Atmospheric stability in cell culture vessels

Summary We have investigated the atmospheric stability in polystyrene and glass cell culture vessels by measuring the dissolved O₂ and CO₂ in the media of both seeded and unseeded culture vessels incubated at 37°C. There was no diffusion of either O₂ or CO₂ through glass vessels. At low partial pressures of oxygen (P_{O 2}), oxygen diffused into the polystyrene flasks at a rate of 1 to 2 mm Hg per 24 hr, and at high P_{O 2}, oxygen diffused slowly out of polystyrene flasks. CO₂ diffused out of polystyrene flasks with a half-time of 260 hr resulting in a considerable elevation in pH. In seeded polystyrene flasks with the P_{O 2} ⩽ room air, cellular oxygen consumption was masked by the inward diffusion of oxygen. In addition, the fall in pH due to metabolic CO₂ and organic acid production during cell growth in polystyrene flasks was buffered by the diffusion of CO₂ out of the vessels. Presented, in part, by Dr. Arthur Balin in partial fulfillment of the requirements for the Ph.D. This work was supported by USPHS grants AG-00378 from the National Institute of Aging and CA-14345 from the National Cancer Institute and NR 202-005 from the Office of Naval Research. A.K.B. is a trainee of the Medical Scientist Training Program, National Institutes of Health (GM 02046).     

Density-dependent effects of oxygen on the growth of mammalian fibroblasts in culture

Various concentrations of oxygen were used to determine the optimum culture medium PO2 for survival and proliferation of attached human and mouse fibroblasts grown from different inoculum sizes. When T-15 flasks were seeded with less than or equal to 2 X 10(4) cells (less than or equal to 1.3 X 10(3) cells/cm2), the highest plating efficiencies and cell yields were obtained with a culture medium PO2 of 40-60 mm Hg. At higher inoculum sizes (10(5) cells per T-15) used routinely for mass cultured, no difference in cell yield or glycolytic activity was observed between cultures gassed with atmospheric, i.e., 18% O2 (growth medium PO2 approximately equal to 125-135 mm Hg) and those gassed with 1% O2 (growth medium PO2 approximately euqal to 40-60 mm Hg). The enhanced clonal growth observed at the latter PO2 results from an increased proliferation rate rather than more efficient attachment and survival of inoculated cells. Glucose uptake and lactic acid accumulation were increased in sparse cultures sparged with 1% O2. A slight extension of lifespan was observed in WI-38 cells serially subcultured with a gas phase of 1% O2.     

Limitations to oxygen diffusion and equilibration in in vitro cell exposure systems in hyperoxia and hypoxia

Exposure of cultured cells to changing gaseous environments is used as a model for understanding both the immediate and long-term effects of such exposures on lung cells in vivo. We conducted experiments with polystyrene tissue culture flasks and plates to determine the time course of changes in oxygen concentration occurring under in vitro conditions. Only a few minutes were required for the concentration of oxygen in the environmental chamber to reach equilibrium with that of the flushing gas. However, >3 h were required for the oxygen content in the medium in the tissue culture flasks and plates to achieve equilibrium. The low solubility of oxygen in aqueous solutions and the limited diffusion of oxygen through a boundary layer of gas above the medium are the major barriers to rapid oxygen transport into the culture medium. The delay in achieving the desired PO(2) within the culture medium limits the temporal precision of any assessment of the correlation of cellular events with the concentration of oxygen to which those cells are exposed.     

Adsorptive loss of secreted recombinant proteins in transgenic rice cell suspension cultures

Adsorptive loss of human cytotoxic T-lymphocyte antigen 4-immunoglobulin (hCTLA4Ig) in transgenic rice cell suspension cultures was investigated using glass flasks, plastic flasks, disposable vessels, and stainless steel vessels. When hCTLA4Ig was added to the glass flasks containing sterile AA medium, a rapid decrease in the concentration of hCTLA4Ig, independent on pH, was observed resulting in more than 90% of the protein loss within 1 h due to the surface adsorption. When the same experiments were performed on four different types of culture equipments mentioned above, the lowest adsorption level was observed in the plastic flasks and the highest level was observed in the glass flasks. The use of the plastic flasks retarded the adsorptive loss of hCTLA4Ig at the early stage of the protein production. There was a significant increase in the production of hCTLA4Ig when the flasks were coated with bovine serum albumin. However, the spike test of purified hCTLA4Ig at two different concentrations of 15 and 100 mg L⁻¹ in 500-mL spinner flasks confirmed that the amount of hCTLA4Ig adsorbed was dependent on the surface area of the flasks but not on the concentrations. In conclusion, although the protein adsorption affected the total amount of the protein yielded to some extent, it could be regarded as a minor factor in transgenic plant cell cultures with higher titer.     

