JPH0655817B2 - Method for producing aminosilicone fine particle emulsion - Google Patents

Method for producing aminosilicone fine particle emulsion

Info

Publication number
JPH0655817B2
JPH0655817B2 JP1108179A JP10817989A JPH0655817B2 JP H0655817 B2 JPH0655817 B2 JP H0655817B2 JP 1108179 A JP1108179 A JP 1108179A JP 10817989 A JP10817989 A JP 10817989A JP H0655817 B2 JPH0655817 B2 JP H0655817B2
Authority
JP
Japan
Prior art keywords
aminosilicone
group
emulsion
epoxy
fine particle
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 - Fee Related
Application number
JP1108179A
Other languages
Japanese (ja)
Other versions
JPH02284959A (en
Inventor
正喜 田中
博司 大橋
典行 廻谷
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.)
Shin Etsu Chemical Co Ltd
Original Assignee
Shin Etsu Chemical Co Ltd
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 Shin Etsu Chemical Co Ltd filed Critical Shin Etsu Chemical Co Ltd
Priority to JP1108179A priority Critical patent/JPH0655817B2/en
Priority to KR1019900005850A priority patent/KR970000404B1/en
Publication of JPH02284959A publication Critical patent/JPH02284959A/en
Publication of JPH0655817B2 publication Critical patent/JPH0655817B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G77/00Macromolecular compounds obtained by reactions forming a linkage containing silicon with or without sulfur, nitrogen, oxygen or carbon in the main chain of the macromolecule
    • C08G77/04Polysiloxanes
    • C08G77/38Polysiloxanes modified by chemical after-treatment
    • C08G77/382Polysiloxanes modified by chemical after-treatment containing atoms other than carbon, hydrogen, oxygen or silicon
    • C08G77/388Polysiloxanes modified by chemical after-treatment containing atoms other than carbon, hydrogen, oxygen or silicon containing nitrogen
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J3/00Processes of treating or compounding macromolecular substances
    • C08J3/02Making solutions, dispersions, lattices or gels by other methods than by solution, emulsion or suspension polymerisation techniques
    • C08J3/03Making solutions, dispersions, lattices or gels by other methods than by solution, emulsion or suspension polymerisation techniques in aqueous media
    • C08J3/07Making solutions, dispersions, lattices or gels by other methods than by solution, emulsion or suspension polymerisation techniques in aqueous media from polymer solutions
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06MTREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
    • D06M15/00Treating fibres, threads, yarns, fabrics, or fibrous goods made from such materials, with macromolecular compounds; Such treatment combined with mechanical treatment
    • D06M15/01Treating fibres, threads, yarns, fabrics, or fibrous goods made from such materials, with macromolecular compounds; Such treatment combined with mechanical treatment with natural macromolecular compounds or derivatives thereof
    • D06M15/03Polysaccharides or derivatives thereof
    • D06M15/05Cellulose or derivatives thereof

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Dispersion Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Silicon Polymers (AREA)
  • Processes Of Treating Macromolecular Substances (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Treatments For Attaching Organic Compounds To Fibrous Goods (AREA)

Description

【発明の詳細な説明】 産業上の利用分野 本発明は、貯蔵安定性、希釈安定性、機械安定性に優
れ、透明感のある外観を有し、繊維処理剤、離型剤、艶
出し剤などとして好適に使用できるアミノシリコーン微
粒子エマルジョンの製造方法に関する。
TECHNICAL FIELD The present invention is excellent in storage stability, dilution stability, mechanical stability, has a transparent appearance, and has a fiber treatment agent, a release agent, and a polishing agent. The present invention relates to a method for producing an aminosilicone fine particle emulsion which can be preferably used as

従来の技術及び発明が解決しようとする課題 従来、アミノシリコーンエマルジョンの製造方法として
は、液状アミノシリコーンを乳化剤を用いて、例えばホ
モミキサーコロイドミルのような高剪断力をかけ得る装
置あるいはプロペラ羽根のような撹拌装置により水中に
乳化分散して製造する方法が知られている。
2. Description of the Related Art Conventionally, as a method for producing an aminosilicone emulsion, a conventional method for producing an aminosilicone emulsion has been described. There is known a method of producing by emulsifying and dispersing in water with such a stirring device.

しかしながら、このような方法にて製造されたアミノシ
リコーンエマルジョンは、平均粒径が0.5μm以上と
大きく、貯蔵安定性、希釈安定性、特には機械的シェア
による安定性が悪く、例えば繊維等を処理する場合、処
理スピードが早いと高速回転するロールによってエマル
ジョン破壊が起こり、処理むら,ロールの汚れ等の問題
を発生し易いという欠点があった。
However, the aminosilicone emulsion produced by such a method has a large average particle size of 0.5 μm or more and is poor in storage stability, dilution stability, particularly stability due to mechanical shear. In the case of processing, when the processing speed is high, there is a drawback that the roll rotating at a high speed causes emulsion breakage, which easily causes problems such as processing unevenness and roll contamination.

更に、アミノシリコーンエマルジョンの製造方法とし
て、低分子の環状シロキサン及びアミノシランを出発物
質とし、乳化散系で強アルカリを触媒として重合高分子
化する、いわゆる乳化重法による製造方法(特公昭56
−38609号公報)もよく知られている。この方法に
よれば、得られるエマルジョンの粒径は0.1〜0.2
μmとかなり小さくすることができ、貯蔵安定性や希釈
安定性はかなり改善されるが、まだ強い機械的シェアに
対する安定性につては不充分であった。更に、上記乳化
重合法は、製法上、出発物質の低分子の環状シロキサン
が約10%未重合のまま残るという本質的な不都合を有
し、この残存低分子シロキサンは、得られるエマルジョ
ンの使用時に揮散し、乾燥工程において熱酸化による白
色粉の生成、周囲の表面に付着することによる塗料のハ
ジキの発生、周囲に存在する電気機器の接点不良の発生
等、使用時に種々の不都合を招来する可能性があるとい
う問題があった。
Further, as a method for producing an aminosilicone emulsion, a low molecular weight cyclic siloxane and an aminosilane are used as starting materials, and a polymer is polymerized in an emulsification system using a strong alkali as a catalyst to produce a polymer.
No. 38,609) is also well known. According to this method, the particle size of the obtained emulsion is 0.1 to 0.2.
Although it can be made as small as μm, the storage stability and the dilution stability are considerably improved, but the stability against a strong mechanical shear is still insufficient. Further, the emulsion polymerization method has an essential disadvantage in that about 10% of the low molecular weight cyclic siloxane as a starting material remains unpolymerized in the manufacturing method, and the residual low molecular weight siloxane has a problem when the resulting emulsion is used. It may lead to various inconveniences during use, such as volatilization and generation of white powder due to thermal oxidation in the drying process, cissing of paint due to adhesion to the surrounding surface, contact failure of electrical equipment existing in the surroundings, etc. There was a problem that there is a property.

