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JPS6335644B2 - - Google Patents
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JPS6335644B2 - - Google Patents

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Publication number
JPS6335644B2
JPS6335644B2 JP55057175A JP5717580A JPS6335644B2 JP S6335644 B2 JPS6335644 B2 JP S6335644B2 JP 55057175 A JP55057175 A JP 55057175A JP 5717580 A JP5717580 A JP 5717580A JP S6335644 B2 JPS6335644 B2 JP S6335644B2
Authority
JP
Japan
Prior art keywords
polymer
water
reaction
hydroxyl group
anhydride
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
Application number
JP55057175A
Other languages
Japanese (ja)
Other versions
JPS56152806A (en
Inventor
Toshihiko Yoshitake
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.)
Kuraray Co Ltd
Original Assignee
Kuraray 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
Application filed by Kuraray Co Ltd filed Critical Kuraray Co Ltd
Priority to JP5717580A priority Critical patent/JPS56152806A/en
Publication of JPS56152806A publication Critical patent/JPS56152806A/en
Publication of JPS6335644B2 publication Critical patent/JPS6335644B2/ja
Granted legal-status Critical Current

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  • Absorbent Articles And Supports Therefor (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)

Description

【発明の詳細な説明】 本発明は水酸基を含有する重合体に一価金属の
水酸化物を作用させ、水酸基の水素を全部または
部分的にアルカリ金属にした後、無水状態で環状
酸無水物を反応させて、エステル化により該重合
体にカルボキシル基および/またはその金属塩を
導入すると同時、またはその後に架橋結合を生成
せしめて得られる高吸水性重合体の製造方法に関
する。
Detailed Description of the Invention The present invention involves reacting a monovalent metal hydroxide to a polymer containing a hydroxyl group to convert all or part of the hydrogen in the hydroxyl group into an alkali metal, and then forming a cyclic acid anhydride in an anhydrous state. The present invention relates to a method for producing a superabsorbent polymer obtained by reacting a carboxyl group and/or a metal salt thereof to the polymer by esterification, and simultaneously or thereafter generating a crosslinking bond.

最近、分子内にカルボキシル基などの電離性基
を有し、かつ分子間架橋結合により網状化された
様な構造を有する高吸水性樹脂が多数提案され、
生理用ナプキン、紙オムツの吸水剤、土壌の保水
剤、脱水剤、メデイカル用途等の諸用途に使用さ
れ始めている。このような樹脂としては、デンプ
ンにアクリロニトリルをグラフト重合しニトリル
基を水和反応して得られる樹脂、デンプンにアク
リル酸をグラフト重合した樹脂、分子間架橋を有
するポリアクリル酸系樹脂などが知られている。
しかしこれらの高吸水性樹脂は、原料が高価であ
つたり、カルボキシル基の含有量が低く親水性あ
るいは吸水性が充分でなかつたり、あるいは製造
方法が煩雑であつたりして必ずしも満足すべきも
のではない。
Recently, many superabsorbent resins have been proposed that have ionizable groups such as carboxyl groups in their molecules and have a network-like structure due to intermolecular cross-linking.
It has begun to be used for various purposes such as sanitary napkins, water absorbing agents for disposable diapers, soil water retaining agents, dehydrating agents, and medical applications. Known examples of such resins include resins obtained by graft polymerizing acrylonitrile onto starch and hydrating the nitrile groups, resins obtained by graft polymerizing acrylic acid onto starch, and polyacrylic acid resins having intermolecular crosslinks. ing.
However, these super absorbent resins are not necessarily satisfactory because their raw materials are expensive, their carboxyl group content is low and their hydrophilicity or water absorption is insufficient, or their manufacturing methods are complicated. .

本発明者はこれらの問題を改良するために検討
を行ない、無水状態下にポリビニルアルコール系
重合体に環状酸無水物を反応させ、エステル化に
よりカルボキシル基を導入した重合体が、極めて
有用な親水性、水溶性を有し、また該重合体に分
子間架橋結合を生成せしるめことにより高い吸水
性能を有する重合体が得られることを見い出し、
先に特許出願を行なつた。
The present inventor conducted studies to improve these problems, and found that a polyvinyl alcohol-based polymer was reacted with a cyclic acid anhydride under anhydrous conditions, and a polymer into which carboxyl groups were introduced through esterification was an extremely useful hydrophilic polymer. discovered that a polymer with high water absorption performance can be obtained by forming intermolecular crosslinks in the polymer,
A patent application was filed first.

