Complete degradation of tetrachloroethene in coupled anoxic and oxic chemostats

Anaerobic tetrachloroethene(C₂Cl₄)-dechlorinating bacteria were enriched in slurries from chloroethene-contaminated soil. With methanol as electron donor, C₂Cl₄ and trichloroethene (C₂HCl₃) were reductively dechlorinated to cis-1,2-dichloroethene (cis-C₂H₂Cl₂), whereas, with l-lactate or formate, complete dechlorination of C₂Cl₄ via C₂HCl₃, cis-C₂H₂Cl₂ and chloroethene (C₂H₃Cl) to ethene was obtained. In oxic soil slurries with methane as a substrate, complete co-metabolic degradation of cis-C₂H₂Cl₂ was obtained, whereas C₂HCl₃ was partially degraded. With toluene or phenol both of the above were readily co-metabolized. Complete degradation of C₂Cl₄ was obtained in sequentially coupled anoxic and oxic chemostats, which were inoculated with the slurry enrichments. Apparent steady states were obtained at various dilution rates (0.02–0.4 h⁻¹) and influent C₂Cl₄-concentrations (100–1000 μM). In anoxic chemostats with a mixture␣of␣formate and glucose as the carbon and electron source, C₂Cl₄ was transformed at high rates (above␣140 μmol l⁻¹ h⁻¹, corresponding to 145 nmol Cl⁻ min⁻¹ mg protein⁻¹) into cis-C₂H₂Cl₂ and C₂H₃Cl. Reductive dechlorination was not affected by addition of 5 mM sulphate, but strongly inhibited after addition of 5 mM nitrate. Our results (high specific dechlorination rates and loss of dechlorination capacity in the absence of C₂Cl₄) suggest that C₂Cl₄-dechlorination in the anoxic chemostat was catalysed by specialized dechlorinating bacteria. The partially dechlorinated intermediates, cis-C₂H₂Cl₂ and C₂H₃Cl, were further degraded by aerobic phenol-metabolizing bacteria. The maximum capacity for chloroethene (the sum of tri-, di- and monochloro derivatives removed) degradation in the oxic chemostat was 95 μmol l⁻¹ h⁻¹ (20 nmol min⁻¹ mg protein⁻¹), and that of the combined anoxic → oxic reactor system was 43.4 μmol l⁻¹ h⁻¹. This is significantly higher than reported thus far. Received: 17 April 1997 / Received revision: 6 June 1997 / Accepted: 7 June 1997     

Methanogenic and perchloroethylene-dechlorinating activity of anaerobic granular sludge

The biodegradation and toxicity of tetrachloroethylene (C₂Cl₄) and trichloroethylene (C₂HCl₃) were studied with different anaerobic enrichment cultures using the following electron donors: acetate, propionate, butyrate, methanol, formate and hydrogen. All of them sustained dechlorination except propionate, for which C₂Cl₄ biodegradation rates were not significant. The best results were obtained with butyrate. Hydrogen appeared to be a relevant electron donor for dechlorination with the present cultures. In the presence of specific inhibitors such as bromoethanesulphonate or molybdate, a slight inhibition of dechlorination was observed. According to dechlorination kinetics, Monod-type behaviour was observed up to 120 μM C₂Cl₄ or 200 μM C₂HCl₃ with K _s values around 7 μM for both compounds. Dechlorination was partially inhibited at higher concentrations. In contrast, methanogens, or at least methane production, were more sensitive to the presence of chlorinated ethylenes and inhibition of methanogenesis was observed to different extents over all the C₂Cl₄/C₂HCl₃ concentration range tested, even at the lowest concentrations. Received: 17 April 1998 / Received revision: 18 June 1998 / Accepted: 19 June 1998     

Change in ammonia-oxidizing microorganisms in enriched nitrifying activated sludge

