JPH06306118A - Production of highly water-absorptive polymer - Google Patents

Production of highly water-absorptive polymer

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Publication number
JPH06306118A
JPH06306118A JP12770393A JP12770393A JPH06306118A JP H06306118 A JPH06306118 A JP H06306118A JP 12770393 A JP12770393 A JP 12770393A JP 12770393 A JP12770393 A JP 12770393A JP H06306118 A JPH06306118 A JP H06306118A
Authority
JP
Japan
Prior art keywords
water
polymer
alkoxytitanium
treatment
added
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP12770393A
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Japanese (ja)
Other versions
JP3482535B2 (en
Inventor
Tetsuya Yamamoto
哲也 山本
Osamu Nakajima
修 中島
Kenji Yoshinaga
憲司 吉永
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.)
Mitsubishi Petrochemical Co Ltd
Original Assignee
Mitsubishi Petrochemical Co Ltd
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Priority to JP12770393A priority Critical patent/JP3482535B2/en
Publication of JPH06306118A publication Critical patent/JPH06306118A/en
Application granted granted Critical
Publication of JP3482535B2 publication Critical patent/JP3482535B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

PURPOSE:To obtain a highly water-absorptive polymer free from a decrease in water absorbency and excellent in dispersibility in water, rate of water absorption, and long-term stability in a state of gel containing absorbed water, by treating a water-soluble and/or water-absorptive polymer with an alkoxytitanium in the presence of water. CONSTITUTION:A water-soluble and/or water-absorptive polymer is treated with an alkoxytitanium in the presence of water. The amount of the alkoxytitanium used is usually about 0.001-10wt.% based on the polymer. The amount of water present is usually about 0.5-300wt.% based on the polymer. The treatment of the polymer is performed by, for example, the wet treatment wherein a slurry made by dispersing the water-absorptive polymer containing water in an inert solvent is mixed with an alkoxytitanium, or the dry treatment wherein an alkoxytitanium is sprayed onto the water-absorptive polymer containing water with agitation.

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、高吸水性ポリマーの製
造法に関するものである。本発明の製造法によって得ら
れる高吸水性ポリマーは、処理による吸水能の低下が無
く、水の分散性、吸水速度、吸水したゲル状態での経時
安定性が改善されるものである。従って、衛生材料、産
業資材関係、農園芸関係等の各種の吸水材料に好適に使
用することが出来る。
FIELD OF THE INVENTION The present invention relates to a method for producing a super absorbent polymer. The superabsorbent polymer obtained by the production method of the present invention does not have a decrease in water absorption capacity due to treatment, and has improved water dispersibility, water absorption rate, and temporal stability in a water-absorbed gel state. Therefore, it can be suitably used for various water absorbing materials such as sanitary materials, industrial materials, agriculture and horticulture.

【0002】[0002]

【従来の技術】従来、高吸水性ポリマーをしては、澱粉
−アクリロニトリルグラフト共重合体の加水分解物、カ
ルボキシメチルセルロール誘導体、ポリアクリル酸
(塩)架橋体、アクリル酸(塩)−ビニルアルコール共
重合体、ポリエチレンオキサイド架橋体等が知らされて
いるが、いずれのポリマーも吸水能は略良好であるが、
水への分散性、吸水速度等の点では充分とは言えない。
2. Description of the Related Art Conventionally, as a super absorbent polymer, a hydrolyzate of a starch-acrylonitrile graft copolymer, a carboxymethylcellulose derivative, a polyacrylic acid (salt) crosslinked product, an acrylic acid (salt) -vinyl Alcohol copolymers, polyethylene oxide cross-linked products, etc. are known, but all of the polymers have substantially good water absorption ability,
It is not sufficient in terms of dispersibility in water, water absorption speed, and the like.

【0003】これに対し、水への分散性、吸水速度を向
上させる方法として、親油性界面活性剤などで表面を被
覆する方法、ポリグリシジル化合物(特公昭61−48
521号公報、特公昭60−18690号公報)、シラ
ンカップリング剤(特開昭61−211305号公報、
特開昭61−252212号公報)、多価アルコール
(特公平1−17411号公報)などで表面架橋させる
方法、二酸化珪素などの無機粉体を滑剤としてポリマー
表面に分散させる方法などが知られている。しかし、い
ずれの方法によっても、吸水したゲル状態での耐久性は
無かった。
On the other hand, as a method for improving the dispersibility in water and the water absorption rate, a method of coating the surface with a lipophilic surfactant or the like, a polyglycidyl compound (Japanese Patent Publication No. 61-48).
521, JP-B-60-18690), silane coupling agents (JP-A-61-211305,
JP-A-61-252212), a method of surface-crosslinking with a polyhydric alcohol (Japanese Patent Publication No. 1-17411), a method of dispersing inorganic powder such as silicon dioxide on a polymer surface as a lubricant, and the like are known. There is. However, none of the methods had durability in a water-absorbed gel state.

