The adsorption isotherms of the polysulfone hollow fiber chelating membrane modified with thionrea as chelating groups for Hg^2+ were determined. The effects of mobile phase conditions and the operating parameters on...The adsorption isotherms of the polysulfone hollow fiber chelating membrane modified with thionrea as chelating groups for Hg^2+ were determined. The effects of mobile phase conditions and the operating parameters on removal performance of the chelating membrane for Hg^2+ were also investigated. The recovery of Hg^2+ decreased at low pH and the optimum range of pH was from 6 to 7. The feed concentration effected on recovery of Hg^2+ at the specified loading amount of Hg^2+. The Hg^2+ could be removed from different concentration feed solution by chelating membrane. The increase of feed flow rate led to slight decrease of recovery of Hg^2+ at the specified loading amount of Hg^2+. The chelating membrane could be operated at height feed flow rate and a large-scale removal of H^2+ could be realized. With the increase of load amount, Hg^2+ recovery decreased, but the saturation degree of chelating membrane increased. According to required recovery of H^2+ and the saturation degree of chelating membrane, the optimum loading amount of Hg^2+ should be selected in the actual removal of H^2+.展开更多
基金the Natural Science Foundation of Tianjin (No05YFJ MJC04200)
文摘The adsorption isotherms of the polysulfone hollow fiber chelating membrane modified with thionrea as chelating groups for Hg^2+ were determined. The effects of mobile phase conditions and the operating parameters on removal performance of the chelating membrane for Hg^2+ were also investigated. The recovery of Hg^2+ decreased at low pH and the optimum range of pH was from 6 to 7. The feed concentration effected on recovery of Hg^2+ at the specified loading amount of Hg^2+. The Hg^2+ could be removed from different concentration feed solution by chelating membrane. The increase of feed flow rate led to slight decrease of recovery of Hg^2+ at the specified loading amount of Hg^2+. The chelating membrane could be operated at height feed flow rate and a large-scale removal of H^2+ could be realized. With the increase of load amount, Hg^2+ recovery decreased, but the saturation degree of chelating membrane increased. According to required recovery of H^2+ and the saturation degree of chelating membrane, the optimum loading amount of Hg^2+ should be selected in the actual removal of H^2+.