In this study, sludge was taken from a municipal wastewater treatment plant that contained a nearly equal number of archaeal amoA genes (5.70 × 10⁶ ± 3.30 × 10⁵ copies mg sludge⁻¹) to bacterial amoA genes (8.60 × 10⁶ ± 7.64 × 10⁵ copies mg sludge⁻¹) and enriched in three continuous-flow reactors receiving an inorganic medium containing different ammonium concentrations: 2, 10, and 30 mM NH₄⁺–N (28, 140, and 420 mg N l⁻¹). The abundance and communities of ammonia-oxidizing archaea (AOA) and ammonia-oxidizing bacteria (AOB) in enriched nitrifying activated sludge (NAS) were monitored at days 60 and 360 of the operation. Early on, between day 0 and day 60 of reactor operation, comparative abundance of AOA amoA genes to AOB amoA genes varied among the reactors depending on the ammonium levels found in the reactors. As compared to the seed sludge, the number of AOA amoA genes was unchanged in the reactor with lower ammonium level (0.06 ± 0.04 mgN l⁻¹), while in the reactors with higher ammonium levels (0.51 ± 0.33 and 0.25 ± 0.10 mgN l⁻¹), the numbers of AOA amoA genes were deteriorated. By day 360, AOA disappeared from the ammonia-oxidizing consortiums in all reactors. The majority of the AOA sequences from all NASs at each sampling period fell into a single AOA cluster, however, suggesting that the ammonium did not affect the AOA communities under this operational condition. This result is contradictory to the case of AOB, where the communities varied significantly among the NASs. AOB with a high affinity for ammonia were present in the reactors with lower ammonium levels, whereas AOB with a low affinity to ammonia existed in the reactors with higher ammonium levels.     

Nitrifying granules cultivation in a sequencing batch reactor at a low organics-to-total nitrogen ratio in wastewater

It is possible to cultivate aerobic granular sludge at a low organic loading rate and organics-to-total nitrogen (COD/N) ratio in wastewater in the reactor with typical geometry (height/diameter = 2.1, superficial air velocity = 6 mm/s). The noted nitrification efficiency was very high (99%). At the highest applied ammonia load (0.3 ± 0.002 mg NH₄⁺–N g total suspended solids (TSS)⁻¹ day⁻¹, COD/N = 1), the dominating oxidized form of nitrogen was nitrite. Despite a constant aeration in the reactor, denitrification occurred in the structure of granules. Applied molecular techniques allowed the changes in the ammonia-oxidizing bacteria (AOB) community in granular sludge to be tracked. The major factor influencing AOB number and species composition was ammonia load. At the ammonia load of 0.3 ± 0.002 mg NH₄⁺–N g TSS⁻¹ day⁻¹, a highly diverse AOB community covering bacteria belonging to both the Nitrosospira and Nitrosomonas genera accounted for ca. 40% of the total bacteria in the biomass.     

Biodegradation of the pesticide 4,6-dinitro-ortho-cresol by microorganisms in batch cultures and in fixed-bed column reactors

A mixed culture of microorganisms able to utilize 4,6-dinitro-ortho-cresol (DNOC) as the sole source of carbon, nitrogen and energy was isolated from soil contaminated with pesticides and from activated sludge. DNOC was decomposed aerobically in batch cultures as well as in fixed-bed column reactors. Between 65% and 84% of the substrate nitrogen was released as nitrate into the medium, and 61% of the carbon from uniformly ¹⁴C-labelled DNOC was recovered as ¹⁴CO₂. The mixed microbial culture also decomposed 4-nitrophenol and 2,4-dinitrophenol but not 2,3-dinitrophenol, 2,6-dinitrophenol, 2,4-dinitrotoluene, 2,4-dinitrobenzoic acid or 2-sec-butyl-4,6-dinitrophenol (Dinoseb). Maximal degradation rates for DNOC by the bacterial biofilm immobilized on glass beads in fixed-bed column reactors were 30 mmol day⁻¹ (l reactor volume)⁻¹, leaving an effluent concentration of less than 5 μg l⁻¹ DNOC in the outflowing medium. The apparent K _s value of the immobilized mixed culture for DNOC was 17 μM. Degradation was inhibited at DNOC concentrations above 30 μM and it ceased at 340 μM, possibly because of the uncoupling action of the nitroaromatic compound on the cellular energy-transducing mechanism. Received: 27 March 1997 / Received revision: 5 June 1997 / Accepted: 7 June 1997     

