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首页> 外文期刊>RSC Advances >Environmentally friendly approach to recover vanadium and tungsten from spent SCR catalyst leach liquors using Aliquat 336
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Environmentally friendly approach to recover vanadium and tungsten from spent SCR catalyst leach liquors using Aliquat 336

机译:使用Aliquat 336从废SCR催化剂浸出液中恢复钒和钨的环保方法

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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 ~(?1) of tungsten and ~0.7 g L ~(?1) of vanadium. The commercial extractant, N -methyl- N , N , N -tri-octyl-ammonium chloride [R _(3) NCH _(3) ] ~(+) 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 H ) 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 _(3) ) > NaOH > NaNO _(3) > NaCl. Stripping isotherm followed by stripping counter-current (CCS) study was carried out for quantitative stripping of the metals.
机译:本研究论文涉及一种环保方法,用于治疗花费选择性催化还原(SCR)催化剂。为了从废SCR催化剂中回收钒(V)和钨(W),利用来自液压冶金加工的浸出液体来开发适当的方法,用于互相提取和可能分离钒和钨。本研究研究了钒和钨的溶剂萃取(也称为液 - 液萃取)利用含有约7g L〜(α1)的钨和〜0.7g L〜(α1)的钒的碱性焙酸浸出溶液。商业萃取剂,N-甲基-N,N,N-辛基 - 氯化铵[R _(3)NCH _(3)]〜(+)CL〜(?)(商业名称Aliquat 336),溶解在埃克森尔? D80(稀释剂)制度并在本研究中采用。进行溶剂萃取研究以确定以下实验参数:平衡pH,萃取剂浓度,稀释剂影响,氯离子浓度,温度和溶出试剂浓度,这些扫描可系统扫描以确定标题金属的定量萃取的最佳条件。斜率分析后使用季铵氯化铵溶剂试剂提出了阴离子交换机制。氯化物的过量补充被证明具有不利影响,进一步支持提取机制。热力学结果显示钒和钨焓(δH)的阳性值,有利于提取反应对任一金属吸收的热敏性质。构建萃取的McCabe-Thiele图,提出钒和钨萃取的3个阶段,在水溶液和钨萃取到有机(O)相比为7?:1,确保超过99.9%和7-折叠富集标题金属。剥离趋势遵循顺序:( NaOH + NaCl)>(NaOH +纳米_(3))> NaOH>纳米_(3)> NaCl。剥离等温线,然后进行剥离逆流(CCS)研究,用于定量剥离金属。

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