JPH0244323B2 - MERAMINNNYOSOJUSHINOSEIZOHOHO - Google Patents

MERAMINNNYOSOJUSHINOSEIZOHOHO

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Publication number
JPH0244323B2
JPH0244323B2 JP21639782A JP21639782A JPH0244323B2 JP H0244323 B2 JPH0244323 B2 JP H0244323B2 JP 21639782 A JP21639782 A JP 21639782A JP 21639782 A JP21639782 A JP 21639782A JP H0244323 B2 JPH0244323 B2 JP H0244323B2
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Japan
Prior art keywords
resin
solution
added
mol
temperature
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
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JP21639782A
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Japanese (ja)
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JPS59108019A (en
Inventor
Tatsuo Ishii
Hideo Ito
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Mitsubishi Chemical Corp
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Nippon Kasei Chemical Co Ltd
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Priority to JP21639782A priority Critical patent/JPH0244323B2/en
Publication of JPS59108019A publication Critical patent/JPS59108019A/en
Publication of JPH0244323B2 publication Critical patent/JPH0244323B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は、放出ホルマリンが少い含浸紙用メラ
ミン−尿素樹脂の製造法に関するものである。 含浸紙は、木目模様その他の模様を印刷した紙
に各種樹脂を含浸乾燥し、これをパーテイクルボ
ード、フラツシユボード、木板等の表面化粧板と
して使用するものである。 上記各種樹脂としては、メラミン樹脂、メラミ
ン−尿素樹脂(以下単にMU樹脂と略記する)あ
るいは尿素樹脂が知られているが、化粧板表面の
耐熱性、耐薬品性等の物理的性質が良好であるた
めMU樹脂が広く利用されて来ている。 従来から、MU樹脂の製造法としては、原料メ
ラミン1モルに対して尿素0.3〜10.0モルであり、
かつホルムアルデヒド1.95〜22.00モルの範囲の
各原料を一度に混合し、アルカリ性物質、たとえ
ば水酸化ナトリウム、水酸化カリウム等を添加し
て加熱縮合を行ない、MU樹脂を製造する方法が
採用されている。 しかしながら、この方法で製造した樹脂では放
出ホルムアルデヒド含有量が高く、得られた化粧
板の品質に今一つ不足するものがあつた。 本発明者らは特定の方法の採用により上記欠点
のない、高品質のMU樹脂が得られることを発見
し本発明を完成した。 すなわち本発明は、 メラミン1.0モル、尿素4.0〜4.5モル及びホルム
アルデヒド5.5〜7.5モルの割合の混合物に2−ジ
メチルまたは2−ジエチルアミノエタノールを添
加することにより該混合物をアルカリ性とし、75
℃〜還流下に保持することにより該混合物を共縮
合させることを特徴とするメラミン−尿素樹脂の
製造法 をその要旨とするものである。 さらに本発明を詳しく説明する。 本発明においてメラミン(以下Mと記す)1モ
ル、尿素(以下Uと記す)4.0〜4.5モル、ホルム