Anaerobic dechlorination of perchloroethene in an extractive membrane bioreactor

An extractive membrane bioreactor (EMB) is described that used an undefined anaerobic culture to dechlorinate tetrachloroethene (C₂Cl₄) reductively in a synthetic wastewater. Comparable reactors described in the literature use set-ups where the bacteria are in direct contact with the wastewater, and thus would require the addition of significant quantities of nutrients to the wastewater stream in practical application. In the EMB, a silicone rubber membrane separates the microbial culture from the wastewater stream, so that addition of nutrients can be minimised. The EMB was operated continuously for 48 days and dechlorinated 359 mol C₂Cl₄/(l biomedium⁻¹ day⁻¹) on average. Lactate was fed as an electron donor and C₂Cl₄ dechlorination was verified by chloride measurements. Particular attention was paid to the reduction of transmembrane C₂Cl₄ flux caused by a membrane-attached biofilm. Following a start-up period, the reactor operation was stable and remained largely unaffected by biofilm thickness and oxygen contamination from the wastewater. Received: 19 January 1998 / Received revision: 8 May 1998 / Accepted: 8 May 1998     

Effect of feed composition and upflow velocity on aggregate characteristics in anaerobic upflow reactors

Two upflow anaerobic hybrid reactors treated lactose and a mixture of ethanol, propionate and butyrate, respectively, at a volumetric loading rate of 3.7 kg chemical oxygen demand (COD) m⁻³day⁻¹, a hydraulic retention time of 5 days and a liquid upflow velocity of 0.01 m/h. Under steady-state conditions, the lactose-fed sludge had much higher (20%–100%) specific methanogenic conversion rates than the volatile-fatty acid␣(VFA)/ethanol-fed sludge for all substrates tested, including VFA. In both reactors, a flocculant sludge developed, although a much higher content of extracellular polysaccharide was measured in the lactose-fed sludge [1900 μg compared to 305 μg uronic acid/g volatile suspended solids (VSS)]. When the liquid upflow velocity of a third, VFA/ethanol-fed reactor was increased to 0.5 m/h, granulation of the sludge occurred, accompanied by a large increase (200%–500%) in the specific methanogenic conversion rates for the syntrophic and methanogenic substrates studied. Granulation reduced the susceptibility of the sludge to flotation. Glucose was degraded at a high rate (100 mg glucose gVSS⁻¹h⁻¹) by the sludge from the third reactor, despite not having been exposed to a sugar-containing influent for 563␣days. Received: 7 June 1996 / Received revision: 23 September 1996 / Accepted: 29 September 1996     

Trichloroethylene degradation and mineralization by pseudomonads and Methylosinus trichosporium OB3b

 To examine the trichloroethylene (C₂HCl₃)-degrading capability of five microorganisms, the maximum rate, extent, and degree of C₂HCl₃ mineralization were evaluated for Pseudomonas cepacia G4, Pseudomonas cepacia G4 PR1, Pseudomonas mendocina KR1, Pseudomonas putida F1, and Methylosinus trichosporium OB3b using growth conditions commonly reported in the literature for expression of oxygenases responsible for C₂HCl₃ degradation. By varying the C₂HCl₃ concentration from 5 μM to 75 μM, V _max and K _m values for C₂HCl₃ degradation were calculated as 9 nmol/(min mg protein) and 4 μM for P. cepacia G4, 18 nmol/(min mg protein) and 29 μM for P. cepacia G4 PR1, 20 nmol/(min mg protein) and 10 μM for P. mendocina KR1, and 8 nmol/(min mg protein) and 5 μM for P. putida F1. This is the first report of these Michaelis-Menten parameters for P. mendocina KR1, P. putida F1, and P. cepacia G4 PR1. At 75 μM, the extent of C₂HCl₃ that was degraded after 6 h of incubation with resting cells was 61%–98%; the highest degradation being achieved by toluene-induced P. mendocina KR1. The extent of C₂HCl₃ mineralization in 6 h (as indicated by concentration of chloride ion) was also measured and varied from 36% for toluene-induced P. putida F1 to 102% for M. trichosporium OB3b. Since C₂HCl₃ degradation requires new bio-mass, the specific growth rate (μ_max) of each of the C₂HCl₃-degradation microorganisms was determined and varied from 0.080/h (M. trichosporium OB3b) to 0.864/h (P. cepacia G4 PR1). Received: 1 May 1995/Received revision: 11 July 1995/Accepted: 26 July 1995     

Biological nitrification–denitrification with alternating oxic and anoxic operations using aerobic granules

