JPH11302567A - Production of thermosetting coating composition - Google Patents
Production of thermosetting coating compositionInfo
- Publication number
- JPH11302567A JPH11302567A JP11471998A JP11471998A JPH11302567A JP H11302567 A JPH11302567 A JP H11302567A JP 11471998 A JP11471998 A JP 11471998A JP 11471998 A JP11471998 A JP 11471998A JP H11302567 A JPH11302567 A JP H11302567A
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- Prior art keywords
- organic solvent
- solution
- resin
- weight
- powder coating
- Prior art date
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Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、熱硬化型塗料組成
物の新規な製造方法に関する。[0001] The present invention relates to a novel method for producing a thermosetting coating composition.
【0002】[0002]
【従来の技術及びその課題】従来の粉体塗料組成物は硬
化型樹脂、硬化剤、添加剤をドライブレンドした後、溶
融混練機により混和分散させ、次いで粉砕、分級させる
ことによって製造してきた。2. Description of the Related Art Conventional powder coating compositions have been produced by dry-blending a curable resin, a curing agent, and additives, mixing and dispersing them by a melt kneader, and then pulverizing and classifying.
【0003】しかしながら、この方法では硬化型樹脂と
硬化剤を熱で溶融させて混練りするため、硬化型樹脂と
硬化剤との反応が進行し高分子量化する。このため粉体
塗料の溶融粘度が高くなり仕上がり性が低下したりする
といった問題点がある。However, in this method, the curable resin and the curing agent are melted by heat and kneaded, so that the reaction between the curable resin and the curing agent proceeds to increase the molecular weight. For this reason, there is a problem that the melt viscosity of the powder coating material is increased and the finish is reduced.
【0004】このような問題点を改善する方法として、
硬化型樹脂、硬化剤、添加剤等の粉体用原料を有機溶剤
に溶解して得られる粉体塗料用原料溶液を減圧下で溶融
混練しながら配合した有機溶剤を除去する方法(特開昭
53−50232号公報、特開昭53−50233号公
報、特開昭53−50234号公報及び特開平5−31
1096号公報)が公知である。しかしながら、これら
の公知の方法によって得られた粉体塗料は、有機溶剤を
全く含まないかもしくは1.5重量%以下の量に調整さ
れたものであり、この様なものを使用しても高度な仕上
がり外観を有する塗膜は得られないことが分かった。[0004] As a method of improving such a problem,
A method in which a raw material solution for a powder coating obtained by dissolving a raw material for a powder such as a curable resin, a curing agent, and an additive in an organic solvent is melt-kneaded under reduced pressure while removing the compounded organic solvent (Japanese Patent Application Laid-Open JP-A-53-50232, JP-A-53-50233, JP-A-53-50234 and JP-A-5-31
No. 1096) is known. However, the powder coatings obtained by these known methods contain no organic solvent or have been adjusted to an amount of 1.5% by weight or less. It was found that a coating film having an excellent finished appearance could not be obtained.
【0005】[0005]
【発明が解決しようとする課題】本発明は、従来の方法
において更に高度な仕上がり外観を有する塗膜が形成で
きる熱硬化型粉体塗料組成物の製造方法を確立すること
を目的とする。SUMMARY OF THE INVENTION An object of the present invention is to establish a method for producing a thermosetting powder coating composition capable of forming a coating film having a higher finished appearance in the conventional method.
【0006】[0006]
【課題を解決するための手段】本発明者らは、かかる問
題を解決するため鋭意研究を重ねた結果、従来の製造方
法において、特に有機溶剤量を特定範囲に調整すること
により、従来からの問題点を解消できることが分かり、
本発明を完成するに至った。Means for Solving the Problems The inventors of the present invention have conducted intensive studies to solve the above-mentioned problems, and as a result, in the conventional production method, in particular, by adjusting the amount of the organic solvent to a specific range, the conventional method was used. It turns out that the problem can be solved,
The present invention has been completed.
