Continuous hydrocarbon fermentation with colloidal emulsion feed. A kinetic model for two-liquid phase culture

Candida tropicalis was cultured in a chemostat-type fermentor with n-hexadecane, dispersed in water as submicron droplets, as the only carbon substrate. The emulsion as well as the aqueous medium were fed continuously into the fermentor. A Monod-type equation can correlate the specific group rate in the continuous fermentor with the concentration of submicron droplets. The same equation can also be fitted to the data for the conventional-type batch culture in the same fermentor in which an oil phase as well as an aqueous phase existed, if the hydrocarbon concentration in the aqueous phase excluding oil drops is employed as the substrate concentration. This demonstrates that Candida tropicalis takes up only submicron droplets of n-hexadecane as the carbon substrate.     

Fed-batch hydrocarbon fermentation with colloidal emulsion feed

Candida tropicalis was cultured with n-hexadecane, dispersed in water as submicron droplets, as the only carbon substrate; the emulsion being fed continuously into a fermentor containing only an aqueous medium (fed-batch culture). The results have demonstrated that the organism takes up hydrocarbon accommodated in the aqueous phase as submicron droplets. The cell/substrate yield for the linear growth phase, where growth was limited by the supply of the substrate, was much higher than the yield for the exponential growth phase.     

Culture in the rotating-wall vessel affects recombinant protein production capability of two insect cell lines in different manners

Summary The production of recombinant secreted alkaline phosphatase protein in virally infected insect cells was studied in shaker flask and high aspect rotating-wall vessel (HARV) culture. Two commonly used cell lines, Spodoptera frugiperda Sf-9 (Sf-9) and a nonaggregating isolate of the Trichoplusia ni BTI-Tn-5B1-4 (Tn-5B1-4) cell line, Trichoplusia ni Tn-5B1-4-NA (TN-5B1-4-NA), were used and monitored for 120-h postinfection. Different responses to culture in the HARV were seen in the two cell lines. While the Sf-9 cell line was able to produce slightly greater amounts of recombinant protein in the HARV than in shaker flask controls, the Tn-5B1-4-NA cell line produced significantly lesser amounts in the HARV than in the shaker flasks. Both cell lines exhibited longer life spans and longer periods of protein production in HARV culture than in shaker flask culture, presumably due to lower levels of shear encountered in the HARV. The important difference was in the protein production rate responses of the two cell lines. While the protein production rates of Sf-9 cells were comparable in both HARV and shaker flask cultures, the protein production rates of Tn-5B1-4-NA cells were much lower in HARV culture than in shaker flask cultures. The conclusion is drawn that cell line-specific adaptation to the HARV strongly influences recombinant protein production.     

Fermentation of n-Paraffins by Yeast

Nutritional requirement of Candida lipolytica AJ 5004 and its productivity of α-ketoglutarate were further studied.

It became clear that this yeast required only thiamine as grown factor, and even if the yeast was cultured in chemically defined medium containing adequate amount of thiamine, it was able to produce as high yield of α-ketoglutarate as in the medium containing 0.02% of corn steep liquor.

It was also shown that the rate of convertion of n-paraffin to α-ketoglutarate gradually increased as the concentration of n-paraffins was decreased or as the incubation time was prolonged. A very high rate of conversion, 71%, was obtained after prolonged culture, for 5 days, with a culture medium containing 8% of n-paraffins.

The productivity of α-ketoglutarate from C₉- to C₂₀-alkanes by the yeast was maximum in the range from C₁₅ to C₁₉, especially from C₁₇ to C₁₉.     

