Growth of the yeast Hansenula anomala with nitrate as sole source of nitrogen under aerobic and anaerobic conditions

Summary The oxygen requirement ofHansenula anomala growing in batch culture on nitrate as sole source of nitrogen was examined. An aeration rate of 0.03 vvm or a constant oxygen partial pressure of 0.01 bar is sufficient for optimal growth.     

Production of shikonin derivatives by cell suspension cultures of Lithospermum erythrorhizon

Differences in the production of shikonin derivatives by callus and suspension cultures of Lithospermum erythrorhizon Sieb. et Zucc. were examined. When Linsmaier and Skoog medium was used in suspension cultures, cell growth was not accompanied by the production of shikonin compounds. Shikonin derivatives were produced, however, when this medium was used in callus cultures. Differences in shikonin production were examined in terms of the nutrient supply, the effect of the agar itself, and the oxygen supply. Shikonin derivatives could be produced without agar by keeping the cells exposed to air while providing an adequate supply of nutrients. In callus cultures, the production of shikonin compounds was reduced remarkedly when the oxygen concentration in the atmosphere was lowered, evidence that shikonin production during L. erythrorhizon cell growth on Linsmaier and Skoog agar medium is enhanced by an abundant supply of oxygen.     

Diacetyl production by immobilized citrate-positiveLactococcus lactis subsp.lactis 3022 in the fibrous Ca-alginate gel

Summary Diacetyl production by (Citr^*)Lactococcus lactis subsp.lactis 3022 was found to be an oxygen-dependent reaction. The diacetyl production by the cells immobilized in conventional Ca-alginate gel beads (Diameter: 3 mm) was lower than that of the cells immobilized in Ca-alginate gel fibers (Diameter: 0.2 mm), probably because oxygen transfer to the immobilized cells is better in gel fibers than in gel beads.     

Physiological constraints in increasing biomass concentration ofEscherichia coli B in fed-batch culture

Summary Fed-batch culture ofE.coli B was carried out to obtain high concentration of biomass. After requirement of oxygen was met by sparging the pure oxygen, physiological constraints were delineated. High partial pressure of CO₂ caused the decrease of the maximum specific growth rate, whereas fermentative byproducts caused the decrease of biomass yield as well as the maximum specific growth rate.     

Production of HBsAg by growth rate control with recombinantSaccharomyces cerevisiae in fed-batch

Summary To maintain a constant specific growth rate for a recombinantS.cerevisiae in fed-batch, the medium feeding rate has been controlled with respect to the hourly calculated glucose uptake rate. The recombinant yeast producing HBsAg showed the exponential production trend in proportion to the exponential cell growth. Total cell yield in fed-batch was about 0.402 g cells/g glucose, and HBsAg was produced about ten times more than in batch. Decrease of growth rate by HBsAg produced was not shown.     

Influence of oxygen supply in the production of biomass ofE. coli cells immobilized in K-carrageenan gel

Summary Cells of a recombinantEscherichia coli, immobilized in K-carrageenan, show improved distribution of growth in the gel when cultured in conditions of high oxygen tension. The production of both biomass and protein codified by recombinant DNA is increased.     

Production of dextranase byLipomyces starkeyi

Summary The optimal growth rate ofLipomyces starkeyi, with dextran as sole carbon source, was found within the pH range 2.5–4.0, and temperature between 25–30°C. This yeast was unable to grow above 33°C. Dextranase production optima paralleled growth optima, except at pH 2.5. Decrease in enzyme yield at this pH could not be attributed to poor yeast growth or enzyme stability.     

Influence of formaldehyde in control of bacterial and fungal contaminants in plant cell cultures: Its effect on growth and secondary metabolite production

Summary Influence of formaldehyde on growth and secondary metabolite production inin vitro grown tissues of pyrethrum, capsicum and carrot were studied. Formaldehyde concentration above 0.025% completely inhibited the growth of addedBacillus andAspergillus in the culture medium. Formaldehyde up to 0.025% level caused slight inhibition in the growth of pyrethrum callus. Callus subjected to 0.05, 0.1 and 0.2% formaldehyde enhanced the level of pyrethrin production in pyrethrum callus, whereas production of phenolics was lower in all the treatments. Growth of carrot callus and anthocyanin production was not inhibited up to a formaldehyde concentration of 0.04%. Similarly, the production of capsaicin in immobilised cell cultures ofCapsicum frutescens was not inhibited up to 0.04% level of formaldeyde. The results demonstrate the usefulness of formaldehyde to control contamination in plant tissue culture.     

