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Novel Process of Simultaneous Removal of Nitric Oxide and Sulfur Dioxide Using a Vacuum Ultraviolet (VUV)-Activated O<sub>2</sub>/H<sub>2</sub>O/H<sub>2</sub>O<sub>2</sub> System in A Wet VUV–Spraying Reactor
170
Citations
34
References
2016
Year
A novel process for NO and SO<sub>2</sub> simultaneous removal using a vacuum ultraviolet (VUV, with 185 nm wavelength)-activated O<sub>2</sub>/H<sub>2</sub>O/H<sub>2</sub>O<sub>2</sub> system in a wet VUV-spraying reactor was developed. The influence of different process variables on NO and SO<sub>2</sub> removal was evaluated. Active species (O<sub>3</sub> and ·OH) and liquid products (SO<sub>3</sub><sup>2-</sup>, NO<sub>2</sub><sup>-</sup>, SO<sub>4</sub><sup>2-</sup>, and NO<sub>3</sub><sup>-</sup>) were analyzed. The chemistry and routes of NO and SO<sub>2</sub> removal were investigated. The oxidation removal system exhibits excellent simultaneous removal capacity for NO and SO<sub>2</sub>, and a maximum removal of 96.8% for NO and complete SO<sub>2</sub> removal were obtained under optimized conditions. SO<sub>2</sub> reaches 100% removal efficiency under most of test conditions. NO removal is obviously affected by several process variables. Increasing VUV power, H<sub>2</sub>O<sub>2</sub> concentration, solution pH, liquid-to-gas ratio, and O<sub>2</sub> concentration greatly enhances NO removal. Increasing NO and SO<sub>2</sub> concentration obviously reduces NO removal. Temperature has a dual impact on NO removal, which has an optimal temperature of 318 K. Sulfuric acid and nitric acid are the main removal products of NO and SO<sub>2</sub>. NO removals by oxidation of O<sub>3</sub>, O·, and ·OH are the primary routes. NO removals by H<sub>2</sub>O<sub>2</sub> oxidation and VUV photolysis are the complementary routes. A potential scaled-up removal process was also proposed initially.
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