High-rate anaerobic digestion of sewage sludge by membrane separation solubilization coupled with UASB process
Abstract Conventional anaerobic digestion (AD) process was often slow and thus required a large digestion tank. Upflow anaerobic sludge blanket (UASB) reactor is an AD technology intended mainly to treat wastewater with a short hydraulic retention time (HRT). However, the potential of this reactor w...
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| Autor*in: |
Yoshida, Gen [verfasserIn] |
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| Format: |
E-Artikel |
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| Sprache: |
Englisch |
| Erschienen: |
2021 |
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| Schlagwörter: |
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| Anmerkung: |
© Springer Japan KK, part of Springer Nature 2021 |
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| Übergeordnetes Werk: |
Enthalten in: Journal of material cycles and waste management - Tokyo [u.a.] : Springer, 1999, 24(2021), 1 vom: 23. Nov., Seite 402-409 |
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| Übergeordnetes Werk: |
volume:24 ; year:2021 ; number:1 ; day:23 ; month:11 ; pages:402-409 |
| Links: |
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| DOI / URN: |
10.1007/s10163-021-01331-3 |
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| Katalog-ID: |
SPR045942382 |
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| 520 | |a Abstract Conventional anaerobic digestion (AD) process was often slow and thus required a large digestion tank. Upflow anaerobic sludge blanket (UASB) reactor is an AD technology intended mainly to treat wastewater with a short hydraulic retention time (HRT). However, the potential of this reactor was often limited when treating wet solid biomass. In this study, the performance of anaerobic submerged membrane bioreactor (AnMBR) was investigated under acidic condition by varying the hydraulic retention time (HRT), from 1.5 d to 2.5 d, and sludge retention time (SRT), from 6 to 12 d, of a mixture of primary and excess sludge. The acidic permeate was thereafter utilized in a UASB reactor at an HRT of 0.5 d. The results showed a COD reduction between 26 and 36% in the AnMBR, while the average COD removal rate was 83% in the UASB reactor. The average pH in the AnMBR was 5.40 and the transmembrane pressure was below 45 mbar throughout the experimental period. The average methane yield in the UASB reactor was 0.25 L/gCOD. These results implied that operating AnMBR under acidic condition is an alternative process to minimize membrane fouling and increase the energy footprint of an AD system. | ||
| 650 | 4 | |a Anaerobic membrane bioreactor |7 (dpeaa)DE-He213 | |
| 650 | 4 | |a Upflow anaerobic sludge blanket |7 (dpeaa)DE-He213 | |
| 650 | 4 | |a Acidic condition |7 (dpeaa)DE-He213 | |
| 650 | 4 | |a Sludge retention time |7 (dpeaa)DE-He213 | |
| 650 | 4 | |a Sewage sludge |7 (dpeaa)DE-He213 | |
| 700 | 1 | |a Seyama, Tomohiro |4 aut | |
| 700 | 1 | |a Andriamanohiarisoamanana, Fetra J. |4 aut | |
| 700 | 1 | |a Hirayasu, Hirofumi |4 aut | |
| 700 | 1 | |a Kasai, Koji |4 aut | |
| 700 | 1 | |a Ihara, Ikko |4 aut | |
| 773 | 0 | 8 | |i Enthalten in |t Journal of material cycles and waste management |d Tokyo [u.a.] : Springer, 1999 |g 24(2021), 1 vom: 23. Nov., Seite 402-409 |w (DE-627)364472340 |w (DE-600)2110671-X |x 1611-8227 |7 nnns |
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10.1007/s10163-021-01331-3 doi (DE-627)SPR045942382 (SPR)s10163-021-01331-3-e DE-627 ger DE-627 rakwb eng Yoshida, Gen verfasserin (orcid)0000-0002-3663-3147 aut High-rate anaerobic digestion of sewage sludge by membrane separation solubilization coupled with UASB process 2021 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © Springer Japan KK, part of Springer Nature 2021 Abstract Conventional anaerobic digestion (AD) process was often slow and thus required a large digestion tank. Upflow anaerobic sludge blanket (UASB) reactor is an AD technology intended mainly to treat wastewater with a short hydraulic retention time (HRT). However, the potential of this reactor was often limited when treating wet solid biomass. In this study, the performance of anaerobic submerged membrane bioreactor (AnMBR) was investigated under acidic condition by varying the hydraulic retention time (HRT), from 