Onsite wastewater denitrification using a hydrogenotrophic hollow-fiber membrane bioreactor

Hydrogenotrophic wastewater denitrification was investigated using a bench-scale hollow-fiber membrane bioreactor (HFMB). In the HFMB, hydrogen (H2) was passed through the lumen of hollow-fiber membranes and nitrified wastewater was supplied to the shell of the reactor. A mass transfer model was dev...

Ausführliche Beschreibung

Bibliographische Detailangaben
Veröffentlicht in:Water environment research : a research publication of the Water Environment Federation. - 1998. - 81(2009), 7 vom: 13. Juli, Seite 680-6
1. Verfasser: Sahu, Ashish K (VerfasserIn)
Weitere Verfasser: Sengupta, Sukalyan, Ergas, Sarina J
Format: Aufsatz
Sprache:English
Veröffentlicht: 2009
Zugriff auf das übergeordnete Werk:Water environment research : a research publication of the Water Environment Federation
Schlagworte:Journal Article Research Support, Non-U.S. Gov't Industrial Waste Membranes, Artificial Hydrogen 7YNJ3PO35Z Nitrogen N762921K75 Oxygen S88TT14065
LEADER 01000naa a22002652 4500
001 NLM190771569
003 DE-627
005 20231223185921.0
007 tu
008 231223s2009 xx ||||| 00| ||eng c
028 5 2 |a pubmed24n0636.xml 
035 |a (DE-627)NLM190771569 
035 |a (NLM)19691248 
040 |a DE-627  |b ger  |c DE-627  |e rakwb 
041 |a eng 
100 1 |a Sahu, Ashish K  |e verfasserin  |4 aut 
245 1 0 |a Onsite wastewater denitrification using a hydrogenotrophic hollow-fiber membrane bioreactor 
264 1 |c 2009 
336 |a Text  |b txt  |2 rdacontent 
337 |a ohne Hilfsmittel zu benutzen  |b n  |2 rdamedia 
338 |a Band  |b nc  |2 rdacarrier 
500 |a Date Completed 23.12.2009 
500 |a Date Revised 23.09.2019 
500 |a published: Print 
500 |a Citation Status MEDLINE 
520 |a Hydrogenotrophic wastewater denitrification was investigated using a bench-scale hollow-fiber membrane bioreactor (HFMB). In the HFMB, hydrogen (H2) was passed through the lumen of hollow-fiber membranes and nitrified wastewater was supplied to the shell of the reactor. A mass transfer model was developed and found to be a good tool to estimate H2 mass transfer coefficients at varying recirculation velocities. Under steady conditions, effluent NO3(-)-N concentrations less than 10 mg/L were achieved at an empty bed contact time of 8.3 hours when pH and membrane fouling were controlled. An average nitrogen flux of 0.88 g NO3(-) -N/m2 x d was observed. Dissolved oxygen in the influent wastewater did not adversely affect overall nitrogen removal. Under transient conditions, similar to those of onsite processes, overall nitrogen removal efficiencies of 74 to 82% were observed. Confocal laser scanning microscopy revealed that the denitrifying biofilm was loosely associated with the membrane surfaces 
650 4 |a Journal Article 
650 4 |a Research Support, Non-U.S. Gov't 
650 7 |a Industrial Waste  |2 NLM 
650 7 |a Membranes, Artificial  |2 NLM 
650 7 |a Hydrogen  |2 NLM 
650 7 |a 7YNJ3PO35Z  |2 NLM 
650 7 |a Nitrogen  |2 NLM 
650 7 |a N762921K75  |2 NLM 
650 7 |a Oxygen  |2 NLM 
650 7 |a S88TT14065  |2 NLM 
700 1 |a Sengupta, Sukalyan  |e verfasserin  |4 aut 
700 1 |a Ergas, Sarina J  |e verfasserin  |4 aut 
773 0 8 |i Enthalten in  |t Water environment research : a research publication of the Water Environment Federation  |d 1998  |g 81(2009), 7 vom: 13. Juli, Seite 680-6  |w (DE-627)NLM098214292  |x 1554-7531  |7 nnns 
773 1 8 |g volume:81  |g year:2009  |g number:7  |g day:13  |g month:07  |g pages:680-6 
912 |a GBV_USEFLAG_A 
912 |a SYSFLAG_A 
912 |a GBV_NLM 
912 |a GBV_ILN_350 
951 |a AR 
952 |d 81  |j 2009  |e 7  |b 13  |c 07  |h 680-6