JPH0656933A - Water-absorbing resin and its production - Google Patents
Water-absorbing resin and its productionInfo
- Publication number
- JPH0656933A JPH0656933A JP20925492A JP20925492A JPH0656933A JP H0656933 A JPH0656933 A JP H0656933A JP 20925492 A JP20925492 A JP 20925492A JP 20925492 A JP20925492 A JP 20925492A JP H0656933 A JPH0656933 A JP H0656933A
- Authority
- JP
- Japan
- Prior art keywords
- water
- polymerization
- absorbent resin
- monomer
- acrylic 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.)
- Granted
Links
Landscapes
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
- Macromonomer-Based Addition Polymer (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、吸水性樹脂およびその
製造方法に関するものである。更に詳しくは、多量の塩
類や有機溶剤を含んだ水性液に対しても高吸水倍率を示
し、かつ、使用後廃棄する際の分解性にも優れた吸水性
樹脂、およびその製造方法に関するものである。FIELD OF THE INVENTION The present invention relates to a water absorbent resin and a method for producing the same. More specifically, the present invention relates to a water absorbent resin which exhibits a high water absorption capacity even for an aqueous liquid containing a large amount of salts or organic solvents, and is also excellent in decomposability upon disposal after use, and a method for producing the same. is there.
【0002】[0002]
【従来の技術】近年、合成高分子の1種として、大量の
水を吸ってゲル化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衛材分野、農林業分野、土木分
野等に幅広く利用されている。2. Description of the Related Art In recent years, a water-absorbent resin that absorbs a large amount of water and gels has been developed as a kind of synthetic polymer, and is used in the field of sanitary materials such as paper diapers and sanitary napkins, the field of agriculture and forestry, and the field of civil engineering. Widely used.
【0003】この様な吸水性樹脂として例えば、ポリア
クリル酸部分中和物架橋体、澱粉−アクリロニトリルグ
ラフト重合体の加水分解物、澱粉−アクリル酸グラフト
重合体の中和物、酢酸ビニル−アクリル酸エステル共重
合体の鹸化物、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、カチオン性モノマー
の架橋体、2−アクリルアミド−2−メチルプロパンス
ルホン酸とアクリル酸との共重合架橋体、2−スルホエ
チルメタクリレートの架橋体など多くが知られ、特に、
原料の入手のし易すさやその優れた吸水特性から、単量
体の主成分としてアクリル酸を用いたアクリル酸系吸水
性樹脂が主流となっている。Examples of such water-absorbent resins include crosslinked polyacrylic acid partially neutralized products, hydrolyzates of starch-acrylonitrile graft polymers, neutralized products of starch-acrylic acid graft polymers, and vinyl acetate-acrylic acid. Saponified product of ester copolymer, hydrolyzate of acrylonitrile copolymer or acrylamide copolymer, cross-linked product of cationic monomer, cross-linked product of 2-acrylamido-2-methylpropanesulfonic acid and acrylic acid, 2 -Many known are cross-linked products of sulfoethyl methacrylate, in particular,
Acrylic acid-based water-absorbent resins using acrylic acid as the main component of the monomer have become the mainstream due to the ease of availability of raw materials and their excellent water absorption properties.
【0004】一般に、これら吸水性樹脂は自重の数百倍
以上の純水を吸水することができるが、その吸水倍率は
被吸収液中に存在する金属塩や有機溶剤の影響を強く受
け、金属塩を多く含む尿や土中水、有機溶剤を多く含む
蓄冷剤水溶液や産業・医療廃水では大幅に吸水倍率が低
下するという欠点が見られ、特に、高濃度の有機溶剤水
溶液では殆ど吸水倍率を示さないことすらあった。Generally, these water absorbent resins can absorb pure water several hundred times their own weight or more, but their water absorption capacity is strongly influenced by the metal salts and organic solvents present in the liquid to be absorbed, and Urine and soil water containing a lot of salt, regenerator aqueous solution containing a lot of organic solvent and industrial / medical wastewater have a drawback that the water absorption coefficient is significantly reduced. I even didn't show it.
【0005】そこで、多量の塩類や有機溶剤を含んだ水
性液に対しても高吸水倍率を示す吸水性樹脂として、例
えば、アクリルアミドやエチレンオキシドなどのノニオ
ン性単量体を用いる方法(特開昭56−22378
号)、スルホン酸などの強酸性単量体を用いる方法(特
開昭56−161412号、特開昭62−144748
号)、4級アンモニウム塩などのカチオン性単量体を用
いる方法(特開昭64−15130号,特開平2−11
9934号,特開平2−242809号)などが報告さ
れている。Therefore, a method using a nonionic monomer such as acrylamide or ethylene oxide as a water absorbent resin having a high water absorption capacity even with an aqueous liquid containing a large amount of salts or organic solvents (JP-A-56). -22378
No.), a method using a strongly acidic monomer such as sulfonic acid (JP-A-56-161412, JP-A-62-144748).
No.), a method using a cationic monomer such as a quaternary ammonium salt (JP-A-64-15130, JP-A-2-11).
9934, JP-A-2-242809) and the like have been reported.
【0006】しかし、ノニオン性の吸水性樹脂は吸水速
度が遅く、飽和吸水倍率に達するのに数時間〜数10時
間を必要とする。また、強酸性単量体やカチオン性単量
体から得られた吸水性樹脂は、その単量体自身が極めて
高価なために、衛材などの使い捨て分野では不適な上、
単量体の重合性も悪いため、その安全性や生産性におい
ても問題があるものであった。However, the nonionic water-absorbent resin has a slow water absorption rate and requires several hours to several tens of hours to reach the saturated water absorption capacity. Further, the water-absorbent resin obtained from a strongly acidic monomer or a cationic monomer is unsuitable in the disposable field such as sanitary materials because the monomer itself is extremely expensive.
Since the polymerizability of the monomer is also poor, there are problems in safety and productivity.
【0007】上記した吸水倍率の問題に加え、使用後の
吸水性樹脂の分解性に関しても近年多くの注目が置かれ
ている。In addition to the above-mentioned problem of water absorption capacity, much attention has recently been paid to the degradability of the water absorbent resin after use.
【0008】近年、環境問題の一つとして、廃棄後の合
成高分子の環境への影響やその分解性が注目されている
が、吸水性樹脂はその大部分が使い捨て分野で用いら
れ、毎年相当量が廃棄されているにも拘らず、これら吸
水性樹脂の分解性は一般に低く、廃棄後も長時間環境に
留まっているのが現実である。吸水性樹脂の分解方法と
しては、紫外線の照射(特開平1−231983号)や
酸化剤の添加(特開平1−284507号)などが知ら
れているが、これらの方法では、複雑な工程を必要と
し、且つその分解率も低いのが現状であった。そこで、
廃棄後は自然に分解する生分解性吸水性樹脂(特開平2
−291292号など)も提案されているが、その生分
解率は低いのみならず、現在使用されている吸水性樹脂
に比べ、高価で且つ諸物性も劣るものであった。Recently, as one of the environmental problems, attention has been paid to the influence of the synthetic polymer on the environment after disposal and its degradability, but most of the water-absorbent resin is used in the disposable field and is equivalent to every year. Although the amount of the water-absorbent resin is discarded, the degradability of these water-absorbent resins is generally low, and it is the reality that they remain in the environment for a long time after the disposal. Known methods for decomposing the water-absorbent resin include irradiation with ultraviolet rays (JP-A-1-231983) and addition of an oxidant (JP-A-1-284507). However, these methods involve complicated steps. At present, it is necessary and the decomposition rate is low. Therefore,
Biodegradable water-absorbent resin that decomposes naturally after disposal
No. 291292) has been proposed, but not only its biodegradation rate is low, but also it is expensive and inferior in various physical properties as compared with the water-absorbent resins currently used.
【0009】[0009]
【発明が解決しようとする課題】本発明は上記現状に鑑
みなされたものであり、従って本発明の目的は、多量の
塩類や有機溶剤を含んだ水性液に対しても、高吸水倍率
を示す吸水性樹脂を提供することにある。SUMMARY OF THE INVENTION The present invention has been made in view of the above circumstances, and therefore an object of the present invention is to exhibit a high water absorption capacity even for an aqueous liquid containing a large amount of salts or organic solvents. It is to provide a water absorbent resin.
