Production of gramicidin S synthetases by Bacillus brevis in continuous culture.

The effects of different nutrient limitations on the production of the two enzymes of gramicidin S biosynthesis were studied during continuous culture of Bacillus brevis. Gramicidin S synthetases I and II were produced in the chemostat under carbon, nitrogen, phosphorus or sulphur limitation. The growth rate, rather than the nature of the limitation, was the major controlling factor in regulating the level of the gramicidin S synthetases. Synthetase production was low at high dilution rates (0.45 to 0.50 h-1) but increased as the dilution rate was lowered. The highest specific activities occurred at dilution rates that were different for each type of limitation: 0.40 h-1 for nitrogen, 0.32 h-1 for carbon, 0.24 h-1 for sulphur and 0.20 h-1 for phosphorus. Phosphorus limitation gave the highest specific activities. At low dilution rates (0.10 to 0.15 h-1), enzyme activities were again low. Sporulation occurred under carbon limitation, but at a lower dilution rate than that which supported optimal gramicidin S synthetase formation. The specific productivity of the synthetases in the chemostat was higher than the highest productivity obtained in batch growth.     

Effects of the dilution rate on cell cycle distribution and PEI-mediated transient gene expression by CHO cells in continuous culture

In this study, a continuous culture system was applied to mammalian cells on large scale, and polyethyleneimine (PEI) mediated transient gene expression (TGE). PEI MAX 40,000 was chosen as a superior reagent from three types of PEI. The cell cycle distribution of cells in batch and continuous cultures was determined, in which the effects of cell cycle distribution on transfection efficiency, post-transfection proliferation and recombinant prothrombin expression were evaluated. Compared with cells from end-log and plateau phase in batch culture, cells from mid-log phase possessed a larger fraction of S and G2/M phase cells and a smaller fraction of G1 phase cells. In the continuous culture, the fraction of cells in the S and G2/M phases increased and the fraction of cells in the G1/G0 phase decreased with increasing dilution rates. Cells from the continuous culture run at highest dilution rate had excellent proliferation, transfection efficiency and protein expression. These results were confirmed by transfecting cells synchronized to different phases. The G2/M arrested cells exhibited a nearly 10-fold increase in recombinant human prothrombin production relative to that of non-dividing cells. The use of continuous culture for large scale transfection demonstrated a better cell physiological state for TGE process.     

Continuous two-stage ABE-fermentation using Clostridium beijerinckii NRRL B592 operating with a growth rate in the first stage vessel close to its maximal value

A two-stage continuous cultivation experiment with Clostridium beijerinckii NRRL B592 is described. The experiment was designed to mimic the two phases of batch culture growth of the organism in a two-stage continuous process. Thus in the first stage turbidostat the organism was grown acidogenically as rapidly as possible, and transferred to the second stage at the 'acid break point'. The second stage was designed to mimic the solventogenesis of the batch culture when it enters late exponential/early stationary phase. The volume of the second stage vessel was calculated to provide the necessary residence time for complete sugar utilization. It was hoped that the experimental set-up chosen would show whether data obtained from batch fermentation could be transferred directly to continuous culture. The culture maintained its ability to produce acetone, 1-butanol and ethanol at a dilution rate of 0.12 h(-1) for the first stage and 2.2 x 10(-2) h(-1) for the second stage and achieved an average overall solvent concentration of 15 g/l and an overall solvent productivity of 0.27 g/l/h for a period of steady-state operation of more than 1600 hours. The productivity of solventogenesis in the first stage was dependent on the value of the growth rate of the culture which was in turn determined in part by the organism employed but also by the medium composition.     

Control of the cell cycle ofCandida utilis by external conditions

A mathematical model of the cell cycle ofCandida utilis in a continuous culture was formulated with respect to dilution rate. It makes it possible to express the duration of morphological stages in minutes, separately for mother cells and daughter cells. These values were compared with equivalent parameters in batch cultures. Duration of the morphological stage with buds was much longer in batch cultures as compared with the same value determined for a continuous culture according to the mathematical model. When using cultivation apparatus with a higher aeration capacity the (S + G₂) phase, i.e. the stage bearing the bud, was reduced also in the batch cultures and approached the values determined for the continuous culture by means of the mathematical model.     

