JPH078883B2 - Method for producing modified water absorbent resin - Google Patents
Method for producing modified water absorbent resinInfo
- Publication number
- JPH078883B2 JPH078883B2 JP4083487A JP4083487A JPH078883B2 JP H078883 B2 JPH078883 B2 JP H078883B2 JP 4083487 A JP4083487 A JP 4083487A JP 4083487 A JP4083487 A JP 4083487A JP H078883 B2 JPH078883 B2 JP H078883B2
- Authority
- JP
- Japan
- Prior art keywords
- water
- resin
- absorbent resin
- water absorption
- polyacrylic acid
- 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
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Landscapes
- Treatments For Attaching Organic Compounds To Fibrous Goods (AREA)
- Processes Of Treating Macromolecular Substances (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Graft Or Block Polymers (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
- Absorbent Articles And Supports Therefor (AREA)
- Treatments Of Macromolecular Shaped Articles (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Description
【発明の詳細な説明】 産業上の利用分野 本発明は改質吸水性樹脂の製造方法に関するもので、さ
らに詳しくは、ポリアクリル酸系吸水性樹脂の表面近傍
部に2次的に架橋を導入し、吸水速度などの性質を改善
する新規な方法に関する。Description: TECHNICAL FIELD The present invention relates to a method for producing a modified water-absorbent resin, and more specifically, it introduces secondary crosslinks in the vicinity of the surface of a polyacrylic acid-based water-absorbent resin. And a novel method for improving properties such as water absorption rate.
吸水性樹脂は自重の数百倍の水を吸収し、また尿や血液
に対しても優れた吸収能を有し、紙おむつ,ナプキンな
どに吸収剤として用いられている。The water-absorbent resin absorbs several hundred times its own weight of water and also has an excellent absorption capacity for urine and blood, and is used as an absorbent in paper diapers, napkins and the like.
従来の技術 吸水性樹脂として種々のタイプが知られるが、ポリアク
リル酸系樹脂が主流を占める。2. Description of the Related Art Although various types of water-absorbent resins are known, polyacrylic acid-based resins dominate.
ポリアクリル酸系吸水性樹脂として、デンプン−アクリ
ロニトリル重合体の加水分解物,デンプン−アクリル酸
グラフト架橋重合体,酢酸ビニル−アクリル酸エステル
共重合体ケン化物,ポリアクリル酸架橋重合体,ポリア
クリル酸系架橋共重合体などがあげられる。As a polyacrylic acid-based water-absorbent resin, starch-acrylonitrile polymer hydrolyzate, starch-acrylic acid graft cross-linked polymer, vinyl acetate-acrylic acid ester copolymer saponified product, polyacrylic acid cross-linked polymer, polyacrylic acid Examples include cross-linked copolymers.
ポリアクリル酸系吸水性樹脂は、アクリル酸単量体単位
を主要な成分として構成され、含まれるカルボキシル基
の一部あるいは全部がアルカリ金属塩に中和された水に
実質的に不溶であるが高度の膨潤性を有する重合体とし
て定義される。The polyacrylic acid-based water-absorbent resin is composed mainly of an acrylic acid monomer unit, and some or all of the carboxyl groups contained therein are substantially insoluble in water neutralized with an alkali metal salt. It is defined as a polymer with a high degree of swelling.
吸水能は架橋あるいは結合点の密度により調節され、自
重の1000倍程度の水を吸収する軟質ゲルから、吸水倍率
が100倍程度の硬質ゲルがみられ、それぞれの用途に応
じて適用される。The water absorption capacity is controlled by the density of crosslinks or bonding points, and from soft gels that absorb about 1000 times the weight of water to hard gels with a water absorption ratio of about 100 times, they are applied according to their respective uses.
吸水性樹脂は粉末あるいは被膜の形態で実用に供され
る。性能は、吸水倍率,吸水速度および吸水ゲルの硬さ
などによって評価される。一般に吸水倍率の大きい軟質
ゲルは吸水速度が低下する傾向がみられる。その原因は
次の現象によると考えられる。The water absorbent resin is practically used in the form of powder or coating. The performance is evaluated by the water absorption capacity, the water absorption speed, the hardness of the water absorbing gel, and the like. Generally, a soft gel having a large water absorption capacity tends to have a low water absorption rate. The cause is considered to be due to the following phenomenon.
