The Process Operation of Reactive Distillation for TAME Synthesis through Multiple Steady-State Conditions
Author:
Affiliation:
1. Department of Chemistry and Chemical Engineering, Yamagata University
2. Department of Chemical Engineering, Tokyo Institute of Technology
Publisher
Society of Chemical Engineers, Japan
Subject
General Chemical Engineering,General Chemistry
Link
https://www.jstage.jst.go.jp/article/kakoronbunshu/40/3/40_13wh109/_pdf
Reference10 articles.
1. Al-Arfaj, M. and W. L. Luyben; “Plantwide Control for TAME Production Using Reactive Distillation,” AIChE J., 50, 1462–1473 (2004)
2. Katariya, A. M., R. S. Kamath, K. M. Moudgalya and S. M. Mahajani; “Non-equilibrium Stage Modeling and Non-linear Dynamic Effects in the Synthesis of TAME by Reactive Distillation,” Comput. Chem. Eng., 32, 2243–2255 (2008)
3. Kim, Y. H.; “Energy Conservation of a Multi-Effect Distillation Column with Internal Heat Integration,” J. Chem. Eng. Jpn., 45, 840–849 (2012)
4. Kumar, M. V. P. and N. Kaistha; “Internal Heat Integration and Controllability of Double Feed Reactive Distillation Column, 2. Effect of Catalyst Redistribution,” Ind. Eng. Chem. Res., 47, 7304–7311 (2008)
5. Luyben, W. L.; Distillation Design and Control Using Aspen Simulation, John Wiley & Sons Inc., New Jersey, USA (2006)
Cited by 2 articles. 订阅此论文施引文献 订阅此论文施引文献，注册后可以免费订阅5篇论文的施引文献，订阅后可以查看论文全部施引文献
1. Energy-saving performance of reactive distillation process for TAME synthesis through multiple steady state conditions;Chemical Engineering and Processing - Process Intensification;2018-08
2. Effect of Operating Conditions on the Multiple Steady States in Reactive Distillation;KAGAKU KOGAKU RONBUNSHU;2014
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