Subcellular distribution of alkalophilic Bacillus penicillinase produced by Escherichia coli HB101 carrying pEAP31

Summary The extracellular production of alkalophilic Bacillus penicillinase by Escherichia coli HB101 carrying pEAP31 was dependent on the cultivation temperature. Extracellular production occurred only above 26°C. The penicillinase produced by the organism grown at lower temperatures accumulated in the periplasm of the cells. At high temperature, the penicillinase accumulated transiently in the periplasm and then was released gradually from the cells. The penicillinase that accumulated in the periplasm of the organism grown at low temperature could also be released by shifting to a high temperature.     

Optimization of cellulase production in batch fermentation byTrichoderma reesei

Maximum cellulase production was sought by comparing the activities of the cellulases produced by differentTrichoderma reesei strains andAspergillus niger. Trichoderma reesei Rut-C30 showed higher cellulase activity than otherTrichoderma reesei strains andAspergillus niger that was isolated from soil. By optimizing the cultivation condition during shake flask culture, higher cellulase production could be achieved. The FP (filter paper) activity of 3.7 U/ml and CMCase (Carboxymethylcellulase) activity of 60 U/ml were obtained from shake flask culture. When it was grown in 2.5L fermentor, where pH and DO levels are controlled, the Enzyme activities were 133.35 U/ml (CMCase) and 11.67 U./ml (FP), respectively. Ammonium sulfate precipitation method was used to recover enzymes from fermentation broth. The dried cellulase powder showed 3074.9 U/g of CMCase activity and 166.7 U/g of FP activity with 83.5% CMCase recovery.     

Optimum Culture Conditions for Production of Exfoliative Toxin by Staphylococcus hyicus

Optimum culture conditions for the production of exfoliative toxin by Staphylococcus hyicus (shET) were examined. High shET activity was obtained from the culture filtrate of HI and TY broth inoculated with S. hyicus. The pH in these two media ranged from 7 to 8.5 during bacterial culture, while the lowest pH in TS and BHI broth was less than 6. shET activity in the culture filtrate from TY broth inoculated with 10⁷ CFU of S. hyicus per ml was higher than that in TY broth inoculated with 10⁶ and 10⁸ CFU of bacteria per ml. When shET activity in the culture filtrate was measured under various shaking conditions, the culture filtrate shaken at 75 oscillations per min had the highest shET activity of the five shaking conditions. shET activity of the culture filtrate of TY broth to which protease inhibitor had been added was the same as that of TY broth without inhibitor. shET activity in a shaking culture in an Erlenmeyer flask was also the same as that in sac culture and that in shaking culture using a shaking (Sakaguchi) flask. shET activity in TY broth supplemented with 100 mM glucose was significantly lower than that in TY broth without glucose. Based on the above results, the optimum culture conditions for the production of shET were as follows: inoculation of 3 × 10⁹ CFU of S. hyicus strain P-1 into 300 ml of TY broth in a 2,000-ml Erlenmeyer flask, and incubation at 37 C with shaking at 75 oscillations per min. Then shET activity of the culture filtrate under appropriate culture conditions was measured after various incubation periods. shET activity was detected 6 hr after inoculation, reached the maximum (2⁵³ exfoliative unit/0.1 ml) at 16 hr and decreased between 20 and 48 hr. Thus, the optimum incubation period was determined to be 16 hr. Then the optimum concentration of ammonium sulfate for isolation of shET from the culture filtrate under appropriate culture conditions was examined. The greatest shET activity was obtained from the fraction salted out with 90% saturated ammonium sulfate. Thus, the optimum concentration of ammonium sulfate for the isolation of shET was determined to be 90% saturation.     

An Improved Method for the Fermentative Production of Coenzyme A from Pantothenic Acid,Cysteine, and 5′-AMP

The cultivation of Brevibacterium ammoniagenes IFO 12071 with pantothenic acid, cysteine, and 5′-adenylic acid gave coenzyme A in a high yield. The organism was stabilized by repeated single colony isolations. The culture conditions optimal for the production of coenzyme A were investigated, and the yield of coenzyme A in the culture broth reached more than 3 mg/ml.

