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首页> 外文期刊>Minerals Engineering >Nickel sulphide concentrate processing via low-temperature calcination with sodium chloride: Part 2-Chemistry and mechanism of interaction
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Nickel sulphide concentrate processing via low-temperature calcination with sodium chloride: Part 2-Chemistry and mechanism of interaction

机译:硫化镍浓缩加工通过低温煅烧用氯化钠:第2部分 - 化学和相互作用机制

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摘要

The low-temperature calcination of nickel sulphide concentrates with NaCl (at 400-450 degrees C) and subsequent hydrometallurgical processing provide a promising alternative to existing nickel sulphide concentrate processing technologies. The advantages of this processing approach arise from the formation of water-soluble compounds of the metals extracted as well as Na2SO4 generation during calcination, which contributes to significant (up to 75%) reduction in SO2 emission. The influences of the calcination conditions on the recoveries of Ni, Cu, and Fe from the calcine via water leaching are investigated. The optimal conditions for the samples investigated are as follows: calcination temperature of 400 degrees C, NaCl content of 50-100%, and calcination duration of 90 min. Based on these results as well as the data published in Part 1 of this study (thermodynamic, X-ray diffraction, and scanning electron microscopic analyses of the interaction products), the chemistry and mechanism of the calcination of the nickel sulphide concentrate with NaCl are suggested. The proposed mechanism entails the oxidation of sulphides to sulphates (at 325-400 degrees C) followed by partial decomposition of the latter at higher temperatures (400-450 degrees C). During calcination, NaCl interacts with the SO2 emitted owing to sulphide oxidation. This interaction further promotes sulphide oxidation at 350-450 degrees C via the consumption of the product of the reaction, i.e., SO2. Additionally, owing to the removal of SO2 from the system, the interaction of NaCl with SO2 decreases the partial pressure of S to values at which Ni remains in the sulphate form, whereas Fe has already transitioned to the oxide form. Calcine leaching provides the opportunity to extract up to 95% of Cu and Ni using water while simultaneously leaving a significant part of Fe in the cake, and this is very important from a technological perspective.
机译:硫化镍浓缩物与NaCl(400-450℃)和随后的氢化冶金加工的低温煅烧提供了现有的硫化镍浓缩加工技术的有希望的替代品。该处理方法的优点是从煅烧过程中提取的金属的水溶性化合物的形成,这导致SO2排放的显着(高达75%)降低有助于显着(高达75%)。研究了煅烧条件对通过水浸出的煅烧物回收率的回收率。研究的样品的最佳条件如下:煅烧温度为400℃,NaCl含量为50-100%,煅烧持续时间为90分钟。基于这些结果以及本研究第1部分(热力学,X射线衍射和扫描相互作用产品的扫描电子显微镜分析)的数据,氧化镍浓缩物与NaCl的煅烧的化学和机制是建议。所提出的机制需要氧化硫化物至硫酸盐(325-400℃),然后在较高温度下部分分解(400-450℃)。在煅烧过程中,NaCl与由于硫化物氧化而发出的SO 2相互作用。该相互作用在350-450℃下通过消耗反应的产物,即SO 2进一步促进硫化物氧化。另外,由于从系统中除去SO 2,NaCl与SO2的相互作用将S的分压降低于Ni保持在硫酸盐形式的值的分压,而Fe已经过渡到氧化物形式。煅烧浸出提供了利用水提取高达95%的Cu和Ni的机会,同时在蛋糕中留下大部分Fe,这是从技术角度来看非常重要的。

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