JPH07119256B2 - Method for producing hydroxyl group-containing chlorinated ethylene-vinyl acetate copolymer - Google Patents
Method for producing hydroxyl group-containing chlorinated ethylene-vinyl acetate copolymerInfo
- Publication number
- JPH07119256B2 JPH07119256B2 JP20081689A JP20081689A JPH07119256B2 JP H07119256 B2 JPH07119256 B2 JP H07119256B2 JP 20081689 A JP20081689 A JP 20081689A JP 20081689 A JP20081689 A JP 20081689A JP H07119256 B2 JPH07119256 B2 JP H07119256B2
- Authority
- JP
- Japan
- Prior art keywords
- vinyl acetate
- eva
- hydroxyl group
- ethylene
- acetate 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 - Fee Related
Links
- 239000005038 ethylene vinyl acetate Substances 0.000 title claims description 50
- 229920001200 poly(ethylene-vinyl acetate) Polymers 0.000 title claims description 50
- 125000002887 hydroxy group Chemical group [H]O* 0.000 title claims description 29
- DQXBYHZEEUGOBF-UHFFFAOYSA-N but-3-enoic acid;ethene Chemical class C=C.OC(=O)CC=C DQXBYHZEEUGOBF-UHFFFAOYSA-N 0.000 title claims description 11
- 238000004519 manufacturing process Methods 0.000 title claims description 8
- 239000000460 chlorine Substances 0.000 claims description 9
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 claims description 8
- 229910052801 chlorine Inorganic materials 0.000 claims description 8
- 239000011248 coating agent Substances 0.000 claims description 8
- 229920001577 copolymer Polymers 0.000 claims description 8
- -1 polypropylene Polymers 0.000 claims description 8
- 239000004743 Polypropylene Substances 0.000 claims description 7
- 239000003973 paint Substances 0.000 claims description 7
- 230000001070 adhesive effect Effects 0.000 claims description 6
- 238000005660 chlorination reaction Methods 0.000 claims description 6
- 239000000976 ink Substances 0.000 claims description 6
- 229920001155 polypropylene Polymers 0.000 claims description 6
- 238000007127 saponification reaction Methods 0.000 claims description 6
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical compound CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 claims description 5
- 239000000835 fiber Substances 0.000 claims description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 5
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims description 4
- 239000005977 Ethylene Substances 0.000 claims description 4
- 239000000853 adhesive Substances 0.000 claims description 4
- 239000003960 organic solvent Substances 0.000 claims description 4
- 239000003795 chemical substances by application Substances 0.000 claims description 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims 2
- 125000000816 ethylene group Chemical group [H]C([H])([*:1])C([H])([H])[*:2] 0.000 claims 1
- 229920000642 polymer Polymers 0.000 description 22
- 239000002904 solvent Substances 0.000 description 11
- 239000000126 substance Substances 0.000 description 9
- 238000000034 method Methods 0.000 description 7
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 6
- 230000000052 comparative effect Effects 0.000 description 6
- 238000006243 chemical reaction Methods 0.000 description 5
- 238000000576 coating method Methods 0.000 description 5
- 229920005989 resin Polymers 0.000 description 5
- 239000011347 resin Substances 0.000 description 5
- 239000005026 oriented polypropylene Substances 0.000 description 4
- 239000000243 solution Substances 0.000 description 4
- VZGDMQKNWNREIO-UHFFFAOYSA-N tetrachloromethane Chemical compound ClC(Cl)(Cl)Cl VZGDMQKNWNREIO-UHFFFAOYSA-N 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- KZBUYRJDOAKODT-UHFFFAOYSA-N Chlorine Chemical compound ClCl KZBUYRJDOAKODT-UHFFFAOYSA-N 0.000 description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 238000005481 NMR spectroscopy Methods 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000005227 gel permeation chromatography Methods 0.000 description 3
- 238000005259 measurement Methods 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 description 2
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 2
- 239000003708 ampul Substances 0.000 description 2
- 238000007033 dehydrochlorination reaction Methods 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 238000004090 dissolution Methods 0.000 description 2
