The scale-up of plant cell culture: Engineering considerations

The enormous versatility of plants has continued to provide the impetus for the development of plant tissue culture as a commercial production strategy for secondary metabolites. Unfortunately problems with slow growth rates and low products yields, which are generally non-growth associated and intracellular, have made plant cell culture-based processes, with a few exceptions, economically unrealistic. Recent developments in reactor design and control, elicitor technology, molecular biology, and consumer demand for natural products, are fuelling a renaissance in plant cell culture as a production strategy. In this review we address the engineering consequences of the unique characteristics of plant cells on the scale-up of plant cell culture.Abbreviations a gas-liquid interfacial area per volume - C dissolved oxygen concentration - C^* liquid phase oxygen concentration in equilibrium with the partial pressure of oxygen in the bulk gas phase - K_L overall mass transfer coefficient - k_L liquid film mass transfer coefficient - m_O2 cell maintenance coefficient for oxygen - OTR oxygen transfer rate - OUR oxygen uptake rate - pO₂ partial pressure of oxygen - STR stirred-tank reactor - v.v.m. volume of gas fed per unit operating volume of reactor per minute - X biomass concentration - Y_x/O2 biomass yield coefficient for oxygen - specific growth rate     

Growth and respiration of rice (Oryza sativa L.) Cells in suspension culture

Studies on the growth and respiration of batch suspension cultures of rice (Oryza sativa L.) in a reference medium containing Murashige-Skoog salts, 2% (w/v) sucrose and yeast extract are reported. It was found that the yeast extract contributed 70% of the phosphate in this medium, and that the cells grew equally well in continued subculture in a defined medium which contained 6 mM phosphate and 3% (w/v) sucrose and the remaining Murashige-Skoog salts. Cell clumps (up to 1.5 mm diameter) were prevalent in the initial cultures in the reference medium. In such cultures the critical O₂ pressure of cell respiration was high (125 M), and ethanol accumulated. When cell clumps were routinely removed during several weekly subcultures on the defined medium cultures were obtained in which no clumps were present, the critical O₂ pressures was decreased to 40 M and no ethanol accumulated.This work was supported by grant PCM-84-03542 from the U.S. National Science Foundation.     

Growth and physiology of potassium-limited chemostat cultures of Paracoccus denitrificans

In potassium-limited chemostat cultures of Paracoccus denitrificans the maximum specific growth rate (µ_max) was found to depend on the input potassium concentration: At 0.21mM µ_max was 0.10–0.11 h^-1; at 0.44 mM 0.15–0.16 h^-1 and at 0.66 mM 0.20–0.21 h^-1. The plots of the specific rates of oxygen-, succinate-and potassium consumption against gave straight lines. The intracellular potassium concentration was a linear function of and varied from 1% (0.13 M) at a value of 0.034 h^-1 to 2.2% (0.29 M) at =0.26 h^-1; the potassium concentration gradient and the potassium concentration in the culture fluid in the steady state were dependent on the input potassium concentration. The potassium concentration gradient varied from 8,900-1,200. At all values 20–25% of the total energy production was used for potassium transport. 350,100 and 30 ATP molecules were calculated to be required to maintain one potassium ion intracellular during 1 h at values of 0.034, 0.197 and 0.257 h^-1 respectively. It is concluded that the amount of circulation of potassium is dependent on the potassium concentration gradient or on the potassium concentration in the culture in the steady state. The dependency of µ_max on the input potassium concentration was explained by the assumption that at low input potassium concentrations the net uptake of potassium (influx-efflux) is not rapidly enough to maintain the high potassium gradient in the existing cells and to establish it in the newly formed cells. At high values and at high input potassium concentrations µ_max is limited by the specific rate of oxygen consumption, which was found to be 11–12 mmol O₂ g dry weight^-1 h^-1 at µ_max for potassium-, succinate-and sulphate-limited chemostat cultures.     

