JPS6211003B2 - - Google Patents

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Publication number
JPS6211003B2
JPS6211003B2 JP12334579A JP12334579A JPS6211003B2 JP S6211003 B2 JPS6211003 B2 JP S6211003B2 JP 12334579 A JP12334579 A JP 12334579A JP 12334579 A JP12334579 A JP 12334579A JP S6211003 B2 JPS6211003 B2 JP S6211003B2
Authority
JP
Japan
Prior art keywords
eva
saponification
weight
butanol
reaction
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
JP12334579A
Other languages
Japanese (ja)
Other versions
JPS5647404A (en
Inventor
Masatoshi Ozaki
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.)
Taoka Chemical Co Ltd
Original Assignee
Taoka Chemical 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 Taoka Chemical Co Ltd filed Critical Taoka Chemical Co Ltd
Priority to JP12334579A priority Critical patent/JPS5647404A/en
Publication of JPS5647404A publication Critical patent/JPS5647404A/en
Publication of JPS6211003B2 publication Critical patent/JPS6211003B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】[Detailed description of the invention]

本発明はエチレン―酢酸ビニル共重合体(以下
EVAと略称する)を粒状または粉末状のままけ
ん化する方法に関する。 一般にEVAのけん化物は、EVAに比較して熱
安定性、機械的性質、耐溶剤性、ガスバリヤー性
等にすぐれ、粉粒体、フイルムあるいは成形品と
して、繊維用接着剤、粉末塗装、接着フイルム、
複合フイルム等に利用される有用な樹脂である。 従来、EVAのけん化方法は通常トルエン、キ
シレンのようなEVAの良溶媒にEVAを溶解さ
せ、溶液状態で水酸化ナトリウム、水酸化カリウ
ム、ナトリウムメチラート等のアルカリ触媒を加
えることにより実施される。いわゆる均一けん化
方法で、この方法によると反応後EVAけん化物
を析出させるために多量のメタノール、エタノー
ルのような非溶媒を加える必要があるばかりか、
単離および回収が非常に煩雑となり、経済性の点
からも好ましい方法ではない。 一方メタノールまたはエタノールのような非溶
媒中でアルカリ触媒を用いてけん化する方法も知
られている。いわゆる不均一けん化法であるが、
一般にEVAのけん化反応は共重合体の固体表面
より起るために、単に低沸点アルコールのみを用
いた場合には固体表面と内部で異なつた程度にけ
ん化が起り、均一なけん化は困難であり、必然的
にけん化反応は長時間を要し工業的には好ましい
方法ではない。特にペレツト状EVAの高けん化
品を得ようとするとこの欠点は顕著である。 この欠点を改良するために、メタノール、エタ
ノール等の低沸点アルコールにn―ブタノールや
t―ブタノールを添加併用し、EVAの原形を維
持しながらEVAを膨潤させて反応時間を短縮さ
せる試みが成されている。(特公昭44−27902)し
かしこの方法によればn―ブタノールやt―ブタ
ノールはEVAに対して5wt%以上を使用すると粒
子間に融着が起り、かつ、EVAを90%以上けん
化することができない。けん化率90%以上を得よ
うとすれば、さらに高級なアルコールを用いねば
ならないが、その場合粒子間の融着が起り不都合
である。これに対して特公昭49−6551号にはメタ
ノールとn―プロパノールまたはi―プロパノー
ルの単独あるいは混合物との混合液を用いて
EVAをけん化率90%以上に容易にけん化する方
法を提案しているが、この方法はオートクレーブ
を用いて窒素置換下に行なわねばならない。 本発明者らは叙上のような酢ビ含量50重量%以
下のEVAの従来法によるけん化方法の欠点を改
良すべく検討し、sec―ブタノールとメタノール
等の低沸点アルコールとの混合溶媒系を用いると
EVAまたは/およびEVAけん化物の粒子間の融
着を起させることなく、かつ常圧で円滑に反応が
進行して、けん化率90%以上のけん化物を容易に
得ることを見出し本発明を完成した。 すなわち、本発明は酢酸ビニル含量50重量%以
下のエチレン―酢酸ビニル共重合体を不均一状態
でけん化するに際し、粒状の該共重合体100重量
部に対してメタノールまたは/およびエタノール
とsec―ブタノールの混合物(混合物中のsec―ブ
タノールの混合比率は15〜80重量%)150〜1000
重量部および触媒0.05〜10当量を加え、90℃以下
の温度で反応せしめ、該共重合体間の融着をおこ
すことなく反応せしめることを特徴とするエチレ
ン―酢酸ビニル共重合体のけん化方法である。 本発明はsec―ブタノールを低級アルコールに
添加した混合溶媒にてけん化反応を行なうのであ
るが、sec―ブタノールはEVAおよびEVAけん化
物を反応中に相互に融着させることなしに、しか
もEVAおよびEVAけん化物両者を良好に膨潤さ
せるために、結果的にけん化反応は不均一法であ
りながら均一法に近い状態で進行する。その結
果、粒状または粉末状のEVA高けん化品が常圧
で短時間で得られるので本発明の方法は工業的に
非常に有利な方法と云える。 本発明に用いられるEVAは、酢酸ビニル含量
が50重量%以下であり、好ましくは35重量%以下
である。酢ビ含量が50重量%を超えると粒子間の
融着が生じやすく、本発明の方法に適用するには
不適当である。EVAのメルトインデツクスは特
に制限するものではないが、通常1〜500%10分
の範囲のものである。 本発明けん化方法に使用する混合溶剤はメタノ
ールまたはエタノールまたはその混合物とsec―
ブタノールとから成るが、混合溶剤中のsec―ブ
タノールの混合比率は15〜80重量%、好ましくは
30〜70重量%である。15重量%以下であると
EVA,EVAけん化物の膨潤が行きとどかず本発
明の効果を発揮するには不十分であり、また80重
量%以上であると加温によりEVAが相互に融着
を起すので好ましくない。混合溶剤量は通常
EVA100重量部に対して150〜1000重量部が用い
られるが、好ましくは250〜600重量部である。
150重量部未満では実質的にけん化を行なわしめ
るのは困難であり、1000重量部を超えても実質的
にはメリツトがなく1000重量部以下で充分な目的
を達する。 本発明のけん化方法に使用される触媒はアルカ
リ触媒であり、水酸化ナトリウム、水酸化カリウ
ム、ナトリウムメチラート、ナトリウムエチラー
ト等が挙げられる。その使用量はEVAに対して
0.05〜10倍当量であり、好ましくは0.1〜3倍当
量である。 本発明けん化方法における反応温度は、用いる
EVAの酢酸ビニル含量、メルトインデツクスに
より異なるが、通常50〜90℃にて行れわれる。90
℃以上ではEVAけん化物相互の融着がみられ、
50℃以下では反応時間が長く、いずれも好ましく
ない。又本発明けん化反応は通常、かくはん装置
付反応器にて常圧下に混合溶剤の沸点近くで行な
わるが、EVAけん化物相互の融着が起らない温
度に制御しつつオートクレーブで反応を行なつて
てもよい。 本発明に於て、sec―ブタノールの使用量につ
いては上述したとおりであるが、sec―ブタノー
ルの量をEVAに対する量比でみると、EVAに対
して20重量%以下では殆んど膨潤効果をもたらさ
ず、EVAの数百倍に及ぶ多量を使用する方が本
発明効果を発揮するに好ましかつたという結果を
得ている。このことは従来法として知られるn―
ブタノールやt―ブタノールをメタノールと混合
し使用するEVAのけん化方法において、n―ブ
タノールやt―ブタノールがEVAの5重量%以
上添加使用する場合には、EVA粒子間に融着が
起るとされている事実からは驚くべきことであつ
た。又さらに、EVAをメタノール単独媒体また
はメタノール、n―ブタノール混合媒体中でそれ
ぞれけん化した場合の低けん化率のけん化物の接
着強度、耐ドライクリーニング性等に比較して、
本発明の方法によつてけん化されたけん化物は、
低けん化率のけん化物であつてもそれらの性質が
著しく向上していることもわかつた。 以下に本発明方法を実施例により説明する。例
においてEVAけん化物の接着強度試験は下記の
方法で行なつた。 150×200mmの60番ブロード布上にEVAけん化
物を20g/m2の割合で撒布し、同大の共布を重ね
たのち、温度140℃、圧力0.2Kg/cm2、時間10秒の
条件でプレスして接着し、基礎試験片を作成す
る。 (1) 初期接着強度 上記基礎試験片を巾25mmで縦に裁断して5枚の
試験片を作成し、引張試験機を使用してそれぞ
れ、つかみ間隔50mm、引張速度200mm/minでは
