JP2007204537A - Resin for polyester-based powder coating and method for producing the resin, and polyester-based powder coating - Google Patents

Resin for polyester-based powder coating and method for producing the resin, and polyester-based powder coating Download PDF

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JP2007204537A
JP2007204537A JP2006022629A JP2006022629A JP2007204537A JP 2007204537 A JP2007204537 A JP 2007204537A JP 2006022629 A JP2006022629 A JP 2006022629A JP 2006022629 A JP2006022629 A JP 2006022629A JP 2007204537 A JP2007204537 A JP 2007204537A
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resin
polyester
powder coating
based powder
coating
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Wataru Kajitani
亘 梶谷
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Nippon Ester Co Ltd
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Nippon Ester Co Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a resin for polyester-based powder coating highly adhesive to to-be-coated objects and containing no heavy metals in consideration of environmental pollution, and to provide such a polyester-based powder coating using the resin. <P>SOLUTION: The resin for polyester-based powder coating is made mainly from an aromatic dicarboxylic acid and a glycol. The resin has a hydroxyl number of 17-65 mgKOH/g. This resin is characterized in containing 100-400 ppm of a magnesium compound coated with titanic acid-based coating layer. A method for producing the above resin is provided, comprising using the above-mentioned magnesium compound as polymerization catalyst and incorporating the magnesium compound at 100-400 ppm based on the final resin. The polyester-based powder coating containing the above resin is also provided. <P>COPYRIGHT: (C)2007,JPO&INPIT

Description

本発明は、耐候性や密着性に優れ、かつアンチモンに代表される重金属を含まない環境面に配慮したポリエステル系粉体塗料用樹脂とその製造方法、ならびにその樹脂を含有するポリエステル系粉体塗料に関するものである。   The present invention relates to a polyester powder coating resin that is excellent in weather resistance and adhesion and is environmentally friendly and does not contain heavy metals such as antimony, a method for producing the same, and a polyester powder coating material containing the resin. It is about.

粉体塗料は、溶剤型塗料と比較して、VOC発生がない無公害型塗料であること、一度で厚塗り塗装が可能であること、塗装直後でも使用に供しうること、多層の重ね塗りが不要であること、比較的安価であること、回収利用が可能であること等の利点が認められ、家電製品、建材、自動車部品等の部材の保護装飾塗料として近年急速に需要が拡大している。
粉体塗料は主として、エポキシ樹脂系、アクリル樹脂系、ポリエステル樹脂系のものが使用されているが、その中でもポリエステル樹脂系粉体塗料はバランスのとれた塗膜性能を有する塗料である。
Compared with solvent-based paints, powder paints are pollution-free paints that do not generate VOCs, can be thickly coated at once, can be used immediately after painting, In recent years, there has been a rapid increase in demand for protective decorative paints for components such as home appliances, building materials, and automobile parts, because they are unnecessary, relatively inexpensive, and can be recovered and used. .
As the powder coating, epoxy resin-based, acrylic resin-based, and polyester resin-based ones are mainly used, and among them, the polyester resin-based powder coating is a coating having a balanced coating film performance.

ポリエステル系粉体塗料用樹脂を製造する時の重縮合触媒には、従来より三酸化アンチモンに代表されるアンチモン化合物が広く用いられている。三酸化アンチモンは安価で、かつ優れた触媒活性を有する重縮合触媒であるが、近年、環境面からアンチモンの安全性に対する問題が欧米をはじめ各国で指摘されている。   Conventionally, antimony compounds represented by antimony trioxide have been widely used as polycondensation catalysts for producing polyester powder coating resins. Antimony trioxide is a polycondensation catalyst that is inexpensive and has excellent catalytic activity. However, in recent years, problems regarding the safety of antimony have been pointed out in Europe and the United States from an environmental viewpoint.

三酸化アンチモン等のアンチモン系触媒に代わる重合触媒の検討も行われており、テトラアルコキシチタネートに代表されるチタン化合物やスズ化合物がすでに提案されているが、これらを用いて製造されたポリエステル系粉体塗料用樹脂は、重合時や塗膜の焼き付け時の着色が激しいという問題点を有する。   Studies on polymerization catalysts to replace antimony catalysts such as antimony trioxide have also been conducted, and titanium compounds and tin compounds represented by tetraalkoxy titanates have already been proposed. Polyester powders produced using these compounds The resin for body paint has a problem that the coloring at the time of polymerization or baking of the coating film is intense.

