Characterization of aggregate size in Taxus suspension cell culture

Plant cells grow as aggregates in suspension culture, but little is known about the dynamics of aggregation, and no routine methodology exists to measure aggregate size. In this study, we evaluate several different methods to characterize aggregate size in Taxus suspension cultures, in which aggregate diameters range from 50 to 2,000 μm, including filtration and image analysis, and develop a novel method using a specially equipped Coulter counter system. We demonstrate the suitability of this technology to measure plant cell culture aggregates, and show that it can be reliably used to measure total biomass accumulation compared to standard methods such as dry weight. Furthermore, we demonstrate that all three methods can be used to measure an aggregate size distribution, but that the Coulter counter is more reliable and much faster, and also provides far better resolution. While absolute measurements of aggregate size differ based on the three evaluation techniques, we show that linear correlations are sufficient to account for these differences (R ² > 0.99). We then demonstrate the utility of the novel Coulter counter methodology by monitoring the dynamics of a batch process and find that the mean aggregate size increases by 55% during the exponential growth phase, but decreases during stationary phase. The results indicate that the Coulter counter method can be routinely used for advanced process characterization, particularly to study the relationship between aggregate size and secondary metabolite production, as well as a source of reliable experimental data for modeling aggregation dynamics in plant cell culture.     

Flow cytometry and cell cycle kinetics in continuous and fed-batch fermentations of budding yeast.

Cell size distributions, obtained either as protein distribution by flow cytometry or as cell volume distribution by a Coulter counter, give relevant information about the growth conditions of populations of budding yeast Saccharomyces cerevisiae. We have previously found a good correlation between these distributions and the growth rate in continuous cultures (Ranzi et al., Biotechnol. Bioeng. 1986, 28, 185-190). We now present determinations of the protein distributions and cell volume distributions during different fed-batch fermentations performed with a simple on/off controller. Since during the fed-batch fermentation a true steady state is not obtained, the distributions continuously change with time, but nevertheless we observed a good correlation between the average of both distributions and the actual growth rate. The behavior of the cell size distributions can be interpreted on the basis of a two-threshold cell cycle model in which both the critical protein content at budding (Ps) and the critical protein content for cell division (Pm) are differently modulated by the growth rate. Additional findings will be presented showing that this model can be used to successfully explain the insurgence and the maintenance of oscillatory states in continuous cultures.     

Study on effect of diluent osmotic pressure on yeast cell strength and cell size using a novel micromanipulation technique

A new micromanipulation technique which has previously been used to measure the mechanical properties of single animal cells has now been applied to yeast cells. In this study this technique was used to measure yeast cell strength and cell size across a 2l batch fermentation. Alternatively the cell size could also be determined using a Coulter counter while cell measurement was diluted with a conducting fluid (Isoton II). For the cell strength, it was found that the osmotic pressure of diluents did affect cell strength. However, it was also found that there was no significant effect of osmotic pressure of diluents on cell size whether a Coulter counter or micromanipulation was used for measurement. Micromanipulation has been shown to be a powerful technique for measuring the mechanical properties of yeast cells and it will be very useful for studying their behaviour in cell disruption equipment, e.g. high-pressure homogenizers.     

Isoelectric precipitation of soy protein. II. Kinetics of protein aggregate growth and breakage

Protein aggregate growth and breakage in agitated suspensions are modeled. The model includes growth of particles by a turbulent collision mechanism and breakage by a hydrodynamic shear mechanism. In the model, breakage results in the splitting of the particles into several small fragments. The model parameters are a growth rate constant and a breakage rate constant. Aggregate size distributions were measured with a Coulter counter and the data interpreted using a population balance that governs the steady-state particle size distribution in a continuous stirred tank reactor. Effects of changes in the operating variables pH, concentration, mean residence time, ionic strength, and mixing power input on the model kinetic parameters are investigated.     

