Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPH0146559B2 - - Google Patents
[go: Go Back, main page]

JPH0146559B2 - - Google Patents

Info

Publication number
JPH0146559B2
JPH0146559B2 JP55080511A JP8051180A JPH0146559B2 JP H0146559 B2 JPH0146559 B2 JP H0146559B2 JP 55080511 A JP55080511 A JP 55080511A JP 8051180 A JP8051180 A JP 8051180A JP H0146559 B2 JPH0146559 B2 JP H0146559B2
Authority
JP
Japan
Prior art keywords
stirring blade
cationic surfactant
blade
water
distance
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.)
Expired
Application number
JP55080511A
Other languages
Japanese (ja)
Other versions
JPS575797A (en
Inventor
Hisashi Kunitachi
Itsuo Hama
Shoji Konishi
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 JP8051180A priority Critical patent/JPS575797A/en
Publication of JPS575797A publication Critical patent/JPS575797A/en
Publication of JPH0146559B2 publication Critical patent/JPH0146559B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Detergent Compositions (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は、カチオン界面活性剤を水中において
微粒化する方法に関するものである。 一般に、カチオン界面活性剤は依類の柔軟効果
に優れ、その中でも特に第4アンモニウム塩であ
るジオクタデシルザメチルアンモニウムクロリド
が衣類用柔軟剤として広く用いられている。これ
ら第4級アンモニウム塩以外にも、 で表わされるフオスフオニウム塩が、一般式が、 で表わされるアミド・アミン塩等のカチオン界面
活性剤も柔軟効果が優れていることが知られてい
る。 これらの界面活性剤は、疎水性の長鎖アルキル
基をもつため、衣類への吸着性に優れているが、
その多くは水に難溶性であり、柔軟剤としてて使
用し易くするために、それらの界面活性剤の殆ん
どは水に分散し、さらにゲル化防止剤として非イ
オン界面活性剤あるいは有機塩、無機塩などを添
加し、低温安定性向上剤としてアルコール等を加
えて粘度を50〜300cp前後に抑えている。 而して、このようなカチオン界面活性剤による
衣類の柔軟効果は、ジオクタデシルザメチルアン
モニウムクロリドの木綿タオルへの吸着量と該木
綿タオルの柔軟性との関係を示す第1図から明ら
かなように、その界面活性剤の衣類等への吸着量
に比例したものとして得られる。 また、そのカチオン界面活性剤の衣類への吸着
量は、その吸着量とカチオン界面活性剤の粒径と
の関係を示した第2図から明らかなように、その
粒径が小さい程多量に吸着される。 即ち、第2図は、第1表に示すA,B2種類の
ジオクタデシルザメチルアンモニウムクロリドを
それぞれ各種濃度で分散させた試料によつて木綿
タオルを柔軟化し、その木綿タオルについてソク
スレー抽出器でクロロホルムを用いてジオクタデ
シルザメチルアンモニウムクロリドの抽出操作を
行い、抽出物中のジオクタデシルジメチルアンモ
ニウムクロリドの量を測定することにより該木綿
タオルへの吸着量を求め、該吸着量をジオクタデ
シルザメチルアンモニウムクロリドの濃度との関
連において示したものである。
The present invention relates to a method for atomizing a cationic surfactant in water. Generally, cationic surfactants have excellent softening effects, and among them, dioctadecylzamethylammonium chloride, which is a quaternary ammonium salt, is particularly widely used as a fabric softener. In addition to these quaternary ammonium salts, The phosphionium salt represented by the general formula is It is also known that cationic surfactants such as amide/amine salts represented by the following formula have excellent softening effects. These surfactants have hydrophobic long-chain alkyl groups, so they have excellent adsorption properties to clothing.
Most of these surfactants are poorly soluble in water, and in order to make them easier to use as softeners, most of these surfactants are dispersed in water, and nonionic surfactants or organic salts are added as anti-gelling agents. , inorganic salts, etc. are added, and alcohol is added as a low-temperature stability improver to suppress the viscosity to around 50 to 300 cp. The softening effect of cationic surfactants on clothing is evident from Figure 1, which shows the relationship between the amount of dioctadecylzamethylammonium chloride adsorbed onto cotton towels and the softness of the cotton towels. It is obtained in proportion to the amount of surfactant adsorbed on clothing, etc. In addition, the amount of cationic surfactant adsorbed onto clothing is clear from Figure 2, which shows the relationship between the amount of adsorption and the particle size of the cationic surfactant. be done. That is, FIG. 2 shows the softening of cotton towels using samples in which the two types of dioctadecylzamethylammonium chloride shown in Table 1, A and B, are dispersed at various concentrations, and the cotton towels are soaked in chloroform using a Soxhlet extractor. The amount of dioctadecyldimethylammonium chloride adsorbed onto the cotton towel was determined by measuring the amount of dioctadecyldimethylammonium chloride in the extract. It is shown in relation to the concentration of chloride.

