Studies on cephalosporin-C production in an air lift reactor using different growth modes of Cephalosporium acremonium

This paper deals with the studies on Cephalosporin-C production in a lab-scale airlift reactor using Cephalosporium acremonium. Various growth modes, viz. pellets and Siran supported bioparticles were used to improve the process over conventional free mycelial fermentation. Cephalosporin-C production was significantly improved by using bioparticles over the free mycelial culture, probably due to the enhanced mass transfer in the fermentation broth. However, the biofilm of the bioparticles became unstable as the fermentation proceeded, and increase in the free cells in the broth occurs. The maximum specific growth rate of free cells, pellets and Siran carrier were observed to be 0·037, 0·033 and 0·045 h⁻¹, respectively. The oxygen transfer coefficient also improved for the immobilised modes (100 h⁻¹, 70 h⁻¹ for Siran carrier and pellets) and thereby enhanced specific antibiotic productivity, 18–28% were observed.     

Production of penicillin in a fluidized-bed bioreactor using a carrier-supported mycelial growth

A carrier-supported mycelial growth of Penicillium chrysogenum was applied to penicillin fermentation system using celite as a support material. Hyphal growth through the pore matrices of the material showed strong anchorages and provided highly stable biofilm growth. With bioparticles developed in such a manner, both cell growth and penicillin production were observed to increase significantly compared to the conventional dispersed filamentous cultures. Maximum values of specific penicillin production rate were found to be constant regardless of the growth form. A three-phase fluidized-bed fermentor was designed and tested for penicillin production using the bioparticles. Two modes of operation, semicontinuous and repeated fed batch, of the fermentor were tried. It was noted that the overgrowth of free mycelia and the development of fluffy loose bioparticles caused poor mixing and made the fermentor operation quite difficult. Control of the bioparticle size and the extension of production phase were therefore considered important to maintain the reactor productivity at a desired level. From the results of repeated fed-batch operation it was found that the control of bioparticle size could be successfully achieved by phosphate-limiting culture condition. Penicillin production under this condition was also observed to be maintained at a high level (about 80% of the maximum) for at least 1 month.     

Expression of a cephalosporin C esterase gene in <Emphasis Type="Italic">Acremonium chrysogenum</Emphasis> for the direct production of deacetylcephalosporin C

A recombinant fungal microorganism capable of producing deacetylcephalosporin C was constructed by transforming a cephalosporin C esterase gene from Rhodosporidium toruloides into Acremonium chrysogenum. The cephalosporin C esterase gene can be expressed from its endogenous R. toruloides promoter or from the Aspergillus nidulans trpC promoter under standard Acremonium chrysogenum fermentation conditions. The expression of an active cephalosporin C esterase enzyme in A. chrysogenum results in the conversion of cephalosporin C to deacetylcephalosporin C in vivo, a novel fermentation process for the production of deacetylcephalosporin C. The stability of deacetylcephalosporin C in the fermentation broth results in a 40% increase in the cephalosporin nucleus.     

Production of Superoxide Dismutase from Streptococcus lactis Using a Bioreactor with a Microfiltration Module

The performance of a bioreactor with a microfiltration module for the production of an intracellular enzyme, superoxide dismutase (SOD), by Streptococcus lactis is described. The fermentation system involving the bioreactor enables the continuous removal of metabolites inhibitory for cell growth and the complete recycling of the cells to the bioreactor. In a fed-batch (FB) culture with filtration, in which the main metabolite, lactic acid, in the culture broth was maintained at a low concentration, S. lactis was cultivated to the high concentration of 15.5 g-dry cells/1. The SOD content of the cells remained at almost a constant level throughout the cultivation and the productivity of SOD as well as cells per unit time was 4.3-fold as high as that in the case of a conventional batch culture without filtration. Repeating the FB culture with filtration enhanced the productivities of SOD and cells further, as compared with those in the case of the FB culture with filtration.     

