Lithium extraction from high-Mg brines using N523/esters systems

Amide extractants for lithium extraction from high‑magnesium brines have demonstrated satisfactory stability and extraction efficacy. However, the presence of interfacial substance when N , N -bis(2-ethylhexyl)-acetamide (N523) is employed in isolation presents a challenge to the process operation. In this study, inexpensive modifier esters (dioctyl phthalate , DOP and acetyl tributyl citrate , ATBC) were introduced into the N523 extraction system, resolving the issue of no cascade effect with N523 alone. The effects of a range of variables on the extraction and phase separation processes were evaluated comparatively for two petroleum-based and green commercial esters. The factors included organic phase composition (including the volume ratio of extractant N523 to ester and concentration in the organic phase), coexisting ions in aqueous solution (including H + , Li + and Cl − concentrations and Fe/Li molar ratios), and phase ratio. The complexation mechanism was characterized using the slope method and FT-IR spectrum. The results of the study demonstrated that the concentration of the total cation (Li + +2Mg 2+ +H + ) in the organic phase exhibited a more consistent and similar trend to that of FeCl 4 − . It was found that the anticipated Li + extraction efficiency could be attained by ensuring the N523/Li molar ratio was no <11.5. Due to the fact that N523 complexes with metal ions , DOP and ATBC exhibited comparable performance and played the same role in promoting phase separation. The three-countercurrent extraction method achieved a Li + extraction efficiency of 99.3 % and a Li/Mg separation factor of 2.8×105, with an enhanced phase-separation effect. The economical DOP and ATBC optimized the N523 system and improved the stable operation of the extraction system while reducing the cost. This provided new ideas and perspectives for its industrial application. • Development of ester to N523 system for recovery of Li from high Mg brines with enhancement of interfacial micro-interaction. • Better cascade extraction effect accompanied by E Li of 99% and β Li/Mg of 2.8×10 5 are achieved. • The complex in MFeCl 4 form was confirmed by equimolar anion/cation calculations in the organic phase.

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Publication Details

Journal
Journal of Water Process Engineering
Published
2024-11-19
DOI
https://doi.org/10.1016/j.jwpe.2024.106513
Citations
2
Primary Topic
Extraction and Separation Processes
Type
article
Field-Weighted Citation Impact
0.43

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article

Lithium extraction from high-Mg brines using N523/esters systems

Yong Niu, Dong Shi, Hailong Lu, Yuze Zhang et al.
2 citations
Journal of Water Process Engineering
Extraction and Separation Processes
0.43
article

Lithium extraction from high-Mg brines using N523/esters systems

Yong Niu, Dong Shi, Hailong Lu, Yuze Zhang, Xiaowu Peng, Nan Liang Chen, Lijuan Li, Jinfeng Li, Lianmin Ji, Sainan Yang, Shaolei Xie
article en
2 citations

Abstract

Amide extractants for lithium extraction from high‑magnesium brines have demonstrated satisfactory stability and extraction efficacy. However, the presence of interfacial substance when N , N -bis(2-ethylhexyl)-acetamide (N523) is employed in isolation presents a challenge to the process operation. In this study, inexpensive modifier esters (dioctyl phthalate , DOP and acetyl tributyl citrate , ATBC) were introduced into the N523 extraction system, resolving the issue of no cascade effect with N523 alone. The effects of a range of variables on the extraction and phase separation processes were evaluated comparatively for two petroleum-based and green commercial esters. The factors included organic phase composition (including the volume ratio of extractant N523 to ester and concentration in the organic phase), coexisting ions in aqueous solution (including H + , Li + and Cl − concentrations and Fe/Li molar ratios), and phase ratio. The complexation mechanism was characterized using the slope method and FT-IR spectrum. The results of the study demonstrated that the concentration of the total cation (Li + +2Mg 2+ +H + ) in the organic phase exhibited a more consistent and similar trend to that of FeCl 4 − . It was found that the anticipated Li + extraction efficiency could be attained by ensuring the N523/Li molar ratio was no <11.5. Due to the fact that N523 complexes with metal ions , DOP and ATBC exhibited comparable performance and played the same role in promoting phase separation. The three-countercurrent extraction method achieved a Li + extraction efficiency of 99.3 % and a Li/Mg separation factor of 2.8×105, with an enhanced phase-separation effect. The economical DOP and ATBC optimized the N523 system and improved the stable operation of the extraction system while reducing the cost. This provided new ideas and perspectives for its industrial application. • Development of ester to N523 system for recovery of Li from high Mg brines with enhancement of interfacial micro-interaction. • Better cascade extraction effect accompanied by E Li of 99% and β Li/Mg of 2.8×10 5 are achieved. • The complex in MFeCl 4 form was confirmed by equimolar anion/cation calculations in the organic phase.

Journal of Water Process EngineeringVol. 68
Qinghai University (CN), Chinese Academy of Sciences (CN), Shanghai Institute of Organic Chemistry (CN)
National Natural Science Foundation of China, Youth Innovation Promotion Association of the Chinese Academy of Sciences, Qinghai Provincial Department of Science and Technology
Openalex Percentile: Top 41%
Extraction and Separation Processes
0.43
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