100～700 mL液体培养基的微波灭菌效果观察

为研究家用微波炉对少量液体培养基的灭菌效果,对100 -700 mL液体培养基采取微波分别进行灭菌,测定其灭菌时间,并对达到灭菌效果的培养基通过接种不同细菌进行质检.结果显示100、200、300、400、500、600、700 mL液体培养基分别在4.5、5.0、7.0、9.0、12.0、19.0、25.0 min达到最有效的灭菌效果.室温保存15 d仍无细菌生长.枯草杆菌黑色变种芽胞菌测试无菌生长.金黄色葡萄球菌、大肠埃希菌及普通变形杆菌在液体培养基里的生长现象、特种后细菌的菌落和形态染色特征及其生化反应均无明显差异.实验表明2 450 MHz,700 W的微波炉对100 - 700 mL的液体培养基不但能快速达到有效的灭菌效果,且营养成分不会被破坏.     

Sterilization of ginseng using a high pressure CO2 at moderate temperatures

The aim of this study was to determine the feasibility of using high pressure CO2 for sterilization of Ginseng powder, as an alternative method to conventional techniques such as gamma-irradiation and ethylene oxide. The Ginseng sample used in this study was originally contaminated with fungi and 5 x 10(7) bacteria/g that was not suitable for oral use. This is the first time that high pressure CO2 has been used for the sterilization of herbal medicine to decrease the total aerobic microbial count (TAMC) and fungi. The effect of the process duration, operating pressure, temperature, and amount of additives on the sterilization efficiency of high pressure CO2 were investigated. The process duration was varied over 15 h; the pressure between 100 and 200 bar and the temperature between 25 and 75 degrees C. A 2.67-log reduction of bacteria in the Ginseng sample was achieved after long treatment time of 15 h at 60 degrees C and 100 bar, when using neat carbon dioxide. However, the addition of a small quantity of water/ethanol/H2O2 mixture, as low as 0.02 mL of each additive/g Ginseng powder, was sufficient for complete inactivation of fungi within 6 h at 60 degrees C and 100 bar. At these conditions the bacterial count was decreased from 5 x 10(7) to 2.0 x 10(3) TAMC/g complying with the TGA standard for orally ingested products. A 4.3 log reduction in bacteria was achieved at 150 bar and 30 degrees C, decreasing the TAMC in Ginseng sample to 2,000, below the allowable limit. However, fungi still remained in the sample. The complete inactivation of both bacteria and fungi was achieved within 2 h at 30 degrees C and 170 bar using 0.1 mL of each additive/g Ginseng. Microbial inactivation at this low temperature opens an avenue for the sterilization of many thermally labile pharmaceutical and food products that may involve sensitive compounds to gamma-radiation and chemically reactive antiseptic agents.     

娄彻氏链霉菌ATCC10739产抗生素Borrelidin发酵条件优化及其分离纯化

对娄彻氏链霉菌ATCC10739固体发酵产生十八元大环内酯抗生素Borrelidin进行了发酵条件的优化。首先筛选得到了理想的发酵培养基;其次考察了发酵时间、起始pH值以及在ISP-2培养基中添加附加碳源、氮源对Borrelidin产量的影响。初步确定最适发酵条件为:ISP-2培养基中添加1%甘油,起始pH值为6.0,培养温度30°C,发酵时间为7 d,产量可达1.336 mg/L。采用有机溶剂萃取、硅胶层析和半制备型高效液相色谱(HPLC)等分离技术纯化得到Borrelidin。     

Diethylpyrocarbonate—An effective agent for the sterilization of different types of nutrient media

A simple and convenient method has been tested for the steriltzation of nutrient media for long-term cultivation of plant cells. Diethylpyrocarbonate is suitable for this task in concentrations about 1000 mg l^-1 The cells cultivated for 15 subsequent passages on media treated by DPC had the same growth parameters, production pattern and ability to transform exogeneous organic compounds as did the controls. The method is suitable for the preparatian of both liquid and agar media, for stabilization of stock solutions and for sterilization of cultivation vessels and tubing.Abbreviations DPC diethylpyrocarbonate - medium MS nutrient medium according to Murashige and Skoog - NAA naphtaleneacetic acid     

Opportunities for the application of real-time bacterial cell analysis using flow cytometry for the advancement of sterilization microbiology

