JPS61275311A - Curable fluoroolefin copolymer and its production - Google Patents
Curable fluoroolefin copolymer and its productionInfo
- Publication number
- JPS61275311A JPS61275311A JP60281932A JP28193285A JPS61275311A JP S61275311 A JPS61275311 A JP S61275311A JP 60281932 A JP60281932 A JP 60281932A JP 28193285 A JP28193285 A JP 28193285A JP S61275311 A JPS61275311 A JP S61275311A
- Authority
- JP
- Japan
- Prior art keywords
- mol
- vinyl ether
- vinyl
- fluoroolefin
- 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.)
- Granted
Links
Abstract
Description
【発明の詳細な説明】
本発明は新規の架橋硬化可能なフルオロオレフィン共重
合体とその製造方法に関するものであり、更に詳しくは
フルオロオレフィン、カルボン酸ビニルエステル、ビニ
ルエーテル、水酸基含有ビニルエーテルからなる架橋硬
化可能なフルオロオレフィン共重合体に関するものであ
る。また、この共重合体を製造するにあたり、各々のモ
ノマーの共重合反応性を利用した収率の高い製造方法に
関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a novel crosslinkable curable fluoroolefin copolymer and a method for producing the same. The present invention relates to possible fluoroolefin copolymers. The present invention also relates to a method for producing this copolymer with high yield by utilizing the copolymerization reactivity of each monomer.
(従来の技術及びその問題点)
フルオロオレフィンポリマーは、耐薬品性、耐熱性、耐
摩耗性、非粘着性等の性質を有しているため広く用いら
れているが、反面、融点が高いため、高温での溶融、焼
付を必要とする。また、溶剤に溶けないためにエマルジ
ョンあるいはディスパージョンの形態でしか使用できず
貯蔵安定性の良好な塗料には適さないものであった。こ
のような欠点を改良し、しかも架橋硬化性を向上せしめ
るために、例えば特開昭57−34107号ではフルオ
ロオレフィン、シクロヘキシルビニルエーテル、アルキ
ルビニルエーテル及びヒドロキシアルキルビニルエーテ
ルからなる共重合体をイソシアネート、メラミン等で硬
化させる方法が提案されている。しかし、かかる共重合
体はインシアネート等の硬化剤との相溶性が必ずしも満
足できず、又、原料のシクロヘキシルビニルエーテルは
特殊なモノマーであり、一般には入手し難い問題がある
。(Prior art and its problems) Fluoroolefin polymers are widely used because they have properties such as chemical resistance, heat resistance, abrasion resistance, and non-adhesion, but on the other hand, they have a high melting point. , requires melting and baking at high temperatures. Furthermore, since it is not soluble in solvents, it can only be used in the form of an emulsion or dispersion, making it unsuitable for paints with good storage stability. In order to improve these drawbacks and improve the crosslinking curability, for example, in JP-A No. 57-34107, a copolymer consisting of fluoroolefin, cyclohexyl vinyl ether, alkyl vinyl ether, and hydroxyalkyl vinyl ether was mixed with isocyanate, melamine, etc. A method of curing has been proposed. However, such copolymers do not necessarily have satisfactory compatibility with curing agents such as incyanate, and the raw material cyclohexyl vinyl ether is a special monomer that is generally difficult to obtain.
(問題点を解決するための手段)
本発明者らは、フルオロオレフィンポリマーの欠点を改
良するために研究を重ねた結果、フルオロオレフィン、
カルボン酸ビニルエステル、ビニルエーテル、水酸基含
有ビニルエ」チルからなる特定組成の四元共重合体によ
り、安価で架橋硬化性を持った共重合体を見い出し、更
に、この共重合体を製造する過程において、各々のモノ
マー仕込み組成を規定することによって、収率が高くな
る事実を見出し本発明に至った。(Means for Solving the Problems) As a result of repeated research to improve the drawbacks of fluoroolefin polymers, the present inventors have found that fluoroolefins,
Using a quaternary copolymer of a specific composition consisting of carboxylic acid vinyl ester, vinyl ether, and hydroxyl group-containing vinyl ethyl, we discovered an inexpensive copolymer with crosslinking and curable properties, and in the process of producing this copolymer, It was discovered that the yield can be increased by specifying the composition of each monomer charged, leading to the present invention.
本発明は下記一般式(A)なる構造を有するフルオロオ
レフィン10〜70モル%、と下記一般式(B)なる構
造を有するカルボン酸ビニルエステル5〜70モル%と
炭素数1〜8までのアルキル基を有するビニルエーテル
5〜70モル%及び下記一般式(C)なる構造を有する
水酸基含有ビニルエー−ナル6,5〜30
有粘度がα05〜2.0dl/77、水酸基価が17〜
200〜KOH/IIであるフルオロオレフィン共重合
体、及び該フルオロオレフィンaモル%、該ビニルエー
テル6モル%、該水酸基含有ビニルエーテルCモル%、
該カルボン酸ビニルエステルdモル%トシタ場合、
[17(b+c)≦a+d<3.5 ( b+c )を
満足する溶液をラジカル開始剤の存在下−20℃〜16
0℃の温度にて重合せしめることを特徴とする該フルオ
ロオレフィン共重合体の製造方法を提供するものである
。The present invention comprises 10 to 70 mol% of a fluoroolefin having a structure represented by the following general formula (A), 5 to 70 mol% of a carboxylic acid vinyl ester having a structure represented by the following general formula (B), and an alkyl having 1 to 8 carbon atoms. 5 to 70 mol% of vinyl ethers having a group and 6,5 to 30 hydroxyl group-containing vinyl ethers having a structure of the following general formula (C), a viscosity of α05 to 2.0 dl/77, and a hydroxyl value of 17 to 30.
