Electrochemical treatment of water containing chlorides under non-ideal flow conditions with BDD anodes
Abstract In this work a undivided parallel plate cell equipped with boron doped diamond (BDD) anode was tested as electrochemical reactor for disinfection of water. Two configurations were adopted: a single pass configuration (SPC) and a recirculated configuration (RC) in which also a reservoir was...
Ausführliche Beschreibung
Gespeichert in:
| Autor*in: |
Vacca, A. [verfasserIn] Mascia, M. [verfasserIn] Palmas, S. [verfasserIn] Da Pozzo, A. [verfasserIn] |
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| Format: |
E-Artikel |
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| Sprache: |
Englisch |
| Erschienen: |
2011 |
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| Schlagwörter: |
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| Übergeordnetes Werk: |
Enthalten in: Journal of applied electrochemistry - Dordrecht [u.a.] : Springer Science + Business Media B.V, 1971, 41(2011), 9 vom: 15. März, Seite 1087-1097 |
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| Übergeordnetes Werk: |
volume:41 ; year:2011 ; number:9 ; day:15 ; month:03 ; pages:1087-1097 |
| Links: |
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| DOI / URN: |
10.1007/s10800-011-0274-3 |
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| Katalog-ID: |
SPR013309013 |
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| 520 | |a Abstract In this work a undivided parallel plate cell equipped with boron doped diamond (BDD) anode was tested as electrochemical reactor for disinfection of water. Two configurations were adopted: a single pass configuration (SPC) and a recirculated configuration (RC) in which also a reservoir was inserted in the hydraulic circuit. In both the experimental configurations the system worked in continuous mode with a flow rate ranging from 0.05 to 0.42 $ dm^{3} $ $ min^{−1} $; in the RC the recirculating flow rate ranged from 0.45 to 6 $ dm^{3} $ $ min^{−1} $. Thermostated (25 °C) galvanostatic electrolyses were carried out with aqueous solutions containing 100 mg $ dm^{−3} $ of chloride ions: values of current density from 2.5 to 5.0 mA $ cm^{−2} $ were used. Steady state data revealed that active chlorine and chlorate ions were the main oxidation products. Particular attention was paid to the hydrodynamics both for SPC and RC: pulse-response curves were experimentally obtained with an inert tracer, and the behaviour of the system was interpreted by models based on a combination of ideal flow reactors, bypass flow elements, and dead zones. The hydrodynamic models were utilized to predict the outlet concentration of the electrolysis products. A good agreement between model predicted and experimental data was obtained for a wide range of experimental conditions. Preliminary disinfection tests were then performed using Escherichia coli as model microorganism. Results were discussed in terms of both disinfection efficiency and by-products formation. | ||
| 650 | 4 | |a Electrochemical treatment |7 (dpeaa)DE-He213 | |
| 650 | 4 | |a Modelling |7 (dpeaa)DE-He213 | |
| 650 | 4 | |a Hydrodynamics |7 (dpeaa)DE-He213 | |
| 650 | 4 | |a Chlorates |7 (dpeaa)DE-He213 | |
| 650 | 4 | |a Active chlorine |7 (dpeaa)DE-He213 | |
| 700 | 1 | |a Mascia, M. |e verfasserin |4 aut | |
| 700 | 1 | |a Palmas, S. |e verfasserin |4 aut | |
| 700 | 1 | |a Da Pozzo, A. |e verfasserin |4 aut | |
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10.1007/s10800-011-0274-3 doi (DE-627)SPR013309013 (SPR)s10800-011-0274-3-e DE-627 ger DE-627 rakwb eng 540 ASE 35.14 bkl Vacca, A. verfasserin aut Electrochemical treatment of water containing chlorides under non-ideal flow conditions with BDD anodes 2011 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Abstract In this work a undivided parallel plate cell equipped with boron doped diamond (BDD) anode was tested as electrochemical reactor for disinfection of water. Two configurations were adopted: a single pass configuration (SPC) and a recirculated configuration (RC) in which also a reservoir was inserted in the hydraulic circuit. In both the experimental configurations the system worked in continuous mode with a flow rate ranging from 0.05 to 0.42 $ dm^{3} $ $ min^{−1} $; in the RC the recirculating flow rate ranged from 0.45 to 6 $ dm^{3} $ $ min^{−1} $. Thermostated (25 °C) galvanostatic electrolyses were carried out with aqueous solutions containing 100 mg $ dm^{−3} $ of chloride ions: