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JPH03179008A - Production of water-absorptive resin of excellent durability - Google Patents

Production of water-absorptive resin of excellent durability

Info

Publication number
JPH03179008A
JPH03179008A JP31767489A JP31767489A JPH03179008A JP H03179008 A JPH03179008 A JP H03179008A JP 31767489 A JP31767489 A JP 31767489A JP 31767489 A JP31767489 A JP 31767489A JP H03179008 A JPH03179008 A JP H03179008A
Authority
JP
Japan
Prior art keywords
water
monomer
absorbent resin
crosslinking agent
weight
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
JP31767489A
Other languages
Japanese (ja)
Other versions
JP2877255B2 (en
Inventor
Kinya Nagasuna
欣也 長砂
Norisuke Suminaga
憲資 角永
Kazumasa Kimura
和正 木村
Tadao Shimomura
下村 忠生
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.)
Nippon Shokubai Co Ltd
Original Assignee
Nippon Shokubai 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 Nippon Shokubai Co Ltd filed Critical Nippon Shokubai Co Ltd
Priority to JP31767489A priority Critical patent/JP2877255B2/en
Publication of JPH03179008A publication Critical patent/JPH03179008A/en
Application granted granted Critical
Publication of JP2877255B2 publication Critical patent/JP2877255B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)

Abstract

PURPOSE:To obtain the title resin excellent in the durability and liquid permeability of a swollen gel and showing a high water absorption rate even to physiologic saline by subjecting an aqueous solution containing a water-soluble, ethylenically unsaturated monomer, a crosslinking agent and a water-soluble chain transfer agent each in a specified amount to aqueous solution polymerization. CONSTITUTION:An aqueous monomer solution of a concentration of from 30wt.% to the saturation concentration containing a water-soluble, ethylenically unsaturated monomer (e.g. acrylic acid/sodium acrylate mixture), 0.005-5mol%, based on this monomer, crosslinking agent (e.g. trimethylolpropane tri-acrylate) and 0.001-1mol%, based on this monomer, water-soluble chain transfer agent (e.g. sodium hypophosphite) is subjected to aqueous solution polymerization.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は耐久性の優れた吸水性樹脂の製造方法に関する
ものである。更に詳しくは、吸水倍率、吸水速度、膨潤
時の耐久性に優れ、膨潤ゲルのベトッキが少なく通液性
に優れた吸水性樹脂の製造方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a method for producing a water-absorbing resin with excellent durability. More specifically, the present invention relates to a method for producing a water-absorbing resin that has excellent water absorption capacity, water absorption rate, and durability during swelling, has less stickiness in the swollen gel, and has excellent liquid permeability.

かかる吸水性樹脂は安価に簡便に製造でき安全性に優れ
ているだけでなく、優れた吸水能を持っているため、生
理用品、紙オムツなどの衛生材料として、農園芸、緑化
用の保水剤として、更にその広範な吸収性物品の材料と
して広く使用できる。
Such water-absorbing resins are not only cheap and easy to produce and have excellent safety, but also have excellent water-absorbing ability, so they can be used as sanitary materials such as sanitary products and disposable diapers, and as water-retaining agents for agriculture, horticulture, and greening. Furthermore, it can be widely used as a material for a wide range of absorbent articles.

【従来の技術〕[Conventional technology]

近年、自重の数10倍から数100倍の水を吸収する吸
水性樹脂が開発され、紙おむつ、生理用ナプキン等の衝
打分野をはじめとして農林業分野、土木分野等に幅広く
用いられている。
In recent years, water-absorbing resins that absorb several tens to hundreds of times their own weight in water have been developed and are widely used in the fields of impact, such as disposable diapers and sanitary napkins, as well as in the fields of agriculture, forestry, and civil engineering.

この様な吸水性樹脂としては、例えばポリアクリル酸部
分中和物架橋体(特開昭55−84304号)、澱粉−
アクリロニトリルグラフト重合体の加水分解物(特公昭
49−43395号)、澱粉−アクリル酸エステル共重
合体の中和物(特開昭51−125468号)、酢酸ビ
ニル−アクリル酸エステル共重合体の鹸化物(特開昭5
2−14689号)、アクリロニトリル共重合体もしく
はアクリルアミド共重合体の加水分解物(特公昭53−
15959号)またはこれらの架橋体などが知られてい
る。
Examples of such water-absorbing resins include crosslinked partially neutralized polyacrylic acid (Japanese Patent Application Laid-open No. 84304/1983), starch-
Hydrolyzate of acrylonitrile graft polymer (Japanese Patent Publication No. 49-43395), neutralized product of starch-acrylic acid ester copolymer (Japanese Patent Publication No. 51-125468), saponification of vinyl acetate-acrylic acid ester copolymer Things (Unexamined Japanese Patent Publication No. 5
2-14689), hydrolyzate of acrylonitrile copolymer or acrylamide copolymer (Japanese Patent Publication No. 1983-
No. 15959) or crosslinked products thereof are known.

これら吸水性樹脂に望まれる特性としては、水性液体に
接した際の高い吸収倍率や優れた吸水速度、水性液体を
含んだ基材から液を吸い上げるための優れた吸引力など
が求められる。
Desired properties for these water-absorbing resins include high absorption capacity and excellent water absorption speed when in contact with aqueous liquids, and excellent suction power for sucking up liquids from substrates containing aqueous liquids.

しかしながら、吸水性樹脂の用途によっては、特に膨潤
ゲルの耐久性、経時安定性が上記特性に加えて必要とな
ってくる。例えば、従来の吸水性樹脂を衛生材料用とし
て紙オムツなどに用いた場合、尿を吸収した吸水性樹脂
の膨潤ゲルが経時的に劣化した分解を起こしたり、また
農園芸用などの長期間の使用で劣化し分解を起こすこと
があった。
However, depending on the use of the water-absorbing resin, durability and stability over time of the swollen gel are required in addition to the above-mentioned properties. For example, when conventional water-absorbing resins are used as sanitary materials such as disposable diapers, the swollen gel of the water-absorbing resin that absorbs urine deteriorates and decomposes over time. It deteriorated with use and could cause decomposition.

これまでに知られている吸水性樹脂の膨潤ゲルの劣化、
分解の防止方法としては吸水性樹脂に含酸素還元性無機
塩やラジカル連鎖禁止剤などを含有させる方法(特開昭
63−118375号、特開昭63−152667号)
、酸化剤を含有させる方法(特開昭63−153060
号)、硫黄含有還元剤を含有させる方法(特開昭63−
272349号)などがある。しかしながら、これらの
方法はいずれも吸水性樹脂に劣化防止のための添加剤を
加える方法であり、他の添加剤を加えるということは、
それら吸水性樹脂が衛生材料などに使用されることを考
えると、安全性の面から必ずしも好ましいらのではなか
った。
Deterioration of the swelling gel of water-absorbing resin, which has been known so far,
A method for preventing decomposition is to add oxygen-containing reducing inorganic salts, radical chain inhibitors, etc. to the water-absorbing resin (JP-A-63-118375, JP-A-63-152667).
, a method of containing an oxidizing agent (Japanese Patent Application Laid-Open No. 63-153060
No.), a method of incorporating a sulfur-containing reducing agent (Japanese Patent Application Laid-open No. 1983-
272349). However, all of these methods involve adding additives to the water-absorbing resin to prevent deterioration, and adding other additives means
Considering that these water-absorbing resins are used for sanitary materials and the like, they are not necessarily desirable from the standpoint of safety.

そこで架橋剤量を多く用いて吸水性樹脂の架橋密度を高
めることで、ゲル強度を高め耐久性を向上させる方法も
あるが、これらの吸水性樹脂は充分な耐久性を持たせる
には、高架橋のため吸水倍率が極端に低くなってしまう
のが実情であった。
Therefore, there is a method to increase the gel strength and improve the durability by increasing the crosslinking density of the water-absorbing resin by using a large amount of cross-linking agent, but in order to have sufficient durability, these water-absorbing resins must be highly cross-linked. Therefore, the actual situation was that the water absorption capacity was extremely low.

このように現在、安全性に優れ、吸水倍率が高く、且つ
耐久性に優れた吸水性樹脂は得られていない。
As described above, at present, a water-absorbing resin with excellent safety, high water absorption capacity, and excellent durability has not been obtained.

また、上記の耐久性に加えて、オムツなどに組み込んだ
際に膨潤ゲルのベトッキや通液性の低下などが問題にな
ることがあった。吸水性樹脂には水溶性となる部分(以
下、これを水可溶分と呼ぶ。)が存在し、これら水可溶
分のため、吸水後の膨潤ゲルがベトライたり、オムツな
どの吸収物品に組み込んだ際にはこのベトッキのため通
液性が低下し、新たな尿が排出された際にモレを起こす
ことがある。水可溶分量は一般に吸水倍率と正の相関関
係にあり、水ひ溶分低減のためには吸水性樹脂の架橋密
度を上げなければならず、その為に可溶分の少ない吸水
性樹脂は吸水倍率も低下してしまうのが実情であった。
In addition to the above-mentioned durability, problems such as stickiness of the swollen gel and decreased liquid permeability may arise when the gel is incorporated into a diaper or the like. Water-absorbing resin has a water-soluble portion (hereinafter referred to as water-soluble portion), and because of these water-soluble portions, the swollen gel may become sticky after absorbing water, and may be difficult to absorb on absorbent articles such as diapers. When incorporated, this stickiness reduces fluid permeability and may cause leakage when new urine is excreted. The water-soluble content generally has a positive correlation with the water absorption capacity, and in order to reduce the water-soluble content, it is necessary to increase the crosslinking density of the water-absorbing resin. The reality is that the water absorption capacity also decreases.

しかして、この様な吸水性樹脂において架橋剤の配合量
を増加すればするほど耐久性が向上することは公知であ
るが、架橋剤の量が増えればそれだけ吸水倍率が低下す
るという問題点があった。
However, it is well known that the greater the amount of crosslinking agent blended in such water-absorbing resins, the better the durability, but the problem is that the water absorption capacity decreases as the amount of crosslinking agent increases. there were.

また吸水性樹脂の製造時に連鎖移動剤を使用することに
より吸水倍率を向上させる技術が開示されている。(U
 S P 4698404 )。しかしこの場合、水や
生理食塩水に対する吸水倍率は確かに向上するが人尿に
対しては吸水倍率の増加は殆ど認められていない。
Furthermore, a technique has been disclosed in which the water absorption capacity is improved by using a chain transfer agent during the production of a water absorbent resin. (U
S P 4698404). However, in this case, although the water absorption capacity for water and physiological saline is certainly improved, there is almost no increase in the water absorption capacity for human urine.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

本発明は上記現状に鑑みなされたものである。 The present invention has been made in view of the above-mentioned current situation.

従って本発明の目的は耐久性の優れた吸水性樹脂の製造
方法を提供することにある。
Therefore, an object of the present invention is to provide a method for producing a water-absorbing resin with excellent durability.

