Physiological and nutritional determinants of protease secretion by Clostridium sporogenes: characterization of six extracellular proteases

Summary Proteases were the principal secretory proteins of Clostridium sporogenes and were optimally produced after active growth at 37° C. Glucose, ammonia and peptides repressed protease production. Protease formation was maximal in cultures grown at pH 6.5, but proteolytic activity exhibited a pH optimum of 7.0–8.0. Protease activity in culture filtrates was stimulated by divalent metal ions (Ca²⁺, Mn²⁺ and Co²⁺) and was strongly inhibited by ethylene diaminetetraacetate (EDTA) and thimerosal. Non-denaturing polyacrylamide gel electrophoresis and HPLC gel filtration demonstrated the presence of six major proteases of low molecular mass (approx. 15–35 kDa). The enzymes were partially purified from non-denaturing gels. Each hydrolysed azocoll and azocasein, but differed in their activity against a range of native collagen substrates. All six enzymes degraded human placental collagen (Type IV) but only one had a broad substrate specificity, being able to hydrolyse the more recalcitrant collagens (Types I, II and III). Experiments with individual proteases showed that their activities were strongly inhibited (40–85%) by 5 mM EDTA, indicating that they were metalloproteases. The enzymes exhibited different susceptibilities to inhibition by either 3 mM phenylmethylsulphonyl-fluoride (PMSF), 5 mM thimerosal, or 10 mM cysteine, which respectively inhibit serine, thiol and metalloproteases.     

Anaerobic degradation of p-cresol in batch and continuous cultures by a denitrifying bacterial consortium

Summary The anaerobic degradation of p-cresol under denitrifying conditions by a bacterial consortium was studied in batch and continuous cultures. Concentrations up to 3 mm were degraded within 5–6 days with 4-hydroxybenzyl alcohol, 4-hydroxybenzaldehyde and 4-hydroxybenzoate as intermediates. Steady states could be maintained at only one dilution rate, D=0.04 h^–1. A further increase in the dilution rate to 0.0 8 h^–1 resulted in culture wash-out. An estimation of the Saturation constant was made (<1 mg/l), taking the maximum specific growth rate as 0.045 h^–1, thus yielding a value of 0.125 mg p-cresol/l. Correspondence to: N. Khoury     

A continuous culture study of the regulation of extracellular protease production inVibrio SA1

During growth ofVibrio SA1 in a lactate-limited chemostat in the presence of 2mm phenylalanine as an inducer, the rate of production of two proteolytic enzymes, namely an endopeptidase and an aminopeptidase, was dependent upon the dilution rate. An optimum in the rate of synthesis of both proteases was observed at a dilution rate of 0.23 h^-1 and enzyme production only occurred between dilution rates of 0.06 and 0.45 h^-1. Without inducer a low rate of aminopeptidase production was found with an optimum at 0.19 h^-1, but only trace amounts of endopeptidase were detectable in the culture. In the presence of inducer the rate of enzyme production increased with increasing dilution rates over the range 0.06 to 0.23 h^-1 which was explained by an increase in saturation of inducer sites. The progressive decrease in the rate of protease production at higher dilution rates was ascribed to an increasing effect of catabolite repression by the increasing concentration of the growth substrate. It was shown that 5mm cyclic AMP could not relieve catabolite repression caused by glucose or lactate. Repression of protease production also occurred in the presence of higher concentrations (5mm) phenylalanine and other amino acids and by ammonium ions. It is suggested that the energy-status of the cell may play an important role in the regulation of protease synthesis inVibrio SA1.This study was supported by the Foundation for Fundamental Biological Research (BION), which is subsidized by the Netherlands Organization for the Advancement of Pure Research (Z.W.O.).     