The advantages and disadvantages of the present method were discussed by comparing them with our original dried cell method.     

Influence of culture conditions on thermostable lipase production by a thermophilic alkalitolerant strain ofBacillus sp

The effect of different culture conditions on thermostable lipase production byBacillus sp. was studied in shake flasks. A maximum enzyme activity of 67–75 nkat/mL was observed in a medium consisting of 0.5% soybean flour and 0.1% stearyl glycerol esters or natural fats. A lipase activity of about 117 nkat/mL was established when the cultivation was carried out in laboratory fermentor at 20% minimal dissolved oxygen level, the enzyme production being increased 1.5 fold compared to that in a flask culture.     

Construction of new excretion vectors: two and three tandemly located promoters are active for extracellular protein production from Escherichia coli

Summary In order to develop a more useful system for extracellular protein production from Escherichia coli, we have constructed the new excretion vectors pEAP82-1, pEAP82-2, and pEAP82-3. These vectors have, respectively, a single, double, and triple penicillinase promoter upstream of a penicillinase structural gene; E. coli HB101 carrying pEAP82-2 or pEAP82-3 produced respectively, about twice or three times as much penicillinase protein than that produced by E. coli carrying pEAP82-1, and 70% to 80% of the protein was excreted into the culture medium. The E. coli carrying pEAP82-3 was cultivated at various temperatures and it was observed that the optimum for extracellular penicillinase production was 30°–37°C. Using this multi-promoter excretion system, the amount of extracellular production of human growth hormone was increased by several fold as observed with penicillinase excretion.     

Effects of agitation and aeration on the production of extracellular glucose oxidase from a recombinant Saccharomycescerevisiae

A recombinant strain of Saccharomyces cerevisiae, GAL-GO2, was developed to facilitate the production of extracellular glucose oxidase (GOD). The recombinant strain secreted 85% (8.7?U/ml) of the total GOD (10.3?U/ml) produced in shake flask culture. For further enhancement of GOD production, optimization of the speed of agitation and the rate of aeration in a stirred tank fermentor was carried out. Response surface methodology with appropriate statistical experimental design was employed for this purpose. The maximal level of extracellular GOD was achieved when the speed of agitation and the rate of aeration were 420?rpm and 0.25?vvm, respectively. The enzyme production was increased by 74% compared to the level obtained under unoptimized conditions.     

Detection of extracellular proteinase of Pseudomonas fragi by enzyme-linked immunosorbent assay

A double-antibody-sandwich, enzyme-linked immunosorbent assay was developed to detect an extracellular proteinase produced by Pseudomonas fragi. The method was capable of detecting 4 g/ml of the proteinase in spiked samples of buffer and broth and 4.2 g/ml in a broth culture of the organism. The assay detected the presence of proteinase at bacterial densities of approximately 10⁴ cfu/ml, which develop after incubation for 15 h at 25°C in a broth medium. All assays could be completed within 7 h. This assay is of value in plotting proteolytic expression in relation to the growth cycle of Ps. fragi in broth culture and may be of value, with development, in other more complex milieux.     

The Effect of Fungal Morphology on Ligninolytic Enzyme Production by a Recently Isolated Wood-Degrading Fungus Trichophyton Rubrum LSK-27

The morphology and ligninolytic enzyme production of a recently isolated wood-degrading fungus Trichophyton rubrum LSK-27 was investigated. In submerged cultures, the organism appeared to be an efficient manganese peroxidase (MnP) producer. When grown in baffled and unbaffled shake flasks with three different working volume/total volume ratios (WV/TV 10, 25 and 50%), the organism displayed notable morphological differences, with variations in pellet shape and size. Cultivation in baffled flasks with 25% WV/TV resulted in higher MnP and also laccase production as well as an earlier appearance of these enzymes in culture broth. However, oxygen limitation conditions inhibited MnP and laccase production and resulted in considerable changes in the morphology of this fungus.     

