LIU Yangxian, PAN Jianfeng, LIU Yong. Mass transfer-reaction kinetics for NO removal by combination process of UV/H2O2 oxidation and CaO absorption[J]. CIESC Journal, 2013, (3): 1062-1068. DOI: 10.3969/j.issn.0438-1157.2013.03.039.
LIU Yangxian, PAN Jianfeng, LIU Yong. Mass transfer-reaction kinetics for NO removal by combination process of UV/H2O2 oxidation and CaO absorption[J]. CIESC Journal, 2013, (3): 1062-1068. DOI: 10.3969/j.issn.0438-1157.2013.03.039.DOI:
the mass transfer-reaction kinetics was experimentally studied for NO removal using a combination process of UV/H2O2 oxidation and CaO absorption(UV/H2O2-CaO process) in a lab-scale UV-bubbling column reactor.The mass transfer-reaction process of NO absorption was analyzed to determine its rate controlling step and some measures that can effectively strengthen NO absorption
and some key kinetic parameters were measured and a theoretical model for NO absorption was established.The results indicate that under experimental conditions
the rate of NO absorption almost linearly increases with NO concentration.With increase of H2O2 and CaO concentrations
the efficiencies of NO removal increase greatly at first
and then its change is small.The absorption of NO by combined UV/H2O2-CaO process follows pseudo-first-order kinetics.The NO absorption rate can be effectively strengthened by increases of turbulence in gas phase body
gas-liquid contact area and NO partial pressure.The values calculated from the theoretical model of NO absorption are in good agreement with the experimental values.