Composite nanofiltration flat sheet membrane
A flat membrane and nanofiltration technology, applied in the field of membrane separation, can solve the problems of weak hydrophilicity and low water flux, and achieve the effects of easy production and control, increased water flux, and increased retention rate
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Embodiment 1
[0013] Example 1: Use polysulfone material as the support membrane, put it into 0.1% sodium polystyrene sulfonate aqueous solution for about 30 seconds, squeeze with a rubber roller to remove excess solution, and put it in an oven at 45° C. for 5 minutes. Soak the treated support membrane in 1% piperazine solution, squeeze the excess solution with a rubber roller again, and then contact the support membrane with 0.1% tribenzoyl chloride organic solvent for 10 seconds, and then place it in a 65°C oven Keep in the middle for 10 minutes, and finally obtain the nanofiltration flat membrane with sodium polystyrene sulfonate coating. The rejection rate and flux of the membrane were tested with 2000ppm magnesium sulfate aqueous solution, and the test results under the test condition of pressure 0.8MPa were: the rejection rate was 99.44%, and the water flux was 44.23LMH.
Embodiment 2
[0014] Example 2: Use polyethersulfone material as a support membrane, put it into 0.75% sodium polystyrene sulfonate aqueous solution for about 30 seconds, squeeze with a rubber roller to remove excess solution, and put it in an oven at 50°C for 5 minutes . Soak the treated support membrane in 1.5% piperazine solution, squeeze the excess solution with a rubber roller again, then contact the support membrane with 0.2% trimetribenzoyl chloride organic solvent for 30 seconds, and then place it in a 65°C oven Keep in the middle for 15 minutes, and finally obtain the nanofiltration flat membrane with sodium polystyrene sulfonate coating. The rejection rate and flux of the membrane were tested with 2000ppm magnesium sulfate aqueous solution, and the test results under the test condition of pressure 0.8MPa were: the rejection rate was 98.36%, and the water flux was 68.21LMH.
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