JPS627229B2 - - Google Patents

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Publication number
JPS627229B2
JPS627229B2 JP13426377A JP13426377A JPS627229B2 JP S627229 B2 JPS627229 B2 JP S627229B2 JP 13426377 A JP13426377 A JP 13426377A JP 13426377 A JP13426377 A JP 13426377A JP S627229 B2 JPS627229 B2 JP S627229B2
Authority
JP
Japan
Prior art keywords
parts
acid
reaction
resin
saturated polyester
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
Application number
JP13426377A
Other languages
Japanese (ja)
Other versions
JPS5466933A (en
Inventor
Tatsuji Asawa
Minoru Fujishima
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.)
Resonac Corp
Original Assignee
Hitachi Chemical 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 Hitachi Chemical Co Ltd filed Critical Hitachi Chemical Co Ltd
Priority to JP13426377A priority Critical patent/JPS5466933A/en
Publication of JPS5466933A publication Critical patent/JPS5466933A/en
Publication of JPS627229B2 publication Critical patent/JPS627229B2/ja
Granted legal-status Critical Current

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  • Paints Or Removers (AREA)

Description

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

本発明は飜和ポリ゚ステルを塗膜圢成成分ずし
お含有する塗料組成物に関し、曎に詳しくは二塩
基酞ず二䟡アルコヌルずの氎酞基含有飜和ポリ゚
ステルを、有機ゞむ゜シアネヌト化合物ず反応さ
せお補造される高分子量の飜和ポリ゚ステルを、
塗膜圢成成分ずしお含有する塗料組成物に関す
る。 埓来、猶甚塗料には猶内面塗料ず猶倖面塗料ず
があり、内面塗料は猶の内面に塗付しお食品によ
぀お猶材が腐食したり、猶材から金属が食品ぞ溶
出するこずによ぀お食品が倉質するのを防ぎ、倖
面塗料は猶倖面に塗付しお猶倖面の防食ず猶倖面
に矎芳を䞎える。 埓぀お内面塗料ずしおは、塗膜が無害で食品に
異臭を䞎えずたた颚味を阻害しないこず、猶材か
ら食品ぞ金属を溶出するのを防止できるこず、塗
装䜜業性がよく也燥性がよいこず、玠地ずの付着
がよく、塗膜のたわみ性、耐摩耗性、耐衝撃性が
よく、補猶工皋で受ける加工倉圢に塗膜が耐える
こず、猶詰の殺菌工皋䞭に塗膜にはがれ、ふく
れ、癜化などを生じないこず、などが芁求され
る。 猶倖面塗料の芁求性胜ずしおは、塗装䜜業性、
也燥性がよく、塗膜の黄倉が少なく、再塗装性が
あり裏う぀りしないこず、玠地や䞋塗り、むンク
の膜ず付着がよく補猶工皋で受ける加工倉圢に塗
膜が耐えるこず、仕䞊ワニスの堎合むンクをにじ
たせたり、倉色させたりしなこず、猶詰の殺菌工
皋䞭に塗膜にはがれ、ふくれ、癜化、黄倉などを
生じないこず、塗膜の光沢がよいこずがあげられ
る。内倖面塗料ずも塗料ずしおの貯蔵安定性がよ
いこずはいうたでもない。 猶内面甚および猶倖面甚塗料はこのような芁求
特性をふたえ、その甚途に応じお皮々の暹脂が塗
膜䞻成分ずしお甚いられおいる。そのため品皮が
非垞に倚いずいう問題点があり䞊蚘芁求を同時に
満足する暹脂の開発が望たれおいた。たずえばキ
ダツプ、゚アゟヌル猶等に甚いる塗料はロヌルコ
ヌタで塗装埌猶の圢状に加工するため、塗装埌の
加工によ぀おも塗膜特性に異垞のないすなわち加
工性の良い塩化ビニル共重合䜓を䞻䜓ずした、い
わゆるビニル系塗料が䞻ずしお甚いられおいる。
しかし塩化ビニル系暹脂のうち、塩化ビニル−
酢酞ビニル共重合䜓は金属ずの付着性が良くな
く、曎に蒞気殺菌をした堎合、光沢の劣化、ふく
れ発生、塗膜剥離等が生じ、耐蒞気殺菌性が劣
る。塩化ビニル−酢酞ビニル共重合䜓のプノ
ヌル暹脂、゚ポキシ暹脂もしくはアミノ暹脂の倉
性䜓は焌付時塗膜が黄倉し易く、耐蒞気殺菌性が
劣るずいう問題がある䞊、曎に塩化ビニル系暹脂
は倖芳の点で光沢が䞍足し、耐溶剀溶解性も良く
ない。 たた猶倖面塗料のホワむトコヌトずしお通垞甚
いられおいるビニル化アルキド暹脂、およびオむ
ルフリヌアルキド暹脂−アミノ暹脂倉性䜓は倖
芳、耐溶剀溶解性、黄倉性、耐蒞気殺菌性、加工
性の点でバランスがずれおいるが、䞊蚘塩化ビニ
ル系暹脂を代替するには加工性が䞍足しおいる。 たた䞻ずしお仕䞊げワニスずしお甚いられおい
る熱硬化性アクリル暹脂は黄倉が少なく、耐蒞気
殺菌性もすぐれおいるが、䞊蚘塩化ビニル系暹脂
を代替するには加工性が䞍足しおいる。 そこで、本発明者らは塩化ビニル系暹脂䞊みの
加工性を有し、金属ずの付着性、耐蒞気殺菌性、
焌付け時の塗膜の黄倉が少なく、光沢のよい暹脂
の開発を行ない、りレタン倉性飜和ポリ゚ステル
がこの芁求を満たすこずを芋い出し、本発明を成
したものである。 本発明に係る塗料組成物は特に、加工性が優れ
おいる。ゆえに、䞊蚘のような猶甚塗料だけでな
く、加工性の芁求されるカラヌトタン塗料ずしお
も有甚であり、䞀般に被塗装䜓特に金属が塗
装埌加工される分野に有甚である。 すなわち本発明は、(a)゚チレン性䞍飜和結合を
有しない二塩基酞たたはそのアルキル゚ステルお
よび(b)二䟡アルコヌルを瞮合反応させお埗られる
初期瞮合物を、(c)有機ゞむ゜シアネヌトでりレタ
ン化し、しかも䞊蚘(a)二塩基酞たたはそのアルキ
ル゚ステル、(b)二䟡アルコヌルおよび(c)有機ゞむ
゜シアネヌトがモル比で、(b)(a)(c)が〜
1.1および(a)(c)が〜100になるように反応させ
お埗られる高分子量飜和ポリ゚ステルを塗膜圢成
成分ずしお含有する塗料組成物に関する。 本発明の塗料組成物の䞻成分である、りレタン
倉性飜和ポリ゚ステルの二塩基酞成分〔(a)成分〕
ずしおはフタル酞、む゜フタル酞、テレフタル
酞、アゞピン酞、セバシン酞、ナフタレンゞカル
ボン酞等の二塩基酞およびこれらの酞無氎物䞊び
にこれらのアルキル゚ステルが挙げられる。二䟡
アルコヌル成分〔(b)成分〕ずしおぱチレングリ
コヌル、ゞ゚チレングリコヌル等のポリ゚チレン
グリコヌル、プロピレングリコヌル、ゞプロピレ
ングリコヌル等のポリプロピレングリコヌル、ネ
オペンチルグリコヌル、ブタンゞオヌル、
−ビス−−オキシプニルプロパン等が
挙げられる。 有機ゞむ゜シアネヌト〔(c)成分〕ずしおは、ヘ
キサメチレンゞむ゜シアネヌト、トリメチルヘキ
サメチレンゞむ゜シアネヌトなどの脂肪族ゞむ゜
シアネヌト、キシリレンゞむ゜シアネヌトなどの
環状脂肪族ゞむ゜シアネヌトおよび、トリレンゞ
む゜シアネヌト、4′−ゞプニルメタンゞむ
゜シアネヌトなどの芳銙族ゞむ゜シアネヌトなど
が挙げられ、たた䞊蚘化合物を䜵甚しおも良い。 耐黄倉性の点から脂肪族ゞむ゜シアネヌトが奜
たしいが付加反応速床の点においお芳銙族ゞむ゜
シアネヌトが望たしい。補造方法は、たず二塩基
酞ず二䟡アルコヌルを150〜280℃奜たしくは200
〜260℃においお〜15時間反応させる。この時
公知の゚ステル觊媒を甚いるこずは䜕らさし぀か
えなく䟋えばゞブチルチンオキサむド、ゞブチル
チンゞラりレヌト等を原料仕蟌量に察しお0.05〜
重量で十分に目的を達するこずができる。反
応は垞圧䞋でも、たた加圧䞋でも行なわれるが、
この時キシレンなどの有機溶媒の存圚䞋に行なう
こずもできる。 次に有機ゞむ゜シアネヌトずのりレタン化反応
においおは、反応を均䞀に行なわせるため、奜た
しくは、トル゚ン、メチル゚チルケトン、酢酞゚
チル、キシレン、セロ゜ルブアセテヌト、゜ルベ
ツ゜100、゜ルベツ゜150商品名゚ツ゜・スタ
ンダヌド石油(æ ª)補芳銙族溶剀などの有機溶媒の
存圚䞋に䞊蚘瞮合物を溶解させ、有機ゞむ゜シア
