Analysis of penicillin V biosynthesis during fed-batch cultivations with a high-yielding strain of Penicillium chrysogenum

Metabolites (both intra- and extracellular) involved in penicillin biosynthesis were measured during fed-batch cultivations with a high-yielding strain of Penicillium chrysogenum. The fed-batch cultivations were carried out on a complex medium containing corn steep liqour. Three distinct phases were observed: (a) a rapid growth phase where free amino acids present in the medium are metabolized, (b) a linear growth phase, and (c) a stationary phase. The specific penicillin production (r _p) is initially high and, during the rapid growth phase, it increases slightly. During the linear growth phase r _p is approximately constant [4–6 mg penicillin V (g dry weight)^–1 h^–1 depending on the operating conditions], whereas it decreases during the stationary phase. During the cultivations the tripeptide Aad-Cys-Val (the first metabolite in penicillin biosynthesis) and 8-hydroxypenillic acid (formed by carboxylation of 6-aminopenicillanic acid, 6-APA) were found to accumulate in the medium, whereas the concentrations of isopenicillin N and 6-APA were found to be approximately constant and low. About 3% of the Aad-Cys-Val formed in the first step of the penicillin biosynthetic pathway is lost to the medium and 4% of the isopenicillin N formed in the second step of the pathway is lost as extracellular isopenicillin N, 6-APA or 8-hydroxypenillic acid. Also the cyclic form of -aminoadipic acid, 6-oxopiperidine-2-carboxylic acid, was found to accumulate in the medium and it was found to be formed in an approximately constant ratio to penicillin V of 6 mol/100 mol.     

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.     

Influence of temperature rise on kinetic parameters during batch propagation of Kluyveromyces fragilis in cheese whey under ambient conditions

Three 5 l working volume fermenters were used to investigate the growth of the yeast Kluyveromyces fragilis in acid cheese whey under ambient temperature in order to assess the specific growth rate and yield, the lactose and oxygen uptake rates during the various phases of batch culture, the effect of increasing temperature on the various kinetic parameters, and the need for a cooling unit for single cell production batch systems. The initial dissolved oxygen in the medium was 5.5 mg l^–1 and the pH was maintained at 4.5. The observed lag phase, specific growth rate and maximum cell number were 4 h, 0.2 h^–1 and 8.4 × 10⁸ cells ml^–1, respectively. About 99% of the lactose in cheese whey was utilized within 20 h, 85% during the exponential growth phase. The specific lactose utilization rates by K. fragilis were 0.20 × 10^–12, 1.457 × 10^–12, 0.286 × 10^–12 and 0.00 g lactose cell^–1 h^–1, for the lag, exponential, stationary and death phases, respectively. The dissolved oxygen concentration in the medium decreased as the cell number increased. The lowest oxygen concentration of 1.2 mg l^–1 was observed during the stationary phase. The volumetric oxygen transfer coefficient was 0.41 h^–1 and the specific oxygen uptake rates were 0.32 × 10^–12, 2.14 × 10^–12, 0.51 × 10^–12 and 0.003 × 10^–12 mg O₂ cell^–1 h^–1, for the lag, exponential, stationary and death phases, respectively. The maximum temperature recorded for the medium was 33 °C, indicating that a cooling unit for batch production of single cell protein at ambient temperature is not needed for this type of bioreactor. The increase in medium temperature affected the cell growth and the lactose and oxygen uptake rates.     

Kinetic characterization and fed-batch fermentation for maximal simultaneous production of esterase and protease from Lysinibacillus fusiformis AU01

The simultaneous production of intracellular esterase and extracellular protease from the strain Lysinibacillus fusiformis AU01 was studied in detail. The production was performed both under batch and fed-batch modes. The maximum yield of intracellular esterase and protease was obtained under full oxygen saturation at the beginning of the fermentation. The data were fitted to the Luedeking–Piret model and it was shown that the enzyme (both esterase and protease) production was growth associated. A decrease in intracellular esterase and increase in the extracellular esterase were observed during late stationary phase. The appearance of intracellular proteins in extracellular media and decrease in viable cell count and biomass during late stationary phase confirmed that the presence of extracellular esterase is due to cell lysis. Even though the fed-batch fermentation with different feeding strategies showed improved productivity, feeding yeast extract under DO-stat fermentation conditions showed highest intracellular esterase and protease production. Under DO-stat fed-batch cultivation, maximum intracellular esterase activity of 820?×?10³ U/L and extracellular protease activity of 172?×?10³ U/L were obtained at the 16th?hr. Intracellular esterase and extracellular protease production were increased fivefold and fourfold, respectively, when compared to batch fermentation performed under shake flask conditions.     

