JPH0452310B2 - - Google Patents
Info
- Publication number
- JPH0452310B2 JPH0452310B2 JP58021691A JP2169183A JPH0452310B2 JP H0452310 B2 JPH0452310 B2 JP H0452310B2 JP 58021691 A JP58021691 A JP 58021691A JP 2169183 A JP2169183 A JP 2169183A JP H0452310 B2 JPH0452310 B2 JP H0452310B2
- Authority
- JP
- Japan
- Prior art keywords
- fluororesin
- aqueous dispersion
- coating
- coating film
- hydroxypropyl methylcellulose
- 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
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- Paints Or Removers (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Description
(産業上の利用分野)
本発明は塗装用フツ素樹脂組成物に関し、さら
に詳しくは塗布乾燥時に塗膜のひび割れが発生せ
ず、かつ焼成後の塗膜表面の平滑性が良好な熱流
動性フツ素樹脂の水分散液に関する。
(従来の技術及びその問題点)
テトラフルオロエチレン・パーフルオロアルキ
ルビニルエーテル共重合体あるいはテトラフルオ
ロエチレン・ヘキサフルオロプロピレン共重合体
のような熱流動性フツ素樹脂は、フツ素樹脂特有
の耐薬品性に優れ、摩擦係数が小さく非粘着性に
富むうえに溶融粘度も他のフツ素樹脂に比べて低
いため、溶融成形が可能である。
近年、熱流動性フツ素樹脂の水分散液が開発さ
れ、基材上にスプレーガン等によつて塗布するこ
とにより手軽にフツ素樹脂をコーテイングした製
品が得られるようになつたが、未だに均一な塗膜
加工を施すことが困難な場合がある。すなわち塗
布乾燥すると塗膜にクラツクが発生してひび割れ
た塗膜になつたり、焼成すると塗膜表面に凸凹が
発生して平滑な表面が得られないことがある。こ
のような塗膜のひび割れや表面平滑性の欠如は直
接製品としての価値を損うため好ましくなく、そ
の防止が望まれている。
特公昭47−21688号公報には、テトラフルオロ
エチレン・ヘキサフルオロプロピレン共重合体の
水性デイスパージヨン中に水溶性メチルセルロー
スあるいはエチルセルロースおよびオイル状ない
しグリース状のトリフルオロクロロエチレン低重
合体を溶解または分散させて成る被覆用組成物が
記載されている。
本発明者らは、テトラフルオロエチレン・パー
フルオロアルキルビニルエーテル共重合体の如
き、熱流動性フツ素樹脂の水性分散液を、表面平
滑性に優れたエナメル化すべく鋭意研究を重ねた
結果、この水性分散液に特定の熱ゲル化温度のヒ
ドロキシプロピルメチルセルロースを添加する
と、この被覆の乾燥時のひび割れを防止し、かつ
焼成後の表面平滑性を顕著に向上させ得ることを
見出した。
(問題点を解決するための手段)
本発明によれば、テトラフルオロエチレン・パ
ーフルオロアルキルビニルエーテル共重合体の如
き熱流動性フツ素樹脂の水分散液に、熱ゲル化温
度が60℃よりも高く且つ70℃以下のヒドロキシプ
ロピルメチルセルロースを樹脂当り2乃至10重量
%配合してなることを特徴とする塗装用フツ素樹
脂組成物が提供される。
(作用)
本発明において、フツ素樹脂の内でも熱流動性
フツ素樹脂を用いるのは、このものがフツ素樹脂
特有の耐薬品性に優れ、摩擦係数が小さく非粘着
性に富むうえに、溶融粘度も他のフツ素樹脂に比
べて低いことによる。
本発明によれば、種々の水溶性セルロース誘導
体の内でも、熱ゲル化温度が60℃よりも高く且つ
70℃以下のヒドロキシプロピルメチルセルロース
を選択し、これを熱流動性フツ素樹脂の水性分散
液に配合することにより、乾燥時の塗膜のひび割
れを防止し、焼成時の塗膜表面を著しく平滑化す
ることができる。
本発明による焼成時の熱流動性フツ素樹脂塗膜
表面を著しく平滑にするという作用効果は、通常
の水溶性バインダーや通常の水溶性セルロース誘
導体には認められないものであり、ヒドロキシプ
ロピルメチルセルロースに特有の作用効果であ
る。この事実は後述する第1表を参照することに
より明らかである。
また、本発明では、ヒドロキシプロピルメチル
セルロースの熱ゲル化温度が60℃よりも高く且つ
70℃以下であることも焼成フツ素樹脂塗膜の平滑
性に関して重要である。後述する第2表に示す通
り、熱ゲル化温度が60℃以下である場合や、熱ゲ
ル化温度が70℃を越える場合には、焼成PFA塗
膜の平滑性が本発明の場合に比して低下する。
本発明において、特定の熱ゲル化温度のヒドロ
キシプロピルメチルセルロースが焼成時にフツ素
樹脂塗膜を著しく平滑にするという作用効果は、
多数の実験の結果、現象として見出されたもので
あり、その理由は未だ十分に明らかではないが、
本発明の組合せでは、熱流動性フツ素樹脂の熱流
動温度と配合剤(バインダー)の分解温度とが近
接しているためと思われる。
(好適態様)
本発明では、熱流動性フツ素樹脂として、テト
ラフルオロエチレン・パーフルオロアルキルビニ
ルエーテル(PFA)単独を用いることが好まし
いが、他の熱流動性フツ素樹脂、例えばテトラフ
ルオロエチレン・ヘキサフルオロプロピレン共重
合体(FEP)、ポリクロロトリフルオロエチレン
(PCTFE)、ポリビニリデンフルオライド
(PVDF)、ポリビニルフルオライド(PVF)、テ
トラフルオロエチレン・エチレン共重合体
(ETFE)等を用いてもよい。これらの内でも、
PFAが最も好ましく、次にFEPが好ましい。
これらの水分散液を得るには、たとえば粉末ま
たは粒状物を用いる場合には、必要に応じてボー
ルミル等で粉砕したのち水中に分散させることに
より得ることができる。そのほか乳化重合によつ
て得られる水分散液あるいはオルガノゾルの水中
エマルジヨンは、そのまま使用できる。これらの
水分散液には、このほか有機液体が混合されてい
てもよいが、多量に配合することは塗布時の作業
環境の面から好ましくない。
ヒドロキシプロピルメチルセルロースは、熱流
動性フツ素樹脂の水分散液に混合したのちの取扱
い性、すなわちスプレーガンでの塗布し易さや塗
