JP2005154704A - Method for producing print ink resin varnish - Google Patents

Method for producing print ink resin varnish Download PDF

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JP2005154704A
JP2005154704A JP2003431277A JP2003431277A JP2005154704A JP 2005154704 A JP2005154704 A JP 2005154704A JP 2003431277 A JP2003431277 A JP 2003431277A JP 2003431277 A JP2003431277 A JP 2003431277A JP 2005154704 A JP2005154704 A JP 2005154704A
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resin
rosin
parts
molecular weight
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Tetsuya Takigawa
哲也 滝川
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Resonac Corp
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Hitachi Kasei Polymer Co Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for producing a print ink resin varnish easily, reasonably, and economically, wherein the print ink resin varnish contains a high molecular weight rosin modified phenol resin and is excellent in high speed printing performance. <P>SOLUTION: The method comprises heating to react (a) a low molecular weight rosin modified phenol resin with (b) a resol type phenol resin and/or a multifunctional acrylate in the presence of (c) a solvent for an offset print ink. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

本発明は、オフセット印刷インキ用樹脂ワニスの製造方法に関する。中でも特に、高速印刷適性に優れる印刷インキ用樹脂ワニスの製造法に関する。The present invention relates to a method for producing a resin varnish for offset printing ink. Especially, it is related with the manufacturing method of the resin varnish for printing inks which is excellent in high-speed printing aptitude.

従来、オフセット印刷インキに使用するロジン変性フェノール樹脂は、ロジン類にレゾール型フェール樹脂及び多価アルコールを加え反応させる方法や、ロジンエステル樹脂にレゾール型フェール樹脂を反応させる方法などにより製造されてきた。これらの反応は200〜270℃の温度において、反応させる塊状重合法が採られてきた。しかしながら、高分子量のロジン変性フェノール樹脂を合成する場合は、合成時に樹脂の溶融粘度が高く、攪拌設備への負荷が大きいため、製造が困難を極めていた。また、高分子量の樹脂は概して軟化点が高い傾向にあるが、このような樹脂は反応系外へ取出すことも難しいという問題があった。Conventionally, rosin-modified phenolic resins used in offset printing inks have been produced by a method of reacting rosins with a resole type fail resin and a polyhydric alcohol, a method of reacting a rosin ester resin with a resole type fail resin, and the like. . A bulk polymerization method in which these reactions are reacted at a temperature of 200 to 270 ° C. has been adopted. However, when synthesizing a high molecular weight rosin-modified phenol resin, the melt viscosity of the resin is high at the time of synthesis, and the load on the agitation equipment is large. Moreover, although high molecular weight resins generally tend to have a high softening point, there is a problem that such resins are difficult to take out of the reaction system.

一方、印刷インキ用樹脂ワニスは、上記の方法などで製造したロジン変性フェノール樹脂をインキ溶剤及び植物油中で加熱溶解し、必要に応じてゲル化剤を添加して、クッキングを行うことにより製造されてきた。相対的に分子量の低いロジン変性フェノール樹脂の場合は大きな問題ではないが、高分子量で、かつ高軟化点の樹脂をインキ溶剤及び植物油に溶解させようとすると、なかなか溶解せず、製造に手間取ることが多かった。On the other hand, a resin varnish for printing ink is manufactured by heating and dissolving the rosin-modified phenolic resin manufactured by the above method in an ink solvent and vegetable oil, adding a gelling agent if necessary, and performing cooking. I came. In the case of a rosin-modified phenolic resin having a relatively low molecular weight, this is not a big problem, but if a resin with a high molecular weight and a high softening point is dissolved in an ink solvent or vegetable oil, it will not be dissolved easily, and it will take time to manufacture. There were many.

近年、オフセット印刷の高速化に伴い、印刷インキ用樹脂においても様々な高速印刷適性が要求されており、特にミスチングの改善が最重要な要求項目となっている。即ち、印刷時のミスチング発生を抑制するため、高粘度、低タックのインキが用いられるようになり、ロジン変性フェノール樹脂に対しては高分子量で高粘度、かつ高軟化点のものが切望されている。In recent years, with the increase in the speed of offset printing, various high-speed printing aptitudes are also required for printing ink resins, and in particular, improvement of misting is the most important requirement. In other words, in order to suppress the occurrence of misting during printing, high viscosity, low tack inks are used, and rosin-modified phenolic resins with high molecular weight, high viscosity and high softening point are desired. Yes.

