Modification of physiological properties in Saccharomyces uvarum and Kluyveromyces bulgaricus grown in presence of polyoxyalkylene glycoĺ-oleic acid condensates

Summary Condensates of polyoxyalkylene glycol of diverse molecular weight esterified by oleic acid, used as antifoam agents in fermentors, were tested on Saccharomyces uvarum and Kluyveromyces bulgaricus. These compounds, used at a concentration of 0.1% (V/V) in the culture medium, stimulated the aerobic growth of the yeasts, and adding oleic acid (up to a concentration of 0.005% V/V in the medium) to the antifoam compounds further increased the final biomass.the presence of the antifoam agents during the development of yeasts increased their viability at the end of the culture and reinforced this viability for a further conservation by freezing. Antifoam agents also stimulated respiration in K. bulgaricus and to a lesser degree in S. uvarum. Flocculation of both yeasts was decreased.Over and above their physico-chemical foam — inhibiting action, polyoxyalkylene glycol compounds had a beneficial effect on the metabolism of yeasts. These compounds have a more positive action on yeasts than colza oil, another industrial antifoam agents.     

Foam control in biopesticide production from sewage sludge

Several antifoam agents were evaluated for the ability to control foam in the production of Bacillus thuringiensis-based biopesticides using sewage sludge as a raw material. Experiments were conducted in shake flasks as well as in 15 l fermentors with controlled parameters. Polypropylene glycol (PPG), the most commonly used antifoam agent in B. thuringiensis fermentation, inhibited cell growth, sporulation and decreased the entomotoxicity yield even at a concentration of 0.1% (v/v) in sewage sludge medium. About 40% reduction in entomotoxicity was observed when PPG was used at 0.3% (v/v). The impact of PPG on sporulation and toxin synthesis in tryptic soy yeast broth (TSYB) medium was also studied. The inhibitory effects were less severe in TSYB than in sludge medium. Another silicone-based antifoam agent, “Antifoam A”, showed less severe effect on growth and stendotoxin production. The problem of the inhibitory effect of chemical antifoam agents on growth and endotoxin production was minimised substantially with the use of vegetable oils such as canola, olive, and peanut oils. Canola and peanut oil stimulated both sporulation and δ-endotoxin synthesis. The stimulus effect varies with the monounsaturated fat contents of oils. Journal of Industrial Microbiology & Biotechnology (2000) 25, 86–92. Received 09 February 2000/ Accepted in revised form 06 June 2000     

Foaming and media surfactant effects on the cultivation of animal cells in stirred and sparged bioreactors.

Foam formation and the subsequent cell damage/losses in the foam layer were found to be the major problems affecting cell growth and monoclonal antibody (MAb) production in stirred and sparged bioreactors for both serum-supplemented and serum-free media. Surfactants in the culture media had a profound effect on cell growth by changing both the properties of bubbles and the qualities of foam formed. Comparable cell growth and MAb production in sparged bioreactors and in stirred and surface-aerated control cultures were observed only in Pluronic F-68 containing culture media. In media devoid of Pluronic F-68, cells became more sensitive to direct bubble aeration in the presence of antifoam agent which was used to suppress foam formation. Compared with serum-supplemented medium, more severe cell damage effects were observed in serum-free medium. In addition, serum-free medium devoid of cells was partially degraded under continuous air sparging. The mechanism of this damage effect was not clear. Pluronic F-68 provided protective effect to cells but not to the medium. A theoretical model based on the surface active properties of Pluronic F-68 was proposed to account for its protective effect on cell growth. Optimum media surfactant composition in terms of maximum cell growth and minimum foam formation was proposed for stirred and sparged animal cell bioreactor.     