【0010】本発明の他の目的は、使用後廃棄時などに
容易に分解させることのできる吸水性樹脂を提供するこ
とにある。Another object of the present invention is to provide a water absorbent resin which can be easily decomposed at the time of disposal after use.
【0011】[0011]
【課題を解決するための手段および作用】本発明者ら
は、上記課題を解決すべく鋭意検討した結果、特定の構
造の官能基を有する吸水性樹脂が、多量の塩類や有機溶
剤を含んだ水性液に対しても高吸水倍率を示し、かつ、
使用後加熱により低分子化合物に容易に分解することを
見い出し、本発明を完成するに至った。Means and Actions for Solving the Problems As a result of intensive investigations by the present inventors to solve the above problems, the water-absorbent resin having a functional group of a specific structure contains a large amount of salts and organic solvents. High water absorption capacity for aqueous liquids, and
The present invention was found to be easily decomposed into a low molecular weight compound by heating after use, and the present invention has been completed.
【0012】即ち、本発明は第1の発明として「一般式
(1)That is, the present invention provides a "general formula (1)" as a first invention.
【0013】[0013]
【化3】 [Chemical 3]
【0014】で示される酸基含有単量体を30〜100
重量%の割合で含む親水性不飽和単量体を重合すること
を特徴とする吸水性樹脂の製造方法。」および第2の発
明として「一般式(2)The acid group-containing monomer represented by
A method for producing a water-absorbent resin, which comprises polymerizing a hydrophilic unsaturated monomer contained in a weight percentage. And a second invention is “general formula (2)
【0015】[0015]
【化4】 [Chemical 4]
【0016】で示される構造単位に由来する成分の総量
が30〜100重量%の割合である吸水性樹脂。」に関
するものである。以下、本発明を更に詳しく説明する。A water absorbent resin in which the total amount of the components derived from the structural unit represented by is 30 to 100% by weight. It is about ". Hereinafter, the present invention will be described in more detail.
【0017】本発明で必須に用いられる一般式(1)で
示される酸基含有単量体(以下、単にアクリル酸オリゴ
マー(塩)と言う。)は、アクリル酸オリゴマー又はア
クリル酸オリゴマー塩であってよく、例えば、n=1の
β−アクリロイルオキシプロピオン酸(塩)、およびn
が2以上の多量体であるオリゴマー酸(塩)からなる混
合物または単品である。The acid group-containing monomer represented by the general formula (1) (hereinafter simply referred to as an acrylic acid oligomer (salt)), which is essential in the present invention, is an acrylic acid oligomer or an acrylic acid oligomer salt. , Β-acryloyloxypropionic acid (salt) in which n = 1, and n
Is a mixture or a single product composed of oligomeric acids (salts) which are multimers of 2 or more.
【0018】本発明において用いるアクリル酸オリゴマ
ー(塩)の使用量は重合に供される親水性不飽和単量体
の全量中30〜100重量%、好ましくは40〜100
重量%、より好ましくは50〜100重量%、更に好ま
しくは70〜100重量%である。アクリル酸オリゴマ
ー(塩)の使用量が30重量%未満では、高塩濃度水溶
液への吸水能や加熱による分解性が低く不十分であり、
又有機溶剤水溶液に対する吸収などで何等改善効果を示
さない。The amount of the acrylic acid oligomer (salt) used in the present invention is 30 to 100% by weight, preferably 40 to 100% by weight based on the total amount of the hydrophilic unsaturated monomer used for the polymerization.
%, More preferably 50 to 100% by weight, further preferably 70 to 100% by weight. When the amount of the acrylic acid oligomer (salt) used is less than 30% by weight, the ability to absorb water into a high salt concentration aqueous solution and the decomposability due to heating are low and insufficient,
Further, it does not show any improvement effect by absorption with respect to the aqueous solution of organic solvent.
【0019】なお、近年、アクリル酸系吸水性樹脂を製
造する際の重合時の相分離を防止するために、第2単量
体を5〜20重量%程度の少量共存させる技術(特開平
1−165610号)が提案され、その際の第2単量体
の1種として、β−アクリロイルオキシプロピオン酸が
例示されている。しかし、かかる少量のβ−アクリロイ
ルオキシプロピオン酸の使用では、何等本発明の目的と
する効果は達成し得ない。Incidentally, in recent years, in order to prevent phase separation at the time of polymerization when producing an acrylic acid-based water-absorbing resin, a technique in which a small amount of the second monomer is present in an amount of about 5 to 20% by weight (Japanese Patent Laid-Open No. No. 165610) is proposed, and β-acryloyloxypropionic acid is exemplified as one kind of the second monomer in that case. However, the use of such a small amount of β-acryloyloxypropionic acid cannot achieve the desired effects of the present invention.
【0020】本発明に必須に用いられるアクリル酸オリ
ゴマー(塩)は、上記した如く一般式(1)で表わされ
るが、式中のnの数としては通常nが1〜10程度、好
ましくは1〜5の混合物または純品が用いられるが、水
や尿の吸水を主目的とする場合、nが1のものの割合が
50〜100モル%のアクリル酸オリゴマー(塩)を用
いることがより好ましい。その際にアクリル酸オリゴマ
ー(塩)中にnが0の酸、即ち、アクリル酸が少量含ま
れていてもよいが、その許容含有量は目的に応じて適宜
用いられる共重合成分としてのアクリル酸の使用量に応
じて決められるべきであり、例えば共重合成分としてア
クリル酸を70重量%用いる場合はアクリル酸オリゴマ
−(塩)中に、総量に対して70重量%以下のアクリル
酸が含まれていて良い。勿論、その含有量が共重合成分
としての使用量に達しない場合は、不足するアクリル酸
を追加すれば良い。The acrylic acid oligomer (salt) that is essential to the present invention is represented by the general formula (1) as described above, and the number of n in the formula is usually about 1 to 10, preferably 1. Although a mixture of 5 to 5 or a pure product is used, when the main purpose is to absorb water or urine, it is more preferable to use an acrylic acid oligomer (salt) in which the ratio of n = 1 is 50 to 100 mol%. At this time, the acrylic acid oligomer (salt) may contain a small amount of an acid with n = 0, that is, acrylic acid, but the permissible content is acrylic acid as a copolymerization component which is appropriately used depending on the purpose. The amount should be determined according to the amount used, for example, when 70% by weight of acrylic acid is used as the copolymerization component, the acrylic acid oligomer (salt) contains 70% by weight or less of the total amount of acrylic acid. You can stay. Of course, if the content does not reach the amount used as the copolymerization component, acrylic acid which is insufficient may be added.
【0021】アクリル酸オリゴマーの合成は公知の手段
によって行われ、例えば、(I)アクリル酸自身のマイ
ケル付加反応、(II)アクリル酸またはアクリル酸クロ
ライドと3−ヒドロキシプロピオン酸とのエステル化反
応、(III) アクリル酸によるβ−プロピオラクトンの開
環反応などによって合成されるが、これらの内、(I)
の合成法が好ましい。また、アクリル酸オリゴマーの入
手法として、アクリル酸製造の際の副生物アクリル酸オ
リゴマーを分離精製するという方法を用いると、大量に
且つ極めて安価な製造も可能である。The acrylic acid oligomer is synthesized by known means, for example, (I) a Michael addition reaction of acrylic acid itself, (II) an esterification reaction of acrylic acid or acrylic acid chloride with 3-hydroxypropionic acid, (III) It is synthesized by a ring-opening reaction of β-propiolactone with acrylic acid, among which (I)
Is preferred. Further, if a method of separating and refining a by-product acrylic acid oligomer in the production of acrylic acid is used as a method of obtaining the acrylic acid oligomer, it is possible to produce it in a large amount at a very low cost.
