Production of trypsin inhibitor by a Cephalosporium sp.

Conditions for the production of the trypsin inhibitor from Cephalosporium sp. KM 388 were investigated. Polypeptone-meat extract-glucose medium supported excellent production of the trypsin inhibitor. In this medium, polypeptone and meat extract were utilized both as carbon and nitrogen sources and as limiting substrates for the cell growth. Glucose was consumed during the stationary growth phase and prevented the disappearance of inhibitor activity. Cephalosporium sp. KM 388 grew at a rate of a first-order reaction for the cell concentrations. Trypsin inhibitor production paralleled cell growth. At 27 degrees C the maximum specific rates of growth and inhibitor production were 0.14 h-1 and 2.1 U of inhibitor/h per mg of cell, respectively. The production rate and the maximum yield of the inhibitor were increased 1.5- and 1.2-fold, respectively, when the initial pH 6.3 was maintained throughout the fermentation.     

Characteristics of Protease Production by Cephalosporium sp

We investigated protease formation by Cephalosporium sp. strain KM388, which produced trypsin inhibitor in the same cultures, in medium containing polypeptone, meat extract, and glucose (natural medium) and in medium containing NaNO₃, glucose, and yeast extract (semisynthetic medium). In natural medium, protease was secreted into the culture broth after cessation of growth caused by consumption of the polypeptone, the growth-limiting substrate. Enzyme formation in the stationary growth phase was due to de novo and so-called preferential synthesis, because cycloheximide immediately inhibited enzyme formation. In semisynthetic medium, protease was produced in parallel with mycelial growth, but production was repressed by the addition of polypeptone to the medium; protease production began after the added polypeptone was consumed. On the other hand, if glucose was eliminated from natural medium, the lag period of initiation of enzyme production was reduced until the late exponential phase. The addition of phosphate up to a concentration of 1.0% to natural medium also shortened the lag period and damped the pH change of the broth during cultivation.     

Characterization of an extracellular glycoprotein inhibitor of trypsin (TI-23) produced by Streptomyces sp. 23

Summary The production of an extracellular trypsin inhibitor, TI-23, was found to parallel the growth of Streptomyces sp. 23 at different cultivation temperatures, reaching a maximum level at late exponential phase. Although the different temperatures (18°, 28° and 37°C) did not greatly affect the growth of the microorganism, they proved to be an important factor for extracellular inhibitory activity. Maximum specific rates of both cell growth and production of the inhibitor were recorded during the cultivation of Streptomyces sp. 23 at 37°C. TI-23 proved to be a monomeric glycoprotein containing 17% carbohydrate and differing in amino acid composition from the known extracellular proteinase inhibitors of streptomycetes. The molecular mass of the inhibitor was estimated to be about 13 kDa and the isoelectric point 4.3. The inhibition spectrum of TI-23 included trypsin as well as some microbial alkaline proteinases.     

Modeling of growth kinetics for an isolated marine bacterium,Oceanimonas sp. BPMS22 during the production of a trypsin inhibitor

Abstract

Protease inhibitors significantly control physiologically relevant protease activities. Protease inhibitors from marine microbial sources are unique due to their rough living environmental conditions. In the present study, a protein protease inhibitor (PI) was produced from marine Oceanimonas sp. BPMS22. Seven different media were screened for the growth of the bacterium and production of PI. Different carbon and nitrogen sources were screened and optimized for the specific protease inhibitor activity. Three different growth models were checked for the best fit of the bacterial growth. A modified Gompertz model was selected as the best model for the growth of Oceanimonas sp. BPMS22 with the maximum specific growth rate of 0.165?hr^?1 and doubling time of 4.2?hr. The production of PI takes place during the non-growing phase of the bacterial growth. A kinetic model for the production of PI during non-growing phase was used for studying various process parameters. From the model, the maximum trypsin inhibitor formation rate of 0.3802?IU per mg of biomass per hour was observed at 49.91?hr.     

