Modelling of Spirulina platensis growth in fresh water using response surface methodology

The influence of nutrient addition on the growth rate of Spirulina platensis in the Mangueira Lagoon water was studied in order to investigate the feasibility of using this water for biomass production. The addition of urea and sodium bicarbonate was studied through surface response methodology, over concentration ranges from 0.0 to 0.01170 M, and 0.0–19.70 gl^–1 respectively. The growth of Spirulina platensis in Mangueira Lagoon water with no addition of nutrients was carried out and compared with the biomass growth after nutrient addition. The results indicated that the optimal level of nutrients was 0.00585 M urea and without the addition of sodium bicarbonate. The biomass concentration was 1.4 gl^–1 in 780 h of cultivation and the doubling time (t _d) was 3.85 days. In 300 h, the biomass concentration in the medium without nutrient addition was 0.9 gl^–1, with a doubling time of 3.80 days.     

The production of lactic acid from whey permeate byLactobacillus helveticus

Summary The effect of pH on growth and lactic acid production ofLactobacillus helveticus was investigated in a continuous culture using supplemented whey ultrafiltrate. Maximum lactate productivity of 5 gl^–1h^–1 occurred at pH 5.5. Whey permeates concentrated up to four times were fermented using batch cultures. Maximum lactic acid concentration of 95 gl^–1 was attained, but residual sugars indicated a possible limitation in growth factors.Nomenclature D Dilution rate [h^–1] - X Biomass [gl^–1] - Glu Glucose consentration [gl^–1] - Gal Galactose consentration [gl^–1] - S Substrate, Lactose consentration [gl^–1] - P Product, Lactate consentration [gl^–1] - Y_p/s Yield, defined as P/S [gg^–1] - r_i Rate of synthesis or consumption of i [gl^–1h^–1]     

Bioreactor culture of Picea mariana Mill. (black spruce) and the species complex Picea glauca-engelmannii (interior spruce) somatic embryos. Growth parameters

Somatic embryo cultures of Picea mariana and the species complex P. glauca-engelmannii were each grown in 7.5-l-capacity mechanically-stirred bioreactors containing 61 medium (LP, von Arnold and Eriksson) with 30 mm sucrose. Growth of both species occurred with no observable signs of shear stress due to mechanical agitation. Growth kinetics were analysed using an array of parameters (settled culture volume, packed culture volume, osmolarity, conductivity, pH). These were compared with fresh weight, dry weight, and somatic embryo number in order to determine what parameters were highly correlated with growth and embryo number. Increasing the sucrose concentration from 30 mm to 60 mm resulted in an increase in biomass and total number of somatic embryos. For P. mariana a maximum dry weight of 6.3 gl^–1 and 3076 embryos ml^–1 occurred in LP medium with 60 mm sucrose after 10–12 days of culture. For P. glauca-engelmannii a maximum dry weight of 4.3 gl^–1 and 2278 embryos ml^–1 occurred in LP medium with 60 mm sucrose after 6–8 days culture. For all sucrose concentrations, fresh weight, dry weight and embryo number were closely correlated with packed culture volume and conductivity for P. mariana, and settled culture volume, packed culture volume and conductivity for P. glauca-engelmannii.Correspondence to: D. I. Dunstan     

A heuristic approach to fed-batch optimisation of streptokinase fermentation

Previous studies have shown that the rate of formation of streptokinase, a secondary metabolite, in batch fermentation is proportional to the specific growth rate of the biomass, which in turn is inhibited by its substrate and the primary product (lactic acid). These kinetics suggest the suitability of fed-batch operation to increase the yield of streptokinase. A near-optimal feed policy has been calculated by the chemotaxis algorithm, and it shows a substrate feed rate decreasing nonlinearly and vanishing after 11 hours. This is followed by batch fermentation for a further 8 hours, at the end of which 12% more streptokinase is generated than by purely batch fermentation. Further improvements in productivity are possible.List of Symbols k _dh^–1 decay constant for active cells - k _ph^–1 decay constant for streptokinase - K _Igl^–1 inhibition constant for lactic acid - K_S gl^–1 inhibition constant for substrate - M gl^–1 lactic acid concentration - P gl^–1 streptokinase concentration - Q 1h^–1 substrate feed rate - S gl^–1 substrate concentration - S _ingl^–1 inlet concentration of substrate - t h time - t _bh end-point of batch fermentation - t _fh end-point of fed-batch fermentation - V l volume of broth in fermenter - V ₀ l initial value of V (at t=0) - V _ml maximum value of V - X gl^–1 total biomass concentration - X _agl^–1 concentration of active biomass - Y _MX yield coefficient for lactic acid from biomass - Y _PX yield coefficient for streptokinase from biomass - Y _XS yield coefficient for biomass from substrate Greek Letters h^–1 specific growth rate of biomass - _mh^–1 maximum specific growth rate     

