Utilization method of chloride type salt lake brine
A salt lake brine and chloride technology, applied in lithium carbonate;/acid carbonate and other directions, can solve the problems of inability to achieve sustainable production, improve product purity, and high sodium content
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Embodiment 1
[0049] Chloride-type salt lake brine stock solution, the main components are (g / l):
[0050] LiCl – 8.7, NaCl – 177, KCl – 37.4, MgCl 2 – 44.5, CaCl 2 – 3.31, SO 4 2- – 3.1.
[0051] Evaporate and concentrate under sunlight, and precipitate impurity salts NaCl, KCl, CaSO when reaching saturation 4 and MgCl 2 ·6H 2 O, get lithium chloride concentrate after filtering off the precipitate, the composition is (g / l): LiCl – 252, NaCl – 2.2, KCl – 0.5, MgCl 2 – 62.4, CaCl 2 – 1.1, SO 4 2- – 0.3.
[0052] Heat 1000 ml of concentrate to 80°C, add a stoichiometric amount (relative to the amount of magnesium ions and calcium ions) of lithium carbonate and mix for 1 hour to remove most of the magnesium and calcium ions in the concentrate, and filter out the resulting MgCO 3 and CaCO 3 precipitation. The concentration of LiCl in the filtrate rises to 305g / l, and the remaining MgCl 2 and CaCl 2 4.1 g / l and 0.12 g / l, respectively. Add 3.19g Ca(OH) 2 and 4.68g Na 2 CO...
Embodiment 2
[0059] High magnesium lithium ratio chloride type salt lake brine, the main components are (g / l):
[0060] LiCl-2.2, MgCl 2 – 486, NaCl – 2.1, KCl – 2.4, CaCl 2 – 1.3, SO 4 2- – 1.1.
[0061] Put 11 liters into the adsorption-desorption column, the main component is LiCl 2Al(OH) 3 ·nH 2 The granular adsorbent of O acts with 45 liters of brine in the filtered state. After the adsorbent adsorbs lithium chloride to a saturated state, use a lithium chloride aqueous solution with a concentration of 5g / l to flush out the salt solution from the adsorption-desorption column, and then treat and desorb lithium chloride with distilled water to obtain the initial concentration of lithium chloride Liquid 14.8 liters, composition (g / l): LiCl – 6.2, MgCl 2 – 6.8, NaCl 2 4 2- < 0.05.
[0062] Carry out evaporation concentration and removal of impurity ions to the above-mentioned primary concentrated solution with the similar process of Example 1, obtain the lithium chloride con...
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