values of current density from 2.5 to 5.0 mA $ cm^{−2} $ were used. Steady state data revealed that active chlorine and chlorate ions were the main oxidation products. Particular attention was paid to the hydrodynamics both for SPC and RC: pulse-response curves were experimentally obtained with an inert tracer, and the behaviour of the system was interpreted by models based on a combination of ideal flow reactors, bypass flow elements, and dead zones. The hydrodynamic models were utilized to predict the outlet concentration of the electrolysis products. A good agreement between model predicted and experimental data was obtained for a wide range of experimental conditions. Preliminary disinfection tests were then performed using Escherichia coli as model microorganism. Results were discussed in terms of both disinfection efficiency and by-products formation. Electrochemical treatment (dpeaa)DE-He213 Modelling (dpeaa)DE-He213 Hydrodynamics (dpeaa)DE-He213 Chlorates (dpeaa)DE-He213 Active chlorine (dpeaa)DE-He213 Mascia, M. verfasserin aut Palmas, S. verfasserin aut Da Pozzo, A. verfasserin aut Enthalten in Journal of applied electrochemistry Dordrecht [u.a.] : Springer Science + Business Media B.V, 1971 41(2011), 9 vom: 15. März, Seite 1087-1097 (DE-627)302466037 (DE-600)1491094-9 1572-8838 nnns volume:41 year:2011 number:9 day:15 month:03 pages:1087-1097 https://dx.doi.org/10.1007/s10800-011-0274-3 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER SSG-OLC-PHA 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_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_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_4012 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_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 35.14 ASE AR 41 2011 9 15 03 1087-1097 |
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10.1007/s10800-011-0274-3 doi (DE-627)SPR013309013 (SPR)s10800-011-0274-3-e DE-627 ger DE-627 rakwb eng 540 ASE 35.14 bkl Vacca, A. verfasserin aut Electrochemical treatment of water containing chlorides under non-ideal flow conditions with BDD anodes 2011 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Abstract In this work a undivided parallel plate cell equipped with boron doped diamond (BDD) anode was tested as electrochemical reactor for disinfection of water. Two configurations were adopted: a single pass configuration (SPC) and a recirculated configuration (RC) in which also a reservoir was inserted in the hydraulic circuit. In both the experimental configurations the system worked in continuous mode with a flow rate ranging from 0.05 to 0.42 $ dm^{3} $ $ min^{−1} $; in the RC the recirculating flow rate ranged from 0.45 to 6 $ dm^{3} $ $ min^{−1} $. Thermostated (25 °C) galvanostatic electrolyses were carried out with aqueous solutions containing 100 mg $ dm^{−3} $ of chloride ions: values of current density from 2.5 to 5.0 mA $ cm^{−2} $ were used. Steady state data revealed that active chlorine and chlorate ions were the main oxidation products. Particular attention was paid to the hydrodynamics both for SPC and RC: pulse-response curves were experimentally obtained with an inert tracer, and the behaviour of the system was interpreted by models based on a combination of ideal flow reactors, bypass flow elements, and dead zones. The hydrodynamic models were utilized to predict the outlet concentration of the electrolysis products. A good agreement between model predicted and experimental data was obtained for a wide range of experimental conditions. Preliminary disinfection tests were then performed using Escherichia coli as model microorganism. Results were discussed in terms of both disinfection efficiency and by-products formation. Electrochemical treatment (dpeaa)DE-He213 Modelling (dpeaa)DE-He213 Hydrodynamics (dpeaa)DE-He213 Chlorates (dpeaa)DE-He213 Active chlorine (dpeaa)DE-He213 Mascia, M. verfasserin aut Palmas, S. verfasserin aut Da Pozzo, A. verfasserin aut Enthalten in Journal of applied electrochemistry Dordrecht [u.a.] : Springer Science + Business Media B.V, 1971 41(2011), 9 vom: 15. März, Seite 1087-1097 (DE-627)302466037 (DE-600)1491094-9 1572-8838 nnns volume:41 year:2011 number:9 day:15 month:03 pages:1087-1097 https://dx.doi.org/10.1007/s10800-011-0274-3 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER SSG-OLC-PHA 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_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_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_4012 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_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 35.14 ASE AR 41 2011 9 15 03 1087-1097 |
