Accumulation of silver by Chromatium vinosum from solutions containing silver thiosulfate

The photosynthetic sulfur bacterium, Chromatium vinosum, was cultured in inorganic photographic processing solutions containing silver thiosulfate complex salt (AgNa₃(S₂O₃)₂) under light. It was found that Chromatium was resistant to Ag and accumulated granular silver in the membrane during growth. The amount of Ag accumulated in the cells depended on the initial concentrations of the Ag salt in the culture solution. When the concentration of Ag was 300 mg/l, the bacteria accumulated Ag as high as 30% of the dry cell weight. The size of the granules was 0.1 to 0.3 m. Results from X-ray microanalysis indicated that these granules consisted mostly of Ag^o with small fractions of Ag₂S and AgCl.     

Cryopreservation of dried axillary buds from plantlets of Asparagus officinalis L. grown in vitro

Dried axillary buds from plantlets of Asparagus lofficinalis L. grown in vitro were successfully cryopreserved. Single node segments (5mm in length) with axillary bud were taken from mature in vitro plantlets. The segments were precultured on solidfied Murashige-Skoog medium (1962) containing 0.7M sucrose at 25 °C in light for 2 days. Thereafter, these precultured segments were subjected to dehydration with silica gel at room temperature for 0 to 24 h. The axillary buds of precultured segments tolerated dehydration to about 14% water content(FW) with 50% lethality (LD₅₀) and the threshold water content at which the dried buds remained alive after exposure to liquid nitrogen was 16.9%(LD₅₀). The maximum rate of survival of cryopreserved buds was about 71% of untreated control. Surviving buds produced shoots and regenerated into plantlets. These results demonstrate the feasibility of cryopreserving dried axillary buds from in vitro plantlets.Abbreviations MS Murashige and Skoog medium(1962) - LN liquid nitrogen - FW fresh weight basis - LD₅₀ the water content at 50% lethality - ABA abscisic acid - NAA -naphthalene acetic acid - BA 6-benzyladenine - DTA differential thermal analysis     

Modeling of the pyruvate production with<Emphasis Type="Italic"> Escherichia coli</Emphasis> in a fed-batch bioreactor

A family of 10 competing, unstructured models has been developed to model cell growth, substrate consumption, and product formation of the pyruvate producing strain Escherichia coli YYC202 ldhA::Kan strain used in fed-batch processes. The strain is completely blocked in its ability to convert pyruvate into acetyl-CoA or acetate (using glucose as the carbon source) resulting in an acetate auxotrophy during growth in glucose minimal medium. Parameter estimation was carried out using data from fed-batch fermentation performed at constant glucose feed rates of q_VG=10 mL h^–1. Acetate was fed according to the previously developed feeding strategy. While the model identification was realized by least-square fit, the model discrimination was based on the model selection criterion (MSC). The validation of model parameters was performed applying data from two different fed-batch experiments with glucose feed rate q_VG=20 and 30 mL h^–1, respectively. Consequently, the most suitable model was identified that reflected the pyruvate and biomass curves adequately by considering a pyruvate inhibited growth (Jerusalimsky approach) and pyruvate inhibited product formation (described by modified Luedeking–Piret/Levenspiel term).List of symbols c_A acetate concentration (g L^–1) - c_A,0 acetate concentration in the feed (g L^–1) - c_G glucose concentration (g L^–1) - c_G,0 glucose concentration in the feed (g L^–1) - c_P pyruvate concentration (g L^–1) - c_P,max critical pyruvate concentration above which reaction cannot proceed (g L^–1) - c_X biomass concentration (g L^–1) - K_I inhibition constant for pyruvate production (g L^–1) - K_I^A inhibition constant for biomass growth on acetate (g L^–1) - K_P saturation constant for pyruvate production (g L^–1) - K_P inhibition constant of Jerusalimsky (g L^–1) - K_S^A Monod growth constant for acetate (g L^–1) - K_S^G Monod growth constant for glucose (g L^–1) - m_A maintenance coefficient for growth on acetate (g g^–1 h^–1) - m_G maintenance coefficient for growth on glucose (g g^–1 h^–1) - n constant of extended Monod kinetics (Levenspiel) (–) - q_V volumetric flow rate (L h^–1) - q_VA volumetric flow rate of acetate (L h^–1) - q_VG volumetric flow rate of glucose (L h^–1) - r_A specific rate of acetate consumption (g g^–1 h^–1) - r_G specific rate of glucose consumption (g g^–1 h^–1) - r_P specific rate of pyruvate production (g g^–1 h^–1) - r_P,max maximum specific rate of pyruvate production (g g^–1 h^–1) - t time (h) - V reaction (broth) volume (L) - Y_P/G yield coefficient pyruvate from glucose (g g^–1) - Y_X/A yield coefficient biomass from acetate (g g^–1) - Y_X/A,max maximum yield coefficient biomass from acetate (g g^–1) - Y_X/G yield coefficient biomass from glucose (g g^–1) - Y_X/G,max maximum yield coefficient biomass from glucose (g g^–1) - growth associated product formation coefficient (g g^–1) - non-growth associated product formation coefficient (g g^–1 h^–1) - specific growth rate (h^–1) - _max maximum specific growth rate (h^–1)     

