤は粘性物の主溶媒であり、溶解性ガスを溶解する、粘性物中に含有した粘性調整剤により粘度を調整し溶解性ガスの気泡を保持するなどの目的で用いられる。 The base is a main solvent for a viscous material, and is used for the purpose of dissolving a soluble gas, adjusting the viscosity with a viscosity adjusting agent contained in the viscous material, and holding the bubbles of the soluble gas.
前記基剤としては、例えば、水、アルコール類、液体油分などが挙げられる。 Examples of the base include water, alcohols, and liquid oil.
前記水としては、例えば、精製水、イオン交換水、海洋深層水などが挙げられる。 Examples of the water include purified water, ion exchange water, and deep sea water.
前記アルコール類としては、例えば、エタノール、プロパノール、イソプロパノールなどの炭素数が2〜3の1価アルコール、エチレングリコール、ジエチレングリコール、プロピレングリコール、ジプロピレングリコール、1,3−ブチレングリコールなどの炭素数が2〜4の2価アルコール、グリセリン、ジグリセリンなどの炭素数が3〜6の3価アルコールなどが挙げられる。 Examples of the alcohol include monohydric alcohols having 2 to 3 carbon atoms such as ethanol, propanol, and isopropanol, ethylene glycol, diethylene glycol, propylene glycol, dipropylene glycol, 1,3-butylene glycol, and the like having 2 carbon atoms. Examples thereof include trihydric alcohols having 3 to 6 carbon atoms such as -4 dihydric alcohols, glycerin, and diglycerin.
前記アルコール類は水と特定の割合で含有する基剤とすることにより、当該基剤に対する溶解性ガスの溶解量が水に対する溶解性ガスの溶解量より低くなるため、後述する気泡化工程を行うことによって粘性物中に溶解している溶解性ガスを気泡化させた後に、溶解性ガスが粘性物中に再度溶解しにくく、気泡を安定に保持することができる。 Since the alcohol contains a base containing water in a specific ratio, the amount of the soluble gas dissolved in the base becomes lower than the amount of the soluble gas dissolved in the water. Thus, after the soluble gas dissolved in the viscous material is bubbled, the soluble gas is difficult to dissolve again in the viscous material, and the bubbles can be held stably.
アルコール類と水とを含有する場合の含有量比(質量比)は1/99〜90/10が好ましい。アルコール類として1価アルコールを含有する場合の1価アルコールと水との含有量比は1/99〜40/60が好ましく、5/95〜35/65がより好ましい。アルコール類として2価アルコールを含有する場合の2価アルコールと水の含有量比が1/99〜90/10が好ましく、5/95〜80/20がより好ましい。 The content ratio (mass ratio) in the case of containing alcohols and water is preferably 1/99 to 90/10. When the monohydric alcohol is contained as the alcohol, the content ratio of the monohydric alcohol to water is preferably 1/99 to 40/60, and more preferably 5/95 to 35/65. When the dihydric alcohol is contained as the alcohol, the content ratio of the dihydric alcohol and water is preferably 1/99 to 90/10, more preferably 5/95 to 80/20.
前記液体油分としては、25℃における粘度が100mPa・s未満のものが挙げられ、例えば、ノルマルヘキサン、イソヘキサン、ケロシン、流動パラフィン、スクワレン、スクワラン、軽質イソパラフィンなどの炭化水素油;アジピン酸ジイソプロピル、コハク酸ジエトキシエチル、コハク酸ジオクチル、ミリスチン酸イソプロピル、パルミチン酸イソプロピル、ミリスチン酸PPG−3ベンジルエーテル、2−エチルヘキサン酸セトステアリル、アジピン酸ジ−2−エチルヘキシルなどのエステル油;メチルポリシロキサン、オクタメチルシクロテトラシロキサン、デカメチルシクロペンタシロキサン、ドデカメチルシクロヘキサシロキサン、メチルシクロポリシロキサン、テトラヒドロテトラメチルシクロテトラシロキサン、オクタメチルトリシロキサン、デカメチルテトラシロキサン、メチルハイドロジェンポリシロキサン、メチルフェニルポリシロキサンなどのシリコーンオイル;オレイン酸、イソステアリン酸などの液体脂肪酸;オレイルアルコールなどの液体の高級アルコール;アボガド油、ツバキ油、トウモロコシ油、ミンク油、オリーブ油、マカダミアナッツ油、シア脂、ナタネ油、ゴマ油、ヒマシ油、アマニ油、サフラワー油、ホホバ油、胚芽油、ヤシ油、バーム油、メドフォーム油などの油脂;などが挙げられる。 Examples of the liquid oil include those having a viscosity of less than 100 mPa · s at 25 ° C., for example, hydrocarbon oils such as normal hexane, isohexane, kerosene, liquid paraffin, squalene, squalane, and light isoparaffin; diisopropyl adipate, succinate Ester oils such as diethoxyethyl acid, dioctyl succinate, isopropyl myristate, isopropyl palmitate, PPG-3 benzyl ether myristate, cetostearyl 2-ethylhexanoate, di-2-ethylhexyl adipate; methyl polysiloxane, octa Methylcyclotetrasiloxane, decamethylcyclopentasiloxane, dodecamethylcyclohexasiloxane, methylcyclopolysiloxane, tetrahydrotetramethylcyclotetrasiloxane, octa Silicone oils such as tiltrisiloxane, decamethyltetrasiloxane, methylhydrogenpolysiloxane, methylphenylpolysiloxane; liquid fatty acids such as oleic acid and isostearic acid; liquid higher alcohols such as oleyl alcohol; avocado oil, camellia oil, corn Oil, mink oil, olive oil, macadamia nut oil, shea fat, rapeseed oil, sesame oil, castor oil, linseed oil, safflower oil, jojoba oil, germ oil, coconut oil, balm oil, medfoam oil, etc .; Can be mentioned.
前記基剤の含有量は、粘性物中70〜99.5質量%が好ましく、75〜99.0質量%がより好ましい。基剤の含有量が70質量%未満の場合は溶解性ガスの溶解量が少なくなる傾向がある。また、99.5質量%を超える場合は他の成分を含有しにくくなる傾向がある。 The content of the base is preferably 70 to 99.5% by mass in the viscous material, and more preferably 75 to 99.0% by mass. When the content of the base is less than 70% by mass, the dissolved amount of the soluble gas tends to decrease. Moreover, when it exceeds 99.5 mass%, it tends to become difficult to contain another component.
また、粘性物の性能や目的などに応じて、種々の有効成分、界面活性剤、pH調整剤、粉体などを含有させることができる。 In addition, various active ingredients, surfactants, pH adjusters, powders, and the like can be included depending on the performance and purpose of the viscous material.
前記有効成分としては、例えば、ポリビニルアルコール、ビニルピロリドン−酢酸ビニル共重合体、(アクリレーツ/アクリル酸アルキル/メタクリル酸エチルアミンオキシド)コポリマー、ビニルピロリドン/N,N−ジメチルアミノエチルメタクリル酸共重合体ジエチル硫酸塩、(アクリル酸オクチルアミド/アクリル酸ヒドロキシプロピル/メタクリル酸ブチルアミノエチル)コポリマー、N−ビニルピロリドン/メタクリルアミド/N−ビニルイミダゾール共重合体、(ジメチルアクリルアミド/アクリル酸ヒドロキシエチル/アクリル酸メトキシエチル)コポリマーなどのスタイリング用樹脂;トウガラシチンキ、アセチルコリン、センブリエキス、ヨウ化ニンニクエキス、イチョウエキス、センブリ抽出エキス、オトギリソウエキス、ミノキシジル、塩化カルプロニウム、スピロノラクトン、ビタミンB6塩酸塩、γ−オリザノール、サークレチン、クロマカリム、セファランチン、ニコランジル、DL−α−トコフェロール、D−α−トコフェロール、酢酸DL−α−トコフェロール、酢酸D−α−トコフェロール、ニコチン酸、DL−α−トコフェロールニコチン酸エステル、ニコチン酸アミド、ニコチン酸ベンジル、ピナシジル血行促進剤;コラーゲン、キシリトール、ソルビトール、マルチトール、ヒアルロン酸、ヒアルロン酸ナトリウム、乳酸ナトリウム、dl−ピロリドンカルボン酸塩、ケラチン、カゼイン、レシチン、尿素などの保湿剤;アニオン性界面活性剤、ノニオン性界面活性剤、両性界面活性剤などの洗浄剤;カチオン性界面活性剤、シリコーン誘導体などのトリートメント剤;パラオキシ安息香酸エステル、安息香酸ナトリウム、フェノキシエタノール、塩化ベンザルコニウム、塩化ベンゼトニウム、塩化クロルヘキシジン、パラクロルメタクレゾールなどの殺菌・防腐剤;パラアミノ安息香酸、パラアミノ安息香酸モノグリセリンエステル、サリチル酸オクチル、サリチル酸フェニル、パラメトキシケイ皮酸イソプロピル、パラメトキシケイ皮酸オクチルなどの紫外線吸収剤;グリシン、アラニン、ロイシン、セリン、トリプトファン、シスチン、システイン、メチオニン、アスパラギン酸、グルタミン酸、アルギニンなどのアミノ酸;レチノール、パルミチン酸レチノール、塩酸ピリドキシン、ニコチン酸ベンジル、ニコチン酸アミド、ニコチン酸dl−α−トコフェロール、ビタミンD2(エルゴカシフェロール)、dl−α−トコフェロール、酢酸dl−α−トコフェロール、パントテン酸、ビオチンなどのビタミン類;アスコルビン酸、α−トコフェロール、ジブチルヒドロキシトルエン、ブチルヒドロキシアニソールなどの酸化防止剤;シャクヤクエキス、ヘチマエキス、バラエキス、レモンエキス、アロエエキス、ショウブ根エキス、ユーカリエキス、セージエキス、茶エキス、海藻エキス、プラセンタエキス、シルク抽出液などの各種抽出液;ラウリルメタクリレート、ゲラニルクロトレート、ミリスチン酸アセトフェノン、酢酸ベンジル、プロピオン酸ベンジル、安息香酸メチル、フェニル酢酸メチルなどの消臭・防臭剤;l−メントール、カンフルなどの清涼剤;クロロヒドロキシアルミニウムなどの制汗剤;酸化亜鉛、アラントインヒドロキシアルミニウム、タンニン酸、クエン酸、乳酸などの収斂剤;アラントイン、グリチルレチン酸、グリチルリチン酸ジカリウム、アズレンなどの抗炎症剤;N,N−ジエチル−m−トルアミド(ディート)、カプリル酸ジエチルアミド、ハーブエキスなどの害虫忌避剤;サリチル酸メチル、インドメタシン、ピロキシカム、フェルビナク、ケトプロフェンなどの消炎鎮痛剤;クロタミトン、d−カンフルなどの鎮痒剤;塩酸ジブカイン、塩酸テトラカイン、リドカイン、塩酸リドカインなどの局所麻酔剤;ジフェンヒドラミン、塩酸ジフェンヒドラミン、マレイン酸クロルフェミラミンなどの抗ヒスタミン剤;合成香料、天然香料などの香料;などが挙げられる。 Examples of the active ingredient include polyvinyl alcohol, vinyl pyrrolidone-vinyl acetate copolymer, (acrylates / alkyl acrylate / methacrylic acid ethylamine oxide) copolymer, vinyl pyrrolidone / N, N-dimethylaminoethyl methacrylic acid copolymer diethyl Sulfate, (octylamide acrylate / hydroxypropyl acrylate / butylaminoethyl methacrylate) copolymer, N-vinylpyrrolidone / methacrylamide / N-vinylimidazole copolymer, (dimethylacrylamide / hydroxyethyl acrylate / methoxy acrylate) Ethyl) copolymer and other styling resins; red pepper tincture, acetylcholine, assembly extract, garlic iodide extract, ginkgo biloba extract, assembly extract, hypericum , Minoxidil, carpronium chloride, spironolactone, vitamin B6 hydrochloride, γ-oryzanol, cerretin, cromakalim, cephalanthin, nicorandil, DL-α-tocopherol, D-α-tocopherol, DL-α-tocopherol acetate, D-α-acetate Tocopherol, nicotinic acid, DL-α-tocopherol nicotinate, nicotinamide, benzyl nicotinate, pinacidil circulation promoter; collagen, xylitol, sorbitol, maltitol, hyaluronic acid, sodium hyaluronate, sodium lactate, dl-pyrrolidonecarboxylic Moisturizers such as acid salts, keratin, casein, lecithin, urea; detergents such as anionic surfactants, nonionic surfactants, amphoteric surfactants; cationic surfactants, silicone derivatives Treatment agents such as the body; bactericides and preservatives such as paraoxybenzoic acid ester, sodium benzoate, phenoxyethanol, benzalkonium chloride, benzethonium chloride, chlorhexidine chloride, parachlormetacresol; paraaminobenzoic acid, monoglycerin ester of paraaminobenzoic acid, UV absorbers such as octyl salicylate, phenyl salicylate, isopropyl paramethoxycinnamate, octyl paramethoxycinnamate; amino acids such as glycine, alanine, leucine, serine, tryptophan, cystine, cysteine, methionine, aspartic acid, glutamic acid, arginine Retinol, retinol palmitate, pyridoxine hydrochloride, benzyl nicotinate, nicotinamide, nicotinic acid dl-α-tocopherol, vitamin Vitamins such as D2 (ergocacyferol), dl-α-tocopherol, dl-α-tocopherol acetate, pantothenic acid, biotin; antioxidants such as ascorbic acid, α-tocopherol, dibutylhydroxytoluene, butylhydroxyanisole; Extracts, loofah extract, rose extract, lemon extract, aloe extract, ginger root extract, eucalyptus extract, sage extract, tea extract, seaweed extract, placenta extract, silk extract, etc .; lauryl methacrylate, geranyl crotolate, myristic acid Deodorizing and deodorizing agents such as acetophenone, benzyl acetate, benzyl propionate, methyl benzoate, methyl phenylacetate; refreshing agents such as l-menthol and camphor; antiperspirants such as chlorohydroxyaluminum Astringents such as zinc oxide, allantoin hydroxyaluminum, tannic acid, citric acid, and lactic acid; anti-inflammatory agents such as allantoin, glycyrrhetinic acid, dipotassium glycyrrhizinate, and azulene; N, N-diethyl-m-toluamide (diet), caprylic acid Pest repellents such as diethylamide and herbal extracts; anti-inflammatory analgesics such as methyl salicylate, indomethacin, piroxicam, ferbinac, ketoprofen; antipruritics such as crotamiton and d-camphor; Anesthetic agents; antihistamines such as diphenhydramine, diphenhydramine hydrochloride, chlorfemiramin maleate; and fragrances such as synthetic fragrances and natural fragrances.