アルデヒド(以下Fと記す)5.5〜7.5モルの割合
で、メラミンと尿素とホルムアルデヒドとを混合
する。 そして、2−ジメチルアミノエタノール又は2
−ジエチルアミノエタノールをMとUとFとの混
合水溶液に添加し、PH10.0〜9.0に調整しMとU
とFとを温度75℃〜環流下で共縮合させる。 この操作は、まずFの水溶液であるホルマリン
を2−ジメチルアミノエタノール又は2−ジエチ
ルアミノエタノールでPH10.0〜9.0に調整し、撹
拌下Mを加えて還流温度に昇温する。後、Uを加
えるが、Uを一度に加えるとUの溶解吸熱のため
反応液温度が70℃以下になり、溶解していたメチ
ロールメラミンが折出するからUは還流下2分割
して加える。 以後80℃で反応を続けるが、共縮合が進行する
につれて、該反応液のPHが徐々に降下するので、
2−ジメチルアミノエタノール又は2−ジエチル
アミノエタノールを添加して該反応液のPHが7.5
より降下しないよう保持する。反応が進行するに
したがつて、反応溶液は5〜20℃の白濁点を示す
ようになり、さらに反応を続けると、水溶液は
1.5〜1.0倍の白濁価を示すようになり、この時点
で溶液を冷却する。 本発明でいう白濁点とは、大量の水の中に反応
物1滴を滴下したとき、まさに白濁を生じるとき
の水の温度をいう。また白濁価とは反応物1容量
部に水を加えて得られた混合液を20℃にした場
合、まさに白濁が生ずるような反応物と水との容
量比倍率という。 このようにして製造して得られたMU樹脂溶液
のPHは、約7.5であるので、含浸紙用MU樹脂溶
液の貯蔵安定性が最も良いPH9.5〜9.0に、2−ジ
メチルアミノエタノール又は2−ジエチルアミノ
エタノール、さらには通常のアルカリ性化合物、
例えば炭酸ナトリウム、トリエチルアミン等で調
整する。 本発明の製造方法により得られたMU樹脂溶液
は、M1モルに対し、Uは4.0〜4.5モル、Fは5.5
〜7.5モルの割合の組成である。このMU樹脂溶
液の遊離ホルムアルデヒド含有量を分析すると、
0.1〜0.3重量%であつた。このMU樹脂溶液を使
用した含浸紙で製造した化粧板の放出ホルムアル
デヒド量は木工板より発生する放出ホルムアルデ
ヒド量と同じで、さらに増加させることはない。 Fのモル数が7.5モルより多いと、得られた
MU樹脂中の遊離ホルムアルデヒドの含有量は
0.8重量%以上となり、このような高い遊離ホル
ムアルデヒド含有量のMU樹脂を使用した化粧板
は、本発明によつて得られたMU樹脂を使用した
化粧板に較べて放出ホルムアルデヒド量が2mg/
以上増加する。 又、Fのモル数が5.5モルより少なければ、M
とUに対してFが不足となり、得られた樹脂から
製造した化粧板の品質は本発明によつて得られた
MU樹脂を使用した化粧板に較べて低下する。 次に本発明において、2−ジメチルアミノエタ
ノール又は2−ジエチルアミノエタノールを触媒
として使用するが、これら以外のアルカリ性触
媒、例えば水酸化ナトリウム、水酸化カリウム、
炭酸ナトリウム、トリエチルアミン、トリエタノ
ールアミン及び炭酸グアニジン等を使用すると、
共縮合反応時間が約30分以内になる。その為、
MU樹脂溶液中の遊離ホルムアルデヒド含有量は
3〜5重量%となり、また、分子量の著しく小さ
いもの及び大きいものが不均一に含有され、反応
終了後数時間以内に白濁するほど貯蔵安定性に乏
しい樹脂溶液が得られた。 これに対して、本発明の2−ジメチルアミノエ
タノール又は2−ジエチルアミノエタノールを使
用すると、反応時間が約100分と長いため、遊離
ホルムアルデヒド含有量は0.1〜0.3重量%にな
り、そしてMU樹脂の大部分がメチロール化共縮
合物となり、樹脂溶液の貯蔵安定期間が温度15〜
25℃で15〜20日と長期間になるMU樹脂溶液が得
られた。ここでいう貯蔵安定期間とは、樹脂溶液
が透明性を失なわず、かつ白濁せず、かつ樹脂溶
液の粘度上昇が製造直後の溶液粘度値の約0.2倍
を越えることがない状態を保つている期間を意味
する。 即ち、本発明はMのモル数よりもUのモル数が
多く、かつFが少ない反応系に弱アルカリ性を示
す2−ジメチルアミノエタノール又は2−ジエチ
ルアミノエタノール触媒を使用すると、均一な分
子量分布の範囲に、M,UおよびFを好ましく共
縮合させていることを示唆するものである。 次に本発明に使用する原料のMおよびUは、特
に精製品を使用する必要はなく、工業規格品で充
分である。又、Fは市販の37〜50重量%のホルマ
リンを使用することができ、又、ホルマリンに含
有されているメタノールおよびギ酸を特に除去し
て使用する必要はない。 さらに本発明によつて得られたMU樹脂溶液
