Spatial distribution of major bacterial species and different volatile fatty acids in a two-phase anaerobic biofilm reactor with PVA gel beads as bio-carrier

Abstract

Conventional completely mixed anaerobic treatment systems limit the chances of the different species of bacteria to spatially group together according to their mutual cooperation and as a result, show a lower efficiency and vulnerability towards shock situations. It is interesting to know about the stratification of the different bacterial species participating in the degradation process and the intermediates that they produce. In this study, we established and optimized a two-phase anaerobic packed bed biofilm reactor system (AnPBR) with porous PVA gel beads used as bio-carriers and ran the reactor system in a steady state to observe the VFAs produced along with the microbial diversity of the predominant species at different stages of the reactor system. We observed that acetate and butyrate were the predominant intermediate VFAs while concentrations of other VFAs such that propionic acid were low. Acetobacterium and Clostridium were found to be the most abundant bacterial species in acidogenic reactor while methanogenic reactor was highly enriched with Methanobacterium and Methanosarcina. Apart from the above, syntrophic populations such as Syntrophobactor wolinii were also observed to be dominant in both the reactors – especially towards the end of acidogenic reactor and the initial part of the methanogenic reactor.     

Degradation of hydroquinone,gentisate, and benzoate by a fermenting bacterium in pure or defined mixed culture

From a methanogenic fixed-bed reactor fed with hydroquinone as sole energy and carbon source, a rodshaped bacterium was isolated in pure culture which could degrade hydroquinone and gentisate (2,5-dihydroxybenzoate). In syntrophic coculture with either Desulfovibrio vulgaris or Methanospirillum hungatei, also benzoate could be degraded. Other substrates such as sugars, fatty acids, alcohols, and cyclohexane derivatives were not degraded. Sulfate, sulfite, or nitrate were not used as external electron acceptor. The isolate was a Gram-negative, non-motile, nonsporeforming strict anaerobe; the guanine-plus-cytosine content of the DNA was 53.2±1.0 mol%. In pure culture, hydroquinone was degraded to acetate and benzoate, probably via an intermediate carboxylation. In syntrophic mixed cultures, all three substrates were converted completely to acetate. Phenol was never detected as a fermentation product.     

Bioremediation of selenite in oil refinery wastewater

Selenium-oxyanion-containing wastewater, with levels of selenite as high as 3690 g Se/l and very low levels of selenate, was treated in a laboratory-scale biological reactor system inoculated with the selenate-respiring bacterium Thauera selenatis. The wastewater contained selenite that had been removed from refinery effluent wastewater using iron-coprecipitation followed by selenite release to yield a more concentrated selenium-containing wastewater. The reactor system consisted of recycling sludge-blanket (500 ml; 200 g sand) and fluidized-bed reactors (500 ml; 150 g sand). The flow rate through the reactor system was 3.5 ml/min. The carbon source fed into the reactor was acetate (3 mM); nitrate was also present (3 mM). The selenium oxyanion levels in the wastewater were reduced by 95%. T. selenatis was the only selenate-reducing bacterium detected in the reactor system and it presumably reduced a portion of the selenate present in the water to selenite. The selenite present in the water, and that formed by selenate reduction, was reduced both by the Thauera and by a population of denitrifying bacteria also present in high numbers in the reactor system.     

Inhibition of the methanogenic fermentation of p-toluic acid (4-methylbenzoic acid) by acetate

The potential inhibitory effect of acetate on p-toluic acid methanogenic fermentation was studied during the continuous operation at 5.3 days hydraulic retention time of an upflow anaerobic sludge blanket reactor fed with a synthetic waste-water containing 3.67 mm p-toluic acid as sole carbon and energy source. In the absence of acetate, a chemical oxygen demand removal efficiency of 56.8% and an estimated p-toluic acid removal efficiency of 62.8% were achieved. Immediately after the addition of 58.3 mm acetate into the reactor influent, p-toluic acid degradation stopped while most of the acetate was consumed. The inhibition is explained by thermodynamic considerations. It is emphasized that such phenomena could occur during the treatment of waste-waters containing high concentrations of acetate and aromatic compounds that require a syntrophic association to be degraded to acetate and H₂. Correspondence to: J. P. Guyot     