本発明の他の目的は、生理食塩水に対してもまた特に人
尿に対しても高い吸水倍率を示し、使い捨てオムツに使
用した際に優れた耐久性を示し、且つ該オムツでの戻り
量も少なく、ゲルのベトッキ感が少なく通液性に優れた
吸水性樹脂の製造方法を提供することにある。
Another object of the present invention is to exhibit a high water absorption capacity for both physiological saline and especially human urine, to exhibit excellent durability when used in disposable diapers, and to reduce the amount of water returned by the diaper. It is an object of the present invention to provide a method for producing a water-absorbing resin which has less sticky feeling and has excellent liquid permeability.

〔課題を解決するための手段及び作用〕本発明者らは、
上記課題を解決すべく鋭意検討した結果、 (1)特定量の架橋剤(B)と水溶性連鎖移動剤(C1
を含有した水溶性エチレン性不飽和単量体(A)水溶液
を特定の濃度範囲で水溶l後重合することにより、吸水
倍率を高く保ちつつ、耐久性が向上し、水可溶分の分子
量の低下に伴いゲルのベトッキ感や通液性も改善された
良好な吸水性樹脂(D)が生産性よく得られること、 (2)  さらに上記(1)の製造方法で得られた吸水
性樹脂(D)の表面近傍を親水性架橋剤(E)で架橋さ
せることにより、更に優れた吸水特性の改善効果を示し
、高い吸水倍率を保ちつつ、より耐久性、ゲルのベトッ
キ感や通液性が向上し、吸水特性に優れた吸水性樹脂(
F)が得られること、を見い出し本発明を完成するに至
った。
[Means and effects for solving the problem] The present inventors,
As a result of intensive studies to solve the above problems, we found that (1) specific amounts of crosslinking agent (B) and water-soluble chain transfer agent (C1)
By polymerizing a water-soluble ethylenically unsaturated monomer (A) aqueous solution containing the following in a specific concentration range, durability is improved while maintaining a high water absorption capacity, and the molecular weight of the water-soluble component is reduced. (2) Furthermore, the water-absorbing resin (D) obtained by the production method of (1) above can be obtained with good productivity, and the sticky feeling and liquid permeability of the gel are also improved as the gel decreases. By cross-linking the vicinity of the surface of D) with a hydrophilic cross-linking agent (E), an even more excellent effect of improving water absorption properties is exhibited, and while maintaining a high water absorption capacity, the gel becomes more durable, has a sticky feel, and has improved liquid permeability. Water-absorbing resin with improved water-absorbing properties (
The present invention was completed based on the discovery that F) can be obtained.

即ち、本発明は、 +7 水溶性エチレン性不飽和単量体(Alおよび該単量体(
A)に対し、架橋剤(B)0.005〜5モル%、水溶
性連鎖移動剤(C)0.001〜1モル%を含有する3
0重量%〜飽和濃度の該単量体(A)水溶液を    
   、水溶液重合させることを特徴とする耐久性の優
れた吸水性樹脂(D)の製造方法。
That is, the present invention provides +7 water-soluble ethylenically unsaturated monomers (Al and the monomers (
3 containing 0.005 to 5 mol% of the crosslinking agent (B) and 0.001 to 1 mol% of the water-soluble chain transfer agent (C) based on A).
The monomer (A) aqueous solution with a concentration of 0% by weight to saturation is
A method for producing a water-absorbing resin (D) with excellent durability, which is characterized by carrying out aqueous solution polymerization.

並びに、 水溶性エチレン性不飽和単量体(A)および該単量体(
A)に対し、架橋剤(BIo、005〜5モル%、水溶
性連鎖移動剤(C)0.001〜1モル%を含有する3
0重量%〜飽和濃度の該単量体(A)水溶液を    
   、水溶液重合させて得た吸水性樹脂(D)の表面
近傍を吸水性樹脂中の官能基と反応しうる親水性架橋剤
(E)で架橋させることを特徴とする耐久性の優れた吸
水性樹脂(F)の製造方法。
and a water-soluble ethylenically unsaturated monomer (A) and the monomer (
3 containing a crosslinking agent (BIo, 005 to 5 mol%, and a water-soluble chain transfer agent (C) 0.001 to 1 mol%, based on A).
The monomer (A) aqueous solution with a concentration of 0% by weight to saturation is
, a water absorbent with excellent durability characterized by crosslinking the surface vicinity of the water absorbent resin (D) obtained by aqueous solution polymerization with a hydrophilic crosslinking agent (E) that can react with a functional group in the water absorbent resin. Method for producing resin (F).

に関すものである。It is related to.

本発明をさらに詳しく説明する。The present invention will be explained in more detail.

本発明に用いる水溶性エチレン性不飽和単量体(A〉(
以下、単量体(A))としては官能基を有するものであ
り、例えばアクリル酸、メタクリル酸、マレイン酸、フ
マール酸、クロトン酸、イタコン酸、ビニルベンゼンス
ルホン酸、2−(メタ)アクリルアミド−2−メチルプ
ロパンスルホン酸2−(メタ)アクリロイルエタンスル
ホン酸、2−(メタ)アクリロイルプロパンスルホン酸
、及びそれらのアルカリ金属塩、アンモニウム塩、アク
リルアミド、メタクリルアミド、2−ヒドロキシエチル
(メタ)アクリレート、メトキシポリエチレングリコー
ル(メタ)アクリレート、N、 N−ジメチルアミノエ
チル(メタ)アクリレート、N。
Water-soluble ethylenically unsaturated monomer (A) used in the present invention
Hereinafter, the monomer (A)) is one having a functional group, such as acrylic acid, methacrylic acid, maleic acid, fumaric acid, crotonic acid, itaconic acid, vinylbenzenesulfonic acid, 2-(meth)acrylamide- 2-methylpropanesulfonic acid 2-(meth)acryloylethanesulfonic acid, 2-(meth)acryloylpropanesulfonic acid, and their alkali metal salts, ammonium salts, acrylamide, methacrylamide, 2-hydroxyethyl (meth)acrylate, Methoxypolyethylene glycol (meth)acrylate, N, N-dimethylaminoethyl (meth)acrylate, N.

N−ジエチルアミノプロビル(メタ)アクリレート、 
N、N−ジエチルアミノプロビル(メタ)アクリルアミ
ド、及びそれらの四級塩などを挙げることができ、これ
らの群から選ばれる少なくとも1種のものが使用できる
N-diethylaminopropyl (meth)acrylate,
Examples include N,N-diethylaminopropyl (meth)acrylamide and quaternary salts thereof, and at least one selected from these groups can be used.

なかでも上記の単量体(A)の内、得られる吸水性樹脂
の性能やコストの点からアクリル酸を主成分として用い
ることが好ましく、その際はアクリル酸及びそのアルカ
リ番属塩および/またはアンモニウム塩の含有率は単量
体(A)の内で50重量%以上とすることが好ましく、
更に好ましくは75重量%以上とすることである。
Among the above monomers (A), it is preferable to use acrylic acid as the main component from the viewpoint of the performance and cost of the resulting water absorbent resin, and in this case, acrylic acid and its alkali salts and/or The content of ammonium salt is preferably 50% by weight or more in the monomer (A),
More preferably, the content is 75% by weight or more.

また本発明において耐久性の優れた吸水性樹脂を得るに
は分子内に2個以上の重合性不飽和基や反応性官能基を
有する架橋剤CB)を特定量用いることが必須である。
Further, in the present invention, in order to obtain a water-absorbing resin with excellent durability, it is essential to use a specific amount of a crosslinking agent CB) having two or more polymerizable unsaturated groups or reactive functional groups in the molecule.

これら架橋剤(B)として例えば、分子内に2個以上の
重合性不飽和基を有する化合物として、例えばN、N’
 −メチレンビスアクリルアミド、(ポリ〉エチレング
リコールジ(メタ)アクリレート、(ポリ)ブロビレン
グリコールジ(メタ)アクリレート、グリセリントリ(
メタ)アクリレート、グリセリンアクリレートメタクリ
レート、(メタ)アクリル酸多価金属塩トリメチロール
プロパントリ(メタ)アクリレート、トリアリルアミン
、トリアリルシアヌレート、トリアリルイソシアヌレー
ト、トリアリルホスフェート等を挙げることができる。
Examples of these crosslinking agents (B) include compounds having two or more polymerizable unsaturated groups in the molecule, such as N, N'
- Methylene bisacrylamide, (poly>ethylene glycol di(meth)acrylate, (poly)brobylene glycol di(meth)acrylate, glycerin tri(
Examples include meth)acrylate, glycerin acrylate methacrylate, (meth)acrylic acid polyvalent metal salt trimethylolpropane tri(meth)acrylate, triallylamine, triallyl cyanurate, triallyl isocyanurate, triallyl phosphate, and the like.

また反応性官能基を有するものとしては、例えば、単量
体ングリコール、ジエチレングリコール、トリエチレン
グリコール、ポリエチレングリコール、プロピレングリ
コール、ジプロピレングリコール、ポリプロピレングリ
コール、グリセリン等の多価アルコール類:(ポリ)エ
チレングリコールジグリシジルエーテル、グリセロール
ポリグリシジルエーテル等の多価グリシジル化合物;エ
チレンジアミン、ポリエチレンイミン等の多価アミン;
その他、多価オキサゾリン化合物、ハロエポキシ化合物
、多価インシアネート、多価金属塩等があり、また分子
内に重合性不飽和基と反応性官能基を合わせ持つものと
してはグリシジル(メタ)アクリレート、N−メチロー
ル(メタ)アクリルアミド等を例示することが出来る。
Examples of those having reactive functional groups include polyhydric alcohols such as monomeric glycol, diethylene glycol, triethylene glycol, polyethylene glycol, propylene glycol, dipropylene glycol, polypropylene glycol, and glycerin: (poly)ethylene Polyvalent glycidyl compounds such as glycol diglycidyl ether and glycerol polyglycidyl ether; polyvalent amines such as ethylenediamine and polyethyleneimine;
In addition, there are polyvalent oxazoline compounds, haloepoxy compounds, polyvalent incyanates, polyvalent metal salts, etc. Also, compounds having both a polymerizable unsaturated group and a reactive functional group in the molecule include glycidyl (meth)acrylate, N -Methylol (meth)acrylamide etc. can be exemplified.

これらの架橋剤(B)のなかでは、分子内に2個以上の
重合性不飽和基を有する化合物を用いることが得られる
吸水性樹脂の耐久性や吸水特性の点から特に好ましい。
Among these crosslinking agents (B), it is particularly preferable to use a compound having two or more polymerizable unsaturated groups in the molecule from the viewpoint of the durability and water absorption characteristics of the resulting water absorbent resin.