Growth ofCatharanthus roseus cell suspensions in bioreactors: On-line analysis of oxygen and carbon dioxide levels in inlet and outlet gas streams

Summary Catharanthus roseus cells (C87N) grown in a 30 litre airlift vessel achieved a growth rate of 0.366 day^–1. The maximum biomass yield (9.13 gl^–1) was recorded after 168 hours (7 days). On-line analysis of the composition of inlet and outlet gas streams during the growth cycle allowed calculation of the metabolic activity of the cultures. Oxygen uptake on a dry weight basis reached a maximum of 4.5×10^–4 Moles O₂ g dry weight^–1 h^–1 after 96 hours (during the mid-logarithmic phase of growth) and a maximum of 2.7×10^–3 Moles O₂ l^–1 h^–1 on a volume basis (towards the end of the logarithmic phase). Carbon dioxide production ran in parallel with oxygen use with maxima at 4.2×10^–4 Moles CO₂ g dry weight^–1 h^–1 and 3.4×10^–3 Moles g l^–1 h^–1 respectively.     

Biomass and icosapentaenoic acid productivities from an outdoor batch culture of Phaeodactylum tricornutum UTEX 640 in an airlift tubular photobioreactor

An outdoor tubular photobioreactor, based on an external-loop airlift, has been used to cultivate the diatom Phaeodactylum tricornutum UTEX 640, rich in icosapentaenoic acid (EPA). The system was operated in batch mode. The specific growth rate in the exponential phase, averaged over the whole day, was 0.254 day^–1 · A 25 gl^–1 maximum biomass concentration was obtained by the end of the culture period. The dissolved oxygen generated never rose over 210% of air saturation nor was there impediment to biomass generation or inhibition of photosynthesis. Furthermore, around 2 × 10¹⁷ quanta cm^–2 s^–1 light intensity seemed to saturate the photosynthetic activity. Biomass losses during the night could be reduced to less than 5% by maintaining the culture at 16°C at night. The maximum concentration and productivity of EPA were 423 mgl^–1 and 13 mgl^–1 day^–1, respectively, at the end of the culture, although a 21-mgl^–1 day^–1 net EPA generation rate was obtained at the linear growth phase.     

A combination of methods for the on-line determination of alcohols in microbial cultures

Summary A new method for the continuous on-line determination of methanol (range 0.2 to 10 gl^–1) and ethanol (0.2 to 120 gl^–1) is described. The rate limiting step is diffusion of the alcohol through the walls of a silicone tube immersed in the culture broth. A sintered SnO₂ sensor was used instead of a Flame Ionization Detector for alcohol determination. Measurement is not affected by bioreactor aeration or agitation rates, dissolved oxygen, carbon dioxide, ammonia or the concentration of cells in the medium. The assay system was tested in extended batch cultivation of Methylomonas sp. with methanol as the sole carbon source (final biomass concentration, 35 gl^–1). Sensor readings agreed well with simultaneous off-line gas chromatographic methanol determination.     

Extractive fermentation of ethanol using membrane distillation

Summary During the anaerobic batch cultivation ofKluyveromyces fragilis on a complex medium containing glucose (100 gl^–1), ethanol was produced at levels resulting in the inhibition of growth and product (ethanol) formation. Continuous extraction of the ethanol using transmembrane distillation resulted in a 87% increase in ethanol productivity from 0.99 to 1.85 gl^–1h^–1.     