Effect of culture conditions on cathepsin B inhibitor production by a marine bacterium, Pseudomonas sp. strain PB01

A novel cathepsin B inhibitor-producing bacterium was isolated from marine sediments and identified based on its 16S rDNA sequence as Pseudomonas sp. strain PB01 (Accession No. EU126129). The growth and enzyme inhibitor production were investigated under various culture conditions. A mixture of organic nitrogen source was required for the optimal production, whereas both glucose and maltose proved to be the effective carbon sources for cathepsin B inhibitor production. Other optimal culture conditions included temperature range between 25 and 28 degrees , initial medium pH of 6.6, and shaking speed of 200 rpm. Under these optimal conditions, the maximum inhibitory activity from culture broth was approximately 50% after 30 h of cultivation. Additionally, kinetic study revealed that inhibitor production paralleled with cell growth, which suggested that the inhibitor may be a primary metabolite of that bacterium.     

Enhanced production of cell-bound cholesterol oxidase from Rhodococcus sp. NCIM 2891 by the statistical method

Classical (one-variable-at-a-time) and statistical methods (Plackett-Burman and Central composite design) were used to optimise growth medium for the production of cholesterol oxidase (COX) from Rhodococcus sp. NCIM 2891. COX activities from the classically and statistically optimised media were 0.75 and 3.25 U/ml, respectively. The statistically optimised medium had 4.33- and 9.7-fold higher enzymatic activity than the classically optimised and un-optimised basal medium, respectively. The ratio of enzyme production to cell growth rate was 29-fold higher in our statistically optimised medium than in the basal medium, indicating that the enzyme production could be classified as mixed type of growth. Cell-bound COX accounted for 90.68?±?2 % of the total enzymatic activity of the growth medium. Interactions between the COX-inducing substrate cholesterol and medium growth substrates yeast extract and (NH₄)₂HPO₄ significantly enhanced the production of cell-bound COX. Our results validate the statistical approach as a potential technique for achieving the large-scale production of cell-bound COX from Rhodococcus sp. NCIM 2891.     

Improved production of curdlan with concentrated cells ofAgrobacterium sp.

The addition of a limited concentration of yeast extract to a minimal salt medium (MSM) enhanced cell growth and increased the production of curdlan whereas nitrogenlimitation was found to be essential for the higher production of curdlan byAgrobacterium sp. ATCC 31749. As the amount of the inoculum increased, the cell growth as well as the production of curdlan also increased in the MSM without a nitrogen source. The cell growth and production of curdlan increased as the initial pH of the medium decreased as low as 5.0. The conversion rate and concentration of curdlan from 2% (w/v) glucose in the MSM with concentrated cells under nitrogen deletion was 67% and 13.4 g/L, respectively. The highest conversion rate of curdlan under the conditions optimized in this study was 71% when the glucose concentration was 1% (w/v).     

Growth behaviour and bioproduction of indole acetic acid by a Rhizobium sp. isolated from root nodules of a leguminous tree Dalbergia lanceolaria

The Rhizobium sp. isolated from healthy and mature root nodules of a leguminous tree, Dalbergia lanceolaria Linn. f., preferred mannitol and KNO3 for growth as carbon and nitrogen sources, respectively. The bacterium produced a high amount (22.3 microg/ml) of indole acetic acid (IAA) from L-tryptophan supplemented basal medium. Growth and IAA production started simultaneously. IAA production was maximum at 20 hr when the bacteria reached the stationary phase of growth. Cultural requirements were optimized for maximum growth and IAA production. The IAA production by the Rhizobium sp. was increased by 270.8% over control when the medium was supplemented with mannitol (1%,w/v), SDS (1 microg/ml), L-asparagine (0.02%,w/v) and biotin (1 microg/ml) in addition to L-tryptophan (2.5 mg/ml). The possible role of IAA production in the symbiosis is discussed.     

Modeling, optimization, and computer control of the cephalosporin C fermentation process

In this study, a cephalosporin C producing strain, Cephalosporium acremonium (ATCC 36225), was chosen to determine the optimal conditions that maximize antibiotic production in a mixed substrate of glucose and sucrose. A model for cell growth and cephalosporin C production at different pH and temperature was developed and the associated parameters were evaluated experimentally. Pontryagin's maximum principle, in conjunction with the model, was used to predict the optimal temperature and pH control profiles to maximize the production of antibiotic.     

