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Technical Papers

Effect of the Mn oxidation state and lattice oxygen in Mn-based TiO2 catalysts on the low-temperature selective catalytic reduction of NO by NH3

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Pages 1085-1092 | Published online: 21 Aug 2012

Figures & data

Figure 1. Effect of calcination temperature on surface area, pore volume, and pore diameter of the Mn/TiO2 catalysts.

Figure 1. Effect of calcination temperature on surface area, pore volume, and pore diameter of the Mn/TiO2 catalysts.

Figure 2. X-ray diffraction patterns of the Mn/TiO2 catalysts with different calcination temperatures (A = anatase TiO2; R = rutile TiO2).

Figure 2. X-ray diffraction patterns of the Mn/TiO2 catalysts with different calcination temperatures (A = anatase TiO2; R = rutile TiO2).

Figure 3. H2-TPR profiles of the Mn/TiO2 catalysts with different calcination temperatures.

Figure 3. H2-TPR profiles of the Mn/TiO2 catalysts with different calcination temperatures.

Figure 4. NH3-TPD profiles of the Mn/TiO2 catalysts with different calcination temperatures using TCD.

Figure 4. NH3-TPD profiles of the Mn/TiO2 catalysts with different calcination temperatures using TCD.

Figure 5. NH3-TPD profiles of the Mn/TiO2 catalysts with different calcination temperatures using mass spectrum. (A) Investigation of NH3, O2 and H2O; (B) investigation of N2, NO, N2O, and NO2 (color figure available online).

Figure 5. NH3-TPD profiles of the Mn/TiO2 catalysts with different calcination temperatures using mass spectrum. (A) Investigation of NH3, O2 and H2O; (B) investigation of N2, NO, N2O, and NO2 (color figure available online).

Figure 6. NO-TPD spectra of the Mn/TiO2 catalysts with different calcination temperatures using mass spectrum. (A) Investigation of NO; (B) investigation of NO2.

Figure 6. NO-TPD spectra of the Mn/TiO2 catalysts with different calcination temperatures using mass spectrum. (A) Investigation of NO; (B) investigation of NO2.

Figure 7. Oxidation activity of NO to NO2 by O2 on the Mn/TiO2 catalysts with different calcination temperatures. (Reaction condition: 200 ppm NO, 8% O2, 6% H2O, GHSV = 60,000 hr−1).

Figure 7. Oxidation activity of NO to NO2 by O2 on the Mn/TiO2 catalysts with different calcination temperatures. (Reaction condition: 200 ppm NO, 8% O2, 6% H2O, GHSV = 60,000 hr−1).

Figure 8. NOx conversion of the Mn/TiO2 catalysts with different calcination temperatures. (Reaction condition: 200 ppm NOx, 8% O2, 6% H2O, NH3/NOx = 1, GHSV = 60,000 hr−1).

Figure 8. NOx conversion of the Mn/TiO2 catalysts with different calcination temperatures. (Reaction condition: 200 ppm NOx, 8% O2, 6% H2O, NH3/NOx = 1, GHSV = 60,000 hr−1).

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