くりし、JIS―L―1089に従つて極大値の大きい
ものから3個、小さいものから3個をとつて計6
個の平均値を算出し、5枚の試験片の平均値をg
で表わした。 (2) 耐ドライクリーリング性 上記基礎試験片の端から5mmのところでミシン
で押え縫いする。JIS―L―0860―1965(ドライ
クリーニングテスト)に準拠し、パークロルエチ
レンを用い40℃、1時間処理、自然乾燥したの
ち、巾25mm、長さ130mmの試験片3枚を採取し、
(1)の初期接着強度試験に準拠してはくりし、3枚
の試験片の平均値gで表わした。 (3) 耐洗濯性 耐ドライクリーニング性と同じように基礎試験
片の端から5mmのところでミシンで押え縫いし、
追加布と共で1Kgになるように洗濯機に投入し、
60℃の湯20に粉末石鹸を0.1%になるように添
加した液を加えて30分間洗濯、排水、40℃の湯で
15分間洗浄、脱水、自然乾燥し、巾25mm、長さ
130mmの試験片3枚を裁断し、(1)の強度試験法に
準じてはくり試験し、3枚の平均値をgで表わし
た。 実施例 1 かくはん機付、内容量500mlのガラス製反応容
器に、酢酸ビニル含量25.5重量%、メルトインデ
ツクス150g/10分のEVAペレツト75g、メタノ
ール150g、sec―ブタノール150g、水酸化ナト
リウム10.4g、シアノ酢酸メチルエステル0.3g
を仕込み、20分かけて昇温し、沸点温度で溶剤を
還流させながら4時間反応を行なつた。反応終了
後冷却してから過し、メタノール洗浄後60〜65
℃の乾燥器で一昼夜乾燥した。得られたペレツト
はけん化度96%であつた。 このペレツトを用いて接着強度試験した結果を
第1表に示した。 実施例 2 実施例1において反時間を2.5時間にした以外
は全く実施例1と同様にして実験し、、けん化度
85%の白色ペレツト状物を得た。このものの接着
強度測定した結果を第1表に示す。 比較例 1 実施例1においてsec―ブタノールを使用せず
にメタノールのみ300gを仕込み沸点で16時間反
応させること以外は実施例1と同様の操作を行な
つた。得られたペレツトは白色のペレツト状であ
り、けん化度は85%であつた。 比較例 2 実施例1に使用した反応器を用い、酢酸ビニル
含量25.5重量%、メルトインデツクス150g/10
分のEVAペレツト75g、n―ブタノール3g、
メタノール300g、水酸化ナトリウム7gを仕込
み、30分を要して沸とうさせ、沸点で5時間反応
させ、以後実施例1同様に処理して白色けん化度
84%のものを得た。 比較例1および2で得たペレツトの接着強度試
験結果を第1表に示す。
The present invention is an ethylene-vinyl acetate copolymer (hereinafter referred to as
This method relates to a method for saponifying EVA (abbreviated as EVA) in granular or powder form. In general, saponified EVA has superior thermal stability, mechanical properties, solvent resistance, gas barrier properties, etc. compared to EVA, and can be used as a powder, film, or molded product as a fiber adhesive, powder coating, or adhesive. film,
It is a useful resin used for composite films, etc. Conventionally, the saponification method of EVA is usually carried out by dissolving EVA in a good solvent for EVA such as toluene or xylene, and adding an alkali catalyst such as sodium hydroxide, potassium hydroxide, or sodium methylate in a solution state. This is a so-called homogeneous saponification method. According to this method, it is not only necessary to add a large amount of non-solvent such as methanol or ethanol to precipitate the saponified EVA after the reaction, but also
Isolation and recovery become very complicated, and this is not a preferred method from an economic point of view. On the other hand, a method of saponification using an alkaline catalyst in a non-solvent such as methanol or ethanol is also known. This is the so-called heterogeneous saponification method,
Generally, the saponification reaction of EVA occurs from the solid surface of the copolymer, so if only a low-boiling alcohol is used, saponification will occur to different degrees on the solid surface and inside, making uniform saponification difficult. The saponification reaction necessarily takes a long time and is not an industrially preferred method. This drawback is particularly noticeable when trying to obtain a highly saponified pellet-like EVA product. In order to improve this drawback, attempts have been made to add n-butanol or t-butanol to low-boiling alcohols such as methanol or ethanol, to swell EVA and shorten the reaction time while maintaining the original shape of EVA. ing. (Japanese Patent Publication No. 44-27902) However, according to this method, if n-butanol or t-butanol is used in an amount of 5wt% or more based on EVA, fusion will occur between particles, and more than 90% of EVA can be saponified. Can not. In order to obtain a saponification rate of 90% or more, higher alcohols must be used, but in this case, fusion between particles occurs, which is inconvenient. On the other hand, Japanese Patent Publication No. 49-6551 uses a mixture of methanol and n-propanol or i-propanol alone or as a mixture.
We have proposed a method to easily saponify EVA to a saponification rate of 90% or higher, but this method must be carried out using an autoclave under nitrogen purge. The present inventors investigated in order to improve the drawbacks of the conventional saponification method for EVA with a vinyl acetate content of 50% by weight or less, and developed a mixed solvent system of sec-butanol and a low boiling point alcohol such as methanol. When used
