Development of medium for enhanced production of glutaminase-free <Emphasis Type="SmallCaps">l</Emphasis>-asparaginase from <Emphasis Type="Italic">Pectobacterium carotovorum</Emphasis> MTCC 1428

Glutaminase-free l-asparaginase is known to be an excellent anticancer agent. In the present study, statistically based experimental designs were applied to maximize the production of glutaminase-free l-asparaginase from Pectobacterium carotovorum MTCC 1428. Nine components of the medium were examined for their significance on the production of l-asparaginase using the Plackett–Burman experimental design. The medium components, viz., glucose, l-asparagine, KH₂PO₄, and MgSO₄·7H₂O, were screened based on their high confidence levels (P < 0.04). The optimum levels of glucose, l-asparagine, KH₂PO₄, and MgSO₄·7H₂O were found to be 2.076, 5.202, 1.773, and 0.373 g L⁻¹, respectively, using the central composite experimental design. The maximum specific activity of l-asparaginase in the optimized medium was 27.88 U mg⁻¹ of protein, resulting in an overall 8.3-fold increase in the production compared to the unoptimized medium.     

Solubilization of enzymes in water-in-oil microemulsions and their rapid and efficient release through use of a pH-degradable surfactant

α-Chymotrypsin and lysozyme were solubilized in a water/O-[(2-tridecyl, 2-ethyl-1,3-dioxolan-4-yl)methoxy]–O′-methoxy poly(ethylene glycol) (CK-2,13 surfactant)/isooctane water-in-oil microemulsion solution at 1.5–2 and 10 g l⁻¹ for 0.15 and 1.2 M CK-2,13, respectively. Upon contact with an equal volume of 0.1 M NaH₂PO₄/Na₂HPO₄ buffer, pH 5, a three-phase system (Winsor-III system) was formed, consisting of a surfactant-rich middle phase and aqueous and isooctane-rich “excess” phases. Both enzymes were rapidly released into the aqueous excess phase, with 70% recovery of each in 30 and 60 min for microemulsion solutions containing 0.15 and 1.2 M surfactant, respectively. The recovered enzymes retained >90% of their original specific activity.     

Fundamental Mechanisms of Phosphate Removal by Anaerobic/Aerobic Activated Sludge in Treating Municipal Wastewater

Acetate is thought to be an important substrate for phosphate removal in anaerobic/aerobic activated sludge (AS) processes. The acetate content in municipal wastewater is low, and the main organic compounds in such wastewater are particulate organic matters (POMs) that are converted to endogenous substrates in AS processes when municipal wastewater is introduced into AS reactors. The question which then arises is which substrate, acetate or POM, is important for phosphate removal in full‐scale AS plants. The rates of phosphate release and substrate uptake were determined using AS harvested from a full‐scale anaerobic/aerobic AS plant and also AS acclimated to peptone under alternate anaerobic and aerobic conditions for 26 months. The rate of phosphate release upon POM addition per AS concentration per unit of time was about 0.84 mg PO₄‐P/(g MLSS·h) irrespective of the wastewater quality. This value was about 0.05 in the case of AS acclimated to peptone for 26 months. When the AS concentration is 2.5 g/L and the mixed liquor retention time is 2 h in the anaerobic zone, about 4.2 mg/L PO₄‐P is released upon POM addition. Hence, phosphate can be removed from municipal wastewater using full‐scale AS plants running under these conditions.     

Impact of Willow Short Rotation Coppice on Water Quality

Short rotation coppice (SRC) with willow has been grown in Sweden from the late 1980s to produce biomass for energy on agricultural land. This study evaluated the effects of SRC on water quality by determining differences in leaching of nitrogen and phosphorus to groundwater of a number of commercial “old” SRC willow stands in Sweden compared to adjacent arable fields grown with “ordinary” crops. The study was conducted in 16 locations under three vegetation seasons. NO₃–N leaching from willow SRC fields was significantly lower than that from reference fields with cereals. The opposite was observed for PO₄–P; concentrations in the groundwater of SRC were higher compared to reference fields. Sewage sludge applications were not responsible for the elevated PO₄–P leaching under SRC compared to reference crops.     

