JPH0372672B2 - - Google Patents

Info

Publication number
JPH0372672B2
JPH0372672B2 JP59046990A JP4699084A JPH0372672B2 JP H0372672 B2 JPH0372672 B2 JP H0372672B2 JP 59046990 A JP59046990 A JP 59046990A JP 4699084 A JP4699084 A JP 4699084A JP H0372672 B2 JPH0372672 B2 JP H0372672B2
Authority
JP
Japan
Prior art keywords
parts
acid
polyester
polyester resin
reference example
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
Application number
JP59046990A
Other languages
Japanese (ja)
Other versions
JPS60192772A (en
Inventor
Noboru Ishikawa
Nobuyoshi Shirai
Hirobumi Takeda
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
DIC Corp
Original Assignee
Dainippon Ink and Chemicals Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Dainippon Ink and Chemicals Co Ltd filed Critical Dainippon Ink and Chemicals Co Ltd
Priority to JP4699084A priority Critical patent/JPS60192772A/en
Publication of JPS60192772A publication Critical patent/JPS60192772A/en
Publication of JPH0372672B2 publication Critical patent/JPH0372672B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Paints Or Removers (AREA)

Description

【発明の詳现な説明】[Detailed description of the invention]

本発明は改良された粉䜓塗料甚暹脂組成物に関
し、さらに詳现には、特定の氎酞基䟡をも぀たポ
リ゚ステル暹脂に倚官胜性有機カルボン酞無氎物
を反応させお埗られる特定の酞䟡などを有した、
か぀氎酞基を残存させた圢のポリ゚ステル暹脂ず
ポリ゚ポキシ化合物ずを必須の成分ずする、塗膜
倖芳、機械的匷床および耐食性にすぐれた塗膜を
圢成するず共に、保存安定性にもすぐれた有甚な
る暹脂組成物に関する。 埓来より、カルボキシル基含有ポリ゚ステル暹
脂ずポリ゚ポキシ化合物ずから成る粉䜓塗料は機
械的匷床、密着性および耐食性にすぐれる凊か
ら、広範な甚途に利甚されおいる。 そのさいに、ポリ゚ポキシ化合物ず組み合せる
べきベヌス・ポリ゚ステル暹脂ずしお、氎酞基を
有するポリ゚ステル暹脂に倚官胜性有機カルボン
酞無氎物を反応させお埗られるカルボキシル基含
有ポリ゚ステル暹脂を䜿甚するこずは、たずえば
特公昭55−15506号明现曞や特公昭58−29342号明
现曞に蚘茉されおいお公知である。 しかしながら、これらの公知文献に蚘茉されお
いる技術に埓う限りにおいおは、40〜70なる酞䟡
を䞭心ずした比范的高い酞䟡のポリ゚ステル暹脂
をベヌス・ポリ゚ステル暹脂を甚いた粉䜓塗料が
䞻であるため、どうしおも粉䜓塗料の保圚安定性
が悪くお、保存䞭にも反応が進行したりしお、そ
の結果、そうした塗料を䜿甚した塗膜の倚くは平
滑性に劣るし、他方、ポリ゚ステル䞭には氎酞基
が殆ど存圚しないような暹脂がベヌス・ポリ゚ス
テル暹脂ずしお甚いられおいるために、ポリ゚ポ
キシ化合物ずの盞溶性が䞍十分ずなり易く、就
䞭、顔料濃床を高めるような堎合には、溶融混緎
時に分散䞍良を生じたりしお、その結果、塗膜の
平滑性たたは鮮映性が劣るずいう欠点もある。 しかるに、本発明者らはこうした䞊述の劂き埓
来技術における諞々の欠点の存圚に鑑みお鋭意研
究の結果、特定範囲内の氎酞基䟡をも぀たポリ゚
ステル暹脂、぀たり䞭間䜓ポリ゚ステルに䟡以
䞊の倚官胜性有機カルボン酞無氎物を必須の成分
ずする䟡以䞊の倚官胜性有機カルボン酞無氎物
以䞋、ポリカルボン酞無氎物ずもいう。を反応
させお埗られる特定の酞䟡および軟化点を有し
た、しかも氎酞基を残存させた圢のポリ゚ステル
暹脂を䜿甚するこずにより、ここに前述された欠
点が悉く解消されるこずを芋出しお、本発明を完
成させるに到぀た。 すなわち、本発明は氎酞基䟡が12.5〜70KOH
mg以䞋、単䜍は省略する。で、か぀酞䟡
が〜10なるポリ゚ステル暹脂−以䞋、
䞭間䜓ポリ゚ステルず略蚘する。にポリカルボ
ン酞無氎物−を反応させお埗られる、酞
䟡が15以䞊30未満で、氎酞基䟡が以䞊で、か぀
軟化点が80〜150℃なるポリ゚ステル暹脂
をベヌス・ポリ゚ステル暹脂成分ずしお60〜97重
量郚ず、分子䞭に少なくずも個の゚ポキシ基
を有するポリ゚ポキシ化合物を架橋硬化剀
成分ずしお〜40重量郚ずを必須の成分ずしお含
んで成る、ポリ゚ポキシ化合物ずの盞溶性も良奜
で、したが぀お粉䜓塗料の保存安定性も良奜であ
り、しかも顔料濃床を高くしおも溶融混緎時にお
ける分散性が良奜にしお、塗膜の平滑性および鮮
映性にすぐれる粉䜓塗料甚暹脂組成物を提䟛する
ものである。 ここにおいお、本発明組成物の䞀必須成分たる
䞊蚘ポリ゚ステル暹脂ずは、埌蚘する劂き
氎酞基を有する䞭間䜓ポリ゚ステル−に
ポリカルボン酞無氎物−を反応させお埗
られる、それぞれ酞䟡が15以䞊30未満なる、奜た
しくは16〜28で、か぀氎酞基䟡が以䞊なる、奜
たしくは〜20で぀あお、軟化点が80〜150℃、
奜たしくは90〜130℃の範囲内にある、特筆すべ
きは積極的に氎酞基を残存せしめるこずにより、
ポリ゚ポキシ化合物ずの盞溶性を図るよう
にした暹脂を指称するものである。 酞䟡が15よりも䜎い堎合には、どうしおも埗ら
れる塗膜の機械的匷床が䞍十分ずなるし、逆に、
30以䞊の堎合には、どうしおも粉䜓塗料の保存安
定性が䜎䞋し、したが぀お保存䞭に反応が進行し
お、その結果は、塗膜の平滑性が劣化するこずに
なるので、いずれも奜たしくない。 他方、圓該ポリ゚ステル暹脂䞭には氎酞
基を残存せしめるこずが必須の条件であり、この
氎酞基䟡がよりも䜎い堎合には、どうしおも埌
蚘するポリ゚ポキシ化合物ずの盞溶性が䞍
十分ずなり、顔料分散性が劣るこずになるので奜
たしくない。 圓該ポリ゚ステル暹脂は、前述したよう
に、氎酞基を有する䞭間䜓ポリ゚ステル−
ずポリカルボン酞無氎物−ずの反応
により埗られるものであ぀お、これら䞡化合物
−ず−ずの反応方法に぀いおは
特に制限を受けるものではないが、そのうちでも
代衚的なものずしおは、䞭間䜓ポリ゚ステル
−にポリカルボン酞無氎物−を付加
反応せしめる方法や、䞭間䜓ポリ゚ステル−
にポリカルボン酞無氎物−を付加さ
せたのち、さらに瞮合反応せしめる方法などが挙
げられる。 ここにおいお、䞊蚘䞭間䜓ポリ゚ステル−
ずは、それぞれ氎酞基䟡が12.5〜70、奜たし
くは13〜50で、か぀酞䟡が〜10、奜たしくは
〜なる範囲内のものを指称するものであり、か
かる範囲内のものである限りは、分岐状構造のも
のであ぀おも、線状構造のものであ぀おもよい。 そしお、圓該䞭間䜓ポリ゚ステル−の
調補方法に぀いおは特に制限はなく、呚知慣甚の
方法がそのたた適甚され埗るし、たた酞成分およ
びアルコヌル成分ずしおは、それぞれ呚知慣甚の
二塩基酞およびたたは倚塩基酞ならびに二䟡ア
ルコヌルグリコヌル類およびたたは倚䟡ア
ルコヌルがそのたた䜿甚し埗るが、そのうちで
も、酞成分ずしお代衚的なものには、テレフタル
酞、む゜フタル酞、フタル酞、メチルテレフタル
酞、トリメリツト酞、ピロメリツト酞およびそれ
らの無氎物あるいはアゞピン酞、セバシン酞、こ
はく酞、マレむン酞、フマル酞、テトラヒドロフ
タル酞、メチル−テトラヒドロフタル酞、ヘキサ
ヒドロフタル酞、メチル−ヘキサヒドロフタル酞
およびそれらの無氎物などがあるし、他方、アル
コヌル成分ずしお代衚的なものには、゚チレング
リコヌル、プロピレングリコヌル、−ブタ
ンゞオヌル、−ブタンゞオヌル、−
ヘキサンゞオヌル、ネオペンチルグリコヌル、む
゜ペンチルグリコヌル、ビスヒドロキシ゚チルテ