【表】 このように、第4アンモニウム塩の衣類への吸
着量は、その粒子が微細である場合に一層増大す
ることから、微細な粒子は柔軟効果に優れている
と結論できる。 しかるに、カチオン界面活性剤は前記のように
衣類への吸着性に優れている反面、その多くは水
に難溶性を示し、しかもカチオン界面活性剤が水
と接触するとその表面が液晶構造となり、そのた
め表面の粘性が増加して粘稠な液体となり、微粒
子化が著しく困難になる。 即ち、多くの合成合成界面活性剤はある濃度以
上で液晶構造をとり、この液晶は分子間の相互作
用は弱いが分子の配列に規則性をもつ結晶性の液
体であるため、通常の水溶液あるいは固体溶融物
に比べて特異な性質をもつことが知られ、粘稠な
液体となることが多い。第4アンモニウム塩の場
合も、例えばジオクタデシルザメチルアンモニウ
ムクロリドやジドデシルジメチルアンモニウムク
ロリドでは、それぞれ第3図及び第4図のような
相図から明らかなように、広い液晶領域を持つこ
とが報告されている。 このような性質をもつ第4アンモニウム塩を水
(温水)中に添加すると、その表面が水と接触し
て第3図及び第4図に示す液晶領域の温度―濃度
範囲に達し、これによつて第4アンモニウム塩の
表面が液晶構造あるいはそれに類する構造とな
り、表面が粘稠化して微粒子化が困難となる。 このようなカチオン界面活性剤を用いた一般的
な柔軟剤等の製造においては、例えば溶融させた
第4アンモニウム塩またはその混合物を第4級ア
ンモニウム塩のクラフト点以上の温度に保ちなが
らゲル化防止剤等を含む温水中へ添加し、バドル
型撹拌機やプロペラ型撹拌機により分散する方法
が採られている。しかしながら上述したように第
4アンモニウム塩は水と接触してその粘性が増大
するため、上記一般の撹拌機によつてはカチオン
界面活性剤の良好な微粒化が困難であり、特に微
細な粒子を得るためには小さい撹拌翼を高速回転
させるホモジナイザー等の乳化用の特殊撹拌機を
用いる必要があるが、上記乳化用の特殊撹拌機は
一度に処理できる柔軟剤の量が少なく、また回分
式として用いる場合には撹拌槽本体内における全
体的混合能力が悪いなど実用化に際して大きな問
題点があつた。 なお、カチオン界面活性剤は上述した衣類の柔
軟化ばかりでなく、他の各種用途、例えば、床つ
や出し剤やカーリンス剤などのはつ水剤、あるい
は繊維の帯電防止剤としても用いられ、これらの
場合にもそのカチオン界面活性剤を水中で微粒子
化しておくのが有効である。 本発明は、上記に鑑みてなされたもので、カチ
オン界面活性剤を一般の撹拌翼によつて能率的に
水中に微分散させる方法を提供しようとするもの
である。 即ち、本発明の方法は、槽本体内の水中におい
て回転する撹拌翼の吸込側にカチオン界面活性剤
を供給し、それを上記撹拌翼に巻込ませることに
より微粒化する方法において、上記撹拌翼とし
て、翼外周側の水を翼前方への軸方向流とする撹
拌翼を用い、上記カチオン界面活性剤を、撹拌翼
の回転中心からの距離aがr/2≦a≦r、且つ
撹拌翼からの距離bがb≦r(但し、rは撹拌翼
の半径)なる位置において供給することを特徴と
するものである。 このような方法によつてカチオン界面活性剤の
微粒化を行うと、後述する実施例から明らかなよ
うに、すぐれた微粒化効果が得られ、しかもホモ
ジナイザー等の乳化用の特殊撹拌機を用いる場合
に比して、極めて能率的に微粒化を行うことが可
能になる。 以下、図面を参照しながら本発明についてさら
に詳細に説明する。 第5図及び第6図A,Bは、本発明の方法を実
施する装置の一例を示し、この装置では、槽本体
1の中央に、駆動源(図示せず)により矢印方向
に回転する回転軸4に取付けた撹拌翼3を配設し
ている。この撹拌翼3は、ジエツト型撹拌翼と呼
ばれるもので、回転軸4から突出する板状の各翼
板3aの周辺側を、湾曲部3bにおいて、全体と
して風車状になように軸線方向に湾曲させてい
る。従つて、例えばプロペラ型の撹拌翼ではその
回転の軸線に沿う軸方向流を発生させるのに対
し、このジエツト型撹拌翼では、翼外周側の水が
翼前方への軸方向流となる。 カチオン界面活性剤を供給する供給管5は、上
記撹拌翼3の回転により生じる水流の吸込側にお
いて、強い吸込流が発生する位置に配設される。
これにより、供給したカチオン界面活性剤の全部
が撹拌翼3に巻込まれて微粒化される。 上記撹拌翼3としては、発生する水流との関係
においてカチオン界面活性剤の微細化を十分なも
のとするため、撹拌翼3の直径が槽本体1の内径
の1/2以下のものが適している。 上記カチオン界面活性剤の供給管5は、撹拌翼
3の背後の翼外周側における吸込流の強い位置ま
で延びる管部5aを備え、この管部5aの先端に
供給口6を開口させたものであるが、該供給管5
としては、第5図に示すような単管により構成し
た管部5aの先端に供給口6を開口させたもの
や、第7図に示すように管部5aの先端を環状管
部5bとして該環状管部5bに供給口6,6…を
開口させたものを用いることができる。また、上
記供給口6は、それを単一の孔とした単孔構造と
することも、さらに第8図及び第9図に示すよう
に多数の単位孔7,7…をもつ複孔構造とするこ
ともでき、これらのいずれの構造においても供給
口6の直径を撹拌翼3の半径の1/2以下とするの
がよい。 第10図は、槽本体1内におけるカチオン界面
活性剤の供給位置を第5図及び第6図A,Bに示
す撹拌翼3との関係において求め、その位置に供
給した場合に該界面活性剤がどの程度撹拌翼3に
巻込されるかを調べた実験結果を示すものであ
る。なお、供給管は第7図のものを使用した。 第10図において、横軸及び縦軸の距離a及び
距離bはそれぞれ第5図におけるa,bを示し、
即ち距離aは供給口6と撹拌翼3の回転中心との
間の距離を、また距離bは供給口6と撹拌翼3と
の間の距離を、それぞれ撹拌翼3の半径rとの関
係において表わしたものである。 この第10図によれば、カチオン界面活性剤の
供給位置、即ち供給口6の位置は、 a=≦2r、 b≦2r で表わされる範囲内とするのが望ましい。 また、第11図及び第12図は、上述した場合
と同じ撹拌翼に対する供給液添加位置と微粒化の
関係についての実験例を示し、第11図はbの値
を一定にしてaを変化させた場合の微粒化状態の
変化を、また第12図はaの値を一定にしてbを
変化させた場合の微粒化状態の変化を示してい
る。これらの実験結果によれば、カチオン界面活
性剤の供給位置は、撹拌翼の回転中心からの距離
aが、 r/2≦a≦r 且つ撹拌翼からの距離bが、 b≦r の範囲において、すぐれた微粒化効果が得られる
ことがわかる。 なお、第11図において、撹拌翼の回転中心か
らの距離aがa<r/2の範囲では、供給液が撹
拌軸に巻き付くようにして翼を通過するため、微
粒化し難い状態になる。また、a>rの範囲で
は、供給液が翼先端部より下方へ吐出するため、
この場合も微粒化し難い状態になる。さらに、第
12図において、撹拌翼からの距離bがb>1の
範囲では、吸込力が低くなるため、供給液が翼に
かからずに分散する状態が増し、翼にかからなか
つたものが粗粒化することになる。 このように、本発明の方法によれば、カチオン
界面活性剤を撹拌翼との特定な位置関係において
供給することにより、一般にジエツト型と呼ばれ
ている撹拌機によつて十分にそれを微分散させる
ことができ、しかも、カチオン界面活性剤を撹拌
翼の方向に案内するガイド等の部材を必要としな
いので、装置の構成も簡略化される。 次に、本発明の実施例を記述する。 実施例 1 槽本体:容積40 撹拌翼:第5図及び第6図A,Bに示す構造の
ジエツト型撹拌翼、翼先端周速11.8m/sec 供給管:供給口径 0.08r×12個、供給位置a
=4/5rの円周上に配列、b=1/4r 上記構成を有する装置により、ポリオキシエチ
レンアルキルフエニルエーテル(0.5%)を含む
40℃に加熱された温水中に供給管から55℃に昇温
されたジ牛脂ジメチルアンモニウムクロリドとエ
チレングリコールとの混合物を30分間で供給し、
分散(熟成)時間を0分間とした。これにより
0.65μ以下の粒子が87%以上になることが確認さ
れたが、同様の実験条件で上記混合物を液面に添
加した比較例では0.65μ以下の粒子が21%以下で
あつた。なお、第13図及び第14図の写真は、
