Growth and anthocyanin production by carrot suspension cultures grown under chemostat conditions with phosphate as the limiting nutrient

Chemostat cultures of carrot suspension cultures, where growth was limited by the concentration of phosphate in the input medium, were achieved by replacing a fixed proportion of the culture with fresh medium at daily intervals. In the range 0.05–0.30mM phosphate in the input medium and at a specific growth rate of 0.357 days^?1, steady-state culture density but not anthocyanin in the cells was strictly proportional to the input phosphate concentration with no intercept. At a phosphate concentration of 0.10mM and growth rates from 0.105 to 0.430 days^?1, the steady-state culture density could not be described by Monod's model of chemostat cultures, but could be described by Nyholm's model. The steady-state levels of anthocyanin were not strictly proportional to the steady-state biomass under all conditions, showing that anthocyanin production is not completely growth associated.     

Production of the macrolide antibiotic tylosin in batch and chemostat cultures

The production of tylosin and related compounds by Streptomyces fradiae NRRL 2702 was studied in batch and chemostat cultures using a soluble synthetic medium. In batch culture, a trophophase–idiophase kinetic pattern was observed with tylosin, macrocin, and relomycin accumulating in the idiophase. When the organism was grown in chemostat culture, the specific rate of production of tylosin and related compounds (q_tylosin) was found to be a function of the growth rate. The maximum value of (q_tylosin) was observed when D = 0.017 hr^?1. At this growth rate only tylosin and relomycin accumulated in the medium. By varying the concentration of glucose in the ingoing medium it was possible to study the effects of glucose on tylosin synthesis in chemostat cultures. At a growth rate of 0.017 hr^?1, the maximum value of q_tylosin was 0.71 mg tylosin/g dry weight (DW)/hr when the glucose uptake rate was 7 mg glucose/g DW-hr. This value of q_tylosin was 40% greater than the maximum q_tylosin observed in batch culture. When glycerol was substituted for glucose in the medium, it was possible in chemostat culutures to get values of q_tylosin approximately 20% greater than those obtained with glucose at the same uptake rate. By varying the concentration of sodium glutamate in the ingoing medium it was possible to show that increasing the specific uptake rate of sodium glutamate increased the values of q_tylosin obtained. Similar chemostat experiments where the inorganic phosphate concentration in the ingoing medium was varied showed that increased the uptake of phosphate decreased the values of q_tylosin obtained. Also increasing the uptake rate of phosphate increased the relomycin-to-tylosin ratio. By taking into consideration the suppressing effects of glucose and the stimulating effects of sodium glutamate on tylosin synthesis, it was possible to formulate a medium that resulted in a value of q_tylosin of 1.1 mg/g/hr being obtained at a growth rate of 0.03 hr^?1. Batch fermentations with this medium did not follow a trophophase–idiophase kinetic pattern, but instead tylosin was actively synthesized during a period of rapid mycelial growth.     

CONTINUOUS CULTURE OF MARINE DIATOMS UNDER SILICATE LIMITATION. II. EFFECT OF LIGHT INTENSITY ON GROWTH AND NUTRIENT UPTAKE OF SKELETONEMA COSTATUM1,2

Two replicate experiments were conducted to investigate the effect of light intensity on the growth and nutrient uptake of Skeletonema costatum (Grev.) Cleve in silicate-limited continuous culture. Each experiment began with 4 identical chemostat cultures of S. costatum growing at the normal laboratory light (0.14 ly · min^?1, continuous illumination) under strong silicate limitation. Screens were placed over 3 cultures reducing them to light intensities of 0.042, 0.021 and 0.0018 ly · min^?1. Based on growth rules, nutrient uptake rates, cell morphology and chemical composition, the cultures receiving 0.021, and 0.0018 ly · min^?1 appeared to he light-limited, whereas the culture receiving 0.14 ly.     