このようなチタン化合物を重合触媒として用いたときの問題点を克服する試みとして、例えば、特許文献1のように、重合触媒としてテトラアルコキシチタネートをコバルト化合物と同時に用いる方法が提案されている。ところが、これらの技術では、テトラアルコキシチタネートを重合触媒として用いた時の着色は低減されるものの、ポリエステル系粉体塗料用樹脂の熱分解を効果的に抑制することは達成されていないため、塗膜物性が低下する問題がある。また、コバルト化合物についても、三酸化アンチモンと同様に、近年、安全性に対する問題が指摘され始めている。   As an attempt to overcome the problems when such a titanium compound is used as a polymerization catalyst, for example, as disclosed in Patent Document 1, a method of using tetraalkoxy titanate as a polymerization catalyst simultaneously with a cobalt compound has been proposed. However, in these techniques, although coloring when tetraalkoxy titanate is used as a polymerization catalyst is reduced, it is not achieved to effectively suppress thermal decomposition of the resin for polyester powder coating. There is a problem that the film physical properties deteriorate. In addition, with respect to cobalt compounds as well as antimony trioxide, in recent years, safety problems have begun to be pointed out.

また、チタン化合物を触媒として用いて重合したポリエステルの熱劣化を抑制する他の試みとして、特許文献2のように、チタン化合物を触媒としてポリエステルを重合した後にリン系化合物を添加する方法が開示されている。しかし、重合後に添加剤を効果的に混ぜ込むことは、生産工程が複雑になるのと同時にコストアップにもつながり実用的でない。   Also, as another attempt to suppress thermal degradation of polyester polymerized using a titanium compound as a catalyst, a method of adding a phosphorus compound after polymerizing a polyester using a titanium compound as a catalyst is disclosed, as in Patent Document 2. ing. However, it is impractical to effectively mix the additives after polymerization, resulting in a complicated production process and cost increase.

アンチモン化合物以外で優れた触媒活性を有し、かつ色調ならびに熱安定性に優れた重合触媒としてゲルマニウム化合物がすでに実用化されているが、この触媒は非常に高価であるという問題点や、重合中に系外へ溜出しやすいため、反応系の触媒濃度が変化し重合の制御が困難になるという課題を有しており、触媒主成分として使用することには問題がある。
特開昭55−116722号公報 特開平10−259296号公報
Germanium compounds have already been put to practical use as polymerization catalysts that have excellent catalytic activity other than antimony compounds and are excellent in color tone and thermal stability. However, this catalyst is very expensive and is undergoing polymerization. However, since the catalyst concentration in the reaction system changes and polymerization control becomes difficult, there is a problem in using it as a catalyst main component.
JP-A-55-116722 JP-A-10-259296

解決しようとする問題点は、重金属を含まない環境問題に配慮したポリエステル系粉体塗料用樹脂を提供しようとするものである。   The problem to be solved is to provide a polyester-based powder coating resin that is free from heavy metals and is environmentally friendly.

本発明は、上記の課題を解決するもので、その要旨は、次の通りである。
(1)主として芳香族ジカルボン酸とグリコールとからなり、水酸基価が17〜65mgKOH/gである樹脂であって、チタン酸からなる被覆層が形成されたマグネシウム化合物を100〜400ppm含有することを特徴とするポリエステル系粉体塗料用樹脂。
(2)重合触媒としてチタン酸からなる被覆層が形成されたマグネシウム化合物を使用し、得られる樹脂に対して前記化合物を100〜400ppm添加すること特徴とする(1)記載のポリエステル系粉体塗料用樹脂の製造方法。
(3)上記(1)記載の樹脂を含有することを特徴とするポリエステル系粉体塗料。
The present invention solves the above-mentioned problems, and the gist thereof is as follows.
(1) A resin mainly composed of an aromatic dicarboxylic acid and glycol and having a hydroxyl value of 17 to 65 mgKOH / g and containing 100 to 400 ppm of a magnesium compound in which a coating layer made of titanic acid is formed. Polyester powder coating resin.
(2) A polyester powder coating composition according to (1), wherein a magnesium compound having a coating layer made of titanic acid is used as a polymerization catalyst, and the compound is added in an amount of 100 to 400 ppm to the resulting resin. Manufacturing method for resin.
(3) A polyester-based powder coating comprising the resin described in (1) above.

本発明によれば、アンチモンに代表される重金属を含まない環境に優しいポリエステル系粉体塗料用樹脂およびポリエステル系粉体塗料が提供される。   ADVANTAGE OF THE INVENTION According to this invention, the resin for polyester type powder coating materials and polyester type powder coating materials which do not contain the heavy metal represented by antimony and are friendly are provided.