Biosynthesis of extracellular low-molecular-mass papain and trypsin inhibitors by Streptomyces sp. 22: effect of cultural conditions

The production of extracellular inhibitors of papain and trypsin by Streptomyces sp. 22 was studied under different cultural conditions including complex and defined media, temperatures ranging from 18 °C to 37 °C and a variety of sole carbon and nitrogen sources. In complex nutritionally rich medium, maximal specific growth rates were obtained at 37 °C, whereas the highest specific production rates for both papain and trypsin inhibitors were registered at 18 °C. Studies on the effect of different carbon and nitrogen sources in defined media underline the importance of the nitrogen source as a strong regulator of the biosynthesis of both inhibitors. Enhanced formation of the inhibitory compounds occurred in the presence of casein. The dynamics of the formation of both inhibitors in defined media showed close association with growth. However, a partial separation of production phases for papain and trypsin inhibitors was observed in complex medium. The results imply differences in the regulation of biosynthesis of the two inhibitors.     

Application of a gratuitous induction system in Kluyveromyces lactis for the expression of intracellular and secreted proteins during fed-batch culture

A gratuitous induction system in the yeast Kluyveromyces lactis was evaluated for the expression of intracellular and extracellular products during fed-batch culture. The Escherichia coli lacZ gene (beta-galactosidase; intracellular) and MFalpha1 leader-BPTI cassette (bovine pancreatic trypsin inhibitor; extracellular) were placed under the control of the inducible K. lactis LAC4 promotor, inserted into partial-pKD1 plasmids, and transformed into a ga1-209 K. lactis strain. To obtain a high level of production, culture conditions for growth and expression were initially evaluated in tube cultures. A selective medium containing 5 g/L glucose (as carbon source) and 0.5 g/L galactose (as inducer) demonstrated the maximum activity of both beta-galactosidase and secreted BPTI. This level of expression had no significant effect on the growth of the recombinant cells; growth rate dropped by approximately 11%, whereas final biomass concentrations remained the same. In shake-flask culture, biomass concentration, beta-galactosidase activity, and BPTI secreted activity were 4 g/L, 7664 U/g dry cell, and 0.32 mg/L, respectively. Fed-batch culture (with a high glucose concentration and a low galactose [inducer] concentration feed) resulted in a 6.5-fold increase in biomass, a 23-fold increase in beta-galactosidase activity, and a 3-fold increase in BPTI secreted activity. The results demonstrate the success of gratuitous induction during high-cell-density fed-batch culture of K. lactis. A very low concentration of galactose feed was sufficient for a high production level.     

Inhibition studies on the membrane-associated phospholipase A2 in vitro and prostaglandin E2 production in vivo of the macrophage-like P388D1 cell. Effects of manoalide, 7,7-dimethyl-5,8-eicosadienoic acid, and p-bromophenacyl bromide

