|本期目录/Table of Contents|

[1]张帆,马翔,姜杰,等.异丙醇与丙酸酐酯化反应的安全控制条件[J].中国安全生产科学技术,2013,9(9):11-14.[doi:10.11731/j.issn.1673-193x.2013.09.002]
 ZHANG Fan,MA Xiang,JIANG Jie,et al.Safetycontrol conditions in esterification of isopropyl alcohol and propionic anhydride[J].JOURNAL OF SAFETY SCIENCE AND TECHNOLOGY,2013,9(9):11-14.[doi:10.11731/j.issn.1673-193x.2013.09.002]
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异丙醇与丙酸酐酯化反应的安全控制条件
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《中国安全生产科学技术》[ISSN:1673-193X/CN:11-5335/TB]

卷:
9
期数:
2013年9期
页码:
11-14
栏目:
学术论著
出版日期:
2013-09-30

文章信息/Info

Title:
Safetycontrol conditions in esterification of isopropyl alcohol and propionic anhydride
作者:
张帆12马翔12姜杰2谢传欣2
(1.青岛科技大学化工学院,山东青岛266042;2.中国石油化工股份有限公司青岛安全工程研究院, 化学品安全控制国家重点实验室,山东青岛266071)
Author(s):
ZHANG Fan 12 MA Xiang 12 JIANG Jie 2 XIE Chuan xin 2
(1.College of Chemical Engineering, Qingdao University of Science and Technology, Qingdao Shandong 266042, China; 2. SINOPEC Safety Engineering Institute, State Key Laboratory of Safety and Control for Chemicals,Qingdao Shandong 266071, China)
关键词:
丙酸异丙酯反应动力学反应失控优化
Keywords:
Isopropyl propionatereaction kineticsrunaway reactionoptimization
分类号:
X937
DOI:
10.11731/j.issn.1673-193x.2013.09.002
文献标志码:
A
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
Abstract:
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.

参考文献/References:

[1]Gary R. Buske. Simple calculations, principles, and techniques to prevent reactive chemicals events in the laboratory [J]. Journal of Chemical Health and Safety, 2010,17(2):912
[2]S.R.Saraf. Classifying Reactive Chemicals[M]. Chemical Engineering Progress, 20043:3437
[3] 彭湘潍,谢传欣,张帆. 化学品活性反应危险性表征方法研究[J]. 中国安全科学学报, 2009, 19(7):7884 PENG Xiangwei, XIE Chuanxin, ZHANG Fan. Research on characterization of chemical reactive hazards[J].China Safety Science Journal, 2009, 19(7):7884
[4] 姜春明,李奇. 过程安全管理与技术的发展与应用[J].中国石油和化工标准与质量, 2007,27(5):4549 JIANG Chunming, LI Qi. Development and application of process safety management and technology[J].China Petroleum and Chemical Standard and Quality, 2007,27(5):4549
[5] 白永忠.化工过程安全中的工艺危害分析方法综述[J].安全、健康和环境, 2009, 9(9):25 BAI Yongzong. Process hazard analysisi methods in chemical process safety[J].Safety Health and Environment, 2009, 9(9):25
[6] 陈利平,陈网桦,彭金华,等. 间歇与半间歇反应热失控危险性评估方法[J]. 化工学报, 2008, 59(12): 29632970 CHEN Liping, CHEN Wanghua, PENG Jinhua,et al. Thermal runaway assessment methods of chemical reactions in batch and semibatch reactors[J]. Journal of Chemical Industry and Engineering, 2008, 59(12): 29632970
[7]ChiMin Shu, YuhJoang Yang. Using VSP2 to separate catalytic and selfdecomposition reactions for hydrogen peroxide in the presence of hydrochloric acid[J]. Themochimica Acta, 2002, 392393(15): 259269
[8]Hans K. Fauske. Properly size vents for nonreactive and reactive chemicals[J]. Chemical Engineering Progress, 2000, 96(2): 1729
[9] 孙峰,谢传欣,黄飞,等. Fe3+掺杂对双氧水热稳定性的影响[J].安全与环境学报, 2010, 10(4): 176180 SUN Feng, XIE Chuanxin, HUANG Fei, et al. Effects of Fe3+ content on the thermal stability of hydrogen peroxide[J]. Journal of Safety and Environment, 2010, 10(4): 176180
[10]Lin, Y. F., Tseng, J. M., Wu, T. C., & Shu, C. M. (2008). Effects of acetone on methyl ethyl ketone peroxide runaway reaction. Journal of Hazard Materials.153, 10711077
[11]Kossoy, A. A., & Akhmetshin, Y. G. (2007). Identification of kinetic models for the assessment of reaction hazards. Process Safety Progress. 10, 101189
[12]Chen, K. Y., Wu, S. H., Wang, Y. W., & Shu, C. M. (2008). Runaway reaction and thermal hazards simulation of cumene hydroperoxide by DSC. Journal of Loss Prevention in the Process Industries. 21, 101109
[13]Kossoy A.A., Hofelich T. (2003). Methodology and software for assessing reactivity ratings of chemical systems. Process Safety Progress. 22, 235 
[14]Kossoy, A., Benin, A., & Akhmetshin, Y. G. (2005). An advanced approach to reactivity rating. assessment of reaction hazards. Journal of Hazard Materials. A118, 917
[15]Fisher F G, Forrest H S, Grossel S S, et al. Emergency Relief System Design Using DIERS Technology [M]. New York:WileyAIChE, 1992

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备注/Memo

备注/Memo:
国家“十二五”科技支撑计划课题(2012BAK13B02)
更新日期/Last Update: 2013-09-30