しかし、この際原料に用いるポリビニルアルコ
ールのけん化度が高い場合は反応が進み難いとい
う難点があつた。同様の現象は他の水酸基含有重
合体例えば各種デンプン類、多糖類、各種セルロ
ース類を用いた場合にも認められた。また、上述
の方法では導入されるカルボキシル基が酸型であ
り、得られる樹脂が酸性を呈するとともに親水
性、水溶性が充分でない等の難点があり、多くの
場合1価金属化合物、アンモニアあるいはアンモ
ニウム化合物、アミン類あるいはアミン塩類等に
よりカルボキシル基を全部または部分的に中和し
てカルボキシル基塩にする工程が必要であつた。
However, when the polyvinyl alcohol used as a raw material has a high degree of saponification, the reaction is difficult to proceed. Similar phenomena were observed when other hydroxyl group-containing polymers such as various starches, polysaccharides, and various celluloses were used. In addition, in the above-mentioned method, the carboxyl group introduced is in the acid type, and the resin obtained is acidic and has problems such as insufficient hydrophilicity and water solubility, and in many cases monovalent metal compounds, ammonia or ammonium A step of completely or partially neutralizing the carboxyl group with a compound, amine, or amine salt to form a carboxyl base salt was required.

本発明者は上述の様な難点のない環状酸無水物
による水酸基含有重合体の変性方法に関して種々
研究を重ねた結果、水酸基を含有する重合体に1
価金属の水酸化物を作用させ、水酸基の水素を全
部または部分的にアルカリ金属に置換した後、無
水状態で環状酸無水物を反応させることにより上
述の目的が達成できることを見い出し、本発明に
到つた。
As a result of repeated research on a method for modifying a hydroxyl group-containing polymer with a cyclic acid anhydride that does not have the above-mentioned difficulties, the present inventor found that
We have discovered that the above object can be achieved by reacting a hydroxide of a valent metal to replace all or part of the hydrogen in the hydroxyl group with an alkali metal, and then reacting the cyclic acid anhydride in an anhydrous state. It has arrived.

本発明において用いられる水酸基含有重合体は
分子内に水酸基を持つ合成及び天然の重合体及び
これらの変性物であり、粉末状のものだけでなく
繊維状物、フイルム状物等も包含する。例えば、
ポリビニルアルコール系重合体、コーンスター
チ、小麦デンプン、タピオカデンプン、バレイシ
ヨデンプン等の各種デンプン類あるいは酸化デン
プン、デキストリンの様な変性デンプン、グアー
ガム、ローカストビーンガム等の各種多糖類、パ
ルプ、綿、麻、サトウキビ絞り糟、ワラ等各種セ
ルロース類等を例としてあげることができる。
The hydroxyl group-containing polymer used in the present invention is a synthetic or natural polymer having a hydroxyl group in the molecule, or a modified product thereof, and includes not only powdered polymers but also fibrous materials, film materials, and the like. for example,
Polyvinyl alcohol polymers, various starches such as corn starch, wheat starch, tapioca starch, potato starch, oxidized starch, modified starches such as dextrin, various polysaccharides such as guar gum and locust bean gum, pulp, cotton, hemp, Examples include various celluloses such as sugarcane pulp and straw.

本発明に用いられる1価金属の水酸化物として
は、水酸化リチウム、水酸化ナトリウム、水酸化
カリウム等をあげることができる。これらは通
常、濃厚な水溶液の状態で水酸基含有重合体の処
理に供される。濃度は5〜50重量%の範囲が好適
であり、水溶液の使用量は樹脂に対して2〜10倍
量の範囲が好適である。
Examples of monovalent metal hydroxides used in the present invention include lithium hydroxide, sodium hydroxide, potassium hydroxide, and the like. These are usually used in the form of concentrated aqueous solutions to treat hydroxyl group-containing polymers. The concentration is preferably in the range of 5 to 50% by weight, and the amount of the aqueous solution used is preferably in the range of 2 to 10 times the amount of the resin.