は、含浸紙製造に使用し易い不揮発分50〜60重量
%、粘度約40〜50CP/20℃程度に水とメタノー
ルを留去する。 なお、本発明によつて得られたMU樹脂溶液に
公知の変性剤、例えば、エチレングリコール、ε
−カプロラクタム、トルエンスルホン酸アミド、
チオ尿素、ジシアンジアミド、砂糖、及びスルフ
アミン酸ナトリウム、水溶性ナイロン等を添加し
て化粧板表面の光沢性、熱安定性、緻密性、弾性
等をより改良し品質を高めることができる。な
お、変性剤の添加量は本発明の場合MとUに対す
るFのモル数が低いため、MとUとFとの合計量
に対して1〜5重量%の範囲が好ましい。 次に、本発明を実施例によつてさらに具体的に
説明するが、本発明は以下の実施例に限定される
ものではない。なお実施例に%とあるのは重量%
を示す。 実施例 1 反応器に37%ホルマリン1520g(18.7モル)を
仕込み、2−ジメチルアミノエタノール(試薬一
級)6.5mlを加えPH10.0に調整した。これに撹拌
下メラミン400g(3.2モル)を加えて還流温度
(96℃)に昇温した。還流開始より5分後及び10
分後に、それぞれ400g(6.7モル)の尿素を加え
て、以後80℃に降温し、同温度を保持してホルム
アルデヒド、メラミン、尿素を反応させた。還流
開始より75分後に反応液は15℃の白濁点を示し、
110分後に白濁価1.2倍に到達したので、減圧下メ
タノールと水の一部を留去しながら反応液を急冷
却した。 この樹脂溶液のPHは7.5であつたので、25%炭
酸ナトリウム水溶液4mlを加えてPH9.5に調整し
た。得られた樹脂溶液の粘度は40.5CP/20℃で
あり、不揮発分は55.5%であつた。 実施例 2 実施例1と同様にメラミンと尿素とホルムアル
デヒドとを反応させた。ただし、変性剤としてエ
チレングリコール40gとε−カプロラクタム30g
とを反応前に加えた。得られた樹脂溶液は粘度
45.0CP/20℃であり、不揮発分は56.3%であつ
た。 実施例 3 反応器に30%ホルマリン1800g(22.2モル)を
仕込み、2−ジエチルアミノエタノール(試薬一
級)7.5mlを加えたPH95に調整した。これに撹拌
下メラミン375g(3.0モル)を加え還流温度に昇
温した。還流開始より5分後及び10分後にそれぞ
れ400g(6.7モル)の尿素を加えて、以後80℃に
降温し、同温度を保持して反応させた。還流開始
より65分後の5℃の白濁点を示した時点で、2−
ジエチルアミノエタノール1.5mlを追加し続いて
反応させた。還流開始より100分後白濁価1.3倍に
到達したので減圧下メタノールと水の一部を留去
しながら、反応液を急冷却した。 この樹脂溶液のPHは7.7であつたので、トリエ
チルアミン2mlを加えてPH9.0に調整した。得ら
れた樹脂溶液の粘度は48.0CP/20℃であり、不
揮発分は60.2%であつた。 比較例1 (本発明でFが多い場合) 反応器に37%ホルマリン1950g(24.1モル)を
仕込み、2−ジメチルアミノエタノール8.2mlを
加えPH9.8に調整した。これに撹拌下メラミン375
g(3.0モル)を加え還流温度に昇温した。還流
開始より5分後及び10分後に、それぞれ375g
(6.3モル)の尿素を加えて、以後80℃に降温し、
同温度を保持して反応させた。還流開始より55分
後に5℃の白濁点を示し、100分後白濁価1.2倍に
到達したので、減圧下メタノールと水の一部を留
去しながら急冷却した。 この樹脂溶液のPHは7.5であつたので25%炭酸
ナトリウム水溶液4mlを加えてPH9.4に調整した。
得られた樹脂溶液の粘度は42CP/20℃であり、
不揮発分は54.5%であつた。 比較例2 (本発明以外の触媒の場合) 反応器に37%ホルマリン1520g(18.7モル)を
仕込み、さらに30%水酸化ナトリウム水溶液1.2
mlを加えPH9.5に調整した。これに撹拌下メラミ
ン400g(3.2モル)を加えて還流温度に昇温し
た。還流開始より5分後及び10分後に、それぞれ
400g(6.7モル)の尿素を加えて、以後80℃に降
温し、同温度を保持して反応させた。還流開始よ
り20分後に20℃の白濁点を示し、30分後に白濁価
10倍に到達したので、減圧下メタノールと水の一
部を留去しながら急冷却した。 この樹脂溶液のPHは7.0であつたので、25%炭
酸ナトリウム水溶液4.5mlを加えてPH9.0に調整し
た。得られた樹脂溶液の粘度は23.0CP/20℃で
あり、不揮発分は52.0%であつた。 参考例1 (従来法の場合) 反応器に37%ホルマリン1490g(18.4モル)と
