Biodegradation of 1,1,1-trichloroethane by a carbon tetrachloride-degrading denitrifying consortium

A denitrifying consortium capable of degrading carbon tetrachloride (CT) was shown to also degrade 1,1,1-trichloroethane (TCA). Fed-batch experiments demonstrated that the specific rate of TCA degradation by the consortium was comparable to the specific rate of CT degradation (approximately 0.01 L/gmol/min) and was independent of the limiting nutrient. Although previous work demonstrated that 4-50% of CT transformed by the consortium was converted to chloroform (CF), no reductive dechlorination products were detected during TCA degradation, regardless of the limiting nutrient. The lack of chlorinated TCA degradation products implies that the denitrifying consortium possesses an alternate pathway for the degradation of chlorinated solvents which does not involve reductive dechlorination. Copyright 1998 John Wiley & Sons, Inc.     

Functional consortium for denitrifying sulfide removal process

Denitrifying sulfide removal (DSR) process simultaneously converts sulfide, nitrate, and chemical oxygen demand from industrial wastewaters to elemental sulfur, nitrogen gas, and carbon dioxide, respectively. This investigation utilizes a dilution-to-extinction approach at 10⁻² to 10⁻⁶ dilutions to elucidate the correlation between the composition of the microbial community and the DSR performance. In the original suspension and in 10⁻² dilution, the strains Stenotrophomonas sp., Thauera sp., and Azoarcus sp. are the heterotrophic denitrifiers and the strains Paracoccus sp. and Pseudomonas sp. are the sulfide-oxidizing denitrifers. The 10⁻⁴ dilution is identified as the functional consortium for the present DSR system, which comprises two functional strains, Stenotrophomonas sp. strain Paracoccus sp. At 10⁻⁶ dilution, all DSR performance was lost. The functions of the constituent cells in the DSR granules were discussed based on data obtained using the dilution-to-extinction approach.     

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     

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     

Sulfate reduction with methanol by a thermophilic consortium obtained from a methanogenic reactor

 An enrichment culture obtained from anaerobic granular sludge of a bench-scale anaerobic reactor degraded methanol at 65°C via sulfate reduction and acetogenesis. Sulfate reduction was the dominant process (S^2-/acetate=2.5). No methane formation was observed. Approximately 30% of the methanol was converted by acetogenic bacteria to acetate, while the remainder was degraded by these bacteria to H₂ and CO₂ in syntrophy with hydrogen-consuming sulfate-reducing bacteria. Pure cultures of sulfate-reducing and acetogenic bacteria were isolated and characterized. Received: 4 December 1995 / Received revision: 15 April 1996 / Accepted: 22 April 1996     

Selenite reduction by a denitrifying culture: batch- and packed-bed reactor studies

Selenite reduction by a bacterial consortium enriched from an oil refinery waste sludge was studied under denitrifying conditions using acetate as the electron donor. Fed-batch studies with nitrate as the primary electron acceptor showed that accumulation of nitrite led to a decrease in the extent of selenite reduction. Also, when nitrite was added as the primary electron acceptor, rapid selenite reduction was observed only after nitrite was significantly depleted from the medium. These results indicate that selenite reduction was inhibited at high nitrite concentrations. In addition to batch experiments, continuous-flow selenite reduction experiments were performed in packed-bed columns using immobilized enrichment cultures. These experiments were carried out in three phases: in phase I, a continuous nitrate feed with different inlet selenite concentration was applied; in phase II, nitrate was fed in a pulsed fashion; and in phase III, nitrate was fed in a continuous mode but at much lower concentrations than the other two phases. During the phase I experiments, little selenite was removed from the influent. However, when the column was operated in the pulse feed strategy (phase II) or in the continuous mode with low nitrate levels (phase III), significant quantities of selenium were removed from solution and retained in the immobilization matrix in the column. Thus, immobilized denitrifying cultures can be effective in removing selenium from waste streams, but nitrate-limited operating conditions might be required.     

Acetylene inhibition of nitrous oxide reduction by denitrifying bacteria

Acetylene (0.1 atm) caused complete or almost complete inhibition of reduction of N₂O by whole cell suspensions of Pseudomonas perfectomarinus, P. aeruginosa and Micrococcus denitrificans. Acetylene did not inhibit reduction of NO₃^? or NO₂^? by these organisms. In the presence of acetylene there was stoichiometric conversion of NO₃^? or NO₂^? to N₂O with negligible subsequent reduction of the latter. In the absence of acetylene there was no or only transient accumulation of N₂O. The data are consistent with the view that N₂O is an obligatory intermediate in the reduction of NO₂^? to N₂ in all of the three organisms studied.     

