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JP2001172395A - Method for producing polymer solution - Google Patents

Method for producing polymer solution

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Publication number
JP2001172395A
JP2001172395A JP37659999A JP37659999A JP2001172395A JP 2001172395 A JP2001172395 A JP 2001172395A JP 37659999 A JP37659999 A JP 37659999A JP 37659999 A JP37659999 A JP 37659999A JP 2001172395 A JP2001172395 A JP 2001172395A
Authority
JP
Japan
Prior art keywords
polymer
solvent
dispersion
liquid
powder
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.)
Pending
Application number
JP37659999A
Other languages
Japanese (ja)
Inventor
Keiko Arai
恵子 新井
Manabu Kobayashi
学 小林
Yutaka Shintani
裕 新谷
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Lion Corp
Original Assignee
Lion Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Lion Corp filed Critical Lion Corp
Priority to JP37659999A priority Critical patent/JP2001172395A/en
Publication of JP2001172395A publication Critical patent/JP2001172395A/en
Pending legal-status Critical Current

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Abstract

(57)【要約】 【解決手段】溶媒を攪拌機で撹拌して、溶媒に気泡を巻
き込み、気−液分散液を形成し、該気−液分散液に高分
子粉体を投入して、膨潤溶解させる 【効果】汎用の撹拌槽で、簡便な方法により高分子のダ
マ化を防止して効率的に高分子を均一に膨潤溶解させる
ことができる。
(57) Abstract: A solvent is stirred by a stirrer, air bubbles are entrained in the solvent to form a gas-liquid dispersion, and a polymer powder is charged into the gas-liquid dispersion to swell. Dissolve [Effect] In a general-purpose stirring tank, it is possible to prevent lumps of the polymer by a simple method and efficiently swell and dissolve the polymer efficiently.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、化粧品、洗浄剤等
に配合される高分子をダマを生じることなく膨潤溶解さ
せて、短時間に均一な高分子溶液得る製造方法に関す
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a uniform polymer solution in a short time by swelling and dissolving a polymer blended in cosmetics, detergents and the like without producing lumps.

【0002】[0002]

【従来の技術】一般に、化粧品、洗浄剤等の組成物に配
合される高分子は、溶媒と接触したと、ダマやままこ等
の未溶解物を形成し、膨潤溶解に長時間を要するという
問題があり、これを解決するために種々の方法が提案さ
れている。例えば、高速攪拌機により25℃以下で30
0秒以内に水溶性高分子を水の中に投入し、直ちに昇温
を行う方法(特開平8−283418号公報)。溶媒を
恒温ジャケット付きタンク内に入れ温度30〜39℃
で、撹拌レイノルズ数が2.0×10以上となる様に
撹拌し、高分子粉体を投入して、分散後、40℃までは
1℃/min以上の速度で昇温し、さらに50〜60℃
まで昇温す方法(特開平11−209476号公報)。
高分子粉体に、溶媒と親和性を有する継粉抑制剤(セル
ロース等)を混合する方法(特開平11−197476
号公報)等である。これらの方法は、特殊な撹拌装置や
厳密な温度管理を必要としたり、第3物質の添加が必要
等の問題があり、汎用的な撹拌槽を用いる簡便な方法が
望まれていた。
2. Description of the Related Art Generally, when a polymer compounded in a composition such as a cosmetic or a detergent is brought into contact with a solvent, it forms undissolved substances such as lumps and cages and takes a long time to swell and dissolve. In order to solve this, various methods have been proposed. For example, 30 ° C. or less with a high-speed
A method in which a water-soluble polymer is put into water within 0 seconds, and the temperature is raised immediately (Japanese Patent Laid-Open No. 8-283418). Put the solvent in a tank with a constant temperature jacket and put the temperature at 30-39 ° C
Then, the mixture is stirred so that the stirring Reynolds number becomes 2.0 × 10 5 or more, the polymer powder is charged, and after the dispersion, the temperature is raised to 40 ° C. at a rate of 1 ° C./min or more. ~ 60 ° C
(JP-A-11-209476).
A method of mixing a powder inhibitor (such as cellulose) having an affinity for a solvent with a polymer powder (JP-A-11-197476).
Publication). These methods require special stirrers, strict temperature control, and the need to add a third substance. Therefore, a simple method using a general-purpose stirring tank has been desired.

