Method for separating elemental boron from boron-containing brine by nanofiltration
A technology of brine and nanofiltration, which is applied in the direction of borate, lithium halide, boron oxide, etc., can solve the problems that boron ore products cannot meet the needs of domestic economic construction, cannot realize the comprehensive utilization of boron resources, and rely on imports of boron products, etc. Achieve the effect of increasing lithium ion yield, low cost and low cost
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Embodiment 1
[0058] Preferably, a method for separating boron from boron-containing brine by nanofiltration is also provided, wherein in the brine, the content of lithium ions is 22g / L, the content of sodium ions is 15g / L, and the content of chloride ions is 136g / L. The boron content is 1800ppm, the brine pH is 4.0, and the brine temperature is 35°C. The specific boron element separation steps are as follows:
[0059] a) adding sodium hydroxide to the feed brine to adjust the pH to 9.5;
[0060] b) The bittern with adjusted pH is pumped into the first-level nanofiltration system, and pressure is applied on both sides of the nanofiltration membrane to form a pressure difference. The pressure difference on both sides of the membrane is controlled to be 27bar, and the temperature of the controlled brine is 27°C; Retentate boron-rich brine 1 and permeate boron-poor brine 1;
[0061] c) lithium ion content in boron-poor brine 1 is 22g / L, sodium ion content is 15g / L, chloride ion content is 13...
Embodiment 2
[0068] Preferably, a method for separating boron from boron-containing brine by nanofiltration is also provided, wherein in the brine, the content of lithium ions is 18g / L, the content of sodium ions is 12g / L, and the content of chloride ions is 111g / L. The boron content is 3300ppm, the brine pH is 12.7, and the brine temperature is 29°C. The specific boron element separation steps are as follows:
[0069] a) adding hydrochloric acid to the feed brine to adjust the pH to 10.0;
[0070] b) The brine with adjusted pH is pumped into the primary nanofiltration system, and pressure is applied on both sides of the nanofiltration membrane to form a pressure difference. The pressure difference on both sides of the membrane is controlled to be 37 bar, and the temperature of the brine is controlled to be 28.5°C; Retentate boron-rich brine 1 and permeate boron-poor brine 1;
[0071] c) lithium ion content in boron-poor brine 1 is 18g / L, sodium ion content is 12g / L, chloride ion content...
Embodiment 3
[0081] Preferably, a method for separating boron from boron-containing brine by nanofiltration is also provided, wherein in the brine, the content of lithium ions is 8g / L, the content of sodium ions is 5g / L, and the content of chloride ions is 48.9g / L , the boron content is 200ppm, the pH of the brine is 5.6, and the temperature of the brine is 41°C. The specific boron element separation steps are as follows:
[0082] a) adding sodium hydroxide to the feed brine to adjust the pH to 9.5;
[0083] b) The brine with adjusted pH is pumped into the first-stage nanofiltration system, and pressure is applied on both sides of the nanofiltration membrane to form a pressure difference. The pressure difference on both sides of the membrane is controlled to be 18 bar, and the temperature of the brine is controlled to be 17° C.; Retentate boron-rich brine 1 and permeate boron-poor brine 1;
[0084] c) The lithium ion content in boron-poor brine 1 is 8g / L, the sodium ion content is 5g / L, ...
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