Physiological aspects of l-lysine production: effect of nutritional limitations on a producing strain of Corynebacterium glutamicum

The effect of nutritional limitations, such as phosphorus and carbon, on the production of l-lysine by Corynebacterium glutamicum was studied in continuous culture. We observed that phosphate-limited cultures at low growth rates were favourable to l-lysine production. l-Lysine was produced when a culture at low dilution rate (0.03 h^–1) was established. A dilution rate of about 0.04 h^–1 should be maintained in order to assure good productivity and an l-lysine yield of 0.53 g/g. Under carbon-limiting conditions the maintenance energy and growth yield of 0.03 g/g·g^–1·h^–1 and 0.41 g/g, respectively, have been obtained. Under these limiting conditions the l-lysine production was not favoured even at lower dilution rates.Correspondence to: N. Coello     

Purification and Characterization of a Fibrinogen-Degrading Protease in Bacteroides fragilis Strain YCH46

A novel fibrinogenolytic protease was purified from Bacteroides fragilis strain YCH46. The protease was extracted from cells by ultrasonic treatment and was purified 425-fold with a recovery of 2.1% by sequential procedures using azocasein as a substrate. The purified protease showed a single band on sodium dodecyl sulfate-polyacrylamide gel electrophoresis with an estimated molecular weight of 100 kDa, which was consistent with the value obtained by gel filtration, indicating a monomeric native structure. Its optimal pH, K_m, and V_max for azocasein were 7.5, 0.2%, and 286 U/min/mg, respectively. The protease activity was completely inhibited by addition of 1 mM Hg²⁺, Cu²⁺, Zn²⁺, diisopropyl fluorophosphate, N-ethylmaleimide or p-chloromercuribenzoate but not by the inhibitors of metalloprotease or aspartic protease, suggesting that the enzyme is a serine-thiol-like protease. The protease hydrolyzed azocasein, casein, fibrinogen, gelatin, and azocoll, but not bovine serum albumin, ovalbumin, fibrin, fibronectin, immunoglobulins, transferrin, hemoglobin or types I, III, and IV collagen. The enzyme also hydrolyzed the chromogenic substrates alanyl-alanine p-nitroanilide, L -valyl-alanine p-nitroanilide, alanyl-alanyl-valyl-alanine p-nitroanilide, and glycyl-proline p-nitroanilide, but was inert toward L -alanine p-nitroanilide, alanyl-alanyl-alanine p-nitroanilide, and N-α-benzoyl-DL -arginine p-nitroanilide. The protease completely hydrolyzed the α-chain of fibrinogen at 37 C within 10 hr and at the same time the time required for clotting of protease-treated fibrinogen by thrombin was prolonged. The fibrinogenolytic activity of a crude extract of B. fragilis was stronger than that of other species of the Bacteroides fragilis group tested: B. ovatus, B. distasonis, B. eggerthii, B. uniformis, and B. thetaiotaomicron. These results suggest that the fibrinogenolytic protease is an important biological factor in Bacteroides infection.     

Production of neutral and alkaline extracellular proteases by the thermophilic fungus, Scytalidium thermophilum, grown on microcrystalline cellulose

Extracellular proteases produced by Scytalidium thermophilum, grown on microcrystalline cellulose, were most active at pH 6.5–8 and 37–45 °C when incubated for 60 min. Highest protease activity was at day 3 where endoglucanase activity was low. Protease activity measurements with and without the protease inhibitors, p-chloromercuribenzoate, PMSF, antipain, E-64, EDTA and pepstatin A, suggest production of thiol-containing serine protease and serine proteases. Endoglucanase and Avicel-adsorbable endoglucanase activity in culture medium was not significantly affected by protease inhibitors.     