上記実施例及び比較例において得られた分散液の
顕微鏡写真(×300)をそれぞれ示し、これによ
つて明らかなように、上記実施例では1μ以上の
粗大粒子が全く見られないのに対し、比較例の場
合にはその粗大粒子が数多く見られ、十分な微粒
化が行われていないことが明白である。
[Table] Since the amount of quaternary ammonium salt adsorbed onto clothing is further increased when the particles are fine, it can be concluded that fine particles have an excellent softening effect. However, although cationic surfactants have excellent adsorption properties to clothing as mentioned above, many of them are poorly soluble in water, and when cationic surfactants come into contact with water, their surface becomes a liquid crystal structure. The surface viscosity increases and becomes a viscous liquid, making it extremely difficult to form particles. In other words, many synthetic surfactants take on a liquid crystal structure at a certain concentration or higher, and this liquid crystal is a crystalline liquid with weak interactions between molecules but regular arrangement of molecules, so it cannot be used in normal aqueous solutions or liquid crystals. It is known to have unique properties compared to solid melts, and often forms a viscous liquid. In the case of quaternary ammonium salts, for example, dioctadecylzamethylammonium chloride and didodecyldimethylammonium chloride have been reported to have wide liquid crystal regions, as is clear from the phase diagrams shown in Figures 3 and 4, respectively. has been done. When a quaternary ammonium salt with such properties is added to water (hot water), its surface comes into contact with the water and reaches the temperature-concentration range of the liquid crystal region shown in Figures 3 and 4, thereby causing As a result, the surface of the quaternary ammonium salt becomes a liquid crystal structure or a similar structure, and the surface becomes viscous, making it difficult to form fine particles. In the production of general softeners using such cationic surfactants, for example, gelation is prevented by maintaining the melted quaternary ammonium salt or its mixture at a temperature equal to or higher than the Kraft point of the quaternary ammonium salt. A method is adopted in which the agent is added to hot water containing the agent and dispersed using a paddle-type stirrer or a propeller-type stirrer. However, as mentioned above, the quaternary ammonium salt increases its viscosity when it comes into contact with water, so it is difficult to properly atomize the cationic surfactant using the above-mentioned general stirrer. In order to obtain this, it is necessary to use a special stirrer for emulsification such as a homogenizer that rotates small stirring blades at high speed, but the special stirrer for emulsification mentioned above can only process a small amount of softener at one time, and cannot be used as a batch type. When used, there were major problems in putting it into practical use, such as poor overall mixing ability within the stirring tank body. Cationic surfactants are used not only for the softening of clothing as mentioned above, but also for various other purposes, such as water repellents such as floor polishes and curling agents, and antistatic agents for textiles. In such cases, it is effective to micronize the cationic surfactant in water. The present invention has been made in view of the above, and aims to provide a method for efficiently finely dispersing a cationic surfactant in water using a general stirring blade. That is, the method of the present invention is a method in which a cationic surfactant is supplied to the suction side of a stirring blade rotating in water in a tank body, and is atomized by