Factors Affecting the Toxic Effect of Tin on Estuarine Microorganisms

Inorganic tin (SnCl₄·H₂O) is toxic to microbial populations obtained from estuarine sediments plated on nutrient medium solidified with either agar or purified agar. The use of gelatin as a gelling agent decreased the apparent toxicity of tin, and toxicity was markedly reduced in medium solidified with silica gel. There was no evidence that toxic agar-tin complexes were involved. Cd, Cu, Pb, Ni, and Zn exhibited similar toxicity patterns; therefore, toxicity levels determined in the laboratory should be extrapolated to the environment with caution. The addition of cysteine to the medium had no effect on tin toxicity. Serine or 3-hydroxyflavone enhanced toxicity, while humic acids or gelatin inhibited toxicity. Replacement of SO₄²⁻ with NO₃⁻ did not alter tin toxicity, but replacement of Cl⁻ with NO₃⁻ decreased tin toxicity. Thus, the toxic effect(s) of tin depend as much on the chemical speciation of the metal as on the total concentration of the metal in the medium.     

Changes in Microbial Biofilm Communities during Colonization of Sewer Systems

The coexistence of sulfate-reducing bacteria (SRB) and methanogenic archaea (MA) in anaerobic biofilms developed in sewer inner pipe surfaces favors the accumulation of sulfide (H₂S) and methane (CH₄) as metabolic end products, causing severe impacts on sewerage systems. In this study, we investigated the time course of H₂S and CH₄ production and emission rates during different stages of biofilm development in relation to changes in the composition of microbial biofilm communities. The study was carried out in a laboratory sewer pilot plant that mimics a full-scale anaerobic rising sewer using a combination of process data and molecular techniques (e.g., quantitative PCR [qPCR], denaturing gradient gel electrophoresis [DGGE], and 16S rRNA gene pyrotag sequencing). After 2 weeks of biofilm growth, H₂S emission was notably high (290.7 ± 72.3 mg S-H₂S liter⁻¹ day⁻¹), whereas emissions of CH₄ remained low (17.9 ± 15.9 mg COD-CH₄ liter⁻¹ day⁻¹). This contrasting trend coincided with a stable SRB community and an archaeal community composed solely of methanogens derived from the human gut (i.e., Methanobrevibacter and Methanosphaera). In turn, CH₄ emissions increased after 1 year of biofilm growth (327.6 ± 16.6 mg COD-CH₄ liter⁻¹ day⁻¹), coinciding with the replacement of methanogenic colonizers by species more adapted to sewer conditions (i.e., Methanosaeta spp.). Our study provides data that confirm the capacity of our laboratory experimental system to mimic the functioning of full-scale sewers both microbiologically and operationally in terms of sulfide and methane production, gaining insight into the complex dynamics of key microbial groups during biofilm development.     

Rapid Methane Oxidation in a Landfill Cover Soil

Methane oxidation rates observed in a topsoil covering a retired landfill are the highest reported (45 g m⁻² day⁻¹) for any environment. This microbial community had the capacity to rapidly oxidize CH₄ at concentrations ranging from <1 ppm (microliters per liter) (first-order rate constant [k] = −0.54 h⁻¹) to >10⁴ ppm (k = −2.37 h⁻¹). The physiological characteristics of a methanotroph isolated from the soil (characteristics determined in aqueous medium) and the natural population, however, were similar to those of other natural populations and cultures: the Q₁₀ and optimum temperature were 1.9 and 31°C, respectively, the apparent half-saturation constant was 2.5 to 9.3 μM, and 19 to 69% of oxidized CH₄ was assimilated into biomass. The CH₄ oxidation rate of this soil under waterlogged (41% [wt/vol] H₂O) conditions, 6.1 mg liter⁻¹ day⁻¹, was near rates reported for lake sediment and much lower than the rate of 116 mg liter⁻¹ day⁻¹ in the same soil under moist (11% H₂O) conditions. Since there are no large physiological differences between this microbial community and other CH₄ oxidizers, we attribute the high CH₄ oxidation rate in moist soil to enhanced CH₄ transport to the microorganisms; gas-phase molecular diffusion is 10⁴-fold faster than aqueous diffusion. These high CH₄ oxidation rates in moist soil have implications that are important in global climate change. Soil CH₄ oxidation could become a negative feedback to atmospheric CH₄ increases (and warming) in areas that are presently waterlogged but are projected to undergo a reduction in summer soil moisture.     