200 to KOH/II, and the fluoroolefin A mol%, the vinyl ether 6 mol%, the hydroxyl group-containing vinyl ether C mol%,
In the case of the carboxylic acid vinyl ester d mol% Toshita, a solution satisfying [17(b+c)≦a+d<3.5 (b+c) is heated at -20°C to 16°C in the presence of a radical initiator.
The present invention provides a method for producing the fluoroolefin copolymer, which is characterized in that the fluoroolefin copolymer is polymerized at a temperature of 0°C.
記
H
0 水素基である。)
本発明で用いられるフルオロオレフィンは一般式体)で
示されるものである。H 0 is a hydrogen group. ) The fluoroolefins used in the present invention are represented by the general formula ().
特に好ましくは、テトラフルオロエチレン、クロロトリ
フルオ四エチレン、へ牛すフルオロプロピレンカ用いラ
レる。その含有量は、共重合体中10〜70モル%であ
り、好ましくは20〜60モル%である。かかる含有量
が10モル%未満では耐候性が不充分であり、70モル
%を越えると硬化物の光沢が低くなる。カルボン酸ビニ
ルエステルは一般式(B)で示されるものが使用される
。Particularly preferred are tetrafluoroethylene, chlorotrifluorotetraethylene, and fluoropropylene. Its content in the copolymer is 10 to 70 mol%, preferably 20 to 60 mol%. If the content is less than 10 mol%, weather resistance will be insufficient, and if it exceeds 70 mol%, the gloss of the cured product will be low. As the carboxylic acid vinyl ester, those represented by general formula (B) are used.
0 素基である。)
例示すれば、酢酸ビニル、プロピオン酸ビニル、酪酸ビ
ニル、ビバリ酸ビニル、カプロン酸ビニル、バーサチッ
ク酸ビニル(C9〜,0のカルボン酸のビニルエステル
)、ラウリン酸ビニル、ステアリン酸ビニル、安息香酸
ビニル、p−t−ブチル安息香酸ビニル、サリチル酸ビ
ニル、シクロヘキサンカルボン酸ビニル等であり、好ま
しくは、少量で塗膜硬度を向上させるバーサチック酸ビ
ニル、シクロヘキサンカルボン酸ビニル、安息香酸ビニ
ル、p−t−ブチル安息香酸ビニルが用いられる。0 It is an elementary group. ) Vinyl acetate, vinyl propionate, vinyl butyrate, vinyl bivalate, vinyl caproate, vinyl versatate (vinyl ester of C9-,0 carboxylic acid), vinyl laurate, vinyl stearate, vinyl benzoate. , vinyl pt-butylbenzoate, vinyl salicylate, vinyl cyclohexanecarboxylate, etc., and preferably vinyl versatate, vinyl cyclohexanecarboxylate, vinyl benzoate, and vinyl cyclohexanecarboxylate, which improve coating hardness in small amounts. Vinyl benzoate is used.
その含有量は共重合体中5〜70モル%であり、好まし
くは10〜60モル%である。かかる量が5モル%未満
では剛性が低く、しかも塗膜硬度が低く粉じんの付着が
著るしい。また70モル%を越えると耐候性が低くなる
。Its content in the copolymer is 5 to 70 mol%, preferably 10 to 60 mol%. If the amount is less than 5 mol%, the rigidity and hardness of the coating film will be low and the adhesion of dust will be significant. Moreover, when it exceeds 70 mol%, weather resistance becomes low.
炭素数1〜8のアルキル基を有するビニルエーテルとし
ては、例エバメチルビニルエーテル、エチルビニルエー
テル、n−7’ロビルビニルエーテル、イングロビルビ
ニルエーテル,n−7”チルビニルエーテル、イソブチ
ルビニルエーテル、t−ブチルビニルエーテル、n−ペ
ンチルビニルエーテル、n−ヘキシルビニルエーテル、
n−オクチルビニルエーテル、2−エチルヘキシルビニ
ルエーテル等の1種又は2種以上が用いられる。その含
有量は共重合体中5〜70モル%であり、好ましくは7
〜60モル%である。Examples of vinyl ethers having an alkyl group having 1 to 8 carbon atoms include evamethyl vinyl ether, ethyl vinyl ether, n-7' lobil vinyl ether, inglobil vinyl ether, n-7'' til vinyl ether, isobutyl vinyl ether, t-butyl vinyl ether, n- -pentyl vinyl ether, n-hexyl vinyl ether,
One or more types of n-octyl vinyl ether, 2-ethylhexyl vinyl ether, etc. are used. Its content is 5 to 70 mol% in the copolymer, preferably 7
~60 mol%.