Microflora of dissimilative nitrate reduction in a denitrifying reactor

The predominant denitrifiers and ammonifiers from methanogenic, aerobic and denitrifying reactor sludge were isolated and characterised. The population of ammonifiers increased by three orders of magnitude during the operation of the denitrifying reactor treating landfill leachate. The predominant ammonifiers were enterobacteria, and the predominant denitrifiers belonged to the genera Alcaligenes and Pseudomonas. Studies in pure culture showed that ammonia production by ammonifiers was favoured by fermentable substrates and by high C/N ratios. For acetate, only nitrite was obtained as the reduction product of nitrate, even at high C/N ratios. Furthermore, for glucose, nitrite addition caused a shift in fermentation products, with an increase in the acetate/ethanol ratio, with no significant differences in growth rates. Received: 14 January 1998 / Received revision: 11 May 1998 / Accepted: 21 May 1998     

Inhibition by sulfide of nitric and nitrous oxide reduction by denitrifying Pseudomonas fluorescens.

The influence of low redox potentials and H2S on NO and N2O reduction by resting cells of denitrifying Pseudomonas fluorescens was studied. Hydrogen sulfide and Ti(III) were added to achieve redox potentials near -200 mV. The control without reductant had a redox potential near +200 mV. Production of 13NO, [13N]N2O, and [13N]N2 from 13NO3- and 13NO2- was followed. Total gas production was similar for all three treatments. The accumulation of 13NO was most significant in the presence of sulfide. A parallel control with autoclaved cells indicated that the 13NO production was largely biological. The sulfide inhibition was more dramatic at the level of N2O reduction; [13N]N2O became the major product instead of [13N]N2, the dominant product when either no reductant or Ti(III) was present. The results indicate that the specific action of sulfide rather than the low redox potential caused a partial inhibition of NO reduction and a strong inhibition of N2O reduction in denitrifying cells.     

Evidence for aromatic ring reduction in the biodegradation pathwayof carboxylated naphthalene by a sulfate reducing consortium

Naphthalene was used as a model compound in order to study the anaerobic pathway of polycyclic aromatic hydrocarbon degradation. Previously we had determined that carboxylation is an initial step for anaerobic metabolism of naphthalene, but no other intermediate metabolites were identified (Zhang & Young 1997). In the present study we further elucidate the pathway with the identification of six novel naphthalene metabolites detected when cultures were fed naphthalene in the presence of its analog 1-fluoronaphthalene. Results from cultures supplemented with either deuterated naphthalene or non-deuterated naphthalene plus [¹³C]bicarbonate confirm that the metabolites originated from naphthalene. Three of these metabolites were identified by comparison with the following standards: 2-naphthoic acid (2-NA), 5,6,7,8-tetrahydro-2-naphthoic acid, and decahydro-2-naphthoic acid. The presence of 5,6,7,8-tetrahydro-2-NA as a metabolite of naphthalene degradation indicates that the first reduction reaction occurs at the unsubstituted ring, rather than the carboxylated ring. The overall results suggest that after the initial carboxylation of naphthalene, 2-NA is sequentially reduced to decahydro-2-naphthoic acid through 5 hydrogenation reactions, each of which eliminated one double bond. Incorporation of deuterium atoms from D₂O into 5,6,7,8-tetrahydro-2-naphthoic acid suggests that water is the proton source for hydrogenation.     

Kinetics of microbial bromate reduction in a hydrogen-oxidizing, denitrifying biofilm reactor

Bromate (BrO(3)(-)) is an oxidized contaminant produced from bromide (Br(-)) during ozonation and advanced oxidation of drinking water. Previous research shows that denitrifying bioreactors can reduce bromate to innocuous bromide. We studied a hydrogen-based, denitrifying membrane-biofilm reactor (MBfR) for bromate reduction, and report the first kinetics for a hydrogen-based bromate reduction process. A mixed-culture MBfR reduced up to 1,500 microg/L bromate to below 10 microg/L with a 50-min hydraulic residence time. Kinetics were determined using short-term tests on a completely mixed MBfR at steady state with an influent of 5 mg N/L nitrate plus 100 microg/L bromate. Short-term tests examined the impact of pH, nitrite, nitrate, and bromate on bromate reduction rates in the MBfR. Kinetic parameters for the process were estimated based on the short-term bromate tests. The q(max) for bromate reduction was 0.12 mg BrO(3)(-) x mg(x)(-1) x day(-1), and the K was 1.2 mg BrO(3)(-)/L. This q(max) is 2-3 times higher than reported for heterotrophic enrichments, and the K is the first reported in the literature. Nitrite and nitrate partially inhibited bromate reduction, with nitrite exerting a stronger inhibitory effect. Bromate was self-inhibitory at concentrations above 15 mg/L, but up to 50 mg/L of bromate had no inhibitory effect on denitrification. The optimum pH was approximately 7. We also examined the performance of an MBfR containing pure culture of the denitrifying bacterium Ralstonia eutropha. Under conditions similar to the mixed-culture tests, no bromate reduction was detected, showing that not all denitrifying bacteria are active in bromate reduction. Our results suggest the presence of specialized, dissimilatory bromate-reducing bacteria in the mixed-culture MBfR.     

