Effect of the aeration and agitation states on tetracycline biosynthesis in semiproduction-capacity apparatus]

The results of the experiments on determination of the effect of aeration and agitation conditions on biosynthesis of tetracycline in the apparatus of semi-production capacity are discussed. It was shown that the antibiotic production level was not connected with the rate of oxygen solution expressed in the sulphite numbers, i.e. this parameter cannot be used as a scaling-up criterion. Accumulation of the antibiotic in the fermentation broth depended on the volume of the air supplied for aeration. It was determined that the level of CO2 dissolved in the fermentation broth did not reach the values having an inhibitory effect on the biosynthetic process.     

Influence of aeration during propagation of pitching yeast on fermentation and beer flavor

The effect of yeast propagated at different aeration conditions on yeast physiology, fermentation ability, and beer quality was investigated using three strains of Saccharomyces cerevisiae. It was shown that yeast cells grown under continuous aeration conditions during propagation were almost two times higher as compared with discontinuous aeration conditions. The maximum of cell growth of all samples reached between 36 h and 48 h. The concentration of trehalose was increased under continuous aerated yeasts, whereas glycogen was decreased. It was also observed that the concentration of glycogen and trehalose in yeast cells had no direct effect on subsequent fermentation ability. The effect of yeast propagated under different aeration conditions on subsequent fermentation ability was different from yeast strains, in which the influence will be most pronounced at the first fermentation. Later, the yeasts might regain its original characteristics in the following fermentations. Generally, continuously propagated yeast had a positive effect on beer quality in subsequent fermentation. Hence, the concentration of aroma compounds obtained with yeast propagated under 6 1/h for 48 h aeration was lower than those grown under other aeration conditions in the bottom yeasts; in particular, the amounts of phenylethyl alcohol, ester, and fatty acids were decreased.     

Effect of the aeration and agitation parameters on the oxytetracycline biosynthesis process under microkinetic conditions

The effect of the aeration levels in flasks on the rate of oxytetracycline biosynthesis and other kinetic characteristics was studied. It was shown that changes in the medium volume in flasks, dilution of the fermentation broth with water or its filtrate and the use of oxygen for aeration had a significant effect on the characteristics studied. Special experiments with low concentrations of the biomass were performed for investigation of the effect of dissolved carbon dioxide on the kinetics of the process.     

Modeling enzyme production with Aspergillus oryzae in pilot scale vessels with different agitation, aeration, and agitator types

The purpose of this article is to demonstrate how a model can be constructed such that the progress of a submerged fed-batch fermentation of a filamentous fungus can be predicted with acceptable accuracy. The studied process was enzyme production with Aspergillus oryzae in 550 L pilot plant stirred tank reactors. Different conditions of agitation and aeration were employed as well as two different impeller geometries. The limiting factor for the productivity was oxygen supply to the fermentation broth, and the carbon substrate feed flow rate was controlled by the dissolved oxygen tension. In order to predict the available oxygen transfer in the system, the stoichiometry of the reaction equation including maintenance substrate consumption was first determined. Mainly based on the biomass concentration a viscosity prediction model was constructed, because rising viscosity of the fermentation broth due to hyphal growth of the fungus leads to significant lower mass transfer towards the end of the fermentation process. Each compartment of the model was shown to predict the experimental results well. The overall model can be used to predict key process parameters at varying fermentation conditions.     

