On-line biomass monitoring by capacitance measurement.

An in-situ, steam-sterilizable capacitance probe was used to follow the biomass concentration on-line, in bioreactors from 20 to 2000 l total volume. Microbial cultures of Saccharomyces cerevisiae, Pichia pastoris and Streptomyces virginiae were grown in batch and fed-batch culture in both defined and complex media in order to demonstrate the wide dynamic operating range of the instrument. A linear correlation was found between the on-line capacitance measurement and the off-line measurements (optical density, OD620; packed mycelial volume, PMV; biomass concentration X, and colony forming units, CFU ml-1) for biomass concentrations (dry cell weight) up to 30 g l-1 (St. virginiae), 106 g l-1 (S. cerevisiae) and 89 g l-1 (P. pastoris). The on-line capacitance measurement was slightly influenced by variations in agitation speed and strong extraneous radio frequencies. A specific capacitance constant (Cs) was defined for all microbial cells which was dependent on cell viability and cell size. The Cs was easy to calculate using the on-line capacitance measurement and an off-line estimation of biomass concentration. The Biomass Monitor proved suitable for precise on-line monitoring of both homogeneous (uni-cellular) and heterogeneous (mycelial) cultures in bioreactors.     

Effects of ammonia and lactate on hybridoma growth, metabolism, and antibody production

The influence of ammonia and lactate on cell growth, metabolic, and antibody production rates was investigated for murine hybridoma cell line 163.4G5.3 during batch culture. The specific growth rate was reduced by one-half in the presence of an initial ammonia concentration of 4 mM. Increasing ammonia levels accelerated glucose and glutamine consumption, decreased ammonia yield from glutamine, and increased alanine yield from glutamine. Although the amount of antibody produced decreased with increasing ammonia concentration, the specific antibody productivity remained relatively constant around a value of 0.22 pg/cell-h. The specific growth rate was reduced by one-half at an initial lactate concentration of 55 mM. Although specific glucose and glutamine uptake rates were increased at high lacatate concentration, they showed a decrease after making corrections for medium osmolarity. The yield coefficient of lactate from glucose decreased at high lactate concentrations. A similar decrease was observed for the ammonia yield coefficient from glutamine. At elevated lactate concentrations, specific antibody productivities increased, possibly due to the increase in medium osmolarity. The specific oxygen uptake rate was insensitive to ammonia and lactate concentrations. Addition of ammonia and lactate increased the calculated metabolic energy production of the cells. At high ammonia and lactate, the contribution of glycolysis to total energy production increased. Decreasing external pH and increasing ammonia concentrations caused cytoplasmic acidification. Effect of lactate on intracellular pH was insignificant, whereas increasing osmolarity caused cytoplasmic alkalinization.     

Effects of ammonia and lactate on growth, metabolism, and productivity of BHK cells

The aim of the present work was to study the effect of ammonia and lactate on growth, metabolism, and productivity of BHK cells producing a recombinant fusion protein. Results show that cell growth was reduced with the increase in ammonia or lactate: k(1/2) of 1.1 mM and 3.5 mM for stirred and stationary cultures, respectively, for ammonia and of 28 mM for both stationary and stirred cultures for lactate, were obtained. The cell-specific consumption rates of both glucose (q(Glc)) and glutamine (q(Gln)) increased, whereas that of oxygen (q(O2)) decreased, with the increase in ammonia or lactate concentrations. The cell-specific production rates of lactate (q(Lac)) increased with an increase in ammonia concentration; similarly for the cell-specific production rates of ammonia (q(Amm)), which also increased with an increase in lactate concentration; on the other hand, both q(Lac) and q(Amm) markedly decreased when lactate or ammonia concentrations were increased, respectively; lactate was consumed at lactate concentrations above 30 mM and ammonia was consumed at ammonia concentrations above 5 mM. In vivo (31)P NMR experiments showed that ammonia and lactate affect the intracellular pH, leading to intracellular acidification, and decrease the content in phosphomonoesters, whereas the cell energy state was maintained. The effect of lactate on cell growth and q(Gln) is partially due to osmolarity, on q(Glc) and q(Amm) is entirely due to osmolarity, but on q(Lac) is mainly due to lactate effect per se. An increase in ammonia from 0 to 20 mM induced a 50% reduction in specific productivity, whereas an increase in lactate from 0 to 60 mM induced a 40% decrease.     

