Multiple shoot induction and leaf and flower bud abscission of Annonacultures as affected by types of ventilation

Nodal explants of Annona squamosa L. and Annona muricata L. were cultured in vitro under various types of ventilation: airtight vessel (sealed condition; number of air exchange 0.1 h^–1), natural ventilation (via a polypropylene membrane; number of air exchange 1.5 h^–1), and forced ventilation (5.0 cm³ min^–1 in a 60 cm³ vessel; number of air exchange 5.0 h^–1). In both species, numbers of leaves, leaf areas and numbers of nodes per shoot increased with improving standards of ventilation, while leaf abscissions were substantially reduced; all the leaves had abscised in the airtight vessels after 12–15 days, but none had done so with forced ventilation. Flower-bud abscission in A. muricatashowed a similar trend after 21 days. These effects were associated with reductions in the accumulation of ethylene within the culture vessels, produced by increasing the efficiency of ventilation; ethylene was not detected in those fitted with a forced ventilation system. CO₂ concentrations in culture headspaces and the net photosynthetic rates of the plantlets were also evaluated. CO₂ concentrations decreased well below the ambient in the natural and airtight vessels; however, under forced ventilation, CO₂ concentrations were significantly higher during the photoperiod, compared to those of the natural ventilation and airtight vessel treatments. In general, net photosynthetic rates per unit leaf area increased with increasing photosynthetic photon flux (PPF) and rates were highest in plantlets grown under forced ventilation, intermediate under natural ventilation and lowest in the airtight vessels.Eighteen different media were investigated for their effects on multiple shoot induction in both species. The best medium for multiple shoot induction and growth in A. squamosa was Murashige and Skoog medium (MS) + 6-benzylaminopurine (BA; 1.5 mg l^–1) + casein hydrolysate (1.0 g l^–1) and for A. muricata MS + BA (1.0 mg l^–1) + naphthaleneacetic acid (NAA; 0.1 mg l^–1).     

Physical environment in non-ventilated culture vessels affects <Emphasis Type="Italic">in vitro</Emphasis> growth and morphogenesis of several cultivars of <Emphasis Type="Italic">Dianthus Caryophyllus</Emphasis> L.

Summary Differences were shown in the environmental conditions inside four types of non-ventilated culture vessels (glass baby-food jars capped with metal steel or Magenta B-caps, jam glass jars capped with metal steel caps, and Magenta GA7 culture vessels) that were incubated in the same external growth room conditions. Vessel light transmittance varied from 83% to 53% and determined the availability of photosynthetic photon flux density (PPFD) for explants. The mean of medium desiccation in the culture period (30 d) was from 2.8 g in vessels with the lowest rate of gas exchange (0.02 h⁻¹) to 10.4 g in vessels with the highest (1.1 h⁻¹). In all cases, the temperature inside the culture vessel increased during the light period and decreased during the dark period, and relative humidity was close to 100%. Results of in vitro growth and morphogenesis of Dianthus caryophyllus L. evs. Scania, White Sim, Angeline, and Pink Calypso provided evidence that the environmental differences detected inside these four types of non-ventilated culture vessels was sufficient to affect micropropagation, mainly related with the specific sensitivity of each cultivar to the gas exchange and medium desiccation determined by the vessel type.     

CO2 gas exchange of the understory plantAsarum europaeum L. in November

The CO₂ gas exchange rates of the Central European perennial understory plantAsarum europaeum L. were measured in late autumn (October 30 to November 30) in its natural habitat day and night.During these measurements the temperature ranged from 0 to 15°C and the absolute air humidity from 3 to 10 mg H₂O·1^–1. Temperature and absolute air humidity over these ranges did not affect CO₂ net assimilation which was determined almost entirely by quantum flux density.CO₂ net assimilation was light saturated at about 100 M·m^–2·s^–1 quantum flux density. The uptake rate at this point was 4.3 mg·dm^–2·h^–1. The compensation point occurred at approximately 1 M·m^–2·s^–1.     

Continuous culture of Candida boidinii variant 60 growing on methanol

Summary A new variant, Candida boidinii variant 60, which is less sensitive to methanol and formaldehyde shocks was grown in continuous cultures with methanol as sole carbon source. The substrate concentration in the feeding medium was either 1% methanol or 3% methanol. Biomass production, methanol consumption, the formation of formaldehyde and gas exchange were measured at different dilution rates. With low methanol feeding (10 g/l) maximal productivity of 0.44 g biomass/l·h is obtained at a dilution rate of 0.14 h^–1. Maximal specific growth rate is 0.18 h^–1. A yield of 0.32 g biomass/g methanol was obtained and the respiration quotient was determined as 0.55. Independently of initial substrate concentration, biomass decreases if methanol and formaldehyde are accumulating in the culture broth.In the culture with high methanol feeding (30 g/l) cell concentratioon increases up to 9 g/l at D=0.04 h^–1. At higher dilution rates methanol and form-aldehyde appear in the medium. Formaldehyde is then preferably oxidized without energy advantages for the cells. It seems that this enables the cells to overcome toxic effects caused by methanol and formaldehyde.     