Biodegradation of Methyl <Emphasis Type="Italic">tert</Emphasis>-Butyl Ether by Enriched Bacterial Culture

Degradation of methyl tert-butyl ether (MTBE) as a sole carbon and energy source was investigated utilizing an enriched bacterial consortium derived from an old environmental MTBE spill. This enriched culture grew on MTBE with concentration up to 500 mg/l, reducing the MTBE in medium to undetectable concentrations in 23 days. Traces of tert-butyl alcohol were detected during MTBE degradation. The degradation was not affected by additional cobalt ions, whereas low concentration of glucose enhanced the rate of degradation. The bacterial community consisted of numerous bacterial genera, the majority being members of the phylum Acidobacteria and genus Terrimonas. The alkane 1-monooxygenase (alk) gene was detected in this consortium. Our findings suggest that environmental degradation of MTBE proceeds along the previously proposed pathway.     

Inhibition of propionate degradation by acetate in methanogenic fluidized bed reactors

Summary The degradation of acetate, propionate and butyrate was monitored during start-up of five lab-scale methanogenic fluidized bed reactors on an artificially prepared waste water. The acetate concentration in the reactor content was found to influence the degradation of propionate but not of butyrate. In general, at acetate levels over 200 mg/l the degradation of propionate was below 60%, whereas the degradation was complete at acetate levels under 100 mg/l. The rationale of the inhibition of propionate degradation by acetate is discussed.     

Methanogenesis in thermophilic biogas reactors

Methanogenesis in thermophilic biogas reactors fed with different wastes is examined. The specific methanogenic activity with acetate or hydrogen as substrate reflected the organic loading of the specific reactor examined. Increasing the loading of thermophilic reactors stabilized the process as indicated by a lower concentration of volatile fatty acids in the effluent from the reactors. The specific methanogenic activity in a thermophilic pilot-plant biogas reactor fed with a mixture of cow and pig manure reflected the stability of the reactor. The numbers of methanogens counted by the most probable number (MPN) technique with acetate or hydrogen as substrate were further found to vary depending on the loading rate and the stability of the reactor. The numbers of methanogens counted with antibody probes in one of the reactor samples was 10 times lower for the hydrogen-utilizing methanogens compared to the counts using the MPN technique, indicating that other non-reacting methanogens were present. Methanogens that reacted with the probe againstMethanobacterium thermoautotrophicum were the most numerous in this reactor. For the acetate-utilizing methanogens, the numbers counted with the antibody probes were more than a factor of 10 higher than the numbers found by MPN. The majority of acetate utilizing methanogens in the reactor wereMethanosarcina spp. single cells, which is a difficult form of the organism to cultivatein vitro. No reactions were observed with antibody probes raised againstMethanothrix soehngenii orMethanothrix CALS-1 in any of the thermophilic biogas reactors examined. Studies using 2-¹⁴C-labeled acetate showed that at high concentrations (more than approx. 1 mM) acetate was metabolized via the aceticlastic pathway, transforming the methyl-group of acetate into methane. When the concentration of acetate was less than approx. 1 mM, most of the acetate was oxidized via a two-step mechanism (syntrophic acetate oxidation) involving one organism oxidizing acetate into hydrogen and carbon dioxide and a hydrogen-utilizing methanogen forming the products of the first microorganism into methane. In thermophilic biogas reactors, acetate oxidizing cultures occupied the niche ofMethanothrix species, aceticlastic methanogens which dominate at low acetate concentrations in mesophilic systems. Normally, thermophilic biogas reactors are operated at temperatures from 52 to 56° C. Experiments using biogas reactors fed with cow manure showed that the same biogas yield found at 55° C could be obtained at 61° C after a long adaptation period. However, propionate degradation was inhibited by increasing the temperature.     