The growth of Pseudomonas putida on m-toluic acid and on toluene in batch and in chemostat cultures

Summary The present study describes the growth of Pseudomonas putida cells (ATCC 33015) in batch and continuous cultures on two toxic substrates; toluene and m-toluic acid as sole carbon and energy sources. In fed-batch cultures on m-toluic acid up to 3.55 g cell dry weight/1 were achieved with a maximal specific growth rate (_max) of 0.1 h^-1. The average cellular yield was 1.42 g cell dry weight/g m-toluic acid utilized. When liquid toluene was added to shake-flask cultures in the presence of 0.7 g/1 m-toluic acid, the average cellular yield obtained was 1.3 g cell dry weight/g toluene utilized and the _max was 0.13 h^-1. Growth on toluene vapour in the presence of 0.7 g/l m-toluic acid in batch cultures resulted in a cellular yield of 1.28 g cell dry weight/g toluene utilized, with growth kinetics almost identical to those with liquid toluene (_max liquid=0.13 h^-1, _max vapour=0.12 h^-1). The maximal biomass concentration was 3.8 g cell dry weight/l, obtained in both cases after 100 h of incubation. Pseudomonas putida was grown in a chemostat initially on 0.7 g/l m-toluic acid and vapour toluene and then in the steady state on toluene as the sole source of carbon and energy. Toluene was added continuously to the culture as vapour with the inflowing airstream. Chemostat cultures could be maintained at steady state for several months on toluene. The maximal biomass concentration obtained in the chemostat culture was 3.2 g cell dry weight/l. The maximum specific growth rate was 0.13 h^-1, with a cellular yield of 1.05 g cell dry weight/g toluene utilized. Approximately 70% of the toluene consumed was converted into biomass, and the remainder was converted to CO₂ and unidentified byproducts.     

The induction and repression of benzene and catechol oxidizing capacity of Pseudomonas putida ML2 studied in perturbed chemostat culture

The oxidation of catechol, an intermediate in benzene catabolism, was studied using transient variations in dissolved oxygen tension (DOT) when a succinate limited steady state culture of Pseudomonas putida ML2 was perturbed with a pulse of another substrate. A model was developed and tested for the effect of fluctuations in oxidizing enzyme activity on DOT. It was found that the rate of induction of catechol oxidizing enzymes was independent of dilution rate up to a relative growth rate /_max of 0.75. Only at higher dilution rates was catabolite repression observed.Abbreviations DOT dissolved oxygen tension - K _L a gas transfer coefficient - specific growth rate - _max maximum specific growth rate - K_s substrate saturation constant     

Dependency of growth yield,maintenance and K s-values on the dissolved oxygen concentration in continuous cultures of Azotobacter vinelandii

Azotobacter vinelandii was grown diazotrophically in sucrose-limited chemostat cultures at either 12, 48, 108, 144 or 192 M dissolved oxygen. Steady state protein levels and growth yield coefficients (Y) on sucrose increased with increasing dilution rate (D). Specific rate of sucrose consumption (q) increased in direct proportion to D. Maintenance coefficients (m) extrapolated from plots of q versus D, as well as from plots of 1/Y versus 1/D exhibited a nonlinear relationship to the dissolved oxygen concentration. Constant maximal theoretical growth yield coefficients (Y ^G) of 77.7 g cells per mol of sucrose consumed were extrapolated irrespective of differences in ambient oxygen concentration. For comparison, glucose-, as well as acetate-limited cultures were grown at 108 M oxygen. Fairly identical m- and Y ^G-values, when based on mol of substrate-carbon with glucose and sucrose grown cells, indicated that both substrates were used with the same efficiency. However, acetate-limited cultures showed significantly lower m- and, at comparable, D, higher Y-values than cultures limited by either sucrose or glucose. Substrate concentrations (K _s) required for half-maximal growth rates on sucrose were not constant, they increased when the ambient oxygen concentration was raised and, at a given oxygen concentration, when D was decreased. Since biomass levels varied in linear proportion to K _s these results are interpreted in terms of variable substrate uptake activity of the culture.Abbreviations D dilution rate - K _s substrate concentration required for half maximal growth rate - m maintenance coefficient - q specific rate of substrate consumption - Y growth yield coefficient - Y ^G maximum theoretical growth yield coefficient     

The effect of dissolved oxygen tension and the utility of oxygen uptake rate in insect cell culture