Optimization of ectoine synthesis through fed-batch fermentation of Brevibacterium epidermis

A production process for ectoine has been developed, using Brevibacterium epidermis DSM20659 as the producer strain. First, the optimal conditions for intracellular synthesis of ectoine were determined. The size of the intracellular ectoine pool is shown to be dependent on the external salt concentration, type of carbon source, and yeast extract concentration. Under the optimized conditions of 1 M NaCl, 50 g/L monosodium glutamate, and 2.5 g/L yeast extract, a maximum concentration of intracellular ectoine of 0.9 g/L was obtained in shake flask cultures. After optimizing the batch fermentation parameters of temperature, pH, agitation, and aeration, the yield could be further increased by applying the fed-batch fermentation principle in 1.5- to 2-L fermentors. Glutamate and yeast extract were fed to the bacterial cells such that the total glutamate concentration in the broth remained constant. A total yield of 8 g ectoine/L fermentation broth was obtained with a productivity of 2 g ectoine/L/day. After the bacterial cells were harvested from the culture broth, the ectoine was recovered from them by a two-step extraction with water and ethanol. Crystallization of the product was obtained after concentration of the extract via evaporation under reduced pressure. After this downstream process, 55% of the ectoine produced in the fermentor could be crystallized in four fractions. The first fractions were of very high purity (98%). This production process can compete with other described production processes for ectoine in productivity and simplicity. Further advantages are the relatively low amounts of NaCl needed and the absence of hydroxyectoine, often a byproduct, in the final product.     

Influence of the intensity of oxygen mass transfer on the biosynthesis of amphotericin B

Influence of oxygen mass transfer intensity characterized by the rate of oxygen dissolution (S) and the agitation rate (n), as well as influence of dissolved oxygen concentration on the process of amphotericin B biosynthesis was studied. It was shown that S = 40 and 110 mg/l. min and n = 450 and 800 min-1 were respectively the lower and the upper levels of the optimal conditions by oxygen mass transfer during amphotericin B biosynthesis. When biosynthesis of amphotericin B was conducted under conditions of the optimal oxygen mass transfer, the dissolved oxygen concentration of about 12 to 15 per cent of the saturation level was critical for the culture respiration. Inhibition of the culture respiration and antibiotic synthesis was induced under conditions of increased oxygen mass transfer intensity (S greater than 110 mg/l. min and n greater than 800 min-1) by high intensity mechanical agitation of the fermentation broth. Under conditions of decreased oxygen mass transfer (S less than 40 mg/l. min and n = less than 450 min-1) it was induced by insufficient supply of oxygen to the culture. On the basis of the results it was shown possible to control the aeration and agitation conditions by the rate of oxygen uptake and dissolved oxygen concentration. The data should be considered in optimization of aeration and agitation conditions in biosynthesis of amphotericin B in large fermenters.     

On-line extraction of volatile fatty acids in acidogenic chemostat culture using a supported liquid membrane

An on-line extraction of volatile fatty acids (acetic and butyric acids) from acidogenic fermentation in chemostat cultures using a supported liquid membrane (SLM) was investigated in order to overcome end-product inhibition. By using SLM, the high-cell-density retaining dilution rate of the chemostat could be increased, thus enhancing the microbial acidogenesis. To further understand this phenomenon, the growth and extraction kinetics were studied. The effect of substrate concentration was found to obey the Haldane equation. Regarding the inhibition by volatile fatty acids, it turned out that undissociated butyric acid rather than acetic acid severely inhibited the growth, corresponding to non-competitive kinetics. The extraction rates of the acids were proportional to their undissociated concentration as well as to the SLM area/broth volume, and butyric acid extraction was easier than that of acetic acid.     

