Treatment of dyeing wastewater by MIC anaerobic reactor
• A modified internal circulation anaerobic reactor including an external circulation system only within the 1st UASB was made. • The MIC reactor enhances mass transfer effect relative to the IC reactor. • Granular sludge was used as the seed sludge. • The optimal flow rate of external circulation i...
Ausführliche Beschreibung
Autor*in: |
Wang, Jiade [verfasserIn] |
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Format: |
E-Artikel |
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Sprache: |
Englisch |
Erschienen: |
2015 |
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Umfang: |
6 |
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Übergeordnetes Werk: |
Enthalten in: Biofuel recovery from microalgae biomass grown in dairy wastewater treated with activated sludge: The next step in sustainable production - de Mendonça, Henrique Vieira ELSEVIER, 2022, an international journal of research and development, Amsterdam [u.a.] |
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Übergeordnetes Werk: |
volume:101 ; year:2015 ; day:15 ; month:09 ; pages:179-184 ; extent:6 |
Links: |
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DOI / URN: |
10.1016/j.bej.2015.06.001 |
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ELV01819575X |
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10.1016/j.bej.2015.06.001 doi GBVA2015002000028.pica (DE-627)ELV01819575X (ELSEVIER)S1369-703X(15)00194-1 DE-627 ger DE-627 rakwb eng 660 540 660 DE-600 540 DE-600 333.7 610 VZ 43.12 bkl 43.13 bkl 44.13 bkl Wang, Jiade verfasserin aut Treatment of dyeing wastewater by MIC anaerobic reactor 2015 6 nicht spezifiziert zzz rdacontent nicht spezifiziert z rdamedia nicht spezifiziert zu rdacarrier • A modified internal circulation anaerobic reactor including an external circulation system only within the 1st UASB was made. • The MIC reactor enhances mass transfer effect relative to the IC reactor. • Granular sludge was used as the seed sludge. • The optimal flow rate of external circulation in MIC reactor was 420L/h. • Applying the modified Stover–Kincannon model to the MIC reactor. MIC anaerobic reactor Elsevier Modified Stover–Kincannon model Elsevier Mixing Elsevier Biogas Elsevier Waste-water treatment Elsevier Mass transfer Elsevier Yan, Jingjia oth Xu, Weijun oth Enthalten in Elsevier de Mendonça, Henrique Vieira ELSEVIER Biofuel recovery from microalgae biomass grown in dairy wastewater treated with activated sludge: The next step in sustainable production 2022 an international journal of research and development Amsterdam [u.a.] (DE-627)ELV007707568 volume:101 year:2015 day:15 month:09 pages:179-184 extent:6 https://doi.org/10.1016/j.bej.2015.06.001 Volltext GBV_USEFLAG_U GBV_ELV SYSFLAG_U SSG-OLC-PHA SSG-OPC-GGO 43.12 Umweltchemie VZ 43.13 Umwelttoxikologie VZ 44.13 Medizinische Ökologie VZ AR 101 2015 15 0915 179-184 6 045F 660 |
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10.1016/j.bej.2015.06.001 doi GBVA2015002000028.pica (DE-627)ELV01819575X (ELSEVIER)S1369-703X(15)00194-1 DE-627 ger DE-627 rakwb eng 660 540 660 DE-600 540 DE-600 333.7 610 VZ 43.12 bkl 43.13 bkl 44.13 bkl Wang, Jiade verfasserin aut Treatment of dyeing wastewater by MIC anaerobic reactor 2015 6 nicht spezifiziert zzz rdacontent nicht spezifiziert z rdamedia nicht spezifiziert zu rdacarrier • A modified internal circulation anaerobic reactor including an external circulation system only within the 1st UASB was made. • The MIC reactor enhances mass transfer effect relative to the IC reactor. • Granular sludge was used as the seed sludge. • The optimal flow rate of external circulation in MIC reactor was 420L/h. • Applying the modified Stover–Kincannon model to the MIC reactor. MIC anaerobic reactor Elsevier Modified Stover–Kincannon model Elsevier Mixing Elsevier Biogas Elsevier Waste-water treatment Elsevier Mass transfer Elsevier Yan, Jingjia oth Xu, Weijun oth Enthalten in Elsevier de Mendonça, Henrique Vieira ELSEVIER Biofuel recovery from microalgae biomass grown in dairy wastewater treated with activated sludge: The next step in sustainable production 2022 an international journal of research and development Amsterdam [u.a.] (DE-627)ELV007707568 volume:101 year:2015 day:15 month:09 pages:179-184 extent:6 https://doi.org/10.1016/j.bej.2015.06.001 Volltext GBV_USEFLAG_U GBV_ELV SYSFLAG_U SSG-OLC-PHA SSG-OPC-GGO 43.12 Umweltchemie VZ 43.13 Umwelttoxikologie VZ 44.13 Medizinische Ökologie VZ AR 101 2015 15 0915 179-184 6 045F 660 |
