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JPH0428002B2 - - Google Patents
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JPH0428002B2 - - Google Patents

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Publication number
JPH0428002B2
JPH0428002B2 JP60249633A JP24963385A JPH0428002B2 JP H0428002 B2 JPH0428002 B2 JP H0428002B2 JP 60249633 A JP60249633 A JP 60249633A JP 24963385 A JP24963385 A JP 24963385A JP H0428002 B2 JPH0428002 B2 JP H0428002B2
Authority
JP
Japan
Prior art keywords
reaction
ethylene
vinyl alcohol
isocyanate
alcohol copolymer
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP60249633A
Other languages
Japanese (ja)
Other versions
JPS62109804A (en
Inventor
Hiroshi Yamamoto
Kihachi Suzuki
Tsukasa Ochiumi
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.)
Nitto Denko Corp
Original Assignee
Nitto Denko Corp
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 Nitto Denko Corp filed Critical Nitto Denko Corp
Priority to JP24963385A priority Critical patent/JPS62109804A/en
Publication of JPS62109804A publication Critical patent/JPS62109804A/en
Publication of JPH0428002B2 publication Critical patent/JPH0428002B2/ja
Granted legal-status Critical Current

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Description

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

産業上の利用分野 本発明は、水溶性溶媒を用いた溶液系で反応を
進行せしめることを特徴とし、イソシアネート系
化合物の導入割合を任意にコントロールすること
ができて、かつ、耐熱性に優れるビニルカルバメ
ート系剥離性処理剤の製造方法に関する。 従来の技術 従来、エチレン・ビニルアルコール共重合体と
アルキルイソシアネートとの反応生成物からなる
ビニルカルバメート系剥離性処理剤の製造方法と
しては、エチレンの共重合割合が0.1〜0.9のエチ
レン・ビニルアルコール共重合体をトルエン、キ
シレンなどの非水溶性溶媒中に溶解あるいは分散
させたのち、8個以上の炭素数を有するアルキル
イソシアネートを加えて反応させる方法が知られ
ていた(特公昭60−30355号公報)。 発明が解決しようとする問題点 しかしながら、上記の非水溶性溶媒のみを用い
る方法ではケン化度の高い、従つて水酸基の含有
割合が多いエチレン・ビニルアルコール共重合体
の使用が不可能なこと、イソシアネート系化合物
の導入割合を任意にコントロールできないこと、
そのためセロハンや紙等からなる親水性基材に対
する密着性に優れる剥離性処理剤の調製が困難で
あること、得られる剥離性処理剤が耐熱性に劣る
ことなどの問題があつた。また、分散方式による
場合にはそのほかに、平均重合度が2000以上のエ
チレン・ビニルアルコール共重合体を用いた場合
その反応速度が著しく遅くなり実用的でないなど
の問題もあつた。 問題点を解決するための手段 本発明者らは上記の問題を克服し、ケン化度、
平均重合度の高いエチレン・ビニルアルコール共
重合体も用いることができ、イソシアネート系化
合物の導入割合を任意にコントトールすることが
できて、得られる剥離性処理剤が耐熱性及び基材
に対する密着性にすぐれるビニルカルバメート系
剥離性処理剤の製造方法を開発するための鋭意研
究を重ねた結果、意外にも水溶性溶媒にエチレ
ン・ビニルアルコールを溶解せしめてこの溶液に
イソシアネート系化合物を加え、反応を溶液状態
維持下に進行完了せしめることによりその目的を
達成しうることを見出し、本発明をなすに至つ
た。 すなわち、本発明は、エチレン・ビニルアルコ
ール共重合体と炭素数が8個以上のアルキル基を
有するイソシアネートとの反応生成物からなる剥
離性処理剤を製造するにあたり、水溶性溶媒を用
いて溶液状態としたエチレン・ビニルアルコール
共重合体とアルキルイソスシネートとを反応開始
から反応終了に至るまでその中間生物も含めて溶
液状態下で反応させることを特徴とする剥離性処
理剤の製造方法を提供するものである。 本発明において用いられるエチレン・ビニルア
ルコール共重合体は水溶性溶媒に可溶なものであ
る。一般には、水溶性の観点よりビニルアルコー
ルの共重合割合が約20モル%以上、就中30〜95モ
ル%のものが用いられる。そのケン化度について
は水溶性溶媒に可溶であることの条件が満足され
る限り特に限定はないが、ケン化度80モル%以上
のものに対して本発明の均一溶解方式としての有
利性が発揮される。従つて、エチレンの共重合割
合が約80モル%以下、就中70〜5モル%のものが
一般に用いられる。なお、該共重合体の平均重合
度としては100〜5000、就中500〜2500が適当であ
る。その平均重合度が100未満であると得られる
剥離性処理剤が膜強度、耐熱性に乏しいものとな
り、5000を超えると溶解性に劣つて反応作業上好
ましくない。 一方、前記した水溶性溶媒としてはジメチルス
ルホキシド、テトラヒドロフラン、N−メチルピ
ロリドン、ジオキサン、アセチルアセトン、ジエ
チレングリコールジメチルエーテル、スルホラ
ン、ブチルラクトン、リン酸トリエチル、乳酸メ
チルなどで代表されるものが用いられる。なお、
反応温度よりも高い沸点を有する水溶性溶媒が一
般に望ましく用いられる。 本発明において用いられるアルキルイソシアネ
ートは炭素数が8個以上のアルキル基を有するも
のである。就中、炭素数が12〜30個のアルキル基
を有するものが剥離性付与能あるいは入手容易性
などの点で好ましく用いられる。その代表例とし
ては、オクチル、ノニル、デシル、ウンデシル、
ドデシル、トリデシル、テトラデシル、ペンタデ
シル、ヘキサデシル、ヘプタデシル、オクタデシ
ル、ノナデシル、エイコシル、ヘンエイコシル、
ドコシル、トリコシル、テトラコシル、ペンタコ
シル、ヘキサコシル、オクタコシル、ナコシル、
トリアコンチルなどの長鎖アルキル基を有するイ
ソシアネートなどをあげることができる。 本発明においては水溶性溶媒を用いて溶液状態
としたエチレン・ビニルアルコール共重合体とア
