Anaerobic degradation of phenol in batch and continuous cultures by a denitrifying bacterial consortium

Summary The anaerobic degradation of phenol under denitrifying conditions by a bacterial consortium was studied both in batch and continuous cultures. Anaerobic degradation was dependent on NO_f3 ^p– and concentrations up to 4 mm phenol were degraded within 2–5 days. During continuous growth in a fermenter, steady states could be maintained at eight dilution rates (D) corresponding to residence times between 12.5 and 50 h. Culture wash-out occurred at D=0.084 h^–1. The kinetic parameters obtained for anaerobic degradation of phenol under denitrifying conditions by the consortium were: maximam specific growth rate = 0.091 h^–1; saturation constant = 4.91 mg phenol/l; true growth yield = 0.57 mg dry wt/mg phenol; maintenance coefficient = 0.013 mg phenol/mg dry wt per hour. The Haldane model inhibition constant was estimated from batch culture data giving a value of 101 mg/l. The requirement of CO₂ for the anaerobic degradation of phenol with NO_f3 ^p– indicates that phenol carboxylation to 4-hydroxybenzoate was the first step of phenol degradation by this culture. 4-Hydroxybenzoate, proposed as an intermediate of phenol carboxylation under these conditions, was detected only in continuous cultures at very low growth rates (D=0.02 h^–1), but was never detected as a free intermediary metabolite either in batch or in continuous cultures. Correspondence to: N. Khoury     

Simultaneous degradation of 3-chlorobenzoate and phenolic compounds by a defined mixed culture ofPseudomonas spp.

A mixed culture of a chlorobenzoate-(3-CBA)-degradingPseudomonas aeruginosa, strain 3mT, and a phenol/cresols-degradingPseudomonas sp., strain CP4, simultaneously and efficiently degraded mixtures of 3-CBA and phenol/cresols. However, strains 3mT and CP4 usedortho- andmeta-ring cleavage pathways, respectively. Degradation of 3-CBA was complete when the 3-CBA was equal in amount to or less than that of phenol. CP4/3mT inoculum ratios (w/w) of 1:1 or 1:2 gave the most effective degradation of both the substrates in the mixture. The mixed culture degraded equimolar mixtures of 3-CBA/phenol up to 10mm. Equimolar mixtures of 3-CBA ando-, m- orp-cresol were also degraded by the mixed culture.The authors are with the Microbiology and Bioengineering Department, Central Food Technological Research Institute, Mysore-570013, India;     

Degradation of phenol by a defined mixed culture immobilized by adsorption on activated carbon and sintered glass

Summary A defined mixed culture of the yeast Cryptococcus elinovii H1 and the bacterium Pseudomonas putida P8 was immobilized by adsorption on activated carbon and sintered glass, respectively. Depending on its adsorption capacity for phenol the activated carbon system could completely degrade 17 g/l in batch culture, whereas the sintered glass system was able to degrade phenol up to 4 g/l. During semicontinuous degradation of phenol (1 g/l) both systems reached constant degradation times with the fourth batch that lasted 8 h when using the activated carbon system and 10 h in the sintered glass system. In the course of continuous degradation of phenol the activated carbon system reached a maximum degradation rate of 9.2 g l^–1 day^–1 compared to 6.4 g l^–1 day^–1degraded by the sintered glass system. 2-Hydroxymuconic acid semialdehyde could be identified and quantitatively determined as a metabolite of phenol degradation by P. putida P8. Increased membrane permeability under the influence of phenol was demonstrated by the examination of K⁺ efflux from P. putida P8. Offprint requests to: H.-J. Rehm     

Degradation kinetics of phenol by immobilized cells of Candida tropicalis in a fluidized bed reactor

Degradation kinetics of phenol by free and agar-entrapped cells of Candida tropicalis was studied in batch cultures. The initial phenol degradation rate achieved with free cells was higher than that obtained with immobilized cells, when phenol concentrations up to 1000 mg l^–1 were used. However, at higher phenol concentrations, the behaviour was quite different. The initial degradation rate of the immobilized yeast cells was about 10 times higher than that of the free cells, at a phenol concentration of 3500 mg l^–1. The semicontinuous and continuous degradation of phenol by immobilized yeast cells was also investigated in a multi-stage fluidized bed reactor. The highest phenol removal efficiencies and degradation rates as well as the lowest values of residual phenol and chemical oxygen demand were obtained in the semicontinuous culture when phenol concentrations up to 1560 mg l^–1 were used.     