A microtest system for the serial assay of phytotoxic compounds using photoautotrophic cell suspension cultures of Chenopodium rubrum

Chenopodium rubrum photoautotrophic cell suspensions were grown in plastic tissue culture dishes under photoautotrophic conditions. Growth was monitored by measuring cell number, packed cell volume, chlorophyll content and oxygen production. Such microtiter dishes are suitable systems for the serial assay of growth inhibition and various physiological effects (i.e. chlorophyll fluorescence, cell viability, oxygen production) of photoautotrophic cells as caused by herbicides and fungal phytotoxins. The applicability of the test system is discussed.Abbreviations pcv packed cell volume - fr.w. fresh weight - rpm revol. per minute - DMSO dimethyl sulfoxide - PMS phenazine methosulfate - NBT nitro-blue tetrazolium chloride     

The kinetics of glucose fermentation bySelenomonas ruminantium HD4 grown in continuous culture

Summary The production of organic acids (acetate, lactate, and propionate) by the anaerobic, ruminal bacteriumSelenomonas ruminantium HD4 was investigated in both glucose-limited and glucose-sufficient (phosphate-limited) continuous cultures. The fermentation pattern of products exhibited a shift upon release of glucose limitation from acetate and propionate to lactate at a dilution rate of 0.2 h^–1. Glucose sufficiency brought about two-to fourfold increase in specific glucose utilization rate, lactate productivity, and lactate yield relative to glucose-limited growth conditions. The increased lactate production under glucose-sufficient growth conditions was attributed to the overutilization of excess glucose.The mention of firm names or trade products does not imply that they are endorsed or recommended by the U.S. Department of Agriculture over other firms or similar products not mentioned.     

Oxygen sensitivity of nitrogenase is not always a limiting factor of growth under nitrogen-fixing conditions inAzotobacter vinelandii

Summary The effect of a combined nitrogen source to oxygen sensitive mutants was examined. For some oxygen sensitive mutants, oxygen sensitivity was not restored by the addition of nitrogen compounds to their medium. One of these mutants showed oxygen resistant nitrogenase activity similar to that of a wild strain. Results imply that oxygen sensitivity of nitrogenase is not always a limiting factor of growth under aerobic nitrogen-fixing conditions inAzotobacter vinelandii.     

The effect of oxygen transfer on the activity of encapsulated whole cell β-galactosidase

The effect of oxygen transfer on the production of immobilized whole cell β-galactosidase has been evaluated. The encapsulated whole cell β-galactosidase was prepared by combining cell encapsulation and culture into one-step. Escherichia coli was encapsulated and cultured in the growth and production media to accumulate β-galactosidase in itself. Sunflower seed oil was coimmobilized to increase the oxygen transfer rate through the capsule membrane. The oxygen transfer rate increased 63 percent and the activity of β-galactosidase increased by 10 percent. The activity of encapsulated β-galactosidase obtained in the concentric air lift reactor was 86 percent higher than that in the shaking incubator. In the concentric air lift reactor, the accumulation of encapsulated whole cell β-galactosidase was primarily dependent on the capsule velocity. While the accumulation of specific β-galactosidase in the capsule increased with volumetric oxygen transfer coefficient, the cell biomass accumulated in the capsule decreased.     

Lipase production byCandida rugosa: Fermentation behaviour

Summary Extracellular lipase production byCandida rugosa growth has been studied. The main growth parameters, and the lipase activity in the culture broth were determined in order to identify the maximum of enzyme activity.The effect of lipidic material and size and growth phase of the inoculum on enzymatic production have been studied. Maximum extracellular lipase activity was associated with an increase in enzyme production when the number of viable cells started to decrease.     

Spore production ofPenicillium roqueforti by simulated solid state fermentation

Summary A culture technique, based on the growth of a microorganism on inert porous particles (e. g. pozzolano) impregnated and continuously fed with substrate is applied to the growth and spore production ofPenicillium roqueforti. The composition and the feed rate of the medium can be controlled, and the biomass is directly estimated.P. roqueforti exhibits a diauxic growth on the medium containing sucrose and malt extract used, and 1.5 10⁹ spores/g pozzolano may be obtained.     

Different temperature profiles of enzyme secretion by two common strains ofTrichoderma reesei

Summary We have investigated the effects of high and low temperature on the synthesis and secretion of cellulases and other enzymes by two common and readily available strains ofTrichoderma reesei. While some effects were similar in both strains QM9414 and RUT-C30 (a reduction in cellulase production but stimulation of xylanase production at high temperature, and alterations in expression of the cellulase complex at low temperature), some specific differences between the strains were determined, most significantly an enhanced specific secretion rate (secretion/growth) at low growth temperature for QM9414.     

