Modeling and Simulation of a Three-Phase Catalytic Slurry Intensified Continuous Chemical Reactor

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Abstract:

This work proposes a dynamic model of a three-phase catalytic slurry intensified continuous reactor. The model is simulated to describe the dynamic behaviors of the hydrogenation of o-cresol on Ni/SiO2 catalyst. The nominal operating point and the transient responses for different input perturbations are discussed.

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Advanced Materials Research (Volumes 466-467)

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141-145

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February 2012

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© 2012 Trans Tech Publications Ltd. All Rights Reserved

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[1] S. Lomel, L. Falk, J.M. Commenge, J.L. Houzelot and K. Ramdani: Chemical Engineering Research and Design 84 (A5) (2006), p.363–369.

DOI: 10.1205/cherd05027

Google Scholar

[2] J.C. Charpentier: Chemical Engineering Journal 134 (2007), p.84–92.

Google Scholar

[3] J.C. Etchells: Process Safety and Environmental Protection, 83(B2) (2005), pp.85-89.

Google Scholar

[4] H. Hichri, A. Armand and J. Andrieu: Chemical Engineering Process 30 (1991), p.133–140.

Google Scholar

[5] J. Wärnä and T. Salmi: Computers in Chemical Engineering, 20 (1) (1996), p.39–47.

Google Scholar

[6] S. Li, S. Bahroun, C. Valentin, C. Jallut and F. De Panthou: Journal of Loss Prevention in the Process Industries, 23(3) (2010), pp.437-445.

DOI: 10.1016/j.jlp.2010.02.001

Google Scholar

[7] S. Bahroun, S. Li, C. Jallut, C. Valentin and F. De Panthou: Journal of Process Control, 20(5) (2010), pp.664-675.

DOI: 10.1016/j.jprocont.2010.03.002

Google Scholar