以下、本発明について詳細に説明する。
本発明において、芳香族ジカルボン酸成分としては、テレフタル酸、イソフタル酸、無水フタル酸、フタル酸、ナフタレンジカルボン酸などの芳香族ジカルボン酸を主体とするものが用いられ、必要に応じてアジピン酸、セバシン酸、ドデカン二酸などの脂肪族ジカルボン酸、さらにはトリメリット酸、ピロメリット酸などの三価以上のカルボン酸を併用することができる。
また、グリコール成分としては、エチレングリコール、ジエチレングリコール、プロピレングリコール、1,4−ブタンジオール、1,6−ヘキサンジオール、ネオペンチルグリコールなどの脂肪族グリコールを主体とするものが用いられ、必要に応じて1,4−シクロヘキサンジメタノールなどの脂環族のアルコール、さらには、トリメチロールプロパン、グリセリン、ペンタエリスリトールなどの三価以上のアルコールを併用することができる。また、必要に応じて4−ヒドロキシ安息香酸、ε−カプロラクトンなどのヒドロキシカルボン酸を併用してもよい。
The present invention will be described in detail below.
In the present invention, as the aromatic dicarboxylic acid component, those mainly composed of aromatic dicarboxylic acid such as terephthalic acid, isophthalic acid, phthalic anhydride, phthalic acid, naphthalenedicarboxylic acid are used, and if necessary, adipic acid, Aliphatic dicarboxylic acids such as sebacic acid and dodecanedioic acid, and trivalent or higher carboxylic acids such as trimellitic acid and pyromellitic acid can be used in combination.
Moreover, as a glycol component, what mainly has aliphatic glycols, such as ethylene glycol, diethylene glycol, propylene glycol, 1, 4- butanediol, 1, 6-hexanediol, neopentyl glycol, is used, as needed An alicyclic alcohol such as 1,4-cyclohexanedimethanol, and trihydric or higher alcohols such as trimethylolpropane, glycerin, and pentaerythritol can be used in combination. Moreover, you may use together hydroxycarboxylic acids, such as 4-hydroxybenzoic acid and (epsilon) -caprolactone, as needed.

本発明のポリエステル系粉体塗料用樹脂は、チタン酸からなる被覆層が形成されたマグネシウム化合物(以下、被覆体ともいう。)を100〜400ppm含有することが必要である。ポリエステル系粉体塗料用樹脂の重合反応時に、被覆体が樹脂に対して100ppm未満になるように添加されると、重合触媒としての活性が十分ではなく、一方、400ppmを超えて添加されると、得られるポリエステル系粉体塗料用樹脂の色調が悪化したり、被覆体がポリエステル系粉体塗料用樹脂中で凝集して異物の原因となり、塗膜外観を損なうことになる。   The polyester-based powder coating resin of the present invention needs to contain 100 to 400 ppm of a magnesium compound (hereinafter also referred to as a coating) on which a coating layer made of titanic acid is formed. When the polyester-based powder coating resin is added so that the coating is less than 100 ppm relative to the resin during the polymerization reaction, the activity as a polymerization catalyst is not sufficient. The color tone of the resulting polyester-based powder coating resin deteriorates, or the coated body aggregates in the polyester-based powder coating resin to cause foreign matters, thereby impairing the appearance of the coating film.

本発明において、チタン酸からなる被覆層が形成されたマグネシウム化合物(被覆体)とは、5〜100℃の範囲温度、好ましくは、15〜70℃の範囲温度でマグネシウム化合物の存在下にチタン化合物を加水分解して、その表面にチタン酸を析出させることによって、マグネシウム化合物の表面にチタン酸からなる被覆層を有せしめたものである。   In the present invention, a magnesium compound (coated body) having a coating layer made of titanic acid is a titanium compound in the presence of a magnesium compound at a temperature in the range of 5 to 100 ° C., preferably in the range of 15 to 70 ° C. Is hydrolyzed, and titanic acid is precipitated on the surface thereof, whereby the surface of the magnesium compound is provided with a coating layer made of titanic acid.

マグネシウム化合物は特に限定されるものではないが、例えば、水酸化マグネシウム、炭酸マグネシウム、酢酸マグネシウム、マグネシウムアセチルアセトネート、酢酸以外のカルボン酸塩などが挙げられ、特に水酸化マグネシウムが好ましい。   Although a magnesium compound is not specifically limited, For example, magnesium hydroxide, magnesium carbonate, magnesium acetate, magnesium acetylacetonate, carboxylates other than acetic acid, etc. are mentioned, Especially magnesium hydroxide is preferable.

チタン化合物としては、チタンハロゲン化物、チタン酸塩、チタンアルコキシド類が用いられる。   Titanium halides, titanates, and titanium alkoxides are used as the titanium compound.

