JPH06192319A - Production of water-absorbing resin - Google Patents
Production of water-absorbing resinInfo
- Publication number
- JPH06192319A JPH06192319A JP34657892A JP34657892A JPH06192319A JP H06192319 A JPH06192319 A JP H06192319A JP 34657892 A JP34657892 A JP 34657892A JP 34657892 A JP34657892 A JP 34657892A JP H06192319 A JPH06192319 A JP H06192319A
- Authority
- JP
- Japan
- Prior art keywords
- water
- absorbent resin
- residual monomer
- powder
- content
- 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.)
- Pending
Links
Landscapes
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、吸水性樹脂の製造方法
に関するものであり、更に詳しくは、吸水諸特性に悪影
響を及ぼすことなく吸水性樹脂中に残存するモノマー含
有量を著しく低減するための製造方法に関するものであ
る。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a water-absorbent resin, and more specifically, to remarkably reduce the content of monomers remaining in the water-absorbent resin without adversely affecting various properties of the water-absorbent resin. The present invention relates to a manufacturing method of.
【0002】[0002]
【従来の技術】近年、生理綿、紙おむつ、あるいはその
他の体液を吸収する衛生材料の一構成材料や農園芸用保
水剤として吸水性樹脂が用いられている。2. Description of the Related Art In recent years, water absorbent resins have been used as a constituent material of sanitary materials that absorb body fluids such as sanitary cotton, disposable diapers, and other water-retaining agents for agriculture and horticulture.
【0003】このよう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、デンプン−アクリロニ
トリルグラフト重合体の加水分解物、デンプン−アクリ
ル酸グラフト重合体の部分中和物、酢酸ビニル−アクリ
ル酸エステル共重合体のケン化物、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ま
たはこれらの架橋体等が知られている。Examples of such water absorbent resins include crosslinked polyacrylic acid partially neutralized products, hydrolyzates of starch-acrylonitrile graft polymers, partially neutralized products of starch-acrylic acid graft polymers, and vinyl acetate. Known are saponified products of acrylic acid ester copolymers, hydrolyzed products of acrylonitrile copolymers or acrylamide copolymers, and crosslinked products thereof.
【0004】しかしながら、これらの吸水性樹脂中に
は、通常、未重合の残存モノマーが存在し、特にこの吸
水性樹脂が衛生材料、食品分野等に使用する際には、そ
の含有量をできるだけ低減させることが好ましい。However, in these water-absorbent resins, unpolymerized residual monomers are usually present. Especially when this water-absorbent resin is used in sanitary materials, food fields, etc., its content should be reduced as much as possible. Preferably.
【0005】従来重合体中の残存モノマーを低減させる
試みは、例えば高分子凝集剤等のごとき水溶性重合体等
の分野で古くから行われている。その方法としては、特
開昭56−103,207号に述べられているように、
(1)重合開始剤を増量あるいは分割添加する方法、
(2)溶媒等による抽出法、(3)残存モノマーを別の
誘導体に導く方法、といった3つに大別される。これら
の技術を吸水性樹脂の残存モノマーの低減にも応用する
ことができる。Attempts to reduce residual monomers in polymers have hitherto been made in the field of water-soluble polymers such as polymer flocculants. As the method, as described in JP-A-56-103,207,
(1) A method of increasing or dividingly adding a polymerization initiator,
The method is roughly classified into three methods: (2) extraction method with a solvent or the like, and (3) method of leading the residual monomer to another derivative. These techniques can also be applied to reduce residual monomers in the water absorbent resin.
【0006】(1)の方法を吸水性樹脂に応用した例と
しては、特開昭56−72,005号公報や特開平1−
24,808号公報が報告されているが、吸水性樹脂に
この方法を応用した場合、水溶性重合体の場合と同じく
重合体の分子量の低下、過度の自己架橋反応に伴う吸収
倍率の低下、水可溶性成分量の増加等が認められ、残存
モノマーは低減されるものの吸水性樹脂の特性が低下す
る。Examples of applying the method (1) to a water absorbent resin include JP-A-56-72005 and JP-A-1-
No. 24,808 has been reported, but when this method is applied to a water-absorbent resin, the molecular weight of the polymer is reduced as in the case of a water-soluble polymer, and the absorption capacity is reduced due to excessive self-crosslinking reaction. An increase in the amount of water-soluble components is observed, and the residual monomer is reduced, but the properties of the water-absorbent resin are deteriorated.
【0007】また、(2)の方法としては、特開平1−
292,003号公報が報告されているが、この方法も
残存モノマーの低減には有効であるが、多量の溶媒の使
用とその回収コストが非常に高く、好ましい方法とはい
い難い。As the method (2), Japanese Patent Laid-Open No. 1-
Although Japanese Patent No. 292,003 has been reported, this method is also effective in reducing the residual monomer, but the use of a large amount of solvent and its recovery cost are very high, and it is difficult to say that this is a preferable method.
【0008】(3)の残存モノマーを別の誘導体へ導く
方法としては、水溶性重合体の場合に於てアミンまたは
アンモニア等を加える方法(特公昭33−2,646号
公報)、亜硫酸水素塩、亜硫酸塩、ピロ亜硫酸塩等を加
える方法(特開昭56−103,207号公報)等が開
示されており、これらをそのまま吸水性樹脂に応用した
例も報告されている(特開平1−62,317号公報お
よび西独特許公開3724709号公報)。しかしなが
ら、本発明者らが行った結果によれば、特開平1−6
2,317号公報に記載された方法では、残存モノマー
の低減レベルは未だ高く、また西独特許公開37247
09号公報の方法においても同様で、これは残存モノマ
ーと反応し得る物質を添加混合し、含水率20〜90%
に調製した後高い温度で乾燥することを特徴とする方法
であるが、この方法においても残存モノマー量は数十p
pmレベルでまだ充分に低減されているとはいいがたか
った。As a method for converting the residual monomer of (3) into another derivative, in the case of a water-soluble polymer, a method of adding amine or ammonia etc. (Japanese Patent Publication No. 33-2646) and bisulfite salt. , A method of adding sulfite, pyrosulfite, etc. (JP-A-56-103,207) and the like, and an example in which they are directly applied to a water-absorbent resin has been reported (JP-A-1- 62,317 and West German Patent Publication 3724709). However, according to the results obtained by the present inventors, JP-A-1-6
In the method described in Japanese Patent No. 2,317, the reduction level of the residual monomer is still high, and the German Patent Publication 37247.
The same is true for the method of JP-A-09-09, in which a substance capable of reacting with the residual monomer is added and mixed to obtain a water content of 20 to 90%.
The method is characterized in that it is dried at a high temperature after it is prepared as described above.
It was hard to say that it was still sufficiently reduced at the pm level.
【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る。The present invention has been made in view of the above situation.
【0010】従って、本発明の目的は、吸水性樹脂の新
規な製造方法を提供することにある。本発明の他の目的
は吸水特性に悪影響を及ぼすことなく、吸水性樹脂中の
残存モノマー含有量を著しく低減するための製造方法を
提供することにある。Accordingly, it is an object of the present invention to provide a new method for producing a water absorbent resin. Another object of the present invention is to provide a production method for significantly reducing the residual monomer content in the water absorbent resin without adversely affecting the water absorption characteristics.
【0011】[0011]
【課題を解決するための手段及び作用】本発明者らは、
上記の目的を達成すべく鋭意検討を行った結果、これら
の諸目的は、(a)吸水性樹脂粉末に、吸水性樹脂粉末
中の残存モノマーと反応し得る物質を添加し含水率25
〜55重量%の吸水性樹脂組成物とする工程 (b)該吸水性樹脂組成物の含水率を上記含水率範囲を
維持しながら120〜200℃の温度で10分間以上加
熱し吸水性樹脂処理物を得る工程 (c)該吸水性樹脂処理物を120℃未満の温度で乾燥
する工程 からなることを特徴とする吸水性樹脂の製造方法により
達成される。Means and Actions for Solving the Problems The present inventors have
As a result of earnestly studying to achieve the above-mentioned object, these various objectives were found to include (a) a water-absorbent resin powder to which a substance capable of reacting with a residual monomer in the water-absorbent resin powder was added.
To 55% by weight of water-absorbent resin composition (b) Water-absorbent resin treatment by heating the water-absorbent resin composition at a temperature of 120 to 200 ° C. for 10 minutes or more while maintaining the water content range of the water-absorbent resin composition. And (c) a step of drying the treated water-absorbent resin at a temperature of less than 120 ° C.
【0012】以下、本発明をさらに詳しく説明する。The present invention will be described in more detail below.