A continuous multistage roller reactor for animal cell culture: 1. Patterns of growth,production and catabolism of a murine hybridoma

A Tubular Liquid Film Reactor was designed as a model system to transfer a batch culture kinetic to a continuous cascade. Cell density, product formation and substrate consumption rates were followed during fermentation at two dilution rates. In spite of the high dilution rates effective in each segment by itself high cell densities of up to 10⁷ cells/ml were achieved due to cell sedimentation. The model character of the reactor was taken to determine critical values of substrate concentrations that influence production rates and result in an adaptation of metabolism.Abbreviations TLFR tubular liquid film reactor     

The use of extraction methods for the quantification of extracellular polymer production byKlebsiella aerogenes under varying cultural conditions

Summary A combination of ultrasonication at 18 W for 10 min and centrifugation at 33,000 g for 60 min was found to achieve the highest recovery of extracellular polymer fromKlebsiella aerogenes, NCTC 8172, allowing both soluble and colloidal phases to be separated. Estimates of the total polymer present, made by gravimetry and by acid hydrolysis, indicated that polymer production was greater in continuous culture than in batch culture, and increased in continuous culture as the dilution rate decreased from 0.5 h^–1 to 0.01 h^–1. Extraction of polymer from these cultures varied in efficiency; up to 73% of the total polymer was extracted at low dilution rates where the colloidal form of polymer was predominant, but only 22% was extracted at high dilution rates where the majority of the polymer was in the soluble phase. Consequently, this extraction method was considered to be unsuitable as a quantitative measure of polymer production.     

Effects on product formation in Lactococcus lactis 65.1 in continuous culture with complete cell recycling

Lactococcus lactis 65.1 was cultivated in a batch culture, which underwent starvation for 3 days, continuous culture and continuous culture with complete cell recycling. The objective was to study the product formation and intracellular protein pattern. Changes from homofermentative to heterofermentative metabolism were observed in continuous culture at the lower dilution rates as well as continuous cultures with complete cell recycling at a fixed dilution rate (D=0.4 h^–1). Changes in intracellular protein pattern were observed when starving the cells in a batch culture and also when recycling the cells in a continuous culture. Some changes were the same in these two cases. The data collected from these experiments show how the fermentation technique can affect the products of the microorganism being cultured and gives some interesting information on the complete cell recycling technique, which is of great interest in fermentation processes.     

The activity of beta-galactosidase and lactose metabolism in Kluyveromyces lactis cultured in cheese whey as a function of growth rate

Aims: Kluyveromyces lactis was cultured in cheese whey permeate on both batch and continuous mode to investigate the effect of time course and growth rate on β‐galactosidase activity, lactose consumption, ethanol production and protein profiles of the cells. Methods and Results: Cheese whey was the substrate to grow K. lactis as a batch or continuous culture. In order to precise the specific growth rate for maximum β‐galactosidase activity a continuous culture was performed at five dilution (growth) rates ranging from 0·06, 0·09, 0·12, 0·18 to 0·24 h^?1. The kinetics of lactose consumption and ethanol production were also evaluated. On both batch and continuous culture a respirofermentative metabolism was detected. The growth stage for maximum β‐gal activity was found to be at the transition between late exponential and entrance of stationary growth phase of batch cultures. Fractionating that transition stage in several growth rates at continuous culture a maximum β‐galactosidase activity at 0·24 h^?1 was observed. Following that stage β‐gal activity undergoes a decline which does not correlate to the density of its corresponding protein band on the gel prepared from the same samples. Conclusion: The maximum β‐galactosidase activity per unit of cell mass was found to be 341·18 mmol ONP min^?1 g^?1 at a dilution rate of 0·24 h^?1. Significance and Impact of the Study: The physiology of K. lactis growing in cheese whey permeate can proven useful to optimize the conversion of that substrate in biomass rich in β‐gal or in ethanol fuel. In addition to increasing the native enzyme the conditions established here can be set to increase yields of recombinant protein production based on the LAC4 promoter in K. lactis host.     

High productivity tank fermentation for gramicidin S synthetases

A high productivity tank fermentation for gramicidin S synthetases has been developed to supply biocatalyst for a preparative-scale ATP-driven cell-free enzymatic synthesis employing the polypeptide antibiotic, gramicidin S, as a model product. A rich, complex medium supports rapid and dense growth of the enzyme-producing microorganism, Bacillus brevis ATCC 9999, accompanied by the appearance of excellentenzyme activities. Under conditions used, the two enzyme fractions of the gramicidin S synthesizing system, as well as the total enzymatic activity for synthesis of gramicidin S, all reach their maxima simultaneously at the point where growth enters the stationary phase. Successful batch enzyme fermentations have been performed at the bench (14 liter) and pilot (180 liter)scales.     

