A method for preparing water glass co-production metal salt crystallization with silicon-rich clay
A technology of metal salt and water glass, applied in the fields of mineral utilization and metallurgy, can solve the problems of high energy consumption, high cost of water glass and high cost of raw quartz sand, and achieve the effects of low energy consumption, low cost and simple process.
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Embodiment 1
[0043] SiO in the silicon-rich clay used in this embodiment 2 The content is 42.85%, Fe 2 o 3 The content is 5.38%, Al 2 o 3 The content is 36.03%.
[0044] The method for preparing water glass co-production metal salt crystallization with silicon-rich clay, the specific steps are as follows:
[0045] S1. Crushing and grinding the silicon-rich clay to 100 mesh to obtain a powdery sample of the silicon-rich clay;
[0046] S2. According to the liquid-solid ratio of 10, place the lithium-rich clay ore powder sample obtained in step 1 in a sulfuric acid solution with a concentration of 4 mol / L, stir and dissolve for 6 hours at a temperature of 80°C, and filter and separate to obtain acid leaching Liquor and acid leaching residue;
[0047] S3, after mixing the acid leaching residue obtained in S2 with the sodium hydroxide solution with a mass concentration of 10% according to a mass ratio of 1:14, stir for 3 hours at a temperature of 60° C., filter to obtain water glass (sodi...
Embodiment 2
[0052] SiO in the silicon-rich clay of this embodiment 2 The content is 42.85%, Fe 2 o 3 The content is 5.38%, Al 2 o 3 The content is 36.03%. Specific steps are as follows:
[0053] The method for preparing water glass co-production metal salt crystallization with silicon-rich clay, the specific steps are as follows:
[0054] S1. Crushing and grinding the silicon-rich clay to 400 mesh to obtain a powdery sample of the silicon-rich clay;
[0055] S2. According to the liquid-solid ratio of 5, place the lithium-rich clay ore powder sample obtained in step 1 in a sulfuric acid solution with a concentration of 10 mol / L, stir and dissolve for 0.5 h at a temperature of 180°C, and separate by filtration to obtain acid Leach liquor and pickling residue;
[0056] S3, after mixing the acid leaching residue obtained in S2 with the sodium hydroxide solution with a mass concentration of 40% according to a mass ratio of 1:3.5, stir at a temperature of 100° C. for 0.5 h, and filter to...
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