The present invention was completed by the discovery that the reaction proceeds smoothly at normal pressure without causing any fusion between particles of EVA or/and EVA saponified product, and that a saponified product with a saponification rate of 90% or more can be easily obtained. did. That is, when saponifying an ethylene-vinyl acetate copolymer having a vinyl acetate content of 50% by weight or less in a heterogeneous state, the present invention uses methanol or/and ethanol and sec-butanol for 100 parts by weight of the granular copolymer. (The mixing ratio of sec-butanol in the mixture is 15-80% by weight) 150-1000
A method for saponifying an ethylene-vinyl acetate copolymer, which comprises adding parts by weight and 0.05 to 10 equivalents of a catalyst and reacting at a temperature of 90°C or lower, thereby causing the reaction to occur without causing fusion between the copolymers. be. In the present invention, the saponification reaction is carried out using a mixed solvent in which sec-butanol is added to a lower alcohol. In order to swell both the saponified products well, the saponification reaction proceeds in a state close to a homogeneous method even though it is a heterogeneous method. As a result, a highly saponified EVA product in the form of granules or powder can be obtained in a short time under normal pressure, so the method of the present invention can be said to be industrially very advantageous. The EVA used in the present invention has a vinyl acetate content of 50% by weight or less, preferably 35% by weight or less. If the vinyl acetate content exceeds 50% by weight, fusion between particles tends to occur, making it unsuitable for application to the method of the present invention. The melt index of EVA is not particularly limited, but is usually in the range of 1 to 500% and 10 minutes. The mixed solvent used in the saponification method of the present invention is methanol or ethanol or a mixture thereof and sec-
However, the mixing ratio of sec-butanol in the mixed solvent is 15 to 80% by weight, preferably
It is 30-70% by weight. 15% by weight or less
EVA and saponified EVA do not fully swell, which is insufficient to exhibit the effects of the present invention, and if it exceeds 80% by weight, the EVA will fuse with each other due to heating, which is not preferable. The amount of mixed solvent is usually
It is used in an amount of 150 to 1000 parts by weight, preferably 250 to 600 parts by weight, based on 100 parts by weight of EVA.
If it is less than 150 parts by weight, it is difficult to carry out saponification, and if it exceeds 1,000 parts by weight, there is virtually no merit, and if it is less than 1,000 parts by weight, the purpose is sufficiently achieved. The catalyst used in the saponification method of the present invention is an alkali catalyst, and examples thereof include sodium hydroxide, potassium hydroxide, sodium methylate, sodium ethylate, and the like. Its usage is against EVA
It is 0.05 to 10 times equivalent, preferably 0.1 to 3 times equivalent. The reaction temperature in the saponification method of the present invention is
Although it varies depending on the vinyl acetate content and melt index of EVA, it is usually carried out at 50 to 90°C. 90
At temperatures above ℃, mutual fusion of EVA saponified substances is observed.
If the temperature is below 50°C, the reaction time will be long, which is not preferable. The saponification reaction of the present invention is usually carried out in a reactor equipped with a stirring device under normal pressure near the boiling point of the mixed solvent, but the reaction can be carried out in an autoclave while controlling the temperature to prevent mutual fusion of EVA saponified products. You can do it. In the present invention, the amount of sec-butanol used is as described above, but when looking at the amount of sec-butanol in terms of the amount ratio to EVA, if it is less than 20% by weight relative to EVA, it has almost no swelling effect. The results showed that it was preferable to use an amount several hundred times as large as that of EVA to achieve the effects of the present invention. This is known as the conventional method n-