しかし、前述したように、高分子量で高粘度、かつ高軟化点であるロジン変性フェノール樹脂は、製造設備の攪拌設備への過負荷、樹脂の反応系外への取出しの難しさ、印刷インキ用樹脂ワニス製造時の煩わしさ等の問題により、該樹脂及び該樹脂を含む印刷インキ用樹脂ワニスの製造は困難を極めていた。However, as mentioned above, rosin-modified phenolic resins with high molecular weight, high viscosity, and high softening point are overloaded to the stirring equipment of manufacturing equipment, difficult to take out the resin out of the reaction system, and for printing inks Due to problems such as annoyance during the production of the resin varnish, it was extremely difficult to produce the resin and a resin varnish for printing ink containing the resin.

本発明は、高分子量で高粘度、かつ高軟化点のロジン変性フェノール樹脂を含有する、高速印刷適正に優れた印刷インキ用樹脂ワニスを容易に、しかも合理的、経済的に製造する方法を提供することを目的とする。The present invention provides a method for easily, rationally and economically producing a printing ink resin varnish excellent in high-speed printing, which contains a high-molecular-weight, high-viscosity, and high-softening point rosin-modified phenolic resin. The purpose is to do.

問題点を解決するための手段Means to solve the problem

本発明者らは、これらの状況に鑑み、鋭意検討を重ねた結果、低分子量のロジン変性フェノール樹脂と、レゾール型フェノール樹脂及び/又は多官能アクリレートとをインキ溶剤の存在下で加熱反応させることで、目的とする高分子量で高粘度、かつ高軟化点のロジン変性フェノール樹脂を含有する、高速印刷適正に優れた印刷インキ用樹脂ワニスが得られることを見出した。In light of these circumstances, the present inventors have conducted extensive studies, and as a result, heat-reacted a low molecular weight rosin-modified phenolic resin, a resole-type phenolic resin and / or a polyfunctional acrylate in the presence of an ink solvent. Thus, it has been found that a resin varnish for printing ink, which contains a rosin-modified phenol resin having a desired high molecular weight, high viscosity, and high softening point and excellent in high-speed printing, can be obtained.

即ち、本発明は、低分子量のロジン変性フェノール樹脂(イ)と、レゾール型フェノール樹脂及び/又は多官能アクリレート(ロ)とを、印刷インキ溶剤(ハ)の存在下に加熱反応させる印刷インキ用樹脂ワニスの製造方法に関する。That is, the present invention relates to a printing ink in which a low molecular weight rosin-modified phenolic resin (I) and a resole type phenolic resin and / or a polyfunctional acrylate (B) are heated and reacted in the presence of a printing ink solvent (C). The present invention relates to a method for producing a resin varnish.

本発明においてロジン変性フェノール樹脂(イ)は、ロジン類にレゾール型フェノール樹脂を反応させ、次いでその反応物と多価アルコールを反応させて製造する方法、ロジンエステル樹脂にレゾール型フェノール樹脂を反応させて製造する方法などにより得られる。In the present invention, the rosin-modified phenolic resin (I) is prepared by reacting a rosin with a resole phenolic resin and then reacting the reaction product with a polyhydric alcohol, and reacting the rosin ester resin with a resole phenolic resin. It is obtained by the manufacturing method.

