JPH0621127B2 - Continuous production method of liquid-absorbent composite - Google Patents

Continuous production method of liquid-absorbent composite

Info

Publication number
JPH0621127B2
JPH0621127B2 JP61087674A JP8767486A JPH0621127B2 JP H0621127 B2 JPH0621127 B2 JP H0621127B2 JP 61087674 A JP61087674 A JP 61087674A JP 8767486 A JP8767486 A JP 8767486A JP H0621127 B2 JPH0621127 B2 JP H0621127B2
Authority
JP
Japan
Prior art keywords
liquid
water
polymer
absorbent composite
monomer
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
JP61087674A
Other languages
Japanese (ja)
Other versions
JPS62243612A (en
Inventor
隆俊 小林
久記 渡辺
明 櫻井
稔 中西
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.)
Kao Corp
Original Assignee
Kao Corp
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Filing date
Publication date
Application filed by Kao Corp filed Critical Kao Corp
Priority to JP61087674A priority Critical patent/JPH0621127B2/en
Publication of JPS62243612A publication Critical patent/JPS62243612A/en
Publication of JPH0621127B2 publication Critical patent/JPH0621127B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Treatments Of Macromolecular Shaped Articles (AREA)
  • Polymerisation Methods In General (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、繊維基材と吸液性ポリマーとの複合体の連続
的製造方法に関するものであり、更に詳しくは、ポリマ
ーの脱落がなく、自由な形状をとらせることが可能な吸
液性複合体の連続的製造方法に関するものであり、本発
明の吸液性複合体は、生理用ナプキン、使いすておむ
つ、包帯などの衛生・医療用品、並びに野菜などの鮮度
保持材、保水材などの農林業分野や土木業分野等、吸液
及び吸液した液体の保持が必要とされる用途に好適に利
用できる。
TECHNICAL FIELD The present invention relates to a continuous method for producing a composite of a fiber base material and a liquid-absorbent polymer, and more specifically, there is no loss of the polymer, The present invention relates to a continuous method for producing an absorbent composite capable of having a free shape, and the absorbent composite of the present invention is a sanitary napkin, disposable diaper, bandage, etc. It can be suitably used for applications, such as freshness-retaining materials such as vegetables, water-retaining materials such as agricultural and forestry fields, civil engineering fields, and the like, which require liquid absorption and liquid retention.

〔従来の技術およびその問題点〕[Conventional technology and its problems]

近年、自重の数十倍から数百倍の水を吸収するいわゆる
吸水性ポリマーが開発され、生理用ナプキンや紙おむつ
等の衛生用品をはじめとして農林業分野、土木業分野等
の保水、吸水材料に利用されている。
In recent years, so-called water-absorbent polymers that absorb several tens to several hundreds of times their own weight of water have been developed, and are used as water-retaining and water-absorbing materials in the fields of agriculture and forestry, civil engineering, etc. It's being used.

用いられている吸水性ポリマーとしては、一般的に顆粒
状のものであり、その形態が顆粒状であるがゆえに、実
使用する場合の多くは紙とのサンドイッチ、パルプに混
入させてエンボス加工等の圧着処理、あるいは熱可塑性
樹脂等による溶封等の複合化を行い、シート状やフィル
ム状等の形状に変えて用いられている。しかしながらこ
れらの複合化方法によってもポリマーの脱落はまぬがれ
得ない。比較的ポリマーの脱落の少ない溶封による複合
化ではポリマーのまわりが熱可塑性樹脂でコーティング
されており、水等の液と接触をさまたげる結果となり、
従って吸収性能を著しく低下させてしまう欠点がある。
The water-absorbent polymer used is generally in the form of granules, and because of its granular form, it is often used in sandwiches with paper, embossed by mixing it with pulp, etc. It is used by being changed into a sheet shape, a film shape, or the like by performing a pressure bonding treatment or a compounding such as fusion sealing with a thermoplastic resin or the like. However, even with these compounding methods, the loss of the polymer cannot be avoided. In the case of complexing by fusion sealing with relatively little loss of polymer, the periphery of the polymer is coated with a thermoplastic resin, which results in blocking contact with liquid such as water,
Therefore, there is a drawback that the absorption performance is significantly reduced.

