Abstract

In accordance with the cerium-lanthanum ratio of fluorocerium ores in the mineralogy of the Baiyun Ebo process, the (Ce,La)CO3F grains were synthesised by hydrothermal method using pure material to simulate bastnaesite minerals, and used as NH3-SCR denitrification catalysts. The activity results showed that the synthetic (Ce,La)CO3F was roasted at 500&#730C, and the NOx conversion was 27% at 200&#730C. The NH3-SCR catalytic activity of the synthesised (Ce,La)CO3F was improved by loaded transition metal Mn. The best catalyst was found to be produced by impregnating (Ce,La)CO3F with 1 mol/L manganese nitrate solution, with a NOx conversion of 80% at 250&#730C. The loading of Mn resulted in the appearance of numerous well-dispersed MnOx species on the catalyst surface, the dispersion of Ce7O12 species was also greatly enhanced, and the reduction in grain size indicated that Mnn+ entered into the (Ce,La)CO3F lattice causing lattice shrinkage. The number of acidic sites on the catalyst surface and the redox capacity were enhanced. The amount of Ce3+ in the catalyst was also enhanced by the introduction of Mnn+, but the proportion of adsorbed oxygen decreased, which indicated that the introduction of Mnn+ was detrimental to the increase in the proportion of adsorbed oxygen. The reaction mechanisms of the (Ce,La)CO3F and Mn/(Ce,La)CO3F catalysts were investigated by in-situ Fourier transform infrared spectroscopy (FTIR). The results showed that catalysts followed the E-R and L-H mechanisms. When loaded with Mn, the main reactive species in the L-H mechanism were the (ad) species on the Br&#248nsted acidic site and the O-Ce3+-O-NO, O-Mn3+-O-NO species. The main reactive species for the E-R mechanism were NH3/ (ad) species and NO. The (ad) species on the Br&#248nsted acidic sites act as the main reactive NH3 (g) adsorbing species, bonded to the Ce4+ in the carrier (Ce,La)CO3F to participate in the acid cycle reaction. The introduction of Mnn+ increases the number of Br&#248nsted acidic sites on the catalyst surface, and acts as an adsorption site for NO, to react with NO to generate more monodentate nitrate species, to participate in the redox cycle reactions. The above results indicated that Mnn+ and (Ce,La)CO3F have a good mutual promotion effect, which makes the loaded catalyst have excellent performance, which provides a theoretical basis for the high value utilization of bastnaesite.

Highlights

  • In recent years, domestic coal consumption has tended to increase and the air pollution problem caused by the coal combustion process has become increasingly serious, with coal-fired power plants representing 60% of the overall emissions from stationary sources

  • The activity results showed that the synthetic (Ce,La)CO3F was roasted at 500 ̊C, and the NOx conversion was 27% at 200 ̊C

  • The NH3-SCR catalytic activity of the synthesised (Ce,La)CO3F was improved by loaded transition metal Mn

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Summary

Introduction

Domestic coal consumption has tended to increase and the air pollution problem caused by the coal combustion process has become increasingly serious, with coal-fired power plants representing 60% of the overall emissions from stationary sources. Cerium-based catalysts have excellent low-temperature catalytic performance, and many researchers have used CeO2 as a carrier to improve the performance of NH3-SCR. The MnOx/CeO2 catalysts prepared with oxalic acid solution as the solvent showed over 80% NO conversion in the range of 100 ̊C - 250 ̊C, and good low temperature sulphur and water resistance, probably because the solvent oxalic acid enhanced the electronic interaction between MnOx and CeO2 and increased the oxygen vacancies in the carrier CeO2, which can promote the decomposition of NO species. This paper is used to improve the catalytic performance of (Ce,La)CO3F by loaded Mn, and to study its NH3-SCR physicochemical properties and reaction mechanism by characterization and in-situ infrared, to clarify the specific reaction mechanism within bastnaesite, and to provide theoretical guidance for the reaction performance and mechanism of rare earth mineral catalysts

Experimental Materials
Preparation of Catalyst
Testing of Catalytic Performance
Catalytic Performance Tests
Physical Phase Structure Analysis
Specific Surface Area Analysis
Redox and Adsorption and Desorption Performance Analysis
Surface Element Valence Analysis
In-Situ Infrared Analysis and Reaction Mechanism Study
Conclusion
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