JP2990212B2 - Colored resin composition and method for producing the same - Google Patents
Colored resin composition and method for producing the sameInfo
- Publication number
- JP2990212B2 JP2990212B2 JP4315616A JP31561692A JP2990212B2 JP 2990212 B2 JP2990212 B2 JP 2990212B2 JP 4315616 A JP4315616 A JP 4315616A JP 31561692 A JP31561692 A JP 31561692A JP 2990212 B2 JP2990212 B2 JP 2990212B2
- Authority
- JP
- Japan
- Prior art keywords
- pigment
- resin
- resin composition
- colored
- water
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Landscapes
- Developing Agents For Electrophotography (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は画像記録用以外の用途に
使用される顔料樹脂組成物の製造方法に関し、更に詳し
くは顔料の分散性に優れた画像記録用以外の用途に使用
される着色樹脂組成物の提供を目的としている。The present invention is applicable to uses other than image recording.
Regarding the method for producing the pigment resin composition to be used , more specifically, it is used for purposes other than image recording excellent in dispersibility of the pigment.
The purpose of the present invention is to provide a colored resin composition.
【0002】[0002]
【従来の技術】従来、顔料樹脂組成物、例えば、プラス
チック用着色剤としては顔料を分散剤と混合したドライ
カラー、顔料を担体樹脂と高濃度に混練したマスターバ
ッチ等が広く使用されている。これらのプラスチック用
着色剤は、顔料粉末と分散剤又は担体樹脂とをロールや
ニーダー等の高剪断機により溶融混練して顔料の分散を
図っているが、一旦乾燥した顔料粉末は粗大な2次凝集
粒子が多数存在する為、これらの粗大粒子を全て数μm
以下にまで再分散させるのは非常に困難である。従来の
プラスチックの着色においては粗大粒子の存在は無論な
いことが好ましいが、それほど厳格には微分散が要求さ
れなかった。2. Description of the Related Art Conventionally, pigment resin compositions, for example, as a colorant for plastics, a dry color in which a pigment is mixed with a dispersant, a master batch in which a pigment is kneaded with a carrier resin at a high concentration, and the like have been widely used. These colorants for plastics disperse the pigment by melting and kneading the pigment powder and a dispersant or a carrier resin with a high shearing machine such as a roll or a kneader. Since there are many agglomerated particles, all these coarse particles are several μm
It is very difficult to redistribute to: In the coloring of conventional plastics, it is preferable that the presence of coarse particles is, of course, preferred, but fine dispersion was not so strictly required.
【0003】[0003]
【発明が解決しようとしている問題点】これに対して近
年に至ってはプラスチック及び繊維等の着色においても
顔料の高分散性が強く要求される様になり、従来の粉体
顔料を用いる方法では対応が困難となりつつある。 On the other hand, in recent years, high dispersibility of pigments has been strongly required even in coloring of plastics and fibers, and the conventional method using powdered pigments is not suitable. Is becoming more difficult .
【0004】又、分散性に優れた顔料樹脂着色物を得る
方法として、顔料の水性ペーストと樹脂とを混練して水
性相の顔料を樹脂相に移行させ、しかる後に水を除去す
ることにより顔料樹脂組成物の製造方法が提案されてい
る(特開平2−175770号公報参照)しかしなが
ら、この方法では、顔料ペーストの存在が前提となって
おり、原料としての顔料が粉末顔料でしか入手し得ない
場合は適用することが出来ない。又、この様な方法で
は、使用する顔料ペーストに含まれる大量の水分の除去
には排水と蒸発との工程が必要であり、そのエネルギー
消費量も無視することは出来ない。従って本発明の目的
は、顔料の水性ペーストを用いることなく、顔料が高濃
度且つ微細に分散した顔料樹脂組成物、例えば、樹脂
用、繊維用、その他の用途に有用な着色剤及び該着色剤
によって着色された画像記録用以外の用途に使用され る
着色樹脂組成物を提供することである。[0004] As a method of obtaining a pigment resin colored material having excellent dispersibility, an aqueous paste of a pigment and a resin are kneaded to transfer an aqueous pigment to a resin phase, and then water is removed to remove the pigment. However, a method for producing a resin composition has been proposed (see Japanese Patent Application Laid-Open No. 2-175770). However, in this method, the presence of a pigment paste is assumed, and the pigment as a raw material can be obtained only as a powder pigment. If not, it cannot be applied. In addition, in such a method, a large amount of water contained in the pigment paste to be used requires a step of drainage and evaporation, and the energy consumption thereof cannot be neglected. Accordingly, an object of the present invention is to provide a pigment resin composition in which a pigment is finely dispersed at a high concentration without using an aqueous paste of the pigment, for example, a colorant useful for resins, fibers, and other uses, and the colorant. to provide a <br/> colored resin composition that is used for applications other than for image recording that has been colored by.
