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Lithium Extraction from an Aqueous Medium through In Situ Synthesis of Aluminum Hydroxide: A Comprehensive Study on Adsorption and Desorption Processes, Kinetics, Isotherm Models, and Thermodynamic Parameters

吸附 解吸 动力学 氢氧化锂 水溶液 化学 萃取(化学) 氢氧化物 锂(药物) 原位 铝 吸附等温线 化学工程 色谱法 无机化学 有机化学 离子交换 离子 量子力学 内分泌学 工程类 物理 医学
作者
Payam Akbari Ziarani,Asghar Molaei Dehkordi
出处
期刊:Industrial & Engineering Chemistry Research [American Chemical Society]
卷期号:63 (1): 445-458 被引量:2
标识
DOI:10.1021/acs.iecr.3c03069
摘要

The increasing demand for lithium across various industries emphasizes the importance of lithium extraction methods. Aluminum hydroxide (Al(OH)3) has emerged as a promising option for extracting lithium from brines due to its selectivity, capacity, and straightforward synthesis process. This study introduces a novel Al(OH)3 synthesis method using water decomposition by activated aluminum powders. In this regard, the influences of several key parameters, including the operating temperature, reaction time, Al-to-Li molar ratio in the solution, initial lithium concentration, and presence of coexisting ions (Mg2+, Ca2+, and Na+) in the lithium solution on the efficiency of lithium removal were investigated carefully. Under appropriate conditions (using Al-based materials composed of Al, CaO, and NaCl), with a reaction time of 48 h, a temperature of 40 °C, an Al-to-Li molar ratio of 4:1, and initial lithium and sodium concentrations of 1 and 20 g/L, respectively, the adsorption efficiency reaches an impressive 99.7%. Notably, the presence of sodium enhances the lithium removal efficiency, with an increase in sodium concentration from 1 to 5 g/L resulting in an improvement from 95.2 to 98.7%. Conversely, the impact of calcium on lithium adsorption is minimal, as an increase in its concentration from 1.0 to 20 g/L only slightly decreases the efficiency from 98.95 to 96.57%. In contrast, the presence of magnesium significantly reduces adsorption efficiency to 24.6% at 4 g/L. The study also investigated the desorption rate using three different leaching solutions (HCl, H2SO4, and H3PO4) and found that chloric acid exhibits the highest desorption rate at 0.20 N (59.27%). Results were analyzed using various isotherm and kinetic models, with the most suitable models identified as the Dubinin–Radushkevich isotherm and the pseudo-second-order kinetic model. Thermodynamic analysis revealed that the reaction is exothermic, leading to increased randomness, and the adsorption process is primarily physical in nature.

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