Isolation of a yeast-lyzing Arthrobacter species and the production of the lytic enzyme complex in batch and continuous-flow fermentors

A gram-negative bacterium strongly lytic toward living cells of the food yeast Saccharomyces fragilis was isolated by continuous-flow enrichment from compost. The organism was identified as a species of Arthrobacter. The extracellular lytic enzyme complex produced by this bacterium contained β-1,3-glucanase, mannan mannohydrolase, and proteolytic activities. The polysaccharases were inducible by whole yeast cells. In chemostat cultures on chemically defined media, synthesis of the polysaccharases was very slight and only detectable at dilution rates below 0.02 hr^?1. Enzyme production in defined media was not solely dependent on growth rate but also was influenced by the growth limiting substrate and the culture history. The production of individual depolymerases and of the lytic activity was studied in batch and chemostat cultures containing yeast as the limiting substrate. The maximum specific growth rate of the Arthrobacter under these conditions was 0.22 hr^?1. β-1,3-Glucanase and proteolytic activities were synthesized by exponentially growing bacteria but maximum lytic titers did not develop until the specific growth rate was declining, at which time mannan mannohydrolase syntheses was induced. In yeast limited chemostats polysaccharase syntheses were greatest at the lowest dilution rates examined, namely 0.02 hr^?1. Further optimization of enzyme production was achieved by feeding the Arthrobacter culture to a second-stage chemostat. A comparison of lytic enzyme productivities in batch and chemostat cultures has been made.     

Glucose uptake of Cytophaga johnsonae studied in batch and chemostat culture

The influence of different physiological states on the glucose uptake and mineralization by Cytophaga johnsonae, a freshwater isolate, was examined in batch and chemostat cultures. At different growth rates under glucose limitation in chemostat cultures, different uptake patterns for ¹⁴C labeled glucose were observed. In batch culture and at high growth rates the glucose uptake potential showed a higher maximum velocity and a much lower substrate affinity than at lower growth rates. These findings and the results of short-term labeling patterns could be explained by two different glucose uptake mechanisms which enable the strain to grow efficiently both at high and low substrate concentrations. Substrate specificity studies showed that a structural change of the C-2 atom of the glucose molecule was tolerated by both systems. The consequences of these results for the ecophysiological classification of the Cytophaga group and for the operation of continuous cultures are discussed.     

Kinetics of biphasic growth of yeast in continuous and fed-batch cultures

The influence of dilution rate on the production of biomass, ethanol, and invertase in an aerobic culture of Saccharomyces carlsbergensis was studied in a glucose-limited chemostat culture. A kinetic model was developed to analyze the biphasic growth of yeast on both the glucose remaining and the ethanol produced in the culture. The model assumes a double effect where glucose regulates the flux of glucose catabolism (respiration and aerobic fermentation) and the ethanol utilization in yeast cells. The model could successfully demonstrate the experimental results of a chemostat culture featuring the monotonic decrease of biomass concentration with an increase of dilution rate higher than 0.2 hr^?1 as well as the maximum ethanol concentration at a particular dilution rate around 0.5 hr^?1. Some supplementary data were collected from an ethanol-limited aerobic chemostat culture and a glucose-limited anaerobic chemostat culture to use in the model calculation. Some parametric constants of cell growth, ethanol production, and invertase formation were determined in batch cultures under aerobic and anaerobic states as summarized in a table in comparison with the chemostat data. Using the constants, a prediction of the optimal control of a glucose fed-batch yeast culture was conducted in connection with an experiment for harvesting a high yield of yeast cells with high invertase activity.     

Interaction between bacteria and the domoic-acid-producing diatom Pseudo-nitzschia multiseries (Hasle) Hasle; can bacteria produce domoic acid autonomously?