膜の均一性保持のためには、2重量%水溶液の粘
度が20℃で400cps以下であることが好ましい。
ヒドロキシプロピルメチルセルロースの配合量
は、熱流動性フツ素樹脂の水分散液の濃度、ヒド
ロキシプロピルメチルセルロースの種類目的とす
る塗膜厚等によつて一概に規定することは難しい
が、樹脂に対し2重量%ないし10重量%、とくに
4重量%ないし6重量%が好ましい。配合量が2
重量%未満であると焼成後の塗膜表面の平滑性が
得られないし、10重量%を越えると焼成後もヒド
ロキシプロピルメチルセルロース分解物が塗膜中
に残留し易く、ピンホールの発生あるいは非粘着
性を損つたりすることがある。
熱流動性フツ素樹脂の水分散液にヒドロキシプ
ロピルメチルセルロースを配合するには公知の如
何なる方法でもよく、該水分散液に撹拌しながら
直接添加する方法、予めヒドロキシプロピルメチ
ルセルロース水溶液を作つておき該水分散液と混
合する方法等が例示できる。
また本発明においてはヒドロキシプロピルメチ
ルセルロースの増粘効果を利用して、塗布時のた
れを防止したり、重ね塗り時のはじきを防止する
こともできる。
塗布時のたれは、垂直面に塗布した水分散液が
流動して塗膜に不均一なしまやたまりを生じる
し、重ね塗り時のはじきは水分散液を用いた塗膜
形成においては一度塗りでは充分な厚さの塗膜が
得られず、重ね塗りをしばしば必要とすることか
ら好ましくない。このようなたれやはじきの防止
は、例えば塗膜厚が10〜30μを目的とするなら
ば。熱流動性フツ素樹脂の水分散液の粘度を
290cps以上になるようにヒドロキシプロピルメチ
ルセルロースを配合することによりたれを防止で
き、さらに350cps以上にすることによりはじきも
防止できる。もちろんヒドロキシプロピルメチル
セルロース以外の公知の増粘剤を用いても、前記
の粘度範囲にすれば、たれやはじきを防止でき
る。尚ここでいう粘度は、B型粘度計により27
℃、60rpmの条件下で測定した値である。
本発明の塗装用フツ素樹脂組成物には、そのほ
か公知の種々の添加剤を配合してもよく、たとえ
ば脂肪酸、高級アルコールの硫酸エステル、アル
キルベンゼンスルホン酸、アルキルナフタレンス
ルホン酸、ポリナフタレンスルホン酸およびこれ
らの塩、フルオロアルキル基を有するカルボン
酸、スルホン酸、リン酸およびこれらの塩、エス
テル、ポリオキシエチレンアルキルエーテル、ポ
リオキシエチレンアルキルフエニルエーテル、ポ
リオキシエチレンアシルエステル、ソルビタン脂
肪酸エステル等の界面活性剤を分散剤またはレベ
リング剤として、オクチルアルコール、シクロヘ
キサノール等の高級アルコール、エチレングリコ
ール、ポリメチルシロキサン等を消泡剤として配
合することができる。そのほか顔料、染料、無機
および有機の充填剤等も配合してもかまわない。
次に実施例を示すが、本発明はその目的が損わ
れない限りこれらの実施例に限定されるものでは
ない。
実施例1および比較例1〜7
372℃での溶融粘度3×105psのPFAを54重量
%分散させたPFA水分散液に第1表に示す配合
物を添加した。できたPFA水分散液組成物をサ
ンドペーパーで粗面化した鉄板上にバーコータで
乾燥時の塗膜厚が20〜25μになるように塗布し、
80℃で10分間乾燥後、380℃で10分間焼成した。
乾燥時の塗膜のひび割れ具合および焼成後の塗膜
表面の平滑性を目視で判定した結果を第1表に示
す(◎…ひび割れ防止性または表面平滑性が非常
に良好、○…良好、△…微少のひび割れありまた
は平滑性やや良好、×…ひび割れありまたは平滑
性なし)。
尚使用した配合物は下記の市販品を用いた。
ヒドロキシプロピルメチルセルロース;メトロ
ーズ
65SH50 信越化学
シリカ;ミズカシル
P−527 水沢化学工業
炭酸カルシウム;白艶華
PZ 白石工業
アクリルエマルジヨン;プライマル
TR−534 ローム&ハースジヤパン
ポリビニルアルコール;ゴーセノール
GH−17 日本合成化学工業
カルボキシメチルセルロース;セロゲン
PR 第1工業製薬
ヒドロキシエチルセルロース;ナトロゾル
250LR ハーキユレス
(Industrial Application Field) The present invention relates to a fluororesin composition for coating, and more specifically, it has a thermal fluidity that does not cause cracking of the coating film during application and drying, and provides a smooth coating film surface after baking. This invention relates to an aqueous dispersion of fluororesin. (Prior art and its problems) Thermofluidic fluoroplastics such as tetrafluoroethylene/perfluoroalkyl vinyl ether copolymer or tetrafluoroethylene/hexafluoropropylene copolymer have chemical resistance unique to fluoroplastics. It has excellent properties such as low coefficient of friction, high non-adhesive properties, and low melt viscosity compared to other fluorocarbon resins, making it possible to melt mold. In recent years, an aqueous dispersion of heat-flowable fluororesin has been developed, and products coated with fluororesin can be easily obtained by applying it onto a substrate using a spray gun, but it is still difficult to obtain a uniform coating. It may be difficult to apply a suitable coating. That is, when