Isolation and characterization of five serine proteases with trypsin-, chymotrypsin- and elastase-like characteristics from the gut of the lugworm Arenicola marina (L.) (Polychaeta)

Summary Five proteases were isolated from the digestive fluid of the lugworm, Arenicola marina L. The enzymes (molecular weight 24.0–24.6 kDa) were classified as serine proteases. Three enzymes showed a cleavage specificity corresponding to mammalian trypsin (E.C. 3.4.21.4). One protease possessed a chymotrypsin-like cleavage pattern (E.C. 3.4.21.1), and the fifth preferred cleavage behind short-chain amino acids like an elastase (E.C. 3.4.21.36). Detailed investigations revealed differences in molecular characteristics and cleavage patterns compared to mammalian proteases, especially in the chymotrypsin- and the elastase-like enzymes.Abbreviations APNE N-acetyl-d/l-Phe -naphthyl ester - BANA N-benzoyl-d/l-Arg -naphthylamide - BAPNA N-benzoyl-d/l-Arg-4-nitroanilide - BIGGANA N-benzoyl-l-Ile-l-Glu-Gly-l-Arg-4-nitroanilide - BLPNA N-benzoyl-d/l-Lys-4-nitroanilide - BTEE N-benzoyl-l-Tyr ethyl ester - enzyme T1/T2/T3 trypsin-like enzyme - enzyme ChT chymotrypsin-like enzyme - enzyme E elastase-like enzyme - GPANA N-glutaryl-l-Phe-4-nitroanilide - MUF 4-methylumbelliferryl - MW molecular weight - PMSF phenylmethylsulphonyl fluoride - SAAPPNA N-succinyl-l-Ala-l-Ala-l-Pro-l-Phe-4-nitroanilide - SBTI soybean trypsin inhibitor - SPPNA N-succinyl-l-Phe-4-nitroanilide - TAME N-tosyl-l-Arg methyl ester - TFA trifluoracetic acid - TLCK N-tosyl-l-Lys chloromethyl ketone - TPCK N-tosyl-l-Phe chloromethyl ketone - TRIS tris(hydroxymethyl)aminomethane     

Effect of culture conditions on astaxanthin production by a mutant of Phaffia rhodozyma in batch and chemostat culture

Temperature and pH had only a slight effect on the astaxanthin content of a Phaffia rhodozyma mutant, but influenced the maximum specific growth rate and cell yield profoundly. The optimum conditions for astaxanthin production were 22°C at pH 5.0 with a low concentration of carbon source. Astaxanthin production was growth-associated, and the volumetric astaxanthin concentration gradually decreased after depletion of the carbon source. The biomass concentration decreased rapidly during the stationary growth phase with a concomitant increase in the cellular content of astaxanthin. Sucrose hydrolysis exceeded the assimilation rates of D-glucose and D-fructose and these sugars accumulated during batch cultivation. D-Glucose initially delayed D-fructose uptake, but D-fructose utilization commenced before glucose depletion. In continuous culture, the highest astaxanthin content was obtained at the lowest dilution rate of 0.043 h^–1. The cell yield reached a maximum of 0.48 g cells·g^–1 glucose utilized between dilution rates of 0.05 h^–1 and 0.07 h^–1 and decreased markedly at higher dilution rates. Correspondence to: J. C. Du Preez     

Development of a continuous system for the degradation of a cyanuric acid by adsorbed Pseudomonas sp. NRRL B-12228

Cyanuric acid in high concentrations (15.5 mm) was degraded completely by Pseudomonas sp. NRRL B-12228 independently of glucose concentration. In the batch fermentations there was a relation between the glucose concentration, on the one hand, and the liberation of ammonia or production of protein, on the other. The greater the supply of carbon, the more biomass was produced, and fewer NH _inf4 ^sup+ ions were released. Continuous fermentations using adsorbed cells could be performed to degrade cyanuric acid. In spite of different glucose feeding there was only a negligible difference in residues of s-triazine. In a one-step continuous system with dilution rates between 0.021 h^–1 and 0.035 h^–1, even a ratio of 0.65 between glucose and cyanuric acid was not sufficient to degrade the cyanuric acid supplied (320–540 mol l^–1 h^–1) completely. When a continuous two-step system was applied with dilution rates between 0.035 h^–1 and 0.056 h^–1, the consumption of carbon source could be minimized while s-triazine degradation up to 860 mol l^–1 h^–1 was complete. In this way the ratio between glucose and cyanuric acid could be increased to 0.25 (molar C:N ratio = 0.33:1). Thereby the process was made considerably more economic.     