In vitro zygotic embryo culture of an endangered forest tree Givotia rottleriformis and factors affecting its germination and seedling growth

Summary This study reports a protocol for germination of Givotia rottleriformis (var. Tel. Thella Poniki) using zygotic embryo culture. A 100% germination was obtained by culturing the embryos on Murashige and Skoog medium containing 30 gl^−1 sucrose. A sucrose concentration lower or higher than 30 gl^−1 resulted in lower germination or promoted callus formation. The seedling growth was promoted by the addition of 100 mgl^−1 tyrosine in the medium. Seedlings germinated in the presence of 0.2–0.4 mgl^−1 α-naphthaleneacetic acid and 0.3–0.5 mgl^−1 indole-3-butyric acid were abnormal, showing a slender stem with slender roots or forming callus with stout roots. Germination also affected embryo orientation in culture; placing embryos upright on the medium was most beneficial for germination. The in vitro-germinated seedlings were acclimatized in soil under shady conditions with a survival rate of 60–70%. These plants were phenotypically normal, healthy, and similar to donor plants. This protocol will be useful for overcoming seed dormancy and for rapid multiplication and conservation of G. rottleriformis using zygotic embryo culture.     

Optimization of submerged culture conditions for exopolysaccharide production in <Emphasis Type="Italic">Sarcodon aspratus</Emphasis> (Berk) S.lto TG-3

The effect of medium components (carbon, nitrogen, and mineral sources) and environmental factors (initial pH and temperature) for mycelial growth and exopolysaccharide (EPS) production in Sarcodon aspratus(Berk) S.lto TG-3 was investigated. The optimal temperature (25°C) and initial pH (5.0) for the EPS production in shake flask cultures of S. aspratus were determined using the two-dimensional contour plot. The most suitable carbon, nitrogen, and mineral sources for EPS production were glucose, yeast extract, CaCl₂ and KH₂PO₄, respectively. Notably, the EPS production was significantly enhanced by supplementation of calcium ion. Subsequently, the optimum concentration of glucose (30gl^–1), yeast extract (15gl^–1), CaCl₂ (1.1gl^–1), and KH₂PO₄ (1.2gl^–1) were determined using the orthogonal matrix method. The effects of nutritional requirement on the mycelial growth of S.aspratuswere in regular sequence of glucose>KH₂PO₄>yeast extract>CaCl₂, and those on EPS production were in the order of glucose>yeast extract>CaCl₂>KH₂PO₄. Under the optimal culture conditions, the maximum EPS concentration in a 5-l stirred-tank reactor was 2.68gl^–1 after 4days of fermentation, which was 6-fold higher than that at a basal medium. The two-dimensional contour plot and orthogonal matrix method allowed us to find the relationship between environmental factors and nutritional requirement by determining optimal operating conditions for maximum EPS production in S.asparatus. The statistical experiments used in this work can be useful strategies for optimization of submerged culture processes for other mushrooms.     

Influence of yeast extract concentrationon batch cultures of Lactobacillus helveticus: growth and production coupling

Lactobacillus helveticus was cultivated batchwise on whey permeate supplemented with 2–30g yeast extract l^-1. For low supplementation levels, growth was slow, and a long maintenance phase in the absence of any cell autolysis was observed. When the yeast extract concentration was increased, growth time increased slightly; under these circumstances, a large increase of maximum biomass concentration was recorded, indicating a clear nitrogen source starvation at low supplement concentration. At the same time the length of the maintenance phase decreased; for a 30gl^-1 supplementation, it vanished and a death phase was observed instead: this behaviour highlighted a shift from nitrogen to carbon source starvation. For more and more supplemented media, the final lactic acid concentration was constant, while fermentation time decreased significantly; a growth-associated production phase was followed by a maintenance production phase. The part played by the former mecha nism was under tight control of yeast extract concentration: for 30gl^-1 supplementation, 83% of total lactic acid was provided by a growth-linked production process.     

