共 50 条
Manganese-Titanium Mixed Ion Sieves for the Selective Adsorption of Lithium Ions from an Artificial Salt Lake Brine
被引:14
|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
来源:
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.
引用
收藏
页数:18
相关论文