Allelic expression in intergeneric fox hybrids (Alopex lagopus × Vulpes vulpes). II. Erythrocyte glucose-6-phosphate dehydrogenase in arctic and silver foxes: Purification and properties

The functional properties of purified glucose-6-phosphate dehydrogenase (G6PD) from the erythrocytes of Arctic foxes (Alopex lagopus) and silver foxes (Vulpes vulpes) were investigated. It was found that pH optima for G6PD range from 8.15 to 8.25 in Arctic foxes and from 10.2 to 10.4 in silver foxes. For G6P, the estimated K _m values were 74×10^–6 m (at pH 8.2) and 166×10^–6 m (at pH 10.2) in Arctic foxes and 58×10^–6 m (at pH 10.2) and 40×10^–6 m (at pH 8.2) in silver foxes. The K _m values for NADP were estimated as 62×10^–6 m (at pH 8.2) and 86×10^–6 m (at pH 10.2) in the Arctic foxes and 15×10^–6 m (at pH 10.2) and 12×10^–6 m (at pH 8.2) in the silver foxes. It was found that Mg²⁺ ions exert a significant activating effect on G6PD in the Arctic fox and do not affect appreciably its activity in the silver fox. The experimental data indicate that slight differences in the electrophoretic mobility of G6PD are associated with considerable functional differences in this enzyme between the two fox species.     

Improvement of a useful enzyme (subtilisin BPN′) by an experimental evolution system

In order to improve a natural enzyme so as to fit industrial purposes, we have applied experimental evolution techniques comprised of successive in vitro random mutagenesis and efficient screening systems. Subtilisin BPN, a useful alkaline serine protease, was used as the model enzyme, and the gene was cloned to an Escherichia coli host-vector system. Primary mutants with reduced activities of below 80% of that of the wild type were first derived by hydroxylamine mutagenesis directly applied to subtilisin gene DNA, followed by screening of clear-zone non-forming transformant colonies cultured at room temperature on plates containing skim-milk. Then, secondary mutants were derived from each primary mutant by the same mutagenic procedure, but screened by detecting transformant colonies incubated at 10°C with clear zones that were greater in size than that of the wild type. One such secondary mutant, 12–12, derived from a primary mutant with 80% activity, was found to gain 150% activity (k _cat/K _m value) of the wild-type when the mutant subtilisin gene was subcloned to a Bacillus subtilis host-vector system, expressed to form secretory mutant enzyme in the medium, and the activity measured using N-succinyl-l-Ala-l-Ala-l-Pro-l-Phe-p-nitroanilide as the substrate. When N-succinyl-l-Ala-l-Ala-l-Pro-l-Leu-p-nitroanilide was used, 180% activity was gained. Genetic analysis revealed that the primary and secondary mutations corresponded to D197N and G131D, respectively. The activity variations found in these mutant subtilisins were discussed in terms of Ca²⁺-binding ability. The thermostability was also found to be related to the activity.     

Development of an immobilized cell reactor for the production of 1,3-propanediol by Citrobacter freundii

Citrobacter freundii DSM 30040 immobilized on modified polyurethane carrier particles PUR 90/16 was used for continuous glycerol fermentation in an anaerobic fixed bed reactor with effluent recycle and pH control (fixed bed loop reactor). The fermentor was run with buffered mineral medium under growth conditions resulting in the permanent renewal of active biomass. The effects of glycerol concentration in the feed, dilution rate (D), pH and temperature (T) were investigated to optimize the process. With 400 mm glycerol in the feed, pH 6.9, T = 36°C and D = 0.5 h^–1 the maximum productivity could be determined as 8.2 g/l per hour of 1,3-propanediol.     

