JPS5824444B2 - Manufacturing method for finely colored hardened resin with excellent solvent resistance and heat resistance - Google Patents
Manufacturing method for finely colored hardened resin with excellent solvent resistance and heat resistanceInfo
- Publication number
- JPS5824444B2 JPS5824444B2 JP54149515A JP14951579A JPS5824444B2 JP S5824444 B2 JPS5824444 B2 JP S5824444B2 JP 54149515 A JP54149515 A JP 54149515A JP 14951579 A JP14951579 A JP 14951579A JP S5824444 B2 JPS5824444 B2 JP S5824444B2
- Authority
- JP
- Japan
- Prior art keywords
- resin
- soluble
- dye
- added
- benzoguanamine
- 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
Links
Landscapes
- Processes Of Treating Macromolecular Substances (AREA)
- Compositions Of Macromolecular Compounds (AREA)
- Phenolic Resins Or Amino Resins (AREA)
Description
【発明の詳細な説明】
本発明は、耐溶剤性、耐熱性に優れた微細着色樹脂の製
法に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing a finely colored resin having excellent solvent resistance and heat resistance.
詳しくはベンゾグアナミン、パラトルエンスルホンアミ
ドおよびホルムアルデヒドから導かれ、染料で染色され
た可溶可融性樹脂を乳化状態を保ちながら硬化触媒の存
在下に硬化せしめることにより得られる微細着色硬化樹
脂の懸濁物から硬化樹脂を分離乾燥することからなる耐
溶剤性、耐熱性に優れた微細着色硬化樹脂の製法に関す
るものである。Specifically, it is a suspension of a finely colored cured resin obtained by curing a dye-dyed soluble fusible resin derived from benzoguanamine, paratoluenesulfonamide and formaldehyde in the presence of a curing catalyst while maintaining an emulsified state. This invention relates to a method for producing a finely colored cured resin with excellent solvent resistance and heat resistance, which involves separating and drying the cured resin from a material.
染料で着色された種々の樹脂微粉末が顔料として応用さ
れている。Various resin fine powders colored with dyes are used as pigments.
使用される染料としては、塩基性染料、酸性染料、油溶
性染料等多岐にわたっているが、染料のもつ鮮明さを顔
料に応用すべく螢光染料を用いることが多い。A wide variety of dyes are used, including basic dyes, acidic dyes, and oil-soluble dyes, but fluorescent dyes are often used in order to apply the brightness of dyes to pigments.
また、樹脂としてはポリ塩化ビニル、ポリアミド、パラ
トルエンスルホンアミド・ホルムアルデヒド樹脂等の熱
可塑性樹脂とアミン樹脂等の熱硬化性樹脂に大別される
。Furthermore, resins are broadly classified into thermoplastic resins such as polyvinyl chloride, polyamide, and paratoluenesulfonamide/formaldehyde resins, and thermosetting resins such as amine resins.
微細着色樹脂の鮮明さをはじめとする種々の物性は、染
料と樹脂の組み合わせにより決定されるが、樹脂に対す
る染料の染着機構は複雑であり、その最適な組み合わせ
を予測することは困難である。The various physical properties of finely colored resin, including its sharpness, are determined by the combination of dye and resin, but the dye dyeing mechanism for resin is complex, and it is difficult to predict the optimal combination. .
染料が樹脂中で鮮明な発色をするためには、染料が樹脂
に均一に溶解することが必要であると考えられている。It is believed that in order for a dye to develop a clear color in a resin, it is necessary for the dye to be uniformly dissolved in the resin.
特に螢光染料の場合、螢光染料が樹脂中で会合したりあ
るいは螢光染料が樹脂中の特定の部分に局在している場
合には、螢光染料の発色は著しく損われ、またそれと共
に耐光性も低下することが知られている。Particularly in the case of fluorescent dyes, if the fluorescent dyes are associated in the resin or if the fluorescent dyes are localized in specific parts of the resin, the color development of the fluorescent dyes will be significantly impaired; It is known that light resistance also decreases.
いわゆる樹脂等の媒体に螢光染料を多量に添加した場合
にみられる濃度消光現象である。This is a so-called concentration quenching phenomenon that occurs when a large amount of fluorescent dye is added to a medium such as a resin.
したがって、染料の溶解性が高い熱可塑性樹脂を用いれ
ば、染料の発色は比較的良好でかつ粉砕によって容易に
微粉末を得ることができるという利点がある反面、耐溶
剤性、耐熱性の良好なものを得ることはできない。Therefore, if a thermoplastic resin with high dye solubility is used, the color development of the dye will be relatively good and fine powder can be easily obtained by crushing, but on the other hand, it will have good solvent resistance and heat resistance. You can't get anything.
一方、熱硬化性樹脂を用いれば、耐溶剤性、耐熱性が優
れている反面、熱硬化性樹脂は熱硬化処理後染料の溶解
性が低面、熱硬化性樹脂は熱硬化処理後染料の溶解性が
低下するため染料の発色を損うことが多(、またその粉
砕による微粉化は非常に困難である。On the other hand, if a thermosetting resin is used, it has excellent solvent resistance and heat resistance, but on the other hand, the solubility of the dye after the thermosetting process is low, and the thermosetting resin has a low solubility of the dye after the thermosetting process. Because the solubility decreases, the color development of the dye is often impaired (and it is extremely difficult to pulverize it into a fine powder).
本発明者らは、染料により着色されたベンゾグアナミン
系可溶可融性樹脂の乳化物に硬化触媒を加え、乳化状態
を保ちながら硬化反応を進め樹脂を不溶不融状態に至ら
しめることKより得られる微細着色硬化樹脂の懸濁物か
ら硬化樹脂を分離乾燥する微細着色硬化樹脂の製法を見
い出し、先に特許出願した。The present inventors added a curing catalyst to an emulsion of benzoguanamine-based soluble and fusible resin colored with a dye, and proceeded with the curing reaction while maintaining the emulsified state to bring the resin into an insoluble and infusible state. We discovered a method for producing finely colored cured resin by separating and drying the cured resin from a suspension of finely colored cured resin, and filed a patent application earlier.
本発明者らによる上記の如き方法で得られる微細着色硬
化樹脂は、熱硬化性樹脂からなるにもかかわらず比較的
多い染料使用量如おいても他の熱硬化性樹脂にみられな
い非常に鮮明な発色を呈するものであるが、特に螢光染
料を用いる場合には濃度消光現象の発現により螢光染料
の樹脂への使用量を十分に多くすることが困難であった
。Although the finely colored cured resin obtained by the method described above by the present inventors is made of a thermosetting resin, it has a very high level of color that is not seen in other thermosetting resins, even when a relatively large amount of dye is used. Although it exhibits vivid color development, it has been difficult to increase the amount of fluorescent dye used in the resin, particularly when using a fluorescent dye, due to the occurrence of concentration quenching phenomenon.
