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 AbstractComparison of freely dissolved concentrations of PAHs in contaminated pot soils under saturated and unsaturated water conditions    Next AbstractLow tolerance to simulated herbivory in Hawaiian seedlings despite induced changes in photosynthesis and biomass allocation »

Biotechnol Prog


Title:Microbial removal of alkanes from dilute gaseous waste streams: kinetics and mass transfer considerations
Author(s):Barton JW; Klasson KT; Koran LJ; Davison BH;
Address:"Chemical Technology Division, Oak Ridge National Laboratory, Tennessee 37831-6226, USA"
Journal Title:Biotechnol Prog
Year:1997
Volume:13
Issue:6
Page Number:814 - 821
DOI: 10.1021/bp970091c
ISSN/ISBN:8756-7938 (Print) 1520-6033 (Linking)
Abstract:"Treatment of dilute gaseous hydrocarbon waste streams remains a current need for many industries, particularly as increasingly stringent environmental regulations and oversight force emission reduction. Biofiltration systems hold promise for providing low-cost alternatives to more traditional, energy-intensive treatment methods such as incineration and adsorption. Elucidation of engineering principles governing the behavior of such systems, including mass transfer limitations, will broaden their applicability. Our processes exploit a microbial consortium to treat a mixture of 0.5% n-pentane and 0.5% isobutane in air. Since hydrocarbon gases are sparingly soluble in water, good mixing and high surface area between the gas and liquid phases are essential for biodegradation to be effective. One liquid-continuous columnar bioreactor was operated for more than 30 months with continued degradation of n-pentane and isobutane as sole carbon and energy sources. The maximum degradation rate observed in this gas-recycle system was 2 g of volatile organic compounds (VOC)/(m3.h). A trickle-bed bioreactor was operated continuously for over 24 months to provide a higher surface area (using a structured packing) with increased rates. Degradation rates consistently achieved were approximately 50 g of VOC/(m3.h) via single pass in this gas-continuous columnar system. Effective mass transfer coefficients comparable to literature values were also measured for this reactor; these values were substantially higher than those found in the gas-recycle reactor. Control of biomass levels was implemented by limiting the level of available nitrogen in the recirculating aqueous media, enabling long-term stability of reactor performance"
Keywords:*Air Pollutants *Alkanes Bacteria/*metabolism Butanes Filtration *Industrial Waste Kinetics Mathematics Pentanes Waste Management/*methods;
Notes:"MedlineBarton, J W Klasson, K T Koran, L J Jr Davison, B H eng Research Support, U.S. Gov't, Non-P.H.S. 1997/12/31 23:53 Biotechnol Prog. 1997 Nov-Dec; 13(6):814-21. doi: 10.1021/bp970091c"

 
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 23-11-2024