メタノール56gとを仕込み、さらに30%水酸化ナ
トリウム水溶液4.0mlを加えPH11.0に調整した。
これに撹拌下メラミン504g(4モル)と尿素240
g(4モル)を加え85℃に昇温した。同温度を保
持し反応させた。85℃から2時間15分後に20℃の
白濁点を示し、2時間40分後に白濁価2.5倍に到
達したので、減圧にしてメタノール、水を留去し
急冷却した。 この樹脂溶液のPHは7.8であつたので25%炭酸
ナトリウム水溶液4mlを加えてPH9.2に調整した。
得られた樹脂溶液の粘度は35.0CP/20℃であり、
不揮発分は50.5%であつた。 実施例1〜3、比較例1〜2、参考例1で得ら
れMU樹脂の貯蔵安定性試験、遊離ホルムアルデ
ヒド含有量分析、化粧板を製造しての放出ホルム
アルデヒド試験及び化粧表面の品質試験を下記の
ように行ない、結果を第1表に示した。 (1) 貯蔵安定性試験 樹脂を15〜25℃の室温に貯蔵し、白濁又は粘度
が1.2倍に上昇するまでの日数を測定した。 (2) 遊離ホルムアルデヒド含有量分析 JIS K−6801の塩化アンモニウム法により分析
した。 (3) 化粧板の製造方法 樹脂1Kgに硬化剤として25重量%パラトルエン
スルホン酸水溶液15〜25g、離形剤としてステア
リン酸ナトリウム(試薬一級)0.1g及び浸透剤
としてポリオキシエチレンノニルフエノールエー
テルであるノニポール95(商品名、三洋化成製)
2gを加えて撹拌混合して含浸樹脂溶液とした。
この樹脂溶液をチタンホワイトを施した80g/m2
のα−セルローズ系白色原紙に含浸し、温度125
℃で乾燥して含浸紙を得た。 含浸紙は200g/m2で、揮発分5〜6%であつ
た。なお揮発分は、含浸紙を160℃で5分間再乾
燥させたときの重量損失である。 この含浸紙を厚さ15mmのパーテクルボード台板
の表裏面に組込み、アスベストクツシヨン入り梨
肌研磨仕上げのアルミ板をコール板としたホツト
プレスで160℃、20Kg/cm2、3分間の条件で加熱
プレスして化粧板を製造した。加熱プレス後の戻
し冷却プレスは行なわなかつた。 (4) 放出ホルムアルデヒドの測定 JIS A5908のアセチルアセトン法により放出ホ
ルムアルデヒド量を測定した。なおパーテクルボ
ード台板は尿素樹脂を接着剤として使用し製造さ
れたものである。 (5) 化粧表面の品質試験 a 外観:化粧表面の状態、光沢度を肉眼で判 定した。 b 耐酸性:0.2規定塩酸の化粧表面に対する 24時間での作用度を判定した。 c 耐熱性:DIN53799による70℃、 20時間加熱で亀裂を生じたかど うかを判定した。 d 耐水性:DIN53799による水蒸気試験 によつて判定した。 e 汚染性:黒色靴墨を塗布した後、拭取り密 封度を判定した。 a〜eの判定は1〜6のスケールで、1は極め
て良好、かつ6は完全に不良を示す。
The present invention relates to a method for producing a melamine-urea resin for impregnated paper that releases less formalin. Impregnated paper is paper printed with woodgrain patterns or other patterns, impregnated with various resins and dried, and used as a decorative surface board for particle boards, flash boards, wood boards, etc. Melamine resins, melamine-urea resins (hereinafter simply referred to as MU resins), and urea resins are known as the above-mentioned resins, but these resins have good physical properties such as heat resistance and chemical resistance on the decorative board surface. Therefore, MU resin has been widely used. Traditionally, the manufacturing method for MU resin has been to use 0.3 to 10.0 moles of urea per 1 mole of raw material melamine.
