Nitrification and denitrification in a system of reciprocating jet bioreactor
Abstract Concept of separation of stages coupled with novel design of reciprocating jet bioreactor have been incorporated in this research for the development of high efficiency treatment system for contaminated wastewaters. Evaluation of pilot plant data reveals that a three stage reciprocating jet...
Ausführliche Beschreibung
Gespeichert in:
| Autor*in: |
Brauer, H. [verfasserIn] |
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| Format: |
Artikel |
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| Sprache: |
Englisch |
| Erschienen: |
1992 |
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| Schlagwörter: |
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| Anmerkung: |
© Springer-Verlag 1992 |
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| Übergeordnetes Werk: |
Enthalten in: Bioprocess engineering - Springer-Verlag, 1986, 7(1992), 6 vom: März, Seite 269-275 |
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| Übergeordnetes Werk: |
volume:7 ; year:1992 ; number:6 ; month:03 ; pages:269-275 |
| Links: |
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| DOI / URN: |
10.1007/BF00386237 |
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| Katalog-ID: |
OLC2106596863 |
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| 520 | |a Abstract Concept of separation of stages coupled with novel design of reciprocating jet bioreactor have been incorporated in this research for the development of high efficiency treatment system for contaminated wastewaters. Evaluation of pilot plant data reveals that a three stage reciprocating jet bioreactor system could be effectively employed for nitrification and denitrification of highly polluted wastewater obtained from Berlin wastewater treatment plant. Such a system with COD destruction stage (residence time 1–3 hours) followed by nitrification stage (residence time 3–4.5 hours) and denitrification stage (residence time 0.3 hours) gives COD destruction rate upto 58 kg COD/($ m^{3} $ day), nitrification rate upto 3.2 NH4+-N/($ m^{3} $ day) and denitrification rate upto 28 kg NO3−-N/($ m^{3} $ day) while providing COD, NH4+-N and NO3−-N conversion of more than 90%. Nitrification and denitrification of wastewater at such a short residence time is possible mainly due to the employment of reciprocating jet bioreactor system. | ||
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10.1007/BF00386237 doi (DE-627)OLC2106596863 (DE-He213)BF00386237-p DE-627 ger DE-627 rakwb eng 570 690 540 VZ 12 ssgn Brauer, H. verfasserin aut Nitrification and denitrification in a system of reciprocating jet bioreactor 1992 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier © Springer-Verlag 1992 Abstract Concept of separation of stages coupled with novel design of reciprocating jet bioreactor have been incorporated in this research for the development of high efficiency treatment system for contaminated wastewaters. Evaluation of pilot plant data reveals that a three stage reciprocating jet bioreactor system could be effectively employed for nitrification and denitrification of highly polluted wastewater obtained from Berlin wastewater treatment plant. Such a system with COD destruction stage (residence time 1–3 hours) followed by nitrification stage (residence time 3–4.5 hours) and denitrification stage (residence time 0.3 hours) gives COD destruction rate upto 58 kg COD/($ m^{3} $ day), nitrification rate upto 3.2 NH4+-N/($ m^{3} $ day) and denitrification rate upto 28 kg NO3−-N/($ m^{3} $ day) while providing COD, NH4+-N and NO3−-N conversion of more than 90%. Nitrification and denitrification of wastewater at such a short residence time is possible mainly due to the employment of reciprocating jet bioreactor system. Nitrification Wastewater Denitrification Wastewater Treatment Wastewater Treatment Plant Annachhatre, A. P. aut Enthalten in Bioprocess engineering Springer-Verlag, 1986 7(1992), 6 vom: März, Seite 269-275 (DE-627)129208922 (DE-600)55154-5 (DE-576)01445761X 0178-515X nnns volume:7 year:1992 number:6 month:03 pages:269-275 https://doi.org/10.1007/BF00386237 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-UMW SSG-OLC-ARC SSG-OLC-TEC SSG-OLC-CHE GBV_ILN_11 GBV_ILN_23 GBV_ILN_32 GBV_ILN_40 GBV_ILN_65 GBV_ILN_70 GBV_ILN_2004 GBV_ILN_2006 GBV_ILN_2018 GBV_ILN_4046 GBV_ILN_4103 GBV_ILN_4307 GBV_ILN_4310 GBV_ILN_4323 GBV_ILN_4328 AR 7 1992 6 03 269-275 |