架橋密度の低い軟質ゲル粒子が水に接触すると表面部が
吸水膨潤して水を捉え、内部への水の浸透を妨げる。一
方、架橋密度の高い硬質ゲルは、軟質ゲルに比べて保水
能が低く、内部への水の浸透を妨げない。その結果、硬
質ゲルの方が軟質ゲルよりも吸水速度が大である。When the soft gel particles having a low cross-linking density come into contact with water, the surface absorbs water and swells, catches water, and impedes the penetration of water into the interior. On the other hand, a hard gel having a high crosslink density has a lower water retention capacity than a soft gel and does not prevent water from penetrating inside. As a result, the hard gel has a higher water absorption rate than the soft gel.
こうした現象は粒子の集合体粉末の場合にもみられる。
軟質ゲル粒子は表面が軟質ゲルで覆われるので塊を形成
し易く、いわゆるままこ現象がみられる。ままこが形成
されると粉末全体への水の浸透が妨げられ、吸水速度は
極端に低下する。This phenomenon is also observed in the case of aggregate powder of particles.
Since the surface of the soft gel particles is covered with the soft gel, lumps are easily formed, and a so-called lingering phenomenon is observed. The formation of moulds hinders the water from penetrating the entire powder, and the water absorption rate is extremely reduced.
ままこの形成および吸水速度は吸水性樹脂への水の浸透
性によって支配される。浸透性と保水性は逆比例の関係
にあり、表面部に浸透性が低く、保水性が高い軟質ゲル
が形成されると、ゲル粒子の集合体としての力学的性質
が低下する。As it is, its formation and water absorption rate are governed by the permeability of water into the water absorbent resin. The permeability and water retention are in inverse proportion to each other, and when a soft gel with low permeability and high water retention is formed on the surface, the mechanical properties of the gel particles as aggregates deteriorate.
粒状,被膜状あるいは繊維状の吸水性樹脂の内部が吸水
倍率の大きい軟質ゲル、外部が浸透性の良好な硬質ゲル
で構成されれば、吸水速度,ゲルの硬さ,吸水倍率,保
水性のバランスのとれた好ましい製品が得られる。If the inside of the granular, film-like or fibrous water absorbent resin is composed of a soft gel with a large water absorption capacity and the outside is a hard gel with good permeability, the water absorption rate, the hardness of the gel, the water absorption capacity, and the water retention A balanced and favorable product is obtained.
吸水性樹脂粒子の表面部に2次的に架橋を形成させ、吸
水性能を改善する試みがみられる(特開昭56−131608,5
7−44627,58−42602,58−117222など)。Attempts have been made to improve water absorption performance by forming secondary crosslinks on the surface of the water-absorbent resin particles (JP-A-56-131608,5).
7-44627, 58-42602, 58-117222, etc.).
発明が解決しようとする問題点 ポリアクリル酸系吸水性樹脂の表面部に架橋を導入して
改質を図る公知の方法は、いずれも重合体に含まれるカ
ルボキシル基あるいはカルボキシレート基の反応性を利
用している。架橋剤として、エチレングリコールジグリ
シジルエーテルに代表されるジグリシジル化合物などの
有機化合物が用いられる。Problems to be Solved by the Invention Known methods for introducing a cross-link into the surface of a polyacrylic acid-based water-absorbent resin for modification include all methods for improving the reactivity of a carboxyl group or a carboxylate group contained in a polymer. We are using. As the cross-linking agent, an organic compound such as a diglycidyl compound represented by ethylene glycol diglycidyl ether is used.
これらの方法は、架橋形成反応に高温あるいは長時間を
要したり、未反応架橋剤の残存,製造コストに負担を与
える複雑な工程を要するなどの問題があり、さらに製品
が衛生材料に多く使用される点からも、人体に対する安
全性の確認されていない有機化合物の使用は好ましくな
い。また改質効果も必ずしも充分とはいえない。These methods have problems such as high temperature or long time required for the cross-linking reaction, residual unreacted cross-linking agent, and complicated process that burdens the manufacturing cost, and moreover, the products are often used as sanitary materials. In view of the above, it is not preferable to use an organic compound whose safety to the human body has not been confirmed. Moreover, the modifying effect is not always sufficient.
