锌(II)和苛性碱含量对铝酸钠溶液分解的影响以及与拜耳法的相关性

IF 4.8 2区 材料科学 Q1 METALLURGY & METALLURGICAL ENGINEERING
Lei Xu , Wen-mi Chen , Yan-jun Zhang , Shang Fan , Jian-qing Pi , Ming-li Wang
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引用次数: 0

摘要

研究了不同苛性碱浓度下锌(Zn)对铝酸钠溶液种子分解过程的影响。结果表明,随着铝酸钠溶液中锌(II)浓度从 0 毫克/升增加到 1000 毫克/升,在苛性钠浓度为 141 克/升时,溶液的分解效率和生成的三氢氧化铝(ATH)的平均粒度变化不大。当苛性碱浓度为 160 g/L 和 177 g/L 时,分解效率分别从 35.8% 和 21.6% 提高到 40.6% 和 24.9%,而 ATH 结晶种子的平均粒度分别从 14.2 和 9.25 μm 提高到 17.9 和 15.9 μm。XRD、FT-IR 和 SEM 分析表明,锌可以进入 ATH 晶种,并与α-ATH 晶面相互作用。它还可能与 AlO 八面体生长结构形成相互作用,从而促进溶液分解并影响晶体生长。研究成果将为提高氧化铝产品质量提供有价值的参考。
本文章由计算机程序翻译,如有差异,请以英文原文为准。

Effect of zinc(II) and caustic content on the decomposition of sodium aluminate solutions and relevance to the Bayer process

Effect of zinc(II) and caustic content on the decomposition of sodium aluminate solutions and relevance to the Bayer process

The impact of zinc (Zn) on the seed decomposition process of sodium aluminate solution at different caustic concentrations was investigated. The results showed that as the concentration of Zn(II) in sodium aluminate solution increased from 0 to 1000 mg/L, the decomposition efficiency of the solution and average grain size of the resulting aluminum tri-hydroxide (ATH) changed little at a caustic concentration of 141 g/L. At caustic concentrations of 160 g/L and 177 g/L, the decomposition efficiency increased from 35.8% and 21.6% to 40.6% and 24.9%, respectively, while average grain size of the ATH crystal seeds increased from 14.2 and 9.25 μm to 17.9 and 15.9 μm, respectively. The XRD, FT-IR, and SEM analyses showed that zinc can enter the ATH seeds and interact with the α-ATH crystal planes. It may also form interactions with the AlO octahedral growth structure, thus promoting solution decomposition and influencing crystal growth. The research results will provide valuable references for improving the quality of alumina products.

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来源期刊
Hydrometallurgy
Hydrometallurgy 工程技术-冶金工程
CiteScore
9.50
自引率
6.40%
发文量
144
审稿时长
3.4 months
期刊介绍: Hydrometallurgy aims to compile studies on novel processes, process design, chemistry, modelling, control, economics and interfaces between unit operations, and to provide a forum for discussions on case histories and operational difficulties. Topics covered include: leaching of metal values by chemical reagents or bacterial action at ambient or elevated pressures and temperatures; separation of solids from leach liquors; removal of impurities and recovery of metal values by precipitation, ion exchange, solvent extraction, gaseous reduction, cementation, electro-winning and electro-refining; pre-treatment of ores by roasting or chemical treatments such as halogenation or reduction; recycling of reagents and treatment of effluents.
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