JPS6051489B2 - Manufacturing method of polyvinyl alcohol hydrogel - Google Patents

Manufacturing method of polyvinyl alcohol hydrogel

Info

Publication number
JPS6051489B2
JPS6051489B2 JP3457478A JP3457478A JPS6051489B2 JP S6051489 B2 JPS6051489 B2 JP S6051489B2 JP 3457478 A JP3457478 A JP 3457478A JP 3457478 A JP3457478 A JP 3457478A JP S6051489 B2 JPS6051489 B2 JP S6051489B2
Authority
JP
Japan
Prior art keywords
polyvinyl alcohol
water
reaction
polymer
soluble
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
JP3457478A
Other languages
Japanese (ja)
Other versions
JPS54125287A (en
Inventor
敏彦 吉武
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 JP3457478A priority Critical patent/JPS6051489B2/en
Publication of JPS54125287A publication Critical patent/JPS54125287A/en
Publication of JPS6051489B2 publication Critical patent/JPS6051489B2/en
Expired legal-status Critical Current

Links

Landscapes

  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
  • Macromonomer-Based Addition Polymer (AREA)

Description

【発明の詳細な説明】 本発明はポリビニルアルコール系含水ゲルの製造に関す
る。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to the production of a polyvinyl alcohol-based hydrogel.

さらに詳しくはラジカル重合性あるいは共重合性の不飽
和結合を有する環状化合物、不飽和アルデヒドからなる
群から選ばれた1つの化合物とポリビニルアルコール系
重合体との反応により得られた側鎖に二重結合を有する
変性ポリビニルアルコール系重合体を単独もしくは水溶
性不飽和単量体と共に水に溶解し、これに水溶性のラジ
カル重合触媒単独もしくは該触媒と水溶性ラジカル重合
促進剤とを添加し、常温下あるいは加熱下に重合架橋せ
しめることを特徴とするポリビニルアルコール系含水ゲ
ルの製造方法に関する。従来、ポリビニルアルコールの
含水ゲルの製造方法としてはポリビニルアルコール水溶
液を冷凍ゲル化させる方法あるいは硼砂等の添加により
ゲル化せしめる方法などが知られているが、前者につい
ては冷凍設備を必要とする上ゲル化させるのにかなり長
時間を必要とする等の難点があり、後者についてはゲル
化速度が余りにも速過ぎるため型に流し込んだり、基材
の表面にコートするような方法などによつて所望の形態
に成型することがむつカルいといつた難点があつた。本
発明者等はこのような難点のないポリビニルアルコール
系含水ゲルの製造法について種々研究を重ねた結果、ラ
ジカル重合性あるいは共重合性の不飽和結合を有する環
状化合物、不飽和アルデヒドなる群から選ばれた1つの
化合物とポリビニルアルコール系重合体との反応により
得られた側鎖に二重結合を有する変性ポリビニルアルコ
ール系重合体を単独もしくは水溶性不飽和単量体と共に
水に溶解し、これに水溶性のラジカル重合触媒単独もし
くは該触媒と水溶性ラジカル重合促進剤とを添加し、常
温下あるいは加熱下に重合架橋せしめる方法を見出し本
発明を完成するに到つたも’のである。
More specifically, the side chain obtained by reacting one compound selected from the group consisting of radically polymerizable or copolymerizable unsaturated bonds and unsaturated aldehydes with a polyvinyl alcohol polymer has double A modified polyvinyl alcohol-based polymer having a bond is dissolved in water alone or together with a water-soluble unsaturated monomer, a water-soluble radical polymerization catalyst alone or a water-soluble radical polymerization catalyst is added thereto, and the mixture is heated at room temperature. The present invention relates to a method for producing a polyvinyl alcohol hydrogel, which is characterized by polymerization and crosslinking under heating or under heating. Conventionally, known methods for producing hydrogels of polyvinyl alcohol include a method of freezing an aqueous solution of polyvinyl alcohol into a gel, or a method of gelling it by adding borax, etc. However, the former method requires refrigeration equipment. There are some disadvantages, such as the fact that it takes quite a long time for the gelation to occur, and in the latter case, the gelation speed is too fast, so it is difficult to obtain the desired result by pouring it into a mold or coating it on the surface of the base material. The problem was that it was difficult to mold it into the desired shape. The present inventors have conducted various studies on methods for producing polyvinyl alcohol-based hydrogels that do not have these drawbacks, and as a result, they have developed a method for producing polyvinyl alcohol-based hydrogels that is free from these difficulties. A modified polyvinyl alcohol polymer having a double bond in the side chain obtained by the reaction of one compound obtained by the reaction with a polyvinyl alcohol polymer is dissolved in water alone or together with a water-soluble unsaturated monomer. The present invention was completed by discovering a method of polymerizing and crosslinking at room temperature or heating by adding a water-soluble radical polymerization catalyst alone or a water-soluble radical polymerization promoter together with the catalyst.