Transition from Anoxygenic to Oxygenic Photosynthesis in a Microcoleus chthonoplastes Cyanobacterial Mat

Benthic cyanobacterial mats with the filamentous Microcoleus chthonoplastes as the dominant phototroph grow in oxic hypersaline environments such as Solar Lake, Sinai. The cyanobacteria are in situ exposed to chemical variations between 200 μmol of sulfide liter⁻¹ at night and 1 atm pO₂ during the day. During experimental H₂S to O₂ transitions the microbial community was shown to shift from anoxygenic photosynthesis, with H₂S as the electron donor, to oxygenic photosynthesis. Microcoleus filaments could carry out both types of photosynthesis concurrently. Anoxygenic photosynthesis dominated at high sulfide levels, 500 μmol liter⁻¹, while the oxygenic reaction became dominant when the sulfide level was reduced below 100 to 300 μmol liter⁻¹ (25 to 75 μmol of H₂S liter⁻¹). An increasing inhibition of the oxygenic photosynthesis was observed upon transition to oxic conditions from increasing sulfide concentrations. Oxygen built up within the Microcoleus layer of the mat even under 5 mmol of sulfide liter⁻¹ (500 μmol of H₂S liter⁻¹) in the overlying water. The implications of such a localized O₂ production in a highly reducing environment are discussed in relation to the evolution of oxygenic photosynthesis during the Proterozoic era.     

Continuous and Batch Production of Chloroperoxidase by Mycelial Pellets of Caldariomyces fumago in an Airlift Fermentor

Batch and continuous production of the extracellular heme glycoprotein chloroperoxidase (CPO) was studied with an airlift fermentor. We induced Caldariomyces fumago CMI 89362 to form pellets by transferring a small inoculum volume in preculture prior to growth in a 1-liter fermentor. Continuous replacement of the fructose-salts medium (dilution rate, 0.008 h⁻¹) supported continuous CPO formation at an average concentration of 128 ± 10 mg of CPO liter⁻¹ for 8 days. Optimum CPO production rates averaged 1.2 ± 0.1 mg of CPO h⁻¹ at dilution rates below 0.033 h⁻¹. Varying the carbohydrate content of the feed solution or the time of starting the feed did not significantly alter the amount of CPO produced. Batch fermentation in the airlift fermentor resulted in maximum CPO concentrations of 280 ± 80 mg of CPO liter⁻¹, although on two separate occasions CPO concentrations reached 400 to 450 mg liter⁻¹, which was double the amount obtained by free hyphae in shake flask culture.     

