化工学报 ›› 2021, Vol. 72 ›› Issue (S1): 421-429.DOI: 10.11949/0438-1157.20201315
收稿日期:
2020-09-17
修回日期:
2020-10-10
出版日期:
2021-06-20
发布日期:
2021-06-20
通讯作者:
黄仁亮
作者简介:
吴中杰(1987—),男,博士研究生,基金资助:
WU Zhongjie1(),LIU Zeyan2,XIE Lianke1,CUI Mei2,HUANG Renliang2()
Received:
2020-09-17
Revised:
2020-10-10
Online:
2021-06-20
Published:
2021-06-20
Contact:
HUANG Renliang
摘要:
聚偏氟乙烯(PVDF)膜因其优异的化学和力学稳定性而被广泛应用于水处理领域,但PVDF膜本身的疏水性,容易使其在处理含油废水的过程中被油滴污染,造成膜孔堵塞。以PVDF微滤膜为基底,通过单宁酸(TA)和聚乙烯亚胺(PEI)共沉积形成了TA/PEI黏附层,经戊二醛共价交联和接枝半胱氨酸(Cys),制备了一种PVDF改性膜(PVDF@TA/PEI-Cys)。改性后的PVDF膜具有良好的亲水性和水下超疏油性,水接触角和水下油接触角分别为22.2°和150.2°。在0.09 MPa下,PVDF@TA/PEI-Cys膜的纯水通量达6328 L/(m2·h),水包油型乳液分离效率高达99.9%。此外,该改性膜还可同时吸附水中的汞离子,最大吸附量为24.7 mg/g。
中图分类号:
吴中杰, 刘则艳, 谢连科, 崔美, 黄仁亮. 聚偏氟乙烯膜亲水改性及其乳液分离与重金属吸附应用[J]. 化工学报, 2021, 72(S1): 421-429.
WU Zhongjie, LIU Zeyan, XIE Lianke, CUI Mei, HUANG Renliang. Preparation of hydrophilic poly(vinylidene fluoride) membrane for oil/water emulsion separation and heavy metal ions adsorption[J]. CIESC Journal, 2021, 72(S1): 421-429.
图2 不同改性PVDF膜的XPS谱图(a)和PVDF@TA/PEI-Cys膜S 2p的XPS谱图(b)
Fig.2 XPS spectra of different PVDF membranes (a) and high-resolution S 2p spectrum of PVDF@TA/PEI-Cys membrane (b)
图6 不同水包油乳液(SDS稳定)的通量和油截留率(a);不同表面活性剂稳定的水包柴油乳液的通量和油截留率(b);柴油/SDS/水乳液分离前后的照片和光学显微镜图像(c)
Fig.6 Emulsion flux and oil rejection ratio of SDS stabilized oil-in-water emulsions (a); Different surfactant stabilized diesel oil-in-water emulsions (b); Photographs and optical microscope images of SDS stabilized diesel oil-in-water emulsion and filtrate (c)
图9 Hg2+浓度随吸附时间的变化(a); Hg2+浓度随吸附时间变化的拟二级动力学拟合曲线(b)
Fig.9 Changes in Hg2+ concentrations with adsorption time (a); Pseudo-second-order kinetic fitting curve of Hg2+ concentrations with adsorption time (b)
Ion | qe(exp)/(mg/g) | Pseudo-second-order kinetic | ||
---|---|---|---|---|
qe/(mg/g) | K2/(g/(mg·min)) | R2 | ||
Hg2+ | 15.9 | 15.82 | 0.004 | 0.9994 |
表1 Hg2+吸附的拟二级动力学模型参数
Table 1 Parameters of pseudo-second-order kinetic model for Hg2+ adsorption
Ion | qe(exp)/(mg/g) | Pseudo-second-order kinetic | ||
---|---|---|---|---|
qe/(mg/g) | K2/(g/(mg·min)) | R2 | ||
Hg2+ | 15.9 | 15.82 | 0.004 | 0.9994 |
图10 不同初始Hg2+浓度下膜的吸附量(a);Langmuir等温吸附模型拟合曲线(b)
Fig.10 Adsorption capacity of PVDF@TA/PEI-Cys membrane at different initial concentrations of Hg2+(a); Fitting curve of Langmuir isotherm adsorption model (b)
Ion | qe(exp)/(mg/g) | Langmuir model | ||
---|---|---|---|---|
qm/(mg/g) | KL/(L/mg) | R2 | ||
Hg2+ | 24.7 | 25.96 | 120.9 | 0.9913 |
表2 Hg2+吸附的Langmuir模型参数
Table 2 Parameters of Langmuir model for Hg2+ adsorption
Ion | qe(exp)/(mg/g) | Langmuir model | ||
---|---|---|---|---|
qm/(mg/g) | KL/(L/mg) | R2 | ||
Hg2+ | 24.7 | 25.96 | 120.9 | 0.9913 |
Membrane | Ion | Capacity/(mg/g) | Ref. |
---|---|---|---|
PVDF@TA/PEI-Cys | Hg2+ | 24.7 | this work |
Zr(Ⅳ)-PVDF | As5+ | 21.5 | [ |
PES/FMBO | As3+ | 73.5 | [ |
PVDF-PAA-MEA | Hg2+ | 55.0 | [ |
PC/HMO | Cu2+ | 29.6 | [ |
PSf/GO | Cu2+ | 68.3 | [ |
PSf/HFO | Pb2+ | 13.2 | [ |
PSf/NFO | Cd2+ | 23.8 | [ |
PVA-PVDF | Pb2+ | 121.2 | [ |
表3 不同膜材料对重金属离子的吸附量比较
Table 3 Comparison of maximum adsorption capacity of different membrane materials for heavy metal ions
Membrane | Ion | Capacity/(mg/g) | Ref. |
---|---|---|---|
PVDF@TA/PEI-Cys | Hg2+ | 24.7 | this work |
Zr(Ⅳ)-PVDF | As5+ | 21.5 | [ |
PES/FMBO | As3+ | 73.5 | [ |
PVDF-PAA-MEA | Hg2+ | 55.0 | [ |
PC/HMO | Cu2+ | 29.6 | [ |
PSf/GO | Cu2+ | 68.3 | [ |
PSf/HFO | Pb2+ | 13.2 | [ |
PSf/NFO | Cd2+ | 23.8 | [ |
PVA-PVDF | Pb2+ | 121.2 | [ |
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