本発明の方法によれば原料ポリビニルアルコール系重合
体の重合度、けん化度、変性剤の種類、変性度、溶液濃
度、水溶性不飽和単量体の種類、添加量、重合触媒の種
類、量、ゲル化温度等を適・宜調節することにより所望
のゲル化速度て所望のゲル強度の含水ゲルを容易に製造
し得る。
According to the method of the present invention, the degree of polymerization of the raw material polyvinyl alcohol polymer, the degree of saponification, the type of modifier, the degree of modification, the solution concentration, the type and amount of water-soluble unsaturated monomer added, the type and amount of the polymerization catalyst By appropriately adjusting the gelling temperature and the like, it is possible to easily produce a hydrogel having a desired gelling rate and a desired gel strength.

本発明において使用される変性ポリビニルアルコール系
重合体の構成原料として用いられるポリビニルアルコー
ル系重合体は酢酸ビニル、その他の各種ビニルエステル
類の重合体及びこれらの共重合体をけん化して得られる
けん化度50モル%以上のもの、酢酸ビニルその他の各
種ビニルエステル類に対して30モル%以下の各種不飽
和単量体、例えばα−オレフィン類、塩化ビニル、アク
リロニトリル、アクリルアミド、アクリル酸エステル類
、メタクリル酸エステル類を共重合せしめた共重合体の
けん化度50モル%以上のものも包含される。
The polyvinyl alcohol polymer used as a constituent raw material of the modified polyvinyl alcohol polymer used in the present invention has a degree of saponification obtained by saponifying vinyl acetate, other various vinyl ester polymers, and copolymers thereof. 50 mol% or more, various unsaturated monomers of 30 mol% or less based on vinyl acetate and other various vinyl esters, such as α-olefins, vinyl chloride, acrylonitrile, acrylamide, acrylic esters, methacrylic acid Copolymers prepared by copolymerizing esters and having a saponification degree of 50 mol% or more are also included.

反応に供されるこれらのポリビニルアルコール系重合体
の重合度は100〜5000の範囲のものが好適であり
、またかかる重合体の形態は粉末状のものが好ましい。
一方、本発明において使用される変性ポリビニルアルコ
ール系重合体の他の1つの構成原料であるラジカル重合
性あるいは共重合性の不飽和結合を有する環状化合物と
しては例えば、無水マレイン酸、無水イタコン酸、ジケ
テン等を、また不飽和アルデヒドとしてはアクロレイン
、クロトンアルデヒド等が好ましくはあげられ、場合に
よつてはこれらを適当に混合して用いることも可能であ
る。
The degree of polymerization of these polyvinyl alcohol polymers to be subjected to the reaction is preferably in the range of 100 to 5,000, and the form of the polymer is preferably a powder.
On the other hand, examples of cyclic compounds having radically polymerizable or copolymerizable unsaturated bonds, which are other constituent raw materials of the modified polyvinyl alcohol polymer used in the present invention, include maleic anhydride, itaconic anhydride, Preferred examples include diketene, and unsaturated aldehydes such as acrolein and crotonaldehyde. In some cases, it is also possible to use a suitable mixture of these.