Ethylene Removal at Low Temperatures under Biofilter and Batch Conditions

Removal of the plant hormone ethylene (C₂H₄) is often required by horticultural storage facilities, which are operated at temperatures below 10°C. The aim of this study was to demonstrate an efficient, biological C₂H₄ removal under such low-temperature conditions. Peat-soil, acclimated to degradation of C₂H₄, was packed in a biofilter (687 cm³) and subjected to an airflow (~73 ml min⁻¹) with 2 ppm (μl liter⁻¹) C₂H₄. The C₂H₄ removal efficiencies achieved at 20, 10, and 5°C, respectively, were 99.0, 98.8, and 98.4%. This corresponded to C₂H₄ levels of 0.022 to 0.032 ppm in the biofilter outlet air. At 2°C, the average C₂H₄ removal efficiency dropped to 83%. The detailed temperature response of C₂H₄ removal was tested under batch conditions by incubation of 1-g soil samples in a temperature gradient ranging from 0 to 29°C with increments of 1°C. The C₂H₄ removal rate was highest at 26°C (0.85 μg of C₂H₄ g [dry weight]⁻¹ h⁻¹), but remained at levels of 0.14 to 0.28 μg of C₂H₄ g (dry weight)⁻¹ h⁻¹ at 0 to 10°C. At 35 to 40°C, the C₂H₄ removal rate was negligible (0.02 to 0.06 μg of C₂H₄ g [dry weight]⁻¹ h⁻¹). The Q₁₀ (i.e., the ratio of rates 10°C apart) for C₂H₄ removal was 1.9 for the interval 0 to 10°C. In conclusion, the present results demonstrated microbial C₂H₄ removal, which proceeded at 0 to 2°C and produced a moderately psychrophilic temperature response.     

Initial Effects of the Mount St. Helens Eruption on Nitrogen Cycle and Related Chemical Processes in Ryan Lake

Ryan Lake, a 1.6-hectare basin lake near the periphery of the tree blowdown area in the blast zone 19 km north of Mount St. Helens, was studied from August to October 1980 to determine the microbial and chemical response of the lake to the eruption. Nutrient enrichment through the addition of fresh volcanic material and the organic debris from the surrounding conifer forest stimulated intense microbial activity. Concentrations of such nutrients as phosphorus, sulfur, manganese, iron, and dissolved organic carbon were markedly elevated. Nitrogen cycle activity was especially important to the lake ecosystem in regulating biogeochemical cycling owing to the limiting abundance of nitrogen compounds. Nitrogen fixation, both aerobic and anaerobic, was active from aerobic benthic and planktonic cyanobacteria with rates up to 210 nmol of N₂ cm⁻¹ h⁻¹ and 667 nmol of N₂ liter⁻¹ h⁻¹, respectively, and from anaerobic bacteria with rates reaching 220 nmol of N₂ liter⁻¹ h⁻¹. Nitrification was limited to the aerobic epilimnion and littoral zones where rates were 43 and 261 nmol of NO₂ liter⁻¹ day⁻¹, respectively. Potential denitrification rates were as high as 30 μmol of N₂O liter⁻¹ day⁻¹ in the anaerobic hypolimnion. Total bacterial numbers ranged from 1 × 10⁶ to 3 × 10⁸ ml⁻¹ with the number of viable sulfur-metal-oxidizing bacteria reaching 2 × 10⁶ ml⁻¹ in the hypolimnion. A general scenario for the microbial cycling of nitrogen, carbon, sulfur, and metals is presented for volcanically impacted lakes. The important role of nitrogen as these lakes recover from the cataclysmic eruption and proceed back towards their prior status as oligotrophic alpine lakes is emphasized.     

Thermodynamics of Formate-Oxidizing Metabolism and Implications for H2 Production

Formate-dependent proton reduction to H₂ (HCOO⁻ + H₂O → HCO₃⁻ + H₂) has been reported for hyperthermophilic Thermococcus strains. In this study, a hyperthermophilic archaeon, Thermococcus onnurineus strain NA1, yielded H₂ accumulation to a partial pressure of 1 × 10⁵ to 7 × 10⁵ Pa until the values of Gibbs free energy change (ΔG) reached near thermodynamic equilibrium (−1 to −3 kJ mol⁻¹). The bioenergetic requirement for the metabolism to conserve energy was demonstrated by ΔG values as small as −5 kJ mol⁻¹, which are less than the biological minimum energy quantum, −20 kJ mol⁻¹, as calculated by Schink (B. Schink, Microbiol. Mol. Biol. Rev. 61:262-280, 1997). Considering formate as a possible H₂ storage material, the H₂ production potential of the strain was assessed. The volumetric H₂ production rate increased linearly with increasing cell density, leading to 2,820 mmol liter⁻¹ h⁻¹ at an optical density at 600 nm (OD₆₀₀) of 18.6, and resulted in the high specific H₂ production rates of 404 ± 6 mmol g⁻¹ h⁻¹. The H₂ productivity indicates the great potential of T. onnurineus strain NA1 for practical application in comparison with H₂-producing microbes. Our result demonstrates that T. onnurineus strain NA1 has a highly efficient metabolic system to thrive on formate in hydrothermal systems.     

