正渗透技术作为一种新兴的膜技术以其低能耗、耐污染的特点在国际上受到越来越多的关注,并且在海水淡化、绿色能源、航空航天、食品浓缩等多个行业得到了迅速发展.综述了正渗透技术在脱盐、浓缩和能源3个不同方面的应用进展,以及国内近几年在正渗透领域所取得的一些研究进展,并展望了该领域未来的发展前景.
参考文献
| [1] | Zhao Shuaifei .Recent developments in forward osmosis:Opportunities and challenges[J].Journal of Membrane Science,2012,396:1. |
| [2] | 高从堦,郑根江,汪锰,王铎,高学理,周勇.正渗透-水纯化和脱盐的新途径[J].水处理技术,2008(02):1-4,8. |
| [3] | J.T. Tinge;G.J.P. Krooshof;T.M. Smeets .Direct osmosis membrane process to de-water aqueous caprolactam with concentrated aqueous ammonium sulphate[J].Chemical Engineering and Processing,2007(6):505-512. |
| [4] | Tan C H;Ng H Y .A novel hybrid forward osmosis-nanofiltration (FO-NF) process for seawater desalination:Draw solution selection and system configuration[J].Desalination Water Treat,2010,13:356. |
| [5] | M.Wallace;Z.Cui;N.P.Hankins .A thermodynamic benchmark for assessing an emergency drinking water device based on forward osmosis[J].Desalination: The International Journal on the Science and Technology of Desalting and Water Purification,2008(1/3):34-45. |
| [6] | Yangali-Quintanilla V;Li Z;Valladares R et al.Indirect desalination of Red Sea water with forward osmosis and low pressure reverse osmosis for water reuse[J].Desalination,2011,280:160. |
| [7] | Li D et al.Forward osmosis desalination using polymer hydrogels as a draw agent:Influence of draw agent,feed solution and membrane on process performance[J].Water Research,2012,47(01):209. |
| [8] | Zhao S;Zou L;Mulcahy D .Brackish water desalination by a hybrid forward osmosis nanofiltration system using divalent draw solute[J].Desalination,2012,284:175. |
| [9] | Robert L.McGinnis;Menachem Elimelech .Energy requirements of ammonia-carbon dioxide forward osmosis desalination[J].Desalination: The International Journal on the Science and Technology of Desalting and Water Purification,2007(1/3):370-382. |
| [10] | Ling M M;Chung T S .Desalination process using super hydrophilic nanoparticles via forward osmosis integrated with ultrafiltration regeneration[J].Desalination,2011,278:194. |
| [11] | HTI teams up with private donor to deliver emergency water filtrations systems directly to haiti[EB/OL].http://www.htiwater.com/assets/pdf/news_ haiti-relief_011910.pdf,2010-01-18. |
| [12] | Collins Ian Ralph .Water flooding method[P].WO,A1,2006/008439,2006-01-26. |
| [13] | Ryan W. Holloway;Amy E. Childress;Keith E. Dennett;Tzahi Y. Cath .Forward osmosis for concentration of anaerobic digester centrate[J].Water research: A journal of the international water association,2007(17):4005-4014. |
| [14] | York R J;Thiel R S;Beaudry E G.Full-scale experience of direct osmosis concentration applied to leachate management[A].Italy,1999 |
| [15] | Tzahi Y. Cath;Dean Adams;Amy E. Childress .Membrane contactor processes for wastewater reclamation in space Ⅱ. Combined direct osmosis, osmotic distillation, and membrane distillation for treatment of metabolic wastewater[J].Journal of Membrane Science,2005(1/2):111-119. |
| [16] | Tzahi Y. Cath;Sherwin Gormly;Edward G. Beaudry;Michael T. Flynn;V. Dean Adams;Amy E. Childress .Membrane contactor processes for wastewater reclamation in space Part Ⅰ. Direct osmotic concentration as pretreatment for reverse osmosis[J].Journal of Membrane Science,2005(1/2):85-98. |
| [17] | Cornelissen, E.R.;Harmsen, D.;Beerendonk, E.F.;Qin, J.J.;Oo, H.;De Korte, K.F.;Kappelhof, J.W.M.N. .The innovative Osmotic Membrane Bioreactor (OMBR) for reuse of wastewater[J].Water Science and Technology,2011(8):1557-1565. |
| [18] | Xiao D;Tang C Y;Zhang J et al.Modeling salt accumulation in osmotic membrane bioreactors:Implications for FO membrane selection and system operation[J].Journal of Membrane Science,2011,366:314. |
| [19] | Andrea Achilli;Tzahi Y.Cath;Eric A.Marchanc .The forward osmosis membrane bioreactor: A low fouling alternative to MBR processes[J].Desalination: The International Journal on the Science and Technology of Desalting and Water Purification,2009(1/3):10-21. |
| [20] | Van der Bruggen B.;Lejon L.;Vandecasteele C. .Reuse, treatment, and discharge of the concentrate of pressure-driven membrane processes [Review][J].Environmental Science & Technology: ES&T,2003(17):3733-3738. |