Influence of dissolved oxygen concentration on the biosynthesis of cephalosporin C.

Cephalosporin C was produced by a highly productive strain of Cephalosporium acremonium under industrial production conditions by fed-batch cultivation in a 40-l stirred-tank reactor using a complex medium containing 50 g l-1 peanut flour. The influence of dissolved oxygen concentration (pO2, DOC), which was maintained at different constant levels between 5 and 40% of its saturation value, during the production phase by means of a parameter-adaptive pO2-controller, on the cephalosporin C biosynthesis, was investigated. The concentrations of cephalosporin C (CPC) and its precursors penicillin N (PEN N), deacetoxycephalosporin C (DAOC), and deacetylcephalosporin C (DAC) were monitored by on-line HPLC. The concentrations of amino acids, valine (VAL), cysteine (CYS), alpha-amino-adipic acid (alpha-AAA), the dipeptide alpha-amino-adipyl-cysteine (AC), and the tripeptide alpha-amino-adipyl-cysteinyl-valine (ACV) were determined by off-line HPLC. By reducing the pO2 in the production phase from 40 to 5% of its saturation value, the CPC concentration diminished from 7.2 to 1.1 g l-1 and the PEN N concentration increased from 2.57 to 7.65 g l-1. The DAC concentration also dropped from 3.13 to 0.42 g l-1; however, the DAOC concentration was less influenced. The concentrations of AC and ACV were also less affected. The small DOC did not lead to an accumulation of the intermediate AC and ACV during the production phase. With increasing DOC in the range of 5-20%, the maximal specific production rate, the cell mass concentration-based and the substrate-based yield coefficients for CPC increased almost linearly, and fell back for PEN N.(ABSTRACT TRUNCATED AT 250 WORDS)     

Some aspects of hybridoma cell cultivation

Summary Two hybridoma cell lines were cultivated in an indirectly aerated 10-1 reactor in batch, fed-batch and continuous (perfusion) operations and in spinner flasks. The medium in the reactor was sampled either by an aseptic cross-flow filtration module integrated into a loop or by an in-situ tubular filter. The glucose concentration was monitored by an on-line flow injection analyzer and the ammonia concentration by an ion-selective electrode. Since the membrane transmission of the high-molecular components decreased during cultivation, the product, a monoclonal antibody, was enriched in the reactor. During cultivation, the concentrations of cells, viable cells, glucose, lactase, acetate, citrate, ammonia, urea, amino acids, proteins, and monoclonal antibodies were determined off-line. The specific growth rate, specific production, and consumption rates of the medium components were influenced considerably by the medium composition, especially by the type and amount of serum used.Offprint requests to: K. Schügerl     

Characterization of changes in PER.C6 cellular metabolism during growth and propagation of a replication-deficient adenovirus vector

PER.C6 cells were cultivated for propagation of a replication-defective adenovirus vector in serum-free suspension bioreactors. Cellular metabolism during cell growth and adenovirus propagation was fully characterized using on-line and off-line methods. The energy metabolism was found to accelerate transiently after adenovirus infection with increases in glucose and oxygen consumption rates. Similar to other mammalian cells, glucose utilization was highly inefficient and a high lactate:glucose yield was observed, both before and after virus infection. A higher consumption of most of the essential amino acids was observed transiently after the infection, likely due to increased protein synthesis requirements for virus propagation. To improve virus propagation, a medium exchange strategy was implemented to increase PER.C6 cell concentration for infection. During cell growth, a 50% increase in glucose consumption and lactate production rates was observed after initiation of the medium exchange in comparison to the batch phase. This decrease in medium capacity only affected the central carbon metabolism and no increase in amino acid consumption was observed. In addition, even though cell concentrations of up to 10 x 10(6) cells/mL were reproducibly obtained by medium exchange, infections at cell concentrations higher than 1 x 10(6) cells/mL did not proportionally improve volumetric adenovirus productivities. No measured nutrient limitation was observed at those high cell concentrations, indicating that adenovirus cell-specific productivity at higher cell concentrations is highly dependent on cell physiology. These results provide a better understanding of PER.C6 cellular metabolism and a basis for intensifying PER.C6 growth and adenovirus propagation.     