Dissolved oxygen tension and oxygen uptake rate are critical parameters in animal cell culture. However, only scarce information of such variables is available for insect cell culture. In this work, the effect of dissolved oxygen tension (DOT) and the utility of on-line oxygen uptake rate (OUR) measurements in monitoring Spodoptera frugiperda (Sf9) cultures were determined. Sf9 cells were grown at constant dissolved oxygen tensions in the range of 0 to 30%. Sf9 metabolism was affected only at DOT below 10%, as no significant differences on specific growth rate, cell concentration, amino acid consumption/production nor carbohydrates consumption rates were found at DOT between 10 and 30%. The specific growth rate and specific oxygen uptake rate followed typical Monod kinetics with respect to DOT. The calculated _max and max were 0.033 h^-1 and 3.82×10^-10 mole cell^-1h^-1, respectively, and the corresponding saturation constants were 1.91 and 1.57%, respectively. In all aerated cultures, lactate was consumed only after glucose and fructose had been exhausted. The yield of lactate increased with decreasing DOT. It is proposed, that an apparent DOT in non-instrumented cultures can be inferred from the lactate yield of bioreactors as a function of DOT. Such a concept, can be a useful and important tool for determining the average dissolved oxygen tension in non-instrumented cultures. It was shown that the dynamic behavior of OUR can be correlated with monosaccharide (fructose and glucose) depletion and viable cell concentration. Accordingly, OUR can have two important applications in insect cell culture: for on-line estimation of viable cells, and as a possible feed-back control variable in automatic strategies of nutrient addition.Abbreviations DOT Dissolved oxygen tension - OUR Oxygen uptake rate - specific oxygen uptake rate - specific growth rate - X_v viable cell concentration - C_L, C^*, and oxygen concentrations in liquid phase, in equilibrium with gas phase, and medium molar concentration, respectively - H Henry's constant - K_La volumetric oxygen transfer coefficient - P_T total pressure - oxygen partial pressure - oxygen molar fraction - i discrete element     

Effects of cadmium accumulation on growth and respiration of a cadmium-sensitive strain of Bacillus subtilis and a selected cadmium resistant mutant

The effects of cadmium on the growth and respiration of two strains of Bacillus subtilis are compared to the accumulation of Cd by viable and cyanide-killed cells, protoplasts and cell fractions of the strains. Growth and respiration of strain 1A1 were significantly inhibited at 10g Cd²⁺/ml while the growth and respiration of strain 1A1R, a selected mutant of 1A1, were only slightly affected. Similarly, 1A1R protoplasts were more resistant to Cd than were 1A1 protoplasts. The differential resistance of the strains correlates with the accumulation of Cd by the two strains, with 1A1 accumulating approximately 10 times the level of Cd after a 4 h exposure to 1 g Cd²⁺/ml. The distributions of Cd throughout the cells, however, were similar between strains. Based on the accumulation of Cd by cyanide-killed protoplasts, uptake of Cd by 1A1 appears to be an active process, while for 1A1R, Cd accumulation is independent of protoplast viability.Non-standard abbreviations SMM Subtilis Minimal Medium - AAS Atomic Absorption Spectrophotometry - TSA Trypticase Soy Agar - PCA Plate Count Agar - INT 2-p-iodophenyl-3-p-nitrophenyl-5-phenyl-2H tetrazolium chloride - dd H₂O double distilled demineralized water - OD Optical Density     

Isolation and culture of Lens culinaris Medik. cv. Eston epicotyl protoplasts to calli

Protoplasts of Lens culinaris Medik. cv. Eston were isolated from epicotyl tissues of seedlings grown on Murashige & Skoog basal medium. For isolating the protoplasts, epicotyl tissues were digested for 12–14 h at 25°C in an isolation mixture (pH 5.7) containing 1% Cellulase RS, 0.5% Driselase, 0.25% Pectolyase Y23, 0.2M calcium chloride, 10 mM mannitol and 10 mM MES. Protoplasts were purified by flotation over 20% sucrose and washed with 0.2 M calcium chloride solution supplemented with 10 mM mannitol. Purified protoplasts were cultured at a density of 10⁵ ml^-1 in agarose (Seaplaque, 0.6%) blocks which were suspended in an identical but liquid KM8P culture medium lacking amino acids, ammonium nitrate, and coconut water but containing 0.35 M glucose and a growth regulator complement of either 2.2 M 2,4-dichlorophenoxyacetic acid (2,4-D), 2.7 M naphthaleneacetic acid (NAA), 2.3 M N-(2-furanylmethyl)-1H-purine-6-amine (kinetin), 2.2 M benzylamino purine (BAP), 2.3 M 2-methyl-4-(1H-purine-6-ylamino)-2-buten-1-ol (zeatin), and 1.4 M gibberellic acid (GA₃), or 5.4 M NAA and 2.2 M each of 2,4-D and BAP. The osmotic potential of the liquid culture medium was gradually reduced over a period of 3 weeks by replacing the spent medium with a fresh medium containing 0.25, 0.1 and 0 M glucose at weekly intervals. About 6% of the dividing protoplasts developed into cell colonies after 3 weeks of culture at 25°C in diffuse light (10 E m^-2s^-1). In 35–42 days the microcolonies were about 1 mm in diameter and developed into calli on transfer to agar-solidified B5 medium supplemented with growth regulators used in the protoplast culture medium and 5 mM glutamine. Attempts to regenerate plants from protoplast-derived calli have so far been unsuccessful.Department of Applied Microbiology and Food Science, University of Saskatchewan     