Lactic acid productivity of a continuous culture of Lactobacillus delbreuckii

Summary Maximum volumetric productivities of biomass (1.40 gl^–1h^–1) and lactic acid (8.93 gl^–1h^–1) for a continuous culture ofLactobacillus delbreuckii occurred between dilution rates 0.35h^–1 and 0.40h^–1. All major nutrients were in excess in these cultures. Glucose utilisation was complete at dilution rates of 0.1h^–1 and lower. Product and biomass yields were constant in the dilution rate range studied (0.05h^–1 to 0.50h^–1).     

Establishment of Orthosiphon stamineus Cell Suspension Culture for Cell Growth

Callus of Orthosiphon stamineus could be induced successfully from petiole, leaf and stem tissues but not roots when cultured on MS medium containing different concentration of NAA (0–4.0 mg l^–1) and 2,4-D (0–2.0 mg l^–1). Highest fresh weight callus production was obtained from leaf explants and those with best friability were obtained on MS medium plus 1.0 mg l^–1 2,4-D plus 1.0 mg l^–1 NAA. Cell suspension cultures were established from these cultures. The appropriate cell inoculum size for the best cell growth was 0.75 g of cells in 20 ml culture medium. Cell suspension culture using MS medium supplemented with 1.0 mg l^–1 2,4-D promoted the best cell growth with maximum biomass of 8.609 g fresh weight and 0.309 g dry weight 24 days after inoculation. Cells that grew in MS medium supplemented with 1.0 mg l^–1 2,4-D reached the stationary growth phase in 15 days as compared to the cells that grew in MS medium supplemented with 1.0 mg l^–1 2,4-D + 1.0 mg l^–1 NAA reached the stationary phase in 24 days. MS medium supplemented with 1.0 mg l^–1 2,4-D was considered as the maintenance medium for maintaining the optimum cell growth of O. stamineus in the cell suspension cultures with 2-week interval subculture.     

Influence of temperature rise on kinetic parameters during batch propagation of Kluyveromyces fragilis in cheese whey under ambient conditions

Three 5 l working volume fermenters were used to investigate the growth of the yeast Kluyveromyces fragilis in acid cheese whey under ambient temperature in order to assess the specific growth rate and yield, the lactose and oxygen uptake rates during the various phases of batch culture, the effect of increasing temperature on the various kinetic parameters, and the need for a cooling unit for single cell production batch systems. The initial dissolved oxygen in the medium was 5.5 mg l^–1 and the pH was maintained at 4.5. The observed lag phase, specific growth rate and maximum cell number were 4 h, 0.2 h^–1 and 8.4 × 10⁸ cells ml^–1, respectively. About 99% of the lactose in cheese whey was utilized within 20 h, 85% during the exponential growth phase. The specific lactose utilization rates by K. fragilis were 0.20 × 10^–12, 1.457 × 10^–12, 0.286 × 10^–12 and 0.00 g lactose cell^–1 h^–1, for the lag, exponential, stationary and death phases, respectively. The dissolved oxygen concentration in the medium decreased as the cell number increased. The lowest oxygen concentration of 1.2 mg l^–1 was observed during the stationary phase. The volumetric oxygen transfer coefficient was 0.41 h^–1 and the specific oxygen uptake rates were 0.32 × 10^–12, 2.14 × 10^–12, 0.51 × 10^–12 and 0.003 × 10^–12 mg O₂ cell^–1 h^–1, for the lag, exponential, stationary and death phases, respectively. The maximum temperature recorded for the medium was 33 °C, indicating that a cooling unit for batch production of single cell protein at ambient temperature is not needed for this type of bioreactor. The increase in medium temperature affected the cell growth and the lactose and oxygen uptake rates.     

