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.     

Combined in-fermenter extraction and cross-flow microfiltration for improved inclusion body processing

In this study we demonstrate a new in-fermenter chemical extraction procedure that degrades the cell wall of Escherichia coli and releases inclusion bodies (IBs) into the fermentation medium. We then prove that cross-flow microfiltration can be used to remove 91% of soluble contaminants from the released IBs. The extraction protocol, based on a combination of Triton X-100, EDTA, and intracellular T7 lysozyme, effectively released most of the intracellular soluble content without solubilising the IBs. Cross-flow microfiltration using a 0.2 microm ceramic membrane successfully recovered the granulocyte macrophage-colony stimulating factor (GM-CSF) IBs with removal of 91% of the soluble contaminants and virtually no loss of IBs to the permeate. The filtration efficiency, in terms of both flux and transmission, was significantly enhanced by in-fermenter Benzonase digestion of nucleic acids following chemical extraction. Both the extraction and filtration methods exerted their efficacy directly on a crude fermentation broth, eliminating the need for cell recovery and resuspension in buffer. The processes demonstrated here can all be performed using just a fermenter and a single cross-flow filtration unit, demonstrating a high level of process intensification. Furthermore, there is considerable scope to also use the microfiltration system to subsequently solubilise the IBs, to separate the denatured protein from cell debris, and to refold the protein using diafiltration. In this way refolded protein can potentially be obtained, in a relatively pure state, using only two unit operations.     

The surface growth and activity ofNitrobacter

The effect of surface attachment on oxidation of nitrite to nitrate byNitrobacter was studied in batch culture, on glass coverslips, and in continuous culture on glass beads and anion exchange resin beads in an air-lift column fermenter. In batch culture, the surfaces stimulated specific growth rate, while in continuous culture, activity of attached cells was less than that of freely suspended cells. Nitrate productivity, free cell productivity, and attached cell concentration increased exponentially at the same specific rate, termed the colonization rate, and nitrate productivity was found to be a convenient estimate of biomass concentration. Permanent attachment was mediated by production of slime material. Surface growth resulted in multiple steady states and the ability to respond quickly to changes in dilution rate. The air-lift column fermenter system provided a convenient system for the study of growth and activity of attached cells and was most suitable when using ion exchange resins as a substratum for attachment.     

A filter fermenter-apparatus and control equipment

Laboratory equipment for cultivation of microorganisms with the removal of cell-free medium is described. Separation is accomplished by filtration through a membrane which is built into a top-driven fermenter. A system is presented which controls the flow rate by automatic cleaning of the filter. Flow schemes for batch and continuous fermentations are shown. The filter fermenter is useful when studying continuous culture with feedback of biomass or processes where growth or product formation rates are influenced by inhibitory metabolites. Results are presented from experiments with Saccharomyces cerevisiae, Pedicoccus pentosaceus, and Zymomonas mobilis.     

Application of mathematical models to the determination optimal glucose concentration and light intensity for mixotrophic culture of Spirulina platensis

The effects of initial glucose concentration and light intensity on specific growth rate, phycocyanin concentration and cell dry weight concentration in mixotrophic batch cultivation of Spirulina platensis using both shake flask and fermenter were investigated. Based on experimental results in shake flask culture, a number of mathematical models were constructed, and the optimal initial glucose concentration and the optimal light intensity were calculated to be S_opt=2.4471 g liter⁻¹ and L_opt=3.8632 klx. Finally, a time-dependent kinetic model for mixotrophic batch cultivation of Spirulina platensis in fermenter was also proposed. This was in good agreement with the experimental results and could be employed to predict the production of biomass and phycocyanin, and the consumption of glucose in fermenter culture.     

