Nano-filtration method for separating magnesium and enriching lithium from salt lake brine
A salt lake brine and nanofiltration technology, applied in chemical instruments and methods, semi-permeable membrane separation, lithium compounds, etc., can solve the problems of large turnover of materials, large amount of evaporated water, complicated operations, etc., and achieve simple and reasonable process flow, raw materials The effect of abundant resource reserves and reliable operation
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Embodiment 1
[0035] This example illustrates the separation effect of a primary nanofilter.
[0036] Separation of salt lake brine with CML-DC nanofiltration membrane, the effective membrane area of the membrane is 1.77m 2 . The nanofilter is composed of membrane modules, security filters, raw water pumps, high-pressure pumps, raw water tanks and product water tanks. Put the raw brine containing lithium 0.369g / L, magnesium 7.0g / L, boron 0.392g / L and sulfate 1.508g / L, pH=5.5 into the raw water tank, at 18-30°C and a pressure difference of 850kPa Next, the raw brine is separated. The separation operation is an intermittent cycle operation, that is, the concentrated liquid at the outlet returns to the raw liquid tank for circulation. Sampling analysis after 4.5 hours, each feed liquid composition is as shown in table 1:
[0037] Table 1.
[0038] Liquid flow g / L Li g / L Mg g / L B g / L SO 4 2-
[0039] Raw brine 0.369 7.0 0.392 1.508
[...
Embodiment 2
[0050] This example illustrates the effect of operating temperature on the separation and permeation performance of nanofiltration. Same as embodiment one. The raw brine was separated and enriched at 25-40°C, and after 4.5 hours, each sample was sampled and analyzed. The results are shown in Table 2:
[0051] Table 2
[0052] Liquid flow g / L Li g / L Mg g / L B g / L SO 4 2-
[0053] Raw brine 0.368 6.96 0.392 1.506
[0054] Concentrated water 0.288 9.00 0.505 2.385
[0055] Permeate 0.655 2.99 0.254 0.049
[0056] Separation factor 6.9 4.5 111.8
[0057] When it can be seen that increasing temperature, compared with embodiment one, the separation performance of nanofiltration membrane will be slightly low, but the permeate yield is brought up to 42% by 35%, and the single stage yield of lithium is brought up to by 65% 75%, improving the utilization rate of raw materials.
Embodiment 3
[0059] This example illustrates the separation effect of multi-stage nanofiltration. Same as embodiment one. Send the raw material brine containing 0.202g / L lithium, 20.1g / L magnesium, 0.357g / L boron and 0.943g / L sulfate, pH=6.0 into the stock solution tank. The raw material brine is subjected to three-stage circulation separation under the action of the difference, that is, the lithium-rich product liquid obtained by the first and second nanofilters is used as the raw material brine separated by the second and third nanofilters, and the lithium-poor concentrated solution obtained by the second and third nanofilters is used as the raw material brine. Water is respectively used as the batching mother liquor of the stock solution separated by the primary and secondary nanofilters. The main feed liquid composition and separation factor obtained from the separation are shown in Table 3:
[0060] table 3
[0061] Liquid flow g / L Li ...
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