このため、安定性が高く、使用性の良好なアミノシリコ
ーン微粒子エマルジョンの製造方法の開発が望まれてい
た。
Therefore, development of a method for producing an aminosilicone fine particle emulsion having high stability and good usability has been desired.

本発明は上記事情に鑑みなされたもので、貯蔵安定性、
希釈安定性、機械安定性に優れ、使用性の良好なアミノ
シリコーン微粒子エマルジョンの製造方法を提供するこ
とを目的とする。
The present invention has been made in view of the above circumstances, storage stability,
It is an object of the present invention to provide a method for producing an aminosilicone fine particle emulsion which has excellent dilution stability and mechanical stability and is easy to use.

課題を解決するための手段及び作用 本発明者は、上記目的を達成するため鋭検討を重ねた結
果、下記一般式(1) 〔但し、式中Rは炭素原子数1〜20の一価炭化粋素
基、水酸基又は−OR′(R′は炭素原子数1〜20の
一価炭化水素基)、Aは式−R(NRNR
(R,Rはそれぞれ炭素原子数1〜6の2価
の炭化水素基、R,R,Rはそれぞれ水素原子又
は炭素原子数1〜20の1価の炭化水素基、zは0〜5
の整数を表わす)で示されるアミノアルキル基であり、
0<x≦3,0≦y<3,0<x+y≦3である。〕 で示されるアミノシリコーン及び/又は上記式(1)で
示されるアミノシリコーンと (ここにRは1価の有機基を表わす)で示されるモノ
エポキシ化合物との反応物であるエポキシ変性アミノシ
リコーンを出発物質として使用し、これに界面活性剤を
上記出発原料((1)式のアミノシリコーン,エポキシ
変性アミノシリコーン)の合計量100重量部に対して
10重量部以上の割合で添加し、常温で均一混合した
後、水を徐々に添加してアミノシリコーン及び/又はエ
ポキシ変性アミノシリコーンを水中に常温で乳化分散さ
せ、次いで、この乳化分散水溶液に酸性物質を上記出発
原料((1)式のアミノシリコーン,エポキシ変性アミ
ノシリコーン)分子中のN原子に対して0.1モル当量
以上となるように添加した後、加熱熟成を行なう(50
〜90℃で1時間以上)ことにより、平均粒径が0.1
μm以下で貯蔵安定性、希釈安定性、機械安定性に優
れ、使用性が高く、かつ透明感のある外観を有するアミ
ノシリコーン微粒子エマルジョンが得られることを見い
出した。
Means and Actions for Solving the Problem The present inventor has conducted extensive studies to achieve the above object, and as a result, the following general formula (1) [Wherein R 1 is a monovalent hydrocarbon group having 1 to 20 carbon atoms, a hydroxyl group or -OR '(R' is a monovalent hydrocarbon group having 1 to 20 carbon atoms), and A is a formula -R. 2 (NR 3 R 4 ) z NR
5 R 6 (R 2 and R 4 are each a divalent hydrocarbon group having 1 to 6 carbon atoms, and R 3 , R 5 and R 6 are each a hydrogen atom or a monovalent hydrocarbon having 1 to 20 carbon atoms. Group, z is 0 to 5
Represents an integer of), an aminoalkyl group represented by
0 <x ≦ 3, 0 ≦ y <3, 0 <x + y ≦ 3. ] And / or an aminosilicone represented by the above formula (1) An epoxy-modified amino silicone which is a reaction product with a monoepoxy compound represented by (wherein R 7 represents a monovalent organic group) is used as a starting material, and a surfactant is added to the starting material ((1)). Formulated aminosilicone, epoxy-modified aminosilicone) in an amount of 10 parts by weight or more based on 100 parts by weight in total, and after homogeneous mixing at room temperature, water is gradually added to aminosilicone and / or epoxy-modified Aminosilicone is emulsified and dispersed in water at room temperature, and then an acidic substance is added to this aqueous emulsified dispersion solution in an amount of 0.1 mol with respect to N atoms in the starting material (aminosilicone of the formula (1), epoxy-modified aminosilicone) molecule. After adding so that the equivalent amount or more, heat aging is performed (50
The average particle size is 0.1.
It has been found that an aminosilicone fine particle emulsion having a storage stability, a dilution stability, a mechanical stability, a high usability, and a transparent appearance can be obtained at a particle size of not more than μm.

即ち、上記方法により得られるアミノシリコーン微粒子
エマルジョンは、上述したように平均粒径が0.1μm
以下であり、非常にエマルジョン粒子が細かいため、従
来の方法で製造されるエマルジョンに比べ各種安定性が
格段に向上する。例えば、貯蔵定定性については、室温
で1年以上もエマルジョン分離等の現象は起こらず、従
来のものに比べ約2倍以上の長期間において安定であ
る。また、希釈安定性もオイルスポット等の発生がなく
極めて良好である。特に機械的安定性につては、従来の
ように高速回転ロールでエマルジョンが破壊したり、処
理むら,ロール等の汚れ等の問題が全く生じない。しか
も、本発明で製造されるアミノシリコーン微粒子エマル
ジョンは、微粒子化して外観が従来の白濁液から透明な
いし半透明になるため、他の併用成分が透明な場合、外
観が損なわれることがない等、繊維処理剤、離型剤、艶
出し剤などの用途に適した特性を有するので使用性が高
い微粒子エマルジョンである。
That is, the aminosilicone fine particle emulsion obtained by the above method has an average particle size of 0.1 μm as described above.
Since it is the following, the emulsion particles are very fine, and thus various types of stability are remarkably improved as compared with an emulsion produced by a conventional method. For example, regarding storage qualitativeness, phenomena such as emulsion separation do not occur even at room temperature for one year or more, and are stable over a long period of about twice or more compared to conventional ones. Further, the dilution stability is extremely good without the occurrence of oil spots and the like. In particular, in terms of mechanical stability, there is no problem such as the conventional one in which the emulsion is broken by the high-speed rotating roll, the processing is uneven, and the roll is dirty. Moreover, since the aminosilicone fine particle emulsion produced by the present invention is made into fine particles and the appearance becomes transparent or translucent from the conventional cloudy liquid, the appearance is not impaired when other combined components are transparent, etc. It is a fine particle emulsion with high usability because it has properties suitable for applications such as fiber treatment agents, release agents, and polishes.