【0022】本発明で用いられるアクリル酸オリゴマー
(塩)は安価な原料である上に、吸水性樹脂の単量体に
多く用いられるアクリル酸に比べ、高沸点で揮発しにく
く、しかも、重合性や安全性に優れている。更に、アク
リル酸オリゴマー(塩)はアクリル酸(塩)と類似の構
造を有するために、現在、主流であるアクリル酸(塩)
系吸水性樹脂の製造設備や製造工程をそのまま用いて、
本発明の吸水性樹脂の製造をも行なうことができる。The acrylic acid oligomer (salt) used in the present invention is an inexpensive raw material and, at the same time, has a higher boiling point and is less likely to volatilize than acrylic acid, which is often used as a monomer of the water-absorbent resin. And excellent in safety. Furthermore, since the acrylic acid oligomer (salt) has a structure similar to that of acrylic acid (salt), acrylic acid (salt), which is currently the mainstream, is used.
Using the manufacturing equipment and manufacturing process of the water-based water absorbent resin,
The water absorbent resin of the present invention can also be produced.
【0023】本発明では親水性不飽和単量体として、上
記したアクリル酸オリゴマー(塩)を必須成分として用
いるものであるが、目的に応じて該アクリル酸オリゴマ
−(塩)以外の親水性単量体および/または疎水性単量
体を第2の単量体として併用してもよい。In the present invention, the above-mentioned acrylic acid oligomer (salt) is used as an essential component as the hydrophilic unsaturated monomer, but a hydrophilic monomer other than the acrylic acid oligomer (salt) may be used depending on the purpose. A monomer and / or a hydrophobic monomer may be used together as the second monomer.
【0024】本発明において併用される第2の単量体と
しては、前記アクリル酸オリゴマ−(塩)と共重合し得
るものであれば特に制限はなく、親水性単量体として例
えば、アクリル酸、メタクリル酸、マレイン酸、無水マ
レイン酸、フマール酸、クロトン酸、イタコン酸、ビニ
ルスルホン酸、スチレンスルホン酸、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、スルホエトキシポリエチ
レングリコールモノ(メタ)アクリレートなどの酸基含
有の親水性単量体およびその塩;アクリルアミド、メタ
アクリルアミド、N−エチル(メタ)アクリルアミド、
N−n−プロピル(メタ)アクリルアミド、N−イソプ
ロピル(メタ)アクリルアミド、N,N−メチル(メ
タ)アクリルアミド、2−ヒドロキシエチル(メタ)ア
クリレート、2−ヒドロキシプロピル(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、ポリエチレングリコールモノ(メタ)アクリレ
ート、ビニルピリジン、N−ビニルピロリドン、N−ア
クリロイルピペリジン、N−アクリロイルピロリジンな
どのノニオン性の親水性単量体;N,N−ジメチルアミ
ノエチル(メタ)アクリレート、N,N−ジエチルアミ
ノエチル(メタ)アクリレート、N,N−ジメチルアミ
ノプロピル(メタ)アクリレート、N,N−ジメチルア
ミノプロピル(メタ)アクリルアミドおよびその四級塩
などのカチオン性の親水性単量体などを挙げることがで
き、これらの群から選ばれる1種あるいは2種以上を使
用できる。また、親水性単量体として、メチル(メタ)
アクリレート、エチル(メタ)アクリレート、酢酸ビニ
ルなどの様に重合体後の官能基の加水分解によって、吸
水性樹脂を形成する親水性不飽和単量体を用いてもよ
い。これら例示の親水性単量体の中でも、アクリル酸オ
リゴマー(塩)との共重合性および得られる吸水性樹脂
の諸物性の面などから、アクリル酸(塩)、メタクリル
酸(塩)、2−(メタ)アクリロイルエタンスルホン酸
(塩)、2−(メタ)アクリルアミド−2−メチルプロ
パンスルホン酸(塩)、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、アクリルアミドが好ましく、
アクリル酸(塩)が更に好ましい。The second monomer used in the present invention is not particularly limited as long as it can be copolymerized with the acrylic acid oligomer (salt), and the hydrophilic monomer is, for example, acrylic acid. , Methacrylic acid, maleic acid, maleic anhydride, fumaric acid, crotonic acid, itaconic acid, vinylsulfonic acid, styrenesulfonic acid, 2- (meth) acrylamido-2-methylpropanesulfonic acid, 2- (meth) acryloylethanesulfone Acid groups, hydrophilic monomers containing an acid group such as 2- (meth) acryloylpropanesulfonic acid, sulfoethoxypolyethylene glycol mono (meth) acrylate and salts thereof; acrylamide, methacrylamide, N-ethyl (meth) acrylamide,
N-n-propyl (meth) acrylamide, N-isopropyl (meth) acrylamide, N, N-methyl (meth) acrylamide, 2-hydroxyethyl (meth) acrylate, 2-hydroxypropyl (meth) acrylate, methoxy polyethylene glycol ( (Meth) acrylate, polyethylene glycol mono (meth) acrylate, vinylpyridine, N-vinylpyrrolidone, N-acryloylpiperidine, N-acryloylpyrrolidine and other nonionic hydrophilic monomers; N, N-dimethylaminoethyl (meth) Cationic agents such as acrylate, N, N-diethylaminoethyl (meth) acrylate, N, N-dimethylaminopropyl (meth) acrylate, N, N-dimethylaminopropyl (meth) acrylamide and quaternary salts thereof. Can be exemplified such as an aqueous monomer can be used alone or in combination of two or more selected from these groups. In addition, as a hydrophilic monomer, methyl (meth)
You may use the hydrophilic unsaturated monomer which forms a water absorbent resin by hydrolysis of the functional group after a polymer like acrylate, ethyl (meth) acrylate, vinyl acetate. Among these exemplified hydrophilic monomers, acrylic acid (salt), methacrylic acid (salt), 2- and the like from the viewpoint of copolymerizability with acrylic acid oligomer (salt) and various physical properties of the resulting water absorbent resin. (Meth) acryloylethanesulfonic acid (salt), 2- (meth) acrylamido-2-methylpropanesulfonic acid (salt), methoxypolyethylene glycol (meth) acrylate, N, N-dimethylaminoethyl (meth) acrylate, acrylamide Preferably
Acrylic acid (salt) is more preferable.
【0025】用いられる疎水性単量体としては、スチレ
ン、塩化ビニル、ブタジエン、イソブテン、エチレン、
プロピレン、ステアリル(メタ)アクリレート、ラウリ
ル(メタ)アクリレートなどが挙げられる。As the hydrophobic monomer used, styrene, vinyl chloride, butadiene, isobutene, ethylene,
Propylene, stearyl (meth) acrylate, lauryl (meth) acrylate, etc. are mentioned.
【0026】これらの第2の単量体を用いる場合は、本
発明の目的を逸脱しない為に親水性不飽和単量体の総量
中で0〜70重量%、好ましくは0〜30重量%で使用
するのが良い。特に、疎水性単量体を用いる時は、得ら
れる吸水性樹脂の吸水能に注意を要する。When these second monomers are used, in order not to deviate from the object of the present invention, the amount of the hydrophilic unsaturated monomer is 0 to 70% by weight, preferably 0 to 30% by weight. Good to use. In particular, when a hydrophobic monomer is used, attention should be paid to the water absorption capacity of the water absorbent resin obtained.
【0027】また、得られる吸水性樹脂の吸水倍率や吸
水速度の点から、本発明で必須に用いられるアクリル酸
オリゴマー、および必要に応じて用いられるその他の酸
基含有の親水性単量体の一部又は全部を塩として用いる
のが好ましい。中和は重合前又は重合後とすることが出
来るが、通常は重合前に中和するのが良い。水や尿の吸
収を主目的とする場合、酸基の中和率は通常30〜10
0モル%、好ましくは40〜95モル%、更に好ましく
は50〜90モル%である。From the viewpoint of water absorption capacity and water absorption rate of the resulting water-absorbent resin, the acrylic acid oligomer, which is essential in the present invention, and other acid group-containing hydrophilic monomers, which are used as necessary, are used. It is preferable to use a part or all of the salt. Neutralization can be performed before or after polymerization, but it is usually preferable to neutralize before polymerization. When the main purpose is to absorb water or urine, the neutralization rate of acid groups is usually 30 to 10.
