JPH0680120B2 - Method for producing water-absorbent plastic composite material - Google Patents
Method for producing water-absorbent plastic composite materialInfo
- Publication number
- JPH0680120B2 JPH0680120B2 JP61193482A JP19348286A JPH0680120B2 JP H0680120 B2 JPH0680120 B2 JP H0680120B2 JP 61193482 A JP61193482 A JP 61193482A JP 19348286 A JP19348286 A JP 19348286A JP H0680120 B2 JPH0680120 B2 JP H0680120B2
- Authority
- JP
- Japan
- Prior art keywords
- water
- gel
- plastic composite
- composite material
- copolymer
- 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 - Lifetime
Links
- 229920003023 plastic Polymers 0.000 title claims description 22
- 239000004033 plastic Substances 0.000 title claims description 22
- 239000002250 absorbent Substances 0.000 title claims description 17
- 239000002131 composite material Substances 0.000 title claims description 12
- 238000004519 manufacturing process Methods 0.000 title claims description 5
- 239000000463 material Substances 0.000 claims description 11
- 238000004898 kneading Methods 0.000 claims description 10
- 229920000247 superabsorbent polymer Polymers 0.000 claims description 5
- 239000004094 surface-active agent Substances 0.000 claims description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 18
- 238000010521 absorption reaction Methods 0.000 description 13
- 229920005989 resin Polymers 0.000 description 12
- 239000011347 resin Substances 0.000 description 12
- NPERTKSDHFSDLC-UHFFFAOYSA-N ethenol;prop-2-enoic acid Chemical compound OC=C.OC(=O)C=C NPERTKSDHFSDLC-UHFFFAOYSA-N 0.000 description 10
- 238000000034 method Methods 0.000 description 9
- -1 polyoxyethylene Polymers 0.000 description 9
- 230000002745 absorbent Effects 0.000 description 7
- 229920001577 copolymer Polymers 0.000 description 7
- 239000008188 pellet Substances 0.000 description 7
- 229920003171 Poly (ethylene oxide) Polymers 0.000 description 6
- 239000006185 dispersion Substances 0.000 description 6
- 238000002474 experimental method Methods 0.000 description 6
- 239000002245 particle Substances 0.000 description 6
- 150000003839 salts Chemical class 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- 239000005038 ethylene vinyl acetate Substances 0.000 description 4
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 230000002776 aggregation Effects 0.000 description 3
- 239000002736 nonionic surfactant Substances 0.000 description 3
- 229920001200 poly(ethylene-vinyl acetate) Polymers 0.000 description 3
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 2
- RRHGJUQNOFWUDK-UHFFFAOYSA-N Isoprene Chemical compound CC(=C)C=C RRHGJUQNOFWUDK-UHFFFAOYSA-N 0.000 description 2
- 238000005054 agglomeration Methods 0.000 description 2
- 125000005907 alkyl ester group Chemical group 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 230000000903 blocking effect Effects 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 238000000354 decomposition reaction Methods 0.000 description 2
- DOIRQSBPFJWKBE-UHFFFAOYSA-N dibutyl phthalate Chemical compound CCCCOC(=O)C1=CC=CC=C1C(=O)OCCCC DOIRQSBPFJWKBE-UHFFFAOYSA-N 0.000 description 2
- 235000014113 dietary fatty acids Nutrition 0.000 description 2
- 229920001971 elastomer Polymers 0.000 description 2
- CYKDLUMZOVATFT-UHFFFAOYSA-N ethenyl acetate;prop-2-enoic acid Chemical compound OC(=O)C=C.CC(=O)OC=C CYKDLUMZOVATFT-UHFFFAOYSA-N 0.000 description 2
- 229930195729 fatty acid Natural products 0.000 description 2
- 239000000194 fatty acid Substances 0.000 description 2
- 229920001684 low density polyethylene Polymers 0.000 description 2
- 239000004702 low-density polyethylene Substances 0.000 description 2
- 239000002480 mineral oil Substances 0.000 description 2
- 235000010446 mineral oil Nutrition 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000004014 plasticizer Substances 0.000 description 2
- 229920000915 polyvinyl chloride Polymers 0.000 description 2
- 239000004800 polyvinyl chloride Substances 0.000 description 2
- 238000010008 shearing Methods 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- 229920002126 Acrylic acid copolymer Polymers 0.000 description 1