being wound around the stirring blade, in which the stirring blade is , using a stirring blade that causes water on the outer circumferential side of the blade to flow in the axial direction toward the front of the blade, and applying the above cationic surfactant to the stirring blade in such a manner that the distance a from the rotation center of the stirring blade is r/2≦a≦r, and from the stirring blade It is characterized by supplying at a position where the distance b is b≦r (where r is the radius of the stirring blade). When the cationic surfactant is atomized by such a method, an excellent atomization effect can be obtained, as is clear from the examples described below.Moreover, when a special stirrer for emulsification such as a homogenizer is used, Compared to this, it becomes possible to perform atomization extremely efficiently. Hereinafter, the present invention will be explained in more detail with reference to the drawings. 5 and 6A and 6B show an example of an apparatus for carrying out the method of the present invention. In this apparatus, a rotor that rotates in the direction of the arrow by a drive source (not shown) is mounted at the center of the tank body 1. A stirring blade 3 attached to a shaft 4 is provided. This stirring blade 3 is called a jet type stirring blade, and the peripheral side of each plate-shaped blade plate 3a protruding from the rotating shaft 4 is curved in the axial direction at the curved portion 3b so as to have a windmill shape as a whole. I'm letting you do it. Therefore, for example, a propeller-type stirring blade generates an axial flow along the axis of rotation, whereas in a jet-type stirring blade, water on the outer peripheral side of the blade flows in an axial direction toward the front of the blade. The supply pipe 5 for supplying the cationic surfactant is arranged on the suction side of the water flow generated by the rotation of the stirring blade 3 at a position where a strong suction flow is generated.
As a result, all of the supplied cationic surfactant is drawn into the stirring blades 3 and atomized. In order to ensure that the cationic surfactant is sufficiently finely divided in relation to the generated water flow, the stirring blade 3 should preferably have a diameter of 1/2 or less of the inner diameter of the tank body 1. There is. The cationic surfactant supply pipe 5 includes a pipe portion 5a that extends to a position where the suction flow is strong on the outer peripheral side of the blade behind the stirring blade 3, and a supply port 6 is opened at the tip of the pipe portion 5a. However, the supply pipe 5
As shown in FIG. 5, the supply port 6 is opened at the tip of a tube section 5a made of a single tube, or as shown in FIG. 7, the tip of the tube section 5a is made into an annular tube section 5b. It is possible to use an annular tube portion 5b having supply ports 6, 6, . . . opened therein. Further, the supply port 6 may have a single-hole structure with a single hole, or may have a multi-hole structure with a large number of unit holes 7, 7, etc. as shown in FIGS. 8 and 9. In either of these structures, the diameter of the supply port 6 is preferably 1/2 or less of the radius of the stirring blade 3. FIG. 10 shows that the supply position of the cationic surfactant in the tank body 1 is determined in relation to the stirring blade 3 shown in FIGS. 5 and 6, A and B, and the surfactant is This figure shows the results of an experiment to determine how much of the liquid is drawn into the stirring blade 3. The supply pipe shown in FIG. 7 was used. In FIG. 10, distance a and distance b on the horizontal and vertical axes respectively indicate a and b in FIG.