本発明で用いるチタン化合物とマグネシウム化合物は、いずれか一方もしくは両者に2種類以上の化合物を用いて被覆体としてもよい。   The titanium compound and magnesium compound used in the present invention may be used as a coating by using two or more kinds of compounds in either one or both.

本発明のポリエステル系粉体塗料用樹脂の水酸基価は17〜65mgKOH/gであることが必要である。ポリエステル系粉体塗料用樹脂の水酸基価が17mgKOH/gに満たないと、樹脂の分子量が高く、流動性が低下するため、塗膜の加工性が低下するばかりか、素材との密着性が悪くなる。一方、水酸基価が65mgKOH/gを超えると、塗料に配合する硬化剤量が多くなり結果としてコストアップになる。また、架橋密度が上がるため、塗膜の平滑性が低下する。   The hydroxyl value of the polyester-based powder coating resin of the present invention is required to be 17 to 65 mgKOH / g. If the hydroxyl value of the polyester powder coating resin is less than 17 mgKOH / g, the molecular weight of the resin is high and the fluidity is lowered, so that not only the processability of the coating film is lowered but also the adhesion to the material is poor. Become. On the other hand, when the hydroxyl value exceeds 65 mgKOH / g, the amount of the curing agent added to the paint increases, resulting in an increase in cost. Moreover, since the crosslink density increases, the smoothness of the coating film decreases.

本発明のポリエステル系粉体塗料用樹脂は、例えば次のように製造することができる。前記のカルボン酸成分、グリコール成分(それらのエステル形成誘導体を含む)などの原料をエステル化反応槽に仕込み、200〜280℃の温度で、窒素ガス雰囲気下で2〜10時間、エステル化反応又はエステル交換反応を行う。次いで、重縮合反応槽に移送し、濃度が100〜400ppmとなるようにチタン酸からなる被覆層が形成されたマグネシウム化合物(被覆体)を添加し、温度200〜300℃、5hPa以下の減圧下で重縮合反応を行い、高重合度のポリエステル系粉体塗料用樹脂を得る。その後グリコール成分を添加して、220〜290℃の反応温度で2〜5時間解重合する方法で製造することが出来る。
または、上記方法で被覆体を添加したのち、温度200〜300℃、100hPa以下の減圧下で重縮合反応を行い、所定の分子量に達した時点で重合を終了することでも製造することが出来る。
The polyester powder coating resin of the present invention can be produced, for example, as follows. Raw materials such as the carboxylic acid component and glycol component (including their ester-forming derivatives) are charged into an esterification reaction vessel, and the esterification reaction or the reaction is performed at a temperature of 200 to 280 ° C. in a nitrogen gas atmosphere for 2 to 10 hours. A transesterification reaction is performed. Subsequently, it is transferred to a polycondensation reaction tank, and a magnesium compound (covered body) in which a coating layer made of titanic acid is formed so as to have a concentration of 100 to 400 ppm is added, and the pressure is reduced to 200 to 300 ° C. and 5 hPa or less. A polycondensation reaction is carried out to obtain a polyester-based powder coating resin having a high degree of polymerization. Thereafter, a glycol component is added, and the polymer can be produced by depolymerization at a reaction temperature of 220 to 290 ° C. for 2 to 5 hours.
Alternatively, it can also be produced by adding a covering by the above method, performing a polycondensation reaction under a reduced pressure of a temperature of 200 to 300 ° C. and 100 hPa or less, and ending the polymerization when a predetermined molecular weight is reached.

チタン酸からなる被覆層が形成されたマグネシウム化合物(被覆体)の添加方法は特に限定されるものではないが、被覆体を分散媒中に分散させたスラリーとして、重縮合反応時に添加することが好ましい。なお、スラリー中の被覆体の含有量は0.5〜3質量%が好ましい。0.5質量%未満では、スラリーの添加量が多くなり、重縮合反応中に多量の溜出物が生成し、コストアップにつながりやすい。逆に、3質量%を超えると、ポリエステル系粉体塗料用樹脂中にスラリーを添加した際に、被覆体の凝集が起こりやすく、被覆体が粗大粒子となり、塗膜外観を損なう原因となりやすい。   The addition method of the magnesium compound (coating body) on which the coating layer made of titanic acid is formed is not particularly limited, but it may be added at the time of the polycondensation reaction as a slurry in which the coating body is dispersed in a dispersion medium. preferable. In addition, 0.5-3 mass% is preferable for content of the coating body in a slurry. If the amount is less than 0.5% by mass, the amount of slurry added increases, and a large amount of distillate is generated during the polycondensation reaction, which tends to increase costs. On the other hand, when the content exceeds 3% by mass, the agglomeration of the coating tends to occur when the slurry is added to the polyester-based powder coating resin, and the coating tends to be coarse particles, which tends to impair the appearance of the coating film.

