2012
DOI: 10.1002/jctb.3732
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Biofiltration of a styrene/acetone vapor mixture in two reactor types under conditions of acetone overloading

Abstract: BACKGROUND: Evaluation of the biodegradation interactions between styrene and acetone, two typical paint solvents and vapor phase pollutants differing in water solubility and biodegradability, was conducted both in a trickle bed reactor (TBR) and a biofilter (BF). The loading rate experiments were performed by increasing the acetone concentration in the inlet air while keeping the styrene concentration and loading rate constant.

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Cited by 16 publications
(29 citation statements)
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“…Detailed descriptions of two bench-scale bioreactors used in this study were provided in previous publication (Paca et al 2012b). The trickle bed reactor (TBR, Fig.…”
Section: Methodsmentioning
confidence: 99%
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“…Detailed descriptions of two bench-scale bioreactors used in this study were provided in previous publication (Paca et al 2012b). The trickle bed reactor (TBR, Fig.…”
Section: Methodsmentioning
confidence: 99%
“…The trickle bed reactor (TBR, Fig. 1 Comamonas testosteroni (G -rods), Pseudomonas putida (G -rods) and Bacillus cereus (G + rods) all being primary styrene and acetone degraders] was immobilized in both the reactors and then used in previous study conducted with the same substrates (Paca et al 2012b). Similar to this previous study, the reactors were operated in a concurrent airwater down-flow mode at the same empty bed retention time of 53 s. The same dilute mineral medium of the following composition was used in both reactors (per liter): 0.4 g (NH 4 ) 2 SO 4 , 0.3 g KNO 3 , 0.1 g NaCl, 0.125 g K 2 HPO 4 , 0.085 g KH 2 PO 4 , 0.34 g MgCl 2 .…”
Section: Methodsmentioning
confidence: 99%
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