【0005】[0005]
【問題点を解決する為の手段】上記目的は以下の本発明
によって達成される。即ち、本発明は、画像記録用以外
の用途に使用される、顔料を樹脂に微細に分散させた顔
料樹脂組成物において、乾燥顔料と熱熔融性樹脂及び分
散助剤としての水とを混合機或は混練機に仕込み混合し
て顔料及び樹脂を湿潤し、加圧下又は常圧下で加熱して
樹脂を熔融させて加熱混練した後、水分を常圧或は減圧
下で蒸発させて乾燥除去することを特徴とする着色樹脂
組成物、及びその製造方法である。The above object is achieved by the present invention described below. That is, the present invention is not limited to image recording.
In a pigment resin composition in which a pigment is finely dispersed in a resin, a dry pigment, a hot-melt resin and water as a dispersing agent are charged into a mixer or kneader and mixed. and the resin was wet, was heated and kneaded by melting the resin by heating under pressure or normal pressure, moisture normally圧或colored resin composition, wherein the benzalkonium be dried removed by evaporation under reduced pressure And a method of manufacturing the same.
【0006】[0006]
【作用】以上の如き本発明によれば、分散助剤としての
水を添加し加圧下又は常圧で、顔料と樹脂とを加熱混練
することにより、水分子の運動が活発になって粉末顔料
の高次凝集体に水分が浸透し、その凝集体を破壊し、顔
料合成時に近い低次凝集粒子状態で樹脂に分散及び拡散
してゆくものと考えられる。従って、その作用効果とし
ては第1に、顔料の分散効果が通常の乾式混練方法より
はるかに向上し、機械的分散では得られない顔料の微粒
子分散が可能となる。第2として、使用する水分量は後
述する様に分散に必要な適量を添加することで足り、従
って顔料と樹脂とを混練後除去する場合は加熱又は減圧
下で蒸発させるだけでよい。According to the present invention as described above, by adding water as a dispersing agent and kneading the pigment and the resin under pressure or at normal pressure, the movement of water molecules becomes active and the powder pigment It is considered that water permeates into the higher order aggregates of the above, breaks down the aggregates, and is dispersed and diffused in the resin in a state of lower order aggregate particles close to the time of pigment synthesis. Accordingly, firstly, the effect of the dispersion is that the effect of dispersing the pigment is much improved compared to the ordinary dry kneading method, and the fine particles of the pigment which cannot be obtained by mechanical dispersion can be dispersed. Secondly, it is sufficient to add an appropriate amount of water necessary for dispersion, as described later. Therefore, when the pigment and the resin are removed after kneading, it is only necessary to evaporate under heating or reduced pressure.
【0007】第3として、水の添加により熔融物と混練
機の金属部分との離型性がよくなり、水の蒸気圧により
熔融物が膨張し、均一分散がスムーズに進む。第4に、
常圧で混練の場合は、水の蒸発潜熱を利用することによ
り、混練の摩擦熱等による温度上昇を抑えることも出
来、更に水を追加することで長時間の混練を可能にし、
顔料の分散をより完全なものとすることが出来る。又、
この様にして得られた着色剤組成物を、更に必要に応じ
て使用目的の樹脂に添加して希釈混練することにより顔
料の分散性に優れた鮮明な実用顔料濃度の着色樹脂組成
物を得ることが出来る。Third, the addition of water improves the releasability between the melt and the metal part of the kneader, and the melt expands due to the vapor pressure of water, whereby uniform dispersion proceeds smoothly. Fourth,
In the case of kneading at normal pressure, the temperature rise due to frictional heat of kneading can be suppressed by using the latent heat of evaporation of water, and kneading for a long time is possible by adding more water.
More complete dispersion of the pigment can be achieved. or,
The colorant composition thus obtained is further added to the intended use resin, if necessary, and the mixture is diluted and kneaded to obtain a colored resin composition having excellent dispersibility of the pigment and a clear practical pigment concentration. I can do it.