レフタレヌト、氎添ビスプノヌル、氎添ビス
プノヌルの゚チレンオキサむド付加物、氎添
ビスプノヌルのプロピレンオキサむド付加
物、トリメチロヌル゚タン、トリメチロヌルプロ
パン、グリセリン、ペンタ゚リスリトヌルおよび
−トリメチルペンタン−−ゞオ
ヌルなどがあるが、モノ゚ポキシ化合物も本発明
におけるグリコヌル類の䞀぀ずしお䜿甚するこず
ができる。 他方、圓該䞭間䜓ポリ゚ステル−に反
応さすべき前蚘ポリカルボン酞無氎物−
ずしおは䟡以䞊の倚塩基性有機カルボン酞無氎
物を党ポリカルボン酞無氎物䞭30〜100重量含
む䟡の芳銙族、脂肪族たたは脂環族の各酞無氎
物が適甚され埗るが、そのうちでも代衚的なもの
には、テレフタル酞、む゜フタル酞、フタル酞、
トリメリツト酞、ピロメリツト酞、こはく酞、ア
ゞピン酞、アれラむン酞、セバシン酞、マレむン
酞、テトラヒドロフタル酞たたはヘキサヒドロフ
タル酞などの酞無氎物がある。 本発明組成物のもう䞀぀の必須構成成分たる前
蚘ポリ゚ポキシ化合物ずは、分子䞭に少
なくずも個の゚ポキシ基を有する化合物を指称
するものであり、そのうちでも特に代衚的なもの
には、ビスプノヌルもしくはビスプノヌル
のゞグリシゞル゚ヌテル、オキシ安息銙酞のグ
リシゞル゚ステル・゚ヌテル゚チレングリコヌ
ルのゞグリシゞル゚ヌテルもしくはトリメチロヌ
ルプロパンのグリシゞル゚ヌテルの劂き倚䟡アル
コヌルのポリゞグリシル゚ヌテルテレフタル酞
のゞグリシゞル゚ステルの劂き二塩基酞のゞグリ
シゞル゚ステルたたはトリグリシゞルむ゜シア
ヌレヌトなどがある。 而しお、本発明の粉䜓塗料甚暹脂組成物は、前
掲された劂きポリ゚ステル暹脂ずポリ゚ポ
キシ化合物ずをそれぞれ必須の成分ずしお
含んで成るものであり、これら䞡必須成分の䜿甚
比率は成分の60〜97重量郚成分の
40〜重量郚、奜たしくは65〜96重量郚35〜
重量郚なる割合が適圓である。 本発明組成物には、さらに架橋硬化反応を促進
させるために、適宜、呚知の觊媒を添加するこず
ができるし、たた塗膜面でのクレヌタヌの発生を
防止し、さらに䞀局平滑性を向䞊せしめるため
に、流動調敎剀流展剀ずしおアクリル酞長鎖
アルキル゚ステル系重合物や、ふ぀玠化合物など
を添加するこずもできる。 かくしお埗られる本発明組成物を甚いお粉䜓塗
料を調補するには、呚知のいずれの方法によ぀お
も可胜である。 埗られた粉䜓塗料を静電スプレヌ法たたは流動
浞挬法などの劂き呚知の方法で塗垃し、次いで焌
き付けるこずにより、すぐれた性胜の塗膜を埗る
こずができる。 次に、本発明を参考䟋、実斜䟋および比范䟋に
より具䜓的に説明するが、郚およびは特に断り
のない限り、すべお重量基準であるものずする。 参考䟋〔ポリ゚ステル暹脂の調補䟋〕 ゚チレングリコヌルの83郚、ネオペンチルグリ
コヌルの327郚、ゞメチルテレフタレヌトの435郚
および酢酞亜鉛の0.4郚からなる混合物を、生成
するメタノヌルを反応系倖に陀去しながら、埐々
に210℃たで昇枩させお行き、その埌も同枩床に
時間保持させおアルコヌル亀換反応を続行せし
めた。 次いで、ここにトリメチロヌルプロパンの
郚、テレフタル酞の149郚、む゜フタル酞の224郚
およびゞ−−ブチル錫オキサむドの0.5郚を加
え、時間を芁しお240℃たで昇枩し、さらに同
枩床で脱氎瞮合せしめお、氎酞基䟡が14で、か぀
酞䟡がなる䞭間䜓ポリ゚ステル−を埗
た。 しかるのち、このポリ゚ステル−を
200℃に降枩し、さらに無氎トリメリツト酞の29
郚を加えお同枩床で時間反応せしめた凊、酞䟡
が23で、氎酞基䟡がで、か぀軟化点が123℃な
る目的暹脂が埗られた。以䞋、これをポリ
゚ステル−ず略蚘する。 参考䟋同䞊 ゚チレングリコヌル、ネオペンチルグリコヌル
およびゞメチルテレフタレヌトの量をそれぞれ
159郚、218郚および452郚に倉曎した以倖は、参
考䟋ず同様にしおアルコヌル亀換反応を、次い
でむ゜フタル酞の䜿甚を欠劂し、か぀トリメチロ
ヌルプロパンおよびテレフタル酞の䜿甚量をそれ
ぞれ20郚および384郚に倉曎した以倖は、参考䟋
ず同様にしお脱氎瞮合反応を行぀お、氎酞基䟡
が30で、か぀酞䟡がなる䞭間䜓ポリ゚ステル
−を埗た。 しかるのち、無氎トリメリツト酞の䜿甚量を45
郚に倉曎した以倖は、参考䟋ず同様にしお䞭間
䜓ポリ゚ステルに反応せしめた凊、酞䟡が28で、
氎酞基䟡が16で、か぀軟化点が124℃なる目的暹
脂が埗られた。以䞋、これをポリ゚ステル
−ず略蚘する。 参考䟋同䞊 ゚チレングリコヌル、ネオペンチルグリコヌル
およびゞメチルテレフタレヌトの䜿甚量をそれぞ
れ136郚、253郚および472郚に倉曎し、か぀
−ヘキサンゞオヌルの29郚をも䜿甚するように
倉曎した以倖は、参考䟋ず同様にしおアルコヌ
ル亀換反応を、次いで20郚のトリメチロヌルプロ
パンの代りに33郚のアゞピン酞を䜿甚するず共
に、テレフタル酞の䜿甚量を308郚に倉曎した以
倖は、参考䟋ず同様にしお脱氎瞮合反応を行぀
お、氎酞基䟡が45で、か぀酞䟡がなる䞭間䜓ポ
リ゚ステル−を埗た。 しかるのち、このポリ゚ステル−を
200℃に降枩し、さらに無氎トリメリツト酞の60
郚を加えお同枩床に時間保持させ、さらに240
℃に昇枩しお同枩床で時間反応せしめた凊、酞
䟡が25で、氎酞基䟡が12で、か぀軟化点が119℃
なる目的暹脂が埗られた。以䞋、これをポ
リ゚ステル−ず略蚘する。 参考䟋〔比范察照甚のポリ゚ステル暹脂の調補
䟋〕 無氎トリメリツト酞の䜿甚量を102郚に倉曎し
た以倖は、参考䟋ず同様にしお酞䟡が57で、氎
酞基䟡がで、か぀軟化点が126℃なる察照甚の
ポリ゚ステル暹脂A′を埗た。以䞋、これを
ポリ゚ステルA′−ず略蚘する。 参考䟋同䞊 ゚チレングリコヌル、ネオペンチルグリコヌル
およびゞメチルテレフタレヌトの䜿甚量をそれぞ
れ141郚、236郚および440郚に倉曎した以倖は、
参考䟋ず同様にしおアルコヌル亀換反応を、次
いでトリメチロヌルプロパン、テレフタル酞およ
びむ゜フタル酞の䜿甚量をそれぞれ郚、172郚
および235郚に倉曎した以倖は、参考䟋ず同様
にしお脱氎瞮合反応を行぀お、氎酞基䟡がで、
か぀酞䟡が20なる察照甚の䞭間䜓ポリ゚ステル
a′−を埗た。 しかるのち、無氎トリメリツト酞の䜿甚量を
郚に倉曎しお、これを䞊蚘ポリ゚ステルa′−
に反応せしめるように倉曎した以倖は、参考
䟋ず同様にしお酞䟡が24で、氎酞基䟡がで、
か぀軟化点が118℃なる察照甚のポリ゚ステル暹
脂A′を埗た。以䞋、これをポリ゚ステル
A′−ず略蚘する。 参考䟋〔ポリ゚ステル暹脂の調補䟋〕 ゚チレングリコヌル、ネオペンチルグリコヌル
およびゞメチルテレフタレヌトの䜿甚量をそれぞ
れ127郚、261郚および442郚に倉曎した以倖は、
参考䟋ず同様にしおアルコヌル亀換反応を、次
いでトリメチロヌルプロパンおよびテレフタル酞
の䜿甚量を19郚および378郚に倉曎した以倖は、
参考䟋ず同様にしお脱氎瞮合反応を行぀お、氎
酞基䟡が27で、か぀酞䟡がなる䞭間䜓ポリ゚ス
テル−を埗た。 しかるのち、無氎トリメリツト酞の䜿甚量を37
郚に倉曎するず共に、13郚の無氎フタル酞をも甚
い、か぀これらの䞡ポリカルボン酞無氎物−
を䞊蚘ポリ゚ステル−に反応せしめ
るように倉曎した以倖は、参考䟋ず同様にしお
酞䟡が28、氎酞基䟡が10で、か぀軟化点が125℃
なる目的ポリ゚ステル暹脂を埗た。以䞋、
これをポリ゚ステル−ず略蚘する。 参考䟋〔ポリ゚ステル暹脂の調補䟋〕 ゞメチルテレフタレヌトDMTの455.5郚、
゚チレングリゎヌルEGの145.7郚、ネオペン
チルグリコヌルNGの244.4郚および酢酞亜鉛
の0.4郚からなる混合物を甚いるように倉曎した
以倖は、参考䟋ず同様に行぀おから、テレフタ
ル酞TPAの385.4郚ずゞ−−ブチル錫ゞオ
キサむドの0.5郚を加えお脱氎瞮合せしめお、氎
酞基䟡が12.5で、か぀、酞䟡がなる䞭間䜓ポリ
゚ステル−を埗た。 次いで、この䞭間䜓ポリ゚ステル−の
1000郚に、無氎トリメリツト酞の27郚を加えるよ
うに倉曎した以倖は、参考䟋ず同様に反応せし
めお、酞䟡が24で、か぀、氎酞基䟡がなる目的
のポリ゚ステル暹脂を埗た。以䞋これをポリ゚ス
テル暹脂−ず略蚘する。 参考䟋同䞊 無氎トリメリツト酞TMAの䜿甚量を36郚
に倉曎するようにした以倖は、参考䟋ず同様に
しお、酞䟡が28で、か぀、氎酞基䟡がなる目的
ポリ゚ステル暹脂を埗た。以䞋、これをポリ゚ス
テル暹脂−ず略蚘する。 参考䟋〔察照甚ポリ゚ステル暹脂A'の調補
䟋〕 DMTを455.2郚、EGを145.6郚、NPGを244.3
郚に、そしお、TPAを385.9郚に倉曎する以倖
は、参考䟋ず同様にしお、氎酞基䟡が12で、か
぀、酞䟡がなる、察照甚の䞭間䜓ポリ゚ステル
を埗た。 次いで、TMAの䜿甚量を23.9郚ずするように
倉曎した以倖は、参考䟋ず同様にしお、酞䟡が