Effect of hydromechanical forces on the production of filamentous haemagglutinin and pertussis toxin ofBordetella pertussis

Summary The production ofBordetella pertussis extracytoplasmic filamentous haemagglutinin (FHA) and pertussis toxin (PT) in a bioreactor under stirring conditions was studied in order to investigate the effect of hydromechanical forces on yields of both antigens. It was shown that FHA loses its haemagglutinin activity when the power transmitted by the agitator and the aerator per unit volume increases, whereas PT production is not affected. The loss of FHA activity can be explained by the action of shear forces on the filamentous structure of this antigen.Nomenclature C^* dissolved oxygen saturation concentration - C₁ dissolved oxygen concentration - D impeller diameter - power transmitted by the agitator and the aerator per unit of liquid volume - E_m maximum local energy dissipation rate per unit of liquid volume - K_La volumetric oxygen transfer coefficient - N impeller speed - Pg power input in aerated system - qO₂m maximum specific oxygen consumption rate - R_e Reynold number (D²N /) - VVM volume of air per volume of fermentation broth per minute - Xm maximum of biomass concentration - o Kolmogorov-microscale - fermentation broth viscosity - fermentation broth kinematic viscosity - fermentation broth density - expt experiment     

Plant regeneration from embryogenic cell suspensions and protoplasts in sugarcane (Saccharum spp.hybrid cv. CoL-54)

Embryogenic callus was developed from young leaves of sugarcane (Saccharum spp.hybrid, cv. CoL-54). A good embryogenic callus response was achieved using MS basal medium containing 2.0 mol (0.5 mg l^-1) picloram under dark conditions at 27±1°C. Initiation of fast growing homogeneous cell suspension cultures was achieved in MS and AA media, both supplemented with g mol (2 mg l^-1) 2,4-d and 500 mg l^-1 CH. Embryogenic callus was reinitiated from embryogenic cell suspension cultures using MS medium containing 30 g l^-1 sucrose, 500 mg l^-1 CH and 2.26 mol (0.5 mg l^-1) 2,4-d after 4–6 weeks of culture under 16-h photoperiod conditions. Plant regeneration was achieved after about 4 weeks in MS medium lacking growth regulators but containing CH (500 mg l^-1) and sucrose (60 g l^-1). Rooting was enhanced by transferring regenerated plantlets to half strength MS basal medium.Totipotent protoplasts with an average yield of 2.0×10⁷ to 1.0×10⁸ ml^-1 were obtained from embryogenic cell suspension cultures at log phase, i.e., 4–5 days after transfer to fresh media. The best growth response was achieved when protoplasts were cultured in a modifed KM8P medium at the density of 2.0×10⁵ m l^-1. Protoplasts were mainly embedded in 0.8% sea plaque agarose. Division efficiency of 22.2% was achieved after 20 days of culture and 0.26% of microcolonies continued growth and formed microcalluses after 30 days of culture under dark conditions. Microcalluses were proliferated in MS medium having 2,4-d (2 mg l^-1) under 16-h photoperiod. Transferring these embryogenic calluses in MS medium +9.29 mol kinetin (2 mg l^-1) +5.37 mol NAA (1.0 mg l^-1) + activated charcoal (200 mg l^-1) for 5 weeks favoured plant regeneration. Shoots and roots were further proliferated in half strength MS basal medium for 2–4 weeks. Regenerated plants were transferred to autoclaved sand for 2 weeks under 16-h photoperiod in growth room and transferred to soil in a greenhouse to raise to maturity.Abbreviations MS salts of Murashige & Skoog (1962) basal medium - AA salts of Muller & Grafe (1978) basal medium - N6 saits of Chuet al. (1975) basal medium - 2,4-d 2,4-dichlorophenoxyacetic acid - CH casein hydrolysate - KM8P protoplast culture medium of Kao & Michayluk (1975) - KPR protoplast culture medium of Kao (1977) - P9 protoplast culture medium (Chen & Shih, 1983) - BA Benzyladenine - Picloram 4-amino-3,5,6-trichloropicolinic acid - NAA Naphthalene acetic acid     

