Yi Fei, Bing Sun, Fan Zhang, 等. Inherently safer reactors and procedures to prevent reaction runaway[J]. 中国化学工程学报(英文版), 2018,(6):1252-1263.
Yi Fei, Bing Sun, Fan Zhang, et al. Inherently safer reactors and procedures to prevent reaction runaway[J]. Chinese Journal of Chemical Engineering, 2018, (6): 1252-1263.
Yi Fei, Bing Sun, Fan Zhang, 等. Inherently safer reactors and procedures to prevent reaction runaway[J]. 中国化学工程学报(英文版), 2018,(6):1252-1263.DOI: 10.1016/j.cjche.2018.03.017.
Yi Fei, Bing Sun, Fan Zhang, et al. Inherently safer reactors and procedures to prevent reaction runaway[J]. Chinese Journal of Chemical Engineering, 2018, (6): 1252-1263.DOI: 10.1016/j.cjche.2018.03.017.
Inherently safer reactors and procedures to prevent reaction runaway
Reaction runaway has longtime been an issue in chemical industry as it often leads to severe accidents if not controlled and inhibited properly. Herein we have reviewed several key considerations and procedures to prevent such phenomena
including inherently safer reactor design
thermal risk assessment and early warning detection of runaway
and pointed out that the basic principle underlying is necessary heat management and construction of resilient processes. For inherently safer reactor design
important factors such as heat removal
heat capacitance
flow behaviors and explosive behaviors have been investigated. The survey shows that heat exchanger (HEX) reactor and microreactor outperform traditional reactors. Meanwhile
we have looked into the effect of thermal risk ranking and safety operation region determining for thermal risk assessment
and the influence of runaway criteria and construction methods for early detection of reaction runaway as well. It shows that thermal risk assessment plays a key role on process design
and early warning detection system (EWDS) is preferable on prevention of reaction runaway. In the end
perspectives regarding inherently safer designs with the measures discussed above have been provided.
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