本発明で用いられる環状酸無水物とは環状構造
を有する多価カルボン酸無水物であり、具体的に
は無水マレイン酸、無水コハク酸、無水グルタル
酸、無水アジピン酸、無水イタコン酸、無水フタ
ル酸、無水トリメリツト酸、テトラクロル無水フ
タル酸、テトラブロム無水フタル酸、無水ヘツト
酸等をあげることができる。これらの水酸基含有
重合体に対する使用量は重合体100重量部に対し
て10〜500重量部の範囲が好適である。
The cyclic acid anhydride used in the present invention is a polyhydric carboxylic acid anhydride having a cyclic structure, and specifically includes maleic anhydride, succinic anhydride, glutaric anhydride, adipic anhydride, itaconic anhydride, and phthalic anhydride. Acids, trimellitic anhydride, tetrachlorophthalic anhydride, tetrabromophthalic anhydride, hectic anhydride, etc. can be mentioned. The amount of these hydroxyl group-containing polymers used is preferably in the range of 10 to 500 parts by weight per 100 parts by weight of the polymer.

水酸基の水素をアルカリ金属に置換した重合体
に対する環状酸無水物の反応は通常、環状酸無水
物と反応性を有しない溶媒中で実施させる。この
様な溶媒としてはベンゼン、トルエン、キシレ
ン、ヘキサン、シクロヘキサン、アセトン、メチ
ルエチルケトン、シクロヘキサノン、テトラヒド
ロフラン、ジオキサン等をあげることができる。
また、反応の進行を容易ならしめるために、ジメ
チルスルホキシド、N―メチルモルホリン・N―
オキサイド、塩化リチウムのアセトアミド溶液の
様な膨潤剤を溶媒として用いることもでき、さら
に上記の溶媒と膨潤剤を混合して用いることもで
きる。これらの使用量は重合体に対して2〜10倍
量の範囲が好適である。
The reaction of a cyclic acid anhydride with a polymer in which hydrogen in a hydroxyl group is replaced with an alkali metal is usually carried out in a solvent that does not have reactivity with the cyclic acid anhydride. Examples of such solvents include benzene, toluene, xylene, hexane, cyclohexane, acetone, methyl ethyl ketone, cyclohexanone, tetrahydrofuran, dioxane, and the like.
In addition, in order to facilitate the progress of the reaction, dimethyl sulfoxide, N-methylmorpholine/N-
A swelling agent such as an acetamide solution of oxide or lithium chloride can be used as a solvent, or a mixture of the above-mentioned solvent and swelling agent can also be used. The amount of these used is preferably in the range of 2 to 10 times the amount of the polymer.

本発明における水酸基含有重合体に対する1価
金属の水酸化物の反応は、通常該重合体を1価金
属の水酸化物の水溶液に浸漬または分散すること
により実施され、必要に応じて撹拌を行なう。処
理温度は室温〜100℃の範囲が好適であり、処理
時間は数分〜数時間の範囲が好適である。反応
後、水溶液は傾斜、濾過、遠心分離、圧搾等の方
法により除かれ、重合体中の残存水分は風乾、加
熱乾燥、真空乾燥等により除去する。水分は可及
的に完全に除去するのが好ましい。水分が残存す
ると次の工程において環状酸無水物と反応し、カ
ルボン酸を副生するので好ましくない。水酸基の
水素のアルカリ金属置換度は、アルカリ水溶液の
量、濃度、処理温度、時間等をコントロールする
ことにより所望の置換度のものを得ることができ
る。通常、置換度は10〜100モル%の範囲が好適
である。
The reaction of a monovalent metal hydroxide with a hydroxyl group-containing polymer in the present invention is usually carried out by immersing or dispersing the polymer in an aqueous solution of a monovalent metal hydroxide, and stirring is performed as necessary. . The treatment temperature is preferably in the range of room temperature to 100°C, and the treatment time is preferably in the range of several minutes to several hours. After the reaction, the aqueous solution is removed by methods such as decanting, filtration, centrifugation, and squeezing, and the remaining moisture in the polymer is removed by air drying, heat drying, vacuum drying, and the like. It is preferable to remove moisture as completely as possible. If water remains, it is not preferable because it will react with the cyclic acid anhydride in the next step and produce carboxylic acid as a by-product. The desired degree of substitution of hydrogen in the hydroxyl group with an alkali metal can be obtained by controlling the amount, concentration, treatment temperature, time, etc. of the aqueous alkali solution. Usually, the degree of substitution is preferably in the range of 10 to 100 mol%.

