Bedoukian   RussellIPM   RussellIPM   Piezoelectric Micro-Sprayer


Home
Animal Taxa
Plant Taxa
Semiochemicals
Floral Compounds
Semiochemical Detail
Semiochemicals & Taxa
Synthesis
Control
Invasive spp.
References

Abstract

Guide

Alphascents
Pherobio
InsectScience
E-Econex
Counterpart-Semiochemicals
Print
Email to a Friend
Kindly Donate for The Pherobase

« Previous Abstract"The physical chemistry of self/non-self: jigsaws, transplants and fetuses"    Next AbstractPropolis volatile compounds: chemical diversity and biological activity: a review »

J Environ Sci Health A Tox Hazard Subst Environ Eng


Title:Treatment of high-strength synthetic sewage in a laboratory-scale upflow anaerobic sludge bed (UASB) with aerobic activated sludge (AS) post-treatment
Author(s):Banihani QH; Field JA;
Address:"Department of Chemical and Environmental Engineering, University of Arizona, Tucson, Arizona, USA. q.banihani@ju.edu.jo"
Journal Title:J Environ Sci Health A Tox Hazard Subst Environ Eng
Year:2013
Volume:48
Issue:3
Page Number:338 - 347
DOI: 10.1080/10934529.2013.726907
ISSN/ISBN:1532-4117 (Electronic) 1093-4529 (Linking)
Abstract:"Performance of a combined system up-flow anaerobic sludge blanket (UASB) followed by aerobic treatment activated sludge (AS) for removal of carbonaceous and nitrogenous contaminants at an average temperature of 25 degrees C was investigated. The combined system was fed with high strength synthetic sewage having chemical oxygen demand (COD) of 2500 mg L(-1). The organic loading rate (OLR) of the UASB reactor was increased gradually from 1.1 to 3.8 gCOD L(r) (-1) d(-1). At steady state condition, the UASB reactor achieved removal efficiency up to 83.5% of total COD (COD(tot)), 74.0% of volatile fatty acid (VFA) and 94.0% of protein. The combined system performed an excellent organic removal pushing the overall removal efficiency of COD(tot), VFA and protein to 91.0%, 99.9% and 98.2%, respectively. When the OLR of the UASB increased to 4.4 g COD L(r) (-1) d(-1), the UASB was overloaded and; thus, its effluent quality deteriorated. In respect to nitrogen removal, both partial nitrification and complete nitrification took place in aerobic post-treatment. When the dissolved oxygen (DO) concentration was >2.0 mg L(-1), complete nitrification (period B) occurred with an average nitrification efficiency of 96.2%. The partial nitrification occurred due to high OLR to AS during the overloading event (period A) and when DO concentration was <2.0 mg L(-1) (period C). The maximum accumulated nitrite concentration in periods A, B and C were 90.0, 0.9 and 75.8 mg NO(-) (2) -N L(-1), respectively. The nitrogen balance results of periods A and C indicated that there was a discrepancy between the amount of ammonium nitrogen removed and the amount of oxidized nitrogen formed. This suggests the occurrence of simultaneous nitrification/denitrification (SND) in aerobic post-treatment"
Keywords:"Aerobiosis *Bioreactors Chromatography, Ion Exchange Colorimetry Flame Ionization Nitrates/*metabolism Nitrification Nitrogen Compounds/metabolism Organic Chemicals/metabolism Oxygen/metabolism Sewage/*microbiology Waste Disposal, Fluid/*methods Water Pol;"
Notes:"MedlineBanihani, Qais H Field, Jim A eng Evaluation Study Research Support, Non-U.S. Gov't England 2012/12/19 J Environ Sci Health A Tox Hazard Subst Environ Eng. 2013; 48(3):338-47. doi: 10.1080/10934529.2013.726907"

 
Back to top
 
Citation: El-Sayed AM 2024. The Pherobase: Database of Pheromones and Semiochemicals. <http://www.pherobase.com>.
© 2003-2024 The Pherobase - Extensive Database of Pheromones and Semiochemicals. Ashraf M. El-Sayed.
Page created on 22-11-2024