Novel design of liquid distributors for VMD performance improvement based on cross-flow membrane module

被引:22
作者
Wang, Li [1 ,2 ,3 ,4 ]
Wang, Hongtao [1 ,2 ,3 ,4 ]
Li, Baoan [1 ,2 ,3 ,4 ]
Wang, Yue [1 ,2 ,3 ]
Wang, Shichang [1 ,3 ]
机构
[1] Tianjin Univ, Sch Chem Engn & Technol, Chem Engn Res Ctr, Tianjin 300072, Peoples R China
[2] Tianjin Univ, State Key Lab Chem Engn, Tianjin 300072, Peoples R China
[3] Tianjin Univ, Tianjin Key Lab Membrane Sci & Desalinat Technol, Tianjin 300072, Peoples R China
[4] Collaborat Innovat Ctr Chem Sci & Engn Tianjin, Tianjin 300072, Peoples R China
关键词
Cross-flow membrane module; CFD; Liquid distributor; Permeate flux; Membrane distillation; DISTILLATION-BASED DESALINATION; MASS-TRANSFER COEFFICIENT; CONTACT; FLUX; ENERGY; PRESSURES; RECOVERY; DEVICES; SYSTEM; SCALE;
D O I
10.1016/j.desal.2014.01.004
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
To enhance the vacuum membrane distillation (VMD) permeate flux of cross-flow membrane module (CF-MM), three kinds of novel liquid distributors were designed and evaluated by computational fluid dynamics (CFD) simulation. Based on the characteristics of the CF-MM, a three-dimensional liquid flow model was built in the shell side of the CF-MM. The feed flow conditions were simulated and calculated. Based on the simulation results, the structural parameters of the liquid distributors were optimized to achieve an even liquid distribution. The pyramidal and dome-like distributors have better liquid distribution than the flat-plate distributor. Two kinds of liquid distributors in flat-plate and pyramidal forms were fabricated and used to study their performances in VMD. Compared with the permeate flux of CF-MM without a distributor, the permeate flux increased to about 5% of the flat-plate distributors, and to about 6% to 12% of the pyramidal distributors. The optimized distributors significantly enhanced the VMD permeate flux of the CF-MM. With the novel pyramidal distributor, a maximum permeate flux of about 72 kg/m(2)h was achieved at feed inlet temperature of 358.15 K, vacuum level of 87 kPa, and feed interstitial velocity of 0.085 m/s. (C) 2014 Elsevier B.V. All rights reserved.
引用
收藏
页码:80 / 86
页数:7
相关论文
共 31 条
[1]  
Abbassi A.E., 2013, DESALINATION, V323, P31
[2]  
Burrieza E. G., 2011, J MEMBRANE SCI, V379, P386
[3]   A framework for better understanding membrane distillation separation process [J].
El-Bourawi, M. S. ;
Ding, Z. ;
Ma, R. ;
Khayet, M. .
JOURNAL OF MEMBRANE SCIENCE, 2006, 285 (1-2) :4-29
[4]   Influence of viscosity and surface tension on performance of gas-liquid contactors with ejector type gas distributor [J].
Elgozali, A ;
Linek, V ;
Fialová, M ;
Wein, O ;
Zahradník, J .
CHEMICAL ENGINEERING SCIENCE, 2002, 57 (15) :2987-2994
[5]   Design for cascade of crossflow direct contact membrane distillation [J].
Gilron, Jack ;
Song, Liming ;
Sirkar, Kamalesh K. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2007, 46 (08) :2324-2334
[6]   Effect of the operating variables on the extraction and recovery of aroma compounds in an osmotic distillation process coupled to a vacuum membrane distillation system [J].
Hasanoglu, A. ;
Rebolledo, F. ;
Plaza, A. ;
Torres, A. ;
Romero, J. .
JOURNAL OF FOOD ENGINEERING, 2012, 111 (04) :632-641
[7]   Integration of membrane distillation into heat paths of industrial processes [J].
Hausmann, Angela ;
Sanciolo, Peter ;
Vasiljevic, Todor ;
Weeks, Mike ;
Duke, Mikel .
CHEMICAL ENGINEERING JOURNAL, 2012, 211 :378-387
[8]   Potential for scaling by sparingly soluble salts in crossflow DCMD [J].
He, Fei ;
Gilron, Jack ;
Lee, Hanyong ;
Song, Liming ;
Sirkar, Kamalesh K. .
JOURNAL OF MEMBRANE SCIENCE, 2008, 311 (1-2) :68-80
[9]   Effects of antiscalants to mitigate membrane scaling by direct contact membrane distillation [J].
He, Fei ;
Sirkar, Kamalesh K. ;
Gilron, Jack .
JOURNAL OF MEMBRANE SCIENCE, 2009, 345 (1-2) :53-58
[10]   Studies on scaling of membranes in desalination by direct contact membrane distillation: CaCO3 and mixed CaCO3/CaSO4 systems [J].
He, Fei ;
Sirkar, Kamalesh K. ;
Gilron, Jack .
CHEMICAL ENGINEERING SCIENCE, 2009, 64 (08) :1844-1859