Continuous culture with complete cell recycle to obtain high cell densities in product inhibited cultures; cultivation ofStreptococcus lactis for production of superoxide dismutase

Summary A cultivation system is described for cultivatingStreptococcus lactis in continuous culture with complete cell recycle. The aim was to obtain high cell densities for the production of su-peroxide dismutase (SOD) while avoiding the growth inhibiting effects of the lactic acid produced. This type of cultivation was performed both at constant and at increasing dilution rates. Comparisons made include those between cell mass productivity and SOD productivity in recycling cultivations and batch cultivations. In the recycling cultivation at increasing dilution rates a cell mass of 19 g/1 was obtained after 22 h of cultivation and the SOD productivity was 43.10³ U/1.h which is four times higher than for batch cultivations. The effect of recyclingS. lactis was also considered and no damage of the microorganisms was observed.     

Continuous antibiotic production by an immobilized cyanobacterium in a seaweed-type bioreactor

The filamentous cyanobacterium,Scytonema sp. TISTR 8208, which produces a cyclic peptide antibiotic, was cultivated for 20 d in a seaweed-type bioreactor containing anchored polyurethan foam strips. Cells immobilized onto the foam strips produced the antibiotic for only several days, and the secreted antibiotic disappeared very rapidly from the medium. Cells accumulated the antibiotic intracellularly in a growth-related manner, and secreted it in the stationary phase. Since the antibiotic has a stable physico-chemical nature, the cells seem to take it up and metabolize it. When continuous cultivation was attempted, stable production of the antibiotic was maintained in the bioreactor for 16 d at a dilution rate of 0.01 h^–1. Three times more antibiotic was produced in the continuous culture than in the batch culture by the 16th day.     

Kinetic analysis of batch and continuous culture of Streptococcus cremoris HP1.

The growth of Streptococcus cremoris on a semidefined medium was studied at initial lactose concentrations of 0.2-5.0% in batch culture, and in lactose-limited chemostat cultures at 0.5% lactose. Kinetic analysis of the batch data, using statisitcal techniques, indicated the importance of lactose limitation and lactic acid inhibition of the growth of S. cremoris. A model for the biomass production, lactose utilization, and lactic acid production in batch culture was proposed. In continuous culture, it was found that steady state populations were maintained at higher dilution rates (D = 0.6-0.7 h-1) than the maximum predicted by batch culture (0.56h-1). No evidence for a selection of fast growing mutants was obtained. Copious growth adhering to the walls of the fermentor (i.e. wall growth) occurred very rapidly at higher dilution rates and this undoubtedly affected steady-state growth and wash-out and, as a consequence, the apparent maximum dilution rate.     

Amino acid consumption by Chloroflexus aurantiacus in batch and continuous cultures

Amino acid consumption was studied with batch and continuous chemostat cultures of Chloroflexus aurantiacus grown phototrophically in complex medium with casamino acids (Pierson and Castenholz 1974). Amino acids like Arg, Asx, Thr, Ala, Tyr, which were utilized during the early exponential phase by cells grown in batch cultures were consumed in chemostat cultures essentially at any of the dilution rates employed (0.018–0.104 h^-1). Those amino acids which were taken up during subsequent phases of growth were consumed in chemostat cultures preferentially at low dilution rates. For example, the consumption of Glx was enhanced during the late exponential phase and at low dilution rates. At high dilution rates Glx was not consumed at all. Since Glx utilization largely paralleled bacteriochlorophyll formation, it is discussed that formation of the photopigment depends on the intracellular availability of Glu as the exclusive precursor for tetrapyrrole synthesis.     

Kinetic analysis of L-lysine production by a fluoropyruvate sensitive mutant of B.lactofermentum

The kinetics of L-lysine production by a fluoropyruvate sensitive (FP^s) mutant of B.lactofermentum have been analysed in batch and continuous culture. Under optimal conditions (viz. T = 30° C, pH = 7.0, DO = 10 % air saturation) it was established that the initial phosphate level could be used to extend the batch culture to give an L-lysine.HCl concentration of 68.0 g/l and a yield of 0.43 g/g. In continuous culture the yield increased at low dilution rates under conditions similar to those for extended batch culture.     

Growth of the thermophilic bacterium Clostridium thermocellum in continuous culture

Clostridium thermocellum is an anaerobic thermophilic bacterium that produces enthanol from cellulosic substrates. When the organism was grown in continuous culture at dilution rates ranging from 0.04 to 0.25 h^-1, growth yields on cellobiose were higher than on glucose, and even higher yields were observed on cellotetraose. However, differences in bacterial yield were much greater at slow growth rates, and it appeared that glucose-grown cells had a fourfold higher (0.41 g substrate/g protein/h) maintenance energy requirement than cellobiose-grown cultures. Cellobiose and glucose were co-utilized in dual substrate continuous culture, and this was in contrast to batch culture experiments which indicated that the organism preferred the disaccharide. These experiments demonstrate that carbohydrate utilization patterns in continuous culture are different from those in batch culture and that submaximal growth rates affect substrate preference and bioenergetic parameters. The mechanisms regulating carbohydrate use may be different in batch versus continuous culture.Published with the approval of the Director of the Kentucky Agricultural Experiment Station as journal article no. 95-07-064.     

