首页> 外文期刊>Journal of Alloys and Compounds: An Interdisciplinary Journal of Materials Science and Solid-state Chemistry and Physics >Collection of magnesium in an Mg-Pb alloy cathode placed at the bottom of the cell in MgCl_2 electrolysis
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Collection of magnesium in an Mg-Pb alloy cathode placed at the bottom of the cell in MgCl_2 electrolysis

机译:在MgCl_2电解槽底部放置的Mg-Pb合金阴极中收集的镁

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摘要

The electrolytic cell features a top inserted graphite anode and a cathode, Mg-Pb alloy, placed at the bottom of the cell to reduce recombination of magnesium and chlorine in the inter-electrode region. The process involved the electrolysis of MgCl_2 to form an Mg-Pb alloy that is heavier than the electrolyte and a subsequent refining of the alloy to obtain electrolytic grade magnesium. To achieve metallic magnesium production rate with the present cell, that is comparable with the conventional methods, higher current densities have to be used with the present system. The effects of current density on the cell performance have been determined in the present study. The evaluation of the results indicated that the major part of applied voltage is the theoretical decomposition potential and the IR drop. Energy consumption increased from 9.2 to 19.8 kW h kg~(-1) of magnesium produced during electrolysis when the current density increased from 0.48 to 1.98 A cm~(-2). The total energy required including the refining is 13.9 k W h kg~(-1) Mg at 1 Acm~(-2). The results obtained show that the present cell could work at comparable production rates to commercial cells with an energy consumption that is at the lower end of 13-18 kW h kg~(-1). Lower production rates can be used to achieve lower energy consumption.
机译:电解池具有顶部插入的石墨阳极和阴极Mg-Pb合金,该阴极位于电解池的底部,可减少电极间区域中镁和氯的重组。该方法涉及电解MgCl_2以形成比电解质重的Mg-Pb合金,然后精炼该合金以获得电解级镁。为了用本电池达到与常规方法相当的金属镁生产速率,必须在本系统中使用更高的电流密度。在本研究中已经确定了电流密度对电池性能的影响。结果评估表明,施加电压的主要部分是理论分解电位和IR降。当电流密度从0.48 A cm〜(-2)增加到1.98 A·cm-1(-1)时,电解过程中产生的镁的能量消耗从9.2 kW h kg·(-1)增加到1。在1 Acm〜(-2)时,包括精炼在内的总能量为13.9 k W h kg〜(-1)Mg。所获得的结果表明,本发明的电池可以以与商业电池相当的生产率工作,其能量消耗为13-18kWh kg·(-1)的下限。较低的生产率可用于降低能耗。

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