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黄铁矿在硝酸溶液中的溶解动力学

The Kinetics of Pyrite Dissolution in Nitric Acid Solution.

作者信息

Teimouri Samaneh, Potgieter Johannes Herman, van Dyk Lizelle, Billing Caren

机构信息

School of Chemical and Metallurgical Engineering, University of the Witwatersrand, Private Bag X3, Wits 2050, South Africa.

Department of Natural Sciences, Manchester Metropolitan University, Chester Street, Manchester M1 5GD, UK.

出版信息

Materials (Basel). 2022 Jun 13;15(12):4181. doi: 10.3390/ma15124181.

Abstract

Refractory sulphidic ore with gold captured in pyrite has motivated researchers to find efficient means to break down pyrite to make gold accessible and, ultimately, improve gold extraction. Thus, the dissolution of pyrite was investigated to understand the mechanism and find the corresponding kinetics in a nitric acid solution. To carry this out, the temperature (25 to 85 °C), nitric acid concentration (1 to 4 M), the particle size of pyrite from 53 to 212 µm, and different stirring speeds were examined to observe their effect on pyrite dissolution. An increase in temperature and nitric acid concentration were influential parameters to obtaining a substantial improvement in pyrite dissolution (95% Fe extraction achieved). The new shrinking core equation (1/3ln (1 - X) + [(1 - X) - 1)]) = kt) fit the measured rates of dissolution well. Thus, the mixed-controlled kinetics model describing the interfacial transfer and diffusion governed the reaction kinetics of pyrite. The activation energies (E) were 145.2 kJ/mol at 25-45 °C and 44.3 kJ/mol at higher temperatures (55-85 °C). A semiempirical expression describing the reaction of pyrite dissolution under the conditions studied was proposed: 1/3ln(1 - X) + [(1 - X) - 1)] = 88.3 [HNO] r e t. The solid residue was analysed using SEM, XRD, and Raman spectrometry, which all identified sulphur formation as the pyrite dissolved. Interestingly, two sulphur species, i.e., S and S, formed during the dissolution process, which were detected using XRD Rietveld refinement.

摘要

黄铁矿中包裹金的难处理硫化矿促使研究人员寻找有效的方法来分解黄铁矿,使金能够被提取出来,并最终提高金的回收率。因此,研究了黄铁矿在硝酸溶液中的溶解情况,以了解其溶解机理并确定相应的动力学。为此,研究了温度(25至85°C)、硝酸浓度(1至4 M)、粒度为53至212 µm的黄铁矿以及不同搅拌速度对黄铁矿溶解的影响。温度和硝酸浓度的升高是显著提高黄铁矿溶解率(铁提取率达到95%)的影响因素。新的收缩核方程(1/3ln(1 - X) + [(1 - X) - 1])= kt)能很好地拟合测量的溶解速率。因此,描述界面传递和扩散的混合控制动力学模型支配着黄铁矿的反应动力学。在25 - 45°C时活化能(E)为145.2 kJ/mol,在较高温度(55 - 85°C)时为44.3 kJ/mol。提出了一个描述在所研究条件下黄铁矿溶解反应的半经验表达式:1/3ln(1 - X) + [(1 - X) - 1] = 88.3 [HNO] r e t。使用扫描电子显微镜(SEM)、X射线衍射仪(XRD)和拉曼光谱仪对固体残渣进行了分析,所有分析都表明随着黄铁矿的溶解有硫生成。有趣的是,在溶解过程中形成了两种硫物种,即S和S,通过XRD Rietveld精修检测到了它们。

https://cdn.ncbi.nlm.nih.gov/pmc/blobs/a730/9229596/361055c5330b/materials-15-04181-g001.jpg

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