前記環状化合物とポリビニルアルコール系重合体との反
応は可及的に水分の存在しない状態で実施する必要があ
るが、反応の溶媒としても環状化合物と反応性を有する
活性水素を持つ様な化合物は不適当であり、活性水素を
有せざる化合物例えば、ベンゼン,トルエン,ヘキサン
,アセトン,メチルエチルケトン,テトラヒドロフラン
,ジオキサン等が用いられる。等に、トルエン,ジオキ
サン等は好適である。可溶性の変性ポリビニルアルコー
ル系重合体を得る方法としては次の三jつの方法がある
。(1)ポリビニルアルコール系重合体に例えば重炭酸
ソーダ、トリエチルアミンの如き触媒の存在下または不
存在下に不飽和環状化合物を反応させる。
The reaction between the cyclic compound and the polyvinyl alcohol polymer must be carried out in the absence of moisture as much as possible, but compounds with active hydrogen that are reactive with the cyclic compound can also be used as reaction solvents. Unsuitable compounds having no active hydrogen, such as benzene, toluene, hexane, acetone, methyl ethyl ketone, tetrahydrofuran, dioxane, etc., are used. For example, toluene, dioxane, etc. are suitable. There are the following three methods for obtaining a soluble modified polyvinyl alcohol polymer. (1) A polyvinyl alcohol polymer is reacted with an unsaturated cyclic compound in the presence or absence of a catalyst such as sodium bicarbonate or triethylamine.

c(2)
ポリビニルアルコール系重合体に一価金属の水酸化物、
アルコキシド、塩類等の存在下に不飽和環状化合物を反
応させる。但し、一価金属の水酸化物、アルコキシド、
塩類等の添加量は、不飽和環状化合物と当量以下である
。 4(3) ポリビニルアルコール系重合体に触媒
の存在下又は不存在下て不飽和環状化合物を反応させ、
次いで一価金属の水酸化物、アルコキシド塩類、アンモ
ニウム塩、アミン類アミン塩類で処理する。処理はこれ
らの化合物を水、その他の溶媒に溶解して変性ポリビニ
ルアルコール粉末と接触させ、カルボキシル基を中和す
るか、あるいは反応した不飽和環状化合物と当量以下の
これらの化合物、変性ポリビニルアルコール樹脂に単に
混合することにより行うことができる。
c(2)
Polyvinyl alcohol polymer with monovalent metal hydroxide,
An unsaturated cyclic compound is reacted in the presence of an alkoxide, salt, etc. However, monovalent metal hydroxides, alkoxides,
The amount of salts etc. added is equal to or less than the amount of the unsaturated cyclic compound. 4(3) Reacting an unsaturated cyclic compound with a polyvinyl alcohol polymer in the presence or absence of a catalyst,
Then, it is treated with a monovalent metal hydroxide, alkoxide salt, ammonium salt, or amine salt. The treatment involves dissolving these compounds in water or other solvents and bringing them into contact with modified polyvinyl alcohol powder to neutralize the carboxyl groups, or by dissolving these compounds or modified polyvinyl alcohol resin in an amount equivalent to or less than the reacted unsaturated cyclic compound. This can be done by simply mixing.

上述の反応は所定量の溶媒に、所定量の不飽和環状化合
物を溶解し、所定量のポリビニルアルコフール系重合体
、触媒、添加剤等を添加し、攪拌分散せしめ、所定温度
で、所定時間加熱攪拌する。
The above reaction involves dissolving a predetermined amount of an unsaturated cyclic compound in a predetermined amount of a solvent, adding a predetermined amount of a polyvinylalcofur polymer, a catalyst, additives, etc., stirring and dispersing the mixture, and heating at a predetermined temperature for a predetermined period of time. Heat and stir.