it is applied and dried, cracks may occur in the coating film, resulting in a cracked coating film, and when it is baked, unevenness may occur on the coating film surface, making it impossible to obtain a smooth surface. Such cracks in the coating film and lack of surface smoothness are undesirable because they directly impair the value of the product, and prevention thereof is desired. Japanese Patent Publication No. 47-21688 discloses that water-soluble methylcellulose or ethylcellulose and an oil-like or grease-like trifluorochloroethylene low polymer are dissolved or dispersed in an aqueous dispersion of a tetrafluoroethylene/hexafluoropropylene copolymer. Coating compositions are described. The present inventors have conducted extensive research to convert aqueous dispersions of heat-flowable fluororesins, such as tetrafluoroethylene/perfluoroalkyl vinyl ether copolymers, into enamels with excellent surface smoothness. It has been found that adding hydroxypropyl methylcellulose at a specific thermal gelling temperature to the dispersion can prevent this coating from cracking when drying and significantly improve the surface smoothness after firing. (Means for Solving the Problems) According to the present invention, an aqueous dispersion of a thermofluid fluororesin such as a tetrafluoroethylene/perfluoroalkyl vinyl ether copolymer has a thermal gelation temperature higher than 60°C. There is provided a fluororesin composition for coating, characterized in that it contains 2 to 10% by weight of hydroxypropyl methyl cellulose having a high temperature and a temperature of 70°C or less per resin. (Function) In the present invention, a thermofluid fluororesin is used among fluororesins because it has excellent chemical resistance unique to fluororesins, has a small friction coefficient, and is highly non-adhesive. This is because the melt viscosity is also lower than that of other fluororesins. According to the present invention, among various water-soluble cellulose derivatives, the thermal gelation temperature is higher than 60°C and
By selecting hydroxypropyl methylcellulose with a temperature below 70℃ and blending it with the aqueous dispersion of thermofluid fluororesin, cracks in the coating film are prevented during drying, and the surface of the coating film is significantly smoothed during baking. can do. The effect of the present invention of significantly smoothing the surface of the heat-flowable fluororesin coating film upon firing is something that is not found in ordinary water-soluble binders or ordinary water-soluble cellulose derivatives, and is unique to hydroxypropyl methylcellulose. This is a unique action and effect. This fact is clear by referring to Table 1 below. Further, in the present invention, the thermal gelation temperature of hydroxypropyl methylcellulose is higher than 60°C and