In order to ascertain the role of phospholipase A2 (PLA2) in the release of arachidonic acid for eicosanoid biosynthesis, we have characterized a Ca2+-dependent PLA2 from P388D1 cells, evaluated inhibitors of its activity, and correlated the effects of these inhibitors on prostaglandin (PG) E2 production in the intact cell. The Ca2+-dependent PLA2 has little preference for the polar head group or sn-2 fatty acid of phospholipids, and we have now found that it will hydrolyze 1-alkyl,2-acyl phospholipids, but it does not show a preference for this substrate over other phospholipids. Inhibitor studies with the Ca2+-dependent PLA2 have shown that arachidonic acid is an effective inhibitor. The analogs of natural fatty acids, eicosatetraynoic acid and octadecyleicosaynoic acid, were ineffective as inhibitors of the P388D1 PLA2. However, 7,7-dimethyl-5,8-eicosadienoic acid was as effective an inhibitor (IC50 = 16 microM) as arachidonic acid. Manoalide and its analog, manoalogue, were found to be good inhibitors of the P388D1 PLA2 (IC50 = 16 and 26 microM, respectively). The irreversible inhibitor of the extracellular PLA2, p-bromophenacyl bromide, was a very poor inhibitor of the P388D1 PLA2, apparent IC50 = 500-600 microM. Quinacrine was also ineffective as an inhibitor as was the cyclooxygenase inhibitor indomethacin. On the cellular level, the P388D1 cells respond to various stimuli to produce PGD2 and PGE2 as the major cyclooxygenase products with minor production of PGI2 and thromboxane A2. Similar arachidonic acid metabolite profiles were seen for calcium ionophore A23187, melittin, and platelet-activating factor. Manoalide, manoalogue, and 7,7-dimethyl-5,8-eicosadienoic acid, effective inhibitors of the isolated PLA2, inhibited PGE2 production in intact P388D1 cells 40-85% in the concentration range studied. In contrast, p-bromophenacyl bromide, which is ineffective as an inhibitor of the P388D1 PLA2, did not significantly effect PGE2 production in the concentration ranges used. These results demonstrate that there may be important differences between the intracellular P388D1 PLA2 and the more commonly studied extracellular forms of PLA2. These differences are also observed in the intact cell studies and emphasize the need for the evaluation of inhibitors both in vitro and in vivo using the isolated enzyme and intact cell. This is the first example of studies aimed at correlating the inhibition of a purified intracellular PLA2 with inhibition of prostaglandin production in the intact cell from which it is derived.     

Histone deacetylase inhibitor valproic acid inhibits proliferation and induces apoptosis in KM3 cells via downregulating VEGF receptor

The expression of vascular endothelial growth factor receptor 1(VEGFR-1) in human multiple myeloma KM3 cells in vitro, effects of valproic acid (VPA), as a histone deacetylase inhibitor, on cell proliferation and apoptosis and the underlying molecular mechanism were investigated. The effects of VPA on the growth of KM3 cells were studied by MTT assay. The apoptosis rate was determined with flow cytometry. The mRNA level of VEGFR was determined by RT-PCR; and immunocytochemistry was used to detect the protein level of ac-H4 and VEGFR. VPA inhibited proliferation of KM3 cells in a time- and dose-dependent manner. Treatment with VPA (4, 2, 1 and 0.5 mmol/L) for 48h, the apoptosis rates of KM3 cells were (13.27+/-3.54)%, (22.13+/-1.20)%, (24.41+/-2.23)% and(40.62+/-4.28)% respectively. The expression of VEGFR-1 in KM3 cells were decreased in VPA-treated group by the immunochemistry and RT-PCR, whereas the acetylated histone H4(ac-H4) accumulated. It suggested VPA could decrease the expression of VEGFR-1 in KM3 cells, and it might play an important role in regulating the proliferation and apoptosis of multiple myeloma cell line KM3 cells. These results provide the framework for clinical trials.     

A comparative evaluation of Cephalosporin C production using various immobilization modes

The production of Cephalosporin C was investigated in a lab-scale 1.4 l air-lift reactor (ALR), using various immobilization modes. Bioparticles were developed by forming biofilm of growing hyphae around an inorganic siran particle which contained spores of the organism. Silk sachet was the other immobilization matrix. The maximum specific growth rate of the Cephalosporium acremonium, free cells, pellets, siran carrier and silk sachets were 0.037, 0.003, 0.047, and 0.035 h(-1), and specific antibiotic productivities (as compared to 100% for free cells) were 180, 150, and 125% for siran carrier, silk sachets and pellets, respectively. Immobilization modes exhibited enhanced volumetric oxygen transfer coefficient and well-controlled, three-phase hydrodynamics.     

Defining an optimal carbon source/methionine feed strategy for growth and cephalosporin C formation by Cephalosporium acremonium.

