会员体验
专利管家(专利管理)
工作空间(专利管理)
风险监控(情报监控)
数据分析(专利分析)
侵权分析(诉讼无效)
联系我们
交流群
官方交流:
QQ群: 891211   
微信请扫码    >>>
现在联系顾问~
热词
    • 13. 发明授权
    • Method for the production of aldehydes
    • 醛的生产方法
    • US06310261B1
    • 2001-10-30
    • US09582780
    • 2000-07-03
    • Bernhard GeisslerMichael RöperEdgar ZellerRocco PacielloJürgen DeckerHartwig VossNorbert Mahr
    • Bernhard GeisslerMichael RöperEdgar ZellerRocco PacielloJürgen DeckerHartwig VossNorbert Mahr
    • C07C4550
    • C08G73/0206B01J31/1658B01J31/1805B01J2231/321B01J2531/80B01J2531/822C07C45/50Y02P20/584C07C47/02
    • The invention relates to a method for the production of aldehydes or aldehydes and alcohols by hydroformylation of olefins in the presence of a complexing catalyst homogeneously dissolved in a reaction mixture, containing a metal of Group VIIIa of the periodic table of the elements and a phosphorus-free, polydentate nitrogen compound suitable for complex formation as ligand at temperatures ranging from 50 to 100° C. and pressures from 20 to 1,000 bar and recirculating the catalyst complex in the hydroformylation reaction, wherein a) derivatized polyamines are used that are substantially non-water soluble and suitable for complex formation and have a mean molecular weight of more than 1,000 Dalton and at least 10 nitrogen atoms; b) the catalyst complex remaining in the bottom of the distillation column and the excess ligands obtained from the reaction mixture are recirculated totally or partially in the hydroformylation once the hydroformylation reaction and the separation or partial separation by distillation of the aldehydes and the alcohols has been completed; c) continues or at least batchwise evacuation of at least part of the high boiler from the bottom of the distillation of the reaction mixture is then carried out.
    • 本发明涉及通过在均匀溶解在含有元素周期表第Ⅷa族金属的反应混合物的络合催化剂存在下烯烃的加氢甲酰化生产醛或醛和醇的方法, 在50至100℃的温度和20至1,000巴的压力下适合于络合物形成配位体的多余的多齿氮化合物,并且在加氢甲酰基化反应中再循环催化剂配合物,其中a)使用基本上不相容的衍生的多胺, 水溶性且适合于络合物形成,并且具有大于1,000道尔顿和至少10个氮原子的平均分子量; b)一旦加氢甲酰化反应和通过蒸馏醛和醇的分离或部分分离已经被残留在蒸馏塔底部的催化剂络合物和从反应混合物中得到的过量配体在加氢甲酰化反应中被全部或部分再循环 完成 c)然后执行从反应混合物的蒸馏底部继续或至少间歇抽出高锅炉的至少一部分。