Medical devices provide critical care and diagnostic applications through patient contact. Sterility assurance level (SAL) may be defined as the probability of a single viable micro-organism occurring on an item after a sterilization process. Sterilization microbiology often relies upon using an overkill validation method where a 12-log reduction in recalcitrant bacterial endospore population occurs during the process that exploits conventional laboratory-based culture media for enumeration. This timely review explores key assumptions underpinning use of conventional culture-based methods in sterilization microbiology. Consideration is given to how such methods may limit the ability to fully appreciate the inactivation kinetics of a sterilization process such as vaporized hydrogen peroxide (VH2O2) sterilization, and consequently design efficient sterilization processes. Specific use of the real-time flow cytometry (FCM) is described by way of elucidating the practical relevance of these limitation factors with implications and opportunities for the sterilization industry discussed. Application of FCM to address these culture-based limitation factors will inform real-time kinetic inactivation modelling and unlock potential to embrace emerging opportunities for pharma, medical device and sterilization industries including potentially disruptive applications that may involve reduced usage of sterilant.     

Automatic equipment for media sterilization

A device is described based on the principle of a simple analog computer which gives an exact determination of the moment at which the heat energy supply should be interrupted to attain a chosen sterilization effect. The temperature of the medium to be sterilized is measured and at temperatures above 100°C. the dependence of the thermal destruction coefficient of microbial spores on temperature is simulated. This variable is integrated with respect to time and the value of this integral at any given moment corresponds to the sterilization effect, at that moment. The device is also fitted with an extrapolator which evaluates, depending on the instantaneous temperature of the medium, the value of sterilization effect which will be produced during the cooling of the medium after the interruption of the heat, energy supply. The total sterilization effect, in the course of the cycle, is continuously and automatically evaluated as a sum of the integrated sterilization effect and of data supplied by the extrapolator. At the moment when this total sterilization effect attains the prescribed value, the device gives a signal for the interruption of the heat energy supply. The value of the sterilization effect is adjustable within broad limits and its evaluation is performed without substantial simplifying assumptions. By the use of this device an exact scale-up method for sterilizing media is achieved, yielding at the same time accurate reproducibility of media sterilization. An automatic control of the sterilization cycle is also possible by means of the device.     

Mixing and propulsion of the contents of the reticulo-rumen]

Roughage intake and digestion by ruminants involve complex interactions between the roughage constituents, the microorganisms in the reticulo-rumen (RR) and its motility. Ruminal digestion requires intense activity, ie comminution of feed particles and mixing and propulsion of digesta. The regular repetition of the contraction sequences in the RR every 50 to 70 s subjects the digesta to a consistent pattern of movements. The particles are distributed according to their functional density which depends on the density of the plant structure of the particle, the liquid inside the particle and also the gas, ie on the degree of particle fermentation. An interwoven mat of large low-density particles fills the dorsal sac and the top of the ventral sac of rumen. This mat traps part of the small high density particles. Squeezed by the contractions, the interwoven mat acts like a filter and lets a liquid containing small particles of high density pass into the bottom of the ventral sac. This liquid then flows into the reticulum and passes through the reticulo-omasal orifice (ROO). Chewing during rumination reduces particle size, eliminates particle gas and aids in separating the low-density particles, which are less fermented, from the heavy residues. The outflow of digesta, made possible by the opening of the ROO during the second phase of the reticular contraction, is highly selective. The effluent does not contain particles greater than 2 mm in size in sheep and 4 mm in cattle. This is due to the buoyancy of the large particles in the reticulum, to the self-filtration of the digesta during the passage through the ROO and possibly to backflow from the omasum to the reticulum. Finally, RR motor activity, ie continuously mixing the digesta and monitoring the evacuation of gas and outflow of digesta, allows the homeostasis in the rumen necessary to microbial fermentation. The characteristics of the ingested particles, their rates of size reduction and density increase, the consistency of digesta and the intensity of the rumen wall stimulations are all factors which depend on the nature of feed and intake level. Via mechanisms which are not yet all well known and/or quantified, these factors act upon the efficiency of the mixing and propulsion of the reticulo-ruminal content and thus upon the retention time of the feed in the RR as well as its digestive utilisation.(ABSTRACT TRUNCATED AT 400 WORDS)     

