Co-Extraction and Stepwise Stripping of Indium and Germanium Using a BGYW–P204 System

To address the co-recovery of indium and germanium from sulfuric-acid systems containing indium and germanium together with their subsequent stepwise stripping, a hydroxamic-acid extractant-di-(2-ethylhexyl)phosphoric acid composite organic phase was investigated for the co-extraction and stepwise stripping of indium and germanium from sulfuric-acid solutions. The effects of extractant composition, aqueous acidity, O/A phase ratio, and extraction time were optimized, and HCl and NH4F were evaluated for stepwise stripping of In and Ge, respectively. Increasing hydroxamic-acid extractant significantly enhanced Ge extraction, while 25 vol% di-(2-ethylhexyl)phosphoric acid provided high extraction efficiencies for both metals. Tri-n-alkylphosphine oxide suppressed Ge extraction and reduced HCl stripping of In; therefore, the organic phase was selected as 15 vol% hydroxamic-acid extractant + 25 vol% di-(2-ethylhexyl)phosphoric acid + 60 vol% diluent. Under the optimized conditions of 15 g/L H2SO4, O/A = 2:1, and 5 min extraction, the extraction efficiencies of Fe, Ge, and In reached 99.9%, 99.7%, and approximately 100%, respectively. Using 3 mol/L HCl, the In stripping efficiency reached 99.8%, whereas Ge was scarcely stripped. Subsequent stripping with 2 mol/L NH4F achieved nearly 100% Ge recovery, although Fe co-stripping was approximately 95%. The hydroxamic-acid extractant-di-(2-ethylhexyl)phosphoric acid system therefore enables efficient co-extraction and stepwise stripping of In and Ge, while suppressing most coexisting impurities.

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Journal
Separations
Published
2026-10-29
DOI
https://doi.org/10.3390/separations13110317
Primary Topic
Extraction and Separation Processes
Type
article
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0.00

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article

Co-Extraction and Stepwise Stripping of Indium and Germanium Using a BGYW–P204 System

Haibei Wang, Zhixing Qin, Zong Guo, Sanping Liu et al.
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Separations
Extraction and Separation Processes
article

Co-Extraction and Stepwise Stripping of Indium and Germanium Using a BGYW–P204 System

Haibei Wang, Zhixing Qin, Zong Guo, Sanping Liu, Zhenyu Wang, Ni Yang, Chaozhen Zheng, Jiajie Han
article en

Abstract

To address the co-recovery of indium and germanium from sulfuric-acid systems containing indium and germanium together with their subsequent stepwise stripping, a hydroxamic-acid extractant-di-(2-ethylhexyl)phosphoric acid composite organic phase was investigated for the co-extraction and stepwise stripping of indium and germanium from sulfuric-acid solutions. The effects of extractant composition, aqueous acidity, O/A phase ratio, and extraction time were optimized, and HCl and NH4F were evaluated for stepwise stripping of In and Ge, respectively. Increasing hydroxamic-acid extractant significantly enhanced Ge extraction, while 25 vol% di-(2-ethylhexyl)phosphoric acid provided high extraction efficiencies for both metals. Tri-n-alkylphosphine oxide suppressed Ge extraction and reduced HCl stripping of In; therefore, the organic phase was selected as 15 vol% hydroxamic-acid extractant + 25 vol% di-(2-ethylhexyl)phosphoric acid + 60 vol% diluent. Under the optimized conditions of 15 g/L H2SO4, O/A = 2:1, and 5 min extraction, the extraction efficiencies of Fe, Ge, and In reached 99.9%, 99.7%, and approximately 100%, respectively. Using 3 mol/L HCl, the In stripping efficiency reached 99.8%, whereas Ge was scarcely stripped. Subsequent stripping with 2 mol/L NH4F achieved nearly 100% Ge recovery, although Fe co-stripping was approximately 95%. The hydroxamic-acid extractant-di-(2-ethylhexyl)phosphoric acid system therefore enables efficient co-extraction and stepwise stripping of In and Ge, while suppressing most coexisting impurities.

SeparationsVol. 13(11)
Beijing General Research Institute of Mining and Metallurgy (CN)
National Key Research and Development Program of China
Responsible consumption and production
Openalex Percentile: Top 23%
Extraction and Separation Processes
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