これら架橋剤(B)の本発明に於ける使用量は、目的と
する吸水倍率の吸水性を得るために水溶性連鎖移動剤(
C)を用いない他は同一条件で行う場合の架橋剤の使用
量に比べて、2〜100倍モル、更に好ましくは4〜1
0倍モルである。具体的には、架橋剤(B)の使用量は
単量体(A)に対して0.005〜5モル%である。こ
れら架橋剤(B)の使用量が0.005モル%未満では
得られた吸水性樹脂の吸水倍率は高いものが得られるが
、耐久性に劣り且つ水可溶骨が多くその分子量も高いた
めゲルのベトッキ感や通液性に劣ったものとなる。また
5モル%を越えて多く使用すると吸水倍率が非常に低い
ものとなってしまう。また架橋剤の使用量は後述する水
溶性連鎖移動剤(C)の使用量にもよるが、好ましくは
0.02〜1モル%であり、更に好ましくは0.04〜
0.4モル%であり、更により好ましくは0.08〜0
.2モル%である。
The amount of these crosslinking agents (B) used in the present invention is determined by adjusting the amount of the water-soluble chain transfer agent (
Compared to the amount of crosslinking agent used under the same conditions except that C) is not used, the amount is 2 to 100 times, more preferably 4 to 1
It is 0 times the mole. Specifically, the amount of the crosslinking agent (B) used is 0.005 to 5 mol% based on the monomer (A). If the amount of crosslinking agent (B) used is less than 0.005 mol%, the resulting water absorbent resin will have a high water absorption capacity, but will have poor durability, and will have a large amount of water-soluble bone and a high molecular weight. The gel becomes sticky and has poor liquid permeability. Moreover, if it is used in an amount exceeding 5 mol %, the water absorption capacity becomes extremely low. The amount of the crosslinking agent used depends on the amount of the water-soluble chain transfer agent (C) described below, but is preferably 0.02 to 1 mol%, more preferably 0.04 to 1 mol%.
0.4 mol%, even more preferably 0.08 to 0
.. It is 2 mol%.

また上記架橋剤(B)の他に、グラフト重合によって架
橋を形成させる方法を併用してもよい。この様な方法と
して、セルロース、澱粉、ポリビニルアルコール等の親
水性高分子の存在下に単量体(A)水溶液を重合させ、
重合時にグラフト重合に起因する架橋を形成させる方法
が挙げられ、これらの水溶性高分子は単量体(A)に対
して1〜50重量%の範囲で用いるのが好ましい。
In addition to the above-mentioned crosslinking agent (B), a method of forming crosslinks by graft polymerization may be used in combination. As such a method, an aqueous monomer (A) solution is polymerized in the presence of a hydrophilic polymer such as cellulose, starch, or polyvinyl alcohol,
Examples include a method of forming crosslinks due to graft polymerization during polymerization, and these water-soluble polymers are preferably used in an amount of 1 to 50% by weight based on the monomer (A).

本発明は特定量の水溶性連鎖移動剤(C)を用い性連鎖
移動剤(C)を選び、且つ通常の製造方法に比べて2〜
100倍モルと多量の架橋剤を使用し高架橋として重合
を行うことで初めて、耐久性が非常に優れ、生理食塩水
のみならず人尿に対してち高い吸水倍率を示し、また水
可溶分の分子量が低いため、ゲルのベトッキ感や適法性
の低下などの悪影響が少ない等と言う、優れた吸水性樹
脂が得られる。
In the present invention, a specific amount of water-soluble chain transfer agent (C) is used, a specific amount of water-soluble chain transfer agent (C) is selected, and compared to the usual manufacturing method,
By using a large amount of cross-linking agent (100 times the mole) and performing polymerization as a highly cross-linked polymer, it has excellent durability, exhibits a high water absorption capacity not only for physiological saline but also for human urine, and has a high water-soluble content. Because of its low molecular weight, it is possible to obtain an excellent water-absorbing resin that has few negative effects such as a sticky gel feel or a decrease in legality.

本発明に使用する水溶性連鎖移動剤(C)としては、水
または水溶性エチレン性不飽和単量体に溶解するもので
あれば特に制限されず、チオール類、チオール酸類、2
級アルコール類、アミン類、次亜燐酸塩類などを挙げる
ことができ、具体的にはメルカプトエタノール、メルカ
プトプロパツール、ドデシルメルカプタン、チオグリコ
ール酸、チオリンゴ酸、3−メルカプトプロピオン酸、
イソプロパツール、次亜燐酸ナトリウム、蟻酸、および
それらの塩類が使用され、これら群から選ばれる1種ま
たは2種以上が用いられるが、その効果から次亜燐酸ナ
トリウムなどの次亜燐酸塩を用いることが好ましい。
The water-soluble chain transfer agent (C) used in the present invention is not particularly limited as long as it dissolves in water or a water-soluble ethylenically unsaturated monomer, and includes thiols, thiol acids,
alcohols, amines, hypophosphites, etc., specifically mercaptoethanol, mercaptopropanol, dodecylmercaptan, thioglycolic acid, thiomalic acid, 3-mercaptopropionic acid,
Isopropanol, sodium hypophosphite, formic acid, and their salts are used, and one or more types selected from these groups are used, but hypophosphites such as sodium hypophosphite are used due to their effectiveness. It is preferable.

水溶性連鎖移動剤(C)の使用量は水溶性連鎖移動剤の
種類や使用量、単量体(A)水溶液の濃度にもよるが、
単量体(A)に対して0.00]〜1モル%であり、好
ましくは0.005〜0.3モル高く吸水倍率が低くな
りすぎて好ましくない。
The amount of water-soluble chain transfer agent (C) used depends on the type and amount of water-soluble chain transfer agent used, and the concentration of the monomer (A) aqueous solution.
The amount is 0.00] to 1 mol %, preferably 0.005 to 0.3 mol %, based on the monomer (A), which is not preferable because the water absorption capacity becomes too low.

また1モル%を越えて多く使用すると水可溶分が増加し
、耐久性がかえって低下するので好ましくない。
Moreover, if it is used in an amount exceeding 1 mol %, the water-soluble content will increase and the durability will actually decrease, which is not preferable.

本発明に用いられる単量体(A>水溶液の濃度としては
30重量%〜飽和濃度、より好ましくは35重量%〜飽
和濃度の範囲である。30重量%未溝の濃度では単位反
応容積当りの生産性が下がり、また乾燥工程にも時間を
要し、生産性が低下して工業的観点から好ましくない。
The monomer used in the present invention (A> The concentration of the aqueous solution is in the range of 30% by weight to saturated concentration, more preferably 35% by weight to saturated concentration. At a concentration of 30% by weight, the concentration is in the range of 30% by weight to saturated concentration. This is unfavorable from an industrial point of view because the productivity decreases and the drying process also takes time.

従来の重合方法では生産性向上のため飽和濃度付近で重
合を行うと自己架橋などの不要な反応が起こり吸水倍率
が低下するため、重合時に使用できる架橋剤(B)の量
が限られ、そのため耐久性に乏しい吸水性樹脂しか得ら
れなかった。しかし本発明の方法によれば、水溶性連鎖
移動剤(C)の使用量を選ぶことによって自己架橋反応
が抑制され、架橋剤CB)の使用量が増やせるので耐久
性に優れた高吸水倍率の吸水性樹脂を高濃度で生産性よ
く製造することができる。
In conventional polymerization methods, when polymerization is performed near saturation concentration to improve productivity, unnecessary reactions such as self-crosslinking occur and the water absorption capacity decreases, which limits the amount of crosslinking agent (B) that can be used during polymerization. Only a water absorbent resin with poor durability was obtained. However, according to the method of the present invention, by selecting the amount of the water-soluble chain transfer agent (C) used, the self-crosslinking reaction is suppressed, and the amount of the crosslinking agent CB) used can be increased, resulting in a high water absorption capacity with excellent durability. Water-absorbing resin can be produced at high concentration and with good productivity.

また必要に応じて単量体(A)水溶液に増粘剤を使用し
てもよい。この様な増粘剤としては、例えばポリビニル
ピロリドン、ポリアクリルアミド、メチルセルロース、
ヒドロキシエチルセルロース等を挙げることができる。
Further, a thickener may be used in the monomer (A) aqueous solution if necessary. Examples of such thickeners include polyvinylpyrrolidone, polyacrylamide, methylcellulose,
Examples include hydroxyethylcellulose.

本発明に於て単量体(A)水溶液を重合させ吸水性樹脂
を得る重合方法としては、公知の重合技術、例えば水溶
液重合、逆相懸濁重合、沈殿重合、塊状重合、紫外線や
電子線などの活性エネルギーによる重合などの、中で、
性能面や生産性やコスト面で優れた吸水性樹脂を得る方
法として水溶液重合が採用される。水溶液重合を行う方
法としては、例えば型枠の中で行う注型重合(特公昭4
8−42466) 、ベルトコンベアー上で重合する方
法(特開昭58−49714)、含水ゲル状重合体を細
分化できるような撹拌羽根を有するニダーなどの中で重
合する方法(特開昭57−34101)などが例示でき
る。
In the present invention, known polymerization techniques such as aqueous solution polymerization, reverse phase suspension polymerization, precipitation polymerization, bulk polymerization, ultraviolet ray or electron beam polymerization can be used to polymerize the monomer (A) aqueous solution to obtain the water absorbent resin. Among them, such as polymerization with active energies such as
Aqueous solution polymerization is used as a method to obtain water-absorbing resins that are excellent in terms of performance, productivity, and cost. As a method for carrying out aqueous solution polymerization, for example, cast polymerization carried out in a mold (Tokuko Kouko 4
8-42466), a method of polymerizing on a belt conveyor (JP-A-58-49714), a method of polymerizing in a kneader or the like having stirring blades capable of dividing the hydrogel polymer into small pieces (JP-A-57-1999), 34101), etc. can be exemplified.

この様な水溶液重合が行われる場合、水溶性連鎖移動剤
(C)による均一な連鎖移動反応や架橋剤(B)による
均一な架橋反応を進行させ、より性能の優れた吸水性樹
脂を得るためには、重合熱が均一に除去されることが好
ましい。そのためには重合ゲルが一体となる重合法では
なく、重合の開始から終了までの全時間あるいは一部で
、好ましくは全時間で反応系の重合ゲルが撹拌され重合
熱の均−な除去がなされることが好ましく、よって重合
反応は回転撹拌翼を有する反応容器内で行われることが
好ましい。回転撹拌翼を有する反応容器としては、特に
制限はないが、重合ゲルに対する撹拌力が大きいものが
好ましく、重合の進行に伴い生成する重合ゲルを回転撹
拌翼によって剪断力を与える反応機なども例示でき、ま
た撹拌力を大きくするためには回転撹拌翼は複数である
ことがより好ましい。反応機としては例えば−軸の混練
機、−軸の押出機、双腕型ニーダ−および三軸ニーダ−
などが挙げられる。また双腕型ニーダーを用いると、重
合ゲルを細かく細分化し重合の全時間にわたり均一に撹
拌ができ重合熱の均一な除去を行えるので、より性能の
優れた吸水性樹脂が得られるので好ましい。
When such aqueous polymerization is performed, in order to proceed with a uniform chain transfer reaction using the water-soluble chain transfer agent (C) and a uniform crosslinking reaction using the crosslinking agent (B), to obtain a water absorbent resin with better performance. It is preferable that the heat of polymerization be removed uniformly. For this purpose, rather than using a polymerization method in which the polymer gel is integrated, the polymer gel in the reaction system is stirred during all or part of the time from the start to the end of polymerization, preferably the entire time, to uniformly remove the polymerization heat. Therefore, it is preferable that the polymerization reaction is carried out in a reaction vessel having a rotating stirring blade. There are no particular restrictions on the reaction vessel having a rotating stirring blade, but one that has a large stirring force for the polymer gel is preferable, and examples include a reactor that uses a rotating stirring blade to apply shearing force to the polymer gel that is produced as the polymerization progresses. In addition, in order to increase the stirring power, it is more preferable to use a plurality of rotating stirring blades. Examples of the reactor include a -shaft kneader, a -shaft extruder, a double-arm kneader, and a three-shaft kneader.
Examples include. Further, it is preferable to use a double-arm kneader because the polymerized gel can be finely divided and stirred uniformly throughout the entire polymerization period, and the heat of polymerization can be uniformly removed, resulting in a water-absorbing resin with better performance.

