JPS6348337A - Production of composite water-absorptive plastic material - Google Patents

Production of composite water-absorptive plastic material

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Publication number
JPS6348337A
JPS6348337A JP19348286A JP19348286A JPS6348337A JP S6348337 A JPS6348337 A JP S6348337A JP 19348286 A JP19348286 A JP 19348286A JP 19348286 A JP19348286 A JP 19348286A JP S6348337 A JPS6348337 A JP S6348337A
Authority
JP
Japan
Prior art keywords
water
plastic material
finely powdered
copolymer
treated
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.)
Granted
Application number
JP19348286A
Other languages
Japanese (ja)
Other versions
JPH0680120B2 (en
Inventor
Masashi Watanabe
渡辺 正支
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.)
Sumitomo Chemical Co Ltd
Original Assignee
Sumitomo 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 Sumitomo Chemical Co Ltd filed Critical Sumitomo Chemical Co Ltd
Priority to JP61193482A priority Critical patent/JPH0680120B2/en
Publication of JPS6348337A publication Critical patent/JPS6348337A/en
Publication of JPH0680120B2 publication Critical patent/JPH0680120B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

PURPOSE:To obtain the titled composite material which is excellent in water absorptivity and water retentivity and can give nonblocking agricultural films, etc., by kneading a finely powdered highly water-absorptive resin treated with a surfactant with a plastic material. CONSTITUTION:A finely powdered highly water-absorptive resin (A) of a mean particles diameter <=100mu, comprising a vinyl acetate/acrylate copolymer sapondificate, etc., is treated with a e.g., a nonionic surfactant (B) in an A to B ratio of 90-10/10-90 by mechanical mixing in, e.g., a ball mill, and the obtained mixture is mixed with a powdery, particulate, palletized or similar plastic material (C) (e.g., low-density PE or ethylene/vinyl acetate copolymer). The resulting mixture is kneaded with rolls, a Banbury mixer, a vented twin- screw extruder or the like.

Description

【発明の詳細な説明】 〈産業上の利用分野〉 本発明は吸水性プラスチック複合材料の製造方法に関す
る0 〈従来の技術とその間pO点〉 従来より、プラスチック材料に微粉状高吸水性樹脂を分
散させ、吸水性を付与させた吸水性プラスチック複合材
料は数多く知られている0しかしながら、微粉状β高吸
水性樹脂は、元来、非常に吸湿性や吸水性が高いため、
これをそのままプラスチック材料中に混入しても良質の
複合材料としての吸水性を十分に付与させることがむす
がしかつ九〇 その原因は、該微粉状高吸水性樹脂がプラスチック材料
との混線中に2次凝集して粗大粒子(いわゆるプッ)を
生じたシ、水分の分散が不十分なため発泡現象を起こし
得られたグラスチック複合材料に「ピンホール」を生じ
たりするためである。寸た、混練時には大きな剪断エネ
ルギーが必要であシ、その結果生ずる発熱によって混練
物が分解を起こし、性能の但下を招いたシする。
[Detailed Description of the Invention] <Industrial Application Field> The present invention relates to a method for manufacturing a water-absorbing plastic composite material. There are many known water-absorbent plastic composite materials that have been given water-absorbing properties.
Even if this is mixed directly into plastic materials, it is difficult to impart sufficient water absorbency as a high-quality composite material. This is because secondary agglomeration occurs to produce coarse particles (so-called "puffs"), and insufficient water dispersion causes a foaming phenomenon, resulting in "pinholes" in the resulting glass composite material. Furthermore, a large amount of shearing energy is required during kneading, and the resulting heat generation causes the kneaded material to decompose, resulting in a decrease in performance.