ルキルイソシアネートを反応させることが必要で
あり、かつ、反応の開始から終了に至るまでその
中間生成物も含めて溶液状態下に反応させること
が必要である。これにより、高ケン化度、高重合
度のエチレン・ビニルアルコール共重合体を用い
ての反応が可能となり、また、イソシアネート系
化合物の導入割合の任意なコントロールが可能と
なる。 前記の反応は一般に、まず所定量のエチレン・
ビニルアルコール共重合体を少なくともこれを溶
かすに必要な量の、通常3〜8重量倍の水溶性溶
媒に溶解させ、この溶液に所定量のアルキルイソ
シアネートを加えて加熱下に進行せしめられる。
その際、必要に応じ中間生成物を溶解させるため
に、すなわち中間生成物が反応系中で析出するこ
とを防止するためにキシレン、トルエン等の非水
溶性溶媒を適宜に加えて、反応系を反応終了まで
溶液状態に維持することが必要である。これによ
り本発明の目的が達成される。従つて、エチレ
ン・ビニルアルコールの非水溶性溶媒による分散
状態下に反応を開始させる方法、中間生成物の析
出を放置する方法では本発明の目的は達成されな
い。 なお、反応の終点は反応系におけるイソシアネ
ート基の消失をもつて判断される。また、反応に
際し、必要に応じて水酸基とイソシアネート基の
反応を促進せしめる例えば有機錫化合物などで代
表される触媒を用いてもよい。 他方、アルキルイソシアネートの使用量はその
目的とする導入割合により適宜に決定される。一
般にはエチレン・ビニルアルコールにおける水酸
基に対し0.1〜1.1当量用いられる。セロハン基
材、紙基材等の親水性基材に対する密着性の点で
は水酸基を残存せしめることが有利である。 得られた反応生成物は、通常メタノール等の媒
体中に反応液を注いで沈殿させたのち洗浄し、そ
の粉砕物をトルエン等に溶解せしめた溶液として
剥離性処理等の実用途に供される。 発明の効果 本発明によれば、水溶性溶媒を用いた溶液反応
系としたので、高ケン化度、高重合度のエチレ
ン・ビニルアルコール共重合体を反応物として使
用することができ、また、イソシアネート化合物
の導入割合を容易にコントロールすることができ
る。 加えて、基材に対する接着力及び剥離特性の熱
安定性(耐熱性)にすぐれる剥離性処理剤を簡単
な操作で効率よく得ることができる利点なども有
している。 実施例 実施例 1〜4 還流冷却器及び水分定量受器を付けた1000c.c.容
の四ツ口フラスコにエチレン・ビニルアルコール
共重合体を入れ、これにジメチルスルホキシドを
加えてかきまぜ、溶液とする。ついで、この溶液
にキシレンを加えて撹拌下140℃で2時間還流さ
せて水分を除去する。 その後、系を100℃に冷却させたのちオクタデ
シルイソシアネートを加えて反応させる。反応の
進行に応じてキシレンを適時加えながら系を常に
均一溶液状態に維持し、120℃で約5時間反応さ
せる。この間、系中の残存イソシアネート基を定
量し、その残存分が消失した時点をもつて反応の
終点とする。 反応終了後、反応液を5重量倍のメタノール中
に注ぎ白色沈殿物を析出させ、ろ別後メタノール
で洗浄し、乾燥粉砕して目的物を得る。 上記の方式で表に示した反応物からなる目的物
を得る。 比較例 1 エチレン・ビニルアルコール共重合体(エチレ
ン共重合割合0.5、平均重合度1700)10部(重量
部、以下同様)をキシレン50部に分散させこれに
オクタデシルイソスシネート45部を加えて120℃
で残存イソシアネート基が消失する時点まで反応
させ、得られた反応液を実施例と同様に処理して
目的物を得る。 比較例 2 ポリビニルアルコール(ケン化度88モル%、平
均重合度1400)20部、キシレン204部、オクタデ
シルイソシアネート116部を用い、比較例1に準
じて処理して目的物を得る。 比較例 3 エチレン・ビニルアルコール共重合体(エチレ
ン共重合割合0.8、ビニルアルコール共重合割合
0.2、平均重合度1000)を用いて実施例と同様な
操作を行つたが、ジメチルスルホキシドに溶解せ
ず目的を達成できなかつた。 評価試験 実施例、比較例で得た反応生成物としての剥離
性処理剤をトルエンに溶解させて1重量%溶液を
調製し、これをセロハンフイルム(厚さ36μm)
上に塗布し(固形物:0.05g/m2)乾燥させて剥
離処理フイルムを得る。 次に、剥離処理フイルムの処理面にセロハン粘
着テープ(No.29、日東電気工業社製)を自重2Kg
のゴムローラにて圧着し、これを20℃又は50℃の
雰囲気下で24時間加温後、180度ピールによる剥
離力(引張速度300mm/分)を測定する。ただし、
50℃下加温物については、加温後20℃雰囲気下に
4時間放置した。結果を表に示す。
Industrial Application Field The present invention is characterized in that the reaction proceeds in a solution system using a water-soluble solvent, and the introduction ratio of isocyanate compounds can be arbitrarily controlled. The present invention relates to a method for producing a carbamate-based peeling treatment agent. BACKGROUND TECHNOLOGY Conventionally, as a method for producing a vinyl carbamate-based stripping agent made of a reaction product of an ethylene/vinyl alcohol copolymer and an alkyl isocyanate, an ethylene/vinyl alcohol copolymer with an ethylene copolymerization ratio of 0.1 to 0.9 has been used. A method was known in which a polymer is dissolved or dispersed in a water-insoluble solvent such as toluene or xylene, and then an alkyl isocyanate having 8 or more carbon atoms is added and reacted (Japanese Patent Publication No. 60-30355). ). Problems to be Solved by the Invention However, with the above method using only a water-insoluble solvent, it is impossible to use an ethylene-vinyl alcohol copolymer that has a high degree of saponification and therefore has a high content of hydroxyl groups. The inability to arbitrarily control the introduction ratio of isocyanate compounds;