かかる量が5モル%未満では共重合体の製造時における
フルオロオレフィンの転化率が低くなり、好ましくない
。また、70モル%を越えると共重合体中のフッ素含量
が低くなり、フッ素ポリマーとしての機能が低い。If the amount is less than 5 mol %, the conversion rate of fluoroolefin during production of the copolymer will be low, which is not preferable. Moreover, if it exceeds 70 mol%, the fluorine content in the copolymer will be low, and the function as a fluoropolymer will be low.
水酸基含有ビニルエーテルは一般式(C)で示されるも
のが使用される。As the hydroxyl group-containing vinyl ether, those represented by general formula (C) are used.
例示すれば、ヒドロキシメチルビニルエーテル、ヒドロ
キシエチルビニルエーテル、6−ヒドロキシプロピルビ
ニルエーテル、2−ヒドロキシプロピルビニルエーテル
、4−ヒドロキシブチルビニルエーテル、3−ヒドロキ
シブチルビニルエーテル、4−ヒドロキシブチルビニル
エーテル、2−ヒドロキシ−2−メチルプロピルビニル
エーテル、5−ヒドロキシペンチルビニルエーテル、6
−ヒドロキシエチルビニルエーテル等が挙げられ、その
含有量は3.5〜60モル%であり、好ましくは5〜2
5モル%である。かかる量が3.5モル%未満では架橋
硬化時間の増加、塗膜の耐薬品性、耐溶剤性、耐汚染性
等の低下が起こる。また、30モル%を越えると共重合
体の浴剤oJ溶性の低下、硬化剤と混合した場合のゲル
化時間の減少による塗料の塗布、施工性の低下が起こる
。Examples include hydroxymethyl vinyl ether, hydroxyethyl vinyl ether, 6-hydroxypropyl vinyl ether, 2-hydroxypropyl vinyl ether, 4-hydroxybutyl vinyl ether, 3-hydroxybutyl vinyl ether, 4-hydroxybutyl vinyl ether, 2-hydroxy-2-methylpropyl Vinyl ether, 5-hydroxypentyl vinyl ether, 6
-Hydroxyethyl vinyl ether and the like, the content of which is 3.5 to 60 mol%, preferably 5 to 2 mol%.
It is 5 mol%. If the amount is less than 3.5 mol%, the crosslinking curing time increases and the chemical resistance, solvent resistance, stain resistance, etc. of the coating film decreases. Moreover, if it exceeds 30 mol %, the solubility of the copolymer in the bath agent OJ decreases, and when mixed with a hardening agent, the gelation time decreases, resulting in a decrease in paint application and workability.
本発明の共重合体はテトラヒドロフラン中、25℃で測
定した固有粘度がα05〜2.0dl/g、好ましくは
a2〜t o at7t)であるものに限定される。固
有粘度が[105dll/11未満の共重合体は分子量
が低く、機械的強度も低下する。また2、Odl/Iを
越える共重合体は分子量が高く、溶液状態とした場合、
粘度が高過ぎ、コーティング操作が難しくなる。また、
本発明の共重合体は水酸基価が、17〜200 a9
KOH/I 、好ましくは、20〜120WKOH/1
である。水酸基価が17 my KOi(/y未満のも
のは硬化物の耐シンナー性が低く、200〜KOH/l
/を越えると硬化時間が短くなり過ぎ、塗布、施工性が
悪くなり、また、硬化物が脆くなり好ましくない。The copolymers of the present invention are limited to those having an intrinsic viscosity of α05 to 2.0 dl/g, preferably a2 to at7t), as measured in tetrahydrofuran at 25°C. A copolymer with an intrinsic viscosity of less than [105 dll/11] has a low molecular weight and a low mechanical strength. 2. Copolymers exceeding Odl/I have high molecular weights, and when made into a solution,
The viscosity is too high, making coating operations difficult. Also,
The copolymer of the present invention has a hydroxyl value of 17 to 200 a9
KOH/I, preferably 20-120WKOH/1
It is. If the hydroxyl value is less than 17 my KOi (/y), the cured product has low thinner resistance, and 200~KOH/l
If it exceeds /, the curing time becomes too short, coating and workability deteriorate, and the cured product becomes brittle, which is not preferable.
本発明の共重合体を収率良く製造するには、次のような
仕込み組成を選択するのが好ましい。すなわちフルオロ
オレフィンaモル%、ビニルエーテル6モル%、水酸基
含有ビニルエーテルCモル%、カルボン酸ビニルエステ
ル46モルとし、次式を満足する場合である。In order to produce the copolymer of the present invention in good yield, it is preferable to select the following charging composition. That is, this is a case where the following formula is satisfied, with fluoroolefin a mol %, vinyl ether 6 mol %, hydroxyl group-containing vinyl ether C mol %, and carboxylic acid vinyl ester 46 mol %.