Aroma compounds produced by Kluyveromyces marxianus in solid state fermentation on a packed bed column bioreactor

Studies were carried out for the production of aroma compounds by Kluyveromyces marxianus grown on cassava bagasse in solid state fermentation using packed bed reactors, testing two different aeration rates. Respirometric analysis was used to follow the growth of the culture. Headspace analysis of the culture by gas chromatography showed the production of 11 compounds, out of which nine were identified. Ethyl acetate, ethanol and acetaldehyde were the major compounds produced. Lower aeration rate (0.06l h^–1 g^–1 of initial dry matter) increased total volatile (TV) production and the rate of production was also increased at this aeration rate. Using an aeration rate of 0.06l h^–1 g^–1 maximum TV concentrations were reached at 24 h and at 40 h with 0.12l h^–1 g^–1.     

Manipulation of the culture environment on <Emphasis Type="Italic">in vitro</Emphasis> air movement and its impact on plantlets photosynthesis

Two-dimensional air current speeds in the culture vessel were measured using a tracer-based visualization technique and the effect of the air movement in the culture vessel on the photosynthesis of in vitro potato plantlets was assessed under a photoautotrophic culture condition. The air current speeds inside the vessel were varied by controlling free convection induced by spatial variations of temperatures in the culture vessel. For all conditions examined, upward air currents were observed around the plantlets in the central part of the culture vessel and downward air currents were observed near inside walls in the culture vessel. The upward and downward air currents were restricted by the presence of the plantlet. The upward air current speeds were affected by plantlet size inside the vessel and it was 24, 8 and 4 mm s⁻¹ in culture vessels with no plantlets, a 10-mm-tall plantlet and a 60-mm-tall plantlet cultured inside the vessel, respectively. The upward air current speed was increased by 2 times by increasing wind velocity above the culture vessel from 0.1 to 1.0 m s⁻¹. Placing the black plate on the medium also increased the air current speeds by 1.5 times. The net photosynthetic rates of the plantlets increased from 2.0 to 2.5 μmol m⁻² s⁻¹ as the upward air current speed in the culture vessel increased from 2.4 to 8.0 mm s⁻¹. The air current speeds in the culture vessel were significantly slow. Enhancement of the air movement in the culture vessel is important to promote photosynthesis of the in vitro plantlets.     

Stomatal and cuticular traits on carnation tissue culture under different ventilation conditions

Establishment of microplants is related to the moisture vapourtransmission of the culture vessel lid. In this respect, stomatal andcuticular physiology were characterized in detached leaves from Dianthuscaryophyllus grown in the glasshouse or in vitro at different rates ofventilation. In vitro plants grown in non-ventilated culture vessels hadless waxes and therefore higher RWL compared to in vitro plants grown at Vr0.86 changes.h^–1. The improvement of stomatal function inleaves obtained in ventilated vessels can be due to a performance of ionicrelations between guard and subsidiary cells, mainly by an increasingK⁺ concentration in the guard cells as ventilation decreases.Moreover, data showthat there is an increase in free ABA in the leavesfromventilated culture vessels to compensate for the conjugated ABA lostduring desiccation. If the proliferation stage proceeds in ventilatedculture vessels, the physiological characteristics of the plants producedare better than those obtained in non-ventilated culture vessels, confirmedby higher survival after soil transplantion.     

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).     