An investigation of the nature of Bohr,Root, and haldane effects inOctopus dofleini hemocyanin

1. The pH dependence of Octopus dofleini hemocyanin oxygenation is so great that below pH 7.0 the molecule does not become fully oxygenated, even in pure O2 at 1 atm pressure. However, the curves describing percent oxygenation as a function of PO2 appear to be gradually increasing in oxygen saturation, rather than leveling out at less than full saturation. Hill plots indicate that at pH 6.6 and below the molecule is stabilized in its low affinity conformation. Thus, the low saturation of this hemocyanin in air is due to the very large Bohr shift, and not to the disabling of one or more functionally distinct O2 binding sites on the native molecule. 2. Experiments in which pH was monitored continuously while oxygenation was manipulated in the presence of CO2 provide no evidence of O2 linked binding of CO2. While CO2 does influence O2 affinity independently of pH, its effect may be due to high levels of HCO3- and CO3-, rather than molecular CO2, and it may entail a lowering of the activities of the allosteric effectors Mg2+ and Ca2+.     

Ethylene from alcohol lamps and natural gas burners: Effects on cotton ovules cultured in vitro

Summary In a transfer hood having positive pressure via flow of filtered air, momentary flaming of flask mouths via an alcohol lamp or natural gas burner introduced variable and often large amounts of ethylene into these culture vessels. Amounts of ethylene introduced depended upon where flask mouths were placed within the flame. Most ethylene diffused out of flasks within 2 hr if adequate fresh air exchange was provided, permitting cotton ovules to respond to hormones in ways reported in previous literature. However, it was concluded that flask-flaming could occasionally account for some variability in hormonal responses of cultured cotton ovules. Specifically, ethylene (assumed to be the most abundant and harmful substance admitted to the flasks via flaming) caused excessive ovular callus formation in combination with GA₃ and decreased the percentage of ovules forming fibers in response to IAA. This work was supported by the National Science Foundation Grant PCM 75-03944.     

Estimating cell specific oxygen uptake and carbon dioxide production rates for mammalian cells in perfusion culture

We present robust methods for online estimation of cell specific oxygen uptake and carbon dioxide production rates (q(O2) and q(CO2), respectively) during perfusion cultivation of mammalian cells. Perfusion system gas and liquid phase mass balance expressions for oxygen and carbon dioxide were used to estimate q(O2), q(CO2) and the respiratory quotient (RQ) for Chinese hamster ovary (CHO) cells in perfusion culture over 12 steady states with varying dissolved oxygen (DO), pH, and temperature set points. Under standard conditions (DO = 50%, pH = 6.8, T = 36.5°C), q(O2) and q(CO2) ranges were 5.14-5.77 and 5.31-6.36 pmol/cell day, respectively, resulting in RQ values of 0.98-1.14. Changes to DO had a slight reducing effect on respiration rates with q(O2) and q(CO2) values of 4.64 and 5.47, respectively, at DO = 20% and 4.57 and 5.12 at DO = 100%. Respiration rates were lower at low pH with q(O2) and q(CO2) values of 4.07 and 4.15 pmol/cell day at pH = 6.6 and 4.98 and 5.36 pmol/cell day at pH = 7. Temperature also impacted respiration rates with respective q(O2) and q(CO2) values of 3.97 and 4.02 pmol/cell day at 30.5°C and 5.53 and 6.25 pmol/cell day at 37.5°C. Despite these changes in q(O2) and q(CO2) values, the RQ values in this study ranged from 0.98 to 1.23 suggesting that RQ was close to unity. Real-time q(O2) and q(CO2) estimates obtained using the approach presented in this study provide additional quantitative information on cell physiology both during bioprocess development and commercial biotherapeutic manufacturing.     