反応はいずれも不均一系で進行するのでポリビニルアル
コール系重合体粉末が均一に変性されるように充分攪拌
しながら行なうことが好ましい。ま7た反応温度は30
〜150′C好ましくは50〜100℃であり、反応時
間は3紛〜1時間好ましくは1〜5時間である。不飽和
環状化合物による変性は変性度1〜100モル%の範囲
内で随意可能であるが、不飽和環状化合物の使用量は所
望の変性度にするのノに必要な量以上であることを要す
る。本発明の目的に対して使用される変性ポリビニルア
ルコールの変性度は5〜50モル%のものが特に好適で
ある。また変性反応時の溶媒の使用量はポリビニルアル
コール系重合体粉末の2〜5倍量が好適であり、反応混
合物は沖過、遠心分離等の方法により固形分を分離した
後沖液は回収工程に移され、反応に用いた溶媒は再使用
に供される。分離された固形分はメタノール,アセトン
等で洗滌され、乾燥される。一方前述した不飽和アルデ
ヒドとポリビニルアルコール系重合体との反応は(1)
ポリビニルアルコール系重合体を水に溶解した後、前記
アルデヒド類、触媒等を加えて均一系て反応させる。
Since all reactions proceed in a heterogeneous system, it is preferable to carry out the reaction with sufficient stirring so that the polyvinyl alcohol polymer powder is uniformly modified. Also, the reaction temperature is 30
-150'C, preferably 50-100C, and reaction time is 3 to 1 hour, preferably 1 to 5 hours. Modification with an unsaturated cyclic compound can be carried out at will within the range of degree of modification from 1 to 100 mol%, but the amount of unsaturated cyclic compound used must be at least the amount necessary to achieve the desired degree of modification. . The degree of modification of the modified polyvinyl alcohol used for the purpose of the present invention is particularly preferably from 5 to 50 mol%. In addition, the amount of solvent used during the modification reaction is preferably 2 to 5 times the amount of polyvinyl alcohol polymer powder. The solvent used in the reaction is reused. The separated solids are washed with methanol, acetone, etc., and dried. On the other hand, the reaction between the aforementioned unsaturated aldehyde and polyvinyl alcohol polymer is (1)
After dissolving the polyvinyl alcohol polymer in water, the above-mentioned aldehydes, a catalyst, etc. are added and reacted in a homogeneous system.

(2)ポリビニルアルコール系重合体粉末をアルコール
等の溶媒中に分散させ、前記アルデヒド類、触媒等を加
えて不均一系で反応させるなどの方法で行なうことがで
きる。反応温度は30〜100C1反応時間は30分〜
10時間、触媒としては塩酸、硫酸等が使用され、変性
度は5〜50モル%が好適である。
(2) The reaction can be carried out by dispersing polyvinyl alcohol polymer powder in a solvent such as alcohol, adding the aldehydes, a catalyst, etc., and reacting in a heterogeneous system. Reaction temperature is 30~100C1 reaction time is 30 minutes~
For 10 hours, hydrochloric acid, sulfuric acid, etc. are used as a catalyst, and the degree of modification is preferably 5 to 50 mol%.

反応混合物は前述した(1)の均一系反応による場合は
沈澱剤を加えて重合体を沈澱させた後、枦過,洗滌,乾
燥される。
In the case of the above-mentioned homogeneous reaction (1), the reaction mixture is filtered, washed and dried after adding a precipitant to precipitate the polymer.

(2)不均一系の場合は沖過,遠心分離等の方法により
固形分を分離し枦液は回収して再使用に供され、一方固
形分はメタノール,アセトン等で洗滌して乾燥される。
以上の如くして得られた側鎖に二重結合を有する変性ポ
リビニルアルコール系重合体は本発明においては通常1
〜5鍾量%の濃度に水、その他の溶媒に溶解して使用さ
れる。
(2) In the case of a heterogeneous system, the solid content is separated by methods such as filtration or centrifugation, and the liquid is collected and reused, while the solid content is washed with methanol, acetone, etc. and dried. .
In the present invention, the modified polyvinyl alcohol polymer having a double bond in the side chain obtained as described above is usually used in 1
It is used by dissolving it in water or other solvents to a concentration of ~5% by weight.

