Optimization of membrane distillation (MD) technology for specific application desalination
Abstract The major desalination problem in remote rural areas is the management and disposal of the brine. Today, conventional desalination technologies known are detent multistage or multistage flash (MSF), the vapor compression (VC), distillation multiple effects (MED), and reverse osmosis. Techno...
Ausführliche Beschreibung
Autor*in: |
Boukhriss, Mokhless [verfasserIn] |
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Format: |
E-Artikel |
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Sprache: |
Englisch |
Erschienen: |
2016 |
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Schlagwörter: |
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Anmerkung: |
© Springer-Verlag London 2016 |
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Übergeordnetes Werk: |
Enthalten in: The international journal of advanced manufacturing technology - London : Springer, 1985, 88(2016), 1-4 vom: 20. Apr., Seite 55-66 |
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Übergeordnetes Werk: |
volume:88 ; year:2016 ; number:1-4 ; day:20 ; month:04 ; pages:55-66 |
Links: |
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DOI / URN: |
10.1007/s00170-016-8756-4 |
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Katalog-ID: |
SPR001900242 |
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520 | |a Abstract The major desalination problem in remote rural areas is the management and disposal of the brine. Today, conventional desalination technologies known are detent multistage or multistage flash (MSF), the vapor compression (VC), distillation multiple effects (MED), and reverse osmosis. Technology desalination of seawater in the presence of a membrane distillation unit driven by solar energy is a possible solution to reduce the energy costs of producing distilled water. The developed model is used to simulate the membrane distillation unit coupled with solar collector system in order to investigate the steady-state behavior of each component of the unit and the entire system exposed to a variation of the entrance parameters and meteorological conditions. The results obtained show the influence of external and internal parameters on the operating characteristics of the membrane distillation unit coupled with solar collector system. A global mathematical model based on heat and mass transfers is developed to investigate both the effect of different operating modes and the variation of functioning parameters and weather conditions on the freshwater production. | ||
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10.1007/s00170-016-8756-4 doi (DE-627)SPR001900242 (SPR)s00170-016-8756-4-e DE-627 ger DE-627 rakwb eng Boukhriss, Mokhless verfasserin aut Optimization of membrane distillation (MD) technology for specific application desalination 2016 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © Springer-Verlag London 2016 Abstract The major desalination problem in remote rural areas is the management and disposal of the brine. Today, conventional desalination technologies known are detent multistage or multistage flash (MSF), the vapor compression (VC), distillation multiple effects (MED), and reverse osmosis. Technology desalination of seawater in the presence of a membrane distillation unit driven by solar energy is a possible solution to reduce the energy costs of producing distilled water. The developed model is used to simulate the membrane distillation unit coupled with solar collector system in order to investigate the steady-state behavior of each component of the unit and the entire system exposed to a variation of the entrance parameters and meteorological conditions. The results obtained show the influence of external and internal parameters on the operating characteristics of the membrane distillation unit coupled with solar collector system. A global mathematical model based on heat and mass transfers is developed to investigate both the effect of different operating modes and the variation of functioning parameters and weather conditions on the freshwater production. Membrane distillation DCMD (dpeaa)DE-He213 Mass transfer (dpeaa)DE-He213 Heat transfer (dpeaa)DE-He213 Modeling (dpeaa)DE-He213 Simulation (dpeaa)DE-He213 Solar collector (dpeaa)DE-He213 Zhani, Khalifa aut Ben Bacha, Habib aut Enthalten in The international journal of advanced manufacturing technology London : Springer, 1985 88(2016), 1-4 vom: 20. Apr., Seite 55-66 (DE-627)270127712 (DE-600)1476510-X 1433-3015 nnns volume:88 year:2016 number:1-4 day:20 month:04 pages:55-66 https://dx.doi.org/10.1007/s00170-016-8756-4 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_105 GBV_ILN_110 GBV_ILN_120 GBV_ILN_138 GBV_ILN_150 GBV_ILN_151 GBV_ILN_152 GBV_ILN_161 GBV_ILN_170 GBV_ILN_171 GBV_ILN_187 GBV_ILN_206 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_250 GBV_ILN_281 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_636 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2007 GBV_ILN_2008 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2026 GBV_ILN_2027 GBV_ILN_2031 GBV_ILN_2034 GBV_ILN_2037 GBV_ILN_2038 GBV_ILN_2039 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2056 GBV_ILN_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2070 GBV_ILN_2086 GBV_ILN_2088 GBV_ILN_2093 GBV_ILN_2106 GBV_ILN_2107 GBV_ILN_2108 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2116 GBV_ILN_2118 GBV_ILN_2119 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2144 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2188 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2446 GBV_ILN_2470 GBV_ILN_2472 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_2548 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4242 GBV_ILN_4246 GBV_ILN_4249 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4326 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 AR 88 2016 1-4 20 04 55-66 |