Therefore, there have been problems such as difficulty in preparing a releasable treatment agent that has excellent adhesion to hydrophilic substrates such as cellophane or paper, and that the resulting releasable treatment agent has poor heat resistance. In addition, when using the dispersion method, there were other problems such as when an ethylene/vinyl alcohol copolymer having an average degree of polymerization of 2000 or more was used, the reaction rate became extremely slow, making it impractical. Means for Solving the Problems The present inventors have overcome the above problems and have improved the degree of saponification,
Ethylene/vinyl alcohol copolymers with a high average degree of polymerization can also be used, and the introduction ratio of isocyanate compounds can be controlled arbitrarily, so that the resulting release treatment agent has good heat resistance and adhesion to the substrate. As a result of intensive research to develop a method for producing a vinyl carbamate-based stripping agent with excellent properties, it was surprisingly possible to dissolve ethylene and vinyl alcohol in a water-soluble solvent, add an isocyanate compound to this solution, and react. The present inventors have discovered that the object can be achieved by allowing the process to proceed while maintaining the solution state, and have thus completed the present invention. That is, the present invention provides a method for producing a stripping agent made of a reaction product of an ethylene/vinyl alcohol copolymer and an isocyanate having an alkyl group having 8 or more carbon atoms. Provided is a method for producing a stripping treatment agent, which comprises reacting an ethylene-vinyl alcohol copolymer and an alkyl isosuccinate in a solution state from the start of the reaction to the end of the reaction, including intermediate products. It is something to do. The ethylene/vinyl alcohol copolymer used in the present invention is soluble in a water-soluble solvent. Generally, from the viewpoint of water solubility, a copolymerization ratio of vinyl alcohol of about 20 mol % or more, particularly 30 to 95 mol %, is used. The degree of saponification is not particularly limited as long as the condition of being soluble in a water-soluble solvent is satisfied, but the present invention is advantageous as a homogeneous dissolution method when the degree of saponification is 80 mol% or more. is demonstrated. Therefore, those having an ethylene copolymerization ratio of about 80 mol % or less, particularly 70 to 5 mol %, are generally used. The average degree of polymerization of the copolymer is suitably from 100 to 5,000, particularly from 500 to 2,500. If the average degree of polymerization is less than 100, the resulting releasable treatment agent will have poor film strength and heat resistance, and if it exceeds 5,000, it will have poor solubility, which is undesirable for reaction work. On the other hand, the water-soluble solvents mentioned above include dimethyl sulfoxide, tetrahydrofuran, N-methylpyrrolidone, dioxane, acetylacetone, diethylene glycol dimethyl ether, sulfolane, butyllactone, triethyl phosphate, methyl lactate, and the like. In addition,
