Simultaneous control of turbidity and dilution rate through adjustment of medium composition in semi-continuous Chlamydomonas cultures

For production of starch in algal cultures, a growth rate limited by a nutrient is an important factor. Under phototrophic conditions, turbidity must be also paid attention, as the shading effect may affect its productivity. Semi-continuous cultivation methods, which enable control of turbidity and dilution rate (D) at the same time, have been developed for evaluation of those factors on starch production in Chlamydomonas sp. A specific feature of the methods is in a process of alternately feeding medium adjusted at two different nitrogen (N) concentrations. In the turbidostat-based method, a turbidostat culture was operated repeating three steps of determining D within a preset interval, alternating media by comparing the D with a preset value, and adjusting D in the next interval by feeding the selected medium. In the chemostat-based method, turbidity of a chemostat culture was controlled by repeating two steps of alternating media by comparing transmitted photon flux intensity (I) with a preset value and adjusting I by feeding the selected medium. D controlled by the turbidostat-based method reached quickly a preset value as low as 0.010/h, and then it was dispersed around but above the preset value. On the other hand, mean N concentrations of fed media formed a plateau. In the chemostat-based method, I was well controlled to a preset value while the mean N concentrations were a bit fluctuated. Starch concentration varied from 0.052 to 0.41 g/L with turbidity and D defined by these methods.     

Continuous production of carotenoids from Dunaliella salina

During the in situ extraction of β-carotene from Dunaliella salina, the causal relationship between carotenoid extraction and cell death indicated that cell growth and cell death should be at equilibrium for a continuous in situ extraction process. In a flat-panel photobioreactor that was operated as a turbidostat cell numbers of stressed cells were kept constant while attaining a continuous well-defined light-stress. In this way it was possible to study the balance between cell growth and cell death and determine whether both could be increased to reach higher volumetric productivities of carotenoids. In the two-phase system a volumetric productivity of 8.3 mg β-carotene L(RV)(-1)d(-1) was obtained. In situ extraction contributed only partly to this productivity. The major part came from net production of carotenoid-rich biomass, due to a high growth rate of the cells and subsequent dilution of the reactor. To reach equilibrium between cell growth and cell death, sparging rates of dodecane could have been increased. However, already at the applied sparging rate of 286 L(dod)L(RV)(-1)min(-1) emulsion formation of the dodecane in the aqueous phase appeared. In a turbidostat without in situ extraction a volumetric productivity of 13.5 mg β-caroteneL(RV)(-1)d(-1) was reached, solely based on the continuous production of carotenoid-rich biomass.     

Development of a novel continuous culture device for experimental evolution of bacterial populations

The availability of a robust and reliable continuous culture apparatus that eliminates wall growth problems would lead to many applications in the microbial field, including allowing genetically engineered strains to recover high fitness, improving biodegradation strains, and predicting likely antibiotic resistance mechanisms. We describe the design and implementation of a novel automated continuous culture machine that can be used both in time-dependent mode (similar to a chemostat) and turbidostat modes, in which wall growth is circumvented through the use of a long, variably divisible tube of growth medium. This tube can be restricted with clamps to create a mobile growth chamber region in which static portions of the tube and the associated medium are replaced together at equal rates. To functionally test the device as a tool for re-adaptation of engineered strains, we evolved a strain carrying a highly deleterious deletion of Elongation Factor P, a gene involved in translation. In 200 generations over 2 weeks of dilution cycles, the evolved strain improved in generation time by a factor of three, with no contaminations and easy manipulation.     

Orthophosphate influx and efflux rates of Chlorella fusca measured in a continuous turbidostat culture with 32P under various conditions