The metabolism of long-chain fatty acids and alcohols byCandida tropicalis andSaccharomyces cerevisiae

The factors affecting the growth ofCandida tropicalis andSaccharomyces cerevisiae on medium- and long-chain fatty acids and alcohols in batch culture were investigated. Growth on solid acids and alcohols dispersed in the medium is a maximum for tetradecanoic acid and tetradecanol. The poorer growth observed on shorter chain lengths can be ascribed to their toxicity to the yeasts, whilst the fall off in growth on the higher members is explained by their increasing insolubility in the medium. When the longer-chain-length acids are dissolved in a non-metabolisable hydrocarbon, the growth ofC. tropicalis is improved, but that ofS. cerevisiae is unaffected. This suggests that acids can enter the cells of the former organism by direct contact with the hydrocarbon droplets. The surface ofS. cerevisiae is too hydrophilic for this transfer mechanism to be possible. Fatty acids dissolved in gas oil are utilized as substrates for the growth ofCandida tropicalis in competition with then-paraffins contained in the gas oil. Each fatty acid contributes to a constant proportion of yeast produced, but this proportion decreases as the chain is lengthened. Thus, in mixtures of gas oil with dodecanoic acid, 65% of the yeast is produced from metabolism of the acid, while with octadecanoic acid only 15% is produced. The log specific rates of utilization of the fatty acids within this range diminish linearly with increasing chain length.     

Search for Yeast Producers of Brassylic and Sebacic Fatty Acids

Yeast cultures belonging to the genera Candida, Torulopsis, Saccharomyces, Debaryomyces, Hansenula, Pichia, and Yarrowia, capable of synthesizing brassylic and sebacic fatty acids, were screened. Overall about 200 cultures grown in media containing decane or tridecane as a sole source of carbon were tested. On the medium with tridecane, yeasts synthesized insignificant amounts of brassylic acid. Sebacic acid was produced more intensively in the medium with n-decane. The culture Candida tropicalis, displaying the highest ability to synthesize sebacic acid, was selected.     

Synthesis of Novel Plant Growth Inhibitors Structurally Related to Abscisic Acid

When paraffin wax is dispersed in medium as emulsion, some kinds of bacteria and yeasts readily grow on it. This paper presents a study on microbial cell production from solid paraffin. In this study a paraffin wax which contains 91% of normal paraffins ranging from C₂₅ to C₃₇ with the melting point of 62.5°C was used as a substate, but no solvent was used for the dispersion of the wax.

As a result of this study, the following have been found out. (1) Many strains of liquid normal paraffin assimilating bacteria and yeasts can assimilate paraffin wax. (2) Dried cell yields on added hydrocarbons of Corynebacterium hydrocarboclastus S-12-B2 and Candida tropicalis S-315-Y1 are 70% and 56% respectively, when they are cultured by wax emulsion of 0.6% concentration. (3) When nonion surface-active agent (Plysurf A210G) was added as an emulsifing agent, highly concentrated wax emulsion was obtained, but the growth of microorganisms on it was slower. Further investigation is needed to obtain better strains of bacteria and yeasts and also to find out optimum culture conditions.     

Respiratory activity of Candida tropicalis during growth on hexadecane and on glucose

Summary Rates of oxygen uptake and the oxygen demand during growth of Candida tropicalis on hexadecane and glucose were determined in batch experiments. Oxygen demand was 2.5 fold higher for the synthesis of one unit of cell mass from hydrocarbon than from glucose. On the other hand specific respiration is of the same order of magnitude for both substrates, e.g. 12 mmoles O₂xh^-1xg^-1 (dry weight) and seems to be a constant of this organism. Higher rates of oxygen supply into the medium had no effect on the specific rates of respiration. Specific growth rates on hexadecane were 2.4 times lower than on glucose. It is concluded, that rates of synthesis of cell components are controlled by the overall capacity of the respiratory pathways.     

Scale-up of purine nucleoside fermentation from a shaking flask to a stirred-tank fermentor

Scaling-up purine nucleoside fermentation by a mutant strain of Bacillus subtilis from a shaking flask to a stirred-tank fermentor was attempted. The dimensions and the operating conditions of the stirred tank were determined in order to satisfy the optimum conditions of O₂ transfer and power consumption per unit volume for the shaking flask. When the purine nucleoside fermentation was carried out in the stirred-tank fermentor under these conditions, in which the temperature simulated that in the shaking flask, the total amount of purine nucleosides produced was almost the same as that in the shaking flask, but the accumulation ratio of guanosine to total nucleotides was different from that in the flask. Since urea could not be utilized so efficiently in the stirred-tank fermentor, the NH^p+ _f4 concentration and the pH of the culture broth were lower than those in the shaking-flask culture during fermentation. The activity of inosine monosphosphate dehydrogenase and the accumulation ratio were significantly affected by the NH^p+ _f4 concentration. When the pH of the stirred-tank culture was maintained at 6.9 by ammonia water to keep the NH^p+ _f4 level higher, the ratio was improved to the same level as that observed in the shaking-flask culture. The fermentation heat calculated from the shaking-flask data and its pattern of change were similar to those in the stirred-tank fermentor. Correspondence to: Y. Sumino     