Biomass relationship to growth and phosphate uptake ofPseudomonas fluorescens,Escherichia coli andAcinetobacter radioresistens in mixed liquor medium

The ability ofPseudomonas fluorescens, Escherichia coli andAcinetobacter radioresistenns to remove phosphate during growth was related to the initial biomass as well as to growth stages and bacterial species. Phosphate was removed by these bacteria under favourable conditions as well as under unfavourable conditions of growth. Experiments showed a relationship between a high initial cell density and phosphate uptake. More phosphate was released than removed when low initial cell densities (10²–10⁵ cells ml^–1) were used. At a high initial biomass concentration (10⁸ cells ml^–1), phosphate was removed during the lag phase and during logarthmic growth byP. fluorescens. Escherichia coli. at high initial biomass concentrations (10⁷ cells ml^–1), accumulated most of the phosphate during the first hour of the lag phase and/or during logarithmic growth and in some cases removed a small quantily of phosphate during the stationary growth phase.Acinetobacter radioresistens, at high initial cell densities (10⁶, 10⁷ cells ml^–1) removed most of phosphate during the first hour of the lag phase and some phosphate during the stationary growth phase.Pseudomonas fluorescens removed phosphate more thanA. radioresistens andE. coli with specific average ranges from 3.00–28.50 mg L^–1 compared to average ranges of 4.92–17.14 mg L^–1 forA. radioresistens and to average ranges of 0.50–8.50 mg L^–1 forE. coli.     

Effects of activated charcoal, explant size, explant position and sucrose concentration on plant and shoot regeneration of Lilium longiflorum via young stem culture

An efficient system for the in vitro plant and shootregeneration of Lilium longiflorum was developed andaccomplished using transverse thin cell layers (tTCL) of young stems.tTCLs were cut transversely along young stems from which the shoot-tipshad been removed. Sections were measured accurately using a graded gridand were cut in 4 mm × 4 mm × 1 mm cubes, eliminatingepidermal tissue, and were cultured on one-half MS medium containing 8 gl^–1 agar, different sucrose concentrations (10, 20, 30 or 40g l^–1), and with or without 1 mg l^–1 activatedcharcoal (AC). Plants formed on the surface of tTCLs within 60 days onone-half MS medium containing 8 g l^–1 agar and 20 gl^–1 sucrose. Sections of 1 mm taken just below the apicalarea developed buds within 15 days, whereas the sections closer to thebase required about 45 days. Shoot regeneration was enhanced whensucrose concentration was used at 30 or 40 g l^–1 after 60days of culture. No root formation occurred. Both shooting and rootingoccurred when sucrose was used at 20 g l^–1. The plantletswere transferred to soil and grew well under greenhouseconditions.     

Outdoor pond cultivation of the subtropical marine red algaGracilaria tenuistipitata in brackish water in Sweden. Growth,nutrient uptake,co-cultivation with rainbow trout and epiphyte control

Pond cultivation of the subtropical, euryhaline macroscopic red algaGracilaria tenuisipitata var.liui Zhanget Xia was carried out in brackish seawater (6–7) in the Gryt archipelago on the east coast of Sweden, using four outdoor tanks of 30–40 m³. Growth rate and nutrient uptake in batch culture were measured with the aim of estimating the water purification capacity ofG. tenuisipitata in outdoor conditions. Its ability to withstand epiphytic infections was also studied. An average growth rate of 4 biomass increase per day was recorded during two seasons with a maximum growth rate of 9 d^–1. The initial biomass was usually 1 kgFW m^–3 (FW, fresh weight). The nutrient uptake capacity was on average ca. 1 g N_i kgFW^–1 d^–1 and 0.08 g P_i kgFW^–1 d^–1 and the uptake rates for NH₄ ⁺-N were higher than those for NO₃ ^–-N. Both the growth rate and the nutrient uptake rate were highest at the highest water temperature. Co-cultivation with rainbow trout (Oncorhynchus mykiss) was tested: with trout fodder as the only nutrient inputG. tenuistipitata could grow and maintain low levels of N_i and P_i with optimum efficiency at a trout: alga ratio of 1:1 (w:w). Epiphytic growth of filamentous green and brown algae was limited, probably as a result of the high pH values caused by inorganic carbon uptake byG. tenuistipitata. The growth ofEnteromorpha intestinalis, the only significant epiphyte, was completely inhibited and the majority of plants died by a few days treatment with 100 µg 1^–1 Cu²⁺, a concentration that did not severely affectG. tenuistipitata. We conclude thatG. tenuistipitata can be cultivated in outdoor ponds in southern Sweden during 5–6 months of the year using aerated or unaerated batch cultures and that wastewater from trout cultivation may be used as a nutrient source, resulting in purification with respect to N and P.     