本発明に於て、水溶液重合に使用されるラジカル重合開
始剤としては水溶性であれば特に制限さハイドロパーオ
キサイド、クメンハイドロパーオキサイド等のハイドロ
パーオキサイド;2.2°−アゾビス(2−アミジノプ
ロパン)二塩酸塩等のアゾ化合物;その他、第二セリウ
ム塩、過マンガン酸塩等が挙げられる。中でも得られた
吸水性樹脂の性能面や分解生成物の安全性等の点から、
過硫酸塩、過酸化水素、アゾ化合物よりなる群から選ば
れる1種または2種以上が好ましい。
In the present invention, radical polymerization initiators used in aqueous solution polymerization are particularly limited as long as they are water-soluble; hydroperoxides such as hydroperoxide and cumene hydroperoxide; Azo compounds such as (propane) dihydrochloride; others include ceric salts, permanganates, and the like. Among them, from the viewpoint of the performance of the obtained water absorbent resin and the safety of decomposition products,
One or more selected from the group consisting of persulfates, hydrogen peroxide, and azo compounds are preferred.

またラジカル重合開始剤が酸化性ラジカル重合開始剤の
場合、還元剤を併用してレドックス系開始剤として用い
ても良い。用いられる還元剤としては、例えば亜硫酸ナ
トリウム、亜硫酸水素ナトリウム等の亜硫酸(水素)塩
;チオ硫酸ナトリウム等のチオ硫酸塩;亜ニチオン酸塩
;硫酸第一銅、硫酸第一鉄等の金属塩;β−アスコルビ
ン酸等の有機還元剤;アニリン、モノエタノールアミン
等のアミン類が挙げられる。
Further, when the radical polymerization initiator is an oxidizing radical polymerization initiator, it may be used as a redox initiator in combination with a reducing agent. Examples of the reducing agent used include sulfite (hydrogen) salts such as sodium sulfite and sodium hydrogen sulfite; thiosulfates such as sodium thiosulfate; dithionites; metal salts such as cuprous sulfate and ferrous sulfate; Examples include organic reducing agents such as β-ascorbic acid; amines such as aniline and monoethanolamine.

ラジカル重合開始剤の使用量は広い範囲とすることがで
きるが、通常、単量体(A)に対して0゜001〜2モ
ル%の範囲とするのが好ましく、更に好ましくは0.0
1〜0.5モル%の範囲である。この使用量が0.00
1モル%未満では重合時間や誘導期間が長くなり、また
残存モノマーも多くなり易く好ましくない。また従来の
重合方法では、残存モノマー低減や誘導期間、重合時間
の短縮のため、重合開始剤量を増加させると自己架橋な
どの不要な反応が起こり吸水倍率が低下するため、使用
できる開始剤量も限られてきていたが、本発明の方法に
よれば、かかる欠点は改善され開始剤量は増加させても
高性能の吸水性樹脂が得られる。しかし2モル%より多
く使用しても、添加量に見合った効果が少ないばかりか
、重合反応の制御が困難となってしまうので好ましくな
い。
The amount of the radical polymerization initiator used can vary widely, but it is usually preferably in the range of 0.001 to 2 mol%, more preferably 0.0001 to 2 mol%, based on the monomer (A).
It is in the range of 1 to 0.5 mol%. This usage amount is 0.00
If it is less than 1 mol %, the polymerization time and induction period will become long, and the amount of residual monomer will also tend to increase, which is not preferable. In addition, in conventional polymerization methods, increasing the amount of polymerization initiator to reduce residual monomers, shorten the induction period, and shorten polymerization time causes unnecessary reactions such as self-crosslinking and reduces water absorption capacity, so the amount of initiator that can be used is However, according to the method of the present invention, these drawbacks are improved and a high-performance water absorbent resin can be obtained even if the amount of initiator is increased. However, even if it is used in an amount greater than 2 mol %, not only will the effect commensurate with the amount added be small, but it will also become difficult to control the polymerization reaction, which is not preferable.

本発明で得られる吸水性樹脂は高濃度で重合させその重
合熱により乾燥と重合を同時に行っても良いし、重合後
の含水率によっては得られた含水ゲルを更に乾燥するこ
とによって吸水性樹脂として使用してもよい。乾燥方法
としては公知の乾燥方法を用いることができ、例えば有
機溶剤中での共沸脱水による方法、強制通風炉、減圧乾
燥器、マイクロ波乾燥器、赤外線乾燥器、所定温度に加
熱されたベルトまたはドラムドライヤー等を用いる乾燥
方法が挙げられる。これらの乾燥方法を用い、重合後の
含水ゲルを80℃以上で、より好性樹脂の劣化が起こる
場合があるので注意を要する。
The water-absorbent resin obtained in the present invention may be polymerized at a high concentration and dried and polymerized simultaneously using the polymerization heat, or depending on the water content after polymerization, the obtained water-containing gel may be further dried to form a water-absorbent resin. May be used as As a drying method, a known drying method can be used, such as a method using azeotropic dehydration in an organic solvent, a forced draft oven, a vacuum dryer, a microwave dryer, an infrared dryer, or a belt heated to a predetermined temperature. Alternatively, a drying method using a drum dryer or the like can be mentioned. If these drying methods are used to heat the hydrogel after polymerization to 80° C. or higher, the hydrophilic resin may deteriorate further, so care must be taken.

また以上の様に重合、乾燥して得られた吸水性樹脂は、
必要により粉砕およびまたは分級して使用される。
In addition, the water-absorbing resin obtained by polymerizing and drying as described above is
It is used after being crushed and/or classified if necessary.

さらに本発明は、前記製造方法によって得られる吸水性
樹脂(D)の表面近傍を特定の親水性架橋剤(E)で架
橋させた吸水性樹脂(F)の製造方法をも提供する0本
発明の前記製造方法によって得られた吸水性樹脂(D)
は、 従来の吸水性樹脂に比べて著しい吸水特性の改善効果を
示し、表面近傍を架橋した吸水性樹脂(F)は表面近傍
を架橋する前の吸水性樹脂CD)に比べ、さらに耐久性
に優れ吸水特性に優れたものになる。
Furthermore, the present invention also provides a method for producing a water absorbent resin (F) in which the vicinity of the surface of the water absorbent resin (D) obtained by the above production method is crosslinked with a specific hydrophilic crosslinking agent (E). Water absorbent resin (D) obtained by the above manufacturing method
shows a remarkable improvement in water absorption properties compared to conventional water absorbent resins, and the water absorbent resin (F) that has been crosslinked near the surface has more durability than the water absorbent resin (CD) that has not been crosslinked near the surface. It has excellent water absorption properties.

本発明に於て使用される親水性架橋剤(E)としてはカ
ルボキシル基と反応しうる官能基を1分子中に2個以上
有する化合物(E−1)及び/または多価金属塩(E−
2)である。例えば吸水性樹脂(D)がカルボキシル基
を有する場合には、化合物(E−1)としてはエチレン
グリコール、ジエチレングリコール、トリエチレングリ
コール、テトラエチレングリコール、ポリエチレングリ
コール、1.4−ブタンジオール、1.5−ベンタンジ
オール、1.6−ヘキサンジオール、ネオペンチルグリ
コール、プロピレングリコール、グリセリン、ポリグリ
セリン、トリメチロールプロパン、ペンタエリスリトー
ル、ソルビトール、ポリビニルアルコール等の多価アル
コール化合物;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、グ
リセロールポリグリシジルエーテル、ジグリセロールボ
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、プロピレングリコールジグリシジルエーテ
ル、ポリプロピレングリコールジグリシジルエーテル等
の多価グリシジルエーテル化合物;エチレンジアミン、
ジエチレントリアミン、トリエチレンテトラミン、ポリ
エチレンイミン等の多価アミン化合物;1.2−エチレ
ンビスオキサゾリン、ポリイソプロペニルオキサゾリン
等の多価オキサゾリン化合物;エビクロロヒドリンなど
のハロエポキシ化合物;その他の多価アジリジン化合物
、多価インシアネート化合物などが挙げられ、多価金属
塩(E−2)としては亜鉛、カルシウム、マグネシウム
、アルミニウム、鉄、ジルコニウム等の水酸化物及び塩
化物などが挙げられる。これらの群より1種または2種
以上を用いることが好ましく、中でも化合物(E−1)
を必須に用いることが好ましく、特に多価アルコール類
、多価グリシジル化合物類、多価アミン類を親水性架橋
剤(E)として用いることが表面架橋効果の点から好ま
しい。また親水性架橋剤(E)として、化合物(E−1
>と多価金属塩(E−2)を併用して用いて混合性を向
上させても構わない。
The hydrophilic crosslinking agent (E) used in the present invention is a compound (E-1) having two or more functional groups capable of reacting with a carboxyl group in one molecule and/or a polyvalent metal salt (E-1).
2). For example, when the water-absorbing resin (D) has a carboxyl group, the compound (E-1) may include ethylene glycol, diethylene glycol, triethylene glycol, tetraethylene glycol, polyethylene glycol, 1.4-butanediol, 1.5 - Polyhydric alcohol compounds such as bentanediol, 1,6-hexanediol, neopentyl glycol, propylene glycol, glycerin, polyglycerin, trimethylolpropane, pentaerythritol, sorbitol, polyvinyl alcohol; ethylene glycol diglycidyl ether, polyethylene glycol di Polyvalent glycidyl ether compounds such as glycidyl ether, glycerol polyglycidyl ether, diglycerol polyglycidyl ether, polyglycerol polyglycidyl ether, propylene glycol diglycidyl ether, polypropylene glycol diglycidyl ether; ethylene diamine,
Polyvalent amine compounds such as diethylenetriamine, triethylenetetramine, polyethyleneimine; polyvalent oxazoline compounds such as 1,2-ethylenebisoxazoline and polyisopropenyloxazoline; haloepoxy compounds such as shrimp chlorohydrin; other polyvalent aziridine compounds, Examples include polyvalent incyanate compounds, and examples of the polyvalent metal salt (E-2) include hydroxides and chlorides of zinc, calcium, magnesium, aluminum, iron, zirconium, and the like. It is preferable to use one or more types from these groups, and among them, compound (E-1)
It is preferable to essentially use polyvalent alcohols, polyvalent glycidyl compounds, and polyvalent amines as the hydrophilic crosslinking agent (E) from the viewpoint of the surface crosslinking effect. In addition, as a hydrophilic crosslinking agent (E), compound (E-1
> and a polyvalent metal salt (E-2) may be used in combination to improve the miscibility.