The interaction between bacteria and phytoplankton is increasingly becoming recognised as an important factor in the physiology of toxin production and the dynamics of harmful algal blooms (HABs). Bacteria can play a direct or indirect role in the production of biotoxins once solely attributed to microalgae. Evidence implicating bacteria as an autonomous source paralytic shellfish poisoning biotoxins raises the question of autonomous bacterial toxigenesis of the neurotoxin domoic acid (DA), the cause of amnesic shellfish poisoning. Here, we examine whether the previously observed bacterial enhancement of DA production by Pseudo-nitzschia multiseries (Hasle) Hasle may be attributable to independent biotoxin production by the extra-cellular bacteria associated with this diatom. The growth and toxicity of six cultures of xenic P. multiseries clone CLN-1 were followed for 24 days. Up to day 14 (mid-stationary phase), DA production was not statistically different among culture flasks. On day 14, P. multiseries cells were removed by gentle filtration from a set of triplicate flasks, leaving the bacteria in the filtrate. Following the removal of the algal cells, DA in the filtrate ceased to increase. Instead, DA levels continuously declined. A follow-up experiment determined that this was likely caused by photodegradation rather than by bacterial degradation. We conclude that after removing P. multiseries cells, the extra-cellular bacteria remaining in the filtrate were incapable of autonomous DA toxigenesis, even in the presence of P. multiseries exudates. However, scanning electron microscopy revealed that P. multiseries cells harboured epiphytic bacteria, the importance of which can still not be ruled out in DA production.     

EFFECT OF THE SINKING RATE OF TWO DIATOMS (THALASSIOSIRA SPP.) ON UPTAKE FROM LOW CONCENTRATIONS OF PHOSPHATE1

The effect of the sinking rate, or rate of medium flow (φ) on the rate of phosphate incorporation (V) by the planktonic diatoms Thalassiosira fluviatilis Hust. and T. pseudonana Hasle & Heimdal in batch and chemostat cultures was determined by passing medium at defined flow rates (0.5–25.0 mm·min^?1) over algae on membrane filters. At concentrations from 1 to 100 μg phosphorus·l^?1 V, increases with increasing velocity of flow, approaching a maximum value (V_m) as described by the empirical relationship: where K_φ is the sinking rate value when V = 1/2 V_m+ V_o and V_o is the uptake at 0 rate of flow. By comparing uptake at controlled flow with uptake in a vigorously stirred medium, the phosphate concentration in the cell boundary layer can be determined. The sinking rate that reduces the phosphate concentration in the boundary layer to half of nominal concentration in the medium is much lower for the larger T. fluviatilis than for T. pseudonana. For both diatoms, it is inversely related to the nominal concentration.     

A Simple and Inexpensive Design of Chemostat Enabling Steady-state Growth of Acer pseudoplatanus L. Cells under Phosphate-limiting Conditions

Operational and constructional details are given of a relativelysimple and inexpensive chemostat designed for the continuousculture of plant cells in suspension. This apparatus permitscontrol of the growth rate of sycamore, Acer pseudoplatanusL. cells in steady-state conditions. By alteration of the rateof input of medium different steady-state growth rates wereobtained over a wide range (mean doubling times from 182 h to36 h). In order to establish a growth-limiting nutrient thetime course of nutrient uptake in batch culture was measured.In batch culture the maximum growth obtained was proportionalto the initial concentration of phosphate when this was belowa concentration of 17 µg P per ml (as phosphate). It isalso shown in chemostat culture that the steady-state cell densityis proportional to the phosphate concentration in the mediumwhen this is below 17 µg P per ml (as phosphate). Phosphatewas therefore established to be the growth rate-limiting nutrientin chemostat culture at a concentration of 8•5 µgP per ml (as phosphate).     

Effects of cultural conditions on the production of phenylalanine from a plasmid-harboring E. coli strain

Summary Phenylalanine production from E. coli KA 197/pJN6 (plasmid harboring genes for aro F, phe A^FBR, Amp^R and Tc^R) was studied under varying nutritional conditions in batch and continuous cultures. In batch culture experiments where growth was deliberately interrupted by limiting concentrations of sulphate and phosphate the phenylalanine production continued from the non-growing cells. However, the depletion of phosphate resulted in an immediate cessation of phenylalanine production but thereafter a low specific rate of phenylalanine formation resumed, while the decrease in specific rate of product formation was less after sulphate depletion. In the chemostat experiments, however, phosphate limitation was the only case where the specific rate of phenylalanine formation remained constant, while at the corresponding time in sulphate and glucose limited chemostats it was declining respectively had ceased.     