[17(b+c )4a+d<3.5 (b+c )こ
の範囲を逸脱する場合には、本発明の目的とする共重合
体が得られないかもしくは収率の悪い結果となることが
あり、工業上好ましくない。すなわち、フルオロオレフ
ィン(Cモル)とカルボン酸ビニルエステル(dモル)
の相(a+d)がビニルエーテル(bモル)と水酸基含
有ビニルエーテル(Cモル)の和(b+e)のα7倍よ
り小さければビニルエーテル及び水酸基含蛍ビニルエー
テルの共重合体中の含量が低くなる恐れがあり、又、3
.5倍を越えるとフルオロオレフィンの転化率が低くな
る。[17 (b+c) 4a+d<3.5 (b+c) If this range is exceeded, the copolymer targeted by the present invention may not be obtained or the yield may be poor, and it may be difficult to obtain an industrially desired copolymer. Undesirable. That is, fluoroolefins (C moles) and carboxylic acid vinyl esters (d moles)
If the phase (a + d) is smaller than α7 times the sum (b + e) of vinyl ether (b mol) and hydroxyl group-containing vinyl ether (C mol), the content of vinyl ether and hydroxyl group-containing vinyl ether in the copolymer may become low, Also, 3
.. When it exceeds 5 times, the conversion rate of fluoroolefins becomes low.
この関係式はフルオロオレフィンとビニルエーテル類と
では交互に共重合し、フルオロオレフィンとカルボン酸
ビニル、及びビニルエーテル類とカルボン酸ビニルとに
おいてはカルボン酸ビニルが優先的に重合するといつ央
験事実から知見したものである。This relational expression shows that fluoroolefins and vinyl ethers copolymerize alternately, and that when fluoroolefins and vinyl carboxylates copolymerize, and when vinyl ethers and vinyl carboxylates, vinyl carboxylates copolymerize preferentially. It is something.
本発明の製造方法では前記の各モノマーをラジカル開始
剤存在下で、塊状重合、溶液重合、懸濁重合、乳化重合
の公知の技術を用いて、回分式、半連続式、連続式の操
作で行なわれる。In the production method of the present invention, each of the above-mentioned monomers is mixed in the presence of a radical initiator using known techniques such as bulk polymerization, solution polymerization, suspension polymerization, and emulsion polymerization in a batch, semi-continuous, or continuous manner. It is done.
ラジカル開始剤としては、アセチルパーオキサイド、ベ
ンゾイルパーオキサイドの如きジアシルパーオキサイド
類、メチルエチルケトンパーオキサイド、シクロヘキサ
ンパーオキサイドの如きケトンパーオキサイド類、過酸
化水素、t−ブチルハイドロパーオキサイド、クメンハ
イドロパーオキサイドの如きハイドロパーオキサイド類
、ジ−t−ブチルパーオキサイド、ジクミルパーオキサ
イドの如きジアルキルパーオキサイド類、t−ブチルパ
ーオキシアセテート、t−ブチルパーオキシピバレート
の如きアルキルパー必要に応じて亜硫酸水素す) 17
ウム、ピロ亜硫酸ナトリウムの如き無機の還元剤、ナフ
テン酸コバルト、ジメチルアニリンの如き有機の還元剤
が用いられる。Examples of radical initiators include diacyl peroxides such as acetyl peroxide and benzoyl peroxide, ketone peroxides such as methyl ethyl ketone peroxide and cyclohexane peroxide, hydrogen peroxide, t-butyl hydroperoxide, and cumene hydroperoxide. hydroperoxides such as di-t-butyl peroxide, dialkyl peroxides such as dicumyl peroxide, alkyl peroxides such as t-butyl peroxyacetate and t-butyl peroxypivalate, and optionally hydrogen sulfite. ) 17
Inorganic reducing agents such as sodium chloride, sodium pyrosulfite, and organic reducing agents such as cobalt naphthenate and dimethylaniline are used.
共重合反応に際して反応fit!度は通常−20℃〜1
30℃の範囲であり、その温度で適度の分解速度を持つ
ラジカル開始剤が選ばれる。また、反応圧力は通常1〜
10 Q h/cx”で、好ましくは5〜,60ゆ/c
rrL”である。Reaction fit during copolymerization reaction! The temperature is usually -20℃~1
The radical initiator is selected in the range of 30° C. and has a moderate decomposition rate at that temperature. In addition, the reaction pressure is usually 1~
10 Q h/cx”, preferably 5 to 60 yu/c
rrL”.