Cephalosporin C production by immobilized Cephalosporium acremonium cells in a repeated batch tower bioreactor

The industrial production of antibiotics with filamentous fungi is usually carried out in conventional aerated and agitated tank fermentors. Highly viscous non-Newtonian broths are produced and a compromise must be found between convenient shear stress and adequate oxygen transfer. In this work, cephalosporin C production by bioparticles of immobilized cells of Cephalosporium acremonium ATCC 48272 was studied in a repeated batch tower bioreactor as an alternative to the conventional process. Also, gas-liquid oxygen transfer volumetric coefficients, k(L)a, were determined at various air flow-rates and alumina contents in the bioparticle. The bioparticles were composed of calcium alginate (2.0% w/w), alumina ( < 44 micra), cells, and water. A model describing the cell growth, cephalosporin C production, oxygen, glucose, and sucrose consumption was proposed. To describe the radial variation of oxygen concentration within the pellet, the reaction-diffusion model forecasting a dead core bioparticle was adopted. The k(L)a measurements with gel beads prepared with 0.0, 1.0, 1.5, and 2.0% alumina showed that a higher k(L)a value is attained with 1.5 and 2.0%. An expression relating this coefficient to particle density, liquid density, and air velocity was obtained and further utilized in the simulation of the proposed model. Batch, followed by repeated batch experiments, were accomplished by draining the spent medium, washing with saline solution, and pouring fresh medium into the bioreactor. Results showed that glucose is consumed very quickly, within 24 h, followed by sucrose consumption and cephalosporin C production. Higher productivities were attained during the second batch, as cell concentration was already high, resulting in rapid glucose consumption and an early derepression of cephalosporin C synthesizing enzymes. The model incorporated this improvement predicting higher cephalosporin C productivity.     

Effect of Biofilm Formation by Bacillus subtilis natto on Menaquinone-7 Biosynthesis

Bacillus subtilis natto is the key microorganism for the industrial production of menaquinone-7. The fermentation of this bacterium in static culture is associated with biofilm formation. The objective of this study was to determine the effect of biofilm formation on menaquinone-7 production to develop a suitable bio-reactor for the production of menaquinone-7. In the static culture, menaquinone-7 biosynthesis showed a linear correlation with biofilm formation (R ² = 0.67) and cell density (R ² = 0.7). The amount of biofilm, cell density and menaquinone-7 formation were a function of nutrient and processing conditions. Glycerol, soy peptone, and yeast extract mixture and 40 °C were found to be the optimum nutrients and temperature for accelerating both biofilm and menaquinone-7 biosynthesis in static culture. However, glucose, mixture of soy peptone and yeast extract and 45 °C were found to be the optima for cell density. As compared to the static culture, the biofilm formation was significantly inhibited when a shaken fermentation was used. However, shaking caused only a small decrease on menaquinone-7 production. These results demonstrate that the biofilm formation is not essential for menaquinone-7 biosynthesis. This study underlines the feasibility of using large scale stirred fermentation process for menaquinone-7 production.     

Changes in Cellular Fatty Acid Composition of Cephalosporium acremonium during Cephalosporin C Production

Cephalosporium acremonium was cultivated in fermentation medium containing sucrose or methyl oleate as a carbon source for cephalosporin C production. The level of antibiotic production was 48 g of cephalosporin C per liter under optimum conditions when methyl oleate was used. The C_18:1 (oleic acid) methyl ester appeared to be utilized faster than the C_18:2 (linoleic acid) methyl ester in fermentation broth. Physiological characteristics of C. acremonium were investigated by determining the fatty acid composition of the total cellular free lipid. Significant changes in cellular fatty acid composition occurred during inoculum cultivation and fermentation. The percentage of C_18:1 increased from 19.1 to 38.5%, but the percentage of C_18:2 decreased from 56.7 to 36.1%, and there was an increase in pH during inoculum cultivation. The cellular fatty acid composition of C. acremonium grown in fermentation medium containing methyl oleate (methyl oleate medium) was significantly different from that in fermentation medium containing sucrose (sucrose medium). The major fatty acids detected were C_16:0 (palmitic acid), C_18:1, and C_18:2. In methyl oleate medium, the ratio of C_18:1 to C_18:2 increased from 0.34 to 1.37, while the cell morphology changed from hyphae to arthrospores and conidia. In contrast, in sucrose medium, the ratio of C_18:1 to C_18:2 decreased from 0.70 to 0.43, and most of the cells remained hyphal at the end of fermentation. We observed that hyphae contained a higher proportion of C_18:2 but arthrospores and conidia contained a higher proportion of C_18:1.     