【0004】一方、吸水したゲル状態での耐久性を向上
させる方法として、高吸水性ポリマーにカーボンブラッ
クまたは活性炭を含有させる方法(特開昭59−382
71号公報)、含酸素還元性無機塩を含有させる方法
(特開昭63−118375号公報)、酸化防止剤を含
有させる方法(特開昭63−127754号公報)、金
属キレート剤を含有させる方法(特開昭63−1469
64号公報)、ラジカル連鎖禁止剤を含有させる方法
(特開昭63−152667号公報)、酸化剤を含有さ
せる方法(特開昭63−153060号公報)、硫黄含
有還元剤を含有させる方法(特開昭63−272349
号公報)、多価金属酸化物を含有させる方法(特開昭6
4−29257号公報)、特定のアミン化合物を含有さ
せる方法(特開平1−275661号公報)などがあ
る。しかし、これらの方法はいずれも高吸水性ポリマー
に添加剤を加える方法であり、添加剤の安全性の点か
ら、添加剤の取扱い、ポリマーの衛生材料としての使用
などを考えると必ずしも好まれる方法ではなかった。
On the other hand, as a method for improving the durability in the gel state of absorbing water, a method of incorporating carbon black or activated carbon into a super absorbent polymer (Japanese Patent Laid-Open No. 59-382).
No. 71), a method of adding an oxygen-containing reducing inorganic salt (JP-A-63-118375), a method of adding an antioxidant (JP-A-63-127754), and a metal chelating agent. Method (JP-A-63-1469)
No. 64), a method of adding a radical chain inhibitor (JP-A-63-152667), a method of adding an oxidizing agent (JP-A-63-153060), and a method of adding a sulfur-containing reducing agent ( JP-A-63-272349
Japanese Laid-Open Patent Publication No. 6), and a method of incorporating a polyvalent metal oxide (Japanese Patent Laid-Open No. 6-242242)
4-29257), a method of incorporating a specific amine compound (JP-A-1-275661), and the like. However, all of these methods are methods of adding an additive to a superabsorbent polymer, and from the viewpoint of the safety of the additive, a method that is always preferable when considering the handling of the additive, the use of the polymer as a sanitary material, etc. Was not.

【0005】[0005]

【発明が解決しようとする課題】本発明は、上記の問題
点を改良して、処理による吸水能の低下が無く、水への
分散性、吸水速度、吸水したゲル状態での経時安定性に
優れるも高吸水性ポリマーを製造する方法を提供しよう
とするものである。
DISCLOSURE OF THE INVENTION The present invention has improved the above-mentioned problems and has no deterioration in water absorption capacity due to treatment, dispersibility in water, water absorption speed, and stability over time in a gel state absorbed by water. It is an object of the present invention to provide a method for producing an excellent superabsorbent polymer.

【0006】[0006]

【課題を解決するための手段】本発明者等は、上記の問
題点を改良する目的で鋭意研究した結果、親水性ポリマ
ーをチタンカップリング剤で処理することにより、吸水
能が低下すること無く、水への分散性、吸水速度、吸水
したゲル状態での経時安定性が改善されることを発見
し、本発明に到達したものである。即ち、本発明は、
「水溶性および/または吸水性ポリマーを水の存在下に
アルコキシチタンで処理することを特徴とする、高吸水
性ポリマーの製造法。」である。
Means for Solving the Problems As a result of intensive studies made by the present inventors for the purpose of improving the above-mentioned problems, as a result of treating a hydrophilic polymer with a titanium coupling agent, the water-absorbing ability does not decrease. It was discovered that the dispersibility in water, the water absorption rate, and the stability with time in a water-absorbed gel state were improved, and the present invention was achieved. That is, the present invention is
"A method for producing a superabsorbent polymer, which comprises treating a water-soluble and / or water-absorbent polymer with alkoxytitanium in the presence of water."

【0007】[0007]

【作用】[Action]

〈水溶性および/または吸水性ポリマー〉本発明におい
て使用される水溶性および/または吸水性ポリマーとし
ては、水を吸水出来るのもであれば特に限定はない。
<Water-soluble and / or water-absorbent polymer> The water-soluble and / or water-absorbent polymer used in the present invention is not particularly limited as long as it can absorb water.