Biotechnological Process for Production of β-Dipeptides from Cyanophycin on a Technical Scale and Its Optimization

A triphasic process was developed for the production of β dipeptides from cyanophycin (CGP) on a large scale. Phase I comprises an optimized acid extraction method for technical isolation of CGP from biomass. It yielded highly purified CGP consisting of aspartate, arginine, and a little lysine. Phase II comprises the fermentative production of an extracellular CGPase (CphE_al) from Pseudomonas alcaligenes strain DIP1 on a 500-liter scale in mineral salts medium, with citrate as the sole carbon source and CGP as an inductor. During optimization, it was shown that 2 g liter⁻¹ citrate, pH 6.5, and 37°C are ideal parameters for CphE_al production. Maximum enzyme yields were obtained after induction in the presence of 50 mg liter⁻¹ CGP or CGP dipeptides for 5 or 3 h, respectively. Aspartate at a concentration of 4 g liter⁻¹ induced CphE_al production with only about 30% efficiency in comparison to that with CGP. CphE_al was purified utilizing its affinity for the substrate and its specific binding to CGP. CphE_al turned out to be a serine protease with maximum activity at 50°C and at pH 7 to 8.5. Phase III comprises degradation of CGP to β-aspartate-arginine and β-aspartate-lysine dipeptides with a purity of over 99% (by thin-layer chromatography and high-performance liquid chromatography), employing a crude CphE_al preparation. Optimum degradation parameters were 100 g liter⁻¹ CGP, 10 g liter⁻¹ crude CphE_al powder, and 4 h of incubation at 50°C. The overall efficiency of phase III was 91%, while 78% (wt/wt) of the used CphE_al powder with sustained activity toward CGP was recovered. The optimized process was performed with industrial materials and equipment and is applicable to any desired scale.     

Streptomyces thermoautotrophicus sp. nov., a Thermophilic CO- and H2-Oxidizing Obligate Chemolithoautotroph

The novel thermophilic CO- and H₂-oxidizing bacterium UBT1 has been isolated from the covering soil of a burning charcoal pile. The isolate is gram positive and obligately chemolithoautotrophic and has been named Streptomyces thermoautotrophicus on the basis of G+C content (70.6 ± 0.19 mol%), a phospholipid pattern of type II, MK-9(H₄) as the major quinone, and other chemotaxonomic and morphological properties. S. thermoautotrophicus could grow with CO (t_d = 8 h), H₂ plus CO₂ (t_d = 6 h), car exhaust, or gas produced by the incomplete combustion of wood. Complex media or heterotrophic substrates such as sugars, organic acids, amino acids, and alcohols did not support growth. Molybdenum was required for CO-autotrophic growth. For growth with H₂, nickel was not necessary. The optimum growth temperature was 65°C; no growth was observed below 40°C. However, CO-grown cells were able to oxidize CO at temperatures of 10 to 70°C. Temperature profiles of burning charcoal piles revealed that, up to a depth of about 10 to 25 cm, the entire covering soil provides a suitable habitat for S. thermoautotrophicus. The K_m was 88 μl of CO liter⁻¹ and V_max was 20.2 μl of CO h⁻¹ mg of protein⁻¹. The threshold value of S. thermoautotrophicus of 0.2 μl of CO liter⁻¹ was similar to those of various soils. The specific CO-oxidizing activity in extracts with phenazinemethosulfate plus 2,6-dichlorophenolindophenol as electron acceptors was 246 μmol min⁻¹ mg of protein⁻¹. In exception to other carboxydotrophic bacteria, S. thermoautotrophicus CO dehydrogenase was able to reduce low potential electron acceptors such as methyl and benzyl viologens.     