Effect of age on the membrane lipid composition of Streptococcus sanguis

The cell membrane of Streptococcus sanguis contains three classes of lipid: neutral lipid, glycolipid and phospholipid. A striking difference in membrane lipid composition between cells in the exponential and in the stationary phases of growth was observed. During the exponential phase, approx. 37–45%, 14–19% and 37–45% of the lipids synthesized were found to be neutral lipid, glycolipid and phospholipid, respectively. The amount of lipid synthesized reached a maximum at the early stationary phase. The amount of phospholipid drastically declined thereafter and that of neutral lipid slightly declined. In contrast, the amount of glycolipid markedly increased and exceeded the amount of phospholipid. The phospholipid present during the exponential phase was found to be mainly phosphatidylglycerol (82–88%) and a small amount of cardiolipin (12–18%). At the stationary phase, the amount of phosphatidylglycerol greatly decreased and reached approx. 16% of that in the early stationary phase, while cardiolipin steadily increased and became the major phospholipid in the late stationary phase. The glycolipid was found to be composed of mainly mono- and diglucosyldiglycerides. At the end of the experiment (after 8 h incubation), the distribution of lipids was found to be: neutral lipid, 46%; glycolipid (monoglucosyldiglyceride, 28%; diglucosyldiglyceride, 13%) 41%; and phospholipid (phosphatidylglycerol, 3%, cardiolipin, 8%) 13%.     

Nucleotide pool changes in coelomic cells (eleocytes) of the polychaete Nereis virens during sexual maturation

Eleocytes (a type of coelomic cell) of the polychaete Nereis virens can store large amounts of adenine nucleotides at certain times. Since eleocytes have specific functions related to gametogenesis, we tested whether the presence of these large nucleotide stores in eleocytes is specific to gender or related to specific events during gametogenesis. Nucleotide pools in eleocytes isolated at different stages of sexual maturation from N. virens were analysed using high-performance liquid chromatography. Eleocytes from immature and male animals had extremely high concentrations of both AMP and ADP (each > 10 μmol/ml of packed cell volume). In eleocytes from male animals, the high nucleotide stores were maintained throughout the maturation phase and decreased at a late stage, while in female animals the nucleotides were degraded at an early stage of maturation. In male eleocytes, the decrease in the adenine nucleotide pool may be the result of its conversion to inosine which is then released by the eleocytes and reutilized by male germ cells for nucleic acid biosynthesis, as has been suggested previously. Our study shows that the time of degradation of the adenine nucleotide pool coincides with the period of spermatogonia proliferation which involves intense nucleic acid synthesis. ATP levels (0.4–1.5 μmol/ml packed cell volume) and the guanine nucleotide pool (GTP+GDP+GMP; 0.08–0.18 μmol/ml packed cell volume) were similar in both sexes, did not change during germ cell development and were decreased only in eleocytes from prespawning females. The GTP/GDP ratios were initially higher (up to 14) in eleocytes from females compared to ratios in eleocytes from immature (4–9) and male animals (up to 8), and decreased during the maturation phase of the animals. GTP levels were correlated with those of ATP; this correlation was much closer in eleocytes from females than from males. The results further support the hypothesis that the adenine nucleotide stores in the eleocytes are maintained as a supply of purine precursors for the growing germ cells.     