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10.1007/s10800-011-0274-3 doi (DE-627)SPR013309013 (SPR)s10800-011-0274-3-e DE-627 ger DE-627 rakwb eng 540 ASE 35.14 bkl Vacca, A. verfasserin aut Electrochemical treatment of water containing chlorides under non-ideal flow conditions with BDD anodes 2011 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Abstract In this work a undivided parallel plate cell equipped with boron doped diamond (BDD) anode was tested as electrochemical reactor for disinfection of water. Two configurations were adopted: a single pass configuration (SPC) and a recirculated configuration (RC) in which also a reservoir was inserted in the hydraulic circuit. In both the experimental configurations the system worked in continuous mode with a flow rate ranging from 0.05 to 0.42 $ dm^{3} $ $ min^{−1} $; in the RC the recirculating flow rate ranged from 0.45 to 6 $ dm^{3} $ $ min^{−1} $. Thermostated (25 °C) galvanostatic electrolyses were carried out with aqueous solutions containing 100 mg $ dm^{−3} $ of chloride ions: values of current density from 2.5 to 5.0 mA $ cm^{−2} $ were used. Steady state data revealed that active chlorine and chlorate ions were the main oxidation products. Particular attention was paid to the hydrodynamics both for SPC and RC: pulse-response curves were experimentally obtained with an inert tracer, and the behaviour of the system was interpreted by models based on a combination of ideal flow reactors, bypass flow elements, and dead zones. The hydrodynamic models were utilized to predict the outlet concentration of the electrolysis products. A good agreement between model predicted and experimental data was obtained for a wide range of experimental conditions. Preliminary disinfection tests were then performed using Escherichia coli as model microorganism. Results were discussed in terms of both disinfection efficiency and by-products formation. Electrochemical treatment (dpeaa)DE-He213 Modelling (dpeaa)DE-He213 Hydrodynamics (dpeaa)DE-He213 Chlorates (dpeaa)DE-He213 Active chlorine (dpeaa)DE-He213 Mascia, M. verfasserin aut Palmas, S. verfasserin aut Da Pozzo, A. verfasserin aut Enthalten in Journal of applied electrochemistry Dordrecht [u.a.] : Springer Science + Business Media B.V, 1971 41(2011), 9 vom: 15. März, Seite 1087-1097 (DE-627)302466037 (DE-600)1491094-9 1572-8838 nnns volume:41 year:2011 number:9 day:15 month:03 pages:1087-1097 https://dx.doi.org/10.1007/s10800-011-0274-3 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER SSG-OLC-PHA 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_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_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_4012 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_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 35.14 ASE AR 41 2011 9 15 03 1087-1097 |
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10.1007/s10800-011-0274-3 doi (DE-627)SPR013309013 (SPR)s10800-011-0274-3-e DE-627 ger DE-627 rakwb eng 540 ASE 35.14 bkl Vacca, A. verfasserin aut Electrochemical treatment of water containing chlorides under non-ideal flow conditions with BDD anodes 2011 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Abstract In this work a undivided parallel plate cell equipped with boron doped diamond (BDD) anode was tested as electrochemical reactor for disinfection of water. Two configurations were adopted: a single pass configuration (SPC) and a recirculated configuration (RC) in which also a reservoir was inserted in the hydraulic circuit. In both the experimental configurations the system worked in continuous mode with a flow rate ranging from 0.05 to 0.42 $ dm^{3} $ $ min^{−1} $; in the RC the recirculating flow rate ranged from 0.45 to 6 $ dm^{3} $ $ min^{−1} $. Thermostated (25 °C) galvanostatic electrolyses were carried out with aqueous solutions containing 100 mg $ dm^{−3} $ of chloride ions: values of current density from 2.5 to 5.0 mA $ cm^{−2} $ were used. Steady state data revealed that active chlorine and chlorate ions were the main oxidation products. Particular attention was paid to the hydrodynamics both for SPC and RC: pulse-response curves were experimentally obtained with an inert tracer, and the behaviour of the system was interpreted by models based on a combination of ideal flow reactors, bypass flow