TY - JOUR
T1 - Inherent safer design for chemical process of 1,4-dioldiacetate-2-butene oxidized by ozone
AU - Hua, Min
AU - Liang, Xinmiao
AU - Wei, Chen Ye
AU - Zhang, Lu
AU - Pan, Xuhai
AU - Jiang, Jiajia
AU - Ni, Lei
AU - Jiang, Juncheng
N1 - Publisher Copyright:
© 2019 Taylor & Francis Group, LLC.
PY - 2020/10/2
Y1 - 2020/10/2
N2 - Oxidation reaction is the typical thermal runaway reaction, and the reaction of 1, 4-dioldiacetate-2-Butene oxidized by ozone was investigated in this study. Firstly, the thermal hazards of the oxidative exothermic reactions were identified and evaluated combined process risk assessment method. The Qualitative Assessment for Inherently Safer Design (QAISD) was used to identify the risk of the reaction process. Meanwhile, the Reaction Calorimeter (RC1e) was used to obtain the thermal properties of the oxidation reaction. Then the inherent safer designs (ISD) were proposed according to the risk assessment results to increase the level of safety of chemical industry technique. 1) ISD I: reaction temperature was improved to –5 °C, and ventilation rate was improved to 200 L•h−1. 2) ISDII: using a tubular reactor as reaction vessel. The results indicated that the severity of the reaction hazard was reduced by 43%, and safety was improved significantly via two ISDs. Moreover, the inherent safety level of the reaction was increased by 63% and 43.4% via ISD Iand II, respectively. The reaction process get closer to inherent safety theories of “minimize,” “substitute,” and “moderate”.
AB - Oxidation reaction is the typical thermal runaway reaction, and the reaction of 1, 4-dioldiacetate-2-Butene oxidized by ozone was investigated in this study. Firstly, the thermal hazards of the oxidative exothermic reactions were identified and evaluated combined process risk assessment method. The Qualitative Assessment for Inherently Safer Design (QAISD) was used to identify the risk of the reaction process. Meanwhile, the Reaction Calorimeter (RC1e) was used to obtain the thermal properties of the oxidation reaction. Then the inherent safer designs (ISD) were proposed according to the risk assessment results to increase the level of safety of chemical industry technique. 1) ISD I: reaction temperature was improved to –5 °C, and ventilation rate was improved to 200 L•h−1. 2) ISDII: using a tubular reactor as reaction vessel. The results indicated that the severity of the reaction hazard was reduced by 43%, and safety was improved significantly via two ISDs. Moreover, the inherent safety level of the reaction was increased by 63% and 43.4% via ISD Iand II, respectively. The reaction process get closer to inherent safety theories of “minimize,” “substitute,” and “moderate”.
KW - Chemical process
KW - Inherent safer design
KW - Oxidation
KW - Qualitative assessment
KW - RC1
KW - Reaction hazard
UR - http://www.scopus.com/inward/record.url?scp=85073806344&partnerID=8YFLogxK
U2 - 10.1080/00986445.2019.1657420
DO - 10.1080/00986445.2019.1657420
M3 - 文章
AN - SCOPUS:85073806344
SN - 0098-6445
VL - 207
SP - 1451
EP - 1461
JO - Chemical Engineering Communications
JF - Chemical Engineering Communications
IS - 10
ER -