本発明の共重合体は、アセトン、メチルエチルケトン、
メチルイソブチルケトン等のケトン類、酢酸エチル、酢
酸プロピル、酢酸イソブチル等の有機溶剤に可溶である
。また、本発明の共重合体は、水酸基含有ビニルエーテ
ル単位中の水酸基が架橋部位となり、メラミン硬化剤、
尿素樹脂硬化剤、多塩基酸硬化剤等を用いて加熱硬化さ
せることができる。メラミン硬化剤としてはブチル化メ
ラミン、メチル化メラミン、エポキシ変性メラミン等が
挙げられ、尿素樹脂硬化剤としてはブチル化尿素、メチ
ル化尿素等が挙げられ、多塩基酸硬化剤としては長鎖脂
肪族ジカルボン酸類、芳香族多価カルボン酸類、ブロッ
ク多価イソシアネート類等が挙げられる。さらK、本発
明の共重合体と多価イソシアたト類との常温硬化が可能
である多価イソシアナート類としては、トリレンジイン
シアナート、ジフェニルメタンジイソシアナート、キシ
リレンジイソシアナートの如キ芳香族インシアナート、
テトラメチレンジイソシアナート、ヘキサメチレンジイ
ソシアナート、トリメチルヘキサンジインシアナートの
如き脂肪族ジイソシアナートイソホロンジイソシアナー
ト、メチルシクロヘキサン−2,4−(または2.6−
)ジイソシアナート、4,4′−メチレンビス(シクロ
ヘキシルイソシアナート)、1,3−ジ(インシアナー
トメチル)−シクロヘキサンの如き脂環族ジインシアナ
ートが用いられ、好ましくはへキサメチレンジイソシア
ナート、キシリレンジイソシアナート等の無黄変ジイソ
シアナート類ならびにそのブロック化物が用いられる。The copolymer of the present invention includes acetone, methyl ethyl ketone,
It is soluble in ketones such as methyl isobutyl ketone, and organic solvents such as ethyl acetate, propyl acetate, and isobutyl acetate. In addition, in the copolymer of the present invention, the hydroxyl group in the hydroxyl group-containing vinyl ether unit becomes a crosslinking site, and the melamine curing agent,
It can be cured by heating using a urea resin curing agent, a polybasic acid curing agent, or the like. Melamine curing agents include butylated melamine, methylated melamine, epoxy-modified melamine, etc., urea resin curing agents include butylated urea, methylated urea, etc., and polybasic acid curing agents include long-chain aliphatic Examples include dicarboxylic acids, aromatic polycarboxylic acids, and block polyisocyanates. Further, examples of polyvalent isocyanates that can be cured at room temperature with the copolymer of the present invention and polyvalent isocyanates include tolylene diisocyanate, diphenylmethane diisocyanate, and xylylene diisocyanate. aromatic incyanate,
Aliphatic diisocyanates such as tetramethylene diisocyanate, hexamethylene diisocyanate, trimethylhexane diisocyanate, isophorone diisocyanate, methylcyclohexane-2,4-(or 2,6-
) diisocyanate, 4,4'-methylenebis(cyclohexyl isocyanate), 1,3-di(incyanatomethyl)-cyclohexane, preferably hexamethylene diisocyanate, Non-yellowing diisocyanates such as diisocyanate and blocked products thereof are used.
さらにジブチルチンジラウレート等の触媒を冷加して硬
化促進が可能である。Furthermore, curing can be accelerated by cooling a catalyst such as dibutyltin dilaurate.
本発明の共重合体と前記インシアナート1を用いて常温
硬化を行うにあたり、水酸基含有ビニルエーテル単位と
多価インシアナート類との配合比は、OH/NC0=1
/CL2〜1/2(当量比)が過当である。When curing at room temperature using the copolymer of the present invention and the incyanate 1, the blending ratio of the hydroxyl group-containing vinyl ether unit and the polyvalent incyanate is OH/NC0=1
/CL2 to 1/2 (equivalent ratio) is appropriate.
(発明の効果及び産業上の利用分野)
本発明の共重合体は耐候性、撥水性、非粘着性、耐汚染
性、耐薬品性に優れ、底面に潤滑性があるために鋼材、
木工品、セラミック製品、ガラス製品、グラスチック製
品の表面コーティング、繊維加工用飛水跋油剤、非粘着
コーティング、すべり軸受光フアイバー鞘材、ソーラー
コレクタ、理化学医療用材料として特に優れている。さ
らに塗料としては、金属用焼付塗料、建築物外装用塗料
、豪雪地帯の屋根用塗料、船舶、自動車、航空機用熟料
として特に優れている。又本発明の製造法は仕込みモノ
マー組成を規定することにより各々のモノマーがポリマ
ーに導入される転換率が80%以上になり工業上有利で
ある。(Effects of the invention and industrial fields of application) The copolymer of the present invention has excellent weather resistance, water repellency, non-adhesiveness, stain resistance, and chemical resistance, and has lubricity on the bottom surface, so it can be used for steel materials, etc.
It is particularly excellent as a surface coating for wood products, ceramic products, glass products, and glass products, a water-repellent oil agent for textile processing, non-adhesive coatings, optical fiber sheath materials for sliding bearings, solar collectors, and materials for physical, chemical, and medical applications. Furthermore, as a paint, it is particularly excellent as a baking paint for metals, a paint for the exterior of buildings, a paint for roofs in areas with heavy snowfall, and a seasoning agent for ships, automobiles, and aircraft. Further, the production method of the present invention is industrially advantageous because the conversion rate of each monomer introduced into the polymer can be 80% or more by specifying the monomer composition to be charged.