Modes of Growth in Mammalian Cells

The increase of cell volume as a function of time was studied throughout the generation cycle in synchronous cultures of Chinese hamster cells using a Coulter aperture and a multichannel analyzer calibrated against known cell volumes. The experimental results were compared to a mathematical model of cell volume increase which considered the effect of the distribution of individual cell generation times on the progress of the population. Several modes of volume increase, including linear and exponential, were considered. The mean volume vs. time curve was rounded at the ends of the cycle even when linear growth was assumed. The experimental results show that cell volume increased in a smooth fashion as a function of time, with no discontinuities in rate detectable at periods when cells may have been undergoing metabolic shifts as, for example, through the phases associated with DNA synthesis, G₁, S, G₂. A statistical test on the comparison of the modal cell volume vs. time data to the predictions of linear and exponential growth models accepted both hypotheses within the resolution of these experiments. However, exponential growth was favored over linear growth in one cell line. Volume dispersion was almost constant with time in both sublines which is also consistent with exponential growth. Limitations of the electronic technique of volume measurement and indications for future experiments are discussed.     

Changes in the incorporation of carbon derived from glucose into cellular pools during the cell cycle of Saccharomyces cerevisiae

The rate of incorporation of 14C derived from [U-14C]glucose into cells of Saccharomyces cerevisiae X2180(1B) was investigated as a function of the cell cycle. After pulse-labelling of exponentially growing populations, centrifugal elutriation was used to isolate various cell fractions of increasing cell size, representing successive stages of the cell cycle. The total amount of 14C incorporated per cell was found to increase continuously during the cell cycle along with cellular protein content and Coulter counter cell volume. This pattern supports the model of exponential cell growth. In order to evaluate changes in intracellular carbon flow during the cell cycle, chemical extraction procedures were used to obtain four cellular fractions enriched in either low-molecular-mass components, lipid material, polysaccharides or proteins. The distribution of 14C among these cellular fractions varied during successive stages of the cell cycle, indicating cell-cycle-dependent fluctuations in intracellular carbon flow. During the G1 phase the flow of 14C into the low-molecular-mass pool increased markedly; concurrently, the rate of incorporation into the polysaccharide-enriched pool decreased.     

Quantification of cell size distribution as applied to the growth of Corynebacterium glutamicum

It is known that the cell size is related to the physiological state of a cell. Therefore, cell size distribution directly reflects the average physiological properties of the cell culture. Cell size distribution can be enumerated by image analysis, flow cytometry and coulter counter. In this study, image analysis was used to characterize the cell size distribution during the growth of Corynebacterium glutamicum and was further analyzed by a distribution function. The parameters of the distribution function indicate the mean value and spread of the distribution. Analysis demonstrated that the maximum specific growth rate was higher (0.67h(-1)) for the growth obtained through serial dilution of seed as compared to growth from a normal seed culture (0.53h(-1)). This was due to a greater percentage of the cell population being in the state of division for the growth through serial dilution in the mid-log phase. The measurement of the cell size distribution demonstrated that the average cell size decreased during the course of growth. The distribution function was also used to enumerate the average specific growth rate of both the conditions of the culture. The demonstrated methodology can be used to predict an average growth property of a cell culture.     

Growth of Azotobacter vinelandii with correlation of Coulter cell size, flow cytometric parameters, and ultrastructure

When Azotobacter vinelandii is grown under nitrogen-fixing conditions, the mean cell volume fluctuates from 2.7 to 6.6 microns 3 as determined using a Coulter counter. When NH4Cl is supplied as nitrogen source, the mean cell volume fluctuates from 4.6 to 7.4 microns3. Parallel experiments using flow cytometric measurements show similar characteristic fluctuations in the narrow forward angle light scattering signal and also in cellular protein content as determined using fluorescein isothiocyanate (FITC) fluorescence. Fluctuations in the perpendicular light scatter signal during batch growth are similar for both sets of growth conditions. Changes in cell morphology and ultrastructure are also similar for both sets of growth conditions, as demonstrated by electron microscopic examination. We conclude that narrow forward angle light scatter is a close correlate of cell size, whereas right angle scatter is an indicator of morphological variations other than size.     

