Process for co-producing lithium carbonate and potassium salt with lithium-containing nanofiltration water
A kind of technology for preparing lithium carbonate and water
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Embodiment 1
[0032] The brine raw materials of this embodiment are a magnesium sulfate sub -salt lake brine in a certain in Tibet in my country.
[0033] The example of this embodiment includes the following steps:
[0034] (1) Drive the pressure of magnesium sulfate sub -salt lakes under the pressure of the high -pressure pump, separate the filtering membrane to obtain lithium -containing nanofiltral water;
[0035] The nanofilin is a polymer organic rolling film with magnesium sulfate of 90WT%.
[0036] Among them, the mineralization of magnesium sulfate sub -salt lake brine is 105g / L, so 4 2- / Mg 2+ The quality ratio is 4.6;
[0037] The pressure of the high -voltage pump is 3MPa;
[0038] (2) Step (1) The natal filtration of lithium -containing sodium chloride salt fields, evaporate crystals, and get finished brine. The NACL content in the finished brine is 25WT%;
[0039] (3) Step (2) The gains obtained by the finished product through D201 strong alkaline anion exchange resin to absorb b...
Embodiment 2
[0045] This embodiment uses brine for a magnesium sulfate sub -salt lake brine in a certain in Qinghai in my country.
[0046] The example of this embodiment includes the following steps:
[0047] (1) Drive the pressure of magnesium sulfate sub -salt lakes under the pressure of the high -pressure pump, and is separated by the natal filter membrane to obtain the lithium -containing nan filtrate water.
[0048] Magnote sulfate sulfate sub -salt lake brine mineralization is 125g / L, so 4 2- / Mg 2+ The quality ratio is 2.4; the pressure of the high -voltage pump is 4.5MPa.
[0049] The nanofilin is a high -molecular organic roll film with a magnesium sulfate of 95WT%. The membrane flux is 28lmh, and the water production water rate (the quality ratio of water production and raw water) is 66%.
[0050] (2) Step (1) The natal filtration of lithium -containing sodium chloride salt fields, evaporate the crystals, and get the finished brine. The NACL content in the finished brine is 21WT%; ...
Embodiment 3
[0057] This embodiment uses brine for a magnesium sulfate sub -salt lake brine in Xinjiang.
[0058] The example of this embodiment includes the following steps:
[0059] (1) Drive the pressure of magnesium sulfate sub -salt lakes under the pressure of the high -pressure pump, and is separated by the natal filter membrane to obtain the lithium -containing nan filtrate water.
[0060] Among them, the mineralization of magnesium sulfate sub -salt lake salt -type salt lake 135g / L, so 4 2- / Mg 2+ Quality ratio 3.7;
[0061] The pressure of the high -voltage pump is 4MPa;
[0062] The nanofilin is a high -molecular organic rolling membrane with magnesium sulfate with 95WT%, 22lmhh, and the water production rate (the quality ratio of water production and raw water) is 75%;
[0063] (2) Step (1) The natal filtration of the lithium containing lithium is introduced into sodium chloride salt fields, evaporated and crystals, and obtained the finished brine. The NACL content in the finished ...
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