JP3522316B2 - Treatment method for water absorbent resin - Google Patents

Treatment method for water absorbent resin

Info

Publication number
JP3522316B2
JP3522316B2 JP32177093A JP32177093A JP3522316B2 JP 3522316 B2 JP3522316 B2 JP 3522316B2 JP 32177093 A JP32177093 A JP 32177093A JP 32177093 A JP32177093 A JP 32177093A JP 3522316 B2 JP3522316 B2 JP 3522316B2
Authority
JP
Japan
Prior art keywords
water
absorbent resin
parts
resin composition
residual monomer
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP32177093A
Other languages
Japanese (ja)
Other versions
JPH06239921A (en
Inventor
勝弘 梶川
欣也 長砂
善彦 増田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nippon Shokubai Co Ltd
Original Assignee
Nippon Shokubai Co Ltd
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Filing date
Publication date
Application filed by Nippon Shokubai Co Ltd filed Critical Nippon Shokubai Co Ltd
Priority to JP32177093A priority Critical patent/JP3522316B2/en
Publication of JPH06239921A publication Critical patent/JPH06239921A/en
Application granted granted Critical
Publication of JP3522316B2 publication Critical patent/JP3522316B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、吸水性樹脂の処理方法
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処理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 treating a water-absorbent resin, and more particularly, to remarkably reduce the content of monomers remaining in the water-absorbent resin without adversely affecting various properties of the water-absorbent resin. Regarding the processing 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
の残存レベルは未だ高く、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
ppmレベルでまだ十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 residual level of residual monomers is still high, and the German Patent Publication 37247
The same is true for the method of Japanese Patent Publication No. 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 being adjusted to 100%, but it was hard to say that even in this method, the residual monomer amount was still sufficiently reduced at a level of several tens of ppm.

【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
規な処理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処理方法を
提供することにある。
Accordingly, it is an object of the present invention to provide a novel method for treating a water absorbent resin. Another object of the present invention is to provide a treatment 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、吸水性樹脂を処理する方法であって、処理
工程が少なくとも下記(a)及び(b)の工程、 (a)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し含水率10〜70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の変化率が20%以
下に保ちながら100〜200℃の温度で10分間以上
加熱する工程 からなることを特徴とする吸水性樹脂の処理方法により
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 objects are a method for treating a water-absorbent resin, and the treatment step is at least the following steps (a) and (b), and (a) water-absorption: Of a water-absorbent resin composition having a water content of 10 to 70% by weight by adding a substance capable of reacting with a residual monomer in the water-absorbent resin to a water-soluble resin (b) Change rate of water content of the water-absorbent resin composition Of 20% or less while heating at a temperature of 100 to 200 ° C. for 10 minutes or more.

【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】本発明における吸水性樹脂とは、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に対
して、本発明の方法は特に有効である。
The water-absorbent resin used in the present invention is a resin that absorbs a large amount of water in water and swells to form a hydrogel, and examples thereof include the conventionally known resins described above. However, considering the necessity and effect of reducing the residual monomer, the method of the present invention is particularly effective for a crosslinked polyacrylic acid partially neutralized product.

【0014】吸水性樹脂の形態としては特に制限はな
く、重合後・乾燥前のゲル状物でも、乾燥・粉砕後の粉
末状物でも更に表面部分及びその近傍が架橋処理された
ものでも何れも使用できる。
The form of the water-absorbent resin is not particularly limited, and any of a gel-like substance after polymerization and before drying, a powdery substance after drying and crushing, and a substance in which the surface portion and the vicinity thereof are further subjected to crosslinking treatment. Can be used.

【0015】本発明では、先ず(a)の工程に於いて所
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、残存モノマー低減の効果から考える
と亜硫酸(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 the monomer. And a nitrogen-containing compound such as ammonia, ammonium salt, hydroxylamine and amino acid; sulfurous acid (salt), hydrogen sulfite, phosphorous acid (salt), hypophosphorous acid (salt) ), Thiosulfate (salt), and other reducing substances. Among these, reducing substances such as sulfurous acid (salt), hydrogen sulfite, phosphorous acid (salt), hypophosphorous acid (salt), and thiosulfuric acid (salt) are preferable in view of the effect of reducing the residual monomer.