Mixed substrate growth of methylotrophic yeasts in chemostat culture: Influence of the dilution rate on the utilisation of a mixture of glucose and methanol

The growth of Hansenula polymorpha and Kloeckera sp. 2201 with a mixture of glucose and methanol (38.8%/61.2%, w/w) and the regulation of the methanol dissimilating enzymes alcohol oxidase, catalase, formaldehyde dehydrogenase and formate dehydrogenase were studied in chemostat culture, as a function of the dilution rate. Both organisms utilized and assimilated glucose and methanol simultaneously up to dilution rates of 0.30 h^-1 (H. polymorpha) and 0.26h^-1, respectively (Kloeckera sp. 2201) which significantly exceeded _max found for the two yeasts with methanol as the only source of carbon. At higher dilution rates methanol utilisation ceased and only glucose was assimilated. Over the whole range of mixed-substrate growth both carbon sources were assimilated with the same efficiency as during growth with glucose or methanol alone.In cultures of H. polymorpha, however, the growth yield for glucose was lowered by the unmetabolized methanol at high dilution rates. During growth on both carbon sources the repression of the synthesis of all catabolic methanol enzymes which is normally caused by glucose was overcome by the inductive effect of the simultaneously fed methanol. In both organisms the synthesis of alcohol oxidase was found to be regulated differently as compared to catalase, formaldehyde and formate dehydrogenase. Whereas increasing repression of the synthesis of alcohol oxidase was found with increasing dilution rates as indicated by gradually decreasing specific activities of this enzyme in cell-free extracts, the specific activities of this enzyme in cell-free extracts, the specific activities of catalase and the dehydrogenases increased with increasing growth rates until repression started. The results indicate similar patterns of the regulation of the synthesis of methanol dissimilating enzymes in different methylotrophic yeasts.Abbreviations and Terms C₁ Methanol - C₆ glucose; D dilution rate (h^-1) - D _c critical dilution rate (h^-1) - q _s specific, rate of substrate consumption (g substrate [g cell dry weight]^-1 h^-1) - q _CO2 and q _O2 are the specific rates of carbon dioxide release and oxygen consumption (mmol [g cell dry weight]^-1 h^-1) - RQ respiration quotient (q _CO2 q _O2 ¹ ) - s ₀(C₁) and s ₀(C₆) are the concentrations of methanol and glucose in the inflowing medium (g l^-1) - s residual substrate concentration in the culture liquid (g l^-1) - Sp. A. enzyme specific activity - x cell dry weight concentration (gl^-1) - Y _X/C6 growth yield on glucose (g cell dry weight [g substrate]^-1     

In vitro plant regeneration of leguminous trees (Albizia spp)

Hypocotyl explants of three leguminous forest tree species, Albizia amara, A. lucida and A. richardiana, have differentiated shoot buds on B₅ basal medium. Maximum number of shoots per explant developed on basal medium augmented with 2,4-D (0.1 M) in A. amara (2) and BA (10 M) for both A. lucida (2) and A. richardiana (1.6). Higher concentrations of auxins in the medium, in general, enhanced rooting and callusing but cytokinins promoted the growth of green calli. BA enchanced the differentiation of shoots in the three species. The in vitro grown shoots of A. amara and A. richardiana, after subculturing on B₅+1 M IAA developed roots (up to 30–40%). These plants have been successfully transferred to the field.Abbreviations 2,4-D 2,4-dichlorophenoxyacetic acid - BA 6-benzylaminopurine - BM Gamborg's B₅ medium with 0.9% agar+3% sucrose - IAA Indole-3-acetic acid - IBA Indole-3-butyric acid - Kn Kinetin - NAA -naphthaleneacetic acid     