That is, the distance a is the distance between the supply port 6 and the center of rotation of the stirring blade 3, and the distance b is the distance between the supply port 6 and the stirring blade 3, in relation to the radius r of the stirring blade 3. It is expressed. According to this FIG. 10, it is desirable that the supply position of the cationic surfactant, that is, the position of the supply port 6, be within the range expressed by a=≦2r, b≦2r. In addition, Fig. 11 and Fig. 12 show experimental examples regarding the relationship between the feed liquid addition position and atomization for the same stirring blade as described above, and Fig. 11 shows the relationship between a and a while keeping the value of b constant. FIG. 12 shows the change in the atomization state when the value of a is kept constant and b is varied. According to these experimental results, the cationic surfactant is supplied at a position where the distance a from the rotation center of the stirring blade is r/2≦a≦r and the distance b from the stirring blade is b≦r. It can be seen that an excellent atomization effect can be obtained. In FIG. 11, when the distance a from the center of rotation of the stirring blade is in the range a<r/2, the feed liquid passes through the blades in a manner that it wraps around the stirring shaft, making it difficult to atomize. In addition, in the range a>r, the supply liquid is discharged downward from the blade tip, so
In this case as well, it becomes difficult to atomize the particles. Furthermore, in Fig. 12, when the distance b from the stirring blade is in the range b>1, the suction force becomes low, so the supply liquid is more likely to be dispersed without hitting the blade, becomes coarse grained. As described above, according to the method of the present invention, by supplying the cationic surfactant in a specific positional relationship with the stirring blade, it can be sufficiently finely dispersed by the jet-type stirrer. In addition, since a member such as a guide for guiding the cationic surfactant in the direction of the stirring blade is not required, the configuration of the device is also simplified. Next, embodiments of the present invention will be described. Example 1 Tank body: Volume 40 Stirring blades: Jet-type stirring blades with the structure shown in Figures 5 and 6 A and B, blade tip peripheral speed 11.8 m/sec Supply pipes: Supply port diameter 0.08r x 12 pieces, supply position a
= Arranged on the circumference of 4/5r, b = 1/4r Contains polyoxyethylene alkyl phenyl ether (0.5%) using an apparatus having the above configuration.
A mixture of dimethylammonium chloride and ethylene glycol heated to 55°C was supplied from a supply pipe into hot water heated to 40°C for 30 minutes,
The dispersion (ripening) time was set to 0 minutes. This results in
It was confirmed that particles with a size of 0.65μ or less accounted for 87% or more, but in a comparative example in which the above mixture was added to the liquid surface under similar experimental conditions, the proportion of particles with a size of 0.65μ or less was 21% or less. The photographs in Figures 13 and 14 are
Microscopic photographs (×300) of the dispersions obtained in the above Examples and Comparative Examples are shown, and it is clear that in the above Examples, no coarse particles of 1μ or more were observed. In the case of the comparative example, many coarse particles were observed, and it is clear that sufficient atomization was not performed.