【0013】本発明に使用される吸水性樹脂粉末とは、
水中に於て多量の水を吸収して膨潤し含水ゲル状物(ヒ
ドロゲル)を形成するものであり、前述した従来公知の
ものを挙げることができるが、残存モノマー低減の必要
性及び効果を考えると、ポリアクリル酸部分中和物架橋
体の粉末を用いるのが特に好ましい。The water-absorbent resin powder used in the present invention is
It absorbs a large amount of water in water and swells to form a hydrated gel (hydrogel). The conventionally known ones mentioned above can be mentioned, but the necessity and effect of reducing residual monomers are considered. It is particularly preferable to use a powder of a crosslinked polyacrylic acid partially neutralized product.
【0014】吸水性樹脂粉末の形態としては重合・乾燥
後粉砕した粉末状のものが好ましく、更に表面部分及び
その近傍が架橋処理されたものがより好ましい。そし
て、その吸水性樹脂粉末中の残存モノマーは1000p
pm未満、好ましくは500ppm未満、より好ましく
は300ppm未満の吸水性樹脂粉末が好適に使用でき
る。As the form of the water-absorbent resin powder, a powdery form obtained by polymerization, drying and pulverization is preferable, and a form in which the surface portion and its vicinity are cross-linked is more preferable. And the residual monomer in the water absorbent resin powder is 1000 p
A water-absorbent resin powder of less than pm, preferably less than 500 ppm, more preferably less than 300 ppm can be suitably used.
【0015】本発明では、先ず(a)の工程で所定の配
合による吸水性樹脂組成物とするが、その際に用いる吸
水性樹脂中の残存モノマーと反応し得る物質とは、該モ
ノマーと化合して異なる化合物に転換し得るものであ
り、例えばアンモニア、アンモニウム塩、ヒドロキシル
アミン、アミノ酸等の窒素含有化合物;亜硫酸(塩)、
亜硫酸水素塩、亜燐酸(塩)、次亜燐酸(塩)、チオ硫
酸(塩)等の還元性物質を挙げることができる。この中
で、残存モノマー低減率から考えると亜硫酸(塩)、亜
硫酸水素塩、ピロ亜硫酸(塩)、チオ硫酸(塩)等の還
元性物質が好ましい。In the present invention, a water-absorbent resin composition having a predetermined composition is first prepared in the step (a). The substance capable of reacting with the residual monomer in the water-absorbent resin used at that time is combined with the monomer. Nitrogen-containing compounds such as ammonia, ammonium salts, hydroxylamine and amino acids; sulfurous acid (salt),
Examples thereof include reducing substances such as hydrogen sulfite, phosphorous acid (salt), hypophosphorous acid (salt), and thiosulfuric acid (salt). Among these, reducing substances such as sulfurous acid (salt), hydrogen sulfite, pyrosulfurous acid (salt), and thiosulfuric acid (salt) are preferable in view of the residual monomer reduction rate.
【0016】この(a)の工程に於いて吸水性樹脂の含
水率は25〜55重量%の範囲でなければならないが、
この含水率への調整は任意の時期であってよく、例えば
吸水性樹脂に吸水性樹脂中の残存モノマーと反応し得る
物質を添加する前若しくは後又は添加中とすることがで
きる。吸水性樹脂を製造するに際しては、水溶性モノマ
−の水溶液重合か又は逆相懸濁重合によるのが多く、こ
れらはいずれも水の存在下に行うのが一般的である。こ
のような重合方法により得られた吸水性樹脂が含水率2
5〜55重量%の範囲にある時は、これをそのまま
(a)の工程に用いてもよい。その際、重合反応が終了
する直前に吸水性樹脂中の残存モノマ−と反応し得る物
質を添加した場合は、(a)の工程が重合反応の中に含
まれていると考えて差し支えなく、こうして得られた吸
水性樹脂組成物は引き続き(b)の工程を行えばよい。
この範囲を外れた条件で水溶性モノマ−を重合し、その
後この範囲に調整するために水を加えたり、あるいは乾
燥を行ってもよいことはもちろんである。また、吸水性
樹脂が乾燥した粉末の場合は含水率25〜55重量%の
範囲とするため水を加える必要がある。この場合残存モ
ノマーと反応し得る物質を水に溶かした水性液を加えて
もよく、残存モノマーと反応し得る物質を加えた後に水
を加えても、水を加えた後に残存モノマーと反応し得る
物質を加えてもよい。In the step (a), the water content of the water absorbent resin must be in the range of 25 to 55% by weight.
The water content may be adjusted at any time, for example, before or after the addition of a substance capable of reacting with the residual monomer in the water-absorbent resin to the water-absorbent resin, or during addition. When producing a water-absorbent resin, it is often carried out by aqueous solution polymerization of a water-soluble monomer or reverse phase suspension polymerization, and these are generally carried out in the presence of water. The water-absorbent resin obtained by such a polymerization method has a water content of 2
When it is in the range of 5 to 55% by weight, it may be used as it is in the step (a). At that time, when a substance capable of reacting with the residual monomer in the water absorbent resin is added immediately before the completion of the polymerization reaction, it may be considered that the step (a) is included in the polymerization reaction, The water absorbent resin composition thus obtained may be subjected to the step (b) subsequently.
It goes without saying that the water-soluble monomer may be polymerized under conditions outside this range, and then water may be added or drying may be carried out in order to adjust to this range. Further, when the water absorbent resin is a dry powder, it is necessary to add water in order to adjust the water content to the range of 25 to 55% by weight. In this case, an aqueous liquid obtained by dissolving a substance capable of reacting with the residual monomer in water may be added, or water may be added after adding the substance capable of reacting with the residual monomer, or the substance may react with the residual monomer after adding water. Substances may be added.
【0017】この含水率が25重量%未満であると残存
モノマーの低減率が低く、一方含水率が55重量%以上
であっても残存モノマーの低減率は低く、更に水量が多
いことにより乾燥に要するエネルギーが大きくなり経済
的に不利である。好ましくは、35〜45重量%であ
る。If the water content is less than 25% by weight, the reduction rate of the residual monomer is low. On the other hand, if the water content is 55% by weight or more, the reduction rate of the residual monomer is low. It requires a large amount of energy and is economically disadvantageous. Preferably, it is 35 to 45% by weight.
【0018】こうして(a)の工程で得られた含水率2
5〜55重量%の吸水性樹脂組成物は、(b)の工程で
含水率をこの範囲に保ちながら120〜200℃の温度
で10分間以上加熱して吸水性樹脂処理物とするが、本
発明では含水率をこの25〜55重量%の範囲に保ちな
がら加熱することが非常に重要で、その結果残存モノマ
ーは著しく低減する。この時の条件として、温度は12
0℃〜200℃好ましくは140℃〜160℃の高温
に、10分間以上、好ましくは30分間以上、より好ま
しくは1時間以上保つのが好適である。尚、加熱時間の
上限は特に限定されないが、通常10時間以下である。
10時間を越えて加熱処理しても効果の向上は特に認め
られず、むしろ吸水性樹脂の劣化を招く場合が有る。好
ましくは5時間以下、より好ましくは3時間以下であ
る。この吸水性樹脂処理物は次に(c)の工程により1
20℃未満の温度で乾燥する。従来の方法によると、乾
燥を高温で行うのが一般的であるが、乾燥を高温で行う
と、一度低減した残存モノマー量が、再び増加するので
好ましくなく、本発明において乾燥は120℃未満とし
なければならない。効果をより高めるために、50〜1
00℃とするのが好ましく、60〜80℃とするのがよ
り好ましい。The water content of 2 thus obtained in step (a)
The water absorbent resin composition of 5 to 55% by weight is heated at a temperature of 120 to 200 ° C. for 10 minutes or more in the step (b) while keeping the water content in this range to give a water absorbent resin treated product. In the invention, it is very important to heat while keeping the water content in the range of 25 to 55% by weight, and as a result, the residual monomer is significantly reduced. At this time, the temperature is 12
It is suitable to keep at a high temperature of 0 ° C. to 200 ° C., preferably 140 ° C. to 160 ° C. for 10 minutes or longer, preferably 30 minutes or longer, more preferably 1 hour or longer. The upper limit of the heating time is not particularly limited, but is usually 10 hours or less.
Even if the heat treatment is performed for more than 10 hours, no particular improvement in the effect is recognized, and rather the water absorbent resin may be deteriorated. It is preferably 5 hours or less, more preferably 3 hours or less. This treated water-absorbent resin is then subjected to 1 by the step (c).