Oxygen protection of nitrogenase in Frankia sp. HFPArI3

O₂ protection of nitrogenase in a cultured Frankia isolate from Alnus rubra (HFPArI3) was studied in vivo. Evidence for a passive gas diffusion barrier in the vesicles was obtained by kinetic analysis of in vivo O₂ uptake and acetylene reduction rates in response to substrate concentration. O₂ of NH ₄ ⁺ -grown cells showed an apparent K _m O₂ of approximately 1M O₂. In N₂-fixing cultures a second K _m O₂ of about 215 M O₂ was observed. Thus, respiration remained unsaturated by O₂ at air-saturation levels. In vivo, the apparent K _m for acetylene was more than 10-fold greater than reported in vitro values. These data were inter oreted as evidence for a gas diffusion barrier in the vesicles but not vegetative filaments of Frankia sp. HFPArI3.     

Callus production,suspension culture and in vitro alkaloid yields of Ephedra

The effects of a range of plant growth regulators on callus production in various Ephedra species were examined. Species examined were E. andina, E. distachya, E. equisitina, E. fragilis var, camplyopoda, E. gerardiana, E. intermedia, E. major ssp procera, E. minima and E. saxatilis. All species produced callus on modified MS medium supplemented with 0.25 M kinetin and 5.0 M 2,4-dichlorophenoxyacetic acid or 1-naphthaleneacetic acid. Neither indole-3-acetic acid nor 3-indolebutyric acid induced significant callus formation but the latter maintained growth of established callus cultures in several species. Suspension cultures of several species were established in MS medium supplemented with 0.25 M kinetin and 5.0 M 2,4-dichlorophenoxyacetic acid or 1-naphthaleneacetic acid. Sustained fresh weight doubling times of 70±7h were recorded for cell suspension cultures of E. andina grown in a semi-continous air-lift bubble bioreactor and a minimum doubling time of 56 h was recorded for E. andina in batch culture. It also proved possible to immobilise E. andina batch cultures in sodium alginate beads.Neither parent plants or in vitro cultures of E. distachya, E. fragilis or E. saxatilis produced alkaloids. Trace quantities of 1-ephedrine and trace-0.14% dwt d-pseudoephedrine were produced by in vitro cultures of other species. The ability to produce alkaloid diminished to zero with successive subcultures.Abbreviations Eph 1-ephedrine - Peph d-pseudoephedrine - RGR relative growth rate - KIN kinetin - 2,4-d 2,4-dichlorophenoxyacetic acid - NAA 1-naphthaleneacetic acid - IBA 3-in-dolebutyric acid - IAA indole-3-acetic acid     

Temporal separation of nitrogen fixation and photosynthesis in the filamentous,non-heterocystous cyanobacterium Oscillatoria sp.

When growing in laternating light-dark cycles, nitrogenase activity (acetylene reduction) in the filamentous, non-heterocystous cyanobacterium Oscillatoria sp. strain 23 (Oldenburg) is predominantly present during the dark period. Dark respiration followed the same pattern as nitrogenase. Maximum activities of nitrogenase and respiration appeared at the same time and were 3.6 mol C₂H₄ and 1.4 mg O₂ mg Chl a ^-1·h^-1, respectively. Cultures, adapted to light-dark cycles, but transferred to continuous light, retained their reciprocal rhythm of oxygenic photosynthesis and nitrogen fixation. Moreover, even in the light, oxygen uptake was observed at the same rate as in the dark. Oxygen uptake and nitrogenase activity coincided. However, nitrogenase activity in the light was 6 times as high (22 mol C₂H₄ mg Chl a ^-1·h^-1) as compared to the dark activity. Although some overlap was observed in which both oxygen evolution and nitrogenase activity occurred simultaneously, it was concluded that in Oscillatoria nitrogen fixation and photosynthesis are separated temporary. If present, light covered the energy demand of nitrogenase and respiration very probably fulfilled a protective function.     

