Recovery of zinc and iron from hot-dip galvanizing spent pickle liquor using solvent extraction

被引:14
|
作者
Hu, Shuxuan [1 ,2 ]
Xu, Caixia [1 ,2 ]
Srinivasakannan, C. [3 ]
Tan, Xuezhi [4 ]
Ni, Shufang [4 ]
Zhang, Jiangpeng [1 ,2 ]
Li, Xiong [1 ,2 ]
Zhang, Heng [1 ,2 ]
Li, Shiwei [1 ,2 ]
机构
[1] Kunming Univ Sci & Technol, Fac Met & Energy Engn, Kunming 650093, Yunnan, Peoples R China
[2] Kunming Univ Sci & Technol, State Key Lab Complex Nonferrous Met Resources Cle, Kunming 650093, Yunnan, Peoples R China
[3] Khalifa Univ, Chem Engn Dept, Abu Dhabi, U Arab Emirates
[4] Zhejiang Huapu Environm Protect Mat Co Ltd, Shaoxing 312072, Zhejiang, Peoples R China
关键词
Cyanex923; Solventextraction; Densityfunctionaltheory(DFT); Mechanismanalysis; N-BUTYL-PHOSPHATE; CHLORIDE SOLUTIONS; PHOSPHORIC-ACID; SEPARATION; SIMULATION; MIXTURES; METALS; COPPER; ION;
D O I
10.1016/j.molliq.2022.119741
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
The disposal of spent pickle liquor from the hot-dip galvanizing process is of serious environmental con-cern that demands development of safe and economical methods. The present work attempts to extract zinc and iron utilizing a mixture of trialkyl-phosphine oxide (Cyanex 923) as the extractant. Isooctanol and sulfonated kerosene was mixed with the extractant to improve the mass transfer as well as to sup-press emulsification. The effect of the extractant concentration, organic phase composition, contact dura-tion, temperature, phase ratio (O/A) were assessed to identify the optimal process conditions. A thorough analysis of the zinc extraction mechanism was carried out utilizing FT-IR, Raman spectroscopy, and ESI-MS analysis. The structures of extractant and extraction complex were simulated using density functional theory (DFT), the overall situation and the local activity index were calculated. The extraction mechanism is proposed based on theoretical simulation and characterization, supported by the experimental results. The extraction process was identified to be exothermic in nature with the extraction efficiency of zinc as high as 95.57% under the optimal conditions. The extraction efficiency of 99.99% for zinc and 1.90% for iron could be achieved in a three-stage countercurrent extraction process. The single stage stripping effi-ciency of zinc was 95.25% with 0.8 mol/L HNO3. The extraction efficiency of zinc was 92.50% after five extraction and stripping cycles. (C) 2022 Elsevier B.V. All rights reserved.
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页数:15
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