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 AbstractRemoval of benzene under acidic conditions in a controlled Trickle Bed Air Biofilter    Next AbstractVisual and olfactory stimuli and fruit maturity affect trap captures of Oriental fruit flies (Diptera: Tephritidae) »

Chemosphere


Title:Treatment of dynamic mixture of hexane and benzene vapors in a Trickle Bed Air Biofilter integrated with cyclic adsorption/desorption beds
Author(s):Aly Hassan A; Sorial GA;
Address:"USEPA, Cincinnati, OH, United States"
Journal Title:Chemosphere
Year:2011
Volume:20101112
Issue:4
Page Number:521 - 528
DOI: 10.1016/j.chemosphere.2010.10.060
ISSN/ISBN:1879-1298 (Electronic) 0045-6535 (Linking)
Abstract:"One of the main challenges that face successful biofiltration is the erratic loading pattern and long starvation periods. However, such patterns are common in practical applications. In order to provide long-term stable operation of a biofilter under these conditions, a cyclic adsorption/desorption beds system with flow switching was installed prior to a biofilter. Different square waves of a mixture containing n-hexane and benzene at a 2:1 ratio were applied to the cyclic adsorption/desorption beds and then fed to a biofilter. The performance of this integrated system was compared to a biofilter unit receiving the same feed of both VOCs. The cyclic adsorption/desorption beds unit successfully achieved its goal of stabilizing erratic loading even with very sharp peaks at the influent concentration equalizing influent concentrations ranging from 10-470 ppmv for n-hexane to 30-1410 ppmv for benzene. The study included different peak concentrations with durations ranging from 6 to 20 min. The cyclic beds buffered the fluctuating influent load and the followed biofilter had all the time a continuous stable flow. Another advantage achieved by the cyclic adsorption/desorption beds was the uninterrupted feed to the biofilter even during the starvation where there was no influent in the feed. The results of the integrated system with regard to removal efficiency and kinetics are comparable to published results with continuous feed studies at the same loading rates. The removal efficiency for benzene had a minimum of 85% while for n-hexane ranged from 50% to 77% according to the loading rate. The control unit showed very erratic performance highlighting the benefit of the utilization of the cyclic adsorption/desorption beds. The biofilter was more adaptable to concentration changes in benzene than n-hexane"
Keywords:"Adsorption Air Pollutants/chemistry/*metabolism Benzene/chemistry/*metabolism Biodegradation, Environmental Carbon Dioxide/analysis/chemistry Filtration/*methods Hexanes/chemistry/*metabolism Kinetics Volatile Organic Compounds/chemistry/*metabolism;"
Notes:"MedlineAly Hassan, Ashraf Sorial, George A eng Research Support, Non-U.S. Gov't England 2010/11/16 Chemosphere. 2011 Jan; 82(4):521-8. doi: 10.1016/j.chemosphere.2010.10.060. Epub 2010 Nov 12"

 
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 18-11-2024