【0016】この(a)の工程に於いて吸水性樹脂の含
水率は10〜70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
の様な重合方法により得られた吸水性樹脂が含水率10
〜70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
いると考えても差し支えなく、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ーを重合し、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10〜70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 10 to 70% 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 10
When it is in the range of up to 70% by weight, leave it as it is (a)
You may use for the process of. 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 a condition outside this range, and then water may be added or drying may be carried out to adjust to this range. When the water-absorbent resin is a dry powder, it is necessary to add water so that the water content is in the range of 10 to 70% 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10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70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、20〜60重量%で、よ
り好ましくは30〜50重量%である。
If the water content is less than 10% by weight, the reduction rate of the residual monomer is low. On the other hand, even if the water content is 70% by weight or more, the reduction rate of the residual monomer is low, and further, the water content is large, which leads to drying. It requires a large amount of energy and is economically disadvantageous. It is preferably 20 to 60% by weight, more preferably 30 to 50% by weight.

【0018】こうして(a)の工程で得られた含水率1
0〜70重量%の吸水性樹脂組成物は、その含水率の変
化率を規定範囲以下に保ちながら加熱することが、非常
に重要で、この時の含水率の変化率を20%以下にする
ことにより残存モノマーは著しく低減する。
The water content of 1 thus obtained in step (a)
It is very important to heat the water-absorbent resin composition of 0 to 70% by weight while keeping the rate of change of the water content within the specified range, and the rate of change of the water content at this time is set to 20% or less. This significantly reduces the residual monomer.

【0019】従来の方法によると、残存モノマーと反応
し得る物質を添加した後の吸水性樹脂をすぐ乾燥してい
たが、本発明では、一定期間乾燥させない状態で高温に
さらしている。
According to the conventional method, the water-absorbent resin after the addition of the substance capable of reacting with the residual monomer was immediately dried, but in the present invention, the water-absorbent resin is exposed to a high temperature without being dried for a certain period.

【0020】そうすることにより残存モノマーは著しく
低減される。この時の条件として、温度は100℃〜2
00℃好ましくは120℃〜180℃より好ましくは1
40℃〜160℃の高温に、含水率の変化率が20%以
下、好ましくは10%以下、より好ましくは1%以下に
なるように、10分以上、好ましくは30分以上、より
好ましくは1時間以上保つことで残存モノマーが著しく
低減できることが判った。
By doing so, the residual monomers are significantly reduced. At this time, the temperature is 100 ° C to 2
00 ° C, preferably 120 ° C to 180 ° C, more preferably 1
At a high temperature of 40 ° C. to 160 ° C., the rate of change in water content is 20% or less, preferably 10% or less, more preferably 1% or less, 10 minutes or more, preferably 30 minutes or more, more preferably 1 It was found that the residual monomer can be remarkably reduced by keeping it for a time or more.

【0021】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 steam. The method of spraying and heating 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 heaters, (pressure resistant) disk heaters, (pressure resistant) fluidized bed heaters. , (Withstand pressure) air flow heater, (withstand pressure) infrared heater, (withstand pressure) hot air heater, (withstand pressure) microwave heater and the like.

【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
び有機溶剤を挙げることができる。
Examples of such additives include inorganic and / or organic water-insoluble particulate powders, surfactants and 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。
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.

【0026】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より好ましい。
また、セピオライト等消臭機能をもつ無機質の水不溶性
微粒子状粉体等も、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。
Among these water-insoluble fine particle powders, inorganic water-insoluble fine particle powders are preferable, and among them, silicon dioxide, titanium dioxide, aluminum oxide, zeolite, kaolin and hydrotalcite are more preferable.
Further, inorganic water-insoluble fine particle 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.

【0027】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.

【0028】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 salts, alkylnaphthalene sulfonates, alkylpolyoxyethylene sulfate salts, dialkylsulfosuccinates, and the like, and nonionic surfactants include sorbitan fatty acid esters. 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.

【0029】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.

【0030】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.

【0031】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 powdered material after dry pulverization or a material in which the surface portion and the vicinity thereof are crosslinked is used as the form of the water-absorbent resin powder, 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.

【0032】更に同様に、本発明の方法により処理され
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, the water absorbent resin treated by the method of the present invention is added with a deodorant, a fragrance, a drug, a plant growth aid,
By interposing a bactericidal agent, a foaming agent, a pigment, a dye, a hydrophilic short fiber, a fertilizer, etc., a new function can be imparted to the resulting water absorbent resin.

【0033】[0033]

【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.

