Investigation on detachable vertical tube evaporator for small scale multi effect distillation system: Design, modelling, fabrication and experimental analysis
Design and experimental performance of a detachable shell vertical tube evaporator with variation in feed water temperature is performed. The modified evaporator operates with a thin film of evaporating feed water on the outer surface of fluted tubes, resulting in high heat transfer coefficient for...
Ausführliche Beschreibung
Gespeichert in:
| Autor*in: |
Deharkar, Rahul [verfasserIn] |
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| Format: |
E-Artikel |
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| Sprache: |
Englisch |
| Erschienen: |
2022 |
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| Schlagwörter: |
Falling film outside fluted tubes |
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| Systematik: |
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| Anmerkung: |
© The Author(s), under exclusive licence to Springer-Verlag GmbH Germany, part of Springer Nature 2022 |
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| Übergeordnetes Werk: |
Enthalten in: Heat and mass transfer - Springer Berlin Heidelberg, 1968, 58(2022), 8 vom: 01. März, Seite 1441-1458 |
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| Übergeordnetes Werk: |
volume:58 ; year:2022 ; number:8 ; day:01 ; month:03 ; pages:1441-1458 |
| Links: |
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| DOI / URN: |
10.1007/s00231-022-03185-3 |
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| Katalog-ID: |
OLC2131318332 |
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| 520 | |a Design and experimental performance of a detachable shell vertical tube evaporator with variation in feed water temperature is performed. The modified evaporator operates with a thin film of evaporating feed water on the outer surface of fluted tubes, resulting in high heat transfer coefficient for performance. Also, salt deposits on the outer surface, make the system easy for cleaning and maintenance. A detachable outer shell further allows ease for tubes maintenance. Baby boiler and parabolic dish collector together producing 30 kg/hr steam were installed with the pilot plant for experimental study. Experimentation of the evaporator as single effect with condenser system recorded a mean heat transfer coefficient of 9446 W/$ m^{2} $K at gain output ratio of 1.8 ± 0.02 for feed inlet temperature, motive steam pressure and temperature in at 100 °C, 1.3 ± 0.028 bar and 103 ± 0.5 °C respectively. The pilot plant with a single effect produce a maximum of 1282 L/day at fresh water cost of 1.05 $/$ m^{3} $. Theoretical Model for multi effect system in parallel feed flow configuration estimates lowest freshwater cost of 0.73 $/$ m^{3} $ and total production of 2668 L/day with 4 effect system. Graphical abstract | ||
| 650 | 4 | |a Detachable shell | |
| 650 | 4 | |a Vertical tube evaporator | |
| 650 | 4 | |a Falling film outside fluted tubes | |
| 650 | 4 | |a Small-scale multi-effect distillation | |
| 650 | 4 | |a Experimental performance | |
| 700 | 1 | |a Mudgal, Anurag |0 (orcid)0000-0001-6888-4664 |4 aut | |
| 700 | 1 | |a Patel, Vivek |4 aut | |
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10.1007/s00231-022-03185-3 doi (DE-627)OLC2131318332 (DE-He213)s00231-022-03185-3-e DE-627 ger DE-627 rakwb eng 530 620 VZ ELIB31 VZ rvk ELIB41 VZ rvk 58.13$jThermische Verfahrenstechnik bkl 50.38$jTechnische Thermodynamik bkl Deharkar, Rahul verfasserin aut Investigation on detachable vertical tube evaporator for small scale multi effect distillation system: Design, modelling, fabrication and experimental analysis 2022 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © The Author(s), under exclusive licence to Springer-Verlag GmbH Germany, part of Springer Nature 2022 Design and experimental performance of a detachable shell vertical tube evaporator with variation in feed water temperature is performed. The modified evaporator operates with a thin film of evaporating feed water on the outer surface of fluted tubes, resulting in high heat transfer coefficient for performance. Also, salt deposits on the outer surface, make the system easy for cleaning and maintenance. A detachable outer shell further allows ease for tubes maintenance. Baby boiler and parabolic dish collector together producing 30 kg/hr steam were installed with the pilot plant