The main objective of the experiments with Chlorella fusca strain 211-8b was to measure, with adequate time resolution, the unidirectional influx rates of phosphate into non-phosphate-starved algae under different steady state conditions (light, temperature, 3-phosphoglycerate influence) or following the addition of several photosynthesis and phosphate transport inhibitors (phenylmercuric acetate, p-chloromercuribenzoate, arsenate). the algae were cultivated in a phosphate rich medium in a continuous turbidostat culture. The phosphate exchange experiments with carrier-free ³²PO ₄ ^3- were performed directly in the continuous culture. The sampling intervals after the tracer addition were 15 s.For a continuous steady state culture grown in the light (25° C) the unidirectional influx rate measured with ³²P is 260 times higher than the net uptake rate (=influx minus efflux rate) calculated from the mass balance using the data of this culture. In all experiments, except the control experiment with trichloroacetic acid killed cells, the specific activity of the intracellular inorganic orthophosphate compartment oscillates around a constant mean value which never reaches the specific activity of the nutrient medium within the duration of the short-term experiments (7.5 min). The inhibitors strongly affect the characteristics of the oscillations. The unidirectional influx rates are constant. Oscillating flushing rates with unlabelled phosphate from a storage compartment have been postulates to explain the oscillations. Oscillating rates from the individual cells are apparently synchronized by an unknown mechanism.     

Microcomputer-assisted systems for recording and control of growing phytoplankton cultures

This report describes a basic unit for microcomputer-assistedrecording of the turbidity of phytoplankton cultures. The unitis applied in several experimental systems for single and multiplebatch and dilution cultures in combination with different typesof control functions. These applications include: (i) singlebatch cultures with double-beam recording, temperature compensation,manual or automatic dilution and sampling; (ii) a multiturbidometerdesigned to record the growth of 16 batch cultures simultaneously;and (iii) a triple cage-culture turbidostat system. Selectedexamples of application with Skeletonema costatum have alsobeen included to illustrate some of the possibilities of suchmicrocomputer-assisted systems. These examples include studiesof ultradian growth rhythms, toxicity testing and light–shadeadaptation.     

Growth of Suspension-cultured Acer pseudoplatanus L. Cells in Automatic Culture Units of Large Volume

A phytostat to mass culture higher plant cells in liquid medium is described. This apparatus allowed the culture in batch, turbidostat and chemostat of 20 liters of cells. Automatic control of cell suspension growth was based on culture turbidity. Changes with time of certain cell characteristics, particularly cell respiration and phospholipid content, indicated that the test time to harvest large amounts of sycamore cells (Acer pseudoplatanus L.) in good physiological state was about 2 days before the end of the exponential phase of growth, when the cell density reached one million cells per milliliter of culture.     

Autoinduction of bacterial bioluminescence in a carbon limited chemostat

Several strains of four species of luminous marine bacteria were maintained in a chemostat at a constant dilution rate and a variety of steady state densities by carbon (glycerol) limitation in order to study the relationship between culture density and bioluminescence activity. In general, luminescence per cell was constant at high culture density, and decreased dramatically at low culture density. For Vibrio fischeri, luminescence decreased to nondectable levels when the culture was maintained at low density; such dark cells were stimulated to synthesize luciferase and became luminous within minutes when purified autoinducer was added to the chemostat. Two strains, Photobacterium phosphoreum NZ11D and Photobacterium leiognathi S1, did not show the decrease in light intensity at low culture density that was characteristic of all other strains tested; they appeared to be constitutive for bioluminescence.Abbreviations BCM basal salts glycerol medium - BM basal salts medium - BSA bovine serum albumin - D dilution rate - DTT dilitiothreitol - LU light unit=2×10¹⁰ quanta s^-1 - OD optical density - SWC sea water complete medium - specific growth rate     

The 96-well twin-layer system: a novel approach in the cultivation of microalgae

A novel system for the growth and maintenance of microalgae has been developed that allows the cultivation of a large number of strains with little manual effort. The system is based on a 96-well microtiter plate in which a membrane filter constitutes the bottom of each well. Algal strains are immobilised on the membranes and provided with culture medium through contact with layers of glass fibre located beneath the membranes in a special cultivation chamber. The configuration effectively separates culture medium from algal cells which allows the simultaneous exchange of the culture medium for 96 strains within a few minutes without the need to transfer the algae. If necessary, algal strains can be transferred using multi-channel pipettes. We demonstrate that a large variety of microalgal strains including delicate flagellates can be reliably grown in the system under axenic conditions and without cross-contamination. As an array system, the 96-well twin-layer system using immobilised algae is also amenable to high-throughput and massively parallel applications increasingly sought after in algal bio- and environmental technology.     