A method has been adopted in which MU resin is produced by mixing raw materials ranging from 1.95 to 22.00 moles of formaldehyde at once, adding an alkaline substance such as sodium hydroxide, potassium hydroxide, etc., and carrying out thermal condensation. However, the resin produced by this method had a high content of released formaldehyde, and the quality of the decorative laminate obtained was somewhat lacking. The present inventors have completed the present invention by discovering that a high-quality MU resin free from the above-mentioned drawbacks can be obtained by employing a specific method. That is, the present invention makes the mixture alkaline by adding 2-dimethyl or 2-diethylaminoethanol to a mixture of 1.0 mole of melamine, 4.0 to 4.5 moles of urea, and 5.5 to 7.5 moles of formaldehyde, and
The gist of the present invention is a method for producing a melamine-urea resin, which is characterized in that the mixture is co-condensed by maintaining the mixture at reflux. The present invention will be further explained in detail. In the present invention, melamine, urea, and formaldehyde are mixed in a ratio of 1 mole of melamine (hereinafter referred to as M), 4.0 to 4.5 moles of urea (hereinafter referred to as U), and 5.5 to 7.5 moles of formaldehyde (hereinafter referred to as F). and 2-dimethylaminoethanol or 2-dimethylaminoethanol or 2-dimethylaminoethanol
- Add diethylaminoethanol to a mixed aqueous solution of M, U, and F, adjust the pH to 10.0 to 9.0, and then add M and U.
and F are co-condensed at a temperature of 75° C. to reflux. In this operation, first, the pH of formalin, which is an aqueous solution of F, is adjusted to 10.0 to 9.0 with 2-dimethylaminoethanol or 2-diethylaminoethanol, and M is added with stirring, and the temperature is raised to reflux temperature. After that, U is added, but if U is added all at once, the temperature of the reaction solution will drop to below 70°C due to endothermic dissolution of U, and the dissolved methylolmelamine will precipitate out, so U is added in two portions under reflux. Thereafter, the reaction was continued at 80°C, but as the cocondensation progressed, the pH of the reaction solution gradually decreased.
Add 2-dimethylaminoethanol or 2-diethylaminoethanol until the pH of the reaction solution is 7.5.
Keep it from falling further. As the reaction progresses, the reaction solution begins to show a cloudy point of 5 to 20℃, and as the reaction continues, the aqueous solution becomes
The solution will show a cloudiness value of 1.5 to 1.0 times, at which point the solution is cooled. The clouding point in the present invention refers to the temperature at which water becomes cloudy when one drop of a reactant is dropped into a large amount of water. In addition, the cloudiness value is the volume ratio of the reactant to water at which cloudiness occurs when the mixture obtained by adding water to 1 volume part of the reactant is heated to 20°C. The pH of the MU resin solution produced in this way is about 7.5, so the pH of the MU resin solution for impregnated paper is adjusted to 9.5 to 9.0, which has the best storage stability. - diethylaminoethanol, as well as the usual alkaline compounds,
For example, adjust with sodium carbonate, triethylamine, etc. The MU resin solution obtained by the production method of the present invention contains 4.0 to 4.5 mol of U and 5.5 mol of F per 1 mol of M.
The composition has a proportion of ~7.5 moles. Analysis of the free formaldehyde content of this MU resin solution revealed that
It was 0.1-0.3% by weight. The amount of formaldehyde released from the decorative board made from paper impregnated with this MU resin solution is the same as the amount of formaldehyde released from wood boards, and does not increase further. When the number of moles of F is more than 7.5 moles, the obtained
The content of free formaldehyde in MU resin is
A decorative laminate using MU resin with such a high free formaldehyde content of 0.8% by weight or more has a release amount of formaldehyde of 2 mg/ml compared to a decorative laminate using MU resin obtained by the present invention.
or more. Also, if the number of moles of F is less than 5.5 moles, M
The quality of the decorative board produced from the resulting resin was lower than that obtained by the present invention.
This is lower than that of decorative boards using MU resin. Next, in the present invention, 2-dimethylaminoethanol or 2-diethylaminoethanol is used as a catalyst, but other alkaline catalysts such as sodium hydroxide, potassium hydroxide,
When using sodium carbonate, triethylamine, triethanolamine, guanidine carbonate, etc.
