Identification of the Kinetic Parameters and Autocatalytic Behavior in Esterification via Isoperibolic Reaction Calorimetry

被引:18
作者
Wei, Hong-Yuan [1 ]
Guo, Zi-Chao [1 ]
Hao, Lin [1 ]
Bai, Wen-Shuai [1 ]
Wang, Rui [1 ]
Li, Shuai [1 ]
机构
[1] Tianjin Univ, Sch Chem Engn & Technol, Tianjin 300072, Peoples R China
关键词
ACETIC-ANHYDRIDE; SEMIBATCH REACTORS; SAFETY; METHANOL; BATCH;
D O I
10.1021/acs.oprd.5b00395
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
In the fine chemical and pharmaceutical industries, the operation of highly exothermic reactions with the autocatalytic features may lead to safety issues. From the safety point of view, identification of the autocatalytic features and the corresponding kinetics for a given reaction are of significant importance. In this work the simultaneots kinetic and thermodynamic analysis of a case reaction of esterification between acetic anhydride and methanol is first carried out under isoperibolic conditions using a reaction calorimeter. Two kinetic models, that is, autocatalytic kinetic model and second order kinetic model, are used to fit the temperature profile. The results show that the calculated reaction enthalpy (Delta H, 67.88 kJ/mol) by the autocatalytic kinetic model is much closer to the experimental value (63.22 kJ/mol) than that by second order model (100.06 kJ/mol), indicating that the autocatalytic kinetic model is more appropriate to the reaction. With the case study, we also demonstrate that an insight into the reaction mechanism and the proper selection of the kinetic model to fit the experimental data is crucial otherwise the improper selection of kinetic model could lead to misleading kinetic or thermodynamic parameters and then result in an incorrect estimation of the risk level of a given reaction.
引用
收藏
页码:1416 / 1423
页数:8
相关论文
共 19 条
[1]   Kinetic parameter estimation of solvent-free reactions: application to esterification of acetic anhydride by methanol [J].
Balland, L ;
Mouhab, N ;
Cosmao, JM ;
Estel, L .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2002, 41 (05) :395-402
[2]   Comparison of criteria for prediction of runaway reactions in the sulphuric acid catalyzed esterification of acetic anhydride and methanol [J].
Casson, Valeria ;
Lister, David George ;
Milazzo, Maria Francesca ;
Maschio, Giuseppe .
JOURNAL OF LOSS PREVENTION IN THE PROCESS INDUSTRIES, 2012, 25 (01) :209-217
[3]   Topological Criteria to Safely Optimize Hazardous Chemical Processes Involving Consecutive Reactions [J].
Copelli, Sabrina ;
Derudi, Marco ;
Rota, Renato .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2010, 49 (10) :4583-4593
[4]   Kinetic investigations of a ketonization reaction using reaction calorimetry [J].
Crevatin, A ;
Mascarello, F ;
Leuthe, B ;
Minder, B ;
Kikic, I .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1999, 38 (12) :4629-4633
[5]   Applications of reaction calorimetry in reaction kinetics and thermal hazard evaluation [J].
Duh, YS ;
Hsu, CC ;
Kao, CS ;
Yu, SW .
THERMOCHIMICA ACTA, 1996, 285 (01) :67-79
[6]   MODELING OF THE VENTED METHANOL ACETIC-ANHYDRIDE RUNAWAY REACTION USING SAFIRE [J].
FRIEDEL, L ;
WEHMEIER, G .
JOURNAL OF LOSS PREVENTION IN THE PROCESS INDUSTRIES, 1991, 4 (02) :110-119
[7]   From Kinetic Study to Thermal Safety Assessment: Application to Peroxyformic Acid Synthesis [J].
Leveneur, Sebastien ;
Thoenes, Martin ;
Hebert, Jean-Pierre ;
Taouk, Bechara ;
Salmi, Tapio .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2012, 51 (43) :13999-14007
[8]   Temperature diagrams for preventing decomposition or side reactions in liquid-liquid semibatch reactors [J].
Maestri, F ;
Rota, R .
CHEMICAL ENGINEERING SCIENCE, 2006, 61 (10) :3068-3078
[9]   THE KINETIC RATE LAW FOR AUTOCATALYTIC REACTIONS [J].
MATAPEREZ, F ;
PEREZBENITO, JF .
JOURNAL OF CHEMICAL EDUCATION, 1987, 64 (11) :925-927
[10]   Safety aspects in modelling and operating of batch and semibatch stirred tank chemical reactors [J].
Milewska, Aleksandra ;
Molga, Eugeniusz .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2010, 88 (3A) :304-319