Kinetics and modelling of kojic acid production by Aspergillus flavus Link in batch fermentation and resuspended mycelial system

An unstructured model based on logistic and Luedeking-Piret equations was proposed to describe growth, substrate consumption and kojic acid production by Aspergillus flavus Link strain 44-1 in batch fermentation and also in a resuspended cell system. The model showed that kojic acid production was non-growth associated. The maximum kojic acid and cell concentrations obtained in batch fermentations using the fermenter with optimized dissolved oxygen control (32.5 g/l and 11.8 g/l, respectively) and using a shake-flask (36.5 and 12.3 g/l, respectively) were not significantly different. However, the maximum specific growth rate and a non-growth-associated rate constant for kojic acid formation (n) for batch fermentation using the fermenter (0.085/h and 0.0125 g kojic acid/g cell.h, respectively) were approximately three and two times higher than the values obtained for fermentation using a shake-flask, respectively. Efficient conversion of glucose to kojic acid was achieved in a resuspended pellet or mycelial system, in a solution containing only glucose with citrate buffer at pH 3.5 and at a temperature of 30 °C. The resuspended cell material in the glucose solution was still active in synthesizing kojic acid after prolonged incubation (up to about 600 h). The rate constant of kojic acid production (n) in a resuspended cell system using 100 g glucose/l was almost constant at an average value of 0.011 g kojic acid/g cell.h up to a cell concentration of 19.2 g/l, above which it decreased. A drastic reduction of n was observed at a cell concentration of 26.1 g/l. However, the yield based on glucose consumed (0.45 g/g) was similar for all cell concentrations investigated.     

Microbial film fermenters: Their present and future applications

The productivity of growth associated fermentations is dependent upon the quantity of biomass contained in the fermenter (microbial hold-up). In contrast, the performance characteristics of a fermenter are dominated by the form in which the microbial hold-up occurs, i.e., whether as films, flocs, or a combination of both. Industrial fermentations using biological films include biological waste-water treatment (trickling filter, rotating disc), the “quick” vinegar process, animal tissue culture, and bacterial leaching. Atkinson and Davies (Trans. Inst. Chem. Eng., 50 , 208 (1972)), proposed a completely mixed microbial film fermenter (CMMFF) based upon the fluidized bed principle, for application to continuous operation when using growth associated systems. The potential performance characteristics of this fermenter are reviewed and the construction of a laboratory scale unit capable ofaseptic operation is described (volume 9 liters, maximum throughput 15 liter/hr). The fermenter has been continuously used for periods up to 2500 hr without contamination when growing brewer's yeast (NCYC 1026 flocculating). The experimental performance characteristics have been interpreted with the aid of the theory for the CMMFF. The knowledge and experience gained to date is used as a basis for speculation as to the future role of microbial film fermenters in the biochemical process industries.     

Improved production of live cells of Lactobacillus rhamnosus by continuous cultivation using glucose-yeast extract medium

In this study, the growth kinetics of Lactobacillus rhamnosus and lactic acid production in continuous culture were assessed at a range of dilution rates (0.05 h(-1) to 0.40 h(-1)) using a 2 L stirred tank fermenter with a working volume of 600 ml. Unstructured models, predicated on the Monod and Luedeking-Piret equations, were employed to simulate the growth of the bacterium, glucose consumption, and lactic acid production at different dilution rates in continuous cultures. The maximum specific growth rate of L. rhamnosus, mu-max, was estimated at 0.40 h(-1), and the Monod cell growth saturation constant, Ks, at approximately 0.25 g/L. Maximum cell viability (1.3 x 10(10) CFU/ml) was achieved in the dilution rate range of D = 0.28 h(-1) to 0.35 h(-1). Both maximum viable cell yield and productivity were achieved at D = 0.35 h(-1). The continuous cultivation of L. rhamnosus at D = 0.35 h(-1) resulted in substantial improvements in cell productivity, of 267% (viable cell count) that achieved via batch cultivation.     