使用されるロジン類はガムロジン、ウッドロジン、トール油ロジン、重合ロジン、不均化ロジン、水素添加ロジン等が挙げられる。また、必要に応じて、これらロジン類にマレイン酸、フマル酸等の不飽和ニ塩基酸を変性して使用することもできる。また、ロジンエステル樹脂は、上記ロジン類に多価アルコールを反応させて得られる。使用する多価アルコールは、従来公知のものが用いられるが、例えばエチレングリコール、ジエチレングリコール、ブタンジオール、2−メチルペンタンジオール、ヘキサンジオール、ネオペンチルグリコール、グリセリン、トリメチロールプロパン、ジメチロールプロピオン酸、トリメチロールエタン、ペンタエリスリトール、ジペンタエリスルトールなどを挙げることができる。なお、多価アルコールは、ロジン類100質量部に対して、5〜15質量部とするのが望ましく、この範囲内であれば樹脂の分子量を所望の範囲に納めることが容易である。レゾール型フェノール樹脂は、フェノール類1モルに対して、ホルムアルデヒド1.5〜3モルの割合で混合し、水酸化ナトリウム、水酸化カリウム、水酸化カルシウム等のアルカリ触媒存在下で縮合重合して得られる。必要に応じて、反応後にアルカリ触媒を中和洗浄する。ここでフェノール類は、従来公知のものが用いられるが、例えば石炭酸、クレゾール、ビスフェノールA、p−ブチルフェノール、p−オクチルフェノール、p−ノニルフェノール、p−ドデシルフェノール等が挙げられる。なお、レゾール型フェノール樹脂は、ロジン類、又はロジンエステル樹脂100質量部に対して10〜100質量部、好ましくは20〜70質量部とするのが望ましい。Examples of rosins used include gum rosin, wood rosin, tall oil rosin, polymerized rosin, disproportionated rosin, and hydrogenated rosin. Further, if necessary, these rosins can be used after modifying an unsaturated dibasic acid such as maleic acid or fumaric acid. The rosin ester resin can be obtained by reacting the rosin with a polyhydric alcohol. As the polyhydric alcohol to be used, conventionally known polyhydric alcohols are used. Mention may be made of methylolethane, pentaerythritol, dipentaerythritol and the like. The polyhydric alcohol is desirably 5 to 15 parts by mass with respect to 100 parts by mass of the rosins, and within this range, it is easy to keep the molecular weight of the resin within a desired range. The resol type phenol resin is obtained by mixing at a ratio of 1.5 to 3 moles of formaldehyde with respect to 1 mole of phenols and performing condensation polymerization in the presence of an alkali catalyst such as sodium hydroxide, potassium hydroxide or calcium hydroxide. It is done. If necessary, the alkali catalyst is neutralized and washed after the reaction. Here, conventionally known phenols are used, and examples thereof include carboxylic acid, cresol, bisphenol A, p-butylphenol, p-octylphenol, p-nonylphenol, and p-dodecylphenol. In addition, it is desirable that the resol type phenol resin is 10 to 100 parts by mass, preferably 20 to 70 parts by mass with respect to 100 parts by mass of rosin or rosin ester resin.

本発明においてロジン変性フェノール樹脂(イ)の重量平均分子量は2000〜100000の、相対的に低分子量のものである必要がある。2000以下では高粘度なワニスが得難く、100000以上ではワニス製造時の溶解に手間取る、また反応管理が困難となる。In the present invention, the weight average molecular weight of the rosin-modified phenolic resin (I) needs to be 2000 to 100000 and a relatively low molecular weight. When the viscosity is 2000 or less, it is difficult to obtain a high-viscosity varnish, and when it is 100,000 or more, it takes time to dissolve the varnish during production, and reaction management becomes difficult.

本発明においてレゾール型フェノール樹脂(ロ)は、上述した方法と同様にして得られる。ロジン変性フェノール樹脂(イ)100質量部に対して10〜100質量部、好ましくは20〜70質量部とするのが望ましい。また、本発明において多官能アクリレート(ロ)は、従来公知のものが用いられるが、例えばエチレングリコールジアクリレート、ネオペンチルグリコールジアクリレート、ヘキサンジオールジアクリレート、トリメチロールプロパンジアクリレート、トリメチロールプロパントリアクリレート、ペンタエリスリトールジアクリレート、ペンタエリスリトールトリアクリレート、ペンタエリスリトールテトラアクリレートなどを挙げることができる。なお、多官能アクリレートは、ロジン変性フェノール樹脂(イ)100質量部に対して概略0.1〜20重量部とするのが望ましく、この範囲内であれば樹脂の分子量を所期の範囲に納めることが容易である。In the present invention, the resol type phenol resin (B) is obtained in the same manner as described above. 10 to 100 parts by weight, preferably 20 to 70 parts by weight, based on 100 parts by weight of the rosin-modified phenol resin (ii). In the present invention, a conventionally known polyfunctional acrylate (b) is used. For example, ethylene glycol diacrylate, neopentyl glycol diacrylate, hexanediol diacrylate, trimethylolpropane diacrylate, trimethylolpropane triacrylate. And pentaerythritol diacrylate, pentaerythritol triacrylate, pentaerythritol tetraacrylate, and the like. The polyfunctional acrylate is preferably about 0.1 to 20 parts by weight with respect to 100 parts by weight of the rosin-modified phenolic resin (ii), and within this range, the molecular weight of the resin falls within the expected range. Is easy.

