Mechanistic modelling of catalytic NOX reduction reactions after hydrogen or ammonia combustion on multiple scales

被引:4
作者
Voglar, J. [1 ]
Terzan, J. [2 ]
Kroflic, A. [1 ]
Hus, M. [1 ,3 ,4 ]
Likozar, B. [1 ,5 ,6 ,7 ]
机构
[1] Natl Inst Chem, Dept Catalysis & Chem React Engn, Hajdrihova 19, Ljubljana 1001, Slovenia
[2] Jozef Stefan Inst, Dept Synth Mat, Jamova Cesta 39, Ljubljana 1000, Slovenia
[3] Assoc Tech Culture Slovenia ZOTKS, Zaloska 65, SL-1000 Ljubljana, Slovenia
[4] Inst Protect Cultural Heritage Slovenia, Poljanska 40, Ljubljana 1000, Slovenia
[5] Univ Ljubljana, Fac Chem & Chem Technol, Vecna Pot 113, Ljubljana 1001, Slovenia
[6] Univ Maribor, Fac Chem & Chem Engn, Smetanova Ul 17, Maribor 2000, Slovenia
[7] Fac Polymer Technol, Ozare 19, SL-2380 Slovenj Gradec, Slovenia
关键词
Hydrogen; Ammonia; Modelling; Selective catalytic reduction; DeNO X; DENSITY-FUNCTIONAL THEORY; LOW-TEMPERATURE SCR; BRIDGED CU PAIRS; IN-SITU DRIFTS; NITROGEN-OXIDES; ACTIVE-SITES; 1ST PRINCIPLES; CLUSTER MODEL; DFT ANALYSIS; ACID SITES;
D O I
10.1016/j.rser.2023.113666
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
This article provides a comprehensive review and evaluation of the selective catalytic reduction (SCR) of nitrogen oxides (NOX) using ammonia as a reducing agent in flue gases produced by the combustion of hydrogen or ammonia with air. Over the years, density functional theory calculations (DFT) have been used extensively to complement experimental results, with emphasis on understanding adsorption modes and reaction mechanisms. Recent advances in this field have led to a shift from non-periodic to more accurate periodic models. It has been shown that the SCR reactions mainly follow the Eley-Rideal mechanism, with NH2NO identified as the most important intermediate. Global kinetic and microkinetic models are widely used, but these models often overlook the crucial role of adsorption of water molecules on catalyst surfaces. Consequently, their utility is reduced under conditions of elevated water vapor concentrations. To address this limitation, numerical fluid dynamics simulations (CFD) have been introduced that include user-defined functions to model chemical deNOX reactions. In particular, the method CFD can also take into account the adsorption of relevant species at the active sites of the catalyst. We highlight a significant knowledge gap in the existing literature: the lack of consideration of the adsorption of water on catalyst surfaces during the selective catalytic reduction of NOX. Consequently, these models are inadequate for flue gases with high water vapor content produced during the combustion of hydrogen or ammonia. Addressing this shortcoming is critical to better understand and accurately predict the performance of SCR under different operating conditions.
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页数:14
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