Aqueous solvents having a boiling point above the reaction temperature are generally preferably used. The alkyl isocyanate used in the present invention has an alkyl group having 8 or more carbon atoms. Among these, those having an alkyl group having 12 to 30 carbon atoms are preferably used from the viewpoint of ability to impart releasability or easy availability. Typical examples include octyl, nonyl, decyl, undecyl,
Dodecyl, tridecyl, tetradecyl, pentadecyl, hexadecyl, heptadecyl, octadecyl, nonadecyl, eicosyl, heneicosyl,
docosyl, tricosyl, tetracosyl, pentacosyl, hexacosyl, octacosyl, nacosyl,
Examples include isocyanates having long-chain alkyl groups such as triacontyl. In the present invention, it is necessary to react the ethylene/vinyl alcohol copolymer and the alkyl isocyanate in a solution state using a water-soluble solvent, and the process including the intermediate products from the start to the end of the reaction is necessary. It is necessary to carry out the reaction under solution conditions. This makes it possible to carry out a reaction using an ethylene/vinyl alcohol copolymer with a high degree of saponification and a high degree of polymerization, and also to arbitrarily control the proportion of the isocyanate compound introduced. The above reaction generally begins with a predetermined amount of ethylene.
The vinyl alcohol copolymer is dissolved in at least the amount necessary to dissolve it, usually 3 to 8 times the weight of the water-soluble solvent, and a predetermined amount of alkyl isocyanate is added to this solution, followed by heating.
At that time, in order to dissolve the intermediate product as necessary, that is, to prevent the intermediate product from precipitating in the reaction system, a water-insoluble solvent such as xylene or toluene may be added as appropriate to the reaction system. It is necessary to maintain the solution state until the end of the reaction. This achieves the object of the invention. Therefore, the object of the present invention cannot be achieved by a method in which the reaction is started in a dispersion state using a water-insoluble solvent of ethylene/vinyl alcohol, or a method in which precipitation of an intermediate product is allowed to occur. The end point of the reaction is determined by the disappearance of isocyanate groups in the reaction system. Further, during the reaction, a catalyst typified by, for example, an organic tin compound, which promotes the reaction between the hydroxyl group and the isocyanate group, may be used as necessary. On the other hand, the amount of alkyl isocyanate to be used is appropriately determined depending on the intended introduction ratio. Generally, it is used in an amount of 0.1 to 1.1 equivalent to the hydroxyl group in ethylene/vinyl alcohol. It is advantageous to leave hydroxyl groups in view of adhesion to hydrophilic substrates such as cellophane substrates and paper substrates. The obtained reaction product is usually poured into a medium such as methanol to precipitate it, then washed, and the pulverized product is dissolved in toluene etc. and used as a solution for practical purposes such as stripping treatment. . Effects of the Invention According to the present invention, since a solution reaction system using a water-soluble solvent is used, an ethylene-vinyl alcohol copolymer with a high degree of saponification and a high degree of polymerization can be used as a reactant. The introduction ratio of