JP6541756B2 - Scrub agents and scrub-containing cleaners - Google Patents
Scrub agents and scrub-containing cleaners Download PDFInfo
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- JP6541756B2 JP6541756B2 JP2017223077A JP2017223077A JP6541756B2 JP 6541756 B2 JP6541756 B2 JP 6541756B2 JP 2017223077 A JP2017223077 A JP 2017223077A JP 2017223077 A JP2017223077 A JP 2017223077A JP 6541756 B2 JP6541756 B2 JP 6541756B2
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K8/00—Cosmetics or similar toiletry preparations
- A61K8/18—Cosmetics or similar toiletry preparations characterised by the composition
- A61K8/72—Cosmetics or similar toiletry preparations characterised by the composition containing organic macromolecular compounds
- A61K8/73—Polysaccharides
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61Q—SPECIFIC USE OF COSMETICS OR SIMILAR TOILETRY PREPARATIONS
- A61Q1/00—Make-up preparations; Body powders; Preparations for removing make-up
- A61Q1/14—Preparations for removing make-up
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61Q—SPECIFIC USE OF COSMETICS OR SIMILAR TOILETRY PREPARATIONS
- A61Q11/00—Preparations for care of the teeth, of the oral cavity or of dentures; Dentifrices, e.g. toothpastes; Mouth rinses
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61Q—SPECIFIC USE OF COSMETICS OR SIMILAR TOILETRY PREPARATIONS
- A61Q19/00—Preparations for care of the skin
- A61Q19/10—Washing or bathing preparations
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61Q—SPECIFIC USE OF COSMETICS OR SIMILAR TOILETRY PREPARATIONS
- A61Q3/00—Manicure or pedicure preparations
- A61Q3/04—Nail coating removers
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61Q—SPECIFIC USE OF COSMETICS OR SIMILAR TOILETRY PREPARATIONS
- A61Q5/00—Preparations for care of the hair
- A61Q5/02—Preparations for cleaning the hair
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61Q—SPECIFIC USE OF COSMETICS OR SIMILAR TOILETRY PREPARATIONS
- A61Q5/00—Preparations for care of the hair
- A61Q5/12—Preparations containing hair conditioners
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Description
本発明は、水との接触により粒子が適度に吸水膨潤し、表面が軟らかく滑らかになることにより、皮膚などへの刺激性が軽減されたスクラブ剤に関する。さらに詳しくは、糊化澱粉を含有する粒子状のスクラブ剤およびスクラブ含有洗浄剤に関する。 The present invention relates to a scrub agent in which the irritation to the skin and the like is reduced by the particles absorbing and swelling appropriately by contact with water and the surface becoming soft and smooth. More particularly, it relates to particulate scrubs and scrub-containing cleaners containing gelatinized starch.
工業用手洗い洗浄剤や洗顔剤、歯磨き粉のスクラブ剤として使用されているマイクロプラスチックビーズ(ポリエチレン、ポリプロピレン、ナイロン等のビーズ状物)について、環境や生態系への悪影響が報告されており、代替素材の需要が高まっている。この問題に関し、近年、生分解性のある天然素材を用いたスクラブ剤の開発が進んでいる。 With regard to micro plastic beads (beads such as polyethylene, polypropylene, nylon, etc.) that are used as scrubs for industrial hand-washing agents, face-washing agents and tooth powders, adverse effects on the environment and ecosystem have been reported. Demand is rising. With regard to this problem, in recent years, development of scrub agents using biodegradable natural materials has progressed.
天然素材を原料としたスクラブ剤の製造方法は、大きく分けて3種類に分類される。
(1)粉砕法
素材をミルやハンマーなどによって粉砕し、スクラブ剤を得る方法。代表的なものとしては、クルミの殻やトウモロコシの穂軸などの植物素材の粉砕物などが挙げられる。
(2)造粒法
撹拌造粒機や流動層造粒機を用いて、素材に対して水溶性結合剤の水溶液を噴霧することで造粒し、スクラブ剤を得る方法。特許文献1および特許文献2には、澱粉やセルロース等の粉状物質を造粒することにより、使用時の圧力や水によって崩壊する使用感の良好なスクラブ粒子が記載されている。
(3)液相法
素材を一度溶解させ、生成した溶液が特定の溶媒や架橋剤の存在下で不溶化することを利用して、スクラブ剤を得る方法。特許文献3にはグルコマンナンゲルを用いた、歯や皮膚への刺激性の低いスクラブ粒子が開示されている。特許文献4には、ゼラチン,寒天等の熱可逆性を有するゲルを形成する水溶性高分子を、アルギン酸塩,ペクチン等の多価金属イオンにより架橋,増粘する水溶性高分子とともに固化させることにより得られる球状造粒物が記載されている。
The manufacturing methods of the scrub agent which uses a natural raw material as a raw material are roughly classified into three types.
(1) A method of obtaining a scrubbing agent by crushing the crushed method material with a mill or a hammer. Typical examples include crushed materials of plant materials such as walnut shells and corn cobs.
(2) Granulation method A method of obtaining a scrub agent by granulating the material by spraying an aqueous solution of a water-soluble binder using a stirring granulator or a fluidized bed granulator. Patent Document 1 and Patent Document 2 describe scrub particles having a good feeling of use that is broken by pressure or water at the time of use by granulating a powdery substance such as starch or cellulose.
(3) Liquid phase method A method of obtaining a scrub agent by dissolving a material once and insolubilizing the produced solution in the presence of a specific solvent or a crosslinking agent. Patent Document 3 discloses scrub particles having low irritation to teeth and skin using glucomannan gel. In Patent Document 4, a water-soluble polymer that forms a thermoreversible gel such as gelatin and agar is solidified with a water-soluble polymer that is crosslinked and thickened by polyvalent metal ions such as alginate and pectin. Spherical granules obtained by
しかしながら、従来の製法で製造させるスクラブ剤には、次のような問題点があった。
(1)粉砕法によって得られるスクラブ剤は、十分なマッサージ効果や汚れの除去効果が認められるが、スクラブ剤表面の形状が滑らかではなく、かつ強度が硬すぎるため、皮膚へ過度の刺激を与える。
(2)造粒法によって得られるスクラブ剤は、崩壊性が高く、皮膚への刺激性が低い反面、その崩壊性のために使用初期しか十分なスクラブ感が得られない点や、水溶性結合剤を用いることから、洗浄剤配合した際に洗浄剤に含まれる水分により、造粒が崩れるという問題がある。
(3)液相法によって得られるスクラブ剤は、粒子の形状や硬度などが改善され、良好なスクラブ感が得られるが、製造時にエタノールや流動パラフィンなど有機溶媒を必要とするため、有機溶媒の回収設備が必要になることや、製造コストの上昇などの問題がある。
However, the scrub agents produced by the conventional method have the following problems.
(1) Although the scrub agent obtained by the pulverization method shows sufficient massage effect and dirt removal effect, the shape of the surface of the scrub agent is not smooth and the strength is too hard to give excessive irritation to the skin. .
(2) The scrub agent obtained by the granulation method has high disintegrability and low irritation to the skin, but on the other hand, a sufficient scrub feeling can be obtained only at the initial stage of use due to the disintegrability, and a water-soluble bond Since the agent is used, there is a problem that the granulation is broken by the water contained in the detergent when blended with the detergent.
(3) Scrub agents obtained by the liquid phase method have improved particle shape and hardness, and good scrub feeling is obtained, but since an organic solvent such as ethanol or liquid paraffin is required at the time of production, There are problems such as the need for recovery equipment and an increase in manufacturing costs.
そこで、本発明においては、優れたスクラブ感を有し、かつ低刺激性、洗浄剤への配合安定性、簡易な製造性を有するスクラブ剤を提供することを目的とする。 Therefore, in the present invention, it is an object of the present invention to provide a scrub agent having excellent scrub feeling and having low irritation, formulation stability to a detergent, and easy manufacturability.