問題点を解決するための手段 本発明者は、先にアクリル酸単量体単位を主要成分とし
て構成する重合体の水性組成物を、水溶性過酸化物ラジ
カル開始剤の存在で加熱し、ラジカル架橋によって重合
体に架橋を導入する吸水性樹脂の製造方法を発明した
(特開昭61−296003)。Means for Solving the Problems The present inventor previously heated an aqueous composition of a polymer composed mainly of an acrylic acid monomer unit in the presence of a water-soluble peroxide radical initiator to give a radical. A method for producing a water-absorbent resin in which crosslinking is introduced into a polymer by crosslinking has been invented (JP-A-61-296003).
本発明者は、先に発明したラジカル架橋法を前述の問題
点を解決する手段として用いることを発想し、本発明の
方法を完成した。The present inventor has conceived that the radical crosslinking method previously invented is used as a means for solving the above-mentioned problems, and completed the method of the present invention.
ポリアクリル酸系重合体の水溶性過酸化物ラジカル開始
剤による架橋のあらましは次に示される。An outline of cross-linking of a polyacrylic acid polymer with a water-soluble peroxide radical initiator is shown below.
(1) 乾燥状態では架橋の形成は阻害され、適度の水
の存在が必要である。(1) In the dry state, the formation of crosslinks is hindered, and it is necessary to have an appropriate amount of water.
(2) 開始剤の架橋効率は温度,水分量によって変化
し、それぞれ最適な範囲がある。(2) The cross-linking efficiency of the initiator varies depending on the temperature and the water content, and each has an optimum range.
(3) 架橋助剤として親水性多官能不飽和化合物が有
効である。(3) A hydrophilic polyfunctional unsaturated compound is effective as a crosslinking aid.
ポリアクリル酸系重合体は、特に金属塩の場合、融点は
みられず、分子運動および反応性の境界といわれる二次
転移点(Tg)は極めて高いと考えられる。水は重合体に
対して可塑剤として作用し、分子運動と反応性を誘起す
ると説明される。Especially in the case of metal salt, the polyacrylic acid polymer has no melting point, and the second transition point (Tg), which is said to be the boundary between molecular motion and reactivity, is considered to be extremely high. Water is explained to act as a plasticizer for the polymer, inducing molecular motion and reactivity.
過酸化物ラジカル開始剤を含む水性溶液をポリアクリル
酸系吸水性樹脂粒子に接触させると、粒子は水性溶液を
吸収して表面近傍に開始剤を含む水性組成物が形成され
る。When the aqueous solution containing the peroxide radical initiator is brought into contact with the polyacrylic acid-based water-absorbent resin particles, the particles absorb the aqueous solution to form an aqueous composition containing the initiator in the vicinity of the surface.
樹脂粉末粒子の表面部に比較的少量の水性溶液を均一に
浸透させる手段として、溶陪として、メタノール,エタ
ノール,アセトン,メチルエチルケトンなどの揮発性水
溶性溶剤を加えた混合溶媒を用いることもできる。水性
溶液は樹脂粉末をかきまぜながら噴霧する方法が好まし
い。As a means for uniformly permeating a relatively small amount of an aqueous solution into the surface of the resin powder particles, a mixed solvent prepared by adding a volatile water-soluble solvent such as methanol, ethanol, acetone or methyl ethyl ketone can be used as a melt. The aqueous solution is preferably sprayed while stirring the resin powder.
過酸化物ラジカル開始剤として、過硫酸アンモン,過硫
酸カリ,過硫酸ナトリウムなどの過硫酸塩,過酸化水素
などの無機化合物のほかに、酢酸および蓚酸などの有機
酸過酸化物などが用いられる。また架橋助剤として、N,
N′−メチレンビスアクリルアミド,エチレングリコー
ルビス(メタ)アクリレート,ポリエチレングリコール
(メタ)アクリレートなどの親水性多官能不飽和化合物
があげられる。架橋助剤の作用は、公知の有機過酸化物
によるエチレン系重合体の架橋の場合と同様と考えられ
る。As peroxide radical initiators, in addition to persulfates such as ammonium persulfate, potassium persulfate and sodium persulfate, inorganic compounds such as hydrogen peroxide, organic acid peroxides such as acetic acid and oxalic acid are used. . Further, as a crosslinking aid, N,
Hydrophilic polyfunctional unsaturated compounds such as N'-methylenebisacrylamide, ethylene glycol bis (meth) acrylate, polyethylene glycol (meth) acrylate and the like can be mentioned. The action of the crosslinking aid is considered to be the same as in the case of crosslinking the ethylene-based polymer with a known organic peroxide.