The density of protein precipitates and its effect on centrifugal sedimentation

Isoelectric soya-protein precipitate densities were measured for mean particle sizes ranging from 3.4-65 mum by gradient centrifugation, centrifugation in water-immiscible solvents, tracerdilution, gravity sedimentation of isolated particles. Coulter counter volume determination, and a comparison of Coulter counter and centrifugal sedimentation size distributions. The immiscible system and tracer dilution methods were both found to be unreliable due to experimental uncertainties. The Coulter counter volume measurement indicated the existence of a density-size relationship with the aggregate density decreasing as the size increased. Comparison with sedimentation measurements showed that the Coulter counter measures 80% of the total aggregate volume for 6-mum particles. The relation between aggregate density (rho(a), kg m (-3)) and size (d, mum) was measured for isoelectric soya protein and casein precipitated by ammonium sulfate, using a comparison of the Coulter counter size distribution and centrifugal sedimentation. The functions were described for soya by \documentclass{article}\pagestyle{empty}\begin{document}$$ \rho _a - 1004 = 246d;{ - 0.408} $$\end{document} and for casein by \documentclass{article}\pagestyle{empty}\begin{document}$$ \rho _a - 1136 = 31d;{ - 0.441} $$\end{document} The gradient centrifugation method measured the buoyant density of hydrated protein precipitate which was independent of size, and is consistent with an aggregate structure consisting of primary particles. However, the aggregate structure was not described for all sizes by the theoretical cubic packing of hard-sphere primary particles, nor by the successive random addition of primary particles. The density-size functions indicated up to a fivefold difference in Stokes settling velocities compared to those calculated assuming a constant density difference.     

Induction of size reduction in Escherichia coli by near-ultraviolet light

Escherichia coli AB1157 cells, growing exponentially at 37 degrees C in 63B1 medium (supplemented with glucose and casamino acids) with a doubling time of 50 min, were subjected to continuous illumination with 366-nm light at a fluence of 1.5 kJ . m-2 X min-1. Under these conditions, the growth rate decreased and after 1 h of illumination, a new stable exponential mode was reached with a doubling-time of 73 min. This reduction in growth rate occurred without any change in the rate of cell division for two generations after the beginning of illumination. Survival was unaffected, implying that cell size must have decreased. This was confirmed with size distribution curves of control and illuminated cells obtained with a Coulter counter. Furthermore electron micrographs of negatively stained cells indicated that illumination results in a 30-40% decrease in cell length, the diameter increasing by 8%. Hence 366-nm light uncouples growth and division rates. Illumination under the above conditions triggered the accumulation in vivo of 8-13-linked tRNA. The stationary level of the 8-13 link, 80% of the maximal level, was reached precisely when the growth rate reached its new stable value. Furthermore, no reduction in growth rate occurred in a nuv- cell lacking 4-thiouridine in its tRNAs. Hence we conclude that the 366-nm photons trigger partial tRNA inactivation with consequent slowing down of protein synthesis and accordingly of the cell growth rate. In addition, the stringent response has at most a minor effect. In conclusion, near-ultraviolet light is able to decrease the rate of cell growth by restricting the availability of charged tRNAs, and this occurs without affecting the cell division rate.     

The crystal violet nuclei staining technique leads to anomalous results in monitoring mammalian cell cultures

Nuclear counts determined by crystal violet staining from samples of stationary or microcarrier cultures of hybridomas, CHO or Vero cells were consistently and significantly higher than cell concentrations determined by the trypan blue or Coulter counter methods. This difference was attributed to the presence of a significant proportion of binucleated cells, which are assumed to be 35% of the cell population in the stationary phase of Vero cultures. The proportion of such cells during exponential growth was variable. However, continuous sub-culture of these cells induced a degree of synchrony during growth which resulted in a cyclic variation of the difference between the cell and nuclei counting techniques. This data indicates that care should be taken in interpreting cell culture profiles based solely on crystal violet nuclei staining counts.     