また、十分に細か(かつ安定な乳化物を得るべき該ベン
ゾグアナミン系可溶可融性樹脂の合成にあたっては、長
時間を要し、酸触媒の使用により樹脂化反応を促進させ
ることも可能であるが、樹脂化反応速度の制御は非常に
困難であった。In addition, it takes a long time to synthesize the benzoguanamine-based soluble fusible resin to obtain a sufficiently fine (and stable) emulsion, and it is also possible to accelerate the resin formation reaction by using an acid catalyst. However, it has been extremely difficult to control the resin formation reaction rate.
本発明者らは、上記の如き困難を克服しベンゾグアナミ
ン系樹脂の耐溶剤性、耐熱性等優れた特徴を保持しなが
ら微細着色硬化樹脂にさらに鮮明な発色をせしめ、さら
には樹脂化反応時間を短縮せしめる方法について研究し
た結果、ベンゾグアナミン、パラトルエンスルホンアミ
ドおよびホルムアルデヒドから導かれた可溶可融性樹脂
を応用することにより、微細着色硬化樹脂にさらに優れ
た鮮明さを付与し、また可溶可融性樹脂の樹脂化反応の
促進ならびにその制御を容易にし、さらには螢光染料を
用いる場合螢光染料の樹脂への使用量の増大を可能なら
しめてより優れた耐光性を付与できることを見い出し本
発明を完成させたものである。The inventors of the present invention have overcome the above-mentioned difficulties, maintained the excellent characteristics of benzoguanamine-based resins such as solvent resistance and heat resistance, made finely colored cured resins more vividly colored, and further improved the resinization reaction time. As a result of research on methods for shortening, the application of soluble fusible resins derived from benzoguanamine, para-toluenesulfonamide and formaldehyde has provided better sharpness to finely pigmented cured resins, and also soluble soluble resins. This book discovered that it is possible to promote and easily control the resinization reaction of a fusible resin, and further, when using a fluorescent dye, it is possible to increase the amount of fluorescent dye used in the resin, thereby imparting better light resistance. It is a completed invention.
本発明は、ベンゾグアナミン99〜65重量部とパラト
ルエンスルホンアミド1〜35重量部の混合物とホルム
アルデヒドを該混合物1モルに対して1.2〜3.5モ
ルの割合で、水媒体中で、反応させて得られる可溶可融
性樹脂を染料で染色し保護コロイドを用いて乳化せしめ
た後、硬化触媒を加えて乳化状態を保ちながら硬化反応
を進め樹脂を不溶不融状態に至らしめ、得られる微細着
色硬化樹脂の懸濁物から硬化樹脂を分離乾燥することを
特徴とするものである。The present invention involves reacting a mixture of 99 to 65 parts by weight of benzoguanamine and 1 to 35 parts by weight of paratoluenesulfonamide with formaldehyde in an aqueous medium at a ratio of 1.2 to 3.5 mol per 1 mol of the mixture. After dyeing the resulting soluble resin with a dye and emulsifying it with a protective colloid, a curing catalyst is added to proceed with the curing reaction while maintaining the emulsified state, bringing the resin to an insoluble and infusible state. This method is characterized by separating and drying the cured resin from a suspension of finely colored cured resin.
尚、本発明における可溶可融性樹脂は、疎水化しており
油中水滴型乳化物に近い状態となっており、アセトン、
ジオキサン、メタノールなどの有機溶媒に対して可溶で
あるが、水に対して実質不溶の樹脂である。The soluble resin in the present invention has been made hydrophobic and is in a state similar to a water-in-oil emulsion.
It is a resin that is soluble in organic solvents such as dioxane and methanol, but substantially insoluble in water.
従来、ハラトルエンスルホンアミド・ホルムアルデヒド
樹脂と熱硬化性アミノ樹脂の共縮合物を用いて微細着色
樹脂を得る試みもなされているが、このような従来公知
の微細着色樹脂に耐溶剤性、耐熱性を付与するためには
、熱硬化性アミン樹脂の割合を増大する必要があり、そ
の結果粉砕による微粉化が非常に困難となり十分に細か
い微細着色樹脂を得ることは困難であった。Conventionally, attempts have been made to obtain finely colored resins using cocondensates of halatoluenesulfonamide/formaldehyde resins and thermosetting amino resins, but these conventionally known finely colored resins have poor solvent resistance and heat resistance. In order to impart this, it is necessary to increase the proportion of the thermosetting amine resin, and as a result, it is extremely difficult to pulverize the resin by pulverization, making it difficult to obtain a sufficiently fine, finely colored resin.
したがって粉砕による微粉化を容易ならしめるためには
耐溶剤性、耐熱性を犠牲にせざるを得ないのが現状であ
る。Therefore, in order to facilitate pulverization by pulverization, it is currently necessary to sacrifice solvent resistance and heat resistance.
本発明は、ベンゾグアナミン、パラトルエンスルホンア
ミドおよびホルムアルデヒドから導かれた可溶可融性樹
脂の乳化物を経由することによって、上記の如き問題点
を一挙に克服し、諸物性に均衡のとれた微細着色硬化樹
脂を与えるものである。The present invention overcomes the above problems at once by using an emulsion of a soluble resin derived from benzoguanamine, paratoluenesulfonamide, and formaldehyde, and provides a microstructure with balanced physical properties. It provides a colored cured resin.
即ち、本発明によって得られる微細着色硬化樹脂は、耐
溶剤性、耐熱性等のベンゾグアナミン系樹脂の優れた特
徴を何ら損うことなくより鮮明な発色を示し、特に螢光
染料を用いた場合、濃度消光現象の発現なく螢光染料の
樹脂への使用量を増大させることが可能となり、耐光性
の改善も顕著なものである。That is, the finely colored cured resin obtained by the present invention exhibits more vivid coloring without impairing the excellent characteristics of benzoguanamine resins such as solvent resistance and heat resistance, and particularly when fluorescent dye is used, It becomes possible to increase the amount of fluorescent dye used in the resin without causing the concentration quenching phenomenon, and the light resistance is also significantly improved.
本発明によって発現する耐溶剤性、耐熱性等の優れた性
質は、まさにベンゾグアナミン・ホルムアルデヒド樹脂
等の熱硬化性樹脂固有のものである。The excellent properties such as solvent resistance and heat resistance developed by the present invention are unique to thermosetting resins such as benzoguanamine formaldehyde resin.