開始剤の使用量は、樹脂に対して0.01〜10重量%の範囲
であるが、通常0.1〜2重量%の範囲で好ましい効果を
与える。The amount of the initiator used is in the range of 0.01 to 10% by weight with respect to the resin, but usually in the range of 0.1 to 2% by weight, a preferable effect is provided.
水は、樹脂表面部を膨潤させると共に開始剤を浸透させ
るのに必要で、その際樹脂はあらかじめブロッキングし
ない程度に含水状態にあってもよい。水性溶媒として樹
脂に加えられる水の量は特に限定されないが、通常樹脂
に対して2〜20重量%の範囲にある。Water is necessary for swelling the resin surface and for penetrating the initiator, and the resin may be in a water-containing state in advance so that it does not block. The amount of water added to the resin as an aqueous solvent is not particularly limited, but is usually in the range of 2 to 20% by weight based on the resin.
架橋助剤は必ずしも必要とされないが、反応条件によっ
ては開始剤の架橋効率を高めるのに有効である。その使
用量は概して開始剤と同程度の範囲にある。Although a crosslinking aid is not always required, it is effective in increasing the crosslinking efficiency of the initiator depending on the reaction conditions. The amount used is generally in the same range as the initiator.
アセトンなどの揮発性有機溶剤は反応前に留去されるの
で、使用量は特に制限されない。水のほかにエチレング
ルコール,プロピレングリコール,グリセリン等の多価
アルコール化合物も樹脂に対して可塑剤として作用する
が、これらの化合物は不揮発性であるので、開始剤に対
して不活性なものが選ばれねばならない。Since the volatile organic solvent such as acetone is distilled off before the reaction, the amount used is not particularly limited. In addition to water, polyhydric alcohol compounds such as ethylene glycol, propylene glycol, and glycerin also act as plasticizers on the resin, but since these compounds are non-volatile, those that are inactive to the initiator are You have to be chosen.
樹脂表面部に架橋を導入し、吸水性能を改善する目的に
は、架橋形成層の厚さと架橋密度が重要であり、水性溶
液の組成,量がそれぞれ調整される。The thickness and crosslink density of the crosslink forming layer are important for the purpose of introducing crosslinks into the resin surface to improve the water absorption performance, and the composition and amount of the aqueous solution are adjusted respectively.
架橋反応は開始剤のラジカル分解によって生ずる。開始
剤として代表的な過硫酸アンモン等の過硫酸塩の水溶液
中の分解速度から、含水膨潤状態にある反応混合物にお
ける開始剤の1分半減期温度は約120℃と推定される。
これにより反応温度は120〜130℃が適切と考えられる。
吸水性樹脂は水は強く吸着するので、100℃以上の高温
においても容易に乾燥することはないが、反応時におけ
る水分の維持が必要である。好ましい加熱方法として、
過熱水蒸気雰囲気下における加熱乾燥があげられる。The crosslinking reaction occurs by radical decomposition of the initiator. From the decomposition rate of persulfate such as ammonium persulfate, which is a typical initiator, in an aqueous solution, it is estimated that the 1-minute half-life temperature of the initiator in the reaction mixture in a water-containing swollen state is about 120 ° C.
From this, it is considered that the appropriate reaction temperature is 120 to 130 ° C.
Since the water absorbent resin strongly adsorbs water, it does not easily dry even at a high temperature of 100 ° C. or higher, but it is necessary to maintain the water content during the reaction. As a preferred heating method,
Heating and drying in a superheated steam atmosphere can be mentioned.