本発明に於て使用された親水性架橋剤(E)の量は上記
、製造方法によって得られた吸水性樹脂(D)100重
量部に対して、0.005〜5重量部、好ましくは0.
01〜1重量部の範囲の割合性架橋剤(E)の量が5重
量部を越える場合、不経済となるばかりか、未反応の親
水性架橋剤(E)が得られた吸水性樹脂(F)に残存す
る可能性がある上に、適正な架橋効果を達成する上で過
剰量となり得られる吸水性樹脂(F)の吸水倍率は小さ
くなり好ましくない。また0、005重量部未満の少な
い量では本発明の効果が得られにくい。
The amount of the hydrophilic crosslinking agent (E) used in the present invention is 0.005 to 5 parts by weight, preferably 0.005 to 5 parts by weight, based on 100 parts by weight of the water absorbent resin (D) obtained by the above manufacturing method ..
If the amount of the proportionate crosslinking agent (E) in the range of 0.01 to 1 part by weight exceeds 5 parts by weight, it will not only be uneconomical, but also unreacted hydrophilic crosslinking agent (E) will be used in the obtained water absorbent resin ( In addition to the possibility that the water-absorbing resin (F) may remain in the water-absorbing resin (F), an excessive amount of the water-absorbing resin (F) to achieve an appropriate crosslinking effect will reduce the water absorption capacity of the water-absorbing resin (F), which is not preferable. Furthermore, if the amount is as small as less than 0,005 parts by weight, it is difficult to obtain the effects of the present invention.

本発明に於て、吸水性樹脂(D)と親水性架橋剤(E)
とを混合する際、水及び/または親水性有機溶剤(G)
を用いてもよい。
In the present invention, water absorbent resin (D) and hydrophilic crosslinking agent (E)
When mixing with water and/or hydrophilic organic solvent (G)
may also be used.

本発明に於て、水の使用量は吸水性樹脂(D)  1d
9り 00重量部当り20重量部#キ、好ましくは0゜5〜1
0重量部の範囲の割合である。
In the present invention, the amount of water used is 1 d of water absorbent resin (D)
20 parts by weight per 900 parts by weight, preferably 0°5-1
The proportion is in the range of 0 parts by weight.

また親水性有機溶剤(G)として例えば、メタノール、
エタノール、n−プロパツール、1so−プロパツール
、n−ブタノール、1so−ブタノール、t−ブタノー
ル等の低級アルコール類;アセトン、メチルエチルケト
ン、メチルブチルケトン等のケトン類;ジオキサン、テ
トラヒドロフラン等のエーテル類、 N、N−ジメチル
ホルムアミド等のアミド類;ジメチルスルホキシド等の
スルホキシド類を挙げることができ、その使用量は吸水
性樹脂(D)100重量部に対して0〜20重量部、好
ましくは0〜8重量部の範囲の割合である。
Further, as the hydrophilic organic solvent (G), for example, methanol,
Lower alcohols such as ethanol, n-propertool, 1so-propertool, n-butanol, 1so-butanol, t-butanol; Ketones such as acetone, methyl ethyl ketone, methyl butyl ketone; Ethers such as dioxane, tetrahydrofuran, N , amides such as N-dimethylformamide; and sulfoxides such as dimethyl sulfoxide; the amount used is 0 to 20 parts by weight, preferably 0 to 8 parts by weight, based on 100 parts by weight of the water absorbent resin (D). This is the percentage of the range.

本発明に於て、吸水性樹脂(D)を親水性架橋剤(E)
と混合し、吸水性樹脂の表面近傍を架橋する方法として
は、以下の様な方法が例示される。
In the present invention, the water absorbent resin (D) is mixed with a hydrophilic crosslinking agent (E).
Examples of methods for crosslinking near the surface of the water absorbent resin include the following methods.

(+)  吸水性樹脂(D)に親水性架橋剤(ε)およ
び必要により、水(水蒸気)及び/または親水性有機溶
剤(G)の混合液を噴霧、あるいは滴下混合する方法。
(+) A method of spraying or dropwise mixing a liquid mixture of a hydrophilic crosslinking agent (ε) and, if necessary, water (steam) and/or a hydrophilic organic solvent (G), onto the water absorbent resin (D).

または、 (II)吸水性樹脂(D)を重合不活性な疎水性有機溶
剤中に分散・懸濁させ、親水性架橋剤(E)および必要
により、水及び/または親水性有機溶剤(G)を撹拌下
に添加する方法。
Or, (II) the water absorbent resin (D) is dispersed/suspended in a polymerization-inactive hydrophobic organic solvent, and the hydrophilic crosslinking agent (E) and, if necessary, water and/or the hydrophilic organic solvent (G) are added. A method of adding under stirring.

この場合、親水性架橋剤(E)を特定の界面活性剤を用
いて、予め疎水性有機溶剤に乳化、懸濁させその乳化液
を吸水性樹脂CD)の分散懸濁液中に添加する方法が好
ましい。
In this case, a method of emulsifying and suspending the hydrophilic crosslinking agent (E) in a hydrophobic organic solvent using a specific surfactant in advance and adding the emulsion to a dispersion suspension of the water absorbent resin CD) is preferred.

または、 (m)  吸水性樹脂(D)を水と親水性有機溶剤(G
)の混合溶剤中に分散させ、親水性架橋剤(E)を添加
する方法。
Or (m) water absorbent resin (D) is mixed with water and hydrophilic organic solvent (G
) is dispersed in a mixed solvent and a hydrophilic crosslinking agent (E) is added.

などが挙げられる。Examples include.

以上の様にして、本発明の方法によって得られる吸水性
樹脂(D)と親水性架橋剤(E)および必要により、水
及び/または親水性有機溶剤(G)を混合して得られた
混合物を加熱処理するには、通常の加熱器や加熱炉を用
いることができる。例えば溝型撹拌乾燥器、回転乾燥器
、円盤乾燥器、ねつ和乾燥器、流動層乾燥器、気流乾燥
器、赤外線乾燥器、誘電加熱乾燥器などである。又(I
I)の方法で吸水性樹脂(Dlに有機溶剤中で親水性架
橋剤(E)を添加した後、有機溶剤中でそのまま加熱し
反応させてもよい。
A mixture obtained by mixing the water absorbent resin (D) obtained by the method of the present invention with the hydrophilic crosslinking agent (E) and, if necessary, water and/or a hydrophilic organic solvent (G) as described above. For heat treatment, a normal heater or heating furnace can be used. Examples include a groove-type stirring dryer, a rotary dryer, a disc dryer, a wet dryer, a fluidized bed dryer, a flash dryer, an infrared dryer, a dielectric heating dryer, and the like. Also (I
After adding the hydrophilic crosslinking agent (E) to the water-absorbing resin (Dl) in an organic solvent by method I), the mixture may be directly heated and reacted in the organic solvent.

加熱処理温度は用いられる親水性架橋剤(E)の種類な
どにもよるが、40〜250℃が好ましく、より好まし
くは90〜220℃の範囲である。
Although the heat treatment temperature depends on the type of hydrophilic crosslinking agent (E) used, it is preferably in the range of 40 to 250°C, more preferably in the range of 90 to 220°C.

40℃未満では反応に時間がかかり生産性の低下を起こ
すのみならず、親水性架橋剤(E)の一部が未反応とな
り得られた吸水性樹脂(F)に残存する恐れがあり好ま
しくない。250℃を越える高温では、吸水性樹脂fD
)の種類によっては熱劣化が起こる場合があるので注意
が必要である。
If it is lower than 40°C, not only will the reaction take a long time and productivity will decrease, but also a portion of the hydrophilic crosslinking agent (E) may become unreacted and remain in the resulting water absorbent resin (F), which is not preferable. . At high temperatures exceeding 250℃, water absorbent resin fD
) Please note that thermal deterioration may occur depending on the type of material.

なお、表面架橋した吸水性樹脂(F)や、表面架橋して
いない吸水性樹脂(D)を必要により破砕造粒してもよ
い。
Incidentally, the surface-crosslinked water-absorbing resin (F) or the surface-uncrosslinked water-absorbing resin (D) may be crushed and granulated if necessary.

[発明の効果] 本発明により得られる吸水性樹脂は従来の方法では得ら
れなかった、膨潤ゲルの耐久性に優れ、生理食塩水や特
に人尿に対しても高吸水倍率で、しかも水ひ溶分の分子
量が低く、膨潤ゲルのベトッキや通液性が大幅に改善さ
れた、安全な吸水性樹脂である。本発明の方法によれば
−この様な優れた吸水性樹脂は、水溶性エチレン性不飽
和単量体(A)を特定量の架橋剤(B)及び特定量の水
溶性連鎖移動剤(fly)の存在下で水溶液重合を行う
だけで簡便に製造でき、更に得られた吸水性樹脂(D)
の表面近傍を特定の親水性架橋剤(E)で架橋させ、吸
水速度や耐久性の格段に向上された吸水性樹脂(F)が
得られる。かかる吸水性樹脂(D)および(F)は、安
価に製造でき従来にない優れた吸水特性を有しているた
め、衛生材料、食品用、土木、は、 (1)従来、高吸水倍率の吸水性樹脂を得るために架橋
剤量を減らして重合を行っていたため、膨潤ゲルの耐久
性が乏しかったが、本発明の方法では多くの架橋剤を用
いても、高吸水倍率なため、膨潤ゲルが優れた耐久性を
示す。
[Effects of the Invention] The water-absorbing resin obtained by the present invention has excellent durability of a swollen gel that could not be obtained by conventional methods, has a high water absorption capacity even in physiological saline and especially human urine, and is water resistant. It is a safe water-absorbing resin that has a low molecular weight of the dissolved component, and has significantly improved stickiness and liquid permeability of the swollen gel. According to the method of the present invention, such an excellent water-absorbing resin can be obtained by combining a water-soluble ethylenically unsaturated monomer (A) with a specific amount of a crosslinking agent (B) and a specific amount of a water-soluble chain transfer agent (fly ) can be easily produced by simply carrying out aqueous polymerization in the presence of the water-absorbent resin (D).
By crosslinking the vicinity of the surface with a specific hydrophilic crosslinking agent (E), a water absorbent resin (F) with significantly improved water absorption rate and durability can be obtained. These water-absorbing resins (D) and (F) can be produced at low cost and have unprecedented water-absorbing properties, so they are used for sanitary materials, food, and civil engineering. In order to obtain a water-absorbing resin, polymerization was carried out with a reduced amount of cross-linking agent, resulting in poor durability of the swollen gel. However, with the method of the present invention, even if a large amount of cross-linking agent is used, the swelling The gel exhibits excellent durability.

(2)  従来の吸水性樹脂では得られなかった、人尿
に対する高い吸水倍率を示す。
(2) It exhibits a high water absorption capacity for human urine, which was not possible with conventional water absorbent resins.

(3)  用いるi量体を飽和濃度近くの高い濃度で重
合させても、自己架橋など不要な反応が抑えられた高性
能の吸水性樹脂が得られる為、高濃度で重合が可能で高
い生産性で製造ができる。
(3) Even if the i-mer used is polymerized at a high concentration near the saturation concentration, a high-performance water-absorbing resin with suppressed unnecessary reactions such as self-crosslinking can be obtained, so polymerization can be performed at a high concentration and high productivity can be achieved. It can be manufactured by nature.

(4)本発明の吸水性樹脂は高い吸水倍率は示すなどの
悪影響を及ぼさない。
(4) The water-absorbing resin of the present invention exhibits a high water absorption capacity and does not have any adverse effects.