前記有効成分を含有する場合の含有量は、粘性物中0.01〜25質量%が好ましく、0.10〜20質量%がより好ましい。有効成分の含有量が0.01質量%未満の場合は有効成分濃度が低く所望の効果が得られにくくなる傾向がある。また、25質量%を超える場合は有効成分濃度が高くなりすぎて含有する有効成分によっては人体に悪影響を及ぼす恐れがある。 When the active ingredient is contained, the content in the viscous material is preferably 0.01 to 25% by mass, and more preferably 0.10 to 20% by mass. When the content of the active ingredient is less than 0.01% by mass, the active ingredient concentration is low and the desired effect tends not to be obtained. Moreover, when it exceeds 25 mass%, an active ingredient density | concentration becomes high too much and there exists a possibility of having a bad influence on a human body depending on the active ingredient to contain.
前記界面活性剤は、気泡を発生しやすくする、気泡を分散させる、洗浄効果を得るなどの目的で用いられる。 The surfactant is used for the purpose of easily generating bubbles, dispersing bubbles, and obtaining a cleaning effect.
前記界面活性剤としては、例えば、非イオン性界面活性剤、カチオン性界面活性剤、アニオン性界面活性剤、両性界面活性剤、シリコーン系界面活性剤、天然界面活性剤、アミノ酸系界面活性剤などが挙げられる。 Examples of the surfactant include nonionic surfactants, cationic surfactants, anionic surfactants, amphoteric surfactants, silicone surfactants, natural surfactants, amino acid surfactants, and the like. Is mentioned.
非イオン性界面活性剤としては、例えば、ポリオキシエチレン(以下、POEと示す)モノラウレート、POEモノステアレート、POEモノオレエートなどのポリオキシエチレン脂肪酸エステル、POEソルビタンモノラウレート、POEソルビタンモノステアレート、POEソルビタンモノオレエートなどのポリオキシエチレンソルビタン脂肪酸エステル、POEグリセリルモノステアレート、POEグリセリルモノオレエートなどのポリオキシエチレングリセリン脂肪酸エステル、POEソルビットモノラウレート、POEソルビットテトラステアレート、POEソルビットテトラオレエートなどのポリオキシエチレンソルビット脂肪酸エステル、POEセチルエーテル、POEステアリルエーテル、POEオレイルエーテル、POEラウリルエーテル、POEベヘニルエーテル、POEオクチルドデシルエーテル、POEイソセチルエーテル、POEイソステアリルエーテルなどのポリオキシエチレンアルキルエーテル、POE・ポリオキシプロピレン(以下、POPと示す)セチルエーテル、POE・POPデシルテトラデシルエーテルなどのポリオキシエチレンポリオキシプロピレンアルキルエーテル、デカグリセリルモノラウレート、デカグリセリルモノミリステート、デカグリセリルモノステアレート、デカグリセリルモノオレエート、デカグリセリルジオレエート、ヘキサグリセリルモノラウレート、ヘキサグリセリルモノステアレート、ヘキサグリセリルモノオレエートなどのポリグリセリン脂肪酸エステル、ポリオキシエチレン硬化ヒマシ油、ラウリン酸PEG、ステアリン酸PEG、オレイン酸PEG、ジステアリン酸PEG、ジイソステアリン酸PEGなどのポリエチレングリコール脂肪酸エステルなどが挙げられる。 Examples of the nonionic surfactant include polyoxyethylene fatty acid esters such as polyoxyethylene (hereinafter referred to as POE) monolaurate, POE monostearate, and POE monooleate, POE sorbitan monolaurate, and POE sorbitan monostearate. Polyoxyethylene sorbitan fatty acid ester such as POE sorbitan monooleate, POE glyceryl monostearate, polyoxyethylene glycerin fatty acid ester such as POE glyceryl monooleate, POE sorbit monolaurate, POE sorbite tetrastearate, POE sorbit Polyoxyethylene sorbite fatty acid ester such as tetraoleate, POE cetyl ether, POE stearyl ether, POE oleyl ether, POE Polyoxyethylene alkyl ethers such as uril ether, POE behenyl ether, POE octyldodecyl ether, POE isocetyl ether, POE isostearyl ether, POE / polyoxypropylene (hereinafter referred to as POP) cetyl ether, POE / POP decyl tetradecyl Polyoxyethylene polyoxypropylene alkyl ethers such as ether, decaglyceryl monolaurate, decaglyceryl monomyristate, decaglyceryl monostearate, decaglyceryl monooleate, decaglyceryl dioleate, hexaglyceryl monolaurate, hexaglyceryl Monostearate, polyglycerin fatty acid ester such as hexaglyceryl monooleate, polyoxyethylene hydrogenated castor oil, lauric acid P G, PEG stearate, PEG oleate, PEG distearate, polyethylene glycol fatty acid esters such diisostearate PEG and the like.
カチオン性界面活性剤としては、例えば、アルキルアンモニウム塩、塩化ステアリルトリメチルアンモニウム、塩化ラウリルトリメチルアンモニウムなどのアルキルトリメチルアンモニウム塩、塩化ジステアリルジメチルアンモニウムなどのジアルキルジメチルアンモニウム塩、塩化ポリ(N,N’−ジメチル−3,5−メチレンピペリジニウム)、塩化セチルピリジニウムなどのアルキルピリジニウム塩、アルキル四級アンモニウム塩、アルキルジメチルベンジルアンモニウム塩などのアルキルベンジルアンモニウム塩、アルキルイソキノリニウム塩、ジアルキルモルホニウム塩、ポリオキシエチレンアルキルアミン、アルキルアミン塩、ポリアミン脂肪酸誘導体、アミルアルコール脂肪酸誘導体、塩化ベンザルコニウム、塩化ベンゼトニウムなどが挙げられる。 Examples of the cationic surfactant include alkylammonium salts, alkyltrimethylammonium salts such as stearyltrimethylammonium chloride and lauryltrimethylammonium chloride, dialkyldimethylammonium salts such as distearyldimethylammonium chloride, and poly (N, N′-chloride). Dimethyl-3,5-methylenepiperidinium), alkyl pyridinium salts such as cetyl pyridinium chloride, alkyl quaternary ammonium salts, alkyl benzyl ammonium salts such as alkyl dimethyl benzyl ammonium salts, alkyl isoquinolinium salts, dialkyl morphoniums Salt, polyoxyethylene alkylamine, alkylamine salt, polyamine fatty acid derivative, amyl alcohol fatty acid derivative, benzalkonium chloride, benzethoni chloride Beam and the like.
アニオン性界面活性剤としては、例えば、アルキル硫酸塩、ポリオキシエチレンアルキルエーテル硫酸塩、N−アシルアミノ酸塩、N−アシルメチルタウリン塩、ポリオキシエチレンアルキルエーテル酢酸塩、アルキルリン酸塩、ポリオキシエチレンアルキルエーテルリン酸塩、セッケン用素地、ラウリン酸ナトリウム、パルミチン酸ナトリウムなどの脂肪酸セッケン、ラウリル硫酸ナトリウム、ラウリル硫酸カリウムなどの高級アルキル硫酸エステル塩、ポリオキシエチレンラウリル硫酸トリエタノールアミン、ポリオキシエチレンラウリル硫酸ナトリウムなどのアルキルエーテル硫酸エステル塩、ラウロイルサルコシンナトリウムなどのN−アシルサルコシン酸、N−ミリストイル−N−メチルタウリンナトリウム、ヤシ油脂肪酸メチルタウリッドナトリウム、ラウリルメチルタウリッドナトリウムなどの高級脂肪酸アミドスルホン酸塩、ポリオキシエチレンオレイルエーテルリン酸ナトリウム、ポリオキシエチレンステアリルエーテルリン酸などのリン酸エステル塩、ジ−2−エチルヘキシルスルホコハク酸ナトリウム、モノラウロイルモノエタノールアミドポリオキシエチレンスルホコハク酸ナトリウム、ラウリルポリプロピレングリコールスルホコハク酸ナトリウムなどのスルホコハク酸塩、リニアドデシルベンゼンスルホン酸ナトリウム、リニアドデシルベンゼンスルホン酸トリエタノールアミン、リニアドデシルベンゼンスルホン酸ナトリウムなどのアルキルベンゼンスルホン酸塩、硬化ヤシ油脂肪酸グリセリン硫酸ナトリウムなどの高級脂肪酸エステル硫酸エステル塩、ロート油などの硫酸化油、ポリオキシエチレンアルキルエーテルカルボン酸、ポリオキシエチレンアルキルアリルエーテルカルボン酸塩、α−オレフィンスルホン酸塩、高級脂肪酸エステルスルホン酸塩、二級アルコール硫酸エステル塩、高級脂肪酸アルキロールアミド硫酸エステル塩、ラウロイルモノエタノールアミドコハク酸ナトリウム、N−パルミトイルアスパラギン酸ジトリエタノールアミン、カゼインナトリウムなどが挙げられる。 Examples of the anionic surfactant include alkyl sulfate, polyoxyethylene alkyl ether sulfate, N-acyl amino acid salt, N-acyl methyl taurate, polyoxyethylene alkyl ether acetate, alkyl phosphate, polyoxy Ethylene alkyl ether phosphates, soap bases, fatty acid soaps such as sodium laurate and sodium palmitate, higher alkyl sulfates such as sodium lauryl sulfate and potassium lauryl sulfate, polyoxyethylene lauryl sulfate triethanolamine, polyoxyethylene Alkyl ether sulfates such as sodium lauryl sulfate, N-acyl sarcosine acid such as sodium lauroyl sarcosine, N-myristoyl-N-methyl taurate sodium, coconut oil fatty acid methyl Higher fatty acid amide sulfonates such as sodium urid, sodium lauryl methyl tauride, phosphoric acid ester salts such as sodium polyoxyethylene oleyl ether phosphate, polyoxyethylene stearyl ether phosphoric acid, sodium di-2-ethylhexyl sulfosuccinate, Sulfosuccinates such as sodium monolauroyl monoethanolamide polyoxyethylene sulfosulphate, sodium lauryl polypropylene glycol sulfosuccinate, sodium lineardodecylbenzenesulfonate, triethanolamine lineardodecylbenzenesulfonate, alkylbenzenesulfone such as sodium lineardodecylbenzenesulfonate Higher fatty acid ester sulfate ester such as acid salt, hydrogenated coconut oil fatty acid sodium glycerol sulfate Salt, sulfated oil such as funnel oil, polyoxyethylene alkyl ether carboxylic acid, polyoxyethylene alkyl allyl ether carboxylate, α-olefin sulfonate, higher fatty acid ester sulfonate, secondary alcohol sulfate ester salt, higher Examples include fatty acid alkylolamide sulfate, sodium lauroyl monoethanolamide succinate, N-palmitoyl aspartate ditriethanolamine, and sodium caseinate.
