Efficient removal of manganese from aquatic solutions by amphistegina filter
Abstract Mono-media filtration vessels of amphistegina and conventional granular activated carbon filters in an assembled semi-pilot filtration unit had been carried out to represent the efficient removal of manganese ions from hydrous solution in a comparison study. Amphistegina tests surfaces have...
Ausführliche Beschreibung
Gespeichert in:
| Autor*in: |
Bakr, A. A. [verfasserIn] El-Salamony, R. A. [verfasserIn] Rabie, A. M. [verfasserIn] El-Zoheiry, R. M. [verfasserIn] |
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| Format: |
E-Artikel |
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| Sprache: |
Englisch |
| Erschienen: |
2020 |
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| Schlagwörter: |
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| Übergeordnetes Werk: |
Enthalten in: International journal of energy and water resources - [Cham] : Springer International Publishing, 2018, 4(2020), 3 vom: 25. Mai, Seite 281-291 |
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| Übergeordnetes Werk: |
volume:4 ; year:2020 ; number:3 ; day:25 ; month:05 ; pages:281-291 |
| Links: |
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| DOI / URN: |
10.1007/s42108-020-00077-2 |
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SPR040754316 |
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| 520 | |a Abstract Mono-media filtration vessels of amphistegina and conventional granular activated carbon filters in an assembled semi-pilot filtration unit had been carried out to represent the efficient removal of manganese ions from hydrous solution in a comparison study. Amphistegina tests surfaces have been characterized for the first time in compared to conventional granular activated carbon media by X-ray diffraction, Fourier Transform Infrared spectroscopy and Brunauer–Emmett–Teller surface area analysis. Also, the surface morphology of granular activated carbon and amphistegina media with manganese chloride adsorption was observed by Atomic Force Microscopy analysis. The filtration unit had been operated at different working conditions such as; flow rates (20, 30, 40, 50 and 60 l/min), operating temperatures (293, 303 and 313 k), initial manganese(II) concentrations (15–105 mg/l), constant pH (7.5) and calculated adsorbent mass for granular activated carbon (34.1 g/l) and amphistegina media (115 g/l). The maximum adsorption capacities of manganese ions by amphistegina (1.17 mg/g) and granular activated carbon (3.36 mg/g) filters had been produced at a temperature of 313 k and at a higher flow rate (60 l/min); while at a lower flow rate (20 l/min), the maximum adsorption capacities were 2.83 mg/g for granular activated carbon filter and 3.42 mg/g for amphistegina filter. The adsorption performance was verified by Freundlich and Langmuir adsorption isotherms. Graphic abstract | ||
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| 650 | 4 | |a Filtration |7 (dpeaa)DE-He213 | |
| 650 | 4 | |a Manganese removal |7 (dpeaa)DE-He213 | |
| 650 | 4 | |a Amphistegina tests |7 (dpeaa)DE-He213 | |
| 650 | 4 | |a Activated carbon |7 (dpeaa)DE-He213 | |
| 650 | 4 | |a Atomic force microscopy |7 (dpeaa)DE-He213 | |
| 700 | 1 | |a El-Salamony, R. A. |e verfasserin |4 aut | |
| 700 | 1 | |a Rabie, A. M. |e verfasserin |4 aut | |
| 700 | 1 | |a El-Zoheiry, R. M. |e verfasserin |4 aut | |
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10.1007/s42108-020-00077-2 doi (DE-627)SPR040754316 (SPR)s42108-020-00077-2-e DE-627 ger DE-627 rakwb eng 333.7 ASE 333.7 ASE Bakr, A. A. verfasserin aut Efficient removal of manganese from aquatic solutions by amphistegina filter 2020 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Abstract Mono-media filtration vessels of amphistegina and conventional granular activated carbon filters in an assembled semi-pilot filtration unit had been carried out to represent the efficient removal of manganese ions from hydrous solution in a comparison study. Amphistegina tests surfaces have been characterized for the first time in compared to conventional granular activated carbon media by X-ray diffraction, Fourier Transform Infrared spectroscopy and Brunauer–Emmett–Teller surface area analysis. Also, the surface morphology of granular activated carbon and amphistegina media with manganese chloride adsorption was observed by Atomic Force Microscopy analysis. The filtration unit had been