これらの欠点を改良すべくポリマーの脱落のない吸収性
物品の提案が数多くなされており、フィルム状、繊維状
等のものが提示されている。フィルム状では表面積が小
さく吸収速度に劣るとともに、面として存在するため吸
収性物品の柔軟性を制約する。一方、繊維状では柔軟性
を満足できても膨潤時のゲル強度が弱い欠点があり、必
ずしも吸収性能が良好でポリマーの脱落のない吸収性物
品が得られているとは言い難い。
In order to improve these drawbacks, many proposals have been made for absorbent articles in which the polymer does not fall off, and film-like, fiber-like and the like have been proposed. In the case of a film, the surface area is small and the absorption rate is poor, and since it exists as a surface, it limits the flexibility of the absorbent article. On the other hand, in the fibrous form, there is a drawback that the gel strength at the time of swelling is weak even though the flexibility is satisfied, and it is hard to say that an absorbent article having a good absorption performance and no polymer falling off is obtained.

更にこれらを改良すべく、繊維状基材に吸水性ポリマー
に転換しうる水溶性のモノマーを含浸、吹きつけ等の手
法を用いて塗工し、熱や電磁放射線にて重合する方法が
提案されている。(特開昭60−149609、特開昭59−2049
75、特実昭57−500546)。これらの技術によりポリマー
の脱落は防止できるものの、吸液性能としては、従来の
顆粒状のものに比較して著しく低下するものであり、吸
液性にすぐれ、ポリマーの脱落のないものの出現が望ま
れている。
In order to further improve these, a method of impregnating a fibrous base material with a water-soluble monomer that can be converted into a water-absorbent polymer, coating using a technique such as spraying, and polymerizing with heat or electromagnetic radiation has been proposed. ing. (JP-A-60-149609, JP-A-59-2049
75, Tokushi Sho 57-500546). Although these techniques can prevent the polymer from falling off, the liquid-absorbing performance is significantly lower than that of the conventional granular ones, and it is expected that a polymer having excellent liquid-absorbing property and no polymer falling off will appear. It is rare.

〔問題点を解決するための手段〕[Means for solving problems]

本発明者らは、上記の状況のもとで、吸液性に優れ、ポ
リマーの脱落のない吸液材について鋭意検討を重ねた結
果、長尺の繊維状基材に、水溶性のエチレン性不飽和モ
ノマー、ラジカル重合開始剤及び水溶性の架橋剤を含む
水溶液を付着させ、特定の雰囲気下を連続的に通過させ
てモノマーを重合させることにより、吸液性に優れ、か
つ液体によって膨潤した際にもポリマーの脱落がなく、
風合いの良好な吸液性複合体が効率的に得られることを
見出し、本発明を完成した。
Under the circumstances described above, the inventors of the present invention have conducted extensive studies on a liquid-absorbent material that is excellent in liquid-absorbing property and does not drop out of the polymer. An aqueous solution containing an unsaturated monomer, a radical polymerization initiator and a water-soluble cross-linking agent was attached, and the monomer was polymerized by continuously passing it under a specific atmosphere, resulting in excellent liquid absorption and swelling with a liquid. Even when the polymer does not fall off,
The present invention was completed by finding that an absorbent composite having a good texture can be efficiently obtained.

即ち、本発明は、水溶性のエチレン性不飽和モノマー、
ラジカル重合開始剤及び水溶性の架橋剤を含有する水溶
液を塗布した少なくとも一部が疎水性繊維で構成されて
いる長尺の繊維状基材を重合不活性で、温度80℃以上で
かつ相対湿度(以下、湿度と略)40%以上の雰囲気のゾ
ーンを連続的に通過させてモノマーを重合せしめて吸液
性を有するポリマーに転換させ、その後乾燥させること
を特徴とする吸液性複合体の連続的製造方法を提供する
ものである。
That is, the present invention is a water-soluble ethylenically unsaturated monomer,
A long fibrous base material, at least a part of which is coated with an aqueous solution containing a radical polymerization initiator and a water-soluble cross-linking agent, is composed of hydrophobic fibers. (Hereinafter, abbreviated as "humidity") is continuously passed through a zone having an atmosphere of 40% or more to polymerize a monomer to convert it into a polymer having a liquid absorbing property, and then to dry the polymer. It is intended to provide a continuous manufacturing method.

