Start-up of Aerobic Granular Biomass System: Fate of Organics and Nutrients Removal From Anaerobic Effluent
Purpose The up-flow anaerobic sludge blanket reactor (UASB) treated effluent does not meet the national disposal standards of certain countries, such as India and Brazil. To meet the required standards, it is necessary to upgrade the UASB technology through a post-treatment system. The present work...
Ausführliche Beschreibung
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| Autor*in: |
Rayaz, Mohd [verfasserIn] |
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E-Artikel |
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| Sprache: |
Englisch |
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2023 |
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© The Author(s), under exclusive licence to Springer Nature B.V. 2023. Springer Nature or its licensor (e.g. a society or other partner) holds exclusive rights to this article under a publishing agreement with the author(s) or other rightsholder(s); author self-archiving of the accepted manuscript version of this article is solely governed by the terms of such publishing agreement and applicable law. |
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| Übergeordnetes Werk: |
Enthalten in: Waste and biomass valorization - [Dordrecht] : Springer Netherlands, 2010, 15(2023), 2 vom: 27. Juni, Seite 945-958 |
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| Übergeordnetes Werk: |
volume:15 ; year:2023 ; number:2 ; day:27 ; month:06 ; pages:945-958 |
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| DOI / URN: |
10.1007/s12649-023-02198-1 |
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SPR054696488 |
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| 520 | |a Purpose The up-flow anaerobic sludge blanket reactor (UASB) treated effluent does not meet the national disposal standards of certain countries, such as India and Brazil. To meet the required standards, it is necessary to upgrade the UASB technology through a post-treatment system. The present work aimed to investigate the optimal operating conditions for the formation of granules in an anaerobic/oxic/anoxic (A/O/A) cyclic mode aerobic granular biomass reactor (AGBR) for the treatment of anaerobic effluent (UASB effluent). Methods Two rectangular reactors, R1 and R2, were used to cultivate aerobic granular biomass (AGB). R1 served as the control reactor and was fed with low-strength synthetic wastewater throughout the study, while R2 was fed with medium strength sewage and UASB effluent over the study periods. Results Granules start-ups were observed on the 30th and 20th days in R1 and R2, respectively. In R1, the removal efficiency of COD, $ NH_{4} $+-N, total nitrogen (TN), and $ PO_{4} $3−-P was achieved 80.86%, 97.46%, 53.6%, and 45%, respectively. Whereas the removal efficiency of COD, $ NH_{4} $+-N, TN, and $ PO_{4} $3−-P was observed 63.61%, 58.18%, 50%, and 40%, respectively, in R2. The results indicated that the short aeration time, comprising 50% of the total cycle time over a 3-h duration, was the most effective operational phase for achieving high removal of organics and nutrients. Conclusion The study demonstrates that the A/O/A AGBR effectively cultivates AGB and removes organics and nutrients from anaerobic effluent. The use of medium-strength sewage as a substrate in R2 proved beneficial in reducing the granule start-up time for treating low-strength anaerobic effluent. | ||
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10.1007/s12649-023-02198-1 doi (DE-627)SPR054696488 (SPR)s12649-023-02198-1-e DE-627 ger DE-627 rakwb eng Rayaz, Mohd verfasserin aut Start-up of Aerobic Granular Biomass System: Fate of Organics and Nutrients Removal From Anaerobic Effluent 2023 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © The Author(s), under exclusive licence to Springer Nature B.V. 2023. Springer Nature or its licensor (e.g. a society or other partner) holds exclusive rights to this article under a publishing agreement with the author(s) or other rightsholder(s); author self-archiving of the accepted manuscript version of this article is solely governed by the terms of such publishing agreement and applicable law. Purpose The up-flow anaerobic sludge blanket reactor (UASB) treated effluent does not meet the national disposal standards of certain countries, such as India and Brazil. To meet the required standards, it is necessary