Degradation of quinoline by immobilized Comamonas acidovorans in a three-phase airlift reactor

Quinolie degradation by Comamonas acidovorans was studied in a continuously operated three-phase airlift reactor. Porous glass beads were applied as support matrix for cell imobilization by colonization. Under steady-state conditions (S approximately 0), cell attachment was poor at low dilution rates but imporved considerably with increasing dilution rate. Conversion of quinoline was investigated below and above the washout for suspended culture (D(crit) = mu(max) = 0.42 h(-1)). With immobilized cells the reactor could be operated at D > mu(max), and complete conversion of quinoline was achieved as long as the specific quinoline feed rate D*S(0)/X did not exceed the maximum specific degradation rate (r(S, max)). The biofilm thickness was about 100 mum, and its efficiency was about 54% compared to suspended organisms. If quinoline overloads were supplied to the reactor, quinoline, as overloads were supplied to the reactor, quinoline, as well as its pathway intermediates, appeared in the reactor and conversion was low. Hence, the immobilized microorganisms remained viable and active. They could survive quinoline overloads. If the quinoline feed rate was reduced agains, complete conversion was reestablished. (c) 1995 John Wiley & Sons, Inc.     

Degradation of aniline and monochlorinated anilines by soil-born Pseudomonas acidovorans strains

Four bacterial strains (CA26, CA28, CA37, and CA45), which all were able to use aniline, 3-chloroaniline (3-CA), and 4-chloroaniline (4-CA) as sole sources of carbon, nitrogen and energy, were isolated after enrichment in aerated soil columns and identified as Pseudomonas acidovorans strains. In addition strains CA26 and CA45 were able to degrade 2-chloroaniline (2-CA) at very low rates. At 25°C strain CA28 was grown on aniline and 3-CA with generation times of 3.0 and 7.7 h, respectively, and exhibited complete mineralization of these substrates in degradation rates of 2.25 mmol aniline and 1.63 mmol 3-CA g^-1 of biomass per hour, respectively. Degradation of 4-CA occurred at 1.54 mmol 4-CA g^-1 of biomass per hour and a generation time of 18.7 h but, in contrast, was not complete due to formation of minor amounts of chlorohydroxymuconic semialdehyde, a meta-cleavage product of 4-chlorocatechol. The initial attack on the substrate, the formation of corresponding chlorocatechols from 3-CA and 4-CA, was found to be the rate-limiting degradation step. Evidence for two different aniline-oxygenase systems in strain CA28 with distinct activity pattern on chlorinated and nonsubstituted anilines was demonstrated by oxygen uptake rate experiments with aniline and chloroaniline pregrown cells. Further degradation was shown to be initialized by catechol dioxygenases.Non-standard abbreviations CA chloroaniline - DCA dichloroaniline - ECM enrichment and cultivation medium - CFU colony forming unit     

High-level expression and characterization of a highly functional Comamonas acidovorans xanthine dehydrogenase in Pseudomonas aeruginosa

An improved procedure is described for the high-level expression of Comamonas acidovorans XDH in Pseudomonas aeruginosa PAO1-LAC. The level of functional expression (56 mg protein/L culture) is found to be 7-fold higher than that observed in Escherichia coli and 30-fold higher than that induced in C. acidovorans. Co-expression of the xdhC gene is required for maximal level of functional expression. Comparison of purified preparations of XDH expressed in the absence of xdhC (XDH(AB)) with that expressed in its presence (XDH(ABC)) shows the increased level of activity due to the level of Mo incorporation. The Fe and FAD contents of expressed enzymes are independent of xdhC co-expression. Electron paramagnetic resonance spectroscopy, circular dichroism spectroscopy, metal analysis, and kinetic properties of recombinant purified XDH(ABC) are identical with those exhibited by the native enzyme. This expression system should serve as a valuable tool for further biophysical and mechanistic investigations of xanthine dehydrogenase by site-directed mutagenesis. A method is also described to evaluate the suitability of P. aeruginosa and other organisms as potential expression hosts for five different sources of xdh genes.     