本発明において印刷インキ溶剤(ハ)は、沸点が200℃以上のオフセット印刷インキ溶剤を使用することができる。これらの溶剤としては、例えば、パラフィン系、ナフテン系の石油系インキ溶剤が用いられる。好適な例としては、新日本石油(株)製のAF5号ソルベント、AF6号ソルベント、AF7号ソルベントなどのインキ溶剤が挙げられる。In the present invention, as the printing ink solvent (c), an offset printing ink solvent having a boiling point of 200 ° C. or higher can be used. As these solvents, for example, paraffinic and naphthenic petroleum ink solvents are used. Preferable examples include ink solvents such as AF5 solvent, AF6 solvent, AF7 solvent manufactured by Nippon Oil Corporation.

本発明の印刷インキ用樹脂ワニスには、植物油を加えることもできる。植物油の好ましい例としては、亜麻仁油、桐油、サフラワー油などの乾性油、大豆油、菜種油、コーン油などの半乾性油、ひまし油、オリーブ油などの不乾性油、脱水ひまし油、熱重合油などの合成乾性油、及びこれらの混合物や再生油が挙げられる。また必要に応じて脂肪酸エステルなどを併用することもできる。なお、植物油の配合量は、ワニス中の固形分100質量部に対し、10〜50質量部が適当である。Vegetable oil can also be added to the resin varnish for printing ink of the present invention. Preferred examples of vegetable oils include drying oils such as linseed oil, tung oil, safflower oil, semi-drying oils such as soybean oil, rapeseed oil, and corn oil, non-drying oils such as castor oil and olive oil, dehydrated castor oil, and thermal polymerization oil. Synthetic drying oils, and mixtures and regenerated oils thereof can be mentioned. Moreover, fatty acid ester etc. can also be used together as needed. In addition, 10-50 mass parts is suitable for the compounding quantity of vegetable oil with respect to 100 mass parts of solid content in a varnish.

本発明の印刷インキ用樹脂ワニスには、必要に応じてゲル化剤を加えて加熱反応させることもできる。ゲル化剤の好ましい例としては、アルミニウムエチルアセトアセテートジイソプロピレート、アルミニウムトリス(エチルアセトアセテート)、アルミニウムイソプロピレート、ステアリン酸アルミニウム、オクチル酸アルミニウムなど公知のものが挙げられ、更にそれらの混合物も使用することができる。なお、ゲル化剤の配合量は、ワニス中の固形分100質量部に対し、0〜5質量部が適当である。ゲル化剤を加えた後、概略150〜180℃で、1〜2時間程度に反応させるのが適当である。The resin varnish for printing ink of the present invention can be heated and reacted by adding a gelling agent as necessary. Preferable examples of the gelling agent include known ones such as aluminum ethyl acetoacetate diisopropylate, aluminum tris (ethyl acetoacetate), aluminum isopropylate, aluminum stearate, aluminum octylate, and mixtures thereof are also used. can do. In addition, 0-5 mass parts is suitable for the compounding quantity of a gelatinizer with respect to 100 mass parts of solid content in a varnish. After adding the gelling agent, it is appropriate to react at about 150 to 180 ° C. for about 1 to 2 hours.

