BACKGROUND: SO 2 is an important gaseous pollutant that seriously affects the environment and human health. The most common method for SO 2 removal is absorption by NaOH solution and then forming HSO 3 − . Since generation of high-value products and reduction of alkali consumption are important for the economy and practical application, selenium-catalyzed HSO 3 − disproportionation was developed in this study.RESULTS: Selenium decreased the reaction temperature of HSO 3 − disproportionation from >433 K to 343 K. The effects of HSO 3 − concentration, temperature, selenium dosage, and stirring intensity were investigated. Selenium could be used at least five times with stable catalytic performance, indicating satisfactory reusability. More importantly, a catalytic mechanism was proposed using dynamic light scattering, differential scanning calorimetry and UV-visible transmittance spectrophotometry. Results showed that selenium-catalyzed HSO 3 − disproportionation experienced a solid-liquid-solid phase transformation process. During this process, SeSO 3 2− and HSe − were identified as the intermediates. Furthermore, products, i.e. sulfur and sodium bisulfate, were characterized to demonstrate their structure and composition.
CONCLUSION: Selenium was an efficient catalyst for HSO 3− disproportionation. This catalytic process offered the advantages of less consumption of alkali and production of high-valuable products, and thus was a potential alternative to other technology for SO 2 removal in practical applications. /jctb As shown in the inset graph, standard HSO 3 − had an obvious characteristic absorption peak at 230-350 nm. However, the peak at 235 nm decreased when reaction time was increased from 10 to