|
|
|
|
LEADER |
01000caa a22002652 4500 |
001 |
NLM218087292 |
003 |
DE-627 |
005 |
20250214012526.0 |
007 |
tu |
008 |
231224s2012 xx ||||| 00| ||eng c |
028 |
5 |
2 |
|a pubmed25n0727.xml
|
035 |
|
|
|a (DE-627)NLM218087292
|
035 |
|
|
|a (NLM)22629614
|
040 |
|
|
|a DE-627
|b ger
|c DE-627
|e rakwb
|
041 |
|
|
|a eng
|
100 |
1 |
|
|a Tawfik, A
|e verfasserin
|4 aut
|
245 |
1 |
0 |
|a Treatment of fruit-juice industry wastewater in a two-stage anaerobic hybrid (AH) reactor system followed by a sequencing batch reactor (SBR)
|
264 |
|
1 |
|c 2012
|
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 28.06.2012
|
500 |
|
|
|a Date Revised 28.05.2012
|
500 |
|
|
|a published: Print
|
500 |
|
|
|a Citation Status MEDLINE
|
520 |
|
|
|a This study has been carried out to assess the performance of a combined system consisting of an anaerobic hybrid (AH) reactor followed by a sequencing batch reactor (SBR) for treatment of fruit-juice industry wastewater at a temperature of 26 degrees C. Three experimental runs were conducted in this investigation. In the first experiment, a single-stage AH reactor was operated at a hydraulic retention time (HRT) of 10.2 h and organic loading rate (OLR) of 11.8 kg COD m(-3) d(-1). The reactor achieved a removal efficiency of 42% for chemical oxygen demand (COD), 50.8% for biochemical oxygen demand (BOD5), 50.3% for volatile fatty acids (VFA) and 56.4% for total suspended solids (TSS). In the second experiment, two AH reactors connected in series achieved a higher removal efficiency for COD (67.4%), BOD5 (77%), and TSS (71.5%) at a total HRT of 20 h and an OLR of 5.9 kg COD m(-3) d(-1). For removal of the remaining portions of COD, BOD5 and TSS from the effluent of the two-stage AH system, a sequencing batch reactor (SBR) was investigated as a post-treatment unit. The reactor achieved a substantial reduction in total COD, resulting in an average effluent concentration of 50 mg L(-1) at an HRT of 11 h and OLR of 5.3 kg COD m(-3) d(-1). Almost complete removal of total BOD5 and oil and grease was achieved, i.e. 10 mg L(-1) and 1.2 mg L(-1), respectively, remained in the final effluent of the SBR
|
650 |
|
4 |
|a Journal Article
|
650 |
|
7 |
|a Industrial Waste
|2 NLM
|
650 |
|
7 |
|a Water Pollutants, Chemical
|2 NLM
|
700 |
1 |
|
|a El-Kamah, H
|e verfasserin
|4 aut
|
773 |
0 |
8 |
|i Enthalten in
|t Environmental technology
|d 1998
|g 33(2012), 4-6 vom: 16. Feb., Seite 429-36
|w (DE-627)NLM098202545
|x 0959-3330
|7 nnns
|
773 |
1 |
8 |
|g volume:33
|g year:2012
|g number:4-6
|g day:16
|g month:02
|g pages:429-36
|
912 |
|
|
|a GBV_USEFLAG_A
|
912 |
|
|
|a SYSFLAG_A
|
912 |
|
|
|a GBV_NLM
|
912 |
|
|
|a GBV_ILN_350
|
951 |
|
|
|a AR
|
952 |
|
|
|d 33
|j 2012
|e 4-6
|b 16
|c 02
|h 429-36
|