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JP3553653B2 - Fiber treatment agent mainly composed of acrylic emulsion - Google Patents
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JP3553653B2 - Fiber treatment agent mainly composed of acrylic emulsion - Google Patents

Fiber treatment agent mainly composed of acrylic emulsion Download PDF

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JP3553653B2
JP3553653B2 JP20410394A JP20410394A JP3553653B2 JP 3553653 B2 JP3553653 B2 JP 3553653B2 JP 20410394 A JP20410394 A JP 20410394A JP 20410394 A JP20410394 A JP 20410394A JP 3553653 B2 JP3553653 B2 JP 3553653B2
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emulsion
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polymerization
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JPH0841784A (en
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正勝 山本
直一 村瀬
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クラリアント インターナショナル リミテッド
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Description

【0001】
【産業上の利用分野】
本発明は繊維を処理して、風合い、強度、耐水性、耐溶剤性、耐薬品性等の物性を向上させる繊維処理剤に関する。さらに詳しくは、乾燥時にエマルジョン粒子が局在化するマイグレーションが発生せず優れた風合いを与える繊維処理剤に関する。
【0002】
【従来の技術】
従来より繊維の処理には合成樹脂の溶液やエマルジョンが用いられてきた。
繊維の処理で要求される最も重要な性能は、風合いである。保護コロイドを用いて得たエマルジョンを用いて繊維を処理すると界面活性剤を用いて得たエマルジョンを使用した場合に較べて繊維の風合いが向上する。
しかしながら、保護コロイドを用いて重合することの出来たエマルジョンとしては酢酸ビニル系のエマルジョンが主であったが、このエマルジョンは耐水性が悪く、しかも酢酸臭があるという欠点があった。
一方アクリル系エマルジョンは酢酸臭もなく、耐水性も良好であるが、重合性が悪く凝集し易いので保護コロイドではエマルジョン重合が出来なかった。
界面活性剤を用いて重合したアクリル系エマルジョンを用いて繊維を処理すると、風合いが悪く、特にバルキイ的風合いは得られない。
さらに、界面活性剤を用いて得たアクリル系エマルジョンは粒子径が大略0.5μm以下の小さい粒子であるためマイグレーションしやすい欠点を有している。
ここで言うマイグレーションとは、基材にエマルジョンを含浸後ドライヤー等で強制乾燥させる際、基材表面の温度が内部に較べて高く表面で水の蒸発が激しく起こるため、エマルジョン粒子が水の流れにつられて表面に移動し樹脂が局在化することでこのような現象により強度、触感、印刷適性、吸水性等に悪影響をおよぼす。
【0003】
【発明が解決しようとする課題】
本発明は、従来の問題点の解決を図るとともに、風合いの良好な、マイグレーションのない、酢酸臭のない繊維処理剤を提供しようとするものである。
【0004】
【課題を解決するための手段】