【0034】また、残存モノマー量及び含水率の変化率
は以下のようにして求めた。
The amount of residual monomer and the rate of change in water content were determined as follows.

【0035】(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) Add 100 ml of deionized water to a beaker containing 200 ml of residual monomer,
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.

【0036】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吸水性樹脂の固形分
換算値を基準とする。) (2)含水率の変化率 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、下記の式で含水率の変化率を計
算した。
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. . (Amounts of residual monomers are all based on the solid content of the water-absorbent resin.) (2) Change rate of water content The water content of the water-absorbent resin composition is 180 ° C. after drying for 3 hours in a dryer. With the weight loss, the rate of change of water content was calculated by the following formula.

【0037】[0037]

【数1】 [Equation 1]

【0038】[0038]

【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 parts of N, N'-methylenebisacrylamide were dissolved in 329 parts of deionized water, and nitrogen gas was blown into this to expel dissolved oxygen. It was 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.

【0039】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メッシュ通過物のポリアクリル酸部分中和物架
橋体である吸水性樹脂(a)を得た。吸水性樹脂(a)
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 mesh to obtain a water-absorbing material which is a crosslinked polyacrylic acid partially neutralized product of 20 mesh. Resin (a) was obtained. Water absorbent resin (a)
The residual monomer content was 223 ppm.

【0040】さらに、この吸水性樹脂(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(b)を得た。吸水性樹脂(b)中の
残存モノマーは230ppmであった。
Furthermore, 100 parts by weight of the water-absorbent resin (a) was mixed with an aqueous liquid consisting of 1 part by weight of glycerin, 4 parts by weight of water and 4 parts by weight of ethanol, and heat-treated at 180 ° C. for 30 minutes to obtain a surface portion. A water-absorbent resin (b) having a cross-linked structure was obtained. The residual monomer content in the water absorbent resin (b) was 230 ppm.

【0041】[0041]

【実施例1】 参考例で得た吸水性樹脂(b)100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(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 1.0 part of silicon dioxide (Aerosil 200 manufactured by Nippon Aerosil Co., Ltd.) was mixed with 100 parts of the water absorbent resin (b) obtained in Reference Example. 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 (b) and silicon dioxide using a high speed paddle type mixer. The water content of the water absorbent resin composition at this time was 37.5% by weight.

【0042】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の含水率は37.1重量%(含
水率変化率−1%)、残存モノマー0.4ppmであっ
た。その後、容器から吸水性樹脂組成物を取り出し、1
00℃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剤を得た。この吸水剤の
残存モノマーは1.4ppm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 for 1 hour in a heating furnace at 50 ° C. The water content of the water absorbent resin composition after the heat treatment was 37.1% by weight (water content change rate-1%), and the residual monomer was 0.4 ppm. Then, remove the water-absorbent resin composition from the container, 1
It was dried with hot air at 00 ° C. for 3 hours and sieved with a 20-mesh wire net to obtain a water-absorbing agent that passed through a 20-mesh. The residual monomer content of this water absorbing agent was 1.4 ppm.

【0043】[0043]

【実施例2】 参考例で得た吸水性樹脂(b)100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200部に溶解し、上記吸水性樹脂(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66.
7重量%であった。
Example 2 To 100 parts of the water absorbent resin (b) obtained in Reference Example, 0.7 part of a sodium dialkylsulfosuccinate (Perex OT-P manufactured by Kao Corporation) as a surfactant was mixed. As a reducing substance, 1 part of sodium hydrogen sulfite was dissolved in 200 parts of water, and the mixture of the water absorbent resin (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 66.
It was 7% by weight.

【0044】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時間加熱処理を行った。加熱
処理後の吸水性樹脂組成物の含水率は55.3重量%
(含水率変化率−17%)、残存モノマー1.2ppm
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、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1.3p
pm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 in a heating furnace at 00 ° C. for 10 hours. The water content of the water absorbent resin composition after the heat treatment is 55.3% by weight.
(Water content change rate -17%), residual monomer 1.2 ppm
Met. Then, the water-absorbent resin composition was taken out of the container, heated at a temperature of 80 ° C. for 3 hours using a fluidized bed dryer, and sieved with a 20-mesh wire net to obtain a 20-mesh passing water-absorbing agent. The residual monomer of this water absorbing agent is 1.3 p
It was pm.