Optimization of protein-production by the baculovirus expression vector system in shake flasks

Summary Shake flasks were successfully employed for the cultivation of Spodoptera frugiperda (Sf-9) insect cells and for the production of \-galactosidase, a recombinant model protein, utilizing the baculovirus expression vector system. The culture doubling time and maximal cell density were 20 h and 5 × 10⁶ cells/ml respectively. The optimal liquid volumes for flasks rotating at 100 rpm were 25–40% of the flask total volume. Enzyme production (about 600 mg/l) was best at a multiplicity of infection of between 1 and 20 and at a cell density at time of infection of 0.7 × 10⁶ cells/ml. At a rotation speed of 100 rpm, Pluronic F-68 had no effect on growth and enzyme production. Offprint requests to: Y. Shoham     

Large Scale Production and Crystallization of Acid Carboxypeptidase from Submerged Culture of Penicillium janthinellum,and Stability of the Crystalline Enzyme

Acid carboxypeptidase of Penicillium janthinellum IFO–8070 was produced effectively in submerged culture on a medium of 4 ~ 5% rice bran. The enzyme production was enlarged to volume cultivation of 150-liters in a 200-liters jar fermentor, and the yield of acid carboxypeptidase per milliliter filtrate reached to the maximum 3 days after inoculation.

Acid carboxypeptidase of low molecular weight (M.W. = 51,000) produced in the liquid culture broth was purified and crystallized in a large scale. Purification steps include Amberlite CG–50 treatment, ammonium sulfate precipitation, dialysis using “Diaflow,” activated charcoal treatment, and condensation using collodion-bag, or condensation and dialysis using “Diaflow.”

The crystals of the acid carboxypeptidase suspended in 50 mm acetate buffer (pH 3.7) were completely stable for six months at 5°C. On the other hand, at low enzyme concentration (0.01 U/ml) in 50 mm acetate buffer (pH 3.7), crystallized enzyme was somewhat labile, whereas, this inactivation was completely depressed by covering enzyme solution with toluene.     

Repeated batch production of alkaline protease by solid-state fermentation using urethane foam as carriers

By immobilizing fungi on a urethane foam carrier (UFC), a novel solid-state fermentation system was developed in order to produce repeatedly industrial useful enzymes. In this study, alkaline protease was produced by growing Aspergillus oryzae 460 (ATCC 20386) in a flask scale. Repeated batch production of alkaline protease was carried out by exchanging a part of the culture broth with fresh medium every 12 hr. The effects of feeding medium composition, and feeding volume were examined. Alkaline protease production stopped in the early phase at high values of soluble starch feeding rate and culture broth dilution rate. The enzyme production continued longer when 10 to 30 g/l polypepton was added to the feeding medium. Using soluble starch solution as feeding medium, a maximum activity of 520,000 U/l-bulk volume alkaline protease was obtained at culture time of 168 hr where the culture conditions of soluble starch concentration and feeding volume were 100 g/l and 0.025 l/l-bulk volume/dose, respectively. Production of the enzyme continued for 300 hr and total aklaline protease activity reached 870,000 U/l-bulk volume by adding 30 g/l polypepton to the fresh medium.     

Production of a Gaseous Saturated-hydrocarbon Mixture by Rhizopus japonicus under Aerobic Conditions

The microbial production, by the genus Rhizopus, of a gaseous saturated-hydrocarbon mixture was studied under aerobic conditions. Rhizopus strains, comprising 13 strains of 9 species, were tested as to their ability to produce a gaseous hydrocarbon mixture. Except for one strain, all the strains tested produced more than two kinds of gaseous hydrocarbons simultaneously when grown in nutrient broth containing glucose. Rhizopus japonicus IFO 4758 was selected as being typical of these producers of mixed gaseous hydrocarbons. When this organism was cultivated in a synthetic medium supplemented with l-cysteine under aerobic conditions, the maximum production of the total gaseous hydrocarbon mixture reached ca. 10 nl/ml culture broth/hr. The gaseous hydrocarbon mixture produced was composed mainly of paraffin hydrocarbons, i.e., ca. 74% pentane, ca. 16% propane and a trace amount of methane. The ratios of saturated to unsaturated, and even to odd number hydrocarbons produced by this fungus were 95 : 5 and 90: 10, respectively. The biosynthetic pathways for the production of these gases are discussed in comparison with the biosynthetic pathways for ethylene and isobutene in microorganisms.     

