Laccase production in semi-solid cultures of Phanerochaete chrysosporium

Cultures of Phanerochaete chrysosporium, operating with an inert carrier (nylon sponge) and a non-inert carrier (barley straw), were employed in order to study laccase production during semi-solid state conditions. Manganese (IV) oxide, added to the cultures increased laccase activity 16-fold especially in barley straw cultures, in which a maximum laccase activity of 360 U/l (one unit is defined as 1 mol of 2,2-azino-di-[3-ethyl-benzothiazoline-(6)-sulphonicacid] oxidized per minute) was achieved.     

Calorimetric control of the specific growth rate during fed-batch cultures of Saccharomyces cerevisiae

The specific growth rate of a Saccharomyces cerevisiae strain with glucose as limiting C-source was estimated from the measured heat flow produced by the cells. For the cultivation a standard 30 l laboratory bioreactor was used, which was extended in such a way that heat balancing is possible. The feed rate was adjusted by a feedforward/feedback controller such that the specific growth rate was kept on the desired set-point value. On the basis of experimental investigations it was demonstrated that the specific growth rate can be controlled at a given set point value below the critical value to prevent the production of growth-inhibitory ethanol due to the Crabtree effect. With this control strategy high biomass concentrations of more than 110 g l(-1) can be obtained.     

A pseudo-exponential feeding method for control of specific growth rate in fed-batch cultures

A simple feeding method for controlling specific growth rate in fed-batch culture was developed. This method applies a constant feed rate using a concentrate reservoir and two mixing chambers in series to simulate the exponential feeding. Fed-batch cultures with Escherichia coli showed that the present feeding method could sustain the cells growing at predetermined specific growth rates, where the time length for exponential growth was dependent on the magnitude of the growth rate. The present feeding method is convenient to operate, requires no computerized control equipments, and thus could expect an extensive application in fed-batch culture.     

Open-loop control of specific growth rate in fed-batch cultures of recombinant E.coli

Summary A computer-based algorithm was used for the open-loop control of specific growth rate in fed-batch cultures of recombinant E.coli.. The control of nutrient feed rate to an exponential trajectory resulted in growth of the culture at a constant specific growth rate. Stable specific growth rates between 0.08 and 0.4 h^–1 were achieved.     

Comparison of specific rates of hybridoma growth and metabolism in batch and continuous cultures

For the mouse hybridoma cell line VO 208, kinetics of growth, consumption of glucose and glutamine, and production of lactate, ammonia and antibodies were compared in batch and continuous cultures. At a given specific growth rate, different metabolic activities were observed: a 40% lower glucose and glutamine consumption rate, but a 70% higher antibody production rate in continuous than in batch culture. Much higher metabolic rates were also measured during the initial lag phase of the batch culture. When representing the variation of the specific antibody production rate as a function of the specific growth rate, there was a positive association between growth and antibody production in the batch culture, but a negative association during the transient phase of the continuous culture. The kinetic differences between cellular metabolism in batch and continuous cultures may be result of modifications in the physiology and metabolism of cells which, in continuous cultures, were extensively exposed to glucose limitations.Institut National Polytechnique de Lorraine, ENSAIA BP 172, 2 avenue de la forêt de Haye, 54505, Vandoeuvre Cedex France     

Simple screening method for molds producing intracellular mycotoxins in pure cultures.

A simple screening method for molds producing the intracellular mycotoxins brevianamide A, citreoviridin, cyclopiazonic acid, luteoskyrin, penitrem A, roquefortine C, sterigmatocystin, verruculogen, viomellein, and xanthomegnin was developed. After removing an agar plug from the mold culture, the mycelium on the plug is wetted with a drop of methanol-chloroform (1:2). By this treatment the intracellular mycotoxins are extracted within seconds and transferred directly to a thin-layer chromatography plate by immediately placing the plug on the plate while the mycelium is still wet. After removal of the plug, known thin-layer chromatographic procedures are carried out. The substrate (Czapek yeast autolysate agar) and growth conditions (25 degrees C for 7 days) used by Penicillium taxonomists proved suitable for the production of the mycotoxins investigated when 60 known toxigenic isolates and 865 cultures isolated from foods and feedstuffs were tested with this screening method.     

