|
|
|
|
| LEADER |
01000caa a22002652 4500 |
| 001 |
NLM272719617 |
| 003 |
DE-627 |
| 005 |
20250221185753.0 |
| 007 |
cr uuu---uuuuu |
| 008 |
231224s2018 xx |||||o 00| ||eng c |
| 024 |
7 |
|
|a 10.1080/09593330.2017.1340344
|2 doi
|
| 028 |
5 |
2 |
|a pubmed25n0908.xml
|
| 035 |
|
|
|a (DE-627)NLM272719617
|
| 035 |
|
|
|a (NLM)28592192
|
| 040 |
|
|
|a DE-627
|b ger
|c DE-627
|e rakwb
|
| 041 |
|
|
|a eng
|
| 100 |
1 |
|
|a Sahariah, Biju Prava
|e verfasserin
|4 aut
|
| 245 |
1 |
0 |
|a Pyridine influence on a sequential anaerobic-anoxic-aerobic FMBR system for phenol, thiocyanate and ammonia removal
|
| 264 |
|
1 |
|c 2018
|
| 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 17.08.2018
|
| 500 |
|
|
|a Date Revised 02.12.2018
|
| 500 |
|
|
|a published: Print-Electronic
|
| 500 |
|
|
|a Citation Status MEDLINE
|
| 520 |
|
|
|a A synthetic wastewater containing various pyridine concentrations (25-250 mg/L) was treated in a sequential anaerobic(B1)-anoxic(B2)-aerobic(B3) fed batch moving bed reactor (FMBR) system. Pyridine was associated with phenol (1500 mg/L), SCN- (800 mg/L), chemical oxygen demand (COD) (5400-5430 mg/L) and NH4+-N (500 mg/L) at hydraulic retention time (HRT) of 6 (B1: 3 days; B2 and B3: 1.5 days each) days. In B1, pyridine removal was 10-12% from influent concentration of 25-100 mg/L and beyond that, it was zero. Removal of phenol (53-39%) and COD (33-22%) occurred in B1, but pyridine above 50 mg/L inhibited both. In B2, 68-90% of pyridine removal occurred along with phenol (>98%), COD (>67%), SCN- (>85%) removal and denitrification. In B2, with an increase in pyridine loading removal rate of phenol, COD and nitrate increased, whereas SCN- removal decreased beyond pyridine loading of 0.031g/L day. In B3, nitrification decreased with high generation of free ammonia. Pyridine degradation in B1, B2 and B3 follows the Stover-Kincannon model with a maximum substrate removal rate of 111.1, 333.3 and 23.81 g/L day, respectively. Thiocyanate removal in B2 and ammonia removal in B3 follows the Bhatia inhibition model with a maximum substrate removal rate of 0.641 and 0.528/day, respectively. The overall efficiency of the FMBR system remained unaffected up to 250 mg pyridine/L at 6 days HRT
|
| 650 |
|
4 |
|a Journal Article
|
| 650 |
|
4 |
|a Fed batch moving bed reactor
|
| 650 |
|
4 |
|a denitrification
|
| 650 |
|
4 |
|a nitrification
|
| 650 |
|
4 |
|a phenol
|
| 650 |
|
4 |
|a pyridine
|
| 650 |
|
4 |
|a thiocyanate
|
| 650 |
|
7 |
|a Pyridines
|2 NLM
|
| 650 |
|
7 |
|a Thiocyanates
|2 NLM
|
| 650 |
|
7 |
|a Water Pollutants, Chemical
|2 NLM
|
| 650 |
|
7 |
|a Phenol
|2 NLM
|
| 650 |
|
7 |
|a 339NCG44TV
|2 NLM
|
| 650 |
|
7 |
|a Ammonia
|2 NLM
|
| 650 |
|
7 |
|a 7664-41-7
|2 NLM
|
| 700 |
1 |
|
|a Anandkumar, J
|e verfasserin
|4 aut
|
| 700 |
1 |
|
|a Chakraborty, Saswati
|e verfasserin
|4 aut
|
| 773 |
0 |
8 |
|i Enthalten in
|t Environmental technology
|d 1998
|g 39(2018), 14 vom: 07. Juli, Seite 1786-1794
|w (DE-627)NLM098202545
|x 1479-487X
|7 nnns
|
| 773 |
1 |
8 |
|g volume:39
|g year:2018
|g number:14
|g day:07
|g month:07
|g pages:1786-1794
|
| 856 |
4 |
0 |
|u http://dx.doi.org/10.1080/09593330.2017.1340344
|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 39
|j 2018
|e 14
|b 07
|c 07
|h 1786-1794
|