これらの変性ポリビニルアルコール系重合体と併用され
る水溶性不飽和単量体としてはアクリルアミド,アクリ
ル酸,アクリル酸塩,ビニルピロリドン,ヒドロキシエ
チルアクリレート,ビニルピリジン塩等をあげることが
出来、これらは勿論混合して用いることも可能である。
これらの水溶性不飽和単量体の使用量は変性ポリビニル
アルコール系重合体の1〜50重量%を置き変えて使用
することが出来る。本発明において使用される水溶性ラ
ジカル重合触媒としては過酸化水素,過硫酸カリ,過硫
酸アンモン等をあげることが出来る。これらの触媒の使
用量は変性ポリビニルアルコール系重合体単独あるいは
該重合体と水溶性不飽和単量体との混合物の水溶液に対
して0.001〜10重量%程度である。更に該触媒と
共に使用される水溶性ラジカル重合促進剤としてはロン
ガリツト,第1鉄塩,酸性亜硫酸ソーダ,チオ硫酸ソー
ダ等があげられ、これらの使用量は前記水溶液に対して
0.001〜10重量%程度である。これら重合触媒と
重合促進剤とを使用する場合には前記変性ポリビニルア
ルコール系重合体もしくは該重合体と水溶性不飽和単量
体とを含む水溶液に対して同時に添加することもできる
が、前記水溶液に触媒を添加したA液と前記水溶液に促
進剤を添加したB液とを別々に調製して使用時にA液と
B液とを混合して重合架橋させる方法が好ましい。また
場合によつては前記促進剤を用いず重合触媒のみで加熱
重合してゲル化させることも可能てある。重合ゲル化温
度はO〜100′Cの範囲であるが好ましくは室温〜8
0℃の範囲であり、またゲル化時間は3囲2〜(4)時
間程度である。本発明においては用途・目的などに応じ
て重合体水溶液に種々の添加物を加えた後、重合ゲル化
させることも出来る。
Examples of water-soluble unsaturated monomers used in combination with these modified polyvinyl alcohol polymers include acrylamide, acrylic acid, acrylates, vinylpyrrolidone, hydroxyethyl acrylate, and vinylpyridine salts. It is also possible to use a mixture.
These water-soluble unsaturated monomers can be used in place of 1 to 50% by weight of the modified polyvinyl alcohol polymer. Examples of the water-soluble radical polymerization catalyst used in the present invention include hydrogen peroxide, potassium persulfate, and ammonium persulfate. The amount of these catalysts used is about 0.001 to 10% by weight based on the aqueous solution of the modified polyvinyl alcohol polymer alone or a mixture of the polymer and a water-soluble unsaturated monomer. Further, water-soluble radical polymerization promoters used together with the catalyst include Rongarite, ferrous salts, acidic sodium sulfite, sodium thiosulfate, etc., and the amount used is 0.001 to 10% by weight based on the aqueous solution. It is about %. When these polymerization catalysts and polymerization promoters are used, they can be added simultaneously to the aqueous solution containing the modified polyvinyl alcohol polymer or the polymer and the water-soluble unsaturated monomer; A preferred method is to separately prepare a solution A, in which a catalyst is added to the aqueous solution, and a solution B, in which a promoter is added to the aqueous solution, and then mix the solutions A and B at the time of use to effect polymerization and crosslinking. In some cases, it is also possible to carry out heating polymerization and gelation using only a polymerization catalyst without using the promoter. The polymerization gelation temperature ranges from 0 to 100'C, but preferably from room temperature to 8
The temperature is in the range of 0°C, and the gelation time is about 2 to 4 hours. In the present invention, it is also possible to polymerize and gel after adding various additives to the aqueous polymer solution depending on the use and purpose.