Silica-immobilized Methylobacterium sp. NP3 and Acinetobacter sp. PK1 degrade high concentrations of phenol

Aims: To immobilize Methylobacterium sp. NP3 and Acinetobacter sp. PK1 to silica and determine the ability of the immobilized bacteria to degrade high concentrations of phenol. Methods and Results: The phenol degradation activity of suspended and immobilized Methylobacterium sp. NP3 and Acinetobacter sp. PK1 bacteria was investigated in batch experiments with various concentrations of phenol. The bacterial cells were immobilized by attachment to or encapsulation in silica. The encapsulated bacteria had the highest phenol degradation rate, especially at initial phenol concentrations between 7500 and 10 000 mg l^?1. Additionally, the immobilized cells could continuously degrade phenol for up to 55 days. Conclusions: The encapsulation of a mixed culture of Methylobacterium sp. NP3 and Acinetobacter sp. PK1 is an effective and easy technique that can be used to improve bacterial stability and phenol degradation. Significance and Impact of the Study: Wastewater from various industries contains high concentrations of phenol, which can cause wastewater treatment failure. Silica‐immobilized bacteria could be applied in bioreactors to initially remove the phenol, thereby preventing phenol shock loads to the wastewater treatment system.     

Substrate-dependent autoaggregation of <Emphasis Type="Italic">Pseudomonas putida</Emphasis> CP1 during the degradation of mono-chlorophenols and phenol

A bacterium, CP1, identified as Pseudomonas putida strain, was investigated for its ability to grow on and degrade mono-chlorophenols and phenols as sole carbon sources in aerobic shaking batch culture. The organism degraded up to 1.56 mM 2- and 3-chlorophenol, 2.34 mM 4-chlorophenol and 8.5 mM phenol using an ortho-cleavage pathway. P. putida CP1, acclimated to degrade 2-chlorophenol, was capable of 3-chlorocatechol degradation, while P. putida, acclimated to 4-chlorophenol degradation, degraded 4-chlorocatechol. Growth of P. putida CP1 on higher concentrations of the mono-chlorophenols, ≥1.56 mM 4-chlorophenol and ≥0.78 mM 2- and 3-chlorophenol, resulted in decreases in cell biomass despite metabolism of the substrates, and the formation of large aggregates of cells in the culture medium. Increases in cell biomass with no clumping of the cells resulted from growth of P. putida CP1 on phenol or on lower concentrations of mono-chlorophenol. Bacterial adherence to hydrocarbons (BATH) assays showed cells grown on the higher concentrations of mono-chlorophenol to be more hydrophobic than those grown on phenol and lower concentrations of mono-chlorophenol. The results suggested that increased hydrophobicity and autoaggregation of P. putida CP1 were a response to toxicity of the added substrates. Journal of Industrial Microbiology & Biotechnology (2002) 28, 316–324 DOI: 10.1038/sj/jim/7000249 Received 27 June 2001/ Accepted in revised form 09 February 2002     

Anaerobic degradation of p-cresol in batch and continuous cultures by a denitrifying bacterial consortium

Summary The anaerobic degradation of p-cresol under denitrifying conditions by a bacterial consortium was studied in batch and continuous cultures. Concentrations up to 3 mm were degraded within 5–6 days with 4-hydroxybenzyl alcohol, 4-hydroxybenzaldehyde and 4-hydroxybenzoate as intermediates. Steady states could be maintained at only one dilution rate, D=0.04 h^–1. A further increase in the dilution rate to 0.0 8 h^–1 resulted in culture wash-out. An estimation of the Saturation constant was made (<1 mg/l), taking the maximum specific growth rate as 0.045 h^–1, thus yielding a value of 0.125 mg p-cresol/l. Correspondence to: N. Khoury     

Degradation of 4-chlorophenol in municipal wastewater by adsorptiv immobilized Alcaligenes sp. A 7-2