to upgrade the UASB technology through a post-treatment system. The present work aimed to investigate the optimal operating conditions for the formation of granules in an anaerobic/oxic/anoxic (A/O/A) cyclic mode aerobic granular biomass reactor (AGBR) for the treatment of anaerobic effluent (UASB effluent). Methods Two rectangular reactors, R1 and R2, were used to cultivate aerobic granular biomass (AGB). R1 served as the control reactor and was fed with low-strength synthetic wastewater throughout the study, while R2 was fed with medium strength sewage and UASB effluent over the study periods. Results Granules start-ups were observed on the 30th and 20th days in R1 and R2, respectively. In R1, the removal efficiency of COD, $ NH_{4} $+-N, total nitrogen (TN), and $ PO_{4} $3−-P was achieved 80.86%, 97.46%, 53.6%, and 45%, respectively. Whereas the removal efficiency of COD, $ NH_{4} $+-N, TN, and $ PO_{4} $3−-P was observed 63.61%, 58.18%, 50%, and 40%, respectively, in R2. The results indicated that the short aeration time, comprising 50% of the total cycle time over a 3-h duration, was the most effective operational phase for achieving high removal of organics and nutrients. Conclusion The study demonstrates that the A/O/A AGBR effectively cultivates AGB and removes organics and nutrients from anaerobic effluent. The use of medium-strength sewage as a substrate in R2 proved beneficial in reducing the granule start-up time for treating low-strength anaerobic effluent. Aerobic granules (dpeaa)DE-He213 Aerobic granular biomass reactor (dpeaa)DE-He213 Anaerobic effluent (dpeaa)DE-He213 Anaerobic phase (dpeaa)DE-He213 Oxic phase (dpeaa)DE-He213 Anoxic phase (dpeaa)DE-He213 Khan, Mohd Aamir aut Khan, Abid Ali aut Khatoon, Fehmeeda (orcid)0000-0002-0254-1252 aut Enthalten in Waste and biomass valorization [Dordrecht] : Springer Netherlands, 2010 15(2023), 2 vom: 27. Juni, Seite 945-958 (DE-627)620147245 (DE-600)2541900-6 1877-265X nnns volume:15 year:2023 number:2 day:27 month:06 pages:945-958 https://dx.doi.org/10.1007/s12649-023-02198-1 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_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_2119 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2144 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2188 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2446 GBV_ILN_2470 GBV_ILN_2472 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_2548 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_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 15 2023 2 27 06 945-958 |
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10.1007/s12649-023-02198-1 doi (DE-627)SPR054696488 (SPR)s12649-023-02198-1-e DE-627 ger DE-627 rakwb eng Rayaz, Mohd verfasserin aut Start-up of Aerobic Granular Biomass System: Fate of Organics and Nutrients Removal From Anaerobic Effluent 2023 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © The Author(s), under exclusive licence to Springer Nature B.V. 2023. Springer Nature or its licensor (e.g. a society or other partner) holds exclusive rights to this article under a publishing agreement with the author(s) or other rightsholder(s); author self-archiving of the accepted manuscript version of this article is solely governed by the terms of such publishing agreement and applicable law. Purpose The up-flow anaerobic sludge blanket reactor (UASB) treated effluent does not meet the national disposal standards of certain countries, such as India and Brazil. To meet the required standards, it is necessary to upgrade the UASB technology through a post-treatment system. The present work aimed to investigate the optimal operating conditions for the formation of granules in an anaerobic/oxic/anoxic (A/O/A) cyclic mode aerobic granular biomass reactor (AGBR) for the treatment of anaerobic effluent (UASB effluent). Methods Two rectangular reactors, R1 and R2, were used to cultivate aerobic granular biomass (AGB). R1 served as the control reactor and was fed with low-strength synthetic wastewater throughout the study, while R2 was fed with medium strength sewage and UASB effluent over the study periods. Results Granules start-ups were observed on the 30th and 20th days in R1 and R2, respectively. In R1, the removal efficiency of COD, $ NH_{4} $+-N, total nitrogen (TN), and $ PO_{4} $3−-P was achieved 80.86%, 97.46%, 53.6%, and 45%, respectively. Whereas the removal efficiency of COD, $ NH_{4} $+-N, TN, and $ PO_{4} $3−-P was observed 63.61%, 58.18%, 50%, and 40%, respectively, in R2. The results indicated that the short aeration time, comprising 50% of the total cycle time over a 3-h duration, was the most effective operational phase for achieving high removal of organics and nutrients. Conclusion The study demonstrates that the A/O/A AGBR effectively cultivates AGB and removes organics and nutrients from anaerobic effluent. The use of medium-strength sewage as a substrate in R2 proved beneficial in reducing the granule start-up time for treating low-strength anaerobic effluent. Aerobic granules (dpeaa)DE-He213 Aerobic granular biomass reactor (dpeaa)DE-He213 Anaerobic effluent (dpeaa)DE-He213 Anaerobic phase (dpeaa)DE-He213 Oxic phase (dpeaa)DE-He213 Anoxic phase (dpeaa)DE-He213 Khan, Mohd Aamir aut Khan, Abid Ali aut Khatoon, Fehmeeda (orcid)0000-0002-0254-1252 aut Enthalten in Waste and biomass valorization [Dordrecht] : Springer Netherlands, 2010 15(2023), 2 vom: 27. Juni, Seite 945-958 (DE-627)620147245 (DE-600)2541900-6 1877-265X nnns volume:15 year:2023 number:2 day:27 month:06 pages:945-958 https://dx.doi.org/10.1007/s12649-023-02198-1 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_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_2119 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2144 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2188 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2446 GBV_ILN_2470 GBV_ILN_2472 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_2548 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_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 15 2023 2 27 06 945-958 |
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10.1007/s12649-023-02198-1 doi (DE-627)SPR054696488 (SPR)s12649-023-02198-1-e DE-627 ger DE-627 rakwb eng Rayaz, Mohd verfasserin aut Start-up of Aerobic Granular Biomass System: Fate of Organics and Nutrients Removal From Anaerobic Effluent 2023 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © The Author(s), under exclusive licence to Springer Nature B.V. 2023. Springer Nature or its licensor (e.g. a society or other partner) holds exclusive rights to this article under a publishing agreement with the author(s) or other rightsholder(s); author self-archiving of the accepted manuscript version of this article is solely governed by the terms of such publishing agreement and applicable law. Purpose The up-flow anaerobic sludge blanket reactor (UASB) treated effluent does not meet the national disposal standards of certain countries, such as India and Brazil. To meet the required standards, it is necessary to upgrade the UASB technology through a post-treatment system. The present work aimed to investigate the optimal operating conditions for the formation of granules in an anaerobic/oxic/anoxic (A/O/A) cyclic mode aerobic granular biomass reactor (AGBR) for the treatment of anaerobic effluent (UASB effluent). Methods Two rectangular reactors, R1 and R2, were used to cultivate aerobic granular biomass (AGB). R1 served as the control reactor and was fed with low-strength synthetic wastewater throughout the study, while R2 was fed with medium strength sewage and UASB effluent over the study periods. Results Granules start-ups were observed on the 30th and 20th days in R1 and R2, respectively. In R1, the removal efficiency of COD, $ NH_{4} $+-N, total nitrogen (TN), and $ PO_{4} $3−-P was achieved 80.86%, 97.46%, 53.6%, and 45%, respectively. Whereas the removal efficiency of COD, $ NH_{4} $+-N, TN, and $ PO_{4} $3−-P was observed 63.61%, 58.18%, 50%, and 40%, respectively, in R2. The results indicated that the short aeration time, comprising 50% of the total cycle time over a 3-h duration, was the most effective operational phase for achieving high removal of organics and nutrients. Conclusion The study demonstrates that the A/O/A AGBR effectively cultivates AGB and removes organics and nutrients from anaerobic effluent. The use of medium-strength sewage as a substrate in R2 proved beneficial in reducing the granule start-up time for treating low-strength anaerobic effluent. Aerobic granules (dpeaa)DE-He213 Aerobic granular biomass reactor (dpeaa)DE-He213 Anaerobic effluent (dpeaa)DE-He213 Anaerobic phase (dpeaa)DE-He213 Oxic phase (dpeaa)DE-He213 Anoxic phase (dpeaa)DE-He213 Khan, Mohd Aamir aut Khan, Abid Ali aut Khatoon, Fehmeeda (orcid)0000-0002-0254-1252 aut Enthalten in Waste and biomass valorization [Dordrecht] : Springer Netherlands, 2010 15(2023), 2 vom: 27. Juni, Seite 945-958 (DE-627)620147245 (DE-600)2541900-6 1877-265X nnns volume:15 year:2023 number:2 day:27 month:06 pages:945-958 https://dx.doi.org/10.1007/s12649-023-02198-1 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_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_2119 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2144 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2188 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2446 GBV_ILN_2470 GBV_ILN_2472 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_2548 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_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 15 2023 2 27 06 945-958 |
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10.1007/s12649-023-02198-1 doi (DE-627)SPR054696488 (SPR)s12649-023-02198-1-e DE-627 ger DE-627 rakwb eng Rayaz, Mohd verfasserin aut Start-up of Aerobic Granular Biomass System: Fate of Organics and Nutrients Removal From Anaerobic Effluent 2023 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © The Author(s), under exclusive licence to Springer Nature B.V. 2023. Springer Nature or its licensor (e.g. a society or other partner) holds exclusive rights to this article under a publishing agreement with the author(s) or other rightsholder(s); author self-archiving of the accepted manuscript version of this article is solely governed by the terms of such publishing agreement and applicable law. Purpose The up-flow anaerobic sludge blanket reactor (UASB) treated effluent does not meet the national disposal standards of certain countries, such as India and Brazil. To meet the required standards, it is necessary to upgrade the UASB technology through a post-treatment system. The present work aimed to investigate the optimal operating conditions for the formation of granules in an anaerobic/oxic/anoxic (A/O/A) cyclic mode aerobic granular biomass reactor (AGBR) for the treatment of anaerobic effluent (UASB effluent). Methods Two rectangular reactors, R1 and R2, were used to cultivate aerobic granular biomass (AGB). R1 served as the control reactor and was fed with low-strength synthetic wastewater throughout the study, while R2 was fed with medium strength sewage and UASB effluent over the study periods. Results Granules start-ups were observed on the 30th and 20th days in R1 and R2, respectively. In R1, the removal efficiency of COD, $ NH_{4} $+-N, total nitrogen (TN), and $ PO_{4} $3−-P was achieved 80.86%, 97.46%, 53.6%, and 45%, respectively. Whereas the removal efficiency of COD, $ NH_{4} $+-N, TN, and $ PO_{4} $3−-P was observed 63.61%, 58.18%, 50%, and 40%, respectively, in R2. The results indicated that the short aeration time, comprising 50% of the total cycle time over a 3-h duration, was the most effective operational phase for achieving high removal of organics and nutrients. Conclusion The study demonstrates that the A/O/A AGBR effectively cultivates AGB and removes organics and nutrients from anaerobic effluent. The use of medium-strength sewage as a substrate in R2 proved beneficial in reducing the granule start-up time for treating low-strength anaerobic effluent. Aerobic granules (dpeaa)DE-He213 Aerobic granular biomass reactor (dpeaa)DE-He213 Anaerobic effluent (dpeaa)DE-He213 Anaerobic phase (dpeaa)DE-He213 Oxic phase (dpeaa)DE-He213 Anoxic phase (dpeaa)DE-He213 Khan, Mohd Aamir aut Khan, Abid Ali aut Khatoon, Fehmeeda (orcid)0000-0002-0254-1252 aut Enthalten in Waste and biomass valorization [Dordrecht] : Springer Netherlands, 2010 15(2023), 2 vom: 27. Juni, Seite 945-958 (DE-627)620147245 (DE-600)2541900-6 1877-265X nnns volume:15 year:2023 number:2 day:27 month:06 pages:945-958 https://dx.doi.org/10.1007/s12649-023-02198-1 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_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_2119 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2144 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2188 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2446 GBV_ILN_2470 GBV_ILN_2472 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_2548 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_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 15 2023 2 27 06 945-958 |