1.5 d to 2.5 d, and sludge retention time (SRT), from 6 to 12 d, of a mixture of primary and excess sludge. The acidic permeate was thereafter utilized in a UASB reactor at an HRT of 0.5 d. The results showed a COD reduction between 26 and 36% in the AnMBR, while the average COD removal rate was 83% in the UASB reactor. The average pH in the AnMBR was 5.40 and the transmembrane pressure was below 45 mbar throughout the experimental period. The average methane yield in the UASB reactor was 0.25 L/gCOD. These results implied that operating AnMBR under acidic condition is an alternative process to minimize membrane fouling and increase the energy footprint of an AD system. Anaerobic membrane bioreactor (dpeaa)DE-He213 Upflow anaerobic sludge blanket (dpeaa)DE-He213 Acidic condition (dpeaa)DE-He213 Sludge retention time (dpeaa)DE-He213 Sewage sludge (dpeaa)DE-He213 Seyama, Tomohiro aut Andriamanohiarisoamanana, Fetra J. aut Hirayasu, Hirofumi aut Kasai, Koji aut Ihara, Ikko aut Enthalten in Journal of material cycles and waste management Tokyo [u.a.] : Springer, 1999 24(2021), 1 vom: 23. Nov., Seite 402-409 (DE-627)364472340 (DE-600)2110671-X 1611-8227 nnns volume:24 year:2021 number:1 day:23 month:11 pages:402-409 https://dx.doi.org/10.1007/s10163-021-01331-3 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_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 24 2021 1 23 11 402-409 |
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10.1007/s10163-021-01331-3 doi (DE-627)SPR045942382 (SPR)s10163-021-01331-3-e DE-627 ger DE-627 rakwb eng Yoshida, Gen verfasserin (orcid)0000-0002-3663-3147 aut High-rate anaerobic digestion of sewage sludge by membrane separation solubilization coupled with UASB process 2021 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © Springer Japan KK, part of Springer Nature 2021 Abstract Conventional anaerobic digestion (AD) process was often slow and thus required a large digestion tank. Upflow anaerobic sludge blanket (UASB) reactor is an AD technology intended mainly to treat wastewater with a short hydraulic retention time (HRT). However, the potential of this reactor was often limited when treating wet solid biomass. In this study, the performance of anaerobic submerged membrane bioreactor (AnMBR) was investigated under acidic condition by varying the hydraulic retention time (HRT), from 1.5 d to 2.5 d, and sludge retention time (SRT), from 6 to 12 d, of a mixture of primary and excess sludge. The acidic permeate was thereafter utilized in a UASB reactor at an HRT of 0.5 d. The results showed a COD reduction between 26 and 36% in the AnMBR, while the average COD removal rate was 83% in the UASB reactor. The average pH in the AnMBR was 5.40 and the transmembrane pressure was below 45 mbar throughout the experimental period. The average methane yield in the UASB reactor was 0.25 L/gCOD. These results implied that operating AnMBR under acidic condition is an alternative process to minimize membrane fouling and increase the energy footprint of an AD system. Anaerobic membrane bioreactor (dpeaa)DE-He213 Upflow anaerobic sludge blanket (dpeaa)DE-He213 Acidic condition (dpeaa)DE-He213 Sludge retention time (dpeaa)DE-He213 Sewage sludge (dpeaa)DE-He213 Seyama, Tomohiro aut Andriamanohiarisoamanana, Fetra J. aut Hirayasu, Hirofumi aut Kasai, Koji aut Ihara, Ikko aut Enthalten in Journal of material cycles and waste management Tokyo [u.a.] : Springer, 1999 24(2021), 1 vom: 23. Nov., Seite 402-409 (DE-627)364472340 (DE-600)2110671-X 1611-8227 nnns volume:24 year:2021 number:1 day:23 month:11 pages:402-409 https://dx.doi.org/10.1007/s10163-021-01331-3 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_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 24 2021 1 23 11 402-409 |