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10.1007/s00170-016-8756-4 doi (DE-627)SPR001900242 (SPR)s00170-016-8756-4-e DE-627 ger DE-627 rakwb eng Boukhriss, Mokhless verfasserin aut Optimization of membrane distillation (MD) technology for specific application desalination 2016 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © Springer-Verlag London 2016 Abstract The major desalination problem in remote rural areas is the management and disposal of the brine. Today, conventional desalination technologies known are detent multistage or multistage flash (MSF), the vapor compression (VC), distillation multiple effects (MED), and reverse osmosis. Technology desalination of seawater in the presence of a membrane distillation unit driven by solar energy is a possible solution to reduce the energy costs of producing distilled water. The developed model is used to simulate the membrane distillation unit coupled with solar collector system in order to investigate the steady-state behavior of each component of the unit and the entire system exposed to a variation of the entrance parameters and meteorological conditions. The results obtained show the influence of external and internal parameters on the operating characteristics of the membrane distillation unit coupled with solar collector system. A global mathematical model based on heat and mass transfers is developed to investigate both the effect of different operating modes and the variation of functioning parameters and weather conditions on the freshwater production. Membrane distillation DCMD (dpeaa)DE-He213 Mass transfer (dpeaa)DE-He213 Heat transfer (dpeaa)DE-He213 Modeling (dpeaa)DE-He213 Simulation (dpeaa)DE-He213 Solar collector (dpeaa)DE-He213 Zhani, Khalifa aut Ben Bacha, Habib aut Enthalten in The international journal of advanced manufacturing technology London : Springer, 1985 88(2016), 1-4 vom: 20. Apr., Seite 55-66 (DE-627)270127712 (DE-600)1476510-X 1433-3015 nnns volume:88 year:2016 number:1-4 day:20 month:04 pages:55-66 https://dx.doi.org/10.1007/s00170-016-8756-4 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_105 GBV_ILN_110 GBV_ILN_120 GBV_ILN_138 GBV_ILN_150 GBV_ILN_151 GBV_ILN_152 GBV_ILN_161 GBV_ILN_170 GBV_ILN_171 GBV_ILN_187 GBV_ILN_206 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_250 GBV_ILN_281 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_636 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2007 GBV_ILN_2008 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2026 GBV_ILN_2027 GBV_ILN_2031 GBV_ILN_2034 GBV_ILN_2037 GBV_ILN_2038 GBV_ILN_2039 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2056 GBV_ILN_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2070 GBV_ILN_2086 GBV_ILN_2088 GBV_ILN_2093 GBV_ILN_2106 GBV_ILN_2107 GBV_ILN_2108 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2116 GBV_ILN_2118 GBV_ILN_2119 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2144 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2188 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2446 GBV_ILN_2470 GBV_ILN_2472 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_2548 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4242 GBV_ILN_4246 GBV_ILN_4249 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4326 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 AR 88 2016 1-4 20 04 55-66 |
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10.1007/s00170-016-8756-4 doi (DE-627)SPR001900242 (SPR)s00170-016-8756-4-e DE-627 ger DE-627 rakwb eng Boukhriss, Mokhless verfasserin aut Optimization of membrane distillation (MD) technology for specific application desalination 2016 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © Springer-Verlag London 2016 Abstract The major desalination problem in remote rural areas is the management and disposal of the brine. Today, conventional desalination technologies known are detent multistage or multistage flash (MSF), the vapor compression (VC), distillation multiple effects (MED), and reverse osmosis. Technology desalination of seawater in the presence of a membrane distillation unit driven by solar energy is a possible solution to reduce the energy costs of producing distilled water. The developed model is used to simulate the membrane distillation unit coupled with solar collector system in order to investigate the steady-state behavior of each component of the unit and the entire system exposed to a variation of the entrance parameters and meteorological conditions. The results obtained show the influence of external and internal