首页> 外国专利> Method for the production of N,N'-dialkyl perylene-3,4,9,10-tetracarboxylic acid diimides in a transparent pigment form

Method for the production of N,N'-dialkyl perylene-3,4,9,10-tetracarboxylic acid diimides in a transparent pigment form

机译:透明颜料形式的N,N′-二烷基per-3,4,9,10-四羧酸二酰亚胺的生产方法

摘要

Preparation of N,N'-dimethyl-perylene-3,4,9,10-tetracarbodiimide (I) involves reacting the dianhydride (II) with NOTLESS 2 mole monomethylamine (III)/mole (II) and NOTLESS 3 times its mass of water at 50-200 degrees C and distilling off unreacted (III). The crude pigment is milled in liquid, aqueous (organic) medium at a power density of over 1.5 kW/l and stirrer peripheral velocity of over 12 m/s, using balls with a diameter 0.9 mm and the pigment is isolated. Pigment dispersant(s) and/or surfactant(s) are added at any time but at the latest during wet milling. In the preparation of N,N'-dimethyl-perylene-3,4,9,10-tetracarbodiimide (I) by reacting perylene-3,4,9,10-tetracarboxylic dianhydride (II) with monomethylamine (III), NOTLESS 2 mole (III)/mole (II) and at least 3 times the mass of water with respect to (II) are used. Reaction is carried out at 50-200 degrees C and unreacted (III) is distilled off. The resultant crude pigment is wet milled in a liquid, aqueous or aqueous-organic medium in a stirred ball mill with a power density of over 1.5 kW/l mill capacity and stirrer peripheral velocity of over 12 m/s, using balls with a diameter 0.9 mm and the resultant pigment is isolated. Additive(s) selected from pigment dispersants and surfactants are added at any time during the process but at the latest during wet milling.
机译:N,N'-二甲基-ylene-3,4,9,10-四碳二亚胺的制备(I)包括使二酐(II)与2摩尔单甲胺(III)/摩尔(II)和3倍于其质量的三元反应将水在50-200摄氏度的温度下蒸馏除去未反应的(III)。使用直径为0.9 mm的球,在功率密度超过1.5 kW / l和搅拌器圆周速度超过12 m / s的液体,水性(有机)介质中研磨粗颜料,并分离出颜料。可以随时添加颜料分散剂和/或表面活性剂,但最迟要在湿磨过程中添加。通过使per-3,4,9,10-四羧酸二酐(II)与单甲胺(III)反应制备N,N'-二甲基-ylene-3,4,9,10-四碳二亚胺(I),NOTSLES 2摩尔(III)/摩尔(II)和相对于(II)使用至少3倍于水的质量。反应在50-200℃下进行,并蒸馏出未反应的(III)。将所得粗颜料在直径为1.5 kW / l的功率密度,搅拌器圆周速度超过12 m / s的搅拌式球磨机中在液态,水性或水性有机介质中湿磨,并使用直径为1.5mm的球。 0.9mm,分离得到的颜料。选自颜料分散剂和表面活性剂的添加剂可在加工过程中的任何时间添加,但最迟在湿磨过程中添加。

著录项

  • 公开/公告号EP0979846B1

    专利类型

  • 公开/公告日2002-02-27

    原文格式PDF

  • 申请/专利权人 CLARIANT GMBH;

    申请/专利号EP19990115365

  • 申请日1999-08-04

  • 分类号C09B5/62;C09B67/04;

  • 国家 EP

  • 入库时间 2022-08-22 00:35:19

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