摘要
The TPR experiments and DTA TG results showed that catalyst Pt Sn K/Al 2O 3 had a better selectivity(94 60%) and yield(48 71%) for isobutane dehydrogenation than Pt Sn/Al 2O 3.
The TPR experiments and DTA TG results showed that catalyst Pt Sn K/Al 2O 3 had a better selectivity(94 60%) and yield(48 71%) for isobutane dehydrogenation than Pt Sn/Al 2O 3.
出处
《应用化学》
CAS
CSCD
北大核心
1999年第4期111-113,共3页
Chinese Journal of Applied Chemistry
基金
中国科学院"九五"重大项目
关键词
异丁烷
脱氢
催化剂
铂
锡
钾
异丁烯
isobutane,dehydrogenation,Pt Sn K/Al 2O 3,supported catalyst