Excretion of l-Tryptophan by Analogue-resistant Mutants of Pseudomonas hydrogenothermophila TH-1 in Autotrophic Cultures

Cells of a thermophilic hydrogen bacterium, Pseudomonas hydrogenothermophila TH-1 were treated with N-methyl-N′-nitro-N-nitrosoguanidine and resulting mutants resistant to tryptophan analogues were selected under autotrophic culture conditions (energy source, H₂; carbon source, CO₂). A mutant strain, 7922, which was resistant to 2000 µg/ml of 5-methyltryptophan and 200–500 µg/ml of 5-fluorotryptophan, was obtained by two step mutations. This mutant excreted 38–70 µg/ml of tryptophan into flask culture broth and a maximum of 200 µg/ml into jar fermentor broth.     

Improved laminaribiose phosphorylase production by <Emphasis Type="Italic">Euglena gracilis</Emphasis> in a bioreactor: A comparative study of different cultivation methods

Laminaribiose phosphorylase (EC 2.4.1.31) catalyzes a reversible phosphorolysis reaction in which laminaribiose, a very high value sugar is produced. This enzyme is not being produced commercially therefore, to realize the most effective method for producing laminaribiose phosphorylase and obtaining as much activity units as possible per liter of culture, different cultivation methods of Euglena gracilis were compared. Heterotrophic and mixotrophic cultivations of Euglena gracilis in two different pHs, in flask and bioreactor were performed. The reverse phosphorolysis activity of laminaribiose phosphorylase produced under different cultivation methods was measured. The heterotrophic approach showed to be the more effective cultivation method as 47.6 IU/L was obtained compared to 27 IU/L in the mixotrophic one. The heterotrophic cultivation then was further investigated under two different pH values of the culture media. The culture at pH 6.8 resulted in 7.94 IU/L/day whereas only 4.06 was obtained for the culture at pH 4. Cultivation in a bioreactor resulted in a distinctive amount of 191.5 IU/L and an activity yield of 9.7 IU/g glucose compared to 5.4 in flask cultivation. Heterotrophic cultivation of Euglena gracilis in a bioreactor containing a culture media at pH 6.8 and controlled operation conditions showed enhanced laminaribiose phosphorylase activity production per liter and day of cultivation.     

Overproduction of extracellular protease activity by Streptomyces C5-A13 in fed-batch fermentation

Summary Streptomyces C5-A13, a non-sporulating, pleiotropic mutant of the anthracycline-producing strain, Streptomyces C5, overproduces extracellular proteolytic activity against the substrate azocasein. This extracellular protease activity was produced primarily during the stationary phase. This appears to be an effect related to growth rate rather than to glucose repression, because only very high concentrations of glucose appear to inhibit protease synthesis. Production of extracellular protease activity was stimulated by the presence of carbonate anions in the medium. The optimal concentration of soluble carbonate was 60–80 mM and the stimulation by carbonate was shown not to be due to a pH effect. Approximately 3200–3500 units of extracellular azocaseinase activity were produced per millititre of culture broth using partially optimized fed-batch fermentation processes. This value represents about ninefold greater activity than produced under shake flask conditions.     