In the EVA saponification method that uses butanol or t-butanol mixed with methanol, if n-butanol or t-butanol is added in an amount of 5% or more by weight of EVA, it is said that fusion will occur between EVA particles. This was surprising considering the fact that Furthermore, compared to the adhesive strength, dry cleaning resistance, etc. of saponified products with a low saponification rate when EVA is saponified in a methanol alone medium or a methanol and n-butanol mixed medium, respectively,
The saponified product saponified by the method of the present invention is
It was also found that the properties of saponified products with low saponification rates were significantly improved. The method of the present invention will be explained below using examples. In the example, the adhesive strength test of saponified EVA was conducted in the following manner. Spread EVA saponification at a rate of 20 g/m 2 on No. 60 broad cloth of 150 x 200 mm, layer the same size cloth, and then apply the mixture at a temperature of 140°C, a pressure of 0.2 Kg/cm 2 and a time of 10 seconds. Press and adhere to create a basic test piece. (1) Initial adhesive strength The above basic test piece was cut vertically to a width of 25 mm to create 5 test pieces, and each was peeled using a tensile testing machine at a gripping interval of 50 mm and a tensile speed of 200 mm/min. According to JIS-L-1089, 3 items with the highest maximum value and 3 items with the lowest maximum value are taken for a total of 6 items.
Calculate the average value of 5 test pieces, and calculate the average value of 5 test pieces in g
It was expressed as (2) Dry creeling resistance Pressure stitch with a sewing machine 5mm from the edge of the above basic test piece. In accordance with JIS-L-0860-1965 (dry cleaning test), three test pieces with a width of 25 mm and a length of 130 mm were collected after treatment with perchlorethylene at 40°C for 1 hour and air drying.
The test pieces were peeled off according to the initial adhesive strength test (1) and expressed as the average value g of the three test pieces. (3) Washing resistance As with dry cleaning resistance, press-stitch with a sewing machine at 5 mm from the edge of the basic test piece.
Put it in the washing machine so that it weighs 1kg with additional cloth,
Add a solution containing 0.1% powdered soap to 60℃ hot water, wash for 30 minutes, drain, and rinse with 40℃ hot water.
Wash for 15 minutes, dehydrate, air dry, width 25mm, length
Three test pieces of 130 mm were cut and subjected to a peel test according to the strength test method (1), and the average value of the three pieces was expressed in g. Example 1 In a glass reaction vessel with a stirrer and a capacity of 500 ml, 75 g of EVA pellets with a vinyl acetate content of 25.5% by weight and a melt index of 150 g/10 minutes, 150 g of methanol, 150 g of sec-butanol, 10.4 g of sodium hydroxide, Cyanoacetic acid methyl ester 0.3g
was charged, the temperature was raised over 20 minutes, and the reaction was carried out for 4 hours while refluxing the solvent at the boiling point temperature. After the reaction is completed, cool it down, filter it, and wash it with methanol.
It was dried in a dryer at ℃ overnight. The obtained pellets had a saponification degree of 96%. Table 1 shows the results of an adhesive strength test using this pellet. Example 2 An experiment was conducted in the same manner as in Example 1 except that the reaction time was changed to 2.5 hours, and the degree of saponification was
An 85% white pellet was obtained. The adhesive strength of this product was measured and the results are shown in Table 1. Comparative Example 1 The same operation as in Example 1 was carried out except that sec-butanol was not used in Example 1 and 300 g of methanol alone was charged and reacted at the boiling point for 16 hours. The obtained pellets were in the form of white pellets, and the degree of saponification was 85%. Comparative Example 2 Using the reactor used in Example 1, vinyl acetate content 25.5% by weight, melt index 150g/10
75g of EVA pellets, 3g of n-butanol,
300g of methanol and 7g of sodium hydroxide were charged, boiled for 30 minutes, reacted at the boiling point for 5 hours, and then treated in the same manner as in Example 1 to obtain a white saponification degree.
Got 84% stuff. Table 1 shows the adhesive strength test results for the pellets obtained in Comparative Examples 1 and 2.