Summary Alcaligenes sp. A 7-2 has been applied in a packed-bed fermenter to degrade 4-chlorophenol in municipal wastewater continuously. With sterile wastewater degradation rates up to 300 mol/l/h were reached when precultivated Alcaligenes sp. A 7-2 had been adsorbed onto the Lecaton-packed-bed-material.The natural microbial population of the wastewater was not able to degrade 4-chlorophenol. Beside an accumulation of the haloaromatic compound a yellow-greenish substance exhibiting the spectral characteristics of 5-chloro-2-hydroxymuconic acid semialdehyde was found.This compound caused a rapid decrease in metabolic activity of the microbial culture.With non-sterile wastewater Alcaligenes sp. A 7-2 could not be established as member of the natural mixed population. Due to the poor retainment of the specialized strain in the packed-bed the degradation capacity of the fermentation system decreased and 4-chlorophenol was accumulated.     

Biodegradation of 4-chlorophenol by adsorptive immobilized Alcaligenes sp. A 7-2 in soil

Summary Alcaligenes sp. A 7-2 immobilized on granular clay has been applied in a percolator to degrade 4-chlorophenol in sandy soil. Good adsorption rates on granular clay were achieved using cell suspensions with high titres and media at pH 8.0. The influence of various parameters such as aeration rate, pH, temperature, concentration of 4-chlorophenol and size of inoculum on the degradation rate were investigated. During fedbatch fermentations under optimal culture conditions, concentrations of 4-chlorophenol up to 160 mg·1^–1 could be degraded. Semicontinuous culture experiments demonstrated that the degradation potential in soil could be well established and enhanced by the addition of immobilized bacteria. Continuous fermentation was performed with varying 4-chlorophenol concentrations in the feed and different input levels. The maximum degradation rate was 1.64 g·1^–1·day^–1. Offprint requests to: H.-J. Rehm     

Degradation of phenol and phenolic compounds by Pseudomonas putida EKII

Summary The phenol-degrading strain Pseudomonas putida EKII was isolated from a soil enrichment culture and utilized phenol up to 10.6 mM (1.0 g·1 ^-1) as the sole source of carbon and energy. Furthermore, cresols, chlorophenols, 3,4-dimethylphenol, and 4-chloro-m-cresol were metabolized as sole substrates by phenol-grown resting cells of strain EKII. Under conditions of cell growth, degradation of these xenobiotics was achieved only in co-metabolism with phenol. Phenol hydroxylase activity was detectable in whole cells but not in cell-free extracts. The specificity of the hydroxylating enzyme was found during transformation of cresols and chlorophenols: ortho- and meta-substituted phenols were degraded via 3-substituted catechols, while degradation of para-substituted phenols proceeded via 4-substituted catechols. In cell-free extracts of phenol-grown cells a high level of catechol 2,3-dioxygenase as well as smaller amounts of 2-hydroxymuconic semialdehyde hydrolyase and catechol 1,2-dioxygenase were detected. The ring-cleaving enzymes were characterized after partial purification by DEAE-cellulose chromatography.     

Enhanced degradation of phenol by <Emphasis Type="Italic">Pseudomonas</Emphasis> sp. CP4 entrapped in agar and calcium alginate beads in batch and continuous processes

Phenol is one of the major toxic pollutants in the wastes generated by a number of industries and needs to be eliminated before their discharge. Although microbial degradation is a preferred method of waste treatment for phenol removal, the general inability of the degrading strains to tolerate higher substrate concentrations has been a bottleneck. Immobilization of the microorganism in suitable matrices has been shown to circumvent this problem to some extent. In this study, cells of Pseudomonas sp. CP4, a laboratory isolate that degrades phenol, cresols, and other aromatics, were immobilized by entrapment in Ca-alginate and agar gel beads, separately and their performance in a fluidized bed bioreactor was compared. In batch runs, with an aeration rate of 1 vol⁻¹ vol⁻¹ min⁻¹, at 30°C and pH 7.0 ± 0.2, agar-encapsulated cells degraded up to 3000 mg l⁻¹ of phenol as compared to 1500 mg l⁻¹ by Ca-alginate-entrapped cells whereas free cells could tolerate only 1000 mg l⁻¹. In a continuous process with Ca-alginate entrapped cells a degradation rate of 200 mg phenol l⁻¹ h⁻¹ was obtained while agar-entrapped cells were far superior and could withstand and degrade up to 4000 mg phenol l⁻¹ in the feed with a maximum degradation rate of 400 mg phenol l⁻¹ h⁻¹. The results indicate a clear possibility of development of an efficient treatment technology for phenol containing waste waters with the agar-entrapped bacterial strain, Pseudomonas sp. CP4.     