It is 0 mol%, preferably 40 to 95 mol%, and more preferably 50 to 90 mol%.
【0028】なお、酸基を中和する場合、本発明の効果
をより高める為に、通常、工業的に行われている様な過
剰の強塩基物質に徐々に酸性物質を添加する中和方法で
はなく、アクリル酸オリゴマーやその重合体が強塩基性
の条件にさらされない様に、酸性領域また弱塩基性領域
での中和が好ましい。酸性で中和を行う方法として、過
剰のアクリル酸オリゴマーやその重合体に、苛性ソーダ
などの塩基性物質を徐々に添加していく中和方法が例示
され、また、弱酸性での中和を行う方法として、炭酸
(水素)塩やアンモニア、1級アミン、2級アミンなど
の弱塩基を用いる中和方法が例示される。In the case of neutralizing the acid group, in order to further enhance the effect of the present invention, a neutralization method in which an acidic substance is gradually added to an excessively strong base substance, which is usually carried out industrially, is used. Instead, neutralization in an acidic region or a weakly basic region is preferable so that the acrylic acid oligomer and its polymer are not exposed to the strongly basic condition. As a method of neutralizing with acid, a neutralizing method of gradually adding a basic substance such as caustic soda to excess acrylic acid oligomer or its polymer is exemplified, and neutralization with weak acidity is also performed. Examples of the method include a neutralization method using a weak base such as carbonic acid (hydrogen) salt, ammonia, primary amine, and secondary amine.
【0029】本発明ではアクリル酸オリゴマー(塩)を
主成分とする親水性不飽和単量体を重合し、かつ、架橋
して吸水性樹脂を得る。In the present invention, a hydrophilic unsaturated monomer containing an acrylic acid oligomer (salt) as a main component is polymerized and crosslinked to obtain a water absorbent resin.
【0030】用いられる架橋方法としては特に制限はな
く、例えば、本発明の親水性不飽和単量体を重合させる
ことで水溶性樹脂を得た後、更に重合中や重合後に架橋
剤を添加して後架橋する方法,ラジカル重合開始剤によ
るラジカル架橋,電子線などによる放射線架橋する方法
なども挙げられるが、性能の優れた吸水性樹脂を生産性
良く得るには、予め所定量の架橋剤を親水性不飽和単量
体に添加して重合を行ない、重合と同時または重合後に
架橋反応させる方法によるのが好ましい。The cross-linking method used is not particularly limited. For example, after obtaining the water-soluble resin by polymerizing the hydrophilic unsaturated monomer of the present invention, a cross-linking agent is added during or after the polymerization. Post-crosslinking, radical crosslinking with a radical polymerization initiator, radiation crosslinking with an electron beam, etc. may be mentioned. However, in order to obtain a water absorbent resin having excellent performance with high productivity, a predetermined amount of the crosslinking agent is previously used. It is preferable to carry out the polymerization by adding it to the hydrophilic unsaturated monomer and carry out a crosslinking reaction simultaneously with or after the polymerization.
【0031】予め所定量の架橋剤を親水性不飽和単量体
に添加して重合を行ない、重合と同時または重合後に架
橋反応させる方法に用いられる架橋剤としては、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)プロピレン
グリコールジ(メタ)アクリレート、トリメチロールプ
ロパントリ(メタ)アクリレート、トリメチロールプロ
パンジ(メタ)アクリレート、(ポリ)エチレングリコ
ールジ(β−アクリロイルオキシプロピオネート)、ト
リメチロールプロパントリ(β−アクリロイルオキシプ
ロピオネート)、ポリ(メタ)アリロキシアルカン、
(ポリ)エチレングリコールジグリシジルエーテル、エ
チレングリコール、ポリエチレングリコール、グリセリ
ン、ペンタエリスリトール、エチレンジアミン、ポリエ
チレンイミンなどが例示される。また、その使用量は親
水性不飽和単量体に対して、通常、0.005〜5モル
%、より好ましくは0.01〜1モル%である。尚、こ
れらの架橋剤の中も、得られる吸水性樹脂の耐久性や吸
水特性、そして製造時の含水ゲルの取扱性などから、分
子内に2個以上の重合性不飽和基を有する重合性架橋剤
を必須に用いることが好ましい。As the crosslinking agent used in the method of adding a predetermined amount of the crosslinking agent to the hydrophilic unsaturated monomer in advance and carrying out the polymerization reaction simultaneously with or after the polymerization, N, N
′ -Methylenebisacrylamide, (poly) ethylene glycol di (meth) acrylate, (poly) propylene glycol di (meth) acrylate, trimethylolpropane tri (meth) acrylate, trimethylolpropane di (meth) acrylate, (poly) ethylene Glycoldi (β-acryloyloxypropionate), trimethylolpropane tri (β-acryloyloxypropionate), poly (meth) allyloxyalkane,
(Poly) ethylene glycol diglycidyl ether, ethylene glycol, polyethylene glycol, glycerin, pentaerythritol, ethylenediamine, polyethyleneimine, etc. are exemplified. The amount used is usually 0.005 to 5 mol% and more preferably 0.01 to 1 mol% with respect to the hydrophilic unsaturated monomer. Even among these cross-linking agents, due to the durability and water absorption properties of the resulting water-absorbent resin, and the handleability of the hydrogel at the time of production, the polymerizability of having two or more polymerizable unsaturated groups in the molecule It is preferable to essentially use a crosslinking agent.
【0032】本発明で上記した親水性不飽和単量体の重
合を行うに際して、バルク重合や沈澱重合を行うことも
可能であるが、性能面や重合の制御の容易さから、親水
性不飽和単量体を溶液として重合を行うことが好まし
い。重合系溶媒としては、親水性不飽和単量体が溶解す
る液体ならば特に制限がなく、水、メタノール、エタノ
ール、アセトン、ジメチルホルムアミド、ジメチルスル
ホキシド等が例示されるが、水または水性液が特に好ま
しい。尚、親水性不飽和単量体の濃度は飽和濃度を越え
てもかまわないが、通常、20重量%〜飽和濃度の範囲
が好ましい。When the above-mentioned hydrophilic unsaturated monomer is polymerized in the present invention, it is possible to carry out bulk polymerization or precipitation polymerization, but the hydrophilic unsaturated monomer is used because of its performance and easy control of polymerization. It is preferable to carry out the polymerization by using the monomer as a solution. The polymerization solvent is not particularly limited as long as it is a liquid in which a hydrophilic unsaturated monomer is dissolved, and examples thereof include water, methanol, ethanol, acetone, dimethylformamide, and dimethyl sulfoxide, but water or an aqueous liquid is particularly preferable. preferable. The concentration of the hydrophilic unsaturated monomer may be higher than the saturated concentration, but is usually preferably in the range of 20% by weight to the saturated concentration.
【0033】また、重合に際して、次亜燐酸塩、チオー
ル類、チオール酸類などの水溶性連鎖移動剤を併用し
て、得られた吸水性樹脂の諸特性の改善や更に分解性の
向上を行っても良い。尚、重合に際して、澱粉、セルロ
ース、ポリビニルアルコール、ポリアクリル酸、ポリア
クリル酸塩架橋体などの合成または天然親水性高分子を
存在させることも、本発明の主旨を何等変更するもので
はない。During polymerization, a water-soluble chain transfer agent such as hypophosphite, thiols and thiolic acids is used in combination to improve various properties of the water absorbent resin and further improve decomposability. Is also good. It should be noted that the presence of a synthetic or natural hydrophilic polymer such as starch, cellulose, polyvinyl alcohol, polyacrylic acid, polyacrylic acid salt cross-linked product in the polymerization does not change the gist of the present invention.