【表】 実施例 3 実施例1において混合溶媒をメタノール175
g、sec―ブタノール50gに代えた以外は実施例
1と同様の操作を行なつた。反応は沸点にて5時
間行なつた結果、けん化度91%の白色のペレツト
を得た。 実施例 4 実施例1において混合溶媒をメタノール100
g、sec―ブタノール200gに代えた以外は実施例
1と同様に操作し、沸点にて4時間の反応でけん
化度99%白色のペレツトを得た。 実施例 5 実施例1において混合溶媒をエタノール100
g、sec―ブタノール150gに代えた以外は実施例
1と同様に操作し、沸点にて5時間反応させてけ
ん化率99%の白色のペレツトを得た。
[Table] Example 3 Methanol 175 was used as the mixed solvent in Example 1.
The same operation as in Example 1 was carried out except that 50 g of sec-butanol was used instead. The reaction was carried out at the boiling point for 5 hours, yielding white pellets with a saponification degree of 91%. Example 4 In Example 1, the mixed solvent was methanol 100%
The procedure was repeated in the same manner as in Example 1 except that 200 g of sec-butanol was used, and white pellets with a saponification degree of 99% were obtained by reaction at the boiling point for 4 hours. Example 5 In Example 1, the mixed solvent was ethanol 100%
The same procedure as in Example 1 was carried out except that 150 g of sec-butanol was used, and the reaction was carried out at the boiling point for 5 hours to obtain white pellets with a saponification rate of 99%.