【0008】かかるポリマーの例としては、例えば、澱
粉−アクリロニトリル共重合体の加水分解物、澱粉−
(メタ)アクリル酸(塩)共重合体、澱粉−(メタ)ア
クリル酸エステル共重合体の加水分解物、カルボキシメ
チルセルロール誘導体、ポリ(メタ)アクリル酸
(塩)、ポリビニルアルコール、(メタ)アクリル酸エ
ステル−酢酸ビニル共重合体の加水分解物、ポリエチレ
ンオキサイド等が挙げられ、それ等の1種または2種以
上を使用することが出来る。
Examples of such polymers include starch-acrylonitrile copolymer hydrolyzate, starch-
(Meth) acrylic acid (salt) copolymer, hydrolyzate of starch- (meth) acrylic acid ester copolymer, carboxymethylcellulose derivative, poly (meth) acrylic acid (salt), polyvinyl alcohol, (meth) Examples thereof include a hydrolyzate of an acrylic acid ester-vinyl acetate copolymer, polyethylene oxide, and the like, and one kind or two or more kinds of them can be used.

【0009】〈アルコキシチタン〉本発明において使用
されるアルコキシチタンとしては、分子中に反応性のア
ルコキシ基を含有する有機チタン化合物であればなんで
もよい。かかるアルコキシチタンの例としては、テトラ
メトキシチタン、テトラエトキシチタン、テトライソプ
ロポキシチタン、テトラブトキシチタン、テトラキス
(2−エチルヘキシルオキシ)チタン、テトラステアリ
ルオキシチタン、テトライソプロポキシチタンポリマ
ー、テトラブトキシチタンポリマー、ジイソプロポキシ
ビス(アセチルアセトナト)チタン、ジブトキシビス
(トリエタノールアミナト)チタン、トリブトキシチタ
ンステアレート、ジヒドロキシビス(ラクタト)チタ
ン、ジイソプロポキシチタンジステアレート等が挙げら
れ、それらの1種または2種以上を使用することが出来
る。
<Alkoxy Titanium> The alkoxy titanium used in the present invention may be any organic titanium compound having a reactive alkoxy group in the molecule. Examples of such alkoxy titanium, tetramethoxy titanium, tetraethoxy titanium, tetraisopropoxy titanium, tetrabutoxy titanium, tetrakis (2-ethylhexyloxy) titanium, tetrastearyloxy titanium, tetraisopropoxy titanium polymer, tetrabutoxy titanium polymer, Examples include diisopropoxybis (acetylacetonato) titanium, dibutoxybis (triethanolaminato) titanium, tributoxytitanium stearate, dihydroxybis (lactato) titanium, diisopropoxytitanium distearate, and one of them or Two or more kinds can be used.

【0010】本発明に使用されるアルコキシチタンの使
用量は、使用するポリマーの種類によって異なるので一
概に規定出来ないが、通常、ポリマーに対して、0.0
01〜10重量%、である。同使用量が少なすぎると改
良効果が得られなくなるし、多すぎると経済的に不利と
なり、時として吸水能が低下する場合がある。
The amount of alkoxytitanium used in the present invention varies depending on the type of polymer used and cannot be specified unconditionally, but is usually 0.0
01 to 10% by weight. If the amount used is too small, the improvement effect will not be obtained, and if it is too large, it will be economically disadvantageous and the water absorption capacity may sometimes decrease.

【0011】〈水〉本発明におけるポリマーのアルコキ
シチタンによる処理は、水の存在下で行わせることを必
須とするものである。この水の存在形態としては、ポリ
マーが予め所定量の水を含有してなるものでも、水を追
加添加してなるものでもよい。本発明における水の存在
量は、使用するポリマーおよびアルコキシチタンの種類
によって異なるので一概に規定出来ないが、通常ポリマ
ーに対して0.5〜300重量%、である。水の存在量
が少なすぎると、アルコキシチタンとの反応が有効に進
行しない。一方、多すぎると、吸水速度の向上効果が低
減して、多量のアルコキシチタンを必要とするため経済
的にも不利となる。
<Water> It is essential that the treatment of the polymer of the present invention with alkoxytitanium is carried out in the presence of water. As a form of existence of this water, the polymer may contain a predetermined amount of water in advance, or water may be additionally added. The amount of water present in the present invention varies depending on the type of polymer and the type of alkoxytitanium used and cannot be specified unconditionally, but is usually 0.5 to 300% by weight relative to the polymer. If the amount of water present is too small, the reaction with the alkoxytitanium will not proceed effectively. On the other hand, if the amount is too large, the effect of improving the water absorption rate is reduced and a large amount of alkoxytitanium is required, which is economically disadvantageous.