【0007】即ち、本発明は 1、有機溶剤に溶解もしくは分散してなる固形分10〜
90重量%の範囲の熱硬化型粉体塗料用原料溶液を、該
有機溶剤量が1.6〜5重量%の範囲になるように減圧
下に加熱溶融混合しながら除去してなることを特徴とす
る熱硬化型塗料組成物の製造方法、 2、下記工程 (1)熱硬化型粉体用樹脂を有機溶剤溶液で製造して有
機溶剤樹脂溶液を得る工程、(2)該有機溶剤樹脂溶液
中に硬化剤を配合して固形分10〜90重量%の範囲の
熱硬化型粉体塗料用原料溶液を得る工程、(3)該有機
溶剤量が1.6〜5重量%の範囲になるように減圧下に
加熱溶融混合しながら除去して熱硬化型粉体塗料組成物
を得る工程、を連続して製造することを特徴とする熱硬
化型塗料組成物に関する。That is, the present invention relates to: 1. A solid content of 10 to 10 dissolved or dispersed in an organic solvent.
A raw material solution for a thermosetting powder coating material in a range of 90% by weight is removed while heating and melting under reduced pressure so that the amount of the organic solvent is in a range of 1.6 to 5% by weight. 2. A method for producing a thermosetting coating composition, 2. The following steps (1) a step of producing a thermosetting powder resin with an organic solvent solution to obtain an organic solvent resin solution, and (2) the organic solvent resin solution A step of mixing a curing agent therein to obtain a raw material solution for a thermosetting powder coating material having a solid content of 10 to 90% by weight, and (3) the amount of the organic solvent is in a range of 1.6 to 5% by weight. And a step of obtaining a thermosetting powder coating composition by removing while heating and mixing under reduced pressure to obtain a thermosetting powder coating composition.
【0008】[0008]
【発明の実施の形態】本発明で使用する熱硬化型粉体塗
料用原料溶液は、有機溶剤に硬化型樹脂、硬化剤及び必
要に応じて添加剤を溶解もしくは分散してなるものであ
る。硬化型樹脂としてはエポキシ基、水酸基、カルボキ
シル基等の官能基を有する、常温で固形のアクリル系樹
脂、ポリエステル系樹脂、エポキシ系樹脂、シリコン系
樹脂、フッ素系樹脂及びこれら2種以上の変性樹脂又は
混合樹脂などが用いられる。硬化型樹脂はガラス転移温
度が40〜100℃、好ましくは50℃〜80℃の範囲で、数平
均分子量が1000〜30000好ましくは2000〜10000のものが
好ましい。ガラス転移温度が40℃より低いと得られる粉
体塗料は粒子同士が融着をおこし耐ブロッキング性が悪
くなるので好ましくない。また100℃より高いと熱フロ
ー時の粘度が上がり仕上がり性が低下するばかりでな
く、溶解性が低下する。また数平均分子量が1000を下回
ると粉体塗料の耐ブロッキング性が劣る。数平均分子量
が30000を超えると塗膜の仕上がり外観が劣るので好ま
しくはない。該ガラス転移温度は、例えばDSC (示査走
査熱量計)によって求めることができる。BEST MODE FOR CARRYING OUT THE INVENTION The raw material solution for a thermosetting powder coating material used in the present invention is obtained by dissolving or dispersing a curable resin, a curing agent and, if necessary, an additive in an organic solvent. As the curable resin, an acrylic resin, a polyester resin, an epoxy resin, a silicone resin, a fluorine resin, and two or more modified resins having functional groups such as an epoxy group, a hydroxyl group, and a carboxyl group which are solid at room temperature. Alternatively, a mixed resin or the like is used. The curable resin preferably has a glass transition temperature of 40 to 100 ° C, preferably 50 to 80 ° C, and a number average molecular weight of 1,000 to 30,000, preferably 2000 to 10,000. If the glass transition temperature is lower than 40 ° C., the resulting powder coating is not preferred because the particles fuse together and the blocking resistance deteriorates. On the other hand, when the temperature is higher than 100 ° C., not only the viscosity at the time of heat flow increases but the finish property decreases, but also the solubility decreases. When the number average molecular weight is less than 1,000, the blocking resistance of the powder coating material is poor. When the number average molecular weight exceeds 30,000, the finished appearance of the coating film is inferior, so that it is not preferable. The glass transition temperature can be determined by, for example, DSC (Differential Scanning Calorimeter).