The in-line measurement of plant cell biomass using radio frequency impedance spectroscopy as a component of process analytical technology

Radio frequency impedance spectroscopy (RFIS) is a robust method for the determination of cell biomass during fermentation. RFIS allows non-invasive in-line monitoring of the passive electrical properties of cells in suspension and can distinguish between living and dead cells based on their distinct behavior in an applied radio frequency field. We used continuous in situ RFIS to monitor batch-cultivated plant suspension cell cultures in stirred-tank bioreactors and compared the in-line data to conventional off-line measurements. RFIS-based analysis was more rapid and more accurate than conventional biomass determination, and was sensitive to changes in cell viability. The higher resolution of the in-line measurement revealed subtle changes in cell growth which were not accessible using conventional methods. Thus, RFIS is well suited for correlating such changes with intracellular states and product accumulation, providing unique opportunities for employing systems biotechnology and process analytical technology approaches to increase product yield and quality.     

Improvement of recombinant protein production with the human adenovirus/293S expression system using fed-batch strategies

The human adenovirus/293S cell expression system is used for the production of either recombinant protein or adenovirus vectors for use in gene therapy. In this work, the production of protein tyrosine phosphatase (PTP1C) was used as a model for the scale-up of both applications. Maximum specific production of 30 to 45 mug of active protein/10(6) cells was maintained upon infection with adenovirus vectors at cell densities between 2 x 10(6) to 3 x 10(6) cells/mL in a 3.5-L bioreactor. This was achieved by resuspending the culture in fresh medium at infection time. The pH was kept at 7.0 throughout the experiment and, at 24 h postinfection, glucose and essential amino acids were added. Attempts to replace the complete change of medium at the time of infection with nutrient supplementation of the used medium led to lower production levels, suggesting that protein expression was limited not by the absence of a key nutrient but by inhibitory factors. Two potentially inhibitory factors were investigated: lactic acid accumulation and increased osmolarity. Medium acidification such as that which would be brought about by lactic acid accumulation was shown to depress PTP1C production. The lactate molecule itself decreased the cell viability when added in concentrations of 20 mM or more. But the specific productivity was affected at higher lactate concentrations of 40 mM or more. Additions of glucose, amino acids, and NaHCO(3) used to control pH, led to increases in osmolarity. Osmolarities above 400 mOsm lowered cell density. However, specific production was not significantly affected below 500 mOsm. But, at 500 mOsm, PTP1C production peak was shifted from 48 to 72 hpi. Because of the cell loss, this per cell yield increase did not translate into higher volumetric production. When glucose concentrations was kept at 5 mM by fed-batch addition, lactate production and increases in osmolarity were reduced. In shake flasks, this method permitted maximum production with cells resuspended either in fresh or spent medium at infection. This fed-batch process was implemented successfully at the 3.5-L scale. Fed-batch with glucose may provide a means to increase infected-cell density beyond 3 x 10(6) cells/mL.     