次の段階の環状酸無水物との反応は、前記溶媒
中に重合体を浸漬あるいは分散させ、次いで所望
量の環状酸無水物を添加、溶解し、加温、撹拌す
る方法が一般的である。反応は終始不均一系で進
行するので、水酸基含有重合体が可及的に均質に
変性される様撹拌下に実施するのが望ましい。反
応は重合体中のアルカリ金属置換水酸基あるいは
酸型の水酸基がエステル化されることにより起こ
り、重合体側鎖にカルボキシル基(塩)が導入さ
れる。このとき反応温度、反応時間、エステル化
度、環状酸無水物の種類等を適当に選ぶことによ
り、ジエステル化反応も同時に行なわせて、分子
間架橋結合を導入することができる。また、場合
によつては、架橋結合を含まない重合体を製造
し、該重合体を加熱処理して架橋結合を導入する
こともできる。このとき、多官能エポキシ化合
物、多官能イソシアネート、多価金属化合物、多
価アミン類、多官能メチロール化合物(ジメチロ
ール尿素、メチロールメラミン等)を架橋剤とし
て用いることもできる。加熱処理は、反応混合物
をそのままあるいは反応混合物より樹脂を分離
し、そのままの状態または何等かの成形をほどこ
した後、50〜200℃、好ましくは80〜150℃に加熱
して行なう。加熱時間は通常、数分〜数時間であ
り、一高分子あたり1ケ〜数十ケの架橋結合を生
成する様に加熱温度、時間を選択するのが好まし
い。吸水性能は架橋密度によつて著しく左右され
るので、所望の吸水能が得られる様に架橋密度を
コントロールするのが好ましい。重合体と環状酸
無水物との反応の進行とともに、通常樹脂が膨潤
肥大化してくるので、反応状況をある程度肉眼で
観察することができる。反応はほぼ定量的に進む
ので、環状酸無水物は重合体を所望のエステル化
度にするにの必要な量程度を使用すればよい。エ
ステル化度は通常10〜100モル%の範囲が好適で
ある。反応温度は通常30〜200℃、好ましくは50
〜150℃の範囲である。反応時間は通常10分〜10
時間、好ましくは1〜5時間の範囲である。
The next step of reaction with the cyclic acid anhydride is generally carried out by immersing or dispersing the polymer in the solvent, then adding and dissolving the desired amount of the cyclic acid anhydride, heating, and stirring. . Since the reaction proceeds in a heterogeneous system throughout, it is desirable to carry out the reaction under stirring so that the hydroxyl group-containing polymer is modified as homogeneously as possible. The reaction occurs when the alkali metal-substituted hydroxyl group or acid type hydroxyl group in the polymer is esterified, and a carboxyl group (salt) is introduced into the side chain of the polymer. At this time, by appropriately selecting the reaction temperature, reaction time, degree of esterification, type of cyclic acid anhydride, etc., it is possible to simultaneously carry out the diesterification reaction and introduce intermolecular cross-linking. In some cases, it is also possible to produce a polymer that does not contain crosslinks and heat-treat the polymer to introduce crosslinks. At this time, polyfunctional epoxy compounds, polyfunctional isocyanates, polyvalent metal compounds, polyvalent amines, polyfunctional methylol compounds (dimethylol urea, methylol melamine, etc.) can also be used as crosslinking agents. The heat treatment is carried out by heating the reaction mixture as it is, or after separating the resin from the reaction mixture and subjecting it to some form of molding, to 50 to 200°C, preferably 80 to 150°C. The heating time is usually several minutes to several hours, and the heating temperature and time are preferably selected so as to form one to several dozen crosslinks per polymer. Since the water absorption performance is significantly influenced by the crosslink density, it is preferable to control the crosslink density so as to obtain the desired water absorption capacity. As the reaction between the polymer and the cyclic acid anhydride progresses, the resin usually swells and becomes enlarged, making it possible to observe the reaction situation with the naked eye to some extent. Since the reaction proceeds almost quantitatively, the cyclic acid anhydride may be used in an amount necessary to bring the polymer to the desired degree of esterification. The degree of esterification is usually preferably in the range of 10 to 100 mol%. The reaction temperature is usually 30-200℃, preferably 50℃
~150℃ range. Reaction time is usually 10 minutes to 10
time, preferably in the range of 1 to 5 hours.