operated at different working conditions such as; flow rates (20, 30, 40, 50 and 60 l/min), operating temperatures (293, 303 and 313 k), initial manganese(II) concentrations (15–105 mg/l), constant pH (7.5) and calculated adsorbent mass for granular activated carbon (34.1 g/l) and amphistegina media (115 g/l). The maximum adsorption capacities of manganese ions by amphistegina (1.17 mg/g) and granular activated carbon (3.36 mg/g) filters had been produced at a temperature of 313 k and at a higher flow rate (60 l/min); while at a lower flow rate (20 l/min), the maximum adsorption capacities were 2.83 mg/g for granular activated carbon filter and 3.42 mg/g for amphistegina filter. The adsorption performance was verified by Freundlich and Langmuir adsorption isotherms. Graphic abstract Water treatment (dpeaa)DE-He213 Filtration (dpeaa)DE-He213 Manganese removal (dpeaa)DE-He213 Amphistegina tests (dpeaa)DE-He213 Activated carbon (dpeaa)DE-He213 Atomic force microscopy (dpeaa)DE-He213 El-Salamony, R. A. verfasserin aut Rabie, A. M. verfasserin aut El-Zoheiry, R. M. verfasserin aut Enthalten in International journal of energy and water resources [Cham] : Springer International Publishing, 2018 4(2020), 3 vom: 25. Mai, Seite 281-291 (DE-627)1041147686 (DE-600)2951257-8 2522-0101 nnns volume:4 year:2020 number:3 day:25 month:05 pages:281-291 https://dx.doi.org/10.1007/s42108-020-00077-2 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_65 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_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_250 GBV_ILN_266 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 AR 4 2020 3 25 05 281-291 |
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10.1007/s42108-020-00077-2 doi (DE-627)SPR040754316 (SPR)s42108-020-00077-2-e DE-627 ger DE-627 rakwb eng 333.7 ASE 333.7 ASE Bakr, A. A. verfasserin aut Efficient removal of manganese from aquatic solutions by amphistegina filter 2020 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Abstract Mono-media filtration vessels of amphistegina and conventional granular activated carbon filters in an assembled semi-pilot filtration unit had been carried out to represent the efficient removal of manganese ions from hydrous solution in a comparison study. Amphistegina tests surfaces have been characterized for the first time in compared to conventional granular activated carbon media by X-ray diffraction, Fourier Transform Infrared spectroscopy and Brunauer–Emmett–Teller surface area analysis. Also, the surface morphology of granular activated carbon and amphistegina media with manganese chloride adsorption was observed by Atomic Force Microscopy analysis. The filtration unit had been operated at different working conditions such as; flow rates (20, 30, 40, 50 and 60 l/min), operating temperatures (293, 303 and 313 k), initial manganese(II) concentrations (15–105 mg/l), constant pH (7.5) and calculated adsorbent mass for granular activated carbon (34.1 g/l) and amphistegina media (115 g/l). The maximum adsorption capacities of manganese ions by amphistegina (1.17 mg/g) and granular activated carbon (3.36 mg/g) filters had been produced at a temperature of 313 k and at a higher flow rate (60 l/min); while at a lower flow rate (20 l/min), the maximum adsorption capacities were 2.83 mg/g for granular activated carbon filter and 3.42 mg/g for amphistegina filter. The adsorption performance was verified by Freundlich and Langmuir adsorption isotherms. Graphic abstract Water treatment (dpeaa)DE-He213 Filtration (dpeaa)DE-He213 Manganese removal (dpeaa)DE-He213 Amphistegina tests (dpeaa)DE-He213 Activated carbon (dpeaa)DE-He213 Atomic force microscopy (dpeaa)DE-He213 El-Salamony, R. A. verfasserin aut Rabie, A. M. verfasserin aut El-Zoheiry, R. M. verfasserin aut Enthalten in International journal of energy and water resources [Cham] : Springer International Publishing, 2018 4(2020), 3 vom: 25. Mai, Seite 281-291 (DE-627)1041147686 (DE-600)2951257-8 2522-0101 nnns volume:4 year:2020 number:3 day:25 month:05 pages:281-291 https://dx.doi.org/10.1007/s42108-020-00077-2 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_65 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_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_250 GBV_ILN_266 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 AR 4 2020 3 25 05 281-291 |