The relationship between nutrient feed rate and specific growth rate in fed batch cultures

Summary Equations are described which relate nutrient feed rate to specific microbial growth rate in fed batch culture. Fed batch cultures are classified into three types: 1) those allowing constant specific microbial growth rate, 2) those in which the rate of change of flow rate is constant and 3) those in which the nutrient flow rate is constant. The basic properties of these three types are described.Symbols F medium flow rate, L³ T^–1 - F _o medium flow rate at zero time, L³ T^–1 - g rate of change of flow rate with time, L³ T^–2 - K _v volume constant, being the total cell weight at zero time divided by the product of the yield coefficient and growth-limiting substrate concentration in the feed, L³ - s _r growth limiting substrate concentration in the feed, ML^–3 - V volume of liquid in the growth vessel, L³ - V _f volume of medium fed to the growth vessel, L³ - V _o volume of liquid in the growth vessel at zero time, L³ - X total weight of cells, M - x concentration of cells, ML^–3 - X _g total weight of cells grown, M - X _o total weight of cells at zero time, M - Y yield coefficient, weight of cells grown per unit weight of growth-limiting substrate - specific microbial growth rate, T^–1     

Determination of specific monoclonal antibody secretion rate during very slow hybridoma growth

A total cell recycling suspension perfusion reactor has been constructed for investigation of specific monoclonal antibody secretion rate of the 9.2.27 murine hybridoma under conditions of a very low growth rate. By rapidly recycling hybridoma cells using a thermostated tangential flow filter, 3.6 mg cell dry weight/cm³ could be maintained at growth rate of <0.05 _max for over 250 h. Under these conditions, secretion of lactate, ammonia and l-alanine were directly related to the rate of l-glutamine supply. Monoclonal antibody accumulated in the reactor to levels in excess of 1400 g/ cm³. Surprisingly, as specific growth rate decreased, the specific immunoglobulin secretion rate remained constant, implying that monoclonal antibody synthesis could be uncoupled from growth.List of Symbols CMF cm³/(min · cm²) cross membrane flow rate - D h^–1 dilution rate - DOT % air saturation dissolved oxygen tension - F _R cm³/min perfusion rate - GlcPR mg/min glucose provision rate - GlnPR mg/min l-glutamine provision rate - N _A mmoles O₂/(dm³ · h) oxygen transfer rate - q _ala mmoles/h l-alanine secretion rate - q _MAB mg MAB · 10^–8 viable cells ^–1 · day^–1 specific MAB secretion rate by viable cells - ¯q _MAB (dimensionless) ¯q _MAB/¯q _{MAB MAX} - ¯q _{NH 3} mmoles/h ammonia secretion rate - S _R mg/cm³ limiting substrate concentration - h^–1 specific growth rate - _app h^–1 apparent growth rate - ¯ (dimensionless) / _MAX - VC cells/cm³ viable cell number     

In vitro shoot regeneration of gladiolus in semi-solid agar versus liquid cultures with support systems

Multiple shoot clusters of gladiolus were established in semi-solid agar (AS) and liquid media appended with membrane raft (MR) and Duroplast foam (DF) support matrix. A difference in optimum combination of α-napthaleneacetic acid (NAA)/6-benzylaminopurine (BAP) for shoot multiplication was noted with culture systems. Maximum regeneration of 33.15 shoots/cluster was obtained with 1 mg l⁻¹ NAA and 2 mg l⁻¹ BAP in liquid medium with membrane support. There were 33.46 and 25.37% increase in shoot regeneration in MR system than AS and DF systems, respectively. Shoot multiplication was rapid in AS and MR systems (relative differentiation rate of 5.7% per 7 days of incubation) when compared to DF system (relative differentiation rate of 4.6% per 7 days of incubation). Shoot multiplication followed a linear trend with incubation time, whereas shoot elongation fitted well with quadratic functions. Such analysis suggests that shoot number increases steadily with time, whereas the rate of shoot elongation was different at different phases of incubation in different culture systems. Shoots in DF system exhibited faster elongation than those in AS and MR systems.     

Determination of growth and lysis kinetics in plant cell suspension cultures from the measurement of esterase release

The death of Medicago sativa L. cells cultivated in a batch culture was investigated by measuring both the appearance of intact dead cells determined on the basis of the trypan blue (TB) dye exclusion, and the release of the cytoplasmic esterase activity into the culture medium upon cell death. Taking into account the strong instability of this released esterase activity, the total dead cell and lysed cell densities have been estimated. A mechanism for cell death and lysis is proposed and the specific rates of cell growth, death and lysis estimated. The specific rate of appearance of TB dead cells was low and essentially constant (0.25 day(-1)) during the first 8 days of the batch culture, and then increased above 1.5 day(-1) after 2 weeks of cultivation. Whereas no lysis occurred during the first seven days, this phenomenon occurred during the second period and accounted for about 20% of the total cell death by the end of the process. Thus, the viability determined by the trypan blue exclusion method appeared to be invalid after 7 days of culture. When lysis of viable cells is taken into consideration, the specific growth rate was significantly increased and growth was shown to continue for a further 8 days. Increased sensitivity of the cells to shear stresses and consequent cell lysis could be the result of a 35% increase in the cell size Copyright 1999 John Wiley & Sons, Inc.