TY - JOUR
T1 - Alkali metal-resistant mechanism for selective catalytic reduction of nitric oxide over V2O5/HWO catalysts
AU - Kang, Running
AU - He, Junyao
AU - Bin, Feng
AU - Dou, Baojuan
AU - Hao, Qinglan
AU - Wei, Xiaolin
AU - Nam Hui, Kwun
AU - San Hui, Kwan
PY - 2021/11/15
Y1 - 2021/11/15
N2 - A series of V
2O
5/HWO catalysts are prepared by hydrothermal and impregnation methods using different precursors, among which the V
2O
5/HWO-C catalyst exhibited the optimal NH
3-SCR performance. Compared to oxalic acid (O) and water (W), commercial bacterial cellulose (C) as a precursor can firstly achieve a more controllable synthesis to form hexagonal WO
3 (HWO) of V
2O
5/HWO-C catalyst. Various characterization (XRD, N
2-BET, TEM, SEM, XPS, EDX mapping, and NH
3/NO-TPD-MS) indicate that a higher specific surface area, abundant active oxygen and surface acidity result from the V
2O
5/HWO-C catalyst. The reason is that HWO-C has an excellent and smooth rod-shaped morphology, which promotes high dispersion of V
2O
5 on its surface. In situ IR results show that the SCR follows the Langmuir-Hinshelwood (L-H) mechanism, where absorbed NO
x intermediate species are formed on the V
2O
5 and react with the NH
4
+ and NH
3abs groups of V
2O
5 and HWO. After loading 1.75 wt% K
+, the obtained K-V
2O
5/HWO-C catalyst exhibits effective resistance to K poisoning and SO
2, and retains 78 % NO
x conversion efficiency at 360 °C after 10 h, attributed to the effective capture of K
+ (1.04 wt%) in HWO-C channels via a new pathway, although approximately 0.71 wt% K
+ are located on HWO-C external surface with weak bonding to V
2O
5.
AB - A series of V
2O
5/HWO catalysts are prepared by hydrothermal and impregnation methods using different precursors, among which the V
2O
5/HWO-C catalyst exhibited the optimal NH
3-SCR performance. Compared to oxalic acid (O) and water (W), commercial bacterial cellulose (C) as a precursor can firstly achieve a more controllable synthesis to form hexagonal WO
3 (HWO) of V
2O
5/HWO-C catalyst. Various characterization (XRD, N
2-BET, TEM, SEM, XPS, EDX mapping, and NH
3/NO-TPD-MS) indicate that a higher specific surface area, abundant active oxygen and surface acidity result from the V
2O
5/HWO-C catalyst. The reason is that HWO-C has an excellent and smooth rod-shaped morphology, which promotes high dispersion of V
2O
5 on its surface. In situ IR results show that the SCR follows the Langmuir-Hinshelwood (L-H) mechanism, where absorbed NO
x intermediate species are formed on the V
2O
5 and react with the NH
4
+ and NH
3abs groups of V
2O
5 and HWO. After loading 1.75 wt% K
+, the obtained K-V
2O
5/HWO-C catalyst exhibits effective resistance to K poisoning and SO
2, and retains 78 % NO
x conversion efficiency at 360 °C after 10 h, attributed to the effective capture of K
+ (1.04 wt%) in HWO-C channels via a new pathway, although approximately 0.71 wt% K
+ are located on HWO-C external surface with weak bonding to V
2O
5.
KW - Alkali metal-resistant
KW - Commercial bacterial cellulose
KW - Poisoning
KW - SCR reaction
KW - V O /HWO catalyst
UR - http://www.scopus.com/inward/record.url?scp=85111803167&partnerID=8YFLogxK
U2 - 10.1016/j.fuel.2021.121445
DO - 10.1016/j.fuel.2021.121445
M3 - Article
VL - 304
JO - Fuel
JF - Fuel
SN - 0016-2361
M1 - 121445
ER -