A kind of preparation method of high flux antifouling inorganic membrane
An inorganic membrane and high-flux technology, applied in chemical instruments and methods, membrane technology, semi-permeable membrane separation, etc., can solve the problems of limited improvement in permeation flux and anti-pollution ability, and unsatisfactory dispersion
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[0030] According to another embodiment of the present invention, the preparation method of the inorganic membrane with nano-rough surface and pore wall is provided, comprising:
[0031] A) Immerse the inorganic membrane in the modification solution, which is a solution that can generate metal or silicon oxide through hydrolysis-polycondensation reaction, and take out the membrane after a predetermined time of reaction;
[0032] B) cleaning the membrane with a solvent;
[0033] C) drying the washed membrane;
[0034] D) The dried membrane is heat-treated to obtain a high-flux membrane.
[0035] According to one embodiment of the present invention, the above-mentioned modifying liquid is Si(OR) 4 Solution, R is alkyl, solute is SiO 2 Calculation based on the mass ratio of the solution, SiO 2 The concentration is 0.01-5%.
[0036] According to an embodiment of the present invention, the modification step A) above is carried out at a temperature ranging from room temperature ...
Embodiment 1
[0043] Prepare the modified solution according to the volume ratio of tetraethyl orthosilicate: water: ethanol: ammonia = 10:270:40:5. The raw material membrane is an asymmetric fly ash base with an average pore diameter of 0.77 μm, an outer diameter of 10 mm, and an inner diameter of 5.5 mm. Ceramic microfiltration membrane, under the pressure difference across the mold of 01.MPa, the pure water flux of the raw material membrane is 1.33m 3 / m 2 h. Immerse the raw material film in the modification solution, heat the modification solution to 70°C, reflux for 4 hours, take out the film, clean the film with absolute ethanol, dry the cleaned film and put it in a heating furnace at 1°C / Raise the temperature to 500°C at a heating rate of 1 minute, keep the temperature at 500°C for 1 hour, and cool down to room temperature naturally to obtain a ceramic membrane with nano-silica surface and pore walls.
[0044] The flux and antifouling ability of the modified ceramic membrane
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Embodiment 2
[0047]Prepare the modified solution according to the volume ratio of tetraethyl orthosilicate: water: ethanol: ammonia water = 1:20:9:5. The raw material membrane is a homogeneous fly ash membrane with an average pore size of 0.3 microns, and the pure water flux of the membrane is 381.1L / m 2 h. Immerse the raw material film in the modification solution, heat the modification solution to 70°C, reflux for 4 hours, take out the film, clean the film with absolute ethanol at 60°C, dry the cleaned film and put it in a heating furnace. Raise the temperature to 500°C at a heating rate of 1°C / min, keep at 500°C for 1 hour, and cool down to room temperature naturally. Under the pressure difference across the mold of 0.1MPa, the measured pure water flux of the modified membrane is 391.32L / m 2 h, increased by 2.68% compared with before modification.
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