また、螢光染料を用いた場合本発明によって得られる螢
光顔料の優れた螢光の鮮明さ、耐光性は、パラトルエン
スルホンアミド・ホルムアルデヒド樹脂の螢光染料を固
溶体として非常に安定に保持し得る性質に基づ(もので
、本発明における可溶可融性樹脂が、その不溶不融化の
後も螢光染料の溶解能を低下することなく螢光染料を硬
化樹脂中に均一に保持するために発現するものである。In addition, when a fluorescent dye is used, the excellent clarity of fluorescence and light resistance of the fluorescent pigment obtained by the present invention are due to the extremely stable retention of the fluorescent dye in the paratoluenesulfonamide/formaldehyde resin as a solid solution. Based on the properties obtained, the soluble fusible resin of the present invention maintains the fluorescent dye uniformly in the cured resin without reducing the ability to dissolve the fluorescent dye even after becoming insoluble. It is something that is expressed for the sake of.
本発明における可溶可融性樹脂は従来公知方法に従って
、例えばベンゾグアナミンとパラトルエンスルホンアミ
ドとからなる混合物1モルに対しホルムアルテヒド1,
2〜3.5モルをpH4〜10、反応温度50〜100
℃の条件で反応させることによって容易に得ることがで
きる。The soluble fusible resin in the present invention is prepared according to a conventionally known method, for example, 1 mol of formaldehyde,
2 to 3.5 mol, pH 4 to 10, reaction temperature 50 to 100
It can be easily obtained by reacting at ℃ conditions.
この場合の樹脂化反応はパラトルエンスルホンアミドを
用いない場合に比較して速(進行し、樹脂化反応時間の
短縮を可能ならしめる。In this case, the resin formation reaction proceeds more quickly than when p-toluenesulfonamide is not used, making it possible to shorten the resin formation reaction time.
一般にはベンゾグアナミン系樹脂の樹脂化反応の促進に
酸触媒が有効であるが、その場合の樹脂化反応の制御は
非常に困難であるが、本発明によるベンゾグアナミン、
パラトルエンスルホンアミドおよびホルムアルデヒドか
ら導かれる可溶可融性樹脂の応用は樹脂化反応の円滑な
促進を容易ならしめるものである。In general, acid catalysts are effective in promoting the resinization reaction of benzoguanamine-based resins, but in that case, it is very difficult to control the resinization reaction.
Application of soluble and fusible resins derived from para-toluenesulfonamide and formaldehyde facilitates smooth promotion of the resinization reaction.
本発明におけるベンゾグアナミンとパラトルエンスルホ
ンアミドの配合割合としては、ベンゾグアナミン99〜
65重量部とパラトルエンスルホンアミド1〜35重量
部の範囲が有効であり、パラトルエンスルホンアミドの
配合割合を増大するにつれて樹脂化反応時間が短縮され
特に螢光染料を用いた場合には得られる微細着色硬化樹
脂の螢光の鮮明さ耐光性は向上していく。In the present invention, the blending ratio of benzoguanamine and paratoluenesulfonamide is 99 to 99%.
A range of 65 parts by weight and 1 to 35 parts by weight of para-toluenesulfonamide is effective, and as the proportion of para-toluenesulfonamide increases, the resin formation reaction time is shortened, especially when a fluorescent dye is used. The sharpness and light resistance of the fluorescent light of the finely colored cured resin will improve.
しかし、範囲を越えて増大しすぎると耐溶剤性、耐熱性
等の物性を損うので注意を要する。However, if the amount increases too much beyond this range, physical properties such as solvent resistance and heat resistance will be impaired, so care must be taken.
また、パラトルエンスルホンアミドの配合割合を1重量
部以下にすると、ベンゾグアナミン、パラトルエンスル
ホンアミドおよびホルムアルデヒドの共縮合によって発
現する効果は極めて微少であり、パラトルエンスルホン
アミドを使用しない可溶可融性樹脂と実質的に同一のも
のとなってしまう。Furthermore, when the blending ratio of para-toluenesulfonamide is 1 part by weight or less, the effect of co-condensation of benzoguanamine, para-toluenesulfonamide and formaldehyde is extremely small, and soluble and fusible products without the use of para-toluenesulfonamide are produced. The resin becomes substantially the same as the resin.
特にベンゾグアナミン85〜7o重i部とパラトルエン
スルホンアミド15〜30重量部の割合からなる混合物
とホルムアルデヒドの共縮合物が、本発明の効果を有効
に発揮するものとして好ましい。In particular, a co-condensate of formaldehyde and a mixture consisting of 85 to 7 parts by weight of benzoguanamine and 15 to 30 parts by weight of paratoluenesulfonamide is preferred as it effectively exhibits the effects of the present invention.
また、次式で算出されるアセトン混和度が150〜35
0%の範囲にある可溶可融性樹脂が後の工程で細か(か
つ安定な乳化物を得るのに好ましいものである。In addition, the acetone miscibility calculated by the following formula is 150 to 35
Soluble fusible resins in the 0% range are preferred to obtain fine (and stable) emulsions in subsequent steps.
アセトン混和度が350%を越えると水との親和性が太
きすぎ攪拌状態下にある保護コロイド水溶液に投入し乳
化させる際に水によって可塑化され軟弱化し、乳化物の
安定性に問題を生じ、また150%以下では可溶可融性
樹脂の粘度が高く乳化操作が困難で粗粒が生じやすい。If the acetone miscibility exceeds 350%, the affinity with water is too strong, and when it is added to an aqueous protective colloid solution under stirring to emulsify it, it becomes plasticized and weakened by the water, causing problems in the stability of the emulsion. If it is less than 150%, the viscosity of the soluble and fusible resin is high, making emulsification difficult and coarse particles likely to occur.
(式中、Wは可溶可融性樹脂2グをアセトン5グに溶解
した溶液に、その温度を25℃に保ちながら、水を滴下
し、該溶液に白濁を生じさせるに要した水量(2)。(In the formula, W is the amount of water required to cause the solution to become cloudy by adding water dropwise to a solution of 2 g of soluble resin dissolved in 5 g of acetone while maintaining the temperature at 25 ° C. 2).
)可溶可融性樹脂を染料で染色し保護コロイドを用いて
乳化せしめる方法としては、種々の方法を挙げることが
できる。) Various methods can be used to dye the soluble resin with a dye and emulsify it with a protective colloid.