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

第1図はジオクタデシルジメチルアンモニウム
クロリドの木綿タオルへの吸着量と木綿タオルの
柔軟性との関係を示す線図、第2図はジオクタデ
シルジメチルアンモニウムクロリド濃度と木綿タ
オルへの吸着量との関係を示す線図、第3図はジ
オクタデシルジメチルアンモニウムクロリド―水
相平衡図、第4図はジドデシルジメチルアンモニ
ウムクロリド―水相平衡図、第5図は本発明を実
施する装置の断面図、第6図A,Bはその撹拌翼
の平面図及び斜視図、第7図ないし第9図は供給
管及び供給口の異種例を示す側面図及び部分斜視
図、第10図はカチオン界面活性剤の添加位置と
撹拌翼への吸込状態の良否を示す説明図、第11
図及び第12図はジエツト型撹拌翼の供給液添加
位置と微粒化の関係を示す線図、第13図及び第
14図は本発明の実施例及びその比較例において
得られた分散液粒子についての図面代用顕微鏡写
真である。 1…槽本体、3…軸流型撹拌翼、5…供給管、
6…供給口。
Figure 1 is a diagram showing the relationship between the amount of dioctadecyldimethylammonium chloride adsorbed onto a cotton towel and the flexibility of the cotton towel, and Figure 2 is a diagram showing the relationship between the concentration of dioctadecyldimethylammonium chloride and the amount of adsorption onto the cotton towel. FIG. 3 is a dioctadecyldimethylammonium chloride-aqueous phase equilibrium diagram, FIG. 4 is a didodecyldimethylammonium chloride-aqueous phase equilibrium diagram, and FIG. 5 is a sectional view of an apparatus for carrying out the present invention. 6A and B are a plan view and a perspective view of the stirring blade, FIGS. 7 to 9 are a side view and a partial perspective view showing different types of supply pipes and supply ports, and FIG. 10 is a diagram of a cationic surfactant. Explanatory diagram showing the addition position and the quality of suction to the stirring blade, No. 11
Figures 1 and 12 are diagrams showing the relationship between the feed liquid addition position of the jet type stirring blade and atomization, and Figures 13 and 14 are diagrams showing the dispersion particles obtained in the examples of the present invention and their comparative examples. This is a micrograph used as a drawing. 1... Tank body, 3... Axial flow type stirring blade, 5... Supply pipe,
6... Supply port.