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10.1007/s42108-020-00077-2 doi (DE-627)SPR040754316 (SPR)s42108-020-00077-2-e DE-627 ger DE-627 rakwb eng 333.7 ASE 333.7 ASE Bakr, A. A. verfasserin aut Efficient removal of manganese from aquatic solutions by amphistegina filter 2020 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Abstract Mono-media filtration vessels of amphistegina and conventional granular activated carbon filters in an assembled semi-pilot filtration unit had been carried out to represent the efficient removal of manganese ions from hydrous solution in a comparison study. Amphistegina tests surfaces have been characterized for the first time in compared to conventional granular activated carbon media by X-ray diffraction, Fourier Transform Infrared spectroscopy and Brunauer–Emmett–Teller surface area analysis. Also, the surface morphology of granular activated carbon and amphistegina media with manganese chloride adsorption was observed by Atomic Force Microscopy analysis. The filtration unit had been operated at different working conditions such as; flow rates (20, 30, 40, 50 and 60 l/min), operating temperatures (293, 303 and 313 k), initial manganese(II) concentrations (15–105 mg/l), constant pH (7.5) and calculated adsorbent mass for granular activated carbon (34.1 g/l) and amphistegina media (115 g/l). The maximum adsorption capacities of manganese ions by amphistegina (1.17 mg/g) and granular activated carbon (3.36 mg/g) filters had been produced at a temperature of 313 k and at a higher flow rate (60 l/min); while at a lower flow rate (20 l/min), the maximum adsorption capacities were 2.83 mg/g for granular activated carbon filter and 3.42 mg/g for amphistegina filter. The adsorption performance was verified by Freundlich and Langmuir adsorption isotherms. Graphic abstract Water treatment (dpeaa)DE-He213 Filtration (dpeaa)DE-He213 Manganese removal (dpeaa)DE-He213 Amphistegina tests (dpeaa)DE-He213 Activated carbon (dpeaa)DE-He213 Atomic force microscopy (dpeaa)DE-He213 El-Salamony, R. A. verfasserin aut Rabie, A. M. verfasserin aut El-Zoheiry, R. M. verfasserin aut Enthalten in International journal of energy and water resources [Cham] : Springer International Publishing, 2018 4(2020), 3 vom: 25. Mai, Seite 281-291 (DE-627)1041147686 (DE-600)2951257-8 2522-0101 nnns volume:4 year:2020 number:3 day:25 month:05 pages:281-291 https://dx.doi.org/10.1007/s42108-020-00077-2 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_65 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_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_250 GBV_ILN_266 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 AR 4 2020 3 25 05 281-291 |
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10.1007/s42108-020-00077-2 doi (DE-627)SPR040754316 (SPR)s42108-020-00077-2-e DE-627 ger DE-627 rakwb eng 333.7 ASE 333.7 ASE Bakr, A. A. verfasserin aut Efficient removal of manganese from aquatic solutions by amphistegina filter 2020 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Abstract Mono-media filtration vessels of amphistegina and conventional granular activated carbon filters in an assembled semi-pilot filtration unit had been carried out to represent the efficient removal of manganese ions from hydrous solution in a comparison study. Amphistegina tests surfaces have been characterized for the first time in compared to conventional granular activated carbon media by X-ray diffraction, Fourier Transform Infrared spectroscopy and Brunauer–Emmett–Teller surface area analysis. Also, the surface morphology of granular activated carbon and amphistegina media with manganese chloride adsorption was observed by Atomic Force Microscopy analysis. The filtration unit had been operated at different working conditions such as; flow rates (20, 30, 40, 50 and 60 l/min), operating temperatures (293, 303 and 313 k), initial manganese(II) concentrations (15–105 mg/l), constant pH (7.5) and calculated adsorbent mass for granular activated carbon (34.1 g/l) and amphistegina media (115 g/l). The maximum adsorption capacities of manganese ions by amphistegina (1.17 mg/g) and granular activated carbon (3.36 mg/g) filters had been produced at a temperature of 313 k and at a higher flow rate (60 l/min); while at a lower flow rate (20 l/min), the maximum adsorption capacities were 2.83 mg/g for granular activated carbon filter and 3.42 mg/g for amphistegina filter. The adsorption performance was verified by Freundlich and Langmuir adsorption isotherms. Graphic abstract Water treatment (dpeaa)DE-He213 Filtration (dpeaa)DE-He213 Manganese removal (dpeaa)DE-He213 Amphistegina tests (dpeaa)DE-He213 Activated carbon (dpeaa)DE-He213 Atomic force microscopy (dpeaa)DE-He213 El-Salamony, R. A. verfasserin aut Rabie, A. M. verfasserin aut El-Zoheiry, R. M. verfasserin aut Enthalten in International journal of energy and water resources [Cham] : Springer International Publishing, 2018 4(2020), 3 vom: 25. Mai, Seite 281-291 (DE-627)1041147686 (DE-600)2951257-8 2522-0101 nnns volume:4 year:2020 number:3 day:25 month:05 pages:281-291 https://dx.doi.org/10.1007/s42108-020-00077-2 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_65 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_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_250 GBV_ILN_266 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 AR 4 2020 3 25 05 281-291 |
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10.1007/s42108-020-00077-2 doi (DE-627)SPR040754316 (SPR)s42108-020-00077-2-e DE-627 ger DE-627 rakwb eng 333.7 ASE 333.7 ASE Bakr, A. A. verfasserin aut Efficient removal of manganese from aquatic solutions by amphistegina filter 2020 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Abstract Mono-media filtration vessels of amphistegina and conventional granular activated carbon filters in an assembled semi-pilot filtration unit had been carried out to represent the efficient removal of manganese ions from hydrous solution in a comparison study. Amphistegina tests surfaces have been characterized for the first time in compared to conventional granular activated carbon media by X-ray diffraction, Fourier Transform Infrared spectroscopy and Brunauer–Emmett–Teller surface area analysis. Also, the surface morphology of granular activated carbon and amphistegina media with manganese chloride adsorption was observed by Atomic Force Microscopy analysis. The filtration unit had been operated at different working conditions such as; flow rates (20, 30, 40, 50 and 60 l/min), operating temperatures (293, 303 and 313 k), initial manganese(II) concentrations (15–105 mg/l), constant pH (7.5) and calculated adsorbent mass for granular activated carbon (34.1 g/l) and amphistegina media (115 g/l). The maximum adsorption capacities of manganese ions by amphistegina (1.17 mg/g) and granular activated carbon (3.36 mg/g) filters had been produced at a temperature of 313 k and at a higher flow rate (60 l/min); while at a lower flow rate (20 l/min), the maximum adsorption capacities were 2.83 mg/g for granular activated carbon filter and 3.42 mg/g for amphistegina filter. The adsorption performance was verified by Freundlich and Langmuir adsorption isotherms. Graphic abstract Water treatment (dpeaa)DE-He213 Filtration (dpeaa)DE-He213 Manganese removal (dpeaa)DE-He213 Amphistegina tests (dpeaa)DE-He213 Activated carbon (dpeaa)DE-He213 Atomic force microscopy (dpeaa)DE-He213 El-Salamony, R. A. verfasserin aut Rabie, A. M. verfasserin aut El-Zoheiry, R. M. verfasserin aut Enthalten in International journal of energy and water resources [Cham] : Springer International Publishing, 2018 4(2020), 3 vom: 25. Mai, Seite 281-291 (DE-627)1041147686 (DE-600)2951257-8 2522-0101 nnns volume:4 year:2020 number:3 day:25 month:05 pages:281-291 https://dx.doi.org/10.1007/s42108-020-00077-2 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_65 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_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_250 GBV_ILN_266 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 AR 4 2020 3 25 05 281-291 |
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Enthalten in International journal of energy and water resources 4(2020), 3 vom: 25. Mai, Seite 281-291 volume:4 year:2020 number:3 day:25 month:05 pages:281-291 |
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Bakr, A. A. @@aut@@ El-Salamony, R. A. @@aut@@ Rabie, A. M. @@aut@@ El-Zoheiry, R. M. @@aut@@ |
