THE EFFECT OF MIXING PROMOTERS ON THE PERFORMANCE OF FORWARD OSMOSIS MEMBRANE SYSTEMS: COMPUTATIONAL FLUID DYNAMICS SIMULATIONS
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Alshwairekh, Ahmed M.
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Qassim Univ, Coll Engn, Dept Mech Engn, Qasim 52571, Saudi ArabiaLehigh Univ, PC Rossin Coll Engn & Appl Sci, Bethlehem, PA 18015 USA
Alshwairekh, Ahmed M.
[2
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Alghafis, Abdullah A.
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Lehigh Univ, PC Rossin Coll Engn & Appl Sci, Bethlehem, PA 18015 USA
Qassim Univ, Coll Engn, Dept Mech Engn, Qasim 52571, Saudi ArabiaLehigh Univ, PC Rossin Coll Engn & Appl Sci, Bethlehem, PA 18015 USA
Alghafis, Abdullah A.
[1
,2
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Alwatban, Anas M.
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Lehigh Univ, PC Rossin Coll Engn & Appl Sci, Bethlehem, PA 18015 USA
Qassim Univ, Coll Engn, Dept Mech Engn, Qasim 52571, Saudi ArabiaLehigh Univ, PC Rossin Coll Engn & Appl Sci, Bethlehem, PA 18015 USA
Alwatban, Anas M.
[1
,2
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Alqsair, Umar F.
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Lehigh Univ, PC Rossin Coll Engn & Appl Sci, Bethlehem, PA 18015 USA
Prince Sattam Bin Abdulaziz Univ, Coll Engn, Dept Mech Engn, Riyadh 16273, Saudi ArabiaLehigh Univ, PC Rossin Coll Engn & Appl Sci, Bethlehem, PA 18015 USA
Alqsair, Umar F.
[1
,3
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Oztekin, Alparslan
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Lehigh Univ, PC Rossin Coll Engn & Appl Sci, Bethlehem, PA 18015 USALehigh Univ, PC Rossin Coll Engn & Appl Sci, Bethlehem, PA 18015 USA
Oztekin, Alparslan
[1
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机构:
[1] Lehigh Univ, PC Rossin Coll Engn & Appl Sci, Bethlehem, PA 18015 USA
Computational fluid dynamics simulations are performed to study the desalination process in forward osmosis modules. Concentration polarization phenomenon is responsible for lowering the water flux permeation through the membrane. It is desired to mitigate the external concentrative and dilutive concentration polarizations by proper mixing of both the feed and the draw solutions. Chevron -type of corrugation with a single triangular shape is used for membrane corrugation. The peak of the corrugation is oriented toward the feed channel. This type of corrugations produces dips in the membrane in the draw side. The dips will not mix the draw solution properly. Net -type spacers of 45 degrees will be placed in the middle of the draw channel. The spacers will work as mixing promoters and add extra support for the membrane. All configurations will have the same Reynold number of 1500 in both channels. k - omega SST turbulence model is used with modules containing mixing promoters, and the laminar model is used with the module without corrugation and spacers. The results indicate that a 14% increase in the water flux is attained with the presence of spacers and membrane corrugation compared with a flat membrane and no spacers. Also, the dilutive concentration polarization has been mitigated significantly compared with the empty case.
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Univ S Australia, SA Water Ctr Water Management & Reuse, Adelaide, SA 5095, AustraliaUniv S Australia, SA Water Ctr Water Management & Reuse, Adelaide, SA 5095, Australia
Zhao, Shuaifei
Zou, Linda
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Univ S Australia, SA Water Ctr Water Management & Reuse, Adelaide, SA 5095, AustraliaUniv S Australia, SA Water Ctr Water Management & Reuse, Adelaide, SA 5095, Australia
Zou, Linda
Mulcahy, Dennis
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Univ S Australia, SA Water Ctr Water Management & Reuse, Adelaide, SA 5095, AustraliaUniv S Australia, SA Water Ctr Water Management & Reuse, Adelaide, SA 5095, Australia