摘要
在国产３８２５型加氢裂化催化剂上，利用连续流动固定床微型反应装置，在４．５～８．５ＭＰａ和３２０～３８０℃条件下，测定了四氢萘加氢反应动力学数据，建立了四氢萘加氢裂化的反应网络和动力学模型。
The kinetic data of tetralin hydrocracking reaction on the 3825 catalyst were obtained in a continuous now fixed-bed microreactor at a temperature range of 320￣380℃ and a pressure rangs of 4. 5-8.5MPa. The reaction network and kinetic model-for tetralin hydrocracking were thus established.
出处
《工业催化》
CAS
1995年第4期26-29,共4页
Industrial Catalysis
基金
中国石化总公司资助