for experimental study. Experimentation of the evaporator as single effect with condenser system recorded a mean heat transfer coefficient of 9446 W/$ m^{2} $K at gain output ratio of 1.8 ± 0.02 for feed inlet temperature, motive steam pressure and temperature in at 100 °C, 1.3 ± 0.028 bar and 103 ± 0.5 °C respectively. The pilot plant with a single effect produce a maximum of 1282 L/day at fresh water cost of 1.05 $/$ m^{3} $. Theoretical Model for multi effect system in parallel feed flow configuration estimates lowest freshwater cost of 0.73 $/$ m^{3} $ and total production of 2668 L/day with 4 effect system. Graphical abstract Detachable shell Vertical tube evaporator Falling film outside fluted tubes Small-scale multi-effect distillation Experimental performance Mudgal, Anurag (orcid)0000-0001-6888-4664 aut Patel, Vivek aut Enthalten in Heat and mass transfer Springer Berlin Heidelberg, 1968 58(2022), 8 vom: 01. März, Seite 1441-1458 Online-Ressource (DE-627)27012635X (DE-600)1476367-9 (DE-576)078128927 1432-1181 nnns volume:58 year:2022 number:8 day:01 month:03 pages:1441-1458 https://dx.doi.org/10.1007/s00231-022-03185-3 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-TEC SSG-OLC-PHY 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_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_101 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_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_250 GBV_ILN_267 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_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_2118 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_4126 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_4328 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 ELIB31 ELIB41 58.13$jThermische Verfahrenstechnik VZ 181570548 (DE-625)181570548 50.38$jTechnische Thermodynamik VZ 106420534 (DE-625)106420534 AR 58 2022 8 01 03 1441-1458 |
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10.1007/s00231-022-03185-3 doi (DE-627)OLC2131318332 (DE-He213)s00231-022-03185-3-e DE-627 ger DE-627 rakwb eng 530 620 VZ ELIB31 VZ rvk ELIB41 VZ rvk 58.13$jThermische Verfahrenstechnik bkl 50.38$jTechnische Thermodynamik bkl Deharkar, Rahul verfasserin aut Investigation on detachable vertical tube evaporator for small scale multi effect distillation system: Design, modelling, fabrication and experimental analysis 2022 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © The Author(s), under exclusive licence to Springer-Verlag GmbH Germany, part of Springer Nature 2022 Design and experimental performance of a detachable shell vertical tube evaporator with variation in feed water temperature is performed. The modified evaporator operates with a thin film of evaporating feed water on the outer surface of fluted tubes, resulting in high heat transfer coefficient for performance. Also, salt deposits on the outer surface, make the system easy for cleaning and maintenance. A detachable outer shell further allows ease for tubes maintenance. Baby boiler and parabolic dish collector together producing 30 kg/hr steam were installed with the pilot plant for experimental study. Experimentation of the evaporator as single effect with condenser system recorded a mean heat transfer coefficient of 9446 W/$ m^{2} $K at gain output ratio of 1.8 ± 0.02 for feed inlet temperature, motive steam pressure and temperature in at 100 °C, 1.3 ± 0.028 bar and 103 ± 0.5 °C respectively. The pilot plant with a single effect produce a maximum of 1282 L/day at fresh water cost of 1.05 $/$ m^{3} $. Theoretical Model for multi effect system in parallel feed flow configuration estimates lowest freshwater cost of 0.73 $/$ m^{3} $ and total production of 2668 L/day with 4 effect system. Graphical abstract Detachable shell Vertical tube evaporator Falling film outside fluted tubes Small-scale multi-effect distillation Experimental performance Mudgal, Anurag (orcid)0000-0001-6888-4664 aut Patel, Vivek aut Enthalten in Heat and mass transfer Springer Berlin Heidelberg, 1968 58(2022), 8 vom: 01. März, Seite 1441-1458 Online-Ressource (DE-627)27012635X (DE-600)1476367-9 (DE-576)078128927 1432-1181 nnns volume:58 year:2022 number:8 day:01 month:03 pages:1441-1458 https://dx.doi.org/10.1007/s00231-022-03185-3 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-TEC SSG-OLC-PHY 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_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_101 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_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_250 GBV_ILN_267 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_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_2118 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_4126 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_4328 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 ELIB31 ELIB41 58.13$jThermische Verfahrenstechnik VZ 181570548 (DE-625)181570548 50.38$jTechnische Thermodynamik VZ 106420534 (DE-625)106420534 AR 58 2022 8 01 03 1441-1458 |
