Production process of lithium chloride
A production process, lithium chloride technology, applied in the field of lithium extraction process, can solve the problems of shortage of lithium chloride, lithium metal and lithium salt resources, unfavorable industrial production and use, and very high requirements for adsorbents, so as to solve the problems of lithium metal and lithium salt The effect of shortage, convenient production process and high purity
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Embodiment 1
[0070] The present embodiment provides a kind of production technology of lithium chloride, comprises the steps:
[0071] Step S1: Concentrating the raw brine by reverse osmosis and electrodialysis in sequence. Among them, the raw brine is obtained after the salt lake brine is treated by the ion exchange adsorption method to extract lithium. The concentration of lithium ions in the raw brine of this embodiment is 0.4g / L, the concentration of magnesium ions is 0.5g / L, and the concentration of sodium ions is 0.4g / L. is 0.3g / L, and the chloride ion concentration is 2.5g / L.
[0072] (a) First, the raw material brine is processed by reverse osmosis to obtain the raw material brine concentrate, the concentration of lithium in the prepared raw material brine concentrate is 4.0g / L, and the prepared light brine is reused for ion exchange of salt lake brine In the process of extracting lithium by adsorption method.
[0073] (b) Next, the raw material brine concentrated solution is pro...
Embodiment 2
[0089] The production process of this embodiment is the same as that of Embodiment 1, except that the components in the raw material brine used are as follows: the concentration of lithium ions is 0.8g / L, the concentration of magnesium ions is 1.5g / L, the concentration of sodium ions is 0.5g / L, and the concentration of chlorine The ion concentration is 4g / L.
[0090] In the first qualified liquid prepared after the first concentration process in step S1, the lithium concentration is 25 g / L. In the second qualified liquid produced after the purification of the first adsorption process in step S2, the concentration of calcium ions is 0.015 mg / L, the concentration of magnesium ions is 0.016 mg / L, the concentration of boron ions is 0.3 mg / L, organic matter The concentration is 3.8mg / L. In the third qualified liquid prepared after the second concentration process in step S3, the concentration of lithium ions is 100 g / L, and the concentration of sodium ions is 3.5 g / L. In the four...
Embodiment 3
[0093] The production process of this embodiment is the same as that of Embodiment 1, except that the components in the raw brine used are: the concentration of lithium ions is 0.5g / L, the concentration of magnesium ions is 1.0g / L, the concentration of sodium ions is 0.4g / L, and the concentration of chlorine The ion concentration is 3g / L.
[0094] In the first qualified liquid prepared after the first concentration process in step S1, the lithium concentration is 20 g / L. In the second qualified liquid produced after the purification of the first adsorption process in step S2, the concentration of calcium ions is 0.010 mg / L, the concentration of magnesium ions is 0.011 mg / L, the concentration of boron ions is 0.4 mg / L, organic matter The concentration is 4.0mg / L. In the third qualified liquid prepared after the second concentration process in step S3, the concentration of lithium ions is 90 g / L, and the concentration of sodium ions is 5 g / L. In the fourth qualified liquid pur...
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