【0008】[0008]
【好ましい実施態様】次に好ましい実施態様を挙げて本
発明を更に具体的に説明する。本発明で使用する顔料と
しては、従来公知の有彩色及び黒色〜白色の有機顔料及
び無機顔料が使用され、例えば、アゾ系、ポリ縮合アゾ
系、アゾメチン基を含むアゾ系、アゾメチン系、アンス
ラキノン系、フタロシアニン系、ペリノン・ペリレン
系、インジゴ・チオインジゴ系、ジオキサジン系、キナ
クリドン系、イソインドリノン系、アニリンブラック系
の顔料及び酸化鉄系スピネル構造形、カーボンブラック
系顔料、酸化チタン系顔料等が挙げられる。それらの中
で特に親油性の高い有機顔料が好ましい。Next, the present invention will be described more specifically with reference to preferred embodiments. As the pigment used in the present invention, conventionally known chromatic and black to white organic pigments and inorganic pigments are used. For example, azo series, polycondensed azo series, azo series containing azomethine group, azomethine series, anthraquinone Pigments, phthalocyanine-based, perinone-perylene-based, indigo-thioindigo-based, dioxazine-based, quinacridone-based, isoindolinone-based, aniline black-based pigments and iron oxide-based spinel structures, carbon black-based pigments, titanium oxide-based pigments and the like. No. Among them, organic pigments having particularly high lipophilicity are preferred.
【0009】本発明において使用する樹脂としては従来
公知の熱可塑性樹脂やマスターバッチの担体樹脂として
使用されている樹脂がいずれも使用することが出来る。
更に高濃度の着色剤を作る場合にはそれと相溶性のある
マスターバッチの担体樹脂等も使用することが出来る。
例えば、ポリスチレン、スチレン−(メタ)アクリル酸
エステル共重合体、スチレン−マレイン酸エステル共重
合体、ロジン変成マレイン酸樹脂、(メタ)アクリル酸
エステル重合体及び共重合体、スチレン−ジエン系共重
合体、ポリエチレン系樹脂、ポリプロピレン系樹脂、ポ
リエステル系樹脂、エポキシ系樹脂、石油樹脂、アルキ
ッド樹脂、ポリ塩化ビニール樹脂、ポリ塩化ビニリデン
樹脂、アクリルニトリルスチレン樹脂、エチレン酢ビ樹
脂、ポリカーボネート樹脂、アセタール樹脂、ポリアミ
ド樹脂、及び各種ワックス類等が使用される。As the resin used in the present invention, any of conventionally known thermoplastic resins and resins used as carrier resins for masterbatches can be used.
Further, when a high-concentration colorant is prepared, a carrier resin of a master batch which is compatible with the colorant can be used.
For example, polystyrene, styrene- (meth) acrylate copolymer, styrene-maleate copolymer, rosin-modified maleic resin, (meth) acrylate polymer and copolymer, styrene-diene copolymer Coalesce, polyethylene resin, polypropylene resin, polyester resin, epoxy resin, petroleum resin, alkyd resin, polyvinyl chloride resin, polyvinylidene chloride resin, acrylonitrile styrene resin, ethylene vinyl acetate resin, polycarbonate resin, acetal resin, Polyamide resins and various waxes are used.
【0010】上記樹脂のうち好ましいものは融点又は軟
化点が約150℃以下、好ましくは130℃以下の常温
で固体の樹脂である。顔料と樹脂成分との比率は、その
着色樹脂組成物の目的によって異なり、高濃度組成物の
場合は約20〜70重量%であり、更に使用目的の樹脂
に添加して希釈混練する場合は約0.01〜10重量%
である。Preferred among the above resins are resins which have a melting point or softening point of about 150 ° C. or lower, and are preferably solid at room temperature of 130 ° C. or lower. The ratio between the pigment and the resin component varies depending on the purpose of the colored resin composition, and is about 20 to 70% by weight in the case of a high-concentration composition. 0.01 to 10% by weight
It is.
【0011】本発明で使用する水としては、イオン交換
水、飲料水、蒸留水、水蒸気、工業用水等が使用され
る。水の添加量は、乾燥顔料と樹脂の総重量に対して1
〜200重量%、好ましくは5〜100重量%である。
本発明における方法は、上記の如き乾燥顔料と熱熔融性
樹脂と水とを混練機に仕込み加圧下又は常圧で加熱熔融
する方法である。混練機中の混練は樹脂の熔融している
状態で行われるので温度は70〜130℃程度で行われ
る。As the water used in the present invention, ion-exchanged water, drinking water, distilled water, steam, industrial water and the like are used. The amount of water added is 1 to the total weight of the dry pigment and the resin.
200200% by weight, preferably 5-100% by weight.