Ethanol fermentation of mixed-sugars using a two-phase, fed-batch process: method to minimize D-glucose repression of Candida shehatae D-xylose fermentations

Candida shehatae cells pre-grown on D-xylose simultaneously consumed mixtures of D-xylose and D-glucose, under both non-growing (anoxic) and actively growing conditions (aerobic), to produce ethanol. The rate of D-glucose consumption was independent of the D-xylose concentration for cells induced on D-xylose. However, the D-xylose consumption rate was approximately three times lower than the D-glucose consumption rate at a 50% D-glucose: 50% D-xylose mixture. Repression was not observed (substrate utilization rates were approximately equal) when the percentage of D-glucose and D-xylose was changed to 22% and 78%, respectively. In fermentations with actively growing cells (50% glucose and D-xylose), ethanol yields from D-xylose increased, the % D-xylose utilized increased, and the xylitol yield was significantly reduced in the presence of D-glucose, compared to anoxic fermentations (Y_ETOH,xylose = 0.2–0.40 g g⁻¹, 75–100%, and Y_xylitol = 0–0.2 g g⁻¹ compared to Y_ETOH,xylose = 0.15 g g⁻¹, 56%, Y_xylitol = 0.51 g g⁻¹, respectively). To increase ethanol levels and reduce process time, fed-batch fermentations were performed in a single stage reactor employing two phases: (1) rapid aerobic growth on D-xylose (μ = 0.32 h⁻¹) to high cell densities; (2) D-glucose addition and anaerobic conditions to produce ethanol (Y_ETOH,xylose = 0.23 g g⁻¹). The process generated high cell densities, 2 × 10⁹ cells ml⁻¹, and produced 45–50 g L⁻¹ ethanol within 50 h from a mixture of D-glucose and D-xylose (compared to 30 g L⁻¹ in 80 h in the best batch process). The two-phase process minimized loss of cell viability, increased D-xylose utilization, reduced process time, and increased final ethanol levels compared to the batch process. Received 23 February 1998/ Accepted in revised form 15 July 1998     

Tripeptides with C-Terminal Arginine as Potential Inhibitors of Urokinase

We synthesized and tested ten peptides with the molecular structure being H–d-Ser–AA–Arg–OH for their effect on the amidolytic activities against urokinase, thrombin, trypsin, plasmin, tissue plasminogen activator and kallikrein. The inserted amino acid in each peptide was either leucine, norleucine, izoleucine, valine, norvaline, α-metyloalanine, α-aminobutanoic acid, homoleucine, tert-leucine or neoglycine. H–d-Ser–NVal–Arg–OH (compound 4) was the most active inhibitor of urokinase plasminogen activator with a K_i value of 0.85 μM. Compound 4 showed cytotoxic effect against MDA-MB-231 and DLD cell lines, respectively, with IC₅₀ values of 25 and 19 μM. Synthesised compounds did not have activity against MCF-7 cancer cells. These peptides were nontoxic against pig’s erythrocytes in vitro.     

Test of Porous Ceramic Material for the Immobilisation of Predominant Nitrifying Bacteria and for the Improvement of the AAO Process

The efficiency of nitrification in a fixed bed reactor was compared to that found in an activated sludge reactor to determine their sensitivity to changing loads and lower temperatures. Two structurally identical lab‐scale systems, using the anaerobic/anoxic/aerobic (AAO) process to remove nitrogen and phosphorus simultaneously, were operated in parallel with secondary clarifiers and sludge return. The first aerobic system was operated as an activated sludge reactor, the second system as a fixed bed reactor. The aerobic fixed bed reactor was filled with porous ceramic materials for the immobilisation of predominantly nitrifying bacteria. The removal efficiencies of 99 % NH₄⁺‐N, 90 % DOC, and 98 % PO₄^3–‐P for normal loads of 0.11 g/L d DOC, 0.06 g/L d NH₄⁺‐N, and 0.0054 g/L d PO₄^3–‐P were achieved for both systems. However, the system with an aerobic fixed bed reactor was characterised by the following advantages over the system with an activated sludge reactor: a shorter time to reach almost complete nitrification, a higher nitrification rate at higher loads of NH₄⁺‐N and a lower sensitivity of nitrification at lower temperatures down to 12 °C.     

