1991
DOI: 10.1007/bf00169766
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Continuous degradation of 3-chloroaniline by calcium-alginate-entrapped cells of Pseudomonas acidovorans CA28: influence of additional substrates

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Cited by 31 publications
(18 citation statements)
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“…Exponentially growing cells were harvested by centrifuging the culture broth at 6,000 rpm for 20 min and washing with a 0.9% (wlv) NaCI solution. The washed cells (1.4g dry wt./I) were immobilized in gel beads of calcium alginate, as described in a previous report (Ferschl et al, 1991). Culture conditions.…”
Section: Methodsmentioning
confidence: 99%
“…Exponentially growing cells were harvested by centrifuging the culture broth at 6,000 rpm for 20 min and washing with a 0.9% (wlv) NaCI solution. The washed cells (1.4g dry wt./I) were immobilized in gel beads of calcium alginate, as described in a previous report (Ferschl et al, 1991). Culture conditions.…”
Section: Methodsmentioning
confidence: 99%
“…Another aniline-degrading pseudomonad, however, was shown to utilize aniline and other organic substrates simultaneously (9). In other studies, it also became apparent that catabolite repression of catabolic pathways for xenobiotic compounds is not as common as could be expected; 3-phenoxybenzoate metabolism by a strain of Pseudomonas delafieldii was shown to be nonsusceptible to catabolite repression (22), as was the degradation of 3-chloroaniline by Pseudomonas acidovorans (7). Release of catabolite repression of catabolic enzymes in a chemostat culture limited by a potentially repressing substrate, as observed in this study, is a generally occurring phenomenon (8,16).…”
mentioning
confidence: 99%
“…The overall COD removal by the two stages exceeded 85%. A continuous suspended draft-tube sparged concentric-tube airlift bioreactor was applied for 3-chloroaniline degradation [65]. The airlift was applied as a system of aerators for treating industrial wastes in an aeration-flotation tank using a system of cylindrical draft-tubes.…”
Section: Modifications Of the Activated-sludge Processesmentioning
confidence: 99%
“…In actual operation, most of the airlift bioreactors lie somewhere between these two extremes and the deviations from ideal flow can have a variety of causes [55,[57][58][59]: incomplete radial mixing, liquid back-mixing, existence of stagnant regions and channelling. Therefore, airlift bioreactors can be considered as plug flow, with superimposed axial dispersion, according to the following equation [36,44,47,[54][55][56][57][58][59][60][61][62][63][64][65][66][67][68][69][70][71] vated cell concentrations…”
mentioning
confidence: 99%