PVDF超濾膜進(jìn)行聚乙二醇甲基丙烯酸甲酯(PEGMA)紫外光照射接枝的膜面表征與抗污染分析
[Abstract]:Polyvinylidene fluoride (PVDF) (PVDF) is widely used in the preparation of membrane materials because of its outstanding chemical, mechanical and thermal properties. However, because of its low surface energy and strong hydrophobicity, it is easy to cause membrane fouling during membrane separation. It limits its further development and application. At present, the modification of PVDF membrane by blending, chemical modification and light grafting is widely used in industry to improve its hydrophilicity and pollution resistance. In this paper, (PEGMA) containing hydrophilic group carbonyl group and polyethylene glycol was grafted onto the surface of hydrophobic PVDF ultrafiltration membrane by UV irradiation, and the hydrophilic modification of the membrane was completed. It was also found that the swelling of the grafted layer could be reduced by adding the crosslinking agent N- N- methylene bisacrylamide (MBAA). This method can not damage the bulk properties of the film by UV irradiation, and the process is simple and the cost is low. In this paper, the effect of membrane modification under different modification conditions was studied. The membrane was characterized by various test methods, and the separation efficiency and antifouling property of the membrane were obtained by using emulsified oil solution and bovine serum protein (BSA) solution. The stability of the grafted layer was tested by acid-base and sodium hypochlorite solution. PEGMA was grafted onto the film by UV irradiation, and the product was detected by Fourier transform infrared spectroscopy (FTIR). The results showed that the grafted PEGMA was successfully grafted to the surface of the film, and the results of field emission scanning electron microscopy (FESEM) showed that, The pore size and porosity of the graft modified membranes were reduced. In terms of surface wettability, the results show that the hydrophilicity of the membrane modified by PEGMA is enhanced, and the contact angle of the membrane surface decreases with the prolongation of the grafting concentration and time, such as the contact angle of the original membrane is about 77 擄. The contact angle of 60min grafted with PEGMA of 80g/L is about 58 擄. For the water flux, it was found that the pure water flux of the membrane decreased with the increase of the grafting concentration and grafting time after grafting with PEGMA, such as the pure water flux of the original membrane was about 184.9L/m2 h, and the pure water flux of the original membrane was about 162.2L/m2 h after the grafting of 60min with PEGMA of 40g/L. With the addition of MBAA, the water absorption of the membrane showed a reverse trend. With the increase of grafting concentration and grafting time, the water absorption of the membrane decreased, and the contact angle of MBAA increased slightly compared with that of pure PEGMA, and the pure water flux decreased slightly. In the simulated pollution experiment, when the BSA solution was filtered, the rejection rate of the original membrane was lower than that of the modified membrane at the beginning of filtration, but with the increase of the filtration time, the rejection rate of the original membrane was higher than that of the modified membrane. However, the rejection rate of PEGMA grafted membranes was lower than that of MBAA grafted membranes. The antifouling ability of the membrane was studied by using emulsified oil solution and BSA solution as the filtration medium. The results showed that the order of the antifouling ability of the membrane was the PEGMA graft membrane of the original membrane PEGMA MBAA. The membrane was immersed in acid-base solution and sodium hypochloride solution. By comparison, it was found that the stability of the modified membrane in these three solutions was in the order of acidic environment, strong oxidizing environment and alkaline environment. The research results of this project can not only broaden the technical thinking of preparing high performance ultrafiltration membrane, but also provide technical support for the research of membrane material exploration, separation process design, membrane process operation management and so on.
【學(xué)位授予單位】:東華大學(xué)
【學(xué)位級(jí)別】:碩士
【學(xué)位授予年份】:2015
【分類號(hào)】:TQ051.893;X505
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