Production of carbonyl reductase by Geotrichum candidum in a laboratory scale bioreactor

Fungal fermentation is very complex in nature due to its nonlinear relationship with the time, especially in batch culture. Growth and production of carbonyl reductase by Geotrichum candidum NCIM 980 have been studied in a laboratory scale stirred tank bioreactor at different pH (uncontrolled and controlled), agitation, aeration and dissolved oxygen concentration. The yield of the process has been calculated in terms of glucose consumed. Initial studies showed that fermenter grown cells have more than 15 times higher activity than that of the shake flask grown cells. The medium pH was found to have unspecific but significant influence on the enzyme productivity. However, at controlled pH 5.5 the specific enzyme activity was highest (306U/mg). Higher agitation had detrimental effect on the cell mass production. Dissolved oxygen concentration was maintained by automatic control of the agitation speed at an aeration rate of 0.6 volume per volume per minute (vvm). Optimization of glucose concentration yielded 21g/l cell mass with and 9.77x10(3)U carbonyl reductase activity/g glucose. Adaptation of different strategies for glucose feeding in the fermenter broth was helpful in increasing the process yield. Feeding of glucose at a continuous rate after 3h of cultivation yielded 0.97g cell mass/g glucose corresponding to 29.1g/l cell mass. Volumetric oxygen transfer coefficient (K(L)a) increased with the increasing of agitation rate.     

Butyric fermentation: metabolic behaviour and production performance of Clostridium tyrobutyricum in a continuous culture with cell recycle

Summary Two physiological characteristics of butyric fermentation, inhibition by the acids produced, butyrate and acetate, and dependence on the growth rate of the distribution of these acids, prompted a study of butyrate production in a continuous fermentation system with cell recycle by microfiltration. The influence of the main operating parameters, glucose input (feed concentration and dilution rate) and bleed dilution rate on production of acids and biomass was studied. The performance of the system greatly exceeded the results obtained in batch and simple continuous fermentations as a high productivity for butyrate (9.5 g l^–1 h^–1) was achieved whilst retaining a satisfactory concentration of butyrate (29.7 g l^–1) and low acetate production (0.6 g l^–1) at a cell biomass concentration of 35 g l^–1. Cell growth rate was found to be a critical parameter for performance stability as oscillations in metabolic activity due to inhibition by acids were observed at bleed dilution rates below 0.016 h^–1.Offprint requests to: J. P. Vandecasteele     

Bioconversion of cellulose wastes to protein and sugar

A schematic representation of the variety of products which can be obtained by microbial conversion of cellulose is presented. Alkaline pre-treatment has been used after milling in all the experiments. Solka-floc or sugarcane bagasse was used as sources of cellulose. A cellulolytic strain of Aspergillus terreus (ATCC 30514) was cultivated in batch-, fed batch and continuous culture up to 7 liter stirred tank fermenter. The general growth characteristics were determined by growing on glucose. Results of experiments on the growth of A. terreus for production of biomass on Solka-floc or Sugarcane bagasse are given, also the ability of crude cellulases to produce sugar syrups by enzymatic hydrolysis of cellulose has been evaluated.     

基因工程人α心钠素发酵研究

本研究采用的基因工程菌为酵母Y33：：YFD71－3,其基因型为α,his,1eu,ade,suc．摇瓶培养时心钠素的表达水平为l～2rag／L。在含有葡萄糖、YNB以及不同量腺嘌呤、组氨酸和亮氨酸的YG培养基中作摇瓶培养．当细胞的生长由腺嘌呤限制时,蛋白的分泌有明显增加·在YG培养基中加入5g／L的CAA后腺嘌呤成为限制性基质,培养基中腺嘌呤、YNB和亮氪酸用量对心钠素的表达有很大影响。在5L反应器中进行补料分批培养,流加葡萄糖、YNB、cAA、腺嘌呤、组氨酸和亮氨酸,心钠素的最高浓度达到24．8mg／L。     

Bioreactor considerations for secondary metabolite production from plant cell tissue culture: Indole alkaloids from Catharanthus roseus

Batch shake flask studies with Catharanthus roseus demonstrated that alkaloid production commenced only after growth had slowed or ceased. To obtain high alkaloid productivities for extended periods, a hormone-free production medium was used. To develop a readily scalable process, both immobilized and suspended cell systems were studied. In the immobilized cell systems, growth, glucose utilization, and alkaloid production were suppressed; for the case of membrane entrapped cells this suppression was observed to be reversible. Based on the oxygen requirements of the cells, and the oxygen transfer capabilities of a pneumatically agitated bubble column, conditions were established that allowed the growth and production dynamics observed in shake flasks to be reproduced in the air sparged column reactor. The requirement for the aseptic exchange of growth for production medium was satisfied by using a coarse cotton filter and coupling filtration to aeration. With this filtration system, media can be rapidly and completely exchanged and the filter can be quickly and effectively backwashed. By coupling filtration to aeration, a two-stage batch operation can be employed while requiring only a single bioreactor. Studies with this system demonstrated its capabilities for alkaloid production.     