本発明者らは、微粉状高吸水性樹脂をあらかじめ鉱物油
、可塑剤などと混合して使用することによシ取扱い中お
よび保管貯蔵中の吸湿や樹脂またはゴムとの混合中に生
じる飛散を防止する方法を提案した(特開昭60−84
860 ) 7バ、この方法によってもある程度は上記
の問題点を解決する。しかるにこの方法では十分な効果
が得られない場合もあった@又、エチレン−酢酸ビニ〃
共重合体をプラスチック材料として用いてfi!l業用
フィルムを作る場合では、この方法によっては!Iν膜
後のフィルムの経時的なプロッキングが大きく、農業用
フィルムとして使用できないとの間開点がある〇 本発明者らは、従来法の欠点を除くため種々検討の末、
あらかじめプラスチックと親和性が優れている界面活性
剤#=判駆計右各乎圧で処刑した微粉状高吸水性樹脂を
プラスチック材料に練込むことによって、該微粉状高吸
水性樹脂が均一に分散できることを見い出し本発明を完
成した。
The present inventors have discovered that by mixing finely powdered superabsorbent resin with mineral oil, plasticizer, etc. in advance, moisture absorption during handling and storage, and scattering that occurs during mixing with resin or rubber, can be prevented. proposed a method to prevent the
860) 7B. This method also solves the above problems to some extent. However, there were cases in which sufficient effects could not be obtained with this method.
Using copolymer as a plastic material, fi! When making industrial film, this method is the best! The blocking of the film after the Iν film is large over time, and there is a point where it cannot be used as an agricultural film.The present inventors have conducted various studies to eliminate the drawbacks of the conventional method.
A surfactant that has excellent affinity for plastics. By kneading the finely powdered superabsorbent resin that has been pre-treated under various pressures into the plastic material, the finely powdered superabsorbent resin is uniformly dispersed. They discovered what could be done and completed the present invention.

〈間開点を解決するための手段〉 本発明は、微粉状高吸水性樹脂を界面活性剤で処理した
後、プラスチック材料と混練する吸水性プブスチック複
合材料の製造方法である。
<Means for Solving the Interval Opening Point> The present invention is a method for producing a water-absorbing public plastic composite material in which a finely powdered super-absorbent resin is treated with a surfactant and then kneaded with a plastic material.

本発明に用いる微粉状高吸水性撲f1¥1(以下囚とす
る。)とは、通常用いられているもので、例えば酢酸と
二μm7クリμ酸エステル共重合体ケン化物、インブチ
レン−無水マレイン酸共重合体変成物の架橋体の塩、架
v!?構造を有するポリアクリル酸(塩)、H粉−アク
リル酸共重合体の塩、ポリエチレンオキサイドの変成物
等があげられる。しかしながら、吸水後のゲル強度が強
く、ゲルの腐敗がなく、また長期耐久性が必要であるこ
とよシ、酢酸ビニル−アクリル酸エステル共重合体ケン
化物またはイソブチレン−無水マレイン醜共重合体変成
物の架橋体の塩が好ましく使用される。これらの高吸水
性樹脂は自重の50〜1000倍の範囲の吸水能力を持
つものが使用でき、さらに100〜500倍のものが吸
水後のゲル強度が仕半−強くより好ましい0また、該微
粉状高吸水性樹脂の粒径は最終吸水性プラスチック複合
品の物性等の特性面から粒子ができるだけ細かいことが
好ましく、平均粒径は100μ以下、特に好ましくは1
0μ以下であることが望ましい。
The finely powdered super absorbent powder f1 ¥1 (hereinafter referred to as "container") used in the present invention is commonly used, such as a saponified product of acetic acid and 2 μm 7 chloride acid ester copolymer, imbutylene-anhydrous Salt of cross-linked product of modified maleic acid copolymer, cross-v! ? Examples include polyacrylic acid (salt) having a structure, a salt of H powder-acrylic acid copolymer, and a modified product of polyethylene oxide. However, since it is necessary to have strong gel strength after water absorption, no gel decay, and long-term durability, saponified vinyl acetate-acrylic acid ester copolymer or modified isobutylene-maleic anhydride copolymer is required. A salt of a crosslinked product of is preferably used. These superabsorbent resins can have a water absorption capacity of 50 to 1000 times their own weight, and those having a water absorption capacity of 100 to 500 times their own weight are more preferable because the gel strength after water absorption is comparable to that of the fine powder. The particle size of the shaped super absorbent resin is preferably as fine as possible from the viewpoint of physical properties of the final water absorbent plastic composite product, and the average particle size is 100μ or less, particularly preferably 1.
It is desirable that it is 0μ or less.

