|
|
|
|
| LEADER |
01000naa a22002652 4500 |
| 001 |
NLM360587682 |
| 003 |
DE-627 |
| 005 |
20231226083328.0 |
| 007 |
cr uuu---uuuuu |
| 008 |
231226s2023 xx |||||o 00| ||eng c |
| 024 |
7 |
|
|a 10.1002/wer.10917
|2 doi
|
| 028 |
5 |
2 |
|a pubmed24n1201.xml
|
| 035 |
|
|
|a (DE-627)NLM360587682
|
| 035 |
|
|
|a (NLM)37559175
|
| 040 |
|
|
|a DE-627
|b ger
|c DE-627
|e rakwb
|
| 041 |
|
|
|a eng
|
| 100 |
1 |
|
|a McCullough, Kester
|e verfasserin
|4 aut
|
| 245 |
1 |
0 |
|a Sidestream bio-P and mainstream anammox in a BNR process with upstream carbon capture
|
| 264 |
|
1 |
|c 2023
|
| 336 |
|
|
|a Text
|b txt
|2 rdacontent
|
| 337 |
|
|
|a ƒaComputermedien
|b c
|2 rdamedia
|
| 338 |
|
|
|a ƒa Online-Ressource
|b cr
|2 rdacarrier
|
| 500 |
|
|
|a Date Completed 28.08.2023
|
| 500 |
|
|
|a Date Revised 29.08.2023
|
| 500 |
|
|
|a published: Print
|
| 500 |
|
|
|a Citation Status MEDLINE
|
| 520 |
|
|
|a © 2023 The Authors. Water Environment Research published by Wiley Periodicals LLC on behalf of Water Environment Federation.
|
| 520 |
|
|
|a The integration of biological phosphorus removal (bio-P) and shortcut nitrogen removal (SNR) processes is challenging because of the conflicting demands on influent carbon: SNR allows for upstream carbon diversion, but this reduction of influent carbon (especially volatile fatty acids [VFAs]) prevents or limits bio-P. The objective of this study was to achieve SNR, either via partial nitritation/anammox (PNA) or partial denitrification/anammox (PdNA), simultaneously with biological phosphorus removal in a process with upstream carbon capture. This study took place in a pilot scale A/B process with a sidestream bio-P reactor and tertiary anammox polishing. Despite low influent rbCOD concentrations from the A-stage effluent, bio-P occurred in the B-stage thanks to the addition of A-stage WAS fermentate to the sidestream reactor. Nitrite accumulation occurred in the B-stage via partial denitrification and partial nitritation (NOB out-selection), depending on operational conditions, and was removed along with ammonia by the tertiary anammox MBBR, with the ability to achieve effluent TIN less than 2 mg/L. PRACTITIONER POINTS: A sidestream reactor with sufficient fermentate addition enables biological phosphorus removal in a B-stage system with little-to-no influent VFA. Enhanced biological phosphorus removal is not inhibited by intermittent aeration and is stable at a wide range of process SRTs. Partial nitritation and partial denitrification are viable routes to produce nitrite within an A/B process with sidestream bio-P, for downstream anammox in a polishing MBBR
|
| 650 |
|
4 |
|a Journal Article
|
| 650 |
|
4 |
|a A/B process
|
| 650 |
|
4 |
|a anammox
|
| 650 |
|
4 |
|a biological phosphorus removal
|
| 650 |
|
4 |
|a carbon capture
|
| 650 |
|
4 |
|a shortcut nitrogen removal
|
| 650 |
|
7 |
|a Nitrites
|2 NLM
|
| 650 |
|
7 |
|a Phosphorus
|2 NLM
|
| 650 |
|
7 |
|a 27YLU75U4W
|2 NLM
|
| 650 |
|
7 |
|a Carbon
|2 NLM
|
| 650 |
|
7 |
|a 7440-44-0
|2 NLM
|
| 650 |
|
7 |
|a Nitrogen
|2 NLM
|
| 650 |
|
7 |
|a N762921K75
|2 NLM
|
| 650 |
|
7 |
|a Sewage
|2 NLM
|
| 650 |
|
7 |
|a Ammonium Compounds
|2 NLM
|
| 700 |
1 |
|
|a Klaus, Stephanie
|e verfasserin
|4 aut
|
| 700 |
1 |
|
|a Wilson, Christopher
|e verfasserin
|4 aut
|
| 700 |
1 |
|
|a Vanrolleghem, Peter A
|e verfasserin
|4 aut
|
| 700 |
1 |
|
|a Gu, April Z
|e verfasserin
|4 aut
|
| 700 |
1 |
|
|a Bott, Charles B
|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 95(2023), 8 vom: 25. Aug., Seite e10917
|w (DE-627)NLM098214292
|x 1554-7531
|7 nnns
|
| 773 |
1 |
8 |
|g volume:95
|g year:2023
|g number:8
|g day:25
|g month:08
|g pages:e10917
|
| 856 |
4 |
0 |
|u http://dx.doi.org/10.1002/wer.10917
|3 Volltext
|
| 912 |
|
|
|a GBV_USEFLAG_A
|
| 912 |
|
|
|a SYSFLAG_A
|
| 912 |
|
|
|a GBV_NLM
|
| 912 |
|
|
|a GBV_ILN_350
|
| 951 |
|
|
|a AR
|
| 952 |
|
|
|d 95
|j 2023
|e 8
|b 25
|c 08
|h e10917
|