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Manganese metallurgy review. Part I: Leaching of ores/secondary materials and recovery of electrolytic/chemical manganese dioxide

机译:锰冶金学评论。第一部分:矿石/辅助材料的浸出和电解/化学二氧化锰的回收

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The world rapidly growing demand for manganese has made it increasingly important to develop processes for economical recovery of manganese from low grade manganese ores and other secondary sources. Part I of this review outlines metallurgical processes for manganese production from various resources, particularly focusing on recent developments in direct hydrometallurgical leaching and recovery processes to identify potential sources of manganese and products which can be economically produced. High grade manganese ores (>40 percent) are typically processed into suitable metallic alloy forms by pyrometallurgical processes. Low grade manganese ores (<40 percent) are conventionally processed by pyrometallurgical reductive roasting or melting followed by hydrometallurgical processing for production of chemical manganese dioxide (CMD), electrolytic manganese (EM) or electrolytic manganese dioxide (EMD). Various direct reductive leaching processes have been studied and developed for processing low manganese ores and ocean manganese nodules, including leaching with ferrous iron, sulfur dioxide, cuprous copper, hydrogen peroxide, nitrous acid, organic reductants, and bio- and electro-reductions. Among these processes, the leaching with cheap sulfur dioxide or ferrous ion is most promising and has been operated in a pilot scale. The crucial issue is the purification of leach liquors and the selective recovery of copper, nickel and cobalt is often difficult from solutions containing soluble iron and manganese. For treatment of manganese bearing materials including waste batteries, spent electrodes, sludges, slags and spent catalysts, a leaching or reductive leaching step is generally needed followed by various purification steps, which makes the processes less economically viable. It is concluded that the recovery of manganese from nickel laterite process effluents which contain 1-5 g/L Mn offers a growing low cost resource of manganese. Part II of this review considers the application of various solvent extraction reagents and precipitation methods for treating such manganese liquors.
机译:世界上对锰的需求迅速增长,因此,开发从低品位锰矿和其他二次资源中经济回收锰的方法变得越来越重要。这篇综述的第一部分概述了利用各种资源生产锰的冶金工艺,尤其着眼于直接湿法冶金浸出和回收工艺的最新发展,以确定可经济生产的锰和产品的潜在来源。高品位锰矿石(> 40%)通常通过火法冶金工艺加工成合适的金属合金形式。低品位锰矿(<40%)通常通过火法还原焙烧或熔融处理,然后进行湿法冶金处理,以生产化学二氧化锰(CMD),电解锰(EM)或电解二氧化锰(EMD)。已经研究和开发了多种直接还原浸出工艺,用于处理低锰矿石和海洋锰结核,包括用亚铁,二氧化硫,铜亚铜,过氧化氢,亚硝酸,有机还原剂以及生物还原和电解还原进行浸出。在这些方法中,用廉价的二氧化硫或亚铁离子浸提是最有前途的,并已在中试规模下进行。关键问题是提纯浸出液,从含可溶性铁和锰的溶液中选择性回收铜,镍和钴通常很困难。为了处理含锰的材料,包括废电池,废电极,污泥,炉渣和废催化剂,通常需要浸出或还原浸出步骤,然后进行各种提纯步骤,这使得该方法在经济上不可行。结论是,从锰含量为1-5 g / L的红土镍工艺废水中回收锰提供了日益增长的低成本锰资源。本文的第二部分考虑了各种溶剂萃取试剂和沉淀方法在处理此类锰液中的应用。

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