Investigation of the solid oxidizer effect on the metal geotechnology efficiency

IF 2.8 Q2 MINING & MINERAL PROCESSING
Khalidilla Yussupov, E. Aben, D. Akhmetkanov, Khairulla Abenk, Saltanat Yussupova
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Abstract

Purpose. The research is aimed at increasing the useful component content in a pregnant solution during in-situ leaching (ISL) using a solid oxidizer and increasing the ferric iron concentration in the leaching solution based on laboratory research. Methods. Laboratory research is performed on a specially developed model electrolyzer for obtaining comparative data on divalent iron oxidation to trivalent iron and the change in the useful component content in a pregnant solution. Firstly, tests are conducted with a basic leaching solution, then on the oxidation of the leaching solution with a solid oxidizer in the form of a lead dioxide plate. Tests are conducted by changing sulphuric acid concentration within 5-50 g/l, amount of divalent iron ions in the solution from 0.5 up to 4.0 g, lead dioxide plate surface area from 19 to 76 cm2. The leaching time is up to 10 hours. Findings. The results of laboratory research on determining the oxidation degree of divalent iron ions and change in the oxidation-reduction potential (ORP) depending on the sulphuric acid concentration and on the initial concentration of divalent iron ions in the initial solution are presented. With a change in the sulphuric acid concentration from 5 to 50 g/l, the oxidation value of divalent iron ions increases from 26.5 to 96.5%, and with an increase in the initial solution concentration of divalent iron, the oxidation degree of divalent iron naturally decreases from 95.2 to 58.8%. In the initial leaching solution, the divalent solution concentration is 312 mg/l, and that of the trivalent solution is 288 mg/l. After oxidation with a solid oxidizer, the divalent and trivalent iron concentrations are 56 and 392 mg/l, respectively. In the course of further laboratory research using core materials from a uranium deposit, it has been revealed that when leaching with a basic solution, the uranium content in the pregnant solution is 19.36 mg/l, and when leaching with a solution after oxidation with a solid oxidizer, it is 27.9 mg/l, which is by 8.54 mg/l more. Originality. New dependences have been determined of the oxidation degree of divalent iron ions to trivalent one on the sulphuric acid concentration and on the initial concentration of divalent iron ions, as well as the useful component content in the pregnant solution on the leaching time when using a solid oxidizer. Practical implications. Using of a solid oxidizer, it is possible to increase the trivalent iron concentration in the leaching solution and the useful component content in the pregnant solution compared with the basic technology, thereby reducing the time of mining uranium reserves. Proposed technology is environmentally friendly, with low capital costs.
固体氧化剂对金属地质技术效率影响的研究
研究目的本研究旨在利用固体氧化剂在原地沥滤(ISL)过程中提高孕液中有用成分的含量,并在实验室研究的基础上提高沥滤溶液中的铁浓度。方法。在专门开发的电解槽模型上进行实验室研究,以获得二价铁氧化成三价铁以及孕溶液中有用成分含量变化的比较数据。首先用基本浸出液进行试验,然后用二氧化铅板形式的固体氧化剂对浸出液进行氧化试验。试验中,硫酸浓度从 5 克/升到 50 克/升,溶液中二价铁离子的含量从 0.5 克到 4.0 克,二氧化铅板的表面积从 19 平方厘米到 76 平方厘米。浸出时间最长为 10 小时。研究结果实验室研究结果表明,二价铁离子的氧化程度和氧化还原电位(ORP)的变化取决于硫酸浓度和初始溶液中二价铁离子的初始浓度。随着硫酸浓度从 5 克/升增加到 50 克/升,二价铁离子的氧化值从 26.5%增加到 96.5%;随着二价铁初始溶液浓度的增加,二价铁的氧化度自然从 95.2%下降到 58.8%。在初始浸出液中,二价溶液浓度为 312 毫克/升,三价溶液浓度为 288 毫克/升。用固体氧化剂氧化后,二价铁和三价铁的浓度分别为 56 毫克/升和 392 毫克/升。在利用铀矿床岩芯材料进行进一步实验室研究的过程中,发现用碱性溶液浸出时,孕液中的铀含量为 19.36 毫克/升,而用固体氧化剂氧化后的溶液浸出时,铀含量为 27.9 毫克/升,多出 8.54 毫克/升。原创性。确定了二价铁离子氧化成三价铁离子的程度与硫酸浓度和二价铁离子初始浓度的新关系,以及使用固体氧化剂时孕液中有用成分含量与浸出时间的新关系。实际意义。与基本技术相比,使用固体氧化剂可以提高浸出液中三价铁的浓度和孕液中有用成分的含量,从而缩短铀矿开采时间。拟议的技术对环境友好,资本成本低。
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来源期刊
Mining of Mineral Deposits
Mining of Mineral Deposits MINING & MINERAL PROCESSING-
CiteScore
5.20
自引率
15.80%
发文量
52
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