【0009】硬化剤としては、脂肪族ポリカルボン酸類
およびその(ポリ)酸無水物、芳香族ポリカルボン酸類
およびその(ポリ)酸無水物、脂肪族、脂環族または芳
香族ポリイソシアネートをフェノール類、カプロラクタ
ム類、アルコール類などのブロック剤でブロックしたも
の等のブロックイソシアネート化合物、ポリエポキシ化
合物、アミノプラスト樹脂、アミド化合物、酸ヒドラジ
ド等が用いられる。As the curing agent, aliphatic polycarboxylic acids and their (poly) acid anhydrides, aromatic polycarboxylic acids and their (poly) acid anhydrides, aliphatic, alicyclic or aromatic polyisocyanates, and phenols Block isocyanate compounds such as those blocked with a blocking agent such as caprolactams and alcohols, polyepoxy compounds, aminoplast resins, amide compounds, acid hydrazides and the like.
【0010】上記した中でもグリシジル基含有アクリル
系樹脂に脂肪族ポリカルボン酸(特にドデカン二酸)を
配合してなる粉体塗料組成物を本発明の方法に適用する
ことが好ましい。[0010] Among the above, it is preferable to apply a powder coating composition obtained by blending an aliphatic polycarboxylic acid (particularly dodecane diacid) to a glycidyl group-containing acrylic resin in the method of the present invention.
【0011】これら以外にも、必要に応じて、例えば、
ワキ防止剤、表面調整剤、酸化防止剤、紫外線吸収剤、
紫外線安定剤、ブロッキング防止剤、流動調整剤、帯電
制御剤、充てん剤、硬化促進剤等の添加剤を配合するこ
とができる。In addition to the above, if necessary, for example,
Anti-armpit agent, surface conditioner, antioxidant, ultraviolet absorber,
Additives such as an ultraviolet stabilizer, an anti-blocking agent, a flow regulator, a charge control agent, a filler, and a curing accelerator can be blended.
【0012】有機溶剤としては、硬化型樹脂を溶解もし
くは分散し加熱、減圧により除去できるものが好まし
い。有機溶剤としては、沸点が50〜300℃のものが
好ましく、特に、トルエン、キシレン、酢酸エチル、酢
酸ブチル、セロソルブ、メチルセロソルブ、メチルセロ
ソルブアセテート、セロソルブアセテート、メチルエチ
ルケトン、メチルイソブチルケトン、エチレングリコー
ルモノメチルエーテル、プロピレングリコールモノメチ
ルエーテル等のものを主有機溶剤として使用することが
好ましい。これらの主有機溶剤は1種もしくは2種以上
混合して使用することができる。また、上記した主有機
溶剤以外に以外に上記した以外のその他の有機溶剤を併
用して使用することができる。As the organic solvent, a solvent which can dissolve or disperse a curable resin and remove it by heating and reduced pressure is preferable. As the organic solvent, those having a boiling point of 50 to 300 ° C. are preferable, and in particular, toluene, xylene, ethyl acetate, butyl acetate, cellosolve, methyl cellosolve, methyl cellosolve acetate, cellosolve acetate, methyl ethyl ketone, methyl isobutyl ketone, ethylene glycol monomethyl ether , And propylene glycol monomethyl ether are preferably used as the main organic solvent. These main organic solvents can be used alone or in combination of two or more. Further, in addition to the main organic solvent described above, other organic solvents other than those described above may be used in combination.
【0013】本発明において、特にグリシジル基含有ア
クリル樹脂を基体樹脂とし、ドデカン二酸を硬化剤とす
る粉体塗料では、基体樹脂を溶解し、ドデカン二酸を溶
解しない有機溶剤として、例えば、キシレン、トルエン
等を使用し、また、基体樹脂及びドデカン二酸を溶解す
る有機溶剤として、例えば、セロソルブ系、エーテル系
等の有機溶剤を使用することが好ましい。これらの有機
溶剤は2種以上混合して使用することができる。In the present invention, in particular, in a powder coating material using a glycidyl group-containing acrylic resin as a base resin and dodecanediacid as a curing agent, an organic solvent that dissolves the base resin and does not dissolve dodecanediacid, for example, xylene , Toluene and the like, and as the organic solvent for dissolving the base resin and dodecanediacid, for example, an organic solvent such as a cellosolve type or an ether type is preferably used. These organic solvents can be used as a mixture of two or more kinds.
