JP2000336304A - Metacresol resin composition for coating material - Google Patents

Metacresol resin composition for coating material

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Publication number
JP2000336304A
JP2000336304A JP11146130A JP14613099A JP2000336304A JP 2000336304 A JP2000336304 A JP 2000336304A JP 11146130 A JP11146130 A JP 11146130A JP 14613099 A JP14613099 A JP 14613099A JP 2000336304 A JP2000336304 A JP 2000336304A
Authority
JP
Japan
Prior art keywords
molecular weight
average molecular
mol
weight average
meta
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.)
Granted
Application number
JP11146130A
Other languages
Japanese (ja)
Other versions
JP4362891B2 (en
Inventor
Toru Saneto
徹 実藤
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.)
Sumitomo Durez Co Ltd
Original Assignee
Sumitomo Durez Co Ltd
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Priority to JP14613099A priority Critical patent/JP4362891B2/en
Publication of JP2000336304A publication Critical patent/JP2000336304A/en
Application granted granted Critical
Publication of JP4362891B2 publication Critical patent/JP4362891B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Phenolic Resins Or Amino Resins (AREA)
  • Paints Or Removers (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a resin for a coating material for a can, having extremely superior fast curability compared to a conventional phenol resin for the coating for the can, and capable of providing a coated film having small potassium permanganate consumption and excellent in processability such as bending. SOLUTION: This metacresol resin composition for a coating material is a reaction product obtained by reacting a prepolymer obtained by reacting metacresol with formaldehydes, with alcohols, having 600-1,800 weight average molecular weight (Mw), and <=3.0 ratio (Mw/Mn) of the weight average molecular weight (Mw) to the number average molecular weight (Mn), and containing >=60% of alkoxylated methylol group.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、エポキシ系缶内面
塗料等の硬化剤として有用な塗料用メタクレゾール樹脂
組成物に関し、短時間硬化性を有し、形成される塗膜の
過マンガン酸カリウム消費量が小さく、曲げ等の加工性
にも優れている塗料用メタクレゾール樹脂組成物に関す
るするものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a meta-cresol resin composition for coatings useful as a curing agent for inner coatings of epoxy cans and the like. The present invention relates to a meta-cresol resin composition for paints that consumes a small amount and has excellent workability such as bending.

【0002】[0002]

【従来の技術】周知のように、エポキシ樹脂−フェノー
ル樹脂系塗料の性能は、配合されるフェノール樹脂の性
質により大きく影響される。実際には、用いられるフェ
ノール成分の種類と組成比、エポキシ樹脂/フェノール
樹脂の比等により硬化性、衛生性、密着性、加工性等の
性能のバランスを変化させ、それぞれの用途に応じた種
々のフェノール樹脂が利用されている。
2. Description of the Related Art As is well known, the performance of an epoxy resin-phenolic resin paint is greatly affected by the properties of the phenolic resin to be blended. Actually, the balance of performance such as curability, hygiene, adhesion, workability, etc. is changed depending on the type and composition ratio of the phenol component used, the ratio of epoxy resin / phenol resin, etc. Phenolic resin is used.

【0003】近年、エポキシ系塗料の硬化剤であるフェ
ノール樹脂に対しては、速硬化性を有することが要求さ
れている。一般に、製缶用塗料の焼き付けは、150〜
300℃で30秒〜20分間程度の条件で行われている
が、このような高温の焼き付けでは、多大な熱エネルギ
ーコストを必要とすると共に、高温におけるヒュームや
ヤニの発生があるため、低温でしかも短時間で硬化する
硬化剤樹脂が要望されている。
In recent years, phenol resins, which are curing agents for epoxy-based paints, have been required to have rapid curability. Generally, the baking of paint for cans is 150-
It is performed at 300 ° C. for about 30 seconds to 20 minutes. However, such high-temperature baking requires a large amount of heat energy cost and generates fumes and tar at high temperatures. In addition, there is a demand for a curing agent resin that cures in a short time.

【0004】しかしながら、従来の二官能性フェノール
類を主成分とした塗料用フェノール樹脂は、重量平均分
子量が400〜800で比較的分子量が低く、且つ低分
子量成分が多く残存するため、エポキシ樹脂系缶内面塗
料の硬化剤として用いた場合、硬化性が低く、過マンガ
ン酸カリウム消費量が高いという問題がある。また、こ
れらの特性を解決するため、三官能性フェノール類やビ
スフェノールAを用いた高分子量のレゾール型フェノー
ル樹脂を用いる例もあるが、メチロール基濃度が高くな
るため、硬化剤単独での自己縮合傾向も高まり、加工性
に劣るという欠点があった。さらに、ビスフェノールA
については、内分泌攪乱物質としての疑いがもたれてい
るため、缶内面塗料の硬化剤として使用するのは好まし
くない。
However, the conventional phenolic resins for coatings containing a difunctional phenol as a main component have a weight average molecular weight of 400 to 800, a relatively low molecular weight, and a large amount of low molecular weight components. When used as a curing agent for paint on the inner surface of a can, there is a problem that curability is low and potassium permanganate consumption is high. In order to solve these characteristics, there is also an example of using a high-molecular-weight resol type phenol resin using trifunctional phenols or bisphenol A. However, since the methylol group concentration becomes high, self-condensation with a curing agent alone is performed. There is also a disadvantage that the tendency is increased and processability is poor. Furthermore, bisphenol A
Is suspected as an endocrine disrupting substance, and it is not preferable to use it as a curing agent for paint on the inner surface of cans.