elements, and dead zones. The hydrodynamic models were utilized to predict the outlet concentration of the electrolysis products. A good agreement between model predicted and experimental data was obtained for a wide range of experimental conditions. Preliminary disinfection tests were then performed using Escherichia coli as model microorganism. Results were discussed in terms of both disinfection efficiency and by-products formation. Electrochemical treatment (dpeaa)DE-He213 Modelling (dpeaa)DE-He213 Hydrodynamics (dpeaa)DE-He213 Chlorates (dpeaa)DE-He213 Active chlorine (dpeaa)DE-He213 Mascia, M. verfasserin aut Palmas, S. verfasserin aut Da Pozzo, A. verfasserin aut Enthalten in Journal of applied electrochemistry Dordrecht [u.a.] : Springer Science + Business Media B.V, 1971 41(2011), 9 vom: 15. März, Seite 1087-1097 (DE-627)302466037 (DE-600)1491094-9 1572-8838 nnns volume:41 year:2011 number:9 day:15 month:03 pages:1087-1097 https://dx.doi.org/10.1007/s10800-011-0274-3 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER SSG-OLC-PHA 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_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_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_4012 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_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 35.14 ASE AR 41 2011 9 15 03 1087-1097 |
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10.1007/s10800-011-0274-3 doi (DE-627)SPR013309013 (SPR)s10800-011-0274-3-e DE-627 ger DE-627 rakwb eng 540 ASE 35.14 bkl Vacca, A. verfasserin aut Electrochemical treatment of water containing chlorides under non-ideal flow conditions with BDD anodes 2011 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Abstract In this work a undivided parallel plate cell equipped with boron doped diamond (BDD) anode was tested as electrochemical reactor for disinfection of water. Two configurations were adopted: a single pass configuration (SPC) and a recirculated configuration (RC) in which also a reservoir was inserted in the hydraulic circuit. In both the experimental configurations the system worked in continuous mode with a flow rate ranging from 0.05 to 0.42 $ dm^{3} $ $ min^{−1} $; in the RC the recirculating flow rate ranged from 0.45 to 6 $ dm^{3} $ $ min^{−1} $. Thermostated (25 °C) galvanostatic electrolyses were carried out with aqueous solutions containing 100 mg $ dm^{−3} $ of chloride ions: values of current density from 2.5 to 5.0 mA $ cm^{−2} $ were used. Steady state data revealed that active chlorine and chlorate ions were the main oxidation products. Particular attention was paid to the hydrodynamics both for SPC and RC: pulse-response curves were experimentally obtained with an inert tracer, and the behaviour of the system was interpreted by models based on a combination of ideal flow reactors, bypass flow elements, and dead zones. The hydrodynamic models were utilized to predict the outlet concentration of the electrolysis products. A good agreement between model predicted and experimental data was obtained for a wide range of experimental conditions. Preliminary disinfection tests were then performed using Escherichia coli as model microorganism. Results were discussed in terms of both disinfection efficiency and by-products formation. Electrochemical treatment (dpeaa)DE-He213 Modelling (dpeaa)DE-He213 Hydrodynamics (dpeaa)DE-He213 Chlorates (dpeaa)DE-He213 Active chlorine (dpeaa)DE-He213 Mascia, M. verfasserin aut Palmas, S. verfasserin aut Da Pozzo, A. verfasserin aut Enthalten in Journal of applied electrochemistry Dordrecht [u.a.] : Springer Science + Business Media B.V, 1971 41(2011), 9 vom: 15. März, Seite 1087-1097 (DE-627)302466037 (DE-600)1491094-9 1572-8838 nnns volume:41 year:2011 number:9 day:15 month:03 pages:1087-1097 https://dx.doi.org/10.1007/s10800-011-0274-3 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER SSG-OLC-PHA 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_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_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_4012 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_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 35.14 ASE AR 41 2011 9 15 03 1087-1097 |
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Electrochemical treatment Modelling Hydrodynamics Chlorates Active chlorine |
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Journal of applied electrochemistry |
