Spinner Vessels Research Articles

Sequential adaptation to serum-free medium for Vero cells cultivation on ultraviolet/ozone (UVO) treated microcarrier

The adoption of serum-free media (SFM) in cell culture has gained prominence as an alternative to serum-supplemented media (SSM) owing to concerns regarding serum variability and quality assurance. Vero cells, widely utilized in viral vaccine production for their susceptibility to various viruses, were the focus of this study. Our primary objective was to adapt Vero cells from SSM to SFM and subsequently upscale the culture from T-flasks to spinner vessels using ultraviolet/ozone (UVO) treated polystyrene (PS) and polycaprolactone (PCL) microcarriers. Cell counting was conducted via haemocytometer and inverted phase microscopy. The results indicated that SFM-adapted Vero cells achieved higher maximum cell concentrations compared to those cultured in SSM, along with a shorter doubling time. However, during cultivation in spinner vessels, Vero cells exhibited lower maximum cell concentrations compared to T-flask cultures, attributed to factors such as cell inoculum size and microcarrier hydrophilicity. This study highlights the successful adaptation of Vero cells to SFM and the potential benefits in terms of cell density and growth kinetics. Furthermore, it sheds light on the challenges encountered during culture upscale, offering valuable insights for optimizing future large-scale production processes. The findings contribute to the advancement of serum-free cell culture systems and their applicability in the production of viral vaccines.

Preparing for cell culture scale-out: establishing parity of bioreactor- and flask-expanded mesenchymal stromal cell cultures

BackgroundCell-based therapies have the potential to become treatment options for many diseases, but efficient scale-out of these therapies has proven to be a major hurdle. Bioreactors can be used to overcome this hurdle, but changing the culture method can introduce unwanted changes to the cell product. Therefore, it is important to establish parity between products generated using traditional methods versus those generated using a bioreactor.MethodsMesenchymal stromal cells (MSCs) are cultured in parallel using either traditional culture flasks, spinner vessels or a new bioreactor system. To investigate parity between the cells obtained from different methods, harvested cells are compared in terms of yield, phenotype and functionality.ResultsBioreactor-based expansion yielded high cell numbers (222–510 million cells). Highest cell expansion was observed upon culture in flasks [average 5.0 population doublings (PDL)], followed by bioreactor (4.0 PDL) and spinner flasks (3.3 PDL). Flow cytometry confirmed MSC identity (CD73+, CD90+ and CD105+) and lack of contaminating hematopoietic cell populations. Cultured MSCs did not display genetic aberrations and no difference in differentiation and immunomodulatory capacity was observed between culture conditions. The response to IFNγ stimulation was similar for cells obtained from all culture conditions, as was the capacity to inhibit T cell proliferation.ConclusionsThe new bioreactor technology can be used to culture large amounts of cells with characteristics equivalent to those cultured using traditional, flask based, methods.

Alginate Encapsulation as a Novel Strategy for the Cryopreservation of Neurospheres

Primary cultures of brain cell neurospheres are valuable in vitro models for neurotoxicology and brain cell research. Such applications would greatly benefit from the development of efficient cryopreservation protocols that assure the availability of viable and genetically stable stocks of functional neurospheres. In this work we aimed at developing an integrated strategy allowing for long-term culture and cryopreservation of brain cell neurospheres with high viability and reduced recovery time postthawing. Microencapsulation in clinical-grade, ultrahigh viscous, highly purified alginate uniformly cross-linked with Ba(2+) was evaluated as the main strategy to avoid the commonly observed loss of cell-cell and cell-matrix interactions with consequent aggregate's fragmentation and decrease in cell viability that occurs postthawing. Brain cells isolated from 16-day-old fetal rats were cultured in spinner vessels as neurospheres, encapsulated at the 5th day of culture, and cryopreserved at day 19. Culture characterization and assessment of postthawing recovery, concerning cell metabolism, aggregate's cell type composition, and neuron-astrocyte interactions were performed through analysis of membrane integrity, metabolic activity assays, and immunohistochemistry. Our results show that the encapsulation process does not affect cell viability's central metabolism; neither cell differentiation nor cell extensions into cell networks are usually observed between neurons and astrocytes within the neurosphere structure. Neurosphere encapsulation resulted in reduced recovery time postthawing and significantly less fragmentation. Further, the use of serum-free CryoStor™ solution provided further protection for both nonencapsulated and encapsulated aggregates compared with serum-supplemented culture medium as the cryopreservation medium.