【0045】[0045]

【実施例3】 参考例で得た吸水性樹脂(b)100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(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16.5重量%であっ
た。
Example 3 Hydrophobized silicon dioxide (Nippon Aerosil Co., Ltd.) was added to 100 parts of the water absorbent resin (b) obtained in Reference Example.
Made, Aerosil R972) 1.0 part 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 the mixture of the water absorbent resin (b) and the hydrophobized silicon dioxide using a high speed paddle type mixer. The water content of the water absorbent resin composition at this time was 16.5% by weight.

【0046】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、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の含水率は15.7重量%(含
水率変化率−5%)、残存モノマー1.0ppmであっ
た。その後、容器から吸水性樹脂組成物を取り出し、1
00℃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剤を得た。この吸水剤の
残存モノマーは1.9ppm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 5 hours in a heating furnace at 80 ° C. The water content of the water absorbent resin composition after the heat treatment was 15.7% by weight (water content change rate -5%), and the residual monomer was 1.0 ppm. Then, remove the water-absorbent resin composition from the container, 1
It was dried with hot air at 00 ° C. for 3 hours and sieved with a 20-mesh wire net to obtain a water-absorbing agent that passed through a 20-mesh. The residual monomer content of this water absorbing agent was 1.9 ppm.

【0047】[0047]

【実施例4】 参考例で得た吸水性樹脂(b)100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(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。
Example 4 To 100 parts of the water absorbent resin (b) obtained in the reference example, 2.0 parts of aluminum oxide (aluminum oxide C manufactured by Degussa Co., Ltd.) 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 (b) and aluminum oxide using a high speed paddle type mixer. The water content of the water absorbent resin composition at this time was 28.6% by weight.

【0048】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
20℃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の含水率は28.6重量%
(含水率変化率0%)、残存モノマー0.9ppm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
剤を得た。この吸水剤の残存モノマーは1.0ppm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 carried out in a heating furnace at 20 ° C. for 10 hours. The water content of the water absorbent resin composition after the heat treatment is 28.6% by weight.
(Water content change rate 0%) and residual monomer was 0.9 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 of 20 mesh passing product. The residual monomer of this water absorbing agent was 1.0 ppm.

【0049】[0049]

【実施例5】 参考例で得た吸水性樹脂(b)100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70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(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41.2重量%であった。
Example 5 To 100 parts of the water absorbent resin (b) obtained in Reference Example, 2.0 parts of activated carbon was mixed. As a reducing substance, 1 part of monoethanolamine, 70 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 (b) and activated carbon using a high speed paddle type mixer. The water content of the water absorbent resin composition at this time was 41.2% by weight.

【0050】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140℃の蒸気を吹き込みなが
ら30分間加熱処理を行った。加熱処理後の吸水性樹脂
組成物の含水率は46.0重量%(含水率変化率12
%)、残存モノマー0.9ppmであった。その後、容
器から吸水性樹脂組成物を取り出し、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
ュ通過物の吸水剤を得た。この吸水剤の残存モノマーは
1.5ppmであった。
Next, the water-absorbent resin composition was put into a heating furnace of a type capable of blowing steam, and heat-treated for 30 minutes while blowing steam at 140 ° C. The water content of the water absorbent resin composition after the heat treatment is 46.0% by weight (the water content change rate is 12%).
%) And residual monomer was 0.9 ppm. Then, the water-absorbent resin composition was taken out from the container, dried with hot air at 100 ° C. for 3 hours, and sieved with a 20-mesh wire net to obtain a water-absorbent agent of 20-mesh passage. The residual monomer content of this water absorbing agent was 1.5 ppm.

【0051】[0051]

【実施例6】 参考例で得た吸水性樹脂(b)100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6
0部に溶解し、上記吸水性樹脂(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 To 100 parts of the water absorbent resin (b) obtained in Reference Example, 2.0 parts of polymethylmethacrylate fine powder was mixed. As a reducing substance, 1 part of sodium hydrogen sulfite is added to 6 parts of water.
It was dissolved in 0 part, and the mixture of the water absorbent resin (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.

【0052】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
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の含水率は37.5重量%
(含水率変化率0%)、残存モノマー1.9ppm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
剤を得た。この吸水剤の残存モノマーは1.9ppm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 10 minutes in a heating furnace at 00 ° C. The water content of the water absorbent resin composition after the heat treatment is 37.5% by weight.
(Water content change rate 0%) and residual monomer was 1.9 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 of 20 mesh passing product. The residual monomer content of this water absorbing agent was 1.9 ppm.