【0003】[0003]

【発明が解決しようとする課題】従って、本発明は、汎
用の撹拌槽で、簡便な方法により高分子のダマ化を防止
して効率的に高分子を均一に膨潤溶解させる方法を提供
することを目的とする。
Accordingly, an object of the present invention is to provide a method for preventing lumping of a polymer by a simple method and efficiently swelling and dissolving the polymer uniformly in a general-purpose stirring tank. With the goal.

【0004】[0004]

【課題を解決するための手段及び発明の実施の形態】本
発明者等は、鋭意研究した結果、溶媒中の気泡が高分子
粉体粒子の凝集を抑制してダマ化を防止できることを見
出し、本発明を完成するに至った。即ち、本発明は、撹
拌槽を用いて、溶媒に高分子粉体を膨潤溶解させて、高
分子溶液を製造する際に、溶媒を攪拌機で撹拌して、溶
媒に気泡を巻き込み、気−液分散液を形成し、該気−液
分散液に高分子粉体を投入して、膨潤溶解させることに
よる高分子溶液の製造方法である。
Means for Solving the Problems and Embodiments of the Invention As a result of intensive studies, the present inventors have found that bubbles in a solvent can suppress aggregation of polymer powder particles and prevent lumping. The present invention has been completed. That is, the present invention uses a stirring tank to swell and dissolve polymer powder in a solvent to produce a polymer solution.When the polymer solution is produced, the solvent is stirred by a stirrer, bubbles are entrained in the solvent, and gas-liquid This is a method for producing a polymer solution by forming a dispersion, adding polymer powder to the gas-liquid dispersion, and swelling and dissolving the polymer powder.

【0005】以下、本発明につき更に詳しく説明する。
なお、以下に記載の配合量の%表示は、質量%のことで
ある。本発明の高分子溶液の製造方法は、まず、第1ス
テップとして、撹拌槽に高分子溶液の製造に必要な溶媒
の1部または全量を投入し、撹拌して溶媒中に気泡を巻
き込んで気−液分散液を形成する。
Hereinafter, the present invention will be described in more detail.
In addition,% indication of the blending amount described below means mass%. In the method for producing a polymer solution according to the present invention, first, as a first step, one part or all of a solvent necessary for producing a polymer solution is charged into a stirring tank, and the mixture is stirred to introduce air bubbles into the solvent and evaporate. Forming a liquid dispersion;

【0006】本発明において、撹拌槽は、パドル、プロ
ペラ、タービン、パルセーター等の撹拌羽根を備えた汎
用のものが使用できる。上記の溶媒中に気泡を巻き込む
撹拌状態は、例えば、図1に示すように、撹拌により生
じたボルテックスの深さ(L)と撹拌停止時の静止液面
の高さ(H)との比率Z=L/H×100(%)が、5
0%以上、特に50〜85%の状態で撹拌することが好
ましい。
In the present invention, as the stirring tank, a general-purpose stirring tank such as a paddle, a propeller, a turbine, and a pulsator can be used. As shown in FIG. 1, for example, the stirring state in which air bubbles are entrapped in the solvent is a ratio Z between the depth (L) of the vortex generated by stirring and the height (H) of the stationary liquid surface when stirring is stopped. = L / H x 100 (%) is 5
It is preferable to stir in a state of 0% or more, particularly 50 to 85%.