Methanogenesis from Sucrose by Defined Immobilized Consortia

A bacterial consortium capable of sucrose degradation primarily to CH₄ and CO₂ was constructed, with acetate as the key methanogenic precursor. In addition, the effect of agar immobilization on the activity of the consortium was determined. The primary fermentative organism, Escherichia coli, produced acetate, formate, H₂, and CO₂ (known substrates for methanogens), as well as ethanol and lactate, compounds that are not substrates for methanogens. Oxidation of the nonmethanogenic substrates, lactate and ethanol, to acetate was mediated by the addition of Acetobacterium woodii and Desulfovibrio vulgaris. The methanogenic stage was accomplished by the addition of the acetophilic methanogen Methanosarcina barkeri and the hydrogenophilic methanogen Methanobacterium formicicum. Results of studies with low substrate concentrations (0.05 to 0.2% [wt/vol]), a growth-limiting medium, and the five-component consortium indicated efficient conversion (40%) of sucrose carbon to CH₄. Significant decreases in yields of CH₄ and rates of CH₄ production were observed if any component of the consortium was omitted. Approximately 70% of the CH₄ generated occurred via acetate. Agar-immobilized cells of the consortium exhibited yields of CH₄ and rates of CH₄ production from sucrose similar to those of nonimmobilized cells. The rate of CH₄ production decreased by 25% when cysteine was omitted from reaction conditions and by 40% when the immobilized consortium was stored for 1 week at 4°C.     

Start-up and operation of a propionate-degrading fluidized-bed reactor

Summary A laboratory-scale fluidized-bed reactor was inoculated with a syntrophically propionate-degrading co-culture. After 24 days of batch operation with propionate and acetate in the medium, the reactor was operated for 8 months with propionate as the sole substrate. The loading rate was 8.5 kg chemical oxygen demand/m³ ·day, yielding a maximal gas production of 4.5 l/l·day at a removal efficiency of 94–99%. The degradation was not inhibited by up to 85mm propionate in pulse experiments, but short-time changes in redox potential above — 300 mV led to a drop in the propionate degradation rate. While Methanocorpusculum sp. and Methanospirillum sp. adhered to the sand in the early phase of the start-up, the consortium in the mature biofilm consisted of Desulfobulbus sp., Methanothrix soehngenii and species of at least three different genera of hydrogenotrophic methanogens. A syntrophic relationship between the sulphate-reducing Desulfobulbus sp. and hydrogenotrophic and acetotrophic methanogens is discussed.Offprint requests to: G. Zellner     

Characteristics of granular methanogenic sludge grown on glucose in a UASB reactor

The formation of granules grown on glucose in an upflow anaerobic sludge blanket (UASB) reactor was investigated. Total granular sludge concentration retained in the UASB reactor was 34.5 g MLSS/l (30.0 g MLVSS/l) during 240 d operation on glucose minimum medium with the supplementation of 1.07 g NaHCO₃ per 1 g glucose. This realized a high-rate methanogenic fermentation of glucose of 17.6 g COD/l-reactor-d at 3.4 d⁻¹ of space velocity. The granules formed were relatively small, ranging mainly from 0.4 to 0.5 mm, had a relatively low cell density of 0.0542–0.0560 g MLVSS/ml, and had low specific gravity (0.97–1.19) due to very low ash content (11–13%). Electron microscopic analysis showed that Methanothrix spp. appeared dominant over the granules. The specific metabolic activities of bacterial trophic groups were the highest for H₂ followed by glucose, acetate, and propionate.     

