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.     

Effect of antifoam addition on gas-liquid mass transfer in stirred fermenters

The influence of three well-known antifoaming agents (polypropylene glycol, silicone and soybean oil) on gas-liquid mass transfer in stirred tanks is studied, both in model and in fermentation media. The effect of antifoam concentration, ionic strength, viscosity, agitation speed and gas flow rate are investigated. It is found that antifoam addition at low concentrations markedly decreases the gas-liquid volumetric mass transfer coefficient, k_La, for the three antifoam agents tested. Although the major effect is on the film coefficient k_L, some effect is also detected on the specific area, a. It is found that the influence of viscosity and antifoam addition are not cumulative: each tends to attenuate the other's effect on mass transfer. Both for silicone and for soybean oil, but not for PPG in the concentration range studied, there is an antifoam concentration above which further antifoam addition starts to improve k_La.     

Fish toxicity and surface tension of non-ionic surfactants: investigations of antifoam agents

Fish toxicity of etho-nonylphenol and of two non-ionic antifoam agents was tested using rainbow trout, Sulmo guirdneri , in 24 h tests. The surface tension of these three compounds was found to depend on concentration and ageing time of the test solutions. The toxicity of the surfactant was about twice as high as known values, with a LC⁵⁰ of 8.5 mg/1 at 15°C. The addition of antifoam agents to the surfactant solutions further lowered the surface tension but did not alter substantially the fish toxicity of the surfactant. Contrary to expectation, the fish survived in concentrated antifoam solutions at surface tensions as low as 31 dyn/cm for more than 24 h without any apparent damage. The relevance of the surface tension regarding the fish toxicity of detergents in general is critically discussed.     

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     

Fouling of microfiltration membranes by broth-free antifoam agents

The fouling tendencies of seven commercial antifoam agents used with microfiltration membranes were investigated in a stirred cell. Parameters such as viscosity, oil droplet size distribution, contact angle, work of adhesion (W(a)), membrane type, operating pressure, and feed concentration were examined. The results show that a silicone-based antifoam, G832, gave a significantly lower flux (相似文献   

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.     

Correction to: Industrial antifoam agents impair ethanol fermentation and induce stress responses in yeast cells

Applied Microbiology and Biotechnology - The article “Industrial antifoam agents impair ethanol fermentation and induce stress responses in yeast cells” was originally published Online...     

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.     

A method for aeration and foam control in fermentation vessels

The production of large quantities of microbial mass, or their by-products, frequently requires aeration and mixing of fluid media. This operation often results in copious production of foam which cannot be exhausted with the effluent air or gas. Foam is usually controlled with antifoam agents which may interfere with product purity, oxygen uptake, and with subsequent product, handling. The process herein described obviates the requirement for antifoam agents or other foam-control methods. In essence, the air (or other gases) and foam in the headspace are continuously withdrawn, entrained in the intake side of a self-priming pump, and reintroduced into the bulk of the process liquid medium. The headspace may be enriched with oxygen or other gases.     

Lipopeptide production from Bacillus sp. GB16 using a novel oxygenation method

During lipopeptide (biosurfactant) production by Bacillus sp. GB16, conventional aeration method using added antifoam agent was unsuccessful due to the excessive formation of foam and the inhibitory effects of the antifoam chemical. A novel integrated method was developed to increase the dissolved oxygen concentration during the microbial production of biosurfactant lipopeptides. This novel method consisted of adding hydrogen peroxide to the medium, which decomposed to oxygen and water by cell's catalase and adding a vegetable oil and Ca-stearate to the medium as antifoam agents, as well as oxygen vectors. The dissolved oxygen concentration could be controlled by the automatic addition of hydrogen peroxide to the bioreactor. A significant improvement, i.e., suppression of foaming and, therefore, a three-fold extension of the cultivation time and, consequently, remarkable increase in the lipopeptide production could be achieved. This result showed that a novel aeration method was effective, especially when excessive foaming caused problems during microbial production of biosurfactant.     

