从粉煤灰渗滤液中回收稀土工艺方案的研究

Anand Rao K , Ram Karan , Madhu Babu J , Rama Devi G , Sreenivas T
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引用次数: 3

摘要

本文阐述了从含稀土2160 ppm的印度煤粉煤灰硫酸渗滤液中分离稀土的两级溶剂萃取方案的发展。渗滤液REE浓度低(305mg /L),杂质含量高(32.6 g/L)。由于渗滤液中存在硅而形成凝胶的问题通过明胶打击来防止,明胶打击降低了溶解硅的含量。采用优化浓度为12% (v/v)和40% (v/v)的D2EHPA溶剂,皂化至40%,在溶剂萃取的第一步和第二步可回收约94%的重稀土和86%的轻稀土(LREE)。采用6 mol/L HCl溶液,在低A/O比条件下,对富集重稀土和低重稀土的两种有机流进行多级交叉汽提,得到富集重稀土和低重稀土的条带溶液。用氢氧化钠中和两种条带液,用二水合草酸沉淀稀土,得到混合稀土精矿,测定了13%的HREE和17.5%的LREE。本研究是首次尝试从印度粉煤灰样品中获得的具有复杂化学性质的实际渗滤液中回收稀土元素。此外,该流程被扩大到实验规模,其中包括易于扩展的过程,如在室温(25°C)和高固体浓度(20% w/v)下浸出,然后是溶剂萃取和沉淀阶段。本研究确定了从印度粉煤灰中回收工业规模稀土元素的高潜力。根据目前的研究,可以从混合稀土草酸盐中分离出单个稀土氧化物,这为未来的研究提供了空间。
本文章由计算机程序翻译,如有差异,请以英文原文为准。

Development of process scheme for recovery of rare earths from leachate of coal flyash

Development of process scheme for recovery of rare earths from leachate of coal flyash

The present paper expounds development of a two stage solvent extraction scheme for separation of rare earths (REE) from a sulfuric acid leachate obtained from an Indian coal flyash sample containing 2160 ppm REE. The leachate has low concentration of REE (305 mg/L) and high content of impurities (32.6 g/L). The problem of gel formation due to presence of Si in the leachate was prevented by gelatin strike which lowered dissolved Si content. About 94% of HREE and 86% of Light Rare Earths (LREE) values could be recovered in first and second stages of solvent extraction stages using D2EHPA solvent of optimized concentrations 12% (v/v) and 40% (v/v) saponified up to 40%, respectively. The two organic streams, former rich in HREE and the later rich in LREE, were subjected to multi stage cross current stripping at low A/O ratio using 6 mol/L HCl solution to obtain strip solutions concentrated in HREE and LREE respectively. The two strip liquors were neutralized with NaOH from which REE were precipitated using oxalic acid dihydrate to produce mixed REE concentrates, assaying 13% HREE and 17.5% LREE. The present study was a maiden attempt to recover REE from the actual leachate, of complex chemistry, obtained from an India flyash sample. Further, the flowsheet was up scaled to bench scale which includes easily scalable processes like leaching at ambient temperature (25 °C) and high solids concentration (20% w/v) followed by solvent extraction and precipitation stages. This study establishes a high potential for the recovery of REE from an Indian coal flyash at industrial scale. Scope exists for future studies on separation of individual rare earths oxides from the mixed REE oxalates that can be produced according to the present study.

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