【0053】[0053]

【実施例7】 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。このゲル
状重合体の残存モノマーは1.2%であった。これを双
腕型ニーダー中でゲル状重合体の固形分100重量部に
対して亜硫酸ナトリウム3部を添加し混合した。
Example 7 141 parts of sodium acrylate, 36.1 parts of acrylic acid, and 0.093 parts of N, N′-methylenebisacrylamide were dissolved in 329 parts of deionized water, and nitrogen gas was blown into this 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. The residual monomer of this gel polymer was 1.2%. In a double-arm kneader, 3 parts of sodium sulfite was added to and mixed with 100 parts by weight of the solid content of the gel polymer.

【0054】次にこの含水率65.0重量%のゲル状重
合体を取り出し内径10cm、長さ10cmの円筒容器
に入れ密閉状態にした後150℃の加熱炉の中、2時間
加熱処理を行った。加熱処理後のゲル状重合体の含水率
は62.0重量%(含水率変化率−5%)、残存モノマ
ー1.3ppmであった。その後、容器から吸水性樹脂
組成物を取り出し、120℃で2時間熱風乾燥を行った
後、粉砕機にて粉砕し20メッシュ金網で篩分けして2
0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1.9ppmであった。
Next, the gel polymer having a water content of 65.0% by weight was taken out, placed in a cylindrical container having an inner diameter of 10 cm and a length of 10 cm and sealed, and then heat-treated in a heating furnace at 150 ° C. for 2 hours. It was The water content of the gel polymer after the heat treatment was 62.0% by weight (water content change rate-5%), and the residual monomer was 1.3 ppm. Then, the water-absorbent resin composition was taken out from the container, dried with hot air at 120 ° C. for 2 hours, pulverized with a pulverizer and sieved with a 20-mesh wire mesh to obtain 2
A water-absorbing agent that passed through 0 mesh was obtained. The residual monomer content of this water absorbing agent was 1.9 ppm.

【0055】[0055]

【実施例8】 参考例で得た吸水性樹脂(b)100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
物質として亜硫酸ナトリウム2部を水70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(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41.5重量%であった。
Example 8 Hydrophobized silicon dioxide (Nippon Aerosil Co., Ltd.) was added to 100 parts of the water absorbent resin (b) obtained in Reference Example.
Made, Aerosil R972) 1.0 part was mixed. As a reducing substance, 2 parts of sodium sulfite is dissolved in 70 parts of water,
An aqueous liquid of reducing substance was prepared. This aqueous liquid was added to and mixed with the mixture of the water absorbent resin (b) and the hydrophobized silicon dioxide using a high speed paddle type mixer. The water content of the water absorbent resin composition at this time was 41.5% by weight.

【0056】次にこの吸水性樹脂組成物をジャケットを
120℃に加熱したパドルドライヤーに投入し、10分
後、この吸水性樹脂組成物の一部を取りだした。この時
の吸水性樹脂組成物の含水率は34.2重量%(含水率
変化率−17.6%)、残存モノマー0.81ppmで
あった。その後、続けて乾燥させながら2時間加熱し
た。加熱処理後の吸水剤の含水率8.5重量%、残存モ
ノマーは0.92ppmであった。
Next, the water absorbent resin composition was put into a paddle dryer whose jacket was heated to 120 ° C., and after 10 minutes, a part of the water absorbent resin composition was taken out. At this time, the water content of the water absorbent resin composition was 34.2% by weight (water content change rate-17.6%), and the residual monomer was 0.81 ppm. Then, it was heated for 2 hours while being continuously dried. The water content of the water absorbing agent after the heat treatment was 8.5% by weight, and the residual monomer content was 0.92 ppm.

【0057】[0057]

【比較例1】 参考例で得た吸水性樹脂(b)100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剤の残存モノマーは21.0p
pmであった。
Comparative Example 1 An aqueous solution prepared by dissolving 0.3 part of sodium hydrogen sulfite in 5 parts of water was added to 100 parts of the water absorbent resin (b) obtained in Reference Example and mixed for 5 minutes using a high speed paddle type mixer. The residual monomer of the obtained water absorbent for comparison was 21.0 p.
It was pm.

