期刊文献+

固定床催化反应器参数敏感性的研究进展 被引量:2

Research Headway of Parametric Sensitivity in Fixed Bed Catalytic Reactor
下载PDF
导出
摘要 对于在固定床催化反应器中进行的强放热反应,当初始条件达到或超过某一限度时,反应系统瞬间产生的热量超过了反应系统本身所能承受的限度或负荷,造成热点温度急剧升高,导致反应系统失去控制,对反应的转化率、选择性以及催化剂的活性和寿命等都有不良影响。对反应系统参数敏感性的研究,实质上就是从理论上揭示出反应系统安全操作上限,使之由于温度升高引起的不良后果能在反应器的设计中和操作前就能避免。文中对上述问题进行了详尽而完整的概括,对今后的发展提出了建议。 For a strong exothermic reaction in a fixed catalytic bed reactor, when the inlet parameters reach or surpass the certain limit, the heat generated by chemical reaction will greatly surpass the heat removed from reaction system, it brings about hot spot temperature to jump up rapidly and be out of control. So there are bad influences on process conversion, selectivity, catalytic activity and span-life. To study the parametric sensitivity is mainly to reveal a safe operation upper limit in theory, thus these bed effects can be avoided in the earlier stages of reactor design and before operation. This paper gives a detail and full summarization for the above problems and advice on henceforth development.
出处 《化工进展》 EI CAS CSCD 1999年第3期36-39,共4页 Chemical Industry and Engineering Progress
基金 中国石化总公司和天津市青年科学基金资助项目
关键词 固定床 催化反应器 飞温 参数敏感性 化工设备 fixed bed catalytic reactor, runaway, parametric sensitivity
  • 相关文献

参考文献6

  • 1吴2鹏 李绍芬 等.-[J].化工学报,1994,(45):422-422. 被引量:1
  • 2吴鹏 李绍芬 等.-[J].高等化学工程学报,1995,(9):162-162. 被引量:1
  • 3吴鹏,96 Asiam-Pacific Chemical Engineering,1996年 被引量:1
  • 4吴鹏,Chin J Chem Eng,1996年,4卷,3期,219页 被引量:1
  • 5吴鹏,高校化学工程学报,1995年,9期,162页 被引量:1
  • 6吴鹏,化工学报,1994年,45卷,422页 被引量:1

同被引文献35

  • 1吴鹏,李绍芬,廖晖.固定床反应器的飞温和参数敏感性[J].化工学报,1994,45(4):422-428. 被引量:9
  • 2吴鹏,李绍芬,廖晖.固定床反应器进行n级反应的飞温判据[J].高校化学工程学报,1995,9(2):162-167. 被引量:4
  • 3袁谓康 朱开宏.化学反应工程分析[M].上海:华东理工大学出版社,1995.138,141. 被引量:3
  • 4Westerterp K R, Molga E J. Safety and runaway prevention in batch and semi-batch reactors--a review. Chemical Engineering Research and Design, 2006, 84 (A7): 543-552. 被引量:1
  • 5Molga Eugeniusz J, Lewak Michal, Westerterp K R. Runaway prevention in liquid-phase homogeneous semi batch reactors. Chemical Engineering Science, 2007, 62: 5074-5077. 被引量:1
  • 6Varma A, Morbidelli M, Wu H. Parametric Sensitivity in Chemical Systems. Cambridge: Cambridge University Press, 1999:1-8. 被引量:1
  • 7Hugo P, Steinbach J. A comparison of the limits of safe operation of a SBR and a CSTR. Chemical Engineering Science, 1986, 41 (4): 1081-1087. 被引量:1
  • 8Steensma M, Westerterp K R. Thermally safe operation of a cooled semi-batch reactor. Slow liquid-liquid reactions. Chemical Engineering Science, 1988, 43 (8) : 2125-2132. 被引量:1
  • 9Steensma Metske, Westerterp K Roel. Thermally safe operation of a semi-batch reactor for liquid liquid reactions. Slow reactions. Industrial and Engineering Chemistry Research, 1990, 29:1259-1270. 被引量:1
  • 10Woezik B A A van, Westerterp K R. Runaway behavior and thermally safe operation of multiple liquid liquid reactions in the semi batch reactor. The nitric acid oxidation of 2-octannol. Chemical Engineering and Processing, 2002, 41:59-77. 被引量:1

引证文献2

二级引证文献38

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部