Distribution of the 7S Proteins in Soybean Globulins by Gel Filtration with Sephadex G-200

The level of isocitrate lyase, an enzyme of glyoxylate cycle, in Candida tropicalis was enhanced at the later period of growth when the yeast was cultivated in a semisynthetic glucose medium. On the other hand, such increase in the enzyme activity was not observed in C. lipolytica grown under the same conditions. In the case of C. tropicalis, high concentrations of glucose remaining in the medium permitted the increase in the enzyme activity and the addition of ethanol, one of the major products from glucose, to the glucose medium did not stimulate the enzyme formation, indicating that the enhanced enzyme level in the yeast was not merely attributable to the release from the repression by glucose or to the induction by ethanol. Biotin, one of the growth-stimulating factors for C. tropicalis, affected markedly the level of isocitrate lyase. That is, the supplementation of biotin to the synthetic glucose medium inhibited completely the increase in the enzyme activity, and reversely the absence of biotin stimulated the enzyme formation in the glucose-assimilating cells. Thiamine, another growth-stimulating factor for C. tropicalis, did not show any effect on the level of isocitrate lyase in the yeast. The level of isocitrate lyase in C. lipolytica growing on glucose was not affected by biotin added exogenously.     

Xylitol production by Candida species grown on a grass hydrolysate

Xylitol was produced by selected species of the yeast Candida after growth on a medium containing a hydrolysate of the North American perennial prairie grass big bluestem. The grass was hydrolysed by a combination of dilute acid and enzymatic treatments. After growth on the medium for 120 h at 30 °C, Candida tropicalis ATCC 750 produced a 1.4-fold higher level of xylitol than did C. tropicalis ATCC 20215 while biomass production by C. tropicalis ATCC 750 was 1.7-fold higher than Candida guilliermondii ATCC 20216. The xylitol yields observed for C. tropicalis ATCC 750, Candida mogii ATCC 18364 and C. guilliermondii ATCC 20216 were at least 1.4-fold higher than the yield observed for C. tropicalis ATCC 20215 after growth for 120 h at 30 °C.     

Enhancement of somatic embryogenesis of Ipomoea batatas in solid eultures and production of mature somatic embryos in liquid cultures for application to a bioreactor production system

Somatic embryos of Ipomoea batatas Lam. (sweet potato cv. White Star) were produced in an airlift bioreactor. This work describes the optimization of the embryogenic system on semisolid medium, followed by transfer of the system to liquid cultures and ultimately to the airlift bioreactor. The physiological age of embryogenic callus influenced the number and overall morphology of the embryo population in both semisolid and liquid medium. Maximum mature embryo production (35 embryos 10 mg^-1 inoculum) was obtained from six-week-old callus at 30°C. Somatic embryogenesis occurred in liquid cultures containing 20 mM NH₄NO₃ and 30 mM KCl. Globular embryos formed and continued development in suspension producing viable, mature cotyledonary embryos by day 14. Embryo formation and development was limited in the bioreactor. Although shear stress was responsible for some embryogenic damage, the effect of purging the system with fresh air needed to be investigated. To isolate aeration effects from shear stress effects, atmospheric determinations were performed on shaker flask cultures. Initially the gas composition within the Erlenmeyer headspace was that of room air. Ethylene increased to a maximum of 6.4 ppm (day 16), maximum CO₂, 21.2%, was also evident on day 16, and oxygen was depleted to a minimum of 8.1% by day 14. Purging the cultures with fresh air reduced the number of embryos formed; however, they were significantly longer than those formed in closed flasks. The gas response model of Ipomoea batatas will enable atmosphere replenishment in the bioreactor mimicking that of the shaker flask environment. Once the damaging effects of shear stress have been overcome, the regulation of bioreactor gasses should allow somatic embryo formation in the bioreactor comparable to that in shaker flasks.     