ネヌトを滎䞋反応させるこずが良い。反応枩床は
50℃〜150℃で、奜たしくは曎に反応を促進する
ため、公知の觊媒䟋えば錫などの金属化合物を適
圓量添加するこずも良い。䟋えば゚ステル化觊媒
ずしお甚いられるゞブチルチンオキサむドはりレ
タン化反応における觊媒ずもなりうる。 䞊蚘(a)、(b)および(c)成分は、モル比(b)(a)
(c)が〜1.1になるように配合される。未満
では、りレタン化埌未反応のむ゜シアネヌト基が
残存し、塗膜特性䞊奜たしくない、たた、1.1を
越えるず高分子量化が困難になる。さらに(a)およ
び(c)成分はモル比で(a)(c)が〜100になるよう
に配合される。未満では、埗られる線状飜和ポ
リ゚ステル䞭に占めるりレタン郚分の濃床が高く
なり、溶剀に察する溶解性が䜎䞋し、モル比が
100を越えるず高分子量化が困難になる。奜たし
くは(a)(c)モル比は10以䞋にされる。 なお、官胜以䞊の倚䟡アルコヌルをアルコヌ
ル成分䞭重量未満䜿甚しおもよい。重量
以䞊になるず高分子量化が䞍可胜になる。 本発明の塗料組成物は、垌釈溶媒ずしお、キシ
レン、゜ルベツ゜100゚ツ゜・スタンダヌド石
æ²¹(æ ª)商品名、゜ルベツ゜150゚ツ゜・スタンダ
ヌド石油(æ ª)商品名、セロ゜ルブアセテヌト、ブ
チルセロ゜ルブ等の有機溶媒を適宜甚いる。曎に
硬化剀ずしおメラミン暹脂、ベンゟグアナミン暹
脂などのアミノ暹脂を甚いおも良く䟋えば、り
レタン倉性飜和ポリ゚ステルに察しお50重量以
䞋。反応促進のためパラトル゚ンスルホン酞等
の酞性觊媒を甚いおも良い䟋えば、りレタン倉
性飜和ポリ゚ステルおよびアミノ暹脂の総量に察
しお重量以䞋。さらに、チタン癜、酞化
鉛、黄鉛、フタロシアニンブルヌ、フタロシアニ
ングリヌン等の着色顔料を添加しおもよい。た
た、゚ポキシ暹脂等の倉性剀を添加しおもよい。 以䞋本発明の実斜䟋を瀺す。郚ずあるのは重量
郚である。 実斜䟋  ゚ステル化反応 テレフタル酞249郚、む゜フタル酞249郚、゚チ
レングリコヌル93郚、ネオペンチルグリコヌル
176.8郚を䞍掻性ガスふんい気䞋、240℃で10時間
反応せしめお酞䟡の初期瞮合物(A)を埗た。この
際觊媒ずしおゞブチルチンオキサむド1.1郚甚い
た。 りレタン化合物 䞊蚘初期瞮合物(A)400郚をキシレンセロ゜ル
ブアセテヌト重量比の混合溶媒600
郚に溶解させた埌、䞍掻性ガスふんい気䞋、100
℃でヘキサメチレンゞむ゜シアネヌト20郚を滎䞋
した。時間滎䞋した埌時間䞀定枩床に保枩
し、ガヌドナヌ粘床−Z1の飜和ポリ゚ステル(A)
を埗た。(b)(a)(c)モル比は1.00で(a)(c)モ
ル比は15であり酞䟡、ヒドロキシ䟡であ぀
た。 塗料化 飜和ポリ゚ステル(A)メラン326商品名日
立化成工業株匏䌚瀟補アミノ暹脂チタン癜
8020100固圢分の重量比になるように混
合し、シンナヌキシレンセロ゜ルブアセテヌ
トで䞍揮発分50になるように調敎した。 実斜䟋  ゚ステル化反応 テレフタル酞249郚、む゜フタル酞249郚、
ブタンゞオヌル310.5郚、ゞブチルチンオキサ
むド1.1郚を䞍掻性ガスふんい気䞋240℃で反応さ
せ10時間で酞䟡の初期瞮合物(B)を埗た。 りレタン化反応 初期瞮合物(B)400郚をキシレンセロ゜ルブア
セテヌト重量比の混合溶媒600郚に
溶解させた埌100℃でヘキサメチレンゞむ゜シア
ネヌト40郚を時間で滎䞋した埌、時間反応さ
せガヌドナヌ粘床−Z1の飜和ポリ゚ステル(B)を
埗た。(b)(a)(c)モル比は1.01で(a)(c)モル
比は7.2であり、酞䟡、ヒドロキシル䟡であ
぀た。塗料化は実斜䟋に準じお行な぀た。 比范䟋  塩化ビニル−酢酞ビニル共重合䜓ずしおVAGH
商品名ナニオンカヌバむド瀟補塩化ビニル暹
脂を甚いトル゚ンメチルむ゜ブチルケトン混
合溶媒に溶かした。 塗料化 VAGHメラン326Bチタン癜8020100
固圢分重量比になるように混合し、シンナヌ
トル゚ンメチルむ゜ブチルケトンむ゜プロ
パノヌルで䞍揮発分40になるように調敎し
た。 比范䟋  ビニル化アルキド暹脂ずしおフタルキツド
903B商品名日立化成工業株匏䌚瀟補アルキ
ド暹脂を甚い実斜䟋ず同じ塗料配合で塗料を
䜜成した。 比范䟋  オむルフリヌアルキド暹脂ずしおフタルキツド
SP×103商品名日立化成工業株匏䌚瀟補アル
キド暹脂を甚い、実斜䟋ず同じ塗料配合で塗
料を䜜成した。 比范䟋  熱硬化性アルキル暹脂ずしおヒタロむド2605
商品名日立化成工業株匏䌚瀟補アクリル暹
脂を甚いた。 塗料化 ヒタロむド2605およびチタン癜をヒタロむド
2605チタン癜100100固圢分の重量比ず
なるように配合し、シンナヌキシレンセロ゜
ルブアセテヌトで䞍揮発分50重量になるよう
に調敎しお塗料ずした。 比范䟋  実斜䟋の初期瞮合物(A)を甚いお䞋蚘の操䜜で
重瞮合反応を行な぀た。 初期瞮合物(A)500郚を真空床mmHg、枩床240
℃で180分反応させ酞1.0、極限粘床0.5330℃、
プノヌルテトラクロル゚タン、0.5
の性状を有する、飜和ポリ゚ステル(D)を埗
た。 ぀いで、実斜䟋ず同じ塗料配合で塗料を䜜成
した。 実斜䟋〜および比范䟋〜で埗た塗料を
䜿甚しお詊隓した結果を衚に瀺す。
The present invention relates to a coating composition containing a saturated polyester as a coating film-forming component, and more specifically to a high molecular weight saturated coating composition produced by reacting a hydroxyl group-containing saturated polyester of a dibasic acid and a dihydric alcohol with an organic diisocyanate compound. polyester,
The present invention relates to a coating composition containing it as a coating film-forming component. Traditionally, there are two types of paint for cans: inner can paint and can outer paint.Inner paint is applied to the inner surface of the can to prevent food from corroding the can material and metals from the can material leaching into the food. The exterior paint is applied to the outside of the can to prevent corrosion and give the outside of the can a beautiful appearance. Therefore, as an inner surface coating, the coating film must be harmless, do not give off an odor to the food, or inhibit the flavor, can prevent metals from being leached from the can stock into the food, and have good coating workability and drying properties. The coating film should adhere well to the substrate, have good flexibility, abrasion resistance, and impact resistance, and should withstand processing deformation during the can manufacturing process. It is required that no whitening occurs. The performance requirements for can exterior paint include painting workability,