Long-term repeated fed-batch ethanol fermentation in aerated condition

In this study, we attempted to assess the process stability of long-term fed-batch ethanol fermentation in the absence and presence of aeration (0.33 vvm). To examine the effect of aeration, a long-term repeated fed-batch operation was conducted for 396 h to mimic a long-term industrial bioethanol production process. In this long-term repeated fed-batch ethanol fermentation experiments, withdrawal-fill operation were conducted every 36 h for 10 repeat cycles. The whole operation was stably sustained in a quasi-steady state. The average maximal cell concentration and the average maximal ethanol production during operation were increased by 81.63 and 12.12%, respectively, when aeration was used. In addition, since aeration was carried out, the average ethanol yield slightly decreased by 4.03% and the average specific ethanol production rate decreased by 46.75% during operation. However, the average ethanol productivity increased by 17.53% when aeration was carried out. After 396 h of long-term repeated fed-batch ethanol fermentation, 1,908.9 g of ethanol was cumulatively produced when aeration was used, which was 12.47%, higher than when aeration was not used (1,697.2 g). Meanwhile, glycerol production was greatly decreased during long-term repeated fed-batch ethanol fermentation, in which the glycerol concentration in the culture broth decreased from about 34∼15 g/L. Thus, we can conclude that cell growth was greatly improved by overcoming ethanol inhibition and glycerol production was remarkably decreased when aeration was carried out, although aeration in ethanol fermentation decreased the specific ethanol production rate and ethanol yield.     

Production of acetone butanol ethanol (ABE) by a hyper-producing mutant strain of Clostridium beijerinckii BA101 and recovery by pervaporation.

A silicone membrane was used to study butanol separation from model butanol solutions and fermentation broth. Depending upon the butanol feed concentration in the model solution and pervaporation conditions, butanol selectivities of 20.88-68.32 and flux values of 158.7-215.4 g m(-)(2) h(-)(1) were achieved. Higher flux values (400 g m(-)(2) h(-)(1)) were obtained at higher butanol concentrations using air as sweep gas. In an integrated process of butanol fermentation-recovery, solvent productivities were improved to 200% of the control batch fermentation productivities. In a batch reactor the hyper-butanol-producing mutant strain C. beijerinckii BA101 utilized 57.3 g/L glucose and produced 24.2 g/L total solvents, while in the integrated process it produced 51.5 g/L (culture volume) total solvents. Concentrated glucose medium was also fermented. The C. beijerinckii BA101 mutant strain was not negatively affected by the pervaporative conditions. In the integrated experiment, acids were not produced. With the active fermentation broth, butanol selectivity was reduced by a factor of 2-3. However, the membrane flux was not affected by the active fermentation broth. The butanol permeate concentration ranged from 26.4 to 95.4 g/L, depending upon butanol concentration in the fermentation broth. Since the permeate of most membranes contains acetone, butanol, and ethanol (and small concentrations of acids), it is suggested that distillation be used for further purification.     

埃博霉素B小试发酵罐发酵条件研究

研究了纤维堆囊菌(Sorangium cellulosum)So F5-76在5 L发酵罐水平上发酵生产埃博霉素B的基本工艺参数,具体考察了接种量、搅拌转速、通气量、添加消泡剂及补糖等5个工艺参数对埃博霉素B发酵产量的影响。最后确定发酵罐基本发酵条件为接种量9%,搅拌转速180 r/min,空气流量3.5 L/min,消泡剂种类选择Antifoam B聚醚类消泡剂,补糖控制在发酵液糖浓度为0.2 g/L,在此条件下埃博霉素B的产量可达25.6 mg/L。     

不同碳源和生长因子条件下粒毛盘菌代谢产物初步研究

采用GC-MS法对一种粒毛盘菌(Lachnum sp.)在不同碳源、生长因子条件下发酵代谢产物的挥发性成分组成与差异进行分析。结果显示,不同碳源和生长因子条件下产生的代谢产物不同,主要包括有机酸、胺类、烷烃类、酯类、醇类、吡咯等物质。分别以20 g/L的葡萄糖、蔗糖、淀粉为碳源的发酵液中检测到的挥发性代谢产物为7、7、10种;添加1 mg/L的V_C、V_(B1)、甘氨酸、色氨酸作为不同生长因子的发酵液中检测到的挥发性代谢产物分别为6、7、7、12种。结果显示粒毛盘菌YM406发酵代谢产物具有丰富的多样性,并且在不同的培养条件下产生的代谢产物存在一定的差异。     

Effect of culture parameters on tobramycin biosynthesis

The effect of temperature, aeration and active acidity of the medium on biosynthesis of tobramycin was studied. The optimal temperature conditions (37 degrees C) were developed. It was shown that biosynthesis of tobramycin depended on the aeration conditions, especially at the beginning of the fermentation process. The initial pH 4.9-6.35 and 6.35-7.1 were found to be optimal for the growth of the tobramycin-producing organism and biosynthesis of the antibiotic, respectively.     