本発明に於いて使用される水溶性のエチレン性不飽和モ
ノマーとしては、一般に吸液性を有するポリマーに転換
しうるものであればいずれでも良い。このような性能を
与える水溶性のモノマーとしては、官能基としてカルボ
ン酸又は/及びその塩、リン酸又は/及びその塩、スル
ホン酸又は/及び塩やヒドロキシル基、アミド基を有す
るエチレン性不飽和モノマーが挙げられる。例えば(メ
タ)アクリル酸(塩)、イタコン酸(塩)、ビニルスル
ホン酸(塩)、ビニルホスホン酸(塩)、ポリエチレン
グリコール(メタ)アクリレート、アクリルアミド等を
挙げることができる。これらは単独又は2種以上の併用
も可能であり、被吸液の性状により選択できる。好まし
くはカルボン酸(塩)官能基を有する水溶性のエチレン
性不飽和モノマーであり、更に好ましくは、アクリル酸
及び/又はその塩である。
The water-soluble ethylenically unsaturated monomer used in the present invention may be any one as long as it can be converted into a polymer having liquid absorbability. Examples of the water-soluble monomer that gives such performance include a carboxylic acid or / and a salt thereof, a phosphoric acid or / and a salt thereof, a sulfonic acid or / and a salt, a hydroxyl group or an ethylenic unsaturated group having a amide group as a functional group. Examples include monomers. For example, (meth) acrylic acid (salt), itaconic acid (salt), vinylsulfonic acid (salt), vinylphosphonic acid (salt), polyethylene glycol (meth) acrylate, acrylamide and the like can be mentioned. These can be used alone or in combination of two or more, and can be selected depending on the properties of the liquid to be absorbed. A water-soluble ethylenically unsaturated monomer having a carboxylic acid (salt) functional group is preferable, and acrylic acid and / or a salt thereof is more preferable.

水溶性ラジカル重合開始剤としては、例えば過酸化物、
ハイドロパーオキシド、あるいはアゾ化合物等が既知の
量で用いられる。これらの重合開始剤は、2種以上を混
合して使用することも可能であり、更には、クロムイオ
ン、亜硫酸塩、ヒドロキシルアミン、ヒドラジン等を加
えてレドックス系重合開始剤として使用することも可能
である。
Examples of the water-soluble radical polymerization initiator include peroxides,
Hydroperoxide, an azo compound or the like is used in a known amount. These polymerization initiators can be used as a mixture of two or more kinds, and can also be used as a redox polymerization initiator by adding chromium ion, sulfite, hydroxylamine, hydrazine and the like. Is.

本発明に於いて使用される架橋剤としてはメチレンビス
アクリルアミドやエチレングリコールジアクリレート、
ポリエチレングリコールジ(メタ)アクリレート、ポリ
グリセロールポリ(メタ)アクリレート等の多官能の水
溶性エチレン性不飽和モノマーや、エチレングリコール
ジグリシジルエーテル、ポリエチレングリコールジグリ
シジルエーテル、ソルビトールポリグリシジルエーテ
ル、ポリグリセロールポリグリシジルエーテル等のポリ
グリシジルエーテル、グリセリンやペンタエリスリトー
ル等のポリオール及びエチレンジアミン、ポリエチレン
イミン等のポリアミン類等が好適に使用しうる。一般的
にその添加量はモノマー 100重量部に対し0.01〜10重量
部であり、10重量部を越えると架橋密度が大きくなりす
ぎ吸液量は低下してしまう。又、0.01重量部未満では架
橋の効果を十分に発現できない。
As the cross-linking agent used in the present invention, methylene bis acrylamide or ethylene glycol diacrylate,
Polyfunctional water-soluble ethylenically unsaturated monomers such as polyethylene glycol di (meth) acrylate, polyglycerol poly (meth) acrylate, ethylene glycol diglycidyl ether, polyethylene glycol diglycidyl ether, sorbitol polyglycidyl ether, polyglycerol polyglycidyl Polyglycidyl ethers such as ethers, polyols such as glycerin and pentaerythritol, and polyamines such as ethylenediamine and polyethyleneimine can be preferably used. Generally, the addition amount is 0.01 to 10 parts by weight with respect to 100 parts by weight of the monomer, and if it exceeds 10 parts by weight, the crosslinking density becomes too high and the liquid absorption amount decreases. Further, if it is less than 0.01 part by weight, the effect of crosslinking cannot be sufficiently exhibited.

本発明では、更に、タルク、クレー、珪藻土等の粉砕し
たフィラーを添加剤として加えることもできる。
In the present invention, a crushed filler such as talc, clay or diatomaceous earth may be further added as an additive.

本発明において上述のモノマー水溶液を付着する長尺の
繊維状基材は、その少なくとも一部に疎水性繊維部を有
することが必要である。
In the present invention, the long fibrous base material to which the aqueous monomer solution is attached needs to have a hydrophobic fiber portion in at least a part thereof.