- 239000004709 Chlorinated polyethylene Substances 0.000 description 1
- 244000043261 Hevea brasiliensis Species 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- 229920001214 Polysorbate 60 Polymers 0.000 description 1
- 229920002125 Sokalan® Polymers 0.000 description 1
- ZJCCRDAZUWHFQH-UHFFFAOYSA-N Trimethylolpropane Chemical compound CCC(CO)(CO)CO ZJCCRDAZUWHFQH-UHFFFAOYSA-N 0.000 description 1
- 238000004220 aggregation Methods 0.000 description 1
- 150000001346 alkyl aryl ethers Chemical class 0.000 description 1
- 150000005215 alkyl ethers Chemical class 0.000 description 1
- 239000002280 amphoteric surfactant Substances 0.000 description 1
- 125000000129 anionic group Chemical group 0.000 description 1
- 239000003945 anionic surfactant Substances 0.000 description 1
- 229940121375 antifungal agent Drugs 0.000 description 1
- 239000003429 antifungal agent Substances 0.000 description 1
- 150000001720 carbohydrates Chemical class 0.000 description 1
- 239000006229 carbon black Substances 0.000 description 1
- 125000002091 cationic group Chemical group 0.000 description 1
- 239000003093 cationic surfactant Substances 0.000 description 1
- 239000011362 coarse particle Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 239000000806 elastomer Substances 0.000 description 1
- 229920006242 ethylene acrylic acid copolymer Polymers 0.000 description 1
- 238000005187 foaming Methods 0.000 description 1
- 235000011187 glycerol Nutrition 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 230000020169 heat generation Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 239000011256 inorganic filler Substances 0.000 description 1
- 229910003475 inorganic filler Inorganic materials 0.000 description 1
- 229920003049 isoprene rubber Polymers 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 229920003052 natural elastomer Polymers 0.000 description 1
- 229920001194 natural rubber Polymers 0.000 description 1
- WXZMFSXDPGVJKK-UHFFFAOYSA-N pentaerythritol Chemical compound OCC(CO)(CO)CO WXZMFSXDPGVJKK-UHFFFAOYSA-N 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 229920001084 poly(chloroprene) Polymers 0.000 description 1
- 239000004584 polyacrylic acid Substances 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 229920001296 polysiloxane Polymers 0.000 description 1
- 229920000346 polystyrene-polyisoprene block-polystyrene Polymers 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 239000005060 rubber Substances 0.000 description 1
- 229920000468 styrene butadiene styrene block copolymer Polymers 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 150000005846 sugar alcohols Polymers 0.000 description 1
- 229920003051 synthetic elastomer Polymers 0.000 description 1
- 239000005061 synthetic rubber Substances 0.000 description 1
- 229920001169 thermoplastic Polymers 0.000 description 1
- 229920001187 thermosetting polymer Polymers 0.000 description 1
- 239000004416 thermosoftening plastic Substances 0.000 description 1
Landscapes
- Processes Of Treating Macromolecular Substances (AREA)
- Compositions Of Macromolecular Compounds (AREA)
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。DETAILED DESCRIPTION OF THE INVENTION <Industrial field of application> The present invention relates to a method for producing a water-absorbent plastic composite material.
<従来の技術とその問題点> 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。<Prior Art and Problems Thereof> A large number of water-absorbent plastic composite materials in which a fine powdery water-absorbent resin is dispersed in a plastic material to impart water absorbability have been known.
しかしながら、微粉状高吸水性樹脂は、元来、非常に高
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ずかしかった。However, since the fine powdery super absorbent resin originally has extremely high humidity and high water absorbability, even if it is mixed in the plastic material as it is, it is possible to sufficiently impart water absorbency as a high-quality composite material. It was difficult.