例えば可溶可融性樹脂に染料を加えて攪拌し該樹脂の染
色を行ない、次いで攪拌状態下にある保護コロイド水溶
液に投入し乳化物を得る方法、可溶可融性樹脂を所望の
染料とともに攪拌状態下にある保護コロイド水溶液に投
入し該樹脂の乳化物を得ると同時に染色する方法、攪拌
状態下にある保護コロイドと水溶性染料を含む水溶液あ
るいは保護コロイドと油溶性染料を含む水性液に可溶可
融性樹脂を投入し該樹脂の乳化物を得ると同時に染色す
る方法、さらにまた可溶可融性樹脂を攪拌状態下にある
保護コロイド水溶液に投入し乳化物を予め調製しておき
、次いで乳化物に水溶性染料を加え十分に攪拌すること
によって染色する方法などを挙げることができる。For example, a method in which a dye is added to a soluble fusible resin, stirred to dye the resin, and then poured into an aqueous protective colloid solution under stirring to obtain an emulsion; A method of dyeing at the same time as obtaining an emulsion of the resin by adding it to an aqueous solution of a protective colloid under stirring; A method in which a soluble fusible resin is added to obtain an emulsion of the resin and dyeing is carried out at the same time, and a soluble fusible resin is added to an aqueous protective colloid solution under stirring to prepare an emulsion in advance. Next, a method of dyeing by adding a water-soluble dye to the emulsion and stirring sufficiently can be mentioned.
本発明における微細着色硬化樹脂の懸濁物は、上記の如
き方法のいずれかに従って可溶可融性樹脂を染料で染色
し保護コロイドを用いて乳化せしめた後、乳化物に硬化
触媒を加え乳化状態を保ちながら硬化反応を進め樹脂を
不溶不融状態に至らしめることにより得られる。The suspension of finely colored hardened resin in the present invention is obtained by dyeing a soluble fusible resin with a dye according to any of the methods described above and emulsifying it using a protective colloid, and then adding a hardening catalyst to the emulsion and emulsifying it. It is obtained by proceeding with the curing reaction while maintaining the resin state to bring the resin to an insoluble and infusible state.
この際、必要ならば、硬化させる前に乳化物100重量
部(固形分換算)に対してBET法で測定された比表面
積が50m′/2〜400 m”/ ?の範囲にあり、
粒径が0.05ミクロン以下の超微粒子状シリカ1〜1
5重量部の範囲の割合で添加することができる。At this time, if necessary, the specific surface area measured by the BET method with respect to 100 parts by weight (solid content) of the emulsion before hardening is in the range of 50 m'/2 to 400 m''/?
Ultrafine particulate silica 1 to 1 with a particle size of 0.05 microns or less
It can be added in proportions ranging from 5 parts by weight.
本発明において用いられる保護コロイドとしては、ポリ
ビニルアルコール、ポリビニルピロリドン、ポリアクリ
ル酸のアルカリ金属塩、スチレン・マレイン酸共重合体
のアルカリ金属塩等を挙げることができ、中でも特にポ
リビニルアルコールが好ましい。Examples of the protective colloid used in the present invention include polyvinyl alcohol, polyvinylpyrrolidone, alkali metal salts of polyacrylic acid, and alkali metal salts of styrene-maleic acid copolymer, among which polyvinyl alcohol is particularly preferred.
また、保護コロイドの使用量は可溶可融性樹脂100重
量部に対し1〜30重量部、好ましくは2〜10重量部
の範囲の割合である。The amount of protective colloid used is 1 to 30 parts by weight, preferably 2 to 10 parts by weight, based on 100 parts by weight of the soluble resin.
本発明において用いられる硬化触媒としては、アミノ系
樹脂の硬化触媒として用いられるもの、例えば塩酸、硫
酸、燐酸等の鉱酸類;安息香酸、フタル酸、酢酸等のカ
ルボン酸類;ベンゼンスルホン酸、バラトルエンスルホ
ン酸、ドテシルベンゼンスルホン酸等のスルホン酸類か
らなる群より適当に選んで使用することができる。The curing catalyst used in the present invention includes those used as curing catalysts for amino resins, such as mineral acids such as hydrochloric acid, sulfuric acid, and phosphoric acid; carboxylic acids such as benzoic acid, phthalic acid, and acetic acid; benzenesulfonic acid, and baratoluene. It can be appropriately selected from the group consisting of sulfonic acids such as sulfonic acid and dotecylbenzenesulfonic acid.
これらの硬化触媒は、可溶可融性樹脂の乳化物100重
量部(固形分換算)に対して0.01〜5重量部の範囲
の割合で添加する。These curing catalysts are added in a proportion ranging from 0.01 to 5 parts by weight per 100 parts by weight (in terms of solid content) of the emulsion of the soluble and fusible resin.
硬化反応時の乳化物のpHは、2.0〜5.5の範囲に
あることが好ましい。The pH of the emulsion during the curing reaction is preferably in the range of 2.0 to 5.5.
硬化反応を終了した後、不溶不融性の硬化樹脂は水媒体
から分離し乾燥して微細着色硬化樹脂とするものである
。After the curing reaction is completed, the insoluble and infusible cured resin is separated from the aqueous medium and dried to obtain a finely colored cured resin.
本発明の方法によって得られた微細着色樹脂は、耐溶剤
性、耐熱性等に優れており、特に可溶可融性樹脂を着色
するのに螢光染料を用いた場合、その増量にもかかわら
ず螢光染料のもつ本来の鮮明さをいかんなく発揮するも
のであり、さらに耐光性にも優れており非常に広範な分
野に有効に用いることができるものである。The finely colored resin obtained by the method of the present invention has excellent solvent resistance, heat resistance, etc., and especially when a fluorescent dye is used to color the soluble fusible resin, despite the increase in the amount of fluorescent dye, It fully demonstrates the original clarity of fluorescent dyes, and also has excellent light resistance, so it can be effectively used in a very wide range of fields.
以下、実施例により本発明をさらに詳しく説明する。Hereinafter, the present invention will be explained in more detail with reference to Examples.
実施例 1
攪拌機、還流冷却器、温度計を備えた四つ目フラスコに
ベンゾグアナミン120′i?(0,64モル)、パラ
トルエンスルホンアミド30f(0,17モル)、濃度
37%のホルムアルデヒド水溶液1181(146モル
)および濃度10%の炭酸ナトリウム水溶液0.47
?を仕込み、攪拌しながら94〜95℃の温度で2時間
反応させてベンゾグアナミン、パラトルエンスルホンア
ミドおよびホルムアルデヒドの可溶可融性樹脂を得た。Example 1 120'i? of benzoguanamine was added to a fourth flask equipped with a stirrer, reflux condenser, and thermometer. (0.64 mol), paratoluenesulfonamide 30f (0.17 mol), 37% concentration formaldehyde aqueous solution 1181 (146 mol) and 10% concentration sodium carbonate aqueous solution 0.47
? were charged and reacted for 2 hours at a temperature of 94 to 95° C. with stirring to obtain a soluble and fusible resin of benzoguanamine, paratoluenesulfonamide and formaldehyde.