【0014】熱硬化型粉体塗料用原料溶液に含まれる有
機溶剤の含有量は、10〜90重量%、好ましくは約2
0〜80重量%の範囲である。有機溶剤の量が10重量
%未満になると原料溶液の粘度が高くなり取扱が困難と
なり、一方、90重量%を超えると脱溶剤に時間がかか
り過ぎるので生産性が劣る。The content of the organic solvent contained in the raw material solution for the thermosetting powder coating is 10 to 90% by weight, preferably about 2% by weight.
It is in the range of 0 to 80% by weight. When the amount of the organic solvent is less than 10% by weight, the viscosity of the raw material solution becomes high and handling becomes difficult. On the other hand, when the amount exceeds 90% by weight, it takes too much time to remove the solvent, resulting in poor productivity.
【0015】かくして得られた熱硬化型粉体塗料用原料
溶液は、最終的に得られる熱硬化型粉体塗料組成物に含
まれる有機溶剤量が1.6〜5重量%、好ましくは1.
8〜4重量%の範囲になるように除去される。有機溶剤
量が1.6重量%未満になると塗膜の平滑性が悪くな
り、一方、5重量%を超えると粉体塗料の耐ブロッキン
グ性が悪くなる。該有機溶剤の含有量の調整は、例え
ば、有機溶剤量が上記した範囲に入るように予め減圧条
件を設定しておき、その設定された減圧下のもとで加熱
溶融混合することにより製造するかもしくは減圧下で除
去できる有機溶剤とこの減圧下では除去できない高沸点
(例えば、140〜300℃)の有機溶剤を特定量配合
しておくことにより製造できる。また、該高沸点の有機
溶剤としては塗膜を焼き付けることにより揮発するもの
を使用することが好ましい。In the thus obtained raw material solution for thermosetting powder coating composition, the amount of the organic solvent contained in the finally obtained thermosetting powder coating composition is 1.6 to 5% by weight, preferably 1.
It is removed so as to be in the range of 8 to 4% by weight. When the amount of the organic solvent is less than 1.6% by weight, the smoothness of the coating film becomes poor, while when it exceeds 5% by weight, the blocking resistance of the powder coating material becomes poor. Adjustment of the content of the organic solvent is performed, for example, by setting pressure reduction conditions in advance so that the amount of the organic solvent falls within the above-described range, and heating and mixing under the set pressure reduction. Alternatively, it can be produced by blending a specific amount of an organic solvent that can be removed under reduced pressure and an organic solvent having a high boiling point (for example, 140 to 300 ° C.) that cannot be removed under reduced pressure. Further, it is preferable to use, as the high boiling point organic solvent, one that volatilizes by baking a coating film.
【0016】上記した原料溶液を減圧下で加熱溶融混合
できる装置としては、特に制限なしに従来のものを使用
することができる。この様な装置としては、従来から使
用されているものは多くあるが、例えば、特開平6−2
3253号公報のスクリュ−型加熱冷却装置、2−25
8043号公報の加熱型攪拌熱処理機等が挙げられる。As a device capable of heating and melting and mixing the above-mentioned raw material solution under reduced pressure, a conventional device can be used without any particular limitation. There are many such devices that have been conventionally used.
No. 3253, screw type heating / cooling apparatus, 2-25
No. 8043, a heating type stirring heat treatment machine and the like.
【0017】このようにして原料溶液を減圧下で加熱溶
融混合して得られた粉体塗料は、冷却、粗粉砕、微粉
砕、分級を行って最終的に製造される。The powder coating obtained by heating and melting and mixing the raw material solution under reduced pressure is finally manufactured by cooling, coarse pulverization, fine pulverization and classification.