Process performance of parallel bioreactors for batch cultivation of Streptomyces tendae

Batch cultivations of the nikkomycin Z producer Streptomyces tendae were performed in three different parallel bioreactor systems (milliliter-scale stirred-tank reactors, shake flasks and shaken microtiter plate) in comparison to a standard liter-scale stirred-tank reactor as reference. Similar dry cell weight concentrations were measured as function of process time in stirred-tank reactors and shake flasks, whereas only poor growth was observed in the shaken microtiter plate. In contrast, the nikkomycin Z production differed significantly between the stirred and shaken bioreactors. The measured product concentrations and product formation kinetics were almost the same in the stirred-tank bioreactors of different scale. Much less nikkomycin Z was formed in the shake flasks and MTP cultivations, most probably due to oxygen limitations. To investigate the non-Newtonian shear-thinning behavior of the culture broth in small-scale bioreactors, a new and simple method was applied to estimate the rheological behavior. The apparent viscosities were found to be very similar in the stirred-tank bioreactors, whereas the apparent viscosity was up to two times increased in the shake flask cultivations due to a lower average shear rate of this reactor system. These data illustrate that different engineering characteristics of parallel bioreactors applied for process development can have major implications for scale-up of bioprocesses with non-Newtonian viscous culture broths.     

Orbital shaker technology for the cultivation of mammalian cells in suspension

For large-scale applications in biotechnology, cultivation of mammalian cells in suspension is an essential prerequisite. Typically, suspension cultures are grown in glass spinner flasks filled to less than 50% of the nominal volume. We propose a superior system for suspension cultures of mammalian cells based on orbital shaker technology. We found that "square-shaped" bottles (square bottles) provide an inexpensive but efficient means to grow HEK-293 EBNA and CHO-DG44 cells to high density. Cultures in agitated 1-L square bottles exceeded the performance of cultures in spinner flasks, reaching densities up to 7 x 10(6) cells/mL for HEK-293 EBNA cells and 5 x 10(6) cells/mL for CHO-DG44 cells in comparison to (2.5-4) x 10(6) cells/mL for cultures of the same cells grown in spinner flasks. For 1-L square bottles, optimal cell growth and viability were observed with a filling volume of 30-40% of the nominal volume and an agitation speed of 130 rpm at a rotational diameter of 2.5 cm. Transient reporter gene expression following gene delivery by calcium phosphate-DNA co-precipitation was the same or slightly better for HEK-293 EBNA cells grown in square bottles as compared to spinner flasks. Reductions in cost, simplified handling, and better performance in cell growth and viability make the agitated square bottle a new and very promising tool for the cultivation of mammalian cells in suspension.     

On-line biomass monitoring of CHO perfusion culture with scanning dielectric spectroscopy

In this work, dielectric spectroscopy was used to monitor two CHO perfusion culture experiments (B14 and B16). The capacitance of the cell suspension was recorded every 20 minutes over an excitation frequency range of 0.2 MHz to 10.0 MHz. A phase plot of the capacitance at a low excitation frequency vs. the value at a higher frequency proved to be an accurate indicator of the major transition points of the culture, i.e., maximum cell viability, end of lactate consumption, point of zero viability. For both experiments, the capacitance signal correlated very well (R(2) >0.98) with viable cell number up to concentrations of 1 x 10(7) cells/mL. Visual observation of the capacitance spectra indicated that changes in the capacitance relative to frequency were related to the cellular morphology. A multivariate model was developed using off-line data that could predict the median cell diameter within a single experiment (B14) with an error of 0.34 microm (2%). Upon extension to a subsequent experiment (B16), the predicted error was 1.18 microm (9%).     

The relationship of plasma ammonia and lactate concentrations to perceived exertion in trained and untrained women

The purpose of this study was to investigate the covariance between perceived exertion (recorded using Borg's category-ratio scale CR-10) and the relative oxygen uptake, and lactate and ammonia concentrations in blood from a peripheral vein. Ratings of perceived exertion (RPE) at 25%, 50%, 75% and 90% maximal oxygen uptake and lactate and ammonia concentrations were compared in well-trained women distance runners (n = 22) and untrained women (n = 10). Ammonia concentrations in peripheral venous blood were significantly correlated with RPE (P less than 0.05), both in the trained and untrained women. Differences between the trained and untrained subjects occurred when the ammonia concentration increased to 148 mumol.l-1 in both groups investigated; similarly, the mean RPE correlated significantly with the lactate concentration (P less than 0.05), both in the trained and untrained women and there was a difference in RPE between groups when lactate concentration in the blood had risen to 4.4 mmol.l-1. It would seem that the correlation of blood ammonia and lactate concentrations with RPE during exercise could be a useful indicator of the development of fatigue.     

