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image/svg+xml Jakob Voss, based on art designer at PLoS, modified by Wikipedia users Nina and Beao Closed Access logo, derived from PLoS Open Access logo. This version with transparent background. http://commons.wikimedia.org/wiki/File:Closed_Access_logo_transparent.svg Jakob Voss, based on art designer at PLoS, modified by Wikipedia users Nina and Beao Journal of the Taiwa...arrow_drop_down
image/svg+xml Jakob Voss, based on art designer at PLoS, modified by Wikipedia users Nina and Beao Closed Access logo, derived from PLoS Open Access logo. This version with transparent background. http://commons.wikimedia.org/wiki/File:Closed_Access_logo_transparent.svg Jakob Voss, based on art designer at PLoS, modified by Wikipedia users Nina and Beao
Journal of the Taiwan Institute of Chemical Engineers
Article . 2016 . Peer-reviewed
License: Elsevier TDM
Data sources: Crossref
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Modeling and optimization of NH3-SCR performance of MnOx/γ-alumina nanocatalysts by response surface methodology

Authors: Parvaneh Nakhostin Panahi; Seyed Mahdi Mousavi;

Modeling and optimization of NH3-SCR performance of MnOx/γ-alumina nanocatalysts by response surface methodology

Abstract

Abstract To model and optimize the NH3-SCR performance of MnOx/γ-alumina nanocatalysts, the response surface methodology (RSM) based on a central composite design (CCD) was employed. The MnOx/γ-alumina nanocatalysts were prepared by homogeneous deposition precipitation and characterized by XRD, H2-TPR, N2 adsorption and TEM. The effect of process variables, including Mn loading, calcination temperature, concentration of O2, NH3/NO ratio and reaction temperature on NOx conversion and N2 selectivity was studied. Analysis of variance confirmed the accuracy and precision of generating quadratic models. The calcination temperature and reaction temperature had the most pronounced effects on NOx conversion and N2 selectivity, respectively. The maximum NH3-SCR performance (94.6% NOx conversion and 93.7% N2 selectivity) was predicted and experimentally validated at the optimum conditions: Mn loading 6.7 wt. %, calcination temperature 507.5 °C, concentration of O2 4.5 (vol. %), NH3/NO ratio 0.94 and reaction temperature 269.8 °C.

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