The co-condensation reaction time is within about 30 minutes. For that reason,
The free formaldehyde content in the MU resin solution is 3 to 5% by weight, and compounds with extremely small and large molecular weights are unevenly contained, making the resin so poor in storage stability that it becomes cloudy within a few hours after the completion of the reaction. A solution was obtained. On the other hand, when 2-dimethylaminoethanol or 2-diethylaminoethanol of the present invention is used, the reaction time is as long as about 100 minutes, the free formaldehyde content is 0.1-0.3% by weight, and the MU resin is large. part becomes a methylolated cocondensate, and the storage stability of the resin solution is at a temperature of 15 to
A MU resin solution that lasted for a long time at 25°C for 15-20 days was obtained. The storage stability period referred to here is the period in which the resin solution does not lose its transparency, does not become cloudy, and the viscosity of the resin solution does not increase by more than about 0.2 times the viscosity of the solution immediately after production. It means the period of time. That is, in the present invention, when a weakly alkaline 2-dimethylaminoethanol or 2-diethylaminoethanol catalyst is used in a reaction system in which the number of moles of U is larger than the number of moles of M and the amount of F is small, a uniform molecular weight distribution range can be obtained. This suggests that M, U and F are preferably co-condensed. Next, as the raw materials M and U used in the present invention, it is not necessary to particularly use purified products, and industrial standard products are sufficient. Furthermore, commercially available 37 to 50% by weight formalin can be used as F, and it is not necessary to specifically remove methanol and formic acid contained in formalin. Furthermore, water and methanol are distilled off from the MU resin solution obtained according to the present invention to a nonvolatile content of 50 to 60% by weight and a viscosity of about 40 to 50 CP/20° C., which can be easily used in the production of impregnated paper. Note that known modifiers such as ethylene glycol, ε
- caprolactam, toluenesulfonamide,
By adding thiourea, dicyandiamide, sugar, sodium sulfamate, water-soluble nylon, etc., the gloss, thermal stability, denseness, elasticity, etc. of the decorative board surface can be further improved and the quality can be enhanced. In addition, in the case of the present invention, since the number of moles of F is low relative to M and U, the amount of the modifier added is preferably in the range of 1 to 5% by weight based on the total amount of M, U, and F. Next, the present invention will be explained in more detail with reference to examples, but the present invention is not limited to the following examples. In addition, % in the examples is weight %.
shows. Example 1 A reactor was charged with 1520 g (18.7 mol) of 37% formalin, and 6.5 ml of 2-dimethylaminoethanol (first class reagent) was added to adjust the pH to 10.0. To this was added 400 g (3.2 mol) of melamine with stirring, and the temperature was raised to reflux temperature (96°C). 5 minutes after the start of reflux and 10
After a few minutes, 400 g (6.7 mol) of urea was added to each, and the temperature was then lowered to 80°C, and the same temperature was maintained to allow formaldehyde, melamine, and urea to react. 75 minutes after the start of reflux, the reaction solution showed a cloudy point of 15°C.
After 110 minutes, the cloudiness value reached 1.2 times, so the reaction solution was rapidly cooled while part of methanol and water was distilled off under reduced pressure. Since the pH of this resin solution was 7.5, 4 ml of a 25% aqueous sodium carbonate solution was added to adjust the pH to 9.5. The resulting resin solution had a viscosity of 40.5CP/20°C and a nonvolatile content of 55.5%. Example 2 Melamine, urea, and formaldehyde were reacted in the same manner as in Example 1. However, 40 g of ethylene glycol and 30 g of ε-caprolactam are used as modifiers.
