A Comparative Study in Vanadium and Tungsten Leaching from Various Sources of SCR Catalysts with Local Difference

被引:4
作者
Su, Qingfa [1 ,2 ,3 ]
Yi, Xianfang [1 ,2 ,3 ]
Miao, Jifa [1 ,2 ,3 ]
Chen, Yanting [1 ,2 ]
Chen, Jinsheng [1 ,2 ]
Wang, Jinxiu [1 ,2 ]
机构
[1] Chinese Acad Sci, Ctr Excellence Reg Atmospher Environm, Inst Urban Environm, Xiamen 361021, Peoples R China
[2] Chinese Acad Sci, Inst Urban Environm, Key Lab Urban Environm & Hlth, Xiamen 361021, Peoples R China
[3] Univ Chinese Acad Sci, Beijing 100049, Peoples R China
关键词
vanadium leaching; tungsten leaching; local difference; color difference; catalyst characterization; V2O5-WO3/TIO2; CATALYST; THERMODYNAMIC ANALYSIS; NOX SCR; REDUCTION; RECOVERY; KINETICS;
D O I
10.3390/su12041499
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Direct leaching with NaOH can be an economically acceptable method for vanadium (V) and tungsten (W) recovery from spent selective catalytic reduction (SCR) catalysts. However, different chemical-physical characteristics of catalysts would affect the V and W leaching. In this paper, the V and W leaching behavior of various sources of SCR catalysts with a local difference (yellow and gray color) were systematically investigated with alkali leaching solution under ambient pressure. Different leaching efficiencies from yellow and gray color areas were correlated with oxidation states and species of V andWon catalyst surfaces, as characterized by X-ray photoelectron spectroscopy (XPS), Raman, Fourier transform infrared spectroscopy (FTIR), and other analytic methods. For the V leaching efficiency, the samples from a gray area of catalysts (40.0-51.0%) were lower than that from the yellow area (66.8-69.8%). The higher molar ratio of V3+ and a lower molar ratio of V5+, and the lower total V content on the surface of the samples from the gray area could be the main reasons for the lower V leaching efficiency. As for theWleaching efficiency, the samples from the gray area (44.6-57.3%) were slightly higher than that from the yellow area (38.0-52.6%) of catalysts. The less total W content of surface species and stronger interaction among V-W-Ti of yellow area samples resulted in the lower leaching efficiency. These differential leaching efficiencies needed to be taken into consideration for recovering V and W from spent SCR catalysts.
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页数:12
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