【0007】次に、第2のステップとして、上記の気−
液分散液に高分子粉体を投入して、膨潤溶解させる。高
分子粉体は、液面に投入した粉体が液中に巻き込まれる
速度より遅い速度で投入することが好ましい。高分子溶
液の製造に必要な全溶媒量の1部を使用して第1ステッ
プの気−液分散液を調製し、これに高分子粉体を投入、
分散した後、残りの溶媒を添加しても良い。高分子粉体
が気−液分散液中に巻き込まれて均一に分散し、膨潤溶
解を開始すると分散液の粘度が徐々に増加するため上記
ボルテックスの深さは徐々に減少し、このため液中に気
泡を巻き込まなくなる。このような状態になると分散液
中の気泡は徐々に抜け、高分子の膨潤溶解が完了する頃
には液中には気泡がほとんどなくなる。高分子溶液の粘
度が急激に増大する場合には気泡が抜けないこともあ
る。本発明は、溶媒中の気泡が、高分子の膨潤溶解の途
中で抜けるような高分子−溶媒の系に適用することが特
に好ましい
Next, as a second step, the above-mentioned energy
The polymer powder is charged into the liquid dispersion and swelled and dissolved. It is preferable that the polymer powder is charged at a speed lower than the speed at which the powder charged on the liquid surface is wound into the liquid. A gas-liquid dispersion of the first step is prepared by using one part of the total amount of the solvent necessary for the production of the polymer solution, and the polymer powder is added thereto.
After the dispersion, the remaining solvent may be added. When the polymer powder is entrained in the gas-liquid dispersion and uniformly dispersed and starts to swell and dissolve, the viscosity of the dispersion gradually increases, so that the depth of the vortex gradually decreases, and thus the No air bubbles get caught in the air. In such a state, bubbles in the dispersion liquid gradually escape, and almost no bubbles remain in the liquid by the time the swelling and dissolution of the polymer is completed. When the viscosity of the polymer solution increases rapidly, bubbles may not be removed. The present invention is particularly preferably applied to a polymer-solvent system in which bubbles in a solvent escape during the swelling and dissolution of the polymer.

【0008】本発明に用いられる溶媒としては、水、ア
ルコール、多価アルコール、油類(油脂、脂肪酸、炭化
水素、エステル等)等又はこれらの混合物又は、これら
溶媒に界面活性剤、高分子、防腐剤、抗菌剤、分散安定
化剤(ピロリン酸ナトリウム等),pH調整剤等の他の
成分が溶解したものも適宜使用できる。特に、好ましく
は、水性溶媒である。
The solvent used in the present invention includes water, alcohols, polyhydric alcohols, oils (oils, fats, fatty acids, hydrocarbons, esters, etc.) or mixtures thereof, or surfactants, polymers, Those in which other components such as a preservative, an antibacterial agent, a dispersion stabilizer (such as sodium pyrophosphate), and a pH adjuster are dissolved can also be used as appropriate. Particularly preferred is an aqueous solvent.

【0009】本発明に用いられる高分子粉体としては、
好ましくは嵩密度1.0g/cm以下の粉体である。
高分子としては、特に限定されないが、例えば、、カル
ボキシメチルセルロース、メチルセルロース、ヒドロキ
シメチルセルロース、ヒドロキシプロピルメチルセルロ
ース、ヒドロキシエチルセルロース等のセルロース誘導
体、キサンタンガム、グアーガム等の天然高分子、カル
ボキシビニルポリマー、ポリアクリル酸、(メタ)アク
リル酸系共重合体等の合成高分子が挙げられる。特に、
セルロース誘導体、キサンタンガム、カルボキシビニル
ポリマー等の膨潤溶解には、顕著な効果が認められるの
で、これらに本発明を適用することが好ましい。
The polymer powder used in the present invention includes:
Preferably, the powder has a bulk density of 1.0 g / cm 3 or less.
Examples of the polymer include, but are not particularly limited to, for example, cellulose derivatives such as carboxymethylcellulose, methylcellulose, hydroxymethylcellulose, hydroxypropylmethylcellulose, and hydroxyethylcellulose; natural polymers such as xanthan gum and guar gum; carboxyvinyl polymer; polyacrylic acid; Synthetic polymers such as (meth) acrylic acid-based copolymers are exemplified. In particular,
Swelling and dissolution of cellulose derivatives, xanthan gum, carboxyvinyl polymer and the like have a remarkable effect, and it is preferable to apply the present invention to these.