Growth study of lactate and ammonia double-resistant clones of HL-60 cells

The possibility that lactate and ammonia accumulation may have less detrimental effect on cell growth than usually admitted is investigated. We report here the isolation of several HL-60 subclones able to proliferate in the presence of 60 mM sodium lactate and 4 mM ammonium chloride, concentrations usually considered to be toxic for cell proliferation. Growth kinetics and final cell densities of these clones in suspension cultures were similar to the HL-60 cell population in control medium as well as in medium containing ammonia and lactate in which control cells were unable to grow. The metabolic pattern of the double-resistant clones revealed that lactate and ammonia formation was inhibited in the presence of lactate and ammonia in the medium, while alanine production and arginine consumption were enhanced irrespective of the medium.     

The effects of microcarrier culture on recombinant CHO cells under biphasic hypothermic culture conditions

A Chinese hamster ovary (CHO) cell line, producing recombinant secreted human placental alkaline phosphatase (SEAP) was investigated under three different culture conditions (suspension cells, cells attached to Cytodex 3 and Cytopore 1 microcarriers) in a biphasic culture mode using a temperature shift to mild hypothermic conditions (33 °C) in a fed-batch bioreactor. The cell viability in both the suspension and the Cytodex 3 cultures was maintained for significantly longer periods under hypothermic conditions than in the single-temperature cultures, leading to higher integrated viable cell densities. For all culture conditions, the specific productivity of SEAP increased after the temperature reduction; the specific productivities of the microcarrier cultures increased approximately threefold while the specific productivity of the suspension culture increased nearly eightfold. The glucose and glutamine consumption rates and lactate and ammonia production rates were significantly lowered after the temperature reduction, as were the yields of lactate from glucose. However, the yield of ammonia from glutamine increased in response to the temperature shift.     

Investigation on the effect of static magnetic field up to 15 mT on the viability and proliferation rate of rat bone marrow stem cells

This investigation was performed to evaluate the influence of the static magnetic field up to 15 mT on the viability and proliferation rate of rat bone marrow stem cells. Cells from passage 5 were trypsinized, and a cell suspension was prepared. The cells were counted and cultured in 25-cm² flasks. They were incubated for 1 d, washed with phosphate-buffered saline, and then exposed with different intensities of static magnetic field (4, 7, and 15 mT) at different exposure times (24, 48, 72, and 96 h). Cells were then washed with phosphate-buffered saline, trypsinized, and a cell suspension was prepared separately from each flask. To investigate the viability and proliferation rates of treated cells, staining with Trypan blue and counting were performed with an optical microscope. The mean number of whole cells and living cells was considered as proliferation and survival rates, respectively. Increasing of intensity and time of static magnetic field exposure decreased the viability percent and proliferation rate in treated groups compared with corresponded control. However, reduced cell viability, where this occurred, is exclusively due to apoptosis since necrosis is never observed by others.     

Metabolism of hybridoma cells and antibody secretion at high cell densities in dialysis tubing.