A dynamic mathematical model for microbial removal of pyritic sulfur from coal

A dynamic mathematical model has been developed to describe microbial desulfurization of coal by Thiobacillus ferrooxidans. The model considers adsorption and desorption of cells on coal particles and microbial oxidation of pyritic sulfur on particle surfaces. The influence of certain parameters, such as microbial growth rate constants, adsorption-descrption constants, pulp density, coal particle size, initial cell and solid phase substrate concentration on the maximum rate of pyritic sulfur removal, have been elucidated. The maximum rate of pyritic sulfur removal was strongly dependent upon the number of attached cells per coal particle. At sufficiently high initial cell concentrations, the surfaces of coal particles are nearly saturated by the cells and the maximum leaching rate is limited either by total external surface area of coal particles or by the concentration of pyritic sulfur in the coal phase. The maximum volumetric rate of pyritic sulfur removal (mg S/h cm(3) mixture) increases with the pulp density of coal and reaches a saturation level at high pulp densities (e.g. 45%). The maximum rate also increases with decreasing particle diameter in a hyperbolic form. Increases in adsorption coefficient or decreases in the desorption coefficient also result in considerable improvements in this rate. The model can be applied to other systems consisting of suspended solid substrate particles in liquid medium with microbial oxidation occurring on the particle surfaces (e.g., bacterial ore leaching). The results obtained from this model are in good agreement with published experimental data on microbial desulfurization of coal and bacterial ore leaching.     

Radiation Resistance of the Microflora Associated with Amniotic Membranes

Summary Amniotic membrane is widely used in the treatment of burn wounds and ulcers of various etiology. As it comes into contact with open wounds, it needs to be perfectly sterile to avoid the transmission of any disease. Accordingly, amniotic membrane needs to bear a high sterility assurance level (SAL). Conventionally, a radiation dose of 25 kGy is the generally accepted dose for sterilization. But to keep intact the biomechanical and other properties, it is sometimes proposed to use a lower dose without compromising an SAL of 10⁻⁶. The initial microbial contamination level and the radiation resistance of the contaminants determine the dose required for sterilization. The microbial species associated with the amniotic membrane from about 70 different batches were isolated. Twenty-two representative bacterial isolates were characterized and tested for survival in an incremental series of radiation doses from 0.5 to 5.0 kGy. The radiation decimal reduction dose (D₁₀) values for the strains were determined. Relatively higher D₁₀ values were recorded for the gram-positive isolates. The D₁₀ values of microbial isolates ranged from 0.16 to 1.3 kGy, and most resistant Bacillus strain had a D₁₀ value of 2.1 kGy. The radiation dose necessary to achieve an SAL of 10⁻⁶ was calculated based on the D₁₀values of the isolated strains. For a bioburden of 1000 Bacillus organism, the sterilization dose of 18.9 kGy is obtained. However, based on the experimental determination of D₁₀ of the radiation-resistant reference strain Bacillus pumilus, the adequate dose for radiation sterilization is found to be 19.8 kGy if bioburden level of 1000 is granted. The results substantiate that radiation dose of 25 kGy assures sterilization of amniotic membranes with bioburden level of 1000 colony forming units.     

Kinetics of sterilization of Lactobacillus brevis cells by the application of high voltage pulses

The technique of irreversible electroporation has been successfully applied to cause a lethal effect on Lactobacillus brevis cells suspended in phosphate buffer solution, Na(2)HPO(4)/NaH(2)PO(4) . H(2)O (0.845/0.186 mM) between parallel plane electrodes. Tests were carried out at different temperatures (24,45,60, and 80 degrees C) to determine if there was a synergistic effect of temperature and electric pulse treatment on the destruction of L. brevis. Experimental results indicate that the viability (log N/N(0); where N(0) and N are the number of cells survived per milliliter before and after pulse voltage application, respectively) of L. brevis decreased with electric field strength E and temperature T and treatment time t(t). The relations between log(N/N(0)) and t(t) and log(N/N(0)) and E indicate that higher field strengths are more effective than higher treatment times in causing destruction of L. brevis cells. It was also found that as the temperature of the liquid medium containing L. brevis cells increased from 24 to 60 degrees C, the death rate of L. brevis cells increased with a decrease in the total treatment time t(t) (pulse width x number of pulses applied). The application of an electric field strength E = 25 kV/cm at 60 degrees C and treatment time t(t) = 10 ms resulted in very high destruction levels of L. brevis cells (N/N(0) = 10(-9)). In comparison with existing steam sterilization technology, this new method of sterilization using relatively low temperature and short treatment time could prove to be an excellent method to minimize thermal denaturation of important nutrient components in liquid media. (c) John Wiley & Sons, Inc.     