Continuous production of extracellular protease by Bacillus subtilis in a two-stage fermentor

Growth and protease production of Bacillus subtilis in semisynthetic and synthetic media were studied in batch culture and in a two-stage, laboratory scale, continuous fermentor. The amount, of extracellular protease production was measured under specific growth conditions in both stages of the ferment or. At the dilution rates employed, the cells in the first stage of the ferment or produced negligible quantities of protease, and the culture primarily functioned as a continuous inoculum for the second stage of the fermentor. The culture effluent from the second stage of the fermentor contained extracellular protease, on the average, equal to 60 per cent, of the activity that had been found in the supernatant of a 48-hr batch culture grown in a medium having the same composition as that in the continuous fermentor. Extracellular protease was produced in semisynthetic medium by B. subtilis in the two-stage fermentor for as long as 20 days without culture degeneration. Additional studies indicated that continuous protease production could also be achieved in a synthetic medium. The RNA/ protein ratios of cells grown in semisynthetic medium in batch culture and in each stage of the two-stage fermentor were examined. There was a positive correlation between the amount of protease produced by the cells and their RNA/ protein ratio. Techniques employed for continuous production of protease by B. subtilis and the potential use of the method for investigating the control of secondary metabolite synthesis are discussed.     

Biomass and lipid enhancement in Ankistrodesmus sp. cultured with reused and minimal nutrients media

Microalgae are a promising feedstock for biofuel production. Lipid content in microalgae could be enhanced under nutrient depletion. This work investigated the effect of the nutrient on lipid accumulation in Ankistrodesmus sp. culture. Batch cultures were carried out using fresh BG11 medium, and after the harvest, the medium was reused for the next culture; this method was repeated two times. The maximum lipid productivity of 29.75 mg L^?1 day^?1 was obtained from the culture with the second reuse medium. In continuous cultures, Ankistrodesmus sp. was cultured in both fresh and modified BG11 mediums. The modified BG11 medium was adjusted to resemble the content of the first reuse medium. As a comparison between batch and continuous cultures, it was proven that the productivity in the continuous culture was better than in the batch, where the achievable maximum biomass and lipid were 188.30 and 38.32 mg L^?1 day^?1. The maximum lipid content of 34.22% was obtained from the continuous culture at a dilution rate of 0.08 day^?1, whereas the maximum saturated and unsaturated fatty acid productivities of 79.96 and 104.54 mg L^?1 day^?1 were obtained at a dilution rate of 0.16 day^?1.     

Optimal conditions for gramicidin S production in continuous culture

In the present study optimal policies have been evaluated for the production of gramicidin S in multistage continuous culture. An economic objective function was developed which took account of the number and size of the reaction vessels, the costs involved in antibiotic extraction, substrate costs, and variability in the selling price of gramicidin S. Optimal values of temperature and pH were 28.3 and 7.24, respectively, and independent of the stage in the system. Using the discrete maximum principle it was shown that a “cut-off” point existed for the selling price of the antibiotic below which production was no longer profitable. Furthermore it was established that beyond 3 stages in a multistage system, only marginal gains in profitability could be made (viz., an increase in 6.3% on going from a 3-stage to a 4-stage system).     

Competition between different strains of Streptococcus cremoris

Abstract Streptococcus cremoris strain HP was found to grow poorly on agar plates under aerobic conditions in comparison to several other strains of S. cremoris (Wg2, ML1, AM1, E8). This made it possible to determine the numbers of strain HP in mixed cultures with other strains under different culture conditions. None of the mixtures was stable in batch cultures as a result of differences in the maximum specific growth rate. In continuous culture under lactose limitation strain HP outcompeted strains E8 and ML1 at low dilution rates, but at high dilution rates and in batch culture the reverse was observed. This represents another example of crossing μ-s curves in anaerobic bacteria.     

Avoiding rapid growth at high cell densities: A potentially important optimisation criterion for hybridoma cultures

Inhibition caused by rapid changes in the environment has earlier been observed in hybridoma cultures following deliberate step-changes in the culture environment. This paper presents evidence of similar effects occurring during the normal span of continuous cultures fed enriched medium at low dilution rates (0.002–0.005 1/h). The effect of this observation on optimisation is discussed. In continuous culture at a dilution rate of 0.013 1/h, a viable cell density of 4×10⁹ cells/l was achieved by gradually increasing the nutrient concentration in the feed medium. The MAb titre was 200 mg/l representing a 6-fold increase compared to batch culture and a 2-fold increase compared to continuous culture using standard medium.