In the field of adiabatic correction for complex reactions
a simple one-stage kinetic model was used to estimate the real reaction kinetics. However
this assumption simplified the real process
inevitably generated inaccurate or even unsafe results. Therefore
it was necessary to find a new correction method for complex reactions. In this work
esterification of acetic anhydride by methanol was chosen as an object reaction of study. The reaction was studied under different conditions by Reaction Calorimeter (RC1). Then
Thermal Safety Software (TSS) was used to establish the kinetic model and estimate the parameters
where
activation energies for three stages were 67.09
81.02
73.77 kJ·mol
-1
respectively
and corresponding frequency factors in logarithmic form were 16.05
19.59
15.72 s
-1
. In addition
two adiabatic tests were performed by Vent Sizing Package2 (VSP2). For accurate correction of VSP2 tests
a new correction method based on Enhanced Fisher method was proposed. Combined with kinetics
adiabatic correction of esterification reaction was achieved. Through this research
accurate kinetic parameters for a three-step kinetic model of
the esterification reaction were acquired. Furthermore
the correlation coefficients between simulated curves and corrected curves were 0.976 and 0.968
which proved the accuracy of proposed new adiabatic correction method. Based on this new method
conservative corrected results were able to be acquired and be applied in safety assessment.
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Complete kinetic model for esterification reaction of lauric acid with glycerol to synthesize glycerol monolaurate
Esterification of acetic acid with isobutanol catalyzed by ionic liquid n-sulfopropyl-3-methylpyridinium trifluoromethanesulfonate: Experimental and kinetic study
Liquid-phase esterification of methacrylic acid with methanol catalyzed by cation-exchange resin in a fixed bed reactor: Experimental and kinetic studies
Reaction kinetics for the heterogeneously resin-catalyzed and homogeneously self-catalyzed esterification of thioglycolic acid with 2-ethyl-1-hexanol
Preparation of solid acid catalyst SO42-/TiO2/γ-Al2O3 for esterification: A study on catalytic reaction mechanism and kinetics
Related Author
Han-Qiao Hu
Yue Zhang
Ming Fan
Yong Cai
Guang-Wen Chu
Liang-Liang Zhang
Meng Shi
Kelei Huang
Related Institution
Research Center of the Ministry of Education for High Gravity Engineering and Technology, Beijing University of Chemical Technology
Petrochemical Research Institute, China National Petroleum Corporation
State Key Laboratory of Organic-Inorganic Composites, Beijing University of Chemical Technology
Guangxi Key Laboratory of Petrochemical Resource Processing and Process Intensification Technology, School of Chemistry and Chemical Engineering, Guangxi University
School of Chemical Sciences, University of Chinese Academy of Sciences