【0010】[0010]

【発明の効果】本発明の高分子溶液の製造方法によれ
ば、汎用の撹拌槽で、簡便な方法により高分子のダマ化
を防止して効率的に高分子を均一に膨潤溶解させること
ができる。
According to the method for producing a polymer solution of the present invention, it is possible to prevent lumping of a polymer by a simple method in a general-purpose stirring tank and efficiently swell and dissolve the polymer efficiently. it can.

【0011】〔実施例、比較例〕以下、実施例及び比較
例を示し、本発明を具体的に説明するが、本発明は、下
記の実施例に制限されるものではない。
Examples and Comparative Examples Hereinafter, the present invention will be described specifically with reference to Examples and Comparative Examples, but the present invention is not limited to the following Examples.

【0012】[0012]

【実施例1】ガラス製500ml容器に250gの水を
入れ、直径38mmのプロペラ3枚羽根を取り付けた撹
拌装置を容器の中心部に設置し、800rpmで撹拌し
た。この時、ボルテックス深さの静止液面高さに対する
比率Zは60%で、内溶液は気泡を巻き込んだ状態であ
った。この気泡分散液に、表1に示した高分子粉体A、
1.25gを10秒で投入したところ、ダマ化すること
なく液中に均一に分散した。更に水を250g添加し、
撹拌を継続したところ、添加した高分子粉体は20分で
すべて膨潤溶解し、気泡の無い高分子溶液を得ることが
できた。
Example 1 A 500-ml glass container was charged with 250 g of water, and a stirrer equipped with three propeller blades having a diameter of 38 mm was installed at the center of the container and stirred at 800 rpm. At this time, the ratio Z of the vortex depth to the static liquid level was 60%, and the internal solution was in a state in which bubbles were involved. The polymer powder A shown in Table 1 was added to this bubble dispersion liquid.
When 1.25 g was charged in 10 seconds, it was uniformly dispersed in the liquid without lumping. Add 250g of water,
When the stirring was continued, all of the added polymer powder was swollen and dissolved in 20 minutes, and a polymer solution without bubbles could be obtained.

【0013】[0013]

【実施例2】撹拌装置を容器壁面と中心部の中間位置に
設置した以外は実施例1と同様にして行った。気液分散
液のZは65%であり、高分子粉体はダマ化することな
く液中に均一に分散し、添加した高分子粉体は25分で
すべて膨潤溶解し、気泡の無い高分子溶液を得ることが
できた。
Example 2 The procedure was performed in the same manner as in Example 1 except that the stirring device was installed at an intermediate position between the vessel wall and the center. The Z of the gas-liquid dispersion is 65%, the polymer powder is uniformly dispersed in the liquid without lumping, and the added polymer powder swells and dissolves in 25 minutes, and is a polymer without bubbles. A solution could be obtained.

【0014】[0014]

【実施例3】ガラス製5リットル容器に2000gの水
を入れ、直径38mmのパドル4枚羽根を取り付けた撹
拌装置を容器の中心部に設置し、1200rpmで撹拌
した。気液分散液のZは60%であり、この気泡分散液
に、表1に示した高分子粉体C、20gを20秒で投入
したところ、ダマ化することなく液中に均一に分散し
た。更に水を2000g添加し、撹拌を継続したとこ
ろ、添加した高分子粉体は20分ですべて膨潤溶解し、
気泡の無い高分子溶液を得ることができた。
Example 3 2000 g of water was put into a 5 liter glass container, and a stirrer equipped with four 38 mm-diameter paddles was installed at the center of the container and stirred at 1200 rpm. The Z of the gas-liquid dispersion was 60%. When 20 g of the polymer powder C shown in Table 1 was added to the bubble dispersion in 20 seconds, the dispersion was uniformly dispersed in the liquid without lumping. . When 2000 g of water was further added and stirring was continued, the polymer powder added was swollen and dissolved in 20 minutes.
A polymer solution without bubbles could be obtained.