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10.1016/j.bej.2015.06.001 doi GBVA2015002000028.pica (DE-627)ELV01819575X (ELSEVIER)S1369-703X(15)00194-1 DE-627 ger DE-627 rakwb eng 660 540 660 DE-600 540 DE-600 333.7 610 VZ 43.12 bkl 43.13 bkl 44.13 bkl Wang, Jiade verfasserin aut Treatment of dyeing wastewater by MIC anaerobic reactor 2015 6 nicht spezifiziert zzz rdacontent nicht spezifiziert z rdamedia nicht spezifiziert zu rdacarrier • A modified internal circulation anaerobic reactor including an external circulation system only within the 1st UASB was made. • The MIC reactor enhances mass transfer effect relative to the IC reactor. • Granular sludge was used as the seed sludge. • The optimal flow rate of external circulation in MIC reactor was 420L/h. • Applying the modified Stover–Kincannon model to the MIC reactor. MIC anaerobic reactor Elsevier Modified Stover–Kincannon model Elsevier Mixing Elsevier Biogas Elsevier Waste-water treatment Elsevier Mass transfer Elsevier Yan, Jingjia oth Xu, Weijun oth Enthalten in Elsevier de Mendonça, Henrique Vieira ELSEVIER Biofuel recovery from microalgae biomass grown in dairy wastewater treated with activated sludge: The next step in sustainable production 2022 an international journal of research and development Amsterdam [u.a.] (DE-627)ELV007707568 volume:101 year:2015 day:15 month:09 pages:179-184 extent:6 https://doi.org/10.1016/j.bej.2015.06.001 Volltext GBV_USEFLAG_U GBV_ELV SYSFLAG_U SSG-OLC-PHA SSG-OPC-GGO 43.12 Umweltchemie VZ 43.13 Umwelttoxikologie VZ 44.13 Medizinische Ökologie VZ AR 101 2015 15 0915 179-184 6 045F 660 |
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10.1016/j.bej.2015.06.001 doi GBVA2015002000028.pica (DE-627)ELV01819575X (ELSEVIER)S1369-703X(15)00194-1 DE-627 ger DE-627 rakwb eng 660 540 660 DE-600 540 DE-600 333.7 610 VZ 43.12 bkl 43.13 bkl 44.13 bkl Wang, Jiade verfasserin aut Treatment of dyeing wastewater by MIC anaerobic reactor 2015 6 nicht spezifiziert zzz rdacontent nicht spezifiziert z rdamedia nicht spezifiziert zu rdacarrier • A modified internal circulation anaerobic reactor including an external circulation system only within the 1st UASB was made. • The MIC reactor enhances mass transfer effect relative to the IC reactor. • Granular sludge was used as the seed sludge. • The optimal flow rate of external circulation in MIC reactor was 420L/h. • Applying the modified Stover–Kincannon model to the MIC reactor. MIC anaerobic reactor Elsevier Modified Stover–Kincannon model Elsevier Mixing Elsevier Biogas Elsevier Waste-water treatment Elsevier Mass transfer Elsevier Yan, Jingjia oth Xu, Weijun oth Enthalten in Elsevier de Mendonça, Henrique Vieira ELSEVIER Biofuel recovery from microalgae biomass grown in dairy wastewater treated with activated sludge: The next step in sustainable production 2022 an international journal of research and development Amsterdam [u.a.] (DE-627)ELV007707568 volume:101 year:2015 day:15 month:09 pages:179-184 extent:6 https://doi.org/10.1016/j.bej.2015.06.001 Volltext GBV_USEFLAG_U GBV_ELV SYSFLAG_U SSG-OLC-PHA SSG-OPC-GGO 43.12 Umweltchemie VZ 43.13 Umwelttoxikologie VZ 44.13 Medizinische Ökologie VZ AR 101 2015 15 0915 179-184 6 045F 660 |
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treatment of dyeing wastewater by mic anaerobic reactor |
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Treatment of dyeing wastewater by MIC anaerobic reactor |
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• A modified internal circulation anaerobic reactor including an external circulation system only within the 1st UASB was made. • The MIC reactor enhances mass transfer effect relative to the IC reactor. • Granular sludge was used as the seed sludge. • The optimal flow rate of external circulation in MIC reactor was 420L/h. • Applying the modified Stover–Kincannon model to the MIC reactor. |
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• A modified internal circulation anaerobic reactor including an external circulation system only within the 1st UASB was made. • The MIC reactor enhances mass transfer effect relative to the IC reactor. • Granular sludge was used as the seed sludge. • The optimal flow rate of external circulation in MIC reactor was 420L/h. • Applying the modified Stover–Kincannon model to the MIC reactor. |
abstract_unstemmed |
• A modified internal circulation anaerobic reactor including an external circulation system only within the 1st UASB was made. • The MIC reactor enhances mass transfer effect relative to the IC reactor. • Granular sludge was used as the seed sludge. • The optimal flow rate of external circulation in MIC reactor was 420L/h. • Applying the modified Stover–Kincannon model to the MIC reactor. |
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Treatment of dyeing wastewater by MIC anaerobic reactor |
url |
https://doi.org/10.1016/j.bej.2015.06.001 |
remote_bool |
true |
author2 |
Yan, Jingjia Xu, Weijun |
author2Str |
Yan, Jingjia Xu, Weijun |
ppnlink |
ELV007707568 |
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isOA_txt |
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hochschulschrift_bool |
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author2_role |
oth oth |
doi_str |
10.1016/j.bej.2015.06.001 |
up_date |
2024-07-06T18:14:36.349Z |
_version_ |
1803854467668377600 |
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