Liquid-phase mass transfer coefficients in bioreactors

Liquid-phase mass transfer coefficient in bioreactors have been examined. A theoretical model based on the surface renewal concept has been devloped. The predicted liquid-phase mass transfer coefficients are compared with the experimental data for a mycelial fermentation broth (Chaetomium cellulolyticum) and model media (carboxymethyl cellulose) in a bench-scale bubble column reactor. The liquid-phase mass transfer coefficient is evaluated by dividing the volumetric mass transfer coefficient obtained experimentally by the specific surface area estimated using the available correlations. The available literature data in bubble column and stirred tank bioreactors is also used to test the validity of the proposed model. A reasonable agreement between the model and the experimental data is found.     

Fermentation of cellulosic materials to mycoprotein foods

A new bioprocess is described in which a cellulolytic, food-grade fungus Neurospora sitophila converts cellulosic materials to protein-rich products for food and fodder. The optimal conditions for the conversion are identified: 35-37 degrees C temperature, pH 5.5, 2.35 ms(-1) agitator tip speed. Scale-up of the production process to 1,300 L is reported. The mycoprotein production data on several types of cellulosic materials (sugarcane bagasse, corn stover, wood cellulose) are presented. The performance of N. sitophila is found to compare favourably with that of Chaetomium cellulolyticum, another cellulolytic organism previously reported on by us.     

Oxygen transfer in slurry bioreactors

The oxygen transfer in bioreactors with slurries having a yield stress was investigated. The volumetric mass transfer coefficients in a 40-L bubble column with simulated fermentation broths, the Theological properties of which were represented by the Casson model, were measured. Experimental data were compared with a theoretical correlation developed on the basis of a combination of Higbie's penetration theory and Kolmogoroff's theory of isotropic turbulence. Comparisons between the proposed correlation and data for the simulated broths show good agreement. The mass transfer data for actual mycelial fermentation broths reported previously by the authors were re-examined. Their Theological data was correlated by the Bingham plastic model. The oxygen transfer rate data in the mycelial fermentation broths fit the predictions of the proposed theoretical correlation.     

Oxygen solubilities in fermentation fluids

Summary Fermentation media consist of a large number of chemicals whose composition undergoes alteration during the course of fermentation. As a result of this, conventional methods and correlations for oxygen solubility measurement and prediction do not apply in these systems. Using a physical method, oxygen solubilities were measured in simulated chemical systems and in fermentation broths. Sugars, salts, and fermentation products were identified as major factors influencing oxygen solubility. Salt effect was correlated with electrical conductivity of the medium, which was easy to measure during fermentation. For mixtures and for fermentation medium, individual influences were found to be log-additive in accordance with Danckwerts (1970).     

Hydrodynamics in bubble column bioreactors with fermentation broths having a yield stress

Summary The hydrodynamics in a bubble column bioreactor with fermentation broths having a yield stress are studied. Specifically, the liquid velocity at the reactor axis, the axial dispersion coefficient, and the gas hold-up are examined. The liquid velocity at the reactor axis and the gas hold-up are measured in a 40-1 bench-scale bubble column fermentor using carboxypolymethylene (Carbopol) aqueous solutions as simulated broths. Theoretical correlations for the liquid velocity at the reactor axis, the axial dispersion coefficient, and the gas hold-up are derived on the basis of an energy balance and the mixing length theory. The correlations are compared with the present data and a reasonable agreement is found. The theoretical predictions are also in satisfactory agreement with the re-examined data for actual fermentation broths which are Chaetomium cellulolyticum and Neurospora sitophila cultured in a 1000-1 pilot-plant scale airlift fermentor.     

