A two-phase partitioning bioreactor (TPPB) achievedsimultaneous and continuous removal and degradation of benzene and toluene froman air stream. The aqueous-organic system utilized n-hexadecane as the organicphase, and the organism Alcaligenes xylosoxidans Y234 in the aqueous phaseto achieve the degradation of benzene and toluene. The system, which operates asa well-mixed dispersion and is therefore resistant to substrate surges, was firstshown to be capable of utilizing toluene while operating at a loading capacity of 235 g m-3 h-1with an elimination capacity of 233 g m-3 h-1. It was also determined that to characterize TPPB performance in terms of elimination capacity thedefinition of elimination capacity must be extended to include the cell mass present, a readilycontrollable variable given the nature of the system. Based on this criterion, it wasestimated that for a cell concentration of 1 g l-1 present in the TPPB, thepotential maximum toluene elimination capacity is 1290 g m-3 h-1 whichis substantially higher than any toluene elimination capacity achieved by biofiltersat a high removal efficiency. If no other factor were to limit the system, eliminationcapacities could be many times higher still, and are dependent on maintaining desiredcell concentrations above 1 g l-1. The TPPB was then operated at nominalloading capacities of 63 g m-3h-1 (benzene) and 51 g m-3 h-1 (toluene) at a removal efficiency greater than 99% to demonstratedthe applicability of this system in dealing with two chemical species simultaneously. TPPBsystems therefore have been shown to be effective at removing gaseous organiccontaminants at high removal efficiencies while also possessing desirable operatingfeatures, such as providing and maintaining high cell concentrations throughout thereactor, and a capacity to effectively deal with high contaminant loadings.
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Univ Manchester, Manchester Interdisciplinary Bioctr, Manchester M1 7DN, Lancs, England
Queens Univ, Dept Chem Engn, Kingston, ON K7L 3N6, CanadaUniv Manchester, Manchester Interdisciplinary Bioctr, Manchester M1 7DN, Lancs, England
Rehmann, Lars
Prpich, George P.
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Queens Univ, Dept Chem Engn, Kingston, ON K7L 3N6, CanadaUniv Manchester, Manchester Interdisciplinary Bioctr, Manchester M1 7DN, Lancs, England
Prpich, George P.
Daugulis, Andrew J.
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Queens Univ, Dept Chem Engn, Kingston, ON K7L 3N6, CanadaUniv Manchester, Manchester Interdisciplinary Bioctr, Manchester M1 7DN, Lancs, England
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Univ Roma La Sapienza, Dept Chem Engn Mat Environm, Via Eudossiana 18, I-00184 Rome, ItalyUniv Roma La Sapienza, Dept Chem Engn Mat Environm, Via Eudossiana 18, I-00184 Rome, Italy
Annesini, M. Cristina
Tomei, M. Concetta
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CNR, Water Res Inst, Via Solaria Km 29-300, I-00015 Rome, ItalyUniv Roma La Sapienza, Dept Chem Engn Mat Environm, Via Eudossiana 18, I-00184 Rome, Italy
Tomei, M. Concetta
Piemonte, Vincenzo
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Univ Campus Biomed Roma, Dept Engn, Unit Chem Phys Fundamentals Chem Engn, Via Alvaro Portillo 21, I-00128 Rome, ItalyUniv Roma La Sapienza, Dept Chem Engn Mat Environm, Via Eudossiana 18, I-00184 Rome, Italy
Piemonte, Vincenzo
Daugulis, Andrew J.
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Queens Univ, Dept Chem Engn, Kingston, ON K7L 3N6, CanadaUniv Roma La Sapienza, Dept Chem Engn Mat Environm, Via Eudossiana 18, I-00184 Rome, Italy
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CNR, Water Res Inst, Via Salaria Km 29-300,CP 10, I-00015 Monterotondo Stazione Ro, ItalyCNR, Water Res Inst, Via Salaria Km 29-300,CP 10, I-00015 Monterotondo Stazione Ro, Italy
Tomei, M. Concetta
Stazi, Valentina
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CNR, Water Res Inst, Via Salaria Km 29-300,CP 10, I-00015 Monterotondo Stazione Ro, ItalyCNR, Water Res Inst, Via Salaria Km 29-300,CP 10, I-00015 Monterotondo Stazione Ro, Italy
Stazi, Valentina
Angelucci, Domenica Mosca
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CNR, Water Res Inst, Via Salaria Km 29-300,CP 10, I-00015 Monterotondo Stazione Ro, ItalyCNR, Water Res Inst, Via Salaria Km 29-300,CP 10, I-00015 Monterotondo Stazione Ro, Italy