- 125000000524 functional group Chemical group 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000000155 melt Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000000465 moulding Methods 0.000 description 2
- 239000008096 xylene Substances 0.000 description 2
- 229920000298 Cellophane Polymers 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- 125000003668 acetyloxy group Chemical group [H]C([H])([H])C(=O)O[*] 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 238000000149 argon plasma sintering Methods 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- 229920006378 biaxially oriented polypropylene Polymers 0.000 description 1
- 239000011127 biaxially oriented polypropylene Substances 0.000 description 1
- 238000011088 calibration curve Methods 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 125000001309 chloro group Chemical group Cl* 0.000 description 1
- 238000004132 cross linking Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 229910010272 inorganic material Inorganic materials 0.000 description 1
- 239000011147 inorganic material Substances 0.000 description 1
- 239000001023 inorganic pigment Substances 0.000 description 1
- 239000012948 isocyanate Substances 0.000 description 1
- 150000002513 isocyanates Chemical class 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000000691 measurement method Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 125000000896 monocarboxylic acid group Chemical group 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 229920006113 non-polar polymer Polymers 0.000 description 1
- 239000011368 organic material Substances 0.000 description 1
- 230000003204 osmotic effect Effects 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 239000004014 plasticizer Substances 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 239000002861 polymer material Substances 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 229920002635 polyurethane Polymers 0.000 description 1
- 239000004814 polyurethane Substances 0.000 description 1
- 229920002689 polyvinyl acetate Polymers 0.000 description 1
- 239000011118 polyvinyl acetate Substances 0.000 description 1
- 230000001376 precipitating effect Effects 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 238000000425 proton nuclear magnetic resonance spectrum Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 229920001897 terpolymer Polymers 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 238000011282 treatment Methods 0.000 description 1
- 150000005671 trienes Chemical class 0.000 description 1
- 238000009281 ultraviolet germicidal irradiation Methods 0.000 description 1
- 229920002554 vinyl polymer Polymers 0.000 description 1
Landscapes
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明はインク用、接着剤用、コーテイング剤用、塗料
用、ポリプロピレン成型品等の種々なプライマー用又は
繊維類処理剤用等の用途に使用される水酸基含有塩素化
エチレン−酢酸ビニル系共重合体の製造法に関するもの
である。DETAILED DESCRIPTION OF THE INVENTION [Industrial field of application] The present invention is applied to various uses such as inks, adhesives, coating agents, paints, various types of primers such as polypropylene moldings, or fibers treating agents. The present invention relates to a method for producing a chlorinated ethylene-vinyl acetate-based copolymer used.
一般にエチレン−酢酸ビニル共重合体(EVAと略称)を
四塩化炭素などのそれ自身は塩素化されない有機溶媒中
に均一に溶解して塩素化すると塩素化エチレン−酢酸ビ
ニル共重合体(本発明ではCl-EVAと略称)が得られる。Generally, ethylene-vinyl acetate copolymer (abbreviated as EVA) is chlorinated by uniformly dissolving it in an organic solvent such as carbon tetrachloride that is not itself chlorinated and chlorinated (in the present invention, Cl-EVA) is obtained.
Cl-EVAを得る方法としてはこのほか反応速度を大きくす
るために又は系全体の反応温度を低く抑えるために紫外
線照射下で塩素化を行なう例もある。(特公昭58-2099
0,特開昭48-4797,特公昭47-46203) 上記の様にして非水系で塩素化して得られたCl-EVAはポ
リマー分子中に塩素基、アセトキシ基などを含んだCl-E
VAであるが、Cl-EVA分子内には水酸基は全く含まれてい
ない。As another method for obtaining Cl-EVA, there is an example in which chlorination is performed under UV irradiation in order to increase the reaction rate or to keep the reaction temperature of the entire system low. (Japanese Patent Publication Sho 58-2099
0, JP-A-48-4797, JP-B-47-46203) Cl-EVA obtained by chlorination in a non-aqueous system as described above is Cl-E containing a chlorine group or an acetoxy group in the polymer molecule.
Although it is VA, no hydroxyl group is contained in the Cl-EVA molecule.
