期刊文献+

直接接触式膜蒸馏不同操作温度下的能耗分析研究 被引量:9

Exergy Analysis of Direct Contact Membrane Distillation under Different Operating Temperatures
下载PDF
导出
摘要 膜蒸馏(MD)过程伴随相变,能量利用效率是决定其是否具有竞争力的重要因素。考察了直接接触式膜蒸馏(DCMD)法海水淡化过程中操作温度对跨膜通量和()效率的影响,计算和分析了不同操作温度下的系统()损失和()效率。结果表明,膜透过侧冷却至常温以下时,冷却部分的()损失较大,占总能耗的35%以上;料液侧温度在50℃以下时膜组件的()损失占总()损失的50%以上,升高至55℃以上时则加热部分()损失比例升高至50%以上。合适的膜蒸馏操作温度可提高系统的()效率,透过侧温度为环境温度(25℃)、膜两侧温差为33.5℃左右时,可获得相对较高的系统总()效率、膜组件()效率和膜通量,膜组件()效率可达50%以上,系统总()效率为0.5%以上。提高膜组件以外其它部分的()效率是提高系统总()效率的关键。 Membrane distillation(MD) is a separation process accompanied with phase change and such that energy utilization is an important aspect for its competitive application.In this paper,the effects of feed temperature(Tf),permeate temperature(Tp) and transmembrane temperature difference on transmembrane water flux and exergy efficiency of direct contact membrane distillation(DCMD) were investigated.A parameter,K,which is defined as the ratio of transmembrane water flux to transmembrane temperature difference,was introduced to evaluate the effect of operating temperature on thermal efficiency of DCMD.The exergy loss and exergy efficiency of the system were calculated and analyzed under different operating temperatures.The results show that K-value increases with an increase in Tf but is hardly affected by the change of Tp.The results of exergy calculation show that the exergy loss in the cooling section of the system is over 35 percentage of the total exergy loss when Tp is below ambient temperature(25℃).The exergy loss in the heating section of the system is over 50 percentage of the total exergy loss when Tf is above 55℃,while the exergy loss in membrane module is above 50 percentage of the total exergy loss when Tf is below 50℃.In general,operating under 25℃ of permeate temperature combined with nearby 33.5℃ of transmembrane temperature difference is favorable to achieve relatively high exergy efficiency of membrane module and of the total system,that is,above 50% and 0.5%,respectively.Besides the of membrane module,improving exergy efficiency of other sections of DCMD system,such as the cooling section and the heating section is of key essential to achieve high exergy efficiency of the total system.
出处 《高校化学工程学报》 EI CAS CSCD 北大核心 2011年第4期565-571,共7页 Journal of Chemical Engineering of Chinese Universities
基金 国家重点基础研究计划(973项目)资助项目(2009CB2199006)
关键词 直接接触式膜蒸馏 操作温度 膜通量 (火用)效率 (火用)损耗 direct contact membrane distillation(DCMD) operating temperature transmembrane flux exergy efficiency exergy loss
  • 相关文献

参考文献12

  • 1王许云,张林,陈欢林.膜蒸馏技术最新研究现状及进展[J].化工进展,2007,26(2):168-172. 被引量:65
  • 2贠延滨,刘丽英,马润宇,FaneAG.浓盐溶液的膜蒸馏机理研究[J].高校化学工程学报,2002,16(4):389-395. 被引量:14
  • 3Bui V A,Vu L T T,Nguyen M H.Simulation and optimisation of direct contact membrane distillation for energy efficiency[J].Desalination,2010,259(1-3):29-37.
  • 4Criscuoli A,Carnevale M C,Drioli E.Evaluation of energy requirements in membrane distillation[J].Chemical Engineering and Processing,2008,47 (7):1098-1105.
  • 5吕晓龙.膜蒸馏过程探讨[J].膜科学与技术,2010,30(3):1-10. 被引量:40
  • 6Criscuoli A,Drioli E.Energetic and exergetic analysis of an integrated membrane desalination system[J].Desalination,1999,124(1-3):243-249.
  • 7Banat F,Jwaied N.Exergy analysis of desalination by solar-powered membrane distillation units[J].Desalination,2008,230(1-3):27-40.
  • 8Al-obaidani S,Curcio E,Macedonio F,et al.Potential of membrane distillation in seawater desalination:Thermal efficiency,sensitivity study and cost estimation[J].J Membr Sci,2008,323(1):85-98.
  • 9FENG Xiao(冯胃).Energy Conservation Principle and Technology of Chemical Engineering(化工节能原理与技术)[M].Beijing(北京):Chemical industry press(化学工业出版社),2009.
  • 10Drioli E,Criscuoli A,Curcio E.Membrane Contactors:Fundamentals,Applications and Potentialities膜接触器一原理、应用及发展前景)[M].LI Na(李娜),JIA Yuan-yuan(贾原嫒),SU Xue-su(苏学素),译.Beijing(北京):Chemical Industry Press(化学工业出版社),2009.

二级参考文献98

  • 1YUN Y, MA R, ZHANG W, et al. Direct contact membrane distillation mechanism for high concentration NaCl solutions [J]. Desalination, 2006, 188 (1/ 3) : 251-262.
  • 2CATH T Y, ADAMS V D, CHILDRESS A E. Experimental study of desalination using direct contact membrane distillation: a new approach to flux enhancement[J]. Journal of Membrane Science, 2004, 228 (1): 5-16.
  • 3CHENG L H, WU P C, CHEN J. Modeling and optimization of hollow fiber DCMD module for desalination [J] .Journal of Membrane Science, 2008, 318 (1/2): 154-166.
  • 4IMDAKM A O, MATSUURA T. Simulation of heat and mass transfer in direct contact membrane distil- lation (MD) : the effect of membrane physical properties[J]. Journal of Membrane Science, 2005, 262 (1/ 2) : 117-128.
  • 5LAGAN F, BARBIERI G, DRIOLI E. Direct contact membrane distillation: modelling and concentration ex- periments[J]. Journal of Membrane Science, 2000, 166 (1): 1-11.
  • 6QTAISHAT M, MATSUURA T, KRUCZEK B, et al. Heat and mass transfer analysis in direct contact membrane distillation[J]. Desalination, 2008, 219 (1/ 3) : 272-292.
  • 7MARTINEZ L, FLORIDO-DIAZ F J, HERNANDEZ A, et al. Charaeterisation of three hydrophobic porous membranes used in membrane distillation: modelling and evaluation of their water vapour permeabilities[J]. Journal of Membrane Science, 2002, 203 (1/2): 15- 27.
  • 8Smoders K,Franken A C M.Terminology for membrane distillation[J].Desalination,1989,72:249-282.
  • 9El-Bourawi M S,Ding a Z,Ma R,Khayet M.A framework for better understanding membrane distillation separation process[J].J Membr Sci,2006,285:4-29.
  • 10Hanemaaijera J H,van Medevoorta J,Jansena A E,et al.Memstill membrane distillation-a future desalination Technology[J].Desalination,2006,199:175-176.

共引文献111

同被引文献108

引证文献9

二级引证文献99

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部