Analyses of foam in Bayer precipitation tanks due to crystal growth modifiers

IF 4.8 2区 材料科学 Q1 METALLURGY & METALLURGICAL ENGINEERING
Lei Xu, Wen-mi Chen, Shang Fan, Yan-jun Zhang
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Abstract

Foam generation in Bayer precipitation tanks is a major issue that affects the energy efficiency of precipitation in these tanks. However, the factors contributing to foam generation remain poorly understood. This work investigated the relationship between different crystal growth modifiers (CGMs) and foam generation during the precipitation process. Results indicate that in pure sodium aluminate solution, the addition of CGMs directly affects the foam volume. Furthermore, the foam generation potential (FGP) of CGMs varies significantly. CGM-A and CGM-B exhibited minimal FGPs at concentrations up to 300 mg/L in sodium aluminate solution containing aluminum tri-hydroxide (ATH) solids, resulting in practically no foam. In contrast, CGM-C presented stronger FGP at 100 mg/L, generating 8 mL of foam. The FGP of CGMs increased following high-temperature treatment at 260 °C. The FT-IR, GC–MS, and 1H NMR analyses indicated that the large amounts of unsaturated fatty acids in CGM-C were a major cause of foaming. After high-temperature treatment, numerous alkane molecules were generated in the CGM-C, which served as foam stabilizers. This study provides valuable reference for further improvement of the alumina production capacity.
晶体生长调节剂对拜耳沉淀池中泡沫的影响分析
拜耳沉淀池中泡沫的产生是影响沉淀池能源效率的主要问题。然而,导致泡沫产生的因素仍然知之甚少。本文研究了不同晶体生长调节剂(cgm)与沉淀过程中泡沫生成的关系。结果表明,在纯铝酸钠溶液中,cgm的加入直接影响泡沫体积。此外,cgm的泡沫生成电位(FGP)也有显著差异。在含有三氢氧化铝(ATH)固体的铝酸钠溶液中,CGM-A和CGM-B在高达300 mg/L的浓度下表现出最小的fgp,几乎不会产生泡沫。相比之下,CGM-C在100 mg/L时表现出更强的FGP,产生8 mL泡沫。经过260℃高温处理后,cgm的FGP增加。FT-IR、GC-MS和1H NMR分析表明,CGM-C中大量的不饱和脂肪酸是导致发泡的主要原因。经过高温处理后,CGM-C中生成了大量的烷烃分子,起到泡沫稳定剂的作用。该研究为进一步提高氧化铝生产能力提供了有价值的参考。
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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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