以下、本発明につき更に詳述する。Hereinafter, the present invention will be described in more detail.

本発明に係るアミノシリコーン微粒子エマルジョンの製
造方法は、上述したように、アミノシリコーン及び/又
はエポキシ変性アミノシリコーンに界面活性剤をアミノ
シリコーン及びエポキシ変性アミノシリコーンの合計量
100重量部に対して10重量部以上添加して水中にア
ミノシリコーン及び/又はエポキシ変性アミノシリコー
ンを乳化分散させ、次いで、前記乳化分散水溶液中に酸
性物質をアミノシリコーン及びエポキシ変性アミノシリ
コーン分子中のN原子に対して0.1モル当量以上添加
した後、加熱熟成を行なうものである。
As described above, the method for producing the aminosilicone fine particle emulsion according to the present invention comprises 10 parts by weight of the aminosilicone and / or the epoxy-modified aminosilicone with a surfactant, based on 100 parts by weight of the total amount of the aminosilicone and the epoxy-modified aminosilicone. Amino silicone and / or epoxy-modified amino silicone is emulsified and dispersed in water by adding at least 1 part by weight, and then an acidic substance is added to the emulsified and dispersed aqueous solution in an amount of 0.1 to N atom in amino silicone and epoxy-modified amino silicone molecule. After adding a molar equivalent or more, heat aging is performed.

この場合、本発明で出発原料として用いられるアミノシ
リコーンは、下記一般式(1) で示されるものである。
In this case, the aminosilicone used as a starting material in the present invention is represented by the following general formula (1) It is shown by.

ここで、式中Rはメチル基,エチル基,プロピル基,
オクチル基,ラウリル基等のアルキル基、ビニル基,ア
リル基等のアルケニル基、フエニル基,トリル基,ナフ
チル基等のアリール基、シクロペンチル基,シククロヘ
キシル基等のシクロアルキル基又はそれらの1部又は全
部の水素原子がハロゲン原子に置換された基等の炭素原
子数1〜20の1価の炭化水素基、水酸基又は−OR′
(R′は炭素原子数1〜20の一価炭化水素基)で示さ
れる基である。
Here, in the formula, R 1 is a methyl group, an ethyl group, a propyl group,
Alkyl group such as octyl group, lauryl group, alkenyl group such as vinyl group, allyl group, aryl group such as phenyl group, tolyl group, naphthyl group, cycloalkyl group such as cyclopentyl group, cyclohexyl group, or part thereof. Or a monovalent hydrocarbon group having 1 to 20 carbon atoms, such as a group in which all hydrogen atoms are replaced by halogen atoms, a hydroxyl group or -OR '
(R 'is a monovalent hydrocarbon group having 1 to 20 carbon atoms).

また、Aは式−R(NRNRで表さ
れるアミノアルキル基で、R,Rはそれぞれメチレ
ン基,エチレン基,プロピレン基,ヘキサメチレン基,
フェニレン基等の炭素原子数1〜6の2価の炭化水素
基、R,R,Rはそれぞれ水素原子又は上記R
と同様の炭素原子1〜20の1価の炭化水素基、zは0
〜5の整数である。このようなアミノアルキル基を示す
ると、−CNH,−CNHCNH
,−C12NHCNH,−C(NH
NH,−C(NHC
,−CNHCNH,−CHNHC
N(C等が挙げられるが、れらに限定されるものではない。
Also, A is an aminoalkyl group of the formula -R 2 (NR 3 R 4) z NR 5 R 6, R 2, R 4 are each a methylene group, an ethylene group, a propylene group, hexamethylene group,
A divalent hydrocarbon group having 1 to 6 carbon atoms such as a phenylene group, R 3 , R 5 and R 6 are each a hydrogen atom or the above R 1
And a monovalent hydrocarbon group having 1 to 20 carbon atoms, z is 0
Is an integer of ~ 5. And view the such aminoalkyl groups, -C 3 H 6 NH 2, -C 3 H 6 NHC 2 H 4 NH
2, -C 6 H 12 NHC 2 H 4 NH 2, -C 3 H 6 (NH
C 2 H 4) 2 NH 2 , -C 3 H 6 (NHC 2 H 4) 3 N
H 2, -C 2 H 4 NHC 2 H 4 NH 2, -CH 2 NHC
2 H 4 N (C 4 H 9 ) 2 , However, the present invention is not limited to these.

なお、x,yは、0<x≦3,0≦y<3,0<x+1
≦3である。
Note that x and y are 0 <x ≦ 3, 0 ≦ y <3, 0 <x + 1.
≦ 3.

(1)式のアミノシリコーンとしては、シリコーン鎖の
末端がトリメチルシリル基で封鎖されたものが一般的で
あるが、必要に応じて、末端が水酸基又はアルコキシ基
等にて封鎖されたものも使用し得る。
As the aminosilicone of the formula (1), a silicone chain having a terminal blocked with a trimethylsilyl group is generally used, but if necessary, a terminal blocked with a hydroxyl group or an alkoxy group may also be used. obtain.

また、本発明では、出発原料として上記(1)式のアミ
ノシリコーンと下記式 で示されるモノエポキシ化合物とを反応させることによ
り得られるエポキシ変性アミノシリコーンを用いること
もできる。
Further, in the present invention, as the starting material, the amino silicone of the above formula (1) and the following formula It is also possible to use an epoxy-modified aminosilicone obtained by reacting with a monoepoxy compound represented by

ここで、上記モノエポキシ化合物中の置換基Rはエポ
キシ基を含有しない1価の有機基であり、好ましくは直
鎖状又は分枝状の炭化水素基とされるが、ポリオキシア
ルキレン基を含むものでもよく、モノエポキシ化合物と
しては下記式で示される化合物を例示することができ
る。
Here, the substituent R 7 in the above monoepoxy compound is a monovalent organic group containing no epoxy group, preferably a linear or branched hydrocarbon group, but a polyoxyalkylene group The compound represented by the following formula can be exemplified as the monoepoxy compound.

