首页> 外国专利> A SUPPORT FOR SILVER CATALYST USED IN THE ETHYLENE OXIDE PRODUCTION, A PREPARATION METHOD FOR THE SAME, A SILVER CATALYST PREPARED FROM THE SAME, AND ITS USE IN THE ETHYLENE OXIDE PRODUCTION

A SUPPORT FOR SILVER CATALYST USED IN THE ETHYLENE OXIDE PRODUCTION, A PREPARATION METHOD FOR THE SAME, A SILVER CATALYST PREPARED FROM THE SAME, AND ITS USE IN THE ETHYLENE OXIDE PRODUCTION

机译:在环氧乙烷生产中使用的银催化剂的支持,其制备方法,由其制备的银催化剂及其在环氧乙烷生产中的用途

摘要

Purpose: for generating a silver catalyst bracket of ethylene oxide, a method of for manufacturing silver catalyst, silver catalyst manufacture is arranged to improve the selectivity of silver catalyst using silver catalyst by identical. ;Construction: the main crystalline phase of an alumina support structure is Alpha-alumina. The specific surface area of bracket is less than or equal to 3.0 m^2/g, preferably 0.5 and 2.0 m^2/g.Between range in the pore space of bracket arrived the range 0. between3 and 0.8 mls/g, preferably 0.4 and 0.7 ml/g.In range between the content of alkali earth metal, preferably barium, in the bracket in 0.05 and 1.Range between 8 wt%, preferably 0.1 and 1.In range between 0 wt%. Fluorine atom percentage on the surface of bracket is in 0.3 and 8.Range between the % of 0 atom, in the range preferably between 0. 5 and 5.The % of 0 atom is based on X-Ray Photoelectron Spectroscopy. ;Copyright KIPO 2012
机译:目的:为了产生环氧乙烷的银催化剂支架,制造银催化剂的方法,安排银催化剂的制造以相同的方式提高使用银催化剂的银催化剂的选择性。 ;构造:氧化铝载体结构的主要结晶相是α-氧化铝。托槽的比表面积小于或等于3.0m ^ 2 / g,优选0.5和2.0m ^ 2 / g。托槽的孔隙空间之间的范围达到0.3至0.8mls / g,优选托架中碱土金属,优选钡的含量在0.4和0.7ml / g之间。范围在0.05和1之间。范围在8wt%之间,优选在0.1和1之间。在0wt%之间。托架表面上的氟原子百分比在0.3和8之间。0原子的百分比之间的范围,优选在0. 5至5之间的范围内。0原子的百分比基于X射线光电子能谱。 ;版权KIPO 2012

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