The effect of the method of methionine addition, growth-limiting carbon source (glucose vs sucrose), and culture growth rate on cephalosporin C production was investigated in a Cephalosporium acremonium defined medium fed batch fermentation. Batch addition of methionine, at a concentration of 3 g/L, prior to the start of a fed sucrose fermentation was found to interfere with the ability of the culture to utilize this sugar, thus limiting growth and decreasing cephalosporin C production. Batch methionine addition had no effect on glucose-limited cultures. Concurrent exponential feeding of methionine with sucrose improved both culture growth and productivity. Under the control of identical carbon source limiting feed profiles, sucrose was observed to support greater cephalosporin C production than glucose. Optimal cephalosporin C production in a C. acremonium defined medium fed batch fermentation was obtained through controlling culture growth during the rapid growth phase at a relatively low level with respect to mumax (mu approximately 0.036 h-1) until achieving a desired cell mass with a concurrent sucrose and methionine feed, followed by maintaining relatively vigorous growth (mu approximately 0.01 h-1) with sucrose for the duration of the fermentation.     

Co-expression of proteinase inhibitor enhances recombinant human granulocyte-macrophage colony stimulating factor production in transgenic rice cell suspension culture

The synthetic gene (sPI-II) harboring the chymotrypsin (C1) and trypsin (T1) inhibitor domains of the Nicotiana alata serine proteinase inhibitor II gene has been previously expressed, and extracellular protease activity was shown to be reduced in the suspension culture medium. In this study, the sPI-II gene was introduced into transgenic rice cells expressing rhGM-CSF (recombinant human granulocyte–macrophage colony-stimulating factor), in an effort to reduce protease activity and increase rhGM-CSF accumulation in the suspension culture medium. The integration and expression of the introduced sPI-II gene in the transgenic rice cells were verified via genomic DNA PCR amplification and Northern blot analysis, respectively. Relative protease activity was found to have been reduced and rhGM-CSF production was increased 2-fold in the co-transformed cell suspension culture with rhGM-CSF and the sPI-II gene, as compared with that observed in the transformed cell suspension culture expressing rhGM-CSF only. These results indicate that a transformed plant cell suspension culture system expressing the proteinase inhibitor can be a useful tool for increasing recombinant protein production.     

Influence of medium composition on the cephalosporin C production with a highly productive strain Cephalosporium acremonium.

Cephalosporin production by a highly productive Cephalosporium acremonium strain was carried out and optimized by fed-batch operation in a 40 l stirred tank reactor using a complex medium containing 30-120 g l-1 peanut flour. The concentrations of cephalosporin C (CPC) and its precursors: penicillin N (PEN N), deacetoxy cephalosporin C (DAOC), and deacetyl cephalosporin C (DAC) were monitored with an on-line HPLC. The concentrations of amino acids valine (VAL), cysteine (CYS), alpha-amino adipic acid (alpha-AAA), the dipeptide alpha-amino-adipyl-cysteine (AC), and the tripeptide alpha-amino-adipyl-cysteinyl-valine (ACV), were determined off-line by HPLC. The RNA content and dry weight of the sediment as well as the oxygen transfer rate (OTR) and the CO2 production rate (CPR) were used to calculate the cell mass concentration (X). The influences of peanut flour (PF) and the on-line monitored and controlled medium components: glucose (GLU), phosphate, methionine (MET) as well as the dissolved oxygen (DOC) on the cell growth, the product formation, and the pathway of cephalosporin C biosynthesis were investigated and evaluated. When the glucose fed-batch cycle was optimized and oxygen transfer limitation was avoided (DOC greater than 20% of the saturation value), high process performance (103.5 g l-1 X, 11.84 g l-1 CPC, a maximum CPC productivity of 118 mg l-1 h-1, and the whole concentration of the beta-lactam antibiotics CPC, DAC, DAOC, PEN N 17.34 g l-1) was achieved by using 100 g l-1 PF in the medium with the optimum concentration of phosphate (260-270 mg l-1) and a low glucose concentration (less than 0.5 g l-1). The cultivations with different medium concentrations demonstrated that the product formation was directly proportional to the cell mass concentration. On the average, the cell mass-based yield coefficient of CPC: YCPC/X amounted to 0.115 g CPC per g cell mass.     