The influence of organic load on granular sludge development in an acetate-fed system

Summary The development of granular sludge in laboratory-scale upflow anaerobic sludge-blanket reactors was studied. Acetate was supplied as sole carbon source in order to select the acetotrophs Methanosarcina and Methanothrix. These microorganisms are dominant in methanogenic ecosystems and their ratio seems to control the speed of granulation. Changing the ratio of the above species was followed on the basis of their different F ₄₂₀-coenzyme content. Five reactors were operated at the same hydraulic retention time but at different feed substrate concentrations. We found that granulation takes place only in acetate-fed systems but this process was slower and the resultant granules looser and less stable than those developed on sugar-starch substrate. In the range of feed acetate levels examined (0.5–0.3 g/1) higher concentrations of feed caused faster granulation of the sludge bed and, presumably, of the microbial population, and resulted in larger granules containing sludge that settled more readily. We found no evidence for selection pressure at substrate concentrations below 0.5 g/1 acetate in the reactor. Offprint requests to: J. Holló     

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     

The effect of oxygen tension on the production of Bacillus thuringiensis subsp. israelensis toxin active against Aedes aegypti larvae

An optimized batch production of Bacillus thuringiensis subsp. israelensis was made in a stirred Bioflo III reactor using a previously selected medium, and operating conditions in the range of 100–500 rev/min stirrer speeds and 0.2–1 air flow/culture medium volume/minute (v/v/m) aeration rates, including five combinations; at the end of fermentation, dry powders were recovered and evaluated against Aedes aegypti larvae at 0.05 mg/l. Later, the lethal concentration inducing 50% mortality (LC₅₀) was determined for the two most toxic powders. The bioinsecticide yields varied from 9.1 to 15.7 g/l and the total fermentation times ranged between 18 and 30.3 h. The toxicity varied for two powders much more than for the others. These were for combinations with 300 rev/min:1 v/v/m and 500 rev/min:0.6 v/v/m, giving mortality percentages of 47.2 and 59.7, with LC₅₀ values of 0.2675 and 0.0685 mg/l, respectively. A t test showed no significant difference. However, the larvicidal powder produced with 300 rev/min:1 v/v/m gave more variable toxicity than the powder obtained with 500 rev/min:0.6 v/v/m.     

Isolation and characterization of a new carbendazim-degrading <Emphasis Type="Italic">Ralstonia</Emphasis> sp. strain

A bacterial strain 1-1 capable of utilizing carbendazim was isolated from carbendazim-treated Qiyang red soils Hunan Province, China. It is gram-negative, rod-shaped, motile with peritrichous flagella, which formed round, smooth, convex and transparent colonies of about 1.1 mm diameter after 3 days of incubation on the isolation and purification medium using carbendazim as the sole carbon and energy sources. The degradation ratios of carbendazim by strain 1-1 were 19.16 and 95.96 in the carbendazim (500 mg/l)-degrading medium and the carbendazim (500 mg/l)-degrading medium supplemented with yeast extract (150 mg/l) within 24 days, respectively. Strain 1-1 was identified as Ralstonia sp. (β-Proteobacteria) based on the results of phenotypic features, G+C mol and phylogenetic analysis of 16S rDNA. Strain 1-1 could become a new bacterial resource for biodegrading carbendazim and might play a bioremediation role for soils contaminated by carbendazim.     

Anaerobic dechlorination of trichloroethene,tetrachloroethene and 1,2-dichloroethane by an acetogenic mixed culture in a fixed-bed reactor

