JPH03220220A - Production of phenolic resin and can coating agent - Google Patents

Production of phenolic resin and can coating agent

Info

Publication number
JPH03220220A
JPH03220220A JP1363690A JP1363690A JPH03220220A JP H03220220 A JPH03220220 A JP H03220220A JP 1363690 A JP1363690 A JP 1363690A JP 1363690 A JP1363690 A JP 1363690A JP H03220220 A JPH03220220 A JP H03220220A
Authority
JP
Japan
Prior art keywords
phenol
resin
component
phenolic resin
water
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.)
Pending
Application number
JP1363690A
Other languages
Japanese (ja)
Inventor
Akira Nagano
永野 晃
Masayuki Nakamura
昌之 中村
Tadashi Kotsuna
忽那 正
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
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 Sumitomo Durez Co Ltd filed Critical Sumitomo Durez Co Ltd
Priority to JP1363690A priority Critical patent/JPH03220220A/en
Publication of JPH03220220A publication Critical patent/JPH03220220A/en
Pending legal-status Critical Current

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

Abstract

PURPOSE:To obtain a phenolic resin useful as a curing agent for can coating agents by reacting a phenol component comprising phenol and a bisphenol with formaldehyde in the presence of a catalyst and specifying the content of a free phenol component. CONSTITUTION:A phenol component (a) is obtained by mixing phenol with 0.1-0.5mol, per mol of the phenol, of a bisphenol (e.g. bisphenol A). Component (a) is reacted with 4.0-6.0mol, per mol of component (a), of formaldehyde (b) at 45-50 deg.C for 2-4hr in the presence of 0.5-1.0mol, per mol of the phenol, of a catalyst (c) comprising an alkali metal hydroxide (e.g. NaOH), and the reaction is continued at 60-80 deg.C for 2-5hr. The formed resin is neutralized, washed with water and dewatered to obtain a phenolic resin of a free phenol component content of 0.1% or below based on the resin solids.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明はエポキシ−フェノール系塗料に利用されるフェ
ノール樹脂の製造方法及びそれを配合した缶塗料の製造
方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method for producing a phenol resin used in epoxy-phenol paints and a method for producing can paints containing the same.

より詳細には、缶用水性塗料中の硬化剤として使用され
た場合に、KMnO4消費量、密着性、硬化性に優れた
塗膜が得られ、かつ得られた!!膜が淡色である缶塗料
配合用フェノール樹脂及び缶塗料の製造方法に関するも
のである。
More specifically, when used as a curing agent in a water-based paint for cans, a coating film with excellent KMnO4 consumption, adhesion, and curability was obtained! ! The present invention relates to a phenolic resin for use in can paint formulations having a light-colored film and a method for producing the can paint.

[従来の技術〕 周知のようにエポキシ−フェノール系塗料の性能は、硬
化剤であるフェノール樹脂の性質によって大きく影響さ
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、触媒の種類と量、ホムルアルデヒド量、エポキシ/
フェノール比等によって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レゾール型フェノール樹脂
が利用されている。しかしながら従来の方法により製造
されるフェノール樹脂は遊離フェノール成分が多く残存
し、エポキシ−フェノール系水性塗料の硬化剤に用いた
場合、K M n O4消費量が高く、密着性に劣ると
いうような欠点があった。
[Prior Art] As is well known, the performance of epoxy-phenolic paints is greatly influenced by the properties of the phenolic resin that is the curing agent. In reality, the type and composition ratio of the phenol component used, the type and amount of the catalyst, the amount of formaldehyde, the epoxy/
Various resol-type phenolic resins are used depending on the purpose, with the balance of performance changing depending on the phenol ratio, etc. However, the phenolic resin produced by the conventional method has many remaining free phenol components, and when used as a curing agent for epoxy-phenolic water-based paints, it has drawbacks such as high KM n O4 consumption and poor adhesion. was there.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