本発明による繊維処理剤は、アクリル系単量体と該単量体と共重合可能な単量体を、単量体に対し2〜10重量%の保護コロイドの存在下でレドックス系重合開始剤を用い、重合温度65℃以下で乳化重合して得た、粒子径1.0〜3.0μmのアクリル系エマルジョンを主剤とするものである。
本発明の好ましい態様によれば、繊維処理剤において、アクリル系単量体と共重合する単量体として酢酸ビニルを全体量体の25重量%以下使用することが好ましい。
本発明の別の好ましい態様によれば、前記保護コロイドはセルロースエーテル系および/またはポリビニルアルコール系である。
本発明のさらに別の好ましい態様によれば、繊維処理剤において、アクリル系単量体を全単量体の70〜99重量%使用することが好ましい。
【0005】
【作用】
本発明の第1の特徴は保護コロイドを用いて重合した、粒子径1.0〜3.0μmのアクリル系エマルジョンを用いることである。
本発明者は保護コロイドを用いて重合した酢酸ビニル系エマルジョンで処理した繊維は風合いが良いのに、界面活性剤を用いて重合したアクリル系エマルジョンで処理した繊維の風合いが悪いのかを研究した結果エマルジョン粒子の大きさが重大な影響を与えていることを解明した。つまりエマルジョン粒子の粒径が小さいと繊維の風合いは劣化する。
粒径が1.0〜3.0μmの粒径でないと質感のあるバルキイな風合いは得られない。また1.0μm以下であるとマイグレーションが発生する傾向が大きい。粒径が3.0μm以上になるとエマルジョンの希釈安定性が劣化する傾向が大きい。
【0006】
本発明の第2の特徴は、保護コロイドの使用量である。単量体に対し保護コロイドの量は2〜10重量%でなければならない。2重量%より少ないとエマルジョンの粒子径が0.5μm以上の大きさにならない。そのため処理した繊維の風合いが良好とならず、またマイグレーションも発生する。保護コロイドが10重量%以上になると増粘を生じ重合時の安定性を悪くし、エマルジョンの安定性も劣化し、さらに耐水性も低下する。
【0007】
本発明の第3の特徴は重合開始剤としてレドックス系の開始剤を使用し0℃〜65℃で重合することである。良好なエマルジョンを得るためには重合温度を65℃以下にする必要があり、そのためには重合開始剤としてレドックス系開始剤を使用する必要がある。この重合条件でないと保護コロイドとアクリル系単量体がグラフト化してしまい、重合安定性が悪くなり良好なエマルジョンが得られない。
【0008】
このように本発明は、保護コロイドを単量体の2〜10重量%使用し、重合開始剤としてレドックス系開始剤を使用し、65℃以下の重合温度でアクリル系単量体と該単量体と共重合可能な単量体を重合させると、これ等の条件が相乗的に作用して粒径0.5μm以上のアクリル系エマルジョンが得られ、このエマルジョンが処理した繊維の風合いを良好とし、マイグレーションを防止する作用を奏する。
注意しなければならないのは、アクリル系単量体と共重合させる単量体として酢酸ビニルを使用する場合である。酢酸ビニルの使用量は全単量体に対し25重量%以下にしなければならない。酢酸ビニルを25重量%以上使用すると耐水性が不充分となり、酢酸臭が発生するからである。
【0009】
本発明で使用される原料物質について説明する。
本発明で使用されるアクリル系単量体としては、
アルキル基の炭素原子が1〜12個のアクリル酸エステルおよびアルキル基の炭素原子が1〜12個のメタアクリル酸エステルである。
本発明で使用されるアクリル系単量体と共重合体と共重合可能な単量体としては、
スチレン、メチルスチレン等の芳香族ビニル化合物、酢酸ビニル、ベオバ(シェル化学株式会社製のα位で分岐した飽和カルボン酸のビニルエステル)、アクリル酸、メタクリル酸、イタコン酸、クロトン酸等の不飽和カルボン酸、ビニルホスフェート、アクリロニトリル、アクリルアミド、N−メチロールアクリルアミド、グリシジルメタクリレート、2−ヒドロキシアルキルアクリレート、アクリル酸アルコキシエチル、ビニルトリエトキシシラン、ビニル(2−メトキシエトキシ)シラン、ビニルトリスアセトキシシラン、γ−メタアクリロプロピルトリメトキシシラン等の多官能シラン系単量体等の官能性単量体、その他エチレン、塩化ビニル、塩化ビニリデンなどがある。重合性不飽和基を2個以上有する単量体も使用でき、例えばジビニルベンゼン、ジビニルアジペート、エチレングリコールジ(メタ)アクリレート、1,3−ブチルジ(メタ)アクリレート、ジアリルフタレートなどが挙げられる。
【0010】
本発明で使用される保護コロイドとしては、