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Vacca, A. @@aut@@ Mascia, M. @@aut@@ Palmas, S. @@aut@@ Da Pozzo, A. @@aut@@ |
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Two configurations were adopted: a single pass configuration (SPC) and a recirculated configuration (RC) in which also a reservoir was inserted in the hydraulic circuit. In both the experimental configurations the system worked in continuous mode with a flow rate ranging from 0.05 to 0.42 $ dm^{3} $ $ min^{−1} $; in the RC the recirculating flow rate ranged from 0.45 to 6 $ dm^{3} $ $ min^{−1} $. Thermostated (25 °C) galvanostatic electrolyses were carried out with aqueous solutions containing 100 mg $ dm^{−3} $ of chloride ions: values of current density from 2.5 to 5.0 mA $ cm^{−2} $ were used. Steady state data revealed that active chlorine and chlorate ions were the main oxidation products. Particular attention was paid to the hydrodynamics both for SPC and RC: pulse-response curves were experimentally obtained with an inert tracer, and the behaviour of the system was interpreted by models based on a combination of ideal flow reactors, bypass flow elements, and dead zones. The hydrodynamic models were utilized to predict the outlet concentration of the electrolysis products. A good agreement between model predicted and experimental data was obtained for a wide range of experimental conditions. Preliminary disinfection tests were then performed using Escherichia coli as model microorganism. 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Vacca, A. |
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Vacca, A. ddc 540 bkl 35.14 misc Electrochemical treatment misc Modelling misc Hydrodynamics misc Chlorates misc Active chlorine Electrochemical treatment of water containing chlorides under non-ideal flow conditions with BDD anodes |
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540 ASE 35.14 bkl Electrochemical treatment of water containing chlorides under non-ideal flow conditions with BDD anodes Electrochemical treatment (dpeaa)DE-He213 Modelling (dpeaa)DE-He213 Hydrodynamics (dpeaa)DE-He213 Chlorates (dpeaa)DE-He213 Active chlorine (dpeaa)DE-He213 |
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ddc 540 bkl 35.14 misc Electrochemical treatment misc Modelling misc Hydrodynamics misc Chlorates misc Active chlorine |
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ddc 540 bkl 35.14 misc Electrochemical treatment misc Modelling misc Hydrodynamics misc Chlorates misc Active chlorine |
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Electrochemical treatment of water containing chlorides under non-ideal flow conditions with BDD anodes |
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Electrochemical treatment of water containing chlorides under non-ideal flow conditions with BDD anodes |
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Vacca, A. |
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Journal of applied electrochemistry |
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Vacca, A. Mascia, M. Palmas, S. Da Pozzo, A. |
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540 ASE 35.14 bkl |
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Vacca, A. |
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10.1007/s10800-011-0274-3 |
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verfasserin |
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electrochemical treatment of water containing chlorides under non-ideal flow conditions with bdd anodes |
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Electrochemical treatment of water containing chlorides under non-ideal flow conditions with BDD anodes |
| abstract |
Abstract In this work a undivided parallel plate cell equipped with boron doped diamond (BDD) anode was tested as electrochemical reactor for disinfection of water. Two configurations were adopted: a single pass configuration (SPC) and a recirculated configuration (RC) in which also a reservoir was inserted in the hydraulic circuit. In both the experimental configurations the system worked in continuous mode with a flow rate ranging from 0.05 to 0.42 $ dm^{3} $ $ min^{−1} $; in the RC the recirculating flow rate ranged from 0.45 to 6 $ dm^{3} $ $ min^{−1} $. Thermostated (25 °C) galvanostatic electrolyses were carried out with aqueous solutions containing 100 mg $ dm^{−3} $ of chloride ions: values of current density from 2.5 to 5.0 mA $ cm^{−2} $ were used. Steady state data revealed that active chlorine and chlorate ions were the main