化工进展
化工進展
화공진전
Chemical Industry and Engineering Progress
2015年
10期
3540-3550
,共11页
谢朋%张忠国%孙涛%吴月%吴秋燕%李继定%李珊
謝朋%張忠國%孫濤%吳月%吳鞦燕%李繼定%李珊
사붕%장충국%손도%오월%오추연%리계정%리산
正渗透%压力阻尼渗透%汲取质%汲取液%反向渗透%浓差极化
正滲透%壓力阻尼滲透%伋取質%伋取液%反嚮滲透%濃差極化
정삼투%압력조니삼투%급취질%급취액%반향삼투%농차겁화
forward osmosis (FO)%pressure-retarded osmosis (PRO)%draw solute%draw solution%reverse permeation%concentration polarization
正渗透(FO)作为一种浓度驱动的膜技术,因其膜污染轻、能耗低和回收率高等优点而逐渐成为膜技术领域的研究热点之一。汲取质的反向渗透是正渗透过程中不可忽视的现象,但其研究相对比较滞后。本文主要介绍了汲取质反渗模型的研究进展,分析了渗透压差、膜表面流速、膜结构与膜材料、温度、汲取质种类、膜取向、离子水力半径等因素对汲取质反向渗透的影响情况,并发现汲取质的反向渗透通量可由其浓度或汲取液渗透压的一元多项式表达。总体而言,FO模式的汲取质反渗模型经过不断发展已相对比较完善,而压力阻尼渗透(PRO)模式的反渗模型则缺陷较大,有待进一步研究;此外,关于汲取质反渗过程影响因素及其影响机制的研究对于汲取质、膜材料的选择与开发,以及正渗透过程的优化均具有重要的指导作用,因此会引起越来越多的关注。
正滲透(FO)作為一種濃度驅動的膜技術,因其膜汙染輕、能耗低和迴收率高等優點而逐漸成為膜技術領域的研究熱點之一。伋取質的反嚮滲透是正滲透過程中不可忽視的現象,但其研究相對比較滯後。本文主要介紹瞭伋取質反滲模型的研究進展,分析瞭滲透壓差、膜錶麵流速、膜結構與膜材料、溫度、伋取質種類、膜取嚮、離子水力半徑等因素對伋取質反嚮滲透的影響情況,併髮現伋取質的反嚮滲透通量可由其濃度或伋取液滲透壓的一元多項式錶達。總體而言,FO模式的伋取質反滲模型經過不斷髮展已相對比較完善,而壓力阻尼滲透(PRO)模式的反滲模型則缺陷較大,有待進一步研究;此外,關于伋取質反滲過程影響因素及其影響機製的研究對于伋取質、膜材料的選擇與開髮,以及正滲透過程的優化均具有重要的指導作用,因此會引起越來越多的關註。
정삼투(FO)작위일충농도구동적막기술,인기막오염경、능모저화회수솔고등우점이축점성위막기술영역적연구열점지일。급취질적반향삼투시정삼투과정중불가홀시적현상,단기연구상대비교체후。본문주요개소료급취질반삼모형적연구진전,분석료삼투압차、막표면류속、막결구여막재료、온도、급취질충류、막취향、리자수력반경등인소대급취질반향삼투적영향정황,병발현급취질적반향삼투통량가유기농도혹급취액삼투압적일원다항식표체。총체이언,FO모식적급취질반삼모형경과불단발전이상대비교완선,이압력조니삼투(PRO)모식적반삼모형칙결함교대,유대진일보연구;차외,관우급취질반삼과정영향인소급기영향궤제적연구대우급취질、막재료적선택여개발,이급정삼투과정적우화균구유중요적지도작용,인차회인기월래월다적관주。
As a concentration-driven membrane process,forward osmosis (FO) is becoming one of the hot spots in the field of membrane technology because of its low fouling,low energy consumption,and high water recovery. Reverse draw solute permeation is a significant phenomenon in FO process,but the research on it is behind other phenomena in FO field. In this paper,the research progress of draw solute reverse osmosis models is reviewed and the effects of such factors as osmosis pressure,membrane surface velocity,membrane structure and materials,solution temperature,draw solute type,membrane orientation,and ionic radius of draw solute on reverse osmosis are analyzed. Draw solute flux can be formulated by a one-dimensional polynomial equation of concentration or osmotic pressure of draw solution. On the whole,the reverse draw solute model of pressure-retarded osmosis (PRO) mode is not as satisfactory as that of FO mode and needs further research. In addition,the research on reverse draw solute permeation is helpful for selecting or developing draw solute and membrane material and optimizing the FO process,so it would attract more and more attention.