22で、か぀、氎酞基䟡がなる、察照甚のポリ゚
ステル暹脂を埗た。以䞋、これをポリ゚ステル暹
脂A'−ず略蚘する。 参考䟋10同䞊 DMTを455.2郚、EGを145.3郚、NPGを243.7
郚に、そしお、TPAを387.9郚に倉曎する以倖
は、参考䟋ず同様にしお、氎酞基䟡が10で、か
぀、酞䟡がなる、察照甚の䞭間䜓ポリ゚ステル
を埗た。 次いで、TMAの䜿甚量を36郚に倉曎する以倖
は参考䟋ず同様にしお、酞䟡が28で、か぀、氎
酞基䟡がなる、察照甚のポリ゚ステル暹脂を埗
た。これをポリ゚ステル暹脂’−ず略蚘
する。 実斜䟋およびならびに比范䟋および 第衚に瀺されるような配合組成比で各成分を
混合し、次いで、実斜䟋ず同様にしお、塗料化
し、しかるのち、塗膜性胜の比范怜蚎を行぀た。 それらの結果は、たずめお、同衚に瀺す。 実斜䟋〜および比范䟋 第衚に瀺されるような配合組成割合で各成分
を混合し、次いで各混合物をスむス囜ブス瀟補
「コニヌダヌPR−46」で溶融混緎し、しかるのち
埮粉砕させおから150メツシナ金網通過分を静電
スプレヌ法により0.8mm厚の燐酞亜鉛凊理鋌板に
膜厚が50〜60Όずなるように各別に塗垃し、次
いで200℃で20分間焌き付けた。 それぞれの塗料に぀いおの塗膜性胜の詊隓結果
は、たずめお同衚に瀺す。
The present invention relates to an improved resin composition for powder coatings, and more particularly to a resin composition with a specific acid value obtained by reacting a polyester resin with a specific hydroxyl value with a polyfunctional organic carboxylic acid anhydride. had,
It forms a coating film that is excellent in appearance, mechanical strength, and corrosion resistance, and has a polyester resin with residual hydroxyl groups and a polyepoxy compound as essential components, and is also useful because it has excellent storage stability. The present invention relates to a resin composition. BACKGROUND ART Powder coatings made of carboxyl group-containing polyester resins and polyepoxy compounds have been used for a wide range of purposes because of their excellent mechanical strength, adhesion, and corrosion resistance. At this time, it is particularly important to use a carboxyl group-containing polyester resin obtained by reacting a polyester resin having hydroxyl groups with a polyfunctional organic carboxylic acid anhydride as the base polyester resin to be combined with the polyepoxy compound. It is described in the specification of Japanese Patent Publication No. 55-15506 and the specification of Japanese Patent Publication No. 58-29342 and is well known. However, as long as the techniques described in these known documents are followed, powder coatings are mainly based on polyester resins with relatively high acid values, mainly in the range of 40 to 70. Therefore, the storage stability of powder coatings is unavoidable, and reactions progress during storage, resulting in many coatings using such coatings having poor smoothness. Since a resin with almost no hydroxyl groups is used as the base polyester resin, it tends to have insufficient compatibility with polyepoxy compounds, and especially when increasing the pigment concentration, it is difficult to melt. Another drawback is that poor dispersion occurs during kneading, resulting in poor coating film smoothness or image clarity. However, in view of the various shortcomings in the prior art as described above, the inventors of the present invention conducted extensive research and found that a polyester resin having a hydroxyl value within a specific range, that is, a polyfunctional polyester having a valence of 3 or more, is used as an intermediate polyester. The specific acid value and softening point obtained by reacting a divalent or higher polyfunctional organic carboxylic acid anhydride (hereinafter also referred to as polycarboxylic acid anhydride) containing a polycarboxylic acid anhydride as an essential component. The present invention was completed based on the discovery that all of the above-mentioned drawbacks can be overcome by using a polyester resin having a polyester resin having hydroxyl groups remaining. That is, the present invention has a hydroxyl value of 12.5 to 70KOH.
mg/g (hereinafter, units are omitted) and has an acid value of 2 to 10 (a-1) (hereinafter,
Abbreviated as intermediate polyester. ) with a polycarboxylic anhydride (a-2), a polyester resin (A) having an acid value of 15 or more and less than 30, a hydroxyl value of 2 or more, and a softening point of 80 to 150°C
