2020
DOI: 10.1016/j.mcat.2020.111044
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Investigation of SO2 and H2O poisoning over Cu-HPMo/TiO2 catalyst for Low temperature SCR: An experimental and DFT study

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Cited by 11 publications
(6 citation statements)
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“…Figure 6a,c,e shows the stable adsorption configurations of NO in CuO X @ MnO X , CuO X , and MnO X , respectively. The adsorption configuration of NO in CuO X was consistent with the results of Jiang et al [49] Moreover, when NO was adsorbed in catalysts such as CuO X @MnO X , CuO X , and MnO X , three kinds of chemical bonds, ON (1.47 Å), CuN (1.51 Å), and MnN (1.68 Å), were formed with adsorption energies of −0.89, −0.95, and −1.44 eV, respectively. This indicated that the three catalysts have strong adsorption of NO.…”
Section: Resultssupporting
confidence: 90%
“…Figure 6a,c,e shows the stable adsorption configurations of NO in CuO X @ MnO X , CuO X , and MnO X , respectively. The adsorption configuration of NO in CuO X was consistent with the results of Jiang et al [49] Moreover, when NO was adsorbed in catalysts such as CuO X @MnO X , CuO X , and MnO X , three kinds of chemical bonds, ON (1.47 Å), CuN (1.51 Å), and MnN (1.68 Å), were formed with adsorption energies of −0.89, −0.95, and −1.44 eV, respectively. This indicated that the three catalysts have strong adsorption of NO.…”
Section: Resultssupporting
confidence: 90%
“…At the early stages of the reaction, activity increases by increasing the reaction time using water vapor as a poison with NO x conversion rising from 21% in 300 min to 30% at the end of the reaction for CoNT. Likewise, NO x conversions over NiNT and PtNT are enhanced to values up to 40% in 150 min, and the value greatly increases to 100% running the reaction beyond this time in 600 min.Most of the findings state that the SCR reactions in the presence of water vapor poison are inhibited since the referred vapor can compete by the active sites of the catalysts through competitive adsorption causing a decay in the NO x conversion at relatively low concentrations, e.g.,1–5% of H 2 O [ 56 , 57 , 58 ].…”
Section: Resultsmentioning
confidence: 99%
“…When water vapor is introduced, the adsorption of H 2 O on the active metal sites may occur, and the Lewis acid sites might be converted into Brønsted acid sites via bonding of a water molecule, in line with the findings [ 60 ]. The literature reports also show that the SO 2 might be harmful to the metal active sites in reason of the permanent and irreversible SO 2 adsorption on the metal, besides the competitive adsorption of NO x , CO and SO 2 for the active sites [ 15 , 56 ]. Another fact is that SO 2 addition may form elemental sulfur, which probably could cover the active metal surface and block the pores causing damage in the catalyst structure [ 8 , 61 ].…”
Section: Resultsmentioning
confidence: 99%
“…81,82 In this regard, various selections of supports were expected to enhance the catalytic performance in the NH 3 -SCR process. [83][84][85] For instance, pretreated raw mud (PRM) was used as a support, and then CuO/PRM catalysts were synthesized by introducing varying CuO contents. 86 The results showed that 7 wt% CuO promoted the redox equilibrium of Cu 2+ + Fe 2+ 2 Cu + + Fe 3+ and induced more Cu + and surface oxygen active species.…”
Section: Support Derivationmentioning
confidence: 99%