Fermentation of glycerol to 1,3-propanediol in continuous cultures of Citrobacter freundii

The conversion of glycerol to 1,3-propanediol by Citrobacter freundii DSM 30040 was optimized in single- and two-stage continuous cultures. The productivity of 1,3-propanediol formation was highest under glycerol limitation and increased with the dilution rate (D) to a maximum of 3.7 g·l^–1·h^–1. Glycerol dehydratase seemed to be the rate-limiting step in 1,3-propanediol formation. Conditions for the two-stage fermentation process were as follows: first stage, glycerol limitation (250mM), pH 7.2, D=0.1 h^–, 31° C; second stage, additional glycerol, pH 6.6, D=0.05 h^–1, 28° C. Under these conditions 875mM glycerol were consumed, the final 1,3-propanediol concentration was 545mM, and the overall productivity 1.38 g·1^–1·h^–1. Correspondence to: G. Gottschalk     

Characterisation of kinetic parameters and metabolic transition of Corynebacterium glutamicum on l-lysine production in continuous culture

Kinetic parameters and physiological states of Corynebacterium glutamicum at the growing and l-lysine-overproducing phase were characterised in continuous culture on threonine-limited complex and minimal media. High l-lysine productivity occurred at dilution rates ranging from 0.1 h^–1 to 0.3 h^–1 on threonine-limited complex medium, and at dilution rates ranging from 0.1 h^–1 to 0.15 h^–1 in minimal medium. l-Lysine yields of 0.25 g/g (0.31 g/g as l-lysine hydrochloride) in complex medium, and of 0.17 g/g (0.21 g/g as l-lysine hydrochloride) in minimal medium, corresponding respectively to intrinsic yields of 0.533 g/g and 0.572 g/g were obtained. These intrinsic yield factors are closed to the theoretical ones (0.608 g/g, 0.75 mol/mol). Intrinsic biomass yields were calculated as 0.658 g/g in complex medium and 0.283 g/g in minimal medium. CO₂ production has been clearly related to l-lysine production. According to our results on specific uptake rates and specific productivities in complex medium, metabolic rearrangement should occur during the transition from the growing phase to the l-lysine-overproducing phase. This phenomenon was further investigated.     

Selection of sulphur sources for the growth of Butyribacterium methylotrophicum and Acetobacterium woodii

Sulphide and cysteine inhibited growth of batch cultures of Butyribacterium methylotrophicum at moderate concentrations (above 0.5 mM) during growth on glucose (10 mM). The ability of several sulphur sources to replace sulphide was tested in cultures of B. methylotrophicum or Acetobacterium woodii. With sulphite (1 mM), thiosulphate (0.5 mM), elemental sulphur, and dithionite (1 mM), but not sulphate (1 mM), cultures of both organisms grew and produced some sulphide. With elemental sulphur as the sulphur source, toxic levels of sulphide accumulated. Optimal levels for the cultivation of B. methylotrophicum with sulphite were 0.5–2.0 mM, but at higher concentrations the growth rate decreased rapidly, while with dithionite up to 4.0 mM the growth rate was relatively unaffected. In chemostat cultures of B. methylotrophicum with dithionite (1 mM) as the sulphur source and glucose as the limiting substrate, dilution rates up to 0.40 h^–1 were obtained. Thiosulphate could only be used in batch cultures in combination with the reductant titanium(III)nitriloacetate, but in continuous cultures the addition of the reductant to the reservoir was not necessary, because once growth had started enough sulphide was produced to keep the fermentor reduced. The maximum growth rate of B. methylotrophicum with thiosulphate in batch and continuous culture was 0.26 h^–1. Both thiosulphate and dithionite are more convenient sulphur sources than sulphide, but dithionite is more versatile because of its reductive properties and the faster growth it allows.Offprint requests to: T. A. Hansen     

Isolation and characterization of a new keratinolytic Bacillus licheniformis strain

A keratin-degrading bacterium strain (K-508) was isolated from partially degraded feathers and characterized. This isolate exhibited a high chicken feather-degrading activity when cultured in feather-containing broth with a growth optimum of pH 7.0 and 47 °C. On the basis of its phenotypic characteristics (quickly moving, Gram-positive rods), the results of metabolic tests and rDNA sequence analysis, it was identified as Bacillus licheniformis. Its fermentation broth showed activity on N-Bz-l-Phe-l-Val-l-Arg-p-nitroanilide, N-Suc-l-Ala-l-Ala-l-Pro-l-Phe-p-nitroanilide, N-CBZ-Gly-Gly-l-Leu-p-nitroanilide and N-CBZ-l-Ala-l-Ala-l-Leu-p-nitroanilide as chromogenic protease substrates at near neutral pH. Both trypsin-like and chymotrypsin-like proteases were constitutively secreted by this strain.     

