JP3466222B2 - Method for producing water absorbent resin - Google Patents

Method for producing water absorbent resin

Info

Publication number
JP3466222B2
JP3466222B2 JP4299293A JP4299293A JP3466222B2 JP 3466222 B2 JP3466222 B2 JP 3466222B2 JP 4299293 A JP4299293 A JP 4299293A JP 4299293 A JP4299293 A JP 4299293A JP 3466222 B2 JP3466222 B2 JP 3466222B2
Authority
JP
Japan
Prior art keywords
water
group
polymer
heat treatment
chemical formula
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
JP4299293A
Other languages
Japanese (ja)
Other versions
JPH069717A (en
Inventor
和敬 夜野
勝弘 梶川
欣也 長砂
好夫 入江
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nippon Shokubai Co Ltd
Original Assignee
Nippon Shokubai Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=26382728&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=JP3466222(B2) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Nippon Shokubai Co Ltd filed Critical Nippon Shokubai Co Ltd
Priority to JP4299293A priority Critical patent/JP3466222B2/en
Publication of JPH069717A publication Critical patent/JPH069717A/en
Application granted granted Critical
Publication of JP3466222B2 publication Critical patent/JP3466222B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Processes Of Treating Macromolecular Substances (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
  • Macromonomer-Based Addition Polymer (AREA)

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製造方法に
関する。さらに詳しくは、本発明は、吸収倍率が高く、
水可溶成分量が少なく、かつ経時安定性に優れた吸水性
樹脂の製造方法に関する。
FIELD OF THE INVENTION The present invention relates to a method for producing a water absorbent resin. More specifically, the present invention has a high absorption capacity,
The present invention relates to a method for producing a water-absorbent resin having a small amount of water-soluble components and excellent stability over time.

【0002】[0002]

【従来の技術】吸水性樹脂は、従来から、紙おむつ(ま
たは使い捨ておむつ)、生理用品、土壌保水剤をはじめ
とする各種吸水材料に利用されている。このような吸水
性樹脂としてはデンプン−アクリロニトリルグラフト共
重合体の加水分解物、デンプン−アクリル酸グラフト共
重合体の中和物、アクリル酸またはアクリル酸塩重合体
の架橋体、ポリエチレンオキシドの部分架橋物、カルボ
キシメチルセルロースの架橋体等が知られている。
2. Description of the Related Art Water-absorbent resins have hitherto been used in various water-absorbing materials such as paper diapers (or disposable diapers), sanitary products and soil water retention agents. Examples of such a water-absorbent resin include a hydrolyzate of a starch-acrylonitrile graft copolymer, a neutralized product of a starch-acrylic acid graft copolymer, a cross-linked acrylic acid or acrylate polymer, and a partial cross-linked polyethylene oxide. And carboxymethyl cellulose cross-linked products are known.

【0003】上記架橋重合体の中では、現在、アクリル
酸をはじめとする水溶性モノエチレン性不飽和単量体を
架橋性モノマーの存在下に共重合することにより得られ
る架橋重合体が原料的にも安価で、吸水特性に優れ、か
つ、腐敗の心配もないことから吸水性樹脂の主流となっ
ている(特開昭60−24807号および米国特許第4
351922号)。
Among the above-mentioned crosslinked polymers, at present, a crosslinked polymer obtained by copolymerizing a water-soluble monoethylenically unsaturated monomer such as acrylic acid in the presence of a crosslinkable monomer is a raw material. Moreover, it is inexpensive, has excellent water absorption properties, and is not worried about spoilage, and thus has become the mainstream of water-absorbent resins (JP-A-60-24807 and US Pat. No. 4).
351922).

【0004】[0004]

【発明が解決しようとする課題】しかしながら、これら
の吸水性樹脂は、通常、吸収倍率が高くなるにつれて水
可溶成分(水に溶けうる成分)の量が多くなるのが実情
である。このような水可溶成分の多い吸水性樹脂をたと
えばおむつ等に長時間使用すると、おむつ表面にぬめり
が生じるという問題、または、通液性が悪くなって実用
上の吸水能力や液の拡散性を低下させるため、もれを生
じ易いという問題等がある。逆に吸水性樹脂中の水可溶
成分を減らすために架橋剤の使用量を増やすと、吸収倍
率が低下し、吸水性樹脂の使用範囲が制限されることに
なる。
However, in these water-absorbent resins, the amount of water-soluble component (component soluble in water) usually increases as the absorption capacity increases. When such a water-absorbent resin containing a large amount of water-soluble components is used for a long time, for example, in a diaper, the problem of sliming on the surface of the diaper, or poor liquid permeability and practical water absorption capacity and liquid diffusivity Therefore, there is a problem that leakage is likely to occur. On the contrary, if the amount of the cross-linking agent used is increased in order to reduce the water-soluble component in the water absorbent resin, the absorption capacity will be reduced and the range of use of the water absorbent resin will be limited.

【0005】また、上記水可溶成分の問題に加えて、膨
潤ゲルの経時安定性の問題もある。例えば、おむつ等に
使用した場合、尿を吸収した吸水性樹脂の膨潤ゲルが経
時的に劣化(ゲルの流動化)を起こし、吸収特性の低下
をまねくという問題点があった。また、農園芸用などの
長時間の使用でも、劣化、分解を起こすことがあった。
これまで知られている吸水性樹脂の膨潤ゲルの劣
化、分解の防止方法としては吸水性樹脂に含酸素還元性
無機塩やラジカル連鎖禁止剤などを含有させる方法(特
開昭63−118375号、特開昭63−152667
号)、酸化剤を含有させる方法(特開昭63−1530
60号)、硫黄含有還元剤を含有させる方法(特開昭6
3−272349号)などがある。しかしながら、これ
らの方法をいずれも吸水性樹脂に劣化防止のための添加
剤を加える方法であり、他の添加剤を加えるということ
は、それら吸水性樹脂が衛生材料などに使用されること
を考えると、安全性の面から必ずしも好ましいものでは
なかった。
In addition to the problem of the water-soluble component, there is a problem of stability of the swollen gel over time. For example, when used in a diaper or the like, there is a problem that the swollen gel of the water-absorbent resin that has absorbed urine deteriorates with time (fluidization of the gel), leading to deterioration of the absorption characteristics. In addition, even if it is used for a long time such as for agricultural and horticultural use, it may be deteriorated or decomposed.
As a known method for preventing the deterioration and decomposition of the swollen gel of the water-absorbent resin, a method of incorporating an oxygen-containing reducing inorganic salt or a radical chain inhibitor into the water-absorbent resin (Japanese Patent Laid-Open No. 63-118375). JP-A-63-152667
No.), a method of incorporating an oxidizing agent (Japanese Patent Laid-Open No. 63-1530).
No. 60), and a method of incorporating a sulfur-containing reducing agent (JP-A-6-61)
3-272349). However, all of these methods are methods of adding an additive for deterioration prevention to the water absorbent resin, and adding other additives means that these water absorbent resins are used for sanitary materials and the like. Therefore, it was not always preferable in terms of safety.

【0006】そこで、架橋剤量を多く用いて、吸水性樹
脂の架橋密度を高めることで、ゲル強度を高め、経時安
定性を向上させる方法もあるが、これらの吸水性樹脂は
十分な経時安定性を持たせるには、高架橋のため吸水倍
率が極端に低くなるという問題点があった。
[0006] Therefore, there is also a method of increasing the crosslink density of the water-absorbent resin by using a large amount of the cross-linking agent to increase the gel strength and improve the stability over time. However, these water-absorbent resins are sufficiently stable over time. In order to impart the property, there is a problem that the water absorption capacity becomes extremely low due to the high crosslinking.

【0007】[0007]

【課題を解決するための手段】本発明者らは、上記課題
を解決するために鋭意検討を重ねた結果、特定構造を持
つ架橋剤の存在下に水溶性エチレン性不飽和単量体を共
重合して得られる重合体をある特定温度範囲で加熱処理
した場合に限って吸収倍率が高く、水可溶成分が少な
く、かつ、経時安定性に優れた吸水性樹脂となり得るこ
とを見い出し、本発明を完成させた。
Means for Solving the Problems As a result of intensive studies to solve the above problems, the present inventors have found that a water-soluble ethylenically unsaturated monomer is used in the presence of a crosslinking agent having a specific structure. It was found that the polymer obtained by polymerization has a high absorption capacity only when it is heat-treated in a certain temperature range, has a small amount of water-soluble components, and can be a water-absorbent resin having excellent stability over time. Completed the invention.

【0008】すなわち、本発明は、水溶性モノエチレン
性不飽和単量体を架橋剤の存在下に水溶液重合し、得ら
れた重合体を加熱処理する吸水性樹脂の製造方法におい
て、前記架橋剤として少なくとも2個の重合性不飽和基
を有すると共に、該少なくとも2個の重合性不飽和基の
間に少なくとも1個の化学式(1)で表わされる単位
That is, the present invention provides a method for producing a water-absorbent resin in which a water-soluble monoethylenically unsaturated monomer is polymerized in an aqueous solution in the presence of a cross-linking agent, and the resulting polymer is heat-treated. Having at least two polymerizable unsaturated groups as a unit, and at least one unit represented by the chemical formula (1) between the at least two polymerizable unsaturated groups.