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A.</subfield><subfield code="e">verfasserin</subfield><subfield code="4">aut</subfield></datafield><datafield tag="245" ind1="1" ind2="0"><subfield code="a">Efficient removal of manganese from aquatic solutions by amphistegina filter</subfield></datafield><datafield tag="264" ind1=" " ind2="1"><subfield code="c">2020</subfield></datafield><datafield tag="336" ind1=" " ind2=" "><subfield code="a">Text</subfield><subfield code="b">txt</subfield><subfield code="2">rdacontent</subfield></datafield><datafield tag="337" ind1=" " ind2=" "><subfield code="a">Computermedien</subfield><subfield code="b">c</subfield><subfield code="2">rdamedia</subfield></datafield><datafield tag="338" ind1=" " ind2=" "><subfield code="a">Online-Ressource</subfield><subfield code="b">cr</subfield><subfield code="2">rdacarrier</subfield></datafield><datafield tag="520" ind1=" " ind2=" "><subfield code="a">Abstract Mono-media filtration vessels of amphistegina and conventional granular activated carbon filters in an assembled semi-pilot filtration unit had been carried out to represent the efficient removal of manganese ions from hydrous solution in a comparison study. Amphistegina tests surfaces have been characterized for the first time in compared to conventional granular activated carbon media by X-ray diffraction, Fourier Transform Infrared spectroscopy and Brunauer–Emmett–Teller surface area analysis. Also, the surface morphology of granular activated carbon and amphistegina media with manganese chloride adsorption was observed by Atomic Force Microscopy analysis. The filtration unit had been operated at different working conditions such as; flow rates (20, 30, 40, 50 and 60 l/min), operating temperatures (293, 303 and 313 k), initial manganese(II) concentrations (15–105 mg/l), constant pH (7.5) and calculated adsorbent mass for granular activated carbon (34.1 g/l) and amphistegina media (115 g/l). The maximum adsorption capacities of manganese ions by amphistegina (1.17 mg/g) and granular activated carbon (3.36 mg/g) filters had been produced at a temperature of 313 k and at a higher flow rate (60 l/min); while at a lower flow rate (20 l/min), the maximum adsorption capacities were 2.83 mg/g for granular activated carbon filter and 3.42 mg/g for amphistegina filter. The adsorption performance was verified by Freundlich and Langmuir adsorption isotherms. 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Bakr, A. A. |
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Bakr, A. A. ddc 333.7 misc Water treatment misc Filtration misc Manganese removal misc Amphistegina tests misc Activated carbon misc Atomic force microscopy Efficient removal of manganese from aquatic solutions by amphistegina filter |
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333.7 ASE Efficient removal of manganese from aquatic solutions by amphistegina filter Water treatment (dpeaa)DE-He213 Filtration (dpeaa)DE-He213 Manganese removal (dpeaa)DE-He213 Amphistegina tests (dpeaa)DE-He213 Activated carbon (dpeaa)DE-He213 Atomic force microscopy (dpeaa)DE-He213 |
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ddc 333.7 misc Water treatment misc Filtration misc Manganese removal misc Amphistegina tests misc Activated carbon misc Atomic force microscopy |
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ddc 333.7 misc Water treatment misc Filtration misc Manganese removal misc Amphistegina tests misc Activated carbon misc Atomic force microscopy |
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ddc 333.7 misc Water treatment misc Filtration misc Manganese removal misc Amphistegina tests misc Activated carbon misc Atomic force microscopy |
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Efficient removal of manganese from aquatic solutions by amphistegina filter |
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Efficient removal of manganese from aquatic solutions by amphistegina filter |
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International journal of energy and water resources |
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efficient removal of manganese from aquatic solutions by amphistegina filter |
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Efficient removal of manganese from aquatic solutions by amphistegina filter |
| abstract |
Abstract Mono-media filtration vessels of amphistegina and conventional granular activated carbon filters in an assembled semi-pilot filtration unit had been carried out to represent the efficient removal of manganese ions from hydrous solution in a comparison study. Amphistegina tests surfaces have been characterized for the first time in compared to conventional granular activated carbon media by X-ray diffraction, Fourier Transform Infrared spectroscopy and Brunauer–Emmett–Teller surface area analysis. Also, the surface morphology of granular activated carbon and amphistegina media with manganese chloride adsorption was observed by Atomic Force Microscopy analysis. The filtration unit had been