本発明において、ロジン変性フェノール樹脂(イ)と、レゾール型フェノール樹脂及び/又は多官能アクリレート(ロ)とを印刷インキ溶剤(ハ)の存在下に加熱反応させるが、その温度は100〜270℃が適当であり、140〜230℃がより好ましい。また、必要に応じて500mmHg以下の減圧条件下において反応させる。In the present invention, the rosin-modified phenolic resin (I) and the resol type phenolic resin and / or the polyfunctional acrylate (B) are heated and reacted in the presence of the printing ink solvent (C), and the temperature is 100 to 270 ° C. Is suitable, and 140-230 degreeC is more preferable. Moreover, it is made to react on the pressure reduction conditions of 500 mmHg or less as needed.

発明の効果The invention's effect

本発明の印刷インキ用樹脂ワニスの製造方法に従えば、高分子量で高粘度、かつ高軟化点のロジン変性フェノール樹脂を含有する印刷インキ用樹脂ワニスを容易に、しかも合理的、経済的に製造できる。なお、本発明に従えば、ロジン変性フェノール樹脂を従来の溶融状態で反応させる塊状重合法に比べ、少ないレゾール型フェノール樹脂量で高分子量で高粘度、かつ高軟化点なロジン変性フェノール樹脂が得られるので、印刷インキ用樹脂ワニスの低コスト化に寄与する。According to the method for producing a resin varnish for printing ink of the present invention, a resin varnish for printing ink containing a rosin-modified phenolic resin having a high molecular weight, a high viscosity, and a high softening point can be easily and rationally and economically produced. it can. According to the present invention, a rosin-modified phenol resin having a high molecular weight, a high viscosity, and a high softening point can be obtained as compared with a bulk polymerization method in which a rosin-modified phenol resin is reacted in a conventional molten state. Therefore, it contributes to the cost reduction of the resin varnish for printing ink.

以下、実施例によって本発明を詳細に説明する。なお、仕込みの部は質量部を表す。Hereinafter, the present invention will be described in detail by way of examples. In addition, the part of preparation represents a mass part.

[合成例1]
攪拌機、水分離器つき反応容器中に中国産ガムロジン800部を仕込み、窒素ガスを吹き込みながら加熱攪拌し、200℃にてペンタエリスリトール80部、酢酸マグネシウム2部を仕込み、270℃で脱水縮合して、酸価が約20となるまで反応させ、ロジンエステル樹脂を合成した。
[Synthesis Example 1]
Charge 800 parts of Chinese gum rosin into a reaction vessel equipped with a stirrer and water separator, heat and stir while blowing nitrogen gas, charge 80 parts of pentaerythritol and 2 parts of magnesium acetate at 200 ° C, and perform dehydration condensation at 270 ° C. The rosin ester resin was synthesized by reacting until the acid value reached about 20.

[合成例2]
攪拌機、冷却器つき反応容器中にp−オクチルフェノール400部、パラホルムアルデヒド(純度92%)140部及び水酸化ナトリウム1部を仕込み、90℃に加熱し、5時間反応してレゾール型フェノール樹脂を得た。
[Synthesis Example 2]
In a reactor equipped with a stirrer and a cooler, 400 parts of p-octylphenol, 140 parts of paraformaldehyde (purity 92%) and 1 part of sodium hydroxide are charged, heated to 90 ° C. and reacted for 5 hours to obtain a resol type phenol resin. It was.

[合成例3]
撹拌機、水分離器付き反応容器中に合成例1で合成したロジンエステル樹脂800部を仕込み、窒素ガスを吹き込みながら加熱撹拌し、240℃にて合成例2で合成したレゾール型フェノール樹脂240部を滴下反応した。得られたロジン変性フェノール樹脂は軟化点140℃、酸価15mgKOH/g、水酸基価60mgKOH/g、AF7号ソルベント(新日本石油(株)製)溶解性4.5倍、重量平均分子量4000である。なお、AF7号ソルベント溶解性とは、樹脂2gをAF7号ソルベント4gに溶解させ、順次AF7号ソルベントを加えていき、白濁を生じ始めた時点までに使用したAF7号ソルベントのg数に樹脂の溶解に使用したAF7号ソルベント4gを加算し、樹脂1g当り何倍のAF7号ソルベントになるかで表示したものである。
[Synthesis Example 3]
In a reaction vessel equipped with a stirrer and a water separator, 800 parts of the rosin ester resin synthesized in Synthesis Example 1 was charged, heated and stirred while blowing nitrogen gas, and 240 parts of resole phenolic resin synthesized in Synthesis Example 2 at 240 ° C. Was dropped. The obtained rosin-modified phenolic resin has a softening point of 140 ° C., an acid value of 15 mg KOH / g, a hydroxyl value of 60 mg KOH / g, an AF7 solvent (manufactured by Shin Nippon Oil Co., Ltd.), solubility 4.5 times, and a weight average molecular weight of 4000. . The AF7 solvent solubility means that 2 g of resin is dissolved in 4 g of AF7 solvent, and AF7 solvent is added in order, and the resin dissolves in the number of grams of AF7 solvent used until the start of cloudiness. 4 g of the AF7 solvent used in the above is added to indicate how many times the AF7 solvent is used per 1 g of resin.