その原因は、該微分状高吸水性樹脂がプラスチック材料
との混練中に2次凝集して粗大粒子(いわゆるブツ)を
生じたり、水分の分散が不十分なため発泡現象を起こし
得られたプ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。また、混練時には大きな剪断エネ
ルギーが必要であり、その結果生ずる発熱によって混練
物が分解を起こし、性能の低下を招いたりする。The cause is that the differentially superabsorbent resin secondary aggregates during kneading with the plastic material to generate coarse particles (so-called lumps), or the foaming phenomenon may occur due to insufficient water dispersion. This is because "pinholes" may occur in the composite material. In addition, a large shearing energy is required at the time of kneading, and the heat generated as a result causes decomposition of the kneaded product, resulting in deterioration of 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り、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
360号公報)。この方法によって上記の問題点をある程
度は解決できるが、必ずしも十分な効果が得られない場
合もあった。例えば、上記方法により微粉状高吸水性樹
脂を鉱物油や可塑剤で処理し、これをエチレン−酢酸ビ
ニル共重合体と混合して農業用フィルムに製膜した場
合、高吸水性樹脂の凝集や飛散はある程度改善できるも
のの、製膜後のフィルムの経時的なブロッキングが大き
くなり、農業用フィルムとしては難点がある。The inventors of the present invention prevent the occurrence of moisture absorption during handling and storage / storage and scattering during mixing with resin or rubber by using a fine powdery super absorbent resin mixed with mineral oil, a plasticizer, etc. in advance. Method has been proposed (JP-A-60-84).
No. 360 bulletin). Although this method can solve the above problems to some extent, it may not always be possible to obtain a sufficient effect. For example, when a fine powdery super absorbent resin is treated with a mineral oil or a plasticizer by the above method, and when this is mixed with an ethylene-vinyl acetate copolymer to form an agricultural film, agglomeration of the super absorbent resin or Although the scattering can be improved to some extent, blocking with time of the film after film formation becomes large, which is a problem as an agricultural film.
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
剤で処理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、該微分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, after various studies to eliminate the drawbacks of the conventional method,
The inventors have found that the differential superabsorbent resin can be uniformly dispersed by kneading a fine powdery superabsorbent resin previously treated with a surfactant having a good affinity for plastics into a plastic material, and completed the present invention.
<問題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ラスチック複
合材料の製造方法である。<Means for Solving Problems> The present invention is a method for producing a water-absorbent plastic composite material, which comprises treating a fine powdery super absorbent polymer with a surfactant and then kneading the plastic material.
本発明に用いる微粉状高吸水性樹脂(以下(A)とす
る。)とは、通常用いられているもので、例えば酢酸ビ
ニル−アクリル酸エステル共重合体ケン化物、イソブチ
レン‐無水マレイン酸共重合体変成物の架橋体の塩、架
橋構造を有するポリアクリル酸(塩)、澱粉−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に
より、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−無水マレイン酸共重合体変成物
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
が強くより好ましい。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10μ以下であることが望ま
しい。The fine powdery super absorbent resin (hereinafter referred to as (A)) used in the present invention is a commonly used one, for example, saponified vinyl acetate-acrylic acid ester copolymer, isobutylene-maleic anhydride copolymer Examples thereof include a salt of a crosslinked product of a combined modified product, a polyacrylic acid (salt) having a crosslinked structure, a salt of a starch-acrylic acid copolymer, and a modified product of polyethylene oxide. However, the gel strength after water absorption is strong,
A salt of a crosslinked product of a saponified vinyl acetate-acrylic acid ester copolymer or a modified isobutylene-maleic anhydride copolymer is preferably used because the gel does not decompose and long-term durability is required. As the highly water-absorbent resin, one having a water absorption capacity in the range of 50 to 1000 times its own weight can be used, and more preferably 100 to 500 times the gel strength after water absorption is strong. Further, the particle size of the fine powdery super absorbent polymer is preferably as fine as possible from the viewpoint of properties such as physical properties of the final absorbent plastic composite, and the average particle size is
It is desirable that it is 100 μm or less, particularly preferably 10 μm or less.
また、本発明に用いる界面活性剤(以下(B)とす
る。)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、
一種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
キシエチレンアルキルアリールエーテル類、ポリオキシ
エチレンアルキルエステル類、ソルビタン脂肪酸エステ
ル類、ポリオキシエチレンソルビタンエーテル−アルキ
ルエステル類、グリセリン、ペンタエリスリトール、ト
リメチロールプロパン、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、シ
リコーン系界面活性剤等があげられる。The surfactant (hereinafter referred to as (B)) used in the present invention is a commonly used one, and anionic, cationic, nonionic and amphoteric surfactants can be used.