It is also important that the temperature is 70°C or less in terms of the smoothness of the fired fluororesin coating film. As shown in Table 2 below, when the thermal gelation temperature is below 60℃ or when the thermal gelation temperature exceeds 70℃, the smoothness of the fired PFA coating film is lower than that of the present invention. and decreases. In the present invention, the effect that hydroxypropyl methylcellulose at a specific thermal gelation temperature significantly smoothes the fluororesin coating film during firing is as follows:
This phenomenon was discovered as a result of numerous experiments, and although the reason is still not fully clear,
This seems to be because in the combination of the present invention, the heat flow temperature of the heat flowable fluororesin and the decomposition temperature of the compounding agent (binder) are close to each other. (Preferred Embodiment) In the present invention, it is preferable to use tetrafluoroethylene/perfluoroalkyl vinyl ether (PFA) alone as the heat-flowable fluororesin, but other heat-flowable fluororesins, such as tetrafluoroethylene/hexane Fluoropropylene copolymer (FEP), polychlorotrifluoroethylene (PCTFE), polyvinylidene fluoride (PVDF), polyvinyl fluoride (PVF), tetrafluoroethylene/ethylene copolymer (ETFE), etc. may also be used. . Among these,
PFA is most preferred, followed by FEP. In order to obtain these aqueous dispersions, for example, when powder or granules are used, they can be obtained by pulverizing them with a ball mill or the like, if necessary, and then dispersing them in water. In addition, aqueous dispersions or organosol emulsions in water obtained by emulsion polymerization can be used as they are. These aqueous dispersions may also contain other organic liquids, but it is not preferable to mix them in large amounts from the viewpoint of the working environment during coating. After hydroxypropyl methylcellulose is mixed with an aqueous dispersion of thermofluid fluororesin, the viscosity of a 2% aqueous solution is required to ensure ease of handling, i.e., ease of application with a spray gun and maintenance of uniformity of the coating film. It is preferably 400 cps or less at 20°C. The amount of hydroxypropyl methylcellulose to be blended is difficult to define, depending on the concentration of the aqueous dispersion of heat-flowable fluororesin, the type of hydroxypropyl methylcellulose, the desired coating thickness, etc. % to 10% by weight, especially 4% to 6% by weight. The amount is 2