Interfacial properties of cell culture media with cell-protecting additives

In an effort to identify key rheological properties that contribute to cell protection against shear damage, we have measured surface shear and dilatationai viscosities, dynamic surface tension, foaminess, and foam stability for media containing cell-protecting additives. In a companion article,(18) we found that cell-to-bubble attachment was decreased in media containing Methocel, Pluronic F68, or polyvinyl alcohol (PVA). In medium containing polyethylene glycol (PEG) or potyvinyl-pyrrolidone (PVP), attachment was increased. PEG, PVP, serum (FBS), and serum albumin (BSA) increased the surface viscosity of the air/medium surface (thus, producing a more rigid interface), whereas F68 and PVA lowered it greatly. Foaming experiments showed that Methocel, PEG, PVA, and F68 decreased the foam half-life while FBS, BSA, and PVP were foam stabilizers. Interestingly, the foam stability of CHO cell suspensions decreased significantly for cell concentrations higher than ca. 2 x 10(6) cells/mL. Nonviable CHO cells reduced foam stability further. Dynamic surface tension values of the media tested were found significantly differentfrom their static surface tension values. The interfacial properties measured and the results presented in the companion study suggest that the additives that lower dynamic surface tension the most (Methocel, F68, and PVA) correlate well with reduced cell-to-bubble attachment, and thus, cell protection. Reduced dynamic surface tension with these additives implies faster surfactant adsorption, mobile interfaces, lower surface viscosity, and foam destabilization. Because PEG and PVP resulted in increased cell-to-bubble attachment and had different interfacial properties, a different mechanism (compared with Methocel, PVP, and F68) is apparently responsible for their protective effect. Finally, cell protection offered by FBS and BSA is attributed to the foam stabilization properties provided by these additives. (c) 1995 John Wiley & Sons Inc.     

Oxygen transfer properties of bubbles in animal cell culture media

Oxygen transfer rates were determined in a bubble aerated animal cell bioreactor. It was found that the oxygen transfer rates increased in the following order: large bubbles ( approximately 5 mm diameter) < intermediate bubbles ( approximately 1 mm diameter) < micron-sized bubbles ( approximately 100 mum diameter). Under certain conditions, the micron-sized bubbles were capable of achieving oxygen transfer rate up to 100 h(-1), a 10-20-fold higher transfer rate than the large bubbles. The effects of medium composition on oxygen transfer rates were different for the three ranges of bubbles studied. For the large bubbles, oxygen transfer rates decreased with increasing medium complexity. The lowest oxygen transfer rate was found in new-born calf serum (NBCS) and/or Pluronic F-68 supplemented media. For the intermediate and micron-sized bubbles, supplementation with NBCS into the culture media resulted in decreased oxygen transfer rate. However, further supplementation with Pluronic F-68 enhanced oxygen transfer rate greatly for both types of bubbles. The highest oxygen transfer rate was found for micron-sized bubbles in Pluronic F-68 supplemented media containing antifoam agent and NBCS.     

Characterisation of HFBII biosurfactant production and foam fractionation with and without antifoaming agents

The effects of foaming on the production of the hydrophobin protein HFBII by fermentation have been investigated at two different scales. The foaming behaviour was characterised in standard terms of the product enrichment and recovery achieved. Additional specific attention was given to the rate at which foam, product and biomass overflowed from the fermentation system in order to assess the utility of foam fractionation for HFBII recovery. HFBII was expressed as an extracellular product during fed-batch fermentations with a genetically modified strain of Saccharomyces cerevisiae, which were carried out with and without the antifoam Struktol J647. In the presence of antifoam, HFBII production is shown to be largely unaffected by process scale, with similar yields of HFBII on dry matter obtained. More variation in HFBII yield was observed between fermentations without antifoam. In fermentations without antifoam, a maximum HFBII enrichment in the foam phase of 94.7 was measured with an overall enrichment, averaged over all overflowed material throughout the whole fermentation, of 54.6 at a recovery of 98.1%, leaving a residual HFBII concentration of 5.3 mg L⁻¹ in the fermenter. It is also shown that uncontrolled foaming resulted in reduced concentration of biomass in the fermenter vessel, affecting total production. This study illustrates the potential of foam fractionation for efficient recovery of HFBII through simultaneous high enrichment and recovery which are greater than those reported for similar systems.     