本発明者は、缶塗料配合用フェノール樹脂について、従
来から要求されてきたエポキシ−フェノール系水性塗料
の塗膜のKMnOa消費量の低下と密着性の向上、淡色
化について鋭意研究を行っり結果、特定のフェノール類
とホルムアルデヒドを特定の割合で、アルカリ金属の水
酸化物を触媒として反応させて得られるフェノール樹脂
がきわめて有効であ゛るとの知見を得た。
The present inventor has conducted extensive research on phenolic resins for can paint formulations to reduce KMnOa consumption, improve adhesion, and lighten the color of epoxy-phenol water-based paints, which have been traditionally required. It has been found that phenolic resins obtained by reacting specific phenols and formaldehyde in specific ratios with an alkali metal hydroxide as a catalyst are extremely effective.

その目的とするところは缶塗料用エポキシーフェノール
系水性塗料の硬化剤として使用した場合、K M n 
Os消費量が小さく、密着性にすぐれ、硬化性がよい、
塗膜が淡色であるといった性能を塗膜に付与することが
可能なフェノール樹脂及び、それを用いた缶塗料を提供
することにある。
Its purpose is that when used as a curing agent for epoxy phenolic water-based paints for can paints, K M n
Low Os consumption, excellent adhesion, and good curing properties.
An object of the present invention is to provide a phenol resin capable of imparting properties such as a light color to a paint film, and a can paint using the same.

〔課題を解決するための手段〕[Means to solve the problem]

本発明の要旨は、フェノールとビスフェノール類をモル
比1:0.1−1:0.5の割合で混合したフェノール
1モルとホルムルデヒド4.0〜6゜0モルとをアルカ
リ金属の水酸化物触媒の存在下で反応させ、遊離フェノ
ール成分をレジン固形分に対して0.1%以下にするこ
とを特徴とするフェノール樹脂の製造方法である。
The gist of the present invention is to hydroxylate an alkali metal by mixing 1 mole of phenol and bisphenols in a molar ratio of 1:0.1 to 1:0.5 with 4.0 to 6.0 moles of formaldehyde. This is a method for producing a phenol resin, which is characterized in that the reaction is carried out in the presence of a chemical catalyst, and the free phenol component is reduced to 0.1% or less based on the solid content of the resin.

本発明において用いられるビスフェノール類は、ビスフ
ェノールA及びビスフェノールFに代表されるビスフェ
ノール類である。
The bisphenols used in the present invention are bisphenols represented by bisphenol A and bisphenol F.

フェノールとビスフェノール類の混合比はフェノール1
モルに対してビスフェノール類を0.1〜0.5モルが
好ましい、ビスフェノール類が多くなるとメチロールフ
ェノール成分が少なくなり分子量的に大きくなるため、
水性エマルシヨンとの相溶性が悪くなるので好ましくな
い。
The mixing ratio of phenol and bisphenols is phenol 1
Preferably, the amount of bisphenols is 0.1 to 0.5 mole per mole, because as the amount of bisphenols increases, the methylolphenol component decreases and the molecular weight increases.
This is not preferable because the compatibility with the aqueous emulsion becomes poor.

また触媒として用いるアルカリ金属の水酸化物は、例え
ば水酸化ナトリウム、水酸化カリウム等が挙げられる0
反応触媒中に存在させるべきアルカリ金属の水酸化物の
量としては、通常フェノール1モルに対して0.5〜1
.0モル程度、好ましくはフェノール1モルに対して0
.7〜0.9モル程度である。触媒のモル比が0.5よ
りも小さいと、樹脂中のメチロール基が少なく塗料とし
た場合に硬化が遅く、相溶性、K M n O4消費量
が悪くなり実用的でなくなる。逆に触媒のモル比が1.
0モルよりも大きいと反応の制御が困難となる。
In addition, examples of the alkali metal hydroxide used as a catalyst include sodium hydroxide, potassium hydroxide, etc.
The amount of alkali metal hydroxide that should be present in the reaction catalyst is usually 0.5 to 1 per mole of phenol.
.. About 0 mole, preferably 0 per mole of phenol
.. It is about 7 to 0.9 mol. If the molar ratio of the catalyst is less than 0.5, there are few methylol groups in the resin, and when used as a coating material, curing is slow and compatibility and K M n O4 consumption are poor, making it impractical. Conversely, if the molar ratio of the catalyst is 1.
If it is larger than 0 mol, it becomes difficult to control the reaction.