通常、反応後の反応混合物は、膨潤した変性樹
脂が溶媒に分散した状態を呈しているので、濾
過、遠心分離等の方法により樹脂部を分離し、濾
液は回収して再使用に供することができる。樹脂
は最後に洗浄、乾燥を行なう。
Usually, the reaction mixture after the reaction is in a state where the swollen modified resin is dispersed in the solvent, so it is possible to separate the resin part by methods such as filtration or centrifugation, and collect the filtrate for reuse. can. Finally, the resin is washed and dried.

上述の様にして得られた変性樹脂は、通常白色
または淡黄色の粉末状、繊維状、フイルム状など
であり、分子間架橋されたものは自重の数倍〜数
百倍の水を数秒〜数分で吸収する優れた吸水性能
を有している。従つて分子間架橋されたものは生
理用ナプキンや紙オムツ用の吸水剤、各種有機溶
媒や石油中の水分の脱水、各種エマルジヨンの脱
水濃縮、土壌の保水剤、消火用、医料用途等に広
い需要を有することが期待される。
The modified resin obtained as described above is usually in the form of a white or pale yellow powder, fiber, film, etc., and intermolecularly crosslinked resin is soaked in several times to hundreds of times its own weight of water for several seconds. It has excellent water absorption ability, absorbing water within minutes. Therefore, intermolecularly cross-linked products can be used as water-absorbing agents for sanitary napkins and disposable diapers, for dehydration of water in various organic solvents and petroleum, for dehydration and concentration of various emulsions, as water retention agents for soil, for fire extinguishing purposes, for medical purposes, etc. It is expected to have wide demand.

以下実施例により本発明をさらに詳細に説明す
るが、本発明はかかる実施例にのみ限定されるも
のではない。
The present invention will be explained in more detail with reference to Examples below, but the present invention is not limited only to these Examples.

実施例 1 ポリビニルアルコール粉末(重合度1700、けん
化度99モル%、粒度100〜200メツシユ)50gを
500c.c.広口瓶に入れ、18%水酸化ナトリウム水溶
液400c.c.に室温で1時間浸漬し、遠心機によりで
きるだけ脱液した。得られたマーセル化ポリビニ
ルアルコールを40℃で減圧乾燥して可及的に水分
を除いた。次に500c.c.三つ口セパラブルフラスコ
に上記のマーセル化ポリビニルアルコールを全量
入れ、無水マレイン酸30g、ジメチルスルホキシ
ド10c.c.、トルエン190c.c.を入れて120℃で3時間撹
拌反応せしめた。反応は懸濁系で進行した。反応
混合物を濾過し、乾燥後秤量した。収量は88gで
あつた。
Example 1 50 g of polyvinyl alcohol powder (polymerization degree 1700, saponification degree 99 mol%, particle size 100-200 mesh)
It was placed in a 500 c.c. wide mouth bottle, immersed in 400 c.c. of an 18% aqueous sodium hydroxide solution for 1 hour at room temperature, and as much liquid as possible was removed using a centrifuge. The obtained mercerized polyvinyl alcohol was dried under reduced pressure at 40°C to remove as much moisture as possible. Next, put all of the above mercerized polyvinyl alcohol into a 500 c.c. three-necked separable flask, add 30 g of maleic anhydride, 10 c.c. of dimethyl sulfoxide, and 190 c.c. of toluene, and stir the reaction at 120°C for 3 hours. I forced it. The reaction proceeded in a suspension system. The reaction mixture was filtered, dried and weighed. The yield was 88g.