The method of the present invention is how you heat melting <br/> A charge pressure or normal pressure kneader and such dry pigment and hot-melt resin and water mentioned above. Since the kneading in the kneading machine is performed in a state where the resin is molten, the kneading is performed at a temperature of about 70 to 130 ° C.
【0012】製造に際しては予め粉末顔料と熱熔融性樹
脂と水とをヘンシルミキサー等で混合し、フラッシャ
ー、ニーダー、押出機、ロールミル等に仕込み或はフラ
ッシャー、ニーダーの場合は粉末顔料と熱熔融性樹脂と
水とを仕込み混合する。次いで加圧下又は常圧で加熱し
て樹脂を熔融させて混練分散し、次いで残留している水
分の除去は常圧又は減圧下で蒸発させて乾燥し、顔料樹
脂混練物が得られる。次いで更に使用目的の被着色樹脂
に添加して希釈混練して分散良好で鮮明な着色樹脂を製
造することが出来る。At the time of production, a powder pigment, a hot-melt resin and water are mixed in advance with a Hensyl mixer or the like, and the mixture is charged into a flasher, kneader, extruder, roll mill, or the like. The water-soluble resin and water are charged and mixed. Then heated under pressure or normal pressure to melt the resin by kneading and dispersing, followed by removal of water remaining was dried by atmospheric pressure or evaporated under reduced pressure, the pigment resin kneaded product are obtained. Then, it is further added to the resin to be colored for use and diluted and kneaded to produce a clear and clear colored resin with good dispersion.
【0013】[0013]
【実施例】次に実施例を挙げて本発明を更に具体的に説
明する。尚、文中、部又は%とあるのは重量基準であ
る。 実施例1 ACポリエチレン6A(アライドケミカル&ダイコーポ
レーション社製)100部及び安定型銅フタロシアニン
ブルー粉末顔料(CIピグメントブルー15:3)60
部及びイオン交換水80部をニーダー型混練機に仕込み
10分間混合し、樹脂微粉末及び粉末顔料をイオン交換
水で湿潤し、そのまま徐々に加熱した。ほぼ95〜11
0℃で樹脂が溶融し、水が混在した状態で混練し水を蒸
発させながら20分間95〜110℃で混練し、次に1
20℃に昇温して混練を続け残留している水分を蒸発さ
せ、脱水乾燥させた。更に120〜130℃にて10分
間混練を続けた。Next, the present invention will be described more specifically with reference to examples. In the description, parts or% are based on weight. Example 1 100 parts of AC polyethylene 6A (manufactured by Allied Chemical & Die Corporation) and stable copper phthalocyanine blue powder pigment (CI Pigment Blue 15: 3) 60
And 80 parts of ion-exchanged water were charged into a kneader-type kneader, mixed for 10 minutes, and the resin fine powder and the powder pigment were wetted with ion-exchanged water and heated gradually as it was. Almost 95-11
The resin is melted at 0 ° C, kneaded in a state where water is mixed, and kneaded at 95 to 110 ° C for 20 minutes while evaporating water.
The temperature was raised to 20 ° C., and the kneading was continued to evaporate the remaining water, followed by dehydration and drying. Kneading was further continued at 120 to 130 ° C. for 10 minutes.
【0014】冷却後更に加熱3本ロールにより混練し、
冷却及び粗砕して青色顔料を30%の濃度で含有する高
濃度着色樹脂組成物を得た。これをスライドグラスに乗
せて加熱溶融させて顕微鏡観察したところ、顔料粒子は
全て微細に分散しており、粗大粒子は認められなかっ
た。上記組成物1部とポリエチレン(住友化学社製、ス
ミカセンG−201)100部とを押出機にて混練して
鮮明に着色された樹脂を得た。これを同様な方法で顕微
鏡で観察したところ、顔料粒子は全て微細に分散してお
り、粗大粒子は認められなかった。After cooling, the mixture is further kneaded with three heated rolls.
After cooling and crushing, a high-concentration colored resin composition containing a blue pigment at a concentration of 30% was obtained. This was placed on a slide glass, heated and melted, and observed under a microscope. As a result, all the pigment particles were finely dispersed, and no coarse particles were observed. One part of the above composition and 100 parts of polyethylene (Sumikasen G-201, manufactured by Sumitomo Chemical Co., Ltd.) were kneaded with an extruder to obtain a sharply colored resin. When this was observed with a microscope by the same method, all the pigment particles were finely dispersed, and no coarse particles were recognized.