Plant regeneration from patchouli protoplasts encapsulated in alginate beads

Mesophyll protoplasts were isolated from leaves of in vitro grown patchouli (Pogostemon cablin Benth.). The protoplasts were encapsulated in alginate beads, approximately 2–3×10³ protoplasts per 25 l bead. Successful colony formation was induced when the protoplast beads were inoculated into a liquid medium supplemented with 10^-6 M NAA and 10^-5 M BA. The frequency of colony formation was improved greatly by the inclusion of several beads per ml medium. To induce high colony formation for a single bead, it was essential to culture protoplasts in the presence of nurse beads containing actively-growing cells of the same species. Rapid regeneration of plants from protoplast-derived calluses was accomplished by a two-step culture procedure with liquid and then solid media. Gas-chromatographic analyses showed that regenerated plants produced an essential oil comprising a full-set of patchouli sesquiterpenes.Abbreviations BA 6-benzylaminopurine - 2,4-D 2,4-dichlorophenoxyacetic acid - f. wt. fresh weight - GC gas chromatography - MES 2-(N-morpholino)ethanesulfonic acid - NAA 1-naphthaleneacetic acid     

Oxidative Stress and Antioxidant Cell Protection Systems in the Microaerophilic Bacterium Spirillum winogradskii

The influence of oxygen availability during cultivation on the biosynthetic processes and enzymatic activities in the microaerophilic bacterium Spirillum winogradskii D-427 was studied, and the roles played by different systems of the defense against oxidation stress were determined. The metabolic adjustments caused by transition from microaerobic (2% O₂) aerobic conditions (21% O₂ of the gas phase) were found to slow down constructive metabolism and increase synthesis of exopolysaccharides as a means of external protection of cells from excess oxygen. This resulted in a twofold decline of the growth yield coefficient. Even though the low activity of catalase is compensated for by a multifold increase in the activities of other cytoplasmic enzymes that defend against toxic forms of O₂—peroxidase and enzymes of the redox system of glutathione (glutathione peroxidase and glutathione reductase)—massive lysis of cells starts in the midexponential phase and leads to culture death in the stationary phase because of H₂O₂ accumulation in the periplasm (up to 10 g/mg protein). The absence in cells of cytochrome-c-peroxidase, a periplasmic enzyme eliminating H₂O₂, was shown. It follows that the major cause of oxidative stress in cells is that active antioxidant defenses are located in the cytoplasm, whereas H₂O₂ accumulates in the periplasm due to the lack of cytochrome-c-peroxidase. The addition to the medium of thiosulfate promotes elimination of H₂O₂, stops cell lysis under aerobic conditions, lends stability to cultures, and results in a threefold increase in the growth yield.     

Production of glutamine by micro-gel bead-immobilized Corynebacterium glutamicum 9703-T cells in a stirred tank reactor

