石灰石碱压浸浸出浆过滤过程中流变学的影响

Md Serajuddin , Anand Rao K , Sulekha Mukhopadhyay
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引用次数: 0

摘要

以铀为燃料的核电站被认为是碳足迹低、环境破坏少的清洁能源。在铀矿石加工过程中,氧化压浸产生的碱性浸出浆的过滤是一个挑战,因为磨矿粒度非常细,而且总溶解溶质(TDS)很高。本研究旨在借助浆料流变学来改善和了解浸出浆的过滤。考察了固体浓度、温度、粒径、助水剂用量对浆料流变特性和过滤性能的影响。浆料流变学采用Herschel-Bulkley模型描述,温度效应采用Arrhenius模型,粒径分布采用roin - rammler PSD模型表示。用流变学参数比较了助脱水剂的用量。结果表明,随着固体浓度的增加(10 ~ 75%,w/w),过滤速率降低,这是由于剪切应力的增加(1400 s−1时,剪切应力为9.93 ~ 757 Pa)。当固含量≤60% (w/w)时,浸出浆表现为剪切变稠,固含量≥70%时表现为剪切变稀。在1300 s−1和441 s−1时,固体填料体积分数分别为0.59和0.54。随着表观粘度(1300 s−1)从0.0195 Pa降低,在高温下观察到过滤速率的增加。在20°C至0.0135 Pa下。s在70°C。在1110 s−1条件下,固体浓度为50%和73% (w/w)时,流体流动活化能分别为5.5和7.1 kJ/mol。当粒径(d90)从66µm变化到42µm时,由于表观粘度从0.0120增加到0.0163 Pa,过滤速率下降。S在1400s−1。以高分子量聚丙烯酰胺为基础的非离子型合成絮凝剂n100与非离子型可生物降解多糖表面活性剂瓜尔胶通过桥接机理形成絮凝体,絮凝效果最佳,因此选用。本工作有助于研究人员更好地理解和改进矿浆的过滤过程。
本文章由计算机程序翻译,如有差异,请以英文原文为准。

Influence of rheology in the filtration of leach slurry generated by alkaline pressure leaching of a limestone ore

Influence of rheology in the filtration of leach slurry generated by alkaline pressure leaching of a limestone ore

The Nuclear Power Plant, which uses uranium as a fuel, is considered as a clean source of energy with low carbon footprint and less environmental damage. In processing the uranium ore, the filtration of alkaline leach slurry generated by oxidative pressure leaching is a challenge due to very fine grind size coupled with high total dissolved solutes (TDS). The present study aimed at improving and understanding the filtration of the leach slurry with the help of slurry rheology. The effect of solid concentration, temperature, particle size, and dosages of dewatering aids on the rheological behavior of the slurry and the filtration performance was investigated. The slurry rheology was delineated by the Herschel–Bulkley model, temperature effects were incorporated using the Arrhenius type model, and particle size distribution (PSD) was represented by the Rosin–Rammler PSD model. The dosages of dewatering aids were compared using rheological parameters. It was found that the filtration rate decreases as solid concentration increases (10 to 75%, w/w) due to an increase in the shear stress (9.93 to 757 Pa at 1400 s−1). The leach slurry showed shear thickening at ≤ 60% solids (w/w) and shear thinning at ≥ 70% solids. The maximum solid packing volume fraction was found to be 0.59 and 0.54 at 1300 and 441 s−1, respectively. Increase in filtration rate was observed at elevated temperatures as the apparent viscosity (at 1300 s−1) decreased from 0.0195 Pa.s at 20 °C to 0.0135 Pa.s at 70 °C. The fluid flow activation energy was determined to be 5.5 and 7.1 kJ/mol at 1110 s−1 for 50 and 73% solid concentration (w/w), respectively. When the particle size (d90) was changed from 66 to 42 µm, a decrease in filtration rate was observed due to an increase in apparent viscosity from 0.0120 to 0.0163 Pa.s at 1400 s−1. The high molecular weight polyacrylamide based non-ionic synthetic flocculant N 100 and non-ionic biodegradable polysaccharide surfactant guar gum formed flocs through the bridging mechanism and gave best flocculation results, and therefore selected. The present work helps the researchers in better understanding and improving the filtration process of ore slurries.

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