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10.1007/s00231-022-03185-3 doi (DE-627)OLC2131318332 (DE-He213)s00231-022-03185-3-e DE-627 ger DE-627 rakwb eng 530 620 VZ ELIB31 VZ rvk ELIB41 VZ rvk 58.13$jThermische Verfahrenstechnik bkl 50.38$jTechnische Thermodynamik bkl Deharkar, Rahul verfasserin aut Investigation on detachable vertical tube evaporator for small scale multi effect distillation system: Design, modelling, fabrication and experimental analysis 2022 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © The Author(s), under exclusive licence to Springer-Verlag GmbH Germany, part of Springer Nature 2022 Design and experimental performance of a detachable shell vertical tube evaporator with variation in feed water temperature is performed. The modified evaporator operates with a thin film of evaporating feed water on the outer surface of fluted tubes, resulting in high heat transfer coefficient for performance. Also, salt deposits on the outer surface, make the system easy for cleaning and maintenance. A detachable outer shell further allows ease for tubes maintenance. Baby boiler and parabolic dish collector together producing 30 kg/hr steam were installed with the pilot plant for experimental study. Experimentation of the evaporator as single effect with condenser system recorded a mean heat transfer coefficient of 9446 W/$ m^{2} $K at gain output ratio of 1.8 ± 0.02 for feed inlet temperature, motive steam pressure and temperature in at 100 °C, 1.3 ± 0.028 bar and 103 ± 0.5 °C respectively. The pilot plant with a single effect produce a maximum of 1282 L/day at fresh water cost of 1.05 $/$ m^{3} $. Theoretical Model for multi effect system in parallel feed flow configuration estimates lowest freshwater cost of 0.73 $/$ m^{3} $ and total production of 2668 L/day with 4 effect system. Graphical abstract Detachable shell Vertical tube evaporator Falling film outside fluted tubes Small-scale multi-effect distillation Experimental performance Mudgal, Anurag (orcid)0000-0001-6888-4664 aut Patel, Vivek aut Enthalten in Heat and mass transfer Springer Berlin Heidelberg, 1968 58(2022), 8 vom: 01. März, Seite 1441-1458 Online-Ressource (DE-627)27012635X (DE-600)1476367-9 (DE-576)078128927 1432-1181 nnns volume:58 year:2022 number:8 day:01 month:03 pages:1441-1458 https://dx.doi.org/10.1007/s00231-022-03185-3 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-TEC SSG-OLC-PHY 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_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_101 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_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_250 GBV_ILN_267 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_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_2118 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_4126 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_4328 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 ELIB31 ELIB41 58.13$jThermische Verfahrenstechnik VZ 181570548 (DE-625)181570548 50.38$jTechnische Thermodynamik VZ 106420534 (DE-625)106420534 AR 58 2022 8 01 03 1441-1458 |
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10.1007/s00231-022-03185-3 doi (DE-627)OLC2131318332 (DE-He213)s00231-022-03185-3-e DE-627 ger DE-627 rakwb eng 530 620 VZ ELIB31 VZ rvk ELIB41 VZ rvk 58.13$jThermische Verfahrenstechnik bkl 50.38$jTechnische Thermodynamik bkl Deharkar, Rahul verfasserin aut Investigation on detachable vertical tube evaporator for small scale multi effect distillation system: Design, modelling, fabrication and experimental analysis 2022 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © The Author(s), under exclusive licence to Springer-Verlag GmbH Germany, part of Springer Nature 2022 Design and experimental performance of a detachable shell vertical tube evaporator with variation in feed water temperature is