operated at different working conditions such as; flow rates (20, 30, 40, 50 and 60 l/min), operating temperatures (293, 303 and 313 k), initial manganese(II) concentrations (15–105 mg/l), constant pH (7.5) and calculated adsorbent mass for granular activated carbon (34.1 g/l) and amphistegina media (115 g/l). The maximum adsorption capacities of manganese ions by amphistegina (1.17 mg/g) and granular activated carbon (3.36 mg/g) filters had been produced at a temperature of 313 k and at a higher flow rate (60 l/min); while at a lower flow rate (20 l/min), the maximum adsorption capacities were 2.83 mg/g for granular activated carbon filter and 3.42 mg/g for amphistegina filter. The adsorption performance was verified by Freundlich and Langmuir adsorption isotherms. Graphic abstract |
| abstractGer |
Abstract Mono-media filtration vessels of amphistegina and conventional granular activated carbon filters in an assembled semi-pilot filtration unit had been carried out to represent the efficient removal of manganese ions from hydrous solution in a comparison study. Amphistegina tests surfaces have been characterized for the first time in compared to conventional granular activated carbon media by X-ray diffraction, Fourier Transform Infrared spectroscopy and Brunauer–Emmett–Teller surface area analysis. Also, the surface morphology of granular activated carbon and amphistegina media with manganese chloride adsorption was observed by Atomic Force Microscopy analysis. The filtration unit had been operated at different working conditions such as; flow rates (20, 30, 40, 50 and 60 l/min), operating temperatures (293, 303 and 313 k), initial manganese(II) concentrations (15–105 mg/l), constant pH (7.5) and calculated adsorbent mass for granular activated carbon (34.1 g/l) and amphistegina media (115 g/l). The maximum adsorption capacities of manganese ions by amphistegina (1.17 mg/g) and granular activated carbon (3.36 mg/g) filters had been produced at a temperature of 313 k and at a higher flow rate (60 l/min); while at a lower flow rate (20 l/min), the maximum adsorption capacities were 2.83 mg/g for granular activated carbon filter and 3.42 mg/g for amphistegina filter. The adsorption performance was verified by Freundlich and Langmuir adsorption isotherms. Graphic abstract |
| abstract_unstemmed |
Abstract Mono-media filtration vessels of amphistegina and conventional granular activated carbon filters in an assembled semi-pilot filtration unit had been carried out to represent the efficient removal of manganese ions from hydrous solution in a comparison study. Amphistegina tests surfaces have been characterized for the first time in compared to conventional granular activated carbon media by X-ray diffraction, Fourier Transform Infrared spectroscopy and Brunauer–Emmett–Teller surface area analysis. Also, the surface morphology of granular activated carbon and amphistegina media with manganese chloride adsorption was observed by Atomic Force Microscopy analysis. The filtration unit had been operated at different working conditions such as; flow rates (20, 30, 40, 50 and 60 l/min), operating temperatures (293, 303 and 313 k), initial manganese(II) concentrations (15–105 mg/l), constant pH (7.5) and calculated adsorbent mass for granular activated carbon (34.1 g/l) and amphistegina media (115 g/l). The maximum adsorption capacities of manganese ions by amphistegina (1.17 mg/g) and granular activated carbon (3.36 mg/g) filters had been produced at a temperature of 313 k and at a higher flow rate (60 l/min); while at a lower flow rate (20 l/min), the maximum adsorption capacities were 2.83 mg/g for granular activated carbon filter and 3.42 mg/g for amphistegina filter. The adsorption performance was verified by Freundlich and Langmuir adsorption isotherms. Graphic abstract |
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| title_short |
Efficient removal of manganese from aquatic solutions by amphistegina filter |
| url |
https://dx.doi.org/10.1007/s42108-020-00077-2 |
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El-Salamony, R. A. Rabie, A. M. El-Zoheiry, R. M. |
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El-Salamony, R. A. Rabie, A. M. El-Zoheiry, R. M. |
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10.1007/s42108-020-00077-2 |
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2024-07-03T18:02:55.206Z |
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| score |
7.399131 |