上記被覆体のスラリーに用いる分散媒は、エチレングリコール、1,2−プロピレングリコール、1,3−プロピレングリコール、ジエチレングリコール、トリエチレングリコール、テトラエチレングリコール、1,2−ブチレングリコール、1,3−ブチレングリコール、2,3−ブチレングリコール、1,4−ブチレングリコールなどが挙げられ、これらの中でも特にエチレングリコールが好ましい。   The dispersion medium used for the slurry of the coating is ethylene glycol, 1,2-propylene glycol, 1,3-propylene glycol, diethylene glycol, triethylene glycol, tetraethylene glycol, 1,2-butylene glycol, 1,3-butylene. Examples thereof include glycol, 2,3-butylene glycol, and 1,4-butylene glycol. Among these, ethylene glycol is particularly preferable.

また、ポリエステル系粉体塗料用樹脂中で被覆体が凝集して異物となり、塗膜外観異常を防ぐには、エチレングリコール等の分散媒に所定量の被覆体を添加し、撹拌混合した後、超音波処理を行うことが好ましい。   Moreover, in order to prevent coating film appearance abnormality by agglomerating the coating in the polyester powder coating resin, and adding a predetermined amount of the coating to a dispersion medium such as ethylene glycol, stirring and mixing, It is preferable to perform ultrasonic treatment.

なお、超音波の周波数は通常の周波数領域でよく、例えば、20kHz程度から100kHzの範囲を適用できる。超音波を発生させる発振源としては、公知の手段でよく、例えば水晶を用いた圧電振動子、ニッケルやフェライトを用いた電歪発振子等が挙げられる。また、超音波処理の時間は、0.5〜5時間の範囲が好ましい。   In addition, the frequency of an ultrasonic wave may be a normal frequency region, and for example, a range of about 20 kHz to 100 kHz can be applied. As an oscillation source for generating ultrasonic waves, known means may be used, and examples thereof include a piezoelectric vibrator using crystal, an electrostrictive oscillator using nickel or ferrite, and the like. In addition, the ultrasonic treatment time is preferably in the range of 0.5 to 5 hours.

さらに、本発明の効果を阻害しない範囲であれば、ヒンダードフェノール系化合物のような抗酸化剤、蛍光剤、染料のような色調改良剤、耐光剤等の添加物がポリエステル系粉体塗料用樹脂に含有されてもよい。   Furthermore, if it does not inhibit the effect of the present invention, additives such as antioxidants such as hindered phenol compounds, color improvers such as fluorescent agents and dyes, and light resistance agents are used for polyester powder coatings. It may be contained in the resin.

次に、本発明のポリエステル系粉体塗料の製造方法について説明する。
ポリエステル系粉体塗料用樹脂に、レベリング剤、添加剤、硬化剤、硬化触媒などを加え、ニーダーまたはロールを用いて70〜140℃で溶融混練することによって製造することが出来る。その後、被塗物に塗装し、通常170〜190℃の温度で、15〜25分間焼き付けることにより、塗膜を得る。
Next, the manufacturing method of the polyester-type powder coating material of this invention is demonstrated.
It can be produced by adding a leveling agent, an additive, a curing agent, a curing catalyst, etc. to a polyester powder coating resin, and melt-kneading at 70 to 140 ° C. using a kneader or a roll. Then, it coats on a to-be-coated object, and a coating film is obtained by baking for 15-25 minutes normally at the temperature of 170-190 degreeC.