Dry at temperatures below 20 ° C. According to the conventional method, the drying is generally performed at a high temperature, but when the drying is performed at a high temperature, the residual monomer amount once reduced is increased again, which is not preferable. There must be. 50 to 1 to enhance the effect
The temperature is preferably 00 ° C, more preferably 60 to 80 ° C.
【0019】上記条件の範囲であれば、(b)の工程に
用いる加熱手段は特に制限されず、典型的な加熱方法と
して、密閉状態で加熱する方法や、開放系で伝導加熱す
る方法や、蒸気を噴霧して加熱する方法が例示される。
密閉状態で加熱する為に使用できる装置は、例えば、オ
ートクレーブ、(耐圧の)溝型撹拌加熱器、(耐圧の)
回転加熱器、(耐圧の)円盤加熱器、(耐圧の)流動層
加熱器、(耐圧の)気流加熱器、(耐圧の)赤外線加熱
器、(耐圧の)熱風加熱器、(耐圧の)マイクロ波加熱
器等が挙げられる。The heating means used in the step (b) is not particularly limited as long as it is within the range of the above conditions, and typical heating methods include heating in a closed state, conduction heating in an open system, and The method of spraying and heating steam is illustrated.
Devices that can be used for heating in a closed state are, for example, autoclaves, (pressure resistant) groove type stirring heaters, (pressure resistant).
Rotary heater, (pressure resistant) disk heater, (pressure resistant) fluidized bed heater, (pressure resistant) air flow heater, (pressure resistant) infrared heater, (pressure resistant) hot air heater, (pressure resistant) micro A wave heater and the like can be mentioned.
【0020】(c)の工程の乾燥に用いる装置は従来か
ら公知のものが使用できるが、(b)の工程で用いた加
熱装置も運転条件によって乾燥手段に用いられる場合
は、(a)の工程に用いる加熱装置と(c)の工程に用
いる乾燥装置とは同一のものであってよい。そして、
(a)の工程(b)の工程共に連続で行っても、バッチ
で行ってもよい。As the apparatus used for drying in the step (c), a conventionally known apparatus can be used, but when the heating apparatus used in the step (b) is also used for the drying means depending on operating conditions, The heating device used in the step and the drying device used in the step (c) may be the same. And
Both the step (a) and the step (b) may be carried out continuously or batchwise.
【0021】本発明では、(b)の吸水性樹脂組成物を
加熱する工程では、できるだけ高温で処理することと、
(c)の吸水性樹脂処理物を乾燥する工程では、できる
だけ低温で行うことが非常に重要である。In the present invention, in the step (b) of heating the water-absorbent resin composition, the treatment is performed at a temperature as high as possible.
In the step of drying the water-absorbent resin-treated product of (c), it is very important to perform it at a temperature as low as possible.
【0022】本発明に於ては、本発明の目的と効果をよ
り高いレベルで達成する目的で添加剤を添加しても良
い。In the present invention, additives may be added for the purpose of achieving the object and effect of the present invention at a higher level.
【0023】このような添加剤としては、無機質および
/または有機質の水不溶性微粒子状粉体、界面活性剤及
び有機溶剤等の分散媒を挙げることができる。Examples of such additives include inorganic and / or organic water-insoluble fine particle powders, surfactants and dispersion media such as organic solvents.
【0024】水不溶性微粒子状粉体としては、例えば二
酸化珪素、二酸化チタン、酸化アルミニウム、酸化マグ
ネシウム、酸化亜鉛、タルク、燐酸カルシウム、燐酸バ
リウム、粘土、珪藻土、ゼオライト、ベントナイト、カ
オリン、ハイドロタルサイト、活性白土等の無機質の水
不溶性微粒子状粉体、セルロース粉末、パルプ粉末、エ
チルセルロース、エチルヒドロキシエチルセルロース、
セルロースアセテートブチレート、変性デンプン、キチ
ン、レーヨン、ポリエステル、ポリエチレン、ポリプロ
ピレン、ポリ塩化ビニル、ポリスチレン、ナイロン、ポ
リメチルメタクリレート、メラミン樹脂、メラミンーベ
ンゾグアナミン樹脂、活性炭、茶の葉等の有機質の水不
溶性微粒子状粉体等が例示でき、これらのうち1種又は
2種以上を使用することができる。Examples of the water-insoluble particulate powder include silicon dioxide, titanium dioxide, aluminum oxide, magnesium oxide, zinc oxide, talc, calcium phosphate, barium phosphate, clay, diatomaceous earth, zeolite, bentonite, kaolin, hydrotalcite, Inorganic water-insoluble fine particle powder such as activated clay, cellulose powder, pulp powder, ethyl cellulose, ethyl hydroxyethyl cellulose,
Cellulose acetate butyrate, modified starch, chitin, rayon, polyester, polyethylene, polypropylene, polyvinyl chloride, polystyrene, nylon, polymethylmethacrylate, melamine resin, melamine-benzoguanamine resin, activated carbon, organic leaves such as tea leaves The powdery particles and the like can be exemplified, and of these, one kind or two or more kinds can be used.
【0025】これらの水不溶性微粒子状粉体の粒子径は
1000μm以下、更に好ましくは50μm以下、最も
好ましくは10μm以下である。またこれら水不溶性微
粒子状粉体の中でも無機質の水不溶性微粒子状粉体がよ
り好ましく、その中でも二酸化珪素、二酸化チタン、酸
化アルミニウム、ゼオライト、カオリン、ハイドロタル
サイトが好ましい。また、セピオライト等消臭機能をも
つ無機物粉体等も、特に好適に本発明に使用できる。さ
らに、有機質の水不溶性微粒子状粉体の中ではパルプ、
セルロース粉末、5μm以下の粒子径を有するメチルメ
タクリレート重合体、例えばポリメチルメタクリレート
粉末、活性炭等が好ましい。これらのもので一部分が疎
水化処理されているものも好適に本発明に使用できる。The particle diameter of these water-insoluble particulate powders is 1000 μm or less, more preferably 50 μm or less, and most preferably 10 μm or less. Among these water-insoluble fine particle powders, inorganic water-insoluble fine particle powders are more preferable, and among them, silicon dioxide, titanium dioxide, aluminum oxide, zeolite, kaolin and hydrotalcite are preferable. Further, inorganic powder having a deodorizing function such as sepiolite can be particularly preferably used in the present invention. Furthermore, among the organic water-insoluble particulate powder, pulp,
Cellulose powder, methylmethacrylate polymer having a particle size of 5 μm or less, such as polymethylmethacrylate powder and activated carbon are preferable. Among these, those partially hydrophobized can also be preferably used in the present invention.
【0026】また界面活性剤としてはアニオン性界面活
性剤、ノニオン性界面活性剤、カチオン性界面活性剤、
両性界面活性剤、高分子界面活性剤等を例示することが
でき、これらのうち1種または2種以上を用いることが
できる。As the surface active agent, an anionic surface active agent, a nonionic surface active agent, a cationic surface active agent,
Examples thereof include amphoteric surfactants and polymer surfactants, and of these, one kind or two or more kinds can be used.
【0027】アニオン性界面活性剤としては、例えば高
級アルコール硫酸エステル塩、アルキルナフタレンスル
ホン酸塩、アルキルポリオキシエチレンサルフェート
塩、ジアルキルスルホコハク酸塩等が、ノニオン性界面
活性剤としては、例えばソルビタン脂肪酸エステル、ポ
リオキシエチレンソルビタン脂肪酸エステル(ポリ)グ
リセリン脂肪酸エステル、ポリオキシエチレンアルキル
エーテル、ポリオキシエチレンアルキルフェノールエー
テル、ポリオキシエチレンアシルエステル、ショ糖脂肪
酸エステル等が、カチオン性界面活性剤としては、例え
ばアルキル第4級アンモニウム塩、アルキルアミン塩類
が、両性界面活性剤としては、例えばアルキルベタイ
ン、レシチン等が、高分子界面活性剤としては、例えば
親油性のカルボキシル基を有するポリマーやエチレンオ
キサイド−プロピレンイオキサイドブロックポリマー等
がそれぞれ使用できる。Examples of the anionic surfactant include higher alcohol sulfate ester salt, alkylnaphthalene sulfonate, alkylpolyoxyethylene sulfate salt, dialkylsulfosuccinate, and the like, and nonionic surfactants include sorbitan fatty acid ester. Polyoxyethylene sorbitan fatty acid ester (poly) glycerin fatty acid ester, polyoxyethylene alkyl ether, polyoxyethylene alkylphenol ether, polyoxyethylene acyl ester, sucrose fatty acid ester, etc. Quaternary ammonium salts, alkylamine salts, amphoteric surfactants such as alkyl betaine and lecithin, and polymer surfactants such as lipophilic carboxyl groups. Polymers and ethylene oxide having - propylene Lee oxide block polymers, etc. can be used respectively.
