1. Selective extraction of lithium ions from salt lake brines using a tributyl phosphate-sodium tetraphenyl boron-phenethyl isobutyrate system.
- Author
-
Li, Rujie, Wang, Yangyang, Duan, Wenjing, Du, Chencan, Tian, Shichao, Ren, Zhongqi, and Zhou, Zhiyong
- Subjects
- *
LITHIUM ions , *SALT lakes , *MAGNESIUM ions , *TRIBUTYL phosphate , *SALT , *SODIUM channels - Abstract
Lithium is a vital aspect of the strategic development of the alternative energy and nuclear industries, and the demand for this metal is currently increasing rapidly. China possesses significant lithium resources, nearly 80 % of which are situated in salt lake brine. Solvent extraction is a viable means of extracting lithium ions from brine that has high magnesium-to-lithium ratio, and provides high selectivity along with ready scale-up to industrial production levels. The most common extraction technology for such scenarios is the tributyl phosphate (TBP)-FeCl 3 -kerosene system. However, this system tends to lose Fe3+ during the extraction process and the concurrent use of acid and alkali can seriously affect the stability of the organic phase. The present work demonstrates a new extraction process employing TBP as the main extractant, sodium tetraphenyl boron as a co-extractant and phenethyl isobutyrate as a diluent. Optimization of the relative amounts of these components along with the phase ratio provided a single-stage lithium ion extraction efficiency of 85.70 % together with a separation factor of lithium to magnesium ions of 1175. The organic phase was washed with a LiCl + NaCl solution to remove impurity ions then stripped five times with a NaHCO 3 solution, with a Li+ stripping efficiency >99 %. During ten replicate extractions, the Li+ extraction efficiency remained stable at approximately 84 %, demonstrating good stability. NMR spectra verified that the binding strength of metal cations to TBP decreased in the order of Li+ > Na+ ≫ Mg2+, indicating selectivity for the extraction of Li+. This single step NaHCO 3 method was adopted to simplify the extraction process. The overall strategy avoids the use of strong acids or bases that otherwise corrode equipment and provides greatly improved long-term stability of the organic phase. • TBP-sodium tetraphenyl boron-phenethyl isobutyrate extraction system was proposed. • A single-stage extraction efficiency of 85.70 % for lithium ion could be obtained. • The maximum separation factor of lithium to magnesium ions reached up to 1175. • NaHCO 3 was used as stripping agent to simplify the extraction process. • The proposed extraction system showed high stability and reusability. [ABSTRACT FROM AUTHOR]
- Published
- 2023
- Full Text
- View/download PDF