One kind or a combination of two or more kinds can be used. Specifically, polyoxyethylene alkyl ethers, polyoxyethylene alkylaryl ethers, polyoxyethylene alkyl esters, sorbitan fatty acid esters, polyoxyethylene sorbitan ether-alkyl esters, glycerin, pentaerythritol, trimethylolpropane Examples thereof include alkyl esters of polyhydric alcohols such as saccharides, polyoxyethylene derivatives thereof, polyoxyethylene alkylamides, fluorosurfactants, silicone surfactants and the like.
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、特にソルビタン脂肪酸
エステル類は(A)との親和性がよく、少量で効果を発
揮するので好ましい。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、合成ゴムなどのエラストマーであ
っても何等の支障もないが、特に、ポリエチレン、エチ
レン−酢酸ビニル共重合体、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、スルホン化ポリ
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−ブタジエン−スチレンブロック共重合
体、天然ゴム、クロロプレンゴム、イソプレンゴムが好
ましい。In particular, nonionic surfactants are preferable in order to suppress a decrease in the water absorption capacity of the super absorbent polymer, and sorbitan fatty acid esters are particularly preferable because they have a good affinity with (A) and exert an effect in a small amount. In addition, the plastic material as the matrix of the water-absorbent plastic composite is thermosetting,
It may be any of thermoplastic, and may be soft, hard or foamed, and may be an elastomer such as synthetic rubber without any problem, but particularly polyethylene, ethylene-vinyl acetate copolymer, or the Saponified product, chlorinated polyethylene, chlorinated polyprene, sulfonated polyethylene, ethylene-isobutylene copolymer, ethylene-acrylic acid copolymer, polyvinyl chloride or its copolymer, styrene-isoprene-styrene block copolymer, styrene -Butadiene-styrene block copolymer, natural rubber, chloroprene rubber and isoprene rubber are preferable.
又(A)と(B)の使用量の割合は、それぞれの用途に
よって異なり限定することができないが、好ましくはA:
B=90/10〜10/90の範囲がよい。なお、吸水性の高いプ
ラスチック材料を得るには、(A)の混合割合を多くす
るのが好ましい。The ratio of the amounts of (A) and (B) used varies depending on the respective applications and cannot be limited, but preferably A:
The range of B = 90/10 to 10/90 is good. In addition, in order to obtain a plastic material having high water absorption, it is preferable to increase the mixing ratio of (A).
本発明において、(A)を(B)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、ヒーターつきブレン
ダー、ボールミル、ミキサー等に(A)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溶剤を加熱除去
する方法等があげられるが、(A)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, as a method for treating (A) with (B), a method of mechanically mixing (A) and (B) into a commonly used Reiki vessel, a blender with a heater, a ball mill, a mixer or the like, Alternatively, there may be mentioned a method in which the solvent is removed by heating after mixing in the presence of a suitable solvent such as toluene and ethyl acetate, but it is preferable to carry out under the condition that (A) is sufficiently covered with (B). .
これをさらにプラスチック材料(粉末状、粒状、ペレッ
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。By further mixing this with a plastic material (powder, granule, pellet, etc.) and mechanically kneading, a water-absorbent plastic composite having excellent uniformity can be produced.
なお、混練はロール、ニーダー、バンバリーミキサー、
ベント式二軸押出機などが用いられる。In addition, kneading is performed by roll, kneader, Banbury mixer,
A vent type twin screw extruder or the like is used.
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、防曇剤等を適宜混入することができる。Further, in the case of the present invention, carbon black, if necessary,
An inorganic filler, a lubricant, an anti-UV agent, a pigment, an antifungal agent, an antifogging agent and the like can be appropriately mixed.
<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、
これらに制限されるものではない。<Examples> Hereinafter, the present invention will be described in more detail with reference to Examples.
It is not limited to these.
なお、プラスチック材料中の微粉状高吸水性樹脂の分散
性は約200μのプレスシートをつくり、顕微鏡(×100
倍)で観察し判定した。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。In addition, the dispersibility of the fine powdery super absorbent resin in the plastic material was made into a press sheet of about 200μ, and a microscope (× 100
The observation was made by doubling). The water absorption of the plastic composite was calculated from the following calculation formula.