【0028】これらの界面活性剤の中でも、最終製品の
吸収性を損なわず、しかも残存モノマー量の低減効果に
も優れたものとしては、水溶性および/または水分散性
の界面活性剤が好ましく、中でもアニオン性界面活性剤
もしくはHLB7以上好ましくはHLB10以上のノニ
オン性界面活性剤が好適に使用できる。Of these surfactants, water-soluble and / or water-dispersible surfactants are preferred as those which do not impair the absorbability of the final product and are excellent in the effect of reducing the amount of residual monomers. Among them, anionic surfactants or nonionic surfactants having HLB of 7 or more, preferably HLB of 10 or more can be preferably used.
【0029】有機溶剤としては、例えばメタノール、エ
タノール、イソプロパノール、ブタノール、エチレング
リコールモノメチルエーテル、エチレングリコールモノ
エチルエーテル、プロピレングリコールモノメチルエー
テル、テトラヒドロフラン、ジメチルホルムアミド、ジ
メチルスルホキシド、アセトン、メチルエチルケトン等
の親水性有機溶剤、n−ペンタン、n−ヘプタン、n−
オクタン、シクロヘキサン、シクロオクタン、メチルシ
クロヘキサン、デカリン、ベンゼン、エチルベンゼン、
トルエン、キシレン等の疎水性有機溶剤を例示すること
ができるが、好ましくは親水性有機溶剤である。Examples of the organic solvent include hydrophilic organic solvents such as methanol, ethanol, isopropanol, butanol, ethylene glycol monomethyl ether, ethylene glycol monoethyl ether, propylene glycol monomethyl ether, tetrahydrofuran, dimethylformamide, dimethyl sulfoxide, acetone and methyl ethyl ketone. , N-pentane, n-heptane, n-
Octane, cyclohexane, cyclooctane, methylcyclohexane, decalin, benzene, ethylbenzene,
Hydrophobic organic solvents such as toluene and xylene can be exemplified, but hydrophilic organic solvents are preferable.
【0030】本発明を実施するに際しては、特に吸水性
樹脂粉末の形態として、乾燥粉砕後の粉末状物または表
面部分及びその近傍が架橋処理されたものを用いる場
合、これら水不溶性微粒子状粉体、界面活性剤、有機溶
剤を用いた方がより残存モノマーが低減できることがあ
る。一般にこれらの使用量は処理される吸水性樹脂10
0重量部に対して、水不溶性微粒子状粉体では0.01
〜5重量部、界面活性剤では0.01〜5重量部、有機
溶剤では0.01〜8重量部用いるのが好ましい。In carrying out the present invention, when a water-absorbent resin powder is used in the form of a powdery material after dry pulverization or one in which the surface portion and the vicinity thereof are cross-linked, these water-insoluble particulate powders are used. In some cases, the use of a surfactant or an organic solvent may reduce the residual monomer. Generally, the amount of these used is the water absorbent resin 10 to be treated.
0.01 parts by weight of water-insoluble particulate powder to 0 parts by weight
˜5 parts by weight, 0.01 to 5 parts by weight for the surfactant, and 0.01 to 8 parts by weight for the organic solvent are preferably used.
【0031】更に同様に、本発明により得られた吸水性
樹脂に消臭剤、香料、薬剤、植物生育助剤、殺菌剤、発
泡剤、顔料、染料、親水性短繊維、肥料等を介在させる
ことにより、得られる吸水性樹脂に新たな機能を付与す
ることもできる。Further, similarly, a deodorant, a fragrance, a drug, a plant growth aid, a bactericide, a foaming agent, a pigment, a dye, a hydrophilic short fiber, a fertilizer and the like are interposed in the water absorbent resin obtained by the present invention. As a result, a new function can be imparted to the resulting water absorbent resin.
【0032】[0032]
【実施例】以下、実施例によって本発明をさらに説明す
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、下記実施例において「部」は特にこ
とわらない限り重量による。The present invention will be further described below with reference to examples, but the scope of the present invention is not limited to these examples. In the following examples, "parts" are by weight unless otherwise specified.
【0033】また、残存モノマー量及び含水率は以下の
ようにして求めた。The residual monomer amount and water content were determined as follows.
【0034】(1)残存モノマー 200mlのビーカーに脱イオン水100mlを加え、
そこに吸水性樹脂1.0gを撹拌下加えて脱イオン水を
全量ゲル化させた。1時間後、リン酸水溶液を5ml添
加することによりゲルを収縮させ、撹拌後、吸水性樹脂
分散液を濾紙を用いて濾過し、濾過液を高速液体クロマ
トグラフィーで分析した。(1) Residual monomer 100 ml of deionized water was added to a beaker of 200 ml,
1.0 g of a water-absorbent resin was added thereto with stirring to make the deionized water entirely gel. After 1 hour, the gel was contracted by adding 5 ml of a phosphoric acid aqueous solution, and after stirring, the water-absorbent resin dispersion was filtered using a filter paper, and the filtrate was analyzed by high performance liquid chromatography.
【0035】一方、既知の濃度を示すモノマー標準液を
同様に分析して得た検量線を外部標準となし、濾過液の
希釈倍率を考慮して、吸水性樹脂中の残存モノマー量を
求めた。(残存モノマー量はすべて対固形分換算値であ
る。) (2)含水率 吸水性樹脂組成物中の含水率は180℃の乾燥器中3時
間放置後の乾燥減量でもって含水率とした。On the other hand, a calibration curve obtained by similarly analyzing a monomer standard solution having a known concentration was used as an external standard, and the amount of residual monomer in the water absorbent resin was determined in consideration of the dilution ratio of the filtrate. . (Amount of residual monomer is all converted to solid content.) (2) Water content The water content of the water absorbent resin composition was defined as the water content by the loss on drying after standing for 3 hours in a dryer at 180 ° C.
【0036】[0036]
【参考例】 アクリル酸ナトリウム141部、アクリル
酸36.1部及びN,N’’−メチレンビスアクリルア
ミド0.093部を脱イオン水329部に溶解し、これ
に窒素ガスを吹き込んで溶存酸素を追い出した。このモ
ノマーの水溶液を30℃に保った。次いで過硫酸ナトリ
ウム0.6部およびl−アスコルビン酸0.01部を加
えて静置重合し、ゲル状の含水重合体を得た。[Reference Example] 141 parts of sodium acrylate, 36.1 parts of acrylic acid and 0.093 part of N, N ″ -methylenebisacrylamide were dissolved in 329 parts of deionized water, and nitrogen gas was blown into the solution to dissolve dissolved oxygen. I kicked it out. An aqueous solution of this monomer was kept at 30 ° C. Then, 0.6 part of sodium persulfate and 0.01 part of 1-ascorbic acid were added and the mixture was allowed to stand to polymerize to obtain a gel-like hydropolymer.
【0037】これを150℃で熱風乾燥を行った後、ハ
ンマー型粉砕機にて粉砕し、20メッシュ金網で篩分け
して20メッシュ通過物の吸水性樹脂粉末(a)を得
た。吸水性樹脂中の残存モノマーは223ppmであっ
た。This was dried with hot air at 150 ° C., then pulverized with a hammer type pulverizer and sieved with a 20-mesh wire net to obtain a water-absorbent resin powder (a) which passed through 20 mesh. The residual monomer content in the water absorbent resin was 223 ppm.
【0038】さらに、この吸水性樹脂粉末(a)100
重量部にグリセリン1重量部、水4重量部およびエタノ
ール4重量部からなる水性液を混合し、180℃で30
分間加熱処理することにより表面部分および近傍が架橋
処理された吸水性樹脂粉末(b)を得た。Further, the water absorbent resin powder (a) 100
An aqueous liquid consisting of 1 part by weight of glycerin, 4 parts by weight of water and 4 parts by weight of ethanol was mixed with 1 part by weight, and the mixture was mixed at 180 ° C. for 30 days.
By heat treatment for minutes, a water absorbent resin powder (b) having a surface portion and the vicinity thereof cross-linked was obtained.
【0039】吸水性樹脂粉末(b)中の残存モノマーは
230ppmであった。The residual monomer content in the water absorbent resin powder (b) was 230 ppm.