Glucose and acetate influences on the behavior of the recombinant strainEscherichia coli HB 101 (GAPDH)

Summary This study highlights data about the production of a recombinant protein (glyceraldehyde-3-phosphate dehydrogenase) byE. coli HB 101 (GAPDH) during batch and fed-batch fermentations in a complex medium. From a small number of experiments, this strain has been characterized in terms of protein production performance and glucose and acetate influences on growth and recombinant protein production. The present results show that this strain is suitable for recombinant protein production, in fed-batch culture 55 g L^–1 of biomass and 6 g L^–1 of GAPDH are obtained. However this strain, and especially GAPDH overproduction is sensitive to glucose availability. During fermentations, maximum yields of GAPDH production have been obtained in batch experiments for glucose concentration of 10 g L^–1, and in fed-batch experiments for glucose availability of 10 g h^–1 (initial volume 1.5 L). The growth of the strain and GAPDH overproduction are also inhibited by acetate. Moreover acetate has been noted as an activator of its own formation.     

Characterization of protease production by a type-III group-BStreptococcus

A type-III group-B streptococcus (Streptococcus agalactiae) isolated from a case of late-onset sepsis was examined for protease production. In broth culture, extracellular proteolytic enzymes were not detected until the late exponential phase of growth with maximal protease production occurring during the stationary phase. Three distinct protease pools were isolated from the supernatant fluids of stationary-phase cultures, employing a combination of ion-exchange chromatography and gel-filtration chromatography. One population of proteases (containing two protease pools separable by gel filtration chromatography) eluted from a diethylaminoethyl cellulose column at a sodium chloride gradient concentration of 0.15M while a second population eluted from the same material at a sodium chloride concentration of 0.35M. These protease pools varied in molecular weights from approximately 25,000 daltons to 160,000 daltons as determined by gel filtration on Sephadex G-200. All three protease preparations had pH optima of 8.0–9.0, and all were active against gelatin, human serum albumin, and casein, but were not active against elastin or collagen. In addition, all three protease preparations completely inactivated purified type-III group-B streptococal neuraminidase. The role of these proteases in the disease process caused by the type-III group-B streptococci must remain speculative at this time.     

Primary metabolism of Aspergillus parasiticus in relation to aflatoxin biosynthesis

Summary The uptake of various ¹⁴C labelled compounds like (1-¹⁴C) glucose, (1-¹⁴C) acetate, (2-¹⁴C) uracil, (1-¹⁴C) leucine and (¹⁴C–CH₃) methionine was studied in Aspergillus parasiticus. A comparative study of asparagine deficient, zinc deficient and SLS cultures revealed different growth patterns. High lipid levels under zinc and asparagine deficiency were observed. During the stationary phase the synthesis of proteins and DNA declined. The uptake of ¹⁴C labelled glucose, methionine and acetate was maximum in asparagine deficient cultures during the transitional and stationary phase of growth. Maximum uptake of labelled methionine and glucose occured during the exponential growth phase (45 h). The uptake of labelled leucine was highest under asparagine deficiency during the exponential and transitional phases but reached a minimum during stationary phase. The uptake of labelled uracil remained high throughout in the asparagine deficient cultures. The mechanism of inhibition of aflatoxin biosynthesis in the absence of zinc and asparagine seems to be different.     

Protease production by Bacillus subtilis in oxygen-controlled,glucose fed-batch fermentations

Summary An open-loop, on-off control system using the dissolved oxygen level to control a glucose feed was used in a study of growth and production of protease by Bacillus subtilis CNIB 8054. With this system, both glucose and oxygen were controlled at low concentrations. In batch fermentations, protease activity in the fermentation broth was maximum when growth had stopped. During oxygen-controlled, glucose fed-batch fermentations, growth and the production of protease activity continued during glucose feeding. Oxygen-controlled, glucose fed-batch fermentations produced more protease activity than batch fermentations, depending upon the set point for dissolved oxygen. These results indicate that control of glucose and oxygen concentrations can result in improvements in protease production.     

Use of swimming speed and egg ratio as predictors of the status of rotifer cultures in aquaculture

This study evaluated the use of egg ratio (eggs rotifer^–1) and swimming speed (mm min^–1) as prediction criteria for production and culture quality in mass cultures of the rotifer Brachionus plicatilis. Egg ratio was determined to be a suitable predictor of rotifer growth and production in the cultures. Low egg ratios (i.e., 0–0.17 eggs rotifer^–1) indicate reduced rotifer population over time (i.e., negative net population growth rates). However, at this time egg ratio dynamics are not suitably understood to predict in advance a sudden population collapse.Swimming speed of reproductive, egg-carrying females in the exponential growth phase was 40–45 mm min^–1. During exponential growth swimming speed was independent of the food used. Lower swimming speeds were obtained in late stationary phase (10–25 mm min^–1) when yeast was used as a food source. Both environmental factors (e.g., accumulating metabolites) and changes in nutritional state of the rotifers may have affected the swimming speed, but environmental factors appear to be the most important. We believe that swimming speed has the potential of becoming an accurate predictor of culture quality in mass cultures of rotifers.     

