Abstract
As an example of the liquid-phase hydrogenation of methyl-phenol ketone to 1-phenylethanol, variants of the construction of a pilot reactor are considered for performing long-term tests of heterogeneous catalysts of a fixed bed. Calculations for the reactor unit during hydrogenation on NTK-11 are presented as an example. It is shown that a cascade of three adiabatic reactors with a catalyst bed height of 4.5 m each is needed to ensure a residual reactant concentration below 1 wt %.
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Original Russian Text © E.A. Karalin, A.V. Oparkin, A.G. Abramov, S.B. Pavlov, N.F. Murtazin, D.M. Appakova, D.V. Ksenofontov, N.P. Miroshkin, Kh.E. Kharlampidi, 2016, published in Kataliz v Promyshlennosti.
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Karalin, E.A., Oparkin, A.V., Abramov, A.G. et al. Endurance tests and kinetic experiment in a plug-flow reactor with a fixed catalyst bed. Catal. Ind. 8, 242–247 (2016). https://doi.org/10.1134/S2070050416030041
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DOI: https://doi.org/10.1134/S2070050416030041