60 to 97 parts by weight as a base polyester resin component, and 3 to 40 parts by weight as a crosslinking curing agent component of a polyepoxy compound (B) having at least two epoxy groups in one molecule. It has good compatibility with the polyepoxy compound, which is composed of The present invention provides a resin composition for powder coatings that has excellent smoothness and sharpness. Here, the above-mentioned polyester resin (A), which is one essential component of the composition of the present invention, is obtained by reacting a polycarboxylic anhydride (a-2) with an intermediate polyester (a-1) having a hydroxyl group as described later. obtained, each having an acid value of 15 to less than 30, preferably 16 to 28, and a hydroxyl value of 2 or more, preferably 3 to 20, and a softening point of 80 to 150°C,
Preferably within the range of 90 to 130°C, it should be noted that by actively leaving hydroxyl groups,
It refers to a resin designed to be compatible with the polyepoxy compound (B). If the acid value is lower than 15, the resulting coating film will inevitably have insufficient mechanical strength;
If it is more than 30, the storage stability of the powder coating inevitably decreases, and the reaction progresses during storage, resulting in deterioration of the smoothness of the coating film. Undesirable. On the other hand, it is an essential condition that hydroxyl groups remain in the polyester resin (A), and if the hydroxyl value is lower than 2, it will inevitably be incompatible with the polyepoxy compound (B) described later. This is not preferable because it results in poor pigment dispersibility. As mentioned above, the polyester resin (A) is an intermediate polyester having a hydroxyl group (a-
1) and polycarboxylic anhydride (a-2), and there are no particular restrictions on the method of reaction between these two compounds (a-1) and (a-2). However, among them, the representative one is intermediate polyester (a
-1) with a polycarboxylic anhydride (a-2), or an intermediate polyester (a-1).
Examples include a method in which a polycarboxylic anhydride (a-2) is added to 1) and then further subjected to a condensation reaction. Here, the intermediate polyester (a-
1) has a hydroxyl value of 12.5 to 70, preferably 13 to 50, and an acid value of 2 to 10, preferably 3.
-8, and as long as it falls within this range, it may have a branched structure or a linear structure. There is no particular restriction on the method for preparing the intermediate polyester (a-1), and well-known and commonly used methods can be applied as they are, and as the acid component and the alcohol component, well-known and commonly used dibasic acids and/or Alternatively, polybasic acids, dihydric alcohols (glycols), and/or polyhydric alcohols can be used as they are, but typical acid components include terephthalic acid, isophthalic acid, phthalic acid, and methyl terephthalic acid. , trimellitic acid, pyromellitic acid and their anhydrides or adipic acid, sebacic acid, succinic acid, maleic acid, fumaric acid, tetrahydrophthalic acid, methyl-tetrahydrophthalic acid, hexahydrophthalic acid, methyl-hexahydrophthalic acid and the like. On the other hand, typical alcohol components include ethylene glycol, propylene glycol, 1,3-butanediol, 1,4-butanediol, and 1,6-butanediol.
Hexanediol, neopentyl glycol, isopentyl glycol, bishydroxyethyl terephthalate, hydrogenated bisphenol A, ethylene oxide adduct of hydrogenated bisphenol A, propylene oxide adduct of hydrogenated bisphenol A, trimethylolethane, trimethylol Examples include propane, glycerin, pentaerythritol, and 2,2,4-trimethylpentane-1,3-diol, but monoepoxy compounds can also be used as one of the glycols in the present invention. On the other hand, the polycarboxylic acid anhydride (a-2) to be reacted with the intermediate polyester (a-1)