本発明者は前記の目的を達成すべく種々検討した結果、糊化澱粉を含有し、かつ糊化度が10〜90%である粒子状のスクラブ剤を使用したところ、使用時に水分を吸収して膨潤し、適度な硬さとなり、優れた使用感が得られることを見出して、本発明を完成するに至った。 As a result of various studies to achieve the above-mentioned purpose, the present inventor uses a particulate scrub agent containing gelatinized starch and having a gelatinization degree of 10 to 90%, and absorbs moisture at the time of use. It has been found that it swells and has an appropriate hardness and an excellent feeling in use can be obtained, and the present invention has been completed.
すなわち本発明は、下記の通りである。
1.糊化澱粉を含有し、かつ糊化度が10〜90%である、粒子状のスクラブ剤。
2.膨潤崩壊率が1.0〜5.0である、1に記載のスクラブ剤。
3.メディアン径が50〜1000μmである、1〜2のいずれかに記載のスクラブ剤。
4.スクラブ剤を洗浄剤に配合時またはスクラブ剤配合洗浄剤を使用時に水と接触させ、スクラブ剤を吸水膨潤させることを特徴とする1〜3のいずれかに記載のスクラブ剤の使用方法。
5.1〜3のいずれかに記載のスクラブ剤を含有する洗浄剤。
That is, the present invention is as follows.
1. Particulate scrubbing agent containing gelatinized starch and having a gelatinization degree of 10 to 90%.
2. The scrub agent according to 1, wherein the swelling disintegration rate is 1.0 to 5.0.
3. The scrub agent according to any one of 1 to 2, wherein the median diameter is 50 to 1000 μm.
4. The method for using a scrub agent according to any one of 1 to 3, characterized in that the scrub agent is brought into contact with water at the time of blending the scrub agent with the detergent or at the time of use.
The detergent containing the scrub agent in any one of 5.1-3.
本発明により得られるスクラブ剤は、乾燥状態において硬度は高いが、洗浄剤への配合時や使用時には粒子が適度に吸水膨潤して軟らかく、更には表面が滑らかになり、全体としてスクラブ剤としてのピーリング機能やマッサージ効果を維持しつつ、軟らかい表面によって皮膚などへの刺激性を軽減することができる。また、有機溶媒などを用いることなく製造できることから、水溶媒で製造可能なスクラブ剤を提供することができる。 The scrub agent obtained by the present invention has high hardness in the dry state, but the particles absorb and swell to a suitable degree at the time of blending with the detergent and at the time of use, and the surface becomes smooth, and as a scrub agent as a whole. The soft surface can reduce irritation to the skin etc while maintaining the peeling function and the massage effect. Moreover, since it can manufacture without using an organic solvent etc., the scrub agent which can be manufactured with a water solvent can be provided.
以下、本発明について詳細に説明する。本発明におけるスクラブ剤は、糊化澱粉を含有し、糊化度が10〜90%であることを特徴とする。 Hereinafter, the present invention will be described in detail. The scrub agent in the present invention is characterized by containing gelatinized starch and having a gelatinization degree of 10 to 90%.
本発明のスクラブ剤に使用できる澱粉としては、馬鈴薯澱粉、コーンスターチ、ハイアミロースコーンスターチ、ワキシーコーンスターチ、豌豆澱粉、緑豆澱粉、甘藷澱粉、タピオカ澱粉、ワキシータピオカ澱粉、サゴ澱粉、米澱粉、モチ米澱粉、アマランサス澱粉、葛澱粉、小麦澱粉等の天然澱粉、それらの加工澱粉(酸分解澱粉、酸化澱粉、エーテル化、エステル化、架橋等の澱粉誘導体等)が挙げられる。前記澱粉は単独で用いてもよく、また2種以上を組み合わせて用いてもよい。中でも、馬鈴薯澱粉、コーンスターチ、豌豆澱粉、緑豆澱粉、甘藷澱粉が本発明には好適に用いられる。 Examples of starch that can be used in the scrub agent of the present invention include potato starch, corn starch, high amylose corn starch, waxy corn starch, green bean starch, green bean starch, sweet potato starch, tapioca starch, waxi tapioca starch, sago starch, rice starch, mochi rice starch, Natural starches such as amaranth starch, mulberry starch and wheat starch, and modified starches thereof (acid-degraded starch, oxidized starch, starch derivatives such as etherification, esterification, crosslinking, etc.) can be mentioned. The starch may be used alone or in combination of two or more. Among them, potato starch, corn starch, green bean starch, green bean starch and sweet potato starch are suitably used in the present invention.
(1)糊化
天然の結晶状態にある未糊化澱粉を水存在下で加熱すると、澱粉粒は徐々に膨潤を始め、粘度が発現する。この現象は糊化の一例であり、水素結合によって結晶構造をとっている澱粉分子鎖が、加熱により水素結合が切れて結晶構造が緩み、分子鎖間に水分子が入り込み、水和するによって起こる。この糊化が開始する温度は糊化開始温度といい、示差走査熱量測定(DSC)の吸熱ピークが現れる点と定義される。糊化澱粉は、未糊化澱粉と比較して、偏光顕微鏡下で観察される澱粉の複屈折の部分/完全消失が確認される。また、このような糊化状態にある澱粉をドラムドライヤーやエクストルーダー等の乾燥装置により、高温状態のまま急速乾燥することによって得られる粉末は、冷水で糊化状態を再現できることから、様々な用途で利用されている。
(1) Gelatinization When ungelatinized starch in a crystalline state is heated in the presence of water, the starch granules gradually start to swell and develop viscosity. This phenomenon is an example of gelatinization, and starch molecular chains having a crystal structure due to hydrogen bonds break due to heating, hydrogen bonds are broken, crystal structure is loosened, and water molecules enter between molecular chains and caused by hydration. . The temperature at which this gelatinization starts is called gelatinization start temperature, and is defined as a point at which an endothermic peak of differential scanning calorimetry (DSC) appears. The gelatinized starch confirms partial / complete disappearance of the birefringence of the starch observed under a polarizing microscope as compared to ungelatinized starch. Moreover, the powder obtained by rapidly drying the starch in such a gelatinized state in a high temperature state with a dryer such as a drum dryer or an extruder can reproduce the gelatinized state with cold water, so that it can be used in various applications. It is used by
(2)老化
一方、糊化澱粉を冷却すると、時間経過に伴い、白濁や離水が起こる。この現象は老化と呼ばれ、澱粉分子鎖間に再び水素結合が構成され、再結晶化して凝集することによって起こる。このような状態の澱粉は、老化澱粉と呼ばれ、未糊化澱粉とは異なる結晶構造を有しており、未糊化澱粉と比較すると、結晶化度の変化や複屈折の消失などが確認することが出来る。老化は高温状態(70℃以上)ではほとんど起こらないが、温度の低下と共に老化進行が加速し、水が凍結する直前の2〜4℃で最大に達する。老化澱粉は前述した特徴から、水への溶解性の低下や酵素分解に対して抵抗性を示し、代表例である春雨や冷ご飯などはレジスタントスターチ(RS)を含む食品として認知されている。
(2) Aging On the other hand, when gelatinized starch is cooled, white turbidity and syneresis occur with the passage of time. This phenomenon is called aging, and is caused by recomposition and aggregation of hydrogen bonds between starch molecular chains again. The starch in such a state is called aged starch and has a crystal structure different from that of ungelatinized starch, and changes in crystallinity and disappearance of birefringence are confirmed as compared with ungelatinized starch. You can do it. Aging hardly occurs at high temperature (70 ° C. or higher), but the aging progresses accelerate as the temperature decreases and reaches a maximum at 2 to 4 ° C. just before water is frozen. Due to the characteristics described above, aged starch is resistant to reduced solubility in water and enzymatic degradation, and vermicelli and cold rice, which are typical examples, are recognized as foods containing resistant starch (RS). .