Good drying properties, little yellowing of the paint film, repaintability and no backing, good adhesion to substrates, undercoats, and ink films, and the ability of the paint film to withstand processing deformation during the can manufacturing process. In this case, the ink should not bleed or change color, the coating should not peel, blister, whiten, yellow, etc. during the sterilization process of canned goods, and the coating should have a good gloss. It goes without saying that both the interior and exterior paints have good storage stability as paints. Based on these required characteristics, various resins are used as the main component of paints for the inside and outside of cans, depending on the application. Therefore, there is a problem that there are a large number of varieties, and it has been desired to develop a resin that simultaneously satisfies the above requirements. For example, paints used for caps, aerosol cans, etc. are processed into the shape of the can after being painted with a roll coater, so they are mainly made of vinyl chloride copolymer, which has good processability and has no abnormality in film properties even after being processed after painting. So-called vinyl-based paints are mainly used.
However, among vinyl chloride resins, vinyl chloride
Vinyl acetate copolymers have poor adhesion to metals, and further, when steam sterilized, deterioration of gloss, blistering, and peeling of the coating occur, resulting in poor steam sterilization resistance. Modified versions of vinyl chloride-vinyl acetate copolymers such as phenolic resins, epoxy resins, or amino resins tend to cause yellowing of the paint film during baking and have poor steam sterilization resistance. It lacks gloss and has poor solvent solubility resistance. In addition, vinylated alkyd resins and oil-free alkyd resin-amino resin modified products, which are commonly used as white coats for can exterior paints, are well-balanced in terms of appearance, solvent solubility, yellowing, steam sterilization resistance, and processability. However, the processability is insufficient to replace the above-mentioned vinyl chloride resin. In addition, thermosetting acrylic resins, which are mainly used as finishing varnishes, have little yellowing and excellent steam sterilization resistance, but are insufficient in processability to replace the above-mentioned vinyl chloride resins. Therefore, the present inventors have found that it has processability comparable to that of vinyl chloride resin, adhesion to metals, steam sterilization resistance,
We developed a resin with good gloss and less yellowing of the coating film upon baking, and discovered that urethane-modified saturated polyester satisfies these requirements, resulting in the present invention. The coating composition according to the present invention has particularly excellent processability. Therefore, it is useful not only as a paint for cans as described above, but also as a color tin paint that requires processability, and is generally useful in fields where objects to be painted (particularly metals) are processed after being painted. That is, the present invention is a method of urethanizing an initial condensate obtained by condensing (a) a dibasic acid having no ethylenically unsaturated bond or an alkyl ester thereof and (b) a dihydric alcohol with (c) an organic diisocyanate. , and the molar ratio of (a) dibasic acid or its alkyl ester, (b) dihydric alcohol, and (c) organic diisocyanate, and (b)/{(a)+(c)} is 1 to
1.1 and (a)/(c) of 5 to 100. The present invention relates to a coating composition containing, as a film-forming component, a high molecular weight saturated polyester obtained by reacting so that (a)/(c) is 5 to 100. Dibasic acid component [component (a)] of urethane-modified saturated polyester, which is the main component of the coating composition of the present invention.