parameters on the operating characteristics of the membrane distillation unit coupled with solar collector system. A global mathematical model based on heat and mass transfers is developed to investigate both the effect of different operating modes and the variation of functioning parameters and weather conditions on the freshwater production. Membrane distillation DCMD (dpeaa)DE-He213 Mass transfer (dpeaa)DE-He213 Heat transfer (dpeaa)DE-He213 Modeling (dpeaa)DE-He213 Simulation (dpeaa)DE-He213 Solar collector (dpeaa)DE-He213 Zhani, Khalifa aut Ben Bacha, Habib aut Enthalten in The international journal of advanced manufacturing technology London : Springer, 1985 88(2016), 1-4 vom: 20. Apr., Seite 55-66 (DE-627)270127712 (DE-600)1476510-X 1433-3015 nnns volume:88 year:2016 number:1-4 day:20 month:04 pages:55-66 https://dx.doi.org/10.1007/s00170-016-8756-4 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_105 GBV_ILN_110 GBV_ILN_120 GBV_ILN_138 GBV_ILN_150 GBV_ILN_151 GBV_ILN_152 GBV_ILN_161 GBV_ILN_170 GBV_ILN_171 GBV_ILN_187 GBV_ILN_206 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_250 GBV_ILN_281 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_636 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2007 GBV_ILN_2008 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2026 GBV_ILN_2027 GBV_ILN_2031 GBV_ILN_2034 GBV_ILN_2037 GBV_ILN_2038 GBV_ILN_2039 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2056 GBV_ILN_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2070 GBV_ILN_2086 GBV_ILN_2088 GBV_ILN_2093 GBV_ILN_2106 GBV_ILN_2107 GBV_ILN_2108 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2116 GBV_ILN_2118 GBV_ILN_2119 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2144 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2188 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2446 GBV_ILN_2470 GBV_ILN_2472 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_2548 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4242 GBV_ILN_4246 GBV_ILN_4249 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4326 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 AR 88 2016 1-4 20 04 55-66 |
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10.1007/s00170-016-8756-4 doi (DE-627)SPR001900242 (SPR)s00170-016-8756-4-e DE-627 ger DE-627 rakwb eng Boukhriss, Mokhless verfasserin aut Optimization of membrane distillation (MD) technology for specific application desalination 2016 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © Springer-Verlag London 2016 Abstract The major desalination problem in remote rural areas is the management and disposal of the brine. Today, conventional desalination technologies known are detent multistage or multistage flash (MSF), the vapor compression (VC), distillation multiple effects (MED), and reverse osmosis. Technology desalination of seawater in the presence of a membrane distillation unit driven by solar energy is a possible solution to reduce the energy costs of producing distilled water. The developed model is used to simulate the membrane distillation unit coupled with solar collector system in order to investigate the steady-state behavior of each component of the unit and the entire system exposed to a variation of the entrance parameters and meteorological conditions. The results obtained show the influence of external and internal parameters on the operating characteristics of the membrane distillation unit coupled with solar collector system. A global mathematical model based on heat and mass transfers is developed to investigate both the effect of different operating modes and the variation of functioning parameters and weather conditions on the freshwater production. Membrane distillation DCMD (dpeaa)DE-He213 Mass transfer (dpeaa)DE-He213 Heat transfer (dpeaa)DE-He213 Modeling (dpeaa)DE-He213 Simulation (dpeaa)DE-He213 Solar collector (dpeaa)DE-He213 Zhani, Khalifa aut Ben Bacha, Habib aut Enthalten in The international journal of advanced manufacturing technology London : Springer, 1985 88(2016), 1-4 vom: 20. Apr., Seite 55-66 (DE-627)270127712 (DE-600)1476510-X 1433-3015 nnns volume:88 year:2016 number:1-4 day:20 month:04 pages:55-66 https://dx.doi.org/10.1007/s00170-016-8756-4 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_105 GBV_ILN_110 GBV_ILN_120 GBV_ILN_138 GBV_ILN_150 GBV_ILN_151 GBV_ILN_152 GBV_ILN_161 GBV_ILN_170 GBV_ILN_171 GBV_ILN_187 GBV_ILN_206 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_250 GBV_ILN_281 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_636 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2007 GBV_ILN_2008 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2026 GBV_ILN_2027 GBV_ILN_2031 GBV_ILN_2034 GBV_ILN_2037 GBV_ILN_2038 GBV_ILN_2039 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2056 GBV_ILN_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2070 GBV_ILN_2086 GBV_ILN_2088 GBV_ILN_2093 GBV_ILN_2106 GBV_ILN_2107 GBV_ILN_2108 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2116 GBV_ILN_2118 GBV_ILN_2119 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2144 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2188 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2446 GBV_ILN_2470 GBV_ILN_2472 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_2548 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4242 GBV_ILN_4246 GBV_ILN_4249 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4326 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 AR 88 2016 1-4 20 04 55-66 |