Wirkung von Ölen und Fettsäuren auf Wachstum und Enzymbildung bei Thermoactinomyees vulgaris. V. Untersuchungen zur Metabolisierung des Öles

The splitting of vegetable and animal oils used as antifoam agents and the metabolization of fatty acids released were analysed during fermentation of T. vulgaris in a 30 l jar fermenter. During cultivation time of 22 hours the oil amount decreased by 60 to 70%. The metabolization of fatty acids is 50 to 90% of the starting level depending on the kind of acid. The eventual effect of the fatty acids released from antifoam oils on the protease production is discussed.     

Cover filter unit for on-line sampling of fungal broths

New cover filter sampling unit was tested in fungal fermentations in the presence of antifoam agents producing sticky fungal polysaccharides. Cover filter unit long-term filter capacity depends on the intensity of the pumping capacity of impeller as well as on the position of the filter unit.     

Surfactant pretreatment of a polysulfone ultrafilter for reduction of antifoam fouling

Effectiveness of surfactant precoat treatment of the polysulfone ultrafilter was first investigated for reduction of membrane fouling in ultrafiltration of antifoam. Fifteen different surfactants, including alcohols and synthetic nonionic surfactants, were tested. In general, pretreatment with nonionic surfactant gave a larger flux than that with alcohol did. The flux increase by pretreatment with nonionic surfactant depended on a hydrophile lipophile balance (HLB) value and type of hydrophobic tail. The most effective surfactant for reducing antifoam fouling among the 15 surfactants was Brij-58 which has an HLB value of 16 and a straight alkyl hydrophobic chain. The ultrafiltration flux of the membrane treated with Brij-58 was almost three times larger than that of untreated membrane. The precoat treatment with Brij-58 was the most effective for reducing antifoam fouling in terms of rejection properties.Furthermore, flux was also improved by the surfactant pretreatment in ultrafiltration of model process streams, such as fermentation media, broth, and yeast suspension with or without antifoam. The surfactant Brij-58 was found to be more effective for reducing membrane fouling in ultrafiltration of model stream YG compared with ethanol or Brij-35. The mean flux increase by the pretreatment with Brij-58 was about 80% in ultrafiltration of the model stream without antifoam. When antifoam was added to the model stream, flux was almost doubled by the pretreatment with Brij-58. The effectiveness of surfactant precoat treatment for reducing membrane fouling was also confirmed in terms of rejection properties. (c) 1994 John Wiley & Sons, Inc.     

OBSERVATIONS ON FOAMING AND ITS INHIBITION IN A BACTERIAL CULTURE

SUMMARY: Inhibition of foaming in a continuous culture of bacteria has been studied. At first, foaming was inhibited by the addition of antifoam to the culture only when a foam layer was present. When the antifoam was added in this way foaming often became intense and antifoam additions had to be more and more frequent. In a preferred method the antifoam was added at regular intervals which were sufficiently short to inhibit foaming completely throughout the intervening periods. This method required less antifoam than the other. The effects of foaming in cultures, its causes, and allied problems are discussed.     

Strategies to overcome foaming and wall-growth during the cultivation of Morinda elliptica cell suspension culture in a stirred-tank bioreactor

Strategies to overcome foaming and wall-growth during the cultivation of Morinda elliptica (Rubiaceae) cell suspension cultures in a stirred-tank bioreactor are described. Of all the strategies applied, only bubble-free aeration was successful in eliminating foaming by 100%. Despite the foaming effect of around 40% in G medium strategy with 0.012% (v/v) antifoam, the maximum dry cell weight attained (19.2 g l^-1) and anthraquinone (AQ) content (4.0 mg g^-1 DW) was nearly three times higher than that achieved in cultivation using 0.025% (v/v) antifoam. For continuous cell growth, the effect of inoculum age should also be considered when anti-foam is to be added. P medium strategy, without antifoam addition, not only promoted both growth (18 g l^-1) and AQ production (9.8 mg g^-1 DW), but also resulted in lower foaming and wall-growth (below 30% level), and higher foaming reduction (30–40%). This revised version was published online in June 2006 with corrections to the Cover Date.     