Isolation, Identification, and Characterization of a Feather-Degrading Bacterium

A feather-degrading culture was enriched with isolates from a poultry waste digestor and adapted to grow with feathers as its primary source of carbon, sulfur, and energy. Subsequently, a feather-hydrolytic, endospore-forming, motile, rod-shaped bacterium was isolated from the feather-degrading culture. The organism was Gram stain variable and catalase positive and demonstrated facultative growth at thermophilic temperatures. The optimum rate of growth in nutrient broth occurred at 45 to 50°C and at pH 7.5. Electron microscopy of the isolate showed internal crystals. The microorganism was identified as Bacillus licheniformis PWD-1. Growth on hammer-milled-feather medium of various substrate concentrations was determined by plate colony count. Maximum growth (approximately 10⁹ cells per ml) at 50°C occurred 5 days postinoculation on 1% feather substrate. Feather hydrolysis was evidenced as free amino acids produced in the medium. The most efficient conditions for feather fermentation occurred during the incubation of 1 part feathers to 2 parts B. licheniformis PWD-1 culture (10⁷ cells per ml) for 6 days at 50°C. These data indicate a potential biotechnique for degradation and utilization of feather keratin.     

Enhanced Biotransformation of Fluoranthene by Intertidally Derived Cunninghamella elegans under Biofilm-Based and Niche-Mimicking Conditions

The aims of the investigation were to ascertain if surface attachment of Cunninghamella elegans and niche intertidal conditions provided in a bioreactor influenced biotransformation of fluoranthene by C. elegans. A newly designed polymethylmethacrylate (PMMA) conico-cylindrical flask (CCF) holding eight equidistantly spaced rectangular strips mounted radially on a circular disc allowed comparison of fluoranthene biotransformation between CCFs with a hydrophobic surface (PMMA-CCF) and a hydrophilic glass surface (GS-CCF) and a 500-ml Erlenmeyer flask (EF). Fluoranthene biotransformation was higher by 22-fold, biofilm growth was higher by 3-fold, and cytochrome P450 gene expression was higher by 2.1-fold when C. elegans was cultivated with 2% inoculum as biofilm culture in PMMA-CCF compared to planktonic culture in EF. Biotransformation was enhanced by 7-fold with 10% inoculum. The temporal pattern of biofilm progression based on three-channel fluorescence detection by confocal laser scanning microscopy demonstrated well-developed, stable biofilm with greater colocalization of fluoranthene within extracellular polymeric substances and filaments of the biofilm grown on PMMA in contrast to a glass surface. A bioreactor with discs rotating at 2 revolutions per day affording 6-hourly emersion and immersion mimicked the niche intertidal habitat of C. elegans and supported biofilm formation and transformation of fluoranthene. The amount of transformed metabolite was 3.5-fold, biofilm growth was 3-fold, and cytochrome P450 gene expression was 1.9-fold higher in the process mimicking the intertidal conditions than in a submerged process without disc rotation. In the CCF and reactor, where biofilm formation was comparatively greater, higher concentration of exopolysaccharides allowed increased mobilization of fluoranthene within the biofilm with consequential higher gene expression leading to enhanced volumetric productivity.     

A chemically defined medium for cephalosporin C production by Paecilomyces persicinus

A chemically defined medium was developed for the biosynthesis of cephalosporin C by Paecilomyces persicinus Nicot strain P-10. Glucose served as the major carbon source and nitrogen was supplied by five amino acids, l-arginine, l-aspartic acid, l-glutamic acid, glycine and dl-methionine. Omission of any of the first four diminished or prevented production of cephalosporin C; omission of methionine did not. Methionine is not critical for the production of cephalosporin C in this defined medium. Production of the antibiotic was affected by the concentrations of inorganic salts employed. Biotin was required for growth and cephalosporin C synthesis. The addition of l-lysine precursors to the medium did not influence cephalosporin C levels and l-lysine itself inhibited antibiotic production. Known precursors of -lactam antibiotics as well as oleic acid did not affect biosynthesis of cephalosporin C. Chemical changes occurring in the defined medium revealed that glucose was efficiently utilized after 96 hours incubation whereas total soluble nitrogen levels increased following an initial sharp decrease. Mycelial weight and cephalosporin C production were both maximal after 96 hours incubation. Mycelial nitrogen was highest after 48 hours incubation whereas mycelial lipid levels were greatest after 72 hours.     