【0015】 実施例2 エポキシ樹脂(シェル石油社製、エピコート1004)
100部及びカーミン6B(C.I.ピグメントレッド
57:1)80部の粉末乾燥顔料及びイオン交換水11
0部をニーダー型混練機に仕込み10分間混合し、樹脂
微粉末及び粉末顔料をイオン交換水で湿潤し、そのまま
徐々に加熱した。ほぼ95〜110℃で樹脂が溶融し、
水が混在した状態で混練し水を蒸発させながら20分間
95〜110℃で混練し、次に120℃に昇温して混練
を続け残留している水分を蒸発させて脱水乾燥させた。Example 2 Epoxy resin (Epicoat 1004, manufactured by Shell Sekiyu KK)
100 parts of powdered pigment and 80 parts of carmine 6B (CI Pigment Red 57: 1) and ion-exchanged water 11
0 parts were charged into a kneader-type kneader, mixed for 10 minutes, and the resin fine powder and the powder pigment were wetted with ion-exchanged water and gradually heated as it was. The resin melts at about 95-110 ° C,
The mixture was kneaded in a state where water was mixed, and the mixture was kneaded at 95 to 110 ° C. for 20 minutes while evaporating the water. Then, the temperature was raised to 120 ° C., and the kneading was continued to evaporate the remaining moisture and dehydrate and dry.
【0016】更に120〜130℃にて10分間混練を
続けた。冷却後更に加熱3本ロールにより混練し、冷却
及び粗砕して青色顔料を30%の濃度で含有する高濃度
着色樹脂組成物を得た。これをスライドグラスに乗せて
加熱溶融させて顕微鏡観察したところ、顔料粒子は全て
微細に分散しており、粗大粒子は認められなかった。上
記組成物1部とエポキシ樹脂100部を粉体同士で混合
後押出機にて混練して鮮明に着色された樹脂を得た。こ
れをスライドグラスに乗せ加熱溶融させて顕微鏡で観察
したところ、顔料粒子は全て微細に分散しており、粗大
粒子は認められなかった。The kneading was further continued at 120 to 130 ° C. for 10 minutes. After cooling, the mixture was further kneaded with a heating three rolls, cooled and crushed to obtain a high-concentration colored resin composition containing a blue pigment at a concentration of 30%. This was placed on a slide glass, heated and melted, and observed under a microscope. As a result, all the pigment particles were finely dispersed, and no coarse particles were observed. One part of the above composition and 100 parts of the epoxy resin were mixed together in a powder extruder and kneaded with an extruder to obtain a sharply colored resin. This was placed on a slide glass, heated and melted, and observed with a microscope. As a result, all the pigment particles were finely dispersed, and no coarse particles were observed.
【0017】 実施例3 メチルメタクリレート樹脂(三洋化成社製、ハイマーS
BM600)100部及びポリ縮合アゾ顔料(C.I.
ピグメントイエロー128)70部の粉末乾燥顔料及び
イオン交換水100部をニーダー型混練機に仕込み10
分間混合し、樹脂微粉末及び粉末顔料をイオン交換水で
湿潤し、そのまま徐々に加熱した。ほぼ95〜110℃
で樹脂が溶融し、水が混在した状態で混練し水を蒸発さ
せながら20分間95〜110℃で混練し次に120℃
に昇温して混練を続け残留している水分を蒸発させて脱
水乾燥させた。更に120〜130℃にて10分間混練
を続けた。Example 3 Methyl methacrylate resin (manufactured by Sanyo Chemical Industries, Hymer S)
BM600) and 100 parts of a polycondensed azo pigment (C.I.
Pigment Yellow 128) 70 parts of the powdery dry pigment and 100 parts of ion-exchanged water are charged into a kneader-type kneader.
After mixing for 1 minute, the resin fine powder and the powder pigment were wetted with ion-exchanged water and gradually heated. About 95-110 ° C
The resin is melted and kneaded in a state where water is mixed, and the mixture is kneaded at 95 to 110 ° C. for 20 minutes while evaporating water, and then 120 ° C.
The mixture was further kneaded to continue the kneading, evaporating the remaining water and dehydrating and drying. Kneading was further continued at 120 to 130 ° C. for 10 minutes.