カルボキシメチルヒドロキシエチルセルロース、ヒドロキシエチルセルロース、メチルセルロース、エチルセルロース、カルボキシメチルセルロース等のセルロースエーテル類、ポリビニルアルコール、アセトアセチル化ポリビニルアルコール等のポリビニルアルコール類、ポリビニルピロリドン、変性ポリアクリルアミド、等が挙げられ、重合安定性の面からセルロールエーテル類が好適に用いられる。
【0011】
本発明で使用されるレドックス系開始剤としては、通常の乳化重合に使用されるもので良く、例えば過硫酸カリウム、過硫酸ナトリウム、過硫酸アンモニウム、過酸化水素、ブチルパーオキサイドなどの過酸化物と還元剤を組み合わせたものが用いられる。
本発明においては、所望により保護コロイドの2重量倍以内で界面活性剤が併用でき、通常の乳化重合に使用されるアニオン性、非イオン性の界面活性剤が用いられ、例えばアニオン性の界面活性剤としてはアルキルベンゼンスルホン酸ソーダ、アルキルスルホン酸ソーダ、ポリオキシエチレンアルキルアリルエーテルスルホン酸ソーダ等が挙げられ、非イオン性の界面活性剤としては、ポリオキシエチレンアルキルアリルエーテル型、ポリオキシエチレンアルキルエーテル型、ポリオキシエチレン化ポリオキシプロピレングリコール型等が挙げられる。界面活性剤を保護コロイドの2重量部以上使用すると粒子径が所望の大きさにならない。
また所望により、防腐剤、消泡剤、顔料、連鎖移動剤、造膜助剤等を添加できる。
【0012】
【実施例】

Figure 0003553653
を仕込んだ重合缶に滴下しながら開始剤にブチルパーオキサイドの酸化剤と亜硫酸ソーダの還元剤のレドックス系開始剤を用いて重合温度45℃で乳化重合を行い、アンモニアでpH調整を行った。
この際、水溶性高分子であるカルボキシメチルヒドロキシエチルセルロースの量は全単量体に対し2.0重量%である。
得られたエマルジョンは、粒子径1.6μm、pH5.0であった。
【0013】
実施例2
重合缶に仕込む水を40重量部、カルボキシメチルヒドロキシエチルセルロースの10%水溶液の量を50重量部に変えた以外は実施例1と同様にした。
この際、水溶性高分子であるカルボキシメチルヒドロキシエチルセルロースの量は全単量体に対し5.0重量%である。
得られたエマルジョンは、粒子径1.8μm、pH5.0であった。
【0014】
実施例3
重合缶に仕込む水を20重量部、カルボキシメチルヒドロキシエチルセルロースの10%水溶液の量を80重量部に変えた以外は実施例1と同様にした。
この際、水溶性高分子であるカルボキシメチルヒドロキシエチルセルロースの量は全単量体に対し8.0重量%である。
得られたエマルジョンは、粒子径1.9μm、pH5.0であった。
【0015】
Figure 0003553653
を仕込んだ重合缶に滴下しながら開始剤にブチルパーオキサイドの酸化剤と亜硫酸ソーダの還元剤のレドックス系開始剤を用いて重合温度45℃で乳化重合を行い、アンモニアでpH調整を行った。
この際、水溶性高分子であるカルボキシメチルヒドロキシエチルセルロースの量は全単量体に対し2.0重量%である。
得られたエマルジョンは、粒子径1.6μm、pH5.0であった。
【0016】
Figure 0003553653
を仕込んだ重合缶に滴下しながら開始剤にブチルパーオキサイドの酸化剤と亜硫酸ソーダの還元剤のレドックス系開始剤を用いて重合温度45℃で乳化重合を行い、アンモニアでpH調整を行った。
この際、水溶性高分子であるカルボキシメチルヒドロキシエチルセルロースの量は全単量体に対し0.15重量%である。
得られたエマルジョンは、粒子径0.20μm、pH5.0であった。
【0017】
比較例2
(保護コロイドの量が過剰で重合安定性が悪い例)
重合缶に仕込む水を20重量部、カルボキシメチルヒドロキシエチルセルロースの10%水溶液の量を120重量部、及び水30重量部に変えた以外は比較例1と同様にした。
この際、水溶性高分子であるカルボキシメチルヒドロキシエチルセルロースの量は全単量体に対し12.0重量%である。
これは、凝集が著しくエマルジョンが得られなかった。
【0018】
Figure 0003553653
を仕込んだ重合缶に滴下しながら開始剤にブチルパーオキサイドの酸化剤と亜硫酸ソーダの還元剤のレドックス系開始剤を用いて重合温度45℃で乳化重合を行い、アンモニアでpH調整を行った。
この際、水溶性高分子であるカルボキシメチルヒドロキシエチルセルロースの量は全単量体に対し2.0重量%である。