If it is less than 10% by weight, the surface smoothness of the coating film after firing cannot be obtained, and if it exceeds 10% by weight, the decomposed product of hydroxypropyl methylcellulose tends to remain in the coating film even after firing, causing pinholes or non-adhesion. It may damage your sexuality. Any known method may be used to blend hydroxypropyl methylcellulose into an aqueous dispersion of a heat-flowable fluororesin, such as adding it directly to the aqueous dispersion while stirring, or adding it directly to the aqueous dispersion while stirring; Examples include a method of mixing with a dispersion liquid. Furthermore, in the present invention, the thickening effect of hydroxypropyl methylcellulose can be utilized to prevent dripping during application and to prevent repelling during overcoating. Sagging during coating occurs when the aqueous dispersion applied to a vertical surface flows, causing uneven streaks or puddles on the coating film, and repellency during multiple coatings occurs when a coating is applied once using an aqueous dispersion. This method is not preferred because a coating film of sufficient thickness cannot be obtained and multiple coats are often required. Prevention of such dripping and repelling is necessary, for example, if the goal is to have a coating thickness of 10 to 30μ. The viscosity of the aqueous dispersion of thermofluid fluororesin
By adding hydroxypropyl methylcellulose to 290 cps or more, dripping can be prevented, and by adding 350 cps or more, splashing can also be prevented. Of course, even if a known thickener other than hydroxypropyl methylcellulose is used, dripping and repelling can be prevented as long as the viscosity is within the above range. The viscosity here is determined by a B-type viscometer at 27
This is a value measured under the conditions of ℃ and 60 rpm. The fluororesin composition for coating of the present invention may also contain various other known additives, such as fatty acids, sulfuric acid esters of higher alcohols, alkylbenzenesulfonic acids, alkylnaphthalenesulfonic acids, polynaphthalenesulfonic acids, and Interfaces of these salts, carboxylic acids having fluoroalkyl groups, sulfonic acids, phosphoric acids and their salts, esters, polyoxyethylene alkyl ethers, polyoxyethylene alkyl phenyl ethers, polyoxyethylene acyl esters, sorbitan fatty acid esters, etc. The activator can be used as a dispersant or leveling agent, and higher alcohols such as octyl alcohol and cyclohexanol, ethylene glycol, polymethylsiloxane, etc. can be blended as antifoaming agents. In addition, pigments, dyes, inorganic and organic fillers, etc. may also be blended. Examples will be shown next, but the present invention is not limited to these examples unless the purpose of the invention is impaired. Example 1 and Comparative Examples 1 to 7 The formulations shown in Table 1 were added to an aqueous PFA dispersion containing 54% by weight of PFA having a melt viscosity of 3×10 5 ps at 372°C. The resulting PFA aqueous dispersion composition was coated with a bar coater on an iron plate roughened with sandpaper so that the dry coating thickness was 20 to 25μ.
After drying at 80°C for 10 minutes, it was baked at 380°C for 10 minutes.