【0058】[0058]

【比較例2】 アクリル酸328部、N,N’−メチレ
ンビスアクリルアミド2.6部を脱イオン水980部に
溶解し、重炭酸ナトリウム127.5部でPH=4.0
に調製した。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水120部に溶解し
たアゾビスアミジノプロパン2塩酸塩0.36部、過硫
酸カリウム0.73部亜硫酸水素ナトリウム1.34
部、及びグルコン酸鉄(II)0.06部を加えて静置重
合し、ゲル状の含水重合体を得た。このゲル状重合体を
破砕し、重合体の固形分100重量部に対してヒドロキ
シルアミン塩酸塩2部を添加し混合した。この含水率7
7.0重量%のゲル状重合体を110℃で2時間熱風乾
燥を行った後、粉砕機にて粉砕し20メッシュの金網で
篩分けして20メッシュ通過物の比較用吸水剤を得た。
この比較用吸水剤の含水率は4.2重量%(含水率変化
率−95%)で、残存モノマーは32.1ppmであっ
た。
Comparative Example 2 328 parts of acrylic acid and 2.6 parts of N, N′-methylenebisacrylamide were dissolved in 980 parts of deionized water, and 127.5 parts of sodium bicarbonate were used to obtain PH = 4.0.
Was prepared. Nitrogen gas was blown into this to expel dissolved oxygen. Azobisamidinopropane dihydrochloride (0.36 parts) obtained by dissolving an aqueous solution of this monomer in 120 parts of water, 0.73 parts of potassium persulfate, and 1.34 parts of sodium hydrogen sulfite.
Parts and 0.06 part of iron (II) gluconate were added and statically polymerized to obtain a gel-like water-containing polymer. This gel polymer was crushed, and 2 parts of hydroxylamine hydrochloride was added to and mixed with 100 parts by weight of the solid content of the polymer. This moisture content 7
7.0% by weight of the gel polymer was dried with hot air at 110 ° C. for 2 hours, then pulverized with a pulverizer and sieved with a 20-mesh wire net to obtain a 20-mesh-passing water absorbent for comparison. .
The water content of this comparative water absorbing agent was 4.2% by weight (water content change rate: -95%), and the residual monomer content was 32.1 ppm.

【0059】[0059]

【比較例3】 参考例で得た吸水性樹脂(b)100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。この比較用吸水剤の含
水率は2.7重量%(含水率変化率−92%)、残存モ
ノマーは80.3ppmであった。
Comparative Example 3 To 100 parts of the water absorbent resin (b) obtained in Reference Example, 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. In addition,
At this time, the water content of the water absorbent resin composition was 33.3% 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 was 2.7% by weight (water content change rate: -92%), and the residual monomer content was 80.3 ppm.

【0060】[0060]

【比較例4】 参考例で得た吸水性樹脂(b)100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。この比較用吸水剤の含水率
は3.3重量%(含水率変化率−96%)、残存モノマ
ーは33.4ppmであった。
Comparative Example 4 In 100 parts of the water absorbent resin (b) obtained in Reference Example, 5 parts of sodium bisulfite was dissolved in 300 parts of water,
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 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 obtain a water-absorbing agent of 20-mesh passing product. The water content of this comparative water absorbent was 3.3% by weight (water content change rate-96%), and the residual monomer was 33.4 ppm.

【0061】[0061]

【比較例5】 参考例で得た吸水性樹脂(b)100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(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、110℃で
10時間熱風乾燥し、20メッシュ金網で篩分けして2
0メッシュ通過物の比較用吸水剤を得た。この比較用吸
水剤の含水率は8.6重量%(含水率変化率49%)
で、残存モノマーは62.5ppmあった。
Comparative Example 5 100 parts of the water-absorbent resin (b) obtained in Reference Example was mixed with hydrophobized silicon dioxide (Nippon Aerosil Co., Ltd.).
Made, Aerosil R972) 1.0 part 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 the mixture of the water absorbent resin (b) and the 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 was taken out, dried with hot air at 110 ° C. for 10 hours, and sieved with a 20 mesh wire mesh to obtain 2
A comparative water-absorbing agent that passed through 0 mesh was obtained. The water content of this comparative water absorbing agent was 8.6% by weight (water content change rate 49%).
The residual monomer was 62.5 ppm.