Purification and characterization of a trypsin-like enzyme with fibrinolytic activity present in the abdomen of horn fly, Haematobia irritans irritans (Diptera: Muscidae)

This work describes the purification and characterization of a trypsin-like enzyme with fibrinolytic activity present in the abdomen of Haematobia irritans irritans (Diptera: Muscidae). The enzyme was purified using a one-step process, consisting of affinity chromatography on SBTI-Sepharose. The purified protease showed one major active proteinase band on reverse zymography with 0.15% gelatin, corresponding to a molecular mass of 25.5 kDa, with maximum activity at pH 9.0. The purified trypsin-like enzyme preferentially hydrolyzed synthetic substrates with arginine residue at the P1 position. The K _m values determined for three different substrates were 1.88 × 10^–4, 1.28 × 10^–4, and 1.40 × 10^–4 M for H--benzoyl-Ile-Glu-Gly-Arg-p-nitroanilide (S2222), dl-Ile-Pro-Arg-p-nitroanilide (S2288), and DL-Phe-Pip-Arg-p-nitroanilide (S2238), respectively. The enzyme was strongly inhibited by typical serine proteinase inhibitors such as SBTI (soybean trypsin inhibitor, K _i = 0.19 nM) and BuXI (Bauhinia ungulata factor Xa inhibitor, K _i = 0.48 nM), and less inhibited by LDTI (leech-derived tryptase inhibitor, K _i = 1.5 nM) and its variants LDTI 2T and 5T (0.8 and 1.5 nM, respectively). The most effective inhibitor for this protease was r-aprotinin (r-BPTI) with a K _i value of 39 pM. Synthetic serine protease inhibitors presented only weak inhibition, e.g., benzamidine with K _i = 3.0 × 10^–4 M and phenylmethylsulfonyl fluoride (PMSF) showed traces of inhibition. The purified trypsin-like enzyme also digested natural substrates such as fibrinogen and fibrin net. The protease showed higher activity against fibrinogen and fibrin than did bovine trypsin. These data suggest that the proteolytic enzyme of H. irritans irritans is more specific to proteins from blood than are the vertebrate digestive enzymes. This enzyme's characteristics may be an adaptation resulting from the feeding behavior of this hematophagous insect.     

Nitrite uptake by Chlamydomonas reinhardtii cells immobilized in calcium alginate

When an initial cell loading of about 30–40 µg chlorophyll (Chl)·g^–1 gel and alginate suspension of 3% (w/v) were used for immobilization of Chlamydomonas reinhardtii, the resulting cell beads showed optimum nitrite uptake rate, at 30° C and pH 7.5, of 14 µmol NO _inf2 ^sup– ·mg^–1 Chl·h^–1, the photosynthetic and respiratory activities being about 120 µmol O₂ produced·mg^–1 Chl·h^–1, and 40 µmol O₂ consumed ·mg^–1 Chl·h^–1, respectively. The nitrite uptake activity required CO₂ in the culture and persisted after 8 days of cells immobilization, or in the presence of 0.2 mm ammonium in the medium. Our data indicate that alginate-entrapped C, reinhardtii cells may provide a stable and functional system for removing nitrogenous contaminants from waste-waters.Correspondence to: C. Vílchez     

