Hollow fiber composite membrane applicator, method for producing said hollow fiber composite membrane and product
A fiber compounding and manufacturing method technology, applied in chemical instruments and methods, membrane technology, semi-permeable membrane separation, etc., can solve the problem of difficult coating on the outside of hollow fiber base membrane, difficulty in accurately controlling the liquid content on the membrane surface, and the quality of the membrane. Difficult to guarantee and other problems, to achieve the effect of simple structure, low cost, uniform coating
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Embodiment 1
[0027] An embodiment of the inventive coating machine is designed as follows: the diameter of the feeding roller 1 and the receiving roller 11 are both 450mm, the height of the drying tube 4 is 1.5M, the height of the drying tube 8 is 1.5M, the length of the stainless steel reaction tube 5 is 1.5M, and the coil The ascent angle is 6 degrees. A contact counter is used to record the number of unwinding and winding layers. The variable frequency motors 12 and 12’ use YST12A, the inverter uses INVERTER’s CVF-72, and the PLC controller 13 uses Siemens’ ST-200CN.
Embodiment 2
[0029] Another embodiment of the inventive coating machine is designed as follows: the diameters of the feeding roller 1 and the receiving roller 11 are both 1000mm, the height of the drying tube 4 is 1M, the height of the drying tube 8 is 2M, the length of the stainless steel reaction tube 5 is 2.5M, and the winding The rise angle is 6 degrees. A contact counter is used to record the number of unwinding and winding layers. The variable frequency motors 12 and 12’ use YST12A, the inverter uses INVERTER’s CVF-72, and the PLC controller 13 uses Siemens’ ST-200CN.
Embodiment 3
[0031] Using the device of Example 1, the water phase concentration is 2% (weight ratio) piperazine aqueous solution, the water phase immersion time is 40 minutes; the concentration of TMC's n-hexane solution is 0.5%, and the polysulfone hollow fiber base membrane stays in the reaction tube The time is 30 seconds (the operating linear speed of the device in Example 1 is 3 m / min), and a uniformly coated nanofiltration hollow fiber composite membrane can be prepared. The air temperature of the front drying tube 4 is 65℃, and the air volume is 1m 3 / min; the air temperature of the post-drying pipe 8 is 75℃, and the air volume is 0.6m 3 / min.
[0032] Experiments show that the obtained hollow fiber nanofiltration composite membrane is effective against 2g / L MgSO under 0.4MPa. 4 The rejection rate can reach 96.8%, and the flux can reach 20.0L / m 2 h.
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