Biomass yields of Chlorella from iron (Y x/Fe) in iron-limited batch cultures

The maximum biomass in iron-limited photosynthetic batch cultures of chlorella increased as the logarithm of the iron concentration. The growth yield from iron (Y _x/Fe) showed a marked inverse relation to the specific growth rate. The maximum biomass yield, g dry biomass/g iron consumed, was 7.5x10³ with specific growth rate 0.108 h^-1; the minimum was 0.79×10³ with specific growth rate 0.145 h^-1. The maximum specific growth rate in the exponential phase of Fe limited cultures varied as the initial Fe concentration. Fe-limited growth made the cells adhere to a glass surface.Abbreviation O.D. optical density     

Regulatory flexibility of methylotrophic yeasts in chemostat cultures: Simultaneous assimilation of glucose and methanol at a fixed dilution rate

The influence of the composition of methanol/glucose-mixtures as only sources of carbon and energy on growth and regulation of the synthesis of enzymes involved in methanol-dissimilation was studied under chemostat conditions at a fixed dilution rate with the methylotrophic yeasts Hansenula polymorpha and Kloeckera sp. 2201. Both carbon sources were found to be utilized completely independently of the composition of the C₁/C₆ mixture. Using mixtures of ¹⁴C-labelled methanol and glucose the growth yield for glucose was found to be constant for all C₁/C₆-mixtures tested and both yeasts. The growth yield for methanol, however, was reduced by up to 25% when the proportion of methanol in the inflowing medium was lower than 20% (w/w with respect to glucose) for H. polymorpha and 50% (w/w with respect to glucose) for Kloeckera sp. 2201 respectively. During growth with C₁/C₆-mixtures containing higher C₁-proportions of methanol regular growth yields for methanol were recorded which corresponded to the growth yields found with methanol as the only carbon source.The regulation of the synthesis of the enzymes of the dissimilatory pathway for methanol was found to be under multiple control. Although glucose was present in the medium methanol had a positive effect on the synthesis of these enzymes. Thus, in addition to derepression induction by methanol was also observed. This inductive effect was found to increase with increasing proportions of methanol in the mixture. Depending on the enzyme, 10–40% methanol in the mixture resulted in a maximal induction with enzyme specific activities equal to those found in cells grown with methanol as the only carbon source. No further enhancements in enzyme specific activities were observed during growth on mixtures containing more than 40% methanol.Abbreviations and terms C₁ Methanol - C₆ glucose - C₁/C₆ mixture compositions are given in % (w/w) - C₀ concentration of ¹⁴C in the inflowing medium (DPM ml^-1) - C(t) concentration of ¹⁴C incorporated in cells as a function of time t (DPM ml^-1) - d dilution rate (h^-1) - DPM disintegrations per minute - q _s q _C1 and q _C6 are specific rates of consumption of substrate, methanol and glucose respectively [g (g cell dry weight)^-1 h^-1] - q _O2 and q _CO2 are the specific rates of oxygen consumption and carbon dioxide release [mmol (g cell dry weight)^-1 h^-1] - RQ respiration quotient (q _CO2 q _O2 ^-1) - s _C1 and s _C6 are the residual concentrations of methanol and glucose in the culture liquid (g l^-1) - s _O/C1 and s _O/C6 are the concentrations of methanol and glucose in the inflowing medium (g l^-1) - Sp.A. enzyme specific activity - x cell dry weight concentration (g l^-1) - Y _X/C1 and Y _X/C6 are growth yields on methanol and glucose respectively (g cell dry weight (g substrate)^-1 - Y _C/C1 growth yield with methanol with respect to carbon (g carbon assimilated (g carbon supplied)^-1 - _m maximum specific growth rate (h^-1)     

Observer design for differential-algebraic model of an aerobic culture of a recombinant yeast