Table 1 shows the results of visual judgment of the degree of cracking of the coating film during drying and the smoothness of the coating film surface after baking (◎...Very good crack prevention or surface smoothness, ○...Good, △ ...Minor cracks or slightly good smoothness, ×...Cracks or no smoothness). The following commercially available formulations were used. Hydroxypropyl methylcellulose; Metrose 65SH50 Shin-Etsu Chemical Silica; Mizukasil P-527 Mizusawa Chemical Calcium carbonate; Hakuenka PZ Shiraishi Kogyo Acrylic emulsion; Primal TR-534 Rohm & Haas Japan Polyvinyl alcohol; Gohsenol GH-17 Nippon Gohsei Carboxymethyl cellulose; Celogen PR Daiichi Kogyo Seiyaku Hydroxyethylcellulose; Natrosol 250LR Hercules
【表】【table】
【表】
実施例2及び比較例8〜10
実施例1と同じPFA水分散液に第2表に示す
セルロース誘導体を配合し、実施例1と同様の試
験を行つた。結果を第2表に示す。
尚、使用したセルロース誘導体は下記の市販品
である。
メチルセルロース;メトローズ
SM100 信越化学
ヒドロキシプロピルメチルセルロース;
メトローズ
60SH50,
65SH400,90SH100,
信越化学[Table] Example 2 and Comparative Examples 8 to 10 The same PFA aqueous dispersion as in Example 1 was blended with the cellulose derivatives shown in Table 2, and the same tests as in Example 1 were conducted. The results are shown in Table 2. The cellulose derivative used is a commercially available product listed below. Methylcellulose; Metrose SM100 Shin-Etsu Chemical Hydroxypropyl methylcellulose; Metrose 60SH50, 65SH400, 90SH100, Shin-Etsu Chemical
【表】
実施例 3
実施例1と同じPFAおよびヒドロキシプロピ
ルメチルセルロースとからなる水分散液にフツ素
系界面活性剤およびシリコン系消泡剤を各々
100ppm配合し、PFAが35重量%になるように水
を加えて調整した。できたPFA水分散液は27℃、
60rpmのB型粘度計での粘度が950cpsであつた。
この水分散液をスプレーガンを用いて鉄板上に塗
布したところ、塗布時のたれや乾燥時の塗膜ひび
割れあるいは重ね塗り時のはじきが生じず、焼成
後の塗膜表面の平滑性にも優れていた。
実施例 4
実施例1と同じPFA水分散液に実施例1と同
じヒドロキシプロピルメチルセルロースをPFA
に対し4重量部配合し、さらにカルボキシメチル
セルロース(セロゲン
PR)を2重量部、シリ
コン系消泡剤を100ppm配合した。できたPFA水
分散液は27℃、60rpmのB型粘度計での粘度が
760cpsであつた。この水分散液を用いてアルミ板
上に塗布したところ、塗布時のたれや乾燥時の塗
膜ひび割れあるいは重ね塗り時のはじきが生じ
ず、焼成後の塗膜表面の平滑性にも優れていた。
実施例 5
372℃での溶融粘度8×104psのFEPを53重量%
分散させたPFA水分散液にヒドロキシプロピル
メチルセルロース(メトローズR65SH50)を5重
量部、実施例3と同じ界面活性剤、消泡剤を
100ppmずつ配合し、FEPが35重量%になるよう
に水を加えて調整した。できたFEP水分散液は、
27℃、60rpmのB型粘度計での粘度が680cpsであ
つた。実施例3と同様に鉄板に塗布したところ、
塗布時のたれ、乾燥時の塗膜のひび割れ、重ね塗
り時のはじきが生じず、焼成後の塗膜表面の平滑
性にも優れていた。
(発明の効果)
本発明によれば、熱ゲル化温度が特定の範囲に
あるヒドロキシプロピルメチルセルロースを選択
し、これをテトラフルオロエチレン・パーフルオ
ロアルキルビニルエーテル共重合体(PFA)の
如き熱流動性フツ素樹脂に配合することにより、
乾燥時の熱流動性フツ素樹脂塗膜のひび割れを防
止し且つ焼成時の熱流動性フツ素樹脂塗膜を著し
く平滑化して、熱流動性フツ素樹脂水分散液をエ
ナメル化することが可能となつた。[Table] Example 3 A fluorine-based surfactant and a silicone-based antifoaming agent were added to the same aqueous dispersion of PFA and hydroxypropyl methylcellulose as in Example 1.
It was mixed with 100ppm and adjusted by adding water so that PFA was 35% by weight. The resulting PFA aqueous dispersion was heated to 27°C.
The viscosity measured with a B-type viscometer at 60 rpm was 950 cps.
When this aqueous dispersion was applied to an iron plate using a spray gun, there was no dripping during application, cracking of the coating during drying, or repellency during overcoating, and the surface of the coating after firing was excellent. was. Example 4 The same hydroxypropyl methylcellulose as in Example 1 was added to the same PFA aqueous dispersion as in Example 1.
