Ethylene glycol oxidation over supported catalyst in tubular reactor

[Display omitted] ► We developed a macrokinetics for oxidation of ethylene glycol into glyoxal. ► We proposed a 2D heterogeneous mathematical model of the process. ► Due to catalyst activity change it is possible to manage the process selectivity. Macrokinetics for chemical transformation of ethylen...

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Veröffentlicht in:	Chemical engineering journal (Lausanne, Switzerland : 1996) Switzerland : 1996), 2011-08, Vol.172 (1), p.399-409
Hauptverfasser:	Salaev, M.A., Krejker, A.A., Magaev, O.V., Malkov, V.S., Knyazev, A.S., Borisova, E.S., Khanaev, V.M., Vodyankina, O.V., Kurina, L.N.
Format:	Artikel
Sprache:	eng
Schlagworte:	Catalysts Chemical engineering Ethylene glycol Ethylene glycol oxidation Glyoxal Mathematical models Modeling and simulation oxidation Pilots Reactors Selectivity Supported catalyst Transformations
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