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     

Microbial treatment of a synthetic sour brine

Summary The ability of the chemoautotroph and facultative anaerobeThiobacillus denitrificans to deodorize and detoxify an oil-field-produced water containing sulphides was evaluated under simulated field conditions. A sulphide-tolerant strain ofT. denitrificans was used to remove inorganic sulphide from a synthetic sour brine containing 4000 mg L^–1 total dissolved solids (TDS) and 100 mg L^–1 sulphide. The sour brine was treated continuously in a rectangular plugflow reactor which approximated the scaled dimensions of an existing field detention pond. The head space of the reactor was purged with N₂ in order to capture H₂S off-gases in a zinc acetate trap. Brine was fed to the reactor continuously for 90 days at rates corresponding to residence times of 0.17–6 days. Temperature and pH ranged from 22 to 40.5°C and 7.5 to 8.8, respectively. The start-up biomass concentration was approximately 100 mg L^–1 (by dry weight). No. additionalT. denitrificans biomass was added to the reactor after start-up. At residence times of 0.3 days and greater inorganic sulphide was undetectable in the effuent. No H₂S was detected in the outlet gas or the zinc acetate trap. Approximately 80% of the sulphide feed was oxidized to sulphate and removed from the reactor in the liquid effluent. The remainder was partially oxidized to elemental sulphur which was retained in the reactor. It is suggested that oxidation of inorganic sulphides byT. denitrificans represents a viable process concept for the treatment of sour water co-produced with oil and gas.     

Chemolithoutotrophic growth of Thiothrix ramosa

Thiothrix has been shown for the first time to be able to grow chemolithoautotrophically with thiosulphate or carbon disulphide as sole energy substrate. Thiosulphate served as the growth-limiting substrate for Thiothrix ramosa in chemostat culture. Maximum growth yield (Y_max) from yields at growth rates between 0.029–0.075 h^-1 was 4.0 g protein/mol thiosulphate oxidized. The key enzyme of the Calvin cycle, ribulose 1,5-bisphosphate carboxylase, was present in these cells, as were rhodanese, adenylyl sulphate (APS) reductase and sulphur-oxidizing enzyme. Thiosulphate-grown cells oxidized thiosulphate, sulphide, tetrathionate and carbon disulphide. Oxidation kinetics for sulphide, thiosulphate and tetrathionate were biphasic: oxygen consumption during the fast first phase of oxidation indicated oxidation of sulphide, and the sulphane moieties of thiosulphate and tetrathionate, to elemental sulphur, before further oxidation to sulphate. Kinetic constants for these four substrates were determined. T. ramosa also grew mixotrophically in batch culture on lactate with a number of organic sulphur compounds: carbon disulphide, methanethiol and diethyl sulphide. Substituted thiophenes were also used as sole substrates. The metabolic versatility of T. ramosa is thus much greater than previously realised.     

Effect of dissolved oxygen concentration on sludge settleability

This laboratory study presents a detailed evaluation of the effects of dissolved oxygen concentration and accumulation of storage polymers on sludge settleability in activated sludge systems with an aerobic selector. The oxygen and substrate availability regime were simulated in laboratory sequencing batch reactor systems. The experiments showed that low dissolved oxygen concentration (1.1 mg O₂ l^–1) had a strong negative effect on sludge settleability, leading to the proliferation of filamentous bacteria (Thiothrix spp., Type 021N and Type 1851). This negative effect was stronger at high chemical oxygen demand loading rate. This indicates that a compartmentalised (plug flow) aerobic contact tank, designed at short hydraulic residence time to guarantee a strong substrate gradient, with low dissolved oxygen concentration, might be worse for sludge settleability than an "overdesigned" completely mixed contact tank. Contrary to the general hypothesis, the maximum specific acetate uptake rate, poly--hydroxybutyrate production rate, and resistance to short starvation periods are similar in both poor- and well-settling sludge. The results of this study support our previous hypothesis on the importance of substrate gradients for the development of filamentous structures in biological flocs, from soluble organic substrate gradients to dissolved oxygen gradients in sludge flocs.     