The mathematical model of an aerobic culture of recombinant yeast presented in work by Zhang et al. (1997) is given by a differential-algebraic system. The classical nonlinear observer algorithms are generally based on ordinary differential equations. In this paper, first we extend the nonlinear observer synthesis to differential-algebraic dynamical systems. Next, we apply this observer theory to the mathematical model proposed in Zhang et al. (1997). More precisely, based on the total cell concentration and the recombinant protein concentration, the observer gives the online estimation of the glucose, the ethanol, the plasmid-bearing cell concentration and a parameter that represents the probability of plasmid loss of plasmid-bearing cells. Numerical simulations are given to show the good performances of the designed observer.Symbols C ₁ activity of pacing enzyme pool for glucose fermentation (dimensionless) - C ₂ activity of pacing enzyme pool for glucose oxidation (dimensionless) - C ₃ activity of pacing enzyme pool for ethanol oxidation (dimensionless) - E ethanol concentration (g/l) - G glucose concentration (g/l) - k _a regulation constant for (g glucose/g cell h^–1) - k _b regulation constant for (dimensionless) - k _c regulation constant for (g glucose/g cell h^–1) - k _d regulation constant for (dimensionless) - K _m1 saturation constant for glucose fermentation (g/l) - K _m2 saturation constant for glucose oxidation (g/l) - K _m3 saturation constant for ethanol oxidation (g/l) - L ( t) time lag function (dimensionless) - p probability of plasmid loss of plasmid-bearing cells (dimensionless) - P recombinant protein concentration (mg/g cell) - q _G total glucose flux culture time (g glucose/g cell h) - t culture time (h) - t _lag lag time (h) - X total cell concentration (g/l) - X ⁺ plasmid-bearing cell concentration (g/l) - Y ^F _{X / G} cell yield for glucose fermentation pathway (g cell/g glucose) - Y ^O _{X / G} cell yield for glucose oxidation pathway (g cell/g glucose) - Y _{X / E} cell yield for ethanol oxidation pathway (g cell/g ethanol) - Y _{E / X} ethanol yield for fermentation pathway based on cell mass (g ethanol·g cell) - ₂ glucoamylase yield for glucose oxidation (units/g cell) - ₃ glucoamylase yield for ethanol oxidation (units/g cell) - µ₁ specific growth rate for glucose fermentation (h^–1) - µ₂ specific growth rate for glucose oxidation (h^–1) - µ₃ specific growth rate for ethanol oxidation (h^–1) - µ_1max maximum specific growth rate for glucose fermentation (h^–1) - µ_2max maximum specific growth rate for glucose oxidation (h^–1) - µ_3max maximum specific growth rate for ethanol oxidation (h^–1)     

Gene transfer in plants of Brassica juncea using Agrobacterium tumefaciens-mediated transformation

An efficient system for gene transfer into plants of Brassica juncea var. India Mustard, mediated by Agrobacterium tumefaciens. was developed through the manipulation of the culture medium and the use of the appropriate Agrobacterium strain. High frequency shoot regeneration (90–100%) was obtained from hypocotyl explants grown on medium containing 0.9% agarose, 3.3 mg/L AgNO₃ and 0.5–2 mg/L BA in combination with 0.01–0.05 mg/L 2,4-D or 0.1–1 mg/L NAA. Of all the Agrobacterium strains tested, A. tumefaciens A208-SE, carrying the disarmed Ti plasmid and a binary vector pROA93, was the most effective for B. juncea transformation. pROA93 carries the coding sequences of the NPTII and the GUS genes, both driven by a common CaMV 35S promoter in two divergent directions. Inoculated explants grown on the selection medium in the presence of 0.5 mg/L BA and 0.1 mg/L NAA gave rise to transgenic shoots at the highest frequency (9%). All R_o transgenic plants were phenotypically normal, but variation in expression patterns of the GUS gene occurred among the transgenic plants in an organ- and tissue-specific manner. Both the NPTII and the GUS genes were transmitted to the R₁ seed progeny and showed co-segregation.Abbreviations BA benzyladenine - 2,4-D 2,4-dichlorophenoxyacetic acid - NAA naphthaleneacetic acid - NPTII neomycin phosphotransferase type II - GUS -glucuronidase - CaMV cauliflower mosaic virus - MS Murashige and Skoog - X-Gluc 5-bromo-4-chloro-3-indolyl-D--glucuronic acid - IBA indolebutyric acid - SDS sodium dodecyl sulfate     