得られたエマルジョンは、粒子径1.4μm、pH5.0であった。
【0019】
比較例4
(一般の開始剤を用い高温で重合した場合重合安定性が悪い例)
実施例1の開始剤を過硫酸アンモニウムに変更し、重合温度80℃で重合を行った。
これは、凝集が著しくエマルジョンが得られなかった。
(65℃以上では、グラフト化が著しく進むためと考えられる。)
【0020】
≪風合い試験≫
レーヨンウェブを、固形分濃度3.75%に調整したエマルジョン浴に1分間浸漬しマングルで絞る。これを80℃×10min.乾燥させる。室温冷却後、得られた不織布の風合いを触感にて評価する。
バルキイで良好な風合いである………○
ペーパーライクの風合いである………×
【0021】
≪耐マイグレーション性試験≫
東洋瀘紙No.2を10cm×10cmに裁断したものを5枚とり、No1〜5と番号を付ける。これを固形分濃度5%に調整したエマルジョン浴に1分間浸漬しマングルで絞る。これをはがれないようにして200℃×20min.乾燥させる。室温冷却後、各瀘紙の樹脂の着量を測定し5枚の平均着量を計算する。この平均着量に対する各瀘紙の着量の増減率を計算する。
評価
各瀘紙の増減率が20%以内である………○
各瀘紙の増減率が20%以上である………×
【0022】
≪耐水性試験≫
風合い試験で得られた不織布の常態での引張強度と水浸漬後の引張強度を測定し、その保持率を計算する。
常態での引張強度:50mm巾の試験片を20℃×65%RHの恒温室中に16時間以上放置後、株式会社島津製作所製 オートグラフにてつかみ巾100mm、引張速度200mm/min.で測定する。(単位 kgf/50mm)
水浸漬後の引張強度:50mm巾の試験片を20℃水中に1時間浸漬し他は同様に測定する。(単位 kgf/50mm)
保持率:常態強度/水浸漬後の強度×100(単位%)
評価
保持率が15%以上である………○
保持率が15%未満である………×
試験結果は表に示す。
【0023】
【表1】
Figure 0003553653
【0024】
比較例1は、粒子径が小さく風合い及び耐マイマイグレーション性において不良だった。
比較例2、4は凝集してエマルジョンとならなかったため試験出来なかった。
比較例3は、風合い及び耐マイグレーション性は良好であったが、酢酸ビニルの共重合比率が高く耐水性が不良であり,また酢酸臭があった。
【0025】
【発明の効果】
本発明は特定量の保護コロイドを用いて、特定の重合条件で重合した粒子径0.5μm以上のアクリル系エマルジョンを用いることにより風合いが良好でマイグレーシヨンも発生しない優れた効果を奏する。[0001]
[Industrial applications]
The present invention relates to a fiber treatment agent for treating fibers to improve physical properties such as hand, strength, water resistance, solvent resistance, and chemical resistance. More specifically, the present invention relates to a fiber treatment agent which gives an excellent texture without causing migration in which emulsion particles are localized upon drying.
[0002]
[Prior art]
Conventionally, a solution or emulsion of a synthetic resin has been used for treating fibers.
The most important performance required in fiber processing is the texture. When the fibers are treated with the emulsion obtained using the protective colloid, the texture of the fibers is improved as compared with the case where the emulsion obtained using the surfactant is used.