Antifungal antibiotic of the basidiomyceteOudemansiella mucida

A pure culture of the basidiomyceteOudemansiella mucida, isolated by the explantation technique, produces an intracellular antifungal antibiotic. The relatively simple basic growth requirements of the producing strain permit its cultivation on agar and liquid nutrient media. During submerse cultivation in medium containing glucose and cornsteep on a shaker apparatus or in a fermentor, the fungus produces 300–600 μg antibiotic/ml. The main growth characteristics of a mycelial culture of the producing strain and details of its transfer to submerse conditions are described. Dedicated to Academician Ivan Málek on the occation of his 60th birthday     

A novel parallel shaken bioreactor system for continuous operation

A novel continuous bioreactor system was developed as a shaken culture vessel for the investigation of the growth kinetics and product formation of microorganisms in milliscale. The novel bioreactor system mainly consists of a specially designed 250-mL shake flask with two inlets, one for gas supply and one for medium supply, and one combined outlet on the side of flask for exhaust gas and culture liquid. As a result of the circulating motion of the fermentation broth in the shake flask, the maximum liquid height reaches the edge of the outlet and the fermentation broth is accelerated into the outlet by centrifugal force. Additionally, the excess fermentation broth leaving the culture vessel is continuously driven by the exhaust gas. Because of the small scale and the simple handling it is possible to operate many of these shaken bioreactor vessels simultaneously. By using parallel vessels operated at different dilution rates on the same shaker, the data for a complete biomass over dilution rate (X-D) diagram of a biological culture can be evaluated in an efficient manner, thus saving money, materials, and time. Continuous fermentations of the yeast Saccharomyces cerevisiae H1022 (ATCC 32167) in the shaken bioreactor system and in a conventional stirred tank fermentor showed very similar results.     

Production of chum salmon cystatin from the recombinant <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> optimized using response surface methodology

Chum salmon cystatin was overexpressed on Saccharomyces cerevisiae YPH 499. At first, the culture condition for the production of recombinant chum salmon cystatin (RC) by S. cerevisiae YPH 499 was optimized in a shake flask using response surface methodology. Three independent variables; medium pH, inducing time, and the amount of inducing assistant, were analyzed to get the optimal condition for the production of RC. The results were fitted to a second-order polynomial equation, in which the determination coefficient (R ²) was 0.904. The highest RC production in a shake flask, 0.57 U/mL was obtained at 5.7 of medium pH, 6.7 h of inducing time, and 5.6 g/L of inducing assistant. Based on the results of shake flask, the effects of agitation and aeration rates on the production of RC by S. cerevisiae YPH 499 were determined for scaleup in a fermentor. The highest production of RC in a fermentor, 0.56 U/mL was obtained at 350 rpm of agitation rate and 1.0 vvm of aeration rate. RC at 100 μg/g showed the highest inhibitory activity against the autolysis of Alaska pollock surimi based on the analysis of TCA-soluble peptides.     

Isolation and characterization of phenol-degrading yeasts from an oil refinery wastewater in Brazil

This study investigated the aerobic degradation of phenol by yeast strains isolated from an oil refinery wastewater from the Northeast of Brazil. The samples displayed low fungal diversity, as only yeast colonies were detected on Sabouraud dextrose agar containing chloramphenicol 0.05% (w/v). Among the isolates, three yeast strains were selected to be evaluated for their potential for degrading high phenol concentrations. These species were identified through morphological and biochemical characteristics as Candida tropicalis, C. rugosa, and Pichia membranaefaciens. Although the strains were able to degrade the phenol concentration present in the wastewater, which was 7 mg l⁻¹, only C. tropicalis was capable of growing at high concentrations of phenol such as 500 mg l⁻¹ and 1,000 mg l⁻¹ in a mineral medium containing this pollutant as the only carbon source. C. rugosa and P. membranaefaciens were inhibited in the presence of 500 mg l⁻¹ of phenol. However, a longer incubation time was needed for C. tropicalis strain to degrade 1,000 mg l⁻¹ of phenol compared to the time required to degrade 500 mg l⁻¹. Moreover, the strain released a significant amount of polysaccharide biosurfactant in the medium probably to minimize the toxic effect of the high phenol concentration. When challenged with 1,500 and 2,000 mg l⁻¹ of phenol, C. tropicalis was unable to grow at the tested conditions. The results indicate that this strain of C. tropicalis can be considered both a good phenol-degrader and biosurfactant-producer. Application of this strain might be useful in bioremediation activities or treatment of phenol-polluted wastewater.     