Aerobic Fermentation of D-Xylose to Ethanol by Clavispora sp

Eleven strains of an undescribed species of Clavispora fermented D-xylose directly to ethanol under aerobic conditions. Strain UWO(PS)83-877-1 was grown in a medium containing 2% D-xylose and 0.5% yeast extract, and the following results were obtained: ethanol yield coefficient (ethanol/D-xylose), 0.29 g g⁻¹ (57.4% of theoretical); cell yield coefficient (dry biomass/D-xylose), 0.25 g g⁻¹; maximum ethanol concentration, 5.9 g liter⁻¹; maximum volumetric ethanol productivity, 0.11 g liter⁻¹ h⁻¹. With initial D-xylose concentrations of 40, 60, and 80 g liter⁻¹, maximum ethanol concentrations of 8.8, 10.9, and 9.8 g liter⁻¹ were obtained, respectively (57.2, 57.1, and 48.3% of theoretical). Ethanol was found to inhibit the fermentation of D-xylose (K_p = 0.58 g liter⁻¹) more than the fermentation of glucose (K_p = 6.5 g liter⁻¹). The performance of this yeast compared favorably with that reported for some other D-xylose-fermenting yeasts.     

A New Sensitive Bioassay for Determination of Microbially Available Phosphorus in Water

The content of assimilable organic carbon has been proposed to control the growth of microbes in drinking water. However, recent results have shown that there are regions where it is predominantly phosphorus which determines the extent of microbial growth in drinking waters. Even a very low concentration of phosphorus (below 1 μg of P liter⁻¹) can promote extensive microbial growth. We present here a new sensitive method to determine microbially available phosphorus concentrations in water down to 0.08 μg of P liter⁻¹. The method is a bioassay in which the analysis of phosphorus in a water sample is based on maximum growth of Pseudomonas fluorescens P17 when the energy supply and inorganic nutrients, with the exception of phosphorus, do not limit bacterial growth. Maximum growth (CFU) in the water sample is related to the concentration of phosphorus with the factor 373,200 ± 9,400 CFU/μg of PO₄-P. A linear relationship was found between cell growth and phosphorus concentration between 0.05 to 10 μg of PO₄-P liter⁻¹. The content of microbially available phosphorus in Finnish drinking waters varied from 0.1 to 10.2 μg of P liter⁻¹ (median, 0.60 μg of P liter⁻¹).     

Effects of Glucose Concentrations on Cadmium, Copper, Mercury, and Zinc Toxicity to a Klebsiella sp

The influence of glucose concentration on Cd, Cu, Hg, and Zn toxicity to a Klebsiella sp. was studied by following the degradation of ¹⁴C-labeled glucose at pH 6.0. Uptake of ¹⁴C into the cells was also determined. The carbon concentrations ranged from 0.01 to 40 mg liter⁻¹, which are equivalent to soluble C concentrations in natural environments. The toxicity of Cu, Cd, and Zn to a Klebsiella sp. was affected considerably by the C concentration. Copper at 10⁻⁵ M was toxic when the carbon concentration was 10 or 40 mg liter⁻¹, while at 0.01 to 1.0 mg liter⁻¹ no toxicity was observed. Cadmium and zinc were toxic at 10⁻² M in media containing 0.01 to 1.0 mg of C liter⁻¹. At C concentrations greater than 1.0 mg liter⁻¹, the inhibition of glucose degradation and carbon assimilation was observed at 10⁻³ M Cd and Zn. The toxicity of mercury seemed to be independent of the C concentration. Results of this study showed that the nutritional state of an organism may have a profound effect on its sensitivity to metals. Metals taken up by an energy-driven transport system may be less toxic under conditions of C starvation. The C concentration should be taken into account when evaluating results from toxicity studies, especially as most microorganisms in nature live under energy-limited conditions.     