Efficient nitrification and denitrification of wastewater containing 1,700 mgl⁻¹ of ammonium-nitrogen was achieved using aerobic granular sludge cultivated at medium-to-high organic loading rates. The cultivated granules were tested in a sequencing batch reactor (SBR) fed with 6.4 or 10.2 kg NH₄⁺-N m⁻³ day⁻¹, a loading significantly higher than that reported in literature. With alternating 2 h oxic and 2 h anoxic operation (OA) modes, removal rate was 45.5 mg NH₄⁺-N g⁻¹ volatile suspended solids⁻¹ h⁻¹ at 6.4 kg NH₄⁺-N m⁻³ day⁻¹ loading and 41.3 ± 2.0 at 10.2 kg NH₄⁺-N m⁻³ day⁻¹ loading. Following the 60 days SBR test, granules were intact. The fluorescence in situ hybridization and confocal laser scanning microscopy results indicate that the SBR-OA granules have a distribution with nitrifers outside and heterotrophs outside that can effectively expose functional strains to surrounding substrates at high concentrations with minimal mass transfer limit. This microbial alignment combined with the smooth granule surface achieved nitrification–denitrification of wastewaters containing high-strength ammonium using aerobic granules. Conversely, the SBR continuous aeration mode yielded a distribution with nitrifers outside and heterotrophs inside with an unsatisfactory denitrification rate and floating granules as gas likely accumulated deep in the granules.     

Anaerobic dechlorination of carbon tetrachloride by free-living and attached bacteria under various electron-donor conditions

The dechlorination of carbon tetrachloride (CCl₄) by free-living and attached bacteria under anaerobic conditions was studied to examine the relationship between porous media and electron donor. Two batch-type experiments, the free-living and attached bacterial systems, were conducted with and without addition of 0.5-mm glass beads. Glucose and acetate were selected as the primary electron donors because they are easily biodegradable. Direct epifluorescence technology, the DAPI (4′ 6-diamidino-2-phenylindole) method, was used for counting the microbial activities. Adding glass beads could accelerate the dechlorination rate of CCl₄. Removals of 44 %–57 % were observed in free-living bacterial system. Whereas a two- to fivefold increase in the CCl₄ dechlorination rate was observed in the attached system. Experimental results and thermodynamic calculations indicated that glucose is a better supplementary substrate than acetate for stimulating the dechlorinating capability of microorganisms because of its relatively high available free energy. A higher concentration of substrate provided more reducing power for attached bacteria to initiate the dechlorination reaction. The pseudo-first-order rate constants of CCl₄ dechlorination ranged from 0.007 day⁻¹ to 0.017 day⁻¹ and from 0.011 day⁻¹ to 0.0625 day⁻¹ for free-living and attached bacterial systems respectively. Microscopic observation revealed a three- to eightfold difference of microbial number between the free-living and attached bacterial systems. On the basis of the results in this study, we can conclude that the presence of porous media and an electron donor can change the dechlorination capabilities of the microorganisms. This work will be valuable in the design of in situ bioremediation as it discusses the specific area of the medium and supplementation with an electron donor to stimulate the indigenous microflora. Received: 21 June 1996 / Received revision: 2 September 1996 / Accepted: 29 September 1996     

Kinetics and characteristics of 70 °C, VFA-grown, UASB granular sludge

We studied in batch reactors the kinetics and characterization of 70 °C, volatile fatty acids (VFAs)-grown, upflow anaerobic sludge blanket granular sludge with 55 and 35 °C sludge as reference. The half-saturation constant (K _s), the inhibition constant (K _i), the maximum specific methane production rate (μ_CH4max), and the inhibition response coefficient (n) of the 70 °C sludge were 6.15 mM, 48.2 mM, 0.132 h⁻¹, and 2.48, respectively, while no inhibition occurred at 55 and 35 °C, where the K _s was 3.67 and 3.82 mM, respectively. At 70 °C, the highest initial specific methanogenic activity (ISMA, 0.311 gCH₄-COD per gram volatile solids per day) on VFAs was about 12–15% lower than that on acetate and three to four times less than the ISMA for the 55 and 35 °C sludge. In the acetate conversion study, residual acetate (79 mg l⁻¹) at 70 °C was three to five times higher than that at 55 and 35 °C. Further, the methane produced as percentage of the acetate consumed at 70 °C (89%) was lower than that at 55 (95%) and 35 °C (97%). At 70 °C, 10% of the ISMA remained after 15 days of starvation as compared to 26% (55 °C) and 92% (35 °C) after 30 days of starvation. Thus, the kinetics of the 70 °C granular sludge seem to differ from those at 55 and 35 °C. Received: 1 February 1999 / Accepted: 20 March 1999     