Comparison of single- and three-stage tower loop reactors

Summary Hansenula polymorpha was cultured for long periods in 254 cm high single and three-stage countercurrent tower loop reactors 20 cm in diameter using ethanol as a substrate in the absence and presence of antifoam agents (Desmophen 3600 and/or soy oil). In the absence of antifoam agents in the three-stage column, much higher volumetric mass transfer coefficients were attained than in the corresponding single-stage column. The cell productivity in the former, however, was only slightly higher than in the single-stage column due to considerable enrichment of the cells in the foam and nonuniform cell concentration distribution in the three-stage column. In the presence of antifoam agents the three-stage column has a higher cell productivity, OTR, k_L a and a lower specific energy requirement with regard to the absorbed oxygen and/or produced cell mass than the single stage column. The reactor performance is especially high if the bubbling layer height is reduced to 20 cm. Soy oil has considerably less foam eliminating property than Desmophen. Since the soy oil is metabolized by the yeast, large amounts are needed to operate these reactors.     

Mechanism investigation for poloxamer 188 raw material variation in cell culture

Variability in poloxamer 188 (P188) raw material, which is routinely used in cell culture media to protect cells from hydrodynamic forces, plays an important role in the process performance. Even though tremendous efforts have been spent to understand the mechanism of poloxamer's protection, the root cause for lot‐to‐lot variation was not clear. A recent study reported that the low performance was not due to toxicity but inefficiency to protect cells (Peng et al., Biotechnol Prog. 2014;30:1411–1418). In this study, it was demonstrated for the first time that the addition of other surfactants even at a very low level can interfere with P188 resulting in a loss of efficiency. It was also found that the performance of P188 lots correlated well with its foam stability. Foam generated from low performing lots in baffled shaker flask lasts longer, which suggests that the components in the foam layers are different. The spiking of foam generated from a low performing lot into the media containing a high performance lot resulted in cell damage and low growth. Analytical studies using size exclusion chromatography (SEC) identified differences in high molecular weight (HMW) species present in the P188 lots. These differences are much clearer when comparing the HMW region of the SEC chromatogram of foam vs. bulk liquid samples. This study shows that low performing lots have enriched HMW species in foam samples due to high hydrophobicity, which can be potentially used as a screening assay. © 2016 American Institute of Chemical Engineers Biotechnol. Prog., 32:767–775, 2016     

Foam and its mitigation in fermentation systems

Key aspects of foaming and its mitigation in fermentation systems are presented. Foam properties and behavior, conditions that affect foaming, and consequences of foaming are discussed, followed by methods to detect and prevent foam, both without and with the use of antifoam, and their implications. Antifoams were catalogued according to their class (e.g., polyalkylene glycols, silicone emulsions, etc.) to facilitate recognition of antifoams possessing similar base compositions. Relatively few published studies directly comparing antifoams experimentally are available, but those reports found only partially identify clear benefits/disadvantages of any one antifoam type. Consequently, desired characteristics, trends in antifoam application, and chemical types of antifoams are evaluated on the basis of a thorough review of available literature reports describing a specific antifoam's usage. Finally, examples of specific foaming situations taken from both the literature and from actual experience in an industrial fermentation pilot plant are examined for their agreement with expected behavior.     

Analysis of cell-to-bubble attachment in sparged bioreactors in the presence of cell-protecting additives