この変性PVA粉末1gを水1に加え、充分
吸水させた。(5分でほぼ吸水平衡に到達した。)
濾紙を軽く接触させて余剰の付着水を除去した
後、吸水ゲルの重量を測定したところ、200gで
あつた。変性PVA1gが200倍の水を極めてすみ
やかに吸収するという優れた吸水性能を示した。
1 g of this modified PVA powder was added to 1 portion of water, and the water was sufficiently absorbed. (Water absorption equilibrium was almost reached in 5 minutes.)
After lightly touching the gel with filter paper to remove excess adhering water, the weight of the water-absorbing gel was measured and found to be 200 g. One gram of modified PVA showed excellent water absorption performance, absorbing 200 times more water extremely quickly.

実施例 2 500c.c.広口瓶にグアーガム50gを入れ、15%水
酸化ナトリウム水溶液400c.c.を入れ、室温で1時
間静置反応させた。反応混合物を遠心分離して充
分に脱液し、固形部を40℃で減圧乾燥した。
Example 2 50 g of guar gum was placed in a 500 c.c. wide-mouthed bottle, 400 c.c. of a 15% aqueous sodium hydroxide solution was added thereto, and the mixture was left to react at room temperature for 1 hour. The reaction mixture was centrifuged to thoroughly remove the liquid, and the solid portion was dried under reduced pressure at 40°C.

500c.c.三つ口セパラブルフラスコに上記のマー
セル化グアーガム55g、無水フタル酸30g、N―
メチルモルホリン・N―オキサイド20c.c.、キシレ
ン180c.c.を入れ、撹拌下130℃で4時間反応させ、
カルボキシル基の導入と分子間架橋結合を同時に
行なつた。反応混合物を濾過し、固形部をメタノ
ールで洗浄、濾過して乾燥、秤量し、淡黄色粉末
状の樹脂84gを得た。
In a 500c.c. three-neck separable flask, 55g of the above mercerized guar gum, 30g of phthalic anhydride, N-
Add 20 c.c. of methylmorpholine/N-oxide and 180 c.c. of xylene and react at 130°C for 4 hours with stirring.
Introduction of carboxyl groups and intermolecular cross-linking were performed simultaneously. The reaction mixture was filtered, and the solid portion was washed with methanol, filtered, dried, and weighed to obtain 84 g of a light yellow powdery resin.

得られた樹脂は架橋結合を有しているので水、
熱水共に不溶であるが、数分内で自重の250倍の
水を吸収する性能を有していた。また、人工尿
(尿素;1.94%、NaCl;0.80%、MgSO4
7H2O;0.11%、CaCl2;0.06%)の吸液性は自重
の80倍であつた。
The obtained resin has cross-linked bonds, so water,
Although it is insoluble in hot water, it has the ability to absorb 250 times its own weight in water within a few minutes. In addition, artificial urine (urea; 1.94%, NaCl; 0.80%, MgSO4 .
The liquid absorption of 7H 2 O (0.11%, CaCl 2 (0.06%)) was 80 times its own weight.

これに対し、デンプンにアクリロニトリルをグ
ラフトし、次いで加水反応して製造された市販の
高吸水性樹脂は、水の吸水率は200倍であつたが、
人工尿の吸液率は30倍であつた。したがつて本実
施例の樹脂は紙オムツ、生理用ナプキンの吸水剤
として極めて有用なものである。
On the other hand, a commercially available super absorbent resin produced by grafting acrylonitrile onto starch and then adding water had a water absorption rate of 200 times higher.
The absorption rate of artificial urine was 30 times higher. Therefore, the resin of this example is extremely useful as a water-absorbing agent for paper diapers and sanitary napkins.