【0040】[0040]
【実施例1】 参考例で得た吸水性樹脂粉末(b)10
0部に、二酸化ケイ素(日本アエロジル(株)製、アエ
ロジル200)1.0部を混合した。還元性物質として
亜硫酸水素ナトリウム1部を水60部イソプロパノール
8部に溶解し、還元性物質の水性液を調整した。この水
性液を上記吸水性樹脂粉末(b)と二酸化ケイ素の混合
物に高速パドル型混合機を用いて添加混合した。なお、
この時の吸水性樹脂組成物の含水率は37.5重量%で
あった。Example 1 Water-absorbent resin powder (b) 10 obtained in Reference Example
1.0 part of silicon dioxide (manufactured by Nippon Aerosil Co., Ltd., Aerosil 200) was mixed with 0 part. As a reducing substance, 1 part of sodium hydrogen sulfite was dissolved in 60 parts of water and 8 parts of isopropanol to prepare an aqueous solution of the reducing substance. This aqueous liquid was added to and mixed with the mixture of the water absorbent resin powder (b) and silicon dioxide using a high speed paddle type mixer. In addition,
At this time, the water content of the water absorbent resin composition was 37.5% by weight.
【0041】次にこの吸水性樹脂組成物を内径10c
m、長さ10cmの円筒容器に入れ密閉状態にした後1
50℃の加熱炉の中、1時間加熱処理を行った。加熱処
理後の吸水性樹脂組成物(吸水性樹脂処理物)の含水率
は28.9重量%、残存モノマー0.89ppmであっ
た。その後、容器から吸水性樹脂組成物を取り出し、8
0℃で3時間熱風乾燥し、20メッシュ金網で篩分けし
て20メッシュ通過物の吸水性樹脂を得た。この吸水性
樹脂の残存モノマーは0.92ppmであった。Next, this water absorbent resin composition was treated with an inner diameter of 10c.
After putting it in a cylindrical container of m and a length of 10 cm and sealing it, 1
Heat treatment was performed for 1 hour in a heating furnace at 50 ° C. The water content of the water absorbent resin composition after heat treatment (water absorbent resin treated product) was 28.9% by weight, and the residual monomer was 0.89 ppm. Then, the water-absorbent resin composition was taken out from the container and
It was dried with hot air at 0 ° C. for 3 hours and sieved with a 20-mesh wire net to obtain a water-absorbent resin that passed through 20-mesh. The residual monomer of this water absorbent resin was 0.92 ppm.
【0042】[0042]
【実施例2】 参考例で得た吸水性樹脂粉末(b)10
0部に、界面活性剤であるジアルキルスルホコハク酸ナ
トリウム(花王(株)製、ペレックスOT−P)0.7
部を混合した。還元性物質として亜硫酸水素ナトリウム
1部を水33部に溶解し、上記吸水性樹脂粉末(b)と
界面活性剤の混合物に高速パドル型混合機を用いて添加
混合した。なお、この時の吸水性樹脂組成物の含水率は
25.0重量%であった。Example 2 Water-absorbent resin powder (b) 10 obtained in Reference Example
In 0 part, 0.7% of sodium dialkylsulfosuccinate (Perox OT-P manufactured by Kao Corporation) which is a surfactant is added.
The parts were mixed. As a reducing substance, 1 part of sodium hydrogen sulfite was dissolved in 33 parts of water, and the mixture of the water-absorbent resin powder (b) and the surfactant was added and mixed using a high speed paddle type mixer. The water content of the water absorbent resin composition at this time was 25.0% by weight.
【0043】次にこの吸水性樹脂組成物を内径10c
m、長さ10cmの円筒容器に入れ密閉状態にした後1
40℃の加熱炉の中、10時間加熱処理を行った。加熱
処理後の吸水性樹脂組成物(吸水性樹脂処理物)の含水
率は24.8重量%、残存モノマー0.83ppmであ
った。その後、容器から吸水性樹脂組成物を取り出し、
流動層乾燥機を用いて60℃の温度で5時間加熱し、2
0メッシュ金網で篩分けして20メッシュ通過物の吸水
性樹脂を得た。この吸水性樹脂の残存モノマーは0.8
4ppmであった。Next, this water-absorbent resin composition was treated with an inner diameter of 10c.
After putting it in a cylindrical container of m and a length of 10 cm and sealing it, 1
Heat treatment was performed in a heating furnace at 40 ° C. for 10 hours. The water content of the water absorbent resin composition after heat treatment (water absorbent resin treated product) was 24.8% by weight, and the residual monomer was 0.83 ppm. Then, take out the water-absorbent resin composition from the container,
Heat in a fluidized bed dryer at a temperature of 60 ° C. for 5 hours, and
It was sieved with a 0-mesh wire mesh to obtain a water-absorbent resin of 20-mesh passing product. The residual monomer of this water absorbent resin is 0.8
It was 4 ppm.
【0044】[0044]
【実施例3】 参考例で得た吸水性樹脂粉末(b)10
0部に、疎水化処理二酸化ケイ素(日本アエロジル
(株)製、アエロジルR972)1.0部を混合した。
還元性物質としてチオ硫酸ナトリウム2部を水67部に
溶解し、還元性物質の水性液を調整した。この水性液を
上記吸水性樹脂粉末(b)と疎水化処理二酸化ケイ素の
混合物に高速パドル型混合機を用いて添加混合した。な
お、この時の吸水性樹脂組成物の含水率は40.2重量
%であった。Example 3 Water-absorbent resin powder (b) 10 obtained in Reference Example
To 0 part, 1.0 part of hydrophobized silicon dioxide (manufactured by Nippon Aerosil Co., Ltd., Aerosil R972) was mixed.
As a reducing substance, 2 parts of sodium thiosulfate was dissolved in 67 parts of water to prepare an aqueous solution of the reducing substance. This aqueous liquid was added to and mixed with a mixture of the water absorbent resin powder (b) and hydrophobized silicon dioxide using a high speed paddle type mixer. The water content of the water absorbent resin composition at this time was 40.2% by weight.
【0045】次にこの吸水性樹脂組成物を内径10c
m、長さ10cmの円筒容器に入れ密閉状態にした後1
60℃の加熱炉の中、30分間加熱処理を行った。加熱
処理後の吸水性樹脂組成物(吸水性樹脂処理物)の含水
率は34.2重量%、残存モノマー0.56ppmであ
った。その後、容器から吸水性樹脂組成物を取り出し、
70℃で5時間熱風乾燥し、20メッシュ金網で篩分け
して20メッシュ通過物の吸水剤を得た。この吸水剤の
残存モノマーは0.56ppmであった。Next, this water-absorbent resin composition was treated with an inner diameter of 10c.
After putting it in a cylindrical container of m and a length of 10 cm and sealing it, 1
Heat treatment was performed for 30 minutes in a heating furnace at 60 ° C. The water content of the water absorbent resin composition after heat treatment (water absorbent resin treated product) was 34.2% by weight, and residual monomer was 0.56 ppm. Then, take out the water-absorbent resin composition from the container,
It was dried with hot air at 70 ° C. for 5 hours and sieved with a 20-mesh wire net to obtain a water-absorbing agent of 20-mesh passing product. The residual monomer content of this water absorbing agent was 0.56 ppm.
【0046】[0046]
【実施例4】 参考例で得た吸水性樹脂粉末(b)10
0部に、酸化アルミニウム(デグサ(株)製、アルミニ
ウムオキサイドC)2.0部を混合した。還元性物質と
して亜硫酸ナトリウム1部を水120部、エタノール2
部に溶解し、還元性物質の水性液を調整した。この水性
液を上記吸水性樹脂粉末(b)と酸化アルミニウムの混
合物に高速パドル型混合機を用いて添加混合した。な
お、この時の吸水性樹脂組成物の含水率は54.7重量
%であった。Example 4 Water-absorbent resin powder (b) 10 obtained in Reference Example
To 0 part, 2.0 parts of aluminum oxide (manufactured by Degussa Co., Ltd., aluminum oxide C) was mixed. As a reducing substance, 1 part of sodium sulfite, 120 parts of water, and 2 parts of ethanol
The solution was dissolved in 1 part to prepare an aqueous liquid of a reducing substance. This aqueous liquid was added to and mixed with the mixture of the water absorbent resin powder (b) and aluminum oxide using a high speed paddle type mixer. The water content of the water absorbent resin composition at this time was 54.7% by weight.