Low temperature reduction of hexavalent chromium by a microbial enrichment consortium and a novel strain of Arthrobacter aurescens

Background  

Chromium is a transition metal most commonly found in the environment in its trivalent [Cr(III)] and hexavalent [Cr(VI)] forms. The EPA maximum total chromium contaminant level for drinking water is 0.1 mg/l (0.1 ppm). Many water sources, especially underground sources, are at low temperatures (less than or equal to 15 Centigrade) year round. It is important to evaluate the possibility of microbial remediation of Cr(VI) contamination using microorganisms adapted to these low temperatures (psychrophiles).     

Simultaneous oxidation of ammonium and p-cresol linked to nitrite reduction by denitrifying sludge

The metabolic capability of denitrifying sludge to oxidize ammonium and p-cresol was evaluated in batch cultures. Ammonium oxidation was studied in presence of nitrite and/or p-cresol by 55 h. At 50 mg/L NH₄⁺-N and 76 mg/L NO₂⁻-N, the substrates were consumed at 100% and 95%, respectively, being N₂ the product. At 50 mg/L NH₄⁺-N and 133 mg/L NO₂⁻-N, the consumption efficiencies decreased to 96% and 70%, respectively. The increase in nitrite concentration affected the ammonium oxidation rate. Nonetheless, the N₂ production rate did not change. In organotrophic denitrification, the p-cresol oxidation rate was slower than ammonium oxidation. In litho-organotrophic cultures, the p-cresol and ammonium oxidation rates were affected at 133 mg/L NO₂⁻-N. Nonetheless, at 76 mg/L NO₂⁻-N the denitrifying sludge oxidized ammonium and p-cresol, but at different rate. Finally, this is the first work reporting the simultaneous oxidation of ammonium and p-cresol with the production of N₂ from denitrifying sludge.     

Identification of genes coding for hydrolytic dehalogenation in the metagenome derived from a denitrifying 4-chlorobenzoate degrading consortium.

A metagenomic approach was taken to investigate the genetic basis for the ability of an anaerobic consortium to grow on either 4-chlorobenzoate or 4-bromobenzoate under denitrifying conditions. Degenerate PCR primers were designed for the family of 4-chlorobenzoyl-CoA dehalogenase genes. The primers were utilized to screen a metagenome library and two overlapping clones were identified which yield a PCR product. The complete sequence of one metagenome clone was determined and genes encoding 4-chlorobenzoyl-CoA ligase (FcbA) and 4-chlorobenzoyl-CoA dehalogenase (FcbB) were identified. Analysis of the ORFs present in the nucleotide sequence suggests that the metagenome clone originated from an uncultured denitrifying microorganism belonging to the Betaproteobacteria. Interestingly, unlike similar gene clusters reported in aerobes, a gene encoding 4-hydroxybenzoyl-CoA thioesterase was not present in the gene cluster. This suggests that 4-hydroxybenzoyl-CoA is further degraded via the anaerobic reduction pathway in the corresponding microorganism instead of through thioester hydrolysis to yield 4-hydroxybenzoate.     

Anaerobic oxidation of p-cresol by a denitrifying bacterium

Metabolism of p-cresol (pCr) under nitrate-reducing conditions is mediated by the denitrifying bacterial isolate PC-07. The methyl substituent of the substrate is oxidized anaerobically by whole-cell suspensions of PC-07 through a series of dehydrogenation and hydration reactions to yield p-hydroxybenzoate (pOHB) in stoichiometric proportions. The partially oxidized intermediates in the pathway p-hydroxybenzyl alcohol and p-hydroxybenzaldehyde can also serve as substrates for pOHB formation. Nitrate is required as the external electron acceptor and is reduced to molecular N2. Reduction of the nitrate is stoichiometric, with pCr serving as the electron donor. In addition, the molar relationship between the electron acceptor (NO3-) reduced to the electron donor oxidized decreased to approximately 2:3 and then to 1:3 when p-hydroxybenzyl alcohol or p-hydroxybenzaldehyde, respectively, served as substrates. The decreased ratios were to be expected when the partially oxidized intermediates served as substrates, because they provided correspondingly less reducing power for pOHB formation. The anaerobic oxidation of pCr by PC-07 demonstrates a mechanism whereby aromatic compounds can be transformed in anoxic environments.     