The role of carbon dioxide in glucose metabolism of Bacteroides fragilis

The effect of CO₂ concentration on growth and glucose fermentation of Bacteroides fragilis was studied in a defined mineral medium. Batch culture experiments were done in closed tubes containing CO₂ concentrations ranging from 10% to 100% (with appropriate amounts of bicarbonate added to maintain the pH at 6.7). These experiments revealed that CO₂ had no influence on growth rate or cell yield when the CO₂ concentration was above 30% CO₂ (minimum available CO₂–HCO ₃ ^- , 25.5 mM), whereas a slight decrease in these parameters was observed at 20% and 10% CO₂ (available CO₂–HCO ₃ ^- , 17 and 8.5 mM, respectively). If CO₂–HCO ₃ ^- concentrations were below 10 mM, the lag phase lengthened and a decrease in maximal growth rate and cell yield were observed. The amount of acetate made decreased, while d-lactate concentration increased. A net production of CO₂ allowed growth under conditions of extremely low concentrations of added CO₂.When B. fragilis was grown in continuous culture with 100% CO₂ or 100% N₂, the dilution rate influenced the concentrations of acetate, succinate, propionate, d-lactate, l-malate and formate formed. Decreasing the dilution rate favored propionate and acetate production under both conditions. When the organism was grown with 100% N₂, the amount of propionate formed was greater than the amount of succinate formed at all dilution rates. Except at slow dilution rates the reverse was true when 100% CO₂ was used. B. fragilis was unable to grow at dilution rates faster than 0.154 h^-1 when grown with 100% N₂; the Y _glc ^max was 67.9 g DW cells/mol glucose and m _s was 0.064 mmol glucose/g DW·h. If the gas atmosphere was 100% CO₂ the organism was washed out of the culture when the dilution rate exceeded 0.38 h^-1; the Y _glc ^max was 59.4 g DW cells/mol glucose and m _s was 0.094 mmol glucose/g DW·h.Measurement of the phosphoenolpyruvate (PEP) carboxykinase (E.C. 4.1.1.49) with whole, permeabilized cells of B. fragilis showed an increase of specific enzyme activity with decreasing CO₂ concentrations. The mechanisms used by B. fragilis to adjust to low levels of CO₂ are discussed.     

Molecular and biochemical characterization of an extracellular serine-protease from <Emphasis Type="Italic">Vibrio metschnikovii</Emphasis> J1

A protease-producing bacterium was isolated from an alkaline wastewater of the soap industry and identified as Vibrio metschnikovii J1 on the basis of the 16S rRNA gene sequencing and biochemical properties. The strain was found to over-produce proteases when it was grown at 30°C in media containing casein as carbon source (14,000 U ml⁻¹). J1 enzyme, the major protease produced by V. metschnikovii J1, was purified by a three-step procedure, with a 2.1-fold increase in specific activity and 33.3% recovery. The molecular weight of the purified protease was estimated to be 30 kDa by SDS-PAGE and gel filtration. The N-terminal amino acid sequence of the first 20 amino acids of the purified J1 protease was AQQTPYGIRMVQADQLSDVY. The enzyme was highly active over a wide range of pH from 9.0 to 12.0, with an optimum at pH 11.0. The optimum temperature for the purified enzyme was 60°C. The activity of the enzyme was totally lost in the presence of PMSF, suggesting that the purified enzyme is a serine protease. The kinetic constants K _m and K _cat of the purified enzyme using N-succinyl-l-Ala-l-Ala-l-Pro-l-Phe-p-nitroanilide were 0.158 mM and 1.14 × 10⁵ min⁻¹, respectively. The catalytic efficiency (K _cat /K _m) was 7.23 × 10⁸ min⁻¹ M⁻¹. The enzyme showed extreme stability toward non-ionic surfactants and oxidizing agents. In addition, it showed high stability and compatibility with some commercial liquid and solid detergents. The aprJ1 gene, which encodes the alkaline protease from V. metschnikovii J1, was isolated, and its DNA sequence was determined. The deduced amino acid sequence of the preproenzyme differs from that of V. metschnikovii RH530 detergent-stable protease by 12 amino acids, 7 located in the propeptide and 5 in the mature enzyme.