本発明における糊化澱粉とは、部分的または完全に糊化した澱粉のことを言い、より詳しくは、糊化度が10%以上である状態を指す。糊化方法としては、加熱糊化法、アルカリ糊化法、圧力・剪断力による糊化法等が挙げられ、特に限定されない。好ましい糊化方法の1つは加熱糊化法であり、加熱糊化を用いる場合の糊化手段としては、ドラムドライヤー,エクストルーダー,ジェットクッカー等の加熱装置を用いる方法や、懸垂式または押出式により麺状で熱水中に投入する方法、シート状に成型し金属板上や蒸気などで加熱する方法などが挙げられる。次に糊化工程の一例を挙げる。まず澱粉と水を混錬して、澱粉スラリー(またはドウ)を得る。この混合物の水分率としては澱粉の種類やその他増粘剤の配合量に応じて調整されるが、成形性や生産効率を考慮すると、水分率25%〜75%程度が好ましい。また、澱粉の一部や、カルボキシメチルセルロースやキサンタンガムなどの増粘多糖類を溶解したものをキャリア糊として混合し、成形性を向上させても良い。続いて、糊化開始温度以上の加熱を行い、前記澱粉スラリー(またはドウ)を糊化させる。加熱温度や加熱時間は、求めるスクラブ剤の物性に応じて適宜調整することが好ましい。 The gelatinized starch in the present invention refers to partially or completely gelatinized starch, and more specifically, to a state in which the gelatinization degree is 10% or more. Examples of the gelatinization method include a heating gelatinization method, an alkali gelatinization method, a gelatinization method using pressure and shear force, and the like, and are not particularly limited. One preferable gelatinization method is a heat gelatinization method, and as a gelatinization means in the case of using a heat gelatinization method, a method using a heating device such as a drum dryer, an extruder, a jet cooker, a hanging type or an extrusion type The method of putting into a hot water in the shape of a noodle by this, the method of shape | molding in a sheet shape, and heating with a metal plate top, a vapor | steam, etc., etc. are mentioned. Next, an example of a gelatinization process is given. First, starch and water are mixed to obtain a starch slurry (or dough). The moisture content of this mixture is adjusted according to the type of starch and the blending amount of other thickeners, but in consideration of moldability and production efficiency, a moisture content of about 25% to 75% is preferable. In addition, a part of starch or one in which a polysaccharide thickener such as carboxymethylcellulose or xanthan gum is dissolved may be mixed as a carrier paste to improve formability. Subsequently, heating is performed at a temperature higher than the gelatinization start temperature to gelatinize the starch slurry (or dough). It is preferable that the heating temperature and the heating time be appropriately adjusted according to the physical properties of the scrubbing agent to be obtained.
本発明のスクラブ剤の水分としては、特に限定されないが、スクラブ剤の保存性や使用時の作業性を考慮すると、30質量%以下が好ましく、20質量%以下がより好ましい。乾燥方法としては、天日干しや風乾に加えて、ドラムドライヤー、エクストルーダー、噴霧乾燥機、凍結乾燥機、棚段式乾燥機、ベルト乾燥機、流動床乾燥機、マイクロウェーブ乾燥機などの乾燥装置を使用することができる。 The water content of the scrub agent of the present invention is not particularly limited, but is preferably 30% by mass or less, more preferably 20% by mass or less, in consideration of the storability of the scrub agent and the workability at the time of use. As a drying method, in addition to sun drying and air drying, drying devices such as drum dryer, extruder, spray dryer, freeze dryer, tray dryer, belt dryer, fluid bed dryer, microwave dryer and the like Can be used.
本発明のスクラブ剤は、必要に応じて粉砕することが好ましい。粉砕方法としては、特に限定されないが、例えば、ハンマーミル、ローラーミル、ピンミル、ジェットミル、ボールミル、ビーズミル、カッターミルなどが挙げられ、必要に応じて整粒機や分級機を用いることができる。粉砕は、水中で行ってもよく、乾燥前または乾燥後に行ってもよい。 It is preferable to grind | pulverize the scrub agent of this invention as needed. The pulverizing method is not particularly limited, and examples thereof include a hammer mill, a roller mill, a pin mill, a jet mill, a ball mill, a bead mill, a cutter mill and the like, and a granulator or classifier may be used if necessary. Grinding may be carried out in water, before or after drying.
本発明のスクラブ剤は、粒子状であれば形状は特に限定されないが、皮膚や眼への刺激性の観点から、より球状に近い形状であることが好ましい。 The shape of the scrub agent of the present invention is not particularly limited as long as it is in the form of particles, but from the viewpoint of skin and eye irritation, it is preferable that the shape is more spherical.
本発明におけるスクラブ剤は、実施例に記載の方法により測定した糊化度が10〜90%であることを特徴とする。更には、より優れた使用感および使用時の持続性や洗浄剤への配合安定性が得られる点から、糊化度が20〜50%であることがより好ましい。糊化度が90%以上では、水への溶解性が高くなるため、また糊化度が10%未満では、澱粉が十分に糊化しておらず吸水性に劣るため、本発明の効果が十分に得られない。 The scrub agent in the present invention is characterized in that the degree of gelatinization measured by the method described in the examples is 10 to 90%. Furthermore, it is more preferable that the gelatinization degree is 20 to 50% from the viewpoint of achieving a better feeling in use, durability during use, and formulation stability to a detergent. If the gelatinization degree is 90% or more, the solubility in water is high, and if the gelatinization degree is less than 10%, the starch is not sufficiently gelatinized and the water absorption is poor, so the effect of the present invention is sufficient. Can not get
所望の糊化度を得るため方法としては、(1)糊化度が10%以上になってから所望の糊化度で糊化を停止する方法(部分糊化法)、(2)所望の糊化度以上に糊化させた後、冷却によって所望の糊化度にする方法(冷却法)、の2つが挙げられる。これらの方法は単独で行ってもよく、また両者を併用して行ってもよい。好ましい方法は冷却法であり、所望の糊化度以上の糊化度とした後、70℃以下に冷却する方法が挙げられる。冷却方法としては特に限定されないが、自然放冷や冷水中での冷却などが挙げられ、必要に応じて、冷蔵や冷凍工程を経てもよい。冷却工程は、乾燥前に行っても、乾燥後に行ってもよい。冷却時の温度としては、−20〜70℃が好ましく、−10〜30℃が更に好ましく、−5℃〜10℃が特に好ましい。また、冷却時間を調節することでも糊化度をコントロールすることができる。 As a method for obtaining a desired gelatinization degree, (1) a method of stopping gelatinization at a desired gelatinization degree after the gelatinization degree reaches 10% or more (partial gelatinization method), (2) desired After gelatinizing to a gelatinization degree or more, two methods of cooling to a desired gelatinization degree (cooling method) may be mentioned. These methods may be performed alone or in combination. A preferred method is a cooling method, which includes a method of cooling to 70 ° C. or less after setting the gelatinization degree to a desired gelatinization degree or more. The cooling method is not particularly limited, and examples thereof include natural cooling and cooling in cold water, etc., and if necessary, it may be subjected to a refrigeration or freezing step. The cooling step may be performed before or after drying. As temperature at the time of cooling, -20-70 ° C is preferred, -10-30 ° C is still more preferred, and -5 ° C-10 ° C are especially preferred. The degree of gelatinization can also be controlled by adjusting the cooling time.
本発明のスクラブ剤の効果は、膨潤崩壊率によって判断できる。実施例に記載の方法により測定した、膨潤崩壊率が1.0以上であるスクラブ剤は、水との接触により吸水し膨潤していることを表しており、肌への刺激性が低減される。一方、膨潤崩壊率が1.0未満であるスクラブ剤は、粒子の崩壊が起こるため、使用時のスクラブ感の持続性や洗浄剤への配合安定性に劣る。本発明におけるスクラブ剤の膨潤崩壊率は、1.0〜5.0であることが好ましい。中でも強いスクラブ感を求める用途においては、1.0〜1.3が好ましい。一方、柔らかいスクラブ感を求める用途においては、1.3〜5.0が好ましく、1.3〜3.0がより好ましく、1.3〜2.1が特に好ましい。 The effect of the scrub agent of the present invention can be judged by the swelling and disintegration rate. The scrub agent having a swelling and disintegration ratio of 1.0 or more, which is measured by the method described in the examples, indicates that it absorbs water and swells by contact with water, and the skin irritation is reduced. . On the other hand, a scrub agent having a swelling / disintegration rate of less than 1.0 causes the particle to be disintegrated, so that the durability of the scrub feeling during use and the compounding stability to a detergent are inferior. It is preferable that the swelling degradation rate of the scrub agent in this invention is 1.0-5.0. Among these, 1.0 to 1.3 is preferable in applications that require a strong scrub feeling. On the other hand, in the application which requests | requires a soft scrub feeling, 1.3-5.0 are preferable, 1.3-3.0 are more preferable, and 1.3-2.1 are especially preferable.