[合成例4]
撹拌機、水分離器付き反応容器中に合成例1で合成したロジンエステル樹脂800部を仕込み、窒素ガスを吹き込みながら加熱撹拌し、240℃にて合成例2で合成したレゾール型フェノール樹脂320部を滴下反応した。得られたロジン変性フェノール樹脂は軟化点170℃、酸価15mgKOH/g、水酸基価65mgKOH/g、AF7号ソルベント(新日本石油(株)製)溶解性3.5倍、重量平均分子量30000である。
[Synthesis Example 4]
In a reaction vessel equipped with a stirrer and a water separator, 800 parts of the rosin ester resin synthesized in Synthesis Example 1 was charged, heated and stirred while blowing nitrogen gas, and 320 parts of resole phenolic resin synthesized in Synthesis Example 2 at 240 ° C. Was dropped. The obtained rosin-modified phenolic resin has a softening point of 170 ° C., an acid value of 15 mg KOH / g, a hydroxyl value of 65 mg KOH / g, an AF7 solvent (manufactured by Shin Nippon Oil Co., Ltd.), a solubility of 3.5 times, and a weight average molecular weight of 30000. .

[実施例1]
攪拌機、水分離器つき反応容器中に合成例3で合成したロジン変性フェノール樹脂700部と合成例2で合成したレゾール型フェノール樹脂100部及びAF7号ソルベント300部を仕込み、窒素ガスを吹き込みながら加熱攪拌して、樹脂を溶解した。その後230℃まで昇温しながら、ロジン変性フェノール樹脂とレゾール型フェノール樹脂との縮合反応で発生した水を水分離機で回収した。230℃で3時間反応させた後、AF7号ソルベント200部、大豆油220部及びALCH−50F(川研ファインケミカル(株)製)8部を投入し、更に180℃で1時間反応させ樹脂ワニス(樹脂固形分50%)を得た。
[Example 1]
In a reaction vessel equipped with a stirrer and a water separator, 700 parts of the rosin-modified phenol resin synthesized in Synthesis Example 3, 100 parts of the resole-type phenol resin synthesized in Synthesis Example 2 and 300 parts of AF7 Solvent were charged and heated while blowing nitrogen gas. Stir to dissolve the resin. Thereafter, while raising the temperature to 230 ° C., water generated by the condensation reaction between the rosin-modified phenol resin and the resol type phenol resin was recovered with a water separator. After reacting at 230 ° C. for 3 hours, 200 parts of AF7 solvent, 220 parts of soybean oil and 8 parts of ALCH-50F (manufactured by Kawaken Fine Chemical Co., Ltd.) are added, and further reacted at 180 ° C. for 1 hour to form a resin varnish ( Resin solid content 50%) was obtained.

[実施例2]
合成例4で合成したロジン変性フェノール樹脂750部と合成例2で合成したレゾール型フェノール樹脂50部を使用した他は、実施例1と同様に合成して樹脂ワニス(樹脂固形分50%)を得た。
[Example 2]
A resin varnish (resin solid content 50%) was synthesized in the same manner as in Example 1 except that 750 parts of the rosin-modified phenol resin synthesized in Synthesis Example 4 and 50 parts of the resole-type phenol resin synthesized in Synthesis Example 2 were used. Obtained.