Distribution of extracellular polymeric substances in aerobic granules

Extracellular matrix provides an architectural structure and mechanical stability for aerobic granules. Distributions of cells and extracellular polymeric substances (EPS), including proteins, α- and β-d-glucopyranose polysaccharides, in acetate-fed granules and phenol-fed granules were probed using a novel quadruple staining scheme. In acetate-fed granules, protein and β-d-glucopyranose polysaccharides formed the core, whereas, the cells and α-d-glucopyranose polysaccharides accumulated in the granule outer layers. Based on these experimental findings, this study indicated that different conclusions can be obtained regarding EPS distributions when granules were stained differently. The core of phenol-fed granules, conversely, was formed principally by proteins; whereas, the cells and α- and β-d-glucopyranose polysaccharides were accumulated at an outer filamentous layer. Using a series of confocal laser scanning microscope (CLSM) images whose threshold values were determined via Otsu’s scheme, the three-dimensional distributions of cells and EPS were produced using a polygonal surface model. Structural information extracted can be applied in further development of comprehensive granule models.     

Production of <Emphasis Type="SmallCaps">l</Emphasis>-lactic acid by <Emphasis Type="Italic">Rhizopus oryzae</Emphasis> using semicontinuous fermentation in bioreactor

Semicontinuous fermentation using pellets of Rhizopus oryzae has been recognized as a promising technology for l-lactic acid production. In this work, semicontinuous fermentation of R. oryzae AS 3.819 for l-lactic acid production has been developed with high l-lactic acid yield and volumetric productivity. The effects of factors such as inoculations, CaCO₃ addition time, and temperature on l-lactic acid yield and R. oryzae morphology were researched in detail. The results showed that optimal fermentation conditions for the first cycle were: inoculation with 4% spore suspension, CaCO₃ added to the culture medium at the beginning of culture, and culture temperature of 32–34°C. In orthogonal experiments, high l-lactic acid yield was achieved when the feeding medium was (g/l): glucose, 100; (NH₄)₂SO₄, 2; KH₂PO₄, 0.1; ZnSO₄·7H₂O, 0.33; MgSO₄·7H₂O, 0.15; CaCO₃, 50. Twenty cycles of semicontinuous fermentation were carried out in flask culture. l-lactic acid yield was 78.75% for the first cycle and 80–90% for the repeated cycles; the activities of lactate dehydrogenases (LDH) were 7.2–9.2 U/mg; fermentation was completed in 24 h for each repeated cycle. In a 7-l magnetically stirred fermentor, semicontinuous fermentation lasted for 25 cycles using pellets of R. oryzae AS 3.819 under the optimal conditions determined from flask cultures. The final l-lactic acid concentration (LLAC) reached 103.7 g/l, and the volumetric productivity was 2.16 g/(l·h) for the first cycle; in the following 19 repeated cycles, the final LLAC reached 81–95 g/l, and the volumetric productivities were 3.40–3.85 g/(l·h).     

Copper (II) complex of 1,10-phenanthroline and <Emphasis Type="SmallCaps">l</Emphasis>-tyrosine with DNA oxidative cleavage activity in the gallic acid

Copper (II) complex of formulation [Cu–Phen–Tyr](H₂O)](ClO₄) (Phen = 1,10-phenanthroline, l-Tyr = l-tyrosine), has been prepared, and their induced DNA oxidative cleavage activity studied. The complex binds to DNA by intercalation, as deduced from the absorption and fluorescence spectral data. Scatchard plots constructed from the absorption titration data gave binding constant 2.44 × 10⁴ M⁻¹ of base pairs. Extensive hypochromism, broadening, and red shifts in the absorption spectra were observed. Upon binding to DNA, the fluorescence from the DNA–ethidium bromide system was efficiently quenched by the copper (II) complex. Stern–Volmer quenching constant 0.61 × 10³ M⁻¹ obtained from the linear quenching plots. [Cu–Phen–Tyr] complex efficiently cleave the supercoiled DNA to its nicked circular form with gallic acid as biological reductant at appropriate complex concentration. The gallic acid as reductant could observably improve copper (II) complex to DNA damage. The pseudo-Michaelis–Menten kinetic parameters (k _cat, K _M) were calculated to be 1.32 h⁻¹ and 5.46 × 10⁻⁵ M for [Cu–Phen–Tyr] complex. Mechanistic studies reveal the involvement of superoxide anions and hydroxyl radical (HO^·) as the reactive species under an aerobic medium.     