Mineralization of 2-aminobenzenesulfonate by a bacterial consortium

A variety of environmental inocula were tested for the development of 2-aminobenzenesulfonate (2-ABS, Orthanilic acid) degrading bacterial enrichment. A bacterial consortium (BC), which could utilize 2-ABS as the sole carbon and energy source, could only be developed from the sludge derived from a wastewater treatment unit of a large chemical industry manufacturing nitro and aminoaromatics. BC consisted of two bacterial strains. Based on 16S rDNA sequence analysis, these strains were identified to be belonging to the genus, Acinetobacter and Flavobacterium. The consortium could degrade 1,000 mg l⁻¹ 2-ABS within 40 h. Evidence for the extensive mineralization of 2-ABS, during the growth of BC, was derived from U.V-spectral and total organic carbon analysis. BC was highly specific for 2-ABS, as other benzene sulfonates tested in this study, including other ABS isomers, were not utilized as growth substrates. 2-ABS removal pattern in the presence of glucose was significantly influenced by acclimation characteristics of the culture. Consortium adapted to 2-ABS/glucose demonstrated the concomitant removal of both substrates, whereas glucose exerted catabolic repression on 2-ABS removal with glucose adapted culture. Presence of chloramphenicol inhibited 2-ABS degradation by cells, pregrown on succinate, indicating that the 2-ABS degrading enzymes are inducible in nature. Thus the presence of 2-ABS is essential for maintaining the high degradation potential. This enrichment culture can find an application in the treatment of 2-ABS containing wastewaters.     

Sugarcane cellulose utilization by a defined microbial consortium

Microorganisms isolated from diverse environmental sources were initially screened for carboxymethylcellulase activity. Nine strains that grew at elevated temperatures and which presented the highest activity were characterized further. Culture supernatants were assayed for potentiation of the enzymatic activity and, based on these results, consortia of four or nine microorganisms were tested for their capacity to grow on, and degrade a sugarcane leaf substrate. As predicted by the supernatant mixes, both consortia assayed were capable of degrading the cellulosic substrate provided. The group comprising of four strains was as efficient as the mix of all nine strains.     

Anaerobic degradation of toluene by a denitrifying bacterium

A denitrifying bacterium, designated strain T1, that grew with toluene as the sole source of carbon under anaerobic conditions was isolated. The type of agar used in solid media and the toxicity of toluene were determinative factors in the successful isolation of strain T1. Greater than 50% of the toluene carbon was oxidized to CO2, and 29% was assimilated into biomass. The oxidation of toluene to CO2 was stoichiometrically coupled to nitrate reduction and denitrification. Strain T1 was tolerant of and grew on 3 mM toluene after a lag phase. The rate of toluene degradation was 1.8 mumol min-1 liter-1 (56 nmol min-1 mg of protein-1) in a cell suspension. Strain T1 was distinct from other bacteria that oxidize toluene anaerobically, but it may utilize a similar biochemical pathway of oxidation. In addition, o-xylene was transformed to a metabolite in the presence of toluene but did not serve as the sole source of carbon for growth of strain T1. This transformation was dependent on the degradation of toluene.     

Anaerobic biodegradation of pentachlorophenol by a methanogenic consortium

An anaerobic consortium degrading pentachlorophenol (PCP) by methanogenic fermentation was enriched from PCP-contaminated soils. In a semi-continuous reactor, PCP biodegradation was unstable and necessitated periodic additions of unacclimated anaerobic sludge waste to restore the activity. In continuous-flow reactors, PCP degradation activity was more stable when a mixture of glucose and sodium formate was used as secondary carbon source instead of glucose. The analysis of the chlorophenol intermediates suggested that the main pathway of PCP dechlorination was PCP 2,3,5,6-tetrachlorophenol 2,3,5-trichlorophenol 3,5-dichlorophenol 3-chlorophenol phenol. In a laboratory-scale continuous-upflow fixed-film column reactor, a PCP removal of more than 99% was achieved at a PCP loading rate of 60 mol (1 reactor volume)^–1 day^–1 for a hydraulic retention time of 0.7 day. Analysis of culture samples taken at different levels in the reactor have shown that, at this PCP loading rate, only the lower part of the reactor was active. 3-chlorophenol and 3,5- and 3,4-dichlorophenol were detected at the different levels of the reactor. A study of the microorganisms in the biofilm was carried out by scanning electron microscopy and suggested that the microorganisms involved in the consortium were present as a well-structured arrangement. Methanosaeta-like microorganisms were observed mainly at the base of the biofilm whereas, at the surface, a larger diversity of morphotypes was observed in which coccoid or small rod organisms were dominant. This work shows the importance of the design and the control of the operation parameters on the efficiency of the fixed-film reactor.