【0018】本発明の方法は、特に上記した工程におい
て、有機溶剤樹脂溶液は、例えば、有機溶剤中でアクリ
ル樹脂となるアクリル酸エステルモノマーやその他の不
飽和モノマー等の原料をラジカル開始剤の触媒の存在下
で溶液ラジカル重合反応して得られる有機溶剤樹脂溶液
としてそのまま使用することができる。即ち、反応容器
中で樹脂の合成と硬化剤の混合の工程を同時に行うこと
ができ、しかも次の減圧、加熱溶融混合の工程を一つの
装置で行うことができ、更にこれらの工程は連続的に組
み合わせることができるので生産性に優れる。In the method of the present invention, particularly in the above-mentioned step, the organic solvent resin solution is prepared by, for example, using a raw material such as an acrylate ester monomer or other unsaturated monomer which becomes an acrylic resin in an organic solvent as a catalyst for a radical initiator. Can be used as it is as an organic solvent resin solution obtained by performing a solution radical polymerization reaction in the presence of. That is, the steps of synthesizing the resin and mixing the curing agent can be performed simultaneously in the reaction vessel, and the next step of depressurization, heating and melting and mixing can be performed by one apparatus, and these steps are continuously performed. High productivity because it can be combined.
【0019】[0019]
【実施例】以下、実施例を揚げて本発明を詳細に説明す
る。尚、特に断らない限り「部」または「%」は重量基
準を表す。DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described in detail below with reference to embodiments. Unless otherwise specified, “parts” or “%” represents a weight basis.
【0020】実施例1 温度計、サーモスタット、撹拌器、還流冷却器および滴
下装置を備えた反応容器に、キシレン100部を仕込
み、窒素ガスを吹き込みながら、82℃に加熱して、シ
クロヘキシルメタクリレート50部、メチルメタクリレ
ート15部、グリシジルメタクリレート35部、アゾビ
スジメチルバレロニトリル7部の混合液を約3時間かけ
て滴下した。滴下終了後82℃で2時間放置し、反応を
終了し、有機溶剤樹脂溶液Aを製造した。Example 1 A reaction vessel equipped with a thermometer, a thermostat, a stirrer, a reflux condenser, and a dropping device was charged with 100 parts of xylene, heated to 82 ° C. while blowing nitrogen gas, and heated to 50 parts of cyclohexyl methacrylate. , A mixture of 15 parts of methyl methacrylate, 35 parts of glycidyl methacrylate, and 7 parts of azobisdimethylvaleronitrile was dropped over about 3 hours. After the completion of the dropwise addition, the mixture was left at 82 ° C. for 2 hours to terminate the reaction, thereby preparing an organic solvent resin solution A.
【0021】次いで、40℃に冷却した樹脂溶液A20
0部にドデカン二酸25部及びキシレンを加え、この配
合したドデカン二酸をサンドミル分散機で樹脂溶液中に
分散した後、固形分74%(有機溶剤含有量26%)の
熱硬化型粉体塗料用原料溶液Bを得た。Next, the resin solution A20 cooled to 40 ° C.
To 0 parts, 25 parts of dodecanedioic acid and xylene were added, and the compounded dodecaneedioic acid was dispersed in a resin solution by a sand mill disperser, and then a thermosetting powder having a solid content of 74% (organic solvent content: 26%) was obtained. A coating material solution B was obtained.
【0022】次いで、得られた樹脂溶液Bを供給導管を
通して連続式減圧脱溶剤装置((株)栗本鐵工所社製、
タイプSCP−100使用)の原料仕込み口に供給し、
熱媒温度100℃、スクリュー回転数20rpm、塗出
量9.1kg/時間、真空度40Torrで製造した。
得られたものを20℃に冷却、粗粉砕、微粉砕し250
メッシュの篩いで分級して実施例1の粉体塗料を得た。Next, the obtained resin solution B is supplied through a supply conduit to a continuous vacuum desolvation apparatus (manufactured by Kurimoto Iron Works Co., Ltd.).
(Using type SCP-100)
It was manufactured at a heating medium temperature of 100 ° C., a screw rotation speed of 20 rpm, a coating amount of 9.1 kg / hour, and a degree of vacuum of 40 Torr.
The obtained product was cooled to 20 ° C., coarsely pulverized, and finely pulverized.
