Thermodynamic and kinetic study of the production of oxygenated compounds: Synthesis of 1,1-diethoxybutane catalyzed by amberlyst-15. Novel Reactive Distillation Process for Phenol Production with a Dry Cation Exchange Resin as the Catalyst. Information about how to use the RightsLink permission system can be found at Catalytic distillation in structured packings: Methyl acetate synthesis. Heat-integrated reactive distillation process for TAME synthesis. Industrial & Engineering Chemistry Research. Ian W. Ashworth, Edward Bush, Lai C. Chan, Janette Cherryman, Brian G. Cox, and James Muir , Srinivasa Rao Korupoju and Jaikumar Keshwan . Reactive distillation for methyl acetate production. Kun Li, Xiao Chen, Weilan Xue, Zuoxiang Zeng, Shan Jiang. Simulation of continuous packed bed reactive distillation column for the esterification process using activity based kinetic model. Chemical Equilibrium and Reaction Kinetics of Heterogeneously Catalyzed n-Hexyl Acetate Esterification. Reactive dividing wall column for hydrolysis of methyl acetate: Design and control. 1. Coupled Reaction/Distillation Process for Hydrolysis of Methyl Acetate. Felicia Januarlia Novita, Hao-Yeh Lee, Moonyong Lee. Silva, Alírio E. Rodrigues. Isobaric Vapor–Liquid Equilibrium Data for Binary Systems of Anisole with Methyl Acetate, Ethyl Acetate, n-Propyl Acetate, and Isopropyl Acetate at 93.9 kPa. Sami H. Ali, Osama Al-Rashed, Fadhel A. Azeez, Sabiha Q. 2 Data on acetic acid–methanol–methyl acetate–water mixture analysised by dual packed column Gas Chromatography. Esterification of Acetic Acid with Methanol over a Cation Exchange Resin. Acetone condensation on a cation exchange resin catalyst: the pseudo equilibrium phenomenon. Enhancement of esterification conversion using novel composite catalytically active pervaporation membranes. Kinetic studies in a batch reactor using ion exchange resin catalysts for oxygenates production: Role of mass transfer mechanisms. Learning Chemistry from Good and (Why Not?) Lumin Li, Lanyi Sun, Delian Yang, Wang Zhong, Yi Zhu, Yuanyu Tian. Alexander Brächer, Richard Behrens, Erik von Harbou, Hans Hasse. Simulation de la distillation catalytique par un nouveau modèle de transfert – Application à la production d'acétate de méthyle. Synthesis of butyl acrylate in a fixed-bed adsorptive reactor over Amberlyst 15. Kinetic study for esterification of lactic acid with ethanol and hydrolysis of ethyl lactate using an ion-exchange resin catalyst. Box 2503, D-26111 Oldenburg, Germany. Size of this PNG preview of this SVG file: Add a one-line explanation of what this file represents. International Journal of Quantum Chemistry. Investigation of Ethyl Lactate Reactive Distillation Process. Kinetics study of esterification of acetic acid with isobutanol in the presence of amberlite catalyst. Bioadditives synthesis from selective glycerol esterification over acidic ion exchange resin as catalyst. Liang Zhang, Haisheng Chen, Yang Yuan, Jieping Yu, Shaofeng Wang, Kejin Huang. A. Pisarenko, L. A. Serafimov. Your IP address has been blocked automatically due to excessive site usage. MINLP Optimization of Side-Reactor Column Configuration Based upon Improved Bat Algorithm. Jer-Wei Lin, A.H. Zaki, Hsien-Tsung Wu, Ho-mu Lin, Ming-Jer Lee. Kinetic Study for the Reactive System of Lactic Acid Esterification with Methanol: Methyl Lactate Hydrolysis Reaction. Efficient conversion of brown grease produced by municipal wastewater treatment plant into biofuel using aluminium chloride hexahydrate under very mild conditions. Mantle, A.J. Ruining He, Yun Zou, Yanbo Dong, Yaseen Muhammad, Sidra Subhan, Zhangfa Tong. Esterification of acrylic acid with 2-ethylhexan-1-ol: Thermodynamic and kinetic study. In contrast, less is known about the emission and source of acetic acid. Product yields and process kinetics. This system is of major importance as a model reaction for reactive distillation. Vapor−Liquid Equilibria at (33.33, 66.66, and 101.33) kPa and Densities at 298.15 K for the System Methanol + Methyl Lactate. de Jong, R. Feijt, E. Zondervan, T.A. Pore diffusion model to predict the kinetics of heterogeneous catalytic esterification of acetic acid and methanol. You have to login with your ACS ID befor you can login with your Mendeley account. In order to diminish the effect of water on the catalysis as a result of the reverse reaction, initial reaction kinetics were measured using a low concentration of sulfuric acid (1 × 10−3 M) and different initial water concentrations. Chemical Engineering and Processing: Process Intensification. Nijhuis, A.B. Reaction Monitoring by Benchtop NMR Spectroscopy Using a Novel Stationary Flow Reactor Setup. Adsorption measurements on a CrOx/γ-Al2O3 catalyst for parameter reduction in kinetic analysis. -toluenesulphonic acid. Development of kinetic models for acid-catalyzed methyl acetate formation reaction: Effect of catalyst concentration and water inhibition. http://pubs.acs.org/page/copyright/permissions.html. Please reconnect. In Bum Ju, Hye-Won Lim, Wonjin Jeon, Dong Jin Suh, Myung-June Park, Young-Woong Suh. Size of this PNG preview of this SVG file: 800 × 214 pixels. E-mail: [email protected] chem.uni-oldenburg.de. Thermodynamic Modeling of Time-Dependent Interfacial Properties in Reactive Liquid–Liquid Systems Close to the Critical Point. Hao Chen, Xingang Li, Lin He, Haifeng Cong. Hydrolysis of methyl acetate using ionic liquids as catalyst and solvent. Clicking on the donut icon will load a page at altmetric.com with additional details about the score and the social media presence for the given article. Dora E. López,, Kaewta Suwannakarn,, James G. Goodwin, Jr., and. M. Duque-Bernal, J. D. Quintero-Arias, W. Osorio-Viana, I. Dobrosz-Gómez, J. Fontalvo, M. Á. Gómez-García. 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