【0009】[0009]

【化6】 [Chemical 6]

【0010】(但し、化学式(1)中のRは、下記一
般式(a)〜(c)よりなる群から選ばれた少なくとも
1種のアルキレン基である。)を有する分子量が600
0以下である架橋剤(I)を前記水溶性モノエチレン性
不飽和単量体に対して0.01〜0.3モル%の割合で
用い、且つ該重合体の加熱処理は重合体の有する官能基
と反応し得る反応性基を少なくとも2個有する架橋剤
(III)の存在下に160〜230℃の加熱処理温度
で行われることを特徴とする吸水性樹脂の製造方法に関
するものである。
[0010] (however, R 1 in the chemical formula (1), following one
At least selected from the group consisting of general formulas (a) to (c)
It is one kind of alkylene group. ) Having a molecular weight of 600
The cross-linking agent (I) of 0 or less is used in a proportion of 0.01 to 0.3 mol% with respect to the water-soluble monoethylenically unsaturated monomer, and the heat treatment of the polymer is carried out by the polymer. It relates to a method for producing a water absorbent resin, which is carried out at a heat treatment temperature of 160 to 230 ° C. in the presence of a crosslinking agent (III) having at least two reactive groups capable of reacting with a functional group.

【化学式20】 また、本発明は、酸基含有単量体および該酸基含有単量
体の金属塩、アンモニウム塩およびアミン塩、ノニオン
性親水性基含有単量体、アミノ基含有単量体および該ア
ミノ基含有単量体の4級化物よりなる群から選ばれる少
なくとも1種の水溶性モノエチレン性不飽和単量体(但
し、次亜燐酸およびチオリンゴ酸を含まない単量体)を
架橋剤の存在下に水溶液重合し、得られた重合体を加熱
処理する吸水性樹脂の製造方法において、前記架橋剤と
して少なくとも2個の重合性不飽和基を有すると共に、
該少なくとも2個の重合性不飽和基の間に少なくとも1
個の化学式(1)で表わされる単位
[Chemical formula 20] The present invention also provides an acid group-containing monomer and the acid group-containing unit amount.
Body metal, ammonium and amine salts, nonions
Hydrophilic group-containing monomer, amino group-containing monomer and
A small amount selected from the group consisting of quaternized products of mino group-containing monomers.
At least one water-soluble monoethylenically unsaturated monomer (however
Monomers that do not contain hypophosphorous acid and thiomalic acid)
Aqueous solution polymerization in the presence of a cross-linking agent, heating the resulting polymer
In the method for producing a water absorbent resin to be treated, with the crosslinking agent
And has at least two polymerizable unsaturated groups,
At least one between the at least two polymerizable unsaturated groups
Unit represented by chemical formula (1)

【化学式21】 (但し、化学式(1)中のR1は、炭素数2〜4のアル
キレン基である。)を有する分子量が6000以下であ
る架橋剤(I)を前記水溶性モノエチレン性不飽和単量
体に対して0.01〜0.3モル%の割合で用い、且つ
該重合体の加熱処理は重合体の有する官能基と反応し得
る反応性基を少なくとも2個有する架橋剤(III)の
存在下に160〜230℃の加熱処理温度で行われるこ
とを特徴とする吸水性樹脂の製造方法である。
[Chemical formula 21] (However, R1 in the chemical formula (1) is an alkane having 2 to 4 carbon atoms.
It is a xylene group. ) Having a molecular weight of 6000 or less
The crosslinking agent (I) is a water-soluble monoethylenically unsaturated monomer
Used in a proportion of 0.01 to 0.3 mol% with respect to the body, and
The heat treatment of the polymer may react with the functional groups of the polymer.
Of a crosslinking agent (III) having at least two reactive groups
In the presence of heat treatment temperatures of 160-230 ° C.
And a method for producing a water-absorbent resin.

【0011】[0011]

【作用】本発明で用いられる水溶性モノエチレン性不飽
和単量体としては、1個のエチレン性不飽和基を有し、
水に溶解性の単量体であれば特に制限されず、たとえ
ば、(メタ)アクリル酸、イタコン酸、2−(メタ)ア
クリロイルエタンスルホン酸、2−(メタ)アクリロイ
ルプロパンスルホン酸、2−(メタ)アクリルアミド−
2−メチルプロパンスルホン酸、ビニルスルホン酸、ス
チレンスルホン酸等の酸基含有単量体;該酸基含有単量
体の金属塩、アンモニウム塩またはアミン塩;(メタ)
アクリルアミド、アルコキシポリエチレングルコール
(メタ)アクリレート等のノニオン性親水基含有単量
体;ジエチルアミノエチル(メタ)アクリレート、ジエ
チルアミノプロピル(メタ)アクリレート、ジメチルア
ミノプロピル(メタ)アクリルアミド等のアミノ基含有
単量体;該アミノ基含有単量体の4級化物等を挙げるこ
とができ、これらの群から選ばれる1種または2種以上
を用いることができる。
The water-soluble monoethylenically unsaturated monomer used in the present invention has one ethylenically unsaturated group,
It is not particularly limited as long as it is a water-soluble monomer, and examples thereof include (meth) acrylic acid, itaconic acid, 2- (meth) acryloylethanesulfonic acid, 2- (meth) acryloylpropanesulfonic acid, 2- ( (Meth) acrylamide
Acid group-containing monomer such as 2-methylpropanesulfonic acid, vinylsulfonic acid, styrenesulfonic acid; metal salt, ammonium salt or amine salt of the acid group-containing monomer; (meth)
Nonionic hydrophilic group-containing monomers such as acrylamide and alkoxypolyethylene glycol (meth) acrylate; amino group-containing monomers such as diethylaminoethyl (meth) acrylate, diethylaminopropyl (meth) acrylate and dimethylaminopropyl (meth) acrylamide A quaternized product of the amino group-containing monomer and the like, and one or more selected from these groups can be used.

【0012】好ましい水溶性モノエチレン性不飽和単量
体は、アクリル酸ならびに、そのアルカリ金属塩、アン
モニウム塩およびアミン塩から選ばれる少なくとも1種
が50重量%以上含んでなる単量体である。ここで塩と
しては、中和率30〜80%が好ましい。中和は重合後
に行ってもよい。
A preferred water-soluble monoethylenically unsaturated monomer is a monomer containing acrylic acid and at least 50% by weight or more of at least one selected from alkali metal salts, ammonium salts and amine salts thereof. Here, the salt preferably has a neutralization ratio of 30 to 80%. Neutralization may be performed after polymerization.

【0013】また、得られる吸水性樹脂の性能を著しく
損なわない範囲で他の単量体を併用してもよく、さら
に、デンプン、セルロース、ポリビニルアルコ−ル等の
天然高分子や合成高分子をグラフト化成分として水溶性
モノエチレン性不飽和単量体に加えて重合させてもよ
い。水溶性モノエチレン性不飽和単量体と併用されうる
他の単量体としては、たとえば、メチル(メタ)アクリ
レート、エチル(メタ)アクリレート、ブチル(メタ)
アクリレート、酢酸ビニル、プロピオン酸ビニルなどが
挙げられ、これらを2種以上併用してもよい。
Further, other monomers may be used in combination so long as the performance of the resulting water-absorbent resin is not significantly impaired, and further natural or synthetic polymers such as starch, cellulose and polyvinyl alcohol may be used. You may polymerize in addition to a water-soluble monoethylenically unsaturated monomer as a grafting component. Other monomers that can be used in combination with the water-soluble monoethylenically unsaturated monomer include, for example, methyl (meth) acrylate, ethyl (meth) acrylate, butyl (meth).
Examples thereof include acrylate, vinyl acetate, vinyl propionate, and the like, and these may be used in combination of two or more kinds.

【0014】本発明に用いられる架橋剤(以下、架橋剤
(I)という)は、分子内に少なくとも1個の下記化学
式(1)で表わされる単位
The cross-linking agent (hereinafter referred to as cross-linking agent (I)) used in the present invention has at least one unit represented by the following chemical formula (1) in the molecule.

【0015】[0015]

【化6】 [Chemical 6]

【0016】(但し、化学式(1)中のR1 は炭素数2
〜4のアルキレン基である。)を少なくも2個の重合性
不飽和基の間に有する化合物である。ここで炭素数2〜
4のアルキレン基は、直鎖状、枝分かれ構造いずれでも
よく、例えば、下記一般式(a)〜(c)に示す化合物
(However, R 1 in the chemical formula (1) has 2 carbon atoms.
To 4 alkylene groups. ) Between at least two polymerizable unsaturated groups. Where the carbon number is 2
The alkylene group of 4 may have either a straight chain structure or a branched structure, and examples thereof include compounds represented by the following general formulas (a) to (c).

【0017】[0017]

【化7】 [Chemical 7]

【0018】等が挙げられる。架橋剤(I)の分子量は
6000を越えないことが好ましく、特に214〜50
00が好ましく、最も好ましくは214〜2500であ
る。
And the like. The molecular weight of the cross-linking agent (I) is preferably not more than 6000, especially 214 to 50
00 is preferable, and 214 to 2500 is most preferable.

【0019】そのような架橋剤(I)の典型例は、下記
化学式(2)
A typical example of such a crosslinking agent (I) is represented by the following chemical formula (2).