Sulphur and sulphate reduction with acetate and propionate in an aerobic process for sulphide removal

Summary Sulphide production rates of sulphur-and sulphate-reducing bacteria up to 50 mg per biomass support particle per day were observed in an aerated sulphide-removal reactor with polyurethane (PUR) foam as carrier material. The optimal pH and temperature for the sulphide-producing bacteria were 8.0 and 30°C respectively. Raschig rings and four types of cube-shaped PUR particles were tested as carrier materials. When using PUR particles, the sulphide production rate was always between 3% and 4% of the sulphide removal rate, dependent on the dimensions and pore size of the polyurethane support particles. With the Raschig rings this ratio was only 2% and for reactors in which no carrier materials were present it was even lower (0.6%). Media containing different mixtures of acetate, propionate, sulphur and sulphate inoculated under anoxic conditions with sludge from the aerated reactor showed the presence of acetate-degrading sulphur-reducing, but not of acetate-degrading sulphate-reducing, bacteria. With propionate as sole electron donor no degradation occurred in the presence of sulphur within 2 weeks, whereas sulphate-dependent propionate oxidation started after 5–6 days incubation. Bacteria were isolated and resembled Desulfuromonas acetoxidans and Desulfobulbus propionicus morphologically and physiologically.     

Effect of ethylene glycol-bis(β-aminoethyl ether)-N,N-tetraacetic acid (EGTA) on stability and activity of methanogenic granular sludge

Summary The effect of the calcium-specific chelant ethylene glycol-bis(\-aminoethyl ether)-N,N-tetraacetic acid (EGTA) on methanogenic granular sludge from a laboratory-scale upflow anaerobic sludge-blanket (UASB) reactor fed propionate and from a full-scale reactor treating paper-mill waste-water was studied. Upon treatment with EGTA both sludge types showed a decrease in the calcium and phosphorus content and a release of protein and polysaccharides, leading to a decrease in strength of papermill granular sludge and a disintegration of propionate-grown granules. After treatment of propionate-grown granular sludge with high EGTA concentrations, the methanogenic activity with propionate and acetate as test substrates decreased by 88 and 33%, respectively. The marked reduction in propionate oxidation activity may be caused by a disruption of the special juxtapositioning of bacteria in the granules. Offsprint requests to: A. J. B. Zehnder     

Effect of molybdate ions on methanation of simulated and natural waste-waters

Summary Sulphate in concentrations of 500 and 1000 mg SO₄-S/l did not inhibit methanation of synthetic waste-water (acetate + methanol + glucose) by sludge from a digester treating neutral spent sulphite process effluents. The role of sulphate reducers in the conversion of those substrates was minor although sulphate-reducing bacteria were present with a viable count similar to that of methane-producing bacteria in the sludge. Neutral spent sulphite liquor was partially converted to methane (40% of chemical oxygen demand) under these conditions.Molybdate (20 mM) inhibited methanation of both synthetic waste-water and neutral spent sulphite liquor. Acetate accumulated in glucose plus molybdate media. Molybdate had a direct inhibitory effect on enriched acetoclastic methane-producing bacteria. Molybdate was bacteriocidic to sulphate-reducing bacteria and bacteriostatic to methane-producing bacteria.     

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.     

Identification,enrichment, and isolation ofThiothrix spp. from environmental samples

We have developed a method to enrich, isolate, and identifyThiothrix spp. in environmental samples. This procedure employs low concentrations of organic compounds, the addition of reduced sulfur compounds (sulfide or thiosulfate), and preparation with spring water that containsThiothrix spp. The enrichment enhanced identification ofThiothrix spp. by promoting deposition of intracellular sulfur granules and inhibiting overgrowth by other bacteria. The relatively high calcium content of the spring water contributed to the culture procedure. With this technique,Thiothrix spp. were observed in two activated sludge systems, a municipal water storage tank, three springs, and four underground freshwater caves in the phreatic zone of the Floridan aquifer. Two differentThiothrix cultures have been isolated from a freshwater cave and a water storage tank by this procedure. It appears that media prepared with spring water known to supportThiothrix spp. can be designed to provide highly selective methods for isolation ofThiothrix spp. from a wide range of environments.Florida Agricultural Experimentation Station, Journal Series Number R-03446.     