Microbial degradation of tetraethyl lead in soil monitored by microcalorimetry

Sieved agricultural soil samples were treated with the anti-knock agent tetraethyl lead (Et₄Pb), and the resulting effects were analyzed by microcalorimetry. Et₄Pb additions resulted in an increase of the heat production rate, provided that oxygen was present and that the soil was not autoclaved. The increased heat production rate was accompanied by degradation of Et₄Pb, as verified by speciation analysis (GC-MS) of the remaining Et₄Pb and its ionic degradation products (triethyl lead and diethyl lead cations). Conclusive evidence was obtained that these transformations were mediated mainly by microbes. At an initial Et₄Pb concentration of 2 g Pb/kg dry weight the biodegradation rate was about 780 μmol day⁻¹ kg dry weight⁻¹, whilst the chemical decomposition was only 50 μmol day⁻¹ kg dry weight⁻¹. A fivefold rise of the initial Et₄Pb concentration resulted in a decrease of the biodegradation rate to 600 μmol day⁻¹ kg dry weight⁻¹ and an increase of the chemical decomposition to 200 μmol day⁻¹ kg dry weight⁻¹. The biodegradation rate was not influenced by the addition of glucose, which means that no indication for a cometabolic attack of Et₄Pb was found. Received: 25 February 1997 / Received revision: 22 April 1997 / Accepted: 27 April 1997     

Starvation is not a prerequisite for the formation of aerobic granules

Activated sludge with sludge volume index (SVI)₃₀ of 77 ml g⁻¹ and SVI₃₀ of 433 ml g⁻¹ was inoculated to start up reactors R1 and R2, respectively. In both R1 and R2, cycle time of 1 h and the influent chemical oxygen demand (COD) concentrations of 1,000 mg l⁻¹ were employed. Initial settling time of 2 min resulted in the loss of a substantial amount of biomass as wash-out and high effluent COD concentrations within the first week of operation. This implied that there was no starvation phase in each cycle of R1 and R2 during the first week of operation. However, aerobic granules with a size above 400 μm formed by day 7. Thus, it was concluded that starvation was not a prerequisite for the formation of aerobic granules. When cycle time was 1 h, the instability of aerobic granules was observed. When cycle time was prolonged to 1.5 h and granular sludge of 200 ml was used to start up reactor R3, the reactor R3 reached steady state within 1 week. SVI, size, and the morphology of granular sludge in R3 remained stable during the 47-day operation, which indicated that prolonged starvation time had positive effects on the stability of aerobic granules.     

Removal of tetrachloroethylene in an anaerobic column bioreactor

Removal of tetrachloroethylene (perchloroethylene; C₂Cl₄) by microbial consortia from two sites with different C₂Cl₄ exposure histories was examined in a bench-scale anaerobic column bioreactor. It was hypothesized that optimal removal would be observed in the reactor packed with sediments having an extensive exposure history. Microbial consortia were enriched from hyporheic-zone (HZ) sediments from the Portneuf aquifer near Pocatello, Idaho, and from industrial-zone (IZ) sediments from a highly contaminated aquifer in Portland, Oregon. Lactate and acetate were the electron donors during experiments conducted over 9 and 7 months for HZ and IZ sediments, respectively. In the HZ bioreactor, the retention time ranged from 31 h to 81 h, and inlet C₂Cl₄ concentrations ranged from 0.1 ppm to 1.0 ppm. Dechlorination of C₂Cl₄ averaged 60% and reached a maximum of 78%. An increase in C:N from 27:1 to 500:1 corresponded to an 18% increase in removal efficiency. Trichloroethylene production corresponded to decreased effluent C₂Cl₄; further intermediates were not detected. In the IZ bioreactor, the retention time varied from 34 h to 115 h; the inlet C₂Cl₄ concentration was 1.0 ppm. C₂Cl₄ removal averaged 70% with a maximum of 98%. Trichloroethylene and cis-dichloroethylene were detected in the effluent. Increases in C:N from 50:1 to 250:1 enhanced dechlorination activity. Received: 3 February 1997 / Received revision: 15 May 1997 / Accepted: 1 June 1997     