However, as the emulsion which can be polymerized by using a protective colloid, a vinyl acetate emulsion is mainly used, but this emulsion has a disadvantage that it has poor water resistance and has an acetic acid smell.
On the other hand, the acrylic emulsion had no odor of acetic acid and had good water resistance, but it was not polymerizable and easily aggregated, so that emulsion polymerization could not be carried out with a protective colloid.
When fibers are treated with an acrylic emulsion polymerized with a surfactant, the texture is poor, and in particular, a bulky texture cannot be obtained.
Further, the acrylic emulsion obtained by using a surfactant has a disadvantage that it is easily migrated because the particle size is small, approximately 0.5 μm or less.
The term “migration” used here means that when the substrate is impregnated with the emulsion and then forcedly dried with a drier or the like, the temperature of the substrate surface is higher than that of the inside and the water evaporates vigorously on the surface. As a result, such a phenomenon adversely affects the strength, the feel, the printability, the water absorption, and the like.
[0003]
[Problems to be solved by the invention]
An object of the present invention is to solve the conventional problems and to provide a fiber treatment agent having a good texture, no migration, and no odor of acetic acid.
[0004]
[Means for Solving the Problems]
The fiber treating agent according to the present invention is a redox polymerization initiator comprising an acrylic monomer and a monomer copolymerizable with the monomer in the presence of 2 to 10% by weight of a protective colloid based on the monomer. And an acrylic emulsion having a particle diameter of 1.0 to 3.0 [mu] m obtained by emulsion polymerization at a polymerization temperature of 65 [deg.] C. or lower.
According to a preferred embodiment of the present invention, it is preferable that in the fiber treating agent, vinyl acetate is used as a monomer copolymerized with the acrylic monomer in an amount of 25% by weight or less based on the whole monomer.
According to another preferred embodiment of the present invention, the protective colloid is of a cellulose ether type and / or a polyvinyl alcohol type.
According to still another preferred embodiment of the present invention, in the fiber treatment agent, it is preferable that the acrylic monomer is used in an amount of 70 to 99% by weight based on all the monomers.
[0005]
[Action]
A first feature of the present invention is to use an acrylic emulsion polymerized with a protective colloid and having a particle size of 1.0 to 3.0 μm.
The present inventor studied whether fibers treated with a vinyl acetate-based emulsion polymerized using a protective colloid had a good feel, but fibers treated with an acrylic emulsion polymerized using a surfactant had a poor feel. It was found that the size of the emulsion particles had a significant effect. That is, if the particle size of the emulsion particles is small, the texture of the fiber deteriorates.
If the particle size is not from 1.0 to 3.0 μm, a bulky texture with a texture cannot be obtained. If the thickness is less than 1.0 μm, migration tends to occur. When the particle diameter is 3.0 μm or more, the dilution stability of the emulsion tends to deteriorate.
[0006]
A second feature of the present invention is the amount of protective colloid used. The amount of protective colloid, based on the monomers, must be between 2 and 10% by weight. If it is less than 2% by weight, the particle size of the emulsion does not become 0.5 μm or more. Therefore, the texture of the treated fiber is not good, and migration occurs. When the content of the protective colloid is 10% by weight or more, the viscosity increases and the stability at the time of polymerization deteriorates, the stability of the emulsion deteriorates, and the water resistance also decreases.
[0007]
A third feature of the present invention is that polymerization is carried out at 0 ° C to 65 ° C using a redox-based initiator as a polymerization initiator. In order to obtain a good emulsion, the polymerization temperature needs to be 65 ° C. or lower, and for that purpose, it is necessary to use a redox initiator as a polymerization initiator. If the polymerization conditions are not satisfied, the protective colloid and the acrylic monomer are grafted, and the polymerization stability is deteriorated, so that a good emulsion cannot be obtained.