【0005】[0005]

【発明が解決しようとする課題】本発明の目的は、エポ
キシ系缶内面塗料等の硬化剤として用いた場合、短時間
硬化性を有し、且つ形成される塗膜の過マンガン酸カリ
ウム消費量が小さく、加工性に優れている塗料用メタク
レゾール樹脂組成物を提供することにある。本発明者
は、上記の課題解決のため鋭意研究を重ねた結果、分子
量分布が狭く、アルコキシ化度の極めて大きな特定分子
量のメタクレゾール樹脂が好ましいことを見いだした。
SUMMARY OF THE INVENTION An object of the present invention is to provide a curing agent for an epoxy can inner coating which has a short curing property and consumes potassium permanganate in a coating film to be formed. It is an object of the present invention to provide a meta-cresol resin composition for coatings, which is small in size and excellent in processability. As a result of intensive studies for solving the above-mentioned problems, the present inventors have found that a metacresol resin having a specific molecular weight, which has a narrow molecular weight distribution and an extremely large degree of alkoxylation, is preferable.

【0006】[0006]

【課題を解決するための手段】本発明は、メタクレゾー
ルとホルムアルデヒド類とを反応させることにより得ら
れるプレポリマーとアルコール類とを反応せしめること
により得られる反応生成物であって、重量平均分子量
(Mw)が600〜1,800で且つ重量平均分子量
(Mw)と数平均分子量(Mn)の比(Mw/Mn)が
3.0以下であり、メチロール基の60%以上がアルコ
キシ化されていることを特徴とする塗料用メタクレゾー
ル樹脂組成物に関する。
SUMMARY OF THE INVENTION The present invention relates to a reaction product obtained by reacting a prepolymer obtained by reacting metacresol with formaldehyde and an alcohol, and comprising a weight average molecular weight ( Mw) is 600 to 1,800, the ratio (Mw / Mn) of the weight average molecular weight (Mw) to the number average molecular weight (Mn) is 3.0 or less, and 60% or more of the methylol groups are alkoxylated. The present invention relates to a meta-cresol resin composition for paints.

【0007】[0007]

【発明の実施の形態】以下、本発明について具体的に説
明する。本発明の塗料用メタクレゾール樹脂組成物を得
るには、例えば下記の3段階の工程をとる方法を挙げる
ことができる。第1工程において、メタクレゾールにホ
ルムアルデヒドを付加してメチロール化し、第2工程に
おいて、メチロール化メタクレゾールの脱水縮合を進め
プレポリマー化し、第3工程において、プレポリマーと
アルコール類とを反応させてアルコキシ化する方法であ
る。
BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, the present invention will be described specifically. In order to obtain the meta-cresol resin composition for a paint of the present invention, for example, a method including the following three steps can be mentioned. In the first step, formaldehyde is added to meta-cresol to form methylol, in the second step, dehydration-condensation of the methylolated meta-cresol proceeds to form a prepolymer, and in the third step, the prepolymer reacts with alcohols to form an alkoxy group. It is a method to become.

【0008】第1工程において、メタクレゾールとホル
ムアルデヒドとの反応が塩基性触媒の存在下で行われ
る。ここでは使用したメタクレゾールをすべて反応さ
せ、メチロール化させることが好ましい。第1工程にお
いては、メタクレゾールのメチロール化以外にメチロー
ル化メタクレゾール類の脱水縮合が一部行われてもよ
い。
In the first step, the reaction between metacresol and formaldehyde is carried out in the presence of a basic catalyst. Here, it is preferable to react all of the used meta-cresol to form methylol. In the first step, dehydration condensation of methylolated metacresols may be partially performed in addition to methylolation of metacresol.

【0009】第1行程において使用されるホルムアルデ
ヒドとしては、ホルマリン、パラホルムアルデヒド等が
挙げられる。ホルムアルデヒドの使用量は、メタクレゾ
ール1モルに対してホルムアルデヒド換算で2.0〜
5.0モルが好ましく、3.0〜4.0モルがより好ま
しい。ホルムアルデヒドの使用量(モル比)が2.0モ
ル未満の場合は、メチロール化されないメタクレゾール
が残存することが多く、一方5.0モルを越えると、樹
脂中のメチロール基濃度が高くなりすぎる傾向がある。
Formaldehyde used in the first step includes formalin, paraformaldehyde and the like. The amount of formaldehyde used is 2.0 to 2.0 mol in terms of formaldehyde per mol of metacresol.
5.0 mol is preferable, and 3.0 to 4.0 mol is more preferable. When the amount of formaldehyde used (molar ratio) is less than 2.0 mol, non-methylolated meta-cresol often remains, while when it exceeds 5.0 mol, the methylol group concentration in the resin tends to be too high. There is.