Enhancement of biological treatment performance of saline wastewater by halophilic bacteria

Performances of biological treatment processes of saline wastewater are usually low because of adverse effects of salt on microbial flora. High salt concentrations in wastewater cause plasmolysis and loss of activity of cells resulting in low COD removal efficiencies. In order to improve biological treatment performance of saline wastewater, a halophilic organism Halobacter halobium was used along with activated sludge culture.A synthetic wastewater composed of diluted molasses, urea, KH₂PO₄ and various concentrations of salt (1%–5% NaCl) was treated in an aerobic-biological reactor by fed-batch operation. Activated sludge culture with and without Halobacter were used as seed cultures. Variations of COD removal rate and efficiency with salt concentration were determined for both cultures and results were compared. Inclusion of Halobacter into activated sludge culture resulted in significant improvements in COD removal efficiency. A rate expression including salt inhibition effect was proposed and kinetic constants were determined by using experimental data.This study was supported by the Technical and Scientific Research Council of Turkey.     

Isocitrate dehydrogenase and glyoxylate cycle enzyme activities in Bradyrhizobium japonicum under various growth conditions

Bradyrhizobium japonicum, the nitrogen-fixing symbiotic partner of soybean, was grown on various carbon substrates and assayed for the presence of the glyoxylate cycle enzymes, isocitrate lyase and malate synthase. The highest levels of isocitrate lyase [165–170 nmol min^–1 (mg protein)^–1] were found in cells grown on acetate or β-hydroxybutyrate, intermediate activity was found after growth on pyruvate or galactose, and very little activity was found in cells grown on arabinose, malate, or glycerol. Malate synthase activity was present in arabinose- and malate-grown cultures and increased by only 50–80% when cells were grown on acetate. B. japonicum bacteroids, harvested at four different nodule ages, showed very little isocitrate lyase activity, implying that a complete glyoxylate cycle is not functional during symbiosis. The apparent K _m of isocitrate lyase for d,l-isocitrate was fourfold higher than that of isocitrate dehydrogenase (61.5 and 15.5 μM, respectively) in desalted crude extracts from acetate-grown B. japonicum. When isocitrate lyase was induced, neither the V _max nor the d,l-isocitrate K _m of isocitrate dehydrogenase changed, implying that isocitrate dehydrogenase is not inhibited by covalent modification to facilitate operation of the glyoxylate cycle in B. japonicum. Received: 10 October 1997 / Accepted: 16 January 1998     

Localization of chitinolytic activities in Fagus sylvatica mycorrhizas

 Localization of chitinolytic activities in Fagus sylvatica (beech) mycorrhizas was examined using a range of fluorogenic 4-methylumbelliferyl [4-MU-(GlcNAc)_1–4] substrates in order to distinguish between exochitinase, endochitinase and β-N–acetylglucosaminidase activities. The validity of the technique was confirmed using onion epidermis cells. In the beech mycorrhiza, endochitinase activity was not detectable above background fluorescence. Exochitinase activity was detected in the fungal sheath and the Hartig net. β-N–Acetylglucosaminidase activity was also mainly associated with the fungal sheath and Hartig net. Individual fungal hyphae extending from these structures also showed substantial β-N–acetylglucosaminidase activity. The cortical cell walls of the host in the Hartig net region also fluoresced brightly. The localization of β-N–acetylglucosaminidase activity was confirmed using a chromogenic histochemical reagent, 5-bromo-4-chloro-3-indolyl-N–acetyl-β-d-glucosaminide (X-GlcNAc). Accepted: 5 December 1995     

Acid–base regulatory ability of the cephalopod (Sepia officinalis) in response to environmental hypercapnia

Acidification of ocean surface waters by anthropogenic carbon dioxide (CO₂) emissions is a currently developing scenario that warrants a broadening of research foci in the study of acid–base physiology. Recent studies working with environmentally relevant CO₂ levels, indicate that some echinoderms and molluscs reduce metabolic rates, soft tissue growth and calcification during hypercapnic exposure. In contrast to all prior invertebrate species studied so far, growth trials with the cuttlefish Sepia officinalis found no indication of reduced growth or calcification performance during long-term exposure to 0.6 kPa CO₂. It is hypothesized that the differing sensitivities to elevated seawater pCO₂ could be explained by taxa specific differences in acid–base regulatory capacity. In this study, we examined the acid–base regulatory ability of S. officinalis in vivo, using a specially modified cannulation technique as well as ³¹P NMR spectroscopy. During acute exposure to 0.6 kPa CO₂, S. officinalis rapidly increased its blood [HCO₃ ⁻] to 10.4 mM through active ion-transport processes, and partially compensated the hypercapnia induced respiratory acidosis. A minor decrease in intracellular pH (pH_i) and stable intracellular phosphagen levels indicated efficient pH_i regulation. We conclude that S. officinalis is not only an efficient acid–base regulator, but is also able to do so without disturbing metabolic equilibria in characteristic tissues or compromising aerobic capacities. The cuttlefish did not exhibit acute intolerance to hypercapnia that has been hypothesized for more active cephalopod species (squid). Even though blood pH (pHe) remained 0.18 pH units below control values, arterial O₂ saturation was not compromised in S. officinalis because of the comparatively lower pH sensitivity of oxygen binding to its blood pigment. This raises questions concerning the potentially broad range of sensitivity to changes in acid–base status amongst invertebrates, as well as to the underlying mechanistic origins. Further studies are needed to better characterize the connection between acid–base status and animal fitness in various marine species.     