A completely noninvasive method of dissolved oxygen monitoring in disposable small‐scale cell culture vessels based on diffusion through permeable vessel walls

Disposable cell culture vessels are extensively used at small scales for process optimization and validation, but they lack monitoring capabilities. Optical sensors that can be easily adapted for use in small‐scale vessels are commercially available for pH, dissolved oxygen (DO), and dissolved carbon dioxide (DCO₂). However, their use has been limited due to the contamination and compatibility issues. We have developed a novel solution to these problems for DO monitoring. Oxygen diffusion through permeable vessel wall can be exploited for noninvasive monitoring. An optical oxygen sensor can be placed outside the oxygen permeable vessel wall thereby allowing oxygen diffusing through the vessel wall to be detected by the sensor. This way the sensor stays separate from the cell culture and there are no concerns about contaminants or leachants. Here we implement this method for two cell culture devices: polystyrene‐made T‐75 tissue culture flask and fluorinated ethylene propylene (FEP)‐made Vuelife^® cell culture bag. Additionally, mammalian and microbial cell cultures were performed in Vuelife^® cell culture bags, proving that a sensor placed outside can be used to track changes in cell cultures. This approach toward noninvasive monitoring will help in integrating cell culture vessels with sensors in a seamless manner. © 2013 American Institute of Chemical Engineers Biotechnol. Prog., 30:172–177, 2014     

Temperature effects on oxygen affinity of human fetal blood

In an effort to understand the effects of temperature changes on fetal oxygenation, the temperature effects were measured on oxygen affinity of whole blood from term human fetuses. The blood obtained was tonometered at delivery in two flasks gassed with 95% N2 (+ 5% CO2 or 20.9% + 5% CO2, and mixed aliquots from each flask in different proportions to obtain samples for analysis of PO2 and percent saturation. The oxyhaemoglobin dissociation curve was constructed and P50 determined at two or three different temperatures for each batch of blood. As temperature increased from 30 to 41 degrees C, human fetal blood bound O2 less avidly, the temperature coefficient for changes in P50 being 0.0255 per degree C. This temperature effect was similar to that in adult blood, although at any temperature O2 affinity of fetal blood was greater than that of the adult. Placental oxygen exchange could be significantly affected by changes in temperature such as occur during hypo- or hyperthermia, as with maternal exercise.     

Accurate control of oxygen level in cells during culture on silicone rubber membranes with application to stem cell differentiation

Oxygen level in mammalian cell culture is often controlled by placing culture vessels in humidified incubators with a defined gas phase partial pressure of oxygen (pO_2gas). Because the cells are consuming oxygen supplied by diffusion, a difference between pO_2gas and that experienced by the cells (pO_2cell) arises, which is maximal when cells are cultured in vessels with little or no oxygen permeability. Here, we demonstrate theoretically that highly oxygen‐permeable silicone rubber membranes can be used to control pO_2cell during culture of cells in monolayers and aggregates much more accurately and can achieve more rapid transient response following a disturbance than on polystyrene and fluorinated ethylene‐propylene copolymer membranes. Cell attachment on silicone rubber was achieved by physical adsorption of fibronectin or Matrigel. We use these membranes for the differentiation of mouse embryonic stem cells to cardiomyocytes and compare the results with culture on polystyrene or on silicone rubber on top of polystyrene. The fraction of cells that are cardiomyocyte‐like increases with decreasing pO₂ only when using oxygen‐permeable silicone membrane‐based dishs, which contract on silicone rubber but not polystyrene. The high permeability of silicone rubber results in pO_2cell being equal to pO_2gas at the tissue‐membrane interface. This, together with geometric information from histological sections, facilitates development of a model from which the pO₂ distribution within the resulting aggregates is computed. Silicone rubber membranes have significant advantages over polystyrene in controlling pO_2cell, and these results suggest they are a valuable tool for investigating pO₂ effects in many applications, such as stem cell differentiation. © 2009 American Institute of Chemical Engineers Biotechnol. Prog., 2010     

Noninvasive oxygen measurements and mass transfer considerations in tissue culture flasks