上記エポキシ変性アミノシリコーンを得る場合、(1)
式のアミノシリコーンと上記エポキシ化合物との配合割
合は、アミノシリコーンに含まれる窒素原子1個に対し
モノエポキシ化合物中のエポキシ基が0.01〜20モ
ル量、特に0.1〜10モル量となる範囲とすることが
好ましい。
To obtain the above epoxy-modified amino silicone, (1)
The compounding ratio of the aminosilicone of the formula and the epoxy compound is 0.01 to 20 mol amount, particularly 0.1 to 10 mol amount of the epoxy group in the monoepoxy compound with respect to one nitrogen atom contained in the aminosilicone. It is preferable to set it as follows.

なお、(1)式のアミノシリコーンと上記モノエポキシ
化合物とは、これらを混合してから40〜80℃程度に
加熱することにより、下記反応式 で示される反応が起こり、アミノシリコーン分子中のア
ミノ基の活性水素基がエポキシ化合物でブロック変性さ
れたエポキシ変性アミノシリコーンが反応生成物として
生じる。
The aminosilicone of the formula (1) and the above monoepoxy compound are mixed in the following reaction formula by heating them to about 40 to 80 ° C. The reaction represented by (1) occurs, and an epoxy-modified aminosilicone in which the active hydrogen group of the amino group in the aminosilicone molecule is block-modified with an epoxy compound is produced as a reaction product.

本発明では、出発原料として(1)式のアミノシリコー
ン及び上記エポキシ変性アミノシリコーンそれぞれの1
種を単独で使用しても2種を混合して使用してもよく、
またアミノシリコーンとエポキシ変性アミノシリコーン
とを併用してもよい(以下、出発原料を総称してアミノ
シリコーン類と称する)。
In the present invention, as the starting material, 1 of each of the aminosilicone of the formula (1) and the above epoxy-modified aminosilicone
The seeds may be used alone or in combination of two,
Further, amino silicone and epoxy-modified amino silicone may be used in combination (hereinafter, starting materials are generically referred to as amino silicones).

本発明のアミノシリコーン微粒子エマルジョンの製造方
法では、まず上記出発原料に界面活性剤を添加し、アミ
ノシリコーン類を水中に分散させる。
In the method for producing an aminosilicone fine particle emulsion of the present invention, first, a surfactant is added to the above starting material to disperse aminosilicones in water.

ここで、使用される界面活性剤は、特に限定されるもの
ではなく、非イオン系界面活性剤、アニオン系界面活性
剤、カチオン系界面活性剤、両性イオン系界面活性剤と
いった従来公知の各種のものが使用可能である。界面活
性剤の具体例としては、ポリオキシエチレンアルキルフ
ェニルエーテル,ポリオキシエチレンアルキルエーテ
ル,ポリオキシエチレンアルキルエステル,ソルビタン
脂肪酸エステル,シヨ糖脂肪酸エステル等の非イオン系
界面活性剤、アルキル硫酸塩,アルキルフェニルスルホ
ン酸塩,ポリオキシエチレンアルキルフェニル硫酸塩等
のアニオン系界面活性剤、アルキルトリメチルアンモニ
ウムクロライド,ジアルキルジメチルアンモニウムクロ
ライド,ベンジルトリメチルアンモニウムクロライド等
のカチオン系界面活性剤、アルキルベタイン,アルキル
アミノ酸等の両性イオン系界面活性剤などが挙げられ、
これらの1種又は2種以上を使用し得るが、中でも他の
イオン性を有する成分との併用性の点からノニオン系界
面活性剤の使用が好ましく、とりわけ使用する界面活性
剤の1種又は2種以上の合計HLB値が12〜15とな
るように用いることが好適である。
Here, the surfactant used is not particularly limited, and various conventionally known surfactants such as nonionic surfactants, anionic surfactants, cationic surfactants and zwitterionic surfactants are used. Things can be used. Specific examples of the surfactant include nonionic surfactants such as polyoxyethylene alkylphenyl ether, polyoxyethylene alkyl ether, polyoxyethylene alkyl ester, sorbitan fatty acid ester and sucrose fatty acid ester, alkyl sulfate, alkyl Anionic surfactants such as phenyl sulfonate and polyoxyethylene alkylphenyl sulfate, cationic surfactants such as alkyltrimethylammonium chloride, dialkyldimethylammonium chloride and benzyltrimethylammonium chloride, amphoteric properties such as alkylbetaine and alkylamino acid Ionic surfactants and the like,
One or more of these may be used, but among them, it is preferable to use a nonionic surfactant from the viewpoint of the combined use with other ionic components, and in particular, one or two of the surfactants used. It is preferable to use it so that the total HLB value of at least one species is 12 to 15.

また、界面活性剤の添加量は、アミノシリコーン類10
0重量部に対して10重量部以上、好ましくは10〜1
00重量部とするもので、添加量が10重量部より少な
いと平均粒径が0.1μm以下の微粒子エマルジョンが
得られず、10重量部より多いと、微粒子エマルジョン
の製造には差し支えないものの、繊維等の処理時に不揮
発成分として残存し、アミノシリコーン類の特性を阻害
する。
The amount of the surfactant added is 10
10 parts by weight or more with respect to 0 parts by weight, preferably 10 to 1
If the addition amount is less than 10 parts by weight, a fine particle emulsion having an average particle size of 0.1 μm or less cannot be obtained, and if it is more than 10 parts by weight, production of the fine particle emulsion may be carried out. It remains as a non-volatile component during the treatment of fibers and the like, and hinders the properties of amino silicones.

本発明において、アミノシリコーン類を水中に乳化分散
させる方法については、アミノシリコーン類と界面活性
剤をプロペラ羽根又はホモミキサー等の攪拌装置で常温
にて混合均一化し、そこへ攪拌下で水を徐々に添加して
O/W型エマルジョンを製造する方法が採用される。な
お、水の使用量は、所望のアミノシリコーン類濃度を基
準にして調整すればよいが、通常アミノシリコーン類1
00重量部に対して100〜1000重量部である。
In the present invention, regarding the method of emulsifying and dispersing the aminosilicones in water, the aminosilicones and the surfactant are mixed and homogenized at room temperature with a stirring device such as a propeller blade or a homomixer, and water is gradually added thereto with stirring. Is used to produce an O / W type emulsion. The amount of water used may be adjusted on the basis of the desired aminosilicone concentration.
It is 100 to 1000 parts by weight with respect to 00 parts by weight.