本発明におけるスクラブ剤の粒径は、使用用途や求めるスクラブ感によって異なるが、実施例に記載の方法により測定した、エタノール中でのメディアン径が、50μm〜1000μmであることが好ましい。特に、肌触りや感触の観点から、100μm〜500μmがより好ましい。一方、メディアン径が50μm未満では、十分なスクラブ感やマッサージ効果が得られない。 Although the particle size of the scrub agent in the present invention varies depending on the use application and the required scrub feeling, it is preferable that the median diameter in ethanol measured by the method described in the examples be 50 μm to 1000 μm. In particular, from the viewpoint of touch and feel, 100 μm to 500 μm is more preferable. On the other hand, if the median diameter is less than 50 μm, sufficient scrub feeling and massage effect can not be obtained.
本発明のスクラブ剤は、澱粉単体でも本発明の特徴であるスクラブ感や洗浄剤への配合安定性を得ることが可能だが、澱粉以外の成分を添加してもよく、本実施の形態の効果に影響を与えない範囲で、必要に応じて、スクラブ剤中に増粘剤、界面活性剤、色素、香料、油分、防腐剤、および保湿剤、ビタミン類などの機能性成分などを添加してもよい。例えば、カルボキシメチルセルロースやキサンタンガムなどの多糖類やミョウバン、ポリ乳酸や酢酸セルロースなどの生分解性のプラスチックなどを添加することにより、製造時の作業性の向上や、スクラブ剤の強度および膨潤性、洗浄剤への配合安定性を向上することができる。また、酸化鉄などの有機/無機顔料や色素を用いて着色スクラブ剤とすることや、界面活性剤や美容液などの各種薬剤を添加することで機能性スクラブ剤とすることもできる。 The scrub agent of the present invention can obtain the scrub feeling and the compounding stability to the detergent characteristic of the present invention even with starch alone, but components other than starch may be added, and the effect of the present embodiment If necessary, add thickeners, surfactants, pigments, perfumes, oils, preservatives, and moisturizers, functional ingredients such as vitamins, etc., to the extent that they do not affect It is also good. For example, by adding polysaccharides such as carboxymethyl cellulose and xanthan gum, and alum, biodegradable plastics such as polylactic acid and cellulose acetate, etc., the workability at the time of production can be improved, the strength and swelling of the scrub agent, and washing The formulation stability to the agent can be improved. Moreover, it can also be set as a functional scrub agent by setting it as a coloring scrub agent using organic / inorganic pigments and pigment | dyes, such as iron oxide, and adding various agents, such as surfactant and a cosmetic liquid.
本発明のスクラブ剤は、洗浄剤に添加して使用する。本発明の洗浄剤は、化粧品用途だけでなく、工業(産業)用途にも用いることができる。化粧品用途としては、洗顔剤、手洗い洗剤、クレンジング剤、石鹸、シャンプー、ボディソープ、リンス、マッサージ剤、パック剤、歯磨き剤、美爪除去剤、入浴剤などに用いることができる。工業(産業)用途としては、工場の作業員が用いる、ヒトの手指や肌用の洗浄剤や機械部品などの洗浄に用いる洗浄剤などが挙げられる。製品形態としては、クリーム状、ペースト状、ジェル状、ゲル状、液状、固形状あるいは粉末状などが挙げられる。 The scrub agent of the present invention is used by being added to a detergent. The cleaning agent of the present invention can be used not only for cosmetic applications but also for industrial applications. For cosmetic use, it can be used for face wash, hand wash detergent, cleansing agent, soap, shampoo, body soap, rinse, massage agent, pack agent, dentifrice, nail remover, bath agent and the like. Industrial (industrial) applications include cleaning agents used by workers in factories, cleaning agents for human hands and skin, cleaning agents for machine parts, and the like. Examples of the product form include cream, paste, gel, gel, liquid, solid or powder.
本発明のスクラブ剤は、皮膚などへの刺激性をより軽減できることから、スクラブ剤を吸水膨潤させて使用することが好ましい。吸水膨潤させる時期としては、特に限定されないが、スクラブ剤含有製品の配合時や保存時、製品の使用時などが挙げられる。 The scrub agent of the present invention can be used by absorbing and swelling the scrub agent, since it can reduce irritation to the skin and the like. The time of water absorption and swelling is not particularly limited, but may be at the time of formulation or storage of the scrub agent-containing product, at the time of use of the product, or the like.
本発明のスクラブ剤を洗浄剤に用いる場合、製品によって配合量を適宜変えることができるが、スクラブ剤の配合量は、洗浄剤全体を100質量%としたとき、0.03〜20質量%であることが好ましく、0.3〜10質量%がより好ましい。また、スクラブ剤の洗浄剤への配合方法は、既に知られている公知の配合方法を用いて行うことができ、予め水中に本発明のスクラブ剤を含浸させ、所望の硬度や膨潤度合に調整した後に配合してもよい。 When the scrub agent of the present invention is used as a detergent, the compounding amount can be appropriately changed depending on the product, but the amount of the scrub agent is 0.03 to 20% by mass based on 100% by mass of the entire detergent. Is preferably 0.3 to 10% by mass. The method of blending the scrub agent into the detergent can be carried out using a known blending method, and the scrub agent of the present invention is previously impregnated in water to adjust to the desired hardness and swelling degree You may mix | blend after.
本発明の洗浄剤は、水を含むことが好ましい。前記水は、洗浄剤に用いられる水であれば特に限定されず、界面活性剤などの洗浄剤に使用される成分に、予め含まれる水でもよい。水の配合量は、洗浄剤全体を100質量%としたとき、1質量%以上であることが好ましく、5質量%以上であることがより好ましく、8質量%以上であることが特に好ましい。水を含むことで、スクラブ剤が適度に吸水膨潤し、表面が軟らかく滑らかになることにより、皮膚などへの刺激性が軽減される。 The detergent of the present invention preferably contains water. The water is not particularly limited as long as it is water used for a detergent, and may be water previously included in components used for a detergent such as a surfactant. The content of water is preferably 1% by mass or more, more preferably 5% by mass or more, and particularly preferably 8% by mass or more, based on 100% by mass of the total amount of the cleaning agent. By containing water, the scrub agent absorbs and swells moderately, and the surface becomes soft and smooth, thereby reducing the irritation to the skin and the like.
本発明の洗浄剤には、洗浄剤で使用される成分、アニオン界面活性剤、両性界面活性剤、非イオン界面活性剤、カチオン界面活性剤、多価アルコール、水溶性高分子、水溶性酸またはその塩、炭化水素、液体油脂、固体油脂、ロウ類、高級アルコール、合成エステル油、シリコーン樹脂、シリコーン油、低級アルコール、金属イオン封鎖剤、粉末成分、紫外線吸収剤、酸化防止剤、pH調整剤、有機アミン、防腐剤、殺菌剤、消炎剤、収斂剤、美白剤、ビタミン類、アミノ酸、血行促進剤、賦活剤、賦形剤、清涼剤、各種抽出物、香料等を、本発明の効果を損なわない範囲で用いることができる。 In the detergent of the present invention, components used in the detergent, anionic surfactant, amphoteric surfactant, nonionic surfactant, cationic surfactant, polyhydric alcohol, water-soluble polymer, water-soluble acid or Its salts, hydrocarbons, liquid oils and fats, solid fats and oils, waxes, higher alcohols, synthetic ester oils, silicone resins, silicone oils, lower alcohols, sequestering agents, powder components, ultraviolet absorbers, antioxidants, pH adjusters Organic amine, preservative, disinfectant, anti-inflammatory agent, astringent, skin-whitening agent, vitamins, amino acid, blood circulation promoter, activator, excipient, refreshing agent, various extracts, flavors, etc. It can be used in the range which does not lose
以下、本発明を実施例にて更に詳しく説明するが、本発明はこれらの実施例のみに限定されるものではない。 Hereinafter, the present invention will be described in more detail by way of examples, but the present invention is not limited to these examples.