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10.1007/s00170-016-8756-4 doi (DE-627)SPR001900242 (SPR)s00170-016-8756-4-e DE-627 ger DE-627 rakwb eng Boukhriss, Mokhless verfasserin aut Optimization of membrane distillation (MD) technology for specific application desalination 2016 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © Springer-Verlag London 2016 Abstract The major desalination problem in remote rural areas is the management and disposal of the brine. Today, conventional desalination technologies known are detent multistage or multistage flash (MSF), the vapor compression (VC), distillation multiple effects (MED), and reverse osmosis. Technology desalination of seawater in the presence of a membrane distillation unit driven by solar energy is a possible solution to reduce the energy costs of producing distilled water. The developed model is used to simulate the membrane distillation unit coupled with solar collector system in order to investigate the steady-state behavior of each component of the unit and the entire system exposed to a variation of the entrance parameters and meteorological conditions. The results obtained show the influence of external and internal parameters on the operating characteristics of the membrane distillation unit coupled with solar collector system. A global mathematical model based on heat and mass transfers is developed to investigate both the effect of different operating modes and the variation of functioning parameters and weather conditions on the freshwater production. Membrane distillation DCMD (dpeaa)DE-He213 Mass transfer (dpeaa)DE-He213 Heat transfer (dpeaa)DE-He213 Modeling (dpeaa)DE-He213 Simulation (dpeaa)DE-He213 Solar collector (dpeaa)DE-He213 Zhani, Khalifa aut Ben Bacha, Habib aut Enthalten in The international journal of advanced manufacturing technology London : Springer, 1985 88(2016), 1-4 vom: 20. Apr., Seite 55-66 (DE-627)270127712 (DE-600)1476510-X 1433-3015 nnns volume:88 year:2016 number:1-4 day:20 month:04 pages:55-66 https://dx.doi.org/10.1007/s00170-016-8756-4 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_105 GBV_ILN_110 GBV_ILN_120 GBV_ILN_138 GBV_ILN_150 GBV_ILN_151 GBV_ILN_152 GBV_ILN_161 GBV_ILN_170 GBV_ILN_171 GBV_ILN_187 GBV_ILN_206 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_250 GBV_ILN_281 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_636 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2007 GBV_ILN_2008 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2026 GBV_ILN_2027 GBV_ILN_2031 GBV_ILN_2034 GBV_ILN_2037 GBV_ILN_2038 GBV_ILN_2039 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2056 GBV_ILN_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2070 GBV_ILN_2086 GBV_ILN_2088 GBV_ILN_2093 GBV_ILN_2106 GBV_ILN_2107 GBV_ILN_2108 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2116 GBV_ILN_2118 GBV_ILN_2119 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2144 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2188 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2446 GBV_ILN_2470 GBV_ILN_2472 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_2548 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4242 GBV_ILN_4246 GBV_ILN_4249 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4326 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 AR 88 2016 1-4 20 04 55-66 |
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Optimization of membrane distillation (MD) technology for specific application desalination Membrane distillation DCMD (dpeaa)DE-He213 Mass transfer (dpeaa)DE-He213 Heat transfer (dpeaa)DE-He213 Modeling (dpeaa)DE-He213 Simulation (dpeaa)DE-He213 Solar collector (dpeaa)DE-He213 |
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optimization of membrane distillation (md) technology for specific application desalination |
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Optimization of membrane distillation (MD) technology for specific application desalination |
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Abstract The major desalination problem in remote rural areas is the management and disposal of the brine. Today, conventional desalination technologies known are detent multistage or multistage flash (MSF), the vapor compression (VC), distillation multiple effects (MED), and reverse osmosis. Technology desalination of seawater in the presence of a membrane distillation unit driven by solar energy is a possible solution to reduce the energy costs of producing distilled water. The developed model is used to simulate the membrane distillation unit coupled with solar collector system in order to investigate the steady-state behavior of each component of the unit and the entire system exposed to a variation of the entrance parameters and meteorological conditions. The results obtained show the influence of external and internal parameters on the operating characteristics of the membrane distillation unit coupled with solar collector system. A global mathematical model based on heat and mass transfers is developed to investigate both the effect of different operating modes and the variation of functioning parameters and weather conditions on the freshwater production. © Springer-Verlag London 2016 |