Cell growth and nutritive value of the tropical benthic diatom, <Emphasis Type="Italic">Amphora</Emphasis> sp., at varying levels of nutrients and light intensity,and different culture locations

Two series of experiments were conducted to determine suitable growth factors for the mass propagation of the local algal isolate Amphora sp. A higher growth rate of 0.2 doubling (μ) day⁻¹ was attained at a lower photosynthetic photon flux density (PPFD; 11.4 μmol photon m⁻²s⁻¹) compared to cultures exposed to higher levels of PPFD (16.1 μmol photon m⁻²s⁻¹, −0.1 μ day ⁻¹; 31.3 μmol photon m⁻²s⁻¹, 0.0 μ day⁻¹). Cultures located inside the laboratory had a significantly higher cell density (133 × 10⁴ cells cm⁻²) and growth rate (0.3 μ day⁻¹) compared to those located outdoors (100 × 10⁴ cells cm⁻², 0.2 μ day⁻¹). A comparison of nutrient medium across two locations showed that lipid content was significantly higher in cultures enriched with F/2MTM (macronutrients + trace metals) and F/2MV (macronutrients + vitamins). Saturated fatty acids were also present in high concentrations in cultures enriched with F/2M (macronutrients only). Significantly higher amounts of saturated fatty acids were observed in cultures located outdoors (33.1%) compared to those located indoors (26.6%). The protein, carbohydrates and n-6 fatty acid content of Amphora sp. were influenced by the location and enrichment of the cultures. This study has identified growth conditions for mass culture of Amphora sp. and determined biochemical composition under those culture conditions. Presented at the 6th Meeting of the Asian Pacific Society of Applied Phycology, Manila, Philippines.     

Repeated batch cultivation of the microalga Spirulina platensis

Summary The cultivation of photosynthetic microorganisms such as the microalga Spirulina platensis can provide an alternative source of food. The water in Mangueira Lagoon (Rio Grande do Sul state, southern Brazil) has several required nutrients for the growth of Spirulina and could be added to culture medium to reduce the cost of producing S. platensis. Although little studied, repeated batch cultivation is a very useful technique because it has a better cost–benefit ratio than other cultivation methods. In a series of runs, we studied the influence of cell concentration, renewal rate and strain on the specific growth rate and biomass productivity of S. platensis during repeated batch cultivation, the runs taking place in 2-l Erlenmeyer flasks for 2160 h at 30 °C and a light intensity of 2500 lux under a 12 h photoperiod. The three factors studied had a significant (P < 0.05) effect on the results (specific growth rate and productivity). Using Zarrouk’s medium, the highest specific growth rate (μ_X) was 0.111 day⁻¹ while the biomass productivity (P _X) was 0.0423 g l⁻¹ day⁻¹, while Mangueira Lagoon water supplemented with 10% Zarrouk’s medium gave μ_X = 0.113 day⁻¹ and a productivity P _X = 0.0467 g l⁻¹ day⁻¹. These values were two to three times higher than the results obtained in batch cultivation, indicating that the repeated batch cultivation of S. platensis is attractive and convenient.     

An upflow microaerobic sludge blanket reactor operating at high organic loading and low dissolved oxygen levels

The activated sludge process (ASP) has high operational costs due to the need for aeration at dissolved O₂ (DO) levels of ≥2 mg l⁻¹ and high capital costs to construct large reactors due to a low organic loading [typically 1 kg chemical oxygen demand (COD) m⁻³ day⁻¹]. A novel method for improving the energy use and treatment efficiency of the ASP via limited oxygenation (0.4 mg DO l⁻¹) and high organic loading (6.2 kg COD m⁻³ day⁻¹) is proposed based on a laboratory-scale ASP for ammonia-rich industrial wastewaters. The sludge blanket phenomenon and granulation occurred simultaneously in the upflow microaerobic reactor.     