[製造例1]
馬鈴薯澱粉4質量部(以下、部とする)を水50部の中に分散し、沸騰浴中にて糊化させキャリア糊とした。このキャリア糊に馬鈴薯澱粉96部と水70部を加えた後、十分に混錬し澱粉スラリー(水分率約62%)とした。ステンレストレイに澱粉スラリーを厚さ1cm程度となるように流し込み、90℃の蒸し器中で15分間糊化を行った後、冷水中にて粗熱をとり、糊化澱粉を得た。更に、前記糊化澱粉を4℃にて冷却して所望の糊化度とした後、棚式乾燥機 (50℃)で水分が20質量%以下になるまで乾燥後、小型粉砕機(柴田科学器機工業株式会社製、SCM−40A型)にて粉砕、篩により分級し、粒度の異なる粒子状のスクラブ剤(A1〜A3)を得た。
Production Example 1
4 parts by mass (hereinafter referred to as a part) of potato starch was dispersed in 50 parts of water and gelatinized in a boiling bath to obtain a carrier paste. After 96 parts of potato starch and 70 parts of water were added to the carrier paste, the mixture was thoroughly kneaded to form a starch slurry (water content: about 62%). The starch slurry was poured into a stainless steel tray to a thickness of about 1 cm, gelatinized in a steamer at 90 ° C. for 15 minutes, and then crude heat was taken in cold water to obtain gelatinized starch. Furthermore, after cooling the gelatinized starch at 4 ° C. to obtain a desired gelatinization degree, it is dried by a tray dryer (50 ° C.) until the water content becomes 20% by mass or less, and then a small pulverizer (Shibata science The mixture was crushed and classified by a sieve according to Kikuchi Kogyo Co., Ltd. (SCM-40A type) to obtain particulate scrub agents (A1 to A3) having different particle sizes.
[製造例2]
製造例1において、4℃を−20℃に変更して冷却させた以外は同様の方法で製造を行い、粒度の異なる粒子状のスクラブ剤(A4,A5)を得た。
Production Example 2
Production was carried out in the same manner as in Production Example 1 except that 4 ° C. was changed to -20 ° C. for cooling, to obtain particulate scrub agents (A4, A5) having different particle sizes.
[製造例3]製造例1において、馬鈴薯澱粉を豌豆澱粉に変更した以外は同様の方法で製造を行い、粒度の異なる粒子状のスクラブ剤(A6〜A9)を得た。 Production Example 3 The procedure of Production Example 1 was repeated except that potato starch was changed to soybean starch to obtain particulate scrub agents (A6 to A9) having different particle sizes.
[製造例4]製造例1において、馬鈴薯澱粉を緑豆澱粉に変更した以外は同様の方法で製造を行い、粒度の異なる粒子状のスクラブ剤(A10,A11)を得た。 Production Example 4 The procedure of Production Example 1 was repeated except that potato starch was changed to mung bean starch, to obtain particulate scrub agents (A10, A11) having different particle sizes.
[製造例5]
カルボキシメチルセルロース0.5部およびミョウバン0.5部を水50部の中に分散し、加温溶解させキャリア糊とした。このキャリア糊に馬鈴薯澱粉70部と甘藷澱粉30部および水120部を加えた後、十分に混錬し、澱粉スラリーとした。ステンレストレイに澱粉スラリーを厚さ1cm程度となるように流し込み、90℃の蒸し器中で15分間糊化を行った後、冷水中にて粗熱をとり、糊化澱粉含有組成物を得た。更に、前記糊化澱粉含有組成物を4℃にて冷却して所望の糊化度とした後、棚式乾燥機 (50℃)で水分が20質量%以下になるまで乾燥後、小型粉砕機にて粉砕、篩により分級し、粒度の異なる粒子状のスクラブ剤(A12,A13)を得た。なお、カルボキシメチルセルロースおよびミョウバンを添加せず、馬鈴薯澱粉70部と甘藷澱粉30部のみで同様の方法を用いて得られる糊化澱粉の糊化度は、10%以上であった。
Production Example 5
0.5 parts of carboxymethylcellulose and 0.5 parts of alum were dispersed in 50 parts of water and dissolved by heating to form a carrier paste. After 70 parts of potato starch, 30 parts of sweet potato starch and 120 parts of water were added to this carrier paste, the mixture was sufficiently kneaded to form a starch slurry. The starch slurry was poured into a stainless steel tray to a thickness of about 1 cm and gelatinized in a steamer at 90 ° C. for 15 minutes, and then crude heat was taken in cold water to obtain a gelatinized starch-containing composition. Furthermore, the gelatinized starch-containing composition is cooled at 4 ° C. to obtain a desired gelatinization degree, and then dried by a tray dryer (50 ° C.) to a water content of 20% by mass or less, and then a small pulverizer The resultant was pulverized and classified by a sieve to obtain particulate scrub agents (A12, A13) having different particle sizes. The gelatinization degree of the gelatinized starch obtained by using the same method only with 70 parts of potato starch and 30 parts of sweet potato starch without adding carboxymethylcellulose and alum was 10% or more.
[製造例6]
カルボキシメチルセルロース0.5部およびキサンタンガム0.5部を水50部の中に分散し、加温溶解させキャリア糊とした。このキャリア糊に馬鈴薯澱粉70部とコーンスターチ30部および水120部を加えた後、十分に混錬し澱粉スラリーとした。ステンレストレイに澱粉スラリーを厚さ1cm程度となるように流し込み、90℃の蒸し器中で15分間糊化を行った後、冷水中にて粗熱をとり、糊化澱粉含有組成物を得た。更に、前記糊化澱粉含有組成物を4℃にて冷却して所望の糊化度とした後、棚式乾燥機 (50℃)で水分が20質量%以下になるまで乾燥後、小型粉砕機にて粉砕、篩により分級し、粒度の異なる粒子状のスクラブ剤(A14,A15)を得た。なお、カルボキシメチルセルロースおよびキサンタンガムを添加せず、馬鈴薯澱粉70部とコーンスターチ30部のみで同様の方法を用いて得られる糊化澱粉の糊化度は、10%以上であった。
Production Example 6
0.5 parts of carboxymethylcellulose and 0.5 parts of xanthan gum were dispersed in 50 parts of water and dissolved by heating to form a carrier paste. After 70 parts of potato starch, 30 parts of corn starch and 120 parts of water were added to this carrier paste, the mixture was sufficiently kneaded to form a starch slurry. The starch slurry was poured into a stainless steel tray to a thickness of about 1 cm and gelatinized in a steamer at 90 ° C. for 15 minutes, and then crude heat was taken in cold water to obtain a gelatinized starch-containing composition. Furthermore, the gelatinized starch-containing composition is cooled at 4 ° C. to obtain a desired gelatinization degree, and then dried by a tray dryer (50 ° C.) to a water content of 20% by mass or less, and then a small pulverizer The resultant was pulverized and classified by a sieve to obtain particulate scrub agents (A14, A15) having different particle sizes. The gelatinization degree of gelatinized starch obtained by using the same method using only 70 parts of potato starch and 30 parts of corn starch without adding carboxymethylcellulose and xanthan gum was 10% or more.