Prodigiosin formation by Serratia marcescens in a chemostat

In a study of the control of metabolite formation, prodigiosin production by Serratia marcescens was used as a model. Specific production rates of prodigiosin formation were determined using batch culture technique. Sucrose as carbon source and NH₄NO₃ as nitrogen source resulted in a specific production rate of 0.476 mg prodigiosin (g cell dry weight)⁻¹ h⁻¹. Prodigiosin formation and productivity was inversely correlated to growth rate when the bacterium was grown under carbon limitation on a defined medium in a chemostat culture. The maximum specific growth rate (μ_max) was 0.54 h⁻¹ and prodigiosin was formed in amounts over 1 mg l⁻¹ up to a growth rate (μ) of 0.3 h⁻¹ at steady state conditions. At a dilution rate of 0.1 h⁻¹ growth at steady state with carbon and phosphate limitation supported prodigiosin formation giving a similar specific yield [1.17 mg prodigiosin (g cell dry weight)⁻¹ and 0.94 mg g⁻¹, respectively], however, cells grown with nitrogen limitation [(NH₄)₂SO₄] did not form prodigiosin. Productivity in batch culture was 1.33 mg l⁻¹ h⁻¹ as compared to 0.57 mg l⁻¹ h⁻¹ in the chemostat.     

Plant regeneration from protoplasts of embryogenic cell suspensions of Coffea arabica L. cv. caturra

Coffee plants were regenerated from protoplasts isolated from embryogenic cell suspension cultures derived from somatic embryos of Coffea arabica L. cv. caturra. Yields of viable protoplasts ranged from 1×10⁵ to 6×10⁵ protoplast/g fresh weight. Protoplast preparations usually contained no contaminating cells, and when present, the number of cells never exceeded 0.1% of the total. Plating efficiencies of protoplast ranged from 1 to 10%. Embryogenic protocolonies obtained after several subcultures in a medium supplemented with 0.5 mg/l each of benzylaminopurine, 2,4-dichlorophenoxyacetic acid and naphtaleneacetic acid, were transferred to a medium lacking plant growth regulators. Well differentiated embryos were formed in selected protocolonies that contained many embryos-like structures. Approximately 70% of the somatic embryos developed into green rooted plantlets which were succesfully transferred to vessels containing sterilized scoria. Plants grown for two months in scoria were finally transferred to greenhouse.Abbreviations B5 medium according to Gamborg et. al.(1968) - BAP 6-benzylaminopurine - 2,4-D 2,4-dichlorophenoxyacetic acid - NAA naphtaleneacetic acid     

Growth and cell wall composition of glucose-limited bean cells (Phaseolus vulgaris L.)

Glucose-limited bean cells (Phaseolus vulgaris L.) were grown in a modified bacterial fermentor at a constant pH of 4.8. The cultures were kept in steady state at different specific growth rates varying from 0.00216 h^–1 to 0.0106 h^–1. Culture conditions are described that are needed to start a continuous culture. First, it was essential to use log-phase cells as starting material. Second, it was important to increase the dilution rate gradually, otherwise cells in the culture aggregated. Cells grown at the highest dilution rate employed contained twice as much protein per gram dry weight as cells grown at the lowest dilution rate. The composition of the cell walls also varied with the dilution rate in contrast to their relatively constant composition when grown in batch culture.     

Molar growth yields,respiration and cytochrome profiles of Beneckea natriegens when grown under carbon limitation in a chemostat

The effect of growth rate on the physiology of Beneckea natriegens was studied in chemostat culture. The molar growth yields (Y) from glucose and oxygen, the specific rates of oxygen (q _{O 2}) and glucose (q _glc) consumption and the specific rate of CO₂ production (q _{CO 2}) were linearly dependent on the growth rate over the dilution rate 0.17 h^-1 to 0.60 h^-1. Further increase in the dilution rate resulted in a decrease in growth yield and respiration rate and these changes were coincident with increases in the specific rate of glucose utilisation and of acetate production. The affinity of Beneckea natriegens for glucose was similar when measured either directly in chemostat culture or in a closed oxygen electrode system using harvested bacteria. The total content of cytochromes decreased with increasing growth rate. However, the quantity of CO-binding cytochromes remained independent of growth rate and correlated with the potential respiration rate.     

Anaerobiosis and low specific growth rates enhance hemolysin BL production by <Emphasis Type="Italic">Bacillus cereus</Emphasis> F4430/73

Bacillus cereus F4430/73 produced the highest levels of hemolysin BL (HBL) when grown under anaerobiosis in MOD medium. Anaerobic cells grown in a chemostat at low specific growth rate (0.1–0.2 h^–1) expressed up to sevenfold more HBL than did cells held at a faster growth rate. At 0.2 h^–1, the presence of 90 mM glucose resulted in inhibition of HBL production. Glucose was found to repress HBL induction at the mRNA level, indicating the potential involvement of catabolite repression in the regulation of HBL. Based on these data, it is suggested that growth rate could be an effector of catabolite regulation of HBL.     

