Correlations for Concentration Polarization and Pressure Drop in Spacer-Filled RO Membrane Modules Based on CFD Simulations

被引:28
作者
Gu, Boram [1 ,2 ]
Adjiman, Claire S. [1 ]
Xu, Xiao Yun [1 ]
机构
[1] Imperial Coll London, Dept Chem Engn, London SW7 2AZ, England
[2] Chonnam Natl Univ, Sch Chem Engn, 77 Yongbong Ro, Gwangju 61186, South Korea
关键词
reverse osmosis (RO); feed spacers; computational fluid dynamics (CFD); concentration polarization (CP); pressure drop; correlations; MODEL;
D O I
10.3390/membranes11050338
中图分类号
Q5 [生物化学]; Q7 [分子生物学];
学科分类号
071010 ; 081704 ;
摘要
Empirical correlations for mass transfer coefficient and friction factor are often used in process models for reverse osmosis (RO) membrane systems. These usually involve four dimensionless groups, namely Reynolds number (Re), Sherwood number (Sh), friction factor (f), and Schmidt number (Sc), with the associated coefficients and exponents being obtained by fitting to experimental data. However, the range of geometric and operating conditions covered by the experiments is often limited. In this study, new dimensionless correlations for concentration polarization (CP) modulus and friction factor are presented, which are obtained by dimensional analysis and using simulation data from computational fluid dynamics (CFD). Two-dimensional CFD simulations are performed on three configurations of spacer-filled channels with 76 combinations of operating and geometric conditions for each configuration, covering a broad range of conditions encountered in RO membrane systems. Results obtained with the new correlations are compared with those from existing correlations in the literature. There is good consistency in the predicted CP with mean discrepancies less than 6%, but larger discrepancies for pressure gradient are found among the various friction factor correlations. Furthermore, the new correlations are implemented in a process model with six spiral wound modules in series and the predicted recovery, pressure drop, and specific energy consumption are compared with a reference case obtained by ROSA (Reverse Osmosis System Analysis, The Dow Chemical Company). Differences in predicted recovery and pressure drop are up to 5% and 83%, respectively, highlighting the need for careful selection of correlations when using predictive models in process design. Compared to existing mass transfer correlations, a distinct advantage of our correlations for CP modulus is that they can be directly used to estimate the impact of permeate flux on CP at a membrane surface without having to resort to the film theory.
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页数:19
相关论文
共 54 条
[1]   Impact of different spacer filaments geometries on 2D unsteady hydrodynamics and concentration polarization in spiral wound membrane channel [J].
Ahmad, A. L. ;
Lau, K. K. .
JOURNAL OF MEMBRANE SCIENCE, 2006, 286 (1-2) :77-92
[2]   Impact of different spacer filament geometries on concentration polarization control in narrow membrane channel [J].
Ahmad, AL ;
Lau, KK ;
Abu Bakar, MZ .
JOURNAL OF MEMBRANE SCIENCE, 2005, 262 (1-2) :138-152
[3]  
[Anonymous], FILMTECTM SW30XHR 44
[4]   SPIRAL WOUND MODULES PERFORMANCE - AN ANALYTICAL SOLUTION .1. [J].
AVLONITIS, S ;
HANBURY, WT ;
BENBOUDINAR, M .
DESALINATION, 1991, 81 (1-3) :191-208
[5]  
BENBOUDINAR M, 1992, DESALINATION, V86, P273
[6]  
Boram G, 2017, THESIS IMPERIAL COLL
[7]   MATHEMATICAL-MODEL OF REVERSE-OSMOSIS IN PARALLEL-WALL CHANNELS WITH TURBULENCE PROMOTING NETS [J].
CHIOLLE, A ;
GIANOTTI, G ;
GRAMONDO, M ;
PARRINI, G .
DESALINATION, 1978, 26 (01) :3-16
[8]   OPTIMAL CHANNEL SPACER DESIGN FOR ULTRAFILTRATION [J].
DACOSTA, AR ;
FANE, AG ;
FELL, CJD ;
FRANKEN, ACM .
JOURNAL OF MEMBRANE SCIENCE, 1991, 62 (03) :275-291
[9]   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
[10]   NET-TYPE SPACERS - EFFECT OF CONFIGURATION ON FLUID-FLOW PATH AND ULTRAFILTRATION FLUX [J].
DACOSTA, AR ;
FANE, AG .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1994, 33 (07) :1845-1851