An anaerobic enrichment culture with glucose as the sole source of carbon and energy plus trichloroethene (TCE) as a potential electron acceptor was inoculated with material from a full size anaerobic charcoal reactor that biologically eliminated dichloromethane from contaminated groundwater (Stromeyer et al. 1991). In subcultures of this enrichment complete sequential transformation of 10 µM TCE viacis-dichloroethene and chloroethene to ethene was reproducibly observed. Maintenance of this activity on subcultivation required the presence of TCE in the medium. The enrichment culture was used to inoculate an anaerobic fixed-bed reactor containing sintered glass Raschig elements as support material. The reactor had a total volume of 1780 ml and was operated at 20 °C in an up-flow mode with a flow rate of 50 ml/h. It was fed continuously with 2 mM glucose and 55 µM TCE. Glucose was converted to acetate as the major product and to a minor amount of methane; TCE was quantitatively dehalogenated to ethene. When, in addition to TCE, tetrachloroethene or 1,2-dichloroethane were added to the system, these compounds were also dehalogenated to ethene. In contrast, 1,1,1-trichloroethane was not dehalogenated, but at 40 µM severely inhibited acetogenesis and methanogenesis. When the concentration of TCE in the feed was raised to 220 µM, chloroethene transiently accumulated, but after an adaptation period ethene was again the only volatile product detected in the effluent. The volumetric degradation rate at this stage amounted to 6.2 µmol/l/h. Since complete transformation of TCE occurred in the first sixth of the reactor volume, the degradation capacity of the system is estimated to exceed this value by factor of about ten.Abbreviations CA chloroethane - 1,1-DCA 1,1-dichloroethane - 1,2-DCA 1,2-dichloroethane - 1,1-DCE 1,1-dichloroethene - c-DCE cis-1,2-dichloroethene - t-DCE trans-1,2-dichloroethene - PCE tetrachloroethene, perchloroethene - 1,1,1-TCA 1,1,1-trichloroethane - TCE trichloroethene - VC chloroethene, vinyl chloride     

Biomethanation of spent wash: Heavy metal inhibition of methanogenesis in synthetic medium

Five heavy metals detected in distillery waste were lead (1.0–8.8 μg/ml), copper (1.7–15.7 μg/ml), zinc (3.1–11.8 μg/ml), iron (36.0–43.5 μg/ml), and manganese (3.0–5.1 μg/ml). Their toxicity to biomethanogenesis in a synthetic medium containing 1% sodium acetate, propionate, or butyrate was measured by batch fermentation, after cultivating the bacterial biomass semicontinuously. Lead, copper, and zinc in decreasing order were found to be toxic to biomethanogenesis. Lead at the concentration of 10 μg/ml completely stopped methane production. Iron did not produce any notable change in the process while manganese stimulated the rate of methane production. The toxicity of lead, copper, and zinc to methanogenic bacteria and methane production was dose-dependent but the growth of acetogenic bacteria was impaired at higher concentrations (2.5–10.0 μg/ml) of lead, copper, and zinc. Manganese stimulated the growth of only methanogenic bacteria, but not that of non-methanogenic bacteria or acetic acid production. The reduction in the synthesis of acetic acid via butyrate was more in the presence of these three metals than the synthesis of this acid via propionate.     

Influence of Co2+, Ni2+ and Fe2+ on the production of tetrapyrroles by Methanosarcina barkeri

Summary The selective formation of three tetrapyrroles, Co-containing corrinoids, Ni-containing factor F₄₃₀ and Fe-containing cytochromes (haems) by Methanosarcina barkeri Fusaro (DSM 804) was achieved as a function of the concentrations of Co²⁺, Ni²⁺ and Fe²⁺ in a methanol minimmum medium. It was found that about 70% of the total tetrapyrroles synthesized was excreted into the culture supernatant. Hence, the continuous production of tetrapyrroles in a fixed-bed reactor (supporter: porous diatomaceous clay) was carried out at a dilution rate of 10 day^-1 (850 ml medium/85 ml column/day). The effluent discharged from the reactor contained the excreted tetrapyrroles, the concentrations of which were dependent upon the Co²⁺, Ni²⁺ and Fe²⁺ concentrations in the feed medium. The maximum productivities from the reactor (1 l basis) were 52 M corrinoids/day, 24 M F₄₃₀/day and 8 M haems/day, respectively.     