A novel parallel shaken bioreactor system for continuous operation

A novel continuous bioreactor system was developed as a shaken culture vessel for the investigation of the growth kinetics and product formation of microorganisms in milliscale. The novel bioreactor system mainly consists of a specially designed 250-mL shake flask with two inlets, one for gas supply and one for medium supply, and one combined outlet on the side of flask for exhaust gas and culture liquid. As a result of the circulating motion of the fermentation broth in the shake flask, the maximum liquid height reaches the edge of the outlet and the fermentation broth is accelerated into the outlet by centrifugal force. Additionally, the excess fermentation broth leaving the culture vessel is continuously driven by the exhaust gas. Because of the small scale and the simple handling it is possible to operate many of these shaken bioreactor vessels simultaneously. By using parallel vessels operated at different dilution rates on the same shaker, the data for a complete biomass over dilution rate (X-D) diagram of a biological culture can be evaluated in an efficient manner, thus saving money, materials, and time. Continuous fermentations of the yeast Saccharomyces cerevisiae H1022 (ATCC 32167) in the shaken bioreactor system and in a conventional stirred tank fermentor showed very similar results.     

Acetic Acid Production by an Electrodialysis Fermentation Method with a Computerized Control System

In acetic acid fermentation by Acetobacter aceti, the acetic acid produced inhibits the production of acetic acid by this microorganism. To alleviate this inhibitory effect, we developed an electrodialysis fermentation method such that acetic acid is continuously removed from the broth. The fermentation unit has a computerized system for the control of the pH and the concentration of ethanol in the fermentation broth. The electrodialysis fermentation system resulted in improved cell growth and higher productivity over an extended period; the productivity exceeded that from non-pH-controlled fermentation. During electrodialysis fermentation in our system, 97.6 g of acetic acid was produced from 86.0 g of ethanol; the amount of acetic acid was about 2.4 times greater than that produced by non-pH-controlled fermentation (40.1 g of acetic acid produced from 33.8 g of ethanol). Maximum productivity of electrodialysis fermentation in our system was 2.13 g/h, a rate which was 1.35 times higher than that of non-pH-controlled fermentation (1.58 g/h).     

三相鼓泡塔生物反应器培养云芝菌合成漆酶

为了提高云芝菌发酵生产漆酶的效率,提出了一种利用自絮凝菌丝球在三相鼓泡塔生物反应器中重复分批发酵产漆酶的新方法。在优化后的产酶条件下,考察维生素C的添加浓度对漆酶活力的影响,并通过在培养基中添加维生素C进行漆酶多批次培养。研究结果表明,维生素C的添加浓度为1.50mmol/L时,可使漆酶活力提高2.6倍。连续进行了10批培养,每批最大漆酶的活力均在1000 U/mL以上,最高酶活出现在第五批为1919.6 U/mL,总培养时间达25 d。此方法所得漆酶对染料靛蓝具有明显的脱色降解作用,在介体1-羟基苯并三唑（HBT）用量0.10%,漆酶用量100 U/L条件下作用40 min时,靛蓝脱色率达到96.7%。该方法采用的三相鼓泡塔生物反应器性能稳定、菌丝球可重复使用,该方法有利于漆酶的高效、规模化生产。     

Optimization of feed conditions in a 2.5-l fed-batch culture using rice oil to improve cephalosporin C production by <Emphasis Type="Italic">Cephalosporium acremonium</Emphasis> M25

Summary Rice oil significantly affected cephalosporin C production in a 2.5-l bioreactor culture of Cephalosporium acremonium M25. To improve cephalosporin C production, the feed conditions of rice oil were optimized. Reducing the feed rate of rice oil improved cephalosporin C production to 1.01 g/l when the consumption rate of rice oil decreased. Overall, under optimal feed conditions in the 2.5-l fed-batch culture, cephalosporin C production increased about four times compared to before optimization.     

Antibiotic production by Streptomyces aureofaciens using self-cycling fermentation

The self-cycling frementation (;rSCF) technique was applied to culture of Streptomyces aureofaciens. SCF is a method of continuous fermentation in which the metabolism of a microorganism is monitored by a measurement such as dissolved oxygen. These data are sent to a computer to allow it to control the system. Tetracycline production was observed only at exceedingly low iron concentrations in the growth medium. Repeatability of cycles was found to be dependent upon the presence of tetracycline in the fermentation broth as well as the strain of microorganism grown in the fermentor. Tetracycline was produced by an improved specific rate when compared to results in the literature for this organism grown using the batch method. (c) 1994 John Wiley & Sons, Inc.     