【0015】[0015]

【実施例4】ガラス製5リットル容器に2000gの水
を入れ、直径38mmのパドル4枚羽根を取り付けた撹
拌装置を容器の中心部に設置し、2300rpmで撹拌
した。気液分散液のZは80%であり、この気泡分散液
に、表1に示した高分子粉体A、40gを20秒で投入
したところ、ダマ化することなく液中に均一に分散し
た。更に水を2000g添加し、回転数を1000rp
mに下げて撹拌を継続した。この時のZは30%とな
り、高分子粉体は20分ですべて膨潤溶解し、気泡の無
い高分子溶液を得ることができた。
Example 4 2000 g of water was put into a 5 liter glass container, and a stirrer equipped with four 38 mm-diameter paddles was installed at the center of the container and stirred at 2300 rpm. The Z of the gas-liquid dispersion was 80%. When 40 g of the polymer powder A shown in Table 1 was added to this bubble dispersion in 20 seconds, they were uniformly dispersed in the liquid without lumping. . Further, 2000 g of water was added, and the number of rotations was set to 1000 rpm.
m and continued stirring. At this time, Z was 30%, and the polymer powder was all swollen and dissolved in 20 minutes, so that a polymer solution without bubbles could be obtained.

【0016】[0016]

【実施例5】ガラス製15リットル容器に3500gの
水を入れ、直径100mmのパルセーターを取り付けた
撹拌装置により350rpmで撹拌した。気液分散液の
Zは80%であり、この気泡分散液に、表1に示した高
分子粉体B、70gを20秒で投入したところ、ダマ化
することなく液中に均一に分散した。更に水とエタノー
ルの1/1(重量比)混合溶液を3000g添加し、撹
拌を継続したところ、高分子粉体は20分ですべて膨潤
溶解し、気泡の無い高分子溶液を得ることができた。
Example 5 3500 g of water was put into a 15-liter glass container, and stirred at 350 rpm by a stirrer equipped with a pulsator having a diameter of 100 mm. Z of the gas-liquid dispersion was 80%, and 70 g of the polymer powder B shown in Table 1 was added to this bubble dispersion in 20 seconds. The dispersion was uniformly dispersed in the liquid without lumping. . Further, 3000 g of a 1/1 (weight ratio) mixed solution of water and ethanol was added, and stirring was continued. As a result, all the polymer powder was swollen and dissolved in 20 minutes, and a polymer solution without bubbles could be obtained. .

【0017】[0017]

【比較例1】ガラス製5リットル容器に2000gの水
を入れ、直径38mmのパドル4枚羽根を取り付けた撹
拌装置を容器の中心部に設置し、600rpmで撹拌し
た。分散液のZは30%であり、この分散液に、表1に
示した高分子粉体Cを徐々に添加したが、粉体が上面に
浮遊し、粉体1.5gを巻き込むまでに5分を要した。
また、実施例3で溶解できた粉体量20gの約13分の
1と非常に少ない量であるにもかかわらず、液中に巻き
込まれた粉体はダマ化し、膨潤溶解するまでに60分を
要した。
Comparative Example 1 2000 g of water was put into a 5-liter glass container, and a stirrer equipped with four paddles having a diameter of 38 mm and attached to the center of the container was stirred at 600 rpm. The Z of the dispersion was 30%, and the polymer powder C shown in Table 1 was gradually added to the dispersion. It took a minute.
In addition, despite the very small amount of about 13 times less than 20 g of the powder that could be dissolved in Example 3, the powder entrapped in the liquid was lumped and swelled and dissolved for 60 minutes. Cost.