【0012】〈処理方法〉本発明におけるポリマーのア
ルコキシチタンによる処理は、種々の態様において実施
することが出来る。その処理態様例としては、例えば、
含水ポリマーを溶媒に分散させたスラリー状態でアルコ
キシチタンを添加する湿式法、含水ポリマーを強制撹拌
しながらアルコキシチタンを乾燥空気または窒素ガスで
噴霧する乾式法、などが挙げられる。ここで、溶媒とし
ては不活性溶媒で有ればよく、例えば、アルコール類、
エーテル類、炭化水素類を挙げることが出来る。本発明
におけるアルコキシチタンによる処理温度は、一連の条
件により異なり、一概に規定出来ないが、通常10〜1
80℃、である。アルコキシチタンにより処理されたポ
リマーは、そのまま、或いは、水分を除去して目的とす
る高吸水性ポリマーとなる。
<Treatment Method> The treatment of the polymer of the present invention with alkoxytitanium can be carried out in various modes. As an example of the processing mode, for example,
Examples thereof include a wet method in which alkoxy titanium is added in a slurry state in which a water-containing polymer is dispersed in a solvent, and a dry method in which alkoxy titanium is sprayed with dry air or nitrogen gas while forcibly stirring the water-containing polymer. Here, the solvent may be an inert solvent, for example, alcohols,
Examples thereof include ethers and hydrocarbons. The treatment temperature with the alkoxytitanium in the present invention varies depending on a series of conditions and cannot be specified unconditionally, but is usually 10 to 1
80 ° C. The polymer treated with alkoxytitanium becomes the target superabsorbent polymer as it is or after removing water.

【0013】[0013]

【実施例】本発明をより具体的に説明するため製造例、
実施例、試験法方法と試験結果を示すものである。
EXAMPLES In order to explain the present invention more specifically, production examples,
It shows an example, a test method and a test result.

【0014】製造例1 撹拌機、還流冷却機、温度計、窒素ガス導入管および滴
下ロートを付設した容量1リットルの五つ口セパラブル
丸底フラスコにシクロヘキサン318gを取り、分散剤
としてソルビタンモノステアレート(HLB4.7)
2.39gを添加して溶解させ、窒素ガスを吹き込んで
溶存酸素を追い出した。別に、コニカルビーカーにアク
リル酸116.5g及びイオン交換水55.8gを取
り、外部より氷冷しながら25%水酸化ナトリウム水溶
液181.2gを徐々に添加しカルボキシル基の70%
を中和した。これに、N,N′−メチレンビスアクリル
アミド0.082g、次亜燐酸ナトリウム1水和物0.
111g、過硫酸カリウム0.121gを溶解させ、窒
素ガスを吹き込んで溶存酸素を追い出した。ついで、こ
のモノマー水溶液を前記セパラブルフラスコに加えて分
散させ、浴温を73℃に昇温して重合反応を開始させた
後、2時間同温度に保持して重合を完結させた。続い
て、浴温を100℃に昇温し、4時間かけて共沸脱水し
た。撹拌を停止すると、湿潤ポリマー粒子が丸底フラス
コの底に沈降したので、デカンテーションでシクロヘキ
サン相と容易に分離出来た。得られた湿潤ポリマーを1
00℃にて減圧乾燥し、吸水性ポリマーAを得た。
Production Example 1 Cyclohexane (318 g) was placed in a 5-liter separable round-bottomed flask having a capacity of 1 liter equipped with a stirrer, a reflux condenser, a thermometer, a nitrogen gas introducing tube and a dropping funnel, and sorbitan monostearate was used as a dispersant. (HLB 4.7)
2.39 g was added and dissolved, and nitrogen gas was blown in to expel dissolved oxygen. Separately, take 116.5 g of acrylic acid and 55.8 g of ion-exchanged water in a conical beaker, and gradually add 181.2 g of 25% sodium hydroxide aqueous solution while cooling with ice from the outside to make 70% of carboxyl groups.
Neutralized. To this, 0.082 g of N, N'-methylenebisacrylamide, sodium hypophosphite monohydrate 0.
111 g and 0.121 g of potassium persulfate were dissolved, and nitrogen gas was blown thereinto to expel dissolved oxygen. Next, this aqueous monomer solution was added to the separable flask to disperse the solution, the bath temperature was raised to 73 ° C. to start the polymerization reaction, and the temperature was kept at the same temperature for 2 hours to complete the polymerization. Subsequently, the bath temperature was raised to 100 ° C. and azeotropic dehydration was performed for 4 hours. When the stirring was stopped, the wet polymer particles settled to the bottom of the round bottom flask, so they could be easily separated from the cyclohexane phase by decantation. 1 for the obtained wet polymer
It was dried under reduced pressure at 00 ° C to obtain a water-absorbent polymer A.