Synthesis and release of proteases byBacteroides fragilis

Protease production byBacteroides fragilis ATCC 25285 was determined in batch and continuous cultures. During exponential growth in batch culture, the majority of proteolysis was cell associated. However, as the bacteria reached stationary phase, most of the intracellular proteases were released into the culture medium. Measurements of alkaline phosphatase and -galactosidase, which are respectively periplasmic and cytoplasmic marker enzymes inB. fragilis, showed that secretion of proteases in the stationary phase was a discrete event and was not associated with a general release of cytoplasmic contents. When the bacterium was grown in continuous culture, cell-associated protease activity increased concomitantly with dilution rate (D=0.03–0.23/h). The ratio of intracellular to whole cell protease activity also increased with growth rate (11 at D=0.03/h; 11.7 at D=0.23/h). Extracellular protease activity was detected only in trace amounts in continuous cultures at the lowest dilution rate. Determinations of the distribution of extracellular protease activity in batch culture after 48 h incubation showed that the majority of proteolysis (ca. 90%) was soluble. Nevertheless, a proportion was associated with particulate fractions, which had high specific activities.     

Feasibility study of exponential feeding strategy in fed-batch cultures for phenol degradation using Cupriavidus taiwanensis

An indigenous phenol-degrading bacterial isolate Cupriavidus taiwanensis R186 was used to degrade phenol from an aqueous solution under fed-batch operation. An exponential feeding strategy combined with dissolved oxygen control was applied based on kinetic characteristics of cell growth and phenol degradation to meet sufficient metabolic needs for cellular growth and achieve the best phenol removal efficiency. Without the stress of phenol inhibition, the optimal set point of specific growth rate of exponential feeding for fed-batch phenol degradation was found to be 0.50–0.55μ_max (μ_max denotes the maximum specific growth rate from Monod model). Meanwhile, the sufficient set point of dissolved oxygen for maximal phenol degradation efficiency was approximately at 10–55% air saturation. With the optimal operation conditions, the best phenol degradation rate was 0.213 g phenol h⁻¹, while a shortest treatment time of 15 h was achieved for complete degradation of 11.35 mM (ca. 3.20 g) of phenol.     

Acetate production byClostridium thermoaceticum in corn steep liquor media

A low-cost nutrient medium based on corn steep liquor (CSL) was developed for the production of acetates byClostridium thermoaceticum. Pre-treatment of CSL with dolime and vitamin supplementation increased the rate of acetate production. Adding excess nutrients in a fed-batch mode minimized by-product formation and increased final acetate concentration from 19 g L^–1 to 40 g L^–1 acetic acid. High yields of acetic acid (0.95 g g^–1 glucose in fed-batch mode) was probably due to the conversion of the lactic acid in CSL into acetic acid by the organism.     

Influence of culture modes on the microbial production of hyaluronic acid by <Emphasis Type="Italic">Streptococcus zooepidemicus</Emphasis>

The principal objective of this study was to assess the effects of culture modes including batch culture, pulse fed-batch culture, constant feeding rate fed-batch culture, and exponential fed-batch culture on the production of hyaluronic acid (HA) by Streptococcus zooepidemicus. Batch cultures had the highest levels of HA productivity, whereas fed-batch cultures were more favorable with regard to cell growth, and exponential fed-batch cultures evidenced the highest cell concentrations. A two-step culture model was proposed to enhance HA production: an exponential fed-batch culture was conducted prior to 8 h and then sucrose supplementation was applied for 8 h to start the batch fermentation of S. zooepidemicus. HA production and productivity were increased by 36 and 37% in the proposed two-step culture process as compared with that observed in the batch culture, respectively. The proposed two-step culture model can be applied in the production of secondary metabolites, and particularly of the exopolysaccharides.     