【0010】第1工程において使用される塩基性触媒と
しては、通常のレゾール型フェノール樹脂を合成する際
に使用される公知のものが使用できる。例えば、水酸化
ナトリウム、水酸化リチウム、水酸化カリウム等のアル
カリ金属の水酸化物、水酸化マグネシウム、水酸化カル
シウム等のアルカリ土類金属の水酸化物、トリエチルア
ミン、トリメチルアミン、エタノールアミンのようなア
ミン類である。塩基性触媒の使用量は、メタクレゾール
1モルに対して0.01〜0.3モルが好ましい。0.
01モル未満ではメチロール化反応が遅く生産性が低下
し、0.3モルを越えると反応が速すぎコントロールし
にくい。
As the basic catalyst used in the first step, a known catalyst used in synthesizing a general resol type phenol resin can be used. For example, hydroxides of alkali metals such as sodium hydroxide, lithium hydroxide and potassium hydroxide, hydroxides of alkaline earth metals such as magnesium hydroxide and calcium hydroxide, amines such as triethylamine, trimethylamine and ethanolamine Kind. The use amount of the basic catalyst is preferably 0.01 to 0.3 mol per 1 mol of metacresol. 0.
If the amount is less than 01 mol, the methylolation reaction is slow and the productivity is lowered, and if it exceeds 0.3 mol, the reaction is too fast to control.

【0011】第1工程の反応条件としては、反応温度を
40〜55℃、反応時間を0.5〜3時間程度にするの
が好ましい。第1行程において重要な点はメタクレゾー
ルの全てをメチロール化することであり、そのためには
反応温度をできるだけ低くすることであるが、40℃未
満では反応が遅く生産性が低下する。
The reaction conditions in the first step are preferably such that the reaction temperature is 40 to 55 ° C. and the reaction time is about 0.5 to 3 hours. The important point in the first step is to convert all of meta-cresol to methylol. To this end, the reaction temperature should be as low as possible. However, if the temperature is lower than 40 ° C., the reaction is slow and the productivity is reduced.

【0012】第2工程においては、第1工程で得られる
メチロール化メタクレゾール類を60℃以上の反応温度
で脱水縮合させプレポリマー化する。プレポリマー化の
程度は、得られるプレポリマーの分子量でコントロール
する。この時の重量平均分子量は300〜1,000が
好ましく、更には400〜800とすることが好まし
い。重量平均分子量が300〜1,000を外れると第
3工程でのアルコキシ化のコントロールが困難になる。
In the second step, the methylolated metacresols obtained in the first step are subjected to dehydration condensation at a reaction temperature of 60 ° C. or more to form a prepolymer. The degree of prepolymerization is controlled by the molecular weight of the resulting prepolymer. The weight average molecular weight at this time is preferably from 300 to 1,000, and more preferably from 400 to 800. If the weight average molecular weight is out of the range of 300 to 1,000, it becomes difficult to control the alkoxylation in the third step.

【0013】第2工程の反応条件としては、反応温度を
60〜80℃、反応時間を1.0〜3時間程度行えば良
い。プレポリマー反応の終了後、使用した塩基性触媒
は、公知の酸、例えば硫酸、酢酸、リン酸等で中和した
後、水洗を行い、減圧濃縮して水分を除去する。
The reaction conditions in the second step may be a reaction temperature of 60 to 80 ° C. and a reaction time of about 1.0 to 3 hours. After completion of the prepolymer reaction, the used basic catalyst is neutralized with a known acid such as sulfuric acid, acetic acid, phosphoric acid, etc., washed with water, and concentrated under reduced pressure to remove water.

【0014】第3工程においては、第2工程で得られる
プレポリマーとアルコール類とを酸性触媒の存在下で反
応させてプレポリマーのアルコキシ化が行われる。
In the third step, the prepolymer obtained in the second step is reacted with an alcohol in the presence of an acidic catalyst to carry out alkoxylation of the prepolymer.

【0015】第3工程において使用される酸性触媒とし
ては、通常公知の触媒例えばシュウ酸、ギ酸、酢酸等が
利用でき、その量はメタクレゾール1モルに対して0.
01〜0.1モル程度、好ましくは0.03〜0,07
モル程度とするのが良い。
As the acidic catalyst used in the third step, generally known catalysts such as oxalic acid, formic acid and acetic acid can be used, and the amount thereof is 0.1 to 1 mol of meta-cresol.
About 01 to 0.1 mol, preferably 0.03 to 0.007
It is good to be about mol.