[0008]
As described above, the present invention uses a protective colloid in an amount of 2 to 10% by weight of a monomer, a redox initiator as a polymerization initiator, and an acrylic monomer and the monomer at a polymerization temperature of 65 ° C. or lower. When a monomer copolymerizable with the body is polymerized, these conditions act synergistically to obtain an acrylic emulsion having a particle size of 0.5 μm or more, and this emulsion improves the texture of the treated fiber. This has the effect of preventing migration.
Care must be taken when using vinyl acetate as the monomer to be copolymerized with the acrylic monomer. The amount of vinyl acetate used must not exceed 25% by weight, based on the total monomers. If vinyl acetate is used in an amount of 25% by weight or more, the water resistance becomes insufficient and an acetic acid odor is generated.
[0009]
The raw material used in the present invention will be described.
As the acrylic monomer used in the present invention,
An alkyl acrylate having 1 to 12 carbon atoms and a methacrylate having 1 to 12 carbon atoms in the alkyl group.
As the acrylic monomer and copolymerizable monomer used in the present invention,
Unsaturation such as aromatic vinyl compounds such as styrene and methylstyrene, vinyl acetate, veova (vinyl ester of saturated carboxylic acid branched at the α-position, manufactured by Shell Chemical Co., Ltd.), acrylic acid, methacrylic acid, itaconic acid, crotonic acid, etc. Carboxylic acid, vinyl phosphate, acrylonitrile, acrylamide, N-methylol acrylamide, glycidyl methacrylate, 2-hydroxyalkyl acrylate, alkoxyethyl acrylate, vinyl triethoxysilane, vinyl (2-methoxyethoxy) silane, vinyl trisacetoxy silane, γ- Examples include functional monomers such as polyfunctional silane monomers such as methacrylopropyltrimethoxysilane, and ethylene, vinyl chloride, and vinylidene chloride. A monomer having two or more polymerizable unsaturated groups can also be used, and examples thereof include divinylbenzene, divinyl adipate, ethylene glycol di (meth) acrylate, 1,3-butyldi (meth) acrylate, and diallyl phthalate.
[0010]
As the protective colloid used in the present invention,
Carboxymethyl hydroxyethyl cellulose, hydroxyethyl cellulose, methyl cellulose, ethyl cellulose, cellulose ethers such as carboxymethyl cellulose, polyvinyl alcohol, polyvinyl alcohols such as acetoacetylated polyvinyl alcohol, polyvinyl pyrrolidone, modified polyacrylamide, and the like, polymerization stability From the viewpoint, cellulose ethers are preferably used.
[0011]
As the redox initiator used in the present invention, those used for ordinary emulsion polymerization may be used.For example, potassium persulfate, sodium persulfate, ammonium persulfate, hydrogen peroxide, and peroxides such as butyl peroxide may be used. A combination of reducing agents is used.
In the present invention, a surfactant can be used in combination within 2 times the weight of the protective colloid, if desired, and anionic and nonionic surfactants used in ordinary emulsion polymerization are used. Examples of the agent include sodium alkylbenzene sulfonate, sodium alkyl sulfonate, and sodium polyoxyethylene alkyl allyl ether sulfonate. Examples of the nonionic surfactant include polyoxyethylene alkyl allyl ether type and polyoxyethylene alkyl ether. And polyoxyethylenated polyoxypropylene glycol types. If the surfactant is used in an amount of 2 parts by weight or more of the protective colloid, the particle size does not become a desired size.
If desired, preservatives, defoamers, pigments, chain transfer agents, film-forming auxiliaries, and the like can be added.
[0012]
【Example】
Figure 0003553653
The emulsion polymerization was carried out at a polymerization temperature of 45 ° C. using a redox initiator such as an oxidizing agent of butyl peroxide and a reducing agent of sodium sulfite as an initiator while dropping the mixture into a polymerization vessel charged with the above, and the pH was adjusted with ammonia.
At this time, the amount of carboxymethyl hydroxyethyl cellulose, which is a water-soluble polymer, is 2.0% by weight based on all monomers.
The obtained emulsion had a particle size of 1.6 μm and a pH of 5.0.