Toxic Effects of Linear Alkylbenzene Sulfonate on Metabolic Activity, Growth Rate, and Microcolony Formation of Nitrosomonas and Nitrosospira Strains

Strong inhibitory effects of the anionic surfactant linear alkylbenzene sulfonate (LAS) on four strains of autotrophic ammonia-oxidizing bacteria (AOB) are reported. Two Nitrosospira strains were considerably more sensitive to LAS than two Nitrosomonas strains were. Interestingly, the two Nitrosospira strains showed a weak capacity to remove LAS from the medium. This could not be attributed to adsorption or any other known physical or chemical process, suggesting that biodegradation of LAS took place. In each strain, the metabolic activity (50% effective concentration [EC₅₀], 6 to 38 mg liter⁻¹) was affected much less by LAS than the growth rate and viability (EC₅₀, 3 to 14 mg liter⁻¹) were. However, at LAS levels that inhibited growth, metabolic activity took place only for 1 to 5 days, after which metabolic activity also ceased. The potential for adaptation to LAS exposure was investigated with Nitrosomonas europaea grown at a sublethal LAS level (10 mg liter⁻¹); compared to control cells, preexposed cells showed severely affected cell functions (cessation of growth, loss of viability, and reduced NH₄⁺ oxidation activity), demonstrating that long-term incubation at sublethal LAS levels was also detrimental. Our data strongly suggest that AOB are more sensitive to LAS than most heterotrophic bacteria are, and we hypothesize that thermodynamic constraints make AOB more susceptible to surfactant-induced stress than heterotrophic bacteria are. We further suggest that AOB may comprise a sensitive indicator group which can be used to determine the impact of LAS on microbial communities.     

Influence of Environmental Factors and Medium Composition on Vibrio gazogenes Growth and Prodigiosin Production

Vibrio gazogenes ATCC 29988 growth and prodigiosin synthesis were studied in batch culture on complex and defined media and in chemostat cultures on defined medium. In batch culture on complex medium, a maximum growth rate of 0.75 h⁻¹ and a maximum prodigiosin concentration of 80 ng of prodigiosin · mg of cell protein⁻¹ were observed. In batch culture on defined medium, maximum growth rates were lower (maximum growth rate, 0.40 h⁻¹), and maximum prodigiosin concentrations were higher (1,500 ng · mg of protein⁻¹). In batch culture on either complex or defined medium, growth was characterized by a period of logarithmic growth followed by a period of linear growth; on either medium, prodigiosin biosynthesis was maximum during linear growth. In batch culture on defined medium, the initial concentration of glucose optimal for growth and pigment production was 3.0%; higher levels of glucose suppressed synthesis of the pigment. V. gazogenes had an absolute requirement for Na⁺; optimal growth occurred in the presence of 100 mM NaCl. Increases in the concentration of Na⁺ up to 600 mM resulted in further increases in the concentration of pigment in the broth. Prodigiosin was synthesized at a maximum level in the presence of inorganic phosphate concentrations suboptimal for growth. Concentrations of KH₂PO₄ above 0.4 mM caused decreased pigment synthesis, whereas maximum cell growth occurred at 1.0 mM. Optimal growth and pigment production occurred in the presence of 8 to 16 mg of ferric ion · liter⁻¹, with higher concentrations proving inhibitory to both growth and pigment production. Both growth and pigment production were found to decrease with increased concentrations of p-aminobenzoic acid. The highest specific concentration of prodigiosin (3,480 ng · mg protein⁻¹) was observed in chemostat cultures at a dilution rate of 0.057 h⁻¹. The specific rate of prodigiosin production at this dilution rate was approximately 80% greater than that observed in batch culture on defined medium. At dilution rates greater than 0.057 h⁻¹, the concentration of cells decreased with increasing dilution rate, resulting in a profile comparable to that expected for linear growth kinetics. No explanation could be found for the linear growth profiles obtained for both batch and chemostat cultures.     