作 用 表面近傍部に架橋が導入された吸水性樹脂粒子は、内部
と外部で架橋密度が異なり、吸水挙動も異なる。吸水倍
率の大きい軟質ゲルの外側を水の浸透性の良好な硬質ゲ
ルで被覆された粒子は、それ自体あるいは集合体とし
て、早い吸水と大きな吸水能を示す。また水は吸水の初
期に粒子内部まで均一に浸透するので、表面は乾いた感
触を与え、集合体として硬い感触が得られる。その結
果、紙おむつなどの衛生材料の吸収剤として好ましい性
質を発揮する。被膜あるいは繊維状の吸水性樹脂の場合
にも、同様な作用効果が発揮される。Water-absorbent resin particles with cross-linking introduced near the working surface have different cross-linking densities inside and outside, and also different water-absorption behavior. The particles obtained by coating the outside of a soft gel having a large water absorption capacity with a hard gel having a good water permeability show fast water absorption and a large water absorption ability as such or as an aggregate. Further, since water evenly penetrates into the inside of the particles at the initial stage of water absorption, the surface gives a dry feel and a hard feel as an aggregate is obtained. As a result, it exhibits preferable properties as an absorbent for sanitary materials such as disposable diapers. In the case of a film or a fibrous water-absorbent resin, the same effect is exhibited.
実施例1. 吸水性樹脂粉末の製造 濃度48%の苛性ソーダ水溶液66.6部,アクリル酸72部,
水85部を混合した水溶液にN,N′−メチレンビスアクリ
ルアミド0.08部および過硫酸カリ0.1部を加えて原液を
調製した。原液を厚さ約1cmの層として容器に入れ、窒
素気中で、約50℃に加熱して重合を開始した。容器を冷
却して反応温度が80℃を越えないように調節して、10分
後にゴム状の重合物を得た。重合物を乾燥し、粉砕して
粉末とした。粉末をふるい分けして、粒度32〜200メッ
シュの樹脂粉末を採取した。Example 1. Production of water-absorbent resin powder 66.6 parts of a 48% strength aqueous caustic soda solution, 72 parts of acrylic acid,
A stock solution was prepared by adding 0.08 part of N, N'-methylenebisacrylamide and 0.1 part of potassium persulfate to an aqueous solution prepared by mixing 85 parts of water. The stock solution was put into a container as a layer having a thickness of about 1 cm, and heated to about 50 ° C. in a nitrogen atmosphere to start polymerization. The container was cooled and adjusted so that the reaction temperature did not exceed 80 ° C., and a rubbery polymer was obtained after 10 minutes. The polymer was dried and ground into a powder. The powder was sieved to collect a resin powder having a particle size of 32 to 200 mesh.
吸水能は、純水および0.9%食塩水中で60分間膨潤させ
たヒドロゲルを80メッシの金網上に別し、重量を測定
して求め、樹脂1g当りの吸水量で表わす。吸水倍率は純
水に対して610倍、0.9%食塩水に対して59倍であった。The water absorption capacity was obtained by separating the hydrogel swollen in pure water and 0.9% saline solution for 60 minutes on a wire mesh of 80 mesh and weighing, and expressed by the amount of water absorption per 1 g of resin. The water absorption capacity was 610 times for pure water and 59 times for 0.9% saline.
樹脂粉末50部をかきまぜながら、これに濃度6%の過硫
酸アンモン水溶液5部を噴霧して樹脂粉末の表面部に均
一に含浸させた。次に含浸物を過熱水蒸気吹込式の温度
130℃の乾燥器中で6分間加熱乾燥した。生成樹脂の水
分量は5%であった。While stirring 50 parts of the resin powder, 5 parts of an aqueous solution of ammonium persulfate having a concentration of 6% was sprayed onto this to uniformly impregnate the surface part of the resin powder. Next, the impregnated material is heated with superheated steam.
It heat-dried for 6 minutes in a 130 degreeC dryer. The water content of the produced resin was 5%.
樹脂粉末の吸水速度は次の方法で測定した。直径15cmの
シャーレに1.5cmの厚さに0.9%食塩水を加え、これに直
径3cm、高さ3cmのポリウレタン製スポンジを置き、その
上に直径3cmのガラスフィルター板(No.2)をのせて、
液がガラスフィルターの表面に達するようにする。ガラ
スフィルターの上に樹脂粉末0.3gをのせ、10分後の吸水
量を測定して比較した。The water absorption rate of the resin powder was measured by the following method. 0.9% saline solution is added to a 1.5 cm thick petri dish with a diameter of 15 cm, a polyurethane sponge with a diameter of 3 cm and a height of 3 cm is placed on it, and a glass filter plate (No. 2) with a diameter of 3 cm is placed on it. ,
Allow the liquid to reach the surface of the glass filter. 0.3 g of resin powder was placed on the glass filter, and the water absorption amount after 10 minutes was measured and compared.
