Spent V2O5-WO3/TiO2 catalyst processing for valuable metals by soda roasting-water leaching

被引:75
作者
Choi, In-Hyeok [1 ,2 ]
Kim, Hye-Rim [3 ]
Moon, Gyeonghye [2 ]
Jyothi, Rajesh Kumar [1 ,2 ]
Lee, Jin-Young [1 ,2 ]
机构
[1] Korea Univ Sci & Technol UST, Dept Resource Recycling, Daejeon 34113, South Korea
[2] Korea Inst Geosci & Mineral Resources KIGAM, Convergence Res Ctr Dev Mineral Resources DMR, Daejeon 34132, South Korea
[3] Korea Resources Corp KORES, Mineral Proc Team, Wonju 26464, South Korea
关键词
Tungsten; Vanadium; Spent SCR catalyst; Water leaching; Soda roasting; SELECTIVE RECOVERY; PART I; VANADIUM; DECOMPOSITION; MOLYBDENUM; EXTRACTION; TUNGSTEN; ACID; ASH;
D O I
10.1016/j.hydromet.2017.12.010
中图分类号
TF [冶金工业];
学科分类号
0806 ;
摘要
In this paper, extraction of vanadium and tungsten from spent selective catalytic reduction (SCR) catalyst by a soda roasting process was investigated. The leaching efficiency of tungsten significantly increased with the increases in Na2CO3 addition, roasting time and temperature. A leaching efficiency of tungsten was achieved with 92% when the spent SCR catalyst was roasted using 10 equivalent ratio of Na2CO3/total wt% of V2O5 and WO3 under the following conditions: particle size of feedstock, < 106 um; roasting temperature, 1073 K; and roasting time, 120 min. Of particular note, increasing the leaching efficiency of tungsten was closely related to the degree of phase transition from TiO2 anatase to its rutile phase and suppression of formation of CaWO4 by increasing the amount of Na2CO3 addition. On the other hand, the leaching efficiency of vanadium was seldom affected by the soda roasting variables, and showed almost constant around 40% throughout the experimental results. This was presumably due to the formation of calcium vanadate by the reaction with CaO in the feedstock. Furthermore, it can be assumed that the leaching efficiency of vanadium was determined by the content of calcium in the feedstock.
引用
收藏
页码:292 / 299
页数:8
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