膜科学与技术

Position：Home >> Abstract

Investigation of the factors influencing the preparation process of cellulose triacetate forward osmosis membrane

Authors： LIU Leilei , WANG Duo* ,WANG Meng , GAO Congjie

Units： Key Laboratory of Marine Chemistry Theory and Technology, Ministry of Education; College of Chemistry and Chemical Engineering, Ocean University of China; Qingdao Shandong Province, 266100

KeyWords： Cellulose triacetate; Phase inversion; Forward osmosis membrane; Membrane

ClassificationCode：TQ028.8

year,volume(issue):pagination： 2011,31(1):77-83

Abstract：

Cellulose triacetate forward osmosis membrane was prepared by phase inversion method. The polymer solution consisted of cellulose triacetate as the membrane material, 1, 4-dioxane and acetone as solvent, and lactic acid as additives. The effects of support materials, solvent evaporation time and the additive content on the membrane performance were investigated. 0.1mol/L NaCl was used as the feed solution and 4mol/L glucose was used as the draw solution. The water flux was between 6 and 7 L / (m2h) and the rejection for NaCl was above 95% .

Funds：

国家“973”计划项目（2009CB623402）；国家自然科学基金项目（20976171）

AuthorIntro：

刘蕾蕾（1985-），女，山东省潍坊市，硕士生，主要从事功能膜材料的制备。*通讯联系人

Reference：

[1] Holloway R W, Childress A E, Dennett K E, et al. Forward osmosis for concentration of anaerobic digester centrate [J]. Water research, 2007, 41: 4005-4014
[2] Beaudry E G, Herron J R. Direct osmosis for concentrating wastewater, Proceedings of the 27th International Conference on Environmental Systems, Lake Tahoe, July 14-17, 1997
[3] Petrotos K B, Lazarides H N. Osmotic concentration of liquid foods[J]. Food Eng., 2001,49: 201-206.
[4] Wrolstad R E, McDaniel M R, Durst R W, et al. Composition and sensory characterization of red raspberry juice concentrated by direct-osmosis or evaporation[J]. Food Sci.1993,58:633-637.
[5] Bhatt P P. Osmotic drug delivery systems for poorly soluble drugs: PharmaVentures Ltd., Oxford, UK[EB/OL].http://www.shirelabs.com/news/11 30 04.pdf,2004.
[6] Su Y C, Lin L A. Water-powered micro drug delivery system[J]. Microelectromech Syst., 2004,13: 75-82.
[7] Loeb S. Energy production at the Dead Sea by pressure-retarded osmosis: challenge or chimera[J]. Desalination, 1998, 120: 247-262.
[8] Loeb S, Hassen F V, Shahaf D. Production of energy from concentrated brines by pressure-retarded osmosis Ⅱ:experimental results and projected energy costs[J]. Membr. Sci.,1976, 1: 249-269.
[9]Cath T Y, Childress A E, Elimelech M. Forward osmosis: principles, applications, and recent developments [J]. Membr. Sci., 2006, 281:70-87.
[10] 高从堦，郑根江，汪锰等.正渗透-水纯化和脱盐的新途径[J].水处理技术,2008,34(2): 1-4.
[11] Liu L L, Wang M, Wang D, et al. Current patents of forward osmosis membrane process[J]. Recent Patents on Chemical Engineering, 2009, 2(1): 1-7.
[12] Sidney L, Leonid T, Emmanuel K, et al. Effect of porous support fabric on osmosis through a Loeb-Sourirajan type asymmetric membrane[J]. Membr. Sci. 1997, 129: 243-249.
[13] McCutcheon J R, Elimelech M. Influence of concentrative and dilutive internal concentration polarization on flux behavior in forward osmosis[J]. Membr. Sci. 2006, 284: 237–247.
[14]McCutcheon J R, Elimelech M. Influence of membrane support layer hydrophobicity on water flux in osmotically driven membrane processes[J]. Membr. Sci. 2008, 318: 458-466.
[15] 卞晓锴，陆晓峰，施柳青. 原子力显微镜及在膜科学技术研究中的应用. 膜科学与技术，2002，22(5): 36-40.
[16] 钱欣，程蓉. 原子力显微镜在合成膜表征中的应用. 膜科学与技术，2004，24(2):62-66.
[17] 张耀鹏，邵惠丽，沈新元等. 用原子力显微镜研究纤维素膜表面形貌和孔径大小的分布. 膜科学与技术，22(2): 13-16

Service：

【Download】【Collect】

《膜科学与技术》编辑部 Address: Bluestar building, 19 east beisanhuan road, chaoyang district, Beijing; 100029 Postal code; Telephone：010-80492417/010-80485372; Fax：010-80485372 ; Email：mkxyjs@163.com