[比較例1]
実施例1と同様の反応容器中に中国産ガムロジン450部を仕込み、窒素ガスを吹き込みながら加熱攪拌し、230℃にて合成例2で合成したレゾール型フェノール樹脂400部を3時間で滴下した。その後グリセリン40部、酸化マグネシウム0.4部を仕込み、270℃で脱水縮合して、酸価が約20となるまで反応させた。得られたロジン変性フェノール樹脂は軟化点175℃、酸価15mgKOH/g、水酸基価75mgKOH/g、AF7号ソルベント(新日本石油(株)製)溶解性1.6倍、重量平均分子量80000である。その後、AF7号ソルベント500部、大豆油220部及びALCH−50F16部を投入し、180℃で1時間反応させ樹脂ワニス(樹脂固形分50%)を得た。
[Comparative Example 1]
450 parts of Chinese gum rosin was charged in the same reaction vessel as in Example 1, and heated and stirred while blowing nitrogen gas, and 400 parts of a resol type phenolic resin synthesized in Synthesis Example 2 was added dropwise at 230 ° C. in 3 hours. Thereafter, 40 parts of glycerin and 0.4 part of magnesium oxide were added and subjected to dehydration condensation at 270 ° C. until the acid value reached about 20. The obtained rosin-modified phenolic resin has a softening point of 175 ° C., an acid value of 15 mg KOH / g, a hydroxyl value of 75 mg KOH / g, an AF7 solvent (manufactured by Shin Nippon Oil Co., Ltd.), a solubility of 1.6 times, and a weight average molecular weight of 80000. . Thereafter, 500 parts of AF7 solvent, 220 parts of soybean oil and 16 parts of ALCH-50F were added and reacted at 180 ° C. for 1 hour to obtain a resin varnish (resin solid content 50%).

[比較例2]
実施例1と同様の反応容器中に合成例1で合成したロジンエステル樹脂400部、合成例2で合成したレゾール型フェノール樹脂400部を3時間で滴下した。得られたロジン変性フェノール樹脂は軟化点170℃、酸価15mgKOH/g、水酸基価65mgKOH/g、AF7号ソルベント(新日本石油(株)製)溶解性4.4倍、重量平均分子量50000である。その後、AF7号ソルベント500部、大豆油220部及びALCH−50F25部を投入し、180℃で1時間反応させ樹脂ワニス(樹脂固形分50%)を得た。
[Comparative Example 2]
In a reaction container similar to that in Example 1, 400 parts of the rosin ester resin synthesized in Synthesis Example 1 and 400 parts of the resol-type phenol resin synthesized in Synthesis Example 2 were dropped in 3 hours. The obtained rosin-modified phenolic resin has a softening point of 170 ° C., an acid value of 15 mg KOH / g, a hydroxyl value of 65 mg KOH / g, solubility of AF7 solvent (manufactured by Shin Nippon Oil Co., Ltd.), 4.4 times, and a weight average molecular weight of 50,000. . Thereafter, 500 parts of AF7 solvent, 220 parts of soybean oil and 25 parts of ALCH-50F were added and reacted at 180 ° C. for 1 hour to obtain a resin varnish (resin solid content 50%).

得られた樹脂ワニスについて、粘度、n−ヘキサン溶解性、重量平均分子量を測定した。測定は以下の方法で行い、結果を表1に示す。About the obtained resin varnish, a viscosity, n-hexane solubility, and the weight average molecular weight were measured. The measurement was performed by the following method, and the results are shown in Table 1.

粘度:E型粘度計を用い、25℃、回転速度10rpmにおいて測定を行った。Viscosity: Measurement was carried out using an E-type viscometer at 25 ° C. and a rotation speed of 10 rpm.

n−ヘキサン溶解性:25℃でワニス1gにn−ヘキサンを滴下しながら混合していき、溶液が濁り始めた時点のn−ヘキサンの滴下量をn−ヘキサン溶解性とした。n-Hexane solubility: n-hexane was added dropwise to 1 g of varnish at 25 ° C. while mixing, and the amount of n-hexane dropped when the solution started to become cloudy was defined as n-hexane solubility.