【0020】[0020]

【化8】 [Chemical 8]

【0021】(但し、化学式(2)中のR2 およびR3
はそれぞれ独立に水素またはメチであり、nは2〜10
0、好ましくは2〜50である。)で表わされる構造を
有する化合物および下記化学式(3)
(However, R 2 and R 3 in the chemical formula (2) are
Are each independently hydrogen or methyl, and n is 2 to 10
It is 0, preferably 2 to 50. And a compound having the structure represented by the following chemical formula (3)

【0022】[0022]

【化9】 [Chemical 9]

【0023】〔但し、化学式(3)中のR2 およびR3
はそれぞれ独立に水素またはメチル基であり、Xは1〜
100個、好ましくは1〜50個の−CH2 CH2
O−で表わされる構2単位(A)、1〜20個、好まし
くは1〜10個の−R4 O−(ここにR4 は炭素数3〜
4のアルキレン基である。)で表される構造単位(B)
が任意の配列で直鎖状に結合した2価の有機基である
か、あるいは、Xは1〜5個、好ましくは1〜3個の−
(CO−CH=CH−CO−O)−で表される構造単位
(C)、2〜100個、好ましくは4〜50個のCH2
CH2 O−で表される構造単位(D)および0〜20
個、好ましくは0〜10個の−R5 O−(ここにR5
炭素数3〜4のアルキレン基である。)で表される構造
単位(E)が任意の配列で直鎖状に結合した2価の有機
基である。]で表わされる構造を有する化合物である。
[However, R 2 and R 3 in the chemical formula (3) are
Are each independently hydrogen or a methyl group, and X is 1 to
100, preferably 1 to 50 -CH2CH2
Structure 2 unit (A) represented by O-, 1 to 20, preferably 1 to 10 -R 4 O- (wherein R 4 has 3 to 10 carbon atoms).
4 is an alkylene group. ) Structural unit (B)
Is a divalent organic group linearly bonded in an arbitrary sequence, or X is 1 to 5, preferably 1 to 3
Structural unit (C) represented by (CO-CH = CH-CO-O)-, 2 to 100, preferably 4 to 50 CH 2
Structural unit (D) represented by CH 2 O- and 0 to 20
, Preferably 0 to 10 structural units (E) represented by —R 5 O— (wherein R 5 is an alkylene group having 3 to 4 carbon atoms) are linear in any sequence. It is a bonded divalent organic group. ] It is a compound which has a structure represented.

【0024】ここで、炭素数3〜4のアルキレン基は上
述のR1 と同様に直鎖状、枝分か構造いずれでもよい。
Here, the alkylene group having 3 to 4 carbon atoms may be linear, branched, or structured similarly to R 1 described above.

【0025】架橋剤(I)としては、例えばポリエチレ
ングリコールジ(メタ)アクリレート、ポリエチレング
リコール−ポリプロピレングリコールブロック共重合体
のジ(メタ)アクリレート、ポリエチレングリコール−
ポリプロピレングリコールランダム共重合体のジ(メ
タ)アクリレート、フマル酸ジ[ポリエチレングリコー
ルモノ(メタ)アクリレート]エステル、マレイン酸ジ
[ポリエチレングリコールモノ(メタ)アクリレート]
エステル等がある。
Examples of the crosslinking agent (I) include polyethylene glycol di (meth) acrylate, polyethylene glycol-polypropylene glycol block copolymer di (meth) acrylate, polyethylene glycol-
Polypropylene glycol random copolymer di (meth) acrylate, fumaric acid di [polyethylene glycol mono (meth) acrylate] ester, maleic acid di [polyethylene glycol mono (meth) acrylate]
There are esters, etc.

【0026】本発明では、架橋剤(I)に合わせて従来
通常に知られている架橋剤を第二架橋剤(以下、架橋剤
(II)という)として少量であれば使用してもよい。
その使用量は一般的に水溶性エチレン性不飽和単量体に
対して0.01モル%以下である。
In the present invention, a conventionally known cross-linking agent may be used as the second cross-linking agent (hereinafter referred to as the cross-linking agent (II)) in a small amount according to the cross-linking agent (I).
The amount used is generally 0.01 mol% or less based on the water-soluble ethylenically unsaturated monomer.

【0027】架橋剤(I)は、本発明の目的を考慮し
て、水溶性モノエチレン性不飽和単量体に対して0.0
1〜0.3モル%の割合で使用されることが必須であ
る。該架橋剤の使用量が0.01モル%未満では、得ら
れる吸水性樹脂の水可溶成分が多くなる場合があり、ま
た、0.3モル%を越えると、加熱処理を加えても吸水
特性の向上が不十分となる場合がある。好ましくは、
0.03〜0.2モル%である。
The crosslinking agent (I) is 0.0 to the water-soluble monoethylenically unsaturated monomer in view of the object of the present invention.
It is essential that it be used in a proportion of 1 to 0.3 mol%. If the amount of the cross-linking agent used is less than 0.01 mol%, the water-soluble component of the resulting water-absorbent resin may increase, and if it exceeds 0.3 mol%, the water-absorbent resin may absorb water even if heat treatment is added. The improvement of the characteristics may be insufficient. Preferably,
It is 0.03 to 0.2 mol%.

【0028】本発明では、水溶性モノエチレン性不飽和
単量体を該架橋剤(I)の存在下に重合させるにはどの
ような方法を採ってもよいが、水溶性モノエチレン性不
飽和単量体を含む単量体成分の水溶液を該架橋剤(I)
の存在下で重合させる方法をとるのがよい。重合方法と
しては、例えば、水溶液重合、逆相懸濁重合、沈殿重合
等の各種の方法を採用することができる。中でも、重合
時の作業性や得られる吸水性樹脂の吸水特性の点からは
水溶液重合法または逆相懸濁重合法が好ましい。 ま
た、重合開始の際にはラジカル重合開始剤を用いて重合
させる方法;放射線、電子線、紫外線を照射して重合さ
せる方法(紫外線照射の場合には、光重合開始剤が使用
されることもある)など通常の方法が採用できる。ラジ
カル重合開始剤としては、一般に使用される水溶性ラジ
カル重合開始剤である過硫酸カリウム、過硫酸ナトリウ
ム、過硫酸アンモニウム等の過硫酸塩;過酸化水素、t
−ブチルハイドロパーオキシド、クメンハイドロパーオ
キシド等のハイドロパーオキシド;2,2’−アゾビス
−2−アミジノプロパン塩酸塩等のアゾ化合物などが挙
げられる。これらのラジカル重合開始剤は1種類を単独
で使用してもよいし、2種類以上混合して使用すること
も可能であり、更には亜硫酸塩、L−アスコルビン酸、
第1鉄塩等の還元剤との組み合わせによりレドックス開
始剤系も用いることができる。ラジカル重合開始剤の使
用量は、単量体に対して0.01〜1.0重量%の割合
が好ましく、0.005〜0.5重量%の割合がより好
ましい。
In the present invention, any method may be used to polymerize the water-soluble monoethylenically unsaturated monomer in the presence of the crosslinking agent (I). An aqueous solution of a monomer component containing a monomer is used as the crosslinking agent (I).
The method of polymerizing in the presence of As the polymerization method, various methods such as aqueous solution polymerization, reverse phase suspension polymerization, and precipitation polymerization can be adopted. Among them, the aqueous solution polymerization method or the reverse phase suspension polymerization method is preferable from the viewpoint of workability during polymerization and the water absorption characteristics of the resulting water absorbent resin. Further, at the time of initiation of polymerization, a method of polymerizing using a radical polymerization initiator; a method of polymerizing by irradiating radiation, an electron beam, or ultraviolet rays (in the case of ultraviolet irradiation, a photopolymerization initiator may also be used. There is a normal method such as As the radical polymerization initiator, persulfates such as potassium persulfate, sodium persulfate and ammonium persulfate which are commonly used water-soluble radical polymerization initiators; hydrogen peroxide, t
-Hydroperoxides such as butyl hydroperoxide and cumene hydroperoxide; and azo compounds such as 2,2'-azobis-2-amidinopropane hydrochloride. These radical polymerization initiators may be used alone or in a mixture of two or more, and further, sulfite, L-ascorbic acid,
Redox initiator systems can also be used in combination with reducing agents such as ferrous salts. The amount of the radical polymerization initiator used is preferably 0.01 to 1.0% by weight, more preferably 0.005 to 0.5% by weight, based on the monomers.

【0029】重合体を水溶液重合法や逆相懸濁重合法で
合成する際には、一般に単量体を水溶液とするのが好ま
しい。その単量体水溶液中の単量体濃度は、広い範囲に
わたって選択が可能であるが、一般に20重量%以上、
好ましくは25重量%以上から飽和濃度までである。必
要があれば、このときに有機溶剤を存在させてもよい。
このような有機溶剤としては、たとえば、メタノール、
エタノール、プロパノール、ブタノールなどの水と相溶
性のあるアルコール類;テトラヒドロフラン、ジオキサ
ンなどの水と相溶性のあるエーテル類;アセトン、メチ
ルエチルケトンなどの水と相溶性のあるケトン類;アセ
トニトリルなどの水と相溶性のあるニトリル類;N,N
−ジブチルホルムアミドなどの水と相溶性のあるアミド
類等が挙げられる。
When the polymer is synthesized by the aqueous solution polymerization method or the reverse phase suspension polymerization method, it is generally preferable to use the monomer as an aqueous solution. The monomer concentration in the monomer aqueous solution can be selected over a wide range, but generally 20% by weight or more,
It is preferably from 25% by weight or more to a saturated concentration. If necessary, an organic solvent may be present at this time.
As such an organic solvent, for example, methanol,
Alcohols that are compatible with water, such as ethanol, propanol, butanol; Ethers that are compatible with water, such as tetrahydrofuran and dioxane; Ketones that are compatible with water, such as acetone and methyl ethyl ketone; Water and phases, such as acetonitrile Soluble nitriles; N, N
Examples include amides that are compatible with water, such as dibutylformamide.