(5)表面近傍を架橋することで、従来の吸水性樹脂の
表面架橋で得られなかった吸水特性の改善効果を示し、
更に優れた耐久性や吸水速度を示す。
(5) By crosslinking near the surface, it shows an improvement effect on water absorption properties that could not be obtained by surface crosslinking of conventional water absorbent resins,
It also shows superior durability and water absorption speed.

(6)従来、残存モノマー低減や誘導期間、重合時間の
短縮のため重合開始剤量を増加させると、自己架橋など
の不要な反応が起こり高吸水倍率のものが得られなかっ
たが、重合開始剤量を増やしても高吸水率のものが得ら
れ低い残存モノマー量となる。
(6) Conventionally, when increasing the amount of polymerization initiator to reduce residual monomer, induction period, and shorten polymerization time, unnecessary reactions such as self-crosslinking occurred, making it impossible to obtain a product with high water absorption capacity. Even if the amount of the agent is increased, a high water absorption rate can be obtained, resulting in a low amount of residual monomer.

等の優れた長所を有するものである。It has excellent advantages such as:

(実施例) 以下、実施例により本発明を説明するが、本発明の範囲
はこれらの実施例にのみ限定されるものではない。尚、
実施例に記載の吸水性樹脂の諸物性は下記の試験方法に
よって測定した値を示す。
(Examples) The present invention will be described below with reference to Examples, but the scope of the present invention is not limited only to these Examples. still,
The physical properties of the water-absorbing resin described in the Examples are the values measured by the following test method.

また、部は重量部を示す。In addition, parts indicate parts by weight.

(1)生理食塩水の吸水倍率 吸水性樹脂1.0gを150m1の0.9重量%塩化す
トリウム水溶液中の入ったビーカーに浸漬し、ゆっくり
マグネチックスターラーで撹拌した。6時間後に膨潤ゲ
ルを金網で濾過し、十分に水切りをした後の膨潤ゲルの
重さを測定し、以下の式で吸水倍率を算出した。
(1) Water absorption capacity of physiological saline 1.0 g of a water absorbent resin was immersed in a beaker containing 150 ml of a 0.9% by weight thorium chloride aqueous solution and slowly stirred with a magnetic stirrer. After 6 hours, the swollen gel was filtered through a wire mesh, the weight of the swollen gel after sufficiently draining water was measured, and the water absorption capacity was calculated using the following formula.

膨潤ゲルの重量 (2)人尿の吸水倍率 (1)の生理食塩水に代えて、成人男子10人からサン
プリングした人尿を用いる以外は同様に行い、人尿での
吸水倍率を測定した。
Weight of swollen gel (2) Water absorption capacity of human urine (1) The same procedure was performed except that human urine sampled from 10 adult males was used instead of physiological saline, and the water absorption capacity of human urine was measured.

(3)水可溶分 吸水性樹脂0.5gを10100Oの脱イオン水中に分
散し、12時間後、濾紙で濾過し、濾液中の固形分を測
定して次式に従って水可溶分を求めた。
(3) Water-soluble content: Disperse 0.5 g of water-absorbing resin in 10100O deionized water, filter it with filter paper after 12 hours, measure the solid content in the filtrate, and calculate the water-soluble content according to the following formula. Ta.

濾液の重量(g)*濾液の固形分(%)(4)水可溶分
の分子量 分子量が既知の種々のポリアクリル酸ナトリウムを標準
にして、ゲルパーミェーションクロマトグラフィーによ
って、(3)の方法でサンプリングした水可溶分の分子
量を求めた。
Weight of filtrate (g) *Solid content of filtrate (%) (4) Molecular weight of water-soluble component By gel permeation chromatography using various sodium polyacrylates with known molecular weights as standards, (3) The molecular weight of the water-soluble components sampled was determined using the method described above.

(5)膨潤ゲルの耐久性 不織布、綿状バルブ、吸水紙および防水フィルムからな
る市販の子供用オムツ(重量72g)を半分に切り、ポ
リマー2.5gを綿状バルブと吸水紙の間に均一に散布
し、成人の人尿120m1を加えて37℃に放置し、6
時間、12時間、18時間後にオムツを開いて中の膨潤
ゲルの様子を観察した。劣化状態が判定は、○〜Δ〜×
の3段階評価とした。
(5) Durability of swollen gel A commercially available children's diaper (weighing 72 g) consisting of non-woven fabric, cotton bulb, water-absorbing paper and waterproof film was cut in half, and 2.5 g of polymer was evenly distributed between the cotton bulb and the water-absorbing paper. 120ml of adult human urine was added and left at 37°C.
After 12 hours and 18 hours, the diaper was opened and the state of the swollen gel inside was observed. The deterioration state is judged as ○~Δ~×
A three-level evaluation was made.

○;膨潤ゲルの形状が保持されている。○: The shape of the swollen gel is maintained.

△ニ一部、膨潤ゲルの形状が崩れている。△D The shape of the swollen gel is partially distorted.

×;膨潤ゲルの形状が崩れ、ドロドロの流動状となって
いる。
×: The shape of the swollen gel is distorted and becomes mushy and fluid.

(6)もどり量 上記膨潤ゲルの耐久性試験に用いた18時間後の子供用
オムツの不織布の上に2つ折りにした23cm*23c
mのペーパータオルを10枚かぶせ、40 g/cm”
の圧力を1分間かけてペーパータオルに戻ってきた尿の
量を測定した。
(6) Amount of recovery: 23 cm * 23 cm folded in half on the non-woven fabric of a child's diaper after 18 hours used in the durability test of the above swelling gel.
Cover with 10 paper towels of 40 g/cm"
The amount of urine that returned to the paper towel was measured by applying pressure for 1 minute.

(7)膨潤ゲルのベトッキ (1)で吸水倍率を測定した後の膨潤ゲルのベトッキ(
ドライ感)を手触りにて測定した。ドライ感の判定は、
○〜Δ〜Xの3段階評価とした。
(7) After measuring the water absorption capacity with the swollen gel Betokki (1), the swollen gel Betokki (
Dry feeling) was measured by touch. Judging the dry feeling
Evaluation was made in three stages: ◯ to Δ to X.

○;膨潤ゲルはかなりサラサラしてドライ感がある。○: The swollen gel has a very smooth and dry feel.

Δ;一部、膨潤ゲルがベトツク。Δ: Part of the swollen gel is sticky.

×;膨潤ゲルがベトッキ、手がヌベヌベしている。×: The swollen gel is sticky and hands are sticky.

(8)膨潤ゲルの通液性 第1図に示すように内径53mmのシャーレlに吸水性
樹脂1.0gを入れ、人尿10m1を注ぎ膨潤ゲル2を
得る。膨潤ゲル2の上に直径53n++nのペーパータ
オル3を置き、更に第1図に示すように、中央に突出し
た筒状部を有する円板状のアクリル樹脂製試験器4を置
<、1時間室温に放置した後、人尿6mlを注入口5よ
り注ぎ、人尿が全てポリマー中に吸収されるまでの時間
を測定し、それをもって、膨潤ゲルの通液性とする。
(8) Liquid permeability of swollen gel As shown in FIG. 1, 1.0 g of a water-absorbing resin is placed in a Petri dish 1 with an inner diameter of 53 mm, and 10 ml of human urine is poured into it to obtain a swollen gel 2. A paper towel 3 with a diameter of 53n++n was placed on top of the swollen gel 2, and a disk-shaped acrylic resin tester 4 with a protruding cylindrical portion in the center was placed on top of the swollen gel 2, as shown in FIG. After leaving it to stand, 6 ml of human urine was poured into the inlet 5, and the time until all of the human urine was absorbed into the polymer was measured, and this was taken as the liquid permeability of the swollen gel.

(実施例1) アクリル酸414g及びアクリル酸ナトリウムの37重
量%水溶液4380g、および架橋剤(B)としてトリ
メチロールプロパントリアクリレート6.815g(対
単量体(A10.1モル%)、水溶性連鎖移動剤(C)
として次亜燐酸ナトリウム1水和物0.195g (対
単量体(A)0.008モル%)、イオン交換水670
gを用いて濃度37%、中和率75%の単量体水溶液を
得た後、窒素ガスを吹き込んで溶存酸素を追い出した。
(Example 1) 414 g of acrylic acid, 4380 g of a 37% by weight aqueous solution of sodium acrylate, and 6.815 g of trimethylolpropane triacrylate as the crosslinking agent (B) (based on monomer (A10.1 mol%)), water-soluble chain Transfer agent (C)
0.195 g of sodium hypophosphite monohydrate (0.008 mol% of monomer (A)), 670 g of ion-exchanged water
After obtaining a monomer aqueous solution with a concentration of 37% and a neutralization rate of 75% using g, nitrogen gas was blown in to drive out dissolved oxygen.

内容積102のシグマ型羽根を2本有するジャケット付
きステンレス製双腕型ねっか機に−ダー)に蓋をつけ、
この反応器に上記の単量体(A)水溶液を送入し、窒素
ガスを吹き込んで反応系内を窒素置換した。ついで2本
のシグマ型羽根を回転させると共に、ジャケットに35
℃の温水を通じて加熱しながら重合開始剤として過硫酸
アンモニウム2.62gと亜硫酸水素ナトリウム0. 
12gを添加することにより重合を開始させた。重合ピ
ーク時に含水ゲル重合体は約5mmの径に細分化されて
おり、更に撹拌を続は重合を開始して60分後に蓋を外
し、ゲルを取り出した。得られた含水ゲル状重合体の細
粒化物を50メツシユの金網上に広げ、170℃の温度
で50分間熱風乾燥した。この乾燥物をハンマー型粉砕
機で粉砕し、20メツシユ金網でふるい分けして20メ
ツシユ1表に示す。
Attach a lid to a jacketed stainless steel double-arm polisher having two sigma-type blades with an internal volume of 102 cm.
The above monomer (A) aqueous solution was introduced into this reactor, and nitrogen gas was blown into the reactor to replace the inside of the reaction system with nitrogen. Next, rotate the two sigma type blades and add 35 to the jacket.
2.62 g of ammonium persulfate and 0.0 g of sodium hydrogen sulfite were added as polymerization initiators while heating through hot water at
Polymerization was initiated by adding 12 g. At the peak of polymerization, the hydrogel polymer was fragmented into pieces with a diameter of about 5 mm, and after further stirring, the lid was removed 60 minutes after polymerization was started, and the gel was taken out. The resulting finely granulated water-containing gel polymer was spread on a 50-mesh wire mesh and dried with hot air at a temperature of 170° C. for 50 minutes. This dried material was ground with a hammer-type grinder and sieved through a 20-mesh wire mesh.

(実施例2) 実施例1に於て、用いられる水溶性連鎖移動剤(C)次
亜燐酸ナトリウムl水和物の使用量をl。
(Example 2) In Example 1, the amount of the water-soluble chain transfer agent (C) sodium hypophosphite l-hydrate used was 1.

219g(対単量体(A)0.05モル%)とする以外
は同様に行い、吸水性樹脂(2)を得た。
A water-absorbing resin (2) was obtained in the same manner except that 219 g (0.05 mol % of monomer (A)) was used.

この吸水性樹脂(2)を同様に評価し、結果を第1表に
示す。
This water absorbent resin (2) was similarly evaluated and the results are shown in Table 1.