[0013]
Example 2
Example 1 was repeated except that the amount of water charged in the polymerization vessel was changed to 40 parts by weight and the amount of a 10% aqueous solution of carboxymethylhydroxyethylcellulose was changed to 50 parts by weight.
At this time, the amount of carboxymethylhydroxyethyl cellulose, which is a water-soluble polymer, is 5.0% by weight based on all monomers.
The obtained emulsion had a particle size of 1.8 μm and a pH of 5.0.
[0014]
Example 3
Example 1 was repeated except that the amount of water charged in the polymerization vessel was changed to 20 parts by weight, and the amount of a 10% aqueous solution of carboxymethylhydroxyethylcellulose was changed to 80 parts by weight.
At this time, the amount of carboxymethylhydroxyethylcellulose, which is a water-soluble polymer, is 8.0% by weight based on all monomers.
The obtained emulsion had a particle size of 1.9 μm and a pH of 5.0.
[0015]
Figure 0003553653
The emulsion polymerization was carried out at a polymerization temperature of 45 ° C. using a redox initiator such as an oxidizing agent of butyl peroxide and a reducing agent of sodium sulfite as an initiator while dropping the mixture into a polymerization vessel charged with the above, and the pH was adjusted with ammonia.
At this time, the amount of carboxymethyl hydroxyethyl cellulose, which is a water-soluble polymer, is 2.0% by weight based on all monomers.
The obtained emulsion had a particle size of 1.6 μm and a pH of 5.0.
[0016]
Figure 0003553653
The emulsion polymerization was carried out at a polymerization temperature of 45 ° C. using a redox initiator such as an oxidizing agent of butyl peroxide and a reducing agent of sodium sulfite as an initiator while dropping the mixture into a polymerization vessel charged with the above, and the pH was adjusted with ammonia.
At this time, the amount of carboxymethylhydroxyethyl cellulose, which is a water-soluble polymer, is 0.15% by weight based on all monomers.
The obtained emulsion had a particle size of 0.20 μm and a pH of 5.0.
[0017]
Comparative Example 2
(Example in which the amount of protective colloid is excessive and polymerization stability is poor)
Comparative Example 1 was carried out in the same manner as in Comparative Example 1 except that the amount of water charged in the polymerization vessel was changed to 20 parts by weight, the amount of a 10% aqueous solution of carboxymethylhydroxyethylcellulose was changed to 120 parts by weight, and to 30 parts by weight of water.
At this time, the amount of carboxymethyl hydroxyethyl cellulose, which is a water-soluble polymer, is 12.0% by weight based on all monomers.
This resulted in significant aggregation and no emulsion was obtained.
[0018]
Figure 0003553653
The emulsion polymerization was carried out at a polymerization temperature of 45 ° C. using a redox initiator such as an oxidizing agent of butyl peroxide and a reducing agent of sodium sulfite as an initiator while dropping the mixture into a polymerization vessel charged with the above, and the pH was adjusted with ammonia.
At this time, the amount of carboxymethyl hydroxyethyl cellulose, which is a water-soluble polymer, is 2.0% by weight based on all monomers.
The obtained emulsion had a particle diameter of 1.4 μm and a pH of 5.0.
[0019]
Comparative Example 4
(Example of poor polymerization stability when polymerized at high temperature using a general initiator)
The polymerization in Example 1 was changed to ammonium persulfate, and polymerization was carried out at a polymerization temperature of 80 ° C.
This resulted in significant aggregation and no emulsion was obtained.
(It is considered that the grafting proceeds remarkably at a temperature of 65 ° C. or higher.)
[0020]
≪Hand test≫
The rayon web is immersed in an emulsion bath adjusted to a solid concentration of 3.75% for 1 minute and squeezed with a mangle. This is 80 ° C. × 10 min. dry. After cooling at room temperature, the texture of the obtained nonwoven fabric is evaluated by touch.