両性型界面活性剤としては、例えば、酢酸ベタイン、イミダゾリウムベタイン、2−ウンデシル−N,N,N−(ヒドロキシエチルカルボキシメチル)−2−イミダゾリンナトリウム、2−ココイル−2−イミダゾリニウムヒドロキサイド−1−カルボキシエチロキシ2ナトリウム塩などのイミダゾリン系両性型界面活性剤、2−ヘプタデシル−N−カルボキシメチル−N−ヒドロキシエチルイミダゾリニウムベタイン、ラウリルジメチルアミノ酢酸ベタイン、アルキルベタイン、アミドベタイン、スルホベタインなどのベタイン系両性型界面活性剤などが挙げられる。 Examples of amphoteric surfactants include betaine acetate, imidazolium betaine, 2-undecyl-N, N, N- (hydroxyethylcarboxymethyl) -2-imidazoline sodium, 2-cocoyl-2-imidazolinium hydroxide. Imidazoline-based amphoteric surfactants such as -1-carboxyethyloxy disodium salt, 2-heptadecyl-N-carboxymethyl-N-hydroxyethylimidazolinium betaine, lauryldimethylaminoacetic acid betaine, alkylbetaine, amide betaine, sulfone Examples include betaine amphoteric surfactants such as betaine.
シリコーン系界面活性剤としては、例えば、ポリオキシエチレン・メチルポリシロキサン共重合体、ポリオキシプロピレン・メチルポリシロキサン共重合体、ポリ(オキシエチレン・オキシプロピレン)・メチルポリシロキサン共重合体などが挙げられる。 Examples of the silicone surfactant include polyoxyethylene / methylpolysiloxane copolymer, polyoxypropylene / methylpolysiloxane copolymer, poly (oxyethylene / oxypropylene) / methylpolysiloxane copolymer, and the like. It is done.
天然界面活性剤としては、例えば、レシチン、サポニン、大豆リン脂質、大豆リゾリン脂質液などが挙げられる。 Examples of the natural surfactant include lecithin, saponin, soybean phospholipid, soybean lysophospholipid solution, and the like.
アミノ酸系界面活性剤としては、例えば、N−ヤシ油脂肪酸アシル−L−グルタミン酸トリエタノールアミン、N−ヤシ油脂肪酸アシル−L−グルタミン酸カリウム、N−ヤシ油脂肪酸アシル−L−グルタミン酸ナトリウム、N−ラウロイル−L−グルタミン酸トリエタノールアミン、N−ラウロイル−L−グルタミン酸カリウム、N−ラウロイル−L−グルタミン酸ナトリウム、N−ミリストイル−L−グルタミン酸カリウム、N−ミリストイル−L−グルタミン酸ナトリウムおよびN−ステアロイル−L−グルタミン酸ナトリウムなどのN−アシルグルタミン酸塩、N−ヤシ油脂肪酸アシル−L−グルタミン酸、N−ラウロイル−L−グルタミン酸、N−ステアロイル−L−グルタミン酸などのN−アシルグルタミン酸、N−ヤシ油脂肪酸アシルグリシンカリウム、N−ヤシ油脂肪酸アシルグリシンナトリウムなどのN−アシルグリシン塩、N−ヤシ油脂肪酸アシル−DL−アラニントリエタノールアミンなどのN−アシルアラニン塩などが挙げられる。 Examples of the amino acid surfactant include N-coconut oil fatty acid acyl-L-glutamate triethanolamine, N-coconut oil fatty acid acyl-L-glutamate potassium, N-coconut oil fatty acid acyl-sodium L-glutamate, N- Lauroyl-L-glutamate triethanolamine, N-lauroyl-L-glutamate potassium, N-lauroyl-L-sodium glutamate, N-myristoyl-L-glutamate potassium, N-myristoyl-L-glutamate sodium and N-stearoyl-L N-acyl glutamate such as sodium glutamate, N-acyl glutamic acid such as N-coconut oil fatty acid acyl-L-glutamic acid, N-lauroyl-L-glutamic acid, N-stearoyl-L-glutamic acid, N-coconut oil fat Acyl glycine potassium, N- acyl glycine salts such as N- cocoyl glycine sodium, N- acyl alanine salts such as N- cocoyl -DL- alanine triethanolamine.
前記界面活性剤を含有する場合の含有量は、粘性物中0.05〜20質量%が好ましく、0.1〜15質量%がより好ましい。前記界面活性剤の含有量が0.05質量%未満の場合は界面活性剤を含有する効果が得られない傾向がある。また、20質量%を超える場合はべたつきやすくなり使用感が低下する傾向がある。 When the surfactant is contained, the content in the viscous material is preferably 0.05 to 20% by mass, and more preferably 0.1 to 15% by mass. When the content of the surfactant is less than 0.05% by mass, the effect of containing the surfactant tends not to be obtained. Moreover, when it exceeds 20 mass%, it will become sticky and there exists a tendency for a usability | use_condition to fall.
前記pH調整剤は、カルボキシビニルポリマーなどの架橋型アクリル系高分子を含有する場合は水性基剤のpHを調整して増粘させ粘性物を調製する、脂肪酸を含有する場合は脂肪酸をケン化して脂肪酸石鹸にする、水に溶解しないスタイリング用樹脂を含有する場合は中和して水溶性を付与する、溶媒に溶解しにくい有効成分を溶解しやすくするなどの目的で用いられる。 When the pH adjuster contains a cross-linked acrylic polymer such as carboxyvinyl polymer, the pH of the aqueous base is adjusted to increase the viscosity to prepare a viscous material. When the fatty acid is contained, the fatty acid is saponified. In the case of containing a styling resin that does not dissolve in water, it is used for the purpose of neutralizing and imparting water solubility, or facilitating dissolution of an active ingredient that is difficult to dissolve in a solvent.
前記pH調整剤としては、例えば、トリエタノールアミン(TEA)、ジエタノールアミン(DEA)、モノエタノールアミン(MEA)、ジイソプロパノールアミン(DIPA)、2−アミノ−2−メチル−1−プロパノール(AMP)、2−アミノ−2−メチル−1,3−プロパンジオール(AMPD)などの有機アルカリ;水酸化カリウム、水酸化ナトリウム、水酸化アンモニウムなどの無機アルカリ;クエン酸、グリコール酸、乳酸、リン酸などの有機酸;塩酸などの無機酸;などが挙げられる。 Examples of the pH adjuster include triethanolamine (TEA), diethanolamine (DEA), monoethanolamine (MEA), diisopropanolamine (DIPA), 2-amino-2-methyl-1-propanol (AMP), Organic alkalis such as 2-amino-2-methyl-1,3-propanediol (AMPD); inorganic alkalis such as potassium hydroxide, sodium hydroxide, ammonium hydroxide; citric acid, glycolic acid, lactic acid, phosphoric acid, etc. Organic acids; inorganic acids such as hydrochloric acid; and the like.
前記pH調整剤を含有する場合の含有量としては、粘性物のpHが5〜9、さらには6〜8となる量であることが好ましい。前記架橋型アクリル系高分子を含有する場合で粘性物のpHが5未満の場合は、架橋型アクリル系高分子の架橋が不充分となり粘性物の粘度が高くなりにくくなる傾向がある。また、pHが9以上の場合は皮膚への刺激が生じやすくなる傾向、さらに容器を腐蝕しやすくなる傾向がある。 When the pH adjuster is contained, the content of the viscous material is preferably 5 to 9, more preferably 6 to 8. When the crosslinkable acrylic polymer is contained and the pH of the viscous material is less than 5, there is a tendency that the crosslinkable acrylic polymer is insufficiently crosslinked and the viscosity of the viscous material is difficult to increase. Further, when the pH is 9 or more, there is a tendency that irritation to the skin tends to occur, and further, the container tends to be corroded.
前記粉末は、気泡を発生しやすくする起泡剤、有効成分を担持する担体、保護剤、付着剤、固体潤滑剤などの目的で用いられる。 The powder is used for purposes such as a foaming agent that easily generates bubbles, a carrier carrying an active ingredient, a protective agent, an adhesive, and a solid lubricant.
前記粉末としては、例えば、タルク、酸化亜鉛、カオリン、雲母、炭酸マグネシウム、炭酸カルシウム、ケイ酸亜鉛、ケイ酸マグネシウム、ケイ酸アルミニウム、ケイ酸カルシウム、シリカ、マイカ、ゼオライト、セラミックパウダー、窒化ホウ素などが挙げられる。 Examples of the powder include talc, zinc oxide, kaolin, mica, magnesium carbonate, calcium carbonate, zinc silicate, magnesium silicate, aluminum silicate, calcium silicate, silica, mica, zeolite, ceramic powder, and boron nitride. Is mentioned.
前記粉体を含有する場合の含有量は、粘性物中0.1〜10質量%が好ましく、0.5〜5質量%がより好ましい。粉体の含有量が0.1質量%未満の場合は粉体を含有する効果が得られにくくなる傾向がある。また、10質量%を超える場合は粘性物中で均一に分散しにくくなる傾向がある。 When the powder is contained, the content in the viscous material is preferably 0.1 to 10% by mass, and more preferably 0.5 to 5% by mass. When the content of the powder is less than 0.1% by mass, the effect of containing the powder tends to be difficult to obtain. Moreover, when it exceeds 10 mass%, there exists a tendency for it to become difficult to disperse | distribute uniformly in a viscous material.
本発明に用いられる粘性物は、粘性調整剤を水などの基剤に溶解または分散させて調製することができる。また必要に応じて含有される有効成分などを水やアルコールに溶解させて調製することができる。なお、粘性物には粉体を分散させてもよい。 The viscous material used in the present invention can be prepared by dissolving or dispersing a viscosity modifier in a base such as water. Moreover, the active ingredient etc. which are contained as needed can be prepared by dissolving in water or alcohol. Note that powder may be dispersed in the viscous material.
前記粘性物の25℃における粘度は、1,000〜200,000mPa・sが好ましく、5,000〜180,000mPa・sがより好ましい。粘性物の粘度が1,000mPa・s未満の場合は粘性物中に溶解性ガスを含む気泡が保持されにくくなる傾向がある。また、200,000mPa・sを超える場合は容器から取り出しにくくなるなど、取り扱いが困難となる傾向がある。 The viscosity of the viscous material at 25 ° C. is preferably 1,000 to 200,000 mPa · s, and more preferably 5,000 to 180,000 mPa · s. When the viscosity of the viscous material is less than 1,000 mPa · s, there is a tendency that bubbles containing a soluble gas are hardly retained in the viscous material. Moreover, when it exceeds 200,000 mPa · s, it tends to be difficult to handle such as difficult to take out from the container.
