首页> 外国专利> Ruthenium catalysts, their production and a process for the preparation of cycloaliphatic polyamines using these catalysts

Ruthenium catalysts, their production and a process for the preparation of cycloaliphatic polyamines using these catalysts

机译:钌催化剂,它们的生产以及使用这些催化剂制备脂环族多胺的方法

摘要

Novel ruthenium catalysts (I) additionally contain hydroxides and/or hydrated oxides of cerium and manganese and/or their dehydration products. Claimed prepn. of ruthenium catalysts (not restricted to (I)) involves converting soluble cpds. of Ru, Ce and Mn into insoluble cpds. and opt. post-treating the products. Also claimed is the prepn. of cycloaliphatic polyamines (II) by hydrogenation of the corresp. aromatic amines (III), using (I) (where Ru is in metal or bonded form) as catalyst. (I) has Ru content 0.1-10 wt.% (as the element), and Mn:Ce wt. ratio 0.3-5.1 (as elements). (I) may additionally contain additives, auxiliaries and/or carriers. (I) is prepd. from Ru(NO3)2 and/or RuCl3, Ce(NO3)3 and Mn(NO3)2, using an alkaline cpd. as precipitant. The ppte, is post-treated by filtration, washing out soluble components, heat-treating shaping and/or reducing the Ru component to the metal. Esp. post-treatment involves drying at 120 degrees C then calcining at 200-450 degrees C. (III) is a di- or triaminobenzene deriv. of formula (IIIa), a di-, tri- or tetraamino-naphthalene of formula (IIIc): R1-R4 = H or 1-10C alkyl; R5, R6, R5a, R6a = H or OH, or 1-10C alkyl, 5-10C cycloalkyl or 6-14C aryl (all opt. substd. by OH and/or NH2); n = 1 or 2; m, m1 = 0-2, where m + m1 = at least 2; R7, R8 = H or 1-10C alkyl (pref. the same Me, Et or iPr). Hydrogenation is effected at 100-360 degrees C and 50-100 bar, using 0.005-0.5 g Ru (as metal) per kg of (III).
机译:新型钌催化剂(I)还包含铈和锰的氢氧化物和/或水合氧化物和/或其脱水产物。声称的准备。钌催化剂(不限于(I))的制备涉及转化可溶性cpds。将Ru,Ce和Mn转化为不溶的cpds。并选择。对产品进行后处理。还声称是prepn。通过氢化相应的化合物制备环脂族多胺(II)。芳香胺(III),使用(I)(其中Ru为金属或键合形式)作为催化剂。 (I)的Ru含量为0.1-10重量%(以元素计),Mn∶Ce重量%。比率0.3-5.1(作为元素)。 (I)可以另外包含添加剂,助剂和/或载体。 (一)准备。使用碱性cpd从Ru(NO3)2和/或RuCl3,Ce(NO3)3和Mn(NO3)2中提取。作为沉淀物。通过过滤,洗出可溶性成分,热处理定形和/或将Ru成分还原为金属对ppte进行后处理。 Esp。后处理包括在120摄氏度下干燥,然后在200-450摄氏度下煅烧。(III)是二氨基或三氨基苯衍生物。式(IIIa)的式(IIIc)的二,三或四氨基萘:R 1 -R 4 = H或1-10C烷基; R 5,R 6,R 5a,R 6a = H或OH,或1-10C烷基,5-10C环烷基或6-14C芳基(均由OH和/或NH2); n = 1或2; m,m 1 = 0-2,其中m + m 1 =至少2; R 7,R 8 = H或1-10C烷基(优选相同的Me,Et或iPr)。氢化在100-360摄氏度和50-100巴下进行,每公斤(III)使用0.005-0.5 g Ru(作为金属)。

著录项

相似文献

  • 专利
  • 外文文献
  • 中文文献
获取专利

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号