was added before the reaction. The resulting resin solution has a viscosity of
The temperature was 45.0CP/20°C, and the nonvolatile content was 56.3%. Example 3 A reactor was charged with 1800 g (22.2 mol) of 30% formalin, and the pH was adjusted to 95 by adding 7.5 ml of 2-diethylaminoethanol (first grade reagent). To this was added 375 g (3.0 mol) of melamine with stirring, and the temperature was raised to reflux temperature. 400 g (6.7 mol) of urea was added 5 minutes and 10 minutes after the start of reflux, and the temperature was then lowered to 80° C., and the reaction was carried out while maintaining the same temperature. 2-
1.5 ml of diethylaminoethanol was added and the reaction was continued. 100 minutes after the start of reflux, the cloudiness value reached 1.3 times, so the reaction solution was rapidly cooled while methanol and part of the water were distilled off under reduced pressure. Since the pH of this resin solution was 7.7, 2 ml of triethylamine was added to adjust the pH to 9.0. The resulting resin solution had a viscosity of 48.0CP/20°C and a nonvolatile content of 60.2%. Comparative Example 1 (In the case of a large amount of F in the present invention) 1950 g (24.1 mol) of 37% formalin was charged into a reactor, and 8.2 ml of 2-dimethylaminoethanol was added to adjust the pH to 9.8. Melamine 375 under stirring
g (3.0 mol) was added thereto, and the temperature was raised to reflux temperature. 375g each after 5 minutes and 10 minutes from the start of reflux.
(6.3 mol) of urea was added, and the temperature was then lowered to 80°C.
The reaction was carried out while maintaining the same temperature. 55 minutes after the start of reflux, a white cloudiness point of 5°C was exhibited, and after 100 minutes, the white cloudiness value reached 1.2 times, so the mixture was rapidly cooled while distilling off part of methanol and water under reduced pressure. Since the pH of this resin solution was 7.5, 4 ml of a 25% aqueous sodium carbonate solution was added to adjust the pH to 9.4.
The viscosity of the obtained resin solution was 42CP/20℃,
The non-volatile content was 54.5%. Comparative Example 2 (In the case of a catalyst other than the present invention) 1520 g (18.7 mol) of 37% formalin was charged into a reactor, and 1.2 g of a 30% aqueous sodium hydroxide solution was added.
ml was added to adjust the pH to 9.5. To this was added 400 g (3.2 mol) of melamine with stirring, and the temperature was raised to reflux temperature. 5 minutes and 10 minutes after the start of reflux, respectively.
After adding 400 g (6.7 mol) of urea, the temperature was lowered to 80° C., and the reaction was carried out while maintaining the same temperature. 20 minutes after the start of reflux, it shows a cloudy point of 20℃, and after 30 minutes, it shows a cloudy value.
When the volume reached 10 times, it was rapidly cooled while distilling off part of the methanol and water under reduced pressure. Since the pH of this resin solution was 7.0, 4.5 ml of a 25% aqueous sodium carbonate solution was added to adjust the pH to 9.0. The resulting resin solution had a viscosity of 23.0CP/20°C and a nonvolatile content of 52.0%. Reference Example 1 (Conventional method) A reactor was charged with 1490 g (18.4 mol) of 37% formalin and 56 g of methanol, and 4.0 ml of a 30% aqueous sodium hydroxide solution was added to adjust the pH to 11.0.
Add to this 504 g (4 mol) of melamine and 240 urea while stirring.
g (4 mol) was added thereto, and the temperature was raised to 85°C. The reaction was carried out while maintaining the same temperature. After 2 hours and 15 minutes from 85°C, it showed a white cloudiness point of 20°C, and after 2 hours and 40 minutes, the white cloudiness value reached 2.5 times, so methanol and water were distilled off under reduced pressure, and the mixture was rapidly cooled. Since the pH of this resin solution was 7.8, 4 ml of a 25% aqueous sodium carbonate solution was added to adjust the pH to 9.2.
The viscosity of the obtained resin solution was 35.0CP/20℃,
The non-volatile content was 50.5%. The storage stability test, free formaldehyde content analysis, release formaldehyde test by producing decorative laminates, and decorative surface quality test of the MU resins obtained in Examples 1 to 3, Comparative Examples 1 to 2, and Reference Example 1 are as follows. The results are shown in Table 1. (1) Storage stability test The resin was stored at room temperature of 15 to 25°C, and the number of days until it became cloudy or the viscosity increased by 1.2 times was measured. (2) Free formaldehyde content analysis Analyzed by the ammonium chloride method of JIS K-6801. (3) Manufacturing method of decorative board 1 kg of resin is mixed with 15 to 25 g of a 25% by weight aqueous paratoluenesulfonic acid solution as a hardening agent, 0.1 g of sodium stearate (first class reagent) as a mold release agent, and polyoxyethylene nonylphenol ether as a penetrating agent. Aru Nonipole 95 (product name, manufactured by Sanyo Chemical)
2 g was added and mixed with stirring to obtain an impregnated resin solution.