The experimental setup, consisting of a bundle of dialysis tubing 2.5 mm in diameter [10-15 kD cutoff, mean pore size 25 A, 20 microns (dry) and 40 microns (wet) wall thickness] inserted into a 1-l glass bioreactor supplied with oxygen and pH electrodes, a porous gas distributor, a sampling tube, and a holder for the eight pieces of dialysis tubing, was developed to investigate the properties and the microenvironment of hybridoma cells enclosed in the tubing during their batch cultivation. The concentrations of low-molecular-weight medium components were the same inside and outside the tubing, and it was possible to control the microenvironment of the cells in the tubing easily. The cell damage caused by mechanical stress was less in the dialysis tubing than in stirred spinner flasks. The influence of the initial cell density in the range from 4 X 10(5) to 1 X 10(8) cells ml-1 and the cultivation time were evaluated according to the total and viable cell concentrations and the cell/cell fragment size distributions. Furthermore, the cell membrane properties, glucose consumption rate, lactate, ammonia and lipid storage material, and the monoclonal antibody production rates as well as intracellular enzyme activities in the culture medium were measured and compared to those in reference cultures in spinner flasks with the same inoculum at low initial cell densities. In dialysis tubing in a concentration range of 5 X 10(6) to 10(8) cells ml-1, the total and viable concentrations of cells remained the same during cultivation.(ABSTRACT TRUNCATED AT 250 WORDS)     

Role of eicosanoids, inositol phosphates and extracellular Ca2+ in cell-volume regulation of rat liver

1. In isolated perfused rat liver, the time-course of volume-regulatory K+ efflux following exposure to hypoosmolar perfusate resembled the leukotriene-C4-induced K+ efflux in normotonic perfusion. Omission of Ca2+ from the perfusion fluid had no effect on volume-regulatory K+ efflux, but abolished completely the leukotriene-C4-induced K+ efflux. 2. Volume-regulatory K+ fluxes following hypoosmolar exposure (225 mOsmol l-1) and subsequent reexposure to normotonic media (305 mOsmol l-1) were not significantly affected by the cyclooxygenase inhibitors indomethacin (5 mumol l-1) or ibuprofen (50 mumol l-1), the leukotriene D4/C4-receptor antagonist 1-[2-hydroxy-3-propyl-4-[4-(1H-tetrazol-5-yl)butoxy]phenyl]etha none (YL 171883, 50 microM), the lipoxygenase inhibitor nordihydroguaiaretic acid (20 microM), the phospholipase-A2 inhibitor bromophenacyl bromide (50 microM) or the thromboxane-receptor antagonist 4-[2-(benzenesulfonamido)ethyl]-phenoxyacetic acid (BM 13.177, 20 microM). Also the effects of hypoosmotic cell swelling on lactate, pyruvate and glucose balance across the liver remained largely unaffected in presence of these inhibitors. Neither exposure of perfused rat liver to hypoosmolar (225 mOsmol l-1) nor to hyperosmolar (385 mOsmol l-1) perfusion media affected hepatic prostaglandin-D2 release. 3. When livers were 3H-labeled in vivo by an intraperitoneal injection of myo-[2-3H]inositol about 16 h prior to the perfusion experiment, cell swelling due to lowering the perfusate osmolarity from 305 mOsmol l-1 to 225 mOsmol l-1 led to about a threefold stimulation of [3H]inositol release. The maximum of hypotonicity-induced [3H]inositol release preceded maximal volume-regulatory K+ efflux by about 30 s, but came after the maximum of water shift into the cells. Hypotonicity-induced [3H]inositol release was largely prevented in presence of Li+ (10 mM), but simultaneously inositol monophosphate accumulated inside the liver within 10 min and a small, but significant increase of inositol trisphosphate 1 min after onset of hypoosmolar exposure was detectable. No stimulation of [3H]inositol release was observed during cell shrinkage by switching the perfusate osmolarity from 225 mOsmol l-1 to 305 mOsmol l-1 or from 305 mOsmol l-1 to 385 mOsmol l-1. No stimulation of [3H]inositol release was observed upon swelling of preshrunken livers by lowering the osmolarity from 385 mOsmol l-1 to 305 mOsmol l-1, although the volume-regulatory K+ efflux under these conditions was almost identical to that observed after lowering the osmolarity from 305 mOsmol l-1 to 225 mOsmol l-1. 4.(ABSTRACT TRUNCATED AT 400 WORDS)     