触媒は添加時の発熱を抑えるために、反応開始時に全量
の2/3を添加し内温安定後残りの1/3を添加するの
が好ましい。
In order to suppress heat generation during addition of the catalyst, it is preferable to add 2/3 of the total amount at the start of the reaction and add the remaining 1/3 after the internal temperature has stabilized.

反応条件としては、初期反応時の温度が45〜55℃、
時間が2〜4時間であって、2次反応時の温度が60℃
〜80℃、時間が2〜5時間が好ましい。
The reaction conditions include a temperature of 45 to 55°C during the initial reaction;
The time is 2 to 4 hours, and the temperature during the secondary reaction is 60°C.
Preferably, the temperature is 80° C. and the time is 2 to 5 hours.

反応後、生成した樹脂を中和後水洗を行い、常圧又は減
圧下で水分を除去するとよい。
After the reaction, the resulting resin is preferably neutralized and then washed with water to remove moisture under normal pressure or reduced pressure.

本発明で得られたフェノール樹脂は常法によりエポキシ
樹脂を主成分とするエマルジ4ンと混合される。このエ
マルシヨンは、エポキシ樹脂にアクリル酸、メタクリル
酸、スチレン等を付加重合させたものも好ましく使用さ
れる。エポキシ樹脂に対するフェノール樹脂の割合は、
通常固形分換算で2〜IO重置%である。
The phenolic resin obtained in the present invention is mixed with an emulsion containing an epoxy resin as a main component by a conventional method. Preferably, this emulsion is one obtained by addition polymerizing acrylic acid, methacrylic acid, styrene, etc. to an epoxy resin. The ratio of phenolic resin to epoxy resin is
It is usually 2 to IO weight percent in terms of solid content.

〔実施例〕〔Example〕

以下に、実施例を掲げて本発明の詳細な説明する。なお
実施例中の1部」は「重量部」を「%」は「重量パーセ
ント」を示す。
The present invention will be described in detail below with reference to Examples. In the examples, "1 part" indicates "part by weight" and "%" indicates "percent by weight."

r実施例zJ フェノール225部(2,39モル)及びビスフェノー
ルA  75部(0,33モル)に37%ホルマリン1
292部(11,95モル)を加え、触媒として25%
水酸化ナトリウム水溶液200部(1,25モル)を添
加し50℃にて1時間反応する。
rExample zJ 225 parts (2,39 mol) of phenol and 75 parts (0,33 mol) of bisphenol A in 1 part of 37% formalin
Added 292 parts (11,95 mol), 25% as catalyst
200 parts (1.25 mol) of sodium hydroxide aqueous solution is added and reacted at 50°C for 1 hour.

ついで25%水酸化ナトリウム水溶液100部(0,6
25モル)を新たに添加し50℃でさらに1.5時間反
応させた後70℃に昇温し2.5時間反応させた0反応
終了後35%硫酸216部(0,77モル)を添加して
中和し、生成した樹脂をブタノール450部、酢酸エチ
ル110部を加えて溶解させ40℃で3回水洗を行った
。水洗後、共沸脱水で水分を除去し目的とするフェノー
ル樹脂を得た。
Next, 100 parts of a 25% aqueous sodium hydroxide solution (0.6
25 mol) was added and reacted for another 1.5 hours at 50°C, then heated to 70°C and reacted for 2.5 hours. After the completion of the reaction, 216 parts (0.77 mol) of 35% sulfuric acid was added. The resulting resin was dissolved by adding 450 parts of butanol and 110 parts of ethyl acetate, and washed with water three times at 40°C. After washing with water, water was removed by azeotropic dehydration to obtain the desired phenol resin.