the isocyanate compound can be easily controlled. In addition, it also has the advantage of being able to efficiently obtain a releasable treatment agent with excellent adhesion to the substrate and excellent thermal stability (heat resistance) of peeling properties with a simple operation. Examples Examples 1 to 4 Put ethylene-vinyl alcohol copolymer into a 1000 c.c. four-necked flask equipped with a reflux condenser and water content receiver, add dimethyl sulfoxide and stir to form a solution. do. Next, xylene was added to this solution, and the mixture was refluxed at 140° C. for 2 hours while stirring to remove water. Then, after cooling the system to 100°C, octadecyl isocyanate is added and reacted. The system is constantly maintained in a homogeneous solution state by adding xylene at appropriate times as the reaction progresses, and the reaction is allowed to proceed at 120°C for about 5 hours. During this time, the amount of isocyanate groups remaining in the system is quantified, and the point at which the remaining amount disappears is defined as the end point of the reaction. After the reaction is completed, the reaction solution is poured into 5 times the weight of methanol to precipitate a white precipitate, which is filtered, washed with methanol, and dried and ground to obtain the desired product. The target product consisting of the reactants shown in the table is obtained in the above manner. Comparative Example 1 10 parts (by weight, the same applies hereinafter) of ethylene/vinyl alcohol copolymer (ethylene copolymerization ratio 0.5, average degree of polymerization 1700) was dispersed in 50 parts of xylene, and 45 parts of octadecyl isosuccinate was added to this to make 120 parts. ℃
The reaction is allowed to proceed until the remaining isocyanate groups disappear, and the resulting reaction solution is treated in the same manner as in Examples to obtain the desired product. Comparative Example 2 Using 20 parts of polyvinyl alcohol (degree of saponification 88 mol%, average degree of polymerization 1400), 204 parts of xylene, and 116 parts of octadecyl isocyanate, the desired product was obtained by processing according to Comparative Example 1. Comparative Example 3 Ethylene/vinyl alcohol copolymer (ethylene copolymerization ratio 0.8, vinyl alcohol copolymerization ratio
Although the same operation as in the example was carried out using an average polymerization degree of 0.2 and 1000, the objective could not be achieved as it did not dissolve in dimethyl sulfoxide. Evaluation test A 1% by weight solution was prepared by dissolving the stripping agent as a reaction product obtained in Examples and Comparative Examples in toluene, and this was applied to a cellophane film (thickness: 36 μm).
It is coated on top (solid matter: 0.05 g/m 2 ) and dried to obtain a release-treated film. Next, apply cellophane adhesive tape (No. 29, manufactured by Nitto Electric Industry Co., Ltd.) to the treated surface of the release-treated film, weighing 2 kg.
Press with a rubber roller, heat this in an atmosphere of 20°C or 50°C for 24 hours, and then measure the peeling force by 180 degree peel (pulling speed 300 mm/min). however,
For the products heated at 50°C, they were left in an atmosphere at 20°C for 4 hours after heating. The results are shown in the table.

