Visible-light-catalysis hollow fiber ultra-filtration membrane based on metal-doped nTiO2 and preparing method
A technology of metal doping and ultrafiltration membranes, applied in chemical instruments and methods, physical/chemical process catalysts, organic compounds/hydrides/coordination complex catalysts, etc., can solve the problems of inability to prepare separation membranes, slow degradation rates, No problems like the production of hollow fiber ultrafiltration membranes have been seen, and the effects of good photocatalytic degradation performance and anti-pollution performance, resistance increase coefficient and contact angle reduction, and visible light catalytic activity improvement have been achieved.
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Embodiment 1
[0028] 62.0% (w / w) of dimethylacetamide, 15.0% (w / w) of polyethylene glycol 400, 1.0% (w / w) of Tween-80 and 3.0% (w / w) of Fe-doped nTiO 2 Add them into the dissolution tank in a certain order, stir evenly; then add 19.0% (w / w) polysulfone, stir and dissolve at 85°C for 8 hours until completely dissolved; then, the obtained casting solution is stirred Stand still at the dissolution temperature for 24 hours to remove the remaining air bubbles in the casting solution.
[0029] The flow rate of the casting solution is controlled at 10.0mL / min, the temperature of the casting solution is 35°C, the temperature of the coagulation bath is 23°C, the height of the air space is 5cm, and the coagulation time of the hollow fiber ultrafiltration membrane is 1.0min. Visible light-catalyzed hollow fiber ultrafiltration membranes were prepared by silk technology. The prepared hollow fiber ultrafiltration membrane was soaked in deionized water and rinsed for 24 hours to wash away the additives...
Embodiment 2
[0032] Iron-doped nTiO 2 Content is reduced to 0.1% (w / w) by 3.0% (w / w), and the content of dimethylacetamide is increased to 64.9% (w / w) by 62.0% (w / w), and all the other are the same as embodiment 1 . Then the prepared iron-doped nTiO 2 The pure water flux of the visible light-catalyzed hollow fiber ultrafiltration membrane is 306.49 L / m 2 ·hr·0.1MPa, the retention rate of bovine serum albumin is 92.76%, the resistance increase coefficient is 1.79, and the contact angle is 85.7°; the degradation and removal rate of fulvic acid is increased from 27.26% (without light, running for 1 hour) to 38.02 % (under simulated visible light, run for 1 hour).
Embodiment 3
[0034] Iron-doped nTiO 2 Content is brought up to 5.0% (w / w) by 3.0% (w / w), and the content of dimethylacetamide is reduced to 60.0% (w / w) by 62.0% (w / w), all the other are with embodiment 1 . Then the prepared iron-doped nTiO 2 The pure water flux of the visible light-catalyzed hollow fiber ultrafiltration membrane is 334.45 L / m 2 ·hr·0.1MPa, the bovine serum albumin retention rate is 92.27%, the resistance increase coefficient is 1.36, and the contact angle is 73.2°; the degradation and removal rate of fulvic acid is increased from 37.03% (without light, running for 1 hour) to 63.37 % (under simulated visible light, run for 1 hour).
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