Production of Sophorolipids from Candida bombicola ATCC 22214 Using Turkish Corn Oil and Honey

The ability of Candida bombicola ATCC 22214 to produce sophorolipids using Turkish corn oil and honey was investigated. Shake flask experiments were carried out both with and without the addition of glucose as the second carbon source. The organism could produce sophorolipids under both conditions but higher production was obtained when corn oil was combined with glucose. The 3 L bioreactor was first operated in batch mode, using both corn oil and glucose. When all the glucose was consumed, ¹/₄th of the broth was pumped out and was replaced by freshly prepared medium containing 10 % [w/v] of cheap market honey as the sole carbon source. Feed was comprised of corn oil. High concentrations of sophorolipids (&#62; 400 g/L) were produced. The crude products obtained from the batch cultivation could be solidified as very light brown solids when unused oil was removed by hexane, while the products of the two‐stage cultivation remained as viscous, honey‐like liquids after identical treatments.     

Production of Glucose Isomerase by Streptomyces flavogriseus

A microorganism that produces glucose isomerase was isolated from soil and identified as a strain of Streptomyces flavogriseus. The organism produced a large quantity of glucose isomerase when grown on straw hemicellulose, xylan, xylose, and H₂SO₄ hydrolysate of ryegrass straw. The organism produced glucose isomerase both intra- and extra-cellularly. The highest level of intracellular glucose isomerase (3.5 U/ml) was obtained in about 36 h by a culture grown on straw hemicellulose; the extracellular enzyme (1.5 U/ml) appeared in cultures grown for about 72 h. About equal levels of enzyme were produced in cultures grown on straw hemicellulose, xylan, xylose, and H₂SO₄ hydrolysate of straw, but production of the enzyme was drastically reduced when the organism was grown on other carbon sources. As a nitrogen source, corn steep liquor produced the best results. Soy flour extract, yeast extract, and various peptones also were adequate substrates for glucose isomerase production. Addition of Mg²⁺, Mn²⁺, or Fe²⁺ to the growth medium significantly enhanced enzyme production. The organism, however, did not require Co²⁺, which is commonly required by microorganisms used in the production of glucose isomerase.     

Enhanced production of alkaline thermostable keratinolytic protease from calcium alginate immobilized cells of thermoalkalophilic Bacillus halodurans JB 99 exhibiting dehairing activity

The thermoalkalophilic Bacillus halodurans JB 99 cells known for production of novel thermostable alkaline keratinolytic protease were immobilized in calcium alginate matrix. Batch and repeated batch cultivation using calcium alginate immobilized cells were studied for alkaline protease production in submerged fermentation. Immobilized cells with 2.5% alginate and 350 beads/flask of initial cell loading showed enhanced production of alkaline protease by 23.2% (5,275 ± 39.4 U/ml) as compared to free cells (4,280 ± 35.4 U/ml) after 24 h. In the semicontinuous mode of cultivation, immobilized cells under optimized conditions produced an appreciable level of alkaline protease in up to nine cycles and reached a maximal value of 5,975 U/ml after the seventh cycle. The enzyme produced from immobilized cells efficiently degraded chicken feathers in the presence of a reducing agent which can help the poultry industry in the management of keratin-rich waste and obtaining value-added products.     

Alkaline inulinase production by a newly isolated bacterium Marinimicrobium sp. LS–A18 and inulin hydrolysis by the enzyme

To date, all of microbial inulinases reported showed optimal activity at pH values ranging from 3.5 to 7.0. A bacterial strain, Marinimicrobium sp. LS-A18, showing high extracellular inulinolytic activity was isolated from a marine solar saltern of the Yellow Sea in China. Maximum enzyme activity was obtained at 55°C and pH 9.0, respectively. The inulinase activity was induced by inulin, but not by the other carbon sources employed. Under the optimal medium and culture condition, the highest inulinase activity, 14.6 U/ml, was obtained after 96 h of incubation at shake flask level. The optimal medium for inulinase production was MHI medium containing 4% inulin, 1% peptone and 5% NaCl, while the optimal culture condition for inulinase production were pH 7.5, temperature 37°C, agitation speed 210 rpm, medium volume 40 ml in 250 ml shake flask, and incubation time 96 h. A large amount of monosaccharides was released after inulin hydrolysis by the inulinase from strain LS-A18. This is the first report on alkaline inulinase production from microorganism.