A:吸水前の重量(g) B:水浸漬48時間後の重量(g) 実験1 あらかじめ、微粉状高吸水性樹脂(スミカゲル SP−51
0、平均粒径=10μm、住友化学工業製)500gに対し、
ノニオン系の界面活性剤(ソルボン S−60、東邦千葉
化学工業製)300gをよく混合したのち、ヒーターつきの
ブレンダーを用い、80〜90℃で約20分間機械的混合を行
い、スミカゲル SP−510粒子の表面をソルボン S−6
0で被覆した。 A: Weight before absorption of water (g) B: Weight after immersion in water for 48 hours (g) Experiment 1 SP-51
0, average particle size = 10 μm, made by Sumitomo Chemical Co., Ltd.) 500 g,
Nonionic surfactant (Sorbone S-60, Toho Chiba
After mixing 300 g of chemical industry) well,
Using a blender, perform mechanical mixing at 80 to 90 ° C for about 20 minutes.
I, Sumika gel Sorbone the surface of SP-510 particles S-6
Coated with 0.
実験2 スミカゲル SP−510に代えて、イソブチレン−無水マ
レイン酸共重合体変成物の架橋体の塩(KIゲル 201K、
クラレイソプレンケミカル社製、平均粒径=8μm)を
使用した他はすべて実験1と同様にして、KIゲル 201K
粒子の表面をソルボン S−60で被覆した。Experiment 2 Sumika gel Instead of SP-510, isobutylene-anhydrous
Cross-linked salt of modified lactic acid copolymer (KI gel 201K,
Kuraray Isoprene Chemical Co., average particle size = 8 μm)
KI gel was the same as in Experiment 1 except that it was used. 201K
Sorbone on the surface of particles Coated with S-60.
実施例1 エチレン−酢酸ビニル共重合体(エバテートH2022、住
友化学工業製)のペレット1000gに対し、実験1で得た
ソルボン S−60で処理したスミカゲル SP−510の混
合物を40g加え、ロール温度120℃で、混練したのち、さ
らに押出機によりストランド状に押出し、これを切断し
てペレットを得た。このペレットを用いて、約200μの
プレスシートをつくり、スミカゲル SP−510の分散性
を顕微鏡で観察したところ、スミカゲル SP−510の分
散は均一であった。Example 1 Ethylene-vinyl acetate copolymer (Evatate H2022, Sumitomo
Obtained in Experiment 1 for 1000 g of pellets (made by Tomo Kagaku)
Sorbon Sumika gel treated with S-60 Mixed SP-510
Add 40g of compound and knead at a roll temperature of 120 ° C.
It is extruded into a strand by an extruder and cut into pieces.
To obtain pellets. Using this pellet,
Making a press sheet, Sumika gel SP-510 dispersibility
When observed under a microscope, Sumika gel SP-510 minutes
The dispersion was uniform.
また、プレスシートの吸水率は5.1%であった。The water absorption of the press sheet was 5.1%.
実施例2 低密度ポリエチレン(ダウポリ 旭ダウ社製)のペレッ
ト1000gと実験2で得たソルボン S−60で処理したKI
ゲル 201Kの混合物を50g加え、ロール温度160℃で混練
したのち、さらに押出機によりストランド状に押出し、
これを切断してペレットを得た。このペレットを用い
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ゲル 201Kの分散性を調べた結果、KIゲル 20
1Kの分散は均一であった。Example 2 Low density polyethylene (Dow Poly Made by Asahi Dow)
1000g and sorbon obtained in Experiment 2 KI treated with S-60
gel Add 50g of 201K mixture and knead at a roll temperature of 160 ℃
After that, further extruded into a strand by an extruder,
This was cut to obtain pellets. Use this pellet
And make a pressed sheet of about 200μ, as in Example 1.
KI gel As a result of examining the dispersibility of 201K, KI gel 20
The 1K dispersion was uniform.
また、プレスシートの吸水率は8.2%であった。The water absorption of the press sheet was 8.2%.
実施例3 実験1で得たソルボン S−60で処理したスミカゲル
SP−510の混合物150g、ジブチルフタレート80g、および
ポリ塩化ビニル(スミリット FS、住友化学工業製)10
00gをヘンシエルミキサーで混合したのち、ロール温度1
50℃で5分間混練後、約2mmのプレスシートを成形し
た。得られたプレスシートのスミカゲル SP−510の分
散は均一であった。Example 3 Sorbone obtained in Experiment 1 Sumika gel treated with S-60
150 g of a mixture of SP-510, 80 g of dibutyl phthalate, and
Polyvinyl chloride (Smilit FS, Sumitomo Chemical Co., Ltd.) 10
After mixing 00g with a Hensiel mixer, roll temperature 1
After kneading at 50 ℃ for 5 minutes, press sheet of about 2mm is formed.