Investigation of hydrodynamic focusing in a microfluidic coulter counter device

The Coulter technique enables rapid analysis of particles or cells suspended in a fluid stream. In this technique, the cells are suspended in an electrically conductive solution, which is hydrodynamically focused by nonconducting sheath flows. The cells produce a characteristic voltage signal when they interrupt an electrical path. The population and size of the cells can be obtained through analyzing the voltage signal. In a microfluidic Coulter counter device, the hydrodynamic focusing technique is used to position the conducting sample stream and the cells and also to separate close cells to generate distinct signals for each cell and avoid signal jam. The performance of hydrodynamic focusing depends on the relative flow ratio between the sample stream and sheath stream. We use a numerical approach to study the hydrodynamic focusing in a microfluidic Coulter counter device. In this approach, the flow field is described by solving the incompressible Navier-Stokes equations. The sample stream concentration is modeled by an advection-diffusion equation. The motion of the cells is governed by the Newton-Euler equations of motion. Particle motion through the flow field is handled using an overlapping grid technique. A numerical model for studying a microfluidic Coulter counter has been validated. Using the model, the impact of relative flow rate on the performance of hydrodynamic focusing was studied. Our numerical results show that the position of the sample stream can be controlled by adjusting the relative flow rate. Our simulations also show that particles can be focused into the stream and initially close particles can be separated by the hydrodynamic focusing. From our study, we conclude that hydrodynamic focusing provides an effective way to control the position of the sample stream and cells and it also can be used to separate cells to avoid signal jam.     

Effects of plating density and age in culture on growth and cell division of neonatal rat heart primary cultures

Summary The cell-type composition of the initial cell population from protease-dispersed neonatal rat heart tissue has been evaluated using time lapse photography and identification of cell type-specific functions. The effects of two commonly employed plating densities on growth and cell division of the two major cell types were examined. Total protein synthesis rates were not affected by plating density but did change with age in culture. Maximum protein synthesis rates were observed during the period of maximum cell division and cell growth (increase in total cell protein), which was from 24 h in culture to the 4th d in culture. After 6 d in culture, synthesis rates for total proteins remained constant for at least 2 wk. Sizing of cells by Coulter counter analysis indicated that essentially all the cells were increasing in size with age in culture. Measurements of cell numbers and rate of DNA synthesis indicated that the extent of cell division was dependent on plating density. Cells disaggregated from neonatal rat hearts consisted of approximately 75% muslce cells and 25% nonmuscle cells. This composition approximates the cell-type composition of the intact neonatal rat heart. In high density cultures there is little cell division and the relative proportionsof the cell types are preserved with time in culture. In low density cultures, proliferation of nonmuscle cells is a significant process and the composition of the cell population changes drastically during the first 2 to 3 d in culture. These results suggest that the low plating density used by many researchers may limit correlation of data derived from such cultures with the physiological state. It also indicates that plating densities should be given in published accounts for comparisons to be made with results from other laboratories. This work was supported in part by U.S. Public Health Service Grant HL10018 and The Pennsylvania State University Agricultural Experiment Station and was authorized for publication as Paper 5490 in the journal series of the Pennsylvania Agricultural Experiment Station.     