【0034】本発明における上記親水性不飽和単量体の
重合方法としては、例えば、ラジカル重合開始剤による
重合、放射線重合、電子線重合、光増感剤による紫外線
重合などを挙げることが出来るが、性能の優れた吸水性
樹脂を得るためには、ラジカル重合開始剤による重合が
好ましい。かかるラジカル重合法としては、例えば、型
枠の中で行う注型重合、ベルトコンベアー上での重合、
含水ゲル状重合体を細分化しながら行う重合などの各種
水溶液重合、逆相懸濁重合、逆相乳化重合、沈澱重合、
バルク重合などの公知の重合方法が例示できるが、逆相
懸濁重合または水溶液重合が特に好ましい。尚、重合の
際、連続重合、回文式重合の区別や減圧、加圧、常圧の
区別は特に問わないし、更に、重合時に繊維基材などを
共存させ吸水性複合体としてもよい。また、重合初期を
除けば、重合温度は実質的に0〜130℃、好ましくは
30〜100℃の範囲に保たれることが好ましい。Examples of the method for polymerizing the hydrophilic unsaturated monomer in the present invention include polymerization with a radical polymerization initiator, radiation polymerization, electron beam polymerization, and ultraviolet polymerization with a photosensitizer. In order to obtain a water absorbent resin having excellent performance, polymerization with a radical polymerization initiator is preferable. Examples of the radical polymerization method include casting polymerization performed in a mold, polymerization on a belt conveyor,
Various aqueous solution polymerizations such as polymerization while subdividing a hydrous gel polymer, reverse phase suspension polymerization, reverse phase emulsion polymerization, precipitation polymerization,
Known polymerization methods such as bulk polymerization can be exemplified, but reverse phase suspension polymerization or aqueous solution polymerization is particularly preferable. In the polymerization, continuous polymerization, palindrome polymerization, and reduced pressure, increased pressure, and normal pressure are not particularly limited, and a fibrous base material may coexist during the polymerization to form a water-absorbent composite. Further, except for the initial stage of the polymerization, it is preferable that the polymerization temperature is kept substantially in the range of 0 to 130 ° C, preferably 30 to 100 ° C.
【0035】重合に用いられるラジカル重合開始剤とし
ては、例えば、過硫酸カリウム、過硫酸アンモニウム、
過硫酸ナトリウム等の過硫酸塩;t−ブチルハイドロパ
ーオキサイド、クメンハイドロパーオキサイド等の有機
過酸化物;過酸化水素;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、亜塩
素酸塩、次亜塩素酸塩、第二セリウム塩、過マンガン酸
塩など公知の開始剤が挙げられるが、これらの中でも、
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種或は2種以上が好ましい。また、酸化性ラジカ
ル重合開始剤を用いる場合、亜硫酸(水素)塩やL−ア
スコルビン酸などの還元剤を併用してもよいし、更にア
ゾ系重合開始剤などを用いる場合は紫外線を併用してよ
い。尚、これらラジカル重合開始剤は重合系に一括添加
してもよいし、逐次添加してもよいが、通常、その使用
量は親水性不飽和単量体に対して0.001〜2モル
%、更に好ましくは0.01〜1モル%である。The radical polymerization initiator used for the polymerization is, for example, potassium persulfate, ammonium persulfate,
Persulfates such as sodium persulfate; Organic peroxides such as t-butyl hydroperoxide and cumene hydroperoxide; Hydrogen peroxide; Azo compounds such as 2,2′-azobis (2-amidinopropane) dihydrochloride Other examples include known initiators such as chlorite, hypochlorite, cerium salt, and permanganate. Among these, among these,
One or more selected from the group consisting of persulfates, hydrogen peroxide and azo compounds are preferable. When an oxidizing radical polymerization initiator is used, a reducing agent such as a sulfurous acid (hydrogen) salt or L-ascorbic acid may be used in combination, and when an azo polymerization initiator is used, ultraviolet rays may be used in combination. Good. In addition, these radical polymerization initiators may be added to the polymerization system all at once or may be added sequentially, but the amount used is usually 0.001 to 2 mol% relative to the hydrophilic unsaturated monomer. , And more preferably 0.01 to 1 mol%.
【0036】重合後のゲル状重合体は用途や重合後の固
形分などに応じて、必要により乾燥される。用いられる
乾燥方法としては、熱風乾燥、疎水性有機溶剤中での共
沸脱水、メタノール等の溶剤を加えることによる脱水な
どの公知の乾燥方法が挙げられ、特に制限はない。The gelled polymer after the polymerization is optionally dried depending on the use and the solid content after the polymerization. The drying method used includes known drying methods such as hot air drying, azeotropic dehydration in a hydrophobic organic solvent, and dehydration by adding a solvent such as methanol, and is not particularly limited.
【0037】本発明における乾燥温度は室温〜150℃
の範囲が好ましく、更に好ましくは60〜130℃であ
る。なお、従来の吸水性樹脂では、生産性や吸水特性な
どの改善のために、150〜250℃という高温乾燥が
好ましく用いられている。しかし、本発明により得られ
る吸水性樹脂の場合、かかる高温での乾燥は、有機溶剤
水溶液や高塩濃度の水溶液に対する吸水能や使用後廃棄
する際の分解性などを低下させる場合があり注意を要す
る。The drying temperature in the present invention is room temperature to 150 ° C.
Is preferable, and more preferably 60 to 130 ° C. In the conventional water absorbent resin, high temperature drying at 150 to 250 ° C. is preferably used in order to improve productivity and water absorption characteristics. However, in the case of the water-absorbent resin obtained by the present invention, such high temperature drying may reduce the water-absorbing ability for an organic solvent aqueous solution or an aqueous solution having a high salt concentration and the decomposability at the time of disposal after use. It costs.
【0038】更に、本発明においては乾燥温度のみなら
ず、重合温度や重合後の加熱温度も、150℃を越える
ことは同様の理由によって好ましくない。よって、本発
明での吸水性樹脂の製造は、重合時から最終製品に至る
全工程で、加熱操作を行う時は実質的に0〜150℃、
好ましくは30〜130℃で行われる。なお、重合開始
時または極初期の単量体の温度や中間の搬送工程などの
温度は、0℃以下であっても何等さしさわりはない。Further, in the present invention, not only the drying temperature but also the polymerization temperature and the heating temperature after the polymerization are more than 150 ° C., which is not preferable for the same reason. Therefore, the production of the water-absorbent resin in the present invention is substantially 0 to 150 ° C. when the heating operation is performed in all steps from the polymerization to the final product.
It is preferably carried out at 30 to 130 ° C. It should be noted that the temperature of the monomer at the start of the polymerization or at the very initial stage, and the temperature in the intermediate conveying step and the like may be 0 ° C. or lower, which does not matter.
【0039】以上の様にして得られた吸水性樹脂は、更
に粉砕や造粒を行って粒度を調整してもよい。例えば粉
末を目的とする場合、平均粒子径10〜2000μm、
更に好ましくは100〜1000μm、最も好ましくは
300〜600μm程度に調製される。また、得られた
吸水性樹脂の表面近傍を更に架橋したり、乾燥前や乾燥
後の吸水性樹脂に亜硫酸(水素)塩などの還元剤、不活
性無機物、界面活性剤などを添加して、その諸物性を改
善してもよい。The water-absorbent resin obtained as described above may be pulverized or granulated to adjust the particle size. For example, when a powder is intended, the average particle size is 10 to 2000 μm,
The thickness is more preferably 100 to 1000 μm, most preferably 300 to 600 μm. Further, the surface of the resulting water-absorbent resin is further cross-linked, or by adding a reducing agent such as a sulfite (hydrogen) salt to the water-absorbent resin before or after drying, an inert inorganic substance, or a surfactant. Its physical properties may be improved.
【0040】更に本発明は新規な吸水性樹脂をも提供す
るものである。即ち、本発明の吸水性樹脂は、一般式
(2)で示される構造単位に由来する成分の総量が30
〜100重量%の割合である新規な吸水性樹脂であり、
ある種の液に対する吸液能に優れ、かつ、加熱すること
によって低分子物質に容易に分解するという従来にない
特性を示す吸水性樹脂である。Further, the present invention also provides a novel water absorbent resin. That is, in the water absorbent resin of the present invention, the total amount of components derived from the structural unit represented by the general formula (2) is 30.
A novel water-absorbent resin having a proportion of ˜100% by weight,
It is a water-absorbent resin that has an unprecedented property that it has an excellent ability to absorb a certain liquid and that it is easily decomposed into a low-molecular substance when heated.
