|
|
|
|
LEADER |
01000naa a22002652 4500 |
001 |
NLM319868311 |
003 |
DE-627 |
005 |
20231225172352.0 |
007 |
cr uuu---uuuuu |
008 |
231225s2021 xx |||||o 00| ||eng c |
024 |
7 |
|
|a 10.1002/wer.1509
|2 doi
|
028 |
5 |
2 |
|a pubmed24n1066.xml
|
035 |
|
|
|a (DE-627)NLM319868311
|
035 |
|
|
|a (NLM)33423314
|
040 |
|
|
|a DE-627
|b ger
|c DE-627
|e rakwb
|
041 |
|
|
|a eng
|
100 |
1 |
|
|a Li, Baoqiang
|e verfasserin
|4 aut
|
245 |
1 |
4 |
|a The inhibitory impact of ammonia on thermally hydrolyzed sludge fed anaerobic digestion
|
264 |
|
1 |
|c 2021
|
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 27.08.2021
|
500 |
|
|
|a Date Revised 27.08.2021
|
500 |
|
|
|a published: Print-Electronic
|
500 |
|
|
|a Citation Status MEDLINE
|
520 |
|
|
|a © 2021 Water Environment Federation.
|
520 |
|
|
|a This study evaluated the impact of ammonia on mesophilic anaerobic digestion (AD) with thermal hydrolysis pretreatment (THP) treating a mixture of primary sludge and waste activated sludge and operated under constant organic loading rate of 9 kg COD/m3 /d. Free ammonia concentrations in the digesters were varied between 37 and 966 mg NH3 -N/L, while maintaining all other operational conditions constant. A decrease in volatile solids reduction from 54 ± 5% (at <554 mg NH3 -N/L) to 35 ± 6% at the maximum free ammonia concentration of 966 mg NH3 -N/L was observed at steady-state conditions. No impact of free ammonia on final dewaterability was detected. Free ammonia thus mostly limited methanogenesis. A free ammonia Monod inhibition constant of 847 ± 222 mg NH3 -N/L for methanogens was estimated based on the digester steady-state methane rates dynamics. This study showed that current THP AD digesters (typically 110-260 mg NH3 -N/L) operate under 12%-18% ammonia inhibition for methanogenesis. Operation under SRT of 15 days, about 2 times more than needed to retain methanogens, can compensate for lower methanogens rates and avoid performance impacts. The later shows a good potential to operate under higher free and total ammonia concentration without jeopardizing performance. PRACTITIONER POINTS: Only from a free ammonia concentration above 554 mg NH3 -N/L, decreased volatile solids reduction and biogas yield were observed. A volatile solids reduction of 35 ± 6% at maximum free ammonia concentration of 966 mg NH3 -N/L was still achieved. A Monod inhibition constant for methanogens of 847 ± 222 mg NH3 -N/L was estimated. It was estimated that current THP AD systems (110-260 mg NH3 -N/L) operate under 12%-18% NH3 inhibition for methanogenesis
|
650 |
|
4 |
|a Journal Article
|
650 |
|
4 |
|a AD
|
650 |
|
4 |
|a NH3
|
650 |
|
4 |
|a TAN
|
650 |
|
4 |
|a THP
|
650 |
|
4 |
|a biosolids
|
650 |
|
4 |
|a free ammonia
|
650 |
|
4 |
|a inhibition kinetics
|
650 |
|
7 |
|a Sewage
|2 NLM
|
650 |
|
7 |
|a Ammonia
|2 NLM
|
650 |
|
7 |
|a 7664-41-7
|2 NLM
|
650 |
|
7 |
|a Methane
|2 NLM
|
650 |
|
7 |
|a OP0UW79H66
|2 NLM
|
700 |
1 |
|
|a Ladipo-Obasa, Mojolaoluwa
|e verfasserin
|4 aut
|
700 |
1 |
|
|a Romero, Adrian
|e verfasserin
|4 aut
|
700 |
1 |
|
|a Wadhawan, Tanush
|e verfasserin
|4 aut
|
700 |
1 |
|
|a Tobin, Michael
|e verfasserin
|4 aut
|
700 |
1 |
|
|a Manning, Elizabeth
|e verfasserin
|4 aut
|
700 |
1 |
|
|a Higgins, Matthew
|e verfasserin
|4 aut
|
700 |
1 |
|
|a Al-Omari, Ahmed
|e verfasserin
|4 aut
|
700 |
1 |
|
|a Murthy, Sudhir
|e verfasserin
|4 aut
|
700 |
1 |
|
|a Novak, John T
|e verfasserin
|4 aut
|
700 |
1 |
|
|a Riffat, Rumana
|e verfasserin
|4 aut
|
700 |
1 |
|
|a De Clippeleir, Haydée
|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 93(2021), 8 vom: 15. Aug., Seite 1263-1275
|w (DE-627)NLM098214292
|x 1554-7531
|7 nnns
|
773 |
1 |
8 |
|g volume:93
|g year:2021
|g number:8
|g day:15
|g month:08
|g pages:1263-1275
|
856 |
4 |
0 |
|u http://dx.doi.org/10.1002/wer.1509
|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 93
|j 2021
|e 8
|b 15
|c 08
|h 1263-1275
|