Method for removing mono-valent negative ion inorganic salt by using nano-filtration constant solvent of forward osmosis technology
An anion, inorganic salt technology, applied in the field of chemical treatment, to achieve the effect of good concentration, less fixed investment and convenient operation
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Embodiment 1
[0018] The feed liquid to be treated is a mixed solution of sodium sulfate and sodium chloride, wherein the mass fraction of sodium sulfate is 14%, and the mass fraction of sodium chloride is 5%. Take part of the feed liquid, control the pressure 3.5MPa, and enter the nanofiltration membrane device at a temperature of 25°C for separation to obtain the nanofiltration concentrate and nanofiltration salt-containing leachate, and then put the above-mentioned nanofiltration concentrate and nanofiltration salt-containing leachate into To the forward osmosis membrane device, wherein the nanofiltration concentrated liquid is used as the driving liquid of the forward osmosis membrane device to carry out forward osmosis concentration on the nanofiltration saline leachate; the processed feed liquid can be divided into concentrated feed liquid and highly concentrated saline liquid; The mass fraction of sodium chloride in the concentrated feed liquid is 1%, and the mass fraction of sodium c...
Embodiment 2
[0020] The feed liquid to be treated is a mixed solution of sodium sulfate and sodium chloride, wherein the mass fraction of sodium sulfate is 8%, and the mass fraction of sodium chloride is 15%. Take part of the feed liquid, first dilute it with water until the mass fraction of sodium chloride is 10%, control the pressure 3.0MPa, and enter the nanofiltration membrane device at a temperature of 25°C for separation to obtain nanofiltration concentrated liquid and nanofiltration salt-containing permeate. Filtrate, and then the above-mentioned nanofiltration concentrated solution and nanofiltration salt-containing leachate enter the forward osmosis membrane device, wherein the nanofiltration concentrate is used as the driving solution of the forward osmosis membrane device to carry out forward osmosis concentration on the nanofiltration salt-containing leachate; The processed feed liquid is divided into concentrated feed liquid and highly concentrated saline liquid, and the highly...
Embodiment 3
[0022] The concentrated feed liquid obtained after the treatment of Example 2 is processed again, that is, it enters the treatment of the nanofiltration membrane device and the forward osmosis membrane device, and the pressure is controlled at 3.0 MPa and the temperature is 25 ° C; finally, the concentration of sodium chloride in the concentrated feed liquid can be obtained. The mass fraction is 0.5%.
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