Foaming and cell flotation in suspended plant cell cultures and the effect of chemical antifoams

Foam development and stability in Atropa belladonna suspensions were investigated as a function of culture conditions. Foaming was due mainly to properties of the cell-free broth and was correlated with protein content; effects due to presence of cells increased towards the end of batch culture. Highest foam levels were measured 11 days after inoculation. Air flow rate was of major importance in determining foam volume; foam volume and stability were also strongly dependent on pH. Foam flotation of plant cells was very effective. After 30 min foaming, ca. 55% of cells were found in the foam; this increased to ca. 75% after 90 min. Polypropylene glycol 1025 and 2025, Pluronic PE 6100, and Antifoam-C emulsion were tested as chemical antifoams. Polypropylene glycol 1025 and Antifoam C at concentrations up to 600 ppm had no adverse effect on growth in shake flasks; Pluronic PE 6100 has an inhibitory effect at all levels tested. Concentrations of polypropylene glycol 2025 and Pluronic PE 6100 as low as 20 ppm reduced foam volumes by a factor of ca. 10. Addition of antifoam reduced k(L)a values in bubble-column and stirred-tank bioreactors. After operation of a stirred reactor for 2 days using Antifoam C for foam control, cell production was limited by oxygen due to the effect of antifoam on mass transfer. Theoretical analysis showed that maximum cell concentrations and biomass levels decline with increasing reactors working volume due to greater consumption of antifoam to prevent foam overflow. The results indicate that when chemical foam control is used in plant cell cultures, head-space volume and tolerable foam levels must be considered to optimize biomass production. (c) 1994 John Wiley & Sons, Inc.     

Cultivation of Bacillus thuringiensis in an airlift reactor with wire mesh draft tubes

An aeration strategy was proposed for foam control in an airlift reactor with double wire mesh draft tubes. The airlift reactor was employed in the cultivation of Bacillus thuringiensis for thuringiensin production. The aeration strategy involved two situations. If the foam rose and touched the foam probe, the air flow rate was dropped to a low value for a certain period. However, if the DO value was already below 10% of the saturation when the air flow rate was dropped, the conventional foam control was employed. The production of thuringiensin based on the proposed strategy was up to 70% higher than that of using the conventional cultivation method with addition of antifoam agents for foam control.     

Fouling effects of yeast culture with antifoam agents on microfilters

The fouling effects of yeast fermentation broths of Candida utilis in the presence of various commercial antifoam agents (PPG2000, B5600, and G832) up to 4.0 mL/L were studied, using Millipore polyvinylidene fluoride 0.22-mum hydrophilic membranes (GVWP), in a stirred-cell system at 50 kPa and 700 rpm. PPG2000, which has a low value of work of adhesion (W(a) of 0.81 mN/m), gave a steady flux of broth of 29 L/(h m(2)) and was found to have no significant fouling effect on the microfiltration of broth. G832, which has a high W(a), (26.0 mN/m) reduced the flux of the broth to 17 L/(h m(2)); i.e., by 42% when only 1.0 mL/L was used. However, B5600, which has a W(a) of 14.3 mN/m, was found to enhance the flux of broth to 54 L/(h m(2)); i.e., by 86%, due to the preferential adsorption of the B5600 components onto the hydrophobic cell contents released. These results were reinforced by the depressurization experiments performed with both hydrophilic (GVWP) and hydrophobic (GVHP) membranes, using both young and aged broths. B5600 was found to be the optimum antifoam agent in this study in terms of membrane performance and defoaming efficiency. (c) 1997 John Wiley & Sons, Inc.     

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.     

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