Examples include dibasic acids such as phthalic acid, isophthalic acid, terephthalic acid, adipic acid, sebacic acid, and naphthalene dicarboxylic acid, their acid anhydrides, and their alkyl esters. Dihydric alcohol components [component (b)] include polyethylene glycols such as ethylene glycol and diethylene glycol, polypropylene glycols such as propylene glycol and dipropylene glycol, neopentyl glycol, butanediol, 2,2
-bis(p-2-oxyphenyl)propane and the like. Organic diisocyanates [component (c)] include aliphatic diisocyanates such as hexamethylene diisocyanate and trimethylhexamethylene diisocyanate, cycloaliphatic diisocyanates such as xylylene diisocyanate, tolylene diisocyanate, 4,4'-diphenylmethane diisocyanate, etc. aromatic diisocyanates, and the above compounds may be used in combination. Aliphatic diisocyanates are preferred from the viewpoint of yellowing resistance, but aromatic diisocyanates are preferred from the viewpoint of addition reaction rate. The production method first involves heating a dibasic acid and a dihydric alcohol at 150 to 280°C, preferably at 200°C.
React for 5-15 hours at ~260°C. At this time, there is no problem in using a known ester catalyst, such as dibutyltin oxide, dibutyltin dilaurate, etc., at a rate of 0.05 to
1% by weight is sufficient to achieve the purpose. The reaction can be carried out under normal pressure or under increased pressure, but
At this time, it can also be carried out in the presence of an organic solvent such as xylene. Next, in the urethanization reaction with an organic diisocyanate, in order to perform the reaction uniformly, preferably toluene, methyl ethyl ketone, ethyl acetate, xylene, cellosolve acetate, Solbetsuso 100, Solbetsuso 150 (trade name: Etsuso Standard Oil Co., Ltd. It is preferable to dissolve the above-mentioned condensate in the presence of an organic solvent such as an aromatic solvent manufactured by A. The reaction temperature is
Preferably, a suitable amount of a known catalyst such as a metal compound such as tin may be added to further promote the reaction at a temperature of 50°C to 150°C. For example, dibutyltin oxide used as an esterification catalyst can also be used as a catalyst in the urethanization reaction. The above (a), (b) and (c) components have a molar ratio (b)/{(a)+
(c)} is blended so that it is 1 to 1.1. If it is less than 1, unreacted isocyanate groups remain after urethanization, which is unfavorable in terms of coating film properties, and if it exceeds 1.1, it becomes difficult to increase the molecular weight. Further, components (a) and (c) are blended so that the molar ratio (a)/(c) is 5 to 100. If it is less than 5, the concentration of the urethane moiety in the obtained linear saturated polyester becomes high, the solubility in the solvent decreases, and the molar ratio decreases.
If it exceeds 100, it becomes difficult to increase the molecular weight. Preferably (a)/(c) (molar ratio) is 10 or less. In addition, you may use less than 5 weight% of trifunctional or more polyhydric alcohols in an alcohol component. 5% by weight
If it exceeds this amount, it becomes impossible to increase the molecular weight. The coating composition of the present invention uses an organic solvent such as xylene, Solbetsuso 100 (trade name of Etsuso Standard Oil Co., Ltd.), Solbetsuso 150 (trade name of Etsuso Standard Oil Co., Ltd.), cellosolve acetate, butyl cellosolve, etc. as a diluting solvent. Use as appropriate. Furthermore, an amino resin such as a melamine resin or a benzoguanamine resin may be used as a curing agent (eg, 50% by weight or less based on the urethane-modified saturated polyester). An acidic catalyst such as para-toluenesulfonic acid may be used to accelerate the reaction (eg, 1% by weight or less based on the total amount of urethane-modified saturated polyester and amino resin). Furthermore, color pigments such as titanium white, lead oxide, yellow lead, phthalocyanine blue, and phthalocyanine green may be added. Furthermore, a modifier such as an epoxy resin may be added. Examples of the present invention will be shown below. Parts are by weight. Example 1 <Esterification reaction> 249 parts of terephthalic acid, 249 parts of isophthalic acid, 93 parts of ethylene glycol, neopentyl glycol