Effects of Organic Acid Anions on the Growth and Metabolism of Syntrophomonas wolfei in Pure Culture and in Defined Consortia

The effects of organic acid anions on the growth of Syntrophomonas wolfei was determined by varying the initial concentration of the acid anion in the medium. The addition of 15 mM acetate decreased the growth rate of a butyrate-catabolizing coculture containing Methanospirillum hungatei from 0.0085 to 0.0029 per hour. Higher initial acetate concentrations decreased the butyrate degradation rate and the yield of cells of S. wolfei per butyrate degraded. Inhibition was not due to the counter ion or the effect of acetate on the methanogen. Initial acetate concentrations above 25 mM inhibited crotonate-using pure cultures and cocultures of S. wolfei. Benzoate and lactate inhibited the growth of S. wolfei on crotonate in pure culture and coculture. Lactate was an effective inhibitor of S. wolfei cultures at concentrations greater than 10 mM. High concentrations of acetate and lactate altered the electron flow in crotonate-catabolizing cocultures, resulting in the formation of less methane and more butyrate and caproate. The inclusion of the acetate-using methanogen, Methanosarcina barkeri, in a methanogenic butyrate-catabolizing coculture increased both the yield of S. wolfei cells per butyrate degraded and the efficacy of butyrate degradation. Butyrate degradation by acetate-inhibited cocultures occurred only after the addition of Methanosarcina barkeri. These results showed that the metabolism of S. wolfei was inhibited by high levels of organic acid anions. The activity of acetate-using methanogens is important for the syntrophic degradation of fatty acids when high levels of acetate are present.     

Bioremediation of selenium oxyanions in San Joaquin drainage water using Thauera selenatis in a biological reactor system

This report describes the use of a new selenate-respiring bacterium, Thauera selenatis, for the bioremediation of selenium (Se, as selenate) in drainage water from the Westlands Water District, San Joaquin Valley. The organism respires selenate anaerobically using acetate as the preferred electron donor. The reduction of selenate is not inhibited by nitrate; both electron acceptors are reduced concomitantly. T. selenatis was inoculated into, and was maintained in, a biological reactor system for anaerobic treatment of selenate-nitrate containing drainage water; a population of denitrifying bacteria was also present. When the pH of inflowing water was 6.9, and 2 mm acetate plus 0.56 mm ammonium chloride were fed into the reactor, selenate/selenite levels were reduced from 350–450 g Se/l to 5.39±3.6 g Se/l. The final product of selenate reduction was elemental Se. Analysis of reactor contents revealed that T. selenatis was the only selenate-respiring organism present in the system. Nitrate in the drainage water was also reduced in the reactor system by 98%. The lab-scale biological reactor system consisted of recycled sludge-blanket (1 l; 400 g sand) and fluidized-bed (1 l; 300 g sand) reactors. At a system flow rate of 6.5 ml/min, the retention time was 140 min. Correspondence to: J. M. Macy     

Continuous anaerobic treatment of wastewaters containing formaldehyde and urea

The toxicity of formaldehyde (FA) in batch assays, using volatile fatty acids (VFA) as co-substrate, and the continuous anaerobic treatment of wastewaters containing FA in upflow anaerobic sludge blanket (UASB) reactors was investigated. In batch studies, FA exerted a 50% methanogenic toxicity on VFA at concentrations of around 100 mg/l, 2.5 times lower than values reported with sucrose. Although at FA concentrations higher than 200 mg/l methanogenesis was completely inhibited, a partial recovery of the bacterial activity was observed after 250 h when the FA had been removed from the medium. The continuous anaerobic degradation of FA at concentrations up to 2 g/l, using 1.6 g/l of glucose as co-substrate, was studied in a UASB reactor. A stable and efficient operation was observed at organic loading rates (OLR) of 6.0 g COD/l·d and with a COD/FA ratio as low as 1.4. A synthetic substrate with the same characteristics as the effluents produced during fibreboard adhesives manufacturing (based on urea-FA), i.e. 0.95 g FA/l and 0.35 g urea/l, was treated in a UASB reactor. The applied OLR and nitrogen loading rate (NLR) were 3.45 g COD/l·d and 0.58 g N/l·d, respectively. COD removal efficiencies were maintained at 90–95%, FA and urea being completely degraded.