Effect of Tenuazonic Acid on In Vitro Amino Acid Incorporation by Rice Embryo Ribosomes

Deacetylcephalosporin C negative mutants, lacking a certain step in the pathway of deacetylcephalosporin C biosynthesis, were obtained from the deacetylcephalosporin C producing mutant No. 40 of Cephalosporium acremonium by treatment with N-methyl-N′-nitro-N-nitrosoguanidine. Among these mutants, the strain No. 40-20 was found to mainly accumulate a cephalosporin compound other than deacetylcephalosporin C and cephalosporin C. The cephalosporin was isolated as crystals from the culture broth of the mutant No. 40-20, and identified as deacetoxycephalosporin C, possessing a D-a-aminoadipyl side chain at C-7, by physical, chemical and biological methods. The profile of deacetoxycephalosporin C fermentation and the examination of the biochemical reduction of deacetylcephalosporin C led us to the conclusion that deacetoxycephalosporin C would be produced through de novo synthesis by this mutant.     

Use of mixed cultures for the fermentation of cereal-based substrates with potential probiotic properties

The production of a new cereal-based probiotic foods with suitable aroma, flavor and pH using mixed culture fermentation has been investigated. This required the selection of suitable types of cereal grains and probiotic microorganisms. In a medium of 5% (w/v) malt suspension the effects of yeast presence on the fermentation of a lactic acid bacterium (LAB), Lactobacillus reuteri, was studied. With different inoculum ratios between the yeast and the LAB, the characteristics of the fermentation broth including pH and the contents of free amino nitrogen (FAN), reducing sugar, lactic acid and ethanol were investigated. It was found that LAB growth was enhanced by the introduction of the yeast. In mixed culture broth pH was lowered and the production of lactic acid and ethanol were increased in comparison against pure LAB culture.     

Enhancement of growth and antibiotic titre inCephalosporium acremonium induced by sesame oil

The role of sesame oil as part of the carbon source on growth and cephalosporin C production byCephalosporium acremonium was studied in shake-flask fermentation. The growth and antibiotic production were maximum on the fifth and sixth day, respectively, irrespective of the presence of sesame oil. Sesame oil enhanced cephalosporin C production by 54%. Analysis of fatty acid profile indicated that C_18∶1, C_18∶2 and C_18∶3 are the major fatty acids inC. acremonium. The percentage of C_18∶2 was higher in the culture grown with sesame oil.     

Simultaneous solid–liquid separation and primary purification of clavulanic acid from fermentation broth of Streptomyces clavuligerus using salting‐out extraction system

Clavulanic acid (CA) is usually used together with other β‐lactam antibiotics as combination drugs to inhibit bacterial β‐lactamases, which is mainly produced from the fermentation of microorganism such as Streptomyces clavuligerus. Recently, it is still a challenge for downstream processing of low concentration and unstable CA from fermentation broth with high solid content, high viscosity, and small cell size. In this study, an integrated process was developed for simultaneous solid–liquid separation and primary purification of CA from real fermentation broth of S. clavuligerus using salting‐out extraction system (SOES). First, different SOESs were investigated, and a suitable SOES composed of ethanol/phosphate was chosen and further optimized using the pretreated fermentation broth. Then, the optimal system composed of 20% ethanol/15% K₂HPO₄ and 10% KH₂PO₄ w/w was used to direct separation of CA from untreated fermentation broth. The result showed that the partition coefficient (K) and recovery yield (Y) of CA from untreated fermentation broth were 29.13 and 96.8%, respectively. Simultaneously, the removal rates of the cells and proteins were 99.8% and 63.3%, respectively. Compared with the traditional method of membrane filtration or liquid–liquid extraction system, this developed SOES showed the advantages of simple operation, shorter operation time, lower process cost and higher recovery yield of CA. These results demonstrated that the developed SOES could be used as an attractive alternative for the downstream processing of CA from real fermentation broth.     

Production of Polyvinyl Alcohol Oxidase by a Symbiotic Mixed Culture

Production of polyvinly alcohol (PVA) oxidase by Pseudomonas sp. strain VM15C, a PVA degrader of a symbiotic PVA-utilizing mixed culture, was examined in various cultures. Despite the absence of PVA in the culture in nutrient broth, VM15C showed approximately the same productivity of PVA oxidase activity as that in the culture with PVA as the sole carbon source, whereas the productivity in the culture with glucose was lower than that of either the nutrient broth or the PVA culture. PVA oxidase activity produced in the nutrient broth culture was predominantly present in the cells, and most of the activity appeared to be in the cytoplasm. In contrast, in the culture with PVA as the sole carbon source, the activity was present in the culture fluid in a larger ratio than in the nutrient broth culture. Thus, production of PVA oxidase activity by this strain was constitutive and repressible, although localization of the produced activity was changed by growth conditions.