(実施例3) 21.988g (対単量体0.2モル%)とし、かつ
水溶性連鎖移動剤(C)次亜燐酸ナトリウム1水和物の
使用量を2.44g (対単量体(A)0゜1モル%)
とする以外は同様に行い、吸水性樹脂(3)を得た。
(Example 3) 21.988 g (0.2 mol % based on monomer), and the amount used of water-soluble chain transfer agent (C) sodium hypophosphite monohydrate was 2.44 g (based on monomer (A) 0°1 mol%)
A water absorbent resin (3) was obtained in the same manner except for the following steps.

この吸水性樹脂(3)を同様に評価し、結果を第1表に
示す。
This water absorbent resin (3) was similarly evaluated and the results are shown in Table 1.

(実施例4) 実施例1に於て、用いられる架橋剤(B)ポリエチレン
グリコールジアクリレート(n=8)を54.97g 
(対単量体0.5”モル%)とし、かつ水溶性連鎖移動
剤(C)次亜燐酸ナトリウム1水和物の使用量を9.7
6g (対単量体(A)0.4モル%)とする以外は同
様に行い、吸水性樹脂(4)を得た。
(Example 4) In Example 1, 54.97 g of the crosslinking agent (B) polyethylene glycol diacrylate (n = 8) used
(0.5" mol% relative to monomer), and the amount of water-soluble chain transfer agent (C) sodium hypophosphite monohydrate used was 9.7"
A water-absorbing resin (4) was obtained in the same manner except that the amount was 6 g (0.4 mol % based on monomer (A)).

この吸水性樹脂(4)を同様に評価し、結果を第1表に
示す。
This water absorbent resin (4) was similarly evaluated and the results are shown in Table 1.

(実施例5) 実施例1に於て、用いられる架橋剤(B)をNN′−メ
チレンビスアクリルアミド2.152g(対単量体fA
)0.06モル%)とし、かつ水溶性連鎖移動剤(C)
をチオリンゴ酸3.45g (対単量体(A)0.1モ
ル%)とする以外は同様に行い、吸水性樹脂(5)を得
た。
(Example 5) In Example 1, the crosslinking agent (B) used was 2.152 g of NN'-methylenebisacrylamide (relative to monomer fA).
)0.06 mol%) and a water-soluble chain transfer agent (C)
A water-absorbing resin (5) was obtained in the same manner except that 3.45 g of thiomalic acid (0.1 mol % relative to monomer (A)) was used.

この吸水性樹脂(5)を同様に評価し、結果を第1表に
示す。
This water absorbent resin (5) was similarly evaluated and the results are shown in Table 1.

(実施例6) 実施例1に於て、用いられるイオン交換水の量を50g
に変更し、単量体(A)水溶酸の濃度を42%とし、用
いられる架橋剤(B)をポリエチレン1゛′7 グリコールジアクリレート(n=14す17.07g(
対単量体(A)0.1モル%)とし、かつ水溶性連鎖移
動剤(C)チオリンゴ酸の使用量を0゜69g(対単量
体(A)0.02モル%)とする以外、同様に行い、吸
水性樹脂(6)を得た。
(Example 6) In Example 1, the amount of ion-exchanged water used was 50g.
The concentration of monomer (A) water-soluble acid was changed to 42%, and the crosslinking agent (B) used was polyethylene 1''7 glycol diacrylate (n = 14, 17.07 g (
0.1 mol% relative to monomer (A)) and the amount of water-soluble chain transfer agent (C) thiomalic acid used was 0.69 g (0.02 mol% relative to monomer (A)). A water absorbent resin (6) was obtained in the same manner.

この吸水性樹脂(6)を同様に評価し、結果を第1表に
示す。
This water absorbent resin (6) was similarly evaluated and the results are shown in Table 1.

(実施例7) 40gのトウモロコシ澱粉及び600gのイオン交換水
を撹拌棒と窒素ガス吹き込み管と温度計器 を備えた反応嚢内に仕込み、55℃で1時間撹拌後、3
0℃に冷却した。この澱粉水溶液にアクリル酸300g
、架橋剤(B)としてN、N’ −メチレンビスアクリ
ルアミド1.92g (対単量体(A)0.3モル%)
、水溶性連鎖移動剤(C)としてチオリンゴ酸0.94
g (対単量体(A)0.15モル%)を溶解させ、濃
度33%、中和率O%の単量体水溶液を得た。
(Example 7) 40 g of corn starch and 600 g of ion-exchanged water were placed in a reaction chamber equipped with a stirring rod, a nitrogen gas blowing tube, and a temperature meter, and after stirring at 55° C. for 1 hour,
Cooled to 0°C. 300g of acrylic acid in this starch aqueous solution
, 1.92 g of N,N'-methylenebisacrylamide as the crosslinking agent (B) (0.3 mol% relative to monomer (A))
, 0.94 thiomalic acid as water-soluble chain transfer agent (C)
g (0.15 mol % relative to monomer (A)) was dissolved to obtain a monomer aqueous solution with a concentration of 33% and a neutralization rate of 0%.

この単量体水溶液を35℃として、重合開始剤として過
硫酸ナトリウム0.20g、12−アスコルピン酸0.
04gを加えて3時間、撹拌しな、がら重合せしめた。
This monomer aqueous solution was heated to 35°C, 0.20 g of sodium persulfate was used as a polymerization initiator, and 0.2 g of 12-ascorbic acid was used as a polymerization initiator.
04 g was added and polymerized for 3 hours without stirring.

得られた含水ゲル状重合物に、30重量%の苛性ソーダ
水溶液を389g加え、中和率70%とし、更に実施例
1と同様に乾燥粉砕し吸水性樹脂(7)を得た。
389 g of a 30% by weight aqueous caustic soda solution was added to the obtained hydrogel polymer to give a neutralization rate of 70%, and the mixture was further dried and ground in the same manner as in Example 1 to obtain a water absorbent resin (7).

この吸水性樹脂(7)を同様に評価し、結果を第1表に
示す。
This water absorbent resin (7) was similarly evaluated and the results are shown in Table 1.

(実施例8) アクリル酸72gに脱イオン水22.2gを加え、更に
これを中和剤として純度85%の水酸化カリウム49.
5gおよび架橋剤(B)としてN。
(Example 8) 22.2 g of deionized water was added to 72 g of acrylic acid, and this was used as a neutralizing agent to prepare 49.9 g of potassium hydroxide with a purity of 85%.
5g and N as crosslinker (B).

N′−メチレンビスアクリルアミド0.1g(対単量体
(A)0.065モル%)、水溶性連鎖移動剤(C)と
してチオリンゴ酸0.225g (対単量体(A10.
15モル%)を順次添加し、濃度70%、中和率75%
の単量体水溶液を調整した。
0.1 g of N'-methylenebisacrylamide (0.065 mol % based on monomer (A)), 0.225 g thiomalic acid (based on monomer (A10.
15 mol%) was added sequentially to achieve a concentration of 70% and a neutralization rate of 75%.
An aqueous monomer solution was prepared.

この単量体水溶液を70℃に保温し、約5mmの厚みに
窒素気流下に保った後、更に過硫酸アンモニウム0.1
gおよび亜硫酸水素ナトリウム0゜02gを添加し重合
を行った。重合は即座に開始し、10分後に殆ど乾燥し
た重合ゲルを取り出し、更に実施例1と同様に乾燥粉砕
し吸水性樹脂(8)を得た。
This monomer aqueous solution was kept at 70°C and kept under a nitrogen stream to a thickness of about 5 mm, and then added with 0.1 ammonium persulfate.
g and 0.02 g of sodium bisulfite were added to carry out polymerization. Polymerization started immediately, and after 10 minutes, the almost dry polymer gel was taken out and further dried and crushed in the same manner as in Example 1 to obtain a water absorbent resin (8).

この吸水性樹脂(8)を同様に評価し、結果を第1表に
示す。
This water absorbent resin (8) was similarly evaluated and the results are shown in Table 1.

(実施例9) 実施例1で得られた吸水性樹脂(5)100部にエチレ
ングリコールジグリシジルエーテル0.1部、水5部、
イソプロピルアルコール1部を混合し、得られた混合物
を乾燥機中に100℃、30分間加熱処理を行い、吸水
性樹脂(9)を得た。
(Example 9) To 100 parts of the water absorbent resin (5) obtained in Example 1, 0.1 part of ethylene glycol diglycidyl ether, 5 parts of water,
1 part of isopropyl alcohol was mixed, and the resulting mixture was heated in a dryer at 100° C. for 30 minutes to obtain a water absorbent resin (9).

この様にして得られた吸水性樹脂(9)の分析結果を第
1表に示す。
Table 1 shows the analysis results of the water absorbent resin (9) thus obtained.

(実施例10) 実施例2で得られた吸水性樹脂(2)100部に、グリ
セリン1部、水6部、アセトン1部を加え、ジャケット
を熱媒で230℃に加熱したブレンダーに投入し、混合
と加熱処理を行い吸水性樹脂(lO)を得た。
(Example 10) 1 part of glycerin, 6 parts of water, and 1 part of acetone were added to 100 parts of the water-absorbing resin (2) obtained in Example 2, and the mixture was placed in a blender heated to 230°C using a heat medium. , mixing and heat treatment were performed to obtain a water absorbent resin (IO).

この様にして得られた吸水性樹脂(10)の分析結果を
第1表に示す。
The analysis results of the water absorbent resin (10) thus obtained are shown in Table 1.

(実施例11) 実施例3で得られた吸水性樹脂(3)100部にエチレ
ングリコールジグリシジルエーテル0. 1部、水3部
、メタノール6部からなる処理溶液を混合した。得られ
た混合物を乾燥機中、130℃で1時間加熱処理するこ
とにより吸水性樹脂(11)を得た。
(Example 11) To 100 parts of the water absorbent resin (3) obtained in Example 3, 0.00 parts of ethylene glycol diglycidyl ether was added. A treatment solution consisting of 1 part water, 3 parts water, and 6 parts methanol was mixed. The resulting mixture was heat-treated at 130° C. for 1 hour in a dryer to obtain a water-absorbing resin (11).

この様にして得られた吸水性樹脂(11)の分析結果を
第1表に示す。
Table 1 shows the analysis results of the water absorbent resin (11) thus obtained.

(実施例12) 実施例4で得られた吸水性樹脂(4)100部に硫酸ア
ルミニウム1部、グリセリン1部、水8部からなる処理
水溶液10部を混合した。得られた混合物を200℃で
30分間加熱処理を行い吸水性樹脂(12)を得た。
(Example 12) 100 parts of the water absorbent resin (4) obtained in Example 4 was mixed with 10 parts of a treated aqueous solution consisting of 1 part of aluminum sulfate, 1 part of glycerin, and 8 parts of water. The resulting mixture was heat-treated at 200° C. for 30 minutes to obtain a water absorbent resin (12).

この様にして得られた吸水性樹脂(12)の分析結果を
第1表に示す。
Table 1 shows the analysis results of the water absorbent resin (12) thus obtained.

(比較例1) 実施例1において、架橋剤(B)の使用量を00273
g (対単量体(A)0.004モル%)とする以外は
同様に行い、比較吸水性樹脂(1)を得た。
(Comparative Example 1) In Example 1, the amount of crosslinking agent (B) used was 00273
Comparative water absorbent resin (1) was obtained in the same manner except that g (0.004 mol% relative to monomer (A)).