【0047】次にこの吸水性樹脂組成物を内径10c
m、長さ10cmの円筒容器に入れ密閉状態にした後1
80℃の加熱炉の中、10時間加熱処理を行った。加熱
処理後の吸水性樹脂組成物(吸水性樹脂処理物)の含水
率は35.2重量%、残存モノマー0.71ppmであ
った。その後、容器から吸水性樹脂組成物を取り出し、
流動床乾燥機を用いて80℃の温度で3時間加熱し、2
0メッシュ金網で篩分けして20メッシュ通過物の吸水
性樹脂を得た。この吸水性樹脂の残存モノマーは0.7
5ppmであった。Next, this water absorbent resin composition was treated with an inner diameter of 10c.
After putting it in a cylindrical container of m and a length of 10 cm and sealing it, 1
Heat treatment was performed in a heating furnace at 80 ° C. for 10 hours. The water content of the water absorbent resin composition after heat treatment (water absorbent resin treated product) was 35.2% by weight, and the residual monomer was 0.71 ppm. Then, take out the water-absorbent resin composition from the container,
Heat using a fluid bed dryer at a temperature of 80 ° C. for 3 hours, and
It was sieved with a 0-mesh wire mesh to obtain a water-absorbent resin of 20-mesh passing product. The residual monomer of this water absorbent resin is 0.7
It was 5 ppm.
【0048】[0048]
【実施例5】 参考例で得た吸水性樹脂粉末(b)10
0部に、活性炭2.0部を混合した。還元性物質として
亜硫酸ナトリウム1部を水54部、イソプロパノール2
部に溶解し、還元性物質の水性液を調整した。この水性
液を上記吸水性樹脂粉末(b)と活性炭の混合物に高速
パドル型混合機を用いて添加混合した。なお、この時の
吸水性樹脂組成物の含水率は35.0重量%であった。Example 5 Water-absorbent resin powder (b) 10 obtained in Reference Example
2.0 parts of activated carbon was mixed with 0 parts. As a reducing substance, 1 part of sodium sulfite, 54 parts of water, and 2 parts of isopropanol
The solution was dissolved in 1 part to prepare an aqueous liquid of a reducing substance. This aqueous liquid was added to and mixed with the mixture of the water-absorbent resin powder (b) and activated carbon using a high speed paddle type mixer. The water content of the water absorbent resin composition at this time was 35.0% by weight.
【0049】次にこの吸水性樹脂組成物を蒸気を吹き込
める形式の加熱炉にいれ120℃の蒸気を吹き込みなが
ら5時間加熱処理を行った。加熱処理後の吸水性樹脂組
成物(吸水性樹脂処理物)の含水率は40.2重量%、
残存モノマー0.53ppmであった。その後、容器か
ら吸水性樹脂組成物を取り出し、50℃で10時間熱風
乾燥し、20メッシュ金網で篩分けして20メッシュ通
過物の吸水性樹脂を得た。この吸水性樹脂の残存モノマ
ーは0.53ppmであった。Next, the water-absorbent resin composition was put in a heating furnace of a type capable of blowing steam, and heat-treated for 5 hours while blowing steam at 120 ° C. The water content of the water absorbent resin composition after heat treatment (water absorbent resin treated product) is 40.2% by weight,
The residual monomer was 0.53 ppm. Then, the water-absorbent resin composition was taken out of the container, dried with hot air at 50 ° C. for 10 hours, and sieved with a 20-mesh wire net to obtain a 20-mesh water-absorbent resin. The residual monomer of this water absorbent resin was 0.53 ppm.
【0050】[0050]
【実施例6】 参考例で得た吸水性樹脂粉末(b)10
0部に、ポリメチルメタクリレート微粉末2.0部を混
合した。還元性物質として亜硫酸水素ナトリウム1部を
水60部に溶解し、上記吸水性樹脂粉末(b)とポリメ
チルメタクリレートの混合物に高速パドル型混合機を用
いて添加混合した。なお、この時の吸水性樹脂組成物の
含水率は37.5重量%であった。Example 6 Water-absorbent resin powder (b) 10 obtained in Reference Example
2.0 parts of polymethylmethacrylate fine powder was mixed with 0 parts. As a reducing substance, 1 part of sodium hydrogen sulfite was dissolved in 60 parts of water, and the mixture of the water absorbent resin powder (b) and polymethylmethacrylate was added and mixed using a high speed paddle type mixer. The water content of the water absorbent resin composition at this time was 37.5% by weight.
【0051】次にこの吸水性樹脂組成物を内径10c
m、長さ10cmの円筒容器に入れ密閉状態にした後2
00℃の加熱炉の中、10分間加熱処理を行った。加熱
処理後の吸水性樹脂組成物(吸水性樹脂処理物)の含水
率は35.2重量%、残存モノマー0.27ppmであ
った。その後、容器から吸水性樹脂組成物を取り出し、
流動床乾燥機を用いて120℃の温度で2時間加熱し、
20メッシュ金網で篩分けして20メッシュ通過物の吸
水性樹脂を得た。この吸水性樹脂の残存モノマーは0.
93ppmであった。Next, this water absorbent resin composition was treated with an inner diameter of 10c.
After putting it in a cylindrical container of m and a length of 10 cm and sealing it, 2
Heat treatment was performed for 10 minutes in a heating furnace at 00 ° C. The water content of the water absorbent resin composition (water absorbent resin treated product) after the heat treatment was 35.2% by weight, and the residual monomer was 0.27 ppm. Then, take out the water-absorbent resin composition from the container,
Heat in a fluid bed dryer at a temperature of 120 ° C. for 2 hours,
The mixture was sieved with a 20-mesh wire mesh to obtain a water-absorbent resin having a 20-mesh flow rate. The residual monomer of this water absorbent resin is 0.
It was 93 ppm.
【0052】[0052]
【比較例1】 参考例で得た吸水性樹脂粉末(b)10
0部に亜硫酸水素ナトリウム0.3部を水5部に溶解し
た水性液を高速パドル型混合機を用いて5分間添加混合
した。得られた比較用吸水性樹脂の残存モノマーは2
1.0ppmであった。Comparative Example 1 Water-absorbent resin powder (b) 10 obtained in Reference Example
An aqueous solution prepared by dissolving 0.3 part of sodium hydrogen sulfite in 0 part of 5 parts of water was added and mixed for 5 minutes using a high speed paddle type mixer. The residual monomer of the obtained comparative water absorbent resin was 2
It was 1.0 ppm.
【0053】[0053]
【比較例2】 参考例で得た吸水性樹脂粉末(b)10
0部に、ヒドロキシルアミン塩酸塩1部を水50部に溶
解し、高速パドル型混合機を用いて添加混合した。な
お、この時の吸水性樹脂組成物の含水率は33.3重量
%であった。この吸水性樹脂組成物を取り出し、120
℃で2時間熱風乾燥し、20メッシュ金網で篩分けして
20メッシュ通過物の吸水剤を得た。この比較用吸水性
樹脂の含水率は2.7重量%、残存モノマーは80.3
ppmであった。Comparative Example 2 Water-absorbent resin powder (b) 10 obtained in Reference Example
To 0 part, 1 part of hydroxylamine hydrochloride was dissolved in 50 parts of water, and the mixture was added and mixed using a high speed paddle type mixer. The water content of the water absorbent resin composition at this time was 33.3% by weight. This water-absorbent resin composition was taken out, and 120
It was dried with hot air at 0 ° C. for 2 hours and sieved with a 20-mesh wire net to obtain a 20-mesh-passing water-absorbing agent. The water content of this comparative water absorbent resin was 2.7% by weight, and the residual monomer content was 80.3.
It was ppm.
【0054】[0054]
【比較例3】 参考例で得た吸水性樹脂粉末(b)10
0部に、亜硫酸水素ナトリウム5部を水300部に溶解
し、高速パドル型混合機を用いて添加混合した。なお、
この時の吸水性樹脂組成物の含水率は75.2重量%で
あった。この吸水性樹脂組成物を取り出し、120℃で
2時間熱風乾燥し、20メッシュ金網で篩分けして20
メッシュ通過物の吸水剤を得た。この比較用吸水性樹脂
の含水率は3.3重量%、残存モノマーは33.4pp
mであった。Comparative Example 3 Water-absorbent resin powder (b) 10 obtained in Reference Example
To 0 part, 5 parts of sodium hydrogen sulfite was dissolved in 300 parts of water, and the mixture was added and mixed using a high speed paddle type mixer. In addition,
At this time, the water content of the water absorbent resin composition was 75.2% by weight. The water-absorbent resin composition was taken out, dried with hot air at 120 ° C. for 2 hours, and sieved with a 20-mesh wire net to give 20
A water absorbent of the mesh passing product was obtained. The water content of this comparative water absorbent resin was 3.3% by weight, and the residual monomer was 33.4 pp.