Degradation of diarylethane structures by Pseudomonas fluorescens biovar I

Pseudomonas fluorescens biovar I was isolated from a pulp mill effluent based on its ability to grow on synthetic media containing 1,2-diarylethane structures as the sole carbon and energy source. Analysis of samples taken from cultures of this strain in benzoin or 4,4-dimethoxybenzoin (anisoin), showed that cleavage between the two aliphatic carbons takes place prior to ring fission. Intermonomeric cleavage was also obtained with crude extracts. Substrates of this reaction were only those 1,2-diarylethane compounds that supported growth of the bacterium. The purification and partial characterization of an enzyme that catalyzes the NADH-dependent reduction of the carbonyl group of benzoin and anisoin is also reported.     

Degradation of 4-nitrobenzoate via 4-hydroxylaminobenzoate and 3,4-dihydroxybenzoate in Comamonas acidovorans NBA-10

Comamonas acidovorans NBA-10 was previously shown to degrade 4-nitrobenzoate via 4-hydroxylaminobenzoate and 3,4-dihydroxybenzoate. Washed cells, grown on a mixture of 4-nitrobenzoate and ethanol, stoichiometrically produced ammonium and 3,4-dihydroxybenzoate from 4-nitrobenzoate under anaerobic conditions provided ethanol was present. In cell extracts 4-hydroxylaminobenzoate was degraded to ammonium and 3,4-dihydroxybenzoate, but this activity was lost upon dialysis. No requirement for a cofactor was found, but rather reduced incubation conditions were necessary to restore enzyme activity. The 4-hydroxylamino-degrading enzyme was purified and the role of this novel type of enzyme in the degradation of nitroaromatic compounds is discussed.Abbreviation 4-ABA 4-aminobenzoate - 4-NBA 4-nitrobenzoate - 4-HABA 4-hydroxylaminobenzoate - 3,4-diHBA 3,4-dihydroxybenzoate     

Metabolism of carbohydrate derivatives by Pseudomonas acidovorans.

Wild-type Pseudomonas acidovorans strain A1 was unable to grow on glycerol or glucose as sole source of carbon and energy although it grew well on gluconate. Spontaneous glycerol-positive mutants, which apparently had become permeable to glycerol, were readily isolated, but glucose-positive mutants did not occur. P. acidovorans lacked glucose dehydrogenase and glucokinase, which were sufficient to account for its inability to grow on glucose. Gluconate was degraded exclusively via a noncoordinately induced Entner-Doudoroff pathway. Phosphogluconate dehydrogenase was undetectable. In contrast to P. aeruginosa, P. acidovorans possessed a single glyceraldehyde-phosphate dehydrogenase activity, which was NAD+ specific and constitutive, and an inducible pyruvate kinase. Moreover, growth of glycerol-positive strain K2 on glycerol did not induce any of the enzymes related to metabolism of hexosephosphate derivatives as occurs in fluorescent pseudomonads.     

Degradation of phenol by a mixed culture of Pseudomonas putida and Cryptococcus elinovii adsorbed on activated carbon

Summary Phenol degradation by a defined mixed culture of Pseudomonas putida P8 and Cryptococcus elinovii H 1, which were immobilized by adsorption on activated carbon, was studied.The immobilized mixed culture was able to degrade phenol up to 17 g/l and degraded it faster than the pure cultures, depending on a complementary metabolism of the two microorganisms.Storage experiments revealed an excellent longterm storage capability of the biocatalyst: activated carbon with adsorbed cells of Pseudomonas putida P8 and Cryptococcus elinovii H1 could be stored up to 12 months without decrease on degradation capacity.Scanning electron micrographs showed that Pseudomonas putida P8 had grown through the pore system of the activated carbon into the inside of the carbon particles.     