Conversion of fat into yeast biomass in protein-containing waste-water

Summary Candida tropicalis S001 was grown on the lipid fraction of a protein-containing waste-water in order to (i) remove fat from the water, and (ii) produre yeast biomass for feed. The yeast cells were separated from the waste-water by sedimentation. Defatted waste-water was used for methane production and gave a yield of a 0.3 m³ methane/kg reduced chemical oxygen demand. The maximum specific growth rate (µ_max) of C. tropicalis growing on waste-water fat at pH 4.0 was 0.35 h^–1; the fat content was decreased from 8 g/l to about 0.1 g/l within 24 h. In continous culture a corresponding reduction was maintained at dilution rates up to 0.36 h^–1. The effect on growth of pH, temperature and CO₂ concentration was studied with triolein as the major carbon source. The µ_max was nearly constant (0.16 h^–1) in the pH and temperature range of 3.2–4.0 and 30°–38° C, respectively; 10% CO₂ was optimal for growth. Growth on triolein resulted in a biomass yield of 0.70 g dry weight/g fat. Offprint requests to: S. Rydin     

Methane production from acetamide in an upflow anaerobic sludge-blanket reactor based on a synergistic association between an aerobic rod and methanogens

Acetamide degradation was investigated in a bench-scale upflow anaerobic sludge-blanket (UASB) reactor, successively fed with acetamide, acetate and acetamide, over a period of 343 days, at different hydraulic retention times (t _HR). The reactor was seeded with the sludge previously described [Guyot et al. (1994) Appl Microbiol Biotechnol, 42:452-456], in which methanogenesis from acetamide was performed through a synergistic relationship between an acetamide-degrading, aerobic rod and methanogens. When the reactor was fed acetamide, the chemical oxygen demand (COD) removal efficiency was 86% at volumetric loads less than 1.18 kg COD m^–3 day ^–1. At higher volumetric loads, the efficiency decreased markedly, e.g. 50.9% at a volumetric organic load of 3.39 kg COD m^–3 day^–1 (1 day t _HR) with an accumulation of both acetamide and acetate. The same reactor, when fed with acetate at t _HR 1 day, reached a high COD removal (99%). Evidence of the inhibition of acetate degradation by acetamide is presented. After a long period (135 days) without feeding the reactor with acetamide, the sludge reactor was still capable of degrading acetamide when this substrate was supplied again. It seems that the synergistic degradation of acetamide by aerobes and methanogens present in the UASB reactor sludge is stable over a long period (343 days), in spite of limiting concentrations of dissolved oxygen in the feed.     

The use of Aspergillus niger for the bioconversion of olive mill waste-waters

Summary Olive mill waste-water was used for protein production in small-scale experiments, using non-sterilized medium without pH control. A 14 g/1 concentration of proteins, 61% chemical oxygen demand removal and a 58% reduction in total phenolic compounds were obtained using an Aspergillus niger strain. The removal of phenolic compounds resulted in a change in the colour of the waste-water from black to brown.Offprint requests to: J. L. Garcia     

Degradation of 3,4-dichloroaniline in synthetic and industrially produced wastewaters by mixed cultures freely suspended and immobilized in a packed-bed reactor

Summary Degradation of 3,4-dichloroaniline (34DCA) in aqueous by undefined cultures of free and immobilized cells was examined. Batch cultures of freely suspended cells and continuous degradation in a packed-bed reactor were studied using both synthetically concocted and industrially produced waste-waters. 34DCA was found to be degraded with a concomitant evolution of chloride ions into the bulk medium. The [acked bed reactor with biomass immobilized on celite diatomaceous earth was found to be capable of degrading over 98% of the 34DCA present in a synthetically concocted inlet stream at a concentration of 250 mg l^–1. Residence times of less than 4 h were employed, giving an overall volumetric degradation rate for the packed bed of 90 mg l^–1 h^–1. The industrially produced wastewater contained, in addition to 34DCA, aniline, 4-chloroaniline, 2,3-dichloroaniline (23DCA) and 3,4-dichloronitrobenzene. The biomass enriched on the synthetic 34DCA waste-water was found to be capable of degrading these compounds in addition to 34DCA with the exception of 23DCA. 34DCA degradation efficiencies of over 95% were obtained for the industrial waste-water at reactor residence times of 4.6 h, giving volumetric degradation rates of 24 mg l^–1 h^–1. Offprint requests to: A. G. Livingston     

Sulphide intrusion in eelgrass (Zostera marina L.)

