Desorption of CO2, SO2, and NH(3)in the vacuum evaporation of desulfurization wastewater
Desorption of CO2, SO2, and NH(3)in the vacuum evaporation of desulfurization wastewater
复制标题
脱硫废水真空蒸发脱附CO2、SO2、NH(3)
DOI:
10.1007/s11356-020-10720-4
复制
发表时间:
2021
影响因子:
5.8
通讯作者:
Chen Shouyan
中科院分区:
文献类型:
--
作者:
Chen Guifang;Sun Xiaofei;Feng Yunqi;Song Zhanlong;Cui Lin;Mao Yanpeng;Ma Chunyuan;Chen Shouyan
Mechanical vapor compression and multi-effect evaporation have been widely used in achieving zero discharge of desulfurization wastewater as they are energy-saving and efficient technologies. Solubilized weak ions, such as CO32-, SO32-, and NH4+, in the desulfurization wastewater are partly converted into CO2, SO2,and NH3, respectively, during the vacuum evaporation process, thus affecting the heat exchange and compressor performance. In this study, the migration and coupling mechanism of CO2, SO2, and NH3desorption in desulfurized wastewater under vacuum evaporation were analyzed. The effects of temperature, pressure, reaction time, and other factors on the migration process were discussed. The hydrolysis and electrolytic equilibrium constants of the related ions were obtained for temperatures between 70 and 90 °C. The results demonstrate the relationship between the desorption capacities of CO2, SO2, and NH3and the hydrolysis constants of their respective ions. The desorption of CO2and NH3increased significantly when CO32−and NH4+coexisted, whereas the SO2desorption capacity remained low under the same experimental conditions. The experimental results indicate that the desorption of CO2, SO2, and NH3is controlled by chemical reactions and can be described by first-order reaction kinetics.