この時の樹脂の粘度は120cps/25°C1不揮発
が41%、遊離フェノ−成分がレジン固形第1表 と同様の方法でフェノール樹脂を製造した。得られたフ
ェノール樹脂の物性を第1表に併せて示す。
The viscosity of the resin at this time was 120 cps/25 DEG C. The non-volatile content was 41%, and the free phenol component was resin solid.A phenol resin was produced in the same manner as shown in Table 1. The physical properties of the obtained phenol resin are also shown in Table 1.

〔塗膜性能試験] 上記実施例1〜3および比較例1〜3で得られたフェノ
ール樹脂を用いて下記のように水性塗料第 を調整し、その塗料をアルし倹に塗布後焼付けを行い、
KMnO,消費量、密着性、外観チエツクなどの試験を
行った。
[Coating film performance test] Using the phenolic resins obtained in Examples 1 to 3 and Comparative Examples 1 to 3 above, water-based paints were prepared as shown below, and the paints were aluminized, applied sparingly, and then baked. ,
Tests were conducted on KMnO, consumption, adhesion, appearance check, etc.

各種試験方法を下記に示し、その試験結果を第2表に示
す。
Various test methods are shown below, and the test results are shown in Table 2.

水性エマルシヨンの調 ■ エピコート1009     100.(1部■ 
ブチルセロソルブ     100.0  部■ メタ
クリル酸        50.0 部■ スチレン 
         16.7 部■ 過酸化ベンゾイル
       4.67部■ ブチルセロソルブ   
   14.2 部■ ジメチルアミノエタノール  
14.3 部■ イオン交換水       450.
0  部反応容器に■■を入れ、115℃にて完全に溶
解させた後■〜■の混合物を1時間にわたって滴下する
0滴下後115℃で2時間反応を行い、反応終了後■を
加えて100℃まで内温を下げる。
Aqueous emulsion formula ■ Epicote 1009 100. (Part 1■
Butyl cellosolve 100.0 parts ■ Methacrylic acid 50.0 parts ■ Styrene
16.7 parts ■ Benzoyl peroxide 4.67 parts ■ Butyl cellosolve
14.2 parts ■ Dimethylaminoethanol
14.3 parts ■ Ion exchange water 450.
0 parts Put ■■ into a reaction container, and after completely dissolving at 115℃, add the mixture of ■~■ dropwise over 1 hour. Lower the internal temperature to 100℃.

ついで■を加えた後■をすこしずつ添加したところ、固
形分23.8%、粘度85cps/25℃の乳白色の水
性エマルジョンを得た。
Then, (1) was added and then (2) was added little by little to obtain a milky white aqueous emulsion with a solid content of 23.8% and a viscosity of 85 cps/25°C.

水性塗料の調整 上記水性エマルジョンと実施例、比較例で得られたフェ
ノール樹脂の固形分の重量比が19対1となるように混
合し安定な水性塗料を得た。
Preparation of water-based paint The above-mentioned water-based emulsion and the phenol resins obtained in Examples and Comparative Examples were mixed so that the solid content weight ratio was 19:1 to obtain a stable water-based paint.

(1)  K M n Oa消費量 上記の方法で調整した各水性塗料を5CIX201のア
ルミ枚にバーコーターで焼付は後の膜厚が5〜7μとな
るように塗布した。
(1) K M n Oa consumption Each of the water-based paints prepared in the above manner was applied to a 5CIX201 aluminum sheet using a bar coater so that the film thickness after baking was 5 to 7 μm.