【0030】重合の温度は、使用するラジカル重合開始
剤の種類等によって種々変えることができるが、通常0
〜150℃、好ましくは10〜100℃である。重合時
の雰囲気圧力は、減圧下〜加圧下の範囲で適宜設定する
ことができる。
The polymerization temperature can be variously changed depending on the kind of the radical polymerization initiator to be used, but it is usually 0.
˜150 ° C., preferably 10˜100 ° C. The atmospheric pressure during the polymerization can be appropriately set in the range of reduced pressure to increased pressure.

【0031】上記使用するラジカル重合開始剤の種類・
量・雰囲気圧力との組み合わせにより重合温度をコント
ロールしてもよい。
Type of radical polymerization initiator used above
The polymerization temperature may be controlled by combining the amount and the atmospheric pressure.

【0032】本発明では重合により得られた重合体を1
60〜230℃という特定温度範囲で加熱処理すること
が必須である。加熱処理が160℃より低い場合および
230℃より高い場合は、得られる吸水性樹脂の吸収倍
率が低く、しかも吸収倍率の割に生成する水可溶成分量
の量が多くなる。好ましくは、加熱処理温度は180〜
200℃である。加熱処理を行うに際しては、重合体が
含水状態にあることが好ましい。より好ましくは、加熱
処理前の水分が30〜95重量%、さらに好ましくは6
0〜95重量%である。
In the present invention, the polymer obtained by the polymerization is
It is essential to perform heat treatment within a specific temperature range of 60 to 230 ° C. When the heat treatment is lower than 160 ° C. or higher than 230 ° C., the absorption capacity of the resulting water absorbent resin is low, and the amount of the water-soluble component produced is large relative to the absorption capacity. Preferably, the heat treatment temperature is 180 to
It is 200 ° C. When the heat treatment is carried out, the polymer is preferably in a water-containing state. More preferably, the water content before the heat treatment is 30 to 95% by weight, and further preferably 6
It is 0 to 95% by weight.

【0033】重合体が含水状態にある際の上記特定温度
範囲での加熱処理の具体的方法としては、例えば、含水
状態にある重合体を加熱処理と同時に乾燥させる方法、
重合体に水を添加して最適含水率に調整した後、加熱処
理する方法、含水状態にある重合体を160℃より低い
温度で水分を減少させ、ついでこの樹脂を加熱処理する
方法、含水状態にある重合体を水分がほとんど減少しな
い状態で加熱処理する方法等が挙げられる。
As a specific method of heat treatment in the above-mentioned specific temperature range when the polymer is in a water-containing state, for example, a method of drying the water-containing polymer at the same time as the heat treatment,
Water is added to the polymer to adjust the water content to an optimum value, and then heat treatment is performed, the water content of the polymer is reduced at a temperature lower than 160 ° C., and then this resin is heat treated, and water content is contained. And the like, for example, by subjecting the polymer to heat treatment in a state where the water content is hardly reduced.

【0034】加熱処理をして得られる吸水性樹脂は必要
により乾燥を行い、さらに必要により粉砕、分級し、製
品とすることができる。
The water-absorbent resin obtained by the heat treatment may be dried if necessary, and further crushed and classified as necessary to obtain a product.

【0035】本願発明の加熱処理には、通常の乾燥器や
加熱炉等を用いることができ、たとえば、溝型攪拌乾燥
器、回転乾燥器、円盤乾燥器、捏和乾燥器、熱風乾燥
器、流動層乾燥器、気流乾燥器、赤外線乾燥器、誘電加
熱乾燥器等が例示できる。
For the heat treatment of the present invention, an ordinary dryer, a heating oven or the like can be used. For example, a groove type stirring dryer, a rotary dryer, a disk dryer, a kneading dryer, a hot air dryer, Examples thereof include a fluidized bed dryer, a gas stream dryer, an infrared dryer, a dielectric heating dryer and the like.

【0036】本願発明の目的をより明確に達成するため
には、本願発明の特定の温度範囲をはずれた温度で加熱
した場合に得られる樹脂の吸収倍率が55倍未満、より好
ましくは50倍未満でかつ本願発明の特定の温度範囲で
加熱処理した場合に得られる吸水性樹脂の吸収倍率が5
5倍以上となるように重合体の重合条件を選択するのが
好適である。重合体を本願発明の特定の温度範囲をはず
れた温度で加熱した場合の樹脂の吸収倍率が55倍以上
となる場合は、本願発明の特定の温度範囲で加熱処理を
行うと水可溶成分が増加する傾向にあり、結果として本
発明が目的とするところの吸収倍率が高くしかも水可溶
成分の少ない吸水性樹脂が得られない場合がある。本願
発明の特定の温度範囲をはずれた温度で加熱した場合の
樹脂の吸収倍率が55倍未満とするには、重合体を得る
際に架橋剤(I)の種類、および/または使用量を適宜
調節したり、他の第二架橋剤を併用する手段等によれば
よい。
In order to more clearly attain the object of the present invention, the absorption capacity of the resin obtained when heated at a temperature outside the specific temperature range of the present invention is less than 55 times, more preferably less than 50 times. And the absorption capacity of the water-absorbent resin obtained by heat treatment in the specific temperature range of the present invention is 5
It is preferable to select the polymerization conditions of the polymer so as to be 5 times or more. When the absorption capacity of the resin is 55 times or more when the polymer is heated at a temperature outside the specific temperature range of the present invention, the water-soluble component is removed by heat treatment at the specific temperature range of the present invention. There is a tendency that the water absorption resin tends to increase, and as a result, a water absorbent resin having a high absorption capacity and a small amount of a water-soluble component, which is the object of the present invention, cannot be obtained. In order to make the absorption capacity of the resin less than 55 times when heated at a temperature outside the specific temperature range of the present invention, the type and / or the amount of the cross-linking agent (I) used in obtaining the polymer are appropriately adjusted. It may be adjusted or a means of using another second crosslinking agent together.

【0037】また重合体を本願発明の特定の温度範囲で
加熱処理する際には、あらかじめ重合体の有する官能基
と反応しうる官能基を2個以上有する第三架橋剤(以
下、架橋剤(III)という)と混合し、加熱処理と同
時にその表面部分において反応させることにより、重合
体粒子の表面近傍の架橋密度を高めて吸水特性や膨潤時
の経時安定性をさらに改善させる事もできる。この場
合、使用できる架橋剤(III)としては、たとえば、
吸水性樹脂がカルボキシル基を有する場合には、多価ア
ルコール類、多価グリシジルエーテル類、多価アミン
類、多価アジリジン類、多価イソシアネート類、アルキ
レンカ−ボネイト類、多価金属塩類等を挙げることがで
きる。その好ましい使用量は重合体の固形分100重量
部に対し、架橋剤(III)が0.005〜5重量部、
好ましくは0.01〜1重量部である。
When the polymer is heat-treated in the specific temperature range of the present invention, a third crosslinking agent having two or more functional groups capable of reacting with the functional group of the polymer in advance (hereinafter referred to as a crosslinking agent ( It is also possible to increase the crosslink density in the vicinity of the surface of the polymer particles and further improve the water absorption characteristics and the stability over time during swelling by mixing with (III)) and reacting at the surface portion simultaneously with the heat treatment. In this case, the cross-linking agent (III) that can be used is, for example,
When the water absorbent resin has a carboxyl group, polyhydric alcohols, polyhydric glycidyl ethers, polyhydric amines, polyhydric aziridines, polyhydric isocyanates, alkylene carbonates, polyhydric metal salts, etc. Can be mentioned. The preferable amount of the crosslinking agent (III) is 0.005 to 5 parts by weight, based on 100 parts by weight of the solid content of the polymer.
It is preferably 0.01 to 1 part by weight.

【0038】さらに、架橋剤(III)を重合体や加熱
処理後の吸水性樹脂に混合する際、架橋剤(III)の
重合体へのしみ込みをコントロールする目的で、水や親
水性有機溶剤を使用することが好ましい。親水性有機溶
剤としては、たとえば、メタノール、エタノール、プロ
パノール等のアルコール類;テトラヒドロフラン、ジオ
キサン等のエーテル類;アセトン、メチルエチルケトン
等のケトン類;アセトニトリル等のニトリル類であり、
これらの1種または2種以上の混合溶剤でもよい。また
このような架橋剤(III)による架橋は、加熱処理後
に得られた吸水性樹脂に行ってもよい。
Further, when the cross-linking agent (III) is mixed with the polymer or the water-absorbent resin after heat treatment, water or a hydrophilic organic solvent is used for the purpose of controlling penetration of the cross-linking agent (III) into the polymer. Is preferably used. Examples of the hydrophilic organic solvent include alcohols such as methanol, ethanol and propanol; ethers such as tetrahydrofuran and dioxane; ketones such as acetone and methyl ethyl ketone; nitriles such as acetonitrile,
One or a mixture of two or more of these may be used. Further, the crosslinking with the crosslinking agent (III) may be performed on the water absorbent resin obtained after the heat treatment.