繊維状基材ウェブに疎水性繊維を混ぜることにより繊維
状基材が疎水性を示し、モノマー水溶液を繊維状基材に
塗布した場合、繊維が疎水性であるがゆえに、水の表面
張力も手伝って、繊維基材上に不連続にモノマー水溶液
が付着した状態を作ることが可能となる。このような形
態にし得る繊維状基材としては、疎水性繊維を5重量%
以上含有するものであればよい。
By mixing hydrophobic fibers into the fibrous base material web, the fibrous base material exhibits hydrophobicity. When the aqueous monomer solution is applied to the fibrous base material, the surface tension of water is also helped because the fibers are hydrophobic. Thus, it becomes possible to make a state in which the aqueous monomer solution is discontinuously attached on the fiber base material. As a fibrous base material capable of having such a form, 5% by weight of hydrophobic fiber is used.
What is necessary is just to contain the above.

用いられる疎水性繊維としては、ポリエステル、ポリプ
ロピレン、ポリエチレン−ポリプロピレン複合繊維等が
挙げられ、これら疎水性繊維が主体となるものが良い。
又、上記疎水性繊維以外でもレーヨン等の親水性繊維の
表面をロジン系あるいはアルキルケテンダイマー系のサ
イズ剤やカチオン系の界面活性剤等で疎水化させたもの
でも良い。
Examples of the hydrophobic fiber used include polyester, polypropylene, polyethylene-polypropylene composite fiber, and the like, and those having these hydrophobic fibers as a main component are preferable.
In addition to the above hydrophobic fibers, the surface of hydrophilic fibers such as rayon may be hydrophobized with a rosin-based or alkyl ketene dimer-based sizing agent or a cationic surfactant.

上記のような形態とした繊維状基材の上にモノマー水溶
液を塗布し、次いで重合させることにより、ポリマーが
膨潤した時でさえ、繊維状基材からのポリマーの脱落が
ほとんどない吸液性複合体が得られる。不連続に繊維状
基材上にポリマーが分布することはポリマーの質量当た
りの表面積も大きくなり、更には繊維間に面状のポリマ
ーが連続的に存在しないことより、吸液性物品としてポ
リマーの吸液性を十分に発揮せしめることが可能とな
り、それだけ高い吸液性を与えることが可能である。
By applying an aqueous monomer solution onto the fibrous base material in the above-mentioned form and then polymerizing it, there is almost no drop-off of the polymer from the fibrous base material even when the polymer swells. The body is obtained. The discontinuous distribution of the polymer on the fibrous base material also increases the surface area per mass of the polymer, and further, since the planar polymer does not continuously exist between the fibers, the polymer can be used as a liquid-absorbent article. It becomes possible to fully exert liquid absorbency, and it is possible to give high liquid absorbability.

モノマー水溶液を繊維状基材に塗布する方法としては、
例えばスクリーン印刷、グラビア印刷等の公知の印刷方
法や、スプレーを用いての噴霧や吹き付け等の方法で可
能である。塗布の効率を高めるために重合不活性な粘度
調整剤や起泡剤の使用も可能である。又、吸水性複合体
に使用時に適したパターン印刷を施しても良い。
As a method of applying the aqueous monomer solution to the fibrous base material,
For example, it is possible to use a known printing method such as screen printing or gravure printing, or a method such as spraying or spraying using a spray. It is also possible to use a polymerization-inert viscosity adjusting agent or a foaming agent in order to enhance the coating efficiency. Further, the water absorbent composite may be subjected to pattern printing suitable for use.

生産性向上のためには、スクリーン印刷、グラビア印刷
などの印刷方式や、含浸方式が望ましい。製品の風合、
感触などの面から特に好ましいのは、スクリーン印刷、
グラビア印刷などの印刷方式である。
In order to improve productivity, a printing method such as screen printing or gravure printing or an impregnation method is desirable. Product texture,
From the aspects of feel and the like, screen printing,
It is a printing method such as gravure printing.

このようにしてモノマー、ラジカル重合開始剤及び水溶
性の架橋剤を含んだモノマー水溶液の付着した繊維状基
材を連続的に重合するにあたり、本発明では加湿の条件
を必須としている。即ち、重合反応を遅滞なく進行さ
せ、しかも吸液物性の優れた吸液体を得るため、重合反
応を阻害しない重合不活性な雰囲気にしておくこと及び
モノマー水溶液の水分揮散を抑制するため加湿状態にし
ておくことが必要である。
In order to continuously polymerize the fibrous base material to which the aqueous monomer solution containing the monomer, the radical polymerization initiator and the water-soluble crosslinking agent is thus polymerized, the humidifying condition is essential in the present invention. That is, the polymerization reaction is allowed to proceed without delay, and in order to obtain a liquid absorbent having excellent liquid absorption properties, a polymerization inactive atmosphere that does not inhibit the polymerization reaction is kept, and a humidified state is set to suppress evaporation of water in the monomer aqueous solution. It is necessary to keep it.

