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Generation mechanism of SO2 on the surface of commercial V/W/Ti DeNOx catalysts |
QING Meng-xia1, LIU Liang1, YIN Zi-jun2, LEI Si-yuan3, WANG Le-le3, SU Sheng2, XIANG Jun2 |
1. School of Energy and Power Engineering, Changsha University of Science and Technology, Changsha 410114, China; 2. State Key Laboratory of Coal Combustion, Huazhong University of Science and Technology, Wuhan 430074, China; 3. Xi'an thermal Power research institute Company Limited, Suzhou branch, Suzhou 215153, China |
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Abstract Based on the serious impact of SO3 generation and emission in coal-fired flue gas on the operation of power plants and the atmospheric environment, the SO3 generation reaction kinetic and reaction mechanism in the surface of a typical commercial honeycomb V/W/Ti DeNOx catalyst are studied. The reaction temperature and SO2 were the key factors affecting the generation of SO3 on the catalyst surface. SO2-SO3 conversion rate increased from 0.2% to 0.65% when the reaction temperature increased from 300℃ to 360℃ under 400×10-6 SO2 condition. After the reaction temperature reached to 400℃, the catalytic activity of V2O5 in catalyst surface increased more significantly, the SO2-SO3 conversion rate increased to 2.3%, and the apparent rate constant of SO3 generation reaction also increased significantly by nearly 3times. The generation path of SO3 on the catalyst surface is: SO2 reacted with V5+-OH to generate intermediate products VOSO4 and HSO4-, and then further reacted to generate SO3. SO2 mainly affected SO3 generation through its adsorption and conversion on the catalyst surface, and its intrinsic kinetic reaction order is 0.52. The intrinsic kinetic reaction order of O2 is 0, the generation reaction of SO3 could be carried out without O2. The presence of O2 could promote SO3 generation reaction, but did not change SO3 generation path.
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Received: 02 December 2020
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