【0041】即ち、本発明の吸水性樹脂は、実使用され
る室温程度では高い耐久性を示すが、加熱や含水状態で
長時間放置すると、低分子物質に容易に分解する。低分
子物質への分解率は加熱によって大きく促進され、短時
間で分解させるためには130℃以上が好ましく、例え
ば、150℃で60分間の加熱では、その8重量%以上
が低分子物質に分解する。よって、本発明の吸水性樹脂
は使用後廃棄する際に低分子物質に容易に熱分解でき、
埋め立て処理や堆肥に導くコンポスト処理に好適であ
る。なお、分解させる際に、酸化剤、還元剤、紫外線な
どを併用することは、本発明の主旨を変更するものでは
ない。That is, the water-absorbent resin of the present invention exhibits high durability at about room temperature when it is actually used, but it easily decomposes into a low-molecular substance when left for a long time in a heated or water-containing state. The decomposition rate into low-molecular substances is greatly accelerated by heating, and 130 ° C or higher is preferable for decomposing in a short time. For example, when heated at 150 ° C for 60 minutes, 8% by weight or more decomposes into low-molecular substances. To do. Therefore, the water-absorbent resin of the present invention can be easily thermally decomposed into a low-molecular substance when discarded after use,
It is suitable for landfill processing and compost processing leading to compost. It should be noted that the combined use of an oxidizing agent, a reducing agent, ultraviolet rays, and the like when decomposing does not change the gist of the present invention.
【0042】[0042]
【発明の効果】本発明の吸水性樹脂およびその製造方法
は、以下の利点を有する。The water absorbent resin of the present invention and the method for producing the same have the following advantages.
【0043】(1)高濃度の有機溶剤水溶液に対して
も、従来の吸水性樹脂に比べ飛躍的に高い吸水倍率を示
す。(1) A water absorption capacity is dramatically higher than that of a conventional water-absorbent resin even for a high-concentration organic solvent aqueous solution.
【0044】(2)耐塩性に優れ、濃い塩濃度溶液に対
しても、高い吸水倍率を示す。(2) It has excellent salt resistance and shows a high water absorption capacity even in a concentrated salt concentration solution.
【0045】(3)常温では高い耐久性を示すが、加熱
することで容易に低分子化合物に分解する。よって、埋
め立て処理や堆肥に導くコンポスト処理などの使用後の
廃棄に好適である。(3) It has high durability at room temperature, but easily decomposes into a low molecular weight compound by heating. Therefore, it is suitable for disposal after use, such as landfill processing and compost processing leading to compost.
【0046】(4)用いる単量体が容易に製造でき安価
で、且つ高い重合性・生産性を示し、加えて、アクリル
酸と比べて高沸点・低揮発性である。(4) The monomer to be used can be easily produced, is inexpensive, exhibits high polymerizability and productivity, and has a high boiling point and low volatility as compared with acrylic acid.
【0047】(5)単量体がアクリル酸誘導体であるた
め、従来広く行われているアクリル酸系吸水性樹脂の製
造方法をそのまま適用できる。(5) Since the monomer is an acrylic acid derivative, the conventionally widely used method for producing an acrylic acid-based water absorbent resin can be applied as it is.
【0048】[0048]
【実施例】以下、実施例によって本発明を説明するが、
本発明の範囲が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.
The scope of the invention is not limited to only these examples. The various physical properties of the water absorbent resin described in the examples are values measured by the following test methods.
【0049】(1)吸水倍率 吸水させる水溶液としては、有機溶剤水溶液の(a)イ
ソプロピルアルコール50重量%水溶液、標準生理食塩
水の(b)0.9%塩化ナトリウム水溶液、高塩濃度水
溶液の(c)5%塩化ナトリウム水溶液、(d)10%
塩化ナトリウム水溶液、(e)20%塩化ナトリウム水
溶液の5種類を用い、各々、吸水倍率を測定した。(1) Water absorption ratio As the aqueous solution to be absorbed, (a) 50% by weight isopropyl alcohol aqueous solution of organic solvent, (b) 0.9% sodium chloride aqueous solution, and high salt concentration aqueous solution ( c) 5% sodium chloride aqueous solution, (d) 10%
The water absorption capacity was measured for each of five types of aqueous sodium chloride solution and (e) 20% aqueous sodium chloride solution.
【0050】測定方法としては、吸水性樹脂0.2gを
入れた不織布製のティーバッグ式袋(40*150m
m)を、(a)〜(e)の所定の水溶液中に2時間浸漬
した後に、ティーバッグ式袋の水切りを行った後の重量
を測定し、以下の式で吸水倍率を算出した。As a measuring method, a non-woven tea bag type bag (40 * 150 m) containing 0.2 g of a water absorbent resin is used.
m) was dipped in the predetermined aqueous solution of (a) to (e) for 2 hours, the tea bag bag was drained, the weight was measured, and the water absorption capacity was calculated by the following formula.
【0051】[0051]
【数1】 [Equation 1]
【0052】(2)分解性 得られた吸水性樹脂を150℃で1時間加熱した後、分
解発生した低分子化合物を定量することで、本発明の吸
水性樹脂特有の現象である低分子化合物への分解性(重
量%)の指標とした。なお、参考のため、分解させる前
の吸水性樹脂中の残存モノマー量も測定したが、何れ
も、0.1重量%以下であった。発生した低分子化合物
の定量方法としては、吸水性樹脂0.5gを1000m
lの脱イオン水中で2時間撹拌した後、その濾液を液体
クロマトクラフィーで分析する手法によった。(2) Degradability The obtained water-absorbent resin is heated at 150 ° C. for 1 hour, and the low-molecular compound decomposed and generated is quantified to obtain a low-molecular compound which is a phenomenon peculiar to the water-absorbent resin of the present invention. Was used as an index of degradability (% by weight). For reference, the amount of residual monomers in the water absorbent resin before decomposition was also measured, but all were 0.1% by weight or less. As a method for quantifying the generated low molecular weight compound, 0.5 g of the water absorbent resin is 1000 m
After stirring in 1 l of deionized water for 2 hours, the filtrate was analyzed by liquid chromatography.
【0053】[0053]
【実施例1】 一般式(1)で表される酸基含有単量体
として、β−アクリロイルオキシプロピオン酸を用い吸
水性樹脂を得た。Example 1 A water absorbent resin was obtained by using β-acryloyloxypropionic acid as the acid group-containing monomer represented by the general formula (1).
【0054】即ち、51.62gの水にβ−アクリロイ
ルオキシプロピオン酸29.81gおよびアクリル酸
9.06gからなる酸基含有単量体を溶解させた後、氷
冷しながら48重量%の苛性ソーダ水溶液19.41g
を徐々に添加することで、常にpHが酸性になるように
酸基を中和した。次いで、中和後の溶液に架橋剤として
ポリエチレングリコールジアクリレート(n=8)を
0.01モル%(対全モノマー)溶解させた。こうし
て、一般式(1)で表される単量体を75重量%含有す
る濃度40%、中和率70%の親水性不飽和単量体水溶
液を得た。That is, after dissolving the acid group-containing monomer consisting of 29.81 g of β-acryloyloxypropionic acid and 9.06 g of acrylic acid in 51.62 g of water, a 48% by weight aqueous solution of sodium hydroxide was added while cooling with ice. 19.41g
Was gradually added to neutralize the acid groups so that the pH was always acidic. Next, 0.01 mol% (relative to all monomers) of polyethylene glycol diacrylate (n = 8) was dissolved as a crosslinking agent in the neutralized solution. Thus, a hydrophilic unsaturated monomer aqueous solution containing 75% by weight of the monomer represented by the general formula (1) and having a concentration of 40% and a neutralization ratio of 70% was obtained.
【0055】別に、撹拌機、還流冷却器、温度計、窒素
ガス導入管および滴下漏斗を備え付けた500mlの4
ツ口セパララブルフラスコを反応容器として用意し、こ
の中にシクロヘキサン200mlおよびソルビタンモノ
ステアレート(HLB4.7)1.0gを入れ、更に窒
素置換した。Separately, 500 ml of 4 equipped with a stirrer, a reflux condenser, a thermometer, a nitrogen gas introducing pipe and a dropping funnel.