重合温度はラジカル重合開始剤の種類及び量、モノマー
の種類によっても異なるが、生産性の点より、高い温度
ですばやく重合を完結することが望まれる。したがっ
て、80℃以上で重合を行うことが望ましい。温度が80℃
より低いと、生産性が悪く、又、吸液体としての製品の
性能が充分でなく、本発明の意図するところではない。
The polymerization temperature varies depending on the type and amount of radical polymerization initiator and the type of monomer, but from the viewpoint of productivity, it is desired to complete the polymerization rapidly at a high temperature. Therefore, it is desirable to carry out the polymerization at 80 ° C or higher. Temperature is 80 ℃
If it is lower, the productivity is poor, and the performance of the product as a liquid absorbent is not sufficient, which is not the intention of the present invention.

しかしながら、重合温度を上昇させると水溶性の水分が
揮散して重合の完結阻害及び吸液物性の低下を招き好ま
しくない。
However, when the polymerization temperature is raised, water-soluble water is volatilized, which hinders the completion of the polymerization and deteriorates the liquid absorbing properties, which is not preferable.

本発明においては、モノマー水溶液を、加湿下に重合せ
しめることを特徴としていることは先に述べた。加湿の
条件は、モノマーの重合時間、重合温度により異なる
が、温度80℃以上でかつ湿度40%以上の加湿状態である
ことが必要である。湿度が40%より低くなると、重合中
にモノマー水溶液の水分が揮散してしまい、吸液体とし
て満足の得られるものでなく、本発明の意図するところ
ではない。
As described above, the present invention is characterized in that the aqueous monomer solution is polymerized under humidification. Humidification conditions differ depending on the polymerization time and polymerization temperature of the monomer, but it is necessary that the temperature is 80 ° C. or higher and the humidity is 40% or higher. If the humidity is lower than 40%, the water content of the monomer aqueous solution is volatilized during the polymerization, which is not satisfactory as a liquid absorbing material, which is beyond the scope of the present invention.

このようにして得られた含水状態の吸液性複合体を乾燥
して、最終吸液体にするが、その乾燥方法として、熱
風、マイクロ波、赤外線等の手段が挙げられる。
The thus obtained water-absorptive liquid-absorbent composite is dried to obtain the final liquid-absorption, and the drying method thereof includes means such as hot air, microwaves, and infrared rays.

又、乾燥前に吸液性の改良として、疎水性繊維の被吸液
物とのぬれを向上すべく、改質剤を塗布することも望ま
しい。改良剤としては非イオン活性剤等が例示できる。
It is also desirable to apply a modifier before drying to improve wettability of the hydrophobic fiber with the substance to be absorbed before drying. Examples of the improving agent include nonionic activators.

最終吸液性複合体は用途に応じ、任意に切断するか或い
はロール状にまきとる。
The final liquid-absorbent composite is optionally cut or rolled into a roll according to the application.

このようにして得られた吸液性複合体は、吸液性に優
れ、且つ、風合良好なものであるばかりでなく、ポリマ
ーの脱落もなく、自由な形態とすることが可能である。
しかも、更に、連続して製造されるので、生産性も良
く、コスト的にもメリットがあり、吸液性ポリマーの使
用範囲を大きく拡大できるものである。
The liquid-absorbent composite thus obtained is not only excellent in liquid-absorbing property and having a good texture, but also can be formed into a free form without the polymer falling off.
In addition, since it is manufactured continuously, it has good productivity and is advantageous in terms of cost, and the range of use of the liquid-absorbent polymer can be greatly expanded.

〔実施例〕〔Example〕

以下に、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、これらの実施例のみに限定される
ものではない。
Hereinafter, the present invention will be specifically described with reference to Examples and Comparative Examples, but the present invention is not limited to these Examples.

なお、飽和吸収量、吸収速度、ポリマー脱落性は、下記
の方法にて評価した。
The saturated absorption amount, absorption rate, and polymer dropout property were evaluated by the following methods.