また、本発明に用いる界面活性剤(以下(B)とする。Further, a surfactant (hereinafter referred to as (B)) used in the present invention.

)とは、通常用いられているものであり、アニオン系、
カチオン系、ノニオン系、両性のものが使用でき、 a
Jまたは二種以上を組み合わせて使用できる。具体的に
は、ポリオキシエチレンアルキルエーテル類、ポリオキ
シエチレンア〃キルアリーμエーテル類、ポリオキシエ
チレンアルキルエステル類、ソpビタンアルキルエステ
/L’類、ソルビタン酸脂肪酸エステル類、ポリオキシ
エチレンソルビタンエーテ〃−アルキルエステル類、グ
リセリン、ペンタエリスリ)−/L’、)!Jメチロー
yプロパン、糖類等の多価アルコールのアルキルエステ
ル類、同ポリオキシエチレン誘導体、ポリオキシエチレ
ンアルキルアミド類、フッ素界面活性剤、ンリコーン系
界面活性剤等があげられる0 特に、高吸水性樹脂の吸水能等の低下を抑えるにはノニ
オン系の界面活性剤が好ましく、特にソルビタン酸脂肪
酸エステ/L’類は囚との親和性がよく、少量で効果を
発揮するので好ましい0また、吸水性プラスチック複合
体のマトリックスとしてのプラスチック材料は熱硬化性
、熱可塑性のいずれでもよく、また軟質、硬質もしくは
発泡体であってもよく、合成ゴムなどのエフストマーで
あっても何等の支障もないが、特に、ポリエチレン、エ
チレン−rh酸ビニル共重合゛体、もしくはそのケン化
物、塩素化ポリエチレン、塩素化ポリプレン、スル・ホ
ン化ホ゛リエチレン、エチレン−イソブチレン共重合体
、エチレン−アクリル酸共重合体、ポリ塩化ビニルもし
くはその共重合体、スチレン−イソプレン−スチレンブ
ロック共重合体、スチレンーブタジエンースチレンブロ
ック共重合体、天然ゴム、クロロプレンゴム、イソプt
/ンゴムが好ましい〇又(4)と(B)の使用光の割合
は、それぞれの用途によって異なシ限定することができ
ないが、好ましくはAふB=90/10〜10/90の
範囲がよい。
) are commonly used, anionic,
Cationic, nonionic, and amphoteric types can be used.
J or a combination of two or more types can be used. Specifically, polyoxyethylene alkyl ethers, polyoxyethylene aryl μ ethers, polyoxyethylene alkyl esters, sobitan alkyl esters/L's, sorbitanic acid fatty acid esters, polyoxyethylene sorbitan ethers, 〃-alkyl esters, glycerin, pentaerythri)-/L',)! Examples include J Methyl-propane, alkyl esters of polyhydric alcohols such as sugars, polyoxyethylene derivatives, polyoxyethylene alkylamides, fluorine surfactants, phosphoricone surfactants, etc. Especially, super absorbent resins. Nonionic surfactants are preferable in order to suppress the decrease in water absorption capacity, etc., and sorbitan acid fatty acid esters/L's are particularly preferable because they have good affinity with particles and are effective with a small amount. The plastic material used as the matrix of the plastic composite may be either thermosetting or thermoplastic, and may be soft, hard, or foamed, and may be made of synthetic rubber or other efstomer without any problem. In particular, polyethylene, ethylene-rh vinyl acid copolymer or saponified product thereof, chlorinated polyethylene, chlorinated polyprene, sulfonated polyethylene, ethylene-isobutylene copolymer, ethylene-acrylic acid copolymer, polychloride Vinyl or its copolymer, styrene-isoprene-styrene block copolymer, styrene-butadiene-styrene block copolymer, natural rubber, chloroprene rubber, isopt
/ rubber is preferable 〇Also, the ratio of light used in (4) and (B) varies depending on the respective use and cannot be limited, but it is preferably in the range of AfB = 90/10 to 10/90. .