Murine hybridomas were cultivated in tissue culture flasks. Dissolved oxygen tensions in the gas and liquid phases during cell growth were monitored. Oxygen levels were measured noninvasively by interrogating an oxygen-sensitive patch mounted on the interior surface of the tissue culture flask with an optrode from outside the tissue culture flask. Readings were made in tissue culture flasks with caps both cracked open and completely closed. Although the oxygen in the gas phase remained near atmospheric oxygen levels in both flasks, over time the liquid-phase oxygen tension at the bottom of the flasks reached zero during cell growth in both the open and closed tissue culture flasks. These results suggest that the widespread practice of cracking open tissue culture flask caps during cell growth with a view to supplying adequate oxygen to cells is ineffective and probably unnecessary.The mass transfer characteristics of the tissue culture flask were also studied. The dominant resistance to oxygen mass transfer to the sensor and the cells was through the liquid media. The mass transfer rates through the liquid layer under standard laboratory conditions were found to be greater than those predicted by diffusion alone. This suggests that mixing at a microscale occurs. Volumetric and specific oxygen consumption rates were also calculated from the sensor data. These consumption rates were comparable with values published elsewhere. (c) 1996 John Wiley & Sons, Inc.     

Microcirculatory hematocrit and blood flow

Direct measurements from many laboratories indicate that the oxygen tension in skeletal muscle is significantly less than in the large veins draining these tissues. Harris (1986) has proposed that because of the parallel anatomic arrangement of large arterioles and venules in skeletal muscle, a counter-current exchange between these vessels can occur. He theorized that diffusion of O2 between arteriole and venule would lower the PO2 in the blood as it enters capillaries and result in a decreased tissue PO2 and an increase in large vein PO2. Calculations (Appendix) show that the amount of O2 transferred between arteriole and venule is inadequate to account for this difference in PO2 between tissue and veins due to the small surface area that is involved. It is well documented that the microcirculatory hematocrit ranges between 20 and 50% of that in the supply vessels. The reduced hematocrit lowers the oxygen content in these vessels and results in a low oxygen tension in the surrounding tissue. True arteriovenous shunts are not present in most skeletal muscles, but 15-20% of the microvessels represent thoroughfare or preferential flow channels. It is suggested that these vessels contain a greater than normal hematocrit to account for a conservation of red cell mass across the microcirculation. Furthermore, it is shown that the hematocrit in the preferential flow channels is an inverse function of the flow rate for any level of the microcirculatory hematocrit. The increased hematocrit raises the flow resistance in these vessels which reduces flow further and represents a positive feedback condition which may contribute to the intermittent and uneven flow patterns which are present within the microcirculation.(ABSTRACT TRUNCATED AT 250 WORDS)     

Effect of mild carboxy-hemoglobin on exercising skeletal muscle: intravascular and intracellular evidence

We studied muscle blood flow, muscle oxygen uptake (VO(2)), net muscle CO uptake, Mb saturation, and intracellular bioenergetics during incremental single leg knee-extensor exercise in five healthy young subjects in conditions of normoxia, hypoxia (H; 11% O(2)), normoxia + CO (CO(norm)), and 100% O(2) + CO (CO(hyper)). Maximum work rates and maximal oxygen uptake (VO(2 max)) were equally reduced by approximately 14% in H, CO(norm), and CO(hyper). The reduction in arterial oxygen content (Ca(O(2))) (approximately 20%) resulted in an elevated blood flow (Q) in the CO and H trials. Net muscle CO uptake was attenuated in the CO trials. Suprasystolic cuff measurements of the deoxy-Mb signal were not different in terms of the rate of signal rise or maximum signal attained with and without CO. At maximal exercise, calculated mean capillary PO(2) was most reduced in H and resulted in the lowest Mb-associated PO(2). Reductions in ATP, PCr, and pH during H, CO(norm), and CO(hyper) occurred earlier during progressive exercise than in normoxia. Thus the effects of reduced Ca(O(2)) due to mild CO poisoning are similar to H.     

Growth kinetics of vitis vinifera cell suspension cultures: I. Shake flask cultures

