Autor: |
Karalin, E., Oparkin, A., Abramov, A., Pavlov, S., Murtazin, N., Appakova, D., Ksenofontov, D., Miroshkin, N., Kharlampidi, Kh. |
Zdroj: |
Catalysis in Industry; Jul2016, Vol. 8 Issue 3, p242-247, 6p |
Abstrakt: |
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 %. [ABSTRACT FROM AUTHOR] |
Databáze: |
Complementary Index |
Externí odkaz: |
|