なお、吸水性の高いプラスチック材料を得るには、(3
)の混合割合を多く使用することが必須である。
In addition, in order to obtain a plastic material with high water absorption, (3
) is essential.

本発明において、囚をCB+で処理する方法としては通
常用いられているライカイ器、ヒーターつきプレンダー
、ボール・ミル、ミキサー等に囚と(B)を入れ機械的
に混合する方法、あるいは、トルエン、酢酸エチル等の
適当な溶剤の共存下で混合した後活剤を加p5除去する
方法等があげられるが、囚が(B)で十分被覆されるよ
うな条件で行なうことが好ましい。
In the present invention, the method of treating the congeal with CB+ is a method of mechanically mixing the convict and (B) in a commonly used laika, blender with heater, ball mill, mixer, etc., or toluene, Examples include a method of mixing in the presence of a suitable solvent such as ethyl acetate and then adding an activating agent to remove P5, but it is preferable to carry out the process under conditions such that the particles are sufficiently coated with (B).

これをさらにブフスチック材料(粉末状、粒状、ベレッ
ト等)と混合した後機械的に混練することによって均一
性のすぐれた吸水性プラスチック複合体を製造すること
ができる0ナオ、混r!ハロール、ニーグー、バンバリ
ーミキサ−、ベント式二軸押出機などが用いられるO また、本発明の場合、必要に応じてカーボンブラック、
無機質充てん剤、滑剤、紫外線防止剤、顔料、防カビ剤
、防農剤等を適宜混入することができる。
By further mixing this with a Buchstick material (powder, granules, pellets, etc.) and then mechanically kneading it, a water-absorbing plastic composite with excellent uniformity can be produced. In the case of the present invention, carbon black,
Inorganic fillers, lubricants, ultraviolet inhibitors, pigments, fungicides, agricultural preventives, and the like can be mixed as appropriate.

〈実施例〉 以下、本発明を実施例によりさらに詳しく説明するが、
これらに制限されろものでは表いりなお、グフスチフク
材料中の微粉状高吸水性樹脂の分散性は約200μのプ
レスシートラつくシ、顕微鏡(X100倍)で観察し判
定した0またプラスチック複合体の吸水性はつぎに示す
計算式から求めた◎ −A 吸水率(@口□×100 A;吸水前の重#、(f) B:水浸漬48時1iJl]後の重ffi if)実験
l あらかじめ、微粉状高吸水性樹脂(スミカゲル■5P−
510、平均粒径−10μm、住人化学工業製) 50
0 f tIC対し、ノニオン系の界面活性剤(ツルポ
ン■5−60、東邦千葉化学1柴Fl )300Fをよ
く混合したのち、ヒーターつきのブレングーを用い、8
0〜90℃で約20分間機械的混合を行い、スミカゲル
■5P−510粒子の表面をツルポン■s−e oで被
覆した。
<Examples> The present invention will be explained in more detail by examples below.
Although not limited by these, the dispersibility of the finely powdered superabsorbent resin in the material is approximately 200μ press sheet, and the water absorption of the plastic composite is determined by observation with a microscope (100x magnification). ◎ -A Water absorption rate (@mouth □ × 100 A: Weight before water absorption, (f) B: Weight after immersion in water 48 hours 1 iJl] ffi if) Experiment l super absorbent resin (Sumikagel■5P-
510, average particle size -10 μm, manufactured by Sumima Kagaku Kogyo) 50
After thoroughly mixing 0 f tIC with 300 F of a nonionic surfactant (Tsurupon 5-60, Toho Chiba Kagaku 1 Shiba Fl), using a blender equipped with a heater,
Mechanical mixing was performed at 0 to 90°C for about 20 minutes, and the surface of the Sumikagel ■5P-510 particles was coated with Tsurpone ■seo.