Biosynthesis of penicillin N and cephalosporin C: Antibiotic production and other features of the metabolism of a Cephalosporium sp

1. The production of penicillin N and cephalosporin C by two mutants of a Cephalosporium sp. has been studied with cultures grown in a chemically defined medium and with suspensions of washed mycelium in water or a buffered salt solution. 2. Antibiotic synthesis began at an early stage of growth and its rate per unit weight of mycelium appeared to pass its maximum as morphological changes were occurring in young hyphae. This rate subsequently declined, but rapid production could continue after net growth had ceased. 3. In a series of shake-flask fermentations in the growth medium, increases in the yield of penicillin N above the mean were correlated with much smaller increases in the yield of cephalosporin C and vice versa. 4. In suspensions of washed mycelium, moderate decreases in the efficiency of aeration increased the yield of penicillin N and decreased that of cephalosporin C. A similar result normally followed the addition of methionine to the suspension fluid, and in both cases there was usually an increase in the yield of the two antibiotics combined. 5. The apparent intracellular concentrations of the antibiotics were much lower than those attained extracellularly and also much lower than those of most of the amino acids in the intracellular pool. No detectable amount of [(14)C]penicillin N added to the extracellular fluid was found to enter the mycelium. 6. Very small amounts of peptide material whose behaviour was similar to that of the sulphonic acid of delta-(alpha-amino-adipoyl)cysteinylvaline on paper electrophoresis at pH1.8 were found in extracts of the mycelium that had been oxidized with performic acid. 6-Aminopenicillanic acid and 7-aminocephalosporanic acid were not detected. 7. Ultrasonic treatment of the mycelium resulted in rapid fragmentation of mycelial chains, rupture of many individual cells, and the liberation of amino acids and other substances into the medium. 8. Ultrasonically treated preparations synthesized penicillin N and cephalosporin C rapidly after a lag of 12hr. Antibiotic synthesis was accompanied by the growth of hyphae from swollen mycelial fragments and by the re-establishment of permeability barriers resulting in the uptake of amino acids from the medium.     

Development of an animal‐component free medium for vero cells culture

This work describes the development of an animal‐component free medium (IPT‐AFM) that allows an optimal growth of Vero cells, an adherent cell line used for the production of viral vaccines. Statistical experimental design was applied to identify crucial nutrients that affect cell growth. Using Medium 199 or MEM as a basal medium, a serum‐free medium (SFM) referred as IPT‐SFM that only enclosed transferrin as a component of animal origin was developed at first. Then, the composition of IPT‐SFM was further improved to obtain an animal‐component free medium named IPT‐AFM. IPT‐AFM contains M199 as a basal medium, plant hydrolysates, epidermal growth factor, ethanolamine, ferric citrate, and vitamin C. Among various plant hydrolysates, specific combinations of soy (Hypep 1510) and wheat gluten (Hypeps 4601 and 4605) hydrolysates, were identified to promote cell growth; whereas individual Hypeps had a minor positive effect on cell growth. Nevertheless, the removal of serum did influence cell attachment. Coating tissue‐culture flasks with teleostean, a product extracted from cold water fish skin, had not only enhanced cell attachment but also improved cell growth performance in static cultures. Different non‐animal proteases were also assessed as an alternative to trypsin. TrypLE Select, a recombinant trypsin, gave the best cell growth performances. Kinetics of cell growth in IPT‐AFM were investigated in T‐flasks, cell growth was comparable with that obtained in MEM+10% fetal calf serum (FCS). A mean cell division number equal to 2.26 ± 0.18 and a specific growth rate μ 0.019 ± 0.003 h^?1 were achieved in IPT‐AFM. © 2009 American Institute of Chemical Engineers Biotechnol. Prog., 2009     

Regulation of cephalosporin synthesis in Cephalosporium acremonium by phosphate and glucose

The regulation of cephalosporin synthesis in Cephalosporium acremonium was studied in a simple chemically-defined medium with glucose as the carbon source. Antibiotic synthesis depended on the phosphate content of the medium. At phosphate concentrations above 2.75 mM maximum antibiotic titres were not reached while glucose uptake and growth rates were increased. Phosphate exerted its effect indirectly by regulating the rate of glucose consumption. The negative effect of high phosphate concentrations could be overcome completely by controlling the sugar supply in fed-batch and chemostat experiments. High actual concentrations of phosphate or of glucose alone had no direct negative effect on antibiotic synthesis.