【0015】実施例1 製造例1で得た吸水性ポリマーA100gとシクロヘキ
サン100gとからなるスラリー溶液に、撹拌下水9g
を添加し、50℃にてジ−n−ブトキシビス(トリエタ
ノールアミナト)チタン1gを添加し30分間混合し
た。続いて、浴温105℃にて減圧下30分間乾燥さ
せ、高吸水性ポリマーを得た。
Example 1 9 g of water with stirring was added to a slurry solution consisting of 100 g of the water-absorbent polymer A obtained in Production Example 1 and 100 g of cyclohexane.
Was added, and 1 g of di-n-butoxybis (triethanolaminato) titanium was added at 50 ° C. and mixed for 30 minutes. Then, it was dried at a bath temperature of 105 ° C. under reduced pressure for 30 minutes to obtain a super absorbent polymer.

【0016】実施例2 吸水性ポリマーA100gとシクロヘキサン100gと
からなるスラリー溶液に、撹拌下水10gを添加し、1
0℃にてジ−i−プロポキシビス(アセチルアセトナ
ト)チタン2gを添加し30分間混合した。続いて、浴
温105℃にて減圧下30分間乾燥させ、高吸水性ポリ
マーを得た。
Example 2 To a slurry solution consisting of 100 g of water-absorbent polymer A and 100 g of cyclohexane was added 10 g of water with stirring, and 1
At 0 ° C, 2 g of di-i-propoxybis (acetylacetonato) titanium was added and mixed for 30 minutes. Then, it was dried at a bath temperature of 105 ° C. under reduced pressure for 30 minutes to obtain a super absorbent polymer.

【0017】実施例3 吸水性ポリマーA100gとシクロヘキサン100gと
からなるスラリー溶液に、撹拌下水6gを添加し、10
℃にてテトライソプロポキシチタン0.5gを添加し3
0分間混合した。続いて、浴温105℃にて減圧下30
分間乾燥させ、高吸水性ポリマーを得た。
Example 3 To a slurry solution consisting of 100 g of the water-absorbent polymer A and 100 g of cyclohexane, 6 g of water was added with stirring and 10
Add 0.5 g of tetraisopropoxy titanium at ℃ 3
Mix for 0 minutes. Then, under reduced pressure at a bath temperature of 105 ° C, 30
After being dried for a minute, a super absorbent polymer was obtained.

【0018】実施例4 吸水性ポリマーA100gとシクロヘキサン100gと
からなるスラリー溶液に、撹拌下水25gを添加し、5
0℃にてテトラ−n−ブトキシチタンのポリマー(日本
曹達株式会社製、B−4)1gを添加し30分間混合し
た。続いて、浴温105℃にて減圧下30分間乾燥さ
せ、高吸水性ポリマーを得た。
Example 4 To a slurry solution consisting of 100 g of water-absorbent polymer A and 100 g of cyclohexane was added 25 g of water with stirring, and 5
At 0 ° C., 1 g of a polymer of tetra-n-butoxytitanium (B-4, manufactured by Nippon Soda Co., Ltd.) was added and mixed for 30 minutes. Then, it was dried at a bath temperature of 105 ° C. under reduced pressure for 30 minutes to obtain a super absorbent polymer.

【0019】実施例5 吸水性ポリマーA100gとシクロヘキサン100gと
からなるスラリー溶液に、撹拌下水20gを添加し、5
0℃にてテトラステアリルオキシチタン3gを添加し3
0分間混合した。続いて、浴温105℃にて減圧下30
分間乾燥させ、高吸水性ポリマーを得た。
Example 5 20 g of water with stirring was added to a slurry solution consisting of 100 g of the water-absorbent polymer A and 100 g of cyclohexane, and 5
Add 3 g of tetrastearyloxytitanium at 0 ° C and add 3
Mix for 0 minutes. Then, under reduced pressure at a bath temperature of 105 ° C, 30
After being dried for a minute, a super absorbent polymer was obtained.