Predicting Production in Light-Limited Continuous Cultures of Algae

Equations relating productivity, growth rate, cell concentration, and light absorption lead to the prediction that, when incident light is below saturating intensity, maximal productivity will occur at half the maximal growth rate. The freshwater alga Chlorella pyrenoidosa TX71105 and the marine alga Dunaliella tertiolecta were grown in a small continuous culture apparatus with turbidostatic control. With both cultures, the cell concentration showed a linear decrease with dilution rate. Productivity was maximal at about one-half the maximal dilution rate. Average mass per cell increased near the maximal dilution rate, causing some asymmetry in the productivity versus dilution rate curve. The chlorophyll content per unit mass decreased in this region, but the chlorophyll content per cell remained constant. Best production rate in a light-limited algal culture was obtained when the growth rate at very low cell concentration was determined in the apparatus and the dilution rate was set at one-half that value.     

Approximation of continuous growth of Cephalotaxus harringtonia plant cell cultures using fed-batch operation

In Cephalotaxus harringtonia plant cell cultures, periods of batch growth that are limited by hexose uptake are too short to make an accurate estimate of the Monod saturation constant. Continuous cultures are infeasible on a laboratory scale, and semicontinuous cultures require too frequent sampling. Fed-batch operation, consisting of intermittent removal from a culture that is fed continuously, was investigated as a possible solution to these problems. For a constant feed rate, computer simulations showed that a steady state can be achieved which is useful for studying growth at different specific growth rates. In terms of the dilution rate it was confirmed that the operation is essentially equivalent to continuous culture when the samples represent a small fraction of the total culture volume. Experiments with glucose or fructose as the carbon source were carried out in shake flasks fed by a multichannel syringe pump. Results indicate that Monod kinetics based on medium glucose levels cannot adequately describe growth under these conditions. Monod's expression for specific growth rate using internal glucose concentration gives an improved correlation.     

Method for studying the adaptation of Escherichia coli to the acidification of the medium

Apparatus permitting to regulate the growth rate of turbidostat culture of microorganisms has been worked out. The process of adaptation of culture microorganisms to the medium acidity has been investigated by the stabilization of growth rate method. The correlation coefficients between adaptation time and changes of acid concentration in medium have been determined. The effect of aeration and density of microorganisms on the parameters of adaptation process has been considered. The conclusion concerning prospects of the growth rate stabilization method application for studying the regularities of culture microorganisms adaptation to the action of the stress has been made.     

Osmotic, biomass, and oxygen effects on the growth rate of Fusarium oxysporum using a dissolved-oxygen-controlled turbidostat

The system described is a modified Hospodka's turbidostat. This device helps to measure the maximum growth rate of fungi in steady-state aerobic conditions with defined and independent concentration of dissolved oxygen, biomass, and substrate even unlimited. The principle consists of a turbidostat controlled by the dissolved oxygen concentration. The inlet medium pump operates when the dissolved oxygen concentration falls below the set point value. This method allows us to study independently effects of different physical and chemical variables on the maximum specific growth rate of microorganisms. A fungus, Fusarium oxysporum 47 isolated from soil, does not show a depressive effect on growth when dissolved oxygen concentration decreases to 5% and osmotic potential to -25 bars. Increasing biomass concentration in the range 0.1-1.0 g/L appears to depress markedly the maximum growth rate.     

On the analysis of unrestricted mixed cultures in determining the fitness of microbial mutants

Summary Equations describing the growth of two microbial strains in unrestricted mixed culture are developed and their use described. With this treatment, mixed cultures maintained in growth by periodic dilution or by use of a turbidostat may be used to obtain a quantitative measure of the adaptive or maladaptive effects of specific mutant alleles.     

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.     

Description of a redox-controlled sulfidostat for the growth of sulfide-oxidizing phototrophs

This paper describes a novel type of continuous culture for the growth of phototrophic sulfur oxidizers under constant concentrations of hydrogen sulfide. The culture maintains a constant concentration of sulfide despite possible variations in external factors likely to affect photosynthetic activity. Variations in biological activity lead to small departures from the steady-state concentration of hydrogen sulfide which result in variations of the redox potential. These changes in redox, monitored through a redox controller, modulate the rate at which the medium is pumped into the culture and therefore govern the dilution rate. As a result, when changes in external factors such as the light supply occur, the dilution rate of the culture adjusts to the new rate of sulfide oxidation, while maintaining a virtually constant concentration of hydrogen sulfide. The system has been successfully tested for an extended period of several weeks and under conditions of shifting illumination (868 to 113, 113 to 23, and 23 to 7 (mu)E(middot)m(sup-2)(middot)s(sup-1)). After changes in illumination, a transition to a new dilution rate started immediately, reaching a new equilibrium in less than 3 h.     