現在Cl-EVAはポリプロピレン系樹脂成型品用などのプラ
イマー、塗料、インキ組成物、繊維類などに広く使用さ
れている。At present, Cl-EVA is widely used for primers such as polypropylene resin molded products, paints, ink compositions, and fibers.
これらの用途は何れもポリプロピレン系樹脂等の無極性
ポリマーに対する良好な付着性、優れた耐熱性、耐候
性、対薬品性に起因するものである。All of these uses result from good adhesion to nonpolar polymers such as polypropylene resins, excellent heat resistance, weather resistance, and chemical resistance.
上記したように優れた性質を有するCl-EVAは分子中にOH
基、NH基、又はCOOH基などの反応性官能基を有しないた
め架橋反応を行なわしめることは不可能であり、またイ
ンク用又は塗料用などの顔料あるいはフイラーなどの有
機系又は無機系物質に対する親和性や分散性には自ずか
ら限度があつた。As described above, Cl-EVA, which has excellent properties, has OH in the molecule.
Since it does not have a reactive functional group such as group, NH group, or COOH group, it is impossible to carry out a crosslinking reaction, and also for organic or inorganic substances such as pigments or fillers for inks or paints. There was a natural limit to affinity and dispersibility.
そのため従来のCl-EVAは芳香族石油樹脂などの他の樹脂
とのブレンドを行なうことにより塗膜硬度、スプレー性
の改善などが行なわれていた。Therefore, conventional Cl-EVA has been improved in coating hardness and sprayability by blending with other resins such as aromatic petroleum resins.
しかしながらこれらはすべて混合系であるため長期間紫
外線などのエネルギーにばく露すると可塑剤等が離脱し
て塗膜が脆くなり、やがて亀裂などが生じ表面保護機能
を失いがちである。本発明は上記の点に着目し、Cl-EVA
分子内に水酸基を含有せしめることにより他の無機材料
又は有機材料との親和性を向上させると同時に、反応性
官能基を有し、例えばイソシアネートと反応させること
によつてポリウレタン系Cl-EVAとして高分子設計上任意
のデザインを可能ならしめるポリマー素材の開発ができ
るようになる新規な共重合分子内に水酸基を含有したCl
-EVAの製造法を提供することを目的とするものである。However, since these are all mixed systems, when exposed to energy such as ultraviolet rays for a long period of time, the plasticizer and the like are released and the coating film becomes brittle, and eventually cracks are likely to occur and the surface protection function tends to be lost. The present invention focuses on the above-mentioned point, and Cl-EVA
By improving the affinity with other inorganic materials or organic materials by containing a hydroxyl group in the molecule, at the same time it has a reactive functional group, for example, by reacting with isocyanate high polyurethane-based Cl-EVA A new copolymer that allows the development of polymer materials that enable any design in molecular design. Cl containing a hydroxyl group in the molecule.
-The purpose is to provide a manufacturing method of EVA.
本発明はEVAなどを塩素系有機溶剤及び水の存在下で塩
素化反応と同時にケン化反応を行なわしめて水酸基含有
塩素化エチレン−酢酸ビニル系共重合体の製造法並びに
かくして得られた分子内に水酸基を含有する塩素化エチ
レン−酢酸ビニル系共重体をインキ用、接着剤用、コー
ティング用、塗料用、ポリプロビレン成型品等のプライ
マー用又は繊維類処理剤用等に使用することを特徴とす
る水酸基含有塩素化エチレン−酢酸ビニル系共重合体の
製造法に関するものである。The present invention is a method for producing a hydroxyl group-containing chlorinated ethylene-vinyl acetate copolymer by performing a saponification reaction simultaneously with chlorination reaction of EVA or the like in the presence of a chlorine-based organic solvent and water, and in the molecule thus obtained. A hydroxyl group characterized by using a chlorinated ethylene-vinyl acetate copolymer containing a hydroxyl group for an ink, an adhesive, a coating, a paint, a primer such as a polypropylene molding product, or a fiber treating agent. The present invention relates to a method for producing a chlorinated ethylene-vinyl acetate copolymer.