Chlorobenzoate catabolism and interactions between Alcaligenes and Pseudomonas species from Bloody Run Creek

A mixed community of bacteria from surface runoff waters of the Hyde Park industrial landfill was enriched on 3-chlorobenzoate. Alcaligenes and Pseudomonas species were dominant in the community. Alcaligenes sp. BR60 carried an unstable plasmid specifying 3-chlorobenzoate catabolism. Metabolites detected in culture supernatants included chlorocatechol and chloro-cis,cis-muconic acid. Oxygen uptake in the presence of 3- and 4-substituted methyl-catechols revealed a catechol-1,2-oxygenase activity specific for substituted catechols with very limited activity for catechol. The isolate grew very slowly on benzoate. Alcaligenes sp. BR60 was isolated in co-culture with Pseudomonas fluorescens NR52. The latter contained no detectable plasmids and did not grow on benzoate or any of the chlorobenzoates in pure culture. Growth of the co-culture in Bloody Run Creek water supplemented with 3-chlorobenzoate indicated that phosphate concentrations in the water severely limited biodegradation. Under phosphate limited conditions in continuous culture, Pseudomonas fluorescens NR52 effectively scavenged available phosphate when it was present at a ratio of 1 cell to 20 of Alcaligenes sp. BR60. Under these conditions the growth of Alcaligenes sp. BR60 on 3-chlorobenzoate was reduced 5 fold, the frequency of plasmid deletion mutants increased, and 96% of the contaminant remained in the outflow in the form of the starting material or metabolites. No evidence was found for conjugation of the plasmid determining chlorobenzoate catabolism in Alcaligenes sp. BR60 to P. fluorescens NR52.Abbreviations 3 and 4 Cba chlorobenzoic acid isomers and growth phenotypes - Ba benzoic acid     

Biodegradation of 4-chlorophenol by entrappedAlcaligenes sp. A 7-2

Summary The degradation of 4-chlorophenol by free and by Ca-alginate-immobilized cells ofAlcaligenes sp. A 7-2 has been studied. Increasing concentrations of 4-chlorophenol (0.4–0.55 mM) were better tolerated and more quickly degraded by the immobilized organisms than by free cells. The capability for haloarene-degradation is inducible. In semicontinuous fermentation at pH 7 a minimal degradation time of 5 h for degrading 0.2 mM 4-chlorophenol was reached. Fermentation temperature was shown to be important for inducing the degradation capability, but to be less important for the degradation rate by induced organisms. High-frequency feeding of small amounts of 4-chlorophenol (0.05 mM) was more favourable than low-frequency feeding of larger amounts (0.15 mM).Continuous fermentation with unbuffered medium allowed a degradation rate of about 2 mmol·l^-1·d^-1; with buffered medium a higher degradation rate of nearly 4 mmol·l^-1·d^-1 was reached, but the Ca-alginate beads dissolved.     

Efficacy of bacterial consortium-AIE2 for contemporaneous Cr(VI) and azo dye bioremediation in batch and continuous bioreactor systems, monitoring steady-state bacterial dynamics using qPCR assays

