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Demonstration Plant Equipment Design and Scale-Up from Pilot Plant of a Leaching and Solvent Extraction Process

机译:淋洗和溶剂萃取过程中试工厂的示范工厂设备设计和放大

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摘要

Germanium recovery from coal fly ash by hydrometallurgical procedures wasstudied at the pilot scale (5 kg of fly ash/h). Results were used to design the equipment of ademonstration-sized plant (200 kg of fly ash/h). The process is based on hydrometallurgicaloperations: firstly a germanium extraction from fly ash by leaching and a consequent Geseparation from the other elements present in the solution by solvent extraction procedures.Based on the experimental results, mass balances and McCabe-Thiele diagrams were appliedto determine the number of steps of the solvent extraction stage. Different arrangements havebeen studied and a countercurrent process with three steps in extraction and six steps inelution was defined. A residence time of 5 min was fixed in both the extraction and elutionstages. Volumetric ratios in extraction and stripping were: aqueous phase/organic phase = 5and organic phase/stripping phase = 5, so a concentration factor of 25 is achieved. Mixersand decanters were completely defined. The maximum extracted and eluted germanium wasestimated and a global efficiency of 94% was achieved. The cost-effectiveness of theequipment was estimated using the Lang factors.
机译:通过湿法冶金法从煤粉煤灰中回收锗的试验规模为(5千克粉煤灰/ h)。结果用于设计示范工厂的设备(粉煤灰200千克/小时)。该工艺基于湿法冶金操作:首先通过浸出从飞灰中萃取锗,然后通过溶剂萃取程序从溶液中存在的其他元素中分离出锗,然后根据实验结果,利用质量平衡和McCabe-Thiele图确定溶剂萃取阶段的步骤数。已经研究了不同的布置,并定义了一个逆流过程,该过程分三步萃取,六步洗脱。在萃取和洗脱阶段中,固定的停留时间均为5分钟。萃取和汽提中的体积比为:水相/有机相= 5,有机相/汽提相= 5,因此浓缩倍数达到25。混合器和析器已完全定义。估计了最大的萃取和洗脱锗,全球效率达到94%。使用Lang因素估算设备的成本效益。

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