【0039】本発明の製造方法により得られた吸水性樹
脂は、従来の吸水性樹脂に比べて吸収倍率が高く、水可
溶成分が少なく、かつ、経時安定性に優れているので、
膨潤時のベトつき感が少なく、通液性が良く、しかも、
これらの性能が長時間維持される。よって衛生材料、土
木、農園芸用などの用途に幅広く利用できる。
The water-absorbent resin obtained by the production method of the present invention has a higher absorption capacity than conventional water-absorbent resins, less water-soluble components, and excellent stability over time.
There is little stickiness when swelling, good liquid permeability, and
These performances are maintained for a long time. Therefore, it can be widely used for sanitary materials, civil engineering, agriculture and horticulture.

【0040】[0040]

【実施例】以下に本発明の具体的な実施例および比較例
を示すが、この発明は下記実施例に限定されない。な
お、実施例および比較例で得られた吸水性樹脂の吸収倍
率と水可溶成分量、ゲルのベタつき、ゲルの経時安定性
は次のようにして求めた。 (a)吸収倍率 得られた吸水性樹脂粉体約0.200gを精秤して不織
布製のティーバッグ式袋(40mm×50mm)に均一
に入れ、0.9%の食塩水に浸漬し、30分後の重量を
測定した。ティーバッグ式袋のみの吸液重量をブランク
として、下記数式(1)に従って吸水性樹脂の吸収倍率
を算出した。
EXAMPLES Specific examples and comparative examples of the present invention will be shown below, but the present invention is not limited to the following examples. The absorption capacity, the amount of water-soluble components, the stickiness of the gel, and the temporal stability of the gel of the water absorbent resins obtained in Examples and Comparative Examples were determined as follows. (A) Absorption capacity About 0.200 g of the obtained water-absorbent resin powder was precisely weighed and uniformly placed in a non-woven tea bag type bag (40 mm x 50 mm), and immersed in 0.9% saline solution, The weight after 30 minutes was measured. The absorption capacity of the water-absorbent resin was calculated according to the following mathematical formula (1), with the liquid absorption weight of only the tea bag type bag as the blank.

【0041】[0041]

【数1】 [Equation 1]

【0042】(b)水可溶成分量 吸水性樹脂粉体0.500gを1000mlの脱イオン
水中に分散させ、12時間攪拌した後、濾紙で濾過し、
濾液の固形分を測定して下記数式(2)に従って水可溶
成分量を求めた。
(B) Water-soluble component amount 0.500 g of the water-absorbent resin powder was dispersed in 1000 ml of deionized water, stirred for 12 hours, and then filtered with a filter paper,
The solid content of the filtrate was measured and the amount of water-soluble components was determined according to the following mathematical formula (2).

【0043】[0043]

【数2】 [Equation 2]

【0044】(c)ゲルのベタつき (a)で吸収倍率を測定した後の膨潤ゲルのベタつきを
手触りにて判定した。
(C) Stickiness of gel The stickiness of the swollen gel after measuring the absorption capacity in (a) was evaluated by touch.

【0045】(d)ゲルの経時安定性 吸水性樹脂粉体2.0gを成人男子10人からサンプリ
ングした人尿50gを使って膨潤させ、37℃で放置し
て、6時間、12時間、18時間後の膨潤ゲルの様子を
観察した。劣化状態の判定は、○〜△〜×の3段階評価
とした。
(D) Stability of gel over time 2.0 g of the water-absorbent resin powder was swollen with 50 g of human urine sampled from 10 adult males and left at 37 ° C. for 6 hours, 12 hours, 18 hours. The appearance of the swollen gel after the lapse of time was observed. The deterioration state was judged by three-level evaluation from ◯ to Δ to ×.

【0046】○:膨潤ゲルの形状が保持されている。
△:一部、膨潤ゲルの形状が崩れている。×:膨潤ゲル
の形状が崩れ、ドロドロの流動状となっている。
◯: The shape of the swollen gel is maintained.
Δ: The shape of the swollen gel is partially broken. X: The shape of the swollen gel is collapsed and becomes a muddy fluid state.

【0047】実施例1 内容積10リットル、シグマ(Σ)型羽根が2本設けら
れたジャケット付きステンレス製双腕型ニーダーにアク
リル酸ナトリウム75モル%とアクリル酸25モル%と
からなるアクリル酸塩系単量体の水溶液5500g(モ
ノマー濃度30重量%)と、架橋剤(I)として、ポリ
エチレングリコールジアクリレート(エチレンオキシド
平均単位数7)8.09g(対単量体0.1モル%)と
を加え、窒素ガスを吹き込み反応系内を窒素置換した。
Example 1 A stainless steel double-arm kneader with a jacket having an internal volume of 10 liters and provided with two sigma (Σ) blades, and an acrylic acid salt containing 75 mol% of sodium acrylate and 25 mol% of acrylic acid. 5500 g of an aqueous solution of a system monomer (monomer concentration 30% by weight) and 8.09 g of polyethylene glycol diacrylate (average number of ethylene oxide units 7) as crosslinking agent (I) (0.1 mol% of monomer) In addition, nitrogen gas was blown into the reaction system to replace it with nitrogen.

【0048】ジャケットに35℃の温水を通じて加温し
ながら、重合開始剤として、過硫酸アンモニウム2.5
gと亜硫酸水素ナトリウム2.5gを添加し、ニーダー
内のシグマ羽根を65r,p,m,で攪拌させながら重
合を開始させた。重合反応は1時間行った。反応終了
後、細分化した含水ゲル2000gを目開き0.3mm
の金網上に置き、180℃の温度で2時間熱風乾燥し
た。この乾燥物をハンマーミルを用いて粉砕し、吸水性
樹脂を得た。このものの吸収倍率は58.9g/g、水
可溶成分は8.3%であった(表1参照)。
While warming the jacket with warm water of 35 ° C., ammonium persulfate 2.5 was added as a polymerization initiator.
g and 2.5 g of sodium hydrogen sulfite were added, and the polymerization was started while stirring the sigma blade in the kneader at 65 r, p, m. The polymerization reaction was carried out for 1 hour. After the reaction is completed, 2000 g of the hydrous gel that has been subdivided is opened by 0.3 mm
It was placed on a wire mesh of No. 1 and dried with hot air at a temperature of 180 ° C. for 2 hours. The dried product was crushed using a hammer mill to obtain a water absorbent resin. This product had an absorption capacity of 58.9 g / g and a water-soluble component of 8.3% (see Table 1).

【0049】比較例1 実施例1で、含水ゲルを150℃の温度で2時間熱風乾
燥した以外は、実施例1と同様に行い、吸水性樹脂を得
た。このものの吸収倍率は48.7g/g、水可溶成分
は8.2%であった(表1参照)。
Comparative Example 1 A water absorbent resin was obtained in the same manner as in Example 1, except that the hydrogel was dried in hot air at a temperature of 150 ° C. for 2 hours. This product had an absorption capacity of 48.7 g / g and a water-soluble component of 8.2% (see Table 1).

【0050】比較例2 実施例1において、架橋剤(I)の代わりにポリプロピ
レングリコールジアクリレート(プロピレンオキシド平
均単位数7)9.92g(対単量体0.1モル%)とし
た以外は実施例1と同様に行い、吸水性樹脂を得た。こ
のものの吸収倍率は48.3g/g、水可溶成分は1
1.1%であった(表1参照)。
Comparative Example 2 The procedure of Example 1 was repeated except that the crosslinking agent (I) was replaced by 9.92 g of polypropylene glycol diacrylate (average number of propylene oxide units: 7) (0.1 mol% based on the monomer). The same procedure as in Example 1 was carried out to obtain a water absorbent resin. This product has an absorption capacity of 48.3 g / g and a water-soluble component of 1
It was 1.1% (see Table 1).

【0051】比較例3 比較例2において、含水ゲルを150℃の温度で2時間
熱風乾燥した以外は、比較例2と同様に行い、吸水性樹
脂を得た。このものの吸収倍率は46.0g/g、水可
溶成分は10.2%であった(表1参照)。
Comparative Example 3 A water absorbent resin was obtained in the same manner as in Comparative Example 2 except that the hydrogel was dried in hot air at a temperature of 150 ° C. for 2 hours. The absorption capacity of this product was 46.0 g / g, and the water-soluble component was 10.2% (see Table 1).

【0052】実施例2 実施例1において、用いられる架橋剤(I)を下記化学
式(5)に示される架橋剤7.52g(0.07モル
%)
Example 2 7.52 g (0.07 mol%) of the crosslinking agent (I) used in Example 1 was used as the crosslinking agent represented by the following chemical formula (5).

【0053】[0053]

【化10】 [Chemical 10]

【0054】とした以外は、実施例1と同様に行い、吸
水性樹脂を得た。このものの吸収倍率は62.2g/
g、水可溶成分は8.3%であった(表1参照)。
A water absorbing resin was obtained in the same manner as in Example 1 except that the above was adopted. The absorption capacity of this product is 62.2 g /
g, water-soluble component was 8.3% (see Table 1).

【0055】比較例4 実施例2で、含水ゲルを150℃の温度で2時間熱風乾
燥した以外は、実施例1と同様に行い、吸水性樹脂を得
た。このものの吸収倍率は52.7g/g、水可溶成分
は8.1%であった(表1参照)。
Comparative Example 4 A water absorbent resin was obtained in the same manner as in Example 1, except that the hydrogel was dried in hot air at a temperature of 150 ° C. for 2 hours. The absorption capacity of this product was 52.7 g / g, and the water-soluble component was 8.1% (see Table 1).