゛クラレボバール205 ” (株式会社クラレ製ホリ
ビニルアルコール、鹸化度87〜89モル%、重合度5
00)6.0Pを水600′f!に溶解して得た水溶液
にホモミキサーを用いて激しく攪拌しながら上記の可溶
可融性樹脂を加え乳化させた。"Kuraray Bobal 205" (Holyvinyl alcohol manufactured by Kuraray Co., Ltd., degree of saponification 87-89 mol%, degree of polymerization 5
00) 6.0P water 600'f! The above-mentioned soluble resin was added to the aqueous solution obtained by dissolving the resin and emulsified with vigorous stirring using a homomixer.
乳化物に60−ダミンFB”(BASF製塩基性染料)
4.5Pを加えて30分間室温で攪拌し染色した。60-Damine FB” (basic dye manufactured by BASF) in the emulsion
4.5P was added and stirred at room temperature for 30 minutes for staining.
次いでIN−硫酸40グを加え、40℃、50℃、60
℃、70℃、80℃、90℃の各温度で順次2時間づつ
加熱攪拌し、乳化状態で樹脂を硬化させて、染料で染色
された不溶不融性の硬化樹脂の懸濁物を得た。Next, 40 g of IN-sulfuric acid was added, and the mixture was heated at 40°C, 50°C, and 60°C.
℃, 70℃, 80℃, and 90℃ for 2 hours with stirring to cure the resin in an emulsified state to obtain a suspension of an insoluble and infusible cured resin dyed with a dye. .
懸濁物より硬化樹脂を戸別し、100℃で乾燥し150
℃で3時間加熱処理した後、乳鉢の中で軽く押しつぶす
ことにより、非常に鮮明な赤紫色螢光を発する硬化樹脂
微粉末を得た。The cured resin was separated from the suspension and dried at 100°C.
After heat treatment at .degree. C. for 3 hours, the mixture was lightly crushed in a mortar to obtain a cured resin fine powder that emitted very clear reddish-purple fluorescence.
実施例 2
実施例1で使用したのと同じフラスコにベンゾグアナミ
ン105P(0,56モル)、パラトルエンスルホンア
ミド4Fl(0,26モル)、濃度37%のホルムアル
デヒド水溶液112グ(1,38モル)および濃度10
%の炭酸ナトリウム水溶液0.459を仕込み、攪拌し
ながら94〜95℃の温度で40分間反応させた。Example 2 In the same flask as used in Example 1 were added benzoguanamine 105P (0.56 mol), paratoluenesulfonamide 4Fl (0.26 mol), 112 g (1.38 mol) of formaldehyde aqueous solution with a concentration of 37% and concentration 10
An aqueous solution of 0.459% sodium carbonate was added, and the mixture was reacted for 40 minutes at a temperature of 94 to 95°C while stirring.
その後゛カヤセットフラビンFN”(日本化薬株式会社
製油溶性染料)7.Elを加え94〜95℃に保ち30
分間攪拌し、染料を可溶可融性樹脂に溶解させ染色した
。Then add ``Kayaset Flavin FN'' (oil-soluble dye manufactured by Nippon Kayaku Co., Ltd.) 7.El and keep at 94-95℃ for 30 minutes.
After stirring for a minute, the dye was dissolved in the soluble resin and dyed.
゛°クラレボバール205”6.1’を水600グに溶
解して得た水溶液にホモミキサーを用いて激しく攪拌し
ながら上記染色された可溶可融性樹脂を加え乳化させた
。The dyed soluble resin was added to an aqueous solution obtained by dissolving ``Kuraray Boval 205''6.1'' in 600 g of water and emulsified with vigorous stirring using a homomixer.
乳化物を30℃まで冷却した後、IN−硫酸40グを加
え、40℃、50℃、60℃、70℃、80℃、90℃
の各温度で順次2時間づつ加熱攪拌し、乳化状態で硬化
させて染料で染色された不溶不融性の硬化樹脂の懸濁物
を1得た。After cooling the emulsion to 30°C, 40 g of IN-sulfuric acid was added, and the mixture was heated at 40°C, 50°C, 60°C, 70°C, 80°C, and 90°C.
The mixture was heated and stirred at each temperature for 2 hours in order, and cured in an emulsified state to obtain a suspension of an insoluble and infusible cured resin dyed with a dye.
懸濁物より硬化樹脂を戸別し、100℃で乾燥し150
℃で3時間加熱処理した後、乳鉢の中で軽(押しつぶす
ことにより、非常に鮮明な黄色螢光を発する硬化樹脂微
粉末を得た。The cured resin was separated from the suspension and dried at 100°C.
After heat treatment at ℃ for 3 hours, the mixture was crushed in a mortar to obtain a cured resin fine powder that emitted a very clear yellow fluorescence.
実施例 3
実施例1で使用したのと同じフラスコにベンゾグアナミ
ン135P(0,72モル)、パラトルエンスルホンア
ミド15S’(0,09モル)、濃度37%のホルムア
ルデヒド水溶液1241(1,53モル)および濃度1
0%の炭酸す) I)ラム水溶液o、5oyを仕込み、
攪拌しながら94〜95℃の温度で3時間10分反応さ
せて可溶可融性樹脂を得た。Example 3 In the same flask as used in Example 1, benzoguanamine 135P (0,72 mol), paratoluenesulfonamide 15S' (0,09 mol), formaldehyde aqueous solution 1241 (1,53 mol) with a concentration of 37% and Concentration 1
0% carbonic acid) I) Prepare 5 oy of rum aqueous solution,
The mixture was reacted for 3 hours and 10 minutes at a temperature of 94 to 95° C. with stirring to obtain a soluble and fusible resin.
°゛クラレボパール205 ” 6.0 ?を水600
?に溶解して得た水溶液にホモミキサーを用いて激しく
攪拌しながら上記の可溶可融性樹脂を加え乳化させた。°゛Kuraray Bhopal 205'' 6.0?Water 600
? The above-mentioned soluble resin was added to the aqueous solution obtained by dissolving the resin and emulsified with vigorous stirring using a homomixer.