実施例 3 1000c.c.広口瓶に綿状パルプ100gを入れ、18%
水酸化カリウム水溶液800c.c.を入れて室温で1時
間静置して反応させた。反応混合物を遠心分離し
て充分に脱液し、固形部を40℃で減圧乾燥して可
及的に水分除去した。
Example 3 Put 100g of cotton pulp into a 1000c.c. wide-mouth bottle and add 18%
800 c.c. of potassium hydroxide aqueous solution was added and allowed to stand at room temperature for 1 hour to react. The reaction mixture was centrifuged to thoroughly remove liquid, and the solid portion was dried under reduced pressure at 40°C to remove as much water as possible.

次に500c.c.広口瓶に上記のマーセル化パルプ全
量と無水フタル酸100g、N―メチルモルホリ
ン・N―オキサイド80c.c.、キシレン720c.c.を入れ、
130℃で5時間無撹拌で反応せしめ、カルボキシ
ル基の導入とジエステル架橋を同時に行ない、反
応混合物を濾過し、樹脂部をメタネールで洗浄
し、乾燥、秤量して淡黄色の繊維状物230gを得
た。
Next, put the entire amount of the above mercerized pulp, 100 g of phthalic anhydride, 80 c.c. of N-methylmorpholine/N-oxide, and 720 c.c. of xylene into a 500 c.c. wide-mouthed bottle.
The reaction was allowed to proceed at 130°C for 5 hours without stirring to simultaneously introduce carboxyl groups and diester crosslinking, filter the reaction mixture, wash the resin with methanol, dry and weigh to obtain 230 g of pale yellow fibrous material. Ta.

得られた変性パルプは架橋しているので水、熱
水共に不溶であるが、数分内で自重の80倍の水を
吸収する能力を有しており、吸水状態においても
繊維状を保つていた。また、未処理の綿状パルプ
と混合してシート化すると良好な吸水材になり、
紙オムツ、生理用ナプキン等に好適であつた。
The resulting modified pulp is cross-linked and therefore insoluble in both water and hot water, but it has the ability to absorb 80 times its own weight in water within a few minutes, and maintains its fibrous form even when it absorbs water. Ta. Also, when mixed with untreated cotton pulp and made into a sheet, it becomes a good water absorbing material.
It was suitable for paper diapers, sanitary napkins, etc.

Claims (1)

【特許請求の範囲】[Claims] 1 水酸基を含有する重合体に1価金属の水酸化
物を作用させ、水酸基の水素を全部または部分的
にアルカリ金属に置換した後、無水状態で環状酸
無水物を反応させてエステル化により該重合体に
カルボキシル基および/またはその金属塩を導入
すると同時またはその後に架橋結合を生成せしめ
ることを特徴とする高吸水性重合体の製造方法。
1. A monovalent metal hydroxide is applied to a polymer containing a hydroxyl group to completely or partially replace the hydrogen of the hydroxyl group with an alkali metal, and then a cyclic acid anhydride is reacted in an anhydrous state to form a monovalent metal by esterification. 1. A method for producing a highly water-absorbing polymer, which comprises introducing a carboxyl group and/or a metal salt thereof into the polymer and generating a crosslink at the same time or after that.
JP5717580A 1980-04-28 1980-04-28 Production of polymeric material Granted JPS56152806A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5717580A JPS56152806A (en) 1980-04-28 1980-04-28 Production of polymeric material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5717580A JPS56152806A (en) 1980-04-28 1980-04-28 Production of polymeric material

Publications (2)

Publication Number Publication Date
JPS56152806A JPS56152806A (en) 1981-11-26
JPS6335644B2 true JPS6335644B2 (en) 1988-07-15

Family

ID=13048193

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5717580A Granted JPS56152806A (en) 1980-04-28 1980-04-28 Production of polymeric material

Country Status (1)

Country Link
JP (1) JPS56152806A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE4442606C2 (en) * 1994-11-30 1998-09-17 Degussa Swellable starch ester, process for its production and use
EP4335890A4 (en) * 2021-07-09 2024-10-02 Lg Chem, Ltd. BIODEGRADABLE SUPERABSORBENT POLYMER AND PROCESS FOR ITS PREPARATION

Also Published As

Publication number Publication date
JPS56152806A (en) 1981-11-26

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