本発明の塗布用組成物は、溶解性ガスを含む気泡を粘性物中に多量に分散、保持していることから外観的な美しさに優れている。この塗布用組成物は、粘性物による効果だけではなく、溶解性ガスによる効果を有する。さらに、気泡の存在により粘性物を塗布面で塗り伸ばしやすくなる。 The coating composition of the present invention is excellent in appearance beauty because a large amount of bubbles containing a soluble gas are dispersed and held in a viscous material. This coating composition has not only an effect due to a viscous material but also an effect due to a soluble gas. Further, the presence of bubbles makes it easy to spread the viscous material on the application surface.
本発明における溶解性ガスとは、溶媒への溶解量が多いガス(例えば、水に対するオストワルド係数が0.5以上である)であり、例えば、二酸化炭素ガス(オストワルド係数:0.83)、亜酸化窒素ガス(オストワルド係数:0.59)、およびこれらの混合ガスなどが挙げられる。なかでもpH調整剤などの配合成分に関係なく、溶解性ガスの気泡が粘性物中で安定した大きさで分散するという点からは亜酸化窒素ガスが好ましく、マッサージ効果および血行促進効果が得られるという点からは二酸化炭素ガスが好ましい。 The soluble gas in the present invention is a gas having a large amount dissolved in a solvent (for example, the Ostwald coefficient with respect to water is 0.5 or more), for example, carbon dioxide gas (Ostwald coefficient: 0.83), Nitrogen oxide gas (Ostwald coefficient: 0.59), and mixed gas thereof can be used. Among them, nitrous oxide gas is preferable from the viewpoint that the bubbles of the soluble gas disperse in a stable size in the viscous material regardless of the blending components such as a pH adjuster, and a massage effect and a blood circulation promoting effect are obtained. From this point, carbon dioxide gas is preferable.
なお、前記溶解性ガスとともに溶媒への溶解量が少ない低溶解性ガス(例えば、水に対するオストワルド係数が0.5未満である)を用いてもよい。低溶解性ガスとしては例えば、窒素ガス(オストワルド係数:0.014)、酸素ガス(オストワルド係数:0.028)、空気(オストワルド係数:0.017)などがあげられる。低溶解性ガスを併用することにより、ガスの粘性物への溶解量を調整し、気泡の大きさや安定性をコントロールすることができる。低溶解性ガスを併用する場合の含有量は、溶解性ガスの効果を充分に得るという点から、分散させるガス中に70質量%以下であることが好ましく、60質量%以下であることがより好ましい。 Note that a low-solubility gas (for example, an Ostwald coefficient with respect to water of less than 0.5) having a small amount of dissolution in a solvent may be used together with the soluble gas. Examples of the low solubility gas include nitrogen gas (Ostwald coefficient: 0.014), oxygen gas (Ostwald coefficient: 0.028), air (Ostwald coefficient: 0.017), and the like. By using a low-solubility gas in combination, the amount of gas dissolved in the viscous material can be adjusted, and the size and stability of the bubbles can be controlled. The content in the case of using a low-solubility gas in combination is preferably 70% by mass or less, more preferably 60% by mass or less, in the gas to be dispersed, from the viewpoint of sufficiently obtaining the effect of the soluble gas. preferable.
塗布用組成物1g中の溶解性ガスを含む気泡の分散量は、0.02〜1.5mlであり、0.03〜1.2mlが好ましく、0.05〜1.0mlがより好ましい。塗布用組成物1g中の分散量が0.02ml未満の場合は塗り伸ばしやすさなどの使用感の向上効果や、溶解性ガス自体の効果が得られにくくなる傾向がある。また、1.5mlを超える場合は、塗布用組成物中の気泡が大きく粘性物の割合が少なくなるため、粘性物の効果が得られにくく、また塗布時に気泡が自然に割れやすくなるため、使用感の向上効果や溶解性ガス自体の効果が得られにくくなる傾向がある。 The dispersion amount of bubbles containing a soluble gas in 1 g of the coating composition is 0.02 to 1.5 ml, preferably 0.03 to 1.2 ml, and more preferably 0.05 to 1.0 ml. When the amount of dispersion in 1 g of the coating composition is less than 0.02 ml, it tends to be difficult to obtain the effect of improving the feeling of use such as ease of spreading and the effect of the soluble gas itself. Also, if the amount exceeds 1.5 ml, the bubbles in the coating composition are large and the ratio of the viscous material is reduced. Therefore, it is difficult to obtain the effect of the viscous material, and the bubbles naturally break easily during application. There is a tendency that the effect of improving the feeling and the effect of the soluble gas itself are hardly obtained.
本発明における塗布用組成物1g中の溶解性ガスを含む気泡の分散量は25℃かつ大気圧下において測定したものとする。この分散量(Vml)は、粘性物のみ(溶解性ガスを分散させる前)1gあたりの体積をXmlとし、溶解性ガスを含む気泡を分散させた粘性物(塗布用組成物)1gあたりの体積をYmlとすると、分散した溶解性ガスの質量は無視できるほど小さいことから、
式:Y−X=V
により求めることができる。
The dispersion amount of bubbles containing a soluble gas in 1 g of the coating composition in the present invention is measured at 25 ° C. and atmospheric pressure. This dispersion amount (Vml) is the volume per 1 g of viscous material (coating composition) in which the volume per 1 g of viscous material (before dispersing the soluble gas) is X ml and the bubbles containing the soluble gas are dispersed. If Y is Yml, the mass of the dispersed dissolved gas is negligibly small.
Formula: Y-X = V
It can ask for.
粘性物中に分散した溶解性ガスを含む気泡の直径は、0.01〜10mmが好ましく、0.05〜8mmがより好ましい。気泡の直径が0.01mm未満の場合は塗り伸ばしやすさなどの使用感の向上効果や、溶解性ガス自体の効果が得られにくくなる傾向がある。また、直径が10mmを超える場合は塗布時に気泡が自然に割れやすくなるため、使用感の向上効果や溶解性ガス自体の効果が得られにくくなる傾向がある。なお、前記気泡の形状としては特に限定されず、真球に近い球状であっても、回転楕円体に近い形状であってもよいが、本発明における気泡の直径は、気泡の最大直径とする。 0.01-10 mm is preferable and, as for the diameter of the bubble containing the soluble gas disperse | distributed in the viscous material, 0.05-8 mm is more preferable. When the diameter of the bubbles is less than 0.01 mm, the effect of improving the feeling of use such as ease of spreading and the effect of the soluble gas itself tend to be difficult to obtain. In addition, when the diameter exceeds 10 mm, the bubbles are naturally easily broken at the time of application, so that it is difficult to obtain the effect of improving the feeling of use and the effect of the soluble gas itself. The shape of the bubble is not particularly limited, and may be a spherical shape close to a true sphere or a shape close to a spheroid, but the bubble diameter in the present invention is the maximum bubble diameter. .
本発明の塗布用組成物の製造方法としては、特に限定されず公知の方法を採用することもできるが、より効率的に粘性物中に溶解性ガスの気泡を小さく多量に分散させることができることから、大気圧以上の高圧条件下または低温条件下で粘性物に溶解性ガスを溶解させる溶解工程、そして減圧または昇温により溶解した溶解性ガスを気泡化させる気泡化工程を含む製造方法とすることが好ましい。また、この製造方法で得られる塗布用組成物は、他の方法で製造されたものに比べ、分散した溶解性ガスの気泡がより真球に近く小さな気泡になるという特徴を有しており、外観的な美しさが一層優れるという点からも好ましい。 The production method of the coating composition of the present invention is not particularly limited, and a known method can be adopted. However, it is possible to more efficiently disperse a small amount of dissolved gas bubbles in a viscous material. From the above, the production method includes a dissolving step of dissolving a soluble gas in a viscous material under a high-pressure condition or a low-temperature condition of atmospheric pressure or higher, and a bubbling step of bubbling the soluble gas dissolved by depressurization or elevated temperature. It is preferable. In addition, the coating composition obtained by this production method has the feature that the bubbles of the dispersed dissolved gas are smaller than the true sphere and smaller than those produced by other methods, It is also preferable from the viewpoint that the appearance beauty is further improved.
高圧条件下で粘性物に溶解性ガスを溶解させる溶解工程としては、溶解させる所望の溶解性ガスを充満させて高圧条件とした圧力タンク内に粘性物を導入し、または粘性物を導入した後、圧力タンク内に所望の溶解性ガスを充満させることで高圧条件とし、その後、ミキサーによる攪拌や多孔質体を用いて粘性物に溶解性ガスを溶解させる溶解工程とすることができる。さらに、粘性物を冷却しながら溶解性ガスを溶解させてもよい。また、溶解工程を行なう前に、圧力タンク内の空気をバキュームして減圧し、粘性物を調製したときに含まれる空気の気泡や溶解している空気を排出する脱気工程を行うことで、粘性物中に効率よく溶解性ガスのみを溶解させることができる。 As a dissolution process for dissolving a soluble gas in a viscous material under high-pressure conditions, the viscous gas is introduced into a pressure tank filled with a desired soluble gas to be dissolved, or after introducing the viscous material. The pressure tank can be filled with a desired soluble gas to obtain a high-pressure condition, and then a dissolution process can be performed in which the soluble gas is dissolved in a viscous material using a mixer or a porous material. Further, the soluble gas may be dissolved while the viscous material is cooled. In addition, before performing the dissolution process, by vacuuming the air in the pressure tank and reducing the pressure, by performing a deaeration process of discharging air bubbles contained in the viscous material and dissolved air, Only the soluble gas can be efficiently dissolved in the viscous material.
液体(粘性物)に対する溶解性ガスの溶解度は圧力に依存し、高圧条件ほど溶解度が高くなることから、高圧条件下で粘性物に溶解性ガスを溶解させる溶解工程を行うことにより、大気圧条件下における飽和溶解量以上の多量の溶解性ガスを粘性物中に溶解させることができる。そのため、得られた塗布用組成物を大気圧条件にするなどの減圧により、粘性物に対する溶解性ガスの飽和溶解量を低下させることで、減圧後の飽和溶解量を超えて溶解している溶解性ガスを気泡として発生(気泡化)させる気泡化工程とすることができる。なお、減圧後の粘性物中には溶解性ガスが飽和溶解した状態となる。また、発生する気泡の大きさや量は溶解工程における圧力や温度の調整、すなわち溶解性ガスの溶解量を調整することでコントロールすることができる。さらに、高圧条件下で溶解性ガスを粘性物中に分散させておくことで減圧により膨張させて、所望の大きさの気泡とすることができる。 The solubility of the soluble gas in the liquid (viscous material) depends on the pressure, and the higher the pressure condition, the higher the solubility. Therefore, by performing the dissolution process to dissolve the soluble gas in the viscous material under the high pressure condition, the atmospheric pressure condition It is possible to dissolve a large amount of soluble gas above the saturated dissolution amount below in the viscous material. Therefore, by reducing the saturated dissolution amount of the soluble gas in the viscous material by reducing the pressure such that the obtained coating composition is at atmospheric pressure, the dissolution that exceeds the saturated dissolution amount after the reduced pressure It can be set as the bubbling process which generate | occur | produces property gas as a bubble (bubble generation). Note that the dissolved gas is saturated and dissolved in the viscous material after decompression. In addition, the size and amount of bubbles generated can be controlled by adjusting the pressure and temperature in the dissolution process, that is, adjusting the dissolution amount of the soluble gas. Furthermore, by disperse | distributing soluble gas in a viscous material under high pressure conditions, it can be expanded by pressure reduction and it can be set as the bubble of a desired magnitude | size.