[製造例7]
ワキシーコーンスターチ4部を水50部の中に分散し、沸騰浴中にて糊化させキャリア糊とした。このキャリア糊にワキシーコーンスターチ96部と水70部を加えた後、十分に混錬し澱粉スラリーとした。ステンレストレイに澱粉スラリーを厚さ1cm程度となるように流し込み、90℃の蒸し器中で15分間糊化を行い、糊化澱粉を得た。更に、前記糊化澱粉を常温で放冷して所望の糊化度とした後、棚式乾燥機 (50℃)で水分が20質量%以下になるまで乾燥後、小型粉砕機にて粉砕、篩により分級し、粒度の異なる粒子状のスクラブ剤(A16,A17)を得た。
Production Example 7
Four parts of waxy corn starch were dispersed in 50 parts of water and gelatinized in a boiling bath to form a carrier paste. After 96 parts of waxy corn starch and 70 parts of water were added to this carrier paste, the mixture was thoroughly kneaded to form a starch slurry. The starch slurry was poured into a stainless steel tray to a thickness of about 1 cm, and gelatinization was performed for 15 minutes in a steamer at 90 ° C. to obtain gelatinized starch. Furthermore, the gelatinized starch is allowed to cool at ordinary temperature to obtain a desired gelatinization degree, and then dried with a shelf dryer (50 ° C.) to a water content of 20% by mass or less, and then crushed with a small crusher, The resultant was classified by a sieve to obtain particulate scrub agents (A16, A17) having different particle sizes.
[製造例8]
ハイアミロースコーンスターチ20部を水50部の中に分散し、沸騰浴中にて糊化させキャリア糊とした。このキャリア糊にハイアミロースコーンスターチ80部と水70部を加えた後、十分に混錬し澱粉スラリーとした。ステンレストレイに澱粉スラリーを厚さ1cm程度となるように流し込み、90℃の蒸し器中で15分間糊化を行った後、冷水中にて粗熱をとり、糊化澱粉を得た。更に、前記糊化澱粉を−5℃で冷却して所望の糊化度とした後、棚式乾燥機 (50℃)で水分が20質量%以下になるまで乾燥後、小型粉砕機にて粉砕、篩により分級し、粒度の異なる粒子状のスクラブ剤(A18,A19)を得た。
Production Example 8
Twenty parts of high amylose corn starch was dispersed in 50 parts of water and gelatinized in a boiling bath to form a carrier paste. After 80 parts of high amylose corn starch and 70 parts of water were added to this carrier paste, the mixture was thoroughly kneaded to form a starch slurry. The starch slurry was poured into a stainless steel tray to a thickness of about 1 cm, gelatinized in a steamer at 90 ° C. for 15 minutes, and then crude heat was taken in cold water to obtain gelatinized starch. Furthermore, after cooling the gelatinized starch at -5 ° C to obtain a desired gelatinization degree, it is dried by a tray dryer (50 ° C) until the water content is 20% by mass or less, and then crushed by a small crusher The resultant was classified by sieve to obtain particulate scrub agents (A18, A19) having different particle sizes.
[比較製造例1]
馬鈴薯澱粉100部に水120部を加え、澱粉スラリーを調製した。得られた澱粉スラリーを、常法に従ってダブルドラムドライヤー(蒸気内圧:6.0kg/cm2、ドラム径φ0.4m、ドラム長さ0.5m、回転数1.2rpm)で糊化および急速乾燥を行い、糊化澱粉を得た。得られた糊化澱粉を、小型粉砕機にて粉砕し、篩により分級し、フィルム状のスクラブ剤(B1)を得た。
[Comparative Production Example 1]
120 parts of water was added to 100 parts of potato starch to prepare a starch slurry. The obtained starch slurry was subjected to gelatinization and rapid drying using a double drum dryer (internal pressure of steam: 6.0 kg / cm 2 , drum diameter φ 0.4 m, drum length 0.5 m, rotation speed 1.2 rpm) according to a conventional method. Conducted to obtain gelatinized starch. The obtained gelatinized starch was ground with a small grinder and classified with a sieve to obtain a film-like scrub agent (B1).
[比較製造例2]
2軸型エクストルーダーに、豌豆澱粉をフィード量22.0g/minで連続的に供給するとともに、3〜5g/minで水を投入し、バレル温度150℃、ダイ出口温度130〜140℃、圧力60〜80kgf/cm2で押出すことにより、糊化および急速乾燥を行い、糊化澱粉を得た。得られた糊化澱粉を、小型粉砕機にて粉砕し、篩により分級し、粒子状のスクラブ剤(B2,B3)を得た。
[Comparative production example 2]
The soybean starch is continuously fed at a feed rate of 22.0 g / min to a twin-screw extruder, and water is introduced at 3 to 5 g / min, barrel temperature 150 ° C, die outlet temperature 130 to 140 ° C, pressure By extruding at 60 to 80 kgf / cm 2 , gelatinization and rapid drying were performed to obtain gelatinized starch. The obtained gelatinized starch was ground with a small grinder and classified with a sieve to obtain a particulate scrub agent (B2, B3).
[比較製造例3]
流動層造粒コーティング装置を用いて、常法に従い、コーンスターチ100部に対してポリビニルアルコール5部を水200部に分散した溶液をバインダー液として造粒を行い、篩により分級し、顆粒状のスクラブ剤(C1)を得た。
[Comparative production example 3]
Using a fluid bed granulation coating apparatus, according to a conventional method, a solution of 5 parts of polyvinyl alcohol dispersed in 200 parts of water with respect to 100 parts of corn starch is granulated using a binder solution, classified by a sieve, and a granular scrub An agent (C1) was obtained.
[比較製造例4]
流動層造粒コーティング装置を用いて、球形細粒状澱粉「グラフローM」(日澱化學株式会社製)100部に対してアルギン酸Na3部を水100部に分散した溶液を球形細粒状澱粉表面にコーティングした。続いて、塩化カルシウム3部を水100部に分散した溶液をコーティングし耐水化を行った。得られた耐水性造粒物を篩により分級し、顆粒状のスクラブ剤(C2)を得た。
[Comparative production example 4]
Using a fluid bed granulation coating apparatus, a solution of 3 parts of sodium alginate dispersed in 100 parts of water with respect to 100 parts of spherical fine granular starch "Graflaw M" (manufactured by Sun Seri Co., Ltd.) is coated on the surface of spherical fine granular starch did. Subsequently, a solution of 3 parts of calcium chloride dispersed in 100 parts of water was coated to perform water resistance. The obtained water-resistant granulated material was classified by a sieve to obtain a granular scrub agent (C2).
表1にスクラブ剤A1〜A19の粒子径、膨潤崩壊率および糊化度を示す。また、比較例として未糊化馬鈴薯澱粉原料(N1)、比較製造例にて作成したスクラブ剤B1〜B3およびC1〜C2、市販のとうもろこし穂軸の粉砕物(D1)、グルコマンナンスクラブ(E1)の粒子径、膨潤崩壊率および糊化度を表2に示す。表1,2に記載の各物性値は、以下の方法により測定した。 Table 1 shows particle sizes, swelling and disintegration rates and gelatinization degrees of the scrub agents A1 to A19. In addition, as a comparative example, non-gelatinized potato starch raw material (N1), scrub agents B1 to B3 and C1 to C2 prepared in the comparative production example, commercially available corn cob ground product (D1), glucomannan scrub (E1) The particle size, the swelling and disintegration rate and the degree of gelatinization of each are shown in Table 2. Each physical property value described in Tables 1 and 2 was measured by the following method.
[粒子径の測定]
レーザ回折式粒子径分布測定装置(SALD−2200 : 株式会社島津製作所製、回分セル使用)を使用して測定を行い、エタノール中および水中にスクラブ剤を分散し、1分後におけるメディアン径を測定値とした。
[Measurement of particle size]
Measure using a laser diffraction particle size distribution analyzer (SALD-2200: manufactured by Shimadzu Corporation, using a batch cell), disperse the scrub agent in ethanol and in water, and measure the median diameter after 1 minute It is a value.
[膨潤崩壊率]
下記の式に従い、スクラブ剤の水中における膨潤崩壊率を算出した。
膨潤崩壊率=(水中におけるスクラブ剤のメディアン径)÷(エタノール中におけるスクラブ剤のメディアン径)
[Swelling disintegration rate]
The swelling and disintegration rate of the scrubbing agent in water was calculated according to the following equation.