Claims (1)

【特許請求の範囲】[Claims] 1 酢酸ビニル含量50重量%以下のエチレン―酢
酸ビニル共重合体を不均一状態でけん化するに際
し、粒状の該共重合体100重量部に対してメタノ
ールまたは/およびエタノールとsec―ブタノー
ルの混合物(混合物中のsec―ブタノールの混合
比率は15〜80重量%)150〜1000重量部および触
媒0.05〜10当量を加え、90℃以下の温度で反応せ
しめ、該共重合体間の融着をおこすことなく反応
せしめることを特徴とするエチレン―酢酸ビニル
共重合体のけん化方法。
1 When saponifying an ethylene-vinyl acetate copolymer with a vinyl acetate content of 50% by weight or less in a heterogeneous state, methanol or/and a mixture of ethanol and sec-butanol (mixture The mixing ratio of sec-butanol in the copolymer is 15-80% by weight) 150-1000 parts by weight and 0.05-10 equivalents of catalyst are added and reacted at a temperature of 90°C or less without causing fusion between the copolymers. A method for saponifying an ethylene-vinyl acetate copolymer, which comprises causing a reaction.
JP12334579A 1979-09-25 1979-09-25 Saponification of ethylene-vinyl acetate copolymer Granted JPS5647404A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12334579A JPS5647404A (en) 1979-09-25 1979-09-25 Saponification of ethylene-vinyl acetate copolymer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12334579A JPS5647404A (en) 1979-09-25 1979-09-25 Saponification of ethylene-vinyl acetate copolymer

Publications (2)

Publication Number Publication Date
JPS5647404A JPS5647404A (en) 1981-04-30
JPS6211003B2 true JPS6211003B2 (en) 1987-03-10

Family

ID=14858256

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12334579A Granted JPS5647404A (en) 1979-09-25 1979-09-25 Saponification of ethylene-vinyl acetate copolymer

Country Status (1)

Country Link
JP (1) JPS5647404A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03148312A (en) * 1989-10-31 1991-06-25 Mitsuboshi Belting Ltd Bicycle tire

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03148312A (en) * 1989-10-31 1991-06-25 Mitsuboshi Belting Ltd Bicycle tire

Also Published As

Publication number Publication date
JPS5647404A (en) 1981-04-30

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