本発明に使用されるEVAはエチレンと酢酸ビニルとの共
重合体でEVA100重量%に対してエチレン成分が95〜5重
量%、酢酸ビニル成分が5〜95重量%のものであり、こ
れらから得られたCl-EVAの塩素含有量は5〜50重量%ま
で塩素化したものであり、同時にケン化度が0.1〜95重
量%までケン化したものである。The EVA used in the present invention is a copolymer of ethylene and vinyl acetate, and has 95 to 5% by weight of ethylene component and 5 to 95% by weight of vinyl acetate component based on 100% by weight of EVA. The chlorine content of the obtained Cl-EVA was chlorinated to 5 to 50% by weight, and at the same time, the degree of saponification was saponified to 0.1 to 95% by weight.
本発明の水酸基含有Cl-EVAには水酸基含有塩素化エチレ
ン−酢酸ビニルのほか、加水分解し得るエチレン系ポリ
マー例えばエチレン−酢酸ビニル−一酸化炭素共重合物
などのターポリマー、更に部分鹸化EVAも含まれる。酢
酸ビニル(又は本発明に含まれるコモノマー)の含有量
を上記5〜95重量%としたのは5%未満ではポリエチレ
ンの性質に近くなり、ケン化及び塩素化を行なつても水
酸基の導入量が少なく、本発明の目的を達成するのが困
難であり、逆に酢酸ビニル含有量が95%を超過するとポ
リ酢酸ビニルの性質が強くなつて、例えばポリプロピレ
ン系樹脂への密着性が劣るようになる。The hydroxyl group-containing Cl-EVA of the present invention includes hydroxyl group-containing chlorinated ethylene-vinyl acetate, hydrolyzable ethylene-based polymers such as ethylene-vinyl acetate-terpolymer such as carbon monoxide copolymer, and partially saponified EVA. included. The content of vinyl acetate (or comonomer contained in the present invention) is set to 5 to 95% by weight as described above. When it is less than 5%, the property is close to that of polyethylene. Is less, it is difficult to achieve the object of the present invention, conversely, when the vinyl acetate content exceeds 95%, the property of polyvinyl acetate becomes stronger, and for example, the adhesion to polypropylene resin becomes poor. Become.
次に実施例によつて本発明を説明する。 Next, the present invention will be described with reference to examples.
実施例1 本発明のOH基含有Cl-EVAは原料EVA75gを耐塩素系溶剤例
えば四塩化炭素又はパークレン又はトリクレン等の溶剤
600gに溶解した後、水75mlを加えて均一又は不均一に塩
素含有量が5〜50重量%になるまで塩素ガスを吹込んで
塩素化した後空気又は窒素で、残留する未反応の塩素を
脱気させるため0.5〜5Kg/cm2Gの水蒸気を吹込んで溶剤
を追出したのち脱溶剤装置によつてペレツト化するか又
は塩素系溶剤をトルエン、キシレン等の汎用溶剤と置換
して均一溶液として得られる。さらに脱溶剤して本発明
の水酸基含有Cl-EVA103gが得られる。収率はEVAに対し
て99%であつた。Example 1 For the OH group-containing Cl-EVA of the present invention, 75 g of the raw material EVA was used as a chlorine-resistant solvent such as carbon tetrachloride or a solvent such as perchlorene or trichlene.
After dissolving in 600 g, add 75 ml of water and blow chlorine gas evenly or non-uniformly until the chlorine content becomes 5 to 50% by weight, then chlorinate and remove residual unreacted chlorine with air or nitrogen. In order to vaporize it, blow steam of 0.5 to 5 kg / cm 2 G to expel the solvent and then pelletize it with a desolventizer, or replace the chlorine-based solvent with a general-purpose solvent such as toluene or xylene to form a uniform solution can get. Further, the solvent is removed to obtain 103 g of the hydroxyl group-containing Cl-EVA of the present invention. The yield was 99% based on EVA.