Photosynthetic characteristics of Cymbidium plantlet in vitro

The photosynthetic characteristics of the Cymbidium plantlet in vitro cultured on Hyponex-agar medium with 2% sucrose were determined based on the measurements of CO₂ concentration inside and outside of the culture vessels. The CO₂ measurements were made with a gas chromatograph at a PPF (photosynthetic photon flux) of 35, 102 and 226 mol m^-2 s^-1, a chamber air temperature of 15, 25 and 35°C and a CO₂ concentration outside the vessel of approximately 350, 1100 and 3000 ppm. The net photosynthetic rates were determined on individual plantlets and were expressed on a dry weight basis. The steady-state CO₂ concentration during the photoperiod was lower inside the vessel than outside the vessel at any PPF greater than 35 mol m^-2s^-1 and at any chamber air temperature. The photosynthetic response curves relating the net photosynthetic rate, PPF, and CO₂ concentration in the vessel and chamber air temperature were similar to those for Cymbidium plants grown outside and other C₃ plants grown outside under shade. The results indicate that CO₂ enrichment for the plantlets in vitro at a relatively high PPF would promote photosynthesis and hence the growth of chlorophyllous shoots/plantlets in vitro and that the plantlets in vitro would make photoautotrophic growth under environmental conditions favorable for photosynthesis.Abbreviations C_in CO₂ concentration in the culture vessel - C_out CO₂ concentration outside the vessel (in the culture room) - PPF photosynthetic photon flux     

Biofilm build-up of Pseudomonas putida in a chemostat at different dilution rates

Summary A test system was set up where the build-up of a biofilm on a defined surface could be studied in a carbon source limited chemostat.The attachment of P. putida ATCC 11172 to glass when growing on L-asparagine was studied at different dilution rates (specific growth rates) from 0.1 to 1.5 h^–1 The number of attached colony forming units (cfu) increased with dilution rate from 1×10⁶ cfu/cm² at 0.1 h^–1 to 4×10⁷ cfu/cm² at 1.0 h^–1 and then the attachment decreased to about 6×10⁶ cfu/cm² at higher dilution rates (1.1–1.5 h^–1). The number of attached cfu was measured after 24 h exposure. The value of the maximum specific growth rate in batch culture was 0.6 h^–1.The total amount of attached cell-mass followed roughly the same pattern as the viable count.The viable count of the cells suspended in the growth medium showed its lowest value at the same dilution rate as resulted in maximum adhesion.It was shown that the effect of growth rate on the biofilm build-up of P. putida is significant, and ought to be borne in mind when continuous culture systems are set up and results evaluated.     

Degradation of sodium anthraquinone sulphonate by free and immobilized bacterial cultures

Aerobic biodegradation of a xenobiotic recalcitrant compound sodium anthraquinone-2-sulphonate (SAS), was investigated using as an inoculum a mixed microbial culture, which was activated sludge from industrial and domestic waste-water treatment plants. The difference in SAS degradation was examined using two main systems: (1) suspended cells and (2) immobilized cells, both in batch and in continuous culture. In the suspended cell system, under continuous culture conditions using SAS as a unique source of carbon and energy, it was possible to degrade about 95% of this substrate after 6 days. Maximal SAS removal rates in the suspended-cell system were 593 mg SAS l^–1 h^–1 and 88.7 mg SAS l^–1 h^–1 for dilution rates (D) of 0.05 h^–1 and 0.075 h^–1, respectively. In the immobilized-cell system, almost all SAS was degraded in 6 days and the maximal removal rate reached 88.7 mg SAS l^–1 h^–1 at D=0.05 h^–1. Application of a continuous-flow enrichment procedure resulted in selection of several kinds of micro-organisms and led to a progressive elimination of some species of Aeromonas. A stable microbial community of 11 strains has been established and characterized at D=0.075 h^–1. Most of them were Gram-negative and belonged to the genus Pseudomonas.     

Effect of the dilution rate on the biomass yield ofBacillus thuringiensis and determination of its rate coefficients under steady-state conditions

Depending on the biomass yield on glucose and the cell morphology ofBacillus thuringiensis, three different metabolic states were observed in continuous culture. At dilution rates between 0.18 h^–1 and 0.31 h^–1 vegetative cells, sporulating bacteria and spores coexisted, while glucose and amino acids were consumed. Only vegetative cells were observed at dilution rates between 0.42 h^–1 and 0.47 h^–1 and glucose was used as the main carbon and energy source. AtD = 0.50 h^–1 the biomass yield on glucose decreases sharply. To define better the specific growth rate range in which the microorganism uses mainly glucose, a dilution rate of 0.25–0.45 h^–1 was studied. The experimental data could be adjusted to a Monod model and the following rate coefficients and growth yields were determined: maximum specific growth rate 0.54 h^–1, saturation constant 0.56 mg glucose ml^–1, biomass growth yields 0.43 g cells (g glucose)^–1, and 0.76 g cells (g oxygen)^–1, and maintenance coefficients 0.065 g glucose (g cells)^–1 h^–1 and 0.039 g oxygen (g cells)^–1 h^–1.     