Heterotrophic growth of Thiobacillus acidophilus in batch and chemostat cultures

Heterotrophic growth of the facultatively chemolithoautotrophic acidophile Thiobacillus acidophilus was studied in batch cultures and in carbon-limited chemostat cultures. The spectrum of carbon sources supporting heterotrophic growth in batch cultures was limited to a number of sugars and some other simple organic compounds. In addition to ammonium salts and urea, a number of amino acids could be used as nitrogen sources. Pyruvate served as a sole source of carbon and energy in chemostat cultures, but not in batch cultures. Apparently the low residual concentrations in the steady-state chemostat cultures prevented substrate inhibition that already was observed at 150 M pyruvate. Molar growth yields of T. acidophilus in heterotrophic chemostat cultures were low. The Y _max and maintenance coefficient of T. acidophilus grown under glucose limitation were 69 g biomass · mol^–1 and 0.10 mmol · g^–1 · h^–1, respectively. Neither the Y _max nor the maintenance coefficient of glucose-limited chemostat cultures changed when the culture pH was increased from 3.0 to 4.3. This indicates that in T. acidophilus the maintenance of a large pH gradient is not a major energy-requiring process. Significant activities of ribulose-1,5-bisphosphate carboxylase were retained during heterotrophic growth on a variety of carbon sources, even under conditions of substrate excess. Also thiosulphate- and tetrathionate-oxidising activities were expressed under heterotrophic growth conditions.     

CONFIRMATION OF DOMOIC ACID PRODUCTION BY PSEUDO‐NITZSCHIA AUSTRALIS (BACILLARIOPHYCEAE) ISOLATED FROM IRISH WATERS1

A nonaxenic isolate of the potentially toxic diatom Pseudo‐nitzschia australis (Frenguelli) from Irish waters was tested in two separate batch culture experiments. When grown under a low irradiance (～12 μmol photons·m ^{? 2}·s ^{? 1} 1 Received 20 March 2001. Accepted 21 August 2002.
; 16:8‐h light:dark cycle) for up to 40 days, the culture produced only trace amounts of the neurotoxin domoic acid (DA) during late stationary phase. Growth at a higher irradiance (～115 μmol photons·m ^{? 2}·s ^{? 1} 1 Received 20 March 2001. Accepted 21 August 2002.
; 12:12‐h light:dark cycle) resulted in DA production starting during late exponential phase and reaching a maximum concentration of 26 pg DA·cell ^{? 1} 1 Received 20 March 2001. Accepted 21 August 2002.
during late stationary phase. Liquid chromatography coupled to mass spectrometry was used to confirm the identity of DA in the culture. Irradiance and photoperiod could be important factors that contribute directly or indirectly to the control of DA production in P. australis. This is the first record of a DA‐producing diatom in Irish waters, and results indicate P. australis may have been the source of DA that has recently contaminated shellfisheries in this area.     

The activity of beta-galactosidase and lactose metabolism in Kluyveromyces lactis cultured in cheese whey as a function of growth rate

Aims: Kluyveromyces lactis was cultured in cheese whey permeate on both batch and continuous mode to investigate the effect of time course and growth rate on β‐galactosidase activity, lactose consumption, ethanol production and protein profiles of the cells. Methods and Results: Cheese whey was the substrate to grow K. lactis as a batch or continuous culture. In order to precise the specific growth rate for maximum β‐galactosidase activity a continuous culture was performed at five dilution (growth) rates ranging from 0·06, 0·09, 0·12, 0·18 to 0·24 h^?1. The kinetics of lactose consumption and ethanol production were also evaluated. On both batch and continuous culture a respirofermentative metabolism was detected. The growth stage for maximum β‐gal activity was found to be at the transition between late exponential and entrance of stationary growth phase of batch cultures. Fractionating that transition stage in several growth rates at continuous culture a maximum β‐galactosidase activity at 0·24 h^?1 was observed. Following that stage β‐gal activity undergoes a decline which does not correlate to the density of its corresponding protein band on the gel prepared from the same samples. Conclusion: The maximum β‐galactosidase activity per unit of cell mass was found to be 341·18 mmol ONP min^?1 g^?1 at a dilution rate of 0·24 h^?1. Significance and Impact of the Study: The physiology of K. lactis growing in cheese whey permeate can proven useful to optimize the conversion of that substrate in biomass rich in β‐gal or in ethanol fuel. In addition to increasing the native enzyme the conditions established here can be set to increase yields of recombinant protein production based on the LAC4 promoter in K. lactis host.     