上記塩素系反応は80〜150℃で行ない得られるが、好ま
しくは90〜120℃である。あまりに温度が低すぎると塩
素化の反応速度及びケン化の反応速度が小さくなり、ま
た反面温度を上げすぎると塩素化及びケン化の反応速度
が大きくなり、場合によつては一旦塩素化されたポリマ
ーが局部加熱により脱塩酸を起し、黒化するので上記適
正温度範囲に保つのがよい。The above chlorine-based reaction can be carried out at 80 to 150 ° C, preferably 90 to 120 ° C. If the temperature is too low, the chlorination reaction rate and the saponification reaction rate will decrease, while if the temperature is too high, the chlorination and saponification reaction rates will increase, and in some cases, once chlorinated. It is preferable to keep the temperature within the above-mentioned appropriate temperature range because the polymer causes dehydrochlorination due to local heating and becomes black.
なお塩素ガスの吹込みは徐々に行ない、吹込量は大きく
しない方が、局部加熱による脱塩酸を避けるために必要
である。Note that it is necessary to gradually blow chlorine gas and not to increase the amount of chlorine gas in order to avoid dehydrochlorination due to local heating.
本発明の方法によつて得られた水酸基含有塩素化エチレ
ン酢酸共重合体の特性は、主として導入された水酸基に
よるものである。水の非共存下で得られたCl-EVAと上記
本発明の方法によつて得られた水酸基含有Cl-EVAとの特
性を下記に比較する。The characteristics of the hydroxyl group-containing chlorinated ethylene acetic acid copolymer obtained by the method of the present invention are mainly due to the introduced hydroxyl group. The characteristics of Cl-EVA obtained in the absence of water and the hydroxyl group-containing Cl-EVA obtained by the above method of the present invention are compared below.
(1)赤外線吸収特性(IR) 第1図、第3図、第5図、第6図に本発明の水酸基含有
Cl-EVA(以下本発明のポリマーという)のIRチヤート
を、第2図、第4図に従来の非水系反応によつて得られ
た水酸基を含有しないCl-EVA(従来のCl-EVAという)の
IRチヤートを示した。(1) Infrared absorption characteristic (IR) In FIG. 1, FIG. 3, FIG. 5 and FIG.
An IR chart of Cl-EVA (hereinafter referred to as a polymer of the present invention) is shown in FIGS. 2 and 4 in which a hydroxyl group-free Cl-EVA (conventional Cl-EVA) obtained by a conventional non-aqueous reaction is used. of
IR chart was shown.
第1図、第3図、第5図、第6図より本発明のポリマー
には3200〜3600cm-1に何れもOH基の吸収が認められる。
一方従来のCl-EVAの比較物質にはOH基の吸収が認められ
ない。From FIGS. 1, 3, 5, and 6, the polymers of the present invention show absorption of OH groups at 3200 to 3600 cm −1 .
On the other hand, no absorption of OH group is observed in the conventional comparative substance of Cl-EVA.
更に表−1にIR測定試料について、本発明のポリマーと
比較物質、(従来のCl-EVA)についてその性質を比較し
た。Further, in Table 1, the properties of the IR measurement sample were compared for the polymer of the present invention and the comparative substance, (conventional Cl-EVA).
表−1の注:1)〜5) 1)ケン化法により行つた。 Note to Table-1: 1) to 5) 1) The saponification method was used.
2)▲▼は光散乱法で、▲▼は浸透圧法で求め
た。2) ▲ ▼ was obtained by a light scattering method, and ▲ ▼ was obtained by an osmotic pressure method.
3)クロロホルムを移動相とし、ゲル浸透クロマトグラ
フイー(GPC)で測定した。カラムはShodex GPC AC-80
4,803,802.5(商品名)を連結して用いた。検量線は標
準ポリスチレンの各▲▼=233,000、92,600、19,00
0、9,000、2,100及び800を用いて作製した。3) Chloroform was used as a mobile phase, and measurement was performed by gel permeation chromatography (GPC). Column is Shodex GPC AC-80
4,803,802.5 (trade name) was used in combination. Calibration curves are standard polystyrene ▲ ▼ = 233,000, 92,600, 19,00
It was prepared using 0, 9,000, 2,100 and 800.