【0062】[0062]

【比較例6】 参考例で得た吸水性樹脂(b)100部
に、還元性物質としてチオ硫酸ナトリウム1部を水19
00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(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 6 To 100 parts of the water absorbent resin (b) obtained in Reference Example, 1 part of sodium thiosulfate as a reducing substance was added to 19 parts of water.
It was dissolved in 00 parts to prepare an aqueous liquid of a reducing substance. This aqueous liquid was added to and mixed with the water absorbent resin (b) using a double arm type kneader. The water content of the water absorbent resin composition at this time was 95.0% by weight.

【0063】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の含水率は76.2重量%(含
水率変化率−20%)、残存モノマー14.2ppmで
あった。その後、容器から吸水性樹脂組成物を取り出
し、150℃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剤を得た。
この比較用吸水剤の残存モノマーは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 the heat treatment was 76.2% by weight (water content change rate -20%), and the residual monomer was 14.2 ppm. Then, the water-absorbent resin composition was taken out of the container, dried with hot air at 150 ° C. for 3 hours, and sieved with a 20-mesh wire net to obtain a 20-mesh-passing water absorbent for comparison.
The residual monomer of this comparative water absorbing agent was 31.6 ppm.

【0064】[0064]

【比較例7】 参考例で得た吸水性樹脂(b)100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(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 7 To 100 parts of the water absorbent resin (b) obtained in the reference example, 2.0 parts of aluminum oxide (aluminum oxide C manufactured by Degussa Co., Ltd.) 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 (b) and aluminum oxide using a high speed paddle type mixer. The water content of the water absorbent resin composition at this time was 28.6% by weight.

【0065】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の含水率は28.5重量%(含
水率変化率0%)、残存モノマー21.7ppm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
吸水剤を得た。この比較用吸水剤の残存モノマーは2
1.8ppm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 the heat treatment was 28.5% by weight (water content change rate 0%), and the residual monomer was 21.7 ppm. Then, the water-absorbent resin composition was taken out of the container and heated at a temperature of 80 ° C. for 3 hours using a fluidized bed dryer,
The mixture was sieved with a mesh wire mesh to obtain a comparative water-absorbing agent that passed through 20 mesh. The residual monomer of this water absorbent for comparison is 2
It was 1.8 ppm.

【0066】[0066]

【比較例8】 参考例で得た吸水性樹脂(b)100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(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 8 To 100 parts of the water absorbent resin (b) obtained in Reference Example, 2.0 parts of activated carbon was mixed. As a reducing substance, 1 part of monoethanolamine, 25 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 (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.

【0067】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の
含水率は19.6重量%(含水率変化率−2%)、残存
モノマー28.2ppmであった。その後、容器から吸
水性樹脂組成物を取り出し、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
の比較用吸水剤を得た。この比較用吸水剤の残存モノマ
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 after standing was 19.6 wt% (water content change rate-2%), and the residual monomer was 28.2 ppm. Then, the water-absorbent resin composition 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-passing water absorbent for comparison. The residual monomer of this comparative water absorbing agent was 30.5 ppm.

【0068】[0068]

【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
後加熱処理工程中の含水率の変化率を一定範囲内に抑え
ること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、また最
適の添加水量であってもすぐに乾燥させると残存モノマ
ーは効率よく低減しない。
As is apparent from the above Examples and Comparative Examples, in order to reduce the residual monomer in the water absorbent resin, the amount of water when adding a substance capable of reacting with the residual monomer and the subsequent heat treatment step It is very important to keep the rate of change of water content within a certain range.Even if the amount of added water is too small or too large, the residual monomer does not decrease efficiently. The residual monomer is not efficiently reduced by drying.

【0069】以上のことから吸水性樹脂中の残存モノマ
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含水率
の変化率を規定範囲内に保ちながら加熱することにより
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剤が得られることが判
り、安全性の高い吸水剤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 in the water-absorbent resin, an appropriate amount of water added when adding a substance capable of reacting with the residual monomer is added so that the rate of change of water content falls within the specified range. It can be seen that the residual monomer can be reduced very efficiently by heating while keeping it at a low temperature. According to the present invention, a water absorbent having almost no residual monomer can be obtained, and a highly safe water absorbent can be stably and efficiently produced. It has become possible.

【0070】従って、本発明の方法により吸水性樹脂を
処理して得られる吸水剤は、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-absorbing agent obtained by treating the water-absorbing resin by the method of the present invention is an absorbent of sanitary materials such as disposable diapers and sanitary napkins, medical water-retaining agent, agricultural and horticultural use by taking advantage of its characteristics. It can be suitably used for applications requiring water absorption and water retention such as water retention agents and other industrial dehydrating agents.

