摘要
采用绝热固定床积分反应器,在工业条件下(500h - 1 ,2 .6 MPa) ,对条形FeCuK 工业催化剂进行了FT合成反应性及宏观动力学考察。在稳态下,用集总的方法,保持一定的轴向温度分布及均温下,求得的宏观动力学方程,与实验数据符合较好。
Activity and macro kinetics of F T synthesis on industrial extruding shaped Fe Cu K catalyst in an adiabatic fixed bed integral reactor were studied The kinetics expression is obtained by using lumping method and keeping a certain axial temperature distribution(average temperature),and it can accord with the experiment data well The reaction was conducted under pressure 1 0~2 6MPa and SV 500h -1 The temperature range of heat point was 240~290℃.
出处
《天然气化工—C1化学与化工》
CAS
CSCD
北大核心
1999年第5期1-4,共4页
Natural Gas Chemical Industry
关键词
集总
宏观动力学
固定床反应器
费托合成
催化剂
adiabatic fixed bed integral reactor
lumping method
macro kinetics of F T synthesis
temperature distribution