Performance Investigation of O-Ring Vacuum Membrane Distillation Module for Water Desalination

A new O-ring flat sheet membrane module design was used to investigate the performance of Vacuum Membrane Distillation (VMD) for water desalination using two commercial polytetrafluoroethylene (PTFE) and polyvinylidene fluoride (PVDF) flat sheet hydrophobic membranes. The design of the membrane modu...

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Main Authors: Adnan Alhathal Alanezi, H. Abdallah, E. El-Zanati, Adnan Ahmad, Adel O. Sharif
Format: Article
Language:English
Published: Wiley 2016-01-01
Series:Journal of Chemistry
Online Access:http://dx.doi.org/10.1155/2016/9378460
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author Adnan Alhathal Alanezi
H. Abdallah
E. El-Zanati
Adnan Ahmad
Adel O. Sharif
author_facet Adnan Alhathal Alanezi
H. Abdallah
E. El-Zanati
Adnan Ahmad
Adel O. Sharif
author_sort Adnan Alhathal Alanezi
collection DOAJ
description A new O-ring flat sheet membrane module design was used to investigate the performance of Vacuum Membrane Distillation (VMD) for water desalination using two commercial polytetrafluoroethylene (PTFE) and polyvinylidene fluoride (PVDF) flat sheet hydrophobic membranes. The design of the membrane module proved its applicability for achieving a high heat transfer coefficient of the order of 103 (W/m2 K) and a high Reynolds number (Re). VMD experiments were conducted to measure the heat and mass transfer coefficients within the membrane module. The effects of the process parameters, such as the feed temperature, feed flow rate, vacuum degree, and feed concentration, on the permeate flux have been investigated. The feed temperature, feed flow rate, and vacuum degree play an important role in enhancing the performance of the VMD process; therefore, optimizing all of these parameters is the best way to achieve a high permeate flux. The PTFE membrane showed better performance than the PVDF membrane in VMD desalination. The obtained water flux is relatively high compared to that reported in the literature, reaching 43.8 and 52.6 (kg/m2 h) for PVDF and PTFE, respectively. The salt rejection of NaCl was higher than 99% for both membranes.
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spelling doaj-art-68f14ffafc6d4aa985ef2db7f4a58e2d2025-08-20T02:35:25ZengWileyJournal of Chemistry2090-90632090-90712016-01-01201610.1155/2016/93784609378460Performance Investigation of O-Ring Vacuum Membrane Distillation Module for Water DesalinationAdnan Alhathal Alanezi0H. Abdallah1E. El-Zanati2Adnan Ahmad3Adel O. Sharif4Department of Chemical Engineering Technology, College of Technological Studies, The Public Authority for Applied Education and Training (PAAET), P.O. Box 117, 44010 Sabah Al-Salem, KuwaitChemical Engineering and Pilot Plant Department, Engineering Research Division, National Research Centre, Dokki, Giza, EgyptChemical Engineering and Pilot Plant Department, Engineering Research Division, National Research Centre, Dokki, Giza, EgyptDepartment of Polymer Engineering and Technology, University of the Punjab, Quaid-e-Azam Campus, P.O. Box 54590, Lahore, PakistanQatar Environment and Energy Research Institute, HBKU, Qatar Foundation, Doha, QatarA new O-ring flat sheet membrane module design was used to investigate the performance of Vacuum Membrane Distillation (VMD) for water desalination using two commercial polytetrafluoroethylene (PTFE) and polyvinylidene fluoride (PVDF) flat sheet hydrophobic membranes. The design of the membrane module proved its applicability for achieving a high heat transfer coefficient of the order of 103 (W/m2 K) and a high Reynolds number (Re). VMD experiments were conducted to measure the heat and mass transfer coefficients within the membrane module. The effects of the process parameters, such as the feed temperature, feed flow rate, vacuum degree, and feed concentration, on the permeate flux have been investigated. The feed temperature, feed flow rate, and vacuum degree play an important role in enhancing the performance of the VMD process; therefore, optimizing all of these parameters is the best way to achieve a high permeate flux. The PTFE membrane showed better performance than the PVDF membrane in VMD desalination. The obtained water flux is relatively high compared to that reported in the literature, reaching 43.8 and 52.6 (kg/m2 h) for PVDF and PTFE, respectively. The salt rejection of NaCl was higher than 99% for both membranes.http://dx.doi.org/10.1155/2016/9378460
spellingShingle Adnan Alhathal Alanezi
H. Abdallah
E. El-Zanati
Adnan Ahmad
Adel O. Sharif
Performance Investigation of O-Ring Vacuum Membrane Distillation Module for Water Desalination
Journal of Chemistry
title Performance Investigation of O-Ring Vacuum Membrane Distillation Module for Water Desalination
title_full Performance Investigation of O-Ring Vacuum Membrane Distillation Module for Water Desalination
title_fullStr Performance Investigation of O-Ring Vacuum Membrane Distillation Module for Water Desalination
title_full_unstemmed Performance Investigation of O-Ring Vacuum Membrane Distillation Module for Water Desalination
title_short Performance Investigation of O-Ring Vacuum Membrane Distillation Module for Water Desalination
title_sort performance investigation of o ring vacuum membrane distillation module for water desalination
url http://dx.doi.org/10.1155/2016/9378460
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AT adnanahmad performanceinvestigationoforingvacuummembranedistillationmoduleforwaterdesalination
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