乳化物に゛°ローダミンFB”4.5Pを加えて30分
間室温で攪拌し、次いでIN−硫酸401を加え、40
℃、50℃、60℃、70℃、80℃、90℃の各温度
で順次2時間づつ加熱攪拌し、乳化状態で樹脂を硬化さ
せて染料で染色された不溶不融性の硬化樹脂の懸濁物を
得た。Add "Rhodamine FB" 4.5P to the emulsion and stir at room temperature for 30 minutes, then add IN-sulfuric acid 401 and stir at room temperature for 30 minutes.
℃, 50℃, 60℃, 70℃, 80℃, and 90℃ for 2 hours with stirring to cure the resin in an emulsified state. A cloudy substance was obtained.
懸濁物より硬化樹脂を戸別し、100℃で乾燥し150
℃で3時間加熱処理した後、乳鉢の中で軽く押しつぶす
ことにより、非常に鮮明な赤紫色螢光を発する硬化樹脂
微粉末を得た。The cured resin was separated from the suspension and dried at 100°C.
After heat treatment at .degree. C. for 3 hours, the mixture was lightly crushed in a mortar to obtain a cured resin fine powder that emitted very clear reddish-purple fluorescence.
実施例 4
実施例1で使用したのと同じフラスコにベンゾグアナミ
ン148S’(0,79モル)、パラトルエンスルホン
アミド2f(0,01モル)、濃度37%のホルムアル
デヒド水溶液129P(1,59モル)および濃度10
%の炭酸す) IJウム水溶液0.52?を仕込み、攪
拌しながら94〜95℃の温度で4時間40分反応させ
て可溶可融性樹脂を得た。Example 4 In the same flask as used in Example 1, benzoguanamine 148S' (0,79 mol), para-toluenesulfonamide 2f (0,01 mol), formaldehyde aqueous solution 129P (1,59 mol) with a concentration of 37% and concentration 10
% carbonic acid) IJum aqueous solution 0.52? were charged and reacted for 4 hours and 40 minutes at a temperature of 94 to 95°C while stirring to obtain a soluble fusible resin.
゛°クラレボバール205”6.01を水600ノに溶
解して得た水溶液にホモミキサーを用いて激しく攪拌し
ながら上記の可溶可融性樹脂を加え乳化させた。To an aqueous solution obtained by dissolving Kuraray Boval 205''6.01 in 600 g of water, the above-mentioned soluble resin was added and emulsified while stirring vigorously using a homomixer.
乳化物に゛°ローダミンFB”4.5Pを加えて30分
間室温で攪拌し、次いでIN−硫酸40?を加え、40
℃、50℃、60℃、70℃、80℃、90℃の各温度
で順次2時間づつ加熱攪拌し、乳化状態で樹脂を硬化さ
せて染料で染色された不溶不融性の硬化樹脂の懸濁物を
得た。Add 4.5P of "Rhodamine FB" to the emulsion, stir at room temperature for 30 minutes, then add 40% IN-sulfuric acid,
℃, 50℃, 60℃, 70℃, 80℃, and 90℃ for 2 hours with stirring to cure the resin in an emulsified state. A cloudy substance was obtained.
懸濁物より硬化樹脂を戸別し、100℃で乾燥し150
℃で3時間加熱処理した後、乳鉢の中で軽く押しつぶす
ことにより、鮮明な赤紫色螢光を発する硬化樹脂微粉末
を得た。The cured resin was separated from the suspension and dried at 100°C.
After heat treatment at ℃ for 3 hours, the mixture was lightly crushed in a mortar to obtain a fine cured resin powder that emitted clear reddish-purple fluorescence.
比較例 l
実施例1で使用したのと同じフラスコにベンゾグアナミ
ン150S’(0,8モル)、濃度37%のホルムアル
デヒド水溶液130f(1,6モル)および濃度10%
の炭酸ナトリウム水溶液0.529を仕込み、攪拌しな
がら94〜95℃の温度で5時間反応させて比較のため
の可溶可融性樹脂を得た。Comparative Example l In the same flask as used in Example 1, benzoguanamine 150S' (0.8 mol), formaldehyde aqueous solution 130f (1.6 mol) with a concentration of 37% and a concentration of 10%
0.529 of an aqueous solution of sodium carbonate was added, and the reaction was carried out at a temperature of 94 to 95° C. for 5 hours with stirring to obtain a soluble and fusible resin for comparison.
゛′クラレボバール205”6.01を水600′y′
に溶解して得た水溶液にホモミキサーを用いて激しく攪
拌しながら比較のための可溶可融性樹脂を加え乳化させ
た。゛'Kurare Bobal 205"6.01 water 600'y'
A soluble and fusible resin for comparison was added to the aqueous solution obtained by dissolving the resin and emulsified with vigorous stirring using a homomixer.
乳化物に゛°ローダミンFB”′4゜52を加えて30
分間室温で攪拌し、次いでIN−硫酸40グを加え、4
0℃、50℃、60℃、70℃、80℃、90℃の各温
度で順次2時間づつ加熱攪拌し、乳化状態で樹脂を硬化
させて、染料で染色された比較不溶不融性樹脂の懸濁物
を得た。Add ゛°Rhodamine FB'''4゜52 to the emulsion and add 30
Stir for 4 minutes at room temperature, then add 40 g of IN-sulfuric acid,
The resin was cured in an emulsified state by heating and stirring at each temperature of 0°C, 50°C, 60°C, 70°C, 80°C, and 90°C for 2 hours, and the comparative insoluble and infusible resin dyed with dye was prepared. A suspension was obtained.
懸濁物より比較樹脂を戸別し、100℃で乾燥し150
℃で3時間加熱処理した後、乳鉢の中で軽く押しつぶす
ことにより、鮮明な赤紫色螢光を発する比較硬化樹脂微
粉末を得た。Comparative resin was separated from the suspension and dried at 100°C.
After heat treatment at .degree. C. for 3 hours, the mixture was lightly crushed in a mortar to obtain comparative fine cured resin powder that emitted clear reddish-purple fluorescence.
しかしながら、このようにして得た比較樹脂微粉末は実
施例1のものに比較して赤紫色螢光の鮮明さが若干劣っ
ていた。However, the comparative fine resin powder obtained in this manner was slightly inferior in the sharpness of the reddish-purple fluorescence compared to that of Example 1.