【0018】[0018]

【比較例2】ガラス製5リットル容器に2000gの水
を入れ、直径38mmのパドル4枚羽根を取り付けた撹
拌装置を容器の中心部に設置し、500rpmで撹拌し
た。分散液のZは30%であり、この分散液に、表1に
示した高分子粉体A、40gを徐々に添加したが、実施
例4と比較して、粉体の巻き込みに10分を要した。し
かも、液中に巻き込まれた粉体はダマ化しており、回転
数を2300rpmに上げても膨潤溶解するまでには6
0分を要した。
Comparative Example 2 2000 g of water was put into a 5-liter glass container, and a stirrer equipped with four paddles having a diameter of 38 mm and attached to the center of the container was stirred at 500 rpm. The dispersion had a Z of 30%. To this dispersion, 40 g of the polymer powder A shown in Table 1 was gradually added. Compared with Example 4, it took 10 minutes to entangle the powder. Cost me. Moreover, the powder entrained in the liquid is lumpy, and even if the rotation speed is increased to 2300 rpm, the powder is swelled and dissolved by 6 times.
It took 0 minutes.

【0019】[0019]

【表1】 [Table 1]

【図面の簡単な説明】[Brief description of the drawings]

【図1】 本発明の撹拌状態を示す図である。FIG. 1 is a diagram showing a stirring state of the present invention.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】撹拌槽を用いて、溶媒に高分子粉体を膨潤
溶解させて、高分子溶液を製造する際に、溶媒を攪拌機
で撹拌して、溶媒に気泡を巻き込み、気−液分散液を形
成し、該気−液分散液に高分子粉体を投入して、膨潤溶
解させることを特徴とする高分子溶液の製造方法。
When a polymer solution is produced by swelling and dissolving a polymer powder in a solvent using a stirring tank, the solvent is stirred by a stirrer, air bubbles are entrained in the solvent, and gas-liquid dispersion is performed. A method for producing a polymer solution, comprising forming a liquid, charging a polymer powder into the gas-liquid dispersion, and swelling and dissolving.
JP37659999A 1999-12-15 1999-12-15 Method for producing polymer solution Pending JP2001172395A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP37659999A JP2001172395A (en) 1999-12-15 1999-12-15 Method for producing polymer solution

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP37659999A JP2001172395A (en) 1999-12-15 1999-12-15 Method for producing polymer solution

Publications (1)

Publication Number Publication Date
JP2001172395A true JP2001172395A (en) 2001-06-26

Family

ID=18507421

Family Applications (1)

Application Number Title Priority Date Filing Date
JP37659999A Pending JP2001172395A (en) 1999-12-15 1999-12-15 Method for producing polymer solution

Country Status (1)

Country Link
JP (1) JP2001172395A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006095756A1 (en) * 2005-03-11 2006-09-14 Taiyo Kagaku Co., Ltd. Thickening composition improved in viscosity manifestation
JP2021102578A (en) * 2019-12-25 2021-07-15 日本メナード化粧品株式会社 Thickener for transparent liquid cosmetic

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006095756A1 (en) * 2005-03-11 2006-09-14 Taiyo Kagaku Co., Ltd. Thickening composition improved in viscosity manifestation
US7744942B2 (en) 2005-03-11 2010-06-29 Taiyo Kagaku Co., Ltd. Thickening composition having improved viscosity-emerging property
JP2021102578A (en) * 2019-12-25 2021-07-15 日本メナード化粧品株式会社 Thickener for transparent liquid cosmetic
JP7433629B2 (en) 2019-12-25 2024-02-20 日本メナード化粧品株式会社 Thickener for transparent liquid cosmetics

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