【0016】第3行程において使用されるアルコール類
としては、n−ブチルアルコール、イソブチルアルコー
ル、n−アミルアルコール等が挙げられる。第3行程に
おいて重要な点はメチロール基の60%以上をアルコキ
シ化することであり、そのためには等量以上のアルコー
ル類の配合が必要となる。プレポリマーに対するアルコ
ール類の配合量は100〜400PHRが好ましく、更
には150〜300PHRが好ましい。100PHRよ
りも低い場合メチロール基のアルコキシ化が不十分とな
り、400PHRより多い場合は、生産性が低下する。
The alcohols used in the third step include n-butyl alcohol, isobutyl alcohol, n-amyl alcohol and the like. An important point in the third step is to alkoxylate at least 60% of the methylol groups, and it is necessary to mix alcohols in equal amounts or more. The blending amount of the alcohol with respect to the prepolymer is preferably 100 to 400 PHR, more preferably 150 to 300 PHR. If it is lower than 100 PHR, the alkoxylation of the methylol group becomes insufficient, and if it is higher than 400 PHR, the productivity decreases.

【0017】反応条件としては、反応温度を80〜13
0℃で、反応時間は縮合水を除去しながら3〜20時間
程度行えば良い。
The reaction conditions are as follows:
The reaction may be performed at 0 ° C. for about 3 to 20 hours while removing the condensed water.

【0018】前記第1、第2及び第3工程を行うことに
より、重量平均分子量(Mw)が600〜1,800で
且つ重量平均分子量(Mw)と数平均分子量(Mn)の
比(Mw/Mn)が3.0以下で、メチロール基の60
%以上がアルコキシ化されている塗料用メタクレゾール
樹脂組成物を得ることができる。
By carrying out the first, second and third steps, the weight average molecular weight (Mw) is from 600 to 1,800 and the ratio of the weight average molecular weight (Mw) to the number average molecular weight (Mn) (Mw / Mn) is 3.0 or less, and 60
% Or more can be obtained.

【0019】本発明の塗料用メタクレゾール樹脂組成物
は上記のようにして得られるが、重量平均分子量(M
w)が600〜1,800、好ましくは800〜1,5
00で、且つ重量平均分子量(Mw)と数平均分子量
(Mn)の比(Mw/Mn)が3.0以下、好ましくは
2.0以下であり、メチロール基の60%以上、好まし
くは70%以上がアルコキシ化されているものである。
本発明の塗料用メタクレゾール樹脂組成物はエポキシ系
缶内面塗料の硬化剤として用いた場合、短時間硬化性を
有し、且つ形成される塗膜は過マンガン酸カリウム消費
量が小さく、曲げ等の加工性に極めて優れた性能を有す
るものである。重量平均分子量が600未満であると硬
化性、過マンガン酸カリウム消費量が悪くなり、一方重
量平均分子量が1,800を越えると加工性が悪くなる
傾向にある。重量平均分子量と数平均分子量の比が3.
0を越えると低分子量成分の影響により過マンガン酸カ
リウム消費量が大きくなり、高分子量成分の影響により
加工性が悪くなる。また、アルコキシ化度が60%未満
であると自己縮合傾向が高まるため加工性が極端に低下
する。
The meta-cresol resin composition for paints of the present invention is obtained as described above, and has a weight average molecular weight (M
w) is from 600 to 1,800, preferably from 800 to 1,5
00 and the ratio (Mw / Mn) of the weight average molecular weight (Mw) to the number average molecular weight (Mn) is 3.0 or less, preferably 2.0 or less, and 60% or more, preferably 70% of the methylol group. The above is what has been alkoxylated.
When the meta-cresol resin composition for a paint of the present invention is used as a curing agent for an inner paint of an epoxy can, it has a short-time curability, and the formed coating film consumes a small amount of potassium permanganate, and has a bending property. It has extremely excellent performance in processability. If the weight average molecular weight is less than 600, the curability and the consumption of potassium permanganate deteriorate, while if the weight average molecular weight exceeds 1,800, the processability tends to deteriorate. 2. The ratio of the weight average molecular weight to the number average molecular weight is 3.
If it exceeds 0, the consumption of potassium permanganate increases due to the influence of the low molecular weight component, and the processability deteriorates due to the effect of the high molecular weight component. If the degree of alkoxylation is less than 60%, the tendency of self-condensation is increased, so that the processability is extremely reduced.

【0020】なお、重量平均分子量及び重量平均分子量
と数平均分子量の比はゲルパーミエーションクロマトグ
ラフ(GPC)によりポリスチレン換算値で求め、アル
コキシ化度はNMRより求めた値である。
The weight average molecular weight and the ratio of the weight average molecular weight to the number average molecular weight are determined by gel permeation chromatography (GPC) in terms of polystyrene, and the degree of alkoxylation is determined by NMR.

