Influence of the synthesis route on the catalytic oxidation of 1,2-dichloroethane over CeO2/H-ZSM5 catalysts

Journal Article (2013)
Author(s)

B. De Rivas (University of the Basque Country)

C. Sampedro (University of the Basque Country)

E. V. Ramos-Fernández (TU Delft - ChemE/Catalysis Engineering)

R. López-Fonseca (University of the Basque Country)

J. Gascon (TU Delft - ChemE/Catalysis Engineering)

M. Makkee (TU Delft - ChemE/Catalysis Engineering)

J. I. Gutiérrez-Ortiz (University of the Basque Country)

Research Group
ChemE/Catalysis Engineering
DOI related publication
https://doi.org/10.1016/j.apcata.2013.02.026 Final published version
More Info
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Publication Year
2013
Language
English
Research Group
ChemE/Catalysis Engineering
Journal title
Applied Catalysis A: General
Volume number
456
Pages (from-to)
96-104
Downloads counter
113

Abstract

The performance of supported CeO2/HZSM-5 catalysts with a nominal CeO2 loading of 10 wt.% was evaluated for the oxidation of one of the most common chlorinated pollutants found in waste streams, namely 1,2-dichloroethane. The influence of the preparation method, such as impregnation in different media (water and ethanol), precipitation and ion exchange, was examined. Structural, morphological and physico-chemical changes caused as a function of the synthesis procedure were analysed by atomic emission spectroscopy, X-ray diffraction, BET measurements, transmission electronic microscopy, X-ray photoelectron spectroscopy, NH3-temperature- programmed desorption, adsorption of CO at low temperature followed by infrared spectroscopy, temperature-programmed reduction with hydrogen, energy dispersive X-ray spectroscopy and dynamic thermogravimetry coupled to mass spectrometry. The enhancement of the catalytic behaviour of the resulting ceria loaded samples with respect to plain H-ZSM5 could be explained on the basis of the synergetic effects of oxygen mobility and acid sites. In particular, the procedure based on impregnation with ethanol led to a highly dispersed ceria catalyst with a larger amount of oxygen vacancies. As a result, this catalyst required a temperature lower than 200 °C for attaining 50% conversion.