Performance comparison between overlapped and woven spacers for membrane distillation

被引:9
作者
Gurreri, Luigi [1 ]
Tamburini, Alessandro [1 ]
Cipollina, Andrea [1 ]
Micale, Giorgio [1 ]
Ciofalo, Michele [1 ]
机构
[1] Univ Palermo UNIPA, Dipartimento Innovaz Ind & Digitale DIID Ingn Chi, Viale Sci Ed 6, I-90128 Palermo, Italy
关键词
Membrane distillation; Computational fluid dynamics; Spacer-filled channels; Thermochromic liquid crystals; THERMOCHROMIC LIQUID-CRYSTALS; MASS FLUX ENHANCEMENT; FILLED CHANNELS; TEMPERATURE POLARIZATION; HEAT-TRANSFER; SEAWATER-DESALINATION; SOLAR-ENERGY; CFD; MODULES; ULTRAFILTRATION;
D O I
10.5004/dwt.2017.20236
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The sustainable production of freshwater from seawater desalination is receiving increasing attention. Recently, some desalination technologies are taking advantage from the coupling with renewable resources; among them, membrane distillation (MD) is one of the most promising since it can be easily powered by low-grade thermal energy. MD being an emerging technology, efforts are required to optimize geometry and operating conditions of real units in order to reduce the unitary freshwater production cost. In particular, temperature polarization is a well-known detrimental effect for the process driving force; spacers are traditionally used to enhance mixing and make temperature boundary layers thinner, at the cost of higher pressure losses. The present work is devoted to testing and comparing the performance of two different two-layer net spacers: overlapped and woven. Investigations were carried out both by experiments and by computational fluid dynamics (CFD) at different Reynolds numbers, ranging from creeping flow to turbulent flow regimes. Experiments (for intermediate to high Re) made use of thermochromic liquid crystals along with digital image processing. Computational results (for low to intermediate Re) were obtained via steady state (low Re) or direct numerical simulations (intermediate Re) along with the unit cell approach. A good agreement between experiments and CFD results was obtained in the range of superposition. Results showed that woven spacers guarantee a better mixing than overlapped ones, especially in the low to intermediate Re range, thus resulting in Nusselt numbers 2.5-3 times higher. On the other hand, the less disturbed flow field induced by overlapped spacers was found to yield friction coefficients up to 4 times lower, thus allowing lower pumping costs. The choice between the two configurations depends crucially on the relative importance attributed to savings in membrane surface area and in pumping energy for any specific application.
引用
收藏
页码:178 / 189
页数:12
相关论文
共 39 条
[1]   The basics and issues of Thermochromic Liquid Crystal Calibrations [J].
Abdullah, Nadia ;
Abu Talib, Abd. Rahim ;
Jaafar, Abdul Aziz ;
Salleh, Mohamad Amran Mohd ;
Chong, Wen Tong .
EXPERIMENTAL THERMAL AND FLUID SCIENCE, 2010, 34 (08) :1089-1121
[2]   Potential of membrane distillation - A comprehensive review [J].
AlHathal Al-Anezi, Adnan ;
Sharif, Adel O. ;
Sanduk, Mohammed I. ;
Khan, Abdul Rahman .
International Journal of Water, 2013, 7 (04) :317-346
[3]   Modelling flow and heat transfer in spacer-filled membrane distillation channels using open source CFD code [J].
Al-Sharif, Sharaf ;
Albeirutty, Mohammed ;
Cipollina, Andrea ;
Micale, Giorgio .
DESALINATION, 2013, 311 :103-112
[4]   Experimental and theoretical evaluation of temperature polarization phenomenon in direct contact membrane distillation [J].
Ali, A. ;
Macedonio, F. ;
Drioli, E. ;
Aljlil, S. ;
Alharbi, O. A. .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2013, 91 (10) :1966-1977
[5]  
Ansys Inc, 2012, ANSYS CFX REFRENCE G
[6]   Comparison of spacers for temperature polarization reduction in air gap membrane distillation [J].
Chernyshov, MN ;
Meindersma, GW ;
de Haan, AB .
DESALINATION, 2005, 183 (1-3) :363-374
[7]   Development of a Membrane Distillation module for solar energy seawater desalination [J].
Cipollina, A. ;
Di Sparti, M. G. ;
Tamburini, A. ;
Micale, G. .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2012, 90 (12) :2101-2121
[8]   Membrane distillation heat transfer enhancement by CFD analysis of internal module geometry [J].
Cipollina, A. ;
Micale, G. ;
Rizzuti, L. .
DESALINATION AND WATER TREATMENT, 2011, 25 (1-3) :195-209
[9]   CFD simulation of a membrane distillation module channel [J].
Cipollina, A. ;
Di Miceli, A. ;
Koschikowski, J. ;
Micale, G. ;
Rizzuti, L. .
DESALINATION AND WATER TREATMENT, 2009, 6 (1-3) :177-183
[10]   SPACER CHARACTERIZATION AND PRESSURE-DROP MODELING IN SPACER-FILLED CHANNELS FOR ULTRAFILTRATION [J].
DACOSTA, AR ;
FANE, AG ;
WILEY, DE .
JOURNAL OF MEMBRANE SCIENCE, 1994, 87 (1-2) :79-98