このような添加物としてはゲルを不透明化させる無機の
微粒子,着色するための染顔料,芳香を附与するための
香料,あるいは水溶液の粘度を調節するための水溶性重
合体、水溶液に遥変性を附与するための遥変性附与剤,
離型を容易にするための離型剤、発泡ゲルを得るための
発泡剤、泡立ちをおさえるための消泡剤等である。また
ゲルを補強する目的でガラス繊維、有機繊維等を添加す
ることも出来る。また重合ゲル化させて得られた含水ゲ
ルを更に冷凍処理してゲル強度を向上させることも出来
る。このように本発明に従えば含水ゲルは柔軟性に富ん
だものから硬いものまで種々の性能をもつたものが得ら
れるので氷枕、防臭剤、等の用途が期待されるほか、従
来から水溶性高分子ゲルが生かされている諸用途に、あ
るいはゲル製造上の特徴を生かした諸分野への応用展開
が期待される。以下、実施例により本発明を具体的に説
明する。実施例1 500ccセパラブルフラスコに部分ケン化ポリビニル
アルコール(重合度1700,ケン化度88モル%、以
下ポリビニルアルコールはPVAと略記する)の粉末5
0f,無水マレイン酸40ダ,重曹17.2y,溶媒と
してジオキサン200ccを加え、70℃で1時間反応
させた。
Such additives include inorganic fine particles to make the gel opaque, dyes and pigments to color the gel, fragrances to impart fragrance, water-soluble polymers to adjust the viscosity of the aqueous solution, and additives that modify the aqueous solution. A far-modifying additive for imparting
These include a mold release agent to facilitate mold release, a foaming agent to obtain a foamed gel, and an antifoaming agent to suppress foaming. Furthermore, glass fibers, organic fibers, etc. can also be added for the purpose of reinforcing the gel. Further, the hydrous gel obtained by polymerization gelation can be further frozen to improve the gel strength. In this way, according to the present invention, hydrogels with various properties ranging from highly flexible to hard ones can be obtained, and are expected to be used as ice pillows, deodorants, etc. Applications are expected to be developed in various applications where polymer gels are used, or in various fields that take advantage of the characteristics of gel manufacturing. Hereinafter, the present invention will be specifically explained with reference to Examples. Example 1 Partially saponified polyvinyl alcohol (polymerization degree 1700, saponification degree 88 mol%, hereinafter polyvinyl alcohol is abbreviated as PVA) powder 5 was placed in a 500cc separable flask.
0f, 40 da of maleic anhydride, 17.2 y of sodium bicarbonate, and 200 cc of dioxane as a solvent were added, and the mixture was reacted at 70°C for 1 hour.

反応混合物を沖過、アセトンにより繰り返し洗滌した後
乾燥し粉末状の変性PVAを得た。該変性PVAの重量
は77yで重量増加から求めた変性率(重量増加率)は
54%であつた。ノ 得られた変性PVAを下記第1表
に示す割合のビニルピロリドンと共に水に溶解し、これ
に0.8%過酸化水素水を加えて3種類のA液(1,2
,3)を調製した。
The reaction mixture was filtered, washed repeatedly with acetone, and then dried to obtain modified PVA in powder form. The weight of the modified PVA was 77y, and the modification rate (weight increase rate) determined from the weight increase was 54%. The obtained modified PVA was dissolved in water together with vinylpyrrolidone in the proportion shown in Table 1 below, and 0.8% hydrogen peroxide solution was added thereto to form three types of solutions A (1, 2).
, 3) was prepared.

また7.8%ロンガリツト水溶液を加えて3種類のB液
(1,2,3)を調製しjた。次いでこれらA液とB液
を同量混合して室温で5分間重合ゲル化を行なつたとこ
ろ、いずれも極めて成形性に富む透明で硬い含水ゲル体
が得られた。実施例2 実施例1において水溶性不飽和単量体としてビニルピロ
リドンの代りに下記第2表に示す割合でアクリルアミド
又はアクリル酸を用いた以外は実施例1と同じ処方にし
たがつて2種類のA液。
In addition, three types of B solutions (1, 2, 3) were prepared by adding a 7.8% Rongarite aqueous solution. Next, equal amounts of these liquids A and B were mixed and polymerized to form a gel at room temperature for 5 minutes. In both cases, transparent and hard hydrogels with excellent moldability were obtained. Example 2 The same formulation as in Example 1 was used except that acrylamide or acrylic acid was used in place of vinylpyrrolidone as the water-soluble unsaturated monomer in the proportions shown in Table 2 below. A liquid.

*(4,5)およびB液(4,5)を調製した、次いで
A液とB液を同量混合して室温で2@間重合ゲル化を行
なつたところ、NO.4については柔軟性に富む含水ゲ
ル体が、またNO.5については弾性を夕おびた含水ゲ
ル体が得られた。実施例3 重合度1700,ケン化度88モル%の部分ケン化PV
A5Oy,ジケテン20y,重曹5y1さらに溶媒とし
てジオキサン200ccを用い、60℃で4時間反応さ
せた。
*(4,5) and B solution (4,5) were prepared.Next, equal amounts of A solution and B solution were mixed and polymerization gelation was performed at room temperature for 2@@, and NO. No. 4 is a highly flexible hydrogel, and No. 4 is a highly flexible hydrogel. In case No. 5, a water-containing gel body with excellent elasticity was obtained. Example 3 Partially saponified PV with polymerization degree of 1700 and saponification degree of 88 mol%
Using A5Oy, 20y of diketene, 5y1 of sodium bicarbonate, and 200cc of dioxane as a solvent, the mixture was reacted at 60°C for 4 hours.