その試験片を200℃で5分間焼付は後、水道水200
dが入った50(ld)−ルビー力に入れてアルミニウ
ム箔でフタをし、130℃で30分のレトルト処理を行
った。このようにして得られた試験水について食品衛生
法記載実験法(厚生省434号)に準じて測定した。
After baking the test piece at 200℃ for 5 minutes,
The mixture was placed in a 50 (ld) ruby strainer containing 100 ml of chlorine, covered with aluminum foil, and subjected to retort treatment at 130° C. for 30 minutes. The test water thus obtained was measured in accordance with the experimental method described in the Food Sanitation Act (Ministry of Health and Welfare No. 434).

(2)密着性 上記K M n Oa消費量の測定に用いる試験片と同
様の塗布焼付を行い、100°Cの水に1時間浸漬する
処理をした。その後試験片の塗膜面にカッターナイフを
使用して約1閣の幅で縦、横それぞれ11本の切り目を
基盤目に入れた。セロハン粘着テープでばくり試験を行
い、未剥離数を分子に示した。
(2) Adhesion The test piece was coated and baked in the same manner as the test piece used for measuring the K M n Oa consumption above, and immersed in water at 100°C for 1 hour. Thereafter, using a cutter knife, 11 vertical and horizontal cuts were made on the coated surface of the test piece, each having a width of about one square. A peeling test was performed using cellophane adhesive tape, and the number of unpeeled pieces was shown in the numerator.

第2表 〔発明の効果〕 本発明の方法により製造されるフェノール樹脂を缶用エ
ポキシ−フェノール系塗料の硬化剤として用いた場合、
K M n Oa消費量が少なくかつ密着性に優れた淡
色の塗膜を得ることができる。
Table 2 [Effects of the Invention] When the phenolic resin produced by the method of the present invention is used as a curing agent for an epoxy-phenolic paint for cans,
A light-colored coating film with low K M n Oa consumption and excellent adhesion can be obtained.

Claims (2)

【特許請求の範囲】[Claims] (1)フェノールとビスフェノール類をモル比1:0.
1〜1:0.5の割合で混合したフェノール類1モルと
ホムルアルデヒド4.0〜6.0モルとをアルカリ金属
の水酸化物触媒の存在下で反応させ、遊離フェノール成
分をレジン固形分に対して0.1%以下にすることを特
徴とするフェノール樹脂の製造方法。
(1) Phenol and bisphenols in a molar ratio of 1:0.
1 mole of phenols mixed at a ratio of 1 to 1:0.5 and 4.0 to 6.0 moles of formaldehyde are reacted in the presence of an alkali metal hydroxide catalyst, and the free phenol components are converted into resin solids. A method for producing a phenolic resin, characterized in that the amount is 0.1% or less.
(2)請求項1記載の方法で得られたフェノール樹脂を
エポキシ樹脂を主成分とする水性エマルジョンに配合す
ることを特徴とする缶塗料の製造方法。
(2) A method for producing a can paint, which comprises blending the phenol resin obtained by the method according to claim 1 into an aqueous emulsion containing an epoxy resin as a main component.
JP1363690A 1990-01-25 1990-01-25 Production of phenolic resin and can coating agent Pending JPH03220220A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1363690A JPH03220220A (en) 1990-01-25 1990-01-25 Production of phenolic resin and can coating agent

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1363690A JPH03220220A (en) 1990-01-25 1990-01-25 Production of phenolic resin and can coating agent

Publications (1)

Publication Number Publication Date
JPH03220220A true JPH03220220A (en) 1991-09-27

Family

ID=11838722

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1363690A Pending JPH03220220A (en) 1990-01-25 1990-01-25 Production of phenolic resin and can coating agent

Country Status (1)

Country Link
JP (1) JPH03220220A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06287261A (en) * 1993-04-06 1994-10-11 Kanebo Nsc Ltd Method for purifying novolak resin
JPH06287262A (en) * 1993-04-06 1994-10-11 Kanebo Nsc Ltd Method for purifying novolak resin

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06287261A (en) * 1993-04-06 1994-10-11 Kanebo Nsc Ltd Method for purifying novolak resin
JPH06287262A (en) * 1993-04-06 1994-10-11 Kanebo Nsc Ltd Method for purifying novolak resin

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