(実施例) 次いで、本発明を実施例により更に説明する。(Example) Next, the present invention will be further explained by examples.
実施例1〜5、比較例1〜2
内容積1001IIIIIのステンレス製耐圧管にメチ
ルインブチルケトン(MIBKと略す)50eeとパー
ブチルpv(日本油脂■#りQ、5#と表1に記載した
量のエチルビニルエーテk (E V Eと略ス)、ヒ
ドロキシブチルビニルエーテル(HBVEと略す)、C
,のアルキル基を有するカルボン酸ビニルエステル〔商
品名グエオバー9(VV−9と略す)、シェル化学■製
〕又は安息香酸ビニルエステル(BZVEと略す)を仕
込み、ドライアイス−メタノール浴で一70℃に冷却し
、窒素ガスを吹き込んで耐圧管内の酸素を除去した。次
いで、液化採取したヘキサフルオロプロピレン(RFP
と略す)あるいはクロロトリフルオロエチレン(CTF
Eと略す)を規定量仕込み封管した。又、テトラフルオ
ロエチレン(TFEと略す)の場合にはパルプ付の耐圧
管を使用し、上記と同様に仕込みを行なった後、TFE
ボンベよりTFEを加圧封入した後パルプを締め、秤量
した。これらの耐圧管を60℃に加温した回転式恒温水
槽に入れ、16時間反応を行なった後、内容物を10倍
量のメタノール中に沈殿させ、80℃で12時間通風乾
燥後収量を測定した。さらK、このポリマーを100−
のアセトンに溶解後、11のメタノールで再沈殿させ、
精製し、乾燥させたものをフッ素含量、NMR,固有粘
度、水酸基価、ガラス転移点の測定に供した。Examples 1 to 5, Comparative Examples 1 to 2 Methyl in butyl ketone (abbreviated as MIBK) 50ee and perbutyl pv (NOF ■#riQ, 5# and the amounts listed in Table 1 were placed in a stainless steel pressure-resistant tube with an internal volume of 1001III). Ethyl vinyl ether (abbreviated as E V E), hydroxybutyl vinyl ether (abbreviated as HBVE), C
, a carboxylic acid vinyl ester having an alkyl group [trade name Gueovar 9 (abbreviated as VV-9), manufactured by Shell Chemical ■] or benzoic acid vinyl ester (abbreviated as BZVE), and heated to -70°C in a dry ice-methanol bath. The tube was cooled to 100 mL, and nitrogen gas was blown into the tube to remove oxygen from the pressure tube. Then, the liquefied hexafluoropropylene (RFP
) or chlorotrifluoroethylene (CTF)
(abbreviated as E) was charged in a specified amount and sealed in a tube. In addition, in the case of tetrafluoroethylene (abbreviated as TFE), use a pressure-resistant tube with pulp, and after preparing it in the same manner as above,
After pressurizing and sealing TFE from the cylinder, the pulp was tightened and weighed. These pressure-resistant tubes were placed in a rotary constant-temperature water bath heated to 60°C, and after reacting for 16 hours, the contents were precipitated in 10 times the volume of methanol, and after drying with ventilation at 80°C for 12 hours, the yield was measured. did. Furthermore, this polymer is 100-
After dissolving in acetone, reprecipitate with methanol in step 11,
The purified and dried product was subjected to measurements of fluorine content, NMR, intrinsic viscosity, hydroxyl value, and glass transition point.
尚、フッ素含量をアリザリンコンブレクラン法によるフ
ッ素の比色定量法から測定し、それに基いてフルオロオ
レフィン成分量を算出した。The fluorine content was measured by colorimetric determination of fluorine using the Alizarin Combrecran method, and the amount of fluoroolefin components was calculated based on the measurement.
NMRの測定は日本電子社製JNM−MH60fiを用
い、テトラメチルシランを内部標準物質として測定した
。その結果、アルキルビニルエーテルとヒドロキシブチ
ルビニルエーテルの一〇−プロトンの合計jik(b+
c)は3.9〜4.6−C−
4,6〜5.9PPMに現われた。NMR measurements were performed using JNM-MH60fi manufactured by JEOL Ltd., using tetramethylsilane as an internal standard substance. As a result, the sum of the 10-protons of alkyl vinyl ether and hydroxybutyl vinyl ether jik(b+
c) appeared at 3.9-4.6-C-4,6-5.9 PPM.
従って、b + c / d (モル比)=(3,9〜
4.6)のピーク面積/ (4,6〜5.9)のピーク
面積・・・・・・・・・(1)
c+d= 100−(a+ b ) = (2
)これを(21に代入すると、
100−(a+b)となる。Therefore, b + c / d (molar ratio) = (3,9 ~
Peak area of 4.6)/Peak area of (4,6-5.9)・・・・・・・・・(1) c+d=100-(a+b)=(2
) Substituting this into (21) gives 100-(a+b).
上式からC(ヒドロキシブチルビニルエーテルik)及
びd(カルボン酸ビニル−fit)が求められる。From the above formula, C (hydroxybutyl vinyl ether ik) and d (vinyl carboxylate-fit) are determined.