It was m.
【0055】[0055]
【比較例4】 参考例で得た吸水性樹脂粉末(b)10
0部に、疎水化処理二酸化ケイ素(日本アエロジル
(株)製、アエロジルR972)1.0部を混合した。
還元性物質としてチオ硫酸ナトリウム2部を水20部に
溶解し、還元性物質の水性液を調整した。この水性液を
上記吸水性樹脂粉末(b)と疎水化処理二酸化ケイ素の
混合物に高速パドル型混合機を用いて添加混合した。な
お、この時の吸水性樹脂組成物の含水率は16.7重量
%であった。次にこの吸水性樹脂組成物を取り出し、1
10℃で10時間熱風乾燥し、20メッシュ金網で篩分
けして20メッシュ通過物の比較用吸水性樹脂を得た。
この比較用吸水性樹脂の含水率は8.6重量%で、残存
モノマーは62.5ppmあった。Comparative Example 4 Water-absorbent resin powder (b) 10 obtained in Reference Example
To 0 part, 1.0 part of hydrophobized silicon dioxide (manufactured by Nippon Aerosil Co., Ltd., Aerosil R972) was mixed.
As a reducing substance, 2 parts of sodium thiosulfate was dissolved in 20 parts of water to prepare an aqueous solution of the reducing substance. This aqueous liquid was added to and mixed with a mixture of the water absorbent resin powder (b) and hydrophobized silicon dioxide using a high speed paddle type mixer. The water content of the water absorbent resin composition at this time was 16.7% by weight. Next, the water absorbent resin composition is taken out and 1
It was dried with hot air at 10 ° C. for 10 hours and sieved with a 20-mesh wire net to obtain a 20-mesh-passed water absorbent resin for comparison.
The water content of this comparative water absorbent resin was 8.6% by weight, and the residual monomer was 62.5 ppm.
【0056】[0056]
【比較例5】 参考例で得た吸水性樹脂粉末(b)10
0部に、還元性物質としてチオ硫酸ナトリウム1部を水
1900部に溶解し、還元性物質の水性液を調整した。
この水性液を上記吸水性樹脂粉末(b)に双腕型ニーダ
ーを用いて添加混合した。なお、この時の吸水性樹脂組
成物の含水率は95.0重量%であった。Comparative Example 5 Water-absorbent resin powder (b) 10 obtained in Reference Example
To 0 part, 1 part of sodium thiosulfate as a reducing substance was dissolved in 1900 parts of water to prepare an aqueous solution of the reducing substance.
This aqueous liquid was added to and mixed with the water-absorbent resin powder (b) using a double-arm kneader. The water content of the water absorbent resin composition at this time was 95.0% by weight.
【0057】次にこの吸水性樹脂組成物を内径10c
m、長さ10cmの円筒容器に入れ密閉状態にした後1
50℃の加熱炉の中、1時間加熱処理を行った。加熱処
理後の吸水性樹脂組成物(吸水性樹脂処理物)の含水率
は76.2重量%、残存モノマー14.2ppmであっ
た。その後、容器から吸水性樹脂処理物を取り出し、1
50℃で3時間熱風乾燥し、20メッシュ金網で篩分け
して20メッシュ通過物の比較用吸水性樹脂を得た。こ
の比較用吸水性樹脂の残存モノマーは31.6ppmで
あった。Next, this water-absorbent resin composition was treated with an inner diameter of 10c.
After putting it in a cylindrical container of m and a length of 10 cm and sealing it, 1
Heat treatment was performed for 1 hour in a heating furnace at 50 ° C. The water content of the water absorbent resin composition after heat treatment (water absorbent resin treated product) was 76.2% by weight, and the residual monomer was 14.2 ppm. Then, take out the water-absorbent resin treated product from the container, 1
It was dried with hot air at 50 ° C. for 3 hours and sieved with a 20-mesh wire net to obtain a 20-mesh-passed water absorbent resin for comparison. The residual monomer of this comparative water absorbent resin was 31.6 ppm.
【0058】[0058]
【比較例6】 参考例で得た吸水性樹脂粉末(b)10
0部に、酸化アルミニウム(デグサ(株)製、アルミニ
ウムオキサイドC)2.0部を混合した。還元性物質と
して亜硫酸ナトリウム1部を水40部、エタノール2部
に溶解し、還元性物質の水性液を調整した。この水性液
を上記吸水性樹脂粉末(b)と酸化アルミニウムの混合
物に高速パドル型混合機を用いて添加混合した。なお、
この時の吸水性樹脂組成物の含水率は28.6重量%で
あった。Comparative Example 6 Water-absorbent resin powder (b) 10 obtained in Reference Example
To 0 part, 2.0 parts of aluminum oxide (manufactured by Degussa Co., Ltd., aluminum oxide C) was mixed. As a reducing substance, 1 part of sodium sulfite was dissolved in 40 parts of water and 2 parts of ethanol to prepare an aqueous solution of the reducing substance. This aqueous liquid was added to and mixed with the mixture of the water absorbent resin powder (b) and aluminum oxide using a high speed paddle type mixer. In addition,
At this time, the water content of the water absorbent resin composition was 28.6% by weight.
【0059】次にこの吸水性樹脂組成物を内径10c
m、長さ10cmの円筒容器に入れ密閉状態にした後8
0℃の加熱炉の中、30分間加熱処理を行った。加熱処
理後の吸水性樹脂組成物(吸水性樹脂処理物)の含水率
は28.5重量%、残存モノマー21.7ppmであっ
た。その後、容器から吸水性樹脂処理物を取り出し、流
動床乾燥機を用いて80℃の温度で3時間加熱し、20
メッシュ金網で篩分けして20メッシュ通過物の比較用
吸水性樹脂を得た。この比較用吸水性樹脂の残存モノマ
ーは21.8ppmであった。Next, this water-absorbent resin composition was treated with an inner diameter of 10c.
8 m after being put in a cylindrical container of 10 cm in length and sealed
Heat treatment was performed for 30 minutes in a heating furnace at 0 ° C. The water content of the water absorbent resin composition after heat treatment (water absorbent resin treated product) was 28.5% by weight, and the residual monomer was 21.7 ppm. Then, the water absorbent resin treated product was taken out of the container and heated at a temperature of 80 ° C. for 3 hours using a fluidized bed dryer,
It was sieved with a mesh wire mesh to obtain a comparative water-absorbent resin having a 20-mesh flow rate. The residual monomer of this comparative water absorbent resin was 21.8 ppm.
【0060】[0060]
【比較例7】 参考例で得た吸水性樹脂粉末(b)10
0部に、活性炭2.0部を混合した。還元性物質として
モノエタノールアミン1部を水25部、イソプロパノー
ル2部に溶解し、還元性物質の水性液を調整した。この
水性液を上記吸水性樹脂粉末(b)と活性炭の混合物に
高速パドル型混合機を用いて添加混合した。なお、この
時の吸水性樹脂組成物の含水率は20.0重量%であっ
た。Comparative Example 7 Water-absorbent resin powder (b) 10 obtained in Reference Example
2.0 parts of activated carbon was mixed with 0 parts. As a reducing substance, 1 part of monoethanolamine was dissolved in 25 parts of water and 2 parts of isopropanol to prepare an aqueous liquid of the reducing substance. This aqueous liquid was added to and mixed with the mixture of the water-absorbent resin powder (b) and activated carbon using a high speed paddle type mixer. The water content of the water absorbent resin composition at this time was 20.0% by weight.
【0061】次にこの吸水性樹脂組成物を内径10c
m、長さ10cmの円筒容器に入れ密閉状態にした後室
温で、10時間放置した。放置後の吸水性樹脂組成物
(吸水性樹脂処理物)の含水率は19.6重量%、残存
モノマー28.2ppmであった。その後、容器から吸
水性樹脂処理物を取り出し、100℃で3時間熱風乾燥
し、20メッシュ金網で篩分けして20メッシュ通過物
の比較用吸水性樹脂を得た。この比較用吸水性樹脂の残
存モノマーは30.5ppmであった。Next, this water absorbent resin composition was treated with an inner diameter of 10c.
It was placed in a cylindrical container having a length of 10 m and a length of 10 cm, and the container was sealed and left at room temperature for 10 hours. The water content of the water absorbent resin composition (treated water absorbent resin) after standing was 19.6% by weight, and the residual monomer was 28.2 ppm. Then, the treated water-absorbent resin was taken out of the container, dried with hot air at 100 ° C. for 3 hours, and sieved with a 20-mesh wire net to obtain a 20-mesh-passed water absorbent resin for comparison. The residual monomer of this comparative water absorbent resin was 30.5 ppm.
