首页 | 本学科首页   官方微博 | 高级检索  
     


A heterogeneous chemical reactor analysis and design laboratory: The kinetics of ammonia decomposition
Affiliation:1. Department of Chemical and Environmental Technology, Faculty of Engineering, Gunma University, 1-5-1, Tenjincho, Kiryu, Gunma 376-8515, Japan;2. Division of Environmental Engineering Science, Faculty of Science and Engineering, Gunma University, 1-5-1, Tenjincho, Kiryu, Gunma 376-8515, Japan;3. Energy Technology Research Institute, National Institute of Advanced Industrial Science and Technology, 16-1, Onogawa, Tsukuba, Ibaraki 305-8569, Japan;4. Department of Mechanical and Aerospace Engineering, SAPIENZA University of Rome, 00184 Rome, Italy;1. Institute for Sustainable Sciences and Development, Hiroshima University, 1-3-1 Kagamiyama, Higashi-Hiroshima 739-8530, Japan;2. Institute for Advanced Materials Research, Hiroshima University, 1-3-1 Kagamiyama, Higashi-Hiroshima 739-8530, Japan
Abstract:A laboratory module for senior-level reaction engineering/reactor design students is described. Students use low-conversion experimental data to explore and characterize the kinetics of ammonia decomposition over various supported catalysts at atmospheric pressure in a packed-bed reactor. Each student team is assigned one of four catalyst types, a reactor temperature, and a series of feed flow rates and compositions. Aggregate data from all student groups is then summarily analyzed per catalyst type. In each experimental trial, the reactor conversion is determined by a thermal conductivity measurement applied to the feed (reactor bypass) and reactor effluent gases. An analysis of the reaction rate across a range of temperatures and varying feed gas partial pressures allows students to test various reaction mechanisms, to suggest rate-determining steps, and to statistically determine rate law parameters. Students typically use the Langmuir–Hinshelwood–Hougen–Watson (LHHW) approach to derive rate law expressions, and determine rate constants through application of the Arrhenius equation. High student numbers (ca. 140) are accommodated through the availability of four experimental stations — each sharing a common source of feed gas and equipped with independent flow controllers and gas analyzers.
Keywords:Reaction kinetics  Plug flow reactor  Heterogeneous catalysis  Reaction engineering  Catalytic gas reactor
本文献已被 ScienceDirect 等数据库收录!
设为首页 | 免责声明 | 关于勤云 | 加入收藏

Copyright©北京勤云科技发展有限公司  京ICP备09084417号