首页> 外国专利> Laboratory reactor for kinetic study of monodispersed catalyst reactions of liquid gas or liquid, comprises a spiral tube, which has a succession of curves for the cocurrent downward flow of the liquid gas or liquid

Laboratory reactor for kinetic study of monodispersed catalyst reactions of liquid gas or liquid, comprises a spiral tube, which has a succession of curves for the cocurrent downward flow of the liquid gas or liquid

机译:用于液体气体或液体的单分散催化剂反应动力学研究的实验室反应器,包括一个螺旋管,该螺旋管具有用于液体气体或液体并流向下流动的一系列曲线

摘要

The laboratory reactor comprises a spiral tube, which has a succession of curves for the cocurrent downward flow of the liquid gas or liquid. The catalyst is present in the form of solid particles of diameter (D) of 0.5-4 mm. The reactor has a catalytic volume V of 10-1 cm 3. The liquid gas or liquid flows in the downward direction. The diameter of the reactor is lower than 8 mm. The reaction is a solid liquid reaction. A certain amount of inert gas is introduced in the reactor so that the superficial velocity of gas is 10% of superficial velocity of the liquid. The laboratory reactor comprises a spiral tube, which has a succession of curves for the cocurrent downward flow of the liquid gas or liquid. The catalyst is present in the form of solid particles of diameter (D) of 0.5-4 mm. The reactor has a catalytic volume V of 10-1 cm 3. The liquid gas or liquid flows in the downward direction. The diameter of the reactor is lower than 8 mm. The reaction is a solid liquid reaction. A certain amount of inert gas is introduced in the reactor so that the superficial velocity of gas is 10% of superficial velocity of the liquid. The solid catalyst has extruded or lobed shape with a diameter of 1-3 mm, or is present in the form of a ball. The catalyst is poly dispersed in which it is represented by two distinct populations of average diameter, where the ratio of the average larger diameter to average smaller diameter is greater than 3.
机译:实验室反应器包括螺旋管,该螺旋管具有用于气体或液体的并流向下流动的一系列曲线。催化剂以直径(D)为0.5-4mm的固体颗粒形式存在。反应器具有10-1cm 3的催化体积V。液态气体或液体向下流动。反应器的直径小于8mm。该反应是固液反应。将一定量的惰性气体引入反应器中,使得气体的表观速度为液体的表观速度的10%。实验室反应器包括螺旋管,该螺旋管具有用于气体或液体的并流向下流动的一系列曲线。催化剂以直径(D)为0.5-4mm的固体颗粒形式存在。反应器具有10-1cm 3的催化体积V。液态气体或液体向下流动。反应器的直径小于8mm。该反应是固液反应。将一定量的惰性气体引入反应器中,使得气体的表观速度为液体的表观速度的10%。固体催化剂具有直径为1-3mm的挤出或裂片形状,或以球的形式存在。催化剂是多分散的,其中由两个不同的平均直径群体表示,其中平均较大直径与平均较小直径之比大于3。

著录项

  • 公开/公告号FR2941632A1

    专利类型

  • 公开/公告日2010-08-06

    原文格式PDF

  • 申请/专利权人 IFP;

    申请/专利号FR20090000450

  • 发明设计人 ROLLAND MATTHIEU;

    申请日2009-02-02

  • 分类号B01J8/06;B01L5/00;

  • 国家 FR

  • 入库时间 2022-08-21 18:26:37

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