Nutritional requirements of Arthroderma tuberculatum

Summary Certain nutritional requirements of one strain ofArthroderma tuberculatum were established in shaken flask culture. Growth was measured on a dry weight basis. The optimum medium for growth consisted of 6 % mono sodium glutamate (or glutamic acid), 4 % glucose, 0.1 % K₂HPO₄ and 0.05 % MgSO₄.7H₂O, with an initial pH range of 7.0–8.0. Maximum growth was attained in this medium after about 4 1/2 days incubation at 28 °C on a rotary shaker.     

Mass propagation of ornamental gentian in liquid medium

An efficient system for clonal mass propagation in liquid culture was established for the propagation of ornamental gentian. In a test of the requirements for three cytokinins [6-benzylaminopurine, N-(2-chloro-4-pyridyl)-N′-phenylurea and N-phenyl-N′-1,2,3-thiadiazol-5-yl urea (TDZ)] in combination with 1-naphthaleneacetic acid (NAA), we found that effective propagation of shoots occurred with 0.01 mg l^–1 TDZ in a 300 ml conical flask that contained 100 ml of medium. The propagation of shoots was also affected by the concentrations of macronutrients (KNO₃, NH₄NO₃ and CaCl₂) and sucrose in Murashige and Skoog's (MS) medium, and it was influenced to some extent by the speed of agitation on an orbital shaker. The most efficient propagation of shoots was achieved in full-strength MS medium supplemented with 0.01 mg l^–1 TDZ and 20 g l^–1 sucrose with agitation at 150 rpm. The propagation of shoots was maximal after 6 weeks of culture (140 shoots from five nodal segments in one flask). Large-scale propagation in a 5-l fermenter was attempted using 3 l of MS medium that contained 0.01 mg l^–1 TDZ and 20 g l^–1 sucrose. More than 2,000 shoots were obtained in the fermenter in 5 weeks following the initial cultivation of five nodal segments for 6 weeks in one 300-ml flask. The shoots that had propagated in the fermenter were transferred directly to soil without prior rooting in vitro and were easily acclimatized within 1 month. Received: 7 October 1997 / Revision received: 16 January 1998 / Accepted: 30 January 1998     

Studies on the Utilization of Hydrocarbons by Microorganisms

Fumaric acid productivity of Candida hydrocarbofumarica in various culture conditions was investigated. Namely, the effects of pH, heavy metal ions, hydrocarbon concentration, aeration and surface active agents were studied.

The addition of CaCO₃ and the aeration were effective for fumaric acid production.

The rate of conversion of n-paraffin to fumaric acid gradually decreased as the concentration of n-paraffins (6%) was increased.

A very high yield, 84% was obtained with a culture medium containing 6% of n-paraffins for 7 days culture.     

Production of poly-D(-)-3-hydroxybutyrate and poly-D(-)-3-hydroxyvalerate by strains ofAlcaligenes latus

Alcaligenes latus strains can accumulate poly-D(-)-3-hydroxybutyrate (PHB) up to about 85% of cell dry weight. The abilities to store poly-D(-)-3-hydroxyvalerate (PHV) of three strains ofA. latus were investigated. With Na-propionate as PHV precursor, strainA. latusDSM 1122 had better PHV accumulation ability than strainsA. latusDSM 1123 and 1124. StrainA. latus DSM 1123 could store PHV when Na-valerate but not Na-propionate served as the PHV precursor. PHB and PHV accumulation byA. latus DSM 1124 rapidly increased when propionic acid and acetic acid were together added to the fermentor. This increase was not obtained in the culture shaker flask and fermentor growing the same strain when Na-propionate alone served as a PHV precursor.