abstractGer |
Abstract The major desalination problem in remote rural areas is the management and disposal of the brine. Today, conventional desalination technologies known are detent multistage or multistage flash (MSF), the vapor compression (VC), distillation multiple effects (MED), and reverse osmosis. Technology desalination of seawater in the presence of a membrane distillation unit driven by solar energy is a possible solution to reduce the energy costs of producing distilled water. The developed model is used to simulate the membrane distillation unit coupled with solar collector system in order to investigate the steady-state behavior of each component of the unit and the entire system exposed to a variation of the entrance parameters and meteorological conditions. The results obtained show the influence of external and internal parameters on the operating characteristics of the membrane distillation unit coupled with solar collector system. A global mathematical model based on heat and mass transfers is developed to investigate both the effect of different operating modes and the variation of functioning parameters and weather conditions on the freshwater production. © Springer-Verlag London 2016 |
abstract_unstemmed |
Abstract The major desalination problem in remote rural areas is the management and disposal of the brine. Today, conventional desalination technologies known are detent multistage or multistage flash (MSF), the vapor compression (VC), distillation multiple effects (MED), and reverse osmosis. Technology desalination of seawater in the presence of a membrane distillation unit driven by solar energy is a possible solution to reduce the energy costs of producing distilled water. The developed model is used to simulate the membrane distillation unit coupled with solar collector system in order to investigate the steady-state behavior of each component of the unit and the entire system exposed to a variation of the entrance parameters and meteorological conditions. The results obtained show the influence of external and internal parameters on the operating characteristics of the membrane distillation unit coupled with solar collector system. A global mathematical model based on heat and mass transfers is developed to investigate both the effect of different operating modes and the variation of functioning parameters and weather conditions on the freshwater production. © Springer-Verlag London 2016 |
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Optimization of membrane distillation (MD) technology for specific application desalination |
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Today, conventional desalination technologies known are detent multistage or multistage flash (MSF), the vapor compression (VC), distillation multiple effects (MED), and reverse osmosis. Technology desalination of seawater in the presence of a membrane distillation unit driven by solar energy is a possible solution to reduce the energy costs of producing distilled water. The developed model is used to simulate the membrane distillation unit coupled with solar collector system in order to investigate the steady-state behavior of each component of the unit and the entire system exposed to a variation of the entrance parameters and meteorological conditions. The results obtained show the influence of external and internal parameters on the operating characteristics of the membrane distillation unit coupled with solar collector system. A global mathematical model based on heat and mass transfers is developed to investigate both the effect of different operating modes and the variation of functioning parameters and weather conditions on the freshwater production.</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">Membrane distillation DCMD</subfield><subfield code="7">(dpeaa)DE-He213</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">Mass transfer</subfield><subfield code="7">(dpeaa)DE-He213</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">Heat transfer</subfield><subfield code="7">(dpeaa)DE-He213</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">Modeling</subfield><subfield code="7">(dpeaa)DE-He213</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">Simulation</subfield><subfield code="7">(dpeaa)DE-He213</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">Solar collector</subfield><subfield code="7">(dpeaa)DE-He213</subfield></datafield><datafield tag="700" ind1="1" ind2=" "><subfield code="a">Zhani, Khalifa</subfield><subfield code="4">aut</subfield></datafield><datafield tag="700" ind1="1" ind2=" "><subfield code="a">Ben Bacha, Habib</subfield><subfield code="4">aut</subfield></datafield><datafield tag="773" ind1="0" ind2="8"><subfield code="i">Enthalten in</subfield><subfield code="t">The international journal of advanced manufacturing technology</subfield><subfield code="d">London : Springer, 1985</subfield><subfield code="g">88(2016), 1-4 vom: 20. 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