A two-necked separable flask was prepared as a reaction vessel, and 200 ml of cyclohexane and 1.0 g of sorbitan monostearate (HLB4.7) were put therein, and the atmosphere was replaced with nitrogen.
【0056】次いで、親水性不飽和単量体を窒素置換
後、過硫酸ナトリウムを0.05モル(対モノマー)溶
解させ、上記セパラブルフラスコに加え、撹拌下分散さ
た。その後、シクロヘキサン相を60℃に昇温させるこ
とで、親水性不飽和単量体の重合を開始させ、更に2時
間重合を継続させた後、得られた含水ゲル状物を共沸脱
水し、更に60℃で減圧乾燥した。こうして得られた吸
水性樹脂1の諸物性を表1に示す。Next, after substituting the hydrophilic unsaturated monomer with nitrogen, 0.05 mol of sodium persulfate (relative to the monomer) was dissolved, added to the separable flask and dispersed with stirring. Then, by heating the cyclohexane phase to 60 ° C., the polymerization of the hydrophilic unsaturated monomer is started, and the polymerization is further continued for 2 hours, and then the obtained hydrous gel is azeotropically dehydrated. Further, it was dried under reduced pressure at 60 ° C. Table 1 shows the physical properties of the water absorbent resin 1 thus obtained.
【0057】[0057]
【実施例2】 実施例1における親水性不飽和単量体の
代わりに、50.25gの水にβ−アクリロイルオキシ
プロピオン酸23.85gおよびアクリル酸14.50
gを溶解させた後、48重量%の苛性ソーダ水溶液2
1.41gで中和し、更に架橋剤としてポリエチレング
リコールジアクリレート(n=8)を0.01モル%
(対全モノマー)溶解さることで、一般式(1)で表さ
れる単量体を60重量%含有する濃度40%、中和率7
0%の親水性不飽和単量体を得た。Example 2 Instead of the hydrophilic unsaturated monomer in Example 1, 23.85 g of β-acryloyloxypropionic acid and 14.50 acrylic acid were added to 50.25 g of water.
After dissolving g, 48 wt% caustic soda aqueous solution 2
Neutralize with 1.41 g, and 0.01 mol% polyethylene glycol diacrylate (n = 8) as a crosslinking agent.
(Vs total monomer) Dissolved to contain 60% by weight of the monomer represented by the general formula (1), concentration 40%, neutralization rate 7
0% of hydrophilic unsaturated monomer was obtained.
【0058】以下、実施例1と同様に重合し、更に共沸
脱水および減圧乾燥することで吸水性樹脂2を得た。結
果を表1に示す。Thereafter, polymerization was carried out in the same manner as in Example 1, followed by azeotropic dehydration and vacuum drying to obtain a water absorbent resin 2. The results are shown in Table 1.
【0059】[0059]
【実施例3】 実施例1における親水性不飽和単量体の
代わりに、48.33gの水にβ−アクリロイルオキシ
プロピオン酸15.90gおよびアクリル酸21.75
gを溶解させた後、48重量%の苛性ソーダ水溶液2
4.06gで中和し、更に架橋剤としてポリエチレング
リコールジアクリレート(n=8)を0.01モル%
(対全モノマー)溶解さることで、一般式(1)で表さ
れる単量体を40重量%含有する濃度40%、中和率7
0%の親水性不飽和単量体を得た。Example 3 Instead of the hydrophilic unsaturated monomer in Example 1, 15.90 g of β-acryloyloxypropionic acid and 21.75 acrylic acid were added to 48.33 g of water.
After dissolving g, 48 wt% caustic soda aqueous solution 2
Neutralization with 4.06 g, 0.01 mol% polyethylene glycol diacrylate (n = 8) as a crosslinking agent
(To all monomers) By dissolving, 40% by weight of the monomer represented by the general formula (1) is contained at a concentration of 40% and a neutralization rate of 7
0% of hydrophilic unsaturated monomer was obtained.
【0060】以下、実施例1と同様に重合し、更に共沸
脱水および減圧乾燥することで吸水性樹脂3を得た。結
果を表1に示す。Thereafter, polymerization was carried out in the same manner as in Example 1, followed by azeotropic dehydration and vacuum drying to obtain a water absorbent resin 3. The results are shown in Table 1.
【0061】[0061]
【実施例4】 実施例1における親水性不飽和単量体の
代わりに、58.83gの水にβ−アクリロイルオキシ
プロピオン酸25.39gおよびアクリル酸8.56g
を溶解させた後、48重量%の苛性ソーダ水溶液17.
22gで中和し、更に架橋剤としてポリエチレングリコ
ールジ(β−アクリロイルオキシプロピオネート)(n
=7)を0.05モル%(対モノマー)溶解さること
で、一般式(1)で表される単量体を73重量%含有す
る濃度35%、中和率70%の親水性不飽和単量体を得
た。Example 4 Instead of the hydrophilic unsaturated monomer in Example 1, 25.39 g of β-acryloyloxypropionic acid and 8.56 g of acrylic acid were added to 58.83 g of water.
After being dissolved, a 48 wt% caustic soda aqueous solution 17.
It was neutralized with 22 g, and polyethylene glycol di (β-acryloyloxypropionate) (n
= 7) is dissolved by 0.05 mol% (relative to the monomer) to contain 73 wt% of the monomer represented by the general formula (1) at a concentration of 35% and a neutralization rate of 70%. A monomer was obtained.
【0062】以下、実施例1において、上記単量体を用
い、且つ分散剤をソルビタンモノステアレートからエチ
ルセルロースに代える以外は実施例1と同様に重合し、
更に共沸脱水および減圧乾燥することで吸水性樹脂4を
得た。結果を表1に示す。Polymerization was carried out in the same manner as in Example 1 except that the above monomers were used and the dispersant was changed from sorbitan monostearate to ethyl cellulose.
Further, water-absorbent resin 4 was obtained by azeotropic dehydration and vacuum drying. The results are shown in Table 1.
【0063】[0063]
【比較例1】 一般式(1)で表される酸基含有単量体
を用いずに、アクリル酸を用いて吸水性樹脂を得た。Comparative Example 1 A water absorbent resin was obtained by using acrylic acid without using the acid group-containing monomer represented by the general formula (1).
【0064】即ち、実施例1の親水性不飽和単量体の調
製において、アクリル酸36.25gを水44.38g
に溶解させた後、48重量%の苛性ソーダ水溶液29.
37gで中和し、更に架橋剤としてポリエチレングリコ
ールジアクリレート(n=8)を0.01モル%(対モ
ノマー)溶解さることで、濃度40%、中和率70%の
アクリル酸塩よりなる親水性不飽和単量体水溶液を得
た。That is, in the preparation of the hydrophilic unsaturated monomer of Example 1, 36.25 g of acrylic acid was added to 44.38 g of water.
After being dissolved in water, a 48 wt% caustic soda aqueous solution 29.
Neutralization with 37 g and 0.01 mol% of polyethylene glycol diacrylate (n = 8) as a cross-linking agent (relative to monomer) were dissolved to obtain a hydrophilic hydrophilic acrylate salt having a concentration of 40% and a neutralization rate of 70%. Aqueous unsaturated monomer aqueous solution was obtained.
【0065】以下、実施例1と同様に重合し、更に共沸
脱水および減圧乾燥することで比較吸水性樹脂1を得
た。結果を表1に示す。Thereafter, polymerization was carried out in the same manner as in Example 1, followed by azeotropic dehydration and vacuum drying to obtain comparative water absorbent resin 1. The results are shown in Table 1.
【0066】[0066]
【比較例2】 一般式(1)で表される酸基含有単量体
の少ない親水性不飽和単量体より吸水性樹脂を得た。Comparative Example 2 A water absorbent resin was obtained from a hydrophilic unsaturated monomer having a small amount of acid group-containing monomer represented by the general formula (1).
