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Extraction of Tungsten and Vanadium from the Spent SCR Catalyst by High Pressure Alkaline Leaching Method

机译:高压碱性浸出法从废SCR催化剂中提取钨和钒

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Tungsten and vanadium are efficiently extracted from honeycomb-type spent selective catalytic reduction (SCR) catalyst by using a high pressure alkali leaching method. Theoretical thermodynamics calculation indicates that WO_3 and V_2O_5 are soluble in sodium hydroxide solution, proving that the extraction of Wand V from the spent SCR catalyst by high pressure alkaline leaching is feasible. The effects of NaOH concentration, leaching temperature and time, liquid-solid ratio and stirring speed on leaching efficiency of W and V are systematically investigated. The leaching efficiency of W and V is 94.3% and 91.2%, respectively, under the optimal conditions: the NaOH concentration of 2mol/L, the leaching temperature 463.5 K, the reaction time 3 h, solid-liquid ratio 0.1 g/ml, the stirring speed of400 r/min. The TiO_2 residue is in anatase crystalline phase.
机译:通过使用高压碱浸出方法,从蜂窝型废选择性催化还原(SCR)催化剂有效地提取钨和钒。理论热力学计算表明WO_3和V_2O_5可溶于氢氧化钠溶液中,证明通过高压碱性浸出从废SCR催化剂中提取魔杖V是可行的。系统地研究了NaOH浓度,浸出温度和时间,液态比和搅拌速度对W和V浸出效率的影响。在最佳条件下,W和V的浸出效率分别为94.3%和91.2%:2mol / L的NaOH浓度,浸出温度463.5k,反应时间3小时,固液比0.1g / ml,搅拌速度为400 r / min。 TiO_2残基是在锐钛矿结晶相处。

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