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10.1007/s10163-021-01331-3 doi (DE-627)SPR045942382 (SPR)s10163-021-01331-3-e DE-627 ger DE-627 rakwb eng Yoshida, Gen verfasserin (orcid)0000-0002-3663-3147 aut High-rate anaerobic digestion of sewage sludge by membrane separation solubilization coupled with UASB process 2021 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © Springer Japan KK, part of Springer Nature 2021 Abstract Conventional anaerobic digestion (AD) process was often slow and thus required a large digestion tank. Upflow anaerobic sludge blanket (UASB) reactor is an AD technology intended mainly to treat wastewater with a short hydraulic retention time (HRT). However, the potential of this reactor was often limited when treating wet solid biomass. In this study, the performance of anaerobic submerged membrane bioreactor (AnMBR) was investigated under acidic condition by varying the hydraulic retention time (HRT), from 1.5 d to 2.5 d, and sludge retention time (SRT), from 6 to 12 d, of a mixture of primary and excess sludge. The acidic permeate was thereafter utilized in a UASB reactor at an HRT of 0.5 d. The results showed a COD reduction between 26 and 36% in the AnMBR, while the average COD removal rate was 83% in the UASB reactor. The average pH in the AnMBR was 5.40 and the transmembrane pressure was below 45 mbar throughout the experimental period. The average methane yield in the UASB reactor was 0.25 L/gCOD. These results implied that operating AnMBR under acidic condition is an alternative process to minimize membrane fouling and increase the energy footprint of an AD system. Anaerobic membrane bioreactor (dpeaa)DE-He213 Upflow anaerobic sludge blanket (dpeaa)DE-He213 Acidic condition (dpeaa)DE-He213 Sludge retention time (dpeaa)DE-He213 Sewage sludge (dpeaa)DE-He213 Seyama, Tomohiro aut Andriamanohiarisoamanana, Fetra J. aut Hirayasu, Hirofumi aut Kasai, Koji aut Ihara, Ikko aut Enthalten in Journal of material cycles and waste management Tokyo [u.a.] : Springer, 1999 24(2021), 1 vom: 23. Nov., Seite 402-409 (DE-627)364472340 (DE-600)2110671-X 1611-8227 nnns volume:24 year:2021 number:1 day:23 month:11 pages:402-409 https://dx.doi.org/10.1007/s10163-021-01331-3 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_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 24 2021 1 23 11 402-409 |
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10.1007/s10163-021-01331-3 doi (DE-627)SPR045942382 (SPR)s10163-021-01331-3-e DE-627 ger DE-627 rakwb eng Yoshida, Gen verfasserin (orcid)0000-0002-3663-3147 aut High-rate anaerobic digestion of sewage sludge by membrane separation solubilization coupled with UASB process 2021 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © Springer Japan KK, part of Springer Nature 2021 Abstract Conventional anaerobic digestion (AD) process was often slow and thus required a large digestion tank. Upflow anaerobic sludge blanket (UASB) reactor is an AD technology intended mainly to treat wastewater with a short hydraulic retention time (HRT). However, the potential of this reactor was often limited when treating wet solid biomass. In this study, the performance of anaerobic submerged membrane bioreactor (AnMBR) was investigated under acidic condition by varying the hydraulic retention time (HRT), from 1.5 d to 2.5 d, and sludge retention time (SRT), from 6 to 12 d, of a mixture of primary and excess sludge. The acidic permeate was thereafter utilized in a UASB reactor at an HRT of 0.5 d. The results showed a COD reduction between 26 and 36% in the AnMBR, while the average COD removal rate was 83% in the UASB reactor. The average pH in the AnMBR was 5.40 and the transmembrane pressure was below 45 mbar throughout the experimental period. The average methane yield in the UASB reactor was 0.25 L/gCOD. These results implied that operating AnMBR under acidic condition is an alternative process to minimize membrane fouling and increase the energy footprint of an AD system. Anaerobic membrane bioreactor (dpeaa)DE-He213 Upflow anaerobic sludge blanket (dpeaa)DE-He213 Acidic condition (dpeaa)DE-He213 Sludge retention time (dpeaa)DE-He213 Sewage sludge (dpeaa)DE-He213 Seyama, Tomohiro aut Andriamanohiarisoamanana, Fetra J. aut Hirayasu, Hirofumi aut Kasai, Koji aut Ihara, Ikko aut Enthalten in Journal of material cycles and waste management Tokyo [u.a.] : Springer, 1999 24(2021), 1 vom: 23. Nov., Seite 402-409 (DE-627)364472340 (DE-600)2110671-X 1611-8227 nnns volume:24 year:2021 number:1 day:23 month:11 pages:402-409 https://dx.doi.org/10.1007/s10163-021-01331-3 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_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 24 2021 1 23 11 402-409 |