実験2 スミカゲル■5P−510の他は、インブチレン−無水
マレイン酸共重合体変成物の架橋体の塩(KIゲφ20
1に、クラレイソ7“レンケミカル社製、平均粒径−8
μm)を使用した他はすべて実験1と同様にして、KI
ゲ/L10201K粒子の表面をツルポン■5−60で
被覆した〇 実施例1 エチレン−酸酢ビニル共重合体(エバテートH2O22
、住人化学工業製)のベレッ)1000tに対し、実験
1で得たツルポン■5−60で熱地したスミカゲル■5
P−510の混合物を40f加え、ロー/l’温度12
0℃で、混練したのち、さらに押出機によυストランド
状に押出し、これを切断してベレットを得た。このベレ
ットを用いて、約200μのプレスシートをつく沙、ス
ミカゲル■5P−510の分散性を顕微鏡で観察したと
ころ、スミカゲル■5P−510の分散は均一であった
Experiment 2 In addition to Sumikagel ■5P-510, salts of crosslinked products of modified inbutylene-maleic anhydride copolymer (KI gel φ20
1, Kurareiso 7" manufactured by Ren Chemical Co., Ltd., average particle size -8
The procedure was the same as in Experiment 1 except that KI
The surface of Ge/L10201K particles was coated with Turpon ■5-60 Example 1 Ethylene-vinyl acid acetate copolymer (evatate H2O22
For 1000 tons of beret (manufactured by Sumikagaku Kogyo Co., Ltd.), Sumikagel heated with 5-60 tsurpon obtained in Experiment 1 5
Add 40f of P-510 mixture, low/l' temperature 12
After kneading at 0°C, the mixture was further extruded into υ strands using an extruder and cut into pellets. Using this pellet, a press sheet of approximately 200 μm was made. The dispersibility of Sumikagel ■5P-510 was observed under a microscope, and the dispersion of Sumikagel ■5P-510 was found to be uniform.

また、プレスシートの吸水率は5.1%であったO 実施例2 低密度ポリエチレン(ダウポリ■旭ダウ社PI )のベ
レット100(z’と夾騎2で得たソルボpS−60で
処理したKIゲル■201にの混合物を501加え、ロ
ー/L’温度160℃で混練したのち、さらに押出機だ
よりストランド状に押出し、これを切断してベレットを
得た。このベレットを用いて、約200μのプレスシー
トをつくり実施例1と同様にして、KIゲyo2011
(の分散性を調べた結果、KIゲル■201にの分散は
均一であった。
Furthermore, the water absorption rate of the press sheet was 5.1%. 501 of the mixture was added to KI Gel ■201, kneaded at a low/L' temperature of 160°C, and then extruded into strands using an extruder and cut into pellets. Using this pellet, approximately A 200μ press sheet was made in the same manner as in Example 1, and KIgeyo2011
As a result of examining the dispersibility of (), it was found that the dispersion in KI Gel ■201 was uniform.

また、プレスシートの吸水率は8.2%であった。Further, the water absorption rate of the press sheet was 8.2%.