本発明のポリエステル系粉体塗料に用いる硬化剤は特に限定されるものではないが、硬化時にラクタムを発生しないウレトジオン環結合型の内部ブロックドイソホロンジイソシアネート(ヒュルス社製BF1540)が好適である。これ以外に、例えばε−カプロラクタムでブロックしたイソホロンジイソシアネート系硬化剤(ヒュルス社製ベスタゴンB−1530、住友バイエルウレタン社製クレランUI)、ε−カプロラクタムでブロックした水添ジフェニルメタンジイソシアネート系硬化剤(McWHORTER社製24−2430)、グリコールウリル系硬化剤(アメリカンサイアナミド社製POWDER LINK1174)などの硬化剤を使用することが可能である。
硬化剤の配合量はポリエステル樹脂の水酸基価に対して0.5〜1.5倍当量、好ましくは0.8〜1.2倍当量とする。
さらに硬化触媒としてジオクチル錫マレエート系硬化触媒(三共有機合成社製「Stann OMF」)などを添加してもよい。
The curing agent used in the polyester powder coating material of the present invention is not particularly limited, but uretdione ring-bonded internal blocked isophorone diisocyanate (BF1540 manufactured by Huls) that does not generate lactam during curing is suitable. Other than this, for example, isophorone diisocyanate curing agent blocked with ε-caprolactam (Hestus Vestagon B-1530, Sumitomo Bayer Urethane Clerant UI), hydrogenated diphenylmethane diisocyanate curing agent blocked with ε-caprolactam (McWHORTER) It is possible to use hardeners, such as a product made from 24-2430) and a glycoluril type hardening | curing agent (POWDER LINK1174 by American Cyanamid Co., Ltd.).
The compounding amount of the curing agent is 0.5 to 1.5 times equivalent, preferably 0.8 to 1.2 times equivalent to the hydroxyl value of the polyester resin.
Further, a dioctyl tin maleate-based curing catalyst (“Stan OMF” manufactured by Sansha Co., Ltd.) may be added as a curing catalyst.

次に、実施例および比較例によって本発明を具体的説明する。
(1)水酸基価
ピリジン50mlにポリエステル系粉体塗料用樹脂3.0g溶解させて無水酢酸0.6ml添加して加熱してアセチル化を行い、0.5モル/lの水酸化カリウムメタノール溶液で滴定して求めた。
(2)色調
日本電飾工業社製の色差計ND−Σ80型を用い、ハンターLab表色計のb値を求めて評価した。b値は値が大きいほど黄色味が強くなり、極端に小さくならない限り、小さい方が良い。
○:b値が15.0未満。
×:b値が15.0以上。
(3)平滑性
塗膜の平滑性と色を目視により評価した。
○:塗膜に凸凹が少なく平滑性が良好で、塗膜の色が良好なもの。
×:塗膜に大きな凸凹があり平滑性が良くない、または、塗膜の色が悪いもの。
(4)耐衝撃性
JIS K 5400に準じ、直径1.27cmの球面を持つ撃ち型とそれに合う窪みを持つ受け台との間に塗膜が球面に接触するように塗装鋼板を挟み込み、その上から0.5kgのおもりを垂直に落下させて、塗膜の破壊する高さを求めた。
○:15cmの高さからおもりを落下させても塗膜に割れが起きなかった。
×:15cmの高さからおもりを落下させたところ、塗膜に割れが起きた。
(5)エリクセン
JIS Z 2247に準じて求めた。
○:2mm押し出しても塗膜に割れやヒビがなかった。
×:2mm押し出したところ、塗膜に割れやヒビが生じた。
Next, the present invention will be specifically described with reference to examples and comparative examples.
(1) Hydroxyl value 3.0 g of a resin for polyester powder coating is dissolved in 50 ml of pyridine, 0.6 ml of acetic anhydride is added, the mixture is heated and acetylated, and a 0.5 mol / l potassium hydroxide methanol solution is used. Determined by titration.
(2) Color tone Using a color difference meter ND-Σ80 manufactured by Nippon Denka Kogyo Co., Ltd., the b value of a Hunter Lab colorimeter was determined and evaluated. The larger the b value, the stronger the yellow color, and the smaller the b value, the better unless it becomes extremely small.
○: b value is less than 15.0.
X: b value is 15.0 or more.
(3) Smoothness The smoothness and color of the coating film were visually evaluated.
○: The coating film has few unevenness, good smoothness, and good coating film color.
X: The coating film has large unevenness and the smoothness is not good, or the coating film has a poor color.
(4) Impact resistance According to JIS K 5400, a coated steel plate is sandwiched between a shooting mold having a spherical surface with a diameter of 1.27 cm and a cradle having a recess corresponding thereto, so that the coating film comes into contact with the spherical surface. A 0.5 kg weight was dropped vertically to determine the height at which the coating film was destroyed.
○: Even if the weight was dropped from a height of 15 cm, the coating film was not cracked.
X: When the weight was dropped from a height of 15 cm, the coating film was cracked.
(5) Eriksen Determined according to JIS Z 2247.
○: The film was not cracked or cracked even when extruded 2 mm.
X: When extruded 2 mm, the coating film was cracked or cracked.