Development of a fermentation method using immobilized cells under unsterile conditions. 2. Ethanol andl-lactic acid production without heat and filter sterilization

A process that was developed for protection of immobilized cells against inhibitory substances in the fermentation medium was applied for ethanol and lactic acid production with neither sterilization of the media, fermentor and other apparatus nor filtration of the aeration gas. The process involves co-immobilization of the fermentation micro-organism with castor oil and suppression of contaminant growth by addition of an anti-microbial substance to the fermentation medium. When 0.1%n-butyl,p-hydroxybenzoate (POBB) was added to the medium, ethanol and lactic acid productions were stable for 60 h and 70 h, respectively, while growth of the contaminants was completely suppressed. Longer process stability was achieved when POBB was replaced with Preventol GD, which has higher partition coefficient between castor oil and water. In this case, both glucose consumption and ethanol production were stable for 140 h. The possibilities of increasing the process stabilities were discussed.     

Oligotrophic bacteria in ultra-pure water systems: Media selection and process component evaluations

Summary Presently, tryptic soy agar (TSA) medium is used in the semiconductor industry to determine the concentration of viable oligotrophic bacteria in ultra-pure water systems. Deionized water from an ultra-pure water pilot plant was evaluated for bacterial growth at specific locations, using a non-selective medium (R2A) designed to detect injured heterotrophic as well as oligotrophic bacteria. Results were compared to those obtained using Tryptic Soy Agar. Statistically greater numbers of bacteria were observed when R2A was used as the growth medium. Total viable bacterial numbers were compared both before and after each treatment step of the recirculating loop to determine their effectiveness in removing bacteria. The reduction in bacterial numbers for the reverse osmosis unit, the ion exchange bed, and the ultraviolet sterilizer were 97.4%, 31.3%, and 72.8%, respectively, using TSA medium, and 98.4%, 78.4%, and 35.8% using R2A medium. The number of viable bacteria increased by 60.7% based on TSA medium and 15.7% based on R2A medium after passage of the water through an in-line 0.2-m pore size nylon filter, probably because of the growth of bacteria on the filter. Our results suggest that R2A medium may give a better representation of the microbial water quality in ultra-pure water systems and therefore a better idea of the effectiveness of the various treatment processes in the control of bacteria.     

Enhancement of L-glutamate oxidase production in liquid fermentation of Streptomyces sp. by calcium addition

Summary The effect of calcium ions on production of extracellular L-glutamate oxidase (GluOx) in liquid fermentation of Streptomyces sp. N1 was investigated. By supplementing a relatively large amount of Ca²⁺ (15–40 mM) to the medium, the GluOx production was significantly enhanced, although the microbial growth was inhibited to some degree. For the first time, the highest production (i.e. 6.5 U/ml) and productivity (i.e. 0.25 U/ml/h) of GluOx as ever reported (i.e., 1.2 U/g medium after 144 h solid state fermentation and 0.59 U/ml after 96 h liquid fermentation) were achieved with addition of 30 mM Ca²⁺.     

Sterilization of medical productsin low-pressure glow discharges

Results are presented from experimental and theoretical studies of the sterilization of medical products by the plasmas of dc glow discharges in different gas media. The sterilization efficiency is obtained as a function of discharge parameters. The plasma composition in discharges in N₂ and O₂ is investigated under the operating conditions of a plasma sterilizer. It is shown that free surfaces of medical products are sterilized primarily by UV radiation from the discharge plasma, while an important role in sterilization of products with complicated shapes is played by such chemically active particles as oxygen atoms and electronically excited O₂ molecules.     

Criteria for evaluating calcium carbonate from the point of view of chlortetracycline biosynthesis]

Calcium carbonate is added to fermentation media in biosynthesis of tetracyclines for providing definite pH values and binding tetracycline into insoluble complexes. Seven different samples were studied with respect to their physical properties, such as the microscopic size of the particles, their form, capacity for agglomeration, specific volume, rate of the particle precipitation and chemical properties, such as purity, buffer capacity, effect on the medium pH before and after sterilization. The above properties were studied in comparison with activity chlortetracycline biosynthesis. Microfine calcium carbonate proved to be the best from the point of view of productivity of Str. aureofaciens. With its use the activity of the culture fluid increased by 20 per cent as compared to the other samples. The titration curve of the sample had the lowest bend.     