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10.1007/s10163-021-01331-3 doi (DE-627)SPR045942382 (SPR)s10163-021-01331-3-e DE-627 ger DE-627 rakwb eng Yoshida, Gen verfasserin (orcid)0000-0002-3663-3147 aut High-rate anaerobic digestion of sewage sludge by membrane separation solubilization coupled with UASB process 2021 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © Springer Japan KK, part of Springer Nature 2021 Abstract Conventional anaerobic digestion (AD) process was often slow and thus required a large digestion tank. Upflow anaerobic sludge blanket (UASB) reactor is an AD technology intended mainly to treat wastewater with a short hydraulic retention time (HRT). However, the potential of this reactor was often limited when treating wet solid biomass. In this study, the performance of anaerobic submerged membrane bioreactor (AnMBR) was investigated under acidic condition by varying the hydraulic retention time (HRT), from 1.5 d to 2.5 d, and sludge retention time (SRT), from 6 to 12 d, of a mixture of primary and excess sludge. The acidic permeate was thereafter utilized in a UASB reactor at an HRT of 0.5 d. The results showed a COD reduction between 26 and 36% in the AnMBR, while the average COD removal rate was 83% in the UASB reactor. The average pH in the AnMBR was 5.40 and the transmembrane pressure was below 45 mbar throughout the experimental period. The average methane yield in the UASB reactor was 0.25 L/gCOD. These results implied that operating AnMBR under acidic condition is an alternative process to minimize membrane fouling and increase the energy footprint of an AD system. Anaerobic membrane bioreactor (dpeaa)DE-He213 Upflow anaerobic sludge blanket (dpeaa)DE-He213 Acidic condition (dpeaa)DE-He213 Sludge retention time (dpeaa)DE-He213 Sewage sludge (dpeaa)DE-He213 Seyama, Tomohiro aut Andriamanohiarisoamanana, Fetra J. aut Hirayasu, Hirofumi aut Kasai, Koji aut Ihara, Ikko aut Enthalten in Journal of material cycles and waste management Tokyo [u.a.] : Springer, 1999 24(2021), 1 vom: 23. Nov., Seite 402-409 (DE-627)364472340 (DE-600)2110671-X 1611-8227 nnns volume:24 year:2021 number:1 day:23 month:11 pages:402-409 https://dx.doi.org/10.1007/s10163-021-01331-3 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_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 24 2021 1 23 11 402-409 |
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Enthalten in Journal of material cycles and waste management 24(2021), 1 vom: 23. Nov., Seite 402-409 volume:24 year:2021 number:1 day:23 month:11 pages:402-409 |
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Anaerobic membrane bioreactor Upflow anaerobic sludge blanket Acidic condition Sludge retention time Sewage sludge |
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Journal of material cycles and waste management |
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Yoshida, Gen @@aut@@ Seyama, Tomohiro @@aut@@ Andriamanohiarisoamanana, Fetra J. @@aut@@ Hirayasu, Hirofumi @@aut@@ Kasai, Koji @@aut@@ Ihara, Ikko @@aut@@ |
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Yoshida, Gen |
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Yoshida, Gen misc Anaerobic membrane bioreactor misc Upflow anaerobic sludge blanket misc Acidic condition misc Sludge retention time misc Sewage sludge High-rate anaerobic digestion of sewage sludge by membrane separation solubilization coupled with UASB process |
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High-rate anaerobic digestion of sewage sludge by membrane separation solubilization coupled with UASB process Anaerobic membrane bioreactor (dpeaa)DE-He213 Upflow anaerobic sludge blanket (dpeaa)DE-He213 Acidic condition (dpeaa)DE-He213 Sludge retention time (dpeaa)DE-He213 Sewage sludge (dpeaa)DE-He213 |
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High-rate anaerobic digestion of sewage sludge by membrane separation solubilization coupled with UASB process |
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Yoshida, Gen Seyama, Tomohiro Andriamanohiarisoamanana, Fetra J. Hirayasu, Hirofumi Kasai, Koji Ihara, Ikko |
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high-rate anaerobic digestion of sewage sludge by membrane separation solubilization coupled with uasb process |
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High-rate anaerobic digestion of sewage sludge by membrane separation solubilization coupled with UASB process |