【0021】本発明の塗料用メタクレゾール樹脂組成物
は、エポキシ系塗料の硬化剤として特に優れた性能を発
揮するが、水酸基を有する、アクリル系、アルキド系、
ポリエステル系などの硬化剤としても優れた性能を発揮
する。また本発明の塗料用メタクレゾール樹脂組成物
は、有機溶剤型塗料のみならず、水系塗料に対しても使
用できる。
The meta-cresol resin composition for a paint of the present invention exhibits particularly excellent performance as a curing agent for an epoxy-based paint, but has an acrylic or alkyd type having a hydroxyl group.
Excellent performance as a curing agent such as polyester. The meta-cresol resin composition for a paint of the present invention can be used not only for an organic solvent type paint but also for a water-based paint.

【0022】[0022]

【実施例】以下、本発明を実施例により説明する。しか
し本発明はこれらの実施例によって限定されるものでは
ない。
The present invention will be described below with reference to examples. However, the present invention is not limited by these examples.

【0023】《実施例1》攪拌機、熱交換機、温度計の
ついた1Lの四つ口フラスコにメタクレゾール108.
0g(1モル)、37%ホルマリン324g(3モル)
を加え、触媒として25%水酸化ナトリウム水溶液16
g(0.1モル)を添加し50℃で3時間、次いで70
℃で3時間反応させた。反応終了後50%硫酸水溶液を
添加して中和し、分離沈殿した樹脂を4回水洗した。更
に、減圧脱水により水分を除去後、生成した重量平均分
子量800のプレポリマー100部に対してn−ブタノ
ールを400部加え、触媒としてギ酸を0.05モル添
加し、100℃にて10時間反応させた。更に、減圧濃
縮により目的とする50%メタクレゾール樹脂ワニス3
00部を得た。生成物のGPCによる重量平均分子量は
1,000、重量平均分子量と数平均分子量の比は1.
5、NMRによるアルコキシ化度は80%であった。
Example 1 Metacresol 108. was placed in a 1 L four-necked flask equipped with a stirrer, heat exchanger and thermometer.
0 g (1 mol), 324 g (3 mol) of 37% formalin
And a 25% aqueous sodium hydroxide solution 16 as a catalyst.
g (0.1 mol) at 50 ° C. for 3 hours, then 70
The reaction was carried out at 3 ° C. for 3 hours. After completion of the reaction, 50% sulfuric acid aqueous solution was added for neutralization, and the separated and precipitated resin was washed four times with water. Further, after water was removed by dehydration under reduced pressure, 400 parts of n-butanol was added to 100 parts of the produced prepolymer having a weight average molecular weight of 800, 0.05 mol of formic acid was added as a catalyst, and the mixture was reacted at 100 ° C. for 10 hours. I let it. Further, the target 50% meta-cresol resin varnish 3 is obtained by concentration under reduced pressure.
00 parts were obtained. The weight average molecular weight of the product by GPC was 1,000, and the ratio of the weight average molecular weight to the number average molecular weight was 1.
5. The degree of alkoxylation by NMR was 80%.

【0024】《実施例2》実施例1と同様の反応装置に
メタクレゾール108.0g(1モル)、37%ホルマ
リン432g(4モル)を加え、触媒としてトリエチル
アミン40g(0.4モル)を添加し50℃で3時間、
次いで70℃で4時間反応させた。反応終了後蟻酸を添
加して中和し、分離沈殿した樹脂を4回水洗した。更
に、減圧脱水により水分を除去後、生成した重量平均分
子量600のプレポリマー100部に対してn−ブタノ
ールを200部加え、触媒としてギ酸を0.03モル添
加し、100℃にて6時間反応させた。更に、減圧濃縮
により目的とする50%メタクレゾール樹脂ワニス28
0部を得た。生成物のGPCによる重量平均分子量は7
00、重量平均分子量と数平均分子量の比は1.7、N
MRによるアルコキシ化度は75%であった。
Example 2 108.0 g (1 mol) of meta-cresol and 432 g (4 mol) of 37% formalin were added to the same reactor as in Example 1, and 40 g (0.4 mol) of triethylamine was added as a catalyst. 3 hours at 50 ° C
Then, the reaction was carried out at 70 ° C. for 4 hours. After completion of the reaction, formic acid was added for neutralization, and the separated and precipitated resin was washed four times with water. Further, after water was removed by dehydration under reduced pressure, 200 parts of n-butanol was added to 100 parts of the produced prepolymer having a weight average molecular weight of 600, and 0.03 mol of formic acid was added as a catalyst, followed by a reaction at 100 ° C. for 6 hours. I let it. Further, the target 50% meta-cresol resin varnish 28 is concentrated by vacuum concentration.
0 parts were obtained. The weight average molecular weight of the product by GPC was 7
00, the ratio of the weight average molecular weight to the number average molecular weight is 1.7, N
The degree of alkoxylation by MR was 75%.