Photoautotrophic growth of cell suspension cultures fromChenopodium rubrum in an airlift fermenter

Summary This communication describes the construction and operation of an airlift fermenter for the photoautotrophic growth of cell suspension cultures fromChenopodium rubrum. The basic batch culture unit provides a culture of 1.51 volume, sufficient to permit frequent aseptic sampling. It can be maintained at any desired temperature and aerated to different extents. Using an initial cell density of about 400,000 cells per ml suspension, the increase in cell number is 270% after a 14 days' growth period, although the stationary phase of growth is not yet reached. The transfer of photoautotrophic cell suspensions fromChenopodium rubrum from stationary growth into the large volume of fresh culture medium in the airlift fermenter results in an immediate protein formation, followed by an exponential phase of cell division, whereas rapid chlorophyll accumulation is delayed by 2 days.The growth capacities of photoautotrophic fermenter cultures including protein and chlorophyll formation as well asin vitro activities of the ribulosebisphosphate carboxylase and the phosphoenolpyruvate carboxylase are greatly lower as compared to photoautotrophic cells propagated in standard two-tier culture vessels using 30 ml culture medium. However the pattern of change in the activities of carboxylation enzymes is quite similar in both culture systems.Photoautotrophic cell suspensions fromChenopodium rubrum grown in an airlift fermenter assimilate about 90 mol CO₂/mg chlorophyll × hour. Dark CO₂ fixation is about 1.5% of the light values.Abbreviations PEF phosphoenolpyruvate - RuDP ribulosebisphosPhate - NS ground glass joints of standardized size made from Duran glass, Schott, Germany     

High cell density culture of the diatom Nitzschia laevis for eicosapentaenoic acid production: fed-batch development

A fed-batch process was developed for high cell density culture of the diatom Nitzschia laevis for enhanced production of eicosapentaenoic acid (EPA). Firstly, among the various medium components, glucose (Glu) was identified as the limiting substrate while nitrate (NO₃⁻), tryptone (Tr) and yeast extract (Ye) were found to promote cell growth by enhancing specific growth rate. Therefore, these components were considered essential and were included in the feed medium for subsequent fed-batch cultivation. With the optimized ratio of NO₃⁻:Tr:Ye being 1:2.6:1.3 (by weight), the relative proportions of glucose to the nitrogen sources in the feed were investigated. The optimal ratios of Glu:NO₃⁻ for specific growth rate and EPA productivity were both determined to be 32:1 (by weight). Finally, based on the residual glucose concentration in the culture, a continuous medium feeding strategy for fed-batch fermenter cultivation was developed, with which, the maximal cell dry weight and EPA yield obtained were 22.1 g l⁻¹ and 695 mg l⁻¹, respectively, which were great improvements over those of batch cultures.     

A new principle of continuous flow cell cultivation

Summary A completely liquid-filled culture chamber with gas exchange across a synthetic membrane (Larsen andNilsson 1985) was incorporated into an automatic continuous flow system. The absence of an airliquid interface in the system permits removal of cell samples, and addition of fresh medium, under strictly sterile conditions. In this system,Tetrahymena pyriformis can be kept under optimal growth conditions in a rich nutrient medium and any defined cell density may be maintained for extended periods of time by varying the dilution rate of the culture. Furthermore, it has been possible to demonstrate, in the slope of the growth curve, even small changes which are difficult to detect in batch cultures since the duration of these changes is short. In the continuous flow system, the relative cell volume distribution and the food vacuole forming capacity of the cells were unaltered; however, all cells contained small refractive granules. The system permits the culture volume to be varied, but a standard volume of 20 ml was maintained in most experiments. Since the culture volume is small, the system requires less than one liter of fresh medium per week to maintain the cells in the exponentially multiplying growth phase.     

