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Open AccessDOI: 10.1016/S1872-5813(25)60613-XOriginal Research

Influence of Preparation Method on the Denitration Performance of Co-Modified Ce/TiO2 Catalysts

Key Laboratory of Energy Heat Conversion and Process Measurement and Control, Ministry of Education, School of Energy and Environment, Southeast University, Nanjing 211189, China

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Influence of Preparation Method on the Denitration Performance of Co-Modified Ce/TiO2 Catalysts
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Published In
Journal of Fuel Chemistry and Technology
Published:January 15, 2026Edition:Vol. 54, Issue 3 • pp. 100-112Citation:YU Chao et al. (2026), Journal of Fuel Chemistry and Technology
Impact FactorPeer-Reviewed Core
Source Journal燃料化学学报

Key Takeaways & Executive Findings

  • • • The Ce-Co0.025/TiO2-SG catalyst, prepared via sol-gel with Co/Ti mass ratio 0.025, achieved >95% NO conversion in the 225–350 °C range, outperforming impregnation and co-precipitation methods, which is critical for meeting ultra-low emission standards in cement plants. • • The catalyst exhibited high N2 selectivity, minimizing undesirable N2O byproduct formation, which is essential for environmental compliance and ammonia slip reduction. • • Characterization revealed abundant surface oxygen vacancies and a high Ce3+ proportion, which enhance redox properties and oxygen mobility, leading to improved low-temperature activity. • • The catalyst displayed the lowest reduction peak temperature in H2-TPR, indicating excellent reducibility, and a mesoporous structure that increased acidic site exposure, both contributing to its superior performance.

Abstract

This study systematically optimized the preparation of Co-modified Ce/TiO2 catalysts and investigated the effects of preparation method and Co loading on their low-temperature denitrification activity. The sol-gel method with a Co/Ti mass ratio of 0.025 (Ce-Co0.025/TiO2-SG) yielded superior performance compared to impregnation and co-precipitation methods. The catalyst maintained NO conversion above 95% in the 225–350 °C range and exhibited high N2 selectivity. Characterization via BET, XRD, XPS, H2-TPR, and in situ DRIFTS revealed that the enhanced activity was attributed to abundant surface oxygen vacancies, a high proportion of Ce3+ species, and prominent acidic sites. The catalyst followed the Eley-Rideal mechanism, effectively inhibiting nitrate intermediate formation and promoting NO-to-NO2 oxidation. This work provides a reference for developing efficient low-temperature denitrification catalysts for industrial applications such as cement production, which emitted 722,000 tons of NOx in 2020, accounting for 17.3% of industrial emissions.

1. Introduction

The cement industry, a cornerstone of infrastructure development, is also a major source of nitrogen oxides (NOx) emissions. In 2023, China produced over 2 billion tons of cement, accounting for more than 50% of global output, and emitted 722,000 tons of NOx in 2020, representing 17.3% of total industrial emissions. Conventional NOx control technologies, such as low-nitrogen burners and staged combustion, achieve only 25–40% efficiency, falling short of ultra-low emission requirements. End-of-pipe solutions like selective non-catalytic reduction (SNCR) reach ~60% efficiency but suffer from high ammonia slip, while selective catalytic reduction (SCR) can exceed 90% efficiency with minimal ammonia slip, making it the preferred technology for stringent regulations.

However, commercial SCR catalysts often exhibit inadequate low-temperature activity, limiting their application in cement flue gas streams where temperatures are typically below 300 °C. This study addresses this bottleneck by developing Co-modified Ce/TiO2 catalysts via different preparation methods. The sol-gel method, with an optimized Co/Ti ratio of 0.025, produced a catalyst with superior low-temperature denitrification performance, maintaining >95% NO conversion at 225–350 °C. The enhanced activity is attributed to abundant oxygen vacancies, high Ce3+ content, and increased acidic sites, which collectively improve redox properties and promote the Eley-Rideal mechanism. These findings offer a promising pathway for efficient low-temperature SCR catalysts tailored to the cement industry.

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Cite This Research Paper
YU Chao, ZHANG Boya, SHEN Kai, HAN Yuxuan, ZHANG Yaping (2026). Influence of Preparation Method on the Denitration Performance of Co-Modified Ce/TiO2 Catalysts. Journal of Fuel Chemistry and Technology. https://doi.org/10.1016/S1872-5813(25)60613-X
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Frequently Asked Questions

What is the optimal Co loading and preparation method for maximizing low-temperature denitration activity?

The optimal catalyst is Ce-Co0.025/TiO2-SG, prepared via sol-gel with a Co/Ti mass ratio of 0.025. It achieves >95% NO conversion in the 225–350 °C range, outperforming catalysts made by impregnation and co-precipitation.

How does the sol-gel method enhance the catalyst's redox properties compared to other methods?

The sol-gel method yields a catalyst with the lowest reduction peak temperature in H2-TPR, indicating superior reducibility. This is attributed to abundant oxygen vacancies and a high Ce3+ proportion, which facilitate electron transfer and oxygen mobility.

What reaction mechanism does the Ce-Co0.025/TiO2-SG catalyst follow, and how does it affect performance?

In situ DRIFTS studies show the catalyst follows the Eley-Rideal (E-R) mechanism, where gaseous NO reacts with adsorbed NH3 species. This pathway effectively inhibits nitrate intermediate formation and enhances NO-to-NO2 oxidation, contributing to high N2 selectivity and low-temperature activity.

What are the key surface characteristics that contribute to the catalyst's high activity?

The catalyst possesses abundant surface oxygen vacancies, a high proportion of Ce3+ species, and prominent acidic sites. These features increase chemisorbed oxygen and enhance NH3 adsorption, promoting the SCR reaction at lower temperatures.

How does the catalyst's performance compare to commercial SCR catalysts in terms of temperature window and selectivity?

The Ce-Co0.025/TiO2-SG catalyst maintains >95% NO conversion from 225 to 350 °C, which is a broader and lower temperature window than many commercial catalysts that typically operate above 300 °C. It also exhibits high N2 selectivity, minimizing N2O byproduct formation.

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