Somatic embryogenesis and plant regeneration in cotton (Gossypium hirsutum L.)

Tissue culture methods for improvement of cotton has lagged seriously compared to other major crops. A method for regeneration of cotton which includes a morphogenetically competent cell suspension was needed to facilitate selection of stress-resistant variants and gene manipulation. Preliminary screening of eight strains of Gossypium hirsutum L. for embryogenic potential resulted in the production of somatic embryos in all strains. Coker 312 was selected for use in the development of a model regeneration system for G. hirsutum. Calli were initiated from hypocotyl tissues of 3-day-old-seedlings. Globular embryos were present after six weeks in culture. Calli were subcultured to liquid suspension in growth regulator-free medium. After three to four weeks, suspensions were sieved to collect globular and heart stage embryos. Collected embryos developed further when plated onto semi-solid medium. To induce germination and plantlet growth, mature embryos were placed on sterile vermiculite saturated with medium. Upon development of roots and two true leaves, plantlets were potted in peat and sand, and hardened. Mature plants and progeny have been obtained with this procedure. A high percentage of infertile plants was observed among the regenerants.Abbreviations NAA 1 naphthaleneacetic acid - IAA indole-3-acetic acid - 2,4-D 2,4-dichlorophenoxyacetic acid - GA₃ gibberellic acid - MS Murashige and Skoog - BA 6 benzylamino purine - 2i P N⁶-(²-isopentenyladenine     

Growth rate influences reductive biodegradation of the organophosphorus pesticide demeton by Corynebacterium glutamicum

The organophosphorous pesticide, demeton-S-methyl was transformed byCorynebacterium glutamicum in co-metabolism with more readilydegradable substrates. Glucose, acetate and fructose were tested as growth substrates, and the highest demeton-S-methyl biotransformation average rate (0.78 mg l^-1 h^-1) and maximum instantaneous rate (1.4 mg l^-1 h^-1) were achieved on fructose. This higher efficiency seems to be linked to the atypical behavior of C. glutamicum grown on fructose, characterized by a prolonged period of accelerating growth instead of a constant growth rate observed on glucose or acetate. More precisely, for growth rates in the 0.1–0.4 h^-1 range, a direct coupling between the specific demeton-S-methyl consumption rate and the growth rate was demonstrated on fructose during batch –, steady state continuous – or continuous cultures with a controlled transient growth rate (accelerostat technology). The demeton-S-methyl biotransformation was more favoured during an acceleration phase of the growth rate.     

Characteristics of fed-batch cultures of recombinant <Emphasis Type="Italic">Escherichia coli</Emphasis> containing human-like collagen cDNA at different specific growth rates

Fed-batch cultures of recombinant Escherichia coli BL21 for producing human-like collagen were performed at different specific growth rates (0.1~0.25 h⁻¹) before induction and at a constant value of 0.05 h⁻¹ after induction by the method of pseudo-exponential feeding. Although the final biomass (around 69 g l⁻¹) was almost the same in all fed-batch cultures, the highest product concentration (13.6 g l⁻¹) was achieved at the specific growth rate of 0.15 h⁻¹ and the lowest (9.6 g l⁻¹) at 0.25 h⁻¹. The mean productivity of human-like collagen was the highest at 0.15 h⁻¹ (0.57 g l⁻¹ h⁻¹) and the lowest at 0.1 h⁻¹ (0.35 g l⁻¹ h⁻¹). In the phase before induction, the cell yield coefficient (Y_X/S) decreased when the specific growth rate increased, while the formation of acetic acid increased upto 2.5 g l⁻¹ at 0.25 h⁻¹. The mean product yield coefficient (Y_P/S) also decreased with specific growth rate increasing. The respiration quotient (RQ) increased slightly with specific growth rate increasing before induction, and the mean value of RQ was around 72%. The optimum growth rate for human-like collagen production was 0.15~0.2 h⁻¹.     