Barkii with good texture ......... ○
It has a paper-like texture .......... ×
[0021]
マ イ グ レ ー シ ョ ン Migration resistance test≫
Toyo Roshi no. No. 2 is cut into 10 cm × 10 cm, and five sheets are taken and numbered No. 1 to No. 5. This is immersed in an emulsion bath adjusted to a solid content concentration of 5% for 1 minute and squeezed with a mangle. 200 ° C. × 20 min. dry. After cooling at room temperature, the amount of resin applied to each filter paper is measured, and the average amount of resin applied to five sheets is calculated. The increase / decrease rate of the applied amount of each filter paper relative to the average applied amount is calculated.
Evaluation The rate of change of each filter paper is within 20%.
The rate of change of each filter paper is 20% or more.
[0022]
水性 Water resistance test≫
The tensile strength in the normal state and the tensile strength after immersion in water of the nonwoven fabric obtained in the hand test are measured, and the retention is calculated.
Tensile strength under normal conditions: A test piece having a width of 50 mm was left in a constant temperature room at 20 ° C. and 65% RH for 16 hours or more, and then gripped with an autograph manufactured by Shimadzu Corporation at a width of 100 mm and a pulling speed of 200 mm / min. Measure with (Unit kgf / 50mm)
Tensile strength after immersion in water: A test piece having a width of 50 mm is immersed in water at 20 ° C. for 1 hour, and the other parts are measured similarly. (Unit kgf / 50mm)
Retention: normal strength / strength after immersion in water x 100 (unit%)
The evaluation retention rate is 15% or more.
Retention rate is less than 15% .... ×
The test results are shown in the table.
[0023]
[Table 1]
Figure 0003553653
[0024]
Comparative Example 1 had a small particle size and was poor in texture and mimigration resistance.
Comparative Examples 2 and 4 could not be tested because they did not aggregate into an emulsion.
In Comparative Example 3, the hand and the migration resistance were good, but the copolymerization ratio of vinyl acetate was high, the water resistance was poor, and the odor of acetic acid was found.
[0025]
【The invention's effect】
According to the present invention, by using an acrylic emulsion having a particle diameter of 0.5 μm or more which is polymerized under specific polymerization conditions using a specific amount of protective colloid, an excellent effect is obtained in which the feeling is good and migration does not occur.

Claims (4)

アクリル系単量体と該単量体と共重合可能な単量体を、単量体に対し2〜10重量%の保護コロイドの存在下でレドックス系重合開始剤を用い、重合温度65℃以下で乳化重合して得た、粒子径1.0〜3.0μmのアクリル系エマルジョンを主剤とする繊維処理剤。An acrylic monomer and a monomer copolymerizable with the monomer are polymerized at a polymerization temperature of 65 ° C. or lower using a redox polymerization initiator in the presence of 2 to 10% by weight of a protective colloid based on the monomer. A fiber treating agent mainly composed of an acrylic emulsion having a particle diameter of 1.0 to 3.0 μm, obtained by emulsion polymerization in the above. アクリル系単量体と共重合する単量体として酢酸ビニルを全単量体の25重量%以下使用する、請求項1に記載された繊維処理剤。The fiber treating agent according to claim 1, wherein vinyl acetate is used as a monomer copolymerized with the acrylic monomer in an amount of 25% by weight or less based on all monomers. 保護コロイドがセルロースエーテル系および/またはポリビニルアルコール系である、請求項1または2に記載された繊維処理剤。3. The fiber treating agent according to claim 1, wherein the protective colloid is a cellulose ether type and / or a polyvinyl alcohol type. アクリル系単量体を全単量体の70〜99重量%使用した、請求項1ないし3のいずれか1項に記載された繊維処理剤。The fiber treating agent according to any one of claims 1 to 3, wherein the acrylic monomer is used in an amount of 70 to 99% by weight of the total monomer.
JP20410394A 1994-07-27 1994-07-27 Fiber treatment agent mainly composed of acrylic emulsion Expired - Fee Related JP3553653B2 (en)

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