Extending Hepatocyte Functionality for Drug-Testing Applications Using High-Viscosity Alginate–Encapsulated Three-Dimensional Cultures in Bioreactors

The maintenance of differentiated hepatocyte phenotype in vitro depends on several factors-in particular, on extracellular matrix interactions, for example, with three-dimensional (3D) matrices. Alginate hydrogel provides the cells with a good extracellular matrix due to the formation of a massive capsule with semi-permeable properties that allows for diffusion of the medium components into the cells as well as efficient waste product elimination. Simultaneously, alginate protects the cells from shear stress caused by the hydrodynamics when cultured in stirred systems such as bioreactors. We have previously developed a hepatocyte aggregate 3D culture system in a bioreactor where improved hepatocyte functionality could be maintained over longer periods (21 days). In this work, ultra-high-viscosity alginate was used for hepatocyte aggregates entrapment. Hepatocyte biotransformation (phase I and II enzymes), CYP450 inducibility, and secretory capacity (albumin and urea production) were monitored. The analyses were performed in both spinner vessels and bioreactors to test the effect of the pO(2) control, unavailable in the spinners. Performance of alginate-encapsulated hepatocyte aggregates in culture was compared with nonencapsulated aggregate cultures in both bioreactor (controlled environment) and spinner vessels. For both culture systems, hepatocytes' metabolic and biotransformation capacities were maintained for up to 1 month, and encapsulated cells in bioreactors showed the best performance. In particular, albumin production rate increased 2- and 1.5-fold in encapsulated aggregates compared with nonencapsulated aggregates in bioreactor and spinner vessels, respectively. Urea production rate increased twofold in encapsulated cultures compared with nonencapsulated cells, in both bioreactor and spinner vessels. Similarly, in both the bioreactor and the spinner system, cell encapsulation resulted in a 1.5- and 2.8-fold improvement of hepatocyte 7-ethoxycoumarin and uridine diphosphate glucuronosyltransferases (UGT) activities, respectively. For all parameters, but for UGT activity, the bioreactor system resulted better than the spinner vessels; for UGT activity no difference was observed between the two. Furthermore, both encapsulated and nonencapsulated 3D culture systems were inducible by 3-methylcholanthrene and dexamethasone. The encapsulated systems consistently showed improved performance over the nonencapsulated cells, indicating that the protection conferred by the alginate matrix plays a relevant role in maintaining the hepatocyte functionalities in vitro.

Stirred bioreactors for the expansion of adult pancreatic stem cells

Adult pluripotent stem cells are a cellular resource representing unprecedented potential for cell therapy and tissue engineering. Complementary to this promise, there is a need for efficient bioprocesses for their large scale expansion and/or differentiation. With this goal in mind, our work focused on the development of three-dimensional (3-D) culture systems for controlled expansion of adult pancreatic stem cells (PSCs). For this purpose, two different culturing strategies were evaluated, using spinner vessels: cell aggregated cultures versus microcarrier technology. The use of microcarrier supports (Cytodex 1 and Cytodex 3) rendered expanded cell populations which retained their self-renewal ability, cell marker, and the potential to differentiate into adipocytes. This strategy surmounted the drawbacks of aggregates in culture which were demonstrably unfeasible as cells clumped together did not proliferate and lost PSC marker expression. Furthermore, the results obtained showed that although both microcarriers tested here were suitable for sustaining cell expansion, Cytodex 3 provided a better substrate for the promotion of cell adherence and growth. For the latter approach, the potential of bioreactor technology was combined with the efficient Cytodex 3 strategy under controlled environmental conditions (pH-7.2, pO2-30% and temperature-37 degrees C); cell growth was more efficient, as shown by faster doubling time, higher growth rate and higher fold increase in cell concentration, when compared to spinner cultures. This study describes a robust bioprocess for the controlled expansion of adult PSC, representing an efficient starting point for the development of novel technologies for cell therapy.

Study of hydrodynamics in microcarrier culture spinner vessels: A particle tracking velocimetry approach

Three-dimensional particle tracking velocimetry (3-D PTV), a modern, quantitative, visualization tool, has been applied to the characterization of the flow field in the impeller region of cell culture reactor vessels. The experimental system used here is a 250-mL microcarrier spinner vessel. The studies were conducted at three different agitation rates, 90, 150, and 210 rpm, corresponding to healthy, mildly damaging, and severely damaging shear intensities, respectively. The flow can be classified into three regions: a predominantly tangential (azimuthal) flow generated by the impeller; a trailing vortex region coming off the impeller tip; and a converging flow region close to the center of the vessel. The latter two are the regions of highest velocity gradients. Energy dissipation rates due to mean velocity gradients were also calculated to characterize the impeller stream. Local specific energy dissipation rates > 10,000 erg/(cm(3)sec) . have been measured. It is proposed that the critical regions for microcarrier culture damage due to impeller hydrodynamics are the trailing vortex region and the high energy converging flow region. Graphical representation of the mean velocity flow fields and the distribution of energy dissipation rates in the impeller region are also presented here. The merits of using the dissipation function (measure of specific energy dissipation rate) as a possible scale-up parameter are also discussed. (c) 1996 John Wiley & Sons, Inc.

Development of hepatocyte spheroids immobilization technique using alternative encapsulation method

Primary hepatocytes of small animals such as rat and rabbit were often used for the study of extracorporeal liver support systems. Freshly isolated rat hepatocytes form spheroids within two days when cultivated as suspension in spinner vessels. These spheroids showed enhanced liver specific functions and more differentiated morphology compared to hepatocytes cultured as monolayers. However