176.8 parts were reacted at 240° C. for 10 hours under a blanket of inert gas to obtain an initial condensate (A) with an acid value of 5. At this time, 1.1 parts of dibutyltin oxide was used as a catalyst. <Urethane compound> 400 parts of the above initial condensate (A) was mixed with 600 parts of a mixed solvent of xylene/cellosolve acetate = 1/1 (weight ratio).
After dissolving in 100 ml, under inert gas atmosphere,
20 parts of hexamethylene diisocyanate was added dropwise at ℃. After dripping for 1 hour, it was kept at a constant temperature for 2 hours, and saturated polyester (A) with a Gardner viscosity of Z-Z 1 was added.
I got it. The (b)/{(a)+(c)} molar ratio was 1.00, the (a)/(c) molar ratio was 15, and the acid value was 2 and the hydroxyl value was 5. <Painting> Saturated polyester (A)/Melan 326 (product name: amino resin manufactured by Hitachi Chemical Co., Ltd.)/Titanium white =
The mixture was mixed to have a weight ratio of 80/20/100 (solid content), and the nonvolatile content was adjusted to 50% with thinner (xylene/cellosolve acetate). Example 2 <Esterification reaction> 249 parts of terephthalic acid, 249 parts of isophthalic acid, 1,
310.5 parts of 4-butanediol and 1.1 parts of dibutyltin oxide were reacted at 240°C under an inert gas atmosphere to obtain an initial condensate (B) with an acid value of 5 in 10 hours. <Urethanization reaction> After 400 parts of the initial condensate (B) was dissolved in 600 parts of a mixed solvent of xylene/cellosolve acetate = 1/1 (weight ratio), 40 parts of hexamethylene diisocyanate was added dropwise at 100°C over 1 hour. Thereafter, the mixture was reacted for 2 hours to obtain a saturated polyester (B) having a Gardner viscosity of Z-Z 1 . The (b)/{(a)+(c)} molar ratio was 1.01 and the (a)/(c) molar ratio was 7.2, with an acid value of 1 and a hydroxyl value of 5. The coating was made according to Example 1. Comparative Example 1 VAGH as vinyl chloride-vinyl acetate copolymer
(trade name: vinyl chloride resin manufactured by Union Carbide) was dissolved in a mixed solvent of toluene/methyl isobutyl ketone. <Painting> VAGH/Melan 326B/Titanium white = 80/20/100
(solid content weight ratio) and adjusted with thinner (toluene/methyl isobutyl ketone/isopropanol) to have a nonvolatile content of 40%. Comparative Example 2 Phthalkyd as vinylated alkyd resin
A paint was prepared using 903B (trade name: alkyd resin manufactured by Hitachi Chemical Co., Ltd.) and the same paint formulation as in Example 1. Comparative example 3 Phthalkyd as oil-free alkyd resin
A paint was prepared using SP×103 (trade name: alkyd resin manufactured by Hitachi Chemical Co., Ltd.) with the same paint formulation as in Example 1. Comparative Example 4 Hytaloid 2605 as thermosetting alkyl resin
(Product name: Acrylic resin manufactured by Hitachi Chemical Co., Ltd.) was used. <Painting> Hitaloid 2605 and titanium white
2605/Titanium White = 100/100 (weight ratio of solid content) was blended, and the nonvolatile content was adjusted to 50% by weight with thinner (xylene/cellosolve acetate) to make a paint. Comparative Example 5 Using the initial condensate (A) of Example 1, a polycondensation reaction was carried out in the following manner. 500 parts of the initial condensate (A) at a vacuum level of 1 mmHg and a temperature of 240
React for 180 minutes at ℃, acid 1.0, intrinsic viscosity 0.53 (30℃,
Phenol/tetrachloroethane = 6/4, 0.5
A saturated polyester (D) having properties of %) was obtained. Then, a paint was prepared using the same paint formulation as in Example 1. Table 1 shows the results of tests using the paints obtained in Examples 1-2 and Comparative Examples 1-5.