Determination of carbohydrates, sugar alcohols, and glycols in cell cultures and fermentation broths using high-performance anion-exchange chromatography with pulsed amperometric detection

Cell cultures and fermentation broths are complex mixtures of organic and inorganic compounds. Many of these compounds are synthesized or metabolized by microorganisms, and their concentrations can impact the yields of desired products. Carbohydrates serve as carbon sources for many microorganisms, while sugar alcohols (alditols), glycols (glycerol), and alcohols (methanol and ethanol) are metabolic products. We used high-performance anion-exchange chromatography with pulsed amperometric detection (HPAE-PAD) to simultaneously analyze for carbohydrates, alditols, and glycerol in growing yeast (Saccharomyces cerevisiae) cultures and their final fermentation broths. Both cultures were grown on complex undefined media, aliquots centrifuged to remove particulates, and the supernatants diluted and directly injected for analysis. Pulsed amperometry allowed a direct detection of the carbohydrates, alditols, and glycols present in the cultures and fermentation broths with very little interference from other matrix components. The broad linear range of three to four orders of magnitude allowed samples to be analyzed without multiple dilutions. Peak area RSDs were 2-7% for 2, 3-butanediol, ethanol, glycerol, erythritol, rhamnose, arabitol, sorbitol, galactitol, mannitol, arabinose, glucose, galactose, lactose, ribose, raffinose, and maltose spiked into a heat-inactivated yeast culture broth supernatant that was analyzed repetitively for 48 h. This method is useful for directly monitoring culture changes during fermentation. The carbohydrates in yeast cultures were monitored over 1 day. A yeast culture with medium consisting primarily of glucose and trace levels of trehalose and arabinose showed a drop in sugar concentration over time and an increase in glycerol. Yeast growing on a modified culture medium consisting of multiple carbohydrates and alditols showed preference for specific carbon sources and showed the ability to regulate pathways leading to catalysis of alternative carbon sources.     

Comparative evaluation of stability of benzylpenicillin in acid media of natural solutions and in culture fluid]

Inactivation of benzylpenicillin in real media i.e. fermentation broths and their filtrates was studied in comparison with the published data on inactivation of commercial benzylpenicillin in aqueous solutions as dependent on the medium pH and temperature. The lowest constant of benzylpenicillin inactivation was shown to be in the fermentation broths.     

Formation of Desacetylcephalosporin C in Cephalosporin C Fermentation

The origin of desacetylcephalosporin C in cephalosporin C fermentation broths was investigated. Esterase activity was detected in cell-free extracts of Cephalosporium acremonium, but these extracts failed to deesterify cephalosporin C. When cephalosporin C was added to sterile and inoculated fermentation media, the antibiotic decayed at nearly identical rates. The formation of desacetylcephalosporin C during the fermentation was measured by quantitative chromatography and by the incorporation of valine-1-(14)C into the molecule. The rate constants obtained from the results of these experiments were equivalent to those for the decay of cephalosporin C in sterile and inoculated media. The data demonstrate that desacetylcephalosporin C is produced by nonenzymatic hydrolysis of cephalosporin C.     

Improvement of production,assay and purification of streptavidin

Summary The production of streptavidin byStreptomyces avidinii in several different media was examined at 24, 48 and 72 hours. Flask studies indicated that fermentation media containing either complex or multiple carbon sources resulted in higher yields of streptavidin than media with a single carbon source. Streptavidin could be detected in crude fermentation broths by use of a tritiated biotin binding assay. This assay appears to give useful estimates of streptavidin production. Depending upon the medium employed, streptavidin yields ranged from 0.5 mg/l to 53 mg/l. Production was successfully scaled up to ten liter fermentors. Streptavidin was purified in a one step process from centrifuged, concentrated fermentation broths by binding the protein to an iminobiotin column at pH 11 followed by elution at pH 4.0. Recovery percentages varied depending upon the solubility of the fermentation media ingredients.     

豚草种带内生真菌及其对种子发芽和幼苗生长的影响

内生真菌是一类共生于植物体内,能够不同程度影响宿主植物生态适应性和竞争能力的微生物。分析内生真菌在豚草种子中的分布、种群结构,以及内生真菌发酵液对种子发芽和幼苗生长的作用。结果显示:发生于6个地区的豚草种子均能分离获得内生真菌,分离率在19%—92.63%之间,不同地区之间差异极显著(P0.01)。内生真菌主要存在于种子的总苞部位,分离率达到65.52%。发生于福建省长乐市松下镇的豚草种带内生真菌种群包含5个属,以链格孢属(Alternaria)真菌为优势菌群,占82.26%;其次为镰孢属(Fusarium)真菌,占9.68%;其它3个属的真菌发生较少,均低于5%。内生真菌主要以水平传播方式在豚草不同世代之间传播。供试的7个内生真菌菌株的发酵液均不同程度地抑制豚草种子发芽,降低幼苗地上部高度、根长度、根数量和总生物量,但不同菌株发酵液之间抑制程度差异明显,显示不同菌株对豚草种子发芽和幼苗生长产生不同的影响。内生真菌发酵液处理后的种子仍然保持较高程度的活力;不同内生真菌发酵液处理后,有活力的种子维持在50%—87.5%之间,均高于(或等于)清水处理的种子,说明内生真菌代谢产物只是抑制种子的发芽,但并不导致种子的腐烂和死亡。这些研究结果初步显示种子携带的内生真菌可能在豚草入侵生物学中发挥重要的作用。     