Growth of microbes in an oil-continuous environment

The growth of microorganisms in fermentations where oil had been maintained as the continuous phase was examined to determine whether advantage could be gained from the increased solubility of oxygen in hydrocarbon. Although cell concentrations were highest in the aqueous phase of oil-continuous systems, due to the large oil fraction, productivities achieved per unit fermenter volume were generally equivalent to those obtained from water-continuous systems. With the oil-continuous emulsions, the power requirement for aeration and mixing was less, and phase reversal resulted in a threefold concentration of cells in the aqueous medium, thereby facilitating their recovery.     

Comparison of specific rates of hybridoma growth and metabolism in batch and continuous cultures

For the mouse hybridoma cell line VO 208, kinetics of growth, consumption of glucose and glutamine, and production of lactate, ammonia and antibodies were compared in batch and continuous cultures. At a given specific growth rate, different metabolic activities were observed: a 40% lower glucose and glutamine consumption rate, but a 70% higher antibody production rate in continuous than in batch culture. Much higher metabolic rates were also measured during the initial lag phase of the batch culture. When representing the variation of the specific antibody production rate as a function of the specific growth rate, there was a positive association between growth and antibody production in the batch culture, but a negative association during the transient phase of the continuous culture. The kinetic differences between cellular metabolism in batch and continuous cultures may be result of modifications in the physiology and metabolism of cells which, in continuous cultures, were extensively exposed to glucose limitations.Institut National Polytechnique de Lorraine, ENSAIA BP 172, 2 avenue de la forêt de Haye, 54505, Vandoeuvre Cedex France     

The physiology of lactate production by Lactobacillus delbreuckii in a chemostat with cell recycle

The physiology of lactate production by Lactobacillus delbreuckii NRRL B-445 in a continuous fermenter with partial cell recycle has been studied and compared with that observed in a conventional chemostat. Partial cell recycle was achieved using a hollow-fiber ultrafiltration cartridge. The biomass growth yield was reduced in the recycle fermenter while culture viability and the cellular content of polysaccharide, protein, carbon, and nitrogen remained constant, suggesting an enlarged specific rate of glucose consumption for nonanabolic (e.g., maintenance) functions. The volumetric productivity of lactate was enhanced in the recycle fermenter due to the complete utilization of glucose. The yield of lactate from biomass and the molar product ratio, lactate: ethanol plus acetate, decreased with increasing recycle ratio. Enhanced formation of ethanol and acetate occurred in the recycle fermenter although lactate remained the major product. The change in product profile was due to glucose limitation. The specific activity of lactate dehydrogenase remained constant during recycle fermentation. These physiological observations have implications for the future application of cell recycle to production processes.     

Kinetics of kojic acid fermentation byAspergillus flavus link S44-1 using sucrose as a carbon source under different pH conditions

Kojic acid production byAspergillus flavus strain S44-1 using sucrose as a carbon source was carried out in a 250-mL shake flask and a 2-L stirred tank fermenter. For comparison, production of kojic acid using glucose, fructose and its mixture was also carried out. Kojic acid production in shake flask fermentation was 25.8 g/L using glucose as the sole carbon source, 23.6 g/L with sucrose, and 6.4 g/L from fructose. Reduced kojic acid production (13.5 g/L) was observed when a combination of glucose and fructose was used as a carbon source. The highest production of kojic acid (40.2 g/L) was obtained from 150 g/L sucrose in a 2 L fermenter, while the lowest kojic acid production (10.3 g/L) was seen in fermentation using fructose as the sole carbon source. The experimental data from batch fermentation and resuspended cell system was analysed in order to form the basis for a kinetic model of the process. An unstructured model based on logistic and Luedeking-Piret equations was found suitable to describe the growth, substrate consumption, and efficiency of kojic acid production byA. flavus in batch fermentation using sucrose. From this model, it was found that kojic acid production byA. flavus was not a growth-associated process. Fermentation without pH control (from an initial culture pH of 3.0) showed higher kojic acid production than single-phase pH-controlled fermentation (pH 2.5, 2.75, and 3.0).