(1) 飽和吸収量 乾燥した吸液性複合体を十分な量の生理食塩水に浸漬
し、1時間放置した。その後80メッシュの金網で水滴が
落ちなくなるまで放置し、重量を測定した。同様の操作
をポリマーのない同一面積の基材で行い重量を測定し
た。これらより以下に示す式によりポリマーの吸収量を
求めた。
(1) Saturated absorption amount The dried liquid-absorbent composite was immersed in a sufficient amount of physiological saline and left for 1 hour. After that, it was left to stand with a 80-mesh wire mesh until water drops did not drop, and the weight was measured. The same operation was performed on a substrate having the same area without polymer to measure the weight. From these, the absorption amount of the polymer was determined by the formula shown below.

W :ポリマーの付着量(g) W1:吸液後の吸収性物品の重量(g) W0:吸収後の基材の重量(g) (2) 吸収速度 乾燥した吸液性複合体を十分な量の生理食塩水に3分間
浸漬し、その後直ちに吸引濾過し、繊維間並びに粒子間
に含まれる間隙水を分離し、重量を測定した。
W: Adhesion amount of polymer (g) W 1 : Weight of absorbent article after liquid absorption (g) W 0 : Weight of substrate after absorption (g) (2) Absorption rate A dried liquid-absorbent composite The sample was immersed in a sufficient amount of physiological saline for 3 minutes, and immediately thereafter, suction filtration was performed to separate interstitial water contained between fibers and particles and weighed.

同様の操作をポリマーのない同一面積の基材で行い重量
を測定した。これらより以下に示す式によりポリマーの
吸収速度とした。
The same operation was performed on a substrate having the same area without polymer to measure the weight. From these, the absorption rate of the polymer was defined by the following formula.

W′:ポリマーの付着量(g) W1′:吸水した後の吸液性複合体の重量(g) W0′:吸収した後の基材の重量(g) (3) ポリマーの脱落 サンプルを多量の生理食塩水中に投じ、ポリマーを十分
に膨潤させた後、5分間撹拌を行い、その後基材から脱
落したポリマーの重量を測定し、下式により脱落量を算
出した。
W ′: Adhesion amount of polymer (g) W 1 ′: Weight of liquid-absorbent composite after absorbing water (g) W 0 ′: Weight of base material after absorbing (g) (3) Polymer falling sample Was poured into a large amount of physiological saline to sufficiently swell the polymer, followed by stirring for 5 minutes, and then the weight of the polymer dropped from the substrate was measured, and the drop amount was calculated by the following formula.

実施例1,2 固形分40重量%の中和度70モル%のアクリル酸ソーダ水
溶液を調整し、このモノマー水溶液に過硫酸ナトリウム
を1重量%(対アクリル酸ソーダモノマー)及びポリエ
チレングリコールジアクリレート(平均オキシエチテン
鎖14モル、商品名NKエステルA−600 新中村化学(株)
製)を750 ppm(対アクリル酸ソーダモノマー)均一に
溶解し、この後、窒素ガスを吹き込み、水溶液中の溶存
酸素を除去した。
Examples 1 and 2 An aqueous solution of sodium acrylate having a solid content of 40% by weight and a degree of neutralization of 70 mol% was prepared, and 1% by weight of sodium persulfate (to sodium acrylate monomer) and polyethylene glycol diacrylate ( Average oxyethene chain 14 mol, trade name NK ester A-600 Shin-Nakamura Chemical Co., Ltd.
(Manufactured by Mitsui Chemical Co., Ltd.) was uniformly dissolved in 750 ppm (sodium acrylate monomer), and then nitrogen gas was blown in to remove dissolved oxygen in the aqueous solution.