As a divalent aromatic, aliphatic or alicyclic acid anhydride containing 30 to 100% by weight of a trivalent or higher polybasic organic carboxylic anhydride based on the total polycarboxylic anhydride, it is possible to apply. Among them, the most representative ones are terephthalic acid, isophthalic acid, phthalic acid,
These include acid anhydrides such as trimellitic acid, pyromellitic acid, succinic acid, adipic acid, azelaic acid, sebacic acid, maleic acid, tetrahydrophthalic acid or hexahydrophthalic acid. The polyepoxy compound (B), which is another essential component of the composition of the present invention, refers to a compound having at least two epoxy groups in one molecule, and among these, particularly representative ones are: are diglycidyl ethers of bisphenol A or bisphenol F, glycidyl esters/ethers of oxybenzoic acid; polydiglycyl ethers of polyhydric alcohols such as diglycidyl ethers of ethylene glycol or glycidyl ethers of trimethylolpropane; Diglycidyl esters of dibasic acids such as glycidyl esters; or triglycidyl isocyanurates. Therefore, the resin composition for powder coating of the present invention contains the above-mentioned polyester resin (A) and polyepoxy compound (B) as essential components, and both of these essential components The usage ratio is 60 to 97 parts by weight of component (A): component (B).
40-3 parts by weight, preferably 65-96 parts by weight: 35-4
A ratio of parts by weight is appropriate. In order to further promote the crosslinking and curing reaction, a well-known catalyst can be appropriately added to the composition of the present invention, and it also prevents the formation of craters on the coating surface and further improves the smoothness. For this purpose, an acrylic acid long-chain alkyl ester polymer, a fluorine compound, or the like may be added as a flow control agent (flow agent). A powder coating can be prepared using the thus obtained composition of the present invention by any known method. By applying the resulting powder coating by a well-known method such as electrostatic spraying or fluidized dipping and then baking, a coating film with excellent performance can be obtained. Next, the present invention will be specifically explained using reference examples, examples, and comparative examples, and all parts and percentages are based on weight unless otherwise specified. Reference Example 1 [Preparation example of polyester resin (A)] A mixture consisting of 83 parts of ethylene glycol, 327 parts of neopentyl glycol, 435 parts of dimethyl terephthalate and 0.4 parts of zinc acetate was prepared by removing the methanol produced from the reaction system. While removing, the temperature was gradually raised to 210°C, and the same temperature was then maintained for 2 hours to continue the alcohol exchange reaction. Next, here is 6 of trimethylolpropane.
149 parts of terephthalic acid, 224 parts of isophthalic acid and 0.5 part of di-n-butyltin oxide were added, the temperature was raised to 240°C over 8 hours, and further dehydration condensation was carried out at the same temperature to form hydroxyl groups. An intermediate polyester (a-1) having a value of 14 and an acid value of 7 was obtained. After that, this polyester (a-1)
The temperature was lowered to 200°C, and then the trimellitic anhydride was heated to 29
When the mixture was reacted at the same temperature for 2 hours, the target resin (A) having an acid value of 23, a hydroxyl value of 5, and a softening point of 123°C was obtained. Hereinafter, this will be abbreviated as polyester (A-1). Reference Example 2 (same as above) The amounts of ethylene glycol, neopentyl glycol and dimethyl terephthalate were
