不同孔径PVDF/Hyflon复合膜在真空膜蒸馏中的应用 
作者:张永兴1,童大庆2,曹娟1,汪朝晖1,汪效祖1
单位: 1.南京工业大学化学化工学院材料化学国家重点实验室,南京 210009; 2. 液化空气(扬州)有限公司,扬州市经济开发区维杨路18号,扬州 225009
关键词: 聚偏氟乙烯,Hyflon AD60,孔径,真空膜蒸馏
出版年,卷(期):页码: 2016,36(1):93-98

摘要:
以三种不同孔径的商品化聚偏氟乙烯(PVDF)平板膜为基膜,浸涂Hyflon AD60后制成疏水型复合膜。在真空膜蒸馏(VMD)的脱盐试验中,考察膜孔径大小对真空膜蒸馏过程的影响。实验结果表明:在进料流量为80L/h、进料温度70℃以及真空度-90kPa条件下,原膜通量随孔径的增大而上升,但稳定性随之下降;经0.5wt%Hyflon AD60涂覆制备的复合膜均能稳定运行24h以上,最大孔径复合膜的平均通量可达31.57kg/(m2.h),同时脱盐率均稳定在99.9%以上。
Composite membranes were prepared by coating a hydrophobic copolymer of Hyflon AD60 on porous flat sheet PVDF membranes with three different pore sizes. During the desalination tests using these original and composite membranes, the effect of mean pore sizes on vacuum membrane distillation (VMD) was investigated. The results showed that the flux of original membrane increased when mean pore size increased under the following conditions: (1) the feed temperature was 70℃, (2) feed flow rate was 80L/h, and (3) vacuum was -90kPa. However, its stability decreased. The composite membrane coated with 0.5wt% Hyflon AD60 could steadily run for over 24h. During this process, the biggest flux reached 31.57 kg/(m2.h) and the desalting rate constantly remained above 99.9%. 
张永兴 (1990-),男,硕士研究生,山东临沂市人,主要研究方向:高分子膜材料制备,Email: zyx9116@163.com,通讯作者:Email: wangxiaozu@njtech.edu.cn

参考文献:
[1] 吴庸烈. 膜蒸馏技术及其应用进展[J].膜科学与技术, 2003, 23(4): 67-73.
[2] Alkhudhiri A, N Darwish, N Hilal. Membrane distillation: A comprehensive review[J]. Desalination, 2012, 287: 2-18.
[3] 环国兰,杜启云,王薇. 膜蒸馏技术研究现状[J].天津工业大学学报, 2009, 28(4): 12-18.
[4] Lawson K W, Lloyd D R. Membrane distillation[J]. Journal of Membrane Science, 1997, 124(1): 1-25.
[5] 申龙,高瑞昶. 膜蒸馏技术最新研究应用进展[J].化工进展, 2013, 33(2): 289-297.
[6] Kullab A , Martin A. Membrane distillation and applications for water purification in thermal cogeneration plants[J]. Separation and Purification Technology, 2011, 76(3): 231-237.
[7] Song L, Ma Z, Liao X, et al. Pilot plant studies of novel membranes and devices for direct contact membrane distillation-based desalination[J]. Journal of Membrane Science, 2008, 323(2): 257-270.
[8] Chiam C-K, Sarbatly R. Vacuum membrane distillation processes for aqueous solution treatment—A review[J].Chemical Engineering and Processing: Process Intensification, 2013, 74: 27-54.
[9] Sun A C, Kosar W, Zhang Y, et al. Vacuum membrane distillation for desalination of water using hollow fiber membranes[J]. Journal of Membrane Science, 2014, 455: 131-142.
[10] El-Bourawi M S, Ding Z, Ma R, et al. A framework for better understanding membrane distillation separation process[J]. Journal of Membrane Science, 2006, 285(1-2): 4-29.
[11] 童大庆,石川,汪效祖,等. 整体非对称性PVDF中空纤维膜在真空膜蒸馏中的应用[J].化工新型材料, 2014, 42(7): 217-220.
[12] Gugliuzza A, Drioli E. PVDF and HYFLON AD membranes: Ideal interfaces for contactor applications[J]. Journal of Membrane Science, 2007, 300(1-2): 51-62.
[13] Gugliuzza A, Drioli E. New performance of hydrophobicfluorinated porous membranes exhibiting particulate-like morphology[J]. Desalination, 2009, 240: 14-20.
[14] Macchione M, Jansen J C, Luca G D, et al. Experimental analysis and simulation of the gas transport in dense Hyflon® AD60X membranes: Influence of residual solvent[J]. Polymer, 2007, 48(9): 2619-2635.
[15]    Garcia-Payo M C, Izquierdo-Gil M A, Fernandez-Pineda C. Wetting Study of Hydrophobic Membranes via Liquid Entry Pressure Measurements with Aqueous Alcohol Solutions[J]. Journal of Colloid and Interface Science, 2000, 230:420-431.
 

服务与反馈:
文章下载】【加入收藏

《膜科学与技术》编辑部 地址:北京市朝阳区北三环东路19号蓝星大厦 邮政编码:100029 电话:010-64426130/64433466 传真:010-80485372邮箱:mkxyjs@163.com

京公网安备11011302000819号