摘要
在重整催化剂烧焦动力学研究的基础上,对连续重整移动床径向再生器中烧炭区的工艺过程进行了数学模拟,计算所得床层温度分布及床层长度等结果与工业生产的实际状况基本吻合.
Based or the kinetics study of combustion of coke on catalytic reforming catalyst, the coke burning in the moving bed radial regenerator in continuous regenerative catalytic reformer was simulated mathematically. The calculated temperature distribution in coke burning zone and bed length required were basically consistent with those in commercial practice.
出处
《炼油设计》
1995年第1期42-45,52,共5页
Petroleum Refinery Engineering