実施例8 実験1で得たツルポンoS−60で処理したスミカゲA
/”5P−510の混合物150り、ジブチルフタレー
ト80f1およびポリ塩化ビニ、11/ (7ミリツト
■FS、住人化学工業製)をヘンシェルミキサーで混合
したのち、ロー/’ ff1M m 150℃で5分間
混線後、約2日のプレスシートを成形した。得られたプ
レスシートのヌミカゲφ5P−510の分散は均一であ
った。
Example 8 Sumikage A treated with Tsurupon oS-60 obtained in Experiment 1
/'' 150 parts of a mixture of 5P-510, 80 f1 of dibutyl phthalate, and polyvinyl chloride, 11/ (7 millimeter FS, manufactured by Sumima Kagaku Kogyo) were mixed in a Henschel mixer, and mixed at 150°C for 5 minutes at 1 M m After that, a press sheet was molded for about 2 days.The dispersion of Numikage φ5P-510 in the obtained press sheet was uniform.

また、プレスシートの吸水率は180%であった。Moreover, the water absorption rate of the press sheet was 180%.

比較例1 エチレン−酢酸ビニル共重合体(エバテート)!202
2、住人化学工業製)のベレット100OFに対し、ス
ミカゲルo8P−510を251加え文以外は実施例1
と同様にして約200μのプレスジ・−トをつくシ、ス
ミカゲA・■5P−510の分;ム性をシ゛η撒4で1
察したところ、スミカゲノヨ5P−510の砦Vが多く
観察され、実施例1と比較し、きわめて分散が不均一で
あった◇また、プレスシートの吸水率は8.5%で、実
施例1よシ吸水性が劣っていた。
Comparative Example 1 Ethylene-vinyl acetate copolymer (evatate)! 202
2. Add 251 parts of Sumikagel o8P-510 to Beret 100OF (manufactured by Sumika Kagaku Kogyo).Except for the following, Example 1
In the same manner as above, make a press sheet of about 200μ, and reduce the elasticity of Sumikage A・■5P-510 by 1 by 4 times.
As a result, many forts V of Sumikagenoyo 5P-510 were observed, and the dispersion was extremely non-uniform compared to Example 1 ◇ Also, the water absorption rate of the press sheet was 8.5%, which was different from Example 1. Water absorption was poor.

比較例2 低静度ポリエチレン(ダウポリ■、旭タウ社製)のベレ
ット1000Fに対し、KIゲIv■201Kを81F
加えた以外は笑施例2と同様にして約200μのプレス
シートをつくシ、KlゲJ201にの分散性を調べた結
果、KXゲ−201にの凝集が多く観察され、実施例2
と比較し、かなシ分散が不均一であった。
Comparative Example 2 KI Ge Iv ■ 201K was used at 81F for Beret 1000F of low static polyethylene (Dow Poly ■, manufactured by Asahi Tau Co., Ltd.)
A press sheet of about 200 μm was made in the same manner as in Example 2, except that the following was added. As a result of examining the dispersibility of KX Ge-201, a large amount of aggregation was observed in KX Ge-201.
In comparison, the kana-shi distribution was non-uniform.

また、プレスシートの吸水率も2.8寿でや−劣ってい
た。
Moreover, the water absorption rate of the press sheet was 2.8 years old, which was slightly inferior.

〈発明の効果〉 本発明の方法により微粉状高吸水性樹脂をプラスチック
材料中に均一に分散することができる。又、混練中に水
分の分散も十分に行なわれ「ピンホール」の発生も防ぐ
ことができる。さらに混、h時の剪断エネルギーも小さ
いので、発熱も低下し混線物の分解も防ぐととができる
0従って、本発明の方法によって製造された吸水性プラ
スチック接合材料は、吸水性にすぐれ、長期にわたシそ
の効果を発揮する。
<Effects of the Invention> By the method of the present invention, a finely powdered superabsorbent resin can be uniformly dispersed in a plastic material. In addition, water is sufficiently dispersed during kneading, and the occurrence of "pinholes" can be prevented. Furthermore, since the shearing energy during mixing and heating is small, heat generation is reduced and decomposition of the mixed material can be prevented. Therefore, the water-absorbing plastic bonding material produced by the method of the present invention has excellent water absorption and can last for a long time. Niwatashi shows its effect.