Nitrogen fixation in the rhizosphere and rhizoplane of barley

Summary Aerobic and anaerobic N₂-fixing bacteria developed in the rhizosphere of barley seedlings and exhibited N₂ase activity when seedlings were grown in sterilized sand-nutrient cultures containing low levels of combined nitrogen. The source of the N₂-fixing bacteria appeared to be the seed. Average daily rates up to 0.9 μmoles C₂H₄ h⁻¹ g⁻¹ dry root tissue were measured, but the intensity of the activity was affected by moisture levels and concentration of combined N in the rhizosphere. Removal and washing of the roots did not remove the activity, and roots remained active even after surface-sterilization. An unidentified aerobic N₂-fixing bacterium was isolated from the rhizoplane of active barley roots. Inoculation of barley seedlings with the aerobic N₂-fixing bacterium enhanced N₂ase activity of excised roots 10-fold, with average rates of 0.9, 1.1 and 1.3 μmoles h⁻¹ g⁻¹ dry root assayed under pO₂ of 0.01, 0.02 and 0.04 atm respectively. The aerobic N₂-fixing bacterium also exhibited N₂ase activity when inoculated into the rhizosphere of oat, rice and wheat seedlings. Microscopic observations of sterilized live and stained barley roots suggest that the aerobic N₂-fixing bacterium is an endophyte which infects root tissue and metamorphoses into vesicle-like structures.     

The closure of the grevelingen estuary: Its influence on phytoplankton primary production and nutrient content

The Grevelingen estuary was cut off from the sea in May 1971, and changed into stagnat lake Grevelingen. After the closure nitrate concentrations decreased to extremely low values (less than 2 μgat NH₃-N/1). Ammonia concentrations varied between 10–30 μgat NH₃-N/1, comparable with the situation before the closure. Phosphate concentrations fluctuated between1–2 μgat PO₄-P/1 in the estuarine phase, and increased to μgat after the closure, presumably caused by decomposition of biological material and release of phosphates from the bottom. Phytoplankton primary production was not markedly affected by the damming up, and amounted to 175 g C/m² in 1971. Communication no. 147 of the Delta Institute for Hydrobiological Research, Yerseke, The Netherlands     

Comparison of biological removal via nitrite with real-time control using aerobic granular sludge and flocculent activated sludge

The process of nitrification–denitrification via nitrite for nitrogen removal under real-time control mode was tested in two laboratory-scale sequencing batch reactors (SBRs) with flocculent activated sludge (R1) and aerobic granular sludge (R2) to compare operational performance and real-time control strategies. The results showed that the average ammonia nitrogen, total inorganic nitrogen (TIN), and chemical oxygen demand (COD) removal during aeration phase were 97.6%, 57.0%, and 90.1% in R2 compared with 98.6%, 48.7%, and 88.1% in R1. The TIN removed in both SBRs was partially due to the presence of simultaneous nitrification–denitrification via nitrite, especially in R2. The specific nitrification and denitrification rates in R2 were 0.0416 mgNH₄⁺–N/gSS-min and 0.1889 mgNO_X⁻–N/gSS-min, which were 1.48 times and 1.35 times that of R1. The higher rates for COD removal, nitrification, and denitrification were achieved in R2 than R1 with similar influent quality. Dissolved oxygen (DO), pH, and oxidization reduction potential, corresponding to nutrient variations, were used as diagnostic parameters to control the organic carbon degradation and nitrification–denitrification via nitrite processes in both SBRs. The online control strategy of granular SBR was similar to that of the SBR with flocculent activated sludge. However, a unique U-type pattern on the DO curve in granular SBR was different from SBR with flocculent activated sludge in aerobic phase.     