前記溶解工程における圧力条件は、大気圧(0.1MPa)よりも0.01〜1.0MPa高い圧力条件が好ましく、0.03〜0.8MPa高い圧力条件がより好ましい。大気圧との差が0.01MPa未満の場合は圧力差が小さく、溶解性ガスを速く溶解させる効果、減圧して気泡化させる効果が得られにくくなる傾向がある。また、大気圧との差が1.0MPaを超える場合は気泡が粗くなり、塗布しにくくなる傾向がある。 The pressure condition in the melting step is preferably a pressure condition higher by 0.01 to 1.0 MPa than atmospheric pressure (0.1 MPa), and more preferably a pressure condition higher by 0.03 to 0.8 MPa. When the difference from the atmospheric pressure is less than 0.01 MPa, the pressure difference is small, and there is a tendency that the effect of dissolving the soluble gas quickly and the effect of reducing the pressure to form bubbles are difficult to obtain. On the other hand, when the difference from the atmospheric pressure exceeds 1.0 MPa, the bubbles become rough and the coating tends to be difficult.
ここで、水溶性高分子としてゼラチンを含有する粘性物を使用する場合は、当該粘性物が流動性を有する状態で前記溶解工程を行うことにより、溶解性ガスを粘性物中に溶解させやすくすることができる。そして、前記の場合と同様に減圧による気泡化工程を行うことで、減圧後に飽和溶解量を超えて溶解している溶解性ガスを気泡として発生(気泡化)させることができる。なお、溶解工程により得られた塗布用組成物(ゼラチン含有)は、流動性がない状態で気泡化工程を行なっても良いが、気泡化しやすい点から流動性のある状態で気泡化工程を行うことが好ましい。また、気泡化工程の前に低温状態で保存するなどにより粘性物の粘度が高くなった場合は加温して流動性を有する状態に戻した後に気泡化工程を行なっても良い。さらに、粘性物が流動性を有する状態で気泡化工程を行なった後に、得られた塗布用組成物を低温にして粘性物の粘度を高くすることで気泡の保持性を向上させることができる。 Here, in the case where a viscous material containing gelatin is used as the water-soluble polymer, the dissolving step is performed in a state where the viscous material has fluidity, so that the soluble gas is easily dissolved in the viscous material. be able to. Then, by performing the bubbling step by reduced pressure as in the case described above, it is possible to generate (bubble) the dissolved gas dissolved in excess of the saturation dissolution amount after the reduced pressure. The coating composition (containing gelatin) obtained by the dissolution step may be subjected to an aeration step in a state where there is no fluidity. However, the foaming step is performed in a fluid state from the viewpoint of being easily aerated. It is preferable. In addition, when the viscosity of the viscous material is increased by storing in a low temperature state before the bubble forming step, the bubble forming step may be performed after heating to return to a fluid state. Furthermore, after the foaming step is performed in a state where the viscous material has fluidity, the retention property of the bubbles can be improved by increasing the viscosity of the viscous material by lowering the temperature of the obtained coating composition.
また、低温条件下で粘性物に溶解性ガスを溶解させる溶解工程としては、低温にした粘性物に対し、ミキサーによる攪拌や多孔質体を用いて溶解性ガスを溶解させる溶解工程とすることができる。 In addition, the dissolution process for dissolving the soluble gas in the viscous material under a low temperature condition may be a dissolution process in which the soluble gas is dissolved in the viscous material at a low temperature by stirring with a mixer or using a porous material. it can.
液体(粘性物)に対する溶解性ガスの溶解度は温度に依存し、低温条件ほど溶解度が高くなることから、常温(25℃)よりも低温条件下で粘性物に溶解性ガスを溶解させる工程を行うことにより、25℃における飽和溶解量以上の多量の溶解性ガスを粘性物中に溶解させることができる。そのため、得られた塗布用組成物を常温にするなどの昇温により、粘性物に対する溶解性ガスの飽和溶解量を低下させることで、昇温後の飽和溶解量を超えて溶解している溶解性ガスを気泡として発生(気泡化)させる気泡化工程とすることができる。なお、この場合も昇温後の粘性物中には溶解性ガスが飽和溶解した状態となる。また、低温条件下で分散した溶解性ガスも昇温により膨張させることで所望の大きさの気泡とすることができる。 Since the solubility of the soluble gas in the liquid (viscous material) depends on the temperature, and the solubility becomes higher as the temperature is lower, the step of dissolving the soluble gas in the viscous material at a temperature lower than normal temperature (25 ° C) is performed. By this, a large amount of soluble gas more than the saturated dissolution amount at 25 ° C. can be dissolved in the viscous material. Therefore, by dissolving the dissolved composition in excess of the saturated dissolved amount after the temperature increase by lowering the saturated dissolved amount of the soluble gas in the viscous material by increasing the temperature such as bringing the obtained coating composition to room temperature. It can be set as the bubbling process which generate | occur | produces property gas as a bubble (bubble generation). In this case as well, the soluble gas is saturated and dissolved in the viscous material after the temperature rise. Moreover, the soluble gas disperse | distributed on low temperature conditions can also be made into the bubble of a desired magnitude | size by expanding by temperature rising.
前記溶解工程における低温条件は、0〜15℃が好ましく、1〜10℃がより好ましい。0℃未満の場合は粘性物が凝固したり、粘性物の粘度が高くなったり、溶解性ガスが溶解しにくくなる傾向がある。また、15℃を超える場合は、溶解性ガスを速く溶解させる効果、昇温して気泡化させる効果が得られにくくなる傾向がある。 0-15 degreeC is preferable and, as for the low temperature conditions in the said melt | dissolution process, 1-10 degreeC is more preferable. When the temperature is lower than 0 ° C., the viscous material tends to solidify, the viscosity of the viscous material increases, or the soluble gas tends to hardly dissolve. Moreover, when it exceeds 15 degreeC, there exists a tendency for the effect which dissolves soluble gas quickly, and the effect which raises temperature and is made into a bubble become difficult to be acquired.
なお、いずれの溶解工程においても、その溶解工程の後、粘性物に溶解せずタンク内等の気相に残留している溶解性ガスを含む気体を、粘性物中に微細な気泡として分散させてから気泡化工程を行うことにより、この気泡が核となって気泡化工程で新たな気泡が発生しやすくなり、粘性物中に微細な気泡を多量に分散させることができる。 In any dissolution process, after the dissolution process, the gas containing the soluble gas that is not dissolved in the viscous material and remains in the gas phase in the tank or the like is dispersed as fine bubbles in the viscous material. By performing the bubble formation process after that, the bubbles become the core and new bubbles are easily generated in the bubble formation process, and a large amount of fine bubbles can be dispersed in the viscous material.
本発明の塗布製品は前記の塗布用組成物を容器に充填することで製造することができる。容器の形状としては特に限定されないが、チューブ容器、パウチ容器、樹脂ボトル、ジャー容器、エアゾール容器などが挙げられ、塗布製品の用途や目的に応じて適宜選択することができる。また、内容物である本願発明の塗布用組成物は、粘性物中に分散している溶解性ガスを含む気泡により外観的な美しさを演出することができることから、外部から内容物が視認できる透光性を有する容器とすることが好ましい。ここで透光性を有する容器としては、例えば、ガラス製、ポリエチレンテレフタレート、ポリエチレンなどの合成樹脂製の容器などが挙げられる。なお、これら容器には弁を設けても良い。 The coated product of the present invention can be produced by filling a container with the coating composition. Although it does not specifically limit as a shape of a container, A tube container, a pouch container, a resin bottle, a jar container, an aerosol container, etc. are mentioned, It can select suitably according to the use and objective of a coated product. In addition, the coating composition of the present invention, which is the content, can produce an external beauty due to the bubbles containing the soluble gas dispersed in the viscous material, so that the content can be visually recognized from the outside. It is preferable to use a light-transmitting container. Examples of the light-transmitting container include a container made of a synthetic resin such as glass, polyethylene terephthalate, and polyethylene. These containers may be provided with valves.
前述の高圧条件下または低温条件下で粘性物に溶解性ガスを溶解させる溶解工程、および、減圧または昇温により溶解した溶解性ガスを気泡化させる気泡化工程を含む製造方法により得られた塗布用組成物は、気泡化工程の後に容器に充填することで塗布製品とすることもできる。 Application obtained by a production method including the above-described dissolving step of dissolving a soluble gas in a viscous material under high-pressure or low-temperature conditions, and the bubbling step of bubbling the soluble gas dissolved by depressurization or elevated temperature The composition for use can also be made into a coated product by filling the container after the bubble forming step.
また、高圧条件下で溶解性ガスを溶解させる溶解工程を含む製造方法の場合は、溶解性ガスを溶解させた塗布用組成物を高圧条件下で耐圧容器などの密封可能な弁付きの容器に充填することで、使用時に弁を開封することにより容器内部の圧力が低下し、塗布用組成物中の溶解性ガスが気泡化するという動きのある美しさを演出することが可能となる。なお、この場合は使用時の開封が減圧により溶解した溶解性ガスを気泡化させる気泡化工程となる。また、耐圧性を有する容器(エアゾール容器など)に充填する場合、該容器内で溶解工程および気泡化工程をひとつの容器内で行なうことができる。ここで、使用時に内部の圧力を低下させることのできる容器としては、耐圧性を有する容器に外部から開閉操作可能な弁を装着したものが挙げられる。 In addition, in the case of a production method including a dissolving step of dissolving a soluble gas under high pressure conditions, the coating composition in which the soluble gas is dissolved is placed in a container with a valve that can be sealed such as a pressure resistant container under high pressure conditions. By filling, the pressure inside the container is lowered by opening the valve at the time of use, and it is possible to produce a moving beauty that the soluble gas in the coating composition is bubbled. In this case, unsealing at the time of use is a bubble forming step for forming a dissolved gas dissolved by decompression into bubbles. In addition, when filling a container having pressure resistance (such as an aerosol container), the dissolving step and the bubble forming step can be performed in one container. Here, examples of the container that can reduce the internal pressure during use include a pressure-resistant container equipped with a valve that can be opened and closed from the outside.
前記耐圧性を有する容器の材質としてはアルミニウムやブリキなどの金属、ポリエチレンテレフタレートなどの合成樹脂、ガラスなどがあげられる。また、これらの耐圧を有する容器内に内袋を挿入し、耐圧を有する外容器と可撓性を有する内容器(容積可変の内容器)の二重構造のエアゾール容器としても良い。これらのエアゾール容器は塗布用組成物の性質や用途に応じて適宜選択することができる。充填した塗布用組成物を全て吐出しやすいという点からは容積可変の内容器と外容器とを有する二重構造のエアゾール容器が好ましい。 Examples of the material of the pressure-resistant container include metals such as aluminum and tin, synthetic resins such as polyethylene terephthalate, and glass. Moreover, it is good also as an aerosol container of the double structure of inserting an inner bag in the container which has these pressure | voltage resistance, and the outer container which has pressure | voltage resistance, and the flexible inner container (volume variable inner container). These aerosol containers can be appropriately selected according to the properties and application of the coating composition. A double-structure aerosol container having a variable volume inner container and an outer container is preferable from the viewpoint that it is easy to discharge all of the filled coating composition.
前記二重構造のエアゾール容器の外容器としては、円盤状のアルミニウムをインパクト成型や絞り・しごき加工などで有底筒状に成型した1ピースタイプの金属容器、ブリキなどの金属板を円筒状にして溶接し、その上下開口に目金部と底部とを巻き締めた3ピースタイプの金属容器、ポリエチレンテレフタレートなどの合成樹脂を用いて2軸延伸ブロー成型などにより有底筒状に成型した樹脂容器、ガラス製の容器など、耐圧性を有する容器が挙げられる。前述のように、外部から内容物が視認できる透光性を有する容器とすることが好ましい。 As the outer container of the double-layered aerosol container, a one-piece type metal container in which disk-shaped aluminum is formed into a bottomed cylindrical shape by impact molding, drawing or ironing, etc., a metal plate such as tinplate is made cylindrical. A three-piece type metal container with a metal base and bottom wound around the top and bottom openings, and a resin container molded into a bottomed cylinder by biaxial stretch blow molding using a synthetic resin such as polyethylene terephthalate And a container having pressure resistance, such as a glass container. As described above, it is preferable that the container has translucency so that the contents can be visually recognized from the outside.