oxidation products. Particular attention was paid to the hydrodynamics both for SPC and RC: pulse-response curves were experimentally obtained with an inert tracer, and the behaviour of the system was interpreted by models based on a combination of ideal flow reactors, bypass flow elements, and dead zones. The hydrodynamic models were utilized to predict the outlet concentration of the electrolysis products. A good agreement between model predicted and experimental data was obtained for a wide range of experimental conditions. Preliminary disinfection tests were then performed using Escherichia coli as model microorganism. Results were discussed in terms of both disinfection efficiency and by-products formation. |
| abstractGer |
Abstract In this work a undivided parallel plate cell equipped with boron doped diamond (BDD) anode was tested as electrochemical reactor for disinfection of water. Two configurations were adopted: a single pass configuration (SPC) and a recirculated configuration (RC) in which also a reservoir was inserted in the hydraulic circuit. In both the experimental configurations the system worked in continuous mode with a flow rate ranging from 0.05 to 0.42 $ dm^{3} $ $ min^{−1} $; in the RC the recirculating flow rate ranged from 0.45 to 6 $ dm^{3} $ $ min^{−1} $. Thermostated (25 °C) galvanostatic electrolyses were carried out with aqueous solutions containing 100 mg $ dm^{−3} $ of chloride ions: values of current density from 2.5 to 5.0 mA $ cm^{−2} $ were used. Steady state data revealed that active chlorine and chlorate ions were the main oxidation products. Particular attention was paid to the hydrodynamics both for SPC and RC: pulse-response curves were experimentally obtained with an inert tracer, and the behaviour of the system was interpreted by models based on a combination of ideal flow reactors, bypass flow elements, and dead zones. The hydrodynamic models were utilized to predict the outlet concentration of the electrolysis products. A good agreement between model predicted and experimental data was obtained for a wide range of experimental conditions. Preliminary disinfection tests were then performed using Escherichia coli as model microorganism. Results were discussed in terms of both disinfection efficiency and by-products formation. |
| abstract_unstemmed |
Abstract In this work a undivided parallel plate cell equipped with boron doped diamond (BDD) anode was tested as electrochemical reactor for disinfection of water. Two configurations were adopted: a single pass configuration (SPC) and a recirculated configuration (RC) in which also a reservoir was inserted in the hydraulic circuit. In both the experimental configurations the system worked in continuous mode with a flow rate ranging from 0.05 to 0.42 $ dm^{3} $ $ min^{−1} $; in the RC the recirculating flow rate ranged from 0.45 to 6 $ dm^{3} $ $ min^{−1} $. Thermostated (25 °C) galvanostatic electrolyses were carried out with aqueous solutions containing 100 mg $ dm^{−3} $ of chloride ions: values of current density from 2.5 to 5.0 mA $ cm^{−2} $ were used. Steady state data revealed that active chlorine and chlorate ions were the main oxidation products. Particular attention was paid to the hydrodynamics both for SPC and RC: pulse-response curves were experimentally obtained with an inert tracer, and the behaviour of the system was interpreted by models based on a combination of ideal flow reactors, bypass flow elements, and dead zones. The hydrodynamic models were utilized to predict the outlet concentration of the electrolysis products. A good agreement between model predicted and experimental data was obtained for a wide range of experimental conditions. Preliminary disinfection tests were then performed using Escherichia coli as model microorganism. Results were discussed in terms of both disinfection efficiency and by-products formation. |
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| title_short |
Electrochemical treatment of water containing chlorides under non-ideal flow conditions with BDD anodes |
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https://dx.doi.org/10.1007/s10800-011-0274-3 |
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Mascia, M. Palmas, S. Da Pozzo, A. |
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| doi_str |
10.1007/s10800-011-0274-3 |
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2024-07-03T18:49:11.850Z |
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|
| score |
7.4000797 |