【0067】即ち、実施例1の親水性不飽和単量体の調
製において、46.33gの水にβ−アクリロイルオキ
シプロピオン酸7.95gおよびアクリル酸29.00
gを溶解させた後、48重量%の苛性ソーダ水溶液2
6.71gで中和し、更に架橋剤としてポリエチレング
リコールジアクリレート(n=8)を0.01モル%
(対モノマー)溶解さることで、一般式(1)で表され
る単量体を20重量%含有する濃度40%、中和率70
%の親水性不飽和単量体を得た。That is, in the preparation of the hydrophilic unsaturated monomer of Example 1, 7.95 g of β-acryloyloxypropionic acid and 29.00 of acrylic acid were added to 46.33 g of water.
After dissolving g, 48 wt% caustic soda aqueous solution 2
Neutralize with 6.71 g, and 0.01 mol% polyethylene glycol diacrylate (n = 8) as a crosslinking agent.
(To Monomer) By being dissolved, the concentration of the monomer represented by the general formula (1) is 20% by weight, the concentration is 40%, and the neutralization rate is 70.
% Hydrophilically unsaturated monomer was obtained.
【0068】以下、実施例1と同様に重合し、更に共沸
脱水および減圧乾燥することで比較吸水性樹脂2を得
た。結果を表1に示す。Thereafter, polymerization was carried out in the same manner as in Example 1, followed by azeotropic dehydration and vacuum drying to obtain comparative water absorbent resin 2. The results are shown in Table 1.
【0069】[0069]
【比較例3】 スルホン酸系の酸基含有単量体より吸水
性樹脂を得た。Comparative Example 3 A water absorbent resin was obtained from a sulfonic acid group-containing acid group-containing monomer.
【0070】即ち、実施例1の親水性不飽和単量体の調
製において、中和率75%で濃度40%のスルホエチル
メタクリレートナトリウム塩水溶液110gに、更に架
橋剤としてポリエチレングリコールジアクリレート(n
=8)を0.01モル%(対モノマー)溶解さることで
親水性不飽和単量体を得た。That is, in the preparation of the hydrophilic unsaturated monomer of Example 1, 110 g of a sulfoethyl methacrylate sodium salt aqueous solution having a neutralization rate of 75% and a concentration of 40% was further added with polyethylene glycol diacrylate (n
= 8) was dissolved in 0.01 mol% (relative to the monomer) to obtain a hydrophilic unsaturated monomer.
【0071】以下、実施例1と同様に重合し、更に共沸
脱水および減圧乾燥することで比較吸水性樹脂3を得
た。結果を表1に示す。Thereafter, polymerization was carried out in the same manner as in Example 1, followed by azeotropic dehydration and drying under reduced pressure to obtain a comparative water absorbent resin 3. The results are shown in Table 1.
【0072】[0072]
【表1】 [Table 1]
【0073】表1から明らかな様に、本発明の吸水性樹
脂は生理食塩水への吸水能も高い上に、しかも、従来の
吸水性樹脂である比較吸水性樹脂と比べ、(1)50%
イソプロパノール水溶液や、(2)20%塩化ナトリウ
ム水溶液など、多量の塩類や有機溶剤を含んだ水性液に
対しても高吸水倍率を示し、かつ、(3)加熱によって
容易に低分子化合物に分解する。As is clear from Table 1, the water-absorbent resin of the present invention has a high ability to absorb physiological saline, and moreover, (1) 50 compared with the comparative water-absorbent resin which is a conventional water-absorbent resin. %
It has a high water absorption capacity even for aqueous solutions containing a large amount of salts and organic solvents such as isopropanol aqueous solution and (2) 20% sodium chloride aqueous solution, and (3) easily decomposes into low molecular weight compounds by heating. .
───────────────────────────────────────────────────── フロントページの続き (72)発明者 増田 善彦 兵庫県姫路市網干区興浜字西沖992番地の 1 株式会社日本触媒姫路研究所内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Yoshihiko Masuda 1 992, Nishioki, Okihama, Aboshi-ku, Himeji-shi, Hyogo 1
Claims (5)
で含む親水性不飽和単量体を重合することを特徴とする
吸水性樹脂の製造方法。1. A general formula (1): A method for producing a water-absorbent resin, comprising polymerizing a hydrophilic unsaturated monomer containing the acid group-containing monomer represented by the above in a proportion of 30 to 100% by weight.
1記載の製造方法。2. The production method according to claim 1, wherein a polymerizable crosslinking agent is allowed to coexist during the polymerization.
下で行われる請求項1記載の製造方法。3. The production method according to claim 1, wherein the polymerization is carried out under a temperature condition of substantially 30 to 100 ° C.
われる請求項1記載の製造方法。4. The production method according to claim 1, wherein the polymerization is carried out by reverse phase suspension polymerization or aqueous solution polymerization.
0重量%の割合である吸水性樹脂。5. A general formula (2): The total amount of components derived from the structural unit represented by
Water-absorbent resin in a proportion of 0% by weight.
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Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH07126215A (en) * | 1993-10-29 | 1995-05-16 | Otsuka Chem Co Ltd | Oligo(beta-propyolactone) macromer and electrolyte and cell using thereof |
JPH07316237A (en) * | 1994-05-20 | 1995-12-05 | Degussa Ag | Polycarboxylate,its production,laundering and cleaning method for woven fiber,cobuilder and builder for detergent, and laundry detergent and detergent |
JP2000026538A (en) * | 1999-06-21 | 2000-01-25 | Nippon Shokubai Co Ltd | Low degradable water-absorbing resin and production thereof |
WO2006011516A1 (en) | 2004-07-28 | 2006-02-02 | Sumitomo Seika Chemicals Co., Ltd. | Method for producing carboxyl group-containing water-soluble polymer |
JP2010506000A (en) * | 2006-10-04 | 2010-02-25 | ザ ユニバーシティ オブ アクロン | Synthesis of inimer and hyperbranched polymers |
EP2673011B1 (en) | 2011-02-07 | 2015-04-08 | Basf Se | Procedure for preparing water absorbing polymer particles having high free swell rate |
CN109843947A (en) * | 2016-11-02 | 2019-06-04 | 诺沃梅尔公司 | Absorbable polymer and its manufacturing method and application thereof |
-
1992
- 1992-08-05 JP JP20925492A patent/JP3251647B2/en not_active Expired - Fee Related
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH07126215A (en) * | 1993-10-29 | 1995-05-16 | Otsuka Chem Co Ltd | Oligo(beta-propyolactone) macromer and electrolyte and cell using thereof |
JPH07316237A (en) * | 1994-05-20 | 1995-12-05 | Degussa Ag | Polycarboxylate,its production,laundering and cleaning method for woven fiber,cobuilder and builder for detergent, and laundry detergent and detergent |
JP2000026538A (en) * | 1999-06-21 | 2000-01-25 | Nippon Shokubai Co Ltd | Low degradable water-absorbing resin and production thereof |
WO2006011516A1 (en) | 2004-07-28 | 2006-02-02 | Sumitomo Seika Chemicals Co., Ltd. | Method for producing carboxyl group-containing water-soluble polymer |
JP2006036982A (en) * | 2004-07-28 | 2006-02-09 | Sumitomo Seika Chem Co Ltd | Method for producing carboxy group-containing water-soluble polymer |
EP1772470A4 (en) * | 2004-07-28 | 2011-02-16 | Sumitomo Seika Chemicals | Method for producing carboxyl group-containing water-soluble polymer |
JP4759236B2 (en) * | 2004-07-28 | 2011-08-31 | 住友精化株式会社 | Method for producing carboxyl group-containing water-soluble polymer |
JP2010506000A (en) * | 2006-10-04 | 2010-02-25 | ザ ユニバーシティ オブ アクロン | Synthesis of inimer and hyperbranched polymers |
EP2673011B1 (en) | 2011-02-07 | 2015-04-08 | Basf Se | Procedure for preparing water absorbing polymer particles having high free swell rate |
CN109843947A (en) * | 2016-11-02 | 2019-06-04 | 诺沃梅尔公司 | Absorbable polymer and its manufacturing method and application thereof |
EP3535305A4 (en) * | 2016-11-02 | 2020-06-24 | Novomer, Inc. | Absorbent polymers, and methods of producing thereof and uses thereof |
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