Adaptation of methane formation and enzyme contents during growth of Methanobacterium thermoautotrophicum (strain ΔH) in a fed-batch fermentor

During growth of Methanobacterium thermoautotrophicum in a fed-batch fermentor, the cells are confronted with a steady decrease in the concentration of the hydrogen energy supply. In order to investigate how the organism responds to these changes, cells collected during different growth phases were examined for their methanogenic properties. Cellular levels of the various methanogenic isoenzymes and functionally equivalent enzymes were also determined. Cells were found to maintain the rates of methanogenesis by lowering their affinity for hydrogen: the apparent K _m ^H2 decreased in going from the exponential to the stationary phase. Simultaneously, the maximal specific methane production rate changed. Levels of H₂-dependent methenyl-tetrahydromethanopterin dehydrogenase (H₂-MDH) and methyl coenzyme M reductase isoenzyme II (MCR II) decreased upon entry of the stationary phase. Cells grown under conditions that favored MCR II expression had higher levels of MCR II and H₂-MDH, whereas in cells grown under conditions favoring MCR I, levels of MCR II were much lower and the cells had an increased affinity for hydrogen throughout the growth cycle. The use of thiosulfate as a medium reductant was found to have a negative effect on levels of MCR II and H₂-MDH. From these results it was concluded that M. thermoautotrophicum responds to variations in hydrogen availability and other environmental conditions (pH, growth temperature, medium reductant) by altering its physiology. The adaptation includes, among others, the differential expression of the MDH and MCR isoenzymes.     

Regulation of nicotinamide adenine dinucleotide phosphate levels in yeast

The steady-state levels and redox states of pyridine nucleotide pools have been studied in yeast as a function of external growth conditions. Yeast grown aerobically on 0.8% glucose show two distinct phases of logarithmic growth, a first phase utilizing glucose with ethanol accumulation, and a second phase utilizing ethanol. During growth on glucose, the size of the NADP pool (NADP⁺ + NADPH) is maintained at approximately 12% the size of the NAD pool (NAD⁺ + NADH). Upon exhaustion of glucose, the mechanism(s) that maintain the levels of NADP relative to NAD are altered, resulting in a rapid 2- to 2.5-fold decrease in the size of the NADP pool relative to the size of the NAD pool. The lower levels of NADP are maintained during growth on ethanol. The NAD pool is approximately 50% NADH during both the glucose and ethanol phases of growth, while the NADP pool is approximately 67 and 48% NADPH during the glucose and ethanol phases of growth, respectively. Rapid media transfer experiments show that the decrease in NADP is reversible, that it does not require the net synthesis of pyridine nucleotide or protein, and that changes in the size of the NADP pool relative to the total pyridine nucleotide pool are correlated with changes in the redox state of the NADP pool.     

Production of extracellular protease from halotolerant bacterium, Bacillus aquimaris strain VITP4 isolated from Kumta coast

A newly isolated halotolerant Bacillus sp. VITP4 was investigated for the production of extracellular protease. 16S rRNA gene analysis identified it as Bacillus aquimaris. Enzyme secretion corresponded with growth (G_t, 38 min) in the basal Zobell medium, reaching a maximum during stationary phase (630 U/ml, 48 h). Protease production was investigated in different salt concentrations (0–4 M). While growth was optimum in the basal medium, higher levels of protease activity were observed in 0.5 M salt medium (728 U/ml, 48 h) and 1 M salt medium (796 U/ml, 78 h) with 21% and 32% increase in production, respectively. Salt concentrations above 2.5 M did not support bacterial growth. The optimum pH and temperature for production were pH 7.5 and 37 °C, respectively. A combination of peptone and yeast extract yielded optimum protease secretion. Inorganic nitrogen sources proved to be less favourable. Production was reduced in the presence of readily available carbon sources owing to catabolic repression. Effect of various salts (1–6%) indicated favourable bacterial growth in these conditions for producing proteolytic molecules with increased activity. The study assumes significance in the ability of the halotolerant bacterium to survive in a wide range of salinity and yield optimum levels of extracellular protease.