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10.1007/s12649-023-02198-1 doi (DE-627)SPR054696488 (SPR)s12649-023-02198-1-e DE-627 ger DE-627 rakwb eng Rayaz, Mohd verfasserin aut Start-up of Aerobic Granular Biomass System: Fate of Organics and Nutrients Removal From Anaerobic Effluent 2023 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © The Author(s), under exclusive licence to Springer Nature B.V. 2023. Springer Nature or its licensor (e.g. a society or other partner) holds exclusive rights to this article under a publishing agreement with the author(s) or other rightsholder(s); author self-archiving of the accepted manuscript version of this article is solely governed by the terms of such publishing agreement and applicable law. Purpose The up-flow anaerobic sludge blanket reactor (UASB) treated effluent does not meet the national disposal standards of certain countries, such as India and Brazil. To meet the required standards, it is necessary to upgrade the UASB technology through a post-treatment system. The present work aimed to investigate the optimal operating conditions for the formation of granules in an anaerobic/oxic/anoxic (A/O/A) cyclic mode aerobic granular biomass reactor (AGBR) for the treatment of anaerobic effluent (UASB effluent). Methods Two rectangular reactors, R1 and R2, were used to cultivate aerobic granular biomass (AGB). R1 served as the control reactor and was fed with low-strength synthetic wastewater throughout the study, while R2 was fed with medium strength sewage and UASB effluent over the study periods. Results Granules start-ups were observed on the 30th and 20th days in R1 and R2, respectively. In R1, the removal efficiency of COD, $ NH_{4} $+-N, total nitrogen (TN), and $ PO_{4} $3−-P was achieved 80.86%, 97.46%, 53.6%, and 45%, respectively. Whereas the removal efficiency of COD, $ NH_{4} $+-N, TN, and $ PO_{4} $3−-P was observed 63.61%, 58.18%, 50%, and 40%, respectively, in R2. The results indicated that the short aeration time, comprising 50% of the total cycle time over a 3-h duration, was the most effective operational phase for achieving high removal of organics and nutrients. Conclusion The study demonstrates that the A/O/A AGBR effectively cultivates AGB and removes organics and nutrients from anaerobic effluent. The use of medium-strength sewage as a substrate in R2 proved beneficial in reducing the granule start-up time for treating low-strength anaerobic effluent. Aerobic granules (dpeaa)DE-He213 Aerobic granular biomass reactor (dpeaa)DE-He213 Anaerobic effluent (dpeaa)DE-He213 Anaerobic phase (dpeaa)DE-He213 Oxic phase (dpeaa)DE-He213 Anoxic phase (dpeaa)DE-He213 Khan, Mohd Aamir aut Khan, Abid Ali aut Khatoon, Fehmeeda (orcid)0000-0002-0254-1252 aut Enthalten in Waste and biomass valorization [Dordrecht] : Springer Netherlands, 2010 15(2023), 2 vom: 27. Juni, Seite 945-958 (DE-627)620147245 (DE-600)2541900-6 1877-265X nnns volume:15 year:2023 number:2 day:27 month:06 pages:945-958 https://dx.doi.org/10.1007/s12649-023-02198-1 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_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_2119 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2144 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2188 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2446 GBV_ILN_2470 GBV_ILN_2472 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_2548 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_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 15 2023 2 27 06 945-958 |
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Springer Nature or its licensor (e.g. a society or other partner) holds exclusive rights to this article under a publishing agreement with the author(s) or other rightsholder(s); author self-archiving of the accepted manuscript version of this article is solely governed by the terms of such publishing agreement and applicable law.</subfield></datafield><datafield tag="520" ind1=" " ind2=" "><subfield code="a">Purpose The up-flow anaerobic sludge blanket reactor (UASB) treated effluent does not meet the national disposal standards of certain countries, such as India and Brazil. To meet the required standards, it is necessary to upgrade the UASB technology through a post-treatment system. The present work aimed to investigate the optimal operating conditions for the formation of granules in an anaerobic/oxic/anoxic (A/O/A) cyclic mode aerobic granular biomass reactor (AGBR) for the treatment of anaerobic effluent (UASB effluent). Methods Two rectangular reactors, R1 and R2, were used to cultivate aerobic granular biomass (AGB). R1 