Effect of oxygen supply on berberine production in cell suspension cultures and immobilized cells ofThalictrum minus

The ample supply of O₂ proved to be of great importance for berberine production in cell suspension culture ofThalictrum minus, as the specific O₂ consumption rate of berberine-producing cells was twice as high as that of non-producing cells. Furthermore, berberine yield increased with increases in the volumetric O₂ transfer coefficient (K_La). Estimation of the optimum conditions of oxygen supply in suspension cultures and immobilized cells according to a known theoretical model assuming O₂ uptake by cells to be a zero-order reaction was in good agreement with the experimental data. The O₂ supply to immobilized cells could be improved by reducing the cell density and radius of the bead.     

Detection of ginkgolide A in Ginkgo biloba cell cultures

Ginkgo biloba cells were cultured in two 500 mL shake flasks and in 2 L and 6 L immobilization bioreactors using MS medium supplemented with 1 mg.L^–1 NAA, 0.1 mg.L^–1 K and 30 g.L^–1 sucrose. Specific growth rates were 0.06 d^–1, 0.11 d^–1 and 0.07 d^–1 for the 2 L and 6 L bioreactors and shake flask cultures, respectively. Extracellular phosphate, nitrate, ammonium and carbohydrate uptake rates of the bio reactor cultures were approximately 17 to 39% slower than those of shake flask cultures. The specific oxygen uptake and carbon dioxide transfer rates of immobilized Ginkgo biloba cells ranged from 0.027 to 0.041 mmol O₂.g^–1.d.w.hr^–1 (maximum uptake at 14 days) and 0.020 to 0.057 mmol CO₂g. ^–1.d.w.hr^–1 (maximum production at 14 days). Extracts from the biomass of the two immobilized and shake flask suspension cultures were analysed for ginkgolide A by GC-MS. Yields of 7, 17, 19 and 7 ng.g. ^–1d.w. of ginkgolide A were determined for shake flask 1, shake flask 2 and the 2 L and 6 L immobilized cultures, respectively. Traces of ginkgolide B were detected with the signal to noise ratio, however, being too low for positive confirmation of this last product.Abbreviations CTR Carbon dioxide transfer rate - DO Dissolved oxygen - g.d.w. Gram dry weight - GA Ginkgolide A - GB Ginkgolide B - GC Gas chromatography - GC-MS Gas chromatography-mass spectrometry - HPLC High performance liquid chromatography - K Kinetin - MS Murashige and Skoog salt medium - N₁K₁MS Complete Murashige and Skoog medium supplemented with 1 mg.L^–1 NAA, 0.1 mg.L^–1 K and 30g.L^–1 sucrose - NAA Naphthaleneacetic acid - OTR Oxygen transfer rate - PAF Platelet Aggregating Factor - q_CO2 Specific carbon dioxide production rate - q_O2 Specific oxygen uptake rate - u Specific growth rate     

The effect of aeration on D-xylose fermentation byPachysolen tannophilus,Pichia stipitis,Kluyveromyces marxianus andCandida shehatae

Summary The fermentation of D-xylose byPachysolen tannophilus Y2460,Pichia stipitis Y7124,Kluyveromyces marxianus Y2415 andCandida shehatae Y12878 was investigated in aerobic, anaerobic and microaerophilic batch cultures. The aeration rate greatly influenced the fermentations; growth, rate of ethanol production and oxidation of ethanol are affected. Of the strains tested,Pichia stipitis appears superior; under anaerobic conditions it converts D-xylose (20 g/l) to ethanol with a yield of 0.40 g/l and it exhibits the highest ethanol specific productivity (3.5 g of ethanol per g dry cell per day) under microaerophilic conditions.     

Bioreactor scale-up and oxygen transfer rate in microbial processes: An overview

In aerobic bioprocesses, oxygen is a key substrate; due to its low solubility in broths (aqueous solutions), a continuous supply is needed. The oxygen transfer rate (OTR) must be known, and if possible predicted to achieve an optimum design operation and scale-up of bioreactors. Many studies have been conducted to enhance the efficiency of oxygen transfer. The dissolved oxygen concentration in a suspension of aerobic microorganisms depends on the rate of oxygen transfer from the gas phase to the liquid, on the rate at which oxygen is transported into the cells (where it is consumed), and on the oxygen uptake rate (OUR) by the microorganism for growth, maintenance and production.     

The effect of temperature on the kinetics of ethanol production by Saccharomyces uvarum

Summary In view of the interest in high productivity fermentations at increased temperatures, the effect of temperature on the kinetics of ethanol production by Saccharomyces uvarum was investigated in the range 25–43°C. Using a mathematical model and a nonlinear computer simulation package, the kinetic parameters at each temperature were estimated. It was found that the optimal temperature for growth was 34°C, while the specific ethanol production rate was maximal at 37–43°C. Up to 37°C, the inhibitory effects of ethanol on growth and specific ethanol production rate were unaffected by temperature. However, above this temperature, ethanol inhibition increased significantly.