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Selective leaching of low-grade phosphate ore using a mixture of organic acids

机译:使用有机酸混合物选择性浸出低级磷酸盐矿石

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In the present study, reverse leaching method by the combination of acetic and lactic acid was used for recovery of phosphate from carbonate phosphate ore which contained about 10% P2O5. In the dissolution experiments, leaching time, temperature, acid concentration, solid/liquid ratio and particle size distribution were selected as important parameters and their effects were evaluated. The results showed that optimization of the leaching condition increased the grade of P2O5 to 29% with recovery of 90%. The kinetic experiments (time-temperature) in optimal conditions revealed that activation energy for the leaching was about 24.27 kJ/mol which is an indication of diffusion control processes and the rate of reaction was achieved as ?1-2/3 α-(1-α)^(2/3) ?=k0e-24.27/RT.t. Results showed that by organic acid leaching, it is possible to produce phosphate concentrate from low grade calcareous phosphate ore. In the present study, the reverse leaching method with the combination of acetic and lactic acid was used for the recovery of phosphate from carbonate phosphate ore, which contained about 10% P2O5. In the experiments carried out on the dissolution, leaching time, temperature, acid concentration, solid/liquid ratio, and particle size distribution were selected as important parameters, and their effects were evaluated. The results showed that the optimization of the leaching condition increased the grade of P2O5 to 29% with a recovery of 90%. The kinetic experiments (time-temperature) in optimal conditions revealed that activation energy for the leaching process was about 24.27 kJ/mol which is an indication of diffusion control processes and the rate of reaction was achieved 0e-24.27/RT.t. Results showed that the application of organic acid leaching would facilitate producing phosphate concentrate from low-grade calcareous phosphate ores.
机译:在本研究中,通过组合乙酸和乳酸的反向浸出方法用于从包含约10%P2O5的碳酸酯磷酸盐矿石中回收磷酸盐。在溶出实验中,选择浸出时间,温度,酸浓度,固体/液体比和粒度分布作为重要参数,并评估其效果。结果表明,浸出条件的优化增加了P2O5的等级,回收率为90%。最佳条件下的动力学实验(时间温度)显示浸出的激活能量为约24.27kJ / mol,这是扩散控制过程的指示,并且达到反应速率为α1-2/3α-(1 -α)^(2/3)?= K0E-24.27 / RT.T。结果表明,通过有机酸浸出,可以从低级钙质磷酸盐矿石中产生磷酸盐浓缩物。在本研究中,具有乙酸和乳酸组合的反向浸出方法用于从碳酸盐磷酸盐矿石中恢复磷酸盐,其含有约10%P2O5。在对溶解的实验中选择浸出时间,温度,酸浓度,固体/液体比和粒度分布作为重要参数,并评估其效果。结果表明,浸出条件的优化增加了P2O5的等级,回收率为90%。最佳条件下的动力学实验(时间温度)显示浸出过程的激活能量为约24.27kJ / mol,其是扩散控制过程的指示,并达到反应速率0e-24.27 / Rt.T。结果表明,有机酸浸出的应用将有助于生产来自低级钙质磷酸盐矿石的磷酸盐浓缩物。

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