フロントページの続き (56)参考文献 特開 平4−106108(JP,A) (58)調査した分野(Int.Cl.7,DB名) C08F 6/00 - 6/28 Continuation of the front page (56) Reference JP-A-4-106108 (JP, A) (58) Fields investigated (Int.Cl. 7 , DB name) C08F 6/00-6/28

Claims (9)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 吸水性樹脂を処理する方法であって、処
理工程が少なくとも下記(a)及び(b)の工程、 (a)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し含水率10〜70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の変化率を20%以
下に保ちながら100〜200℃の温度で10分間以上
加熱する工程 からなることを特徴とする吸水性樹脂の処理方法。
1. A method for treating a water-absorbent resin, comprising at least the following steps (a) and (b), wherein (a) the water-absorbent resin is capable of reacting with residual monomers in the water-absorbent resin. Step (b) of adding a substance to obtain a water-absorbent resin composition having a water content of 10 to 70% by weight, while maintaining the rate of change of the water content of the water-absorbent resin composition at 20% or less, at a temperature of 100 to 200 ° C. A method for treating a water-absorbent resin, comprising a step of heating for at least minutes.
【請求項2】 処理する吸水性樹脂が、ポリアクリル酸
部分中和物架橋体である請求項1記載の処理方法。
2. The treatment method according to claim 1, wherein the water absorbent resin to be treated is a crosslinked polyacrylic acid partially neutralized product.
【請求項3】 吸水性樹脂中の残存モノマーと反応し得
る物質が還元性物質である請求項1記載の処理方法。
3. The treatment method according to claim 1, wherein the substance capable of reacting with the residual monomer in the water absorbent resin is a reducing substance.
【請求項4】 工程(a)が、含水率30〜50重量%
の吸水性樹脂組成物とする請求項1記載の処理方法。
4. The step (a) comprises a water content of 30 to 50% by weight.
2. The treatment method according to claim 1, wherein the water absorbent resin composition is used.
【請求項5】 工程(b)の含水率の変化率が、1%以
下である請求項1記載の処理方法。
5. The treatment method according to claim 1, wherein the rate of change of the water content in the step (b) is 1% or less.
【請求項6】 工程(b)の加熱を、密閉状態および/
または高湿雰囲気下に行う請求項1記載の処理方法。
6. The heating in step (b) is performed in a closed state and / or
Alternatively, the treatment method according to claim 1, which is performed in a high humidity atmosphere.
【請求項7】 工程(b)に於ける加熱温度が、140
〜160℃である請求項1記載の処理方法。
7. The heating temperature in step (b) is 140.
The treatment method according to claim 1, wherein the treatment temperature is 160 ° C.
【請求項8】 工程(b)に於ける加熱時間が1時間以
上である請求項1記載の処理方法。
8. The processing method according to claim 1, wherein the heating time in step (b) is 1 hour or more.
【請求項9】 工程(a)における吸水性樹脂組成物
が、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種の添加剤を含む請求項1に記載の処理方
法。
9. 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 processing method according to claim 1, further comprising:
JP32177093A 1992-12-25 1993-12-21 Treatment method for water absorbent resin Expired - Lifetime JP3522316B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP32177093A JP3522316B2 (en) 1992-12-25 1993-12-21 Treatment method for water absorbent resin

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP34657992 1992-12-25
JP4-346579 1992-12-25
JP32177093A JP3522316B2 (en) 1992-12-25 1993-12-21 Treatment method for water absorbent resin

Publications (2)

Publication Number Publication Date
JPH06239921A JPH06239921A (en) 1994-08-30
JP3522316B2 true JP3522316B2 (en) 2004-04-26

Family

ID=26570590

Family Applications (1)

Application Number Title Priority Date Filing Date
JP32177093A Expired - Lifetime JP3522316B2 (en) 1992-12-25 1993-12-21 Treatment method for water absorbent resin

Country Status (1)

Country Link
JP (1) JP3522316B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102176927B (en) * 2008-08-12 2014-08-27 巴斯夫欧洲公司 Superabsorbers with a low residual monomer content,method for producing superabsorbers with a low residual monomer content, sanitation product comprising superabsorbers and producing method thereof

Also Published As

Publication number Publication date
JPH06239921A (en) 1994-08-30

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