反応混合物を?過、アセトンにより繰り返し洗滌した後
乾燥し粉末状の変性PVAを得た。秤量した結果変性P
VAの重量は60yであつた。重量増加から求めた変性
率(重量増加率)は20%であつた。この変性PVA粉
末を水に溶解して10%濃度の水溶液100yを調製し
、これにさらに過硫酸カリ1qを溶解して60゜Cで5
時間加熱し重合ゲル化を行なつたところ極めて弾力性に
富・む含水ゲル体が得られた。実施例4 500ccセパラブルフラスコに重合度1700,ケン
化度99モル%以上の完全ケン化PVA粉末50y,3
0%含水メタノール200cc,クロトンアルデヒド1
0y又は20q,硫酸1yを加え、60℃で1時間アセ
タール化反応を行なつた。
Reaction mixture? After repeated washing with filtration and acetone, the powder was dried to obtain modified PVA in powder form. Denatured P as a result of weighing
The weight of VA was 60y. The modification rate (weight increase rate) determined from the weight increase was 20%. This modified PVA powder was dissolved in water to prepare 100 y of a 10% aqueous solution, which was further dissolved with 1 q of potassium persulfate and heated at 60°C for 5 y.
When heated for a period of time to polymerize and gel, a hydrogel with extremely high elasticity was obtained. Example 4 Completely saponified PVA powder 50y,3 with a degree of polymerization of 1700 and a degree of saponification of 99 mol% or more was placed in a 500cc separable flask.
0% water-containing methanol 200cc, crotonaldehyde 1
0y or 20q and 1y of sulfuric acid were added, and an acetalization reaction was carried out at 60°C for 1 hour.

反応混合物を淵過、アセトンにより繰り返し洗滌した後
乾燥し粉末状の変性PVAを得た。重量増加から変性率
(重量増加率)を求めた。以上の結果を第3表にまとめ
て示す。
The reaction mixture was filtered, washed repeatedly with acetone, and then dried to obtain powdery modified PVA. The modification rate (weight increase rate) was determined from the weight increase. The above results are summarized in Table 3.

第3表 次いで上記NO..6で得られた変性PVA粉末を下記
第4表に示す割合でビニルピロリドン,アクリルアミド
又はアクリル酸と共に水に溶解し、これに0.8%過酸
化水素水を加えて3種類のA液(6−1,6−2,6−
3)を調製した。
Table 3 then the above No. .. The modified PVA powder obtained in step 6 was dissolved in water together with vinylpyrrolidone, acrylamide, or acrylic acid in the proportions shown in Table 4 below, and 0.8% hydrogen peroxide was added thereto to form three types of solutions A (6 -1,6-2,6-
3) was prepared.

また7.8%ロンガリツト水溶液を加えて3種類のB液
(6一1,6−2,6−3)を調製した。次いでA液と
B液を同量混合して重合ゲル化を行なつたところ、NO
..6−1について反応開始後m分で含水ゲル体が、ま
たNO..6−2およびNO.6−3については反応開
始後1時間でいずれも弾力性に富む含水ゲル体が得られ
た。第4表 実施例5 実施例4て得られたNO..7の変形PVM粉末を水に
溶解して10%濃度の水溶液100ダを調製した。
In addition, three types of B solutions (6-1, 6-2, 6-3) were prepared by adding a 7.8% Rongarit aqueous solution. Next, when liquid A and liquid B were mixed in equal amounts to polymerize and gel, NO.
.. .. Regarding No. 6-1, a hydrogel was formed at m minutes after the start of the reaction, and NO. .. 6-2 and NO. Regarding 6-3, a highly elastic hydrogel was obtained in all cases 1 hour after the start of the reaction. Table 4 Example 5 NO. obtained in Example 4. .. The modified PVM powder No. 7 was dissolved in water to prepare 100 dah of a 10% aqueous solution.