【0025】《実施例3》実施例1と同様の反応装置に
メタクレゾール108.0g(1モル)、80%パラホ
ルムアルデヒド188g(ホルムアルデヒドとして5モ
ル)、水200gを加え、触媒として25%水酸化ナト
リウム水溶液64g(0.4モル)を添加し50℃で1
時間、次いで80℃で2時間反応させた。反応終了後酢
酸を添加して中和し、分離沈殿した樹脂を4回水洗し
た。更に、減圧脱水により水分を除去後、生成した重量
平均分子量1,000のプレポリマー100部に対して
n−アミルアルコールを150部加え、触媒として酢酸
を0.03モル添加し、100℃にて10時間反応させ
た。更に、減圧濃縮により目的とする50%メタクレゾ
ール樹脂ワニス310部を得た。生成物のGPCによる
重量平均分子量は1,400、重量平均分子量と数平均
分子量の比は2.0、NMRによるアルコキシ化度は7
0%であった。
Example 3 108.0 g (1 mol) of metacresol, 188 g of 80% paraformaldehyde (5 mol as formaldehyde) and 200 g of water were added to the same reaction apparatus as in Example 1, and 25% of water was used as a catalyst. Add 64 g (0.4 mol) of aqueous sodium solution and add
The reaction was allowed to proceed for 2 hours at 80 ° C. After completion of the reaction, acetic acid was added for neutralization, and the separated and precipitated resin was washed four times with water. Further, after removing water by dehydration under reduced pressure, 150 parts of n-amyl alcohol was added to 100 parts of the produced prepolymer having a weight average molecular weight of 1,000, and 0.03 mol of acetic acid was added as a catalyst. The reaction was performed for 10 hours. Furthermore, 310 parts of the target 50% meta-cresol resin varnish was obtained by vacuum concentration. The weight average molecular weight of the product by GPC was 1,400, the ratio of the weight average molecular weight to the number average molecular weight was 2.0, and the degree of alkoxylation by NMR was 7
It was 0%.

【0026】《比較例1》実施例1と同様の反応装置に
メタクレゾール108.0g(1モル)、37%ホルマ
リン324g(3モル)を加え、触媒として25%水酸
化ナトリウム水溶液1.6g(0.01モル)を添加し
50℃で3時間、次いで70℃で3時間反応させた。反
応終了後50%硫酸水溶液を添加して中和し、分離沈殿
した樹脂を3回水洗した。更に、減圧脱水により水分を
除去後、生成した重量平均分子量600のプレポリマー
100部に対してn−ブタノールを80部加え、触媒と
してギ酸を0.05モル添加し、100℃にて10時間
反応させた。更に、減圧濃縮により50%メタクレゾー
ル樹脂ワニス220部を得た。生成物のGPCによる重
量平均分子量は1,400、重量平均分子量と数平均分
子量の比は3.2、NMRによるアルコキシ化度は65
%であった。
Comparative Example 1 108.0 g (1 mol) of metacresol and 324 g (3 mol) of 37% formalin were added to the same reactor as in Example 1, and 1.6 g of a 25% aqueous sodium hydroxide solution as a catalyst ( (0.01 mol) was added and reacted at 50 ° C. for 3 hours and then at 70 ° C. for 3 hours. After the completion of the reaction, a 50% aqueous sulfuric acid solution was added for neutralization, and the separated and precipitated resin was washed three times with water. Further, after removing water by dehydration under reduced pressure, 80 parts of n-butanol was added to 100 parts of the produced prepolymer having a weight average molecular weight of 600, 0.05 mol of formic acid was added as a catalyst, and the reaction was carried out at 100 ° C. for 10 hours. I let it. Furthermore, 220 parts of a 50% meta-cresol resin varnish was obtained by vacuum concentration. The product had a weight average molecular weight by GPC of 1,400, a ratio of the weight average molecular weight to the number average molecular weight of 3.2, and a degree of alkoxylation by NMR of 65.
%Met.

【0027】《比較例2》実施例1と同様の反応装置に
同様の反応装置にメタクレゾール108.0g(1モ
ル)、37%ホルマリン432g(4モル)を加え、触
媒として25%水酸化ナトリウム水溶液3.2g(0.
02モル)を添加し50℃で3時間、次いで70℃で2
時間反応させた。反応終了後50%硫酸水溶液を添加し
て中和し、分離沈殿した樹脂を3回水洗した。更に、減
圧脱水により水分を除去後、生成した重量平均分子量7
00のプレポリマー100部に対してn−ブタノールを
150部加え、100℃にて2時間反応させた。更に、
減圧濃縮により50%メタクレゾール樹脂ワニス240
部を得た。生成物のGPCによる重量平均分子量は90
0、重量平均分子量と数平均分子量の比は1.8、NM
Rによるアルコキシ化度は30%であった。
Comparative Example 2 108.0 g (1 mol) of meta-cresol and 432 g (4 mol) of 37% formalin were added to the same reactor as in Example 1, and 25% sodium hydroxide was used as a catalyst. 3.2 g of aqueous solution (0.
02 mol) at 50 ° C. for 3 hours and then at 70 ° C. for 2 hours.
Allowed to react for hours. After the completion of the reaction, a 50% aqueous sulfuric acid solution was added for neutralization, and the separated and precipitated resin was washed three times with water. Furthermore, after removing water by dehydration under reduced pressure, the resulting weight average molecular weight 7
150 parts of n-butanol was added to 100 parts of the prepolymer No. 00 and reacted at 100 ° C. for 2 hours. Furthermore,
50% meta-cresol resin varnish 240 by concentration under reduced pressure
Got a part. The weight average molecular weight of the product by GPC is 90.
0, ratio of weight average molecular weight to number average molecular weight is 1.8, NM
The degree of alkoxylation by R was 30%.