Determination of cell lysis and death kinetics in continuous hybridoma cultures from the measurement of lactate dehydrogenase release

The death of the hybridoma VO 208 in a continuous culture at pH 7 and 6.8 was investigated by measuring both the appearance of visible dead cells which do not exclude the trypan blue dye and the release of lactate dehydrogenase (LDH) in the culture medium. The intracellular LDH was found to be completely released either when live cells lysed or when they were transformed into visible dead cells. No significant lysis of blue dead cells could be observed at the two different pH. Using a LDH balance over the culture system, cell lysis was found negligible at pH 7, but accounted for 20% of the total cell death at pH 6.8. A methodology is proposed to evaluate the rate constants of hybridoma lysis and total death. For the investigated cell line in continuous culture, the calculated total cell death rate constant was found to increase from 0.002 h^–1 to 0.01 h^–1 when decreasing the pH from 7 to 6.8.Abbreviations D dilution rate (h^–1) - k_b specific trypan-blue dead cells appearance rate (h^–1) - k_L specific lysis rate of viable cells (h^–1) - k_d specific death rate (h-1) - LDH₀ lactate dehydrogenase activity in the feed culture medium (IU.l^–1) - LDH lactate dehydrogenase activity in the outlet culture medium (IU.l^–1) - LDH_i intracellular lactate dehydrogenase activity of viable cells (IU.10^–9 cells) - r_LDH total rate of LDH release (IU.h^–1.L^–1) - r_b transformation rate of viable cells into blue dead cells (10⁹ cells.h^–1.L^–1) - x_v viable cell concentration (10⁹ cells.l^–1) - x_b trypan-blue dead cell concentration (10⁹ cells.l^–1)     

Seasonal changes in the contribution of root respiration to total soil respiration in a cool-temperate deciduous forest

A trenching method was used to determine the contribution of root respiration to soil respiration. Soil respiration rates in a trenched plot (R _trench) and in a control plot (R _control) were measured from May 2000 to September 2001 by using an open-flow gas exchange system with an infrared gas analyser. The decomposition rate of dead roots (R _D) was estimated by using a root-bag method to correct the soil respiration measured from the trenched plots for the additional decaying root biomass. The soil respiration rates in the control plot increased from May (240–320 mg CO₂ m^–2 h^–1) to August (840–1150 mg CO₂ m^–2 h^–1) and then decreased during autumn (200–650 mg CO₂ m^–2 h^–1). The soil respiration rates in the trenched plot showed a similar pattern of seasonal change, but the rates were lower than in the control plot except during the 2 months following the trenching. Root respiration rate (R _r) and heterotrophic respiration rate (R _h) were estimated from R _control, R _trench, and R _D. We estimated that the contribution of R _r to total soil respiration in the growing season ranged from 27 to 71%. There was a significant relationship between R _h and soil temperature, whereas R _r had no significant correlation with soil temperature. The results suggest that the factors controlling the seasonal change of respiration differ between the two components of soil respiration, R _r and R _h.     

High efficiency styrene biodegradation in a biphasic organic/water continuous reactor

Styrene was degraded as sole source of carbon and energy by a selected bacterial community in a two-phase aqueous-organic medium (80%:20%, vol/vol). Silicone oil was used to solubilize styrene, which is sparingly soluble in water and to prevent its toxicity toward microorganisms. Preliminary studies with the mixed population in batch cultures indicate that the specific activity and the maximum growth rate at optimal 3H 6.0 were 46 mg·g^–1·h^–1 and 0.15 h^–1, respectively. In pH-regulated chemostat cultures, styrene was degraded at dilution rates ranging from 0.05 to 0.20 h^–1. Kinetic parameters and the proportion of each strain in the mixed culture were followed. At 0.20 h^–1, only one strain as compared to four initially present, remained in the medium. This strain Pseudomonas aeruginosa, degrades styrene with a specific activity of 293 mg·g^–1·h^–1. Such results could lead to industrial treatment of waste gas or water polluted with styrene. Correspondence to: J,-M. Lebeault     

The influence of H2, CO2 and dilution rate on the continuous fermentation of acetone-butanol

Summary The effect of product gases, H₂ and CO₂, on solvent production was studied using a continuous culture of alginate-immobilized Clostridium acetobutylicum. Initially, in order to find the optimum dilution rate for aceton--butanol production in this system, fermentations were carried out at various dilution rates. With 10% H₂ and 10% CO₂ in the sparging gas, a dilution rate of 0.07 h^–1 was found to maximize volumetric productivity (0.58 g·l^–1·h^–1), while the maximum specific productivity of 0.27 g^–·h^–1 occured at 0.12 h^–1. Continuous cultures with vigorous sparging of N₂ produced only acids. It was concluded that in the case of continuous fermentation H₂ is essential for good solvent production, although good solvent production is possible in an H₂-absent environment in the case of batch fermentations. When the fermentation was carried out at atmospheric pressure under H₂-enriched conditions, the presence of CO₂ in the sparging gas did not slow down glucose metabolism; rather it changed the direction of the phosphoroclastic reaction and as a result increased the butanol/acetone ratio.     