架橋処理された試料の吸水倍率は、純水に対して560
倍、0.9%食塩水に対して54倍であった。一方、吸水速
度として表わされる樹脂1gに換算した吸水量(吸水倍
率)は、未処理試料の10倍に対して、処理試料は33倍で
あった。未処理試料はままこの生成によって、粉末の均
一な膨潤が妨げられたためである。一方、処理試料は均
一に膨潤した。The water absorption capacity of the cross-linked sample is 560 against pure water.
It was 54 times that of 0.9% saline. On the other hand, the water absorption amount (water absorption ratio) converted into 1 g of the resin, which was expressed as a water absorption rate, was 33 times in the treated sample, compared with 10 times in the untreated sample. This is because the formation of the untreated sample left the uniform swelling of the powder prevented. On the other hand, the treated sample swelled uniformly.
実施例2. 実施例1で調製した樹脂粉末を用いた。Example 2. The resin powder prepared in Example 1 was used.
樹脂粉末50部をかきまぜながら、濃度7%の過硫酸カリ
水溶液4部にアセトン8部を加えた混合液を噴霧して含
浸させた。While stirring 50 parts of the resin powder, a mixture of 4 parts of a 7% aqueous potassium persulfate solution and 8 parts of acetone was sprayed and impregnated.
含浸物からアセトンを蒸発させた後、実施例1と同様に
加熱乾燥した。After evaporating acetone from the impregnated material, it was heated and dried in the same manner as in Example 1.
架橋処理試料の吸水倍率は、純水に対して550倍、0.9%
食塩水に対して52倍であった。一方、吸水倍率として表
わされる吸水倍率は38倍であった。Water absorption capacity of cross-linked sample is 550 times that of pure water, 0.9%
52 times that of saline. On the other hand, the water absorption capacity expressed as the water absorption capacity was 38 times.
実施例3. 実施例1で調製した樹脂粉末を用いた。Example 3 The resin powder prepared in Example 1 was used.
樹脂粉末50部をかきまぜながら、濃度4%の過硫酸アン
モン水溶液5部にN,N′−メチレンビスアクリルアミド
0.1部とメチルエチルケトン5部を加えた混合物を噴霧
して含浸させた。While stirring 50 parts of the resin powder, 5 parts of an aqueous solution of ammonium persulfate having a concentration of 4% was added to N, N'-methylenebisacrylamide.
A mixture of 0.1 parts and 5 parts of methyl ethyl ketone was sprayed and impregnated.
含浸物からメチルエチルケトンを蒸発させた後、過熱水
蒸気吹込式の温度120℃の乾燥器気中で10分間加熱乾燥
した。生成樹脂の水分量は6%であった。After evaporating methyl ethyl ketone from the impregnated material, it was heated and dried for 10 minutes in a superheated steam blowing type dryer at a temperature of 120 ° C. The water content of the produced resin was 6%.
架橋処理試料の吸水倍率は、純水に対して530倍、0.9%
食塩水に対して51倍であった。一方、吸水速度として表
わされる吸水倍率は40倍であった。The water absorption capacity of the crosslinked sample is 530 times that of pure water, 0.9%
It was 51 times that of saline. On the other hand, the water absorption ratio expressed as the water absorption rate was 40 times.
実施例4. デンプン/ポリアクリル酸グラフト型の市販吸水性樹脂
(三洋化成:サンウエットIM−300)を用いた。吸水倍
率は純水に対して670倍、0.9%食塩水に対して64倍と測
定された。Example 4 A commercially available water-absorbent resin of starch / polyacrylic acid graft type (Sanyo Kasei: Sunwet IM-300) was used. The water absorption capacity was measured to be 670 times for pure water and 64 times for 0.9% saline solution.
樹脂粉末50部をかきまぜながら、濃度7%の過硫酸カリ
水溶液4部にアセトン6部を加えた混合液を噴霧して含
浸させた。While stirring 50 parts of the resin powder, a mixed solution of 4 parts of potassium persulfate aqueous solution having a concentration of 7% and 6 parts of acetone was sprayed and impregnated.