Degradation of phenol by a coimmobilized entrapped mixed culture

Summary The degradation of phenol by a defined mixed culture, consisting of Pseudomonas putida P8 and Cryptococcus elinovii H1, was studied. The microorganisms were entrapped either in 30 g·l^-1 calcium-alginate or in chitosan-alginate. Chitosan-alginate entrapment was suitable for a continuous culture. The coimmobilized mixed culture of Cryptococcus elinovii H1 which degrades phenol via an ortho pathway and of Pseudomonas putida P8 which uses the meta cleavage pathway was able to degrade high phenol concentrations up to 3.2 g·l^-1 in semicontinuous cultures. The degradation performance in continuous cultures could reach a maximum of 0.41 g·l^-1·h^-1 phenol. The mixed culture could be stored for up to six months without loss of phenol degradation capacity.Dedicated to Professor Dr. Dr. h. c. K. Esser on the occasion of his 65th birthday     

Cyanide production by Pseudomonas fluorescens and Pseudomonas aeruginosa.

Of 200 water isolates screened, five strains of Pseudomonas fluorescens and one strain of Pseudomonas aeruginosa were cyanogenic. Maximum cyanogenesis by two strains of P. fluorescens in a defined growth medium occurred at 25 to 30 degrees C over a pH range of 6.6 to 8.9. Cyanide production per cell was optimum at 300 mM phosphate. A linear relationship was observed between cyanogenesis and the log of iron concentration over a range of 3 to 300 microM. The maximum rate of cyanide production occurred during the transition from exponential to stationary growth phase. Radioactive tracer experiments with [1-14C]glycine and [2-14C]glycine demonstrated that the cyanide carbon originates from the number 2 carbon of glycine for both P. fluorescens and P. aeruginosa. Cyanide production was not observed in raw industrial wastewater or in sterile wastewater inoculated with pure cultures of cyanogenic Pseudomonas strains. Cyanide was produced when wastewater was amended by the addition of components of the defined growth medium.     

Topology of the anion-selective porin Omp32 from Comamonas acidovorans.

Limited proteolysis experiments were performed with outer membranes from Comamonas acidovorans to probe the topology of its major protein component, the anion-selective porin Omp32. Proteinase K treatment above a critical temperature of 42 degrees C cleaved the surface-exposed regions of the porin, yielding membrane-embedded fragments which were separated by SDS polyacrylamide gel electrophoresis or reversed phase chromatography. The identification of the proteinase K-sensitive sites was performed by microsequencing. This allowed us to determine six surface-exposed sites of the porin, all located in nonconserved primary structure regions. These results along with the previously determined amino acid sequence and in conjunction with some structural constraints applicable to porins allowed us to propose a chain-folding model of the Omp32 porin. The features of our model are compared with the structure of the Rhodobacter capsulatus porin, recently established by X-ray crystallography (Weiss et al., 1991) and they are used to elucidate the structural basis of the anion selectivity.     

Mass production of lipase by fed-batch culture of Pseudomonas fluorescens

Summary High concentration production of an extracellular enzyme, lipase, was achieved by a fed-batch culture of Pseudomonas fluorescens. During the cultivation, temperature, pH and dissolved oxygen concentration wwre maintained at 23°C, 6.5 and 2–5 ppm, respectively. Olive oil was used as a carbon source for microbial growth. To produce lipase effectively the specific feed rate of olive oil had to be maintained in a range of 0.04–0.06 (g oil) · (g dry cell)^-1 · h^-1. The CO₂ evolution rate was monitored to estimate the requirement of olive oil. The ratio of feed rate of olive oil to the CO₂ evolution rate was varied in the range of 20–60 g oil/mol CO₂. The higher value of the ratio accelerated microbial growth, but did not favour lipase production. Once the high cell concentration of 60 g/l had been achieved, the ratio was changed from 50 to 30 g oil/mol CO₂ to accelerate the lipase production. By this CO₂-dependent method a very high activity of lipase, 1980 units/ml, was obtained. Both the productivity and yield of lipase were prominently increased compared with a conventional batch culture.     

Degradation of polycyclic aromatic hydrocarbons by a strain of Pseudomonas fluorescens 16N2

The growth of Pseudomonas fluorescens 16N2 on naphthalene was accompanied with accumulation of salicylate in the culture medium and induction of gentisate 1,2-dioxygenase and catechol 1,2-dioxygenase. The transformation of anthracene by the cells growing on hexadecane led to the formation of 3-hydroxy-2-naphthoate and salicylate. Pathways for naphthalene and anthracene degradation are proposed.