Bacterial consortium-AIE2 with a capability of contemporaneous Cr(VI) reduction and azo dye RV5 decolourization was developed from industrial wastewaters by enrichment culture technique. The 16S rRNA gene based molecular analyses revealed that the consortium bacterial community structure consisted of four bacterial strains namely, Alcaligenes sp. DMA, Bacillus sp. DMB, Stenotrophomonas sp. DMS and Enterococcus sp. DME. Cumulative mechanism of Cr(VI) reduction by the consortium was determined using in vitro Cr(VI) reduction assays. Similarly, the complete degradation of Reactive Violet 5 (RV5) dye was confirmed by FTIR spectroscopic analysis. Consortium-AIE2 exhibited simultaneous bioremediation efficiencies of (97.8 ± 1.4) % and (74.1 ± 1.2) % in treatment of both 50 mg l⁻¹ Cr(VI) and RV5 dye concentrations within 48 h of incubation at pH 7 and 37°C in batch systems. Continuous bioreactor systems achieved simultaneous bioremediation efficiencies of (98.4 ± 1.5) % and (97.5 ± 1.4) % after the onset of steady-state at 50 mg l⁻¹ input Cr(VI) and 25 mg l⁻¹ input RV5 concentrations, respectively, at medium dilution rate (D) of 0.014 h⁻¹. The 16S rRNA gene copy numbers in the continuous bioreactor as determined by real-time PCR assay indicated that Alcaligenes sp. DMA and Bacillus sp. DMB dominated consortium bacterial community during the active continuous bioremediation process.     

Nitrite and nitrate synthesis from pyruvic-oxime by anAlcaligenes sp.

AnAlcaligenes sp. isolated from soil was characterized as to its ability to oxidize and grow on pyruvic-oxime. Abundant nitrification of pyruvic-oxime was demonstrated with maximal nitrite and nitrate production of 1867 mg NO₂ ^–-N per liter and 42 mg NO₃ ^–-N per liter. TheAlcaligenes sp. oxidized hydroxylamine and this metabolism was stimulated when either acetate or pyruvate was present. This organism was also capable of limited pyruvic-oxime oxidation when cultured in an acidic medium. The metabolism of pyruvic-oxime and nitrification by theAlcaligenes sp. in the environment are discussed.     

Catabolic instability,plasmid gene deletion and recombination in Alcaligenes sp. BR60

An Alcaligenes sp. BR60, isolated from surface runoff waters of the Hyde Park industrial landfill, contained a novel 85 kb catabolic plasmid (pBR60) functional in 3-chlorobenzoate (3Cba) degradation. The plasmid exhibited a spontaneous 3.2% frequency of deletion of a 14 kb fragment specifying 3Cba degradation. The deletion mutant BR40 and mitomycin C cured strains were not able to grow on 3Cba and had reversion frequencies of less than 10^-10 cell^-1 generation^-1. Transformation or conjugation of pBR60 into cured strains restored catabolic activity. An EcoRI, BgIII, HindIII and SaII restriction map of the deletion region was constructed, and EcoRI and HindIII fragments spanning the deletion region of the plasmid were cloned in pUC18. Conjugation of resistance plasmid R 68.45 into Alcaligenes sp. BR60, with selection on antibiotics, resulted in the elimination of pBR60 and maintenance of unaltered R68.45. In 30% of the exconjugants, 3Cba degradative capacity was retained, although variation in the regulation of 3Cba degradation was observed in these strains. Hybridization of deletion region fragments to BgIII digested total DNA of BR60 and the R68.45 cured exconjugants revealed the presence of pBR60 deletion region sequences in the chromosome of exconjugants. Hybridization also revealed a repeated sequence flanking the deletion region of pBR60. Selection on 4-chlorobenzoate as a sole source of carbon and energy resulted in the isolation of 4Cba⁺ mutants of Alcaligenes sp. BR60.Abbreviations 3 and 4 Cba chlorobenzoic acid isomers and growth phenotypes - HPLC high pressure liquid chromatography - ATCC American Type Culture Collection     

Evaluation ofl-lactic acid production in batch, fed-batch, and continuous cultures ofRhizopus sp. MK-96-1196 using an airlift bioreactor

Various processes which producel-lactic acid using ammonia-tolerant mutant strain,Rhizopus sp. MK-96-1196, in a 3 L airlift bioreactor were evaluated. When the fed-batch culture was carried out by keeping the glucose concentration at 30 g/l, more than 140 g/l ofl-lactic acid was produced with a product yield of 83%. In the case of the batch culture with 200 g/l of initial glucose concentration, 121 g/L ofl-lactic acid was obtained but the low product yield based on the amount of glucose consumed. In the case of a continuous culture, 1.5 g/l/h of the volumetric productivity with a product yield of 71% was achieved at dilution rate of 0.024 h⁻¹. Basis on these results three processes were evaluated by simple variable cost estimation including carbon source, steam, and waste treatment costs. The total variable costs of the fed-batch and continuous cultures were 88% and 140%, respectively, compared to that of batch culture. The fed-batch culture with highl-lactic acid concentration and high product yield decreased variable costs, and was the best-suited for the industrial production ofl-lactic acid.     