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10.1007/BF00386237 doi (DE-627)OLC2106596863 (DE-He213)BF00386237-p DE-627 ger DE-627 rakwb eng 570 690 540 VZ 12 ssgn Brauer, H. verfasserin aut Nitrification and denitrification in a system of reciprocating jet bioreactor 1992 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier © Springer-Verlag 1992 Abstract Concept of separation of stages coupled with novel design of reciprocating jet bioreactor have been incorporated in this research for the development of high efficiency treatment system for contaminated wastewaters. Evaluation of pilot plant data reveals that a three stage reciprocating jet bioreactor system could be effectively employed for nitrification and denitrification of highly polluted wastewater obtained from Berlin wastewater treatment plant. Such a system with COD destruction stage (residence time 1–3 hours) followed by nitrification stage (residence time 3–4.5 hours) and denitrification stage (residence time 0.3 hours) gives COD destruction rate upto 58 kg COD/($ m^{3} $ day), nitrification rate upto 3.2 NH4+-N/($ m^{3} $ day) and denitrification rate upto 28 kg NO3−-N/($ m^{3} $ day) while providing COD, NH4+-N and NO3−-N conversion of more than 90%. Nitrification and denitrification of wastewater at such a short residence time is possible mainly due to the employment of reciprocating jet bioreactor system. Nitrification Wastewater Denitrification Wastewater Treatment Wastewater Treatment Plant Annachhatre, A. P. aut Enthalten in Bioprocess engineering Springer-Verlag, 1986 7(1992), 6 vom: März, Seite 269-275 (DE-627)129208922 (DE-600)55154-5 (DE-576)01445761X 0178-515X nnns volume:7 year:1992 number:6 month:03 pages:269-275 https://doi.org/10.1007/BF00386237 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-UMW SSG-OLC-ARC SSG-OLC-TEC SSG-OLC-CHE GBV_ILN_11 GBV_ILN_23 GBV_ILN_32 GBV_ILN_40 GBV_ILN_65 GBV_ILN_70 GBV_ILN_2004 GBV_ILN_2006 GBV_ILN_2018 GBV_ILN_4046 GBV_ILN_4103 GBV_ILN_4307 GBV_ILN_4310 GBV_ILN_4323 GBV_ILN_4328 AR 7 1992 6 03 269-275 |
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10.1007/BF00386237 doi (DE-627)OLC2106596863 (DE-He213)BF00386237-p DE-627 ger DE-627 rakwb eng 570 690 540 VZ 12 ssgn Brauer, H. verfasserin aut Nitrification and denitrification in a system of reciprocating jet bioreactor 1992 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier © Springer-Verlag 1992 Abstract Concept of separation of stages coupled with novel design of reciprocating jet bioreactor have been incorporated in this research for the development of high efficiency treatment system for contaminated wastewaters. Evaluation of pilot plant data reveals that a three stage reciprocating jet bioreactor system could be effectively employed for nitrification and denitrification of highly polluted wastewater obtained from Berlin wastewater treatment plant. Such a system with COD destruction stage (residence time 1–3 hours) followed by nitrification stage (residence time 3–4.5 hours) and denitrification stage (residence time 0.3 hours) gives COD destruction rate upto 58 kg COD/($ m^{3} $ day), nitrification rate upto 3.2 NH4+-N/($ m^{3} $ day) and denitrification rate upto 28 kg NO3−-N/($ m^{3} $ day) while providing COD, NH4+-N and NO3−-N conversion of more than 90%. Nitrification and denitrification of wastewater at such a short residence time is possible mainly due to the employment of reciprocating jet bioreactor system. Nitrification Wastewater Denitrification Wastewater Treatment Wastewater Treatment Plant Annachhatre, A. P. aut Enthalten in Bioprocess engineering Springer-Verlag, 1986 7(1992), 6 vom: März, Seite 269-275 (DE-627)129208922 (DE-600)55154-5 (DE-576)01445761X 0178-515X nnns volume:7 year:1992 number:6 month:03 pages:269-275 https://doi.org/10.1007/BF00386237 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-UMW SSG-OLC-ARC SSG-OLC-TEC SSG-OLC-CHE GBV_ILN_11 GBV_ILN_23 GBV_ILN_32 GBV_ILN_40 GBV_ILN_65 GBV_ILN_70 GBV_ILN_2004 GBV_ILN_2006 GBV_ILN_2018 GBV_ILN_4046 GBV_ILN_4103 GBV_ILN_4307 GBV_ILN_4310 GBV_ILN_4323 GBV_ILN_4328 AR 7 1992 6 03 269-275 |