performed. The modified evaporator operates with a thin film of evaporating feed water on the outer surface of fluted tubes, resulting in high heat transfer coefficient for performance. Also, salt deposits on the outer surface, make the system easy for cleaning and maintenance. A detachable outer shell further allows ease for tubes maintenance. Baby boiler and parabolic dish collector together producing 30 kg/hr steam were installed with the pilot plant for experimental study. Experimentation of the evaporator as single effect with condenser system recorded a mean heat transfer coefficient of 9446 W/$ m^{2} $K at gain output ratio of 1.8 ± 0.02 for feed inlet temperature, motive steam pressure and temperature in at 100 °C, 1.3 ± 0.028 bar and 103 ± 0.5 °C respectively. The pilot plant with a single effect produce a maximum of 1282 L/day at fresh water cost of 1.05 $/$ m^{3} $. Theoretical Model for multi effect system in parallel feed flow configuration estimates lowest freshwater cost of 0.73 $/$ m^{3} $ and total production of 2668 L/day with 4 effect system. Graphical abstract Detachable shell Vertical tube evaporator Falling film outside fluted tubes Small-scale multi-effect distillation Experimental performance Mudgal, Anurag (orcid)0000-0001-6888-4664 aut Patel, Vivek aut Enthalten in Heat and mass transfer Springer Berlin Heidelberg, 1968 58(2022), 8 vom: 01. März, Seite 1441-1458 Online-Ressource (DE-627)27012635X (DE-600)1476367-9 (DE-576)078128927 1432-1181 nnns volume:58 year:2022 number:8 day:01 month:03 pages:1441-1458 https://dx.doi.org/10.1007/s00231-022-03185-3 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-TEC SSG-OLC-PHY 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_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_101 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_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_250 GBV_ILN_267 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_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_2118 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_4126 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_4328 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 ELIB31 ELIB41 58.13$jThermische Verfahrenstechnik VZ 181570548 (DE-625)181570548 50.38$jTechnische Thermodynamik VZ 106420534 (DE-625)106420534 AR 58 2022 8 01 03 1441-1458 |
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10.1007/s00231-022-03185-3 doi (DE-627)OLC2131318332 (DE-He213)s00231-022-03185-3-e DE-627 ger DE-627 rakwb eng 530 620 VZ ELIB31 VZ rvk ELIB41 VZ rvk 58.13$jThermische Verfahrenstechnik bkl 50.38$jTechnische Thermodynamik bkl Deharkar, Rahul verfasserin aut Investigation on detachable vertical tube evaporator for small scale multi effect distillation system: Design, modelling, fabrication and experimental analysis 2022 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © The Author(s), under exclusive licence to Springer-Verlag GmbH Germany, part of Springer Nature 2022 Design and experimental performance of a detachable shell vertical tube evaporator with variation in feed water temperature is performed. The modified evaporator operates with a thin film of evaporating feed water on the outer surface of fluted tubes, resulting in high heat transfer coefficient for performance. Also, salt deposits on the outer surface, make the system easy for cleaning and maintenance. A detachable outer shell further allows ease for tubes maintenance. Baby boiler and parabolic dish collector together producing 30 kg/hr steam were installed with the pilot plant for experimental study. Experimentation of the evaporator as single effect with condenser system recorded a mean heat transfer coefficient of 9446 W/$ m^{2} $K at gain output ratio of 1.8 ± 0.02 for feed inlet temperature, motive steam pressure and temperature in at 100 °C, 1.3 ± 0.028 bar and 103 ± 0.5 °C respectively. The pilot plant with a single effect produce a maximum of 1282 L/day at fresh water cost of 1.05 $/$ m^{3} $. Theoretical Model for multi effect system in parallel feed flow configuration estimates lowest freshwater cost of 0.73 $/$ m^{3} $ and total production of 2668 L/day with 4 effect system. Graphical abstract Detachable shell Vertical tube evaporator Falling film outside fluted tubes Small-scale multi-effect distillation Experimental performance Mudgal, Anurag (orcid)0000-0001-6888-4664 aut Patel, Vivek aut Enthalten in Heat and mass transfer Springer