また、前記容積可変の内容器としては、可撓性を有するポリエチレン(PE)やポリプロピレン(PP)などのポリオレフィン、エチレン−ビニルアルコール共重合体(EvOH)、ナイロン(NY)などの合成樹脂を用いてダイレクトブロー成型などにより有底筒状に成型され、前記合成樹脂の単層構造あるいはPE/EvOH/PE、PE/NY/PEなどの積層構造のものとすることができる。また、1枚または複数枚のシートを溶着または貼着しパウチタイプの袋としてもよい。当該シートとしてはポリエチレン、ポリエチレンテレフタレート、ナイロン、エバールなどの合成樹脂シートがあげられる。なかでも、粘性物を内容器内に充填し、溶解性ガスを内容器と外容器との間に充填し、内容器から溶解性ガスを透過させて粘性物に溶解させる場合は、ポリエチエン、ポリプロピレン、ナイロン、ポリエチレンテレフタレートなどの溶解性ガスの透過性が高い(透過しやすい)合成樹脂製の単層構造の内容器を用いることが好ましい。 Moreover, as said inner container of variable volume, synthetic resins, such as polyolefins, such as flexible polyethylene (PE) and polypropylene (PP), ethylene-vinyl alcohol copolymer (EvOH), and nylon (NY), are used. Then, it is molded into a bottomed cylinder by direct blow molding or the like, and can have a single layer structure of the synthetic resin or a laminated structure such as PE / EvOH / PE, PE / NY / PE. One or a plurality of sheets may be welded or adhered to form a pouch-type bag. Examples of the sheet include synthetic resin sheets such as polyethylene, polyethylene terephthalate, nylon, and eval. In particular, when filling the inner container with a viscous substance, filling the soluble gas between the inner container and the outer container, and allowing the soluble gas to permeate through the inner container and dissolve in the viscous substance, polyethylene, polypropylene It is preferable to use an inner container of a single layer structure made of a synthetic resin having a high permeability of a soluble gas such as nylon or polyethylene terephthalate (easy to permeate).
エアゾール容器内で溶解工程および気泡化工程を行う製造方法について説明する。 The manufacturing method which performs a melt | dissolution process and an aeration process in an aerosol container is demonstrated.
エアゾール容器を用いて粘性物と溶解性ガスとを容器内に充填する場合の溶解工程は、粘性物と溶解性ガスとを充填した容器内の平衡圧力を前述の圧力条件とし、粘性物に溶解性ガスを溶解させる工程とすることができる。また、気泡化工程は外部から開閉操作可能な弁(エアゾールバルブ)を開放することで容器内を減圧する工程とすることができる。 When a viscous material and a soluble gas are filled into the container using an aerosol container, the dissolution process is performed under the above-described pressure condition in the container filled with the viscous material and the soluble gas. It can be set as the process of dissolving sex gas. The bubble forming step can be a step of decompressing the inside of the container by opening a valve (aerosol valve) that can be opened and closed from the outside.
次に、二重構造のエアゾール容器を用い、粘性物は内容器内に充填し、溶解性ガスは内容器と外容器との間に充填する場合の製造方法について、添付の図面を参照して説明するが、この態様に限定されるものではない。 Next, referring to the attached drawings, a manufacturing method in the case where a double structure aerosol container is used, the viscous material is filled in the inner container, and the soluble gas is filled between the inner container and the outer container. Although described, it is not limited to this mode.
この製造方法は充填工程、溶解工程および気泡化工程を含む。充填工程は、粘性物を内容器2内に充填した後、外容器1と内容器2との間の空間に溶解性ガス5を充填し、エアゾールバルブ3で外容器1の開口部を固着する工程とすることができる(図1(a))。溶解工程としては、所定の時間、静置や振とうすることで外容器1と内容器2の間の空間にある溶解性ガスを内容器2内へ透過させ、内容器2内の粘性物4に溶解性ガスを飽和溶解させる溶解工程とすることができる(図1(b))。ここで、充填された溶解性ガスは内容器を透過し、内容器内および内容器と外容器との間が平衡圧力となるので、この平衡圧力が前述の圧力条件となるように溶解性ガスを充填することが好ましい。そして、内容器2内の気相部6に残存している溶解性ガスを容器を上下に振とうするなどして粘性物に分散させた後、外部から開閉操作可能な弁(エアゾールバルブ3)を開放することで内容器内の圧力を減圧して飽和溶解量を下げ、粘性物中に溶解していた溶解性ガスを気泡7として発生させる気泡化工程を行うことができる(図1(c))。 This manufacturing method includes a filling step, a dissolving step, and an aeration step. In the filling step, after the viscous material is filled in the inner container 2, the space between the outer container 1 and the inner container 2 is filled with the soluble gas 5, and the opening of the outer container 1 is fixed by the aerosol valve 3. This can be a process (FIG. 1A). In the dissolution step, the soluble gas in the space between the outer container 1 and the inner container 2 is permeated into the inner container 2 by standing or shaking for a predetermined time, and the viscous material 4 in the inner container 2 is passed through. It can be set as the melt | dissolution process which dissolves a soluble gas in saturation (FIG.1 (b)). Here, since the filled soluble gas permeates through the inner container and the equilibrium pressure is obtained in the inner container and between the inner container and the outer container, the soluble gas is adjusted so that the equilibrium pressure becomes the aforementioned pressure condition. Is preferably filled. Then, after the soluble gas remaining in the gas phase portion 6 in the inner container 2 is dispersed in a viscous material by shaking the container up and down, etc., a valve (aerosol valve 3) that can be opened and closed from the outside By releasing the pressure, the pressure in the inner container is reduced to lower the saturated dissolution amount, and a bubble forming step can be performed in which the soluble gas dissolved in the viscous material is generated as bubbles 7 (FIG. 1 (c) )).
なお、前述の充填工程において、内容器内に粘性物を充填せずに、外容器と内容器との間の空間に溶解性ガスを充填し、外容器の開口部をエアゾールバルブで固着し、次いで、エアゾールバルブを開放して内容器内の空気を排出した後に、エアゾールバルブより粘性物を充填することにより、効率良く溶解性ガスのみを粘性物に溶解させることができる。 In the above-described filling step, the inner container is not filled with a viscous substance, but the space between the outer container and the inner container is filled with a soluble gas, and the opening of the outer container is fixed with an aerosol valve, Next, after the aerosol valve is opened and the air in the inner container is discharged, by filling the viscous material from the aerosol valve, only the soluble gas can be efficiently dissolved in the viscous material.
一方、低温条件下で溶解させる溶解工程により得られた塗布用組成物の場合は、使用するまで低温条件を維持し、使用時に温度を上昇させることで塗布用組成物中の溶解性ガスが気泡化するという動きのある美しさを演出することが可能となる。なお、この場合は使用時に温度を上昇させることが昇温により溶解した溶解性ガスを気泡化させる気泡化工程となる。 On the other hand, in the case of a coating composition obtained by a dissolution process that dissolves under low temperature conditions, the low temperature conditions are maintained until use, and the soluble gas in the coating composition is bubbled by increasing the temperature during use. It is possible to produce beauty with the movement of becoming. In this case, raising the temperature at the time of use is a bubble forming step for bubbling the dissolved gas dissolved by the temperature rise.
本発明の塗布製品は、外観的な美しさの向上だけでなく、粘性物による効果および溶解性ガスの気泡による効果を有する塗布製品であることから、整髪料、シャンプー、コンディショナー、クレンジング、育毛剤などの頭皮・頭髪用製品、消炎鎮痛剤、鎮痒剤、制汗剤、収斂剤、保湿剤、ほてり止めなど、皮膚に使用する製品などに好適に用いることができる。 The coated product of the present invention is a coated product having not only an improvement in appearance beauty but also an effect due to viscous substances and an effect due to bubbles of soluble gas. Therefore, the hair styling agent, shampoo, conditioner, cleansing, hair restorer It can be suitably used for products used on the skin such as scalp / hair products, anti-inflammatory analgesics, antipruritics, antiperspirants, astringents, moisturizers, anti-hot flashes and the like.
以下、実施例によって本発明をより具体的に説明するが、本発明はこれらに限定されるものではない。 EXAMPLES Hereinafter, although an Example demonstrates this invention more concretely, this invention is not limited to these.
評価方法を下記に示す。 The evaluation method is shown below.
<粘性物の粘度>
調製した粘性物を25℃に調整し、B型粘度計(型式BL、東京計器工業(株)製)を用いて粘度を測定した。
<Viscosity of viscous material>
The prepared viscous material was adjusted to 25 ° C., and the viscosity was measured using a B-type viscometer (model BL, manufactured by Tokyo Keiki Kogyo Co., Ltd.).
<減圧時の気泡化>
高圧条件を経て塗布製品を製造する工程中の気泡化工程において塗布用組成物中に発生した気泡の有無を確認、次の基準で評価した。
○:均一な大きさの気泡が発生した。
△:気泡は発生したが、大きさが不均一であった。
×:気泡が発生しなかった。
<Bubbling during decompression>
The presence or absence of bubbles generated in the coating composition in the aeration process in the process of producing a coated product through high pressure conditions was confirmed and evaluated according to the following criteria.
○: Bubbles of uniform size were generated.
Δ: Bubbles were generated, but the sizes were not uniform.
X: Air bubbles were not generated.
<昇温時の気泡化>
低温条件を経て塗布製品を製造する工程中の気泡化工程において塗布用組成物中に発生した気泡の有無を確認し、次の基準で評価した。
○:均一な大きさの気泡が発生した。
△:気泡は発生したが、大きさが不均一であった。
×:気泡が発生しなかった。
<Bubbling during temperature rise>
The presence or absence of bubbles generated in the coating composition in the foaming step in the process of producing a coated product through low temperature conditions was confirmed and evaluated according to the following criteria.
○: Bubbles of uniform size were generated.
Δ: Bubbles were generated, but the sizes were not uniform.
X: Air bubbles were not generated.
<気泡の分散量>
試験用塗布製品を25℃に調整し、塗布用組成物を容積25mlの半球状のガラス容器に取り出し、塗布用組成物をすりきって質量を測定し、25(ml)をその質量(g)で除することで当該塗布用組成物1gあたりの体積(ml)を算出した。そして、あらかじめ算出しておいた粘性物のみ1gあたりの体積(ml)との差を気泡の分散量とした。
<Bubble dispersion amount>
The test coated product was adjusted to 25 ° C., the coating composition was taken out into a hemispherical glass container with a volume of 25 ml, the coating composition was ground and the mass was measured, and 25 (ml) was mass (g). The volume (ml) per gram of the coating composition was calculated. And the difference with the volume (ml) per g of only the viscous material calculated beforehand was made into the dispersion | distribution amount of a bubble.
<気泡の直径>
試験用塗布製品を25℃に調整し、塗布用組成物中に分散した溶解性ガスを含む気泡から任意に選択された5個の気泡の直径を測定し、その平均値を気泡の直径とし、次の基準で評価した。
○ :0.01〜10mmであった。
×1:0.01mm未満であった。
×2:10mmよりも大きかった。
<Bubble diameter>
The test coated product was adjusted to 25 ° C., the diameter of five bubbles arbitrarily selected from bubbles containing a soluble gas dispersed in the coating composition was measured, and the average value was taken as the bubble diameter, Evaluation was made according to the following criteria.
A: 0.01 to 10 mm.
X1: It was less than 0.01 mm.
X2: It was larger than 10 mm.
<塗り伸ばし易さ>
試験用塗布製品から塗布用組成物を取り出し、皮膚上に塗布し、指で塗り伸ばしたときの状態を評価した。
○:抵抗を感じることなく、なめらかに伸びた。
×:途中で抵抗を感じ、伸ばしにくかった。
<Ease of spreading>
The coating composition was removed from the test coating product, applied to the skin, and the state when spread with a finger was evaluated.
