Manganese-Titanium Mixed Ion Sieves for the Selective Adsorption of Lithium Ions from an Artificial Salt Lake Brine

被引:17
作者
Ding, Yaxuan [1 ]
Nhung, Nguyen Thi Hong [1 ]
An, Jiahao [1 ]
Chen, Hao [1 ]
Liao, Lianying [1 ]
He, Chunlin [1 ]
Wang, Xinpeng [1 ]
Fujita, Toyohisa [1 ]
机构
[1] Guangxi Univ, Sch Resources Environm & Mat, Nanning 530004, Peoples R China
关键词
lithium-ion sieve; salt lake brine; DL-malic acid; ion exchange; lithium selectivity; EXTRACTION; RECOVERY; OXIDE; SEPARATION; MAGNESIUM; STABILITY; WATER; ACID; LI;
D O I
10.3390/ma16114190
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
Lithium recovery is imperative to accommodate the increase in lithium demand. Salt lake brine contains a large amount of lithium and is one of the most important sources of lithium metal. In this study, Li2CO3, MnO2, and TiO2 particles were mixed, and the precursor of a manganese-titanium mixed ion sieve (M-T-LIS) was prepared by a high-temperature solid-phase method. M-T-LISs were obtained by DL-malic acid pickling. The adsorption experiment results noted single-layer chemical adsorption and maximum lithium adsorption of 32.32 mg/g. From the Brunauer-Emmett-Teller and scanning electron microscopy results, the M-T-LIS provided adsorption sites after DL-malic acid pickling. In addition, X-ray photoelectron spectroscopy and Fourier transform infrared results showed the ion exchange mechanism of the M-T-LIS adsorption. From the results of the Li+ desorption experiment and recoverability experiment, DL-malic acid was used to desorb Li+ from the M-T-LIS with a desorption rate of more than 90%. During the fifth cycle, the Li+ adsorption capacity of the M-T-LIS was more than 20 mg/g (25.90 mg/g), and the recovery efficiency was higher than 80% (81.42%). According to the selectivity experiment, the M-T-LIS had good selectivity for Li+ (adsorption capacity of 25.85 mg/g in the artificial salt lake brine), which indicates its good application potential.
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页数:18
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