Abstract

A sulfated sintered ore catalyst (SSOC) was prepared to improve the denitration performance of the sintered ore catalyst (SOC). The catalysts were characterized by X-ray Fluorescence Spectrometry (XRF), Brunauer–Emmett–Teller (BET) analyzer, X-ray diffraction (XRD), X-ray photoelectron spectroscopy (XPS) and diffuse reflectance infrared spectroscopy (DRIFTS) to understand the NH3-selective catalytic reduction (SCR) reaction mechanism. Moreover, the denitration performance and stability of SSOC were also investigated. The experimental results indicated that there were more Brønsted acid sites at the surface of SSOC after the treatment by sulfuric acid, which lead to the enhancement of the adsorption capacity of NH3 and NO. Meanwhile, Lewis acid sites were also observed at the SSOC surface. The reaction between −NH2, NH 4 + and NO (E-R mechanism) and the reaction of the coordinated ammonia with the adsorbed NO2 (L-H mechanism) were attributed to NOx reduction. The maximum denitration efficiency over the SSOC, which was about 92%, occurred at 300 °C, with a 1.0 NH3/NO ratio, and 5000 h−1 gas hourly space velocity (GHSV).

Highlights

  • Nitrogen oxide (NOx ) is one of the major atmospheric pollutants and is mainly generated from the combustion of fossil fuel, which has serious harmful effects on human health and the ecological environment

  • The results indicated thatmain the main components of sintered ore catalyst (SOC)

  • It could be seen that the NOx conversion was stable at about 92%, which indicated that sulfated sintered ore catalyst (SSOC) has a good denitration stability

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Summary

Introduction

Nitrogen oxide (NOx ) is one of the major atmospheric pollutants and is mainly generated from the combustion of fossil fuel, which has serious harmful effects on human health and the ecological environment. The new ultra-low emission standard of air pollutants for the iron and steel industry will be issued by Chinese government and require that NOx concentration in the sintering flue gas should be below 50 mg/m3. The sintering flue gas must be heated to the reaction temperature of the catalyst by using additional fuels. Han et al and Chen et al [14,15] proposed that the hot sintered ore was used as catalysts for NOx removal from the sintering flue gas. The denitration efficiency was too low and the NOx concentration from the sintering flue gas could reach the limit after SCR over the sintered ore. The catalytic oxidization of NH3 over γ–Fe2 O3 was suppressed This process resulted in an obvious promotion of NOx conversion. The reaction mechanisms of SCR over SSOC were discussed

Characterizations
The indicated that the components of SOC were were α-Fe2α-Fe
Adsorption of NH3
Co-Adsorption of NO and O2
DRIFT spectra of SSOCininthe thecondition condition of1000 ppm NONO and and
Reaction between NH3 and NO
SCR performance
SCR Performance
Catalyst preparation
Catalyst Characterization
Conclusions
Full Text
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