【表】【table】

【表】【table】

Claims (1)

【特許請求の範囲】 1 エチレン・ビニルアルコール共重合体と炭素
数が8個以上のアルキル基を有するイソシアネー
トとの反応生成物からなる剥離性処理剤を製造す
るにあたり、 水溶性溶媒を用いて溶液状態としたエチレン・
ビニルアルコール共重合体とアルキルイソシアネ
ートとを反応開始から反応終了に至るまでその中
間生成物も含めて溶液状態下で反応させることを
特徴とする剥離性処理剤の製造方法。
[Claims] 1. In producing a stripping treatment agent made of a reaction product of an ethylene/vinyl alcohol copolymer and an isocyanate having an alkyl group having 8 or more carbon atoms, a solution is prepared using a water-soluble solvent. Ethylene
A method for producing a stripping treatment agent, which comprises reacting a vinyl alcohol copolymer and an alkyl isocyanate in a solution state, including their intermediate products, from the start of the reaction to the end of the reaction.
JP24963385A 1985-11-07 1985-11-07 Production of releasable treatment Granted JPS62109804A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP24963385A JPS62109804A (en) 1985-11-07 1985-11-07 Production of releasable treatment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP24963385A JPS62109804A (en) 1985-11-07 1985-11-07 Production of releasable treatment

Publications (2)

Publication Number Publication Date
JPS62109804A JPS62109804A (en) 1987-05-21
JPH0428002B2 true JPH0428002B2 (en) 1992-05-13

Family

ID=17195925

Family Applications (1)

Application Number Title Priority Date Filing Date
JP24963385A Granted JPS62109804A (en) 1985-11-07 1985-11-07 Production of releasable treatment

Country Status (1)

Country Link
JP (1) JPS62109804A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6348304A (en) * 1986-08-14 1988-03-01 Nitto Electric Ind Co Ltd Production of releasable treating agent
JP4857792B2 (en) * 2006-02-02 2012-01-18 三菱化学株式会社 Urethane reaction product and process for producing the same

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6030355B2 (en) * 1979-04-21 1985-07-16 一方社油脂工業株式会社 Peeling agent
JPS56149438A (en) * 1980-04-21 1981-11-19 Kuraray Co Ltd Preparation of ethylene-vinyl alcohol copolymer membrane with improved perfomance
JPS58146405A (en) * 1982-02-24 1983-09-01 Nitto Electric Ind Co Ltd Treatment of permselective ultrafilter membrane

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JPS62109804A (en) 1987-05-21

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