| [21] | Wanling Tang;How Yong Ng .Concentration of brine by forward osmosis: Performance and influence of membrane structure[J].Desalination: The International Journal on the Science and Technology of Desalting and Water Purification,2008(1/3):143-153. |
| [22] | Voltaire Sant'Anna;Ligia Damasceno Ferreira Marczak;Isabel Cristina Tessaro .Membrane concentration of liquid foods by forward osmosis: Process and quality view[J].Journal of food engineering,2012(3):483-489. |
| [23] | Nayak C A;Valluri S S;Rastogi N K .Effect of high or low molecular weight of components of feed on transmembrane flux during forward osmosis[J].Journal of Food Engineering,2011,106:48. |
| [24] | Konstantinos B. Petrotos;Harris N. Lazarides .Osmotic concentration of liquid foods[J].Journal of Food Engineering,2001(2/3):201-206. |
| [25] | 杨萍.反渗透及其在果汁浓缩上的应用[J].湛江水产学院学报,1994(02):81. |
| [26] | Koseoglou S S;Lawson J T;Lusas E W .Vegetable juice produced with membrane technology.Process combining ultrafiltration and reverse osmosis yields fresh tasting,clarified juices[J].Food Technology,1991,45(01):124. |
| [27] | John R Herron;Edward G Beaudry;Carl E Jochums .Osmotic concentration apparatus and method for direct osmotic concentration for fruit juices[P].US,5281430,1994-01-25. |
| [28] | Konstantinos B Petrotos;Peter Quantick;Heracles Petropakis .A study of thedirect osmotic concentration of tomato juice in tubular membrane-module configuration L The effect of certain basic process parameters on the process performance[J].Journal of Membrane Science,1998,150(01):99. |
| [29] | Devoe Irving W .Osmosis process for producing energy[P].WO,A1,2005/019643,2005-03-03. |
| [30] | Robert L McGinnis;Jeffrey R McCutcheon;Menachem Elimelech .A novel ammonia-carbon dioxide osmotic heat engine for power generation[J].Journal of Membrane Science,2007,305(1-2):13. |
| [31] | Steimel,Lyle H .Method and apparatus for providing treatment chemicals to process water systems[P].WO,A1,2007/084256,2007-07-26. |
| [32] | Qian Yang;Kai Yu Wang;Tai-Shung Chung .A novel dual-layer forward osmosis membrane for protein enrichment and concentration[J].Separation and Purification Technology,2009(3):269-274. |
| [33] | Chetan A. Nayak;Navin K. Rastogi .Forward osmosis for the concentration of anthocyanin from Garcinia indica Choisy[J].Separation and Purification Technology,2010(2):144-151. |
| [34] | Wang, K.Y.;Teoh, M.M.;Nugroho, A.;Chung, T.-S. .Integrated forward osmosis-membrane distillation (FO-MD) hybrid system for the concentration of protein solutions[J].Chemical Engineering Science,2011(11):2421-2430. |
| [35] | Sapna K Deo;Elissavet A Moschou et al.Responsive drug delivery systems[J].Analytical Chemistry,2003,5:207. |
| [36] | 樊晋琼,苏燕,王铎.二氧化钛/聚酰胺正渗透复合膜的制备与表征[J].水处理技术,2012(09):43-46,53. |
| [37] | 李丽丽,王铎.醋酸纤维素正渗透膜的制备及其性能研究[J].功能材料,2012(05):595-598. |
| [38] | 刘蕾蕾,王铎,汪锰,高从堦.三醋酸纤维素正渗透膜制备过程中影响因素的研究[J].膜科学与技术,2011(01):77-83. |
| [39] | 许高杰,刘安康,何涛,李雪梅.MAPTES-Fe3O4的制备及作为可回收驱动液的研究[J].南京工业大学学报（自然科学版）,2012(05):104-107. |
| [40] | 马宇春,刘安康,陈登星,李刚,何涛,李雪梅.基于乙二胺四乙酸的正渗透驱动液的研究[J].南京工业大学学报（自然科学版）,2012(03):79-83. |
| [41] | 李海兰,贾玉香,胡仰栋.以荷电化碳纳米管构筑正渗透膜用于海水淡化的分子动力学模拟[J].物理化学学报,2012(03):573-577. |
| [42] | 贾玉香,李燕,胡仰栋.正渗透过程中纳米碳管膜的盐水通道行为[J].物理化学学报,2011(01):228-232. |
| [43] | Yu-xiang Jia;Hai-lan Li;Meng Wang .Carbon nanotube: Possible candidate for forward osmosis[J].Separation and Purification Technology,2010(1):55-60. |
| [44] | Zhu, H.;Zhang, L.;Wen, X.;Huang, X. .Feasibility of applying forward osmosis to the simultaneous thickening, digestion, and direct dewatering of waste activated sludge[J].Bioresource Technology: Biomass, Bioenergy, Biowastes, Conversion Technologies, Biotransformations, Production Technologies,2012(1):207-213. |
| [45] | Zhang Hanmin;Ma Yanjie;Jiang Tao et al.Influence of activated sludge properties on flux behavior in osmosis membrane bioreactor(OMBR)[J].Journal of Membrane Science,2012,390-391:270. |
上一张
下一张
上一张
下一张
计量
- 下载量()
- 访问量()
文章评分
- 您的评分：
-
10%
-
20%
-
30%
-
40%
-
50%