The powder coating of Example 1 was obtained by classification with a mesh sieve.
【0023】実施例2〜3 実施例1において表1に記載の条件、組成以外は実施例
1と同様にして実施例2〜3の粉体塗料を製造した。Examples 2 to 3 The powder coatings of Examples 2 to 3 were produced in the same manner as in Example 1 except for the conditions and compositions shown in Table 1.
【0024】比較例1〜2 実施例1において表1に記載の条件、組成以外は実施例
1と同様にして比較例1〜2の粉体塗料を製造した。Comparative Examples 1-2 The powder coatings of Comparative Examples 1-2 were produced in the same manner as in Example 1, except for the conditions and compositions shown in Table 1.
【0025】結果を表1に示す。The results are shown in Table 1.
【0026】[0026]
【表1】 [Table 1]
【0027】表1において、*1はプロピレングリコー
ルモノメチルエーテル/ブチルセロソルブ=1/1重量
比、*2はキシレン/スワゾール1000=98/2重
量比の意味を表す。In Table 1, * 1 means propylene glycol monomethyl ether / butyl cellosolve = 1/1 weight ratio, and * 2 means xylene / swazole 1000 = 98/2 weight ratio.
【0028】表1において、固形分(又は有機溶剤量)
はサンプル1gを150℃×1時間加熱乾燥して測定し
たものを(加熱後のサンプル重さ/初期サンプルの重
さ)×100の式で求めた。In Table 1, solid content (or amount of organic solvent)
Was measured by heating and drying 1 g of a sample at 150 ° C. × 1 hour, and was determined by the formula of (weight of sample after heating / weight of initial sample) × 100.
【0029】表1における試験は次の様にして行った。The tests in Table 1 were performed as follows.
【0030】粉体塗料の耐ブロッキング性;ポリエチレ
ン袋に入れた粉体塗料を30℃の貯蔵室に1カ月放置し
た後、粉体塗料の状態を調べた。○は初期のものと比較
して全く変化なく良好なもの、△は小さな塊を生じ、そ
の塊を手でほぐすのが大変であるもの、×は全体が大き
な塊になるものを示す。Blocking resistance of powder coating: The powder coating placed in a polyethylene bag was left in a storage room at 30 ° C. for one month, and the state of the powder coating was examined. ○ indicates a good one without any change compared to the initial one, △ indicates a small clump which is difficult to loosen by hand, and × indicates a large clump as a whole.
【0031】塗膜仕上がり外観:燐酸亜鉛化成処理を施
した厚さ0.8mmのダル鋼鈑上にエポキシ系カチオン
電着塗料を乾燥膜厚20ミクロンとなるように電着塗装
し、焼き付けた。次いで該素材の表面に粉体塗料を膜厚
が約50ミクロンとなるように静電塗装し、乾燥器で1
60℃で30分加熱硬化させた。得られた塗板について
次の試験を行い下記の基準で評価した。○は良好なも
の、△は平滑感が劣るもの、×は平滑感が非常に劣るも
の。Finish appearance of coating film: An epoxy-based cationic electrodeposition coating material was electrodeposited on a 0.8 mm thick dull steel plate subjected to a zinc phosphate chemical conversion treatment so as to have a dry film thickness of 20 μm, and baked. Then, the surface of the material is electrostatically coated with a powder coating so that the film thickness becomes about 50 microns, and dried by a dryer.
The composition was cured by heating at 60 ° C. for 30 minutes. The following test was performed on the obtained coated plate and evaluated according to the following criteria.は: good, △: poor smoothness, x: very poor smoothness.
【0032】塗膜の耐ワキ性:上記と同様の方法で塗膜
を形成して下記の基準で塗膜の耐ワキ性を評価した。○
はワキがないもの、△ワキが認められるもの、×ワキが
著しく認められるもの。Coating resistance of coating film: A coating film was formed in the same manner as described above, and the coating resistance of the coating film was evaluated according to the following criteria. ○
Indicates that there is no armpit, △ that armpit is recognized, and x is marked.