To investigate the mechanisms of cell protection provided by medium additives against animal cell injury in sparged bioreactors, we have analyzed the effect of various additives on the cell-to-bubble attachment process using CHO cells in suspension. Cell-to-bubble attachment was examined using three experimental techniques: (1) cell-bubble induction time analysis (cell-to-bubble attachment times); (2) forming thin liquid films and observing the movement and location of cells in the thin films; and (3) foam flotation experiments. The induction times we measured for the various additives are as follows: no additive (50 to 500 ms), polyvinyl pyrrolidone (PVP: 20 to 500 ms), polyethylene glycol (PEG: 200 to 1000 ms), 3% serum (500 to 1000 ms), polyvinyl alcohol (PVA: 2 to 10 s), Pluronic F68 (5 to 20 s), and Methocel (20 to 60 s). In the thin film formation experiments, cells in medium with either F68, PVA, or Methocel quickly flowed out of draining thin liquid films and entered the plateau border. When using media with no additive or with serum, the flow of cells out of the thin liquid film and film drainage were slower than for media containing Pluronic F68. PVA, or Methocel. With PVP and PEG, the thin film drainage was much slower and cells remained trapped in the film. For the foam flotation experiments, a separation factor (ratio of cell concentration in the foam catch to that in the bubble column) was determined for the various additives. In the order of increasing separation factors (i.e., increasing cell attachment to bubbles), the additives are as follows: Methocel, PVA, Pluronic F68, 3% serum, serum-free medium with no additives, PEG, and PVP. Based on the results of these three different cell-to-bubble attachment experiments, we have classified the cell-protecting additives into three groups: (1) Pluronic F68, PVA, and Methocel (reduced cell-to-bubble attachment); (2) PEG and PVP (high or increased cell-to-bubble attachment); and (3) FBS (reduced cell attachment butslower drainage films compared with F68, PVA, and Methocel with some cell entrapment in those films). These phenomena are discussed in relation to the interfacial properties of the media reported in a companion Study (this issue). (c) 1995 John Wiley & Sons Inc.     

Increased hGM-CSF production and secretion with Pluronic F-68 in transgenic<Emphasis Type="Italic">Nicotiana tabacum</Emphasis> suspension cell cultures

The effects of Pluronic F-68, a nonionic surfactant, on the production and secretion of human granulocyte-macrophage colony-stimulating factor (hGM-CSF) in a transgenicNicotiana tabacum cell suspension culture were investigated in this study. The addition of Pluronic F-68 was shown to extend cell survival in the stationary phase, but had no influence on effective initial cell growth. With regard to production, it increased the level of extracellular hGM-CSF two-fold. This may be attributable not only to the enhanced expression level, but also to the improved permeability of the cell membrane due to the interaction between Pluronic F-68 and the cell membrane and cell wall. The effect of Pluronic F-68 on the production and secretion of hGM-CSF in a bioreactor was also evaluated. hGM-CSF production in the bioreactor after the addition of Pluronic F-68 proved more effective than in flask cultures.     

Statins and foam cell formation: impact on LDL oxidation and uptake of oxidized lipoproteins via scavenger receptors

The uptake of oxidized lipoproteins via scavenger receptors and the ensuing formation of foam cells are key events during atherogenesis. Foam cell formation can be reduced by treatment with 3-hydroxy-3-methylglutaryl coenzyme A (HMG-CoA) reductase inhibitors (statins). The efficacy of statins is evidently due not only to their cholesterol-lowering properties, but also to lipid-independent pleiotropic effects. This review focuses on lipid-independent pleiotropic effects of statins that influence foam cell formation during atherogenesis, with special emphasis on oxidative pathways and scavenger receptor expression.     

Agitation and aeration effects in suspension mammalian cell cultures

Three different hybridoma cell lines, grown in serum-free media with different levels of Pluronic F-68, were subjected to a shear force of 0.6 N m^-2. Some protective effect due to the polymer was found, indicating it to be a potentially useful adjuvant in serum-free media. Other observations of liquid and gas effects at the reactor level have been included here. A discussion of the difference between suspension and microcarrier cultures, in relation to hydrodynamic effects, is included.     

