P507萃取分离粉煤灰酸浸液中稀土元素钇

郝龙龙 ,  秦身钧 ,  康帅 ,  庞薇 ,  李神勇 ,  吕大炜 ,  郑雪 ,  李萌

科学技术与工程 ›› 2025, Vol. 25 ›› Issue (32) :13761-13770

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科学技术与工程 ›› 2025, Vol. 25 ›› Issue (32) :13761-13770 DOI: 10.12404/j.issn.1671-1815.2500392
矿冶工程

P507萃取分离粉煤灰酸浸液中稀土元素钇

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Extraction and Separation of Rare Earth Element Yttrium from Acid Leaching Solution of Coal Fly Ash with P507

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摘要

为了从粉煤灰浸出液中有效地萃取分离稀土元素Y,结合模拟萃取体系对其进行探讨。以纯La-Y氯化物混合模拟液作为试验对象,使用2-乙基己基磷酸单2-乙基己基酯(P507)作为萃取剂,研究稀土元素模拟液中Y的萃取过程及其最优条件。试验结果表明:杂质离子Al3+和Fe3+与Y3+存在竞争效应,会降低Y的萃取率。从模拟液中萃取Y的最优萃取条件为:常温,萃取剂体积分数3%、相比VO∶VA=1∶1、模拟液pH=1.6、萃取时间25 min、振荡速率150 r/min,在此条件下,Y的萃取率为97.25%;通过研究萃取机理,发现萃合物组成为YCl2 H3A4;萃取动力研究表明,萃取速率与Y3+、P507和HCl浓度的非线性关系符合速率方程。根据以上模拟试验数据,以粉煤灰浓缩浸出液替代模拟液进行萃取试验,结果表明:除去杂质离子Fe3+后,最优条件下稀土元素Y萃取率82.89%,比除杂前提升60%以上,稀土元素整体萃取率为67.73%,较除杂前提升40%以上。此外,除杂可有效增加Y与其他稀土元素的分离系数,有利于粉煤灰浸出液中Y的分离提取。

Abstract

The extraction and separation of rare earth element Y from coal fly ash leachate were systematically investigated using a simulated extraction system. A mixed chloride solution of pure La-Y was employed as the experimental object, with 2-ethylhexyl phosphonic acid mono-2-ethylhexyl ester (P507) serving as the extractant. The extraction process of Y in the simulated rare earth solution and its optimal conditions were studied. Experimental results reveal that impurity ions Al3+ and Fe3+ exhibit competitive effects with Y3+, significantly reducing Y extraction efficiency. The optimal extraction conditions for Y from the simulated solution were determined as follows: room temperature, extraction agent volume fraction 3%, oil to water ratio (VO∶ VA) = 1∶ 1, solution pH of 1.6, extraction time of 25 minutes, and oscillation rate of 150 r/min. Under these conditions, the extraction rate of Y reaches 97.25%. Mechanistic studies identified the extracted complex composition as YCl2H3A4 Kinetic analysis demonstrates that the extraction rate followed a nonlinear relationship with Y3+, P507, and HCl concentrations, consistent with the derived rate equation. Subsequent experiments were conducted using concentrated coal fly ash leachate instead of the simulated solution. Results show that after removing Fe3+ impurities, the extraction rate of Y under optimized conditions increases by over 60% to 82.89%. The overall rare earth extraction efficiency improves by more than 40%, reaching 67.73%. Furthermore, impurity removal effectively enhances the separation coefficients between Y and other rare earth elements, facilitating selective Y extraction from the leachate.

关键词

钇 / P507 / 粉煤灰酸浸液 / 稀土离子模拟液 / 萃取 / 萃取机理

Key words

yttrium / P507 / coal fly ash leaching solution / rare earth ion simulation liquid / extraction / extraction mechanism

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郝龙龙, 秦身钧, 康帅, 庞薇, 李神勇, 吕大炜, 郑雪, 李萌. P507萃取分离粉煤灰酸浸液中稀土元素钇[J]. 科学技术与工程, 2025, 25(32): 13761-13770 DOI:10.12404/j.issn.1671-1815.2500392
HAO Long-long, QIN Shen-jun, KANG Shuai, PANG Wei, LI Shen-yong, LÜ Da-wei, ZHENG Xue, LI Meng. Extraction and Separation of Rare Earth Element Yttrium from Acid Leaching Solution of Coal Fly Ash with P507[J]. Science Technology and Engineering, 2025, 25(32): 13761-13770 DOI:10.12404/j.issn.1671-1815.2500392

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基金资助

国家自然科学基金(42172191)

河北省自然科学基金(D2024402011)

青岛市科技惠民示范专项(24-1-8-cspz-24-nsh)

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