Product inhibition and its removal on josamycin fermentation by Streptomyces narbonensis var. josamyceticus

Josamycin formation was shown to be closely associated with the degree of mycelial growth. Media using glycerol or glucose were slight in josamycin accumulation. However, the mycelial growth and product formation were interrupted in the course of the fermentation. The self-resistance level of the producing organism against josamycin was shown to be not higher than 1 mg per ml. In media using fatty oil, the organism grew smoothly and gave a concentration of josamycin at least 5 times higher than the self-resistance levelMost of the josamycin was distributed in the oily phase of the broth. The josamycin concentration of the water phase of the broth was less than the self-resistance level, except in the later period of the fermentation. Unsaturated fatty acids remaining in the broth were found to be the best extractors of josamycin. It was concluded that the enhanced josamycin accumulation of this fermentation resulted from the removal of the product inhibition.     

Industrial production of disodium 5′-guanylate

A process for manufacturing disodium 5′-guanylate was devised. 5′-Amino 4-imidazole carboxamide riboside (AICA-R) was accumulated with an amount over 100 times those reported in the literature by fermentation of D -glucose with a non-exacting purineless mutant derived from Bacillus megaterium JAM 1245) by x-ray irradiation. The influence of RNA, amino acids, and salts on AICA-R accumulation was clarified. Appropriate aeration and agitation was found necessary. The (60-hr, cultivation of the medium containing 8% of D -glucose gave AICA-R in the concentration above, 11 g/l. AICA-R thus accumulated was separated from the fermentation broth by ion-exchange technique and subjected to synthetic processes to yield disodium 5′-guanylatc with the yield over 40%, based on AICA-R.     

土传真菌病害拮抗菌的筛选及其生防效果研究

为了获得对主要粮食作物水稻、小麦和经济作物大豆常见土传病害具有防治效果的生防菌,本研究从土壤中筛选到一株对所选6种病原真菌均有较好拮抗效果的菌株。基于形态学、生理生化特性及16S rDNA序列分析进行菌种鉴定,利用菌丝生长速率法对其无菌滤液和挥发性气体的抑菌效果进行验证,同时研究了其无菌滤液的热稳定性、酸碱稳定性和对蛋白酶K的稳定性。结果表明:本研究筛选到一株贝莱斯芽孢杆菌Bacillus velezensis CX-2,其无菌滤液对6种病原真菌的抑菌率在71%~95%之间,对小麦纹枯病菌、小麦全蚀病菌的抑菌率分别高达90.13%、94.34%;挥发性气体对6种病原菌的抑菌率在45%~80%之间;无菌滤液中的抗菌活性物质具有较强的热稳定性和对蛋白酶K的稳定性;无菌滤液pH在5~9之间时具有稳定的抑菌活性。该菌株可作为作物土传真菌病害生防菌剂较为理想的功能菌株。     

Oxygen requirement and energy relations of itaconic acid fermentation by Aspergillus terreus NRRL 1960