○: It stretched smoothly without feeling resistance.
×: Resistance was felt on the way and it was difficult to stretch.
<気泡の保持性>
試験用塗布製品を、25℃に設定した恒温室に3日間静置し、気泡の状態を次の基準で評価した。
○:塗布製品全体に気泡が分散していた。
△:気泡は存在するが容器上部に集まっていた。
×:気泡が消失した。
<Bubble retention>
The test coated product was allowed to stand in a thermostatic chamber set at 25 ° C. for 3 days, and the state of bubbles was evaluated according to the following criteria.
○: Air bubbles were dispersed throughout the coated product.
Δ: Bubbles were present but collected at the top of the container.
X: Bubbles disappeared.
実施例1〜15、比較例1〜4(高圧条件)
表1に示す処方に従って各粘性物を調製した。さらに、下記工程により試験用塗布製品を製造した。
1.得られた粘性物を圧力タンク内に導入する工程
2.圧力タンク内の空気をバキュームして大気圧(0.1MPa(絶対圧))から0.01MPa(絶対圧)に減圧し、粘性物に含まれる空気の気泡を排出する脱気工程
3.圧力タンク内に溶解性ガスを導入し、圧力タンク内で混合し粘性物に溶解性ガスを溶解させ、圧力タンク内が所定の圧力となるように加圧する溶解工程
4.圧力タンク内で溶解性ガスを飽和溶解させた後に、圧力タンク内の気相部に残存している溶解性ガスを粘性物に分散させる工程
5.粘性物に気泡を分散させた後に、圧力タンク内の圧力を大気圧に減圧することにより溶解性ガスを気泡として発生させる気泡化工程
6.前述の工程により得られた塗布用組成物をチューブ容器に充填する工程
なお、使用した粘性物、溶解性ガス、ガスを溶解させた時の圧力タンク内の圧力と大気圧との差(溶解時圧力)を表2および表3に示す。そして得られた粘性物および試験用塗布製品について上記の評価を行った。評価結果を表2および表3に示す。また、実施例3、4および比較例2の試験用塗布製品の外観を、気泡の直径測定のために用いた定規(最小目盛:1mm)とともに撮影した写真を表4に示す。
Examples 1-15, Comparative Examples 1-4 (high pressure conditions)
Each viscous material was prepared according to the formulation shown in Table 1. Further, a test coated product was produced by the following steps.
1. 1. Step of introducing the obtained viscous material into the pressure tank 2. Deaeration step of vacuuming the air in the pressure tank to reduce the pressure from atmospheric pressure (0.1 MPa (absolute pressure)) to 0.01 MPa (absolute pressure), and discharging air bubbles contained in the viscous material. 3. Dissolving step of introducing a soluble gas into the pressure tank, mixing in the pressure tank, dissolving the soluble gas in a viscous material, and pressurizing the pressure tank so as to have a predetermined pressure. 4. Dissolve the soluble gas remaining in the gas phase in the pressure tank after the soluble gas is saturated and dissolved in the pressure tank. 5. Bubble formation step of generating dissolved gas as bubbles by reducing the pressure in the pressure tank to atmospheric pressure after dispersing the bubbles in the viscous material. The step of filling the tube composition with the coating composition obtained by the above-described steps. Note that the difference between the pressure in the pressure tank and the atmospheric pressure when dissolving the used viscous material, soluble gas, and gas (when dissolved) Table 2 and Table 3 show the pressure). Then, the above evaluation was performed on the obtained viscous material and the test coated product. The evaluation results are shown in Table 2 and Table 3. Table 4 shows photographs taken of the appearances of the test coated products of Examples 3 and 4 and Comparative Example 2 together with a ruler (minimum scale: 1 mm) used for measuring the diameter of bubbles.
実施例16〜23、比較例5〜8(低温条件)
表1に示す処方に従って各粘性物を調製した。さらに、下記工程により試験用塗布製品を製造した。
1.得られた粘性物を密封タンク内に導入する工程
2.密封タンク内の空気をバキュームして大気圧(0.1MPa(絶対圧))から0.01MPa(絶対圧)に減圧し、粘性物に含まれる空気の気泡を排出する脱気工程
3.粘性物を低温(5℃)に調整した後に溶解性ガスを大気圧まで導入し、密封タンク内で混合し粘性物に溶解性ガスを溶解させる溶解工程
4.密封タンク内で溶解性ガスを飽和溶解させた後に、密封タンク内の気相部に残存している溶解性ガスを粘性物に分散させる工程
5.粘性物に気泡を分散させた後に、密封タンク内の温度を上げ、溶解していた溶解性ガスを気泡化させる気泡化工程
6.前述の工程により得られた塗布用組成物をチューブ容器に充填する工程
なお、使用した粘性物、溶解性ガス、ガスを溶解させた時の温度(溶解時温度)、および気泡化させた時の温度(気泡化時温度)を表5に示す。そして得られた粘性物および試験用塗布製品について上記の評価を行った。評価結果を表5に示す。
Examples 16-23, Comparative Examples 5-8 (low temperature conditions)
Each viscous material was prepared according to the formulation shown in Table 1. Further, a test coated product was produced by the following steps.
1. 1. Step of introducing the obtained viscous material into a sealed tank 2. Deaeration step of vacuuming the air in the sealed tank and reducing the pressure from atmospheric pressure (0.1 MPa (absolute pressure)) to 0.01 MPa (absolute pressure) to discharge air bubbles contained in the viscous material. 3. A dissolving step in which a viscous gas is adjusted to a low temperature (5 ° C.) and then a soluble gas is introduced to atmospheric pressure and mixed in a sealed tank to dissolve the soluble gas in the viscous material. 4. Dissolve the soluble gas remaining in the gas phase in the sealed tank in a viscous material after the dissolved gas is saturated and dissolved in the sealed tank. 5. After the bubbles are dispersed in the viscous material, the temperature in the sealed tank is increased, and the dissolved gas that has been dissolved is bubbled. The step of filling the tube composition with the coating composition obtained by the above-mentioned steps Note that the viscous material used, the soluble gas, the temperature at which the gas was dissolved (temperature at the time of dissolution), and the time when it was bubbled Table 5 shows the temperature (temperature during bubbling). Then, the above evaluation was performed on the obtained viscous material and the test coated product. The evaluation results are shown in Table 5.
表4に示す写真からわかるように、実施例3は0.5〜2mm程度の直径を有する気泡が均一に分散しており、実施例4は0.1〜1mm程度の直径を有する気泡が均一に分散しているのに対し、比較例2は圧力タンク内で気泡を分散させた際の大きな気泡と、減圧した際に発生した非常に小さな気泡とが不均一に分散していた。 As can be seen from the photograph shown in Table 4, in Example 3, bubbles having a diameter of about 0.5 to 2 mm are uniformly dispersed, and in Example 4, bubbles having a diameter of about 0.1 to 1 mm are uniform. On the other hand, in Comparative Example 2, large bubbles when the bubbles were dispersed in the pressure tank and very small bubbles generated when the pressure was reduced were non-uniformly dispersed.
実施例24〜31、比較例9〜12(高圧条件、チューブ容器使用、ゼラチン含有)
表6に示す処方に従って各粘性物を調製した。さらに、下記工程により試験用塗布製品を製造した。
1.得られた粘性物を所定の温度とし、流動性を有する状態で圧力タンク内に導入する工程
2.圧力タンク内の空気をバキュームして大気圧(0.1MPa(絶対圧))から0.01MPa(絶対圧)に減圧し、粘性物に含まれる空気の気泡を排出する脱気工程
3.圧力タンク内に溶解性ガスを導入し、圧力タンク内で混合し粘性物に溶解性ガスを溶解させ、圧力タンク内が所定の圧力となるように加圧する溶解工程
4.圧力タンク内で溶解性ガスを飽和溶解させた後に、圧力タンク内の気相部に残存している溶解性ガスを粘性物に分散させる工程
5.粘性物に気泡を分散させた後に、圧力タンク内の圧力を大気圧に減圧することにより溶解性ガスを気泡として発生させる気泡化工程
6.前述の工程により得られた塗布用組成物をチューブ容器に充填する工程
7.塗布用組成物を充填したチューブを低温(5℃)に1時間静置し、気泡の保持力を向上させる工程
なお、使用した粘性物、溶解性ガス、ガスを溶解させた時の圧力タンク内の圧力と大気圧との差(溶解時圧力)および粘性物の温度を表7に示す。そして得られた粘性物および試験用塗布製品について上記の評価を行った。評価結果を表7に示す。
Examples 24-31, Comparative Examples 9-12 (high pressure conditions, use of tube container, containing gelatin)
Each viscous material was prepared according to the formulation shown in Table 6. Further, a test coated product was produced by the following steps.
1. 1. Step of introducing the obtained viscous material into a pressure tank in a state having a predetermined temperature and fluidity. 2. Deaeration step of vacuuming the air in the pressure tank to reduce the pressure from atmospheric pressure (0.1 MPa (absolute pressure)) to 0.01 MPa (absolute pressure), and discharging air bubbles contained in the viscous material. 3. Dissolving step of introducing a soluble gas into the pressure tank, mixing in the pressure tank, dissolving the soluble gas in a viscous material, and pressurizing the pressure tank so as to have a predetermined pressure. 4. Dissolve the soluble gas remaining in the gas phase in the pressure tank after the soluble gas is saturated and dissolved in the pressure tank. 5. Bubble formation step of generating dissolved gas as bubbles by reducing the pressure in the pressure tank to atmospheric pressure after dispersing the bubbles in the viscous material. 6. Filling the tube container with the coating composition obtained by the above process A step of allowing the tube filled with the coating composition to stand at a low temperature (5 ° C.) for 1 hour to improve the retention of bubbles. In the pressure tank when the used viscous substance, soluble gas, and gas are dissolved Table 7 shows the difference between the pressure and the atmospheric pressure (pressure during dissolution) and the temperature of the viscous material. Then, the above evaluation was performed on the obtained viscous material and the test coated product. Table 7 shows the evaluation results.
実施例32〜35、比較例13〜16(高圧条件、エアゾール容器使用、ゼラチン含有)
表6に示す処方に従って各粘性物を調製した。さらに、下記工程により試験用塗布製品を製造した(図1参照)。
1.得られた粘性物を外容器と内容器とを有する二重構造のエアゾール容器の内容器に充填する工程
2.外容器と内容器との間の空間に溶解性ガスを充填し、エアゾールバルブで外容器の開口部を固着する工程(図1(a))
3.40℃で3日間静置し、粘性物に内容器を透過した溶解性ガスを溶解させる溶解工程(図1(b))
4.内容器内で溶解性ガスを飽和溶解させた後に、内容器内の気相部に残存している溶解性ガスを粘性物に分散させる工程
5.粘性物に気泡を分散させた後に、エアゾール容器内の圧力を減圧することにより溶解性ガスを気泡として発生させる気泡化工程(図1(c))
なお、使用した粘性物、溶解性ガス、ガスを溶解させた時のエアゾール容器内の圧力と大気圧との差(溶解時圧力)および粘性物の温度を表8に示す。そして得られた粘性物および試験用塗布製品について上記の評価を行った。評価結果を表8に示す。
Examples 32-35, Comparative Examples 13-16 (high pressure conditions, use of aerosol container, containing gelatin)
Each viscous material was prepared according to the formulation shown in Table 6. Further, a test coated product was produced by the following steps (see FIG. 1).
1. 1. Filling the inner container of a double-structured aerosol container having an outer container and an inner container with the obtained viscous material A process of filling the space between the outer container and the inner container with a soluble gas and fixing the opening of the outer container with an aerosol valve (FIG. 1 (a)).
3. Dissolving step of standing at 40 ° C. for 3 days to dissolve the soluble gas that has passed through the inner container into the viscous material (FIG. 1B)
4). 4. Dissolve the soluble gas remaining in the gas phase in the inner container in a viscous material after the soluble gas is saturated and dissolved in the inner container. A bubble forming step in which dissolved gas is generated as bubbles by reducing the pressure in the aerosol container after the bubbles are dispersed in the viscous material (FIG. 1 (c)).