Sporulation of Clostridium cellulolyticum while grown in cellulose-batch and cellulose-fed continuous cultures on a mineral-salt based medium

Clostridium cellulolyticum sporulation was investigated during growth on cellulose fibers in a mineral-salt based medium which corresponds to conditions linked to its natural ecological niche. At steady state of the continuous cultures under limitation and with an excess of cellulose and/or ammonium, bacterial cells mainly sporulated at low dilution rates (D), at least 10% sporulation being observed at the lowest D tested. Increasing the cellulose concentration in the feed-medium reservoir increased the percentage of spores in the bioreactor. It appeared that the remaining undigested cellulose could serve as an exogenous carbon source supply at a continuous but limited rate throughout the sporulation process. In addition to the proportion of carbon and nitrogen, the influence of the environmental pH on spore formation was studied. In cellulose-fed continuous cultures at a constant D and a pH decreasing from 7.2 to 6.4, the percentage of spores increased to 14% at the lowest pH tested. When C. cellulolyticum was grown in batch culture, the level of sporulation was dramatically higher in unregulated-pH fermentation compared to pH-controlled growth conditions at pH 7.2 since in the former it reached 45% within 5 days of cultivation. It then appeared that a low specific growth rate and a low environmental pH in the presence of an insoluble carbon substrate were the major factors inducing sporulation in C. cellulolyticum. Furthermore, since the spores adhere to the carbon substrate (the cellulose) the bacteria gain advantages when the environment allows germination thanks to the recovery of suitable growth conditions. By allowing the maintenance and the integrity of the bacteria in the microbiota, spore formation could then explain the successful survival of C. cellulolyticum in cellulosic anaerobic habitats where low environmental pH conditions are often found.     

Vibrating membrane filtration for recovery and concentration of insect killing nematodes

New experimental data are reported that demonstrate the use of a novel vibrating membrane filter (VMF) for the combined recovery and concentration of two species of nematodes, S. feltiae and P. hermaphrodita, from mature liquid fermentation cultures. The disk membrane module had a working surface area of 0.2 m(2) and was operated at a constant flow rate of 0.2 m(3) h(-1). The recovery of the viable nematodes from the spent media and nonviable nematodes was assisted by an independently imposed oscillatory motion of the disk assembly, which produced an intense shear field at the membrane surface with calculated mean values on the order of 10(4) s(-1). Adult (nonviable) nematodes in the fermentation culture were preferentially dissolved in a detergent (sodium dodecylsulfate) and successfully separated from the juveniles using the VMF equipment. Permeate fluxes on the order of 15 to 30 L/m(2/)h were achieved for an operating transmembrane pressure of 800 mbar. Industrial-scale liquid fermentation for the manufacture of nematodes as biopesticides produces the viable nematode life stages in low-concentration suspension containing large quantities of spent media and other waste material. The VMF equipment provided a flexible operation for separation, cleaning, and concentration of viable nematodes from the fermentation broths.     

Enhancing penicillin fermentations by increased oxygen solubility through the addition of n-hexadecane

n-Hexadecane was added to fermentation media to increase the medium oxygen solubilities, thus enhancing oxygen transfer rates in penicillin fermentations. For shake flask fermentations, cells were found to grow faster in the flasks with n-hexadecane than those without. The addition of n-hexadecane to penicillin fermentations was shown to significantly increase cell growth and penicillin production and reduce formation of mycelial pellets. The result was attributed to the enhancement of oxygen transfer in mycelial fermentations due to the higher oxygen solubilities of fermentation media achieved by adding n-hexadecane.     