4)JISK-6730に準じて、塩素化EVAを0.2〜0.5g精秤
し、キシレン100mlに溶解させた後、0.2N-NaOHメタノー
ル溶液60mlを加え、加水分解を完全に行なわしめ、水層
/油層を分液し、0.4N-HCl水溶液30mlを加え、フリーの
酢酸分を定量する。4) According to JIS K-6730, 0.2-0.5 g of chlorinated EVA was precisely weighed and dissolved in 100 ml of xylene, then 60 ml of 0.2N-NaOH methanol solution was added to completely hydrolyze the water layer / The oil layer is separated, 30 ml of 0.4N-HCl aqueous solution is added, and free acetic acid content is quantified.
5)すべてポリマーの希薄トリエン溶液から大量のメタ
ノール中に沈澱させて精製、乾燥させたポリマーをトル
エン溶液として再溶解させた状態からキヤストフイルム
としたものを用いた。5) A cast film was prepared by re-dissolving a polymer obtained by precipitating a polymer from a dilute triene solution of the polymer in a large amount of methanol, and then drying the polymer.
6)メルトフローレート 本発明のOH含有Cl-EVAのメルトフローレート(MFR)をA
STM-D-1238-57Tに基いて測定した。測定結果を表−1に
示した。6) Melt flow rate The melt flow rate (MFR) of OH-containing Cl-EVA of the present invention is A
It was measured based on STM-D-1238-57T. The measurement results are shown in Table-1.
メルトフローレートが1g/10分以下になると有機溶剤に
対する溶解性が悪くなり、500g/10分以上になると分子
量が小さくなりすぎ接着剤やコーテイング剤として実用
に耐えなくなる。If the melt flow rate is 1 g / 10 minutes or less, the solubility in organic solvents will be poor, and if it is 500 g / 10 minutes or more, the molecular weight will be too small to be practically used as an adhesive or coating agent.
(2)水酸基価 表−1より明かなように比較物質(従来のCl-EVA)は何
れも水酸基価が0なのに対して、本発明のポリマーは20
〜72KOH mg/gの水酸基価を有することがわかる。(2) Hydroxyl value As is clear from Table 1, the comparative substances (conventional Cl-EVA) all have a hydroxyl value of 0, whereas the polymer of the present invention has a hydroxyl value of 20.
It can be seen that it has a hydroxyl value of ˜72 KOH mg / g.
(3)核磁気共鳴(プロトンNMR) 本発明の新規ポリマー(表−1物質No.4)についてのNM
Rチヤートを第7図に示した。本発明のポリマー、表−
1のNo.1、No.3のNMRチヤートは各ピークの面積比が異
なるのみで基本的には第7図と大差はない。なお溶媒は
CDCl3を、また内部標準としてはベンゼンを使用した。(3) Nuclear magnetic resonance (proton NMR) NM of the novel polymer of the present invention (Table-1 substance No. 4)
The R chart is shown in FIG. Polymers of the invention, Table-
The No. 1 and No. 3 NMR charts of No. 1 are basically the same as those of FIG. 7 except that the area ratio of each peak is different. The solvent is
CDCl 3 was used and benzene was used as an internal standard.
(4)対溶剤、溶解特性 本発明の新規ポリマー1,2(表−1)を相当する比較物
質(従来のCl-EVA)(1),(2)と対比する形で溶剤
のSP値(溶解性パラメーター)(δh,δp)を用いて整
理した結果を表−2、表−3及び第8図〜第11図に示し
た。(測定方法) 50mgのポリマー(乾燥)と1.0gの溶媒をアンプル中に封
入し一晩膨閏させた後、130℃のオイルバス中で1時間
放置し、以後100℃になつてから1時間、更に25℃で1
時間、かつ冷凍機を使用して10℃で1時間それぞれ恒温
とした後のアンプル液の透明性により各温度における溶
解、不溶の何れかを判断した。上記第8図〜第10図より
本発明のポリマーは比較物質(従来のCl-EVA)に比較し
てδpの溶解領域がやや高い方に存在することがわか
る。(4) Solvent / Solubility Property The SP value of the solvent in the form of comparing the novel polymers 1 and 2 (Table 1) of the present invention with corresponding comparative substances (conventional Cl-EVA) (1) and (2) ( Solubility parameters) ([delta] h, [delta] p) are used for the results, and the results are shown in Tables 2 and 3 and FIGS. 8 to 11. (Measurement method) 50 mg of polymer (dry) and 1.0 g of solvent were sealed in an ampoule, allowed to swell overnight, and then left in an oil bath at 130 ° C for 1 hour, then 1 hour after reaching 100 ° C. , 1 at 25 ℃
Whether it was dissolved or insoluble at each temperature was judged based on the transparency of the ampoule liquid after being kept at a constant temperature of 10 ° C. for 1 hour using a refrigerator. It can be seen from FIGS. 8 to 10 that the polymer of the present invention has a slightly higher dissolution region of δp than the comparative substance (conventional Cl-EVA).