Vitis vinifera cell suspension cultures carried out in shake flasks were closely examined for biomass growth and cell division in relation to carbohydrate, NH(4), NO(3)PO(4), and dissolved oxygen (DO)consumption. After inoculation, the oxygen uptake rate of the cultures measured on-tine was observed to increase continuously to a maximum value of 3.8 mmol O(2)L(-1)h(-1) at day 7 when cell division ceased and dissolved oxygen reached its lowest level of 17% air saturation. During this first phase of growth, the specific oxygen uptake rate remained constant at approximately 0.6 mmol 02 O(2) g(-1) dw h(-1)or approximately 2.2 mumol O(2), (10(6) cells)(-1) h(-1) whereas dry biomass concentration increased exponentially from 1.5 to 6.0 g dw L(-1). Thereafter, dry biomass concentration increased linearly to approximately 14 g dw L(-1) at day 14 following nitrate and carbohydrate uptake. During this second phase of growth, the biomass wet-to-dry weight ratio was found to increase in an inverse relationship with the estimated osmotic pressure of the culture medium. This corresponded to inflection points in the dry and wet biomass concentration and packed cell volume curves. Furthermore, growth and nutrient uptake results suggest that extracellular ammonium or phosphate ion availability may limit cell division. These findings indicate that cell division and biomass production of plant cell cultures may not always be completely associated, which suggests important new avenues to improve their productivity. (c) 1995 John Wiley & Sons, Inc.     

Fine needle aspiration as a tool to establish primary human breast cancer cultures in vitro

OBJECTIVE: To verify the potential role of fine needle aspiration (FNA) cytology in obtaining malignant cells from primary breast cancer for establishment of a primary breast cancer cell line. STUDY DESIGN: In four patients with primary breast cancer subjected to FNA for diagnostic purposes, we attempted to establish primary cultures. We successfully obtained one primary cell line, originating in micropapillary invasive breast carcinoma. FNA material obtained under sterile conditions was centrifuged, and the cell pellet was washed with Dulbecco Modified Medium. The resulting suspension was seeded in 25-cm2 tissue culture flasks. The flasks were maintained with released caps in a 37 degrees C incubator with a humidified atmosphere of 5% CO2 in air. After one week, cells attached to the bottom of the flasks and began proliferating. When a culture became confluent, the cells were treated with 0.05% trypsin/0.02% EDTA in a PBS solution and subcultured. The flasks were observed daily with an inverted microscope, and culture passages were performed weekly. RESULTS: The cell line obtained was named I2FPRW and exhibited morphologic and immunohistochemical features of epithelial cells of mammary origin. The cells were positive for cytokeratins (AE1/AE3 and CK 7), EMA and c-erbB-2. At this writing, this cell line was in the 15th passage of subculturing in the flasks with 10% FBS. CONCLUSION: In the present study we demonstrated that is possible to establish a breast cancer cell line from material obtained by FNA cytology. FNA seems to be a valuable method of obtaining malignant cells from breast cancer able to grow free of fibroblasts in cell cultures.     

Optical sensor enabled rocking T-flasks as novel upstream bioprocessing tools

During the past decade, novel disposable cell culture vessels (generally referred to as Process Scouting Devices or PSDs) have become increasingly popular for laboratory scale studies and seed culture generation. However, the lack of engineering characterization and online monitoring tools for PSDs makes it difficult to elucidate their oxygen transfer capabilities. In this study, a mass transfer characterization (k_La) of sensor enabled static and rocking T‐flasks is presented and compared with other non‐instrumented PSDs such as CultiFlask 50®, spinner flasks, and SuperSpinner D 1000®. We have also developed a mass transfer empirical correlation that accounts for the contribution of convection and diffusion to the volumetric mass transfer coefficient (k_La) in rocking T‐flasks. We also carried out a scale‐down study at matched k_La between a rocking T75‐flask and a 10 L (2 L filling volume) wave bioreactor (Cultibag®) and we observed similar DO and pH profiles as well as maximum cell density and protein titer. However, in this scale‐down study, we also observed a negative correlation between cell growth and protein productivity between the rocking T‐flask and the wave bioreactor. We hypothesize that this negative correlation can be due to hydrodynamic stress difference between the rocking T‐flask and the Cultibag. As both cell culture devices share key similarities such as type of agitation (i.e., rocking), oxygen transfer capabilities (i.e., k_La) and disposability, we argue that rocking T‐flasks can be readily integrated with wave bioreactors, making the transition from research‐scale to manufacturing‐scale a seamless process. Biotechnol. Bioeng. 2012;109: 2295–2305. © 2012 Wiley Periodicals, Inc.     

