TY - JOUR
T1 - Solvent extraction and separation of zinc-iron from spent pickling solution with tri-n-octylamine
AU - Xu, Caixia
AU - Zhou, Junwen
AU - Yin, Shaohua
AU - Wang, Yongmi
AU - Zhang, Liangjing
AU - Hu, Shuxuan
AU - Li, Xiong
AU - Li, Shiwei
N1 - Publisher Copyright:
© 2021 Elsevier B.V.
PY - 2022/1/1
Y1 - 2022/1/1
N2 - Studies on the effective extraction and separation of zinc-iron from spent pickling solution using tri-n-octylamine (TOA) with solvent extraction were investigated. Single extraction efficiency of 83.75% is obtained under the optimal conditions (organic phase consisting of 30% (v/v) extractant TOA, 20% (v/v) modifier iso-octanol, and 50% (v/v) diluent sulfonated kerosene, organic phase volume: aqueous phase volume of 2:1, and extraction time 10 min), while only 1.8% iron is co-extracted. McCabe-Thiele diagram is employed to analyze the number of theoretical stages needed for the effective extraction of zinc, and it is found that under five-stage counter-current extraction, almost all the zinc ions are extracted. A stripping efficiency of more than 90% from the loaded organic phase is achieved by 2.0 mol/L NH3·H2O and organic phase volume: aqueous phase volume of 1:2. Furthermore, the extraction mechanism of zinc with TOA accompanied by anion exchange is demonstrated by FT-IR spectra analysis and ESI-MS analysis, and the structure of the extracted complex is confirmed as [R3NHZnCl3].
AB - Studies on the effective extraction and separation of zinc-iron from spent pickling solution using tri-n-octylamine (TOA) with solvent extraction were investigated. Single extraction efficiency of 83.75% is obtained under the optimal conditions (organic phase consisting of 30% (v/v) extractant TOA, 20% (v/v) modifier iso-octanol, and 50% (v/v) diluent sulfonated kerosene, organic phase volume: aqueous phase volume of 2:1, and extraction time 10 min), while only 1.8% iron is co-extracted. McCabe-Thiele diagram is employed to analyze the number of theoretical stages needed for the effective extraction of zinc, and it is found that under five-stage counter-current extraction, almost all the zinc ions are extracted. A stripping efficiency of more than 90% from the loaded organic phase is achieved by 2.0 mol/L NH3·H2O and organic phase volume: aqueous phase volume of 1:2. Furthermore, the extraction mechanism of zinc with TOA accompanied by anion exchange is demonstrated by FT-IR spectra analysis and ESI-MS analysis, and the structure of the extracted complex is confirmed as [R3NHZnCl3].
KW - Separation of zinc-iron
KW - Solvent extraction
KW - Spent pickling solution
KW - Tri-n-octylamine
UR - http://www.scopus.com/inward/record.url?scp=85114042694&partnerID=8YFLogxK
U2 - 10.1016/j.seppur.2021.119579
DO - 10.1016/j.seppur.2021.119579
M3 - Article
AN - SCOPUS:85114042694
SN - 1383-5866
VL - 278
JO - Separation and Purification Technology
JF - Separation and Purification Technology
M1 - 119579
ER -