【0062】[0062]
【比較例8】 実施例−1で得られた吸水性樹脂処理物
(含水率28.9重量%)を150℃で3時間乾燥させ
て比較用吸水性樹脂を得た。この比較用吸水性樹脂の残
存モノマーは11.2ppmであった。Comparative Example 8 The treated water absorbent resin (water content 28.9% by weight) obtained in Example-1 was dried at 150 ° C. for 3 hours to obtain a comparative water absorbent resin. The residual monomer of this comparative water absorbent resin was 11.2 ppm.
【0063】[0063]
【比較例9】 実施例−2で得られた吸水性樹脂処理物
(含水率24.8重量%)を180℃で2時間乾燥させ
て比較用吸水性樹脂を得た。この比較用吸水性樹脂の残
存モノマーは19.3ppmであった。Comparative Example 9 The treated water-absorbent resin (water content 24.8% by weight) obtained in Example-2 was dried at 180 ° C. for 2 hours to obtain a comparative water-absorbent resin. The residual monomer of this comparative water absorbent resin was 19.3 ppm.
【0064】[0064]
【発明の効果】以上の実施例及び比較例より明らかなよ
うに、吸水性樹脂粉末中の残存モノマーを低減するに
は、残存モノマーと反応し得る物質を添加する際の水量
とその後の加熱処理工程中の含水率の変化が特定の含水
率範囲内にとどまることと、その時の温度及び時間が非
常に重要であり、添加水量が少なすぎても多すぎても残
存モノマーは効率よく低減しないし、最適の添加水量で
あってもすぐに乾燥させたり、高温で乾燥させると残存
モノマーは効率よく低減しない。As is clear from the above Examples and Comparative Examples, in order to reduce the residual monomer in the water absorbent resin powder, the amount of water when adding a substance capable of reacting with the residual monomer and the subsequent heat treatment. It is very important that the change in water content during the process stays within a specific water content range and the temperature and time at that time are very important.Even if the amount of added water is too small or too large, the residual monomer is not efficiently reduced. However, even if the amount of added water is optimum, the residual monomer is not efficiently reduced if it is immediately dried or dried at high temperature.
【0065】以上のことから残存モノマーを効率よく低
減させるためには、残存モノマーと反応し得る物質を添
加する際の添加水量を適量添加しその含水率を特定範囲
内に維持しながら加熱し、更に、その後できるだけ低温
で乾燥することにより、残存モノマーを非常に効率よく
低減でき、本発明によれば、殆ど残存モノマーの無い吸
水性樹脂が得られることが判り、安全性の高い吸水性樹
脂を安定に効率よく生産することが可能になった。From the above, in order to efficiently reduce the residual monomer, an appropriate amount of water added when adding a substance capable of reacting with the residual monomer is added, and heating is performed while maintaining the water content within a specific range. Further, by drying at a temperature as low as possible after that, it is possible to reduce the residual monomer very efficiently, and according to the present invention, it was found that a water absorbent resin containing almost no residual monomer was obtained, and a highly safe water absorbent resin was obtained. It has become possible to produce stably and efficiently.
【0066】従って、本発明により得られる吸水性樹脂
は、その特徴を生かして使い捨ておむつや生理用ナプキ
ン等の衛生材料の吸収剤、医療用保水剤、農園芸用保水
剤、その他諸工業用脱水剤等の吸水性や保水性を必要と
する用途に好適に利用することができる。Therefore, the water-absorbent resin obtained by the present invention makes use of its characteristics to absorb sanitary materials such as disposable diapers and sanitary napkins, medical water retention agents, agricultural and horticultural water retention agents, and other industrial dehydration agents. It can be suitably used for applications requiring water absorption and water retention of agents and the like.
Claims (8)
程が少なくとも下記(a)、(b)及び(c)の工程、 (a)吸水性樹脂粉末に、吸水性樹脂粉末中の残存モノ
マーと反応し得る物質を添加し含水率25〜55重量%
の吸水性樹脂組成物とする工程 (b)該吸水性樹脂組成物の含水率を上記含水率範囲に
維持しながら120〜200℃の温度で10分間以上加
熱し吸水性樹脂処理物を得る工程 (c)該吸水性樹脂処理物を120℃未満の温度で乾燥
する工程 からなることを特徴とする吸水性樹脂の製造方法。1. A method for producing a water-absorbent resin, comprising at least the following steps (a), (b) and (c), wherein (a) the water-absorbent resin powder has residuals in the water-absorbent resin powder: Water content of 25-55% by weight
(B) a step of heating the water absorbent resin composition at a temperature of 120 to 200 ° C. for 10 minutes or more to obtain a water absorbent resin treated product while maintaining the water content of the water absorbent resin composition in the above water content range. (C) A method for producing a water-absorbent resin, comprising the step of drying the treated water-absorbent resin at a temperature of less than 120 ° C.
中和物架橋体である請求項1記載の製造方法。2. The method according to claim 1, wherein the water absorbent resin powder is a crosslinked polyacrylic acid partially neutralized product.
し得る物質が亜硫酸(塩)、亜硫酸水素(塩)、ピロ亜
硫酸(塩)、チオ硫酸(塩)からなる群から選ばれた少
なくとも一種である請求項1記載の製造方法。3. The substance capable of reacting with the residual monomer in the water absorbent resin powder is at least one selected from the group consisting of sulfite (salt), hydrogen sulfite (salt), pyrosulfite (salt) and thiosulfate (salt). The manufacturing method according to claim 1, wherein
170℃である請求項1記載の製造方法。4. The heating temperature in step (b) is 150 to
The production method according to claim 1, which is 170 ° C.
上である請求項1記載の製造方法。5. The production method according to claim 1, wherein the heating time in step (b) is 1 hour or more.
0℃である請求項1記載の製造方法。6. The drying temperature in step (c) is 60-8.
The production method according to claim 1, which is 0 ° C.
更に、有機質および/または無機質の水不溶性微粒子状
粉体、界面活性剤、有機溶剤よりなる群から選ばれた少
なくとも1種の添加剤を含有する請求項1に記載の製造
方法。7. The water-absorbent resin composition in step (a) further comprises at least one additive selected from the group consisting of organic and / or inorganic water-insoluble particulate powder, a surfactant and an organic solvent. The manufacturing method according to claim 1, further comprising:
量%までなされる請求項1記載の製造方法。8. The production method according to claim 1, wherein in the step (c), the drying is performed up to a water content of 15% by weight.
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP34657892A JPH06192319A (en) | 1992-12-25 | 1992-12-25 | Production of water-absorbing resin |
DE69317636T DE69317636T2 (en) | 1992-12-25 | 1993-12-23 | Absorber and method of making an absorbent resin |
EP93310492A EP0605215B1 (en) | 1992-12-25 | 1993-12-23 | Absorbent and method for production of absorbent resin |
US08/802,284 US5866678A (en) | 1992-12-25 | 1997-02-20 | Absorbent and method for production of absorbent resin |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP34657892A JPH06192319A (en) | 1992-12-25 | 1992-12-25 | Production of water-absorbing resin |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH06192319A true JPH06192319A (en) | 1994-07-12 |
Family
ID=18384374
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP34657892A Pending JPH06192319A (en) | 1992-12-25 | 1992-12-25 | Production of water-absorbing resin |
Country Status (1)
Country | Link |
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JP (1) | JPH06192319A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006299234A (en) * | 2005-02-15 | 2006-11-02 | Nippon Shokubai Co Ltd | Water absorbent resin and method for production thereof |
JP2010504418A (en) * | 2006-09-25 | 2010-02-12 | ビーエーエスエフ ソシエタス・ヨーロピア | Continuous production method of water-absorbing polymer particles |
JP2011528050A (en) * | 2008-07-15 | 2011-11-10 | ビーエーエスエフ ソシエタス・ヨーロピア | Method for producing water-absorbing polymer particles |
-
1992
- 1992-12-25 JP JP34657892A patent/JPH06192319A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006299234A (en) * | 2005-02-15 | 2006-11-02 | Nippon Shokubai Co Ltd | Water absorbent resin and method for production thereof |
JP2010504418A (en) * | 2006-09-25 | 2010-02-12 | ビーエーエスエフ ソシエタス・ヨーロピア | Continuous production method of water-absorbing polymer particles |
JP2011528050A (en) * | 2008-07-15 | 2011-11-10 | ビーエーエスエフ ソシエタス・ヨーロピア | Method for producing water-absorbing polymer particles |
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