【0020】製造例2 コニカルフラスコ中にアクリル酸39.1gを外部より
冷却しつつ22.6重量%の水酸化ナトリウム水溶液7
6.5gを滴下して80%を中和を行った。ついで重合
開始剤として過硫酸カリウム0.13gを添加し室温に
て溶解させた。撹拌機、還流冷却機、温度計、窒索ガス
導入管および滴下ロートを付設した容量500mlの五
つ口セパラブル丸底フラスコにシクロヘキサン213g
と、ソルビタンモノラウリレート1.9gを添加して溶
解させた後、窒素ガスを吹き込んで溶存酸素を追い出し
た。コニカルフラスコの内容物を前記五つ口フラスコに
滴下し懸濁させ、再び系内を窒素で充分置換した後に、
昇温を行い、浴温を55〜60℃に保持して3時間重合
反応を行った。得られた重合液を減圧下で蒸発乾固する
ことにより、吸水性ポリマーBを得た。
Production Example 2 While cooling 39.1 g of acrylic acid in a conical flask from the outside, a 22.6 wt% sodium hydroxide aqueous solution 7 was added.
6.5 g was added dropwise to neutralize 80%. Then, 0.13 g of potassium persulfate was added as a polymerization initiator and dissolved at room temperature. Cyclohexane of 213 g in a five-neck separable round bottom flask with a capacity of 500 ml equipped with a stirrer, a reflux condenser, a thermometer, a nitrogen gas introducing pipe and a dropping funnel.
Then, 1.9 g of sorbitan monolaurate was added and dissolved, and then nitrogen gas was blown thereinto to expel dissolved oxygen. After the contents of the conical flask were added dropwise to the five-necked flask and suspended, and the system was sufficiently replaced with nitrogen again,
The temperature was raised and the bath temperature was maintained at 55 to 60 ° C. to carry out a polymerization reaction for 3 hours. The water-absorbent polymer B was obtained by evaporating the obtained polymerization liquid to dryness under reduced pressure.

【0021】実施例6 製造例2で得た吸水性ポリマーB100gとシクロヘキ
サン100gとからなるスラリー溶液に、撹拌下水9g
を添加し、50℃にてジ−n−ブトキシビス(トリエタ
ノールアミナト)1gを添加し30分間混合した。続い
て、浴温105℃にて減圧下30分間乾燥させ、高吸水
性ポリマーを得た。
Example 6 9 g of water with stirring was added to a slurry solution consisting of 100 g of the water-absorbent polymer B obtained in Production Example 2 and 100 g of cyclohexane.
Was added, and 1 g of di-n-butoxybis (triethanolaminato) was added at 50 ° C. and mixed for 30 minutes. Then, it was dried at a bath temperature of 105 ° C. under reduced pressure for 30 minutes to obtain a super absorbent polymer.

【0022】製造例3 アクリル酸74.95モル%、アクリル酸25モル%、
およびトリメチロールプロパントリアクリレート0.0
5モル%からなるアクリル酸塩系モノマー43重量%の
水溶液100重量部を、過硫酸アンモニウム0.015
重量部および亜硫酸水素ナトリウム0.005重量部を
用いて窒素雰囲気中55〜80℃で静置重合し、ゲル状
含水ポリマーを得た。このポリマーを180℃の熱風乾
燥機で乾燥後、ハンマー型粉砕機で粉砕し、28メッシ
ュ金網で篩分けして、28メッシュ通過物(ポリマー
C)を得た。
Production Example 3 74.95 mol% of acrylic acid, 25 mol% of acrylic acid,
And trimethylolpropane triacrylate 0.0
100 parts by weight of an aqueous solution of 43% by weight of an acrylic acid salt monomer consisting of 5 mol% was added with 0.015% of ammonium persulfate.
The polymer was allowed to stand still at 55 to 80 ° C. in a nitrogen atmosphere using parts by weight and 0.005 parts by weight of sodium hydrogen sulfite to obtain a gel-like hydropolymer. This polymer was dried with a hot air drier at 180 ° C., then pulverized with a hammer type pulverizer, and sieved with a 28 mesh wire net to obtain a 28 mesh passed product (polymer C).

【0023】実施例7 ポリマーC100gとn−ブタノール100gとからな
るスラリー溶液に、撹拌下水10gを添加し、70℃に
てジ−n−ブトキシビス(トリエタノールアミナト)チ
タン1gを添加し30分間混合した。続いて、浴温12
0℃にて減圧下60分間乾燥させ、高吸水性ポリマーを
得た。
Example 7 To a slurry solution consisting of 100 g of polymer C and 100 g of n-butanol, 10 g of water was added with stirring, and 1 g of di-n-butoxybis (triethanolaminato) titanium was added at 70 ° C. and mixed for 30 minutes. did. Then, bath temperature 12
It was dried at 0 ° C. under reduced pressure for 60 minutes to obtain a super absorbent polymer.