比較例 2
実施例1で使用したのと同じフラスコにベンゾグアナミ
ン12Of(0,64モル)、メラミン30P(0,2
4モル)、濃度37%のホルムアルデヒド水溶液161
7P(2,0モル)および濃度10%の炭酸ナトリウム
水溶液0−65Pを仕込み、攪拌しながら94〜95℃
の温度で3時間30分反応させて比較のための可溶可融
性樹脂を得た。Comparative Example 2 In the same flask as used in Example 1, benzoguanamine 12Of (0.64 mol) and melamine 30P (0.2
4 mol), formaldehyde aqueous solution 161 with a concentration of 37%
7P (2.0 mol) and 10% sodium carbonate aqueous solution 0-65P were prepared and heated to 94-95℃ while stirring.
The reaction was carried out at a temperature of 3 hours and 30 minutes to obtain a soluble resin for comparison.
6クラレポバール205”6−01を水600グに溶解
して得た水溶液にホモミキサーを用いて激しく攪拌しな
がら比較のための可溶可融性樹脂を加え乳化させた。A soluble and fusible resin for comparison was added to an aqueous solution obtained by dissolving 6 Kuraray Poval 205''6-01 in 600 g of water and emulsified it while stirring vigorously using a homomixer.
乳化物に゛ローダミンFB”4.52を加えて30分間
室温で攪拌し、次いでIN−硫酸402を加え、40℃
、50℃、60℃、70℃、80℃、90℃の各温度で
順次2時間づつ加熱攪拌し乳化状態で樹脂を硬化させて
染料で染色された比較不溶不融性樹脂の懸濁物を得た。Rhodamine FB"4.52 was added to the emulsion and stirred at room temperature for 30 minutes, then IN-sulfuric acid 402 was added and heated at 40°C.
, 50° C., 60° C., 70° C., 80° C., and 90° C. by heating and stirring for 2 hours at a time to harden the resin in an emulsified state to obtain a suspension of comparative insoluble and infusible resin dyed with a dye. Obtained.
懸濁物より比較樹脂を戸別し、ioo℃で乾燥し150
℃で3時間加熱処理した後、乳鉢の中で軽く押しつぶす
ことにより鮮明な赤紫色螢光を発する比較硬化樹脂微粉
末を得た。Comparative resin was separated from the suspension and dried at 150°C.
After heat treatment at .degree. C. for 3 hours, the mixture was lightly crushed in a mortar to obtain comparative fine cured resin powder that emitted clear reddish-purple fluorescence.
しかしながら、このようにして得た比較樹脂微粉末は実
施例1のものに比較して赤紫色螢光の鮮明さが劣ってい
た。However, the comparative fine resin powder obtained in this manner had inferior reddish-purple fluorescence in sharpness compared to that of Example 1.
比較例 3
実施例1で使用したのと同じフラスコにベンゾグアナミ
ン90 P (0,48モル)、ハラトルエンスルホン
アミド60f((135モル)、濃度37%のホルムア
ルデヒド水溶液106.21 (1,31モル)および
濃度■O%の炭酸ナトリウム水溶液0.42?を仕込み
、攪拌しながら94〜95℃の温度で20分間反応させ
て比較のための可溶可融性樹脂を得た。Comparative Example 3 In the same flask as used in Example 1, benzoguanamine 90P (0.48 mol), halatoluenesulfonamide 60F ((135 mol), and formaldehyde aqueous solution with a concentration of 37% 106.21 (1.31 mol) were added. Then, an aqueous sodium carbonate solution having a concentration of 10% (0.42%) was charged, and the mixture was allowed to react at a temperature of 94 to 95° C. for 20 minutes with stirring to obtain a soluble and fusible resin for comparison.
゛クラレボバール205”6.02を水600グに溶解
して得た水溶液にホモミキサーを用いて激しく攪拌しな
がら比較のための可溶可融性樹脂を加え乳化させた。A soluble resin for comparison was added to an aqueous solution obtained by dissolving Kuraray Boval 205''6.02 in 600 g of water and emulsified while stirring vigorously using a homomixer.
乳化物に゛ローダミンFB”4.52を加えて30分間
室温で攪拌し、次いでIN−硫酸401を加え、40℃
、50℃、60℃、70℃、80℃、90℃の各温度で
順次2時間づつ加熱攪拌し、乳化状態で樹脂を硬化させ
て、染料で染色された比較のための硬化樹脂の懸濁物を
得た。Rhodamine FB"4.52 was added to the emulsion and stirred at room temperature for 30 minutes, then IN-sulfuric acid 401 was added and the mixture was heated at 40°C.
, 50°C, 60°C, 70°C, 80°C, and 90°C with heating and stirring for 2 hours each to cure the resin in an emulsified state, and then create a suspension of cured resin dyed with a dye for comparison. I got something.
懸濁物より比較樹脂を戸別し、100℃で乾燥し150
℃で3時間加熱処理した後乳鉢の中で軽く押しつぶすこ
とにより、非常に鮮明な赤紫色螢光を発す比較樹脂微粉
末を得た。Comparative resin was separated from the suspension and dried at 100°C.
After heat treatment at 0.degree. C. for 3 hours, the mixture was lightly crushed in a mortar to obtain a comparative fine resin powder that emitted very clear reddish-purple fluorescence.
しかしながら、このようにして得た比較樹脂微粉末は実
施例1のものに比較して耐熱性が劣り、150℃加熱処
理によって樹脂の融着が認められ、また耐溶剤性も劣っ
ておりアセトン等のケトン類:酢酸エチル等のエステル
類中で樹脂の溶解が認められた。However, the comparative resin fine powder obtained in this way had inferior heat resistance compared to that of Example 1, and fusion of the resin was observed after heat treatment at 150°C, and it also had inferior solvent resistance, such as acetone, etc. Ketones: Dissolution of the resin was observed in esters such as ethyl acetate.
実施例 5
実施例1〜4および比゛較例1〜3で得られた樹脂微粉
末の耐溶剤性を下記の方法で試験した。Example 5 The solvent resistance of the fine resin powders obtained in Examples 1 to 4 and Comparative Examples 1 to 3 was tested by the following method.
結果は、第1表に示したとおりであった。The results were as shown in Table 1.
く試験方法〉
樹脂微粉末をメチルエチルケトンに分散して得られた液
を顕微鏡(倍率:400倍)により観察する。Test method> A liquid obtained by dispersing fine resin powder in methyl ethyl ketone is observed using a microscope (magnification: 400 times).
耐溶剤性に劣る樹脂微粉末は、メチルエチルケトンに分
散する際その表面がメチルエチルケトンに冒され粘着性
を有し微粉末同志が凝集し粗大化する現象を認める。When a fine resin powder with poor solvent resistance is dispersed in methyl ethyl ketone, its surface is affected by the methyl ethyl ketone and becomes sticky, and a phenomenon in which the fine powder aggregates and becomes coarse is observed.