次に、本発明では水中に乳化分散したアミノシリコーン
類に酸性物質を添加してpH調整を行うもので、酸性物質
を添加するとアミノシリコーン類中のアミノ基と酸性物
質が反応してアミン塩が形成され、このためアミノシリ
コーン類の親水性が増し、続いて後述する加熱熟成工程
を行なうことにより、微粒子エマルジョンを生成させる
ことができる。
Next, in the present invention, the pH is adjusted by adding an acidic substance to aminosilicones that are emulsified and dispersed in water.When an acidic substance is added, the amino group in the aminosilicone reacts with the acidic substance to form an amine salt. As a result, the hydrophilicity of the aminosilicone is increased, and a fine particle emulsion can be formed by subsequently performing a heat aging step described later.

この場合、酸性物質としては、例えば塩酸,硫酸,リン
酸等の無機酸,ギ酸,酢酸プロピオン酸,ラウリン酸,
ステアリン酸等の有機酸などが挙げげられるが、反応
性、取り扱いの面からギ酸,酢酸等の低級脂肪酸が好ま
しい。
In this case, examples of the acidic substance include inorganic acids such as hydrochloric acid, sulfuric acid, phosphoric acid, formic acid, propionic acid acetate, lauric acid,
Examples thereof include organic acids such as stearic acid, and lower fatty acids such as formic acid and acetic acid are preferable in terms of reactivity and handling.

更に、酸性物質の使用量は、アミノシリコーン類分子中
の窒素原子に対して0.1モル当量以上、好ましくは
0.1〜1モル当量の範囲とするもので、0.1モル当
量より少ないとアミノシリコーン類の親水性が不十分で
平均粒径0.1μm以下の微粒子エマルジョンを得るこ
とができない。なお、酸性物質の使用量は0.1モル当
量以上であれば特に制限はないが、繊維等の処理時に酸
性物質が揮散又は揮散成分として生じ、アミノシリコー
ン類の特性低下を招く可能性があることから、より好ま
しくは0.1〜1モル当量である。
Further, the amount of the acidic substance used is in the range of 0.1 molar equivalent or more, preferably 0.1 to 1 molar equivalent, and less than 0.1 molar equivalent with respect to the nitrogen atom in the aminosilicone molecule. Therefore, the hydrophilicity of aminosilicones is insufficient, and a fine particle emulsion having an average particle size of 0.1 μm or less cannot be obtained. The amount of the acidic substance used is not particularly limited as long as it is 0.1 molar equivalent or more, but the acidic substance may be volatilized or may be generated as a volatilized component during the treatment of the fiber and the like, which may lead to deterioration of the properties of the aminosilicone. Therefore, it is more preferably 0.1 to 1 molar equivalent.

本発明では、このようにアミノシリコーン類の乳化分散
水溶液に酸性物質を添加した後、加熱して熟成を行な
う。この加熱熟成工程を行なうことにより、上述したア
ミノシリコーン類中のアミノ基と酸性物質との反応、す
なわちアミノシリコーン類の親水化が促進される。その
アミノシリコーン類の親水化と加熱による熱エネルギー
のため、エマルジョン粒子が水分子によって細断され、
エマルジョン粒子が細分化して微粒子化する。
In the present invention, the acidic substance is added to the emulsion-dispersed aqueous solution of aminosilicones in this manner, and then the mixture is heated for aging. By carrying out this heat aging step, the reaction between the amino group in the amino silicone and the acidic substance described above, that is, the hydrophilization of the amino silicone is promoted. Due to the hydrophilicity of the amino silicones and the heat energy generated by heating, the emulsion particles are shredded by water molecules,
The emulsion particles are subdivided into fine particles.

ここで、加熱熟成は、50〜90℃、特に60〜80℃
で1時間以上、特に3〜20時間の条件で行なうことが
好ましい。温度が50℃より低かったり、熟成時間が1
時間に満たないと、満足な微粒子エマルジョンが得られ
ない場合があり、90℃より高い温度ではエマルジョン
破壊の原因となる場合がある。
Here, the heat aging is performed at 50 to 90 ° C, particularly 60 to 80 ° C.
It is preferable to carry out the treatment for 1 hour or longer, especially for 3 to 20 hours. Temperature is lower than 50 ℃, aging time is 1
If the time is not reached, a satisfactory fine particle emulsion may not be obtained, and if the temperature is higher than 90 ° C, the emulsion may be broken.

なお、加熱熟成は、アミノシリコーン類の乳化分散液を
プロペラ羽根等の攪拌装置で攪拌しながら行なうことが
好適である。
The heat aging is preferably performed while stirring the emulsified dispersion liquid of aminosilicones with a stirring device such as a propeller blade.

以上説明した本発明の方法により得られるアミノシリコ
ーン微粒子エマルジョンは、そのままで繊維処理剤、離
型剤、艶出し剤などとして各種用途に使用することがで
きるが、必要に応じて他の水性処理剤、例えば撥水剤、
吸水加工の帯電防止剤、難燃剤等を添加し使用しても差
し支えない。
The aminosilicone fine particle emulsion obtained by the method of the present invention described above can be used as it is as a fiber treatment agent, a release agent, a polish, etc. for various purposes, but other aqueous treatment agents may be used as necessary. , For example water repellent,
Antistatic agents for water absorption processing, flame retardants, etc. may be added and used.

発明の効果 以上説明したように、本発明の製造方法によれば、平均
粒径0.1μm以下で貯蔵安定性、希釈安定性、機械安
定性に優れたアミノシリコーン微粒子エマルジョンを得
ることができ。更に、本発明方法で得られるエマルジョ
ンは、外観が透明ないし半透明であるので、他の透明成
分と併用しても外観を損なうことがない上、浸透性が良
好であるので、例えば繊維を処理する場合、厚地布でも
内部まで均一に処理することができ、柔軟性等のアミノ
シリコーンの特性を充分に付与することも可能であり、
繊維処理剤、離型剤、艶出し剤等として有用である。
EFFECTS OF THE INVENTION As described above, according to the production method of the present invention, an aminosilicone fine particle emulsion having an average particle size of 0.1 μm or less and excellent in storage stability, dilution stability and mechanical stability can be obtained. Further, since the emulsion obtained by the method of the present invention has a transparent or translucent appearance, it does not impair the appearance even when used in combination with other transparent components, and has good permeability, and therefore, for example, fibers are treated. In this case, even thick cloth can be uniformly processed to the inside, and it is also possible to sufficiently impart aminosilicon characteristics such as flexibility.
It is useful as a fiber treatment agent, a release agent, a polish, and the like.