【0024】(試験方法) 〈吸水能〉高吸水性ポリマー約1gを精秤し、250メ
ッシュのナイロン袋(10cm×10cmの大きさ)に
入れ、500ccの人工尿に30分間浸漬する。その
後、ナイロン袋を引き上げ、15分水切りした後、重量
測定し、ブランク補正をして、高吸水性ポリマー1gが
吸水した人工尿の重量を吸水能とした。尚、人工尿の組
成は下記に示す通りである。 尿素 1.94重量% 塩化ナトリウム 0.80重量% 塩化カルシウム 0.06重量% 硫酸マグネシウム 0.11重量% 純水 97.09重量%
(Test method) <Water absorption capacity> About 1 g of a super absorbent polymer is precisely weighed, put in a 250 mesh nylon bag (10 cm x 10 cm), and immersed in 500 cc of artificial urine for 30 minutes. Then, the nylon bag was pulled up and drained for 15 minutes, then weighed and subjected to blank correction, and the weight of the artificial urine absorbed by 1 g of the superabsorbent polymer was defined as the water absorption capacity. The composition of artificial urine is as shown below. Urea 1.94% by weight Sodium chloride 0.80% by weight Calcium chloride 0.06% by weight Magnesium sulfate 0.11% by weight Pure water 97.09% by weight

【0025】〈吸水速度〉第1図に示す装置を用いて測
定した。高吸水性ポリマー1g1を小穴の開いた支持板
2の上に設けた不織布3の上に置く。下方より人工尿4
を接触させ、10分間にポリマーが吸収した人工尿の重
量をもって吸水速度とした。図1中の5は人工尿を入れ
たビューレットであり、9は空気入口であって。栓6で
封じられたビューレットの空間部が減圧されるのを防止
している。8と7はバルブであって、夫々空気量と尿量
を調節する。
<Water Absorption Rate> The water absorption rate was measured using the apparatus shown in FIG. The super absorbent polymer 1g1 is placed on the non-woven fabric 3 provided on the support plate 2 having small holes. Artificial urine from below 4
Was contacted, and the weight of the artificial urine absorbed by the polymer in 10 minutes was defined as the water absorption rate. Reference numeral 5 in FIG. 1 is a burette containing artificial urine, and 9 is an air inlet. The space in the burette enclosed by the stopper 6 is prevented from being decompressed. Reference numerals 8 and 7 are valves for adjusting the amount of air and the amount of urine, respectively.

【0026】〈水への分散性〉ビーカーに水を入れ、少
量の高吸水性ポリマーを落とした時の分散の様子を観察
し、ママコ生成の有無を目視判断した。 ○:ママコ発生せず ×:ママコができる
<Dispersibility in Water> Water was placed in a beaker, and a state of dispersion when a small amount of superabsorbent polymer was dropped was observed, and the presence or absence of mamako formation was visually judged. ○: Mamako does not occur ×: Mamako is possible

【0027】〈ゲル強度〉高吸水性ポリマー1.6gに
予め40℃に保持した人工尿40gを吸水させ、同温度
で一定時間保持後、レオメーター(不動工業NRM−2
002J型)により、セルがゲルに入り込む時点の力を
ゲル強度として測定した。
<Gel strength> 40 g of artificial urine previously held at 40 ° C. was absorbed into 1.6 g of a superabsorbent polymer, and the mixture was kept at the same temperature for a certain period of time and then a rheometer (Fudo Kogyo NRM-2
(002J type), the force at the time when the cell entered the gel was measured as the gel strength.

【0028】〈ゲルの状態〉24時間後のゲル強度を測
定した後の膨潤ゲルの状態を手触りにて測定し、下記の
三段評価を行った。 ○:膨潤ゲルはさくさくとしていてドライ感がある。 △:一部、膨潤ゲルがべとつく。 ×:膨潤ゲルがべとつき、手がぬべぬべする。 表1は、上記の実施例および実験例によって得られた高
吸水性ポリマーの吸水性能の評価結果を示すものであ
る。
<Gel state> After measuring the gel strength after 24 hours, the state of the swollen gel was measured by touch, and the following three-stage evaluation was performed. ◯: The swollen gel is crispy and has a dry feeling. Δ: Swelling gel is partly sticky. X: The swollen gel is sticky and the hands are greasy. Table 1 shows the evaluation results of the water absorption performance of the superabsorbent polymers obtained in the above Examples and Experimental Examples.

