Method for preparing chemically perforated polyvinylidene fluoride hollow fiber ultrafiltration membrane
A polyvinylidene fluoride and ultrafiltration membrane technology, applied in chemical instruments and methods, membrane technology, semi-permeable membrane separation, etc., can solve the problem of low pore size and pore density, insufficient mechanical strength of the membrane, and inability to fully meet production needs, etc. problems, achieve high rejection rate, improve membrane flux and rejection rate
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Embodiment 1
[0035] The preparation steps are as follows (see figure 1 shown):
[0036] 1) Preparation of film casting solution: Add polyvinylidene fluoride, chemical porogen, solvent and additives into the stirring tank 1 according to the following ratio, stir and blend at a constant temperature, and then pour it into the defoaming tank 2 Static defoaming at constant temperature to obtain a homogeneous casting solution;
[0037] (2) Spinning hollow fiber membranes: at the spinning speed set by the dry-wet spinning equipment, the core liquid in the core liquid tank 3 is injected into the spinneret according to the set core liquid volume and the homogeneous casting liquid 4. Extrude the homogeneous casting liquid and the core liquid from the spinneret 4 to obtain polyvinylidene fluoride hollow fiber membranes.
[0038](3) Phase-separation treatment: Step 2) After the polyvinylidene fluoride hollow fiber membrane obtained has a dry distance of 1-30 cm, it enters the first gel bath 5 and th...
Embodiment 2
[0046] The preparation steps are the same as in Example 1, and the specific preparation conditions are as follows:
[0047]
[0048] The inner diameter of the obtained hollow fiber ultrafiltration membrane is about 0.96mm, the outer diameter is about 1.47mm, and the pure water flux under 0.1MPa reaches 684L / (m 2 · h), the rejection rate of BSA is basically maintained above 90%, and the tensile strength is about 3.1MPa.
Embodiment 3
[0050] The preparation steps are the same as in Example 1, and the specific preparation conditions are as follows:
[0051]
[0052] The inner diameter of the obtained hollow fiber ultrafiltration membrane is about 0.78mm, the outer diameter is about 1.34mm, and the pure water flux under 0.1MPa reaches 430L / (m 2 · h), the rejection rate of BSA is basically kept above 95%, and the tensile strength is about 3.5MPa.
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