Division Cycle of Myxococcus xanthus III. Kinetics of Cell Growth and Protein Synthesis

The kinetics of cell growth and protein synthesis during the division cycle of Myxococcus xanthus was determined. The distribution of cell size for both septated and nonseptated bacteria was obtained by direct measurement of the lengths of 8,000 cells. The Collins-Richmond equation was modified to consider bacterial growth in two phases: growth and division. From the derived equation, the growth rate of individual cells was computed as a function of size. Nondividing cells (growth phase) comprised 91% of the population and took up 87% of the time of the division cycle. The absolute and specific growth rates of nondividing cells were observed to increase continually throughout the growth phase; the growth rate of dividing cells could not be determined accurately by this technique because of changes in the geometry of cells between the time of septation and physical separation. The rate of protein synthesis during the division cycle was measured by pulselabeling an exponential-phase culture with radio-active valine or arginine and then preparing the cells for quantitative autoradiography. By measuring the size of individual cells as well as the number of grains, the rate of protein synthesis as a function of cell size was obtained. Nondividing cells showed an increase in both the absolute and specific rates of protein synthesis throughout the growth phase; the specific rate of protein synthesis for dividing cells was low when compared to growthphase cells. Cell growth and protein synthesis are compared to the previously reported kinetics of deoxyribonucleic acid and ribonucleic acid synthesis during the division cycle.     

Development of an optical method for monitoring protoplast formation from cultured plant cells

The size distribution of cell aggregates during protoplast isolation from Catharanthus roseus and Nicotiana tabacum was measured by a Coulter counter. It was observed that a gradual reduction in the size of cell aggregates occured during protoplast formation. A previously developed specialized spectrophotometer for the photometric measurement of plant cell concentration was used for continuous monitoring of the reduction in the size distribution of cell aggregates during protoplast formation. This made it possible to use changes in optical density (O.D.) to distinguish the three stages in protoplast formation—plasmolysis, maceration and cell wall digestion. During the processes of maceration and cell wall digestion, the O.D. decreased and reached a steady value at the end of each process. Consequently, changes in the O.D. could be used to determine precisely the end of each process. The cell wall digestion process was described by a simple first order reaction model and the rate of protoplast formation (cell wall digestion) was quantitatively evaluated from the rate constant (k) of this reaction. By using the values of k, the optimal enzymatic reaction conditions for isolating protoplasts from C. roseus and N. tabacum cells were determined.     

Tidal variations in suspended matter floc size in the Elbe river and Dollard estuaries

In-situ floc size measurements were made in suspended matter of the Elbe and Dollard estuaries. Floc size was found to be generally smaller in the surface water than in the bottom water and varied systematically with time in relation to the tidal phase. Maximum floc size was also related to particle concentration and, in the Dollard, probably also to flow on and off the tidal flats. Salinity and the total organic matter content of the suspended matter played a minor or no role. Since flocs break up into uniform size distributions during sampling and analysis, Coulter counter particle size was about constant during the tidal cycle. temporarily at Netherlands Institute for Sea Research, Texel, The Netherlands.     

A 3D in situ cell counter reveals that breast tumor cell (MDA‐MB‐231) proliferation rate is reduced by the collagen matrix density

Many cell types require the biophysical and biochemical cues within the 3D extracellular matrix (ECM) to exhibit their true physiologically relevant behavior. As a result, cell culture platforms have been evolving from traditional 2D petridish plates into 3D biomatrices, and there is a need for developing analytic tools to characterize 3D cell culture. The existing cell counting method, using a hemocytometer or coulter counter, requires that cells are suspended in fluids prior to counting. This poses a challenge for 3D cell culture as cells are embedded in a 3D biomatrix. We use a facile 3D cell counting method that overcomes this limitation and allows for in situ cell counting in a 3D cell culture using equipment that is commonly available in a biology lab. Using a breast tumor cell line, MDA‐MB‐231, as a model system, we demonstrated that MDA‐MB‐231 cells (1) grow slower within a 3D collagen matrix than on a 2D substrate for an extended growth time (a week) with a comparable, initial cell‐to‐cell distance, (2) their cell growth rate decreases with the increase of collagen concentration, showing a linear growth rate rather than an exponential growth rate. Further work using flow cytometry showed that the observed growth rate reduction was consistent with the retardation of the transition to S (synthesis) phase in the cell cycle. This work demonstrates the validity of the 3D cell counting method and the importance of cell–ECM interactions in cell proliferation. © 2015 American Institute of Chemical Engineers Biotechnol. Prog., 31:990–996, 2015     