Influence of inoculum age on hybridoma culture kinetics

To determine the influence of the inoculum age on the kinetics of hybridoma growth and metabolism, spinner flasks have been inoculated with cells previously propagated in T flasks for 43, 52, 62 and 71 hr respectively. Increasing the age of the inoculum is found to result in a longer lag phase, in a lower maximum specific growth rate and in a reduced maximal cell density. During the growth phase specific rates of glucose and glutamine uptake and of ammonia and lactate production are similar. However, with the older inoculum, much higher metabolic activities are observed during the lag phase. The production of antibodies is delayed with increasing inoculum age, but the final antibody concentrations are similar, which indicates a higher specific antibody production rate when inoculating with older cells.     

Influence of medium composition on the cephalosporin C production with a highly productive strain Cephalosporium acremonium.

Cephalosporin production by a highly productive Cephalosporium acremonium strain was carried out and optimized by fed-batch operation in a 40 l stirred tank reactor using a complex medium containing 30-120 g l-1 peanut flour. The concentrations of cephalosporin C (CPC) and its precursors: penicillin N (PEN N), deacetoxy cephalosporin C (DAOC), and deacetyl cephalosporin C (DAC) were monitored with an on-line HPLC. The concentrations of amino acids valine (VAL), cysteine (CYS), alpha-amino adipic acid (alpha-AAA), the dipeptide alpha-amino-adipyl-cysteine (AC), and the tripeptide alpha-amino-adipyl-cysteinyl-valine (ACV), were determined off-line by HPLC. The RNA content and dry weight of the sediment as well as the oxygen transfer rate (OTR) and the CO2 production rate (CPR) were used to calculate the cell mass concentration (X). The influences of peanut flour (PF) and the on-line monitored and controlled medium components: glucose (GLU), phosphate, methionine (MET) as well as the dissolved oxygen (DOC) on the cell growth, the product formation, and the pathway of cephalosporin C biosynthesis were investigated and evaluated. When the glucose fed-batch cycle was optimized and oxygen transfer limitation was avoided (DOC greater than 20% of the saturation value), high process performance (103.5 g l-1 X, 11.84 g l-1 CPC, a maximum CPC productivity of 118 mg l-1 h-1, and the whole concentration of the beta-lactam antibiotics CPC, DAC, DAOC, PEN N 17.34 g l-1) was achieved by using 100 g l-1 PF in the medium with the optimum concentration of phosphate (260-270 mg l-1) and a low glucose concentration (less than 0.5 g l-1). The cultivations with different medium concentrations demonstrated that the product formation was directly proportional to the cell mass concentration. On the average, the cell mass-based yield coefficient of CPC: YCPC/X amounted to 0.115 g CPC per g cell mass.     

On-line determination of glucose and lactate concentrations in animal cell culture based on fibre optic detection of oxygen in flow-injection analysis.

A flow-injection analysis (FIA) system based on fibre optic detection of oxygen consumption using immobilized glucose oxidase (GOD) and lactate oxidase (LOD) is described for the on-line monitoring of glucose and lactate concentrations in animal cell cultures. The consumption of oxygen was determined via dynamic quenching by molecular oxygen of the fluorescence of an indicator. GOD and LOD were immobilized on controlled pore glass (CPG) in enzyme reactors which were directly linked to a specially designed fibre optic flow-through cell covering the oxygen optrode. The system is linear for 0-30 mM glucose, with an r.s.d. of 5% at 30 mM (five measurements) and for 0-30 mM lactate, with an r.s.d. of 5% at 30 mM (five measurements). The enzyme reactors used were stable for more than 4 weeks in continuous operation, and it was possible to analyse up to 20 samples per hour. The system has been successfully applied to the on-line monitoring of glucose and lactate concentrations of an animal cell culture designed for the production of recombinant human antithrombine III (AT-III). Results of the on-line measurement obtained by the FIA system were compared with the off-line results obtained by a glucose and lactate analyser from Yellow Springs Instrument Company (YSI).