Effect of the methods of sterilization on the quality of nutrient media and on the level of antibiotic production]

It was shown that conditions for heat sterilization of nutrient media for biosynthesis of antibiotics had an impact on their biochemical composition and activity of a fermentation broth in production of penicillin and erythromycin. The temperature of 120 degrees C and the time of 25 minutes proved to be optimal for sterilization of the media in regard to both preservation of their biochemical composition and providing of the maximum antibiotic productivity on the one hand and maintenance of the sterility during the fermentation process on the other hand.     

EXPLORING THE OPTIMUM CONDITIONS FOR MAXIMIZING THE MICROBIAL GROWTH OF Candida intermedia BY RESPONSE SURFACE METHODOLOGY

Exploring optimum and cost-efficient medium composition for microbial growth of Candida intermedia Y–1981 yeast culture growing on whey was studied by applying a multistep response surface methodology. In the first step, Plackett–Burman (PB) design was utilized to determine the most significant fermentation medium factors on microbial growth. The medium temperature, sodium chloride and lactose concentrations were determined as the most important factors. Subsequently, the optimum combinations of the selected factors were explored by steepest ascent (SA) and central composite design (CCD). The optimum values for lactose and sodium chloride concentrations and medium temperature were found to be 18.4 g/L, 0.161 g/L, and 32.4°C, respectively. Experiments carried out at the optimum conditions revealed a maximum specific growth rate of 0.090 1/hr; 42% of total lactose removal was achieved in 24 h of fermentation time. The obtained results were finally verified with batch reactor experiments carried out under the optimum conditions evaluated.     

L-asparaginase production by isolated Staphylococcus sp. - 6A: design of experiment considering interaction effect for process parameter optimization

AIMS: Evaluation of fermentation process parameter interactions for the production of l-asparaginase by isolated Staphylococcus sp. - 6A. METHODS AND RESULTS: Fractional factorial design of experimentation (L18 orthogonal array of Taguchi methodology) was adopted to optimize nutritional (carbon and nitrogen sources), physiological (incubation temperature, medium pH, aeration and agitation) and microbial (inoculum level) fermentation factors. The experimental results and software predicted enzyme production values were comparable. CONCLUSION: Incubation temperature, inoculum level and medium pH, among all fermentation factors, were major influential parameters at their individual level, and contributed to more than 60% of total l-asparaginase production. Interaction data of selected fermentation parameters could be classified as least and most significant at individual and interactive levels. Aeration and agitation were most significant at interactive level, but least significant at individual level, and showed maximum severity index and vice versa at enzyme production. SIGNIFICANCE AND IMPACT OF THE STUDY: All selected factors showed impact on l-asparaginase enzyme production by this isolated microbial strain either at the individual or interactive level. Incubation temperature, inoculum concentration, pH of the medium and nutritional source (glucose and ammonium chloride) had impact at individual level, while aeration, agitation and incubation time showed influence at interactive level. Significant improvement (ninefold increase) in enzyme production by this microbial isolate was noted under optimized environment.     

Effects of microorganisms on effective oxygen diffusion coefficients and solubilities in fermentation media

Effective oxygen diffusion coefficients and solubilities were measured for submerged cultures of Saccharomyces cerevisiae, Escherichia coli, and Penicillium chrysogenum. Both effective oxygen diffusion coefficients and solubilities were found to decrease with increasing cell concentrations in the fermentation media. Comparison of the experimental results of effective oxygen diffusion coefficients in fermentation media with values theoretically predicted on the assumption of unpenetrable microbial cells indicates that oxygen molecules diffuse through the cells during the diffusion process. Within the cell concentration range of typical submerged fermentations, the effective oxygen diffusion coefficient of the fermentation media can be described as D(e) = A(1)f + A(2)f(2). In this equation, fis the cell volume fraction and both A(1) and A(2) are functions of the shape of the cells and the ratio of effective oxygen diffusion coefficient in microbial cells to that in the medium.