Effects of norepinephrine on neonatal rat cardiocyte growth and differentiation

Summary Norepinephrine stimulates the growth in size of nondividing neonatal cardiocytes. During this time the neonatal cardiocyte is in a period of transition in which the cell can synthesize DNA and yet does not divide. Because the cell undergoes karyokinesis without cytokinesis the objective of this study was to determine whether the norepinephrine-induced growth in size of the neonatal cardiocyte was accompanied by an increase in a) the number of cardiocytes synthesizing DNA, b) the number of binucleate cardiocytes, and c) organized myofibrils. One- to four-d-old neonatal rat heart cells were isolated and placed in serum-free medium which was then supplemented with serum, norepinephrine, norepinephrine plus propranolol, or isoproterenol. After 4 d the number and size of the cells was determined using a Coulter counter. In other cultures cardiocytes were fixed on Days 0, 1, 2, and 4, and an increase in the number of binucleate cardiocytes was found in all treatment groups including controls. However, the rate of binucleation was faster in the norepinephrine group. It was also determined by proliferating cell nuclear antigen (PCNA) antibody staining that by Day 4, over 50% of the cardiocytes were in the cell cycle. The percentage of cells in which PCNA could be detected was higher in the norepinephrine and norepinephrine plus propranolol groups. Furthermore, there was a concomitant increase in the amount and organization of myofibrils in the catecholamine-treated cardiocytes. Supported in part by grant No. HL 29351 from the National Institutes of Health, by a grant from the American Heart Association and with the support of the Southeastern Pennsylvania and Pennsylvania Affiliates of the American Heart Association.     

Effect of dilution rate on growth, productivity, cell cycle and size, and shear sensitivity of a hybridoma cell in a continuous culture

To study the effects of the growth rate of the hybridoma cell Mn12 on productivity, cell cycle, cell size, and shear sensitivity, six continuous cultures were run at dilution rate of 0.011, 0.021, 0.023, 0.030, 0.042, and 0.058 h(-1). This particular hybridoma cell appeared to be unstable in continuous culture with respect to specific productivity, as a sudden drop occurred after about 30 generations in continuous culture, accompanied by the appearance of two populations with respect to the cytoplasmic lgG content. The specific productivity increased with increasing growth rate. The shear sensitivity of the cell, as measured in a small air-lift loop reactor, increased with increasing growth rate. The mean relative cell size, as determined with a flow cytometer, increased with increasing growth rates. Furthermore, the fraction of cells in the S phase increased, and the fraction of cells in the G1/G0 phase decreased with increasing growth rates. (c) 1993 John Wiley & Sons, Inc.     

Specific monoclonal antibody productivity and the cell cycle-comparisons of batch,continuous and perfusion cultures

A selection of mouse hybridoma cell lines showed a variation of approximately two orders of magnitude in intracellular monoclonal antibody contents. The different levels directly influenced apparent specific monoclonal antibody productivity during the death phase but not during the growth phase of a batch culture. The pattern of changes in specific productivity during culture remained basically similar even though at different levels for all cell lines tested. Arresting the cells in the G₁ phase using thymidine increased the specific productivity, cell volume and intracellular antibody content but at the same time led to decreased viability. In continuous culture DNA synthesis decreased with decreasing dilution rate though without an accompanying change in cell cycle and cell size distributions. The data shows both the decrease in viability and intracellular antibody content to be important factors which influence the negative association between specific antibody productivity and growth rate. In high cell density perfusion culture, when the cell cycle was prolonged by slow growth, viability was low and dead, but not lysed, cells were retained in the system, the specific antibody productivity was nearly two fold higher than that obtained in either batch or continuous cultures. The results imply that the prolongation of G₁ phase and the increase in death rate of cells storing a large amount of antibody together cause an apparent increase in specific antibody productivity.