The production of Pseudomonas putida for the hydroxylation of toluene to its cis-glycol

A constitutive blocked mutant (UV4) of Pseudomonas putida was grown in a 2.5-l fermentor on a mineral salts medium. Glucose was fed normally over an 18-h period. Gluconate reached about 5 gl^–1 in the medium and then fell to zero as it was utilised. The maximum toluene dioxygenase specific activity (2 g g^–1 h^–1) was obtained over the last 6 h of the fermentation when the pH was fully controlled. In fermentations done at low dissolved O₂ tension (DOT) values there was an overall reduction in the cellular enzyme level. When stored at 4°C in phosphate buffer, pH 7.0, harvested bacteria lost half their activity in about 90 h.     

Extracellular amylolytic system of the yeast Lipomyces kononenkoae

Summary A strain of the yeast Lipomyces kononenkoae which converted starch into SCP with a high yield, produced three extracellular amylases which were purified from the culture fluid by Ficoll concentration, dialysis, isopropanol precipitation and DE-cellulose chromatography: an -amylase, a glucoamylase and a debranching transferase. The latter transferred -1,6-glucosyl units from panose to glucose forming maltose and appeared to have some debranching activity on amylopectin. The -amylase had the following properties: MW 38000 daltons; no effect of added calcium ions on activity; optimum temperature and pH for activity around 40°C and pH 5.5; H and S of heat inactivation 24360 cal mol^–1 and 29.2 cal deg^–1 mol^–1; range of pH stability pH 4–6.5; pI=7.1; final low molecular weight products of starch hydrolysis, maltose and glucose; K_m (40°C, pH 5.5) for starch 2.7 gl^–1, for maltotriose 109 gl^–1; uncompetitive inhibition by maltose with K_i (40°C, pH 5.5) 29.5 gl^–1. The glucoamylase had the following properties: MW 81500 daltons; optimum temperature and pH for activity around 50°C and pH 4.5: H and S of heat inactivation 20400 cal mol^–1 and 17.7 cal deg^–1 mol^–1; range of pH stability pH 4–6.5; pI=6.1; K_m (30°C, pH 4.5) for soluble starch 16.2 gl^–1, for maltose 0.36 gl^–1, for p-nitrophenyl--D-glucoside 0.35 gl^–1; competitive inhibition by glucose with K_i (30°C, pH 4.5) 4.7 gl^–1.     

Antimicrobial activity of food-related Penicillium sp. against pathogenic bacteria in laboratory media and a cheese model system

Food-related Penicillium species ( n ep fy1 = rs 34) and Geotrichum candidum ( n = 11) grown on Czapek Dox and brie agar were tested for their ability to suppress growth of pathogenic bacteria. Ten out of 13 P. camemberti showed antagonistic activity while the other species did not interact significantly with the bacterial growth. The order of inhibition was: Gram-negative bacteria and Bacillus cereus > Listeria monocytogenes , Lactococcus sp. > Micrococcus sp. whereas Lactobacillus sp., Staphylococcus aureus and some Micrococcus sp. were unaffected. When Salmonella typhimurium was inoculated together with P. camemberti P25 in brie agar, bacterial growth was inhibited during the first 6 d of incubation whereafter growth started. The inhibition of L. monocytogenes was similar but less pronounced. The antimicrobial activity produced by P. camemberti P25 and L84 was enhanced with increasing amount of sucrose in the medium. The activity was increased at low pH and destroyed at pH above 8. It was detectable at 15°C but not at 37°C indicating that volatile metabolites might be involved. No significant accumulation of organic acids and no secondary metabolites such as mycotoxins were detected. HSGC-MS analysis indicated that acetaldehyde, benzaldehyde, 3-methylbutanal and 1-octen-3-ol were produced by P. camemberti during the period when inhibitory activity was observed. Pure acetaldehyde and benzaldehyde were shown to be inhibitory to L. monocytogenes and Salm. typhimurium when grown at 15°C and pH 5·5 and 7·0.