Claims (1)

【特許請求の範囲】[Claims] 1 ラジカル重合性あるいは共重合性の不飽和結合を有
する環状化合物、不飽和アルデヒドからなる群から選ば
れた1つの化合物とポリビニルアルコール系重合体との
反応により得られる側鎖に二重結合を有する変性ポリビ
ニルアルコール系重合体を有する変性ポリビニルアルコ
ール系重合体を単独もしくは水溶性不飽和単量体と共に
水に溶解し、これに水溶性のラジカル重合触媒単独もし
くは該触媒と水溶性ラジカル重合促進剤とを添加し、常
温下あるいは加熱下に重合架橋せしめることを特徴とす
るポリビニルアルコール系含水ゲルの製造法。
1 A cyclic compound having a radically polymerizable or copolymerizable unsaturated bond, having a double bond in the side chain obtained by the reaction of one compound selected from the group consisting of unsaturated aldehydes and a polyvinyl alcohol polymer. A modified polyvinyl alcohol-based polymer having a modified polyvinyl alcohol-based polymer is dissolved in water alone or together with a water-soluble unsaturated monomer, and a water-soluble radical polymerization catalyst alone or a water-soluble radical polymerization promoter is added thereto. 1. A method for producing a polyvinyl alcohol-based hydrogel, which comprises adding and polymerizing and crosslinking at room temperature or under heating.
JP3457478A 1978-03-23 1978-03-23 Manufacturing method of polyvinyl alcohol hydrogel Expired JPS6051489B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3457478A JPS6051489B2 (en) 1978-03-23 1978-03-23 Manufacturing method of polyvinyl alcohol hydrogel

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3457478A JPS6051489B2 (en) 1978-03-23 1978-03-23 Manufacturing method of polyvinyl alcohol hydrogel

Publications (2)

Publication Number Publication Date
JPS54125287A JPS54125287A (en) 1979-09-28
JPS6051489B2 true JPS6051489B2 (en) 1985-11-14

Family

ID=12418087

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3457478A Expired JPS6051489B2 (en) 1978-03-23 1978-03-23 Manufacturing method of polyvinyl alcohol hydrogel

Country Status (1)

Country Link
JP (1) JPS6051489B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0692467B2 (en) * 1986-10-06 1994-11-16 信越化学工業株式会社 Reversible hydrogel and method for producing the same

Also Published As

Publication number Publication date
JPS54125287A (en) 1979-09-28

Similar Documents

Publication Publication Date Title
CA1109052A (en) Highly absorbent polymeric compositions from polyhydroxy polymer graft copolymers
US4151225A (en) Method for the modification of polyvinylidene fluoride
JPH05504984A (en) Crosslinked or non-crosslinked maleic anhydride-alkyl vinyl ether polymer slurry
JPH0317844B2 (en)
US2486190A (en) Imidized polyacrylamides
KR100298515B1 (en) Manufacturing method of crosslinked polymer containing carboxyl group
JP2611125B2 (en) Improvement in the production of powdered water-absorbent resin by inverse suspension polymerization of acrylic monomer
KR860001409B1 (en) Method of producing for bead-like polymer production
JPH05301916A (en) Polyvinyl acetal having improved melt viscosity characteristics, its production and its use
JP3732557B2 (en) Carboxyl group-containing polymer composition
JPS6051489B2 (en) Manufacturing method of polyvinyl alcohol hydrogel
US3030341A (en) Manufacture of prepolymers
JP2004300193A (en) Aqueous emulsion
JPS5846122B2 (en) Chemical modification method of acrylamide polymer
JPH07228625A (en) Modified polyvinyl alcohol
JPH0222312A (en) Production of polymer containing crosslinking type carboxyl group
JPH02305808A (en) Polymerizable composition containing crosslinked polymer particle, its production and its curing
US2558396A (en) Method of preparing finely divided plasticized polymerized materials and products thereof
JPS6031329B2 (en) Hydrosol production method
JPS6124047B2 (en)
JPS6150482B2 (en)
US2616878A (en) Process for polymerizing methyl methacrylate
JP3055411B2 (en) Allyl-based crosslinked polymer ultrafine particle aqueous dispersion and production method thereof
JPH03224628A (en) Base for gel
JPS6045207B2 (en) Production method of water-soluble polycarboxylate