Use of the glucose oxidase system to measure oxygen transfer rates

This investigation used the glucose oxidase system to simulate oxygen transfer rate in fermentation broths. It was demonstrated that the fungal preparation contained sufficient lactonase activity so that D -glucono-δ-lactone did not accumulate and that the rate of production of gluconic acid was proportional to the oxygen uptake rate. Enzyme concentrations of 1.5–2 g/1 were found adequate to determine oxygen absorption rates in shake flasks while maintaining the dissolved oxygen concentration of low levels. The apparent Michaelis constant for oxygen, K_m(O₂), was found to be 27% saturation with air; this value along with experimentally determined uptake rates could be used to calculate dissolved oxygen concentration in lieu of using a dissolved oxygen probe. Enzyme concentrations of 5 g/l were sufficient to give linear acid production and low dissolved oxygen concentrations in a bench-scale fermenter with no foaming or enzyme deactivation. The method is considered more valid and easier to employ than previously utilized techniques such as sulfite oxidation. Extension of the system to evaluating aeration effectiveness and scaleup of fermentation equipment is discussed.     

Relationship between morphology,rheology and polygalacturonase production by Aspergillus sojae ATCC 20235 in submerged cultures

A full factorial statistical design, with the factors of, two taxonomically different strains, seven types of seed culture formulations (slants) and two types of fermentation media were used to investigate the effect of these parameters on the morphology and polygalacturonase production. The rheology of the final fermentation medium was analyzed and appropriate mathematical model was applied to calculate suspension viscosity. It was found that most fermentation broths showed non-Newtonian flow behavior. According to statistical analysis, factors of strain types and fermentation media and the interaction between them were found significant on the enzyme activity. The effect of seed culture formulations (slants) were found insignificant at the significance level of 1%. Interaction of slants with strain types and fermentation media were also found insignificant. Considering the morphology of the final culture, Aspergillus sojae with the desired pellet morphology in a complex media, inoculated with a seed culture prepared from molasses resulted in maximum polygalacturonase enzyme activity (0.2 U/ml) and lowest suspension viscosity with a broth rheology close to Newtonian flow behavior.     

Relationships between cellobiose catabolism, enzyme levels, and metabolic intermediates in Clostridium cellulolyticum grown in a synthetic medium

Continuous cultures, under cellobiose sufficient concentrations (14. 62 mM) using a chemically defined medium, were examined to determine the carbon regulation selected by Clostridium cellulolyticum. Using a synthetic medium, a q(cellobiose) of 2.57 mmol g cells(-1) h(-1) was attained whereas the highest value obtained on complex media was 0.68 mmol g cells(-1) h(-1) (Payot et al. 1998. Microbiology 144:375-384). On a synthetic medium at D = 0.035 h(-1) under cellobiose excess, lactate and ethanol biosynthesis were able to use the reducing equivalents supplied by acetic acid formation and the H(2)/CO(2) ratio was found equal to 1. At a higher dilution rate (D = 0.115 h(-1)), there was no lactate production and the pathways toward ethanol and NADH-ferredoxin-hydrogenase contributed to balance the reducing equivalents; in this case a H(2)/CO(2) ratio of 1.54 was found. With increasing D, there was a progressive increase (i) in the steady-state concentration of NADH and NAD(+) pools from 11.8 to 22.1 micromol (g cells) (-1), (ii) in the intracellular NADH/NAD(+) ratios from 0.43 to 1.51. On synthetic media, under cellobiose excess the carbon flow was also equilibrated by three overflows: exopolysaccharide, extracellular protein, and amino acid excretions. At D = 0.115 h(-1), 34% of the cellobiose consumed was converted into exopolysaccharides; this deviation of the carbon flow and the increase of the phosphoroclastic activity decreased dramatically the pyruvate excretion and explained the break in lactate production. Whatever the dilution rate, C. cellulolyticum, using ammonium and cellobiose excess, always spilled usual amino acids accompanied by other amino compounds. In vitro, GAPDH, phosphoroclastic reaction, alcohol dehydrogenase, and acetate kinase activities were high under conditions giving high in vivo specific production rates. There were also correlations between the in vitro lactate dehydrogenase activity and in vivo lactate production, but in contrast with the preceding activities, these two parameters decreased with D. All the results demonstrate that C. cellulolyticum was able to optimize carbon catabolism from cellulosic substrates in a synthetic medium.     