Sudden events of seagrass die‐off have been suggested to be induced by invasion of the phytotoxin sulphide under environmental stress generating low oxygen supply in seagrass tissues. Laboratory experiments were conducted with eelgrass (Zostera marina L.) to measure intra‐plant changes in oxygen and sulphide by means of microelectrodes at different oxygen concentrations in the water column. The objectives were to examine whether sulphide intrusion into seagrass tissues can be induced, to determine the role of plant oxygen status for sulphide intrusion and to determine how fast internal sulphide pools are depleted after internal oxygen supplies have been restored. Under conditions with oxygen partial pressures (pO₂) above 7.4 kPa (> 35% of air saturation) within eelgrass rhizomes or meristematic tissues no intrusion of sulphide occurred in spite of high sediment concentrations of gaseous sulphide (> 1000 µm ). Lack of sulphide intrusion at high internal pO₂ suggested that oxygen release from the roots ensured complete re‐oxidation of sulphide in the rhizosphere. Under oxygen stress, however, the experiments clearly demonstrated intrusion of sulphide in eelgrass rhizomes and meristematic tissues. Rates of sulphide intrusion were controlled by internal pO₂, which in turn was controlled by water column oxygen concentrations. Maximum internal sulphide content reached 325 µm which by far exceeded the 1–10 µm known to inhibit mitochondrial activity in eukaryotic cells. Sulphide and low levels of oxygen could coexist in the eelgrass tissues reflecting fast internal transport of sulphide and slow rates of sulphide re‐oxidation. Upon re‐establishment of high internal oxygen concentrations the depletion of the sulphide pool was slow (half‐life = 20–30 min) indicating, that sulphide re‐oxidation within the eelgrass tissue was not bacterially or enzymatically facilitated but occurred by simple chemical oxidation. The results of this study are consistent with the proposed detrimental role of sulphide intrusion in events of sudden seagrass die‐off.     

Point source detoxification of an industrially produced 3,4-dichloroaniline-manufacture wastewater using a membrane bioreactor

A membrane bioreactor has been used to treat an industrially produced waste-water containing aniline, 4-chloroaniline, 2,3-dichloroaniline and 3,4-dichloroaniline. Conventional direct biological treatment of such effluents cannot be implemented without some form of pretreatment or dilution because of the hostile inorganic composition of the waste-water. In order to overcome this problem a membrane separation step selectively removes the organics from the waste-water and subsequent biodegradation takes place in the biological growth compartment of the reactor system. At a waste-water flow rate of 69 ml h^–1 (corresponding to a contact time of approximately 1.5 h) over 99% of the organic compounds quoted above were removed and biodegraded. Correspondence to: A. G. Livingston     

Isolation ofThiothrix in pure culture and observation of a filamentous epiphyte onThiothrix

Thiothrix was isolated from two sites, one in Arizona and the other in Florida, although the former strain was subsequently lost. This is the first report of the isolation ofThiothrix in pure culture. The cells in aThiothrix bloom found in a stock tank had filamentous “appendages”, which proved to consist of a segmented, trichomatous, epiphytic bacterium.     

Biofouling of Groundwater Systems by Thiothrix spp.

Thiothrix spp., sulfide-oxidizing filamentous bacteria, were found to be a principal bacterial component of aquatic biofilms causing biofouling in selected municipal water storage tanks, private wells, and drip irrigation systems in Florida. Treatments of up to 200 ppm chlorine in the affected systems could not prevent return of the biofouling problem. The water originated from the upper Floridan aquifer and associated surficial aquifers in central and north Florida. Samples were examined where visible biofilms had a white, filamentous appearance, indicative of Thiothrix spp. The detection of Thiothrix spp. was confirmed by enzyme-liked immunosorbent assay (ELISA), indirect immunofluorescence (IIF), and microbiological procedures. It was estimated through immunocytochemical procedures that Thiothrix spp. comprised 18% of the biofilm in the municipal water storage tanks. These observations confirm that specific biological and chemical interactions may induce physical changes leading to significant biofouling. Received: 6 November 1996 / Accepted: 14 March 1997     