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10.1007/BF00386237 doi (DE-627)OLC2106596863 (DE-He213)BF00386237-p DE-627 ger DE-627 rakwb eng 570 690 540 VZ 12 ssgn Brauer, H. verfasserin aut Nitrification and denitrification in a system of reciprocating jet bioreactor 1992 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier © Springer-Verlag 1992 Abstract Concept of separation of stages coupled with novel design of reciprocating jet bioreactor have been incorporated in this research for the development of high efficiency treatment system for contaminated wastewaters. Evaluation of pilot plant data reveals that a three stage reciprocating jet bioreactor system could be effectively employed for nitrification and denitrification of highly polluted wastewater obtained from Berlin wastewater treatment plant. Such a system with COD destruction stage (residence time 1–3 hours) followed by nitrification stage (residence time 3–4.5 hours) and denitrification stage (residence time 0.3 hours) gives COD destruction rate upto 58 kg COD/($ m^{3} $ day), nitrification rate upto 3.2 NH4+-N/($ m^{3} $ day) and denitrification rate upto 28 kg NO3−-N/($ m^{3} $ day) while providing COD, NH4+-N and NO3−-N conversion of more than 90%. Nitrification and denitrification of wastewater at such a short residence time is possible mainly due to the employment of reciprocating jet bioreactor system. Nitrification Wastewater Denitrification Wastewater Treatment Wastewater Treatment Plant Annachhatre, A. P. aut Enthalten in Bioprocess engineering Springer-Verlag, 1986 7(1992), 6 vom: März, Seite 269-275 (DE-627)129208922 (DE-600)55154-5 (DE-576)01445761X 0178-515X nnns volume:7 year:1992 number:6 month:03 pages:269-275 https://doi.org/10.1007/BF00386237 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-UMW SSG-OLC-ARC SSG-OLC-TEC SSG-OLC-CHE GBV_ILN_11 GBV_ILN_23 GBV_ILN_32 GBV_ILN_40 GBV_ILN_65 GBV_ILN_70 GBV_ILN_2004 GBV_ILN_2006 GBV_ILN_2018 GBV_ILN_4046 GBV_ILN_4103 GBV_ILN_4307 GBV_ILN_4310 GBV_ILN_4323 GBV_ILN_4328 AR 7 1992 6 03 269-275 |
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10.1007/BF00386237 doi (DE-627)OLC2106596863 (DE-He213)BF00386237-p DE-627 ger DE-627 rakwb eng 570 690 540 VZ 12 ssgn Brauer, H. verfasserin aut Nitrification and denitrification in a system of reciprocating jet bioreactor 1992 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier © Springer-Verlag 1992 Abstract Concept of separation of stages coupled with novel design of reciprocating jet bioreactor have been incorporated in this research for the development of high efficiency treatment system for contaminated wastewaters. Evaluation of pilot plant data reveals that a three stage reciprocating jet bioreactor system could be effectively employed for nitrification and denitrification of highly polluted wastewater obtained from Berlin wastewater treatment plant. Such a system with COD destruction stage (residence time 1–3 hours) followed by nitrification stage (residence time 3–4.5 hours) and denitrification stage (residence time 0.3 hours) gives COD destruction rate upto 58 kg COD/($ m^{3} $ day), nitrification rate upto 3.2 NH4+-N/($ m^{3} $ day) and denitrification rate upto 28 kg NO3−-N/($ m^{3} $ day) while providing COD, NH4+-N and NO3−-N conversion of more than 90%. Nitrification and denitrification of wastewater at such a short residence time is possible mainly due to the employment of reciprocating jet bioreactor system. Nitrification Wastewater Denitrification Wastewater Treatment Wastewater Treatment Plant Annachhatre, A. P. aut Enthalten in Bioprocess engineering Springer-Verlag, 1986 7(1992), 6 vom: März, Seite 269-275 (DE-627)129208922 (DE-600)55154-5 (DE-576)01445761X 0178-515X nnns volume:7 year:1992 number:6 month:03 pages:269-275 https://doi.org/10.1007/BF00386237 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-UMW SSG-OLC-ARC SSG-OLC-TEC SSG-OLC-CHE GBV_ILN_11 GBV_ILN_23 GBV_ILN_32 GBV_ILN_40 GBV_ILN_65 GBV_ILN_70 GBV_ILN_2004 GBV_ILN_2006 GBV_ILN_2018 GBV_ILN_4046 GBV_ILN_4103 GBV_ILN_4307 GBV_ILN_4310 GBV_ILN_4323 GBV_ILN_4328 AR 7 1992 6 03 269-275 |