これはポリマー中に導入されたOHの効果によるものであ
る。第8図、第9図、第10図、第11図共に、ポリマー/
溶媒=5(重量)/100(重量)とした。This is due to the effect of OH incorporated in the polymer. Polymers shown in FIG. 8, FIG. 9, FIG. 10, and FIG.
Solvent = 5 (weight) / 100 (weight).
〔発明の効果〕 本発明の効果を纒めると次の通りである。 [Effects of the Invention] The effects of the present invention are summarized as follows.
(i)本発明のOH基含有Cl-EVAはその含有するOH基に起
因する良好な耐溶解性を生かして例えば自動車バンパー
のプライマーなどの自動車塗料、OH基含有による無機質
顔料との良好な親和性に起因する優れた発色性を持つイ
ンキ組成物、塗料、各種のプライマーや繊維処理用など
に広く利用することができる。(I) The OH group-containing Cl-EVA of the present invention makes good use of the good resistance to dissolution due to the contained OH groups, and thus has a good affinity with, for example, automobile paints such as automobile bumper primers and inorganic pigments containing OH groups. It can be widely used for ink compositions, paints, various primers and fiber treatments, etc., which have excellent color development due to their properties.
(ii)接着特性 表−4に本発明のOH基含有Cl-EVAの接着特性を示した。(Ii) Adhesive Properties Table 4 shows the adhesive properties of the OH group-containing Cl-EVA of the present invention.
表−4により本発明のOH基含有Cl-EVAは対OPP密着性、O
PP/OPP剥離強度について何れも比較物質として使用した
従来のCl-EVAを上廻る性能を有することがわかる。According to Table-4, the OH group-containing Cl-EVA of the present invention has an adhesion to OPP, O
It can be seen that the PP / OPP peel strength is superior to that of the conventional Cl-EVA used as a comparative substance.
(方法) 対OPP密着性:2軸延伸ポリプロピレンフイルム(OPP)
(厚さ60μ;TOYOBO(株)製)上にポリマーのトルエン
溶液を塗布して80℃の温風で30分間強制乾燥した後、1
晩風乾した塗膜に対し、巾0.5cmの井げたに切目を作
り、ニチバン(株)製セロハンテープで5回はがして、
そのはがれた回数目を表示する。このテストを井げたの
5個に対して行い、その平均値を取る。 (Method) Adhesion to OPP: Biaxially oriented polypropylene film (OPP)
(Thickness 60μ; manufactured by TOYOBO Co., Ltd.) was coated with a toluene solution of the polymer, and was forcibly dried with warm air at 80 ° C for 30 minutes, and then 1
Make a notch in the width of 0.5 cm for the air-dried coating film and peel it off 5 times with cellophane tape made by Nichiban Co., Ltd.
The number of times it has peeled off is displayed. This test is carried out on 5 wells and the average value is taken.
剥離強度:上記の乾燥塗膜フイルムに対し、130℃、1Kg
/cm2Gで1秒間ヒートシールした後、1時間室温で養生
したものを、巾0.9cmに切断し1cm当りの剥離強度を求め
た。Peel strength: 130 ° C, 1Kg against the above dry coating film
After heat-sealing at / cm 2 G for 1 second, the material was aged at room temperature for 1 hour, cut into a width of 0.9 cm, and the peel strength per 1 cm was determined.