The effectiveness of using micro-gel bead-immobilized cells for aerobic processes was investigated. Glutamine production by Corynebacterium glutamicum, 9703-T, cells was used as an example. The cells were immobilized in Sr-alginate micro-gel beads 500 m in diameter and used for fermentation processes in a stirred tank reactor with a modified impeller at 400 min^–1. Continuous production of glutamine was carried out for more than 220 h in this reactor and no gel breakage was observed. As a result of the high oxygen transfer capacity of this system, the glutamine yield from glucose was more than three times higher, while the organic acid accumulation was more than 24 times lower than those obtained with 3.0 mm-gel bead-immobilized cells in an airlift fermentor under similar experimental conditions. During the continuous fermentations there was evolution and proliferation of non-glutamine producing strains which led to a gradual decrease in the productivity of the systems. Although a modified production medium which suppresses cell growth during the production phase was effective in maintaining the productivity, the stability of the whole system was shortened due to high cell deactivation rate in such a medium.List of Symbols C kg/m³ glutamine concentration - C _A mol/m ³ local oxygen concentration inside the gel beads - C _AS mol/m ³ oxygen concentration at the surface of the gel beads - De m²/h effective diffusion coefficient of oxygen in the gel bead - DO mol/m³ dissolved oxygen concentration - F dm³/h medium flow rate - K h^–1 glutamine decomposition rate constant - Km mol/m³ Michaelis Menten constant - QO _2max mol/(kg · h) maximum specific respiration rate - R m radius of the gel beads - r m radial distance - t h time - V _C dm ³ volume of the gel beads - V _L dm ³ liquid volume in the reactor - Vm mol/(m³ · h) maximum respiration rate - X kg/m³ cell concentration - x r/R - y C _A /C_AS - h^–1 cell deactivation rate constant - Thiele modulus defined by R(Vm/De Km) ^1/2 - C _AS /Km - _C kg/(m³-gel · h) specific glutamine formation rate - _c dm³-gel/dm³ V _C /V _L      

Different effects of inorganic and triethyl lead on growth and ultrastructure of lily pollen tubes

Summary Pollen tubes ofLilium longiflorum growingin vitro were treated for 1 h with inorganic lead (Pb) and with triethyl lead (TriEL) and studied by light and electron microscopy. Pb was considerably more toxic in relation to inhibition of pollen tube growth (EC₅₀=6 M Pb) than was TriEL (EC₅₀=60 M TriEL). On the other hand, at almost the entire concentration range tested (25-500 M) TriEL caused aberrant tubes and tube swellings. Pb did not cause tube swellings, even at highly growth-impairing concentrations. Pb (60 M) predominantly affected the ultrastructure of the growing cell walls without impairing the distribution of the cell organelles in the tube tips. In contrast, 50 and 100 M TriEL did not visibly influence cell wall ultrastructure but it severely damaged dictyosomes; 100 M TriEL also disturbed the original order of cell organelles in the tube tips. Cortical microtubules were selectively and completely destructed by TriEL at concentrations (50 M) where no effect on polar organization of the tube tips occurred but they remained unimpaired by 60 M Pb, indicating selective and effective interaction of TriEL with these cell organelles.Abbreviations EC⁵⁰ effective lead concentration causing 50% inhibition of pollen tube growth - MTs microtubules - Pb inorganic lead - TriAL trialkyl lead - TriEL triethyl lead     

Anthraquinones production,hydrogen peroxide level and antioxidant vitamins in Morinda elliptica cell suspension cultures from intermediary and production medium strategies

The effects of medium strategies [maintenance (M), intermediary (G), and production (P) medium] on cell growth, anthraquinone (AQ) production, hydrogen peroxide (H₂O₂) level, lipid peroxidation, and antioxidant vitamins in Morinda elliptica cell suspension cultures were investigated. These were compared with third-stage leaf and 1-month-old callus culture. With P medium strategy, cell growth at 49 g l^–1, intracellular AQ content at 42 mg g^–1 DW, and H₂O₂ level at 9 mol g^–1 FW medium were the highest as compared to the others. However, the extent of lipid peroxidation at 40.4 nmol g^–1 FW and total carotenoids at 13.3 mg g^–1 FW for cultures in P medium were comparable to that in the leaf, which had registered sevenfold lower AQ and 2.2-fold lower H₂O₂ levels. Vitamin C content at 30–120 g g^–1 FW in all culture systems was almost half the leaf content. On the other hand, vitamin E content was around 400–500 g g^–1 FW in 7-day-old cultures from all medium strategies and reduced to 50–150 g g^–1 FW on day 14 and 21; as compared to 60 g g^–1 FW in callus and 200 g g^–1 FW in the leaf. This study suggests that medium strategies and cell growth phase in cell culture could influence the competition between primary and secondary metabolism, oxidative stresses and antioxidative measures. When compared with the leaf metabolism, these activities are dynamic depending on the types and availability of antioxidants.Abbreviations AQ Anthraquinone - DW Dry cell weight - FW Fresh cell weight - G Intermediary medium - M Maintenance medium - MDA Malondialdehyde - P Production medium - ROS Reactive oxygen species - TBA Thiobarbituric acid - t_d Doubling time