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Nitrification and denitrification in a system of reciprocating jet bioreactor |
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Nitrification and denitrification in a system of reciprocating jet bioreactor |
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Brauer, H. |
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1992 |
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Brauer, H. Annachhatre, A. P. |
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nitrification and denitrification in a system of reciprocating jet bioreactor |
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Nitrification and denitrification in a system of reciprocating jet bioreactor |
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Abstract Concept of separation of stages coupled with novel design of reciprocating jet bioreactor have been incorporated in this research for the development of high efficiency treatment system for contaminated wastewaters. Evaluation of pilot plant data reveals that a three stage reciprocating jet bioreactor system could be effectively employed for nitrification and denitrification of highly polluted wastewater obtained from Berlin wastewater treatment plant. Such a system with COD destruction stage (residence time 1–3 hours) followed by nitrification stage (residence time 3–4.5 hours) and denitrification stage (residence time 0.3 hours) gives COD destruction rate upto 58 kg COD/($ m^{3} $ day), nitrification rate upto 3.2 NH4+-N/($ m^{3} $ day) and denitrification rate upto 28 kg NO3−-N/($ m^{3} $ day) while providing COD, NH4+-N and NO3−-N conversion of more than 90%. Nitrification and denitrification of wastewater at such a short residence time is possible mainly due to the employment of reciprocating jet bioreactor system. © Springer-Verlag 1992 |
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Abstract Concept of separation of stages coupled with novel design of reciprocating jet bioreactor have been incorporated in this research for the development of high efficiency treatment system for contaminated wastewaters. Evaluation of pilot plant data reveals that a three stage reciprocating jet bioreactor system could be effectively employed for nitrification and denitrification of highly polluted wastewater obtained from Berlin wastewater treatment plant. Such a system with COD destruction stage (residence time 1–3 hours) followed by nitrification stage (residence time 3–4.5 hours) and denitrification stage (residence time 0.3 hours) gives COD destruction rate upto 58 kg COD/($ m^{3} $ day), nitrification rate upto 3.2 NH4+-N/($ m^{3} $ day) and denitrification rate upto 28 kg NO3−-N/($ m^{3} $ day) while providing COD, NH4+-N and NO3−-N conversion of more than 90%. Nitrification and denitrification of wastewater at such a short residence time is possible mainly due to the employment of reciprocating jet bioreactor system. © Springer-Verlag 1992 |
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Abstract Concept of separation of stages coupled with novel design of reciprocating jet bioreactor have been incorporated in this research for the development of high efficiency treatment system for contaminated wastewaters. Evaluation of pilot plant data reveals that a three stage reciprocating jet bioreactor system could be effectively employed for nitrification and denitrification of highly polluted wastewater obtained from Berlin wastewater treatment plant. Such a system with COD destruction stage (residence time 1–3 hours) followed by nitrification stage (residence time 3–4.5 hours) and denitrification stage (residence time 0.3 hours) gives COD destruction rate upto 58 kg COD/($ m^{3} $ day), nitrification rate upto 3.2 NH4+-N/($ m^{3} $ day) and denitrification rate upto 28 kg NO3−-N/($ m^{3} $ day) while providing COD, NH4+-N and NO3−-N conversion of more than 90%. Nitrification and denitrification of wastewater at such a short residence time is possible mainly due to the employment of reciprocating jet bioreactor system. © Springer-Verlag 1992 |
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