第1図、第3図、第5図、第6図は本発明の新規ポリマ
ーのIRチヤート、第2図、第4図は従来のCl-EVAのIRチ
ヤート、第7図は本発明の新規ポリマーのNMRチヤート
の図、第8図、図−10は本発明の新規ポリマーの溶解性
を示すδp−δh図、第9図、第11図は比較物質従来の
Cl-EVAの溶解性を示すδp−δhの図である。1, 3, 5, and 6 are IR charts of the novel polymer of the present invention, FIGS. 2 and 4 are IR charts of conventional Cl-EVA, and FIG. 7 is a novel chart of the present invention. The NMR chart of the polymer, FIG. 8 and FIG. 10 show the solubility of the novel polymer of the present invention. FIG. 9 and FIG.
It is a figure of (delta) p- (delta) h which shows the solubility of Cl-EVA.
Claims (3)
機溶剤及び水の存在下で塩素化反応と同時に鹸化反応を
行わしめることを特徴とする水酸基含有塩素化エチレン
−酢酸ビニル系共重合体の製造法。1. A hydroxyl group-containing chlorinated ethylene-vinyl acetate copolymer characterized in that an ethylene-vinyl acetate copolymer is subjected to a saponification reaction simultaneously with a chlorination reaction in the presence of a chlorine-based organic solvent and water. Manufacturing method.
チレン成分が95〜5重量%、酢酸ビニル成分が5〜95重
量%のエチレン酢酸ビニル系共重合体を使用することを
特徴とする請求項1記載の水酸基含有塩素化エチレン−
酢酸ビニル系共重合体の製造法。2. An ethylene vinyl acetate-based copolymer having an ethylene component of 95 to 5 wt% and a vinyl acetate component of 5 to 95 wt% in the ethylene vinyl acetate-based copolymer is used. Hydrochloric acid-containing chlorinated ethylene described
A method for producing a vinyl acetate copolymer.
素化エチレン−酢酸ビニル系共重合体を、インク用、接
着剤用、コーティング剤用、塗料用、ポリプロピレン成
型品等のプロイマー用又は繊維類処理剤用に使用するこ
とを特徴とする請求項1記載の水酸基含有塩素化エチレ
ン−酢酸ビニル系共重合体の製造法。3. The hydroxyl group-containing chlorinated ethylene-vinyl acetate copolymer produced according to claim 1 for use in inks, adhesives, coating agents, paints, polypropylene, etc., or fibers. The method for producing a hydroxyl group-containing chlorinated ethylene-vinyl acetate copolymer according to claim 1, which is used as a treating agent.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP20081689A JPH07119256B2 (en) | 1989-08-01 | 1989-08-01 | Method for producing hydroxyl group-containing chlorinated ethylene-vinyl acetate copolymer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP20081689A JPH07119256B2 (en) | 1989-08-01 | 1989-08-01 | Method for producing hydroxyl group-containing chlorinated ethylene-vinyl acetate copolymer |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0364304A JPH0364304A (en) | 1991-03-19 |
| JPH07119256B2 true JPH07119256B2 (en) | 1995-12-20 |
Family
ID=16430675
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP20081689A Expired - Fee Related JPH07119256B2 (en) | 1989-08-01 | 1989-08-01 | Method for producing hydroxyl group-containing chlorinated ethylene-vinyl acetate copolymer |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH07119256B2 (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100343348C (en) * | 2005-12-07 | 2007-10-17 | 江苏常铝铝业股份有限公司 | Hot sealing coating for calorifier aluminum foil, and its preparation method and coating method |
| JP7767889B2 (en) * | 2021-12-09 | 2025-11-12 | 東ソー株式会社 | Hydroxyl-containing chlorosulfonated polyolefin |
| JP2023132945A (en) * | 2022-03-11 | 2023-09-22 | 東ソー株式会社 | Urethane resin forming composition and two-component adhesive |
-
1989
- 1989-08-01 JP JP20081689A patent/JPH07119256B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0364304A (en) | 1991-03-19 |
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