この様にして得られた比較吸水性樹脂(1)の分析結果
を第1表に示す。
Table 1 shows the analysis results of the comparative water absorbent resin (1) thus obtained.

(比較例2) 実施例1において、水溶性連鎖移動剤(C)次亜燐酸ナ
トリウム1水和物を添加しない以外は同様に行い、比較
吸水性樹脂(2)を得た。
(Comparative Example 2) A comparative water absorbent resin (2) was obtained in the same manner as in Example 1 except that the water-soluble chain transfer agent (C) sodium hypophosphite monohydrate was not added.

この様にして得られた比較吸水性樹脂(2)の分析結果
を第1表に示す。
Table 1 shows the analysis results of the comparative water absorbent resin (2) thus obtained.

(比較例3) 実施例1において、水溶性連鎖移動剤(C1次亜燐酸ナ
トリウム1水和物を添加せず、架橋剤(B)の使用量を
3.41.g(対単量体(A)0.05モル%)とする
以外は同様に行い、比較吸水性樹脂(3)を得た。
(Comparative Example 3) In Example 1, the water-soluble chain transfer agent (C1 sodium hypophosphite monohydrate was not added, and the amount of crosslinking agent (B) used was 3.41.g (relative to the monomer ( Comparative water-absorbing resin (3) was obtained in the same manner except that A) was 0.05 mol %).

この様にして得られた比較吸水性樹脂(3)の分析結果
を第1表に示す。
Table 1 shows the analysis results of the comparative water absorbent resin (3) thus obtained.

(比較例4〉 実施例1において、水溶性連鎖移動剤(C)次亜燐酸ナ
トリウム1永和物を添加せず、架橋剤(B)をN、N′
−メチレンビスアクリルアミド17゜73g(対単量体
(A)0.5モル%)とする以外は同様に行い、比較吸
水性樹脂(4)を得た。
(Comparative Example 4) In Example 1, the water-soluble chain transfer agent (C) sodium hypophosphite 1-eternal was not added, and the crosslinking agent (B) was replaced with N, N'
A comparative water-absorbent resin (4) was obtained in the same manner except that 17.73 g of -methylenebisacrylamide (0.5 mol % based on monomer (A)) was used.

この様にして得られた比較吸水性樹脂(4)の分析結果
を第1表に示す。
Table 1 shows the analysis results of the comparative water absorbent resin (4) thus obtained.

(比較例5) 実施例7において、架橋剤(B)を添加しない以外は同
様に行い、比較吸水性樹脂(5)を得た。
(Comparative Example 5) A comparative water absorbent resin (5) was obtained in the same manner as in Example 7 except that the crosslinking agent (B) was not added.

この様にして得られた比較吸水性樹脂(5)の分析結果
を第1表に示す。
Table 1 shows the analysis results of the comparative water absorbent resin (5) thus obtained.

(比較例6〜8) 比較吸水性樹脂(6)〜(8)を得た。(Comparative Examples 6 to 8) Comparative water absorbent resins (6) to (8) were obtained.

この様にして得られた比較吸水性樹脂(6)〜(8)の
分析結果を第1表に示す。
Table 1 shows the analysis results of the comparative water absorbent resins (6) to (8) thus obtained.

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

第1図は膨潤ゲルの適法性試験器具を示したものである
。 1・・・・・・ シャーレ 2・・・・・・ 膨潤ゲル 3・・・・・・ ベーパータオル 4・・・・・・ アクリル樹脂製試験器5・・・・・・
 注入口
FIG. 1 shows an apparatus for testing the legality of a swollen gel. 1... Petri dish 2... Swelling gel 3... Vapor towel 4... Acrylic resin tester 5...
Inlet

Claims (1)

【特許請求の範囲】 1、水溶性エチレン性不飽和単量体(A)および該単量
体(A)に対し、架橋剤(B)0.005〜5モル%お
よび水溶性連鎖移動剤(C)0.001〜1モル%を含
有する30重量%〜飽和濃度の該単量体(A)水溶液を
、水溶液重合させることを特徴とする耐久性の優れた吸
水性樹脂(D)の製造方法。 2、水溶性エチレン性不飽和単量体(A)および該単量
体(A)に対し、架橋剤(B)0.005〜5モル%お
よび水溶性連鎖移動剤(C)0.001〜1モル%を含
有する30重量%〜飽和濃度の該単量体(A)水溶液を
、水溶液重合させて得た吸水性樹脂(D)の表面近傍を
吸水性樹脂(D)中の官能基と反応しうる親水性架橋剤
(E)で架橋させることを特徴とする耐久性の優れた吸
水性樹脂(F)の製造方法。 3、水溶性連鎖移動剤(C)が次亜燐酸塩である請求項
1または2記載の製造方法。 4、架橋剤(B)の使用量が水溶性エチレン性不飽和単
量体(A)に対して0.02〜1モル%である請求項1
または2記載の製造方法。 5、水溶性エチレン性不飽和単量体(A)水溶液の濃度
が35重量%〜飽和濃度である請求項1または2記載の
製造方法。 6、水溶性エチレン性不飽和単量体(A)がアクリル酸
およびアクリル酸アルカリ金属塩および/またはアンモ
ニウム塩を少なくとも50重量%含んでなる請求項1ま
たは2記載の製造方法。 7、水溶性エチレン性不飽和単量体(A)水溶液を回転
撹拌軸を有する反応器内で、水溶液重合させることを特
徴とする請求項1または2記載の製造方法。 8、回転撹拌翼を有する反応容器が複数の回転撹拌翼を
有してなる請求項7に記載の製造方法。 9、複数の回転撹拌軸を有する反応容器が双腕型ニーダ
ーである請求項8に記載の製造方法。 10、架橋剤(B)の使用量が水溶性エチレン性不飽和
単量体(A)に対して0.04〜0.4モル%である請
求項9に記載の製造方法。 11、吸水性樹脂(D)100重量部に対して、水0〜
20重量部および親水性有機溶剤(G)0〜20重量部
の存在下、カルボキシル基と反応しうる2個以上の官能
基を有する化合物(E−1)及び/または多価金属塩(
E−2)からなる群から選ばれた少なくとも1種の親水
性架橋剤(E)を0.005〜5重量部を混合し、40
〜250℃で加熱することよりなる請求項2記載の製造
方法。 12、親水性架橋剤(E)が化合物(E−1)である請
求項11記載の製造方法。 13、化合物(E−1)が多価アルコール化合物、多価
グリシジルエーテル化合物、多価オキサゾリン化合物及
び多価アミン化合物からなる群から選ばれる1種または
2種以上のものである請求項12記載の製造方法。 14、水が吸水性樹脂(D)100重量部に対して0.
5〜10重量部の量で用いられてなる請求項11記載の
製造方法。 15、親水性有機溶剤(G)が吸水性樹脂(D)101
重量部に対して0〜8重量部の量で用いられてなる請求
項11記載の製造方法。 16、加熱が90〜220℃である請求項11記載の製
造方法。
[Scope of Claims] 1. A water-soluble ethylenically unsaturated monomer (A) and 0.005 to 5 mol% of a crosslinking agent (B) and a water-soluble chain transfer agent (based on the monomer (A)). C) Production of a highly durable water-absorbing resin (D) characterized by aqueous polymerization of an aqueous solution of the monomer (A) containing 0.001 to 1 mol% and having a concentration of 30% to saturation. Method. 2. Water-soluble ethylenically unsaturated monomer (A) and 0.005 to 5 mol% of crosslinking agent (B) and 0.001 to 5 mol% of water-soluble chain transfer agent (C) based on the monomer (A) A functional group in the water absorbent resin (D) is formed near the surface of the water absorbent resin (D) obtained by aqueous polymerization of an aqueous solution of the monomer (A) containing 1 mol % at a concentration of 30 wt.% to saturated concentration. A method for producing a water absorbent resin (F) with excellent durability, which comprises crosslinking with a reactive hydrophilic crosslinking agent (E). 3. The manufacturing method according to claim 1 or 2, wherein the water-soluble chain transfer agent (C) is a hypophosphite. 4. Claim 1, wherein the amount of crosslinking agent (B) used is 0.02 to 1 mol% based on the water-soluble ethylenically unsaturated monomer (A).
Or the manufacturing method described in 2. 5. The manufacturing method according to claim 1 or 2, wherein the concentration of the water-soluble ethylenically unsaturated monomer (A) aqueous solution is 35% by weight to saturated concentration. 6. The production method according to claim 1 or 2, wherein the water-soluble ethylenically unsaturated monomer (A) contains at least 50% by weight of acrylic acid and an alkali metal salt and/or ammonium salt of acrylic acid. 7. The production method according to claim 1 or 2, wherein the aqueous solution of the water-soluble ethylenically unsaturated monomer (A) is polymerized in a reactor having a rotating stirring shaft. 8. The manufacturing method according to claim 7, wherein the reaction vessel having a rotating stirring blade has a plurality of rotating stirring blades. 9. The manufacturing method according to claim 8, wherein the reaction vessel having a plurality of rotating stirring shafts is a double-arm kneader. 10. The manufacturing method according to claim 9, wherein the amount of the crosslinking agent (B) used is 0.04 to 0.4 mol% based on the water-soluble ethylenically unsaturated monomer (A). 11. Water 0 to 100 parts by weight of water absorbent resin (D)
In the presence of 20 parts by weight and 0 to 20 parts by weight of a hydrophilic organic solvent (G), a compound (E-1) having two or more functional groups capable of reacting with a carboxyl group and/or a polyvalent metal salt (
E-2) 0.005 to 5 parts by weight of at least one hydrophilic crosslinking agent (E) selected from the group consisting of
3. The manufacturing method according to claim 2, which comprises heating at ~250<0>C. 12. The manufacturing method according to claim 11, wherein the hydrophilic crosslinking agent (E) is the compound (E-1). 13. The compound (E-1) according to claim 12, wherein the compound (E-1) is one or more compounds selected from the group consisting of polyhydric alcohol compounds, polyhydric glycidyl ether compounds, polyvalent oxazoline compounds, and polyvalent amine compounds. Production method. 14. Water content is 0.0% per 100 parts by weight of water absorbent resin (D).
12. The method according to claim 11, wherein the amount is 5 to 10 parts by weight. 15. Hydrophilic organic solvent (G) is water absorbent resin (D) 101
The manufacturing method according to claim 11, wherein the method is used in an amount of 0 to 8 parts by weight. 16. The manufacturing method according to claim 11, wherein the heating is performed at a temperature of 90 to 220°C.
JP31767489A 1989-12-08 1989-12-08 Manufacturing method of water absorbent resin with excellent durability Expired - Lifetime JP2877255B2 (en)

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Application Number Priority Date Filing Date Title
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Publication Number Publication Date
JPH03179008A true JPH03179008A (en) 1991-08-05
JP2877255B2 JP2877255B2 (en) 1999-03-31

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Cited By (24)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5773542A (en) * 1995-03-23 1998-06-30 Kao Corporation Process for producing polymer particles
JP2000136203A (en) * 1998-08-24 2000-05-16 Nippon Shokubai Co Ltd Production of water-containing gel product of water- absorbing resin
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