Bio catalytic oxidation of sulphide laden wastewater from leather industry using sulfide: Quinone oxidoreductase immobilized bio reactor

Abstract

Anaerobic treatment of sulphate rich wastewater results in high amount of sulphide in liquid phase and gaseous phase. Sulphide is malodorous in gaseous phase and toxic even at very low concentrations in liquid phase and causes objectionable environmental issues. In the present investigation the sulphide present in the UASB treated post tanning wastewater was oxidised into elemental sulphur using Sulfide: Quinone oxidoreductase (SQR) immobilized Functionalized Carbon-silica matrix (FCSM) packed bed reactor. The variables employed for the production of Bacillus clausii biomass for the extraction of SQR were optimized using RSM. The purified SQR showed the maximum activity and stability at pH 6.0 to 8.0 and the percentage oxidation of sulphide at HRT of 24?h were 99.2%?±?0.2 at pH 6.0; 99.6%?±?0.2 at pH 7.0 and 99.6%?±?2.12 at pH 8.0. The effect of temperature on SQR activity was optimized and it established the maximum activity and stability at 40?°C with sulphide oxidation of 99.6%?±?0.8%. The optimum conditions for immobilization of SQR onto FCSM were time, 240?min; pH, 7.0; temperature, 40?°C and SQR concentration, 10?mg/g. The immobilization of SQR onto FCSM obeyed the Langmuir isotherm model. The immobilization of SQR onto FCSM was confirmed by SEM, FT-IR, XRD, TGA and DSC analyses. The SQR-FCSM packed bed reactor was operated separately for the oxidation of sulfide in UASB treated post-tanning wastewater under continuous mode at different HRTs and it recorded the maximum sulphide oxidation by 99?±?0.1% at HRT of 15?h with residual sulphide of 2.4?±?1.1?mg/L. The formation of elemental Sulphur was confirmed by XRD studies. The present investigation provides the scope for the removal of sulphide and thereby substantial reduction in Total Dissolved Solids from post tanning wastewater without addition of chemicals.     

Investigations of cephalosporin C production in an airlift tower loop reactor

Summary Cephalosporin C was produced by Cephalosporium acremonium in a 60 l airlift loop reactor on complex medium (with 30 kg/m³ peanut flour) in fed-batch operation. A final product concentration of 5 kg/m³ and a maximum productivity of 45 g/m³ h were attained. On-line analysis was used to determine ammonia, methionine, phosphate, reducing sugar and cephalosporin C by an autoanalyser, glucose by a flow injection analyser and cephalosporin C, penicillin N, deacetoxycephalosporin C, deacetylce-phalosporin C and methionine by HPLC. The volumetric productivity of the stirred tank reactor was higher than that of the airlift reactor because of differences in cell concentration. Specific productivities in relative to cell mass were similar in the two reactors. The substrate yield coefficient in the airlift reactor was twice that in the stirred tank reactor.Nomenclature E _o2 efficiency of oxygen transfer with regard to the specific power input - K _La volumetric mass transfer coefficient - OTR oxygen transfer rate - P power input - PR volumetric productivity of CPC - q _a volumetric aeration rate/broth volume (vvm) - SPR specific productivity with regard to RNA - V _L broth volume in reactor - z relative height of the aerated reactor     

Effect of an anaerobic bacterial consortium isolated from termites on the degradation of olive-mill waste-water

Summary A microbial consortium obtained by enrichment culture on syringate of termite gut material was used to improve the anaerobic degradation of olive-mill waste-water (OMW). Addition of the consortium (1/4 v/v) to the control inoculum originating from waste-water sludge, increased methane production by 50% over the control during anaerobic digestion of OMW prefermented by Aspergillus niger. This increase was related to enhanced acetate production in the presence of the consortium. When OMW was not prefermented by A. niger, no improvement in methane production was observed, indicating that the aerobic degradation of inhibitory substances is needed for the consortium to express its potential. Correspondence to: J. L. Garcia