【0056】実施例1〜2および比較例1〜4より、加
熱処理温度が150℃の場合および本発明に用いられる
架橋剤(I)以外の架橋剤を使用した場合、吸収倍率が
低い。
From Examples 1 and 2 and Comparative Examples 1 to 4, the absorption capacity is low when the heat treatment temperature is 150 ° C. and when a crosslinking agent other than the crosslinking agent (I) used in the present invention is used.

【0057】実施例3 実施例1において、用いられる架橋剤(I)を下記化学
式(6)に示される架橋剤9.66g(0.07モル
%)
Example 3 In Example 1, the crosslinking agent (I) used was 9.66 g (0.07 mol%) of the crosslinking agent represented by the following chemical formula (6).

【0058】[0058]

【化11】 [Chemical 11]

【0059】とした以外は、実施例1と同様に行い、吸
水性樹脂を得た。このものの吸収倍率は56.4g/
g、水可溶成分は10.3%であった(表2参照)。
A water absorbing resin was obtained in the same manner as in Example 1 except that the above was carried out. The absorption capacity of this product is 56.4 g /
g, water-soluble component was 10.3% (see Table 2).

【0060】比較例5 実施例3において、用いられる架橋剤(I)の量を4.
14g(対単量体0.03モル%)に変更し、含水ゲル
を150℃の温度で2時間熱風乾燥した以外は同様に行
い、吸水性樹脂を得た。このものの吸収倍率は55.2
g/g、水可溶成分は18.4%であった。ゲルはベタ
つき、尿に対する経時安定性も悪い(表2参照)。
Comparative Example 5 In Example 3, the amount of the crosslinking agent (I) used was 4.
A water absorbent resin was obtained in the same manner except that the amount of the water-containing gel was changed to 14 g (0.03 mol% based on the monomer) and the hydrogel was dried with hot air at a temperature of 150 ° C. for 2 hours. The absorption capacity of this product is 55.2.
The g / g and water-soluble components were 18.4%. The gel is sticky and has poor stability over time in urine (see Table 2).

【0061】比較例6 実施例3において、用いられる架橋剤(I)の代わりに
トリメチロールプロパントリアクリレート1.66g
(対単量体0.03モル%)とする以外は同様に行い、
吸水性樹脂を得た。このものの吸収倍率は56.2g/
g、水可溶成分は20.2%であった。ゲルはベタつ
き、ゲルの経時安定性も悪い(表2参照)。
Comparative Example 6 1.66 g of trimethylolpropane triacrylate instead of the crosslinking agent (I) used in Example 3
The same procedure is performed except that (0.03 mol% relative to the monomer),
A water absorbent resin was obtained. The absorption capacity of this product is 56.2 g /
g, the water-soluble component was 20.2%. The gel is sticky and the stability of the gel over time is poor (see Table 2).

【0062】実施例3および比較例5〜6より、本発明
以外の方法で、ほぼ同等の吸収倍率の吸水性樹脂を得よ
うとした場合、水可溶成分が増え、ゲルはベタつき、ゲ
ルの経時安定性も悪い。
From Example 3 and Comparative Examples 5 to 6, when it was attempted to obtain a water-absorbent resin having almost the same absorption capacity by a method other than the present invention, the water-soluble component increased, the gel became sticky, and the gel Poor stability over time.

【0063】実施例4 実施例1と同様の双腕型ニーダーにアクリル酸カリウム
75モル%とアクリル酸20モル%およびアクリルアミ
ド5モル%とからなる単量体成分の水溶液5500g
(モノマー濃度35重量%)に、架橋剤(I)として、
下記化学式(7)に示される化合物14.1g(対単量
体0.1モル%)
Example 4 5500 g of an aqueous solution of a monomer component containing 75 mol% of potassium acrylate, 20 mol% of acrylic acid and 5 mol% of acrylamide was added to the same double-arm kneader as in Example 1.
(Monomer concentration 35% by weight), as a cross-linking agent (I),
14.1 g of the compound represented by the following chemical formula (7) (0.1 mol% based on the monomer)

【0064】[0064]

【化12】 [Chemical 12]

【0065】を加え、窒素ガスを吹き込み、反応系内を
窒素置換した。
Then, nitrogen gas was blown into the reaction system to replace the atmosphere in the reaction system with nitrogen.

【0066】次いで、重合開始剤として、過硫酸ナトリ
ウム2.0gとL−アスコルビン酸0.1gを添加し、
ニーダー内のシグマ型羽根を65r,p,m,で攪拌さ
せながら重合を開始させた。
Then, 2.0 g of sodium persulfate and 0.1 g of L-ascorbic acid were added as polymerization initiators,
Polymerization was started while stirring the sigma type blade in the kneader at 65r, p, m.

【0067】反応終了後、細分化したゲルを目開き0.
3mmの金網上に置き、200℃の温度で1時間熱風乾
燥した。この乾燥物をハンマーミルを用いて粉砕し、吸
水性樹脂を得た。このものの吸収倍率は59.2g/
g、水可溶成分は12.4%であった(表3参照)。
After completion of the reaction, the subdivided gel was opened with a mesh size of 0.
It was placed on a 3 mm wire mesh and dried with hot air at a temperature of 200 ° C. for 1 hour. The dried product was crushed using a hammer mill to obtain a water absorbent resin. The absorption capacity of this product is 59.2 g /
g, water-soluble component was 12.4% (see Table 3).

【0068】実施例5 実施例4において、用いられる架橋剤(I)をポリエチ
レングリコールジアクリレート(エチレンオキシド平均
単位数45)60.5g(対単量体0.15モル%)と
した以外は、実施例4と同様に行い、吸水性樹脂を得
た。このものの吸収倍率は57.3g/g、水可溶成分
は12.1%であった(表3参照)。
Example 5 Example 5 was repeated except that the cross-linking agent (I) used was 60.5 g of polyethylene glycol diacrylate (average number of ethylene oxide units: 45) (0.15 mol% based on the monomer). The same procedure as in Example 4 was carried out to obtain a water absorbent resin. The absorption capacity of this product was 57.3 g / g, and the water-soluble component was 12.1% (see Table 3).

【0069】比較例7 実施例4において、用いられる架橋剤(I)の代わりに
メチレンビスアクリルアミド0.72g(対単量体0.
03モル%)とした以外は実施例4と同様に行い、吸水
性樹脂を得た。このものの吸収倍率は55.9g/g、
水可溶成分は20.4%であった。ゲルはベタつき、尿
に対する経時安定性も悪い(表3参照)。 比較例8 実施例4において、反応終了後、細分化されたゲルを1
20℃の温度で4時間熱風乾燥した以外は実施例4と同
様に行い、吸水性樹脂を得た。このものの吸収倍率は4
6.2g/g、水可溶成分は11.8%であった。吸収
倍率が実施例4に比べ低い(表3参照)。
COMPARATIVE EXAMPLE 7 In Example 4, 0.72 g of methylenebisacrylamide was used instead of the crosslinking agent (I) used.
(03 mol%), except that the same procedure as in Example 4 was carried out to obtain a water absorbent resin. The absorption capacity of this product is 55.9 g / g,
The water-soluble component was 20.4%. The gel is sticky and has poor stability over time in urine (see Table 3). Comparative Example 8 In Example 4, after the reaction was completed, 1
A water-absorbent resin was obtained in the same manner as in Example 4, except that hot-air drying was performed at a temperature of 20 ° C for 4 hours. This product has an absorption capacity of 4
The content of water-soluble component was 6.2 g / g, 11.8%. Absorption capacity is lower than in Example 4 (see Table 3).

【0070】実施例6 実施例1で得られた吸水性樹脂100重量部に架橋剤
(III)の溶液として、グリセリン0.3部、水2
部、イソプロピルアルコール8部よりなる水性液を加
え、得られた混合物を180℃の乾燥機の中に入れ、2
0分間加熱して架橋反応を行うことにより吸水性樹脂を
得た。このものの吸収倍率は58倍で、ゲルの経時安定
性は良好であった(表4参照)。
Example 6 As a solution of the crosslinking agent (III) in 100 parts by weight of the water absorbent resin obtained in Example 1, 0.3 part of glycerin and 2 parts of water were added.
Part, an aqueous liquid consisting of 8 parts of isopropyl alcohol was added, and the resulting mixture was placed in a dryer at 180 ° C. for 2 minutes.
A water-absorbent resin was obtained by heating for 0 minutes to carry out a crosslinking reaction. The absorption capacity of this product was 58 times, and the stability of the gel over time was good (see Table 4).

【0071】比較例9 実施例6において、比較例6で得られた吸水性樹脂を用
いた以外は実施例6と同様に行い、吸水性樹脂を得た。
このものの吸収倍率は55倍で、ゲルの経時安定性は、
比較例6に比べ若干の改善はみられたものの、未だ不安
定であった。また、ゲルはベタついた(表4参照)。
Comparative Example 9 A water absorbent resin was obtained in the same manner as in Example 6 except that the water absorbent resin obtained in Comparative Example 6 was used.
The absorption capacity of this product is 55 times, and the stability of the gel over time is
Although slightly improved as compared with Comparative Example 6, it was still unstable. Further, the gel was sticky (see Table 4).