含浸物からアセトンを蒸発させた後、実施例1と同様に
加熱乾燥した。After evaporating acetone from the impregnated material, it was heated and dried in the same manner as in Example 1.
架橋処理試料の吸水倍率は、純水に対して590倍、0.9%
食塩水に対して59倍であった。一方、吸水速度として表
わされる吸水倍率は未処理試料の15倍に対して37倍であ
った。The water absorption capacity of the crosslinked sample is 590 times that of pure water, 0.9%
It was 59 times that of saline. On the other hand, the water absorption ratio, which was expressed as the water absorption rate, was 37 times that of the untreated sample, which was 15 times.
効 果 実施例に示されるように、本発明の方法によって、表面
近傍部に架橋の導入された吸水性樹脂粉末は、吸水速度
が著しく増大し、ままこの生成が防止され、また吸水ゲ
ルの硬さも向上する。被膜あるいは繊維状樹脂の場合も
粉末の場合と同様な効果が発揮される。As shown in the Examples, by the method of the present invention, the water-absorbent resin powder in which cross-linking has been introduced in the vicinity of the surface has a significantly increased water-absorption rate, and this generation is prevented as it is. Also improves. In the case of a film or fibrous resin, the same effect as in the case of powder is exhibited.
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 C08J 7/12 7310−4F C08K 5/14 C08L 33/02 LHR D06M 14/10 ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI Technical display area C08J 7/12 7310-4F C08K 5/14 C08L 33/02 LHR D06M 14/10
Claims (4)
酸化物ラジカル開始剤を含む水性溶液を接触させて含水
膨潤状態とし、樹脂を加熱して、ラジカル開示剤の分解
を通じて樹脂の表面近傍部の重合体分子鎖に架橋を導入
することを特徴とする改質吸水性樹脂の製造方法。1. A surface of a polyacrylic acid-based water-absorbent resin is brought into contact with an aqueous solution containing a peroxide radical initiator to bring it into a water-containing swelling state, and the resin is heated to decompose the radical disclosing agent. A method for producing a modified water absorbent resin, which comprises introducing a crosslink into a polymer molecular chain in the vicinity thereof.
に含まれるカルボキシル基の60〜90モル%がアルカリ金
属塩の形態にある特許請求の範囲第1項記載の方法。2. The method according to claim 1, wherein 60 to 90 mol% of the carboxyl groups contained in the polymer of the polyacrylic acid-based water-absorbent polymer are in the form of an alkali metal salt.
飽和化合物を含んでなる特許請求の範囲第1項記載の方
法。3. The method according to claim 1, wherein the aqueous solution contains a hydrophilic polyfunctional unsaturated compound as a crosslinking aid.
酸化物ラジカル開始剤を含む水性溶液を接触させて含水
膨潤状態とし、樹脂を過熱水蒸気雰囲気下に加熱する特
許請求の範囲第1項記載の方法。4. A method of heating a resin in a superheated steam atmosphere by bringing an aqueous solution containing a peroxide radical initiator into contact with the surface of the polyacrylic acid-based water-absorbent resin to bring the resin into a water-containing swelling state. Method described in section.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US07/057,193 US4783510A (en) | 1986-06-04 | 1987-06-03 | Process for improving a water absorbent polyacrylic acid polymer and an improved polymer produced by said process |
| EP19870108131 EP0248437A3 (en) | 1986-06-04 | 1987-06-04 | A process for improving a water absorbent polyacrylic acid polymer and an improved polymer produced by said process |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61-130560 | 1986-06-04 | ||
| JP13056086 | 1986-06-04 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6399211A JPS6399211A (en) | 1988-04-30 |
| JPH078883B2 true JPH078883B2 (en) | 1995-02-01 |
Family
ID=15037174
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP4083487A Expired - Lifetime JPH078883B2 (en) | 1986-06-04 | 1987-02-24 | Method for producing modified water absorbent resin |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH078883B2 (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2008120742A1 (en) | 2007-03-29 | 2008-10-09 | Nippon Shokubai Co., Ltd. | Particulate water absorbent and process for producing the same |
