Application of a Mathematical Model to the Sierra Indiana Ore Leaching Process Containing Thorium, by Means of H2SO4 Solution and HCl

Pedro Orrego, P. Fleming, J. Skeet, Ramón Ávila
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Abstract

The existence of the thorium element in the ores from the Atacama region, Chile, and its importance in the activities of the nuclear industry, have generated the interest of the Chilean Nuclear Energy Commission (CChEN) to study the technical feasibility of its recovery, like ThO2 through the implementation of hydrometallurgical techniques, such as leaching, solvent extraction, among others. The present work has become a report about the research carried out in the Extractive Metallurgy Area of the Department of Advanced Materials of CChEN, whose objective is to know the behavior of the thorium element when the mineral carrier is leached. The leaching tests were carried out in a glass reactor in batch mode, by mechanical agitation, varying different operational parameters, such as: type of leaching solution, concentration of acid in the solution, system temperature and granulometry of the mineral. The results indicate that there is technical feasibility for the recovery of thorium by leaching the mineral carrier with hydrochloric and/or sulfuric solution. The highest recovery of thorium for a sulfuric solution was 70.0% and for a hydrochloric solution of 83.8%, so the process presents a good efficiency in both cases. For a hydrochloric solution, the mathematical model of the thorium recovery efficiency obtained is: Y=31.14+26.25*X1+8.69*X2−0.82*X3+9.5*X12−0.83*X13−3.71*X23−1.83*X123+6.45 The concentration of HCl and temperature, as well as their interaction, significantly affect the recovery of thorium for Sierra Indiana mineral, as well as temperature and granulometry. The previous model gives a good representativeness of 99.98%. For a sulfuric solution, the mathematical model of the thorium recovery efficiency obtained is: Y=29.78+25.92*X1+0.99*X2−1.05*X3−2.05*X12−9.84*X13−5.26*X23−3.87*X123+15.18 The model indicates that the recovery of thorium for the mineral is significantly affected by the concentration of sulfuric acid, and to a lesser degree by the temperature and granulometry. The model provides a representativeness of 98.3%.
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数学模型在Sierra Indiana含钍矿石H2SO4溶液和HCl浸出过程中的应用
智利阿塔卡马地区矿石中钍元素的存在及其在核工业活动中的重要性,引起了智利核能委员会(CChEN)的兴趣,研究其回收的技术可行性,如通过实施湿法冶金技术,如浸出、溶剂萃取等。本工作已成为陈晨先进材料部萃取冶金领域的研究报告,其目的是了解矿物载体浸出时钍元素的行为。浸出试验在玻璃反应器中分批进行,通过机械搅拌,改变不同的操作参数,如:浸出溶液的类型,溶液中的酸浓度,系统温度和矿物的粒度。结果表明,用盐酸或硫酸溶液浸出矿物载体回收钍在技术上是可行的。硫酸溶液中钍的最高回收率为70.0%,盐酸溶液中钍的最高回收率为83.8%,因此该工艺在两种情况下都具有良好的效率。在盐酸溶液中,得到的钍回收率数学模型为:Y=31.14+26.25*X1+8.69*X2 - 0.82*X3+9.5*X12 - 0.83*X13 - 3.71*X23 - 1.83*X123+6.45。HCl浓度、温度、粒度等因素对Sierra Indiana矿物中钍的回收率有显著影响。之前的模型给出了99.98%的良好代表性。对于硫酸溶液,得到的钍回收率的数学模型为:Y=29.78+25.92*X1+0.99*X2 - 1.05*X3 - 2.05*X12 - 9.84*X13 - 5.26*X23 - 3.87*X123+15.18。该模型表明,硫酸浓度对矿物钍的回收率有显著影响,温度和粒度对钍回收率的影响较小。该模型的代表性为98.3%。
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