Swelling disintegration rate = (median diameter of scrub agent in water) ÷ (median diameter of scrub agent in ethanol)
[糊化度の測定]
A1、A4、A6、A10、A12、A14、A16、A18およびN1、B1、B2のスクラブ剤について、必要に応じて各スクラブ剤を小型粉砕機にて精粉し、100mesh篩を通したものを測定サンプルとする。糊化度は以下の方法により測定を行った。
[Measurement of gelatinization degree]
The scrub agents A1, A4, A6, A10, A12, A14, A16, A18 and N1, B1, B2 are scrubbed with a small crusher, if necessary, after passing through a 100 mesh sieve Let it be a measurement sample. The gelatinization degree was measured by the following method.
(試薬)
・ 0.8M酢酸緩衝液(pH 6.0)
・ 2M酢酸液
・ 酵素液 (1mL中にプルラナーゼ3.4単位,β-アミラーゼ0.8単位を含む)
プルラナーゼ,β-アミラーゼを0.8 mol/L 酢酸緩衝液(pH 6.0)に溶解し、不溶性部分をNo.2のろ紙でろ過する。
・ 銅試液
A液:15%硫酸銅液(CuSO4・5H2O 15g/100mL)
B液:無水炭酸ソーダ25g, ロッセル塩25g, 炭酸水素ナトリウム20g,無水硫酸ソーダ200gをイオン交換水で1Lとする。
A液 1.0mL,B液 25mLの割合で混じ銅試薬として用いる。
・ ネルソン試液
モリブデン酸アンモニウム25gを900mLのイオン交換水にとかし、これに濃硫酸42gおよびひ酸水素二ナトリウム七水和物3gを加える。さらにイオン交換水を加えて全量1Lとする。
(reagent)
0.8 M acetate buffer (pH 6.0)
・ 2M acetic acid solution
・ Enzyme solution (containing 3.4 units of pullulanase and 0.8 units of β-amylase in 1 mL)
Pullulanase and β-amylase were dissolved in 0.8 mol / L acetate buffer (pH 6.0), and the insoluble portion was dissolved in no. Filter with 2 filter paper.
・ Copper test solution
Solution A: 15% copper sulfate solution (CuSO 4 · 5 H 2 O 15 g / 100 mL)
Solution B: 25 g of anhydrous sodium carbonate, 25 g of Russel salt, 20 g of sodium hydrogen carbonate and 200 g of anhydrous sodium sulfate are made 1 L with ion-exchanged water.
Use as a copper reagent mixed with 1.0 mL of solution A and 25 mL of solution B.
Nelson's test solution 25 g of ammonium molybdate is dissolved in 900 mL of deionized water, to which 42 g of concentrated sulfuric acid and 3 g of disodium hydrogen arsenate heptahydrate are added. Further, ion exchange water is added to make the total amount 1 liter.
(測定方法)
1.試料100mgをガラス製ホモジナイザー(テフロン(登録商標)ペストル付き)にとり、10mLのイオン交換水を加え、ホモジナイザーを上下して十分に分散を行う。この後、4mLずつを2本の50mLメスフラスコにとる。
2.1本は0.8M酢酸緩衝液(pH6.0)で定容し、(A)試料用サンプルとする。他の1本には0.4mLの10M 水酸化ナトリウム水溶液(NaOH) を加えて、3〜5分50℃の温浴中で完全に糊化させる。その後、2mLの2M酢酸を加えて中和する。0.8M酢酸緩衝液(pH 6.0)で定容し(B)完全糊化試料とする。
3.試験管に(A)(B)それぞれについて4mL採取し、酵素液1mLを加え、40℃で30分間振とう恒温槽中で反応を行う。同時に(a)ブランク試験用として、試料用サンプル4mLと失活酵素(10分間煮沸、沈殿物をNo.2のろ紙でろ過)1mLを加えた区分をつくる。
4.反応終了後、5分間沸騰浴中で酵素を失活させ、5倍に希釈する。これより1mL採取し、ソモジー-ネルソン(Somogyi−Nelson法)に準じて還元力を測定する。
<ソモジー-ネルソン法に準じた方法>
5.ネジ付試験管に試料1mLと銅試薬1mLを加えて栓をし、沸騰浴中で10分間加熱する。
6.その後急冷し、ネルソン試薬1mLを加えて混合し酸化銅(I)(Cu2O)を溶かして発色させる。イオン交換水を20mL加えて希釈する。
7.15分後500nmの吸光度を測定する。
8.次式に従い、糊化度を測定する。
糊化度(%)=((A)試料用サンプルの吸光度 ―(a)ブランクの吸光度))÷((B)完全糊化試料の吸光度 ―(a)ブランクの吸光度))×100
(Measuring method)
1. 100 mg of a sample is placed in a glass homogenizer (with Teflon® pestle), 10 mL of ion exchange water is added, and the homogenizer is moved up and down to achieve sufficient dispersion. After this, take 4 mL each into two 50 mL volumetric flasks.
2. Make a volume of 0.8M acetate buffer (pH 6.0), and use this as the sample for (A) sample. Add 0.4 mL of 10 M aqueous sodium hydroxide solution (NaOH) to the other and allow to gelatinize completely in a 50 ° C water bath for 3 to 5 minutes. Then neutralize by adding 2 mL of 2 M acetic acid. Make volume with 0.8 M acetate buffer (pH 6.0) (B) to make a completely gelatinized sample.
3. 4 mL of each of (A) and (B) is collected in a test tube, 1 mL of an enzyme solution is added, and the reaction is performed in a shaking thermostat at 40 ° C. for 30 minutes. At the same time, for (a) blank test, make a section to which 4 mL of sample for sample and 1 mL of inactivated enzyme (boiled for 10 minutes, filter precipitate with No. 2 filter paper) are added.
4. After completion of the reaction, inactivate the enzyme in a boiling bath for 5 minutes and dilute 5 times. From this, 1 mL is collected, and the reducing power is measured according to Somogyi-Nelson (Somogyi-Nelson method).
<Method based on Somogyi-Nelson method>
5. Add 1 mL of sample and 1 mL of copper reagent to a threaded test tube, stopper and heat in a boiling bath for 10 minutes.
6. After quenching, 1 mL of Nelson's reagent is added and mixed to dissolve copper (I) oxide (Cu 2 O) and develop color. Add 20 mL of deionized water to dilute.
7. Measure absorbance at 500 nm after 15 minutes.
8. The degree of gelatinization is measured according to the following equation.
Degree of gelatinization (%) = ((A) absorbance of sample for sample-(a) absorbance of blank)) ((B) absorbance of completely gelatinized sample-(a) absorbance of blank) x 100
[実施例1〜19]
市販の洗顔フォーム(花王株式会社製:ビオレスキンケア洗顔料 リッチモイスチャー、成分に水を含む)95部にスクラブ剤A1〜A19を5部添加し、十分に混合分散した。スクラブ剤単独および得られたスクラブ剤配合洗顔フォームを使用した際の官能評価を行った。評価項目及び評価方法は以下の通りとし、結果を表3に示す。
[Examples 1 to 19]
Five parts of the scrub agent A1 to A19 were added to 95 parts of a commercially available facial cleansing foam (manufactured by Kao Corporation: Biole skin care face cleanser rich moisture, the ingredients contain water), and thoroughly mixed and dispersed. A sensory evaluation was conducted using the scrub agent alone and the resulting scrub agent-containing facial wash foam. Evaluation items and evaluation methods are as follows, and the results are shown in Table 3.
(使用感の評価)
(試験区A)乾燥状態のスクラブ剤1g、(試験区B)スクラブ剤配合洗顔フォーム1g、(試験区C)スクラブ剤配合洗顔フォーム1gに水10gを添加したもの、以上の3つに関して、手のひらで擦り合わせた際のスクラブ感(粒子感)を評価した。
+3:スクラブ感がかなり強い
+2:スクラブ感が強い
+1:適度なスクラブ感(0よりもやや強い)
0:適度なスクラブ感
−1:適度なスクラブ感(0よりもやや弱い)
−2:スクラブ感が弱い
−3:スクラブ感がかなり弱い、或いはスクラブ感を感じない
(Evaluation of feeling of use)
(Test area A) 1 g of dry scrubbing agent, (Test area B) 1 g of scrub agent-containing face wash foam, (Test area C), 1 g of scrub agent-containing face wash foam with 10 g of water added The scrub feeling (graininess) when rubbed together was evaluated.
