期刊文献+

异丙醇与丙酸酐酯化反应的安全控制条件 被引量:2

Safety-control conditions in esterification of isopropyl alcohol and propionic anhydride
下载PDF
导出
摘要 针对异丙醇与丙酸酐酯化合成丙酸异丙酯工艺的反应失控危险性,利用泄放尺寸实验仪(VSP2)研究了其反应的放热特性,选择自催化模式模拟得到了反应动力学参数,并与实验数据进行了对比验证;利用得到动力学模型,模拟了该工艺在半间歇模式、反应温度为70℃时,中试规模(>100L)条件下的反应特点,分析了反应失控的危险性,并针对加料程序进行了优化设计,得到最佳控制方法。 Vent size Package 2 (VSP2) was used to analyze the thermal behavior in synthesis reaction of isopropyl propionate, The reaction kinetics were simulated with autocatalytic model, and validated by experimentations. The reaction characteristics were simulated in semi-batch mode, with the reaction temperature of 70℃, pilot-scale (100L). The hazards of runaway reaction were discussed, and the feed program was optimized.
出处 《中国安全生产科学技术》 CAS CSCD 2013年第9期11-14,共4页 Journal of Safety Science and Technology
基金 国家"十二五"科技支撑计划课题(2012BAK13B02)
关键词 丙酸异丙酯 反应动力学 反应失控 优化 Isopropyl propionate reaction kinetics runaway reaction optimization
  • 相关文献

参考文献15

二级参考文献54

  • 1梁志宏,耿惠民.过氧化氢爆炸事故浅析[J].消防科学与技术,2004,23(6):602-604. 被引量:13
  • 2钱新明,刘丽,张杰.绝热加速量热仪在化工生产热危险性评价中的应用[J].中国安全生产科学技术,2005,1(4):13-18. 被引量:29
  • 3高大元,何碧,何松伟,董海山,李敬明.Arrhenius方法的局限性讨论[J].含能材料,2006,14(2):132-135. 被引量:33
  • 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.
  • 5Molga Eugeniusz J, Lewak Michal, Westerterp K R. Runaway prevention in liquid-phase homogeneous semi batch reactors. Chemical Engineering Science, 2007, 62: 5074-5077.
  • 6Varma A, Morbidelli M, Wu H. Parametric Sensitivity in Chemical Systems. Cambridge: Cambridge University Press, 1999:1-8.
  • 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.
  • 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.
  • 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.
  • 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.

共引文献77

同被引文献24

  • 1田震.化工过程开发中本质安全化设计策略[J].中国安全科学学报,2006,16(12):4-8. 被引量:30
  • 2吴宗之.基于本质安全的工业事故风险管理方法研究[J].中国工程科学,2007,9(5):46-49. 被引量:37
  • 3T A Kletz. What you don't have, can't leak[J]. Chem Ind,1978,10 (6) : 287-292.
  • 4T.A. Kletz. Cheaper, Safer Plants or Wealth and Safety at Work-Notes on Inherently Safer and Simpler Plants[M]. Rugby, UK: IChemE, 1984:31-52.
  • 5T.A. Kletz. Process plants: A handbook for inherently safer design [M]. Bristol, PA,USA: Taylor & Francis,1998:67-89.
  • 6Center for Chemical Process Safety (CCPS). Inherently safer chemical processes: A life cycle approach[M]. New York, NY, USA: American Institute of Chemical Engineers, 1996:134-189.
  • 7Edwards D W, Lawrence D. Assessing the inherent safety of chemical process routes: Is there a relation between plant costs and inherent safety? [J]. Chemical Engineering Research & De- sign, 1993,71(Part B):252-258.
  • 8Heikkila " A-M, Hurme M, Ja "" rvela "' inen M. Safety consid- erations in process synthesis [J]. Computers and Chemical Engi- neering, 1996,20:S115-S120.
  • 9INSIDE Project. The INSET toolkit, http://www.aeat-safety-an- drisk, com/html/inside.html,2001.
  • 10Palaniappan C, Srinivasan R, and Tan R. Expert system for the design of inherently safer processes. 1. Route selection stage [J]. Ind Eng Chem Res, 2002,a(41 ):6695-6710.

引证文献2

二级引证文献11

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