長尺のロールにまいた坪量が45g/m2のポリエチレン−ポ
リプロピレンの複合繊維(ES繊維)のみからなる疎水性
繊維ウェブ(実施例1)、等重量のポリエチレン−ポリ
プロピレンの複合繊維(ES繊維)及びレーヨンからなる
繊維ウェブ(実施例2)の上に上記水溶液を第1図に示
す装置を用い、塗布、重合、乾燥を連続的に行い、吸液
性複合体を得た。塗工はウェブの上にそれぞれ、グラビ
ア印刷機(水玉模様の版)で150g/m2となるように塗布
した。重合は100 ℃、65%RH、重合ゾーン滞留時間2分
で行った。加湿は重合ゾーンに蒸気をふき込む方法によ
り行われ、調湿センサーにより湿度を制御した。乾燥は
120度、熱風にて行った。塗工ゾーン(5)及び重合ゾ
ーン(6)は窒素ガスを吹き込み、不活性ガス雰囲気と
し、又、この時のラインスピードは2m/分であった。
Hydrophobic fiber web (Example 1) consisting of polyethylene-polypropylene composite fibers (ES fiber) having a basis weight of 45 g / m 2 spread on a long roll (Example 1), equal weight of polyethylene-polypropylene composite fibers (ES fiber) ) And rayon (Example 2), the above aqueous solution was continuously applied, polymerized and dried using the apparatus shown in FIG. 1 to obtain a liquid-absorbent composite. The coating was applied on the web by a gravure printing machine (a polka dot plate) at 150 g / m 2 . The polymerization was carried out at 100 ° C., 65% RH, and the residence time in the polymerization zone was 2 minutes. Humidification was performed by a method of blowing steam into the polymerization zone, and humidity was controlled by a humidity control sensor. Drying was performed with hot air at 120 degrees. Nitrogen gas was blown into the coating zone (5) and the polymerization zone (6) to make it an inert gas atmosphere, and the line speed at this time was 2 m / min.

実施例3 実施例1に準じて行った。但し、モノマー水溶液を複合
繊維に付着する方法として、塗工ゾーン内のグラビア印
刷機に代わり、スクリーン印刷手法を用い、上記溶液を
100g/m2塗工し、実施例1に準じ重合した。この時のラ
インスピードは10m/分であり、重合ゾーン滞留時間1分
であった。乾燥は熱風に代わり、マイクロ波にて行い、
連続的に吸液性複合体を得た。
Example 3 It carried out according to Example 1. However, as a method of attaching the aqueous monomer solution to the composite fiber, a screen printing method is used instead of the gravure printing machine in the coating zone, and the above solution is used.
It was coated at 100 g / m 2 and polymerized according to Example 1. The line speed at this time was 10 m / min, and the residence time in the polymerization zone was 1 minute. Drying is performed by microwave instead of hot air,
A liquid-absorbent composite was continuously obtained.

実施例4 実施例1に準じて行った。但し、アクリル酸ソーダの代
わりに 100モル%中和された固形分20重量%のビニルホ
スホン酸ソーダを用いる以外実施例1と同様、連続的に
吸液性複合体を得た。
Example 4 It carried out according to Example 1. However, a liquid-absorbent composite was continuously obtained in the same manner as in Example 1 except that 100 mol% neutralized sodium vinylphosphonate having a solid content of 20% by weight was used instead of sodium acrylate.

実施例5 実施例1に準じて行った。但し、ポリエチレングリコー
ルジアクリレート(平均オキシエチレン鎖14モル、商品
名NKエステルA−600 新中村化学(株)製)に代わり、メ
チレンビスアクリルアミドを500ppm(対モノマー)用い
る以外実施例1と同様に連続的に吸液性複合体を得た。
Example 5 It carried out according to Example 1. However, polyethylene glycol diacrylate (average oxyethylene chain 14 mol, trade name NK ester A-600 manufactured by Shin-Nakamura Chemical Co., Ltd.) was replaced with methylenebisacrylamide at 500 ppm (as a monomer) in the same manner as in Example 1. The liquid-absorbent composite was obtained.

実施例6 実施例2に準じて行った。但し、ポリエチレングリコー
ルジアクリレート(平均オキシエチレン鎖14モル、商品
名NKエステルA−600 新中村化学(株)製)を750ppm(対
モノマー)用い、90℃,100%湿度とし、実施例2と同
様、連続的に吸液性複合体を得た。
Example 6 It carried out according to Example 2. However, polyethylene glycol diacrylate (average oxyethylene chain 14 mol, trade name NK ester A-600 manufactured by Shin-Nakamura Chemical Co., Ltd.) was used at 750 ppm (against monomer) at 90 ° C. and 100% humidity, and the same as Example 2. Then, the liquid-absorbent composite was continuously obtained.

比較例1,2 実施例1に準じて行った。但し、重合時、90℃の温度で
10%湿度(比較例1)、120 ℃で加湿なし(比較例2)
で重合を行う以外は実施例1と同様に連続的に吸液性複
合体を得た。
Comparative Examples 1 and 2 were carried out according to Example 1. However, at the temperature of 90 ° C during polymerization
10% humidity (Comparative Example 1), no humidification at 120 ° C (Comparative Example 2)
A liquid-absorbent composite was continuously obtained in the same manner as in Example 1 except that the polymerization was carried out.

得られた吸液性複合体について測定した結果を表1に示
す。
Table 1 shows the measurement results of the obtained liquid-absorbent composite.

