Esterification of benzoic acid using Ti3AlC2 and SO42−/Ti3AlC2 ceramic as acid catalysts. http://pubs.acs.org/page/copyright/permissions.html, https://doi.org/10.1080/00986445.2018.1428960, https://doi.org/10.1016/j.cep.2017.08.012, https://doi.org/10.1016/j.ceramint.2013.04.077, https://doi.org/10.1016/j.cej.2011.09.049, https://doi.org/10.1016/j.jtice.2010.07.010, https://doi.org/10.1016/j.jtice.2009.12.001.
Find more information about Crossref citation counts. not otherwise permitted to reproduce, republish, redistribute, or sell any Supporting Information Gaodong Yang, Pingkeng Wu, Zheng Zhou, Xiangpo He, Weimin Meng, and Zhibing Zhang .
Chemical Engineering and Processing: Process Intensification.
Xianglei Shan, Zhenmin Cheng, and Ying Li . Files available from the ACS website may be downloaded for personal use only. the Altmetric Attention Score and how the score is calculated. Xianglei Shan, Zhenmin Cheng, Peiqing Yuan. The hydrolysis of ethyl benzoate was also … Dhia Y. Aqar, Nejat Rahmanian, Iqbal M. Mujtaba.
Kai-Wen Chan, Yu-Ting Tsai, Ho-mu Lin, Ming-Jer Lee.
redistribute this material, requesters must process their own requests via the RightsLink permission Article Views are the COUNTER-compliant sum of full text article downloads since November 2008 (both PDF and HTML) across all institutions and individuals. A, B, C, and D = benzoic acid, ethanol, ethyl benzoate, and water, respectively, Af = Arrhenius preexponential factor of the forward reaction (mol min-1 kg-1), Aij/R and Aji/R = interaction energy parameters in the NRTL model (K), Ar = Arrhenius preexponential factor of the reverse reaction (mol min-1 kg-1), CA0 = inlet concentration of benzoic acid (mol cm-3), CD0 = inlet concentration of water (mol cm-3), E0,f = activation energy of the forward reaction (kJ mol-1), E0,r = activation energy of the reverse reaction (kJ mol-1), F = volumetric flow rate of feed (cm3 min-1), FA = molar flow rate of benzoic acid in feed (mol min-1), FD = molar flow rate of water in feed (mol min-1), Δhf = molar heat of ethyl benzoate synthesis (kJ mol-1), kf = rate constant of forward reaction (mol min-1 kg-1), kr = rate constant of reverse reaction (mol min-1 kg-1), KD = adsorption equilibrium constant of water, Ka = equilibrium constant in terms of activity, Kγ = equilibrium constant in terms of activity coefficient, K1,2 = ratio of adsorption constants between components 1 and 2, n0 = total initial number of moles in the liquid phase (mol), nis = number of moles of component i adsorbed on the surface per unit mass of absorbent (mol g-1), ns = the constant total number of moles which can be accommodated in the adsorbed phase by unit mass of solid (mol g-1), Nf = number of data points of synthesis of ethyl benzoate, Nr = number of data points of hydrolysis of ethyl benzoate, p = number of parameters in the kinetic models, −rA = reaction rate of benzoic acid (mol min-1 kg-1), −rD = reaction rate of water (mol min-1 kg-1), Δx = change in the mole fraction in the liquid phase, θB0 = molar ratio of feed (ethanol to benzoic acid), θC0‘ = molar ratio of ethyl benzoate to water.
To whom correspondence should be addressed. system. without permission from the American Chemical Society. Closed-Loop Model-Based Design of Experiments for Kinetic Model Discrimination and Parameter Estimation: Benzoic Acid Esterification on a Heterogeneous Catalyst. The esterification of benzoic acid with ethanol was implemented at temperatures between 323.15 and 353.15 K under various molar ratios of feed, θB0 (ethanol to benzoic acid). Users are Kinetic modeling of benzoic acid esterification using functionalized silica gel. Conor Waldron, Arun Pankajakshan, Marco Quaglio, Enhong Cao, Federico Galvanin. E-mail: [email protected]. Kinetic Study of Dowex 50 Wx8-Catalyzed Esterification and Hydrolysis of Benzyl Acetate. Reaction kinetics and mechanism for hydration of cyclohexene over ion-exchange resin and H-ZSM-5. The Canadian Journal of Chemical Engineering. Your Mendeley pairing has expired. Fax: 886-2-2737-6644. http://pubs.acs.org/page/copyright/permissions.html.
Solvent Effects on Hydration of Cyclohexene over H-ZSM-5 Catalyst. This material is available free of charge via the Internet at http://pubs.acs.org. Information. The kinetic behavior of the synthesis and hydrolysis of ethyl benzoate over an acidic cation-exchange resin, Amberlyst 39, was investigated with a fixed-bed reactor at atmospheric pressure. 2- What impurity might be found in … The kinetic behavior of the synthesis and hydrolysis of ethyl benzoate over an acidic cation-exchange resin, Amberlyst 39, was investigated with a fixed-bed reactor at atmospheric pressure.
Journal of the Taiwan Institute of Chemical Engineers. Electronic Supporting Information files are available without a subscription to ACS Web Editions. These metrics are regularly updated to reflect usage leading up to the last few days. Kinetics of esterification of benzoic acid and isoamyl alcohol catalyzed by The LHHW model yielded the best representation for the kinetic behavior of the liquid−solid catalytic synthesis and hydrolysis of ethyl benzoate. REQUIREMENTS.
The equilibrium conversion of benzoic acid in the esterification was found to increase with an increase in both temperature and θB0. Phone: 886-2-2737-6643. When benzonitrile is heated with aqueous sodium hydroxide solution, it liberates ammonia gas and converts to sodium benzoate which on acidification gives benzoic acid.
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