【0018】冷却後更に加熱3本ロールにより混練し、
冷却及び粗砕して青色顔料を30%の濃度で含有する高
濃度着色樹脂組成物を得た。これをスライドグラスに乗
せて加熱溶融させて顕微鏡観察したところ、顔料粒子は
全て微細に分散しており、粗大粒子は認められなかっ
た。上記組成物1部とメチルメタクリレート樹脂100
部を粉体混合後押出機にて混練して鮮明に着色された樹
脂を得た。これをスライドグラスに乗せ加熱溶融させて
顕微鏡で観察したところ、顔料粒子は全て微細に分散し
ており、粗大粒子は認められなかった。After cooling, the mixture is further kneaded with three heated rolls.
After cooling and crushing, a high-concentration colored resin composition containing a blue pigment at a concentration of 30% was obtained. This was placed on a slide glass, heated and melted, and observed under a microscope. As a result, all the pigment particles were finely dispersed, and no coarse particles were observed. 1 part of the above composition and methyl methacrylate resin 100
After mixing the powder, the mixture was kneaded with an extruder to obtain a sharply colored resin. This was placed on a slide glass, heated and melted, and observed with a microscope. As a result, all the pigment particles were finely dispersed, and no coarse particles were observed.
【0019】 実施例4 ポリエステル樹脂(東レ社製、ケットR247)100
部及びジメチルキナクリドン(C.I.ピグメントレッ
ド57:1)60部の粉末乾燥顔料及び水90部をニー
ダー型混練機に仕込み10分間混合し、樹脂微粉末及び
粉末顔料をイオン交換水で湿潤し、そのまま徐々に加熱
した。ほぼ90〜100℃で樹脂が溶融し、水が混在し
た状態で混練し水を蒸発させながら20分間90〜10
0℃で混練し次に120℃に昇温して混練を続け残留し
ている水分を蒸発させ、脱水乾燥させた。Example 4 Polyester Resin (Ket R247, manufactured by Toray Industries, Inc.) 100
And 90 parts of water and 90 parts of dimethylquinacridone (CI Pigment Red 57: 1) were charged into a kneader-type kneader and mixed for 10 minutes, and the resin fine powder and the powder pigment were wetted with ion-exchanged water. And gradually heated. The resin melts at about 90 to 100 ° C, and is kneaded in a state where water is mixed, and the water is evaporated for 90 minutes to 90 to 90 ° C.
After kneading at 0 ° C., the temperature was raised to 120 ° C., and the kneading was continued to evaporate the remaining water, followed by dehydration and drying.
【0020】更に120〜130℃にて10分間混練を
続けた。冷却後更に加熱3本ロールにより混練し、冷却
及び粗砕して青色顔料を30%の濃度で含有する高濃度
着色樹脂組成物を得た。これをスライドグラスに乗せて
加熱溶融させて顕微鏡観察したところ、顔料粒子は全て
微細に分散しており、粗大粒子は認められなかった。上
記組成物1部とポリエステル樹脂100部を粉体混合後
押出機にて混練して鮮明に着色された樹脂を得た。これ
をスライドグラスに乗せ加熱溶融させて顕微鏡で観察し
たところ、顔料粒子は全て微細に分散しており、粗大粒
子は認められなかった。Kneading was further continued at 120 to 130 ° C. for 10 minutes. After cooling, the mixture was further kneaded with a heating three rolls, cooled and crushed to obtain a high-concentration colored resin composition containing a blue pigment at a concentration of 30%. This was placed on a slide glass, heated and melted, and observed under a microscope. As a result, all the pigment particles were finely dispersed, and no coarse particles were observed. One part of the above composition and 100 parts of a polyester resin were mixed with a powder and kneaded with an extruder to obtain a sharply colored resin. This was placed on a slide glass, heated and melted, and observed with a microscope. As a result, all the pigment particles were finely dispersed, and no coarse particles were observed.
【0021】 実施例5 ポリスチレン樹脂(三洋化成社製、ハイマーST−9
5)100部及び安定型銅フタロシアニンブルー顔料6
0部の粉末顔料及び水80部をニーダー型混練機に仕込
み10分間混合し、樹脂微粉末及び粉末顔料をイオン交
換水で湿潤し、そのまま徐々に加熱した。ほぼ90〜1
00℃で樹脂が溶融し、水が混在した状態で混練し水を
蒸発させながら20分間90〜100℃で混練し次に1
20℃に昇温して混練を続け残留している水分を蒸発さ
せ、脱水乾燥させた。更に120〜130℃にて10分
間混練を続けた。冷却後更に加熱3本ロールにより混練
し、冷却及び粗砕して青色顔料を30%の濃度で含有す
る高濃度着色樹脂組成物を得た。これをスライドグラス
に乗せて加熱溶融させて顕微鏡観察したところ、顔料粒
子は全て微細に分散しており、粗大粒子は認められなか
った。Example 5 Polystyrene resin (manufactured by Sanyo Chemical Co., Ltd., Hymer ST-9)
5) 100 parts and stable copper phthalocyanine blue pigment 6
0 parts of the powder pigment and 80 parts of water were charged into a kneader type kneader and mixed for 10 minutes, and the resin fine powder and the powder pigment were wetted with ion-exchanged water and heated gradually as it was. Almost 90-1
The resin is melted at 00 ° C., kneaded in a state where water is mixed, and kneaded at 90-100 ° C. for 20 minutes while evaporating water.
