Abstract

Thermal treatment either in the presence of oxygen (calcination) or of a reducing agent (reduction) result is all the time a key issue within the preparation of a catalyst. In this work, a microwave plasma treatment was chosen as an alternative to typical calcinations, because it is a more energy efficient process. Thus, a Microwave Fluidized Bed Plasma reactor (MFBP) was employed in catalyst synthesis process under different gas compositions, such as argon and argon/oxygen mixtures over g-alumina supported silver catalysts, which are generally used for selective reduction of NOx by ethanol. After the first catalytic tests performed in the presence of plasma treated catalyst, it can be concluded that plasma treatment process represents an interesting alternative to conventional calcination during catalyst synthesis, resulting in a more sustainable process, moreover in view of its industrial application. In order to understand the particular effect of plasma treatment, the catalysts submitted to this treatment were carefully characterized by means of thermo gravimetric analysis (TGA), differential thermal analysis (DTA) and UV-VIS-NIR.

Highlights

  • All around the world, the major chemical engineering processes are catalytic processes

  • A Microwave Fluidized Bed Plasma reactor (MFBP) was employed in catalyst synthesis process under different gas compositions, such as argon and argon/oxygen mixtures over -alumina supported silver catalysts, which are generally used for selective reduction of NOx by ethanol

  • In order to understand the particular effect of plasma treatment, the catalysts submitted to this treatment were carefully characterized by means of thermo gravimetric analysis (TGA), differential thermal analysis (DTA) and UV-VIS-NIR

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Summary

Introduction

The major chemical engineering processes are catalytic processes. Most the used catalysts are heterogeneous supported catalysts. An effective catalyst is generally described to have a high specific surface area in which the catalytic phase ishighly dispersed. In commercial form, the final catalyst should possess high mechanical strength and resistance to high temperatures [1]. Conventional synthesis of supported catalysts comprises four main steps, namely: 1) impregnation of the active phase; 2) maturation; 3) drying; 4) thermal activation such as calcination or reduction. The lack of an accurate control of some of these operations results in catalytic preparation procedures, which may be far from perfect [2,3]

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