<HashMap><database>biostudies-literature</database><scores/><additional><omics_type>Unknown</omics_type><volume>7(10)</volume><submitter>Dong A</submitter><pubmed_abstract>Low-temperature selective catalytic oxidation (SCO) is crucial for removing the NH&lt;sub>3&lt;/sub> slip from the upstream of NH&lt;sub>3&lt;/sub>-selective catalytic reduction (NH&lt;sub>3&lt;/sub>-SCR). Herein, combining zeolite Cu-SAPO34 and the active oxidant mullite SmMn&lt;sub>2&lt;/sub>O&lt;sub>5&lt;/sub>, we developed mixed-phase catalysts SmMn&lt;sub>2&lt;/sub>O&lt;sub>5&lt;/sub>/Cu-SAPO34 by grinding powder mixtures to achieve a low-temperature activity and a reasonable N&lt;sub>2&lt;/sub> selectivity. The physicochemical properties of the catalysts were characterized by X-ray diffraction (XRD), Brunauer-Emmett-Teller (BET) measurement, scanning electron microscopy (SEM), transmission electron microscopy (TEM), X-ray photoelectron spectroscopy (XPS), and in situ diffuse reflectance infrared Fourier transform spectroscopy (DRIFTS). The evaluation of NH&lt;sub>3&lt;/sub> oxidation activity showed that for 30 wt % SmMn&lt;sub>2&lt;/sub>O&lt;sub>5&lt;/sub>/Cu-SAPO34, 90% NH&lt;sub>3&lt;/sub> conversion was at a temperature of 215 °C in the presence of 500 ppm NH&lt;sub>3&lt;/sub&gt; and 21% O&lt;sub>2&lt;/sub> balanced with N&lt;sub>2&lt;/sub>. The in situ DRIFTS spectra reveal the internal SCR mechanism (i-SCR), i.e., NH&lt;sub>3&lt;/sub> oxidizing to NO &lt;i>&lt;sub>x&lt;/sub>&lt;/i> on mullite and NO &lt;i>&lt;sub>x&lt;/sub>&lt;/i> subsequently to proceed with SCR reactions, leading to higher conversion and selectivity over the mixed catalysts. This work provides a strategy to design the compound catalyst to achieve low-temperature NH&lt;sub>3&lt;/sub> oxidation via synergistic utilization of the advantages of each individual catalyst.</pubmed_abstract><journal>ACS omega</journal><pagination>8633-8639</pagination><full_dataset_link>https://www.ebi.ac.uk/biostudies/studies/S-EPMC8928535</full_dataset_link><repository>biostudies-literature</repository><pubmed_title>Mixed Catalyst SmMn&lt;sub>2&lt;/sub>O&lt;sub>5&lt;/sub>/Cu-SAPO34 for NH&lt;sub>3&lt;/sub>-Selective Catalytic Oxidation.</pubmed_title><pmcid>PMC8928535</pmcid><pubmed_authors>Yang Z</pubmed_authors><pubmed_authors>Wang W</pubmed_authors><pubmed_authors>Dong A</pubmed_authors></additional><is_claimable>false</is_claimable><name>Mixed Catalyst SmMn&lt;sub>2&lt;/sub>O&lt;sub>5&lt;/sub>/Cu-SAPO34 for NH&lt;sub>3&lt;/sub>-Selective Catalytic Oxidation.</name><description>Low-temperature selective catalytic oxidation (SCO) is crucial for removing the NH&lt;sub>3&lt;/sub> slip from the upstream of NH&lt;sub>3&lt;/sub>-selective catalytic reduction (NH&lt;sub>3&lt;/sub>-SCR). Herein, combining zeolite Cu-SAPO34 and the active oxidant mullite SmMn&lt;sub>2&lt;/sub>O&lt;sub>5&lt;/sub>, we developed mixed-phase catalysts SmMn&lt;sub>2&lt;/sub>O&lt;sub>5&lt;/sub>/Cu-SAPO34 by grinding powder mixtures to achieve a low-temperature activity and a reasonable N&lt;sub>2&lt;/sub> selectivity. The physicochemical properties of the catalysts were characterized by X-ray diffraction (XRD), Brunauer-Emmett-Teller (BET) measurement, scanning electron microscopy (SEM), transmission electron microscopy (TEM), X-ray photoelectron spectroscopy (XPS), and in situ diffuse reflectance infrared Fourier transform spectroscopy (DRIFTS). The evaluation of NH&lt;sub>3&lt;/sub> oxidation activity showed that for 30 wt % SmMn&lt;sub>2&lt;/sub>O&lt;sub>5&lt;/sub>/Cu-SAPO34, 90% NH&lt;sub>3&lt;/sub> conversion was at a temperature of 215 °C in the presence of 500 ppm NH&lt;sub>3&lt;/sub&gt; and 21% O&lt;sub>2&lt;/sub> balanced with N&lt;sub>2&lt;/sub>. The in situ DRIFTS spectra reveal the internal SCR mechanism (i-SCR), i.e., NH&lt;sub>3&lt;/sub> oxidizing to NO &lt;i>&lt;sub>x&lt;/sub>&lt;/i> on mullite and NO &lt;i>&lt;sub>x&lt;/sub>&lt;/i> subsequently to proceed with SCR reactions, leading to higher conversion and selectivity over the mixed catalysts. This work provides a strategy to design the compound catalyst to achieve low-temperature NH&lt;sub>3&lt;/sub> oxidation via synergistic utilization of the advantages of each individual catalyst.</description><dates><release>2022-01-01T00:00:00Z</release><publication>2022 Mar</publication><modification>2025-04-04T20:22:15.653Z</modification><creation>2025-04-04T20:22:15.653Z</creation></dates><accession>S-EPMC8928535</accession><cross_references><pubmed>35309489</pubmed><doi>10.1021/acsomega.1c06648</doi></cross_references></HashMap>