Benomyl: A broad spectrum fungicide for use in plant cell and protoplast culture

The systemic fungicide methyl-1-(butylcarbamoyl)-2-benzimidazole carbamate (benomyl), is a broad spectrum fungicide. Benomyl at concentrations up to 50 mg/l does not inhibit the growth of suspension cultures ofNicotiana tabacum, Datura innoxia, Daucus carota, Glycine canescens, andSolanum tuberosum nor growth ofN. tabacum orN. plumbaginifolia protoplasts if benomyl is dissolved by autoclaving or boiling. Addition of benomyl dissolved in dimethyl sulfoxide results in a visible toxicity. Benomyl, at 6.25–50 mg/l preventsPenicillium spp. growth in both protoplast and cell cultures and can be used to remove fungal contaminates after one to three transfers without visibly retarding plant cell growth. Due to the broad spectrum of fungicidal activity, and nontoxicity at high concentrations when dissolved by boiling or autoclaving, benomyl can be used effectively to control or prevent fungal contamination in plant cell and protoplast cultures.     

Transformation of Solanum integrifolium poir via Agrobacterium tumefaciens: Plant regeneration and progeny analysis

Summary The wild species Solanum integrifolium represents a source of pest and disease resistance genes for breeding strategies of the cultivated species Solanum melongena. Somatic hybridization via protoplast fusion between the two species may provide a valuable tool for transferring polygenic traits into the cultivated species. The availability of S.integrifolium cells carrying dominant selectable markers would facilitate the heterokaryon rescue. An appropriate methodology for in vitro culture and plant regeneration from leaf explants of S.integrifolium is reported. Efficient leaf-disk transformation via co-cultivation with Agrobacterium tumefaciens led to the regeneration of transformed plants carrying the reporter genes GUS and NPT-II. Transformed individuals were obtained through selection on kanamycin-containing medium. Stable genetic transformation was assessed by histochemical and enzymatic assays for GUS and NPT-II activity, by the ability of leaf disks to initiate callus on Km-containing medium, Southern blot analyses of the regenerated plants, and genetic analysis of their progenies. Selfed-seed progeny of individual transformed plants segregated seedlings capable to root and grow in selective condition, while untransformed progeny did not. Genetic analyses of progeny behaviour showed that the reporter gene NPT-II segregated as single as well as two independent Mendelian factors. In two cases an excess of kanamycin-sensitive seedlings was obtained, not fitting into any genetic hypothesis.Abbreviations MS Murashige and Skoog (1962) medium - NOS nopaline synthase - NPT-II neomycin phosphotransferase - GUS beta-glucuronidase - LB Luria and Bertani medium - KIN 6-furfurylaminopurine - BAP 6-benzylaminopurine - 2iP N⁶-(2-isopentyl)adenine - ZEA zeatin - TDZ Thidiazuron     

Adenine nucleotides,substrate utilization and dinitrogen fixation in Rhodobacter capsulatus

Rhodobacter capsulatus strain 37b4 was grown diazotrophically in phototrophic chemostat culture with 30 mM of d,l-malate and 2 mM of ammonium. Illumination was varied at constant dilution rate (D) and vice versa, respectively. When D was raised from 0.035 to 0.165 h^-1 at 30 klx, the steady state cell protein level as well as malate consumption decreased. d-malate was utilized only at D=0.035 h^-1. Specific cellular activities of nitrogenase, as determined by acetylene reduction as well as by dinitrogen (N₂) fixation, increased and approached constancy at D>0.075 h^-1. Specific ATP contents of cells increased with increasing D, while specific ADP and AMP contents exhibited no significant variations. Consequently, energy charge values as well as molar ratios of ATP/ADP (T/D) increased. Raising illumination from 6 to 30 klx at D=0.075 h^-1 resulted in an increase of the steady state protein level as well as of l-malate consumption. d-malate was not utilized under these conditions. Specific nitrogenase activity of cells increased at the lower and levelled off at the higher illuminations. Specific ATP contents of cells stayed constant but specific ADP contents increased with increasing illumination. The energy charge did not vary significantly, while the T/C ratio decreased between 6 and 18 klx and stayed constant at the higher illuminations. The results do not reveal any relationship between nitrogenase activity and the cellular levels or relative proportions of different adenine nucleotides. However, when steady state amounts of fixed N₂ were plotted versus steady state T/D ratios, an inverse proportion became apparent, irrespective of the growth conditions employed. On the other hand, specific nitrogenase activity increased linearly when the rate of malate consumption increased. The results suggest that under steady state conditions the T/D ratio reflects the amount of ATP required to keep the amount of fixed N₂ at a given level, while the rate at which nitrogenase functions depends on the rate at which the carbon and electron source, malate, is utilized by the organisms.