【0072】比較例10 実施例6において、比較例6で得られた吸水性樹脂に架
橋剤(II)の溶液を混合後、40分間加熱する以外
は、実施例6と同様に行い、吸水性樹脂を得た。このも
ののゲルの経時安定性は良好であるが、ゲルはベタつい
た。吸収倍率は47倍であった(表4参照)。
Comparative Example 10 The procedure of Example 6 was repeated except that the solution of the cross-linking agent (II) was mixed with the water absorbent resin obtained in Comparative Example 6 and the mixture was heated for 40 minutes. A resin was obtained. Although this gel had good stability over time, the gel was sticky. The absorption capacity was 47 times (see Table 4).

【0073】[0073]

【表1】 [Table 1]

【0074】[0074]

【表2】 [Table 2]

【0075】[0075]

【表3】 [Table 3]

【0076】[0076]

【表4】 [Table 4]

【0077】[0077]

【発明の効果】本発明の吸水性樹脂の製造方法は、上記
特定の構造を持つ架橋剤(I)の存在下で水溶性モノエ
チレン性不飽和単量体の共重合を行い、さらに得られた
樹脂を160〜230℃の温度で加熱処理することを特
徴とする。
The method for producing a water-absorbent resin of the present invention is further obtained by copolymerizing a water-soluble monoethylenically unsaturated monomer in the presence of a crosslinking agent (I) having the above-mentioned specific structure. The resin is heat-treated at a temperature of 160 to 230 ° C.

【0078】この方法によれば、吸収倍率が高く、水可
溶成分が少なく、ゲルの経時安定性の優れた吸水性樹脂
が得られる。
According to this method, a water absorbent resin having a high absorption capacity, a small amount of water-soluble components and excellent gel stability over time can be obtained.

フロントページの続き (51)Int.Cl.7 識別記号 FI // C08L 33:02 C08L 33:02 (72)発明者 入江 好夫 兵庫県姫路市網干区興浜字西沖992番地 の1 株式会社日本触媒 姫路研究所内 (56)参考文献 特開 平3−179008(JP,A) (58)調査した分野(Int.Cl.7,DB名) C08F 8/00 - 8/50 Continuation of front page (51) Int.Cl. 7 Identification code FI // C08L 33:02 C08L 33:02 (72) Inventor Yoshio Irie 1 992 Nishi-oki, Akihama, Aboshi-ku, Himeji-shi, Hyogo Nihon Catalysis Himeji Laboratory Co., Ltd. (56) References JP-A-3-179008 (JP, A) (58) Fields investigated (Int.Cl. 7 , DB name) C08F 8 / 00-8 / 50

Claims (9)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 水溶性モノエチレン性不飽和単量体を架
橋剤の存在下に水溶液重合し、得られた重合体を加熱処
理する吸水性樹脂の製造方法において、前記架橋剤とし
て少なくとも2個の重合性不飽和基を有すると共に、該
少なくとも2個の重合性不飽和基の間に少なくとも1個
の化学式(1)で表わされる単位 【化1】 (但し、化学式(1)中のR、下記一般式(a)〜
(c)よりなる群から選ばれた少なくとも1種のアルキ
レン基である。)を有する分子量が6000以下である
架橋剤(I)を前記水溶性モノエチレン性不飽和単量体
に対して0.01〜0.3モル%の割合で用い、且つ該
重合体の加熱処理は重合体の有する官能基と反応し得る
反応性基を少なくとも2個有する架橋剤(III)の存
在下に160〜230℃の加熱処理温度で行われること
を特徴とする吸水性樹脂の製造方法。 【化2】
1. A method for producing a water-absorbent resin, which comprises subjecting a water-soluble monoethylenically unsaturated monomer to aqueous solution polymerization in the presence of a cross-linking agent, and subjecting the resulting polymer to heat treatment, wherein at least two crosslinking agents are used. And a unit represented by the chemical formula (1) having at least two polymerizable unsaturated groups between the at least two polymerizable unsaturated groups. (However, R 1 in the chemical formula (1) is represented by the following general formula (a) to
It is at least one alkylene group selected from the group consisting of (c) . Is used in a proportion of 0.01 to 0.3 mol% with respect to the water-soluble monoethylenically unsaturated monomer, and a heat treatment of the polymer is carried out. Is carried out at a heat treatment temperature of 160 to 230 ° C. in the presence of a cross-linking agent (III) having at least two reactive groups capable of reacting with a functional group of the polymer. . [Chemical 2]
【請求項2】 酸基含有単量体および該酸基含有単量体
の金属塩、アンモニウム塩およびアミン塩、ノニオン性
親水性基含有単量体、アミノ基含有単量体および該アミ
ノ基含有単量体の4級化物よりなる群から選ばれる少な
くとも1種の水溶性モノエチレン性不飽和単量体(但
し、次亜燐酸およびチオリンゴ酸を含まない単量体)を
架橋剤の存在下に水溶液重合し、得られた重合体を加熱
処理する吸水性樹脂の製造方法において、 前記架橋剤として少なくとも2個の重合性不飽和基を有
すると共に、該少なくとも2個の重合性不飽和基の間に
少なくとも1個の化学式(1)で表わされる単位 【化3】 (但し、化学式(1)中のR1は、炭素数2〜4のアル
キレン基である。)を有する分子量が6000以下であ
る架橋剤(I)を前記水溶性モノエチレン性不飽和単量
体に対して0.01〜0.3モル%の割合で用い、且つ
該重合体の加熱処理は重合体の有する官能基と反応し得
る反応性基を少なくとも2個有する架橋剤(III)の
存在下に160〜230℃の加熱処理温度で行われるこ
とを特徴とする吸水性樹脂の製造方法。
2. An acid group-containing monomer and the acid group-containing monomer
Metal salts, ammonium salts and amine salts, nonionic
Hydrophilic group-containing monomer, amino group-containing monomer and the amino group
A small amount selected from the group consisting of quaternized products of non-group-containing monomers.
At least one water-soluble monoethylenically unsaturated monomer (however
Monomers that do not contain hypophosphorous acid and thiomalic acid)
Aqueous solution polymerization in the presence of a cross-linking agent, heating the resulting polymer
In the method for producing a water absorbent resin to be treated , at least two polymerizable unsaturated groups are contained as the crosslinking agent.
And between the at least two polymerizable unsaturated groups
At least one unit represented by the chemical formula (1) : (However, R1 in the chemical formula (1) is an alkane having 2 to 4 carbon atoms.
It is a xylene group. ) Having a molecular weight of 6000 or less
The crosslinking agent (I) is a water-soluble monoethylenically unsaturated monomer
Used in a proportion of 0.01 to 0.3 mol% with respect to the body, and
The heat treatment of the polymer may react with the functional groups of the polymer.
Of a crosslinking agent (III) having at least two reactive groups
In the presence of heat treatment temperatures of 160-230 ° C.
And a method for producing a water-absorbent resin.
【請求項3】 含水状態にある重合体を160〜230
℃で加熱処理したのち、さらに該重合体の加熱処理が該
重合体の有する官能基と反応し得る反応性基を少なくと
も2個有する架橋剤の存在下に160〜230℃の該加
熱処理が行なわれる請求項1または2に記載の方法。
3. A polymer having a water content of 160 to 230
After heat treatment at ℃, further heat treatment of the polymer
Reduce the number of reactive groups that can react with the functional groups of the polymer
In the presence of a cross-linking agent having two
The method according to claim 1, wherein heat treatment is performed.
【請求項4】 含水状態にある重合体の160〜230
℃での加熱処理によって加熱処理後の重合体の吸収倍率
を向上させる請求項1〜3のいずれか1つに記載の製造
方法。
4. A polymer having a water content of 160 to 230.
Absorption capacity of polymer after heat treatment by heat treatment at ℃
Manufacturing according to any one of claims 1 to 3, which improves the
Method.
【請求項5】 含水状態にある重合体の160〜230
℃での加熱処理による吸収倍率の向上が重合体の固形分
あたり1g/g以上である請求項1〜4のいずれか1つ
に記載の方法。
5. A polymer having a water content of 160 to 230.
Improving the absorption capacity by heat treatment at ℃ increases the solid content of the polymer.
It is 1 g / g or more per one, Any one of Claims 1-4.
The method described in.
【請求項6】 該架橋剤(I)は、下記化学式(2) 【化4】 (但し、化学式(2)中のR2およびR3はそれぞれ独
立に水素またはメチル基を表わし、nは2〜100であ
る。) で表わされる構造を有してなる請求項2〜5のいずれか
1つに記載の方法。
6. The cross- linking agent (I) has the following chemical formula (2) : (However, R2 and R3 in the chemical formula (2) are each
Vertically represents hydrogen or a methyl group, and n is 2 to 100.
It ) The structure according to any one of claims 2 to 5 having a structure represented by
The method according to one.
【請求項7】 該架橋剤(I)は、下記化学式(3) 【化5】 [但し、化学式(3)中のR2およびR3はそれぞれ独
立に水素またはメチル基を表わし、Xは1〜100個の
−CH2CH2O−で表わされる構造単位(A)、1〜
20個の−R4O−(ここにR4は炭素数3〜4のアル
キレン基である。)で表わされる構造単位(B)が、任
意の配列で直鎖状に結合した2価の有機基であるか、あ
るいは、Xは1〜5個の−(CO−CH=CH−CO−
O)−で表される構造単位(C)、2〜100個の−C
H2CH2O−で表される構造単位(D)および0〜2
0個の−R5O−(ここにR5は炭素数3〜4のアルキ
レン基である。)で表される構造単位(E)が任意の配
列で直鎖状に結合した2価の有機基である。]で表わさ
れる構造を有してなる請求項1〜5のいずれか1つに記
載の方法。
7. The cross- linking agent (I) has the following chemical formula (3) : [However, R2 and R3 in the chemical formula (3) are each
Vertically represents hydrogen or a methyl group, and X is 1 to 100
Structural unit (A) represented by -CH2CH2O-, 1-
20 -R4O- (where R4 is an alkyl group having 3 to 4 carbon atoms)
It is a xylene group. ) Is a structural unit (B)
Is the divalent organic group linearly bonded in the desired sequence?
In other words, X is 1 to 5-(CO-CH = CH-CO-
O)-, a structural unit (C) represented by 2 to 100 -C
Structural unit (D) represented by H2CH2O- and 0 to 2
0 -R5O- (where R5 is an alkyl group having 3 to 4 carbon atoms)
It is a len group. ) The structural unit (E) represented by
It is a divalent organic group linearly linked in a row. ]]
The structure according to claim 1, which has a structure
How to list.
【請求項8】 水溶性モノエチレン性不飽和単量体を架
橋剤の存在下に重合し、得られた重合体を加熱処理する
吸水性樹脂の製造方法において、前記架橋剤として少な
くとも2個の重合性不飽和基を有すると共に、該少なく
とも2個の重合性不飽和基の間に少なくとも1個の化学
式(1)で表わされる単位 【化6】 (但し、化学式(1)中のRは下記一般式(a)〜
(c) 【化7】 よりなる群から選ばれた少なくとも1種のアルキレン基
である。)を有する架橋剤(I)を前記水溶性モノエチ
レン性不飽和単量体に対して0.01〜0.3モル%の
割合で用い、且つ重合体の加熱処理の温度が160〜2
30℃であることを特徴とする吸水性樹脂の製造方法。
8. A method for producing a water-absorbent resin in which a water-soluble monoethylenically unsaturated monomer is polymerized in the presence of a cross-linking agent, and the resulting polymer is heat-treated, wherein at least two cross-linking agents are used. A unit having a polymerizable unsaturated group and at least one unit represented by the chemical formula (1) between the at least two polymerizable unsaturated groups: (However, R 1 in the chemical formula (1) is represented by the following general formula (a) to
(C) [Chemical formula 7] It is at least one alkylene group selected from the group consisting of: Is used in a proportion of 0.01 to 0.3 mol% with respect to the water-soluble monoethylenically unsaturated monomer, and the heat treatment temperature of the polymer is 160 to 2
A method for producing a water absorbent resin, which is at 30 ° C.
【請求項9】 酸基含有単量体および該酸基含有単量体
の金属塩、アンモニウム塩およびアミン塩、ノニオン性
親水性基含有単量体、アミノ基含有単量体および該アミ
ノ基含有単量体の4級化物よりなる群から選ばれる少な
くとも1種の水溶性モノエチレン性不飽和単量体(但
し、次亜燐酸およびチオリンゴ酸を含まない単量体)を
架橋剤の存在下に水溶液重合し、得られた重合体を加熱
処理する吸水性樹脂の製造方法において、前記架橋剤と
して少なくとも2個の重合性不飽和基を有すると共に、
該少なくとも2個の重合性不飽和基の間に少なくとも1
個の化学式(1)で表わされる単位 【化8】 (但し、化学式(1)中のRは炭素数2〜4のアルキ
レン基である。)を有する架橋剤(I)を前記水溶性モ
ノエチレン性不飽和単量体に対して0.01〜0.3モ
ル%の割合で用い、加熱処理されるべき重合体が含水状
態であり、且つ重合体の加熱処理の温度が180〜20
0℃であることを特徴とする吸水性樹脂の製造方法。
9. An acid group-containing monomer and the acid group-containing monomer
Metal salts, ammonium salts and amine salts, nonionic
Hydrophilic group-containing monomer, amino group-containing monomer and the amino group
Of at least one water-soluble monoethylenically unsaturated monomer selected from the group consisting of quaternized non-group-containing monomers (provided that it does not contain hypophosphorous acid and thiomalic acid) In a method for producing a water-absorbent resin, which comprises polymerizing an aqueous solution in the presence of the polymer and heat-treating the obtained polymer, the polymer has at least two polymerizable unsaturated groups as the cross-linking agent,
At least one between the at least two polymerizable unsaturated groups
A unit represented by the chemical formula (1) (However, R 1 in the chemical formula (1) is an alkylene group having 2 to 4 carbon atoms.) The crosslinking agent (I) is added to the water-soluble monoethylenically unsaturated monomer in an amount of 0.01 to It is used in a proportion of 0.3 mol%, the polymer to be heat treated is in a water-containing state, and the temperature of the heat treatment of the polymer is 180 to 20.
It is 0 degreeC, The manufacturing method of the water absorbent resin characterized by the above-mentioned.
JP4299293A 1992-03-05 1993-03-03 Method for producing water absorbent resin Expired - Lifetime JP3466222B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4299293A JP3466222B2 (en) 1992-03-05 1993-03-03 Method for producing water absorbent resin