固有粘度はテトラヒドロフランの1%溶液を用い25℃
でクペロード粘度計により測定した。Intrinsic viscosity was measured at 25°C using a 1% solution of tetrahydrofuran.
It was measured using a Kuperod viscometer.
水酸基価は無水酢[Kよるアセチル化法によって測定し
た。これに基いてヒドロキシブチルビニルエーテル量を
算出した。The hydroxyl value was measured by an acetylation method using anhydrous vinegar [K]. Based on this, the amount of hydroxybutyl vinyl ether was calculated.
又、ガラス転位温度はTGA−DSCにより測定した。Moreover, the glass transition temperature was measured by TGA-DSC.
(注)HFP:ヘキサフルオロプロピレン、CTFE:
クロロトリフルオロエチレン、TFE:テトラフルオロ
エチレン、EVE:エチルビニルエーテル、HBVE
:ヒドロキシブチルビニルエーテル、VV−9:ウエオ
バ−9(カルボン酸ビニルエステル)、BZVE:安息
香酸ピニル
上記各ポリマーはいずれも酢酸エチル、酢酸ブチル、ア
セトン、メチルエチルケトン、テトラヒドロフラン、四
塩化炭素、トルエン、キシレン等の有機溶剤に可溶であ
った。(Note) HFP: Hexafluoropropylene, CTFE:
Chlorotrifluoroethylene, TFE: Tetrafluoroethylene, EVE: Ethyl vinyl ether, HBVE
: Hydroxybutyl vinyl ether, VV-9: Ueover-9 (carboxylic acid vinyl ester), BZVE: Pinyl benzoate The above polymers include ethyl acetate, butyl acetate, acetone, methyl ethyl ketone, tetrahydrofuran, carbon tetrachloride, toluene, xylene, etc. It was soluble in organic solvents.
実施例1〜5及び比較例1〜2の各ポリマー50gをト
ルエン25g1メチルイノプチルケf−y251に俗解
し無色透明な溶液を得た。この溶液にタイベークCR−
90(石原産業■製)271を加えてボールミルで24
時間混合し白色ミルベースを製造した。これに該ポリマ
ーの水酸基とインシアネート基が当量になる様にパーノ
ックDN−950(ヘキサメチレンジイソシアネート系
、大日本インキ化学■製)を加え、メチルエチルケトン
にて脱脂処理したJIS G−3)41鋼板上にアプリ
ケーターにより塗布し80℃にて30分間焼付硬化させ
た後、2日間放置し物性テストに供した。葦膜の厚みは
35〜40μであり、表2の結果を得た。50 g of each of the polymers of Examples 1 to 5 and Comparative Examples 1 to 2 was mixed with 25 g of toluene and 1 methyl inoptyl compound f-y251 to obtain a colorless and transparent solution. Add Thai Bake CR- to this solution.
90 (manufactured by Ishihara Sangyo ■) 271 and milled in a ball mill to 24
A white mill base was produced by mixing for a period of time. Parnock DN-950 (hexamethylene diisocyanate type, manufactured by Dainippon Ink Chemical Co., Ltd.) was added to this so that the hydroxyl groups and incyanate groups of the polymer were equivalent, and a JIS G-3) 41 steel plate was degreased with methyl ethyl ketone. The coating was applied to the surface using an applicator, baked and cured at 80° C. for 30 minutes, and then left to stand for 2 days before being subjected to physical property tests. The thickness of the reed film was 35 to 40 μm, and the results shown in Table 2 were obtained.
実施例1〜5の塗膜は良好な物性を示すが、比較例1は
耐溶剤性に劣り、又、比較例2は柔軟すぎる塗膜であり
、屋外自然暴mf粉じんの付着があり光沢保持が劣る。The coating films of Examples 1 to 5 exhibit good physical properties, but Comparative Example 1 has poor solvent resistance, and Comparative Example 2 has a coating film that is too flexible, has adhesion of outdoor natural MF dust, and is unable to maintain gloss. is inferior.
実施例6〜9
表3に記載した景のモノマーから実施例1〜5と全(同
様にして目的とする共重合体を得た。同表に得られた共
重合体の性状を示した。また、実施例1〜5と全く同様
にし【合成した各ポリマーから硬化塗膜を得た。塗膜性
能は表4に示した通り良好であった。Examples 6 to 9 Target copolymers were obtained in the same manner as in Examples 1 to 5 from the monomers shown in Table 3. The properties of the obtained copolymers are shown in the same table. In addition, cured coating films were obtained from each of the synthesized polymers in exactly the same manner as in Examples 1 to 5. The coating performance was good as shown in Table 4.