【0028】《比較例3》実施例1と同様の反応装置に
パラクレゾール75.6g(0.7モル)、メタクレゾ
ール32.4g(0.3モル)、37%ホルマリン24
3g(3モル)を加え、触媒として25%水酸化ナトリ
ウム水溶液48g(0.3モル)を添加し50℃で3時
間、次いで80℃で1時間反応させた。反応終了後25
%硫酸水溶液を添加して中和し、分離沈殿した樹脂を3
回水洗した。更に、減圧脱水により水分を除去後、生成
した重量平均分子量700のプレポリマー100部に対
してn−ブタノールを150部加え、100℃にて7時
間反応させた。更に、減圧濃縮により50%クレゾール
樹脂ワニス200部を得た。生成物のGPCによる重量
平均分子量は1,300、重量平均分子量と数平均分子
量の比は1.8、NMRによるアルコキシ化度は70%
であった。
Comparative Example 3 In the same reactor as in Example 1, 75.6 g (0.7 mol) of paracresol, 32.4 g (0.3 mol) of metacresol, and 24% of 37% formalin 24
3 g (3 mol) was added, and 48 g (0.3 mol) of a 25% aqueous sodium hydroxide solution was added as a catalyst, followed by reaction at 50 ° C. for 3 hours and then at 80 ° C. for 1 hour. 25 after reaction
% Sulfuric acid aqueous solution to neutralize and separate and precipitate the resin.
Washed twice. Further, after water was removed by dehydration under reduced pressure, 150 parts of n-butanol was added to 100 parts of the produced prepolymer having a weight average molecular weight of 700, and reacted at 100 ° C. for 7 hours. Further, 200 parts of a 50% cresol resin varnish was obtained by concentration under reduced pressure. The product has a weight average molecular weight by GPC of 1,300, a ratio of the weight average molecular weight to the number average molecular weight of 1.8, and a degree of alkoxylation by NMR of 70%.
Met.

【0029】[塗膜性能試験]上記実施例1〜3及び比
較例1〜3で得られたクレゾール樹脂を用いて下記のよ
うにして塗料を調製し、その塗料をアルミ板に塗布後焼
付け処理を行い、加工性、過マンガン酸カリウム消費
量、密着性の試験を実施した。各種試験方法を下記に示
し、その試験結果を表1に示す。
[Coating film performance test] Using the cresol resins obtained in Examples 1 to 3 and Comparative Examples 1 to 3, coating materials were prepared as follows, and the coating materials were applied to an aluminum plate and baked. , And tests for workability, potassium permanganate consumption, and adhesion were conducted. Various test methods are shown below, and the test results are shown in Table 1.

【0030】1.塗料の調製 エピコート1009(油化シェルエポキシ(株)製エポ
キシ樹脂)30部をブチルセロソルブ50部とキシレン
50部の混合溶剤に溶解して固形分30%のエポキシ樹
脂溶液とした。このエポキシ樹脂溶液と実施例1〜3及
び比較例1〜3で得られたクレゾール樹脂を固形分の重
量比が9対1となるように混合し試験塗料を得た。
1. Preparation of Paint 30 parts of Epicoat 1009 (epoxy resin manufactured by Yuka Shell Epoxy Co., Ltd.) was dissolved in a mixed solvent of 50 parts of butyl cellosolve and 50 parts of xylene to obtain an epoxy resin solution having a solid content of 30%. The epoxy resin solution was mixed with the cresol resins obtained in Examples 1 to 3 and Comparative Examples 1 to 3 so that the weight ratio of the solid content was 9: 1 to obtain a test paint.