実施例、比較例 以下、実施例及び比較例を示して本発明を具体的に説明
するが、本発明は下記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 specifically described with reference to Examples and Comparative Examples, but the present invention is not limited to the following Examples.

〔実施例1〕 下記式 で示されるアミノシリコーン150gとポリオキシエチ
レンフェニルエーテル(HLB=13.3)50gを2
ビーカーに仕込み、ホモミキサー(特殊機化工業社
製)5000rpmにて室温で5分間均一に混合した後、
同一攪拌下、水800gを徐々に加え、均一に乳化分散
させた(エマルジョンA)。
Example 1 The following formula 150 g of amino silicone and 50 g of polyoxyethylene phenyl ether (HLB = 13.3) are added.
After charging in a beaker and homogenously mixing for 5 minutes at room temperature with a homomixer (made by Tokushu Kika Kogyo Co., Ltd.) at 5000 rpm,
Under the same stirring, 800 g of water was gradually added to uniformly emulsify and disperse (Emulsion A).

更に、同一攪拌下、酢酸4.6g(アミノシリコーン中
のN原子に対して1.0モル当量)を添加した後、10
分間攪拌を続けた(エマルジョンB)。
Further, under the same stirring, 4.6 g of acetic acid (1.0 molar equivalent to N atom in aminosilicone) was added, and then 10
Stirring was continued for a minute (emulsion B).

このエマルジョンBを容量2のフラスコに移し、プロ
ペラ羽根100rpmで攪拌下、80℃で4時間加熱熟成
を行なってアミノシリコーン微粒子エマルジョンを得た
(エマルジョンC)。
This emulsion B was transferred to a flask having a capacity of 2 and aged with heating at 80 ° C. for 4 hours under stirring with a propeller blade of 100 rpm to obtain an aminosilicone fine particle emulsion (emulsion C).

〔比較例1〕 乳化重合法の例として、オクタメチルシクロテトラシロ
キサン140.6g、N−β(アミノエチル)−γ−ア
ミノプロピルメチルジメトキシシラン7.8g、ヘキサ
メチルジシロキサン1.5g、ラウリルトリメチルアン
モニウムクロライド50gを2ビーカーに仕込み、ホ
モミキサー5000rpmにて5分間均一に混合した後、
同一攪拌下、水781gを徐々に加え、均一に乳化分散
させた後、容量2のフラスコに移し、プロペラ羽根1
00rpmで攪拌下、水酸化カリウム1gを水19gに溶
解したものを添加した。その後、80℃で40時間加熱
して重合反応を行ない、30℃で10時間保持後、酢酸
2gで中和した(エマルジョンD)。
Comparative Example 1 As an example of the emulsion polymerization method, 140.6 g of octamethylcyclotetrasiloxane, 7.8 g of N-β (aminoethyl) -γ-aminopropylmethyldimethoxysilane, 1.5 g of hexamethyldisiloxane, lauryltrimethyl. 50 g of ammonium chloride was charged into a 2 beaker and homogenized for 5 minutes at a homomixer of 5000 rpm.
Under the same stirring, 781 g of water was gradually added to uniformly emulsify and disperse, and then transferred to a flask having a capacity of 2 and propeller blade 1
Under stirring at 00 rpm, 1 g of potassium hydroxide dissolved in 19 g of water was added. Then, the mixture was heated at 80 ° C. for 40 hours to carry out a polymerization reaction, kept at 30 ° C. for 10 hours, and then neutralized with 2 g of acetic acid (emulsion D).

〔比較例2〕 実施例1において、酢酸を0.3g(アミノシリコーン
類中のN原子に対して0.065モル当量)を使用した
他は同様にエマルジョンを製造した(エマルジョン
E)。
[Comparative Example 2] An emulsion was prepared in the same manner as in Example 1 except that 0.3 g of acetic acid (0.065 molar equivalent relative to N atoms in aminosilicones) was used (emulsion E).

〔比較例3〕 実施例1において、界面活性剤を10gとした他は同様
にエマルジョンを製造した(エマルジョンF)。
[Comparative Example 3] An emulsion was prepared in the same manner as in Example 1 except that the amount of the surfactant was 10 g (emulsion F).

実施例1及び比較例1〜3で得られたエマルジョンの評
価結果を第1表に示す。
Table 1 shows the evaluation results of the emulsions obtained in Example 1 and Comparative Examples 1 to 3.

第1表の結果より、従来の乳化重合法で製造した場合
(比較例1)、及び酸性物質の添加量や界面活性剤の添
加量が本発明範囲外の場合(比較例2,3)、平均粒径
0.1μm以下の微粒子エマルジョンを得ることができ
ず、乳白色の外観でエマルジョンの貯蔵安定性や機械安
定性も低いものであるが、本発明の方法で製造したエマ
ルジョン(実施例1、エマルジョンC)は、平均粒径が
0.1μm以下で透明感のある外観であり、約2倍以上
の長期間において安定で貯蔵安定性に優れ、希釈安定性
はオイルスポット等の発生がなく極めて良好で、かつ機
械安定性も良好であることが確認された。
From the results shown in Table 1, when produced by the conventional emulsion polymerization method (Comparative Example 1), and when the addition amount of the acidic substance or the addition amount of the surfactant is outside the range of the present invention (Comparative Examples 2 and 3), A fine particle emulsion having an average particle size of 0.1 μm or less cannot be obtained, and the emulsion has a milky white appearance and low storage stability and mechanical stability. However, the emulsion produced by the method of the present invention (Example 1, Emulsion C) has an average particle size of 0.1 μm or less and has a transparent appearance, is stable for a long time of about 2 times or more and has excellent storage stability, and has diluting stability that no oil spots occur. It was confirmed that it was good and mechanical stability was also good.