【衚】 第衚䞭の塗膜特性は䞋蚘のようにしお枬定し
た。 塗装条件および詊隓法 塗装方法 ロヌルで0.25mmのブリキ板に膜厚が150mg
100cm2になるように塗装し、180℃で10分間焌付
けた。 塗膜詊隓法 Γ付着性 mm四方のゎバン目100コを゚リクセン詊
隓機でmm抌し出し埌セロハンテヌプではく
りし、残぀たゎバン目を分子に瀺した。 Γ黄倉性 色差蚈で色差を枬定した。ただし、焌付条
件を210℃で60分間ずした。 Γ加工法 盎埄20mmの深さ40mmのキダツプ打抜き詊隓
機で詊隓片を打抜き、はがれ床合を刀定し
た。 Γ耐蒞気殺菌性 加工性詊隓したキダツプおよび平板を1.5
気圧の蒞気殺菌装眮に入れ60分蒞気殺菌し、
光沢の保持率、ふくれの発生床合、塗膜のは
がれを刀定した。 実斜䟋  実斜䟋の初期瞮合物(A)400郚をトル゚ンメ
チル゚チルケトン重量比の混合溶媒
600郚に溶解させた埌、䞍掻性ガスふんい気䞋、
80℃でヘキサメチレンゞむ゜シアネヌト20郚を滎
䞋した。時間滎䞋で時間䞀定枩床に保枩しガ
ヌドナ粘床15秒25℃の飜和ポリ゚ステル(A)を
埗た。 実斜䟋  実斜䟋の初期瞮合物(B)400郚をトル゚ンメ
チル゚チルケトン重量比の混合溶媒
600郚に溶解させた埌80℃でヘキサメチレンゞむ
゜シアネヌト40郚を時間で滎䞋し、時間反応
させガヌドナ粘床15秒25℃の飜和ポリ゚ステ
ル(B)を埗た。 実斜䟋  実斜䟋の初期瞮合物(A)400郚をトル゚ンメ
チル゚チルケトン重量比の混合溶媒
600郚に溶解させた埌䞍掻性ガスふんい気䞋、80
℃でヘキサメチレンゞむ゜シアネヌト15郚を実斜
䟋ず同様に滎䞋した。ガヌドナ粘床10秒25
℃の飜和ポリ゚ステル(C)を埗た。 比范䟋  実斜䟋の初期瞮合物(B)を甚いお䞋蚘の操䜜で
重瞮合反応を行な぀た。 初期瞮合物(A)500郚を真空床mmHg、枩床240
℃で180分反応させ酞䟡2.0、極限粘床0.5330
℃、プノヌルテトラクロル゚タン
、0.5の性状を有する飜和ポリ゚ステル暹
脂(D)を埗た。 比范䟋  む゜フタル酞249郚、アゞピン酞219郚、
ヘキサンゞオヌル118郚、トリメチロヌルプロパ
ン260郚を䞍掻性ガスふんい気䞋240℃で反応さ
せ、酞䟡玄10のオむルフリヌアルキツド(E)を埗
た。 比范䟋  ゚ステル化反応 テレフタル酞249郚、む゜フタル酞249郚、゚チ
レングリコヌル214郚、トリメチロヌルプロパン
67郚を䞍掻性ガスふんい気䞋240℃で反応させ酞
䟡玄の初期瞮合物(D)を埗た。 りレタン化反応 初期瞮合物(D)400郚をトル゚ンメチル゚チル
ケトン重量比の混合溶媒600郚に溶
解させた埌、80℃でヘキサメチレンゞむ゜シアネ
ヌト63郚を時間で滎䞋し、時間反応させ、り
レタン化オむルフリヌアルキツド暹脂(F)を埗た。 比范䟋  ゚ステル化反応 テレフタル酞249郚、む゜フタル酞249郚、
ブタンゞオヌル405郚、ゞブチルチンオキサむ
ド1.1郚を䞍掻性ガスふんい気䞋240℃で反応させ
10時間で酞䟡の初期瞮合物(E)を埗た。 りレタン化反応 初期瞮合物(E)400郚をトル゚ンメチル゚チル
ケトン重量比の混合溶媒600郚に溶
解させた埌、80℃でヘキサメチレンゞむ゜シアネ
ヌト252郚を時間で滎䞋し時間反応させ飜和
ポリ゚ステル暹脂(G)を埗た。しかし宀枩で溶解性
が劣りゲル状を呈した。 このようにしお埗られた飜和ポリ゚ステル暹脂
(A)〜(G)の暹脂特性および塗膜特性を衚に瀺す。 衚䞭の塗膜特性は、䞋蚘のようにしお枬定し
た。 塗装条件および詊隓法 塗料配合 Γ暹脂メラン28商品名日立化成工業株匏
䌚瀟補メラミン暹脂チタン癜8020
100固圢分の重量比 ΓP.W.C.50 Γシンナキシレンセロ゜ルブアセテヌト
で䞍揮発分50に調敎。 塗装方法 ロヌル塗装 膜厚20ÎŒ 基材は0.25mmのブリキ板 焌付け枩床 180℃10分 塗膜詊隓法 Γ耐氎性100×200mmの詊隓板を100℃沞氎䞭
10時間浞挬し、光沢の倉化ブリスタの発生床
合を比范した。 ブリスタ評䟡 点 異垞なし ASTM D714−54T 点 8F 点 6F
[Table] The coating film properties in Table 1 were measured as follows. Coating conditions and test methods Coating method Roll to coat a 0.25mm tin plate with a film thickness of 150mg/
It was painted to a size of 100cm 2 and baked at 180℃ for 10 minutes. Coating film test method Γ adhesion 100 1 mm square squares were extruded for 6 mm using an Erichsen tester, then peeled off with cellophane tape, and the remaining squares were shown as molecules. Γ Yellowing Color difference was measured using a color difference meter. However, the baking conditions were 210°C for 60 minutes. Γ Processing method A test piece was punched out using a cap punching tester with a diameter of 20 mm and a depth of 40 mm, and the degree of peeling was determined. Γ Steam sterilization resistance Processability tested caps and flat plates were 1.5
Put it in an atmospheric pressure steam sterilizer and steam sterilize it for 60 minutes.
The gloss retention rate, degree of blistering, and peeling of the paint film were evaluated. Example 3 400 parts of the initial condensate (A) of Example 1 was added to a mixed solvent of toluene/methyl ethyl ketone = 8/2 (weight ratio).
After dissolving in 600 parts, under an inert gas atmosphere,
20 parts of hexamethylene diisocyanate was added dropwise at 80°C. The mixture was added dropwise for 1 hour and kept at a constant temperature for 2 hours to obtain a saturated polyester (A) having a Gardner viscosity of 15 seconds (25°C). Example 4 400 parts of the initial condensate (B) of Example 2 was added to a mixed solvent of toluene/methyl ethyl ketone = 8/2 (weight ratio).