+3: Scrub feeling is quite strong +2: Scrub feeling is strong +1: Moderate scrub feeling (slightly stronger than 0)
0: Moderate scrub feeling -1: Moderate scrub feeling (somewhat weaker than 0)
-2: Scrub feeling is weak -3: Scrub feeling is very weak or does not feel scrub feeling
(持続性の評価)
試験区Bにおいて、継続して1分間手のひらで擦り合わせを行う。1分後のスクラブ感(粒子感)に関して、持続性を評価した。
◎:1分後も使用直後と同等のスクラブ感を感じる
○:1分後もスクラブ感を感じる
×:スクラブ感を感じない
(Evaluation of sustainability)
In test area B, continue rubbing with palm for 1 minute. The durability was evaluated with respect to the sense of scrub after 1 minute (graininess).
: 1: Scrub feeling equal to that immediately after use even after 1 minute ○: Scrub feel after 1 minute ×: No scrub feeling
(刺激性の評価)
試験区Cにおいて、手のひらで擦り合わせを行った際の刺激性を評価した。
◎:痛感などの刺激性がない
○:痛感などの刺激性がほとんどない
×:痛感などの刺激性があり、不快感がある
(Evaluation of irritation)
In the test zone C, the irritant ability when rubbing with a palm was evaluated.
:: no sensation of irritant such as pain ○: hardly irritant such as sensation of pain x: irritant such as sensation of pain, and discomfort
(配合安定性の評価)
調整したスクラブ剤配合洗顔フォームを50℃の恒温機中に1週間保存した。1週間後、試験区Bと同様に試験を行い、配合安定性を評価した。
◎:1週間後も調製直後と同程度のスクラブ感を有している
○:1週間後もスクラブ感を有している(◎よりやや劣る)
×:1週間後、調製直後よりもスクラブ感が大きく低下、或いは消失している
(Evaluation of formulation stability)
The adjusted scrubbing face wash foam was stored in a thermostat at 50 ° C. for one week. After one week, a test was conducted in the same manner as in Test Area B to evaluate the compounding stability.
◎: Scrub feeling similar to that immediately after preparation after 1 week ○: Scrub feeling after 1 week (slightly inferior to よ り)
X: After 1 week, the feeling of scrub decreased significantly or disappeared immediately after preparation
(総合評価)
S:使用感(試験区B、C)の評価が±1または0であり、かつ、持続性・刺激性・配合安定性のうち、×を含まず◎が2個以上である場合
A:使用感(試験区B、C)の評価が±1または0であり、かつ、持続性・刺激性・配合安定性のうち、×を含まず◎が1個である場合
B:使用感(試験区B、C)の評価が±1または0であり、かつ、持続性・刺激性・配合安定性の全てが○である場合
C:使用感(試験区B、C)の評価が±2または±3である、または、持続性・刺激性・配合安定性のうち、×が1個以上である場合
(Comprehensive evaluation)
S: Evaluation of feeling in use (test area B, C) is ± 1 or 0, and out of durability, irritation and compounding stability, x is not included and 以上 is 2 or more A: use When the evaluation of feeling (test area B, C) is ± 1 or 0, and 持 続 is one out of sustained, irritating, and compounding stability B: feeling of use (test area B, when the evaluation of C) is ± 1 or 0, and all of the persistence, irritation and compounding stability are C C: Evaluation of feeling in use (test area B, C) is ± 2 or ± 3 or in the case of x being 1 or more among durability, irritation and compounding stability
[比較例1〜8]
スクラブ剤A1をスクラブ剤N1、B1〜B3、C1〜C2、D1、E1に変更した以外は実施例1と同様の方法でスクラブ剤配合洗顔フォーム作成し、官能評価を行った。結果を表4に示す。
[Comparative Examples 1 to 8]
A scrub agent-containing cleansing foam was prepared and sensory evaluation was performed in the same manner as in Example 1 except that the scrub agent A1 was changed to the scrub agents N1, B1 to B3, C1 to C2, D1 and E1. The results are shown in Table 4.
表1〜4の結果からわかるように、糊化度が10〜90%であるスクラブ剤(A1〜A19)は、乾燥粒子状態では高い硬度を有しているため、強いスクラブ感があり、やや刺激性を感じる。しかし、洗浄剤への配合時や使用時において、水分を吸収することにより粒子の膨潤や表面の軟化が起こり、結果として使用時の刺激性が低下している。更に、水の存在下においても溶解や崩壊が起こらず、粒子形状を保つため、良好な持続性や洗浄剤への配合安定性が得られる。
一方、糊化度が90%以上であるスクラブ剤(B1〜B3)を使用した場合、上記A1〜A19と同様に粒子の膨潤は起こるが、本発明の特徴であるスクラブ感や洗浄剤への配合安定性が得られない。
As can be seen from the results in Tables 1 to 4, the scrub agents (A1 to A19) having a degree of gelatinization of 10 to 90% have high hardness in the dry particle state, and thus have a strong scrub feeling, I feel irritating. However, when incorporated into detergents and used, swelling of the particles and softening of the surface occur by absorbing moisture, and as a result, the irritation during use decreases. Furthermore, dissolution or disintegration does not occur even in the presence of water, and the particle shape is maintained, so that good durability and formulation stability to a detergent can be obtained.
On the other hand, when a scrubbing agent (B1 to B3) having a degree of gelatinization of 90% or more is used, swelling of particles occurs as in the above A1 to A19, but the scrub feeling and the cleaning agent which are the features of the present invention Compounding stability can not be obtained.
(処方例1〜7)
以下に本発明のスクラブ剤を含有する洗浄剤の処方例を示すが、処方例は各製品の製造における常法により製造したもので、剤中の含有量のみを示した。又、本発明はこれらの処方に限定されるわけではない。なお、各表に記載の数値は、組成物全体を100とした時の質量%である。
(Prescription Examples 1 to 7)
Although the formulation example of the cleaning agent containing the scrub agent of this invention is shown below, a formulation example is what was manufactured by the usual method in manufacture of each product, and showed only the content in an agent. Also, the present invention is not limited to these formulations. In addition, the numerical value described in each table is mass% when the whole composition is set to 100.
処方例1〜7に記載のスクラブ含有洗浄料は、いずれも使用時に痛感などの不快感がなく、かつ長期保存後も良好な使用感を有しており、更には洗浄性および/またはマッサージ効果に優れるものであった。 All the scrub-containing cleansing agents described in Formulation Examples 1 to 7 have no discomfort such as a feeling of pain when used, and have a good feeling of use even after long-term storage, and further the cleansing property and / or the massage effect Was excellent.
本発明のスクラブ剤は、糊化澱粉を含有することを特徴とするものである。前記スクラブ剤は優れたスクラブ感を有し、かつ肌に痛感を感じない等の低い刺激性、洗浄剤への配合安定性を併せ持つ。 The scrub agent of the present invention is characterized by containing gelatinized starch. The above-mentioned scrubbing agents have an excellent scrubbing feeling, and also have low irritation such as not to feel pain on the skin and formulation stability to detergents.
Claims (4)
The cleaning agent containing the scrub agent in any one of Claims 1-2 .
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2017223077A JP6541756B2 (en) | 2017-11-20 | 2017-11-20 | Scrub agents and scrub-containing cleaners |
| PCT/JP2018/042608 WO2019098358A1 (en) | 2017-11-20 | 2018-11-19 | Scrubbing agent and detergent containing scrubbing agent |
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| Application Number | Priority Date | Filing Date | Title |
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| JP2017223077A JP6541756B2 (en) | 2017-11-20 | 2017-11-20 | Scrub agents and scrub-containing cleaners |
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| JP6541756B2 true JP6541756B2 (en) | 2019-07-10 |
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| JP2003063939A (en) * | 2001-08-28 | 2003-03-05 | Lion Corp | Dentifrice composition |
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