Cueva Sola Ana Belen, Parhi Pankaj Kumar, Lee Jin-Young, Kang Hee Nam, Jyothi Rajesh Kumar
Convergence Research Center for Development of Mineral Resources (DMR), Korea Institute of Geoscience and Mineral Resources (KIGAM) Daejeon 34132 Korea
Department of Resource Recycling, Korea University of Science and Technology (UST) Daejeon 34113 Korea.
RSC Adv. 2020 May 26;10(34):19736-19746. doi: 10.1039/d0ra02229b.
This research paper deals with an environmentally friendly approach for the treatment of spent selective catalytic reduction (SCR) catalyst. To recover vanadium (V) and tungsten (W) from spent SCR catalyst, leach liquors from hydrometallurgical processing were utilized to develop a proper methodology for extraction and possible separation of vanadium and tungsten from each other. This study investigated the solvent extraction (also called liquid-liquid extraction) of vanadium and tungsten utilizing the alkaline roasted leached solution containing approximately ∼7 g L of tungsten and ∼0.7 g L of vanadium. The commercial extractant, -methyl-,,-tri-octyl-ammonium chloride [RNCH]Cl (commercial name Aliquat 336), was dissolved in Exxsol™ D80 (diluent) system and adopted in this research. Solvent extraction studies were performed to determine the following experimental parameters: equilibrium pH, extractant concentration, diluent influence, chloride ion concentration, temperature, and stripping reagent concentration, which were systematically scanned to ascertain the optimum conditions for quantitative extraction of both title metals. An anion exchange mechanism was proposed using the quaternary ammonium chloride solvent reagent after slope analysis. Excess supplement of chloride proved to have adverse effects, further supporting the extraction mechanism. Thermodynamics results show positive values for enthalpy (Δ) for vanadium and tungsten, favoring the endothermic nature of the extraction reaction towards the uptake of either metal. McCabe-Thiele plots for extraction were constructed, suggesting 2 and 3 stages for vanadium and tungsten extraction, respectively, at the aqueous (A) to organic (O) phase ratio of 7 : 1, ensuring more than 99.9% and 7-fold enrichment of both title metals. The stripping trend follows the order: (NaOH + NaCl) > (NaOH + NaNO) > NaOH > NaNO > NaCl. Stripping isotherm followed by stripping counter-current (CCS) study was carried out for quantitative stripping of the metals.
本研究论文探讨了一种环境友好型处理废选择性催化还原(SCR)催化剂的方法。为了从废SCR催化剂中回收钒(V)和钨(W),利用湿法冶金工艺的浸出液开发了一种合适的方法,用于钒和钨的萃取以及彼此之间的可能分离。本研究利用含有约7 g/L钨和约0.7 g/L钒的碱性焙烧浸出溶液,对钒和钨进行了溶剂萃取(也称为液-液萃取)研究。商业萃取剂甲基三辛基氯化铵[RNCH]Cl(商品名Aliquat 336)溶解在Exxsol™ D80(稀释剂)体系中,并应用于本研究。进行了溶剂萃取研究以确定以下实验参数:平衡pH值、萃取剂浓度、稀释剂影响、氯离子浓度、温度和反萃剂浓度,系统地扫描这些参数以确定两种目标金属定量萃取的最佳条件。在斜率分析后,使用季铵氯化物溶剂试剂提出了一种阴离子交换机制。过量补充氯离子被证明具有不利影响,进一步支持了萃取机制。热力学结果表明钒和钨的焓(Δ)值为正值,有利于萃取反应吸收任何一种金属的吸热性质。构建了萃取的麦凯布-蒂勒图,表明在水相(A)与有机相(O)的比例为7∶1时,钒和钨萃取分别需要2级和3级,确保两种目标金属的富集率均超过99.9%且达到7倍。反萃趋势遵循以下顺序:(NaOH + NaCl)>(NaOH + NaNO)> NaOH > NaNO > NaCl。进行了反萃等温线以及反萃逆流(CCS)研究以对金属进行定量反萃。