Berlin Heidelberg, 1968 58(2022), 8 vom: 01. März, Seite 1441-1458 Online-Ressource (DE-627)27012635X (DE-600)1476367-9 (DE-576)078128927 1432-1181 nnns volume:58 year:2022 number:8 day:01 month:03 pages:1441-1458 https://dx.doi.org/10.1007/s00231-022-03185-3 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-TEC SSG-OLC-PHY 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_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_101 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_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_250 GBV_ILN_267 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_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_2118 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_4126 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_4328 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 ELIB31 ELIB41 58.13$jThermische Verfahrenstechnik VZ 181570548 (DE-625)181570548 50.38$jTechnische Thermodynamik VZ 106420534 (DE-625)106420534 AR 58 2022 8 01 03 1441-1458 |
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Enthalten in Heat and mass transfer 58(2022), 8 vom: 01. März, Seite 1441-1458 volume:58 year:2022 number:8 day:01 month:03 pages:1441-1458 |
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The modified evaporator operates with a thin film of evaporating feed water on the outer surface of fluted tubes, resulting in high heat transfer coefficient for performance. Also, salt deposits on the outer surface, make the system easy for cleaning and maintenance. A detachable outer shell further allows ease for tubes maintenance. Baby boiler and parabolic dish collector together producing 30 kg/hr steam were installed with the pilot plant for experimental study. Experimentation of the evaporator as single effect with condenser system recorded a mean heat transfer coefficient of 9446 W/$ m^{2} $K at gain output ratio of 1.8 ± 0.02 for feed inlet temperature, motive steam pressure and temperature in at 100 °C, 1.3 ± 0.028 bar and 103 ± 0.5 °C respectively. The pilot plant with a single effect produce a maximum of 1282 L/day at fresh water cost of 1.05 $/$ m^{3} $. Theoretical Model for multi effect system in parallel feed flow configuration estimates lowest freshwater cost of 0.73 $/$ m^{3} $ and total production of 2668 L/day with 4 effect system. 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Deharkar, Rahul |
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Deharkar, Rahul ddc 530 rvk ELIB31 rvk ELIB41 bkl 58.13$jThermische Verfahrenstechnik bkl 50.38$jTechnische Thermodynamik misc Detachable shell misc Vertical tube evaporator misc Falling film outside fluted tubes misc Small-scale multi-effect distillation misc Experimental performance Investigation on detachable vertical tube evaporator for small scale multi effect distillation system: Design, modelling, fabrication and experimental analysis |
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530 620 VZ ELIB31 VZ rvk ELIB41 VZ rvk 58.13$jThermische Verfahrenstechnik bkl 50.38$jTechnische Thermodynamik bkl Investigation on detachable vertical tube evaporator for small scale multi effect distillation system: Design, modelling, fabrication and experimental analysis Detachable shell Vertical tube evaporator Falling film outside fluted tubes Small-scale multi-effect distillation Experimental performance |
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ddc 530 rvk ELIB31 rvk ELIB41 bkl 58.13$jThermische Verfahrenstechnik bkl 50.38$jTechnische Thermodynamik misc Detachable shell misc Vertical tube evaporator misc Falling film outside fluted tubes misc Small-scale multi-effect distillation misc Experimental performance |
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Investigation on detachable vertical tube evaporator for small scale multi effect distillation system: Design, modelling, fabrication and experimental analysis |
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Deharkar, Rahul |
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Deharkar, Rahul Mudgal, Anurag Patel, Vivek |
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Deharkar, Rahul |
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10.1007/s00231-022-03185-3 |
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investigation on detachable vertical tube evaporator for small scale multi effect distillation system: design, modelling, fabrication and experimental analysis |
| title_auth |
