Heat and Mass Transport in Modeling Membrane Distillation Configurations: A Review

被引:123
作者
Olatunji, Samuel O. [1 ]
Camacho, Lucy Mar [1 ]
机构
[1] Texas A&M Univ Kingsville, Dept Environm Engn, Kingsville, TX 78363 USA
关键词
membrane distillation; heat transfer; mass transfer; temperature polarization; concentration polarization; MD configurations; desalination; DIRECT-CONTACT MEMBRANE; NEURAL-NETWORK MODEL; OF-THE-ART; VACUUM MEMBRANE; AIR-GAP; NUMERICAL-SIMULATION; WATER DESALINATION; TEMPERATURE POLARIZATION; SEAWATER DESALINATION; OPERATING PARAMETERS;
D O I
10.3389/fenrg.2018.00130
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Identification and mitigation of challenges associated with membrane distillation (MD) modeling are very crucial to the applicability of MD technology in the industry. Several research studies have been carried out on direct contact membrane distillation (DCMD) modeling because of its simplicity, while other MD configurations have gained little attention. Most studies conducted on MD modeling were achieved based on uniform membrane pore size and pore size distribution assumption. This study exploits the homogeneity of these assumptions to conduct a modeling review for temperature polarization (TP) and concentration polarization (CP), as they apply to MD configurations. TP and CP phenomena have been identified as two of the main challenges to advance MD modeling for further development of MD technology. Their impact are detailed in the heat and mass transfer mechanisms discussed. Thermal conductivity of common hydrophobic commercial membrane materials at different temperatures are presented in this study. The use of optimal operating flow rates, suitable membranes, and proper module design are recommended as viable solutions to reduce the effect of TP and CP on permeate flux decay.
引用
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页数:18
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