実施例1
テレフタル酸7.386kmol(1227kg)、イソフタル酸3.1662kmol(526kg)、水10質量%混合ネオペンチルグリコール13.187kmol(1526kg)をエステル化反応槽に仕込み、圧力0.25MPa、温度260℃で6時間エステル化反応を行った。得られたエステル化物を重縮合反応槽に移送した後、重縮合触媒として、水酸化マグネシウムの表面にチタン酸からなる被覆層が形成された被覆体(堺化学工業社製チタンコートMGZ)の濃度が1.5質量%に調製されたエチレングリコールスラリー58.3kg(被覆体の含有量がポリエステル系粉体塗料用樹脂に対して350ppm)を加え0.5hPaに減圧し、280℃で4時間重縮合反応を行い、極限粘度0.45dl/gの樹脂を得た。次いでこの樹脂にグリセリン0.264kmol(23.8kg)、トリメチロールプロパン0.053kmol(7.1kg)を添加して常圧下、270℃で1時間解重合反応を行い、表1に示す特性値のポリエステル系粉体塗料用樹脂を得た。
得られたポリエステル系粉体塗料用樹脂にウレトジオン環結合型の内部ブロックドイソホロンジイソシアネート(ヒュルス社製「BF1540」)を配合し、ブチルポリアクリレート系レベリング剤(BASF社製「アクロナール4F」)、ベンゾイン、ルチル型二酸化チタン顔料(石原産業社製「タイペークCR−90」)を添加し、ヘンシェルミキサー(三井三池製作所製「FM10B型」)でドライブレンドした後、コ・ニーダ(ブッス社製「PR−46型」)を用いて100℃で溶融混練し冷却、粉砕後140メッシュ(106μm)の金網で分級して粉体塗料を得た。得られた粉体塗料をリン酸亜鉛処理鋼板上に膜厚が50〜60μmとなるように静電塗装して、180℃で20分焼き付けを行った。塗膜の性能を表1に示す。
Example 1
7.386 kmol (1227 kg) of terephthalic acid, 3.1626 kmol (526 kg) of isophthalic acid, and 13.187 kmol (1526 kg) of neopentyl glycol mixed with 10% by weight of water were charged into an esterification reaction tank, and the pressure was 0.25 MPa and the temperature was 260 ° C. A time esterification reaction was performed. After the obtained esterified product is transferred to a polycondensation reaction tank, the concentration of a coated body (a titanium coat MGZ manufactured by Sakai Chemical Industry Co., Ltd.) in which a coating layer made of titanic acid is formed on the surface of magnesium hydroxide as a polycondensation catalyst. 58.3 kg of ethylene glycol slurry prepared at 1.5% by mass (the content of the coating is 350 ppm with respect to the polyester powder coating resin), and the pressure is reduced to 0.5 hPa, and the weight is increased at 280 ° C. for 4 hours. A condensation reaction was performed to obtain a resin having an intrinsic viscosity of 0.45 dl / g. Next, 0.264 kmol (23.8 kg) of glycerin and 0.053 kmol (7.1 kg) of trimethylolpropane were added to this resin, and a depolymerization reaction was performed at 270 ° C. for 1 hour under normal pressure. The characteristic values shown in Table 1 were obtained. A polyester powder coating resin was obtained.
The resulting polyester-based resin for powder coatings is blended with uretdione ring-bonded internal blocked isophorone diisocyanate ("BF1540" from Huls), butylpolyacrylate leveling agent ("Acronal 4F" from BASF), benzoin , Rutile type titanium dioxide pigment (“Taipek CR-90” manufactured by Ishihara Sangyo Co., Ltd.) was added and dry blended with a Henschel mixer (“FM10B type” manufactured by Mitsui Miike Manufacturing Co., Ltd.). 46 type ") was melt-kneaded at 100 ° C, cooled, pulverized, and then classified with a 140 mesh (106 µm) wire mesh to obtain a powder coating material. The obtained powder coating material was electrostatically coated on a zinc phosphate-treated steel sheet so as to have a film thickness of 50 to 60 μm, and baked at 180 ° C. for 20 minutes. Table 1 shows the performance of the coating film.

実施例2〜5
実施例1と同様な方法で、仕込組成、重合触媒の添加量を変更し、表1に示すようなポリエステル系粉体塗料用樹脂を得た。更に得られたポリエステル系粉体塗料用樹脂を用いて表1に示す配合比率でポリエステル系粉体塗料を得た。
Examples 2-5
In the same manner as in Example 1, the charge composition and the addition amount of the polymerization catalyst were changed to obtain a polyester powder coating resin as shown in Table 1. Further, a polyester powder coating material was obtained at the blending ratio shown in Table 1 using the obtained polyester powder coating resin.

