2003
DOI: 10.1023/a:1025099427538
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Abstract: A two-phase bioreactor consisting of hexadecane dispersed in an aqueous, cell-containing medium (organic fraction = 0.33) was used to trap toluene vapours from an air stream. The affinity for toluene by the solvent resulted in high efficiency of removal and transfer to the aqueous phase based on equilibrium transfer. The system was readily able to handle a loading capacity of 748 mg l(-1) h(-1) at a toluene degradation efficiency of greater than 98%.

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Cited by 61 publications
(5 citation statements)
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“…Since their inception, TPPBs have been used in various designs to treat single substrate feeds of benzene ( 3 , 4 , 9 , 10 ), toluene ( , ), and ethylbenzene (), as well as a mixed feed of benzene and toluene (). The most recent research focused on demonstrating steady-state operation with a culture whose maintenance energy requirements consumed the entire substrate supply ().…”
Section: Introductionmentioning
confidence: 99%
“…Since their inception, TPPBs have been used in various designs to treat single substrate feeds of benzene ( 3 , 4 , 9 , 10 ), toluene ( , ), and ethylbenzene (), as well as a mixed feed of benzene and toluene (). The most recent research focused on demonstrating steady-state operation with a culture whose maintenance energy requirements consumed the entire substrate supply ().…”
Section: Introductionmentioning
confidence: 99%
“…; 92.4% for bacterium J2, 84.8% for bacterium J6 (39). However, the highest toluene metabolizing efficiencies (99 and 98%) have been reported so far for Rhodococcus erythropolis and Alcaligenes xylosoxidans respectively (40,41). The isolates with minimal toluene removal were found to be IUBT23 (28% ± 4.24) and IUBT26 (50% ± 9.19).…”
Section: Toluene Removal Efficiencymentioning
confidence: 84%
“…For this reason, this work aims to separate previously these pollutant components with the intention of applying later specific processes to each component. Trying to avoid this kind of mass transfer limitations, several studies have proposed the use of multiphasic reactors or bioreactors, generally called two‐phase partitioning (bio)reactor (TPPR) 14, 15. This type of contactors involves the use of a second liquid phase which is nonaqueous and plays two different roles: (i) it increases the mass transfer rate of hydrophobic VOCs from gas to liquid phase, and (ii) it enhances the mass transfer from organic to aqueous phase due to a high driving force.…”
Section: Introductionmentioning
confidence: 99%