Adsorbents for extractive bioconversion applied to the acetone-butanol fermentation

Summary Four different polymeric resins were tested as adsorbents in extractive bioconversion applied to the fermentative production of acetone and butanol by Clostridium acetobutylicum. The polymers were tested for their ability to adsorb butanol from pure solutions, and fermentation broths. Furthermore, the effect on the fermentability of the media was tested. The pH was increased to prevent adsorption of intermediates such as acetic and butyric acids. Bonopore, the polymer giving the best adsorption pattern with no undesirable effects, was tested in repeated batch cultures with C. acetobutylicum.     

An improved procedure for production of human epidermal growth factor from recombinant E. coli

An improved procedure for the fermentation and purification of human epidermal growth factor (hEGF) was developed. Recombinant Escherichia coli HB-101 [lacUV5omp08hEGF] harboring plasmid lacUV5omp08hEGF encoding hEGF was used in fermentation to increase levels of hEGF. Medium composition, and the levels of inoculum, inducer (isopropyl-beta-D-thiogalactoside) and ampicillin were optimized with respect to volumetric fermentation of hEGF. As a result, the hEGF concentration reached a high value of 242 mg l(-1) and the amount of heterogeneous protein decreased by 62% compared with that before optimization in batch fermentation. High-quality hEGF was purified from the fermentation culture by centrifugation, salting-out, resuspension, recentrifugation and finally gel chromatography on a Grad-iFrac System using Sephadex G-50 superfine. The purity of hEGF and the total yield were more than 94% and higher than 36%, respectively, and SDS-PAGE of the purified hEGF demonstrated a single band corresponding to an hEGF standard. In particular, a very important phenomenon was found, i.e. that the amount of heterogenous protein in fermentation broths cultured in media with high concentrations of lactose is far less than that cultured in media with high concentrations of glucose.     

Studies of Clostridium cellulolyticum ATCC 35319 under dialysis and co-culture conditions

A. Gehin, C. Cailliez, E. Petitdemange And L. Benoit. 1996. The degradation of cellulose by Clostridium celulolyticum has been studied in several ways; (1) in batch fermentation in 50-ml sealed-cap flasks, referred to as the control; (2) in batch fermentation with pH at 7.2; (3) fermentation in dialysis which permits elimination of all the products of metabolism; (4) fermentation in dialysis with a constant bubbling of nitrogen; (5) in co-culture with Clostridium A22 in batch with and without pH regulation and with dialysis. H₂, CO₂, acetate, ethanol and lactate were the major end-products of cellobiose and cellulose fermentation. Compared to batch culture, growth of CI. cellulolyticum on cellobiose increased by a factor of 10 in dialysed culture. The end products from the dialysed culture were detected in a small range compared to the concentration for the batch culture. Related to the biomass, CMCase activities were of the same level, showing a direct relation between the biomass formation and the cellulase production. The percentage of cellulose degradation (50%) by CI. cellulolyticum was greater when dialysis of end products with a constant bubbling of nitrogen took place during the course of fermentation (6 d) in comparison with cultures in 50-ml sealedcap flasks (23%), in a fermentor (36%) or using dialysis without N₂ bubbling (40%). The presence of two micro-organisms produced no further enzyme activities and hence the percentage of cellulose degradation was quite similar in mono- and co-culture. No synergistic action was found between two cellulolytic strains.     

Sampling of solid spent agar media for gas chromatography of diffused acidic fermentation products

Abstract Sampling and processing of solid agar media for gas chromatographic analysis is described. Small pieces of agar are cut from a 'sterile' area of the plate leaving the actual bacterial growth undisturbed for further tests. It is shown that diffused fermentation acids are adequately represented in these samples to permit their use for phenotypic and taxonomic characterization of isolates. Because of the established qualitative and quantitative correspondence of fermentation patterns from agar-grown and from broth-grown bacteria, respectively, the method is offered as a rapid alternative for the sampling of spent culture broths. In addition, the sampling of spent agar plugs seems to hold promise for the study of defined mixed cultures and of mixed growth from primary plates.