This resin solution was coated with titanium white at 80g/ m2.
impregnated into α-cellulose white base paper and heated to a temperature of 125
The impregnated paper was obtained by drying at ℃. The impregnated paper weighed 200 g/m 2 and had a volatile content of 5-6%. The volatile content is the weight loss when the impregnated paper is re-dried at 160°C for 5 minutes. This impregnated paper was incorporated into the front and back surfaces of a particle board base plate with a thickness of 15 mm, and a hot press using an aluminum plate with a pear-polished finish containing asbestos cushion as a caul plate was used at 160°C, 20 kg/cm 2 for 3 minutes. A decorative board was manufactured by hot pressing. Return cooling press after hot pressing was not performed. (4) Measurement of released formaldehyde The amount of released formaldehyde was measured by the acetylacetone method of JIS A5908. The particle board base plate is manufactured using urea resin as an adhesive. (5) Quality test of decorative surface a. Appearance: The condition and gloss of the decorative surface were judged with the naked eye. b Acid resistance: The degree of action of 0.2N hydrochloric acid on the decorative surface over 24 hours was determined. c. Heat resistance: Judgment was made as to whether or not cracks occurred when heated at 70°C for 20 hours according to DIN53799. d Water resistance: Determined by water vapor test according to DIN53799. e Stainability: After applying black shoe polish, the degree of sealing was determined by wiping. The ratings a-e are on a scale of 1-6, with 1 being extremely good and 6 being completely bad.

【表】【table】

【表】 第1表の結果で、本発明によるMU樹脂は、パ
ーテクルボード台板よりの放出ホルムアルデヒド
量と同じであり増加させなかつた。 又、本発明のようにM含量よりU含量が多い
MU樹脂で製造された化粧板の表面品質評価は、
一般にスケール3以下であれば表裏面の被覆に適
当とされており、本発明により得られた化粧板の
品質はこれを満足することも確められた。 さらに、MU樹脂溶液の貯蔵安定性も15日以上
であり、工業的実施に支障はきたさないものであ
る。
Table 1 shows that the MU resin according to the present invention did not increase the amount of formaldehyde released from the particle board base plate. Also, as in the present invention, the U content is higher than the M content.
Surface quality evaluation of decorative board manufactured with MU resin is as follows:
Generally, scale 3 or less is considered suitable for coating the front and back surfaces, and it was confirmed that the quality of the decorative board obtained by the present invention satisfies this requirement. Furthermore, the storage stability of the MU resin solution is 15 days or more, and there is no problem in industrial implementation.

Claims (1)

【特許請求の範囲】[Claims] 1 メラミン1.0モル、尿素4.0〜4.5モル及びホル
ムアルデヒド5.5〜7.5モルの割合の混合物に2−
ジメチルまたは2−ジエチルアミノエタノールを
添加することにより該混合物をアルカリ性とし、
75℃〜還流下に保持することにより該混合物を共
縮合させることを特徴とするメラミン−尿素樹脂
の製造方法。
1. 2- to a mixture of 1.0 mol of melamine, 4.0-4.5 mol of urea and 5.5-7.5 mol of formaldehyde
making the mixture alkaline by adding dimethyl or 2-diethylaminoethanol;
A method for producing a melamine-urea resin, which comprises cocondensing the mixture by maintaining the mixture at 75°C or higher under reflux.
JP21639782A 1982-12-10 1982-12-10 MERAMINNNYOSOJUSHINOSEIZOHOHO Expired - Lifetime JPH0244323B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP21639782A JPH0244323B2 (en) 1982-12-10 1982-12-10 MERAMINNNYOSOJUSHINOSEIZOHOHO

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP21639782A JPH0244323B2 (en) 1982-12-10 1982-12-10 MERAMINNNYOSOJUSHINOSEIZOHOHO

Publications (2)

Publication Number Publication Date
JPS59108019A JPS59108019A (en) 1984-06-22
JPH0244323B2 true JPH0244323B2 (en) 1990-10-03

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Country Link
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012241204A (en) * 2011-05-16 2012-12-10 Nippon Steel Engineering Co Ltd Ceramic burner for hot blast stove

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