The effect of interrupting aeration on itaconic acid fermentation by A. terreus NRRL 1960 has been studied. Under the conditions used, stopping aeration for 5 min led to a complete cessation of itaconic acid production, which was only slowly restored after 24 h when aeration was resumed. After a 5-min break in aeration and in the presence of 0.1 mM cycloheximide no itaconic acid was formed even after 3 days. It seems that, upon oxygen shortage, a rapid destruction of the itaconic-acid-producing mechanism takes place, which is restored only aerobically in a slow process involving protein synthesis. Itaconic acid fermentation is also effectively stopped by metabolic inhibitors of ATP formation, pointing to the need for biochemical energy in maintaining the fermentation. ATP is possibly needed to maintain a proper physiological (i.e. near neutral) pH inside the cells, counteracting the acid produced in the fermentation process and the low external pH (below 2.0). Inhibitors of plasma membrane ATPase have no effect on itaconic acid fermentation. This indicates that the plasma membrane might be impermeable to H⁺ and that ATP might rather be involved in the transport of itaconic acid out of the cell. It is suggested that insufficient aeration may leads to insufficient production of ATP which, in turn, leads to damage of the metabolic machinery by acid produced in the fermentation process.     

Effects of the addition of different nitrogen sources in the tequila fermentation process at high sugar concentration

AIMS: To study the effect of the addition of different nitrogen sources at high sugar concentration in the tequila fermentation process. METHODS AND RESULTS: Fermentations were performed at high sugar concentration (170 g l(-1)) using Agave tequilana Weber blue variety with and without added nitrogen from different sources (ammonium sulfate; glutamic acid; a mixture of ammonium sulfate and amino acids) during the exponential phase of growth. All the additions increased the fermentation rate and alcohol efficiency. The level of synthesis of volatile compounds depended on the source added. The concentration of amyl alcohols and isobutanol were decreased while propanol and acetaldehyde concentration increased. CONCLUSIONS: The most efficient nitrogen sources for fermentation rate were ammonium sulfate and the mixture of ammonium sulfate and amino acids. The level of volatile compounds produced depended upon types of nitrogen. The synthesis of some volatile compounds increased while others decreased with nitrogen addition. SIGNIFICANCE AND IMPACT OF THE STUDY: The addition of nitrogen could be a strategy for improving the fermentation rate and efficiency in the tequila fermentation process at high sugar Agave tequilana concentration. Furthermore, the sensory quality of the final product may change because the synthesis of the volatile compounds is modified.     

Regulation of the biosynthesis of aminoacylase and pigments by strains of Actinomyces of the genus Streptoverticillium

For using actinomyceteous extracellular aminoacylase in production of optically active amino acids it is necessary to have the fermentation broth with lowered contents of extracellular pigments whose accumulation dynamics in the process of the strain growth correlates with the dynamics of the enzyme biosynthesis. The results of the studies showed that it was possible to regulate biosynthesis of the aminoacylase and pigments in the direction of increasing the enzyme production and decreasing the pigment formation by using a medium of the respective composition and providing the respective high temperature and sufficient aeration for the strains.     

Characteristics of the methane fermentation of waste of animal husbandry complexes with respect to the biomass of microorganisms and volatile fatty acids

The content of microbial biomass and the concentration of volatile fatty acids were comparatively studied in the tanks where the waste products of three stock farms were subjected to methane fermentation. The biomass content was shown to vary from 19 to 30% of the dry matter weight and the concentration of volatile fatty acids from 0 to 4.5 g per litre. The low concentrations of acetic and propionic acids together with the high biomass content were indicative of an active balanced microbial association. The parameters can be used to assess the operation of methane fermentation tanks.     

Changes in morphology of Paecilomyces japonica and their effect on broth rheology during production of exo-biopolymers

The influence of Paecilomyces japonica pellet morphology on fermentation broth rheology and exobiopolymer production was investigated in a 5-1 jar fermenter. Rapid formation of pellets was observed after the first day of fermentation; and these slowly increased in size and roughness. This, together with the increase in biomass concentration, altered the transport characteristics and broth rheology towards a pseudoplastic nature which, in turn, influenced cell growth and exo-biopolymer production. At mild agitation, high aeration and optimum substrate concentration, pellets were the most predominant morphological form, compared with free mycelia. The broth rheology showed pseudoplastic behavior; and the fungal morphology was closely related to the rheological properties.