Real-time monitoring of shake flask fermentation and off gas using triple disposable noninvasive optical sensors

Bioprocess development is a data-driven process requiring a large number of experiments to be conducted under varying conditions. Small-scale upstream bioprocess development is often performed in shake flasks because they are inexpensive and can be operated in parallel. However, shake flasks are often not equipped to accurately monitor critical process parameters such as pH, dissolved oxygen, and CO2 concentrations. Therefore, there is no definitive information on oxygen supply of growing cells, CO2 formation, and pH changes. Here we describe several shake flask fermentations where all three parameters are monitored by disposable noninvasive optical sensors. The sensitive element of these sensors is a thin, luminescent patch affixed inside the flask. Small electronic devices for excitation and fluorescence detection are positioned outside the shake flask for noninvasive monitoring. By measuring the process parameters throughout the course of the E. coli fermentations, we obtain information that is not routinely available in shake flask fermentations. For example, for cultures with only a few millimeters liquid depth, oxygen limitation can occur at relatively low agitation speeds. Under certain conditions oscillations in dissolved oxygen can occur. An increase in shaker speed and a decrease in culture volume can increase the oxygen availability and reduce the duration of oxygen limitation.     

Loss of secreted antibody from transgenic plant tissue cultures due to surface adsorption

The role of surface adsorption in the disappearance of secreted foreign proteins from the medium of transgenic plant cell and organ cultures was investigated. When mouse monoclonal IgG1 was added to sterile plant culture media in glass shake flasks, the antibody concentration declined rapidly demonstrating that antibody was labile in the plant culture environment even in the absence of biomass and proteases. Elution of bound antibody from the surfaces of the flasks indicated that adsorption had contributed to the observed loss of antibody from solution. Antibody retention in sterile plant culture media was improved significantly when protein-resistant polymer coatings were applied to the glass vessels containing the antibody solutions. Pluronic F127 applied at a concentration of 1 mg mL(-1) to a primary dimethyldichlorosilane layer on glass yielded the best results in sterile Murashige and Skoog medium. When this coating was used in shake flasks for culture of transgenic tobacco hairy roots, there was a significant improvement in the accumulation of secreted recombinant antibody in the medium consistent with a reduction in antibody adsorption. Medium antibody levels eventually declined, however, as medium protease concentrations rose rapidly towards the end of the culture period. This work demonstrates that surface adsorption reduces the medium antibody titre observed in transgenic plant tissue cultures.     

Photosynthetic activities of spinach leaf protoplasts

Photosynthetic activities of protoplasts isolated from spinach leaf (Spinacia oleracea L.) were investigated. The protoplasts were stable up to 9 hr, without loss of the original activity of CO(2) fixation (33-75 mumoles CO(2)/mg Chl.hr) and light-dependent O(2) evolution (33-40 mumoles O(2)/mg Chl.hr), when stored in 0.8 m mannitol-0.05 m N-tris (hydroxymethyl)-methylglycine-NaOH buffer, pH 7, at 4 C in dark. The optimum pH of 8.5 for CO(2) fixation reaction carried out in the present experimental condition employed is about the same as that reported for intact spinach chloroplasts. The CO(2) concentration for half-maximal rate of CO(2) fixation by protoplasts. "Km (CO(2))," were determined to be 19.8 mum (pH 7) and 42 mum (pH 8.5) and are similar to those observed for intact spinach chloroplasts. Protoplasts showed postillumination CO(2) fixation. Over-all results indicate that spinach protoplasts are as active as the intact plant leaf tissues in their photosynthetic activities.     

A shaken disposable bioreactor system for controlled insect cell cultivations at milliliter‐scale

While wave‐mixed and stirred bag bioreactors are common devices for rapid, safe insect cell culture‐based production at liter‐scale, orbitally shaken disposable flasks are mainly used for screening studies at milliliter‐scale. In contrast to the two aforementioned bag bioreactor types, which can be operated with standard or disposable sensors, shaker flasks have not been instrumented until recently. The combination of 250 mL disposable shake flasks with PreSens's Shake Flask Reader enables both pH and dissolved oxygen to be measured, as well as allowing characterization of oxygen mass transfer. Volumetric oxygen transfer coefficients (k_La‐values) for PreSens 250 mL disposable shake flasks, which were determined for the first time in insect cell culture medium at varying culture volumes and shaker frequencies, ranged between 4.4 and 37.9/h. Moreover, it was demonstrated that online monitoring of dissolved oxygen in shake flasks is relevant for limitation‐free growth of insect cells up to high cell densities in batch mode (1.6×10⁷ cells/mL) and for the efficient expression of an intracellular model protein.