Production of xanthan by in-flow cultures of Xanthomonas campestris

The kinetics of xanthan formation in Xanthomonas campestris continuous and fed-batch fermentations was studied along with metabolic changes due to growth rate variation. A maximum growth rate within the range 0.11–0.12 h^–1 was obtained from the continuous culture data in defined medium, producing xanthan at rates up to 0.36 g l^–1 h^–1 corresponding to a maximum 67% glucose conversion at a dilution rate (D) of 0.05 h^–1. Comparatively, fed-batch cultivation was more efficient, producing maximum xanthan at 0.75 g l^–1 h^–1 and 63% glucose conversion at 0.1 h^–1. When reaching D=0.062 h^–1 in continuous cultures, a change was observed and the values of the specific rate of substrate consumption shifted, initiating an uncoupled growth region expressing a lack of balance of the catabolic and anabolic reactions. The deviation was not accompanied by a change in specific xanthan production indicating that xanthan metabolism was not affected by D. For fed-batch-grown X. campestris cells within the range D=0.03–0.1 h^–1, both metabolic parameters changed linearly with the growth rate showing a wide region coupled to growth. Outside that range, glucose accumulated and the specific xanthan production dropped, suggesting substrate inhibition. Correspondence to: J. C. Roseiro     

Actinorhodin production by Streptomyces coelicolor A3(2): kinetic parameters related to growth,substrate uptake and production

The dynamics of an Streptomyces coelicolor A3(2) culture in a 20-l computer-controlled batch bioreactor was investigated both experimentally and theoretically. In defined medium, depending on the initial conditions, the calculated value of some of the kinetic parameters were: maximum specific growth rate, 0.03 h^–1; death rate constant, 1.4–6.3 × 10^–3 h^–1; observed biomass yield, 0.21 g cells g^–1 glucose and the maintenance coefficient for the cells, 0.0448 g glucose g^–1 cells h^–1. According to both experimental observations and the Luedeking-Piret model, actinorhodin production was found to be growth-associated. This paper provides the first published quantitative information on the main kinetic parameters describing the activity of S. coelicolor in batch culture. Correspondence to: F. Mavituna     

Desulfurization of model and diesel oils by resting cells of Gordona sp.

The desulfurization activity of the resting cells of Gordona sp. CYKS1 was strongly depended on harvest time and the highest value when the cells had been harvested in the early growth phase (0.12 mg sulfur g^–1 cell^–1 h^–1). For the model oil, hexadecane containing dibenzothiophene, the specific desulfurization rate decreased as the reaction proceeded. Both the specific and the volumetric desulfurization rates were not significantly affected by the aqueous-to-oil phase ratio. The diesel oils, light gas oil and a middle distillate unit feed were desulfurized at higher rates (ca. 0.34 mg sulfur g^–1 cell^–1 h^–1) than the model oil (0.12 mg sulfur g^–1 cell^–1 h^–1).     

High photosynthetic photon flux and high CO2 concentration under increased number of air exchanges promote growth and photosynthesis of four kinds of orchid plantlets in vitro

Summary In vitro plantlets of Phalaenopsis ‘Happy Valentine’, Neofinetia falcate Hu, Cymbidium kanran Makino, and Cymbidium goeringii Reichb. f. were grown under photoautotrophic [high photosynthetic photon flux (PPF), high CO₂ concentration, and increased number of air exchanges] and heterotrophic (low PPF, low CO₂ concentration, no air exchanges) culture conditions. After 40 d of culture, a significant difference in plantlet growth was observed between the two cultures. Total fresh and dry mass were on average 1.5 times greater in photoautotrophic culture than in heterotrophic culture. Higher net photosynthetic rates were also observed for Phalaenopsis in photoautotrophic culture. In photoautotrophic culture, little difference was observed in air temperature between the inside and outside of the culture vessel, whereas in heterotrophic culture, air temperature inside the culture vessel was 1–2°C higher than that outside the culture vessel. Relative humidity inside the culture vessel was remarkably different between the two cultures: 83–85% in photoautotrophic culture and 97–99% in heterotrophic culture. These results indicated that growth and net photosynthetic rate of in vitro orchid plantlets were susceptible to the culture environments such as PPF, CO₂ concentration, relative humidity (RH), and the number of air exchanges, which would allow a more efficient micropropagation system for these orchid plants.