After dissolving the mixture in 600 parts, 40 parts of hexamethylene diisocyanate was added dropwise at 80°C over 1 hour, and the mixture was reacted for 2 hours to obtain a saturated polyester (B) having a Gardner viscosity of 15 seconds (25°C). Example 5 400 parts of the initial condensate (A) of Example 1 was added to a mixed solvent of toluene/methyl ethyl ketone = 8/2 (weight ratio).
After dissolving in 600 parts, under an inert gas atmosphere, 80 parts
15 parts of hexamethylene diisocyanate was added dropwise in the same manner as in Example 1. Gardna viscosity 10 seconds (25
A saturated polyester (C) was obtained. Comparative Example 6 Using the initial condensate (B) of Example 1, a polycondensation reaction was carried out in the following manner. 500 parts of the initial condensate (A) at a vacuum level of 1 mmHg and a temperature of 240
The reaction was carried out at ℃ for 180 minutes, with an acid value of 2.0 and an intrinsic viscosity of 0.53 (30
°C), phenol/tetrachloroethane = 6/
A saturated polyester resin (D) having properties of 4.0.5%) was obtained. Comparative Example 7 249 parts of isophthalic acid, 219 parts of adipic acid, 1,6
118 parts of hexanediol and 260 parts of trimethylolpropane were reacted at 240°C under an inert gas atmosphere to obtain an oil-free alkyd (E) with an acid value of about 10. Comparative Example 8 <Esterification reaction> 249 parts of terephthalic acid, 249 parts of isophthalic acid, 214 parts of ethylene glycol, trimethylolpropane
67 parts were reacted at 240°C under an inert gas atmosphere to obtain an initial condensate (D) with an acid value of about 3. <Urethanization reaction> After dissolving 400 parts of the initial condensate (D) in 600 parts of a mixed solvent of toluene/methyl ethyl ketone = 8/2 (weight ratio), 63 parts of hexamethylene diisocyanate was added dropwise at 80°C over 1 hour. The mixture was reacted for 2 hours to obtain a urethanized oil-free alkyd resin (F). Comparative Example 9 <Esterification reaction> 249 parts of terephthalic acid, 249 parts of isophthalic acid, 1,
405 parts of 4-butanediol and 1.1 parts of dibutyltin oxide were reacted at 240°C under an atmosphere of inert gas.
An initial condensate (E) with an acid value of 5 was obtained in 10 hours. <Urethanization reaction> After dissolving 400 parts of the initial condensate (E) in 600 parts of a mixed solvent of toluene/methyl ethyl ketone = 8/2 (weight ratio), 252 parts of hexamethylene diisocyanate was added dropwise at 80°C over 2 hours. The reaction was carried out for 3 hours to obtain a saturated polyester resin (G). However, the solubility was poor at room temperature and it took on a gel-like appearance. Saturated polyester resin thus obtained
Table 2 shows the resin properties and coating film properties of (A) to (G). The coating film properties in Table 2 were measured as follows. Painting conditions and test methods Paint formulation Γ resin/Melan 28 (product name: melamine resin manufactured by Hitachi Chemical Co., Ltd.)/Titanium white = 80/20/
100 (weight ratio of solids) ΓP.WC=50% Γ thinner (xylene/cellosolve acetate)
Adjust the non-volatile content to 50%. Coating method Roll coating Film thickness 20ÎŒ Base material: 0.25mm tin plate Baking temperature 180℃ 10 minutes Coating film test method Γ Water resistance: 100 x 200mm test plate in boiling water at 100℃
After soaking for 10 hours, changes in gloss and degree of blistering were compared. Blister evaluation 5 points No abnormality (ASTM D714-54T) 3 points 8F 1 point 6F