実施例 6
実施例1〜4および比較例1〜3で得られた微細着色硬
化樹脂の耐光性を下記の方法で試験した。Example 6 The light resistance of the finely colored cured resins obtained in Examples 1 to 4 and Comparative Examples 1 to 3 was tested by the following method.
結果は第2表に示したとおりであった。The results were as shown in Table 2.
く試験方法〉
微細着色硬化樹脂をポリプロピレン(三井石油化学株式
会社製品”J〜600 ” )へ1%混入し射出成型に
より厚さ3闘の着色プレートを作成する。Test method> 1% of finely colored cured resin is mixed into polypropylene (Mitsui Petrochemical Co., Ltd. product "J~600") and a colored plate with a thickness of 3 mm is prepared by injection molding.
得られた着色ブレードをキセノンウェザ−メーター(ス
ガ試験機株式会社製品”WE−6X−HC” )中で2
時間、4時間、8時間露光し、着色プレートの変色度を
肉眼で測定する。The obtained colored blade was placed in a xenon weather meter (“WE-6X-HC” manufactured by Suga Test Instruments Co., Ltd.) for 2 hours.
After exposure for 4 hours, 8 hours, and 8 hours, the degree of discoloration of the colored plate was measured with the naked eye.
実施例 7
実施例1〜4および比較例1においてアセトン混和度2
50%を示す可溶可融性樹脂を調製するのに要した時間
は、第3表に示したとおりであった。Example 7 Acetone miscibility 2 in Examples 1 to 4 and Comparative Example 1
The time required to prepare a 50% soluble fusible resin was as shown in Table 3.
第3表から明らかなように、本発明に従えば目的とする
可溶可融性樹脂を短時間で調製できるものである。As is clear from Table 3, according to the present invention, the desired soluble and fusible resin can be prepared in a short time.
Claims (1)
ンスルホンアミド1〜35 重1の割合で成る混合物と
ホルムアルデヒドを該混合物1モルに対して1.2〜3
.5モルの割合で、水媒体中で、反応させて得られる可
溶可融性樹脂を染料で染色し保護コロイドを用いて乳化
せしめた後、硬化触媒を加えて乳化状態を保ちながら硬
化反応を進め樹脂を不溶不融状態に至らしめ、得られる
微細着色硬化樹脂の懸濁物から硬化樹脂を分離乾燥する
ことを特徴とする耐溶剤性、耐熱性に優れた微細着色硬
化樹脂の製法。1 A mixture consisting of 99 to 65 parts by weight of benzoguanamine and 1 to 35 parts by weight of paratoluenesulfonamide and formaldehyde in a ratio of 1.2 to 3 parts by weight per 1 mole of the mixture.
.. The soluble resin obtained by reacting in an aqueous medium at a ratio of 5 moles is dyed with a dye and emulsified using a protective colloid, and then a curing catalyst is added and the curing reaction is carried out while maintaining the emulsified state. A method for producing a finely colored cured resin having excellent solvent resistance and heat resistance, which comprises advancing the resin to an insoluble and infusible state, and separating and drying the cured resin from a suspension of the resulting finely colored cured resin.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP54149515A JPS5824444B2 (en) | 1979-11-20 | 1979-11-20 | Manufacturing method for finely colored hardened resin with excellent solvent resistance and heat resistance |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP54149515A JPS5824444B2 (en) | 1979-11-20 | 1979-11-20 | Manufacturing method for finely colored hardened resin with excellent solvent resistance and heat resistance |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5672015A JPS5672015A (en) | 1981-06-16 |
| JPS5824444B2 true JPS5824444B2 (en) | 1983-05-21 |
Family
ID=15476818
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP54149515A Expired JPS5824444B2 (en) | 1979-11-20 | 1979-11-20 | Manufacturing method for finely colored hardened resin with excellent solvent resistance and heat resistance |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5824444B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| TWI229094B (en) | 2001-09-28 | 2005-03-11 | Nippon Catalytic Chem Ind | Amino resin crosslinked particles and producing process thereof |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5227679B2 (en) * | 1972-10-04 | 1977-07-21 |
-
1979
- 1979-11-20 JP JP54149515A patent/JPS5824444B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5672015A (en) | 1981-06-16 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| Wu et al. | Monodispersed or narrow-dispersed melamine–formaldehyde resin polymer colloidal spheres: preparation, size-control, modification, bioconjugation and particle formation mechanism | |
| JP6016907B2 (en) | Water redispersible epoxy polymer powder and method for producing the same | |
| CN105170041A (en) | Reversible thermochromic microcapsule pigment preparation method | |
| JPS6040887B2 (en) | Manufacturing method of microcapsules | |
| JP4141845B2 (en) | How to incorporate colorants | |
| US3945980A (en) | Process for producing finely divided hardened resins | |
| WO1985000535A1 (en) | Process for producing microcapsules | |
| WO2009148146A1 (en) | Fine resin particle aqueous dispersion, method for producing same and method for producing toner particles | |
| US3455856A (en) | Pigmented printing ink and method | |
| US4069176A (en) | Process for producing dyed finely divided hardened benzoguanamine resins having uniform particle size and excelling in dispersibility | |
| JPH0655275B2 (en) | Method for producing melamine formaldehyde microcapsules | |
| JPH02273540A (en) | Manufacture of micro-capsule | |
| CN112795049B (en) | Pre-foaming thermal expansion microsphere, preparation method and application thereof | |
| JPS5824444B2 (en) | Manufacturing method for finely colored hardened resin with excellent solvent resistance and heat resistance | |
| JP4631016B2 (en) | Surface-treated cured amino resin particles and method for producing the same | |
| JPH0717723B2 (en) | Process for producing cured resin spherical fine particles having a uniform particle size | |
| JP4126546B2 (en) | Method for producing colored spherical composite cured melamine resin particles | |
| CN116672980A (en) | Preparation method of stable photochromic high-molecular material formaldehyde-free photosensitive microcapsule | |
| KR100589643B1 (en) | Amino resin crosslinked particles and producing process therefor | |
| JPH01207314A (en) | Cured fine particle having excellent light resistance | |
| TWI278486B (en) | Process for producing amino resin particles | |
| KR0151716B1 (en) | Manufacturing method of thermosetting fluorescent pigment | |
| JPS585924B2 (en) | thailand thorns | |
| JP4652361B2 (en) | Amino resin crosslinked particles | |
| JP4455752B2 (en) | Manufacturing method of colored resin spherical fine particles |