The alcohol exchange reaction was carried out in the same manner as in Reference Example 1, except that the amounts were changed to 159 parts, 218 parts, and 452 parts. Then, the use of isophthalic acid was omitted, and the amounts of trimethylolpropane and terephthalic acid were changed to 20 parts and 20 parts, respectively. A dehydration condensation reaction was carried out in the same manner as in Reference Example 1, except that the amount was changed to 384 parts, to obtain an intermediate polyester (a-1) having a hydroxyl value of 30 and an acid value of 3. After that, the amount of trimellitic anhydride used was reduced to 45%.
The intermediate polyester was reacted in the same manner as in Reference Example 1 except that the acid value was 28,
A target resin (A) having a hydroxyl value of 16 and a softening point of 124°C was obtained. Hereinafter, this will be abbreviated as polyester (A-2). Reference Example 3 (same as above) The amounts of ethylene glycol, neopentyl glycol and dimethyl terephthalate were changed to 136 parts, 253 parts and 472 parts, respectively, and 1,
The alcohol exchange reaction was carried out in the same manner as in Reference Example 1, except that 29 parts of 6-hexanediol was also used, and then 33 parts of adipic acid was used instead of 20 parts of trimethylolpropane. A dehydration condensation reaction was carried out in the same manner as in Reference Example 2, except that the amount of terephthalic acid used was changed to 308 parts, to obtain an intermediate polyester (a-1) having a hydroxyl value of 45 and an acid value of 6. Ta. After that, this polyester (a-1)
The temperature was lowered to 200°C, and then 60°C of trimellitic anhydride was added.
240 g of water and kept at the same temperature for 2 hours, then
When the temperature was raised to ℃ and reacted at the same temperature for 3 hours, the acid value was 25, the hydroxyl value was 12, and the softening point was 119℃.
The desired resin (A) was obtained. Hereinafter, this will be abbreviated as polyester (A-3). Reference Example 4 [Preparation example of polyester resin for comparison] The same procedure as Reference Example 2 was carried out except that the amount of trimellitic anhydride used was changed to 102 parts, and the acid value was 57, the hydroxyl value was 0, and the softening A control polyester resin (A') having a temperature of 126°C was obtained. Hereinafter, this will be abbreviated as polyester (A'-1). Reference Example 5 (same as above) except that the amounts of ethylene glycol, neopentyl glycol, and dimethyl terephthalate were changed to 141 parts, 236 parts, and 440 parts, respectively.
The alcohol exchange reaction was carried out in the same manner as in Reference Example 1, and then the dehydration condensation was carried out in the same manner as in Reference Example 1, except that the amounts of trimethylolpropane, terephthalic acid, and isophthalic acid used were changed to 5 parts, 172 parts, and 235 parts, respectively. After the reaction, the hydroxyl value is 6,
A control intermediate polyester (a'-1) having an acid value of 20 was obtained. Afterwards, the amount of trimellitic anhydride used was reduced to 7
This is changed to the above polyester (a′-
The acid value was 24, the hydroxyl value was 4,
A control polyester resin (A') having a softening point of 118°C was obtained. Hereinafter, this will be abbreviated as polyester (A'-2). Reference Example 6 [Preparation example of polyester resin (A)] Except that the amounts of ethylene glycol, neopentyl glycol, and dimethyl terephthalate were changed to 127 parts, 261 parts, and 442 parts, respectively.
The alcohol exchange reaction was carried out in the same manner as in Reference Example 1, except that the amounts of trimethylolpropane and terephthalic acid used were changed to 19 parts and 378 parts.