【衚】 Γ加工性 70×40mmの詊隓片をたお方向に䞭心郚から
折り曲げ、0.25mmのブリキ板を板スペヌサ
ずしおはさみ180℃に折り曲げプレスした。 点 クラツクなし 点 箄1/3クラツク 点 党面クラツク 以䞊より明らかなように、本発明の塗料組成物
は耐黄倉性、付着性、光沢、ブロツキング性が良
奜であり、特に、加工性が顕著に優れおいる。さ
らに、耐蒞気殺菌性にも優れおいる。
[Table] Γ Workability A 70 x 40 mm test piece was bent from the center in the vertical direction, and a 0.25 mm tin plate was used as a spacer with scissors and bent and pressed at 180°C. 5 points: No cracks 3 points: Approximately 1/3 crack 1 point: Fully cracked As is clear from the above, the coating composition of the present invention has good yellowing resistance, adhesion, gloss, and blocking properties, and in particular has good processability. Remarkably superior. Furthermore, it has excellent steam sterilization resistance.

Claims (1)

【特蚱請求の範囲】[Claims]  (a)゚チレン性䞍飜和結合を有しない二塩基酞
たたはそのアルキル゚ステルおよび(b)二䟡アルコ
ヌルを瞮合反応させお埗られる初期瞮合物を(c)有
機ゞむ゜シアネヌトでりレタン化し、しかも䞊蚘
(a)二塩基酞たたはそのアルキル゚ステル、(b)二䟡
アルコヌルおよび(c)有機ゞむ゜シアネヌトがモル
比で、(b)(a)(c)が〜1.1および(a)(c)が
〜100になるように反応させお埗られる高分子
量飜和ポリ゚ステルを塗膜圢成成分ずしお含有す
る塗料組成物。
1. An initial condensate obtained by condensation reaction of (a) a dibasic acid having no ethylenically unsaturated bond or its alkyl ester and (b) a dihydric alcohol is urethanized with (c) an organic diisocyanate, and the above-mentioned
(a) dibasic acid or its alkyl ester, (b) dihydric alcohol, and (c) organic diisocyanate in molar ratio, (b)/{(a)+(c)} from 1 to 1.1 and (a)/ A coating composition containing, as a film-forming component, a high molecular weight saturated polyester obtained by reaction such that (c) is 5 to 100.
JP13426377A 1977-11-09 1977-11-09 Coating composition Granted JPS5466933A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13426377A JPS5466933A (en) 1977-11-09 1977-11-09 Coating composition

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13426377A JPS5466933A (en) 1977-11-09 1977-11-09 Coating composition

Publications (2)

Publication Number Publication Date
JPS5466933A JPS5466933A (en) 1979-05-29
JPS627229B2 true JPS627229B2 (en) 1987-02-16

Family

ID=15124200

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13426377A Granted JPS5466933A (en) 1977-11-09 1977-11-09 Coating composition

Country Status (1)

Country Link
JP (1) JPS5466933A (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6569421B2 (en) * 2014-09-19 2019-09-04 荒川化孊工業株匏䌚瀟 Resin composition for can inner coating

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Publication number Publication date
JPS5466933A (en) 1979-05-29

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