Potential for aflatoxin B1 and B2 production by Aspergillus flavus strains isolated from rice samples

In this study, we investigated the potential for aflatoxin B₁ (AFB₁) and B₂ (AFB₂) production in rice grain by 127 strains of Aspergillus flavus isolated from rice grains collected from China. These strains were inoculated onto rice grains and incubated at 28 °C for 21 days. AFB₁ and AFB₂ were extracted and quantified by high-performance liquid chromatography coupled with fluorescence detection. Among the tested strains, 37% produced AFB₁ and AFB₂ with levels ranging from 175 to 124 101 μg kg⁻¹ for AFB₁ and from not detected to 10 329 μg kg⁻¹ for AFB₂. The mean yields of these isolates were 5884 μg kg⁻¹ for AFB₁ and 1968 μg kg⁻¹ for AFB₂. Overall, most of the aflatoxigenic strains produced higher levels of AFB₁ than AFB₂ in rice. The obtained information is useful for assessing the risk of aflatoxin contamination in rice samples.     

Biochar Enhances Aspergillus niger Rock Phosphate Solubilization by Increasing Organic Acid Production and Alleviating Fluoride Toxicity

During fungal rock phosphate (RP) solubilization, a significant quantity of fluoride (F⁻) is released together with phosphorus (P), strongly inhibiting the process. In the present study, the effect of two F⁻ adsorbents [activated alumina (Al₂O₃) and biochar] on RP solubilization by Aspergillus niger was examined. Al₂O₃ adsorbed part of the F⁻ released but also adsorbed soluble P, which makes it inappropriate for microbial RP solubilization systems. In contrast, biochar adsorbed only F⁻ while enhancing phosphate solubilization 3-fold, leading to the accumulation of up to 160 mg of P per liter. By comparing the values of F⁻ measured in solution at the end of incubation and those from a predictive model, it was estimated that up to 19 mg of F⁻ per liter can be removed from solution by biochar when added at 3 g liter⁻¹ to the culture medium. Thus, biochar acted as an F⁻ sink during RP solubilization and led to an F⁻ concentration in solution that was less inhibitory to the process. In the presence of biochar, A. niger produced larger amounts of citric, gluconic, and oxalic acids, whether RP was present or not. Our results show that biochar enhances RP solubilization through two interrelated processes: partial removal of the released F⁻ and increased organic acid production. Given the importance of organic acids for P solubilization and that most of the RPs contain high concentrations of F⁻, the proposed solubilization system offers an important technological improvement for the microbial production of soluble P fertilizers from RP.     

Protozoan Bacterivory and Escherichia coli Survival in Drinking Water Distribution Systems