A dehydration condensation reaction was carried out in the same manner as in Reference Example 2 to obtain an intermediate polyester (a-1) having a hydroxyl value of 27 and an acid value of 3. After that, the amount of trimellitic anhydride used was reduced to 37%.
parts, and also used 13 parts of phthalic anhydride, and both of these polycarboxylic anhydrides (a-
2) was changed to react with the above polyester (a-1) in the same manner as in Reference Example 1, and the acid value was 28, the hydroxyl value was 10, and the softening point was 125 ° C.
A desired polyester resin (A) was obtained. below,
This is abbreviated as polyester (A-4). Reference Example 7 [Preparation example of polyester resin (A)] 455.5 parts of dimethyl terephthalate (DMT),
The procedure was carried out in the same manner as in Reference Example 1, except that a mixture consisting of 145.7 parts of ethylene glycol (EG), 244.4 parts of neopentyl glycol (NG), and 0.4 parts of zinc acetate was used, and then terephthalic acid ( 385.4 parts of TPA) and 0.5 parts of di-n-butyltin dioxide were added and subjected to dehydration condensation to obtain an intermediate polyester (a-1) having a hydroxyl value of 12.5 and an acid value of 9. Next, this intermediate polyester (a-1)
The reaction was carried out in the same manner as in Reference Example 1, except that 27 parts of trimellitic anhydride was added to 1000 parts, to obtain a target polyester resin having an acid value of 24 and a hydroxyl value of 2. Hereinafter, this will be abbreviated as polyester resin (A-5). Reference Example 8 (same as above) A target polyester having an acid value of 28 and a hydroxyl value of 2 was produced in the same manner as Reference Example 7, except that the amount of trimellitic anhydride (TMA) used was changed to 36 parts. Resin was obtained. Hereinafter, this will be abbreviated as polyester resin (A-6). Reference Example 9 [Example of preparation of control polyester resin (A')] 455.2 parts of DMT, 145.6 parts of EG, 244.3 parts of NPG
A control intermediate polyester having a hydroxyl value of 12 and an acid value of 9 was obtained in the same manner as in Reference Example 7 except that TPA was changed to 385.9 parts. Next, the acid value was determined in the same manner as in Reference Example 7, except that the amount of TMA used was changed to 23.9 parts.
22 and a hydroxyl value of 5, a control polyester resin was obtained. Hereinafter, this will be abbreviated as polyester resin (A'-3). Reference example 10 (same as above) 455.2 parts of DMT, 145.3 parts of EG, 243.7 parts of NPG
A control intermediate polyester having a hydroxyl value of 10 and an acid value of 9 was obtained in the same manner as in Reference Example 7 except that TPA was changed to 387.9 parts. Next, a control polyester resin having an acid value of 28 and a hydroxyl value of 2 was obtained in the same manner as in Reference Example 7 except that the amount of TMA used was changed to 36 parts. This is abbreviated as polyester resin (A'-3). Examples 6 and 7 and Comparative Examples 3 and 4 Each component was mixed in the composition ratio shown in Table 1, and then made into a paint in the same manner as in Example 2, and then the coating film performance was compared. I considered it. The results are summarized in the same table. Examples 1 to 5 and Comparative Examples 1 and 2 Each component was mixed in the composition ratio as shown in Table 1, and then each mixture was melt-kneaded using "Conneader PR-46" manufactured by Buss, Switzerland. After pulverization, the amount that passed through 150 meshes was applied to a 0.8 mm thick zinc phosphate treated steel plate separately by electrostatic spraying to a film thickness of 50 to 60 Όm, and then baked at 200° C. for 20 minutes. The coating film performance test results for each paint are summarized in the same table.