[比較例4] 実施例1において、アミノシリコーン、界面活性剤、水
を仕み、80℃昇温後、ホモミキサー500rpmにて
5分間均一に混合し、更にホモミキサー5000rpm
にて5分間均一に混合した後、同量の酢酸を添加独て更
に10分間拌を続けた(エマルジョンG)。
[Comparative Example 4] In Example 1, the aminosilicone, the surfactant and the water were charged, the temperature was raised to 80 ° C, and the mixture was uniformly mixed at 500 rpm for 5 minutes, and further homomixer 5000 rpm.
After uniformly mixing for 5 minutes, the same amount of acetic acid was added and stirring was continued for another 10 minutes (emulsion G).

このエマルジョンGをフラスコに移し、80℃で4時間
加熱を行なった(エマルジョンH)。
This emulsion G was transferred to a flask and heated at 80 ° C. for 4 hours (emulsion H).

これらエマルジョンG,Hの評価結果を下記に示す。The evaluation results of these emulsions G and H are shown below.

エマルジョンG 外観 青白半透明液体 平均粒径 0.15μm 貯蔵安定性 6カ月で分離離 希釈安定性 良好 機械安定性 干渉膜あり エマルジョンH 外観 青白半透明液体 平均粒径 0.12μm 貯蔵安定性 6カ月で分離 希釈安定性 良好 機械安定性 干渉膜あり 上記の結果より、酸性物質(酢酸)添加前に熱がかかる
と、アミノシリコーンと界面活性剤との親和性が減少す
るためにエマルジョン粒径が大きくなり、後で酸化性物
質を添加し、加熱しても、細粒化に限界があり、最終エ
マルジョンの粒径が0.1μm以下にならないことが認
められる。
Emulsion G Appearance Blue-white translucent liquid Average particle size 0.15 μm Storage stability 6 months Separation / diluting stability Good mechanical stability With interference film Emulsion H Appearance Blue-white translucent liquid Average particle size 0.12 μm Storage stability 6 months Separation Dilution stability Good mechanical stability With interference film From the above results, when heat is applied before adding an acidic substance (acetic acid), the affinity between aminosilicone and surfactant decreases and the emulsion particle size increases. However, it is recognized that even if an oxidizing substance is added later and heated, there is a limit to the atomization, and the particle size of the final emulsion does not become 0.1 μm or less.

〔実施例2〕 下記式 で示されるアミノシリコーン150gを使用し、酸性物
質としてギ酸1.3g(アミノシリコーン中のN原子に
対して0.5モル当量)を使用した他は実施例1と同様
にエマルジョンを製造した。
Example 2 The following formula An emulsion was produced in the same manner as in Example 1 except that 150 g of the aminosilicone represented by 1) was used and 1.3 g of formic acid (0.5 molar equivalent to N atom in aminosilicone) was used as the acidic substance.

〔実施例3〕 下記式 で示されるアミノシリコーン150gとポリオキシエチ
レンラウリルエーテル(HLB=14.0)15.0g
を使用し、酸性物質としてギ酸1.1g(アミノシリコ
ーン中のN原子に対して0.1モル当量)を使用した他
は実施例1と同様にエマルジョンを製造した。
Example 3 The following formula 150g of aminosilicone and 15.0g of polyoxyethylene lauryl ether (HLB = 14.0)
Was used and 1.1 g of formic acid (0.1 molar equivalent to N atom in aminosilicone) was used as an acidic substance, and an emulsion was produced in the same manner as in Example 1.

〔実施例4〕 攪拌機、温度計、還流冷却器及び窒素ガス導入口を設け
た容量1のガラス製反応器に、実施例1で使用しアミ
ノシリコーン300g及び式 で示されるモノエポキシ化合物11.4g(アミノシリ
コーン中のN原子に対して1.0モル当量)を仕込み、
窒素ガスの通気下に60℃で5時間反応させたところ、
不揮発分(105℃/3Hrs)97.6%、粘度154
00csのアミノシリコーンが得られた。このアミノシリ
コーンを用いて実施例1と同じ方法でエマルジョンを製
造した。
Example 4 A glass reactor having a capacity of 1 equipped with a stirrer, a thermometer, a reflux condenser and a nitrogen gas inlet was used in Example 1 and 300 g of aminosilicone and the formula were used. 11.4 g of monoepoxy compound represented by (1.0 molar equivalent to N atom in aminosilicone) was charged,
When reacted at 60 ° C for 5 hours under aeration of nitrogen gas,
Nonvolatile matter (105 ° C / 3Hrs) 97.6%, viscosity 154
00 cs of aminosilicone was obtained. An emulsion was produced using this aminosilicone in the same manner as in Example 1.

実施例2〜4で得られたエマルジョンの評価結果を第2
表に示す。
The evaluation results of the emulsions obtained in Examples 2 to 4 are second
Shown in the table.

第2表の結果より、本発明方法により得られるエマルジ
ョンは、平均粒径が0.1μm以下で透明感のある外観
を有し、各種安定性に優れていることがわかった。
From the results shown in Table 2, it was found that the emulsion obtained by the method of the present invention has an average particle size of 0.1 μm or less, has a transparent appearance, and is excellent in various stability.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 廻谷 典行 群馬県安中市磯部2丁目13番1号 信越化 学工業株式会社シリコーン電子材料技術研 究所内 (56)参考文献 特表 平2−503204(JP,A) 国際公開88/8436(WO,A) ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Noriyuki Maiya, 13-1 Isobe, Annaka-shi, Gunma Shin-Etsu Chemical Co., Ltd. Silicone Electronic Materials Research Laboratory (56) References -503204 (JP, A) International publication 88/8436 (WO, A)