It was The resulting pressed sheet Sumika gel SP-510 minutes
The dispersion was uniform.
比較例1 エチレン−酢酸ビニル共重合体(エバテートH2022、住
友化学工業製)のペレット1000gに対し、スミカゲル S
P−510を25g加えた以外は実施例1と同様にして約200μ
のプレスシートをつくり、スミカゲル SP−510の分散
性を顕微鏡で観察したところ、スミカゲル SP−510の
凝集が多く観察され、実施例1と比較し、きわめて分散
が不均一であった。Comparative Example 1 Ethylene-vinyl acetate copolymer (Evatate H2022, Sumitomo
Sumika gel for 1000 g of pellets (made by Tomo Kagaku) S
About 200 μm in the same manner as in Example 1 except that 25 g of P-510 was added.
Make a pressed sheet of, Sumika gel SP-510 dispersion
When the sex was observed with a microscope, Sumika gel SP-510
A large amount of agglomeration was observed, which was extremely dispersed as compared with Example 1.
Was uneven.
また、プレスシートの吸水率は3.5%で、実施例1より
吸水性が劣っていた。The water absorption of the press sheet was 3.5%, which was inferior to that of Example 1.
比較例2 低密度ポリエチレン(ダウポリ 、旭ダウ社製)のペレ
ット1000gに対し、KIゲル 201Kを31g加えた以外は実施
例2と同様にして約200μのプレスシートをつくり、KI
ゲル 201Kの分散性を調べた結果、KIゲル 201Kの凝集
が多く観察され、実施例2と比較し、かなり分散が不均
一であった。Comparative Example 2 Low Density Polyethylene (Dow Poly Made by Asahi Dow)
KI gel for 1000g Implemented except that 31g of 201K was added
Create a press sheet of about 200μ in the same manner as in Example 2, and use KI
gel As a result of examining the dispersibility of 201K, KI gel 201K aggregation
Were observed in many cases, and the dispersion was considerably uneven as compared with Example 2.
It was one.
また、プレスシートの吸水率も2.3%でやゝ劣ってい
た。The water absorption of the press sheet was 2.3%, 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。さらに混練時の剪断エネルギーも小さい
ので、発熱も低下し混練物の分解も防ぐことができる。<Effects of the Invention> By the method of the present invention, a fine powdery super absorbent polymer can be uniformly dispersed in a plastic material. Further, the water is sufficiently dispersed during the kneading, and the occurrence of "pinhole" can be prevented. Furthermore, since the shearing energy at the time of kneading is also small, heat generation is reduced and decomposition of the kneaded product can be prevented.
従って、本発明の方法によって製造された吸水性プラス
チック複合材料は、吸水性にすぐれ、長期にわたりその
効果を発揮する。Therefore, the water-absorbent plastic composite material produced by the method of the present invention is excellent in water absorption and exerts its effect for a long period of time.
又、本発明の方法を農業用フイルムの製造に応用した場
合でも、製膜後のフイルムが経時的なブロッキングを起
こすことはない。Even when the method of the present invention is applied to the production of an agricultural film, the film after film formation does not cause blocking with time.
Claims (1)
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。1. A method for producing a water-absorbent plastic composite material, which comprises treating a fine powdery super absorbent polymer with a surfactant and then kneading it with a plastic material.
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 JPS6348337A (en) | 1988-03-01 |
JPH0680120B2 true 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) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0710922B2 (en) * | 1989-04-26 | 1995-02-08 | 日本合成化学工業株式会社 | Granulation method of super absorbent polymer |
JP2684217B2 (en) * | 1989-06-15 | 1997-12-03 | 三洋化成工業株式会社 | Moldable water absorbent resin composition |
JP3361570B2 (en) * | 1993-06-24 | 2003-01-07 | 株式会社荏原総合研究所 | Microorganism immobilization method using polymer hydrogel granules |
Citations (5)
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 |
-
1986
- 1986-08-19 JP JP61193482A patent/JPH0680120B2/en not_active Expired - Lifetime
Patent Citations (5)
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 |
Also Published As
Publication number | Publication date |
---|---|
JPS6348337A (en) | 1988-03-01 |
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