Chemostat production of pediocin SM‐1 by Pediococcus pentosaceus Mees 1934

Production of the bacteriocin pediocin SM‐1 by Pediococcus pentosaceus Mees 1934 was investigated in pH‐controlled batch and chemostat cultures using a complex medium containing glucose, sucrose or fructose. In chemostat cultures operated at 150 rpm, 30°C, 60% dissolved oxygen tension, pH 6.5, and D = 0.148 h^?1, the pediocin titer reached 185 AU/mL representing an increase of 32% compared with batch cultures in which glucose was used as the carbon source. Pediocin biosynthesis was markedly affected by the growth rate of the producer microorganism. For all carbon sources tested, pediocin production appeared to take place only at dilution rates lower than μ_max. However, only glucose supported production at the very low dilution rate of 0.05 h^?1 indicating a direct regulation of pediocin biosynthesis by the carbon source. Glucose supported higher biomass productivity and higher pediocin titers and yields compared with the other sugars used. © 2015 American Institute of Chemical Engineers Biotechnol. Prog., 31:1481–1486, 2015     

Growth characteristics and oxidative capacity of<Emphasis Type="Italic"> Acetobacter aceti</Emphasis> IFO 3281: implications for <Emphasis Type="SmallCaps">l</Emphasis>-ribulose production

We studied the growth characteristics and oxidative capacities of Acetobacter aceti IFO 3281 in batch and chemostat cultures. In batch culture, glycerol was the best growth substrate and growth on ethanol occurred only after 6 days delay, although ethanol was rapidly oxidized to acetic acid. In continuous culture, both glycerol and ethanol were good growth substrates with similar characteristics. Resting cells in a bioreactor oxidized ribitol to l-ribulose with a maximal specific rate of 1.2 g g^–1 h^–1). The oxidation of ribitol was inhibited by ethanol but not by glycerol. Biomass yield (Y_SX; C-mmol/C-mmol) on ethanol and glycerol was low (0.21 and 0.17, respectively). In the presence of ribitol the yield was somewhat higher (0.25) with ethanol but lower (0.13) with glycerol, with respectively lower and higher CO₂ production. In chemostat cultures the oxidation rate of ribitol was unaffected by ethanol or glycerol. Cell-free extract oxidized ethanol very slowly but not ribitol; the oxidative activity was located in the cell membrane fraction. Enzymatic activities of some key metabolic enzymes were determined from steady-state chemostat with ethanol, glycerol, or ethanol/glycerol mixture as a growth limiting substrate. Based on the measured enzyme activities, metabolic pathways are proposed for ethanol and glycerol metabolism.     

Regulation of proteinase synthesis in Lactococcus lactis

The synthesis of extracellular serine proteinase of Lactococcus lactis was studied during the growth in a batch and a continuous culture on chemically defined media. In a batch culture the proteinase synthesis started during the exponential phase of growth and the highest proteinase concentrations were found at the end of the exponential and beginning of the stationary phase of growth. During the growth in a lactose-limited chemostat with amino acids as the sole source of nitrogen, the specific rate of proteinase synthesis was maximal at a μof 0.23 h^?1. At higher growth rates the proteinase productin declined. The proteinase synthesis was dependent on the amino acid sources in the medium. In batch cultures of L. lactis grown on a chemically defined medium with amino acids, the proteinase production was increased four-fold compared to media containing casein or a tryptic digest of casein as the sole source of nitrogen. The inhibition of the rate of proteinase synthesis by casein and peptides was also observed during the growth in a chemostat. The addition of the dipeptide leucylproline (final concentration of 100 μM) to a lactose-limited continuous culture during the steady state (D = 0.23 h^?1) resulted in a transient inhibition of the rate of proteinase synthesis. This suggested that exogenously supplied peptides control the regulation of proteinase synthesis of L. lactis.     