In addition, 2 parts by weight of carboxymethyl cellulose (Celogen PR) and 100 ppm of a silicone antifoaming agent were added. The viscosity of the resulting PFA aqueous dispersion using a B-type viscometer at 27°C and 60 rpm is
It was 760cps. When this aqueous dispersion was applied to an aluminum plate, there was no sagging during application, cracking of the coating during drying, or repellency during overcoating, and the surface of the coating after firing was excellent. . Example 5 53% by weight FEP with melt viscosity 8×10 4 ps at 372°C
5 parts by weight of hydroxypropyl methyl cellulose (Metrose R 65SH50) and the same surfactant and antifoaming agent as in Example 3 were added to the dispersed PFA aqueous dispersion.
They were mixed in 100 ppm increments and adjusted by adding water so that the FEP was 35% by weight. The resulting FEP aqueous dispersion is
The viscosity measured using a Type B viscometer at 27°C and 60 rpm was 680 cps. When applied to an iron plate in the same manner as in Example 3,
There was no sagging during application, no cracking of the coating film during drying, no repellency during overcoating, and the surface smoothness of the coating film after baking was also excellent. (Effects of the Invention) According to the present invention, hydroxypropyl methyl cellulose having a thermal gelation temperature within a specific range is selected, and this is added to a thermofluidic material such as tetrafluoroethylene/perfluoroalkyl vinyl ether copolymer (PFA). By blending with base resin,
It is possible to enamel a heat-flowable fluororesin aqueous dispersion by preventing cracks in the heat-flowable fluororesin coating during drying and significantly smoothing the heat-flowable fluororesin coating during firing. It became.
Claims (1)
温度が60℃よりも高く且つ70℃以下のヒドロキシ
プロピルメチルセルロースを該樹脂当り2乃至10
重量%配合してなることを特徴とする塗装用フツ
素樹脂組成物。 2 熱流動性フツ素樹脂がテトラフルオロエチレ
ン・パーフルオロアルキルビニルエーテル共重合
体である請求項1記載の組成物。 3 熱流動性フツ素樹脂がテトラフルオロ・ヘキ
サフルオロプロピレン共重合体である請求項1記
載の組成物。[Claims] 1. Hydroxypropyl methylcellulose having a thermal gelation temperature higher than 60°C and lower than 70°C is added to an aqueous dispersion of a thermofluid fluororesin in an amount of 2 to 10% per resin.
A fluororesin composition for painting, characterized in that it contains % by weight. 2. The composition according to claim 1, wherein the thermofluid fluororesin is a tetrafluoroethylene/perfluoroalkyl vinyl ether copolymer. 3. The composition according to claim 1, wherein the thermofluid fluororesin is a tetrafluoro-hexafluoropropylene copolymer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58021691A JPS59147057A (en) | 1983-02-14 | 1983-02-14 | Fluororesin composition for coating |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58021691A JPS59147057A (en) | 1983-02-14 | 1983-02-14 | Fluororesin composition for coating |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS59147057A JPS59147057A (en) | 1984-08-23 |
| JPH0452310B2 true JPH0452310B2 (en) | 1992-08-21 |
Family
ID=12062089
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP58021691A Granted JPS59147057A (en) | 1983-02-14 | 1983-02-14 | Fluororesin composition for coating |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS59147057A (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2006095825A1 (en) * | 2005-03-10 | 2006-09-14 | Daikin Industries, Ltd. | Polytetrafluoroethylene aqueous dispersion composition, polytetrafluoroethylene resin film and polytetrafluoroethylene resin impregnated article |
| JP2014001360A (en) * | 2012-05-25 | 2014-01-09 | Olympus Corp | Elastomer composition and molded product |
| KR20230093515A (en) * | 2020-11-06 | 2023-06-27 | 다이킨 고교 가부시키가이샤 | Water-based paint compositions and painted articles |
| KR20230096106A (en) * | 2020-11-06 | 2023-06-29 | 다이킨 고교 가부시키가이샤 | Water-based paint compositions and painted articles |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| BE788611A (en) * | 1971-09-09 | 1973-03-08 | Rhone Poulenc Sa | PREPARATION OF NITRILE BY AMMOXIDATION OF BUTADIENE |
| DE2843475A1 (en) * | 1978-10-05 | 1980-04-17 | Bayer Ag | MONOAZO DYES |
-
1983
- 1983-02-14 JP JP58021691A patent/JPS59147057A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS59147057A (en) | 1984-08-23 |
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