2011
DOI: 10.1016/j.cej.2010.12.034
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CFD simulation of water removal from water/ethylene glycol mixtures by pervaporation

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Cited by 118 publications
(44 citation statements)
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References 24 publications
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“…Recently Rezakazemi et al (2011) proposed a model for PV separation of water/ethylene glycol solution based on solving equations of mass and momentum conservation (Navier-Stokes equations) with Finite Element Method (FEM) [25]. Effect of temperature and velocity was investigated in their research and their results were in good agreement with experimental data.…”
Section: Introductionsupporting
confidence: 70%
“…Recently Rezakazemi et al (2011) proposed a model for PV separation of water/ethylene glycol solution based on solving equations of mass and momentum conservation (Navier-Stokes equations) with Finite Element Method (FEM) [25]. Effect of temperature and velocity was investigated in their research and their results were in good agreement with experimental data.…”
Section: Introductionsupporting
confidence: 70%
“…Extensive studies have been conducted for mass transfer modeling of PV systems [23][24][25][26][27][28][29][30]. Recently Rezakazemi et al (2011) proposed a model for PV separation of water/ethylene glycol solution based on solving equations of mass and momentum conservation (Navier-Stokes equations) with Finite Element Method (FEM) [25]. Effect of temperature and velocity was investigated in their research and their results were in good agreement with experimental data.…”
Section: Introductionsupporting
confidence: 50%
“…This produces a complex morphology and transport situation. Extensive studies have been conducted for mass transfer modeling of PV systems [23][24][25][26][27][28][29][30]. Recently Rezakazemi et al (2011) proposed a model for PV separation of water/ethylene glycol solution based on solving equations of mass and momentum conservation (Navier-Stokes equations) with Finite Element Method (FEM) [25].…”
Section: Introductionmentioning
confidence: 99%
“…at t=0, C w-f =C 0,w and u=u 0 (25) Where C w-f is water concentration in feed phase, C 0,w is its initial value and u 0 is the initial velocity of the feed flow. The boundary conditions for mass conservation equations in the feed phase are as follows: at z=L, Outflow condition (26) at z=0, C w-f =C 0,w (Inlet boundary) (27) at r=R 3 ,…”
Section: Feed Phase Simulationmentioning
confidence: 99%
“…Extensive studies have been conducted for mass transfer modeling of PV systems [23][24][25][26][27][28][29][30]. Recently Rezakazemi et al (2011) proposed a model for PV separation of water/ethylene glycol solution based on solving equations of mass and momentum conservation (Navier-Stokes equations) with Finite Element Method (FEM) [25].…”
Section: Introductionmentioning
confidence: 99%