| US7473739B2 (en) | 2004-02-05 | 2009-01-06 | Nippon Shokubai Co., Ltd. | Particulate water absorbent agent and production method thereof, and water absorbent article |
| WO2009028568A1 (en) | 2007-08-28 | 2009-03-05 | Nippon Shokubai Co., Ltd. | Process for producing water-absorbing resin |
| US9062140B2 (en) | 2005-04-07 | 2015-06-23 | Nippon Shokubai Co., Ltd. | Polyacrylic acid (salt) water-absorbent resin, production process thereof, and acrylic acid used in polymerization for production of water-absorbent resin |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0655838B2 (en) * | 1988-05-24 | 1994-07-27 | 株式会社日本触媒 | Surface treatment method for water absorbent resin |
| US5883158A (en) * | 1994-08-12 | 1999-03-16 | Kao Corporation | Process for producing improved super absorbent polymer |
| JP5008790B2 (en) * | 1999-10-29 | 2012-08-22 | 株式会社日本触媒 | Surface-crosslinked water-absorbing resin and surface-crosslinking method of water-absorbing resin |
| JP5022226B2 (en) | 2004-12-10 | 2012-09-12 | 株式会社日本触媒 | Surface treatment method for water absorbent resin |
| EP1757648A1 (en) | 2005-08-23 | 2007-02-28 | Nippon Shokubai Co.,Ltd. | Disclosure of a method of surface cross-linking superabsorbent polymer particles using ultraviolet radiation and Brönsted acids |
| WO2007119730A1 (en) * | 2006-04-10 | 2007-10-25 | Nippon Shokubai Co., Ltd. | Method for production of modified water absorbent resin |
| CA2649299A1 (en) * | 2006-04-10 | 2007-10-25 | The Procter & Gamble Company | An absorbent member comprising a modified water absorbent resin |
| JP5191105B2 (en) * | 2006-06-27 | 2013-04-24 | 住友精化株式会社 | Method for producing water absorbent resin particles and water absorbent resin particles obtained thereby |
| SA08290556B1 (en) | 2007-09-07 | 2012-05-16 | نيبون شوكوباي كو. ، ليمتد | Binding Mehtod of Water Absorbent Resins |
| WO2009048160A1 (en) * | 2007-10-09 | 2009-04-16 | Nippon Shokubai Co., Ltd. | Surface treatment method for water-absorbent resin |
| JP5390509B2 (en) * | 2007-10-09 | 2014-01-15 | 株式会社日本触媒 | Surface treatment method for water absorbent resin |
| JP5524042B2 (en) | 2008-03-13 | 2014-06-18 | 株式会社日本触媒 | Method for producing particulate water-absorbing agent mainly composed of water-absorbing resin |
| US8546492B2 (en) | 2008-04-11 | 2013-10-01 | Nippon Shokubai, Co., Ltd. | Surface treatment method for water-absorbing resin and production method for water-absorbing resin |
| WO2010100936A1 (en) | 2009-03-04 | 2010-09-10 | 株式会社日本触媒 | Process for producing water-absorbing resin |
| WO2014162843A1 (en) * | 2013-04-05 | 2014-10-09 | 株式会社日本触媒 | Process for manufacturing water-absorbing material, and water -absorbing material |
-
1987
- 1987-02-24 JP JP4083487A patent/JPH078883B2/en not_active Expired - Lifetime
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7473739B2 (en) | 2004-02-05 | 2009-01-06 | Nippon Shokubai Co., Ltd. | Particulate water absorbent agent and production method thereof, and water absorbent article |
| US9062140B2 (en) | 2005-04-07 | 2015-06-23 | Nippon Shokubai Co., Ltd. | Polyacrylic acid (salt) water-absorbent resin, production process thereof, and acrylic acid used in polymerization for production of water-absorbent resin |
| WO2008120742A1 (en) | 2007-03-29 | 2008-10-09 | Nippon Shokubai Co., Ltd. | Particulate water absorbent and process for producing the same |
| WO2009028568A1 (en) | 2007-08-28 | 2009-03-05 | Nippon Shokubai Co., Ltd. | Process for producing water-absorbing resin |
| EP2690114A1 (en) | 2007-08-28 | 2014-01-29 | Nippon Shokubai Co., Ltd. | Process for producing water-absorbing resin |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6399211A (en) | 1988-04-30 |
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