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Removal of Metal Impurities from the Spent Hydroprocessing Catalyst and Acid Leaching Kinetics of Aluminum

机译:从废液加工催化剂中除去金属杂质和铝的酸浸出动力学

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The impurity metal of Al in spent hydroprocessing catalyst (Mo-Ni/Al_2O_3) was removed by HCl, and the metals of Mo and Ni were preliminarily enriched. The results show that the leaching efficiency of Al was 88.62%, and the leaching efficiency of Mo and Ni were 16.32% and 28.74%, respectively. The results were achieved under optimal leaching conditions: the particle size was 150 μm, the concentration of HCl was 4 mol/L, the leaching temperature was 90 °C, and the leaching time was 120 min. The kinetics of the leaching behavior of Al showed that the acid leaching reaction of Al was in accorded with the equation 1-2/3X-(1-X)~(2/3)=K2t, R~2=0.97734, which was controlled by internal diffusion. X-ray diffraction analysis of the leaching residue revealed the existence of residual metals Mo(MoO_3, MoO_2(ClO_4)_2)and Ni(NiS). The separation of Al from Mo and Ni has been preliminarily realized, which is conducive to further efficient recovery of Mo and Ni.
机译:通过HCl除去废液加工催化剂中Al的杂质金属(Mo-Ni / Al_2O_3),纯化Mo和Ni的金属富集。 结果表明,Al的浸出效率为88.62%,Mo和Ni的浸出效率分别为16.32%和28.74%。 结果在最佳浸出条件下实现:粒度为150μm,HCl的浓度为4mol / L,浸出温度为90℃,浸出时间为120分钟。 A1的浸出行为的动力学表明,Al的酸浸出反应与等式1-2 / 3x-(1-x)〜(2/3)= K2T,R〜2 = 0.97734 由内部扩散控制。 浸出残余物的X射线衍射分析显示存在残留金属MO(MOO_3,MOO_2(CLO_4)_2)和Ni(NIS)的存在。 初步实现了来自Mo和Ni的Al的分离,有利于进一步有效地回收Mo和Ni。

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