The temperature was raised to 20 ° C., and the kneading was continued to evaporate the remaining water, followed by dehydration and drying. Kneading was further continued at 120 to 130 ° C. for 10 minutes. After cooling, the mixture was further kneaded with a heating three rolls, cooled and crushed to obtain a high-concentration colored resin composition containing a blue pigment at a concentration of 30%. This was placed on a slide glass, heated and melted, and observed under a microscope. As a result, all the pigment particles were finely dispersed, and no coarse particles were observed.
【0022】上記組成物1部とポリスチレン樹脂100
部を粉体混合後押出機にて混練して鮮明に着色された樹
脂を得た。これをスライドグラスに乗せ加熱溶融させて
顕微鏡で観察したところ、顔料粒子は全て微細に分散し
ており、粗大粒子は認められなかった。One part of the above composition and polystyrene resin 100
After mixing the powder, the mixture was kneaded with an extruder to obtain a sharply colored resin. This was placed on a slide glass, heated and melted, and observed with a microscope. As a result, all the pigment particles were finely dispersed, and no coarse particles were observed.
【0023】[0023]
【効果】以上の如き本発明によれば、分散助剤としての
水を添加して加圧下又は常圧で加熱混練することにより
次の様な効果が期待出来る。先ず第1に、分散効果が通
常の乾式混練方法よりはるかに向上し、機械的分散では
得られない微粒子分散が可能となる。第2として、使用
する水分量は分散に必要な適量を添加することで足り、
従ってそれを混練後除去する場合は加熱又は減圧下で蒸
発させるだけでよい。According to the present invention as described above, the following effects can be expected by adding water as a dispersing aid and kneading under pressure or under normal pressure. First, the dispersing effect is much improved as compared with the ordinary dry kneading method, and fine particle dispersion that cannot be obtained by mechanical dispersion can be achieved. Second, the amount of water to be used is sufficient by adding an appropriate amount necessary for dispersion.
Therefore, when it is removed after kneading, it is only necessary to evaporate under heating or reduced pressure.
【0024】第3として、水添加により熔融物と混練機
の金属部分との離型性がよくなり、水の蒸気圧により熔
融物が膨張し、均一分散がスムーズに進む。第4に、常
圧で混練する場合は、水の蒸発潜熱を利用することによ
り混練の摩擦熱等による温度上昇を抑えることも出来、
更に水を追加することで長時間の混練を可能にし、顔料
の分散をより完全なものとすることが出来る。又、この
様にして得られた着色剤組成物を、更に必要に応じて使
用目的の樹脂に添加して希釈混練することにより分散性
の優れた鮮明な実用顔料濃度の着色樹脂組成物を得るこ
とが出来る。Third, the releasability between the melt and the metal part of the kneader is improved by the addition of water, the melt expands due to the vapor pressure of water, and uniform dispersion proceeds smoothly. Fourth, when kneading at normal pressure, the temperature rise due to frictional heat of kneading can be suppressed by utilizing the latent heat of evaporation of water,
Further, by adding water, kneading can be performed for a long time, and the pigment can be more completely dispersed. Further, the colorant composition thus obtained is further added to a resin for use as needed, and the mixture is diluted and kneaded to obtain a colored resin composition having excellent dispersibility and a clear practical pigment concentration. I can do it.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 中村 道衛 東京都中央区日本橋馬喰町1丁目7番6 号 大日精化工業株式会社内 (72)発明者 中村 允昌 東京都中央区日本橋馬喰町1丁目7番6 号 大日精化工業株式会社内 (72)発明者 浜田 寿治 東京都中央区日本橋馬喰町1丁目7番6 号 大日精化工業株式会社内 (56)参考文献 特開 昭53−88844(JP,A) 特開 平3−47710(JP,A) 特開 平6−148937(JP,A) (58)調査した分野(Int.Cl.6,DB名) B29B 7/88 ──────────────────────────────────────────────────続 き Continuing on the front page (72) Michie Nakamura 1-7-6 Nihombashi Bakurocho, Chuo-ku, Tokyo Inside Dainichi Seika Kogyo Co., Ltd. (72) Yoshimasa Nakamura 1-chome Nihonbashi Bakurocho, Chuo-ku, Tokyo No. 7 in Dainichi Seika Kogyo Co., Ltd. (72) Inventor Jusuji Hamada 1-7-6 Nihonbashi Bakurocho, Chuo-ku, Tokyo In Dainichi Seika Kogyo Co., Ltd. (56) References JP-A-53-88844 (JP) JP-A-3-47710 (JP, A) JP-A-6-148937 (JP, A) (58) Fields investigated (Int. Cl. 6 , DB name) B29B 7/88
Claims (7)
料を樹脂に微細に分散させた顔料樹脂組成物において、
乾燥顔料と熱熔融性樹脂及び分散助剤としての水とを混
合機或は混練機に仕込み混合して顔料及び樹脂を湿潤
し、加圧下又は常圧下で加熱して樹脂を熔融させて加熱
混練した後、水分を常圧或は減圧下で蒸発させて乾燥除
去することを特徴とする着色樹脂組成物。1. A pigment resin composition in which a pigment is finely dispersed in a resin, which is used for purposes other than image recording .
