Characteristics and kinetics of steam-gasification regeneration for Coked FCC catalyst in a micro-fluidized bed reactor

被引：0
|
作者：
Zhang, Yuming [1 ,2 ]
Sun, Guogang [1 ]
Gao, Shiqiu [2 ]
Xu, Guangwen [2 ]
机构：
[1] State Key Laboratory of Heavy Oil Processing, China University of Petroleum, Beijing,102249, China
[2] State Key Laboratory of Multiphase Complex Systems, Institute of Process Engineering, Chinese Academy of Sciences, Beijing,100190, China
来源：
Shiyou Xuebao, Shiyou Jiagong/Acta Petrolei Sinica (Petroleum Processing Section) | 2014年 / 30卷 / 06期
关键词：
Carbon - Activation energy - Cracks - Coke - Fluidized beds - Supersaturation - Heavy oil production - Reaction kinetics - Chemical reactors - Crude oil - Fluidized bed furnaces - Fluid catalytic cracking - Pore size - Steam;
D O I：
10.3969/j.issn.1001-8719.2014.06.013
中图分类号：
学科分类号：
摘要：
引用
收藏
页码：1043 / 1051
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