Claims (1)
ィン10〜70モル%、と下記一般式(B)なる構造を
有するカルボン酸ビニルエステル5〜70モル%と炭素
数1〜8までのアルキル基を有するビニルエーテル5〜
70モル%及び下記一般式(C)なる構造を有する水酸
基含有ビニルエーテル3.5〜50モル%の組成を有し
、かつ共重合体の固有粘度が0.05〜2.0dl/g
、水酸基価が17〜200mgKOH/gであるフルオ
ロオレフィン共重合体。 記 (A)▲数式、化学式、表等があります▼(XはH、、
Cl、F、CF_3、OCF_3、OC_3F_7であ
る。) (B)▲数式、化学式、表等があります▼(R_1は炭
素数1〜17までの脂肪族、芳香族、脂環族から選ばれ
る炭化 水素基である。) (C)▲数式、化学式、表等があります▼(R_2は炭
素数1〜6までのアルキレン基である。) (2)前記カルボン酸ビニルエステルが炭素数9〜10
なる脂肪族カルボン酸のビニルエステルである特許請求
の範囲第1項記載のフルオロオレフィン共重合体。 (3)前記カルボン酸ビニルエステルがシクロヘキサン
カルボン酸ビニルである特許請求の範囲第1項に記載の
フルオロオレフィン共重合体。 (4)前記カルボン酸ビニルエステルが安息香酸ビニル
である特許請求の範囲第1項に記載のフルオロオレフィ
ン共重合体。 (5)前記カルボン酸ビニルエステルがパラ−tert
−ブチル安息香酸ビニルである特許請求の範囲第1項に
記載のフルオロオレフィン共重合体。 (6)前記一般式(A)なる構造を有するフルオロオレ
フィン10〜70モル、と下記一般式(B)なる構造を
有するカルボン酸ビニルエステル5〜70モル%と炭素
数1〜8までのアルキル基を有するビニルエーテル5〜
70モル、及び下記一般式(C)なる構造を有する水酸
基含有ビニルエーテル3.5〜30モル%の共重合体を
製造するにあたり、仕込み組成をフルオロオレフィンa
モル%、ビニルエーテルbモル%、水酸基含有ビニルエ
ーテルcモル%、カルボン酸ビニルエステルdモル%と
した場合、 0.7(b+c)≦a+d<3.5(b+c)を満足す
る溶液をラジカル開始剤の存在下−20℃〜130℃の
温度にて重合せしめることを特徴とする共重合体の製造
方法。[Scope of Claims] 1) 10 to 70 mol% of a fluoroolefin having a structure represented by the following general formula (A), 5 to 70 mol% of a carboxylic acid vinyl ester having a structure represented by the following general formula (B), and a carbon number of 1 Vinyl ethers with up to 8 alkyl groups 5-
It has a composition of 70 mol% and 3.5 to 50 mol% of a hydroxyl group-containing vinyl ether having the structure of the following general formula (C), and the intrinsic viscosity of the copolymer is 0.05 to 2.0 dl/g.
, a fluoroolefin copolymer having a hydroxyl value of 17 to 200 mgKOH/g. Note (A) ▲ There are mathematical formulas, chemical formulas, tables, etc. ▼ (X is H,
They are Cl, F, CF_3, OCF_3, and OC_3F_7. ) (B) ▲ There are mathematical formulas, chemical formulas, tables, etc. ▼ (R_1 is a hydrocarbon group selected from aliphatic, aromatic, and alicyclic groups with 1 to 17 carbon atoms.) (C) ▲ Numerical formulas, chemical formulas , tables, etc. ▼ (R_2 is an alkylene group having 1 to 6 carbon atoms.) (2) The carboxylic acid vinyl ester has 9 to 10 carbon atoms.
The fluoroolefin copolymer according to claim 1, which is a vinyl ester of an aliphatic carboxylic acid. (3) The fluoroolefin copolymer according to claim 1, wherein the vinyl carboxylate ester is vinyl cyclohexanecarboxylate. (4) The fluoroolefin copolymer according to claim 1, wherein the carboxylic acid vinyl ester is vinyl benzoate. (5) The carboxylic acid vinyl ester is para-tert.
The fluoroolefin copolymer according to claim 1, which is vinyl -butylbenzoate. (6) 10 to 70 mol% of a fluoroolefin having the structure represented by the general formula (A) above, 5 to 70 mol% of a carboxylic acid vinyl ester having the structure represented by the following general formula (B), and an alkyl group having 1 to 8 carbon atoms. Vinyl ether with 5~
In producing a copolymer containing 70 mol and 3.5 to 30 mol % of a hydroxyl group-containing vinyl ether having the structure of the following general formula (C), the charging composition was changed to fluoroolefin a.
When mol%, vinyl ether b mol%, hydroxyl group-containing vinyl ether c mol%, and carboxylic acid vinyl ester d mol%, a solution satisfying 0.7 (b + c) ≦ a + d < 3.5 (b + c) is a radical initiator. A method for producing a copolymer, comprising polymerizing at a temperature of -20°C to 130°C in the presence of a copolymer.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP26683184 | 1984-12-18 | ||
JP59-266831 | 1984-12-18 |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS61275311A true JPS61275311A (en) | 1986-12-05 |
JPH0662719B2 JPH0662719B2 (en) | 1994-08-17 |
Family
ID=17436255
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP60281932A Expired - Fee Related JPH0662719B2 (en) | 1984-12-18 | 1985-12-17 | Curable fluoroolefin copolymer and process for producing the same |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0662719B2 (en) |
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