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首页> 外文期刊>Hydrometallurgy >Leaching kinetics of rare earth elements and fluoride from mixed rare earth concentrate after roasting with calcium hydroxide and sodium hydroxide
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Leaching kinetics of rare earth elements and fluoride from mixed rare earth concentrate after roasting with calcium hydroxide and sodium hydroxide

机译:用氢氧化钙和氢氧化钠烘烤混合稀土浓缩物中稀土元素和氟化物的浸出动力学

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AbstractThe complex leaching kinetics of rare earth elements and fluoride with a HCl-AlCl3solution was investigated for the mixed rare earth concentrate after roasting with calcium hydroxide and sodium hydroxide. The effects of HCl concentration, temperature, reaction time, liquid-solid ratio (L/S), AlCl3concentration and stirring speed on leaching kinetics were explored. The results show that the extractions of REEs and fluoride were 86.05% and 90.23%, respectively, under the conditions: 3mol/L HCl, 0.5mol/L AlCl3, 70°C, 10mL/g liquid-solid ratio, 300rpm stirring speed and 40min. The XRD and SEM analysis of the samples before and after acid leaching show that the rare earth oxides and fluorite were completely leached. The apparent activation energies of leaching REEs and fluoride were calculated, which were 26.95kJ/mol for REEs and 20.70kJ/mol for fluoride. The kinetic data of extractions of REEs and fluoride all fitted a new variant of the shrinking core model, in which both the interfacial transfer and the diffusion through the product layer affected the reaction rate.Graphical abstractThe relationship between 1/3ln(1?x)+[(1?x)?1/3?1] and reaction time for extractions of REEs (a) and fluoride (b).A new variant of the shrinking core model was used to fit the kinetic data in this work. The rate constants of different temperature were calculated with the equation of ln(1?x)/3+[(1?x)?1/3?1]=K3t, and the correlation coefficients were both upon 0.95. The apparent activation energies were calculated to be 26.95kJ/mol for REEs and 20.70kJ/mol for fluoride according to Arrhenius equation.Display OmittedHighlights?The main factors influenced the extractions of REEs and fluoride were indicated, which were different between REEs and fluoride.?The liquid-solid ratio of 10ml/g was reduced compared to the data (20ml/g) given in some literatures.?The results of leaching experiments indicated that the leaching process was efficiently with lower acid concentrate.?With a new variant of the shrinking core model, the apparent activation energies were 26.95 and 20.70kJ/mol for REEs and fluoride.]]>
机译:<![cdata [ 抽象 稀土元素的复杂浸出动力学和HCL-ALCL 3 / CE:INF>用氢氧化钙和氢氧化钠焙烧混合稀土浓缩物的溶液。探讨了HCl浓度,温度,反应时间,液态比(L / S),ALCL 3 浓度和搅拌速度的效果。结果表明,在条件下,REES和氟化物的提取分别为86.05%和90.23%:3mol / L HCl,0.5mol / L Alcl 3 ,70℃,10ml / g液态比,300rpm搅拌速度和40min。酸浸出前后样品的XRD和SEM分析表明稀土氧化物和萤石完全浸出。计算浸出簧片和氟化物的表观活化能量,为REEES为26.95kJ / mol,氟化物20.70kJ / mol。 REES和氟化物提取的动力学数据全部拟合了缩小核心模型的新变型,其中界面转移和通过产品层的扩散影响反应速率。 图形抽象 < ce:abstract-sec id =“AS0010”View =“全部”> 1 / 3Ln(1?x)+ [(1?x )?1/3 α1]和萃取Rees(a)和氟化物(b)的反应时间。 使用缩小核心模型的新变体用于符合这项工作中的动力学数据。使用LN(1≤x)/ 3 + [(1≤x)的等式计算不同温度的速率常数? 1/3 ?1] = K 3 T,并且相关系数均为0.95。根据Arrhenius方程计算表观活化能量为26.95kJ / mol,氟化镍和20.70kJ / mol。 显示省略 亮点 < CE:列表项ID =“LI0005”> 主要因素影响REES和氟化物提取的主要因素,在Rees和氟之间不同。 与某些文献中给出的数据(20ml / g)相比,10ml / g的液态比率减少。 具有缩小核心模型的新变种,可视激活能量为26.95和20.70kJ / mol,用于REES和氟化物。 ]]>

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