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP4832192 1992-03-05
JP4-48321 1992-03-05
JP4299293A JP3466222B2 (en) 1992-03-05 1993-03-03 Method for producing water absorbent resin

Publications (2)

Publication Number Publication Date
JPH069717A JPH069717A (en) 1994-01-18
JP3466222B2 true JP3466222B2 (en) 2003-11-10

Family

ID=26382728

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4299293A Expired - Lifetime JP3466222B2 (en) 1992-03-05 1993-03-03 Method for producing water absorbent resin

Country Status (1)

Country Link
JP (1) JP3466222B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5123569B2 (en) * 2001-10-03 2013-01-23 株式会社日本触媒 A solution containing a (meth) acrylic acid polymer, a solution containing an unsaturated polyalkylene glycol copolymer, and a detergent using them
MXPA05012802A (en) * 2003-06-06 2006-02-22 Basf Ag (meth)acrylic ester for alkylenylene glycol and the use thereof.
DE102005002412A1 (en) * 2005-01-18 2006-07-27 Basf Ag Process for the preparation of polymers by spray polymerization

Also Published As

Publication number Publication date
JPH069717A (en) 1994-01-18

Similar Documents

Publication Publication Date Title
EP0559476B1 (en) Method for the production of absorbent resin
US5281683A (en) Process for producing water-absorbent resin
JP2877255B2 (en) Manufacturing method of water absorbent resin with excellent durability
US5506324A (en) Method of preparation of crosslinked hydrophilic resins
US6914099B2 (en) Water absorbent resin particles of crosslinked carboxyl-containing polymers with low monomer content
US5489647A (en) Hydrophilic, swellable graft polymers
JP2008522003A (en) Cross-linking agent for super absorbent polymer
JP2013100529A (en) Production process for water-absorbent resin
WO2006094907A1 (en) Hydrolytically stable postcrosslinked superabsorbents
PT873187E (en) POLYMERS RETICULATED WITH AMINOATED ALCOOES INSATURATED WITH CAPACITY TO INCREASE VOLUME WITH WATER ITS PREPARATION AND UTILIZATION
JP2995276B2 (en) Manufacturing method of water absorbent resin
WO1994020547A1 (en) Water absorbent resin particles of crosslinked carboxyl containing polymers and method of preparation
JPH0826085B2 (en) Method for producing water-absorbent resin having excellent durability
JP3259143B2 (en) Method for producing water absorbent resin
JPH06122707A (en) Production of water-absorbent resin
JP3349768B2 (en) Method and composition for producing acrylate polymer
JP2901368B2 (en) Method for producing salt-resistant water-absorbent resin
JP3466222B2 (en) Method for producing water absorbent resin
JPS6136309A (en) Water-absorbent resistant to salt and light
JP4213808B2 (en) Water absorbing agent and method for producing the same
JPH0656933A (en) Water-absorbing resin and its production
JPH0218899B2 (en)
JP3187370B2 (en) Manufacturing method of water absorbent resin with excellent durability
JPS62205101A (en) Production of highly water absorbing polymer having improved absorbing power
JPH02253845A (en) Water absorbing agent having superior salt resistance

Legal Events

Date Code Title Description
RD04 Notification of resignation of power of attorney

Free format text: JAPANESE INTERMEDIATE CODE: R3D04

FPAY Renewal fee payment (prs date is renewal date of database)

Year of fee payment: 4

Free format text: PAYMENT UNTIL: 20070829

FPAY Renewal fee payment (prs date is renewal date of database)

Year of fee payment: 5

Free format text: PAYMENT UNTIL: 20080829

FPAY Renewal fee payment (prs date is renewal date of database)

Year of fee payment: 6

Free format text: PAYMENT UNTIL: 20090829

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100829

Year of fee payment: 7

FPAY Renewal fee payment (prs date is renewal date of database)

Year of fee payment: 7

Free format text: PAYMENT UNTIL: 20100829

FPAY Renewal fee payment (prs date is renewal date of database)

Year of fee payment: 8

Free format text: PAYMENT UNTIL: 20110829

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120829

Year of fee payment: 9

FPAY Renewal fee payment (prs date is renewal date of database)

Year of fee payment: 9

Free format text: PAYMENT UNTIL: 20120829

FPAY Renewal fee payment (prs date is renewal date of database)

Year of fee payment: 10

Free format text: PAYMENT UNTIL: 20130829

EXPY Cancellation because of completion of term