比較例1〜4
実施例1〜5と同様な方法で、仕込組成、重合触媒の添加量を変更し表1に示すようなポリエステル系粉体塗料用樹脂を得た。更に得られたポリエステル系粉体塗料用樹脂を用いて表1に示す配合比率でポリエステル系粉体塗料を得た。
Comparative Examples 1-4
In the same manner as in Examples 1 to 5, the charge composition and the addition amount of the polymerization catalyst were changed to obtain a polyester powder coating resin as shown in Table 1. Further, a polyester powder coating material was obtained at the blending ratio shown in Table 1 using the obtained polyester powder coating resin.

実施例1〜5で得られたポリエステル系粉体塗料用樹脂の色調は良好であり、ポリエステル系粉体塗料は物性や塗膜のフロー性、色が良好であった。
比較例1は、ポリエステル系粉体塗料用樹脂の色調が悪く、塗膜の色が悪い結果となった。比較例2は、ポリエステル系粉体塗料用樹脂の水酸基価が高く、塗膜の平滑性が劣る結果となった。比較例3は、ポリエステル系粉体塗料用樹脂の水酸基価が低く、塗膜の平滑性が劣り、耐衝撃性とエリクセンが悪かった。比較例4は、ポリエステル系粉体塗料用樹脂の重合触媒の添加量が少なかったため、重合度が上がらず反応を途中で中止した。

The color tone of the resin for polyester powder coating obtained in Examples 1 to 5 was good, and the polyester powder coating had good physical properties, flow property of coating film, and color.
In Comparative Example 1, the color tone of the polyester powder coating resin was poor and the color of the coating film was poor. In Comparative Example 2, the polyester-based powder coating resin had a high hydroxyl value, resulting in poor smoothness of the coating film. In Comparative Example 3, the hydroxyl value of the polyester-based powder coating resin was low, the smoothness of the coating film was poor, and the impact resistance and elixsen were poor. In Comparative Example 4, since the addition amount of the polymerization catalyst of the polyester powder coating resin was small, the degree of polymerization did not increase and the reaction was stopped midway.

Claims (3)

主として芳香族ジカルボン酸とグリコールとからなり、水酸基価が17〜65mgKOH/gである樹脂であって、チタン酸からなる被覆層が形成されたマグネシウム化合物を100〜400ppm含有することを特徴とするポリエステル系粉体塗料用樹脂。 A polyester mainly composed of an aromatic dicarboxylic acid and a glycol and having a hydroxyl value of 17 to 65 mgKOH / g and containing 100 to 400 ppm of a magnesium compound having a coating layer made of titanic acid. -Based powder coating resin. 重合触媒としてチタン酸からなる被覆層が形成されたマグネシウム化合物を使用し、得られる樹脂に対して前記化合物を100〜400ppm添加すること特徴とする請求項1記載のポリエステル系粉体塗料用樹脂の製造方法。 2. The polyester-based powder coating resin according to claim 1, wherein a magnesium compound having a coating layer made of titanic acid is used as a polymerization catalyst, and the compound is added in an amount of 100 to 400 ppm based on the resulting resin. Production method. 請求項1記載の樹脂を含有することを特徴とするポリエステル系粉体塗料。

A polyester-based powder paint comprising the resin according to claim 1.

JP2006022629A 2006-01-31 2006-01-31 Resin for polyester-based powder coating and method for producing the resin, and polyester-based powder coating Pending JP2007204537A (en)

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WO2011034156A1 (en) * 2009-09-15 2011-03-24 堺化学工業株式会社 Polycondensation catalyst for the production of polyesters, and polyester production method using same
JP2012077112A (en) * 2010-09-30 2012-04-19 Sakai Chem Ind Co Ltd Polycondensation catalyst for manufacturing polyester and method for manufacturing polyester by using the same
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Publication number Priority date Publication date Assignee Title
WO2011034156A1 (en) * 2009-09-15 2011-03-24 堺化学工業株式会社 Polycondensation catalyst for the production of polyesters, and polyester production method using same
JP2011063640A (en) * 2009-09-15 2011-03-31 Sakai Chem Ind Co Ltd Polycondensation catalyst for producing polyester, and method for producing polyester using the same
CN102482406A (en) * 2009-09-15 2012-05-30 堺化学工业株式会社 Polycondensation catalyst for the production of polyesters, and polyester production method using same
KR20120083385A (en) * 2009-09-15 2012-07-25 사까이가가꾸고오교가부시끼가이샤 Polycondensation catalyst for producing polyester and method for producing polyester using the same
US8901029B2 (en) 2009-09-15 2014-12-02 Sakai Chemical Industry Co., Ltd. Polycondensation catalyst for producing polyester and method for producing polyester using the same
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JP2012077112A (en) * 2010-09-30 2012-04-19 Sakai Chem Ind Co Ltd Polycondensation catalyst for manufacturing polyester and method for manufacturing polyester by using the same
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