The production of hemicellulose-degrading enzymes byBacillus macerans in anaerobic culture

Summary The cell-associated and exocellular hemicellulolytic polysaccharide depolymerase and glycoside hydrolase activity ofBacillus macerans NCDO 1764 was monitored over a range of anaerobic growth conditions in batch and continuous culture. The enzymes were detectable throughout the complete growth cycle in batch culture reaching and maintaining maximum levels in the stationary phase. In continuous culture enzyme activity was largely independent of growth rate (D=0.025–0.1 h^-1) although the activity was reduced at higher dilution rates (0.125–0.15 h^-1). Although activity was detectable over a wide pH range (pH 5.5–7.5) it was pH dependent, and maximum activities of both the cell-associated and exocellular enzymes were measured in cultures maintained at pH 6.5–7.0±0.1.The principal metabolites formed anaerobically from xylose byB. macerans in batch and continuous culture were acetic acid, formic acid and ethanol which represented 95–99% of the products formed. Smaller amounts of acetone,d,l-lactic acid and succinic acid were formed together with traces of butyric acid (<5 nmol/ml) and isovaleric acid (<25 nmol/ml). The proportions of the metabolites produced varied with growth conditions and were influenced by the pH of the culture and the rate and stage of growth of the microorganism.     

Development of a continuous system for the degradation of a cyanuric acid by adsorbed Pseudomonas sp. NRRL B-12228

Cyanuric acid in high concentrations (15.5 mm) was degraded completely by Pseudomonas sp. NRRL B-12228 independently of glucose concentration. In the batch fermentations there was a relation between the glucose concentration, on the one hand, and the liberation of ammonia or production of protein, on the other. The greater the supply of carbon, the more biomass was produced, and fewer NH _inf4 ^sup+ ions were released. Continuous fermentations using adsorbed cells could be performed to degrade cyanuric acid. In spite of different glucose feeding there was only a negligible difference in residues of s-triazine. In a one-step continuous system with dilution rates between 0.021 h^–1 and 0.035 h^–1, even a ratio of 0.65 between glucose and cyanuric acid was not sufficient to degrade the cyanuric acid supplied (320–540 mol l^–1 h^–1) completely. When a continuous two-step system was applied with dilution rates between 0.035 h^–1 and 0.056 h^–1, the consumption of carbon source could be minimized while s-triazine degradation up to 860 mol l^–1 h^–1 was complete. In this way the ratio between glucose and cyanuric acid could be increased to 0.25 (molar C:N ratio = 0.33:1). Thereby the process was made considerably more economic.     

Role of oxygen in the utilization of phenol by Pseudomonas CF600 in continuous culture

The dissolved oxygen (DO) level is the key factor which decides the rate of degradation of the organic load in aerobic growth conditions. In this study the role of DO levels on the utilization of phenols has been reported using the continuous culture system. A phenol-utilizing strain, Pseudomonas CF600 has been used as a model. Its phenol-degrading capacity was studied using continuous cultivation for a period of 60 days. The bioreactor was kept at a dilution rate of 0.006 h^–1 with DO levels maintained at 2, 3, and 4 ppm keeping all the other cultivation conditions constant. Physiological variations under the cultivation conditions were studied by monitoring off-line phenol utilization and respirometric analysis of harvested culture against different substrates. It was observed that the accumulation of 2-hydroxymuconate semialdehyde (HMS), an intermediate in the phenol degradation pathway, depends on the DO level. The maximum level of HMS in the medium observed was 3.92 M when DO was maintained at 2 ppm whereas with 3 ppm of DO, HMS level was below 0.4 M. Oxygen uptake data of the cells harvested from cultures grown at different DO levels showed that the uptake was highest at 3 ppm DO for all the substrates tried. When phenol was used as substrate, the oxygen uptake rate was 42.66, 66.36 and 35.55 nM/min/mg dry weight of cells at 4, 3 and 2 ppm DO respectively. Results show that DO levels influence the rate of phenol utilization in Pseudomonas CF600.