Investigation on detachable vertical tube evaporator for small scale multi effect distillation system: Design, modelling, fabrication and experimental analysis |
| abstract |
Design and experimental performance of a detachable shell vertical tube evaporator with variation in feed water temperature is performed. The modified evaporator operates with a thin film of evaporating feed water on the outer surface of fluted tubes, resulting in high heat transfer coefficient for performance. Also, salt deposits on the outer surface, make the system easy for cleaning and maintenance. A detachable outer shell further allows ease for tubes maintenance. Baby boiler and parabolic dish collector together producing 30 kg/hr steam were installed with the pilot plant for experimental study. Experimentation of the evaporator as single effect with condenser system recorded a mean heat transfer coefficient of 9446 W/$ m^{2} $K at gain output ratio of 1.8 ± 0.02 for feed inlet temperature, motive steam pressure and temperature in at 100 °C, 1.3 ± 0.028 bar and 103 ± 0.5 °C respectively. The pilot plant with a single effect produce a maximum of 1282 L/day at fresh water cost of 1.05 $/$ m^{3} $. Theoretical Model for multi effect system in parallel feed flow configuration estimates lowest freshwater cost of 0.73 $/$ m^{3} $ and total production of 2668 L/day with 4 effect system. Graphical abstract © The Author(s), under exclusive licence to Springer-Verlag GmbH Germany, part of Springer Nature 2022 |
| abstractGer |
Design and experimental performance of a detachable shell vertical tube evaporator with variation in feed water temperature is performed. The modified evaporator operates with a thin film of evaporating feed water on the outer surface of fluted tubes, resulting in high heat transfer coefficient for performance. Also, salt deposits on the outer surface, make the system easy for cleaning and maintenance. A detachable outer shell further allows ease for tubes maintenance. Baby boiler and parabolic dish collector together producing 30 kg/hr steam were installed with the pilot plant for experimental study. Experimentation of the evaporator as single effect with condenser system recorded a mean heat transfer coefficient of 9446 W/$ m^{2} $K at gain output ratio of 1.8 ± 0.02 for feed inlet temperature, motive steam pressure and temperature in at 100 °C, 1.3 ± 0.028 bar and 103 ± 0.5 °C respectively. The pilot plant with a single effect produce a maximum of 1282 L/day at fresh water cost of 1.05 $/$ m^{3} $. Theoretical Model for multi effect system in parallel feed flow configuration estimates lowest freshwater cost of 0.73 $/$ m^{3} $ and total production of 2668 L/day with 4 effect system. Graphical abstract © The Author(s), under exclusive licence to Springer-Verlag GmbH Germany, part of Springer Nature 2022 |
| abstract_unstemmed |
Design and experimental performance of a detachable shell vertical tube evaporator with variation in feed water temperature is performed. The modified evaporator operates with a thin film of evaporating feed water on the outer surface of fluted tubes, resulting in high heat transfer coefficient for performance. Also, salt deposits on the outer surface, make the system easy for cleaning and maintenance. A detachable outer shell further allows ease for tubes maintenance. Baby boiler and parabolic dish collector together producing 30 kg/hr steam were installed with the pilot plant for experimental study. Experimentation of the evaporator as single effect with condenser system recorded a mean heat transfer coefficient of 9446 W/$ m^{2} $K at gain output ratio of 1.8 ± 0.02 for feed inlet temperature, motive steam pressure and temperature in at 100 °C, 1.3 ± 0.028 bar and 103 ± 0.5 °C respectively. The pilot plant with a single effect produce a maximum of 1282 L/day at fresh water cost of 1.05 $/$ m^{3} $. Theoretical Model for multi effect system in parallel feed flow configuration estimates lowest freshwater cost of 0.73 $/$ m^{3} $ and total production of 2668 L/day with 4 effect system. Graphical abstract © The Author(s), under exclusive licence to Springer-Verlag GmbH Germany, part of Springer Nature 2022 |
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Investigation on detachable vertical tube evaporator for small scale multi effect distillation system: Design, modelling, fabrication and experimental analysis |
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