【衚】【table】

【衚】【table】

Claims (1)

【特蚱請求の範囲】  氎酞基䟡が12.5〜70KOHmgで、
か぀酞䟡が〜10KOHmgなるポリ゚ステル
暹脂−に倚官胜性有機カルボン酞無氎物
−を反応させお埗られる、酞䟡が15KOH
mg以䞊30KOHmg未満で、氎酞基䟡が
2KOHmg以䞊で、か぀軟化点が80〜150℃な
るポリ゚ステル暹脂の60〜97重量郚ず、 分子䞭に少なくずも個の゚ポキシ基
を有するポリ゚ポキシ化合物の〜40重量郹 ずを必須の成分ずしお含んで成る、粉䜓塗料甚暹
脂組成物。
[Scope of Claims] 1 (A) A hydroxyl value of 12.5 to 70 KOHmg/g,
and an acid value of 15 KOH obtained by reacting a polyester resin (a-1) with an acid value of 2 to 10 KOH mg/g with a polyfunctional organic carboxylic acid anhydride (a-2).
mg/g or more and less than 30KOH mg/g, and the hydroxyl value is
60 to 97 parts by weight of a polyester resin containing 2KOHmg/g or more and having a softening point of 80 to 150°C; (B) 3 to 40 parts by weight of a polyepoxy compound having at least two epoxy groups in one molecule; A resin composition for powder coating, comprising as an essential component.
JP4699084A 1984-03-14 1984-03-14 Resin composition for powder coating Granted JPS60192772A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4699084A JPS60192772A (en) 1984-03-14 1984-03-14 Resin composition for powder coating

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4699084A JPS60192772A (en) 1984-03-14 1984-03-14 Resin composition for powder coating

Publications (2)

Publication Number Publication Date
JPS60192772A JPS60192772A (en) 1985-10-01
JPH0372672B2 true JPH0372672B2 (en) 1991-11-19

Family

ID=12762633

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4699084A Granted JPS60192772A (en) 1984-03-14 1984-03-14 Resin composition for powder coating

Country Status (1)

Country Link
JP (1) JPS60192772A (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62260871A (en) * 1986-05-07 1987-11-13 Dainippon Ink & Chem Inc Resin composition for powder coating
JPH01141961A (en) * 1987-11-30 1989-06-02 Nippon Light Metal Co Ltd Coating composition for preventing filamentous corrosion of aluminum material
JP2539706B2 (en) * 1991-02-22 1996-10-02 倧日本塗料株匏䌚瀟 Powder coating composition
KR19990061666A (en) * 1997-12-31 1999-07-26 김충섞 Heat Resistant Powder Coating Composition

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS53132034A (en) * 1977-04-25 1978-11-17 Dainippon Ink & Chem Inc Resin composition for coating powder
JPS5667373A (en) * 1979-11-02 1981-06-06 Toyobo Co Ltd Resin composition for powdered paint

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS53132034A (en) * 1977-04-25 1978-11-17 Dainippon Ink & Chem Inc Resin composition for coating powder
JPS5667373A (en) * 1979-11-02 1981-06-06 Toyobo Co Ltd Resin composition for powdered paint

Also Published As

Publication number Publication date
JPS60192772A (en) 1985-10-01

Similar Documents

Publication Publication Date Title
US4499239A (en) Resin composition for powder coating
US4087479A (en) Heat-curable resin compositions for powder paints
US6184311B1 (en) Powder coating composition of semi-crystalline polyester and curing agent
EP0521992B1 (en) Coating compositions
US4740580A (en) One-step process for the preparation of carboxyl group-terminated polyesters
JP2810500B2 (en) Powder paint
US6555226B1 (en) Polyester resin for powder coating
JPS59108065A (en) Powder paint
JPH04214771A (en) Resin composition for powder coating
US5162058A (en) Coating powder composition
JPH0372672B2 (en)
JPS62260871A (en) Resin composition for powder coating
JPS6136030B2 (en)
JP3385487B2 (en) Resin composition for powder coating
JPS6226677B2 (en)
US5449528A (en) Process for the production of matt epoxy resin coatings
JP2689155B2 (en) Resin composition for thermosetting coating and powder coating
JPH0329830B2 (en)
JP2827386B2 (en) Resin composition for powder coating
JP2662247B2 (en) Low temperature curing type resin composition for powder coating
JPS5825118B2 (en) Fun Taiyo Yoji Yushisoseibutsu
JPS6119664B2 (en)
JPS5837343B2 (en) Polyester resin composition for powder coating
JPS588431B2 (en) Fun Taiyo Yoji Yushisoseibutsu
JPS6329691B2 (en)

Legal Events

Date Code Title Description
EXPY Cancellation because of completion of term