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Abstract Conventional anaerobic digestion (AD) process was often slow and thus required a large digestion tank. Upflow anaerobic sludge blanket (UASB) reactor is an AD technology intended mainly to treat wastewater with a short hydraulic retention time (HRT). However, the potential of this reactor was often limited when treating wet solid biomass. In this study, the performance of anaerobic submerged membrane bioreactor (AnMBR) was investigated under acidic condition by varying the hydraulic retention time (HRT), from 1.5 d to 2.5 d, and sludge retention time (SRT), from 6 to 12 d, of a mixture of primary and excess sludge. The acidic permeate was thereafter utilized in a UASB reactor at an HRT of 0.5 d. The results showed a COD reduction between 26 and 36% in the AnMBR, while the average COD removal rate was 83% in the UASB reactor. The average pH in the AnMBR was 5.40 and the transmembrane pressure was below 45 mbar throughout the experimental period. The average methane yield in the UASB reactor was 0.25 L/gCOD. These results implied that operating AnMBR under acidic condition is an alternative process to minimize membrane fouling and increase the energy footprint of an AD system. © Springer Japan KK, part of Springer Nature 2021 |
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Abstract Conventional anaerobic digestion (AD) process was often slow and thus required a large digestion tank. Upflow anaerobic sludge blanket (UASB) reactor is an AD technology intended mainly to treat wastewater with a short hydraulic retention time (HRT). However, the potential of this reactor was often limited when treating wet solid biomass. In this study, the performance of anaerobic submerged membrane bioreactor (AnMBR) was investigated under acidic condition by varying the hydraulic retention time (HRT), from 1.5 d to 2.5 d, and sludge retention time (SRT), from 6 to 12 d, of a mixture of primary and excess sludge. The acidic permeate was thereafter utilized in a UASB reactor at an HRT of 0.5 d. The results showed a COD reduction between 26 and 36% in the AnMBR, while the average COD removal rate was 83% in the UASB reactor. The average pH in the AnMBR was 5.40 and the transmembrane pressure was below 45 mbar throughout the experimental period. The average methane yield in the UASB reactor was 0.25 L/gCOD. These results implied that operating AnMBR under acidic condition is an alternative process to minimize membrane fouling and increase the energy footprint of an AD system. © Springer Japan KK, part of Springer Nature 2021 |
| abstract_unstemmed |
Abstract Conventional anaerobic digestion (AD) process was often slow and thus required a large digestion tank. Upflow anaerobic sludge blanket (UASB) reactor is an AD technology intended mainly to treat wastewater with a short hydraulic retention time (HRT). However, the potential of this reactor was often limited when treating wet solid biomass. In this study, the performance of anaerobic submerged membrane bioreactor (AnMBR) was investigated under acidic condition by varying the hydraulic retention time (HRT), from 1.5 d to 2.5 d, and sludge retention time (SRT), from 6 to 12 d, of a mixture of primary and excess sludge. The acidic permeate was thereafter utilized in a UASB reactor at an HRT of 0.5 d. The results showed a COD reduction between 26 and 36% in the AnMBR, while the average COD removal rate was 83% in the UASB reactor. The average pH in the AnMBR was 5.40 and the transmembrane pressure was below 45 mbar throughout the experimental period. The average methane yield in the UASB reactor was 0.25 L/gCOD. These results implied that operating AnMBR under acidic condition is an alternative process to minimize membrane fouling and increase the energy footprint of an AD system. © Springer Japan KK, part of Springer Nature 2021 |
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High-rate anaerobic digestion of sewage sludge by membrane separation solubilization coupled with UASB process |
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https://dx.doi.org/10.1007/s10163-021-01331-3 |
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Seyama, Tomohiro Andriamanohiarisoamanana, Fetra J. Hirayasu, Hirofumi Kasai, Koji Ihara, Ikko |
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Seyama, Tomohiro Andriamanohiarisoamanana, Fetra J. Hirayasu, Hirofumi Kasai, Koji Ihara, Ikko |
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10.1007/s10163-021-01331-3 |
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2024-07-03T19:18:26.722Z |
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| score |
7.40018 |