Claims (1)

【特許請求の範囲】[Claims] 微粉状高吸水性樹脂を界面活性剤で処理した後、プラス
チック材料と混練する吸水性プラスチック複合材料の製
造方法。
A method for producing a water-absorbing plastic composite material, in which a finely powdered super-absorbent resin is treated with a surfactant and then kneaded with a plastic material.
JP61193482A 1986-08-19 1986-08-19 Method for producing water-absorbent plastic composite material Expired - Lifetime JPH0680120B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61193482A JPH0680120B2 (en) 1986-08-19 1986-08-19 Method for producing water-absorbent plastic composite material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61193482A JPH0680120B2 (en) 1986-08-19 1986-08-19 Method for producing water-absorbent plastic composite material

Publications (2)

Publication Number Publication Date
JPS6348337A true JPS6348337A (en) 1988-03-01
JPH0680120B2 JPH0680120B2 (en) 1994-10-12

Family

ID=16308762

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61193482A Expired - Lifetime JPH0680120B2 (en) 1986-08-19 1986-08-19 Method for producing water-absorbent plastic composite material

Country Status (1)

Country Link
JP (1) JPH0680120B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2646430A1 (en) * 1989-04-26 1990-11-02 Nippon Synthetic Chem Ind PROCESS FOR THE PREPARATION OF RESIN PARTICLES WITH HIGH WATER ABSORBING CAPACITY
JPH0320364A (en) * 1989-06-15 1991-01-29 Sanyo Chem Ind Ltd Moldable water-absorptive resin composition
JPH0780282A (en) * 1993-06-24 1995-03-28 Ebara Res Co Ltd Polymeric hydrogel granular material, production thereof and immobilization of bacteria using the same

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57167307A (en) * 1981-04-09 1982-10-15 Sumitomo Chem Co Ltd Production of highly water-absorbing polymeric material having improved water absorption rate
JPS58180233A (en) * 1982-04-19 1983-10-21 Nippon Shokubai Kagaku Kogyo Co Ltd Absorbing agent
JPS59145230A (en) * 1983-02-07 1984-08-20 Sumitomo Chem Co Ltd Production of highly water-swellable vulcanized rubber product
JPS60210645A (en) * 1984-04-04 1985-10-23 Sumitomo Electric Ind Ltd Rubbery elastomer composition
JPS62149335A (en) * 1985-12-24 1987-07-03 Nippon Shokubai Kagaku Kogyo Co Ltd Water absorbent

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57167307A (en) * 1981-04-09 1982-10-15 Sumitomo Chem Co Ltd Production of highly water-absorbing polymeric material having improved water absorption rate
JPS58180233A (en) * 1982-04-19 1983-10-21 Nippon Shokubai Kagaku Kogyo Co Ltd Absorbing agent
JPS59145230A (en) * 1983-02-07 1984-08-20 Sumitomo Chem Co Ltd Production of highly water-swellable vulcanized rubber product
JPS60210645A (en) * 1984-04-04 1985-10-23 Sumitomo Electric Ind Ltd Rubbery elastomer composition
JPS62149335A (en) * 1985-12-24 1987-07-03 Nippon Shokubai Kagaku Kogyo Co Ltd Water absorbent

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2646430A1 (en) * 1989-04-26 1990-11-02 Nippon Synthetic Chem Ind PROCESS FOR THE PREPARATION OF RESIN PARTICLES WITH HIGH WATER ABSORBING CAPACITY
JPH0320364A (en) * 1989-06-15 1991-01-29 Sanyo Chem Ind Ltd Moldable water-absorptive resin composition
JPH0780282A (en) * 1993-06-24 1995-03-28 Ebara Res Co Ltd Polymeric hydrogel granular material, production thereof and immobilization of bacteria using the same

Also Published As

Publication number Publication date
JPH0680120B2 (en) 1994-10-12

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