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】下記一般式(1) [但し、式中Rは炭素原子数1〜20の一価炭化水素
基、水酸基又は−OR′(R′は炭素原子数1〜20の
一価炭化水素基)、Aは式−R(NRNR
(R,Rはそれぞれ炭素原子数1〜6の2価
の炭化水素基、R,R,Rはそれぞれ水素原子又
は炭素原子数1〜20の1価の炭化水素基、zは0〜5
の整数を表す)で示されるアミノアルキル基であり、0
<x≦3,0≦y<3,0<x+y≦3である。] で示されるアミノシリコーン及び/又は上記式(1)で
示されるアミノシリコーンと (ここにRは1価の有機基を表す)で示されるモノエ
ポキシ化合物との反応物であるエポキシ変性アミノシリ
コーンに、界面活性剤をアミノシリコーン及びエポキシ
変性アミノシリコーン合計量100重量部に対して10重量
部以上添加して常温で均一混合した後、水を徐々に添加
してアミノシリコーン及び/又はエポキシ変性アミノシ
リコーンを常温で乳化分散させ、次いで、前記乳化分散
水溶液中に酸性物質をアミノシリコーン及びエポキシ変
性アミノシリコーン分子中のN原子に対して0.1モル当
量以上添加した後、50〜90℃1時間以上加熱熟成を行な
うことを特徴とするアミノシリコーン微粒子エマルジョ
ンの製造方法。
1. The following general formula (1) [Wherein R 1 is a monovalent hydrocarbon group having 1 to 20 carbon atoms, a hydroxyl group or -OR '(R' is a monovalent hydrocarbon group having 1 to 20 carbon atoms), and A is a formula -R 2 (NR 3 R 4 ) z NR
5 R 6 (R 2 and R 4 are each a divalent hydrocarbon group having 1 to 6 carbon atoms, and R 3 , R 5 and R 6 are each a hydrogen atom or a monovalent hydrocarbon having 1 to 20 carbon atoms. Group, z is 0 to 5
Is an aminoalkyl group represented by
<X ≦ 3,0 ≦ y <3,0 <x + y ≦ 3. ] And / or an aminosilicone represented by the above formula (1) (Wherein R 7 represents a monovalent organic group), an epoxy-modified aminosilicone which is a reaction product with a monoepoxy compound represented by the formula: 10 parts by weight or more and uniformly mixed at room temperature, water is gradually added to emulsify and disperse the aminosilicone and / or the epoxy-modified aminosilicone at room temperature, and then the acidic substance is added to the aqueous solution of the emulsified dispersion. A method for producing an aminosilicone fine particle emulsion, which comprises adding 0.1 molar equivalent or more to N atom in silicone and epoxy-modified aminosilicone molecule, and then heat aging at 50 to 90 ° C. for 1 hour or more.
JP1108179A 1989-04-27 1989-04-27 Method for producing aminosilicone fine particle emulsion Expired - Fee Related JPH0655817B2 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP1108179A JPH0655817B2 (en) 1989-04-27 1989-04-27 Method for producing aminosilicone fine particle emulsion
KR1019900005850A KR970000404B1 (en) 1989-04-27 1990-04-26 Method for manufacturing aminosilicone emulsion

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1108179A JPH0655817B2 (en) 1989-04-27 1989-04-27 Method for producing aminosilicone fine particle emulsion

Publications (2)

Publication Number Publication Date
JPH02284959A JPH02284959A (en) 1990-11-22
JPH0655817B2 true JPH0655817B2 (en) 1994-07-27

Family

ID=14477997

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1108179A Expired - Fee Related JPH0655817B2 (en) 1989-04-27 1989-04-27 Method for producing aminosilicone fine particle emulsion

Country Status (2)

Country Link
JP (1) JPH0655817B2 (en)
KR (1) KR970000404B1 (en)

Families Citing this family (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU641014B2 (en) * 1990-06-01 1993-09-09 Unilever Plc Liquid fabric conditioner and dryer sheet fabric conditioner containing compatible silicones
AU641013B2 (en) * 1990-06-01 1993-09-09 Unilever Plc Liquid fabric conditioner and dryer sheet fabric conditioner containing fabric softener, aminosilicone and bronsted acid compatibiliser
US6451905B2 (en) * 1999-02-16 2002-09-17 Crompton Corporation Shear stable aminosilicone emulsions
JP4539815B2 (en) * 2003-02-19 2010-09-08 信越化学工業株式会社 Scratch shielding agent for glass container and glass container
JP4761396B2 (en) * 2007-02-14 2011-08-31 信越化学工業株式会社 Textile treatment agent
EP2139941A1 (en) 2007-04-11 2010-01-06 Dow Corning Corporation Silcone polyether block copolymers having organofunctional endblocking groups
US8940284B2 (en) 2010-04-01 2015-01-27 The Procter & Gamble Company Organosilicones
JP5640879B2 (en) * 2011-04-22 2014-12-17 信越化学工業株式会社 Silicone microemulsion composition
KR101554410B1 (en) * 2011-06-20 2015-09-18 더 프록터 앤드 갬블 캄파니 Process of making beta-hydroxyamino compounds
CN113185710B (en) * 2021-04-26 2021-11-23 广东赛安特新材料有限公司 Amino silicone oil emulsion and preparation method thereof

Also Published As

Publication number Publication date
JPH02284959A (en) 1990-11-22
KR900015801A (en) 1990-11-10
KR970000404B1 (en) 1997-01-09

Similar Documents

Publication Publication Date Title
KR900009041B1 (en) Process for the preparation of an aqueous emulsion of silses quioxane
JP2832143B2 (en) Silicone fine particles and method for producing the same
US5707435A (en) Ammonium siloxane emulsions and their use as fiber treatment agents
US20030143176A1 (en) Compositions containing silicone oil-in-water emulsions, salts, alcohols and solvents
EP0444633A2 (en) Polyorganosiloxane-based elastomer powder and method for its preparation
JPH0159390B2 (en)
US4894412A (en) Process for preparing self-crosslinkable aminosiloxane emulsion
JPH0655817B2 (en) Method for producing aminosilicone fine particle emulsion
JPH0478657B2 (en)
JP4073085B2 (en) Suspension type silicone adhesive, method for producing the same, and method for producing an adhesive substrate
JP2008506006A (en) Organopolysiloxane resin emulsion produced by emulsion polymerization
JP3495110B2 (en) Amino group-containing organopolysiloxane microemulsion and process for producing the same
JPS6261219B2 (en)
JP3495109B2 (en) Amino group-containing organopolysiloxane microemulsion and method for producing the same
EP1160372A1 (en) Synthetic fiber treatment agent composition
JPH0114345B2 (en)
US6479583B2 (en) Polymerization of silicone microemulsions
JP2002194675A (en) Fiber treatment agent
JP3142766B2 (en) Polyorganosiloxane emulsion
JPH0559284A (en) Microsuspension of cured silicone and its production
JPH09228255A (en) Fiber treatment agent
JPH0825255B2 (en) Water repellent paperboard
CN119998417A (en) Emulsion composition of film-forming organopolysiloxane and method for producing the same
JP2002194674A (en) Emulsion composition for fiber treating agent and method for producing the same
JP3164740B2 (en) Aqueous coating agent for textile fabric and coated textile fabric

Legal Events

Date Code Title Description
LAPS Cancellation because of no payment of annual fees