Studying electrical parameters of contact and contactless polarization of particles under the electrochemical treatment of mineral suspensions

IF 0.2 Q4 FORESTRY Lesnoy Zhurnal-Forestry Journal Pub Date : 2023-04-25 DOI:10.21440/0536-1028-2023-2-9-20
I. Morozov, A. Valtseva
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Abstract

Introduction. Electrochemical treatment of mineral suspensions is used in electrochemical conditioning of flotation pulp and electrochemical dissolution of minerals and metals in the processes of gold-bearing products electrochemical chlorination. Research objective is to develop and implement the procedures for determining the values of the liquid phase resistance, contact resistance under contact polarization, and ion discharge energy loss resistance under contactless polarization of the electrically conductive part. Methods of research. Equivalent circuits of electrochemical processes have been built for various electrochemical cells. Circuits for various polarizations of electrically conductive particles are established. A formula is proposed for calculating the electrically conductive particle resistance through the electrical resistivity of a unit of volume. A procedure has been developed for calculating the liquid phase resistance through the resistance increment under changing distance between the electrodes. The contact area and pressure influence on the value of the contact resistance is studied through the contact of pyrite and chalcopyrite with an iron electrode. Results. When studying the electrical resistivity of the liquid phase, it was found that increased distance between the current-carrying electrodes leads to an equivalent increase in the liquid phase resistance. It has been established that increased pressure and contact area between the contacting particles and the current-carrying electrode results in decreased contact resistance. The contact resistance between the particle and the electrode in the electrolyte solution is much less than the contact resistance under dry surfaces contact. This phenomenon is explained by electrons tunneling through the electrolyte film. The obtained experimental data on the determination of the liquid phase resistance, contact resistance and ion discharge energy loss resistance make it possible to mathematically describe the processes of electrochemical chlorination under a large number of particles in the pulp. Conclusions and scope of results. Procedures have been developed and specific data have been obtained on the liquid phase resistance, contact resistance, and ion discharge resistance. They can be used for practical application when implementing electrochemical technologies for mineral suspensions treatment.
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研究了矿物悬浮液在电化学处理下颗粒的接触极化和非接触极化的电参数
介绍。矿物悬浮液的电化学处理主要用于浮选矿浆的电化学调理和含金产品电化学氯化过程中矿物和金属的电化学溶解。研究目的是制定并实现导电部分的液相电阻、接触极化下的接触电阻和非接触极化下离子放电能量损失电阻的测定程序。研究方法。已经为各种电化学电池建立了电化学过程的等效电路。建立了导电粒子的各种极化电路。提出了用单位体积的电阻率计算导电粒子电阻的公式。本文提出了一种通过电极间距变化时的电阻增量来计算液相电阻的方法。通过铁电极接触黄铁矿和黄铜矿,研究了接触面积和压力对接触电阻值的影响。结果。在研究液相电阻率时,发现载流电极之间距离的增加会导致液相电阻的等效增加。已经确定,接触颗粒与载流电极之间的压力和接触面积的增加会导致接触电阻的降低。在电解质溶液中,颗粒与电极之间的接触电阻远小于干燥表面接触下的接触电阻。这种现象可以用电子穿隧穿过电解质薄膜来解释。所得的测定液相电阻、接触电阻和离子放电能量损失电阻的实验数据,使得用数学方法描述纸浆中大量颗粒情况下的电化学氯化过程成为可能。结论和结果范围。已经制定了程序,并获得了有关液相电阻、接触电阻和离子放电电阻的具体数据。它们可用于实际应用时实施电化学技术的矿物悬浮液处理。
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