served as the control reactor and was fed with low-strength synthetic wastewater throughout the study, while R2 was fed with medium strength sewage and UASB effluent over the study periods. Results Granules start-ups were observed on the 30th and 20th days in R1 and R2, respectively. In R1, the removal efficiency of COD, $ NH_{4} $+-N, total nitrogen (TN), and $ PO_{4} $3−-P was achieved 80.86%, 97.46%, 53.6%, and 45%, respectively. Whereas the removal efficiency of COD, $ NH_{4} $+-N, TN, and $ PO_{4} $3−-P was observed 63.61%, 58.18%, 50%, and 40%, respectively, in R2. The results indicated that the short aeration time, comprising 50% of the total cycle time over a 3-h duration, was the most effective operational phase for achieving high removal of organics and nutrients. Conclusion The study demonstrates that the A/O/A AGBR effectively cultivates AGB and removes organics and nutrients from anaerobic effluent. 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Rayaz, Mohd |
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Rayaz, Mohd misc Aerobic granules misc Aerobic granular biomass reactor misc Anaerobic effluent misc Anaerobic phase misc Oxic phase misc Anoxic phase Start-up of Aerobic Granular Biomass System: Fate of Organics and Nutrients Removal From Anaerobic Effluent |
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Start-up of Aerobic Granular Biomass System: Fate of Organics and Nutrients Removal From Anaerobic Effluent Aerobic granules (dpeaa)DE-He213 Aerobic granular biomass reactor (dpeaa)DE-He213 Anaerobic effluent (dpeaa)DE-He213 Anaerobic phase (dpeaa)DE-He213 Oxic phase (dpeaa)DE-He213 Anoxic phase (dpeaa)DE-He213 |
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misc Aerobic granules misc Aerobic granular biomass reactor misc Anaerobic effluent misc Anaerobic phase misc Oxic phase misc Anoxic phase |
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start-up of aerobic granular biomass system: fate of organics and nutrients removal from anaerobic effluent |
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Start-up of Aerobic Granular Biomass System: Fate of Organics and Nutrients Removal From Anaerobic Effluent |
| abstract |
Purpose The up-flow anaerobic sludge blanket reactor (UASB) treated effluent does not meet the national disposal standards of certain countries, such as India and Brazil. To meet the required standards, it is necessary to upgrade the UASB technology through a post-treatment system. The present work aimed to investigate the optimal operating conditions for the formation of granules in an anaerobic/oxic/anoxic (A/O/A) cyclic mode aerobic granular biomass reactor (AGBR) for the treatment of anaerobic effluent (UASB effluent). Methods Two rectangular reactors, R1 and R2, were used to cultivate aerobic granular biomass (AGB). R1 served as the control reactor and was fed with low-strength synthetic wastewater throughout the study, while R2 was fed with medium strength sewage and UASB effluent over the study periods. Results Granules start-ups were observed on the 30th and 20th days in R1 and R2, respectively. In R1, the removal efficiency of COD, $ NH_{4} $+-N, total nitrogen (TN), and $ PO_{4} $3−-P was achieved 80.86%, 97.46%, 53.6%, and 45%, respectively. Whereas the removal efficiency of COD, $ NH_{4} $+-N, TN, and $ PO_{4} $3−-P was observed 63.61%, 58.18%, 50%, and 40%, respectively, in R2. The results indicated that the short aeration time, comprising 50% of the total cycle time over a 3-h duration, was the most effective operational phase for achieving high removal of organics and nutrients. Conclusion The study demonstrates that the A/O/A AGBR effectively cultivates AGB and removes organics and nutrients from anaerobic effluent. The use of medium-strength sewage as a substrate in R2 proved beneficial in reducing the granule start-up time for treating low-strength anaerobic effluent. © The Author(s), under exclusive licence to Springer Nature B.V. 2023. Springer Nature or its licensor (e.g. a society or other partner) holds exclusive rights to this article under a publishing agreement with the author(s) or other rightsholder(s); author self-archiving of the accepted manuscript version of this article is solely governed by the terms of such publishing agreement and applicable law. |
| abstractGer |