Continuous culture of RPMI 8226 human cells

Continuous culture of RPMI 8226 human hematopoietic cells was performed. The viable cell number and glucose, lactate and ammonium concentrations became constant within 3–4 days at a constant dilution rate. The viable cell number decreased at low and high dilution rates. The growth and product yields slightly depended on the dilution rate, except for product yield for lactate based on cell number. Growth characteristics of these cells at various dilution rates could be expressed by equations considering the maintenance energy in growth yield. Maximum specific growth rate could be evaluated from the wash-out profile and the known inhibition constants.     

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.     

Kinetic analysis of the growth of Chlorella vulgaris

The energy of the total transmitted light was subtracted from that of the incident light in a culture vessel and the difference was divided by the weight of cells. The value thus obtained was defined as the amount, E(x), of light energy absorbed per unit cell weight per unit time.Batch and continuous cultures of Chlorella vulgaris were carried out at 30 degrees C in the pH range of 6.4-6.7 while restricting illumination. Next the specific growth rate, mu, in the batch culture and the fixed dilution rate, D, in the continuous culture were plotted against E(x). The results showed that the relation between D and E(x) can be expressed in a Michaelis-Menten equation, where the maximal specific growth rate is 0.24 h (-1) and the saturation constant is 6.58 kcal/g . h.Cell concentration calculated by substituting the apparent concentration, X(e), of incubated cells and the apparent maintenance constant, M(e), for this equation agreed with that observed in almost all growth phases. Furthermore, from the change of chlorophyll productivity and the relationship between D and E(x) expressed in this equation, it is assumed that E(x) involves the light energy directly utilized in photosynthesis in the cells and that which is converted into, e.g., heat. This equation also indicated that a maximum in the growth yield existed. Then the growth yield of 0.029 g/kcal obtained at the incident light of 1.46 or 2.63 cal/cm(2) . h was maximum (maximal conversion efficiency of light energy, 15.6%).These results indicate that this method of deriving the equation for the growth rate from this study is a useful procedure for obtaining bioengineering findings.     

Physiological factors affecting streptomycin production by Streptomyces griseus ATCC 12475 in batch and continuous culture

Abstract Conditions of growth are described for the production of streptomycin by Streptomyces griseus ATCC 12475 using chemically defined minimal medium and complex medium. It was found using batch cultures that early synthesis of the antibiotic occurred during growth in minimal medium but was delayed until the onset of stationary phase in complex medium. This effect was independent of whether spores or vegetative cells were used as inoculum. Stability of streptomycin biosynthesis in continuous culture was dependent on dilution rate and medium employed. Cultures were highly unstable when grown on complex medium but could be maintained in steady states in continuous culture using minimal medium when the dilution rate was increased in a stepwise manner, starting at a dilution rate of 0.02 h⁻¹ (15% of μ _max). The effect of changing dilution rate on growth, streptomycin production and the level of streptomycin phosphotransferase was examined using this technique.     

Effect of interstage mixing in multistage culture systems on continuous biomass production

The significance of the interstage mixing on important process parameters of biomass production was studied. The experiments were performed in a multistage tower fermentor and in fermentors in series. The interstage mixing effect can be evaluated under conditions of geometrical similarity, identity of oxygen transfer rate, and identity of dilution rate per stage in the individual stages of both culture systems. Candida utilis was cultivated on a synthetic medium with ethanol as the sole carbon and energy source in the concentration range 10–100 g/liter. Dilution rate, temperature, and pH in each stage of both culture systems were kept constant. It was demonstrated that in the multistage tower fermentor the definite backflow which ensures the permanent reinoculation by adapted cells significantly decreases the inhibitory effect of higher ethanol concentrations on the cell growth and on the rate of ethanol utilization.