A dry pigment, a hot-melt resin and water as a dispersing agent are charged and mixed in a mixer or kneader to wet the pigment and the resin, and then heated under pressure or normal pressure to melt the resin and heat-knead. after, moisture normally圧或colored resin composition characterized and Turkey be dried removed by evaporation under reduced pressure.
び/又は無機顔料である請求項1に記載の着色樹脂組成
物。2. The colored resin composition according to claim 1, wherein the pigment is a chromatic, black or white organic pigment and / or an inorganic pigment.
対して1〜200重量部である請求項1に記載の着色樹
脂組成物。3. The colored resin composition according to claim 1, wherein the water content is 1 to 200 parts by weight based on 100 parts by weight of the total amount of the pigment and the resin.
する固体状の組成物である請求項1に記載の着色樹脂組
成物。4. The colored resin composition according to claim 1, wherein the colored resin composition is a solid composition containing a pigment at a high concentration.
使用目的の被着色樹脂に添加して希釈混練してなること
を特徴とする着色樹脂組成物。5. A colored resin composition obtained by adding the colored resin composition according to claim 1 to a resin to be colored and diluting and kneading it.
樹脂組成物の製造において、乾燥顔料と熱熔融性樹脂及
び分散助剤としての水とを混合機、或は混練機に仕込み
混合して顔料及び樹脂を湿潤し、加圧下又は常圧下で加
熱して樹脂を熔融させて顔料と樹脂とを加熱混練した
後、水分を常圧或は減圧下で蒸発させて乾燥除去するこ
とを特徴とする着色樹脂組成物の製造方法。6. Coloring used for purposes other than image recording
In the production of a resin composition, a dry pigment and a hot-melt resin and water as a dispersing aid are mixed in a mixer or kneader, mixed and wetted, and the pigment and the resin are wetted and heated under pressure or under normal pressure. after by melting the resin by heating and kneading a pigment and a resin Te, moisture normally圧或the method for producing a colored resin composition, wherein the dry removal to Turkey <br/> evaporated under reduced pressure.
目的の被着色樹脂に添加して希釈混練することを特徴と
する着色樹脂組成物の製造方法。7. A method for producing a colored resin composition, comprising adding the colored resin composition according to claim 6 to a resin to be colored and diluting and kneading the resin.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4315616A JP2990212B2 (en) | 1992-11-02 | 1992-11-02 | Colored resin composition and method for producing the same |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4315616A JP2990212B2 (en) | 1992-11-02 | 1992-11-02 | Colored resin composition and method for producing the same |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH06143253A JPH06143253A (en) | 1994-05-24 |
| JP2990212B2 true JP2990212B2 (en) | 1999-12-13 |
Family
ID=18067511
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP4315616A Expired - Fee Related JP2990212B2 (en) | 1992-11-02 | 1992-11-02 | Colored resin composition and method for producing the same |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2990212B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2005306986A (en) * | 2004-04-21 | 2005-11-04 | Tokyo Printing Ink Mfg Co Ltd | Colorant for polyolefin resin and its production method |
-
1992
- 1992-11-02 JP JP4315616A patent/JP2990212B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH06143253A (en) | 1994-05-24 |
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