【0031】2.塗膜性能試験方法 上記の方法で調製した各塗料を0.3mmのアルミ板
(5052材)に乾燥塗膜厚5〜7μmとなるようにバ
ーコーターで塗布して、240℃で2分間焼き付けを行
った。そして、以下の示す塗膜性能を測定した。 (1)ゾル分率 塗装したアルミ板を所定の寸法に切り出し、メチルエチ
ルケトンの沸点で1時間抽出し、抽出前後の重量差と塗
膜重量から未硬化成分(ゾル分)の比率を求めた。 (2)過マンガン酸カリウム消費量 塗膜1cm2 当たり1mlのイオン交換水を用い130
℃で30分のレトルト抽出を行い、得られた試験液につ
いて食品衛生法記載の測定法(厚生省434号)に準じ
て測定した。 (3)加工性 塗装したアルミ板を3cm×5cmに切断した試験片
を、塗装面が外側になるように予備折り曲げし、試験片
と同じ板厚のアルミ板3枚をスペーサーとしてはさみこ
み、次いで3Kgの鉄ブロックを30cmの高さからか
ら落下させて曲げ加工を施した。この折り曲げ試験片の
折り曲げ加工部を1%食塩水中に漬積させ、試験片を+
極にして6Vの直流負荷をかけたときの電流値(mA)
を読みとって評価した。
2. Coating performance test method Each coating prepared by the above method was applied to a 0.3 mm aluminum plate (5052 material) with a bar coater so as to have a dry coating thickness of 5 to 7 μm, and baked at 240 ° C. for 2 minutes. went. And the following coating film performance was measured. (1) Sol fraction The coated aluminum plate was cut into a predetermined size, extracted at the boiling point of methyl ethyl ketone for 1 hour, and the ratio of the uncured component (sol component) was determined from the weight difference before and after extraction and the coating film weight. (2) Potassium permanganate consumption Using 1 ml of ion-exchanged water per 1 cm 2 of the coating film, 130
A retort extraction was performed at 30 ° C. for 30 minutes, and the obtained test liquid was measured according to the measurement method described in the Food Sanitation Law (Ministry of Health and Welfare No. 434). (3) Workability A test piece obtained by cutting a painted aluminum plate to 3 cm x 5 cm is preliminarily bent so that the painted surface is on the outside, and three aluminum plates having the same thickness as the test piece are inserted as spacers, and then 3 kg. Was dropped from a height of 30 cm to perform bending. The bent part of this bending test piece is immersed in 1% saline solution, and the test piece is +
Current value when a 6V DC load is applied as a pole (mA)
Was read and evaluated.

【0032】3.試験結果3. Test results

【表1】 [Table 1]

【0033】[0033]

【発明の効果】本発明の塗料用メタクレゾール樹脂組成
物は、エポキシ系缶内面塗料等の硬化剤として用いた場
合、短時間硬化性を有し、且つ形成される塗膜は過マン
ガン酸カリウム消費量が小さく、加工性に優れた性能を
有するので、たとえば食物などを保存する缶詰や飲料用
缶などの金属製缶の缶内面塗料の硬化剤として好適に使
用しうるものである。
When the meta-cresol resin composition for a paint of the present invention is used as a curing agent for an inner paint of an epoxy can or the like, it has a short-time curing property, and the formed coating film is potassium permanganate. Since it has low consumption and excellent workability, it can be suitably used as a curing agent for paints on the inner surface of metal cans such as cans for storing foods and the like and beverage cans.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 メタクレゾールとホルムアルデヒド類と
を反応させることにより得られるプレポリマーとアルコ
ール類とを反応せしめることにより得られる反応生成物
であって、重量平均分子量(Mw)が600〜1,80
0で且つ重量平均分子量(Mw)と数平均分子量(M
n)の比(Mw/Mn)が3.0以下であり、メチロー
ル基の60%以上がアルコキシ化されていることを特徴
とする塗料用メタクレゾール樹脂組成物。
1. A reaction product obtained by reacting a prepolymer obtained by reacting meta-cresol with formaldehyde with an alcohol, and having a weight average molecular weight (Mw) of 600 to 1,80.
0, weight average molecular weight (Mw) and number average molecular weight (M
A meta-cresol resin composition for paints, wherein the ratio (Mw / Mn) of n) is 3.0 or less and 60% or more of the methylol groups are alkoxylated.
JP14613099A 1999-05-26 1999-05-26 Metacresol resin composition for paint Expired - Lifetime JP4362891B2 (en)

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* Cited by examiner, † Cited by third party
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WO2015156094A1 (en) * 2014-04-10 2015-10-15 Dic株式会社 Alkoxylated resol-type phenol resin manufacturing method, alkoxylated resol-type phenol resin, resin composition, and coating
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Publication number Priority date Publication date Assignee Title
WO2015156094A1 (en) * 2014-04-10 2015-10-15 Dic株式会社 Alkoxylated resol-type phenol resin manufacturing method, alkoxylated resol-type phenol resin, resin composition, and coating
JP2015206056A (en) * 2014-04-10 2015-11-19 Dic株式会社 Method for producing alkoxylated resol-type phenol resin, alkoxylated resol-type phenol resin, resin composition and coating
JP5850288B1 (en) * 2014-04-10 2016-02-03 Dic株式会社 Process for producing alkoxylated resol type phenolic resin, alkoxylated resol type phenolic resin, resin composition and paint
KR20160147251A (en) 2014-04-10 2016-12-22 디아이씨 가부시끼가이샤 Alkoxylated resol-type phenol resin manufacturing method, alkoxylated resol-type phenol resin, resin composition, and coating
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