Table 8 shows the viscous material used, the soluble gas, the difference between the pressure in the aerosol container when the gas was dissolved and the atmospheric pressure (pressure during dissolution), and the temperature of the viscous material. Then, the above evaluation was performed on the obtained viscous material and the test coated product. The evaluation results are shown in Table 8.
実施例36〜39、比較例17〜20(高圧条件)
表9に示す処方に従って各粘性物を調製した。さらに、実施例1と同様の工程により試験用塗布製品を製造した。評価結果を表10に示す。
Examples 36 to 39, Comparative Examples 17 to 20 (high pressure conditions)
Each viscous material was prepared according to the formulation shown in Table 9. Further, a test coated product was produced by the same process as in Example 1. Table 10 shows the evaluation results.
処方例1 シェービングジェル
下記の粘性物を調製し、実施例1の試験用塗布製品と同じ製造条件(高圧条件、溶解性ガス、溶解時圧力等)により塗布製品を製造した。
Formulation Example 1 Shaving Gel The following viscous material was prepared, and a coated product was produced under the same production conditions (high pressure conditions, soluble gas, pressure during dissolution, etc.) as the test coated product of Example 1.
<粘性物>
ポリオキシエチレン(20)セチルエーテル(*6) 1.0
カルボキシビニルポリマー(*3) 1.0
トリエタノールアミン 0.5
プロピレングリコール 3.0
ソルビトール 2.0
l−メントール 0.2
ヒアルロン酸 0.01
グリチルリチン酸ジカリウム 0.2
メチルパラベン 0.1
エタノール 10.0
精製水 81.99
合計(質量部) 100.0
*6:BC−20(商品名)、日光ケミカルズ株式会社製
<Viscous material>
Polyoxyethylene (20) cetyl ether (* 6) 1.0
Carboxyvinyl polymer (* 3) 1.0
Triethanolamine 0.5
Propylene glycol 3.0
Sorbitol 2.0
l-Menthol 0.2
Hyaluronic acid 0.01
Dipotassium glycyrrhizinate 0.2
Methylparaben 0.1
Ethanol 10.0
Purified water 81.99
Total (parts by mass) 100.0
* 6: BC-20 (trade name), manufactured by Nikko Chemicals Co., Ltd.
処方例2 整髪料
下記の粘性物を調製し、実施例2の試験用塗布製品と同じ製造条件(高圧条件、溶解性ガス、溶解時圧力等)により塗布製品を製造した。
Formulation Example 2 Hairdressing The following viscous material was prepared, and a coated product was produced under the same production conditions as the test coated product of Example 2 (high pressure conditions, soluble gas, pressure during dissolution, etc.).
<粘性物>
ポリオキシエチレン(60)硬化ヒマシ油(*7) 1.0
パラフィン 1.0
ワセリン 2.0
ステアリン酸 1.0
トリエタノールアミン 1.5
プロピレングリコール 3.0
ビニルピロリドン−酢酸ビニル共重合体(*8) 3.0
メチルパラベン 0.1
精製水 87.4
合計(質量部) 100.0
*7:HCO−60(商品名)、日光ケミカルズ株式会社製
*8:PVA−4650(商品名)、大阪有機化学工業社製
<Viscous material>
Polyoxyethylene (60) hydrogenated castor oil (* 7) 1.0
Paraffin 1.0
Vaseline 2.0
Stearic acid 1.0
Triethanolamine 1.5
Propylene glycol 3.0
Vinylpyrrolidone-vinyl acetate copolymer (* 8) 3.0
Methylparaben 0.1
Purified water 87.4
Total (parts by mass) 100.0
* 7: HCO-60 (trade name), manufactured by Nikko Chemicals Co., Ltd. * 8: PVA-4650 (trade name), manufactured by Osaka Organic Chemical Industry Co., Ltd.
処方例3 ボディクリーム
下記の粘性物を調製し、実施例16の試験用塗布製品と同じ製造条件(低温条件、溶解性ガス、溶解時温度、気泡化時温度等)により塗布製品を製造した。
Formulation Example 3 Body Cream The following viscous product was prepared, and a coated product was produced under the same production conditions as the test coated product of Example 16 (low temperature conditions, soluble gas, temperature at dissolution, temperature at the time of foaming, etc.).
<粘性物>
ポリオキシエチレン(4)ステアリルエーテル(*9) 1.0
ステアリルアルコール 2.0
スクワラン 2.0
カルボキシビニルポリマー(*3) 1.5
水酸化ナトリウム 0.1
グリセリン 3.0
メチルパラベン 0.1
精製水 90.3
合計(質量部) 100.0
*9:BS−4(商品名)、日光ケミカルズ株式会社製
<Viscous material>
Polyoxyethylene (4) stearyl ether (* 9) 1.0
Stearyl alcohol 2.0
Squalane 2.0
Carboxyvinyl polymer (* 3) 1.5
Sodium hydroxide 0.1
Glycerin 3.0
Methylparaben 0.1
Purified water 90.3
Total (parts by mass) 100.0
* 9: BS-4 (trade name), manufactured by Nikko Chemicals Co., Ltd.
処方例4 シャンプー
下記の粘性物を調製し、実施例1の試験用塗布製品と同じ製造条件(高圧条件、溶解性ガス、溶解時圧力等)により塗布製品を製造した。
Formulation Example 4 Shampoo The following viscous material was prepared, and a coated product was produced under the same production conditions (high pressure conditions, soluble gas, pressure during dissolution, etc.) as the test coated product of Example 1.
<粘性物>
N−ヤシ油脂肪酸アシル−L−グルタミン酸ナトリウム(*10) 5.0
モノラウリン酸デカグリセリル(*11) 5.0
ラウリル硫酸ナトリウム(*12) 2.0
カルボキシビニルポリマー(*3) 1.0
カラギーナン(*4) 0.5
トリエタノールアミン 0.5
プロピレングリコール 3.0
メチルパラベン 0.1
トウガラシチンキ 0.5
l−メントール 0.1
香料 0.1
エタノール 10.0
精製水 72.2
合計(質量部) 100.0
*10:アミソフトCS−11(商品名)、味の素株式会社製
*11:サンソフトM−12J(商品名)、太陽化学株式会社製
*12:SLS(商品名)、日光ケミカルズ株式会社製
<Viscous material>
N-coconut oil fatty acid acyl-sodium L-glutamate (* 10) 5.0
Decaglyceryl monolaurate (* 11) 5.0
Sodium lauryl sulfate (* 12) 2.0
Carboxyvinyl polymer (* 3) 1.0
Carrageenan (* 4) 0.5
Triethanolamine 0.5
Propylene glycol 3.0
Methylparaben 0.1
Pepper tincture 0.5
l-Menthol 0.1
Fragrance 0.1
Ethanol 10.0
Purified water 72.2
Total (parts by mass) 100.0
* 10: Amisoft CS-11 (trade name), manufactured by Ajinomoto Co., Inc. * 11: Sunsoft M-12J (trade name), manufactured by Taiyo Chemical Co., Ltd. * 12: SLS (trade name), manufactured by Nikko Chemicals Co., Ltd.
処方例5 保湿乳液
下記の粘性物を調製し、実施例1の試験用塗布製品と同じ製造条件(高圧条件、溶解性ガス、溶解時圧力等)により塗布製品を製造した。
Formulation Example 5 Moisturizing emulsion The following viscous product was prepared, and a coated product was produced under the same production conditions (high pressure conditions, soluble gas, pressure during dissolution, etc.) as the test coated product of Example 1.
<粘性物>
ポリオキシエチレンモノステアレート(*13) 1.0
キサンタンガム(*2) 1.5
ベヘニルアルコール 1.0
メドフォーム油 1.0
プロピレングリコール 3.0
グリセリン 2.0
ヒアルロン酸 0.01
メチルパラベン 0.1
精製水 90.39
合計(質量部) 100.0
*13:TS−10V(商品名)、日光ケミカルズ株式会社製
<Viscous material>
Polyoxyethylene monostearate (* 13) 1.0
Xanthan gum (* 2) 1.5
Behenyl alcohol 1.0
Medfoam oil 1.0
Propylene glycol 3.0
Glycerin 2.0
Hyaluronic acid 0.01
Methylparaben 0.1
Purified water 90.39
Total (parts by mass) 100.0
* 13: TS-10V (trade name), manufactured by Nikko Chemicals Co., Ltd.
得られた処方例1〜5の塗布製品について、実施例および比較例と同様に上記の評価を行った。評価結果を表11に示す。 About the obtained coated product of the prescription examples 1-5, said evaluation was performed similarly to the Example and the comparative example. The evaluation results are shown in Table 11.
1 外容器
2 内容器
3 エアゾールバルブ
4 粘性物
5 溶解性ガス
6 気相部
7 溶解性ガスの気泡
DESCRIPTION OF SYMBOLS 1 Outer container 2 Inner container 3 Aerosol valve 4 Viscous material 5 Soluble gas 6 Gas phase part 7 Bubble of soluble gas
Claims (5)
前記粘性物は、粘性調整物が基材に溶解または分散されており、
25℃かつ大気圧下において、塗布用組成物1g中に溶解性ガスを含む気泡が0.02〜1.1ml分散しており、
前記溶解性ガスは、
二酸化炭素ガスを含み、
水に対するオストワルド係数が0.5以上であり、
前記粘性物中に飽和溶解しており、
前記気泡の直径は、0.01〜10mmであり、
前記粘性物の25℃における粘度は、1,000〜200,000mPa・sであり、
頭皮、頭髪、皮膚に使用される、塗布用組成物。 A coating composition in which bubbles of a soluble gas are dispersed in a viscous material,
In the viscous material, the viscosity-adjusted product is dissolved or dispersed in the base material,
At 25 ° C. and atmospheric pressure, 0.02 to 1.1 ml of bubbles containing a soluble gas are dispersed in 1 g of the coating composition ,
The soluble gas is
Containing carbon dioxide gas,
Ostwald coefficient for water is 0.5 or more,
Saturated and dissolved in the viscous material,
The diameter of the bubbles is 0.01 to 10 mm,
The viscosity of the viscous material at 25 ° C. is 1,000 to 200,000 mPa · s,
An application composition for use on the scalp, hair and skin .
前記粘性物は、粘性調整物が基材に溶解または分散されており、In the viscous material, the viscosity-adjusted product is dissolved or dispersed in the base material,
25℃かつ大気圧下において、塗布用組成物1g中に溶解性ガスを含む気泡が0.02〜1.5ml分散しており、At 25 ° C. and atmospheric pressure, 0.02 to 1.5 ml of bubbles containing a soluble gas are dispersed in 1 g of the coating composition,
前記溶解性ガスは、The soluble gas is
亜酸化窒素ガスを含み、Contains nitrous oxide gas,
水に対するオストワルド係数が0.5以上であり、Ostwald coefficient for water is 0.5 or more,
前記気泡の直径は、0.01〜10mmであり、The diameter of the bubbles is 0.01 to 10 mm,
前記粘性物の25℃における粘度は、1,000〜200,000mPa・sであり、The viscosity of the viscous material at 25 ° C. is 1,000 to 200,000 mPa · s,
頭皮、頭髪、皮膚に使用される、塗布用組成物。An application composition for use on the scalp, hair and skin.
粘性物に溶解性ガスを大気圧以上の圧力下で溶解させる溶解工程と、
圧力を大気圧に戻し、粘性物に溶解した溶解性ガスの一部を気泡化させる気泡化工程とを有する塗布製品の製造方法。 A method for producing a coated product according to claim 3 ,
A dissolution process for dissolving a soluble gas in a viscous material under a pressure higher than atmospheric pressure;
A method for producing a coated product, the method comprising returning the pressure to atmospheric pressure and bubbling a part of the soluble gas dissolved in the viscous material.
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