Physiological, biochemical, and mathematical studies of micro-aerobic continuous ethanol fermentation by Saccharomyces cerevisiae. II: intracellular metabolite and enzyme assays at steady state chemostat cultures

Intracellular metabolite concentration and enzyme activity measurements were made to explain the new metabolic and growth phenomena seen in the micro-aerobic, continuous yeast cultures described in Part I. The results of these assays suggested mechanisms for the observed maximum in the specific ethanol productivity as a function of the oxygen feed rate, changing ATP yields, the effects of antifoam, and the sharp changes in the biomass concentration with small changes in the oxygenation. Measured were the intracellular concentrations of ATP, NADH, glucose 6-phosphate, pyruvate, glycerol, and ethanol, and the activities of hexokinase and alcohol dehydrogenase. Rate-limiting steps were identified by the accumulation of metabolites upstream and the depletion of metabolites downstream of the step.A potential mechanism for the stimulation of fermentation with decreasing oxygenation was an activation of glucose transport by an accumulating intracellular ATP concentration. The inhibition of fermentation at yet lower oxygenation rates may have been caused by the continued accumulation of ATP to the point that the glycolytic kineses were inhibited. A mechanism for the changing ATP yields and intracellular ATP concentration proposed the existence of ATPases or ATP waste reactions stimulated by both oxygen and ATP. Antifoam had the effect of decreasing the resistance for glycerol transport out of the cell. The resulting stimulation of glycerol production and inhibition of ethanol production decreased the intracellular ATP content. Finally, intracellular ethanol was found not to accumulate to levels of higher than the extracellular concentration.     

Permeability and membrane sterol distribution in Saccharomyces uvarum and Kluyveromyces bulgaricus grown in presence of polyoxyalkylene glycol-oleic acid condensates

Summary Antifoam agents, such as polyoxyalkylene glycol-oleic acid condensates, increase cell permeability in Saccharomyces uvarum, but decrease cell permeability in Kluyveromyces bulgaricus.In S. uvarum it was found that the increase in cell permeability is related to a significantly higher level of total sterols. In K. bulgaricus, in which a decrease of permeability was observed, the overall level of sterols is lower.Determination of the sterol derivatives showed that in S. uvarum the content of all sterols identified was increased; in K. bulgaricus only the ergosterol content was increased. The difference in behaviour of the two yeasts grown in the presence of antifoam agents could be attributed to an effect of these agents on sterol biosynthesis.     

<Emphasis Type="Italic">N</Emphasis>-acetyl cysteine suppresses the foam cell formation that is induced by oxidized low density lipoprotein via regulation of gene expression

Foam cells derived from macrophages have been implicated as markers of early stage atherosclerosis development. In this study, we found that N-acetyl cysteine (NAC), a well-known inhibitor of reactive oxygen species (ROS), decreased the generation of ROS and suppressed foam cell formation in the presence of oxidized low density lipoprotein through down-regulation of cluster of differentiation 36 expression. We investigated gene expression profiles in order to determine the effects of NAC on foam cell formation using a microarray analysis. The level of apolipoprotein E, which is involved in lipid efflux, was increased and the levels of the antioxidant genes glutathione peroxidase 1 and 3 were also increased. The expression levels of the oxidative stress response and the DNA repair genes were decreased. These results were confirmed using quantitative real-time PCR. Our results indicate that oxidative stress plays an important role in foam cell formation, and that regulation of oxidation using antioxidants is a potential therapeutic method for blocking atherosclerosis development.     

Understanding and modeling alternating tangential flow filtration for perfusion cell culture

Alternating tangential flow (ATF) filtration has been used with success in the Biopharmaceutical industry as a lower shear technology for cell retention with perfusion cultures. The ATF system is different than tangential flow filtration; however, in that reverse flow is used once per cycle as a means to minimize fouling. Few studies have been reported in the literature that evaluates ATF and how key system variables affect the rate at which ATF filters foul. In this study, an experimental setup was devised that allowed for determination of the time it took for fouling to occur for given mammalian (PER.C6) cell culture cell densities and viabilities as permeate flow rate and antifoam concentration was varied. The experimental results indicate, in accordance with D'Arcy's law, that the average resistance to permeate flow (across a cycle of operation) increases as biological material deposits on the membrane. Scanning electron microscope images of the post‐run filtration surface indicated that both cells and antifoam micelles deposit on the membrane. A unique mathematical model, based on the assumption that fouling was due to pore blockage from the cells and micelles in combination, was devised that allowed for estimation of sticking factors for the cells and the micelles on the membrane. This model was then used to accurately predict the increase in transmembane pressure during constant flux operation for an ATF cartridge used for perfusion cell culture. © 2014 American Institute of Chemical Engineers Biotechnol. Prog., 30:1291–1300, 2014     