【0029】[0029]

【表1】 [Table 1]

【0030】[0030]

【発明の効果】本発明によれば、処理による吸水能の低
下が無く、水への分散性、吸水速度、吸水したゲル状態
での経時安定性に優れた高吸水性ポリマーを製造するこ
とが出来る。
EFFECTS OF THE INVENTION According to the present invention, it is possible to produce a highly water-absorbent polymer which is free from deterioration in water absorption capacity due to treatment and is excellent in dispersibility in water, water absorption speed, and stability over time in a water-absorbed gel state. I can.

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

【図1】高吸水性ポリマーの吸水速度を測定するのに使
用した装置の概略を示す説明図である。
FIG. 1 is an explanatory diagram showing an outline of an apparatus used for measuring a water absorption rate of a superabsorbent polymer.

【符号の説明】 1 高吸水性ポリマー 2 小穴の開いた支持板 3 不織布 4 人工尿 5 ビューレット 6 ゴム栓 7 バルブ 8 バルブ 9 空気入口[Explanation of symbols] 1 Super absorbent polymer 2 Support plate with small holes 3 Nonwoven fabric 4 Artificial urine 5 Viewlet 6 Rubber stopper 7 Valve 8 Valve 9 Air inlet

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 水溶性および/または吸水性ポリマーを
水の存在下にアルコキシチタンで処理することを特徴と
する、高吸水性ポリマーの製造法。
1. A method for producing a superabsorbent polymer, which comprises treating a water-soluble and / or water-absorbent polymer with alkoxytitanium in the presence of water.
【請求項2】 水を吸水性ポリマーに対し0.5〜30
0重量%存在させる、請求項1に記載された高吸水性ポ
リマーの製造法。
2. Water in an amount of 0.5 to 30 relative to the water-absorbing polymer.
The method for producing a superabsorbent polymer according to claim 1, wherein 0% by weight is present.
【請求項3】 アルコキシチタンを吸水性ポリマーに対
し0.001〜10重量%使用する、請求項1または2
に記載された高吸水性ポリマーの製造法。
3. The alkoxy titanium is used in an amount of 0.001 to 10% by weight based on the water-absorbing polymer.
The method for producing a superabsorbent polymer described in 1.
【請求項4】 アルコキシチタンによる処理が、含水吸
水性ポリマーを不活性溶剤に分散させたスラリーにアル
コキシチタンを添加し混合する湿式処理である、請求項
1ないし3のいずれか1項に記載された高吸水性ポリマ
ーの製造法。
4. The method according to claim 1, wherein the treatment with the alkoxytitanium is a wet treatment in which the alkoxytitanium is added to and mixed with a slurry in which a water-containing water-absorbing polymer is dispersed in an inert solvent. For producing super absorbent polymer.
【請求項5】 アルコキシチタンによる処理が、含水吸
水性ポリマーを撹拌しつつアルコキシシランを噴霧する
乾式処理である、請求項1ないし3のいずれか1項に記
載された高吸水性ポリマーの製造法。
5. The method for producing a superabsorbent polymer according to claim 1, wherein the treatment with the alkoxytitanium is a dry treatment in which the alkoxysilane is sprayed while stirring the hydrous water-absorbent polymer. .
JP12770393A 1993-04-21 1993-04-21 Method for producing superabsorbent polymer Expired - Lifetime JP3482535B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12770393A JP3482535B2 (en) 1993-04-21 1993-04-21 Method for producing superabsorbent polymer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12770393A JP3482535B2 (en) 1993-04-21 1993-04-21 Method for producing superabsorbent polymer

Publications (2)

Publication Number Publication Date
JPH06306118A true JPH06306118A (en) 1994-11-01
JP3482535B2 JP3482535B2 (en) 2003-12-22

Family

ID=14966622

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Link
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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5883158A (en) * 1994-08-12 1999-03-16 Kao Corporation Process for producing improved super absorbent polymer
US6313231B1 (en) 1997-07-03 2001-11-06 Kao Corporation Superabsorbent resin composition
US6448320B1 (en) 1997-01-31 2002-09-10 Kao Corporation Superabsorbent resin composition and method for producing the same
JP2016102161A (en) * 2014-11-28 2016-06-02 Sdpグローバル株式会社 Absorbent resin particle, absorber and absorbent article including the same

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5883158A (en) * 1994-08-12 1999-03-16 Kao Corporation Process for producing improved super absorbent polymer
US6448320B1 (en) 1997-01-31 2002-09-10 Kao Corporation Superabsorbent resin composition and method for producing the same
US6313231B1 (en) 1997-07-03 2001-11-06 Kao Corporation Superabsorbent resin composition
JP2016102161A (en) * 2014-11-28 2016-06-02 Sdpグローバル株式会社 Absorbent resin particle, absorber and absorbent article including the same

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