Purpose The up-flow anaerobic sludge blanket reactor (UASB) treated effluent does not meet the national disposal standards of certain countries, such as India and Brazil. To meet the required standards, it is necessary to upgrade the UASB technology through a post-treatment system. The present work aimed to investigate the optimal operating conditions for the formation of granules in an anaerobic/oxic/anoxic (A/O/A) cyclic mode aerobic granular biomass reactor (AGBR) for the treatment of anaerobic effluent (UASB effluent). Methods Two rectangular reactors, R1 and R2, were used to cultivate aerobic granular biomass (AGB). R1 served as the control reactor and was fed with low-strength synthetic wastewater throughout the study, while R2 was fed with medium strength sewage and UASB effluent over the study periods. Results Granules start-ups were observed on the 30th and 20th days in R1 and R2, respectively. In R1, the removal efficiency of COD, $ NH_{4} $+-N, total nitrogen (TN), and $ PO_{4} $3−-P was achieved 80.86%, 97.46%, 53.6%, and 45%, respectively. Whereas the removal efficiency of COD, $ NH_{4} $+-N, TN, and $ PO_{4} $3−-P was observed 63.61%, 58.18%, 50%, and 40%, respectively, in R2. The results indicated that the short aeration time, comprising 50% of the total cycle time over a 3-h duration, was the most effective operational phase for achieving high removal of organics and nutrients. Conclusion The study demonstrates that the A/O/A AGBR effectively cultivates AGB and removes organics and nutrients from anaerobic effluent. The use of medium-strength sewage as a substrate in R2 proved beneficial in reducing the granule start-up time for treating low-strength anaerobic effluent. © The Author(s), under exclusive licence to Springer Nature B.V. 2023. Springer Nature or its licensor (e.g. a society or other partner) holds exclusive rights to this article under a publishing agreement with the author(s) or other rightsholder(s); author self-archiving of the accepted manuscript version of this article is solely governed by the terms of such publishing agreement and applicable law. |
| abstract_unstemmed |
Purpose The up-flow anaerobic sludge blanket reactor (UASB) treated effluent does not meet the national disposal standards of certain countries, such as India and Brazil. To meet the required standards, it is necessary to upgrade the UASB technology through a post-treatment system. The present work aimed to investigate the optimal operating conditions for the formation of granules in an anaerobic/oxic/anoxic (A/O/A) cyclic mode aerobic granular biomass reactor (AGBR) for the treatment of anaerobic effluent (UASB effluent). Methods Two rectangular reactors, R1 and R2, were used to cultivate aerobic granular biomass (AGB). R1 served as the control reactor and was fed with low-strength synthetic wastewater throughout the study, while R2 was fed with medium strength sewage and UASB effluent over the study periods. Results Granules start-ups were observed on the 30th and 20th days in R1 and R2, respectively. In R1, the removal efficiency of COD, $ NH_{4} $+-N, total nitrogen (TN), and $ PO_{4} $3−-P was achieved 80.86%, 97.46%, 53.6%, and 45%, respectively. Whereas the removal efficiency of COD, $ NH_{4} $+-N, TN, and $ PO_{4} $3−-P was observed 63.61%, 58.18%, 50%, and 40%, respectively, in R2. The results indicated that the short aeration time, comprising 50% of the total cycle time over a 3-h duration, was the most effective operational phase for achieving high removal of organics and nutrients. Conclusion The study demonstrates that the A/O/A AGBR effectively cultivates AGB and removes organics and nutrients from anaerobic effluent. The use of medium-strength sewage as a substrate in R2 proved beneficial in reducing the granule start-up time for treating low-strength anaerobic effluent. © The Author(s), under exclusive licence to Springer Nature B.V. 2023. Springer Nature or its licensor (e.g. a society or other partner) holds exclusive rights to this article under a publishing agreement with the author(s) or other rightsholder(s); author self-archiving of the accepted manuscript version of this article is solely governed by the terms of such publishing agreement and applicable law. |
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Start-up of Aerobic Granular Biomass System: Fate of Organics and Nutrients Removal From Anaerobic Effluent |
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Khan, Mohd Aamir Khan, Abid Ali Khatoon, Fehmeeda |
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| score |
7.3986425 |