ALKALINE PHOSPHATASE IN FRESHWATER CLADOPHORA‐EPIPHYTE ASSEMBLAGES: REGULATION IN RESPONSE TO PHOSPHORUS SUPPLY AND LOCALIZATION1

Extracellular alkaline phosphatase enzyme activity (APA) is important for algal phosphorus (P) acquisition in P‐limited freshwater ecosystems and is often used as an indicator of P deficiency. APA allows access to organic P (monophosphate esters), but the regulation of APA in response to availability of both PO₄³⁻ and organic P is poorly characterized. This study aimed to examine the regulation of APA in freshwater Cladophora‐epiphyte assemblages in response to PO₄³⁻ and a hydrolyzable organic P source, and for the first time to apply enzyme linked fluorescence (ELF) to localize APA within freshwater macroalgal‐epiphyte assemblages. In response to elevated PO₄³⁻ concentrations, a component of net APA was suppressed, but there was also a constitutive APA, which was maintained even after prolonged exposure to nearly 1,000 μM PO₄³⁻ and saturation of internal P pools. When supplied with organic glycerol P as the sole P source, the algae maintained APA in excess of needs for supplying PO₄³⁻ for uptake, resulting in PO₄³⁻ release into the medium. Constitutive APA may be adaptive to growth under chronic P limitation in oligotrophic freshwater habitats. Excess APA and release of PO₄³⁻ could benefit different algal and bacterial partners within assemblages. APA in both Cladophora sp. and epiphytic algae was localized with ELF only when ethanol fixation was omitted. In algal subsamples exposed to different P treatments, there was no correlation between bulk APA (using 4‐methylumbelliferyl phosphate [MUP] substrate) and % cell labeling with ELF, suggesting that ELF labeling of APA was at best semiquantitative in the algal assemblages.     

Influence of magnetic field on activity of given anaerobic sludge

Two modes of magnetic fields were applied in the Cr⁶⁺ removal sludge reactors containing two predominated strains—Bacillus sp. and Brevibacillus sp., respectively. The magnetic field mode I* of 0–4.5 or 0–14 mT between pieces was obtained by setting the magnetic pieces with the surface magnetic density of 0–6 or 0–20 mT into the reactor, and the magnetic field mode II* of 6, 20, or 40 mT on the return line was obtained by controlling the working distance of the permanent magnet outside the sludge return line. The effects of different magnetic fields on the activity of the given anaerobic sludge were studied by comparing with the control (absent of magnetic field). The results showed that the magnetic field of 0–4 mT improved the activity of given sludge most effectively, U_{max·\textCH4} U_{{\max \cdot {\text{CH}}_{4} }} (the peak methane-producing rate) and the methane producing volume per gCOD_Cr reached 64.3 mlCH₄/gVSS.d and 124 mlCH₄/gCOD_Cr, which increased by 20.6 and 70.7%, respectively, compared with the control. And the magnetic field of 20 mT took second place. It could be concluded that the input of some magnetic field could improve the activity of anaerobic sludge by increasing the transformation efficiency of COD_Cr matters to methane, and the total organic wastage did not increase.     

Screening and characterization of an aerobic nitrifying-denitrifying bacterium from activated sludge

Taking advantage of the good biocompatibility and high efficiency of nitrogen removal with microbes, nitrifying and denitrifying bacteria, are becoming increasingly more widely used for wastewater treatment and prevention of eutrophication. In this research, an aerobic nitrifying-denitrifying bacterium was successfully screened from activated sludge and identified as Pseudomonas sp. (CCTCC No M2010209) by the 16S rDNA sequence. The activity verification confirmed its nitrifying-denitrifying capability of removing ammonium, nitrate and nitrite nitrogen. The types of carbon sources and carbon-nitrogen ratio greatly influenced the removal efficiency of NH₄ ⁺-N and NO₃ ⁻-N. When the initial concentrations of NH₄ ⁺-N and NO₃ ⁻-N in synthetic wastewater were less than 70 and 50 mg/L, the nitrogen removal rates reached 94 and 90% in 9 h, respectively. Preliminary comparisons of nitrogen removal capacity between this isolate and other commercial preparations in the treatment of synthetic wastewater revealed its promising potential to be used in the actual wastewater treatment.