The development of bacterial communities in drinking water distribution systems leads to a food chain which supports the growth of macroorganisms incompatible with water quality requirements and esthetics. Nevertheless, very few studies have examined the microbial communities in drinking water distribution systems and their trophic relationships. This study was done to quantify the microbial communities (especially bacteria and protozoa) and obtain direct and indirect proof of protozoan feeding on bacteria in two distribution networks, one of GAC water (i.e., water filtered on granular activated carbon) and the other of nanofiltered water. The nanofiltered water-supplied network contained no organisms larger than bacteria, either in the water phase (on average, 5 × 10⁷ bacterial cells liter⁻¹) or in the biofilm (on average, 7 × 10⁶ bacterial cells cm⁻²). No protozoa were detected in the whole nanofiltered water-supplied network (water plus biofilm). In contrast, the GAC water-supplied network contained bacteria (on average, 3 × 10⁸ cells liter⁻¹ in water and 4 × 10⁷ cells cm⁻² in biofilm) and protozoa (on average, 10⁵ cells liter⁻¹ in water and 10³ cells cm⁻² in biofilm). The water contained mostly flagellates (93%), ciliates (1.8%), thecamoebae (1.6%), and naked amoebae (1.1%). The biofilm had only ciliates (52%) and thecamoebae (48%). Only the ciliates at the solid-liquid interface of the GAC water-supplied network had a measurable grazing activity in laboratory test (estimated at 2 bacteria per ciliate per h). Protozoan ingestion of bacteria was indirectly shown by adding Escherichia coli to the experimental distribution systems. Unexpectedly, E. coli was lost from the GAC water-supplied network more rapidly than from the nanofiltered water-supplied network, perhaps because of the grazing activity of protozoa in GAC water but not in nanofiltered water. Thus, the GAC water-supplied network contained a functional ecosystem with well-established and structured microbial communities, while the nanofiltered water-supplied system did not. The presence of protozoa in drinking water distribution systems must not be neglected because these populations may regulate the autochthonous and allochthonous bacterial populations.     

Lidocaine,Dexmedetomidine and Their Combination Reduce Isoflurane Minimum Alveolar Concentration in Dogs

The effects of intravenous (IV) lidocaine, dexmedetomidine and their combination delivered as a bolus followed by a constant rate infusion (CRI) on the minimum alveolar concentration of isoflurane (MAC_ISO) in dogs were evaluated. Seven healthy adult dogs were included. Anaesthesia was induced with propofol and maintained with isoflurane. For each dog, baseline MAC (MAC_ISO/BASAL) was determined after a 90-minute equilibration period. Thereafter, each dog received one of the following treatments (loading dose, CRI): lidocaine 2 mg kg⁻¹, 100 µg kg⁻¹ minute⁻¹; dexmedetomidine 2 µg kg⁻¹, 2 µg kg⁻¹ hour⁻¹; or their combination. MAC was then determined again after 45- minutes of treatment by CRI. At the doses administered, lidocaine, dexmedetomidine and their combination significantly reduced MAC_ISO by 27.3% (range: 12.5–39.2%), 43.4% (33.3–53.3%) and 60.9% (46.1–78.1%), respectively, when compared to MAC_ISO/_BASAL. The combination resulted in a greater MAC_ISO reduction than the two drugs alone. Their use, at the doses studied, provides a clinically important reduction in the concentration of ISO during anaesthesia in dogs.     

Ammonium Removal by the Oxygen-Limited Autotrophic Nitrification-Denitrification System

The present lab-scale research reveals the potential of implementation of an oxygen-limited autotrophic nitrification-denitrification (OLAND) system with normal nitrifying sludge as the biocatalyst for the removal of nitrogen from nitrogen-rich wastewater in one step. In a sequential batch reactor, synthetic wastewater containing 1 g of NH₄⁺-N liter⁻¹ and minerals was treated. Oxygen supply to the reactor was double-controlled with a pH controller and a timer. At a volumetric loading rate (B_v) of 0.13 g of NH₄⁺-N liter⁻¹ day⁻¹, about 22% of the fed NH₄⁺-N was converted to NO₂⁻-N or NO₃⁻-N, 38% remained as NH₄⁺-N, and the other 40% was removed mainly as N₂. The specific removal rate of nitrogen was on the order of 50 mg of N liter⁻¹ day⁻¹, corresponding to 16 mg of N g of volatile suspended solids⁻¹ day⁻¹. The microorganisms which catalyzed the OLAND process are assumed to be normal nitrifiers dominated by ammonium oxidizers. The loss of nitrogen in the OLAND system is presumed to occur via the oxidation of NH₄⁺ to N₂ with NO₂⁻ as the electron acceptor. Hydroxylamine stimulated the removal of NH₄⁺ and NO₂⁻. Hydroxylamine oxidoreductase (HAO) or an HAO-related enzyme might be responsible for the loss of nitrogen.