The absorption–oxidation of nitrogen oxide (NO) induced by aqueous solutions of sodium persulfate (Na 2 S 2 O 8 ) in the presence of SO 2 has been studied in a bubble column reactor operated in semibatch mode. The effects of Na 2 S 2 O 8 concentration (0.01–0.20 M), temperature (23–70 °C), 1550 ppm gas-phase SO 2, and solution pH on NO removal (1000 ppm gas-phase concentration) were investigated. The presence of SO 2 dramatically improved NO gas absorption and oxidation while it was itself completely removed. The NO fractional conversions in the presence of SO 2 ranged from 77% to 83%, with the greatest effect occurring at lower temperatures (23 and 30 °C). While persulfate concentration of 0.1 M appeared optimal for aqueous NO removal, both in the absence and presence of SO 2, significant improvements in NO removal were observed for persulfate concentrations of >0.05 M but antagonistic effects were observed with concentrations of <0.05 M in the presence of SO 2, compared to without SO 2 . The pH range of 6.5–8.5 appears to be ideal for NO removal in the presence of SO 2 . The individual and simultaneous chemistry of NO x and SO 2 removal by persulfate is discussed. The results demonstrate the feasibility of removing NO x and SO x simultaneously by aqueous scrubbing.
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Adewuyi et al. (2013) studied this question.
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