Claims (1)

【特許請求の範囲】 1 槽本体内の水中において回転する撹拌翼の吸
込側にカチオン界面活性剤を供給し、それを上記
撹拌翼に巻込ませることにより微粒化する方法に
おいて、 上記撹拌翼として、翼外周側の水を翼前方への
軸方向流とする撹拌翼を用い、 上記カチオン界面活性剤を、撹拌翼の回転中心
からの距離aがr/2≦a≦r、且つ撹拌翼から
の距離bがb≦r(但し、rは撹拌翼の半径)な
る位置において供給する、 ことを特徴とする水中におけるカチオン界面活性
剤の微粒化方法。
[Scope of Claims] 1. A method of supplying a cationic surfactant to the suction side of a stirring blade rotating in water in a tank body and atomizing it by winding it into the stirring blade, the stirring blade comprising: Using a stirring blade that causes water on the outer circumferential side of the blade to flow in the axial direction toward the front of the blade, the above cationic surfactant is applied at a distance a from the rotation center of the stirring blade such that r/2≦a≦r, and from the stirring blade to A method for atomizing a cationic surfactant in water, characterized in that the distance b is supplied at a position where b≦r (where r is the radius of a stirring blade).
JP8051180A 1980-06-13 1980-06-13 Pulverization of cationic surfactant in water Granted JPS575797A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8051180A JPS575797A (en) 1980-06-13 1980-06-13 Pulverization of cationic surfactant in water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8051180A JPS575797A (en) 1980-06-13 1980-06-13 Pulverization of cationic surfactant in water

Publications (2)

Publication Number Publication Date
JPS575797A JPS575797A (en) 1982-01-12
JPH0146559B2 true JPH0146559B2 (en) 1989-10-09

Family

ID=13720333

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8051180A Granted JPS575797A (en) 1980-06-13 1980-06-13 Pulverization of cationic surfactant in water

Country Status (1)

Country Link
JP (1) JPS575797A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01254232A (en) * 1988-04-01 1989-10-11 Miyoshi Oil & Fat Co Ltd Production of aqueous solution of amine-amide type cationic surface active agent
ES2812203T3 (en) * 2015-07-22 2021-03-16 Mitsubishi Gas Chemical Co Method to produce high purity terephthalic acid

Also Published As

Publication number Publication date
JPS575797A (en) 1982-01-12

Similar Documents

Publication Publication Date Title
US2442972A (en) Aqueous dispersions of electropositive materials
EP0195459B1 (en) Foam composition used in paper treatment
US2277788A (en) Treatment of textiles and composition useful therefor
CN106283863A (en) A kind of emulsion-type high fatty alcohol defoamer
JP2002513447A (en) Sizing emulsion
JPH0321666A (en) Production of micro emulsion of cyclohexylamino group-containing organopolysiloxane
US3951853A (en) Defoamer composition
CN119775818B (en) Composite defoaming agent and preparation method thereof
JPH0146559B2 (en)
CA1120348A (en) Method of forming glass fiber dispersions with cationic quaternary ammonium surfactants having at least two long chain groups
US3374100A (en) Water repellent compositions
CN113754879A (en) Synthesis method of alkyl polyoxyethylene ether quaternary ammonium salt surfactant
DE19731615B4 (en) Dilution-stable concentrates of antifoam emulsions and methods of reducing foam
CN108395546A (en) A kind of ester type waxes lotion and preparation method thereof
JPH0348946B2 (en)
CN110371992A (en) It is a kind of regulate and control microemulsion reaction methods monodisperse silica sphere particle method and products thereof and purposes
US2481692A (en) Cotton treated with a cation active amine
CN119266003A (en) A kind of AKD emulsion and preparation method thereof
JPH04136270A (en) Oil for textile treatment
US2495845A (en) Textile sizing composition
Li et al. Study of synthesizing energy storage microcapsules in PVA spinning solution and thermal regulating fibers prepared by this solution
JP3994091B2 (en) Method for continuously producing high-concentration liquid softener composition and high-concentration liquid softener composition obtained thereby
JP3231172B2 (en) Method for producing di-long chain tertiary amine / acid salt
JPH01254232A (en) Production of aqueous solution of amine-amide type cationic surface active agent
JPS6211539A (en) Continuous production method of concentrated cationic surfactant dispersion