Transformation of indole and quinoline by Desulfobacterium indolicum (DSM 3383)

Degradation of indole and quinoline by Desulfobacterium␣indolicum was studied in batch cultures. The first step in the degradation pathway of indole and quinoline was a hydroxylation at the 2 position to oxindole and 2-hydroxyquinoline respectively. These hydroxylation reactions followed saturation kinetics. The kinetic parameters for indole were an apparent maximum specific transformation rate (V _Amax) of 263 μmol mg total protein⁻¹ day⁻¹ and an apparent half-saturation constant (K _Am) of 139 μM. The V _Amax for quinoline was 170 μmol mg total protein⁻¹ day⁻¹ and K _Am was 92 μM. Oxindole inhibited indole hydroxylation whereas 2-hydroxyquinoline stimulated quinoline hydroxylation. An adaptation period of approximately 20 days was required before transformation of 2-hydroxyquinoline in cultures previously grown on quinoline. Indole and quinoline were hydroxylated with a lag phase shorter than 4 h in a culture adapted to ethanol. Chloramphenicol inhibited the hydroxylation of indole and quinoline in ethanol-adapted cells, indicating an inducible enzyme system. Chloramphenicol had no effect on the hydroxylation of indole in quinoline-adapted cells or on the hydroxylation of quinoline in indole-adapted cells. This indicated that it was the same inducible enzyme system that hydroxylated indole and quinoline. Received: 16 July 1996 / Received revision: 23 September 1996 / Accepted: 29 September 1996     

Reclamation of an activated-sludge microbial consortium by selective biostimulation

Our previous study showed that an activated-sludge process broke down at the phenol-loading rate of 1.5 g l⁻¹ day⁻¹, when non-flocculating bacteria (called R6T and R10) overgrew the sludge, resulting in a sludge washout. In this study, we attempted to circumvent this breakdown problem by reclaiming the consortium structure. Activated sludge was fed phenol, and the phenol-loading rate was increased stepwise from 0.5 g l⁻¹ day⁻¹ to 1.0 g l⁻¹ day⁻¹ and then to 1.5 g l⁻¹ day⁻¹. Either galactose or glucose (at 0.5 g l⁻¹ day⁻¹) was also supplied to the activated sludge from the phenol-loading rate of 1.0 g l⁻¹ day⁻¹. Pure culture experiments have suggested galactose to be a preferential substrate for a floc-forming bacterium (R6F) that predominantly degrades phenol under low phenol-loading conditions. Supplying galactose allowed sustainment of the R6F population and suppression of the overgrowth of R6T and R10 at the phenol-loading rate of 1.5 g l⁻¹ day⁻¹. This measure allowed the activated-sludge process to treat phenol at a phenol-loading rate up to 1.5 g l⁻¹ day⁻¹, although it broke down at 2.0 g l⁻¹ day⁻¹. In contrast, supplying glucose reduced the R6F population and allowed the activated-sludge process to break down at the phenol-loading rate of 1.0 g l⁻¹ day⁻¹. This study demonstrated that reclamation of the activated-sludge consortium by selective biostimulation of the floc-forming population improved the phenol-treating ability of the process. Received: 13 January 2000 / Received revision: 10 March 2000 / Accepted: 7 April 2000     

Pentachlorophenol biodegradation kinetics of an oligotrophic fluidized-bed enrichment culture

A fluidized-bed reactor (FBR) was used to enrich an aerobic chlorophenol-degrading microbial culture. Long-term continuous-flow operation with low effluent concentrations selected oligotrophic microorganisms producing good-quality effluent for pentachlorophenol(PCP)-contaminated water. PCP biodegradation kinetics was studied using this FBR enrichment culture. The results from FBR batch experiments were modeled using a modified Haldane equation, which resulted in the following kinetic constants: q _max = 0.41 mg PCP mg protein⁻¹ day⁻¹, K _S = 16 μg l⁻¹, K _i = 5.3 mg l⁻¹, and n = 3.5. These results show that the culture has a high affinity for PCP but is also inhibited by relatively low PCP concentrations (above 1.1 mg PCP l⁻¹). This enrichment culture was maintained over 1 year of continuous-flow operation with PCP as the sole source of carbon and energy. During continuous-flow operation, effluent concentrations below 2 μg l⁻¹ were achieved at 268 min hydraulic retention time (t _HR) and 2.5 mg PCP l⁻¹ feed concentration. An increase in loading rate by decreasing t _HR did not significantly deteriorate the effluent quality until a t _HR decrease from 30 min to 21 min resulted in process failure. Recovery from process failure was slow. Decreasing the feed PCP concentration and increasing t _HR resulted in an improved process recovery. Received: 10 October 1996 / Received revision: 21 January 1997 / Accepted: 24 January 1997