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首页> 外文期刊>Journal of Membrane Science >Preparation and characterization of PVDF-PFS A blend hollow fiber UF membrane
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Preparation and characterization of PVDF-PFS A blend hollow fiber UF membrane

机译:混合中空纤维超滤膜PVDF-PFS的制备与表征

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Polyvinylidene fluoride (PVDF)-perfluorosulfonic acid (PFSA) blend hollow fiber ultrafiltration (UF) membranes were prepared by wet-spinning method using pure water as an external coagulation solution. Coagulation kinetics of PVDF-PFSA-DMAc system was measured by light transmittance experiment. Using PEG10000 (M_w = 10,000), lysozyme (M_w = 14,400), PEG20000 (M_w = 20,000) and BSA (M_w = 67,000), the separation performances of PVDF-PFS A blend hollow fiber UF membranes were obtained. Based on the experimental results, the delayed demixing process was observed for the dope solution M-1 without PFSA-H while the instantaneous demixing process was observed for the others with PFSA-H in the dope solutions M-2 to M-6. The precipitation rate increased with the increment of the PFSA-H concentration in PVDF-PFSA dope solution. The bore fluid solution with 95:5 DMAc:H_2O resulted in single finger-like voids for PVDF-PFSA-H UF membrane. The pure water permeation flux of PVDF-PFSA-H UF membranes firstly increased from <0.1 x 10~(-5) to 119.1 x 10~(-5) L m~(-2) h~(-1) Pa~(-1) (<0.1 to 119.1 Lm~(-2)h~(-1) bar~(-1))for M-1 to M-4(1) and 137 x 10~(-5) L m~(-2) h~(-1) Pa~(-1) (137 L m~(-2) h~(-1) bar~(-1)) for M-4(2), and decreased from 119.1 x 10~(-5) to 79 x 10~(-5) L m~(-2) h~(-1) Pa~(-1) (119.1 to 79Lm~(-2) h~(-1) bar~(-1)) for M-4(1), M-5 and M-6 as the PFSA-H concentration changed from 0% to 5% and total PVDF-PFSA-H concentration was 20wt.%. The molecular weight cut-off (MWCO) of PVDF-PFSA blend hollow fiber UF membranes spun from 20 wt.% PVDF-PFSA-H concentration with 3-5 wt.% PFSA-H was about 20,000 while that spun from 22 wt.% PVDF-PFSA-H or PVDF-PFSA-Na concentration with 5 wt.% PFSA-H or PFSA-Na was about 10,000. As the W_(PFSA-H)/W_(PVDF) increases from 2/18 to 5/15 for M-3-M-6, J_(BSA)/J_w, increases from 0.53 to 0.79. The anti-fouling property of PVDF-PFSA-H blend UF membrane is superior to PVDF-PFSA-Na blend membrane. Based on FTIR spectra, PFSA-H existed in PVDF-PFSA blend hollow fiber UF membranes. There is no obvious variation of the intensity of the characteristic peak at 983 cm~(-1) assigned to C-O-C group of PFSA-H molecules. This also illustrated that PVDF-PFSA-H blend hollow fiber UF membranes were stable.
机译:采用纯水为外部混凝液,通过湿纺法制备了聚偏氟乙烯(PVDF)-全氟磺酸(PFSA)共混中空纤维超滤(UF)膜。通过透光实验测量了PVDF-PFSA-DMAc体系的凝结动力学。使用PEG10000(M_w = 10,000),溶菌酶(M_w = 14,400),PEG20000(M_w = 20,000)和BSA(M_w = 67,000),获得PVDF-PFS A共混中空纤维超滤膜的分离性能。根据实验结果,观察到在没有PFSA-H的涂料溶液M-1中存在延迟的混合过程,而在M-2至M-6的涂料溶液中对具有PFSA-H的其他溶液观察到了瞬时混合过程。随着PVDF-PFSA涂料溶液中PFSA-H浓度的增加,沉淀速率增加。具有95:5 DMAc:H_2O的钻孔液溶液导致PVDF-PFSA-H UF膜出现单指状空隙。 PVDF-PFSA-H UF膜的纯水渗透通量首先从<0.1 x 10〜(-5)增加到119.1 x 10〜(-5)L m〜(-2)h〜(-1)Pa〜( -1)(对于M-1至M-4(1)和137 x 10〜(-5)L m〜(<0.1至119.1 Lm〜(-2)h〜(-1)bar〜(-1)) M-4(2)的(-2)h〜(-1)Pa〜(-1)(137 L m〜(-2)h〜(-1)bar〜(-1)),从119.1降低x 10〜(-5)至79 x 10〜(-5)L m〜(-2)h〜(-1)Pa〜(-1)(119.1至79Lm〜(-2)h〜(-1) M-4(1),M-5和M-6的bar〜(-1))随PFSA-H浓度从0%变为5%,总PVDF-PFSA-H浓度为20wt。%。从20 wt。%的PVDF-PFSA-H浓度和3-5 wt。%PFSA-H纺丝得到的PVDF-PFSA共混中空纤维UF膜的分子量截留值(MWCO)约为20,000,而从22 wt。具有5重量%的PFSA-H或PFSA-Na的5%PVDF-PFSA-H或PVDF-PFSA-Na浓度为约10,000。对于M-3-M-6,随着W_(PFSA-H)/ W_(PVDF)从2/18增加到5/15,J_(BSA)/ J_w从0.53增加到0.79。 PVDF-PFSA-H共混超滤膜的防污性能优于PVDF-PFSA-Na共混膜。基于FTIR光谱,PFDF-PFSA共混中空纤维超滤膜中存在PFSA-H。 PFSA-H分子的C-O-C基团在983 cm〜(-1)处的特征峰强度没有明显变化。这也说明PVDF-PFSA-H共混中空纤维超滤膜是稳定的。

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