Effect of urea on the production of 2,3-butanediol by K. oxytoca

This paper deals with the production of 2,3- butanediol by K. oxytoca in batch cultures. The effect of urea on various kinetic parameters was studied by replacing the ammonium salts in the medium with the corresponding nitrogen equivalent in the form of urea. The specific growth rate and the product yield in an unacclimatised batch culture were found to be 0.29 h^?1 and 0.26 g·g^?1 respectively. The acclimatised batch cultures on the other hand behaved similar to that grown using the original medium with a specific growth rate of 0.66 h^?1 and the product yield of 0.345 g·g^?1. However the cultures were unable to grow when urea was used both as the carbon and nitrogen source.     

Diversity and distribution of epibiotic bacteria on Pseudo-nitzschia multiseries (Bacillariophyceae) in culture, and comparison with those on diatoms in native seawater

Previous studies on the interaction between bacteria and harmful algal bloom species have mostly considered the bacteria in the bulk solution. Here, we document the abundance and mode of attachment of bacteria growing on the cell surface of the domoic acid-producing diatom Pseudo-nitzschia multiseries (Hasle) Hasle in culture, compared with diatoms in field samples. The epiphytic bacteria were examined by scanning electron microscopy to visualize their morphology and mode of attachment. Two P. multiseries cultures were studied: clone CLN-1 and sub-clone CLN-1-NRC; the latter had been maintained in another laboratory for 2 years. Each of these P. multiseries cultures exhibited a clearly different assemblage of epibiotic bacteria, even though both originated from the same parent culture. The bacterial diversity was greater in clone CLN-1 (nine distinct morphotypes seen) than in sub-clone CLN-1-NRC (six morphotypes). The former clone also produced more domoic acid than the latter. There was a succession of bacterial morphotypes as well as an increase in the number of epiphytic bacteria per diatom cell during the progression from exponential to stationary phase. The most diverse and common morphotypes were rod-shaped cells (e.g. a Caulobacter-like bacterium attached by a discoid holdfast). Epibionts showed a preference for attachment at specific regions of the host diatom frustule, e.g. the raphe or cingulum, locations where organic matter may be extruding from the diatom cell. Most diatom cells carried only one to five bacteria, and up to ca. 60% of the intact diatom cells (although intact cells themselves were infrequent) were still free of epibiotic bacteria at the end of the 31-day batch culture experiment. Sequencing of the SSU rRNA gene showed that five of the eight bacterial strains isolated from the P. multiseries cultures were members of the Alphaproteobacteria, three of the Gammaproteobacteria and one of the Bacteroidetes. A morphologically diverse assemblage of epibiotic bacteria was also found on both centric and pennate planktonic diatoms in natural coastal waters. Of the eight morphotypes recorded, all but two were also found in the cultures. Relatively fewer wild diatom cells carried bacteria compared to cells in culture. We hypothesize that the diversity and abundance of epiphytic bacteria may explain some of the variability seen in the production of DA by different P. multiseries clones, and should be considered as another important and controllable variable that influences diatom cell physiology.     

Formaldehyde Production by Cells of a Mutant of Candida boidinii S2 Grown in Methanol-limited Chemostat Culture

Formaldehyde production was investigated with cells of a mutant, AOU-1, of a methanol yeast, Candida boidinii S2 grown in methanol-limited chemostat culture. The highest productivity was shown with cells from the culture at a dilution rate of 0.075 hr^-1, when cells had the highest activity of alcohol oxidase and almost minimum activity of formaldehyde dehydrogenase. Under optimal reaction conditions, 950 mm formaldehyde was produced in 10-hr reaction with the cells. By the chemostat culture, not only formaldehyde productivity but also cell productivity was improved in comparison with batch culture. A maximum cell productivity of 0.2 g · liter^-1 · hr^-1 and a cell yield of 47% were obtained.