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

第1図は本発明の製造方法の1例を示す略示図である。 1……巻出しロール、2……巻き取りロール 3……ガイドロール、4……ニップロール 5……塗工ゾーン、6……重合ゾーン 7……乾燥ゾーン、8……グラビアロール 9……バックロール、10……モノマー水溶液 FIG. 1 is a schematic view showing an example of the manufacturing method of the present invention. 1 ... Unwinding roll, 2 ... Winding roll 3 ... Guide roll, 4 ... Nip roll 5 ... Coating zone, 6 ... Polymerization zone, 7 ... Drying zone, 8 ... Gravure roll, 9 ... Back Roll, 10 ... Monomer aqueous solution

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】水溶性のエチレン性不飽和モノマー、ラジ
カル重合開始剤及び水溶性の架橋剤を含有する水溶液を
塗布した少なくとも一部が疎水性繊維で構成されている
長尺の繊維状基材を、重合不活性で、温度80℃以上でか
つ相対湿度40%以上に加湿した雰囲気のゾーンを連続的
に通過させてモノマーを重合せしめて吸液性を有するポ
リマーに転換させ、その後乾燥させることを特徴とする
吸液性複合体の連続的製造方法。
1. A long fibrous substrate coated with an aqueous solution containing a water-soluble ethylenically unsaturated monomer, a radical polymerization initiator and a water-soluble crosslinking agent, at least a part of which is composed of hydrophobic fibers. Is continuously passed through a zone of a polymerization-inert, humidified atmosphere at a temperature of 80 ° C or higher and a relative humidity of 40% or higher to polymerize the monomer to convert it into a liquid-absorbent polymer, and then dry it. A method for continuously producing a liquid-absorbent composite, comprising:
【請求項2】水溶性のエチレン性不飽和モノマーがアク
リル酸又はアクリル酸塩を主成分とするものである特許
請求の範囲第1項記載の吸液性複合体の連続的製造方
法。
2. The continuous method for producing a liquid-absorbent composite according to claim 1, wherein the water-soluble ethylenically unsaturated monomer has acrylic acid or an acrylic acid salt as a main component.
JP61087674A 1986-04-16 1986-04-16 Continuous production method of liquid-absorbent composite Expired - Fee Related JPH0621127B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61087674A JPH0621127B2 (en) 1986-04-16 1986-04-16 Continuous production method of liquid-absorbent composite

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61087674A JPH0621127B2 (en) 1986-04-16 1986-04-16 Continuous production method of liquid-absorbent composite

Publications (2)

Publication Number Publication Date
JPS62243612A JPS62243612A (en) 1987-10-24
JPH0621127B2 true JPH0621127B2 (en) 1994-03-23

Family

ID=13921489

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61087674A Expired - Fee Related JPH0621127B2 (en) 1986-04-16 1986-04-16 Continuous production method of liquid-absorbent composite

Country Status (1)

Country Link
JP (1) JPH0621127B2 (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA1314355C (en) * 1987-04-30 1993-03-09 Yoshio Irie Hydrophilic polymer and method for production thereof
JPH0678402B2 (en) * 1987-05-06 1994-10-05 三洋化成工業株式会社 Method for producing super absorbent composite
JP2642436B2 (en) * 1988-08-30 1997-08-20 三菱化学株式会社 Manufacturing method of water absorbent resin
CA2002016A1 (en) * 1988-11-21 1990-05-21 Koji Miyake Manufacturing method, continuous manufacturing method, product and manufacturing apparatus of absorbent composite
JPH0753949B2 (en) * 1988-11-21 1995-06-07 株式会社日本触媒 Method for producing water-absorbent composite and continuous production method

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5246199A (en) * 1975-08-05 1977-04-12 Seiren Co Ltd Modification of polyester fiber
JPS54155296A (en) * 1978-05-29 1979-12-07 Sanyo Chem Ind Ltd Preparation of water-soluble polymer
JPS5818481A (en) * 1981-07-22 1983-02-03 東レ株式会社 Treatment of polyester fiber
JPS60151381A (en) * 1984-01-17 1985-08-09 アロン化成株式会社 Continuous production of long water absorbable composite material
JPS6155202A (en) * 1984-08-25 1986-03-19 マルハ株式会社 Paper and cloth article provided with high water absorbability
JPH0689077B2 (en) * 1985-07-22 1994-11-09 ユニ・チャーム株式会社 Method for producing water-absorbent composite

Also Published As

Publication number Publication date
JPS62243612A (en) 1987-10-24

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