【0033】ペレットフロー性:ペレットフロ−性:粉
体塗料約0.8gを直径13mm、高さ約4mmの円筒状にな
るように30Kg/mm2 加圧成型したものを、水平に保
ったアルミニウム板の上に乗せ、 150℃で10分間加熱フ
ロ−させた時の広がり長さを測定した。Pellet flow property: Pellet flow property: An aluminum plate which was formed by pressing about 0.8 g of powder coating material into a cylindrical shape having a diameter of 13 mm and a height of about 4 mm at a pressure of 30 kg / mm 2 and kept horizontally. And the spread length when heated at 150 ° C. for 10 minutes was measured.
【0034】[0034]
【発明の効果】本発明は、上記した如き構成を有するこ
とから、特に仕上がり外観に優れた塗膜を形成すること
ができる。According to the present invention, since it has the above-described structure, a coating film having particularly excellent finished appearance can be formed.
Claims (2)
形分10〜90重量%の範囲の熱硬化型粉体塗料用原料
溶液を、該有機溶剤量が1.6〜5重量%の範囲になる
ように減圧下に加熱溶融混合しながら除去してなること
を特徴とする熱硬化型塗料組成物の製造方法。1. A raw material solution for a thermosetting powder coating material having a solid content of 10 to 90% by weight dissolved or dispersed in an organic solvent is reduced to an organic solvent amount of 1.6 to 5% by weight. A method for producing a thermosetting coating composition, wherein the composition is removed while being heated, melted and mixed under reduced pressure.
化型粉体用樹脂の有機溶剤樹脂溶液を得る工程、 (2)該有機溶剤樹脂溶液中に硬化剤を配合して固形分
10〜90重量%の範囲の熱硬化型粉体塗料用原料溶液
を得る工程、 (3)該有機溶剤量が1.6〜5重量%の範囲になるよ
うに減圧下に加熱溶融混合しながら除去して熱硬化型粉
体塗料組成物を得る工程、を連続して製造することを特
徴とする熱硬化型塗料組成物。2. The following steps: (1) a step of synthesizing a resin for thermosetting powder in an organic solvent to obtain an organic solvent resin solution of the resin for thermosetting powder; Adding a curing agent to the mixture to obtain a raw material solution for a thermosetting powder coating material having a solid content of 10 to 90% by weight, (3) the amount of the organic solvent is in a range of 1.6 to 5% by weight. A step of obtaining a thermosetting powder coating composition by removing while heating and mixing under reduced pressure to obtain a thermosetting powder coating composition.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11471998A JPH11302567A (en) | 1998-04-24 | 1998-04-24 | Production of thermosetting coating composition |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11471998A JPH11302567A (en) | 1998-04-24 | 1998-04-24 | Production of thermosetting coating composition |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH11302567A true JPH11302567A (en) | 1999-11-02 |
Family
ID=14644916
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP11471998A Pending JPH11302567A (en) | 1998-04-24 | 1998-04-24 | Production of thermosetting coating composition |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH11302567A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1253174A1 (en) * | 2001-04-25 | 2002-10-30 | Mitsubishi Gas Chemical Company, Inc. | Method of producing polyester powdery coating material |
EP1245647A3 (en) * | 2001-03-13 | 2003-12-10 | Mitsubishi Gas Chemical Company, Inc. | Method of producing powdery coating material |
US7192994B2 (en) | 2001-04-25 | 2007-03-20 | Mitsubishi Gas Chemical Co., Inc. | Method of producing polyester powdery coating material |
-
1998
- 1998-04-24 JP JP11471998A patent/JPH11302567A/en active Pending
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1245647A3 (en) * | 2001-03-13 | 2003-12-10 | Mitsubishi Gas Chemical Company, Inc. | Method of producing powdery coating material |
US6933348B2 (en) | 2001-03-13 | 2005-08-23 | Mitsubishi Gas Chemical Co., Inc. | Method of producing powdery coating material |
EP1253174A1 (en) * | 2001-04-25 | 2002-10-30 | Mitsubishi Gas Chemical Company, Inc. | Method of producing polyester powdery coating material |
US7192994B2 (en) | 2001-04-25 | 2007-03-20 | Mitsubishi Gas Chemical Co., Inc. | Method of producing polyester powdery coating material |
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