An image analysis technique to estimate the cell density and biomass concentration of Trichoderma reesei

Aim:  The objective is to develop an automated image analysis protocol to quantify the cell volume fraction of filamentous fungi ( Trichoderma reesei ) and estimate the biomass concentration.
Methods and Results:  Both dry weight and image analyses were performed on samples collected periodically from 7-l stirred tank fermentations. Using the projected area of lactophenol blue-stained hyphae, the fraction occupied by the cells in a given volume was estimated. Combined with the biomass dry weight obtained by filtration, the method was used to estimate the density of filamentous fungi. Knowing the density of fungi, the algorithm was employed to quantitatively assess the biomass evolution during the course of fermentation even in the presence of solid particles.
Conclusions:  A density of 0.334 g dry weight cm⁻³ was found for T. reesei RUT C-30. The image analysis protocol allowed successful estimation of biomass concentration in the presence or absence of solid particles.
Significance and Impact of the Study:  Methods to quantify biomass during the industrial production of cellulase with T. reesei are often limited due to the presence of solid substrates. The image analysis protocol presented here offers a quick and easy way to estimate biomass concentration of filamentous micro-organisms in insoluble medium.     

Perilipin and adipophilin expression in lipid loaded macrophages

Lipid-filled macrophages (foam cells) are a defining feature of atherosclerotic plaques. Foam cells contain lipid droplet-associated proteins that in other cell types regulate lipid turnover. In foam cell such proteins may directly affect lipid droplet formation and lipid efflux. Differentiated primary human monocytes or THP-1 cells were lipid loaded by incubation with aggregated low density lipoproteins (AgLDL) or VLDL resulting in macrophage foam cells with predominantly cholesterol ester or triglyceride-rich lipid droplets, respectively. Lipid droplets were isolated and major proteins identified by mass spectrometry, among them the apolipoprotein B-48 receptor that has not previously been recognized in this context. Expression of two proteins, perilipin and adipophilin, was quantified by Western blots of cell lysates. Perilipin content decreased and adipophilin increased with lipoprotein lipid loading regardless of intracellular neutral lipid composition. This protein expression pattern may hinder lipid turnover in macrophage foam cells, thereby increasing lipid content of atherosclerotic plaques.     

Cell death from bursting bubbles: Role of cell attachment to rising bubbles in sparged reactors

Bursting bubbles are thought to be the dominant cause of cell death in sparged animal or insect cell cultures. Cells that die during the bubble burst can come from three sources: cells suspended near the bubble; cells trapped in the bubble lamella; and cells that attached to the rising bubble. This article examines cell attachment to rising bubbles using a model in which cell attachment depends on cell radius, bubble radius, and cell–bubble attachment time. For bubble columns over 1 m in height and without protective additives, the model predicts significant attachment for 0.5‐ to 3‐mm radius bubbles, but no significant attachment in the presence of protective additives. For bubble columns over 10 cm in height, and without protective additives, the model predicts significant attachment for 50‐ to 100‐μm radius bubbles, but not all protective additives prevent attachment for these bubbles. The model is consistent with three sets of published data and with our experimental results. Using hybridoma cells, serum‐free medium with antifoam, and 1.60 ± 0.05 mm (standard error) radius bubbles, we measured death rates consistent with cell attachment to rising bubbles, as predicted by the model. With 1.40 ± 0.05 mm (SE) radius bubbles and either 0.1% w/v Pluronic‐F68 or 0.1% w/v methylcellulose added to the medium, we measured death rates consistent with no significant cell attachment to rising bubbles, as predicted by the model. © 1999 John Wiley & Sons, Inc. Biotechnol Bioeng 62: 468–478, 1999.