重量平均分子量:GPC分析による分子量(ポリスチレン換算)測定を行った。Weight average molecular weight: The molecular weight (polystyrene conversion) was measured by GPC analysis.

Figure 2005154704
Figure 2005154704

表1の各々樹脂ワニスについて、ワニス60部とカーミン6B36部を三本ロールミルで練肉し、更にタックが6〜7、フローが30〜35mm/minになるよう各々のワニス及びAF7号ソルベントで調整して試験用紅インキを得た。For each resin varnish in Table 1, 60 parts of varnish and 36 parts of Carmine 6B are kneaded with a three-roll mill and adjusted with each varnish and AF No. 7 solvent so that the tack is 6 to 7 and the flow is 30 to 35 mm / min. Thus, a red ink for test was obtained.

表2に各インキの性状と評価結果を示す。Table 2 shows the properties and evaluation results of each ink.

Figure 2005154704
Figure 2005154704

表2のインキ性能評価は以下の様に行った。The ink performance evaluation in Table 2 was performed as follows.

タック:デジタルインコメーター((株)東洋精機製作所製)を用いて測定した。Tack: Measured using a digital incometer (manufactured by Toyo Seiki Seisakusho).

フロー:並行板粘度計((株)東洋精機製作所製)を用いて測定した。Flow: Measured using a parallel plate viscometer (manufactured by Toyo Seiki Seisakusho).

光沢:インキ0.3ccをRIテスター(明製作所社製)でアート紙に展色した後、熱風乾燥機中120℃、5秒で乾燥させ、室温で24時間経過した時点で光沢計(ガードナー社製)を用いて60°鏡面反射率を測定した。Gloss: After 0.3 cc of ink was developed on art paper with an RI tester (Made Seisakusho), it was dried in a hot air dryer at 120 ° C. for 5 seconds, and after 24 hours at room temperature, a gloss meter (Gardner) The specular reflectance at 60 ° was measured using

乳化率:リソトロニック(ノボマチック社製)を用い、25gのインキにイオン交換水を2ml/minの速度で滴下して、飽和したところでの乳化率を測定した。Emulsification rate: Using Lysotronic (manufactured by Novomatic), ion-exchanged water was added dropwise to 25 g of ink at a rate of 2 ml / min, and the emulsification rate when saturated was measured.

ミスチング量:インキ1.3ccをデジタルインコメーター((株)東洋精機製作所製)1分当り2000回転で1分間回転させた時にロール下方に飛散したミストの量を精秤した。Misting amount: The amount of mist splashed below the roll was precisely weighed when 1.3 cc of ink was rotated at 2000 rpm per minute for a digital incometer (manufactured by Toyo Seiki Seisakusho).

表2から、実施例1及び実施例2を用いたインキは比較例1及び比較例2(従来のロジン変性フェノール樹脂を溶解)用いたインキと比較して、全ての評価項目において同等以上であり、特に乳化率、及び耐ミスチング性の点で優れた性能を有する。From Table 2, the ink using Example 1 and Example 2 is equivalent or better in all evaluation items compared with the ink using Comparative Example 1 and Comparative Example 2 (dissolving conventional rosin-modified phenolic resin). In particular, it has excellent performance in terms of emulsification rate and misting resistance.

Claims (1)

低分子量のロジン変性フェノール樹脂(イ)と、レゾール型フェノール樹脂及び/又は多官能アクリレート(ロ)とを、印刷インキ溶剤(ハ)の存在下に加熱反応させる印刷インキ用樹脂ワニスの製造方法。A process for producing a resin varnish for printing ink, in which a low molecular weight rosin-modified phenolic resin (I), a resol type phenolic resin and / or a polyfunctional acrylate (B) are heated and reacted in the presence of a printing ink solvent (C).
JP2003431277A 2003-11-21 2003-11-21 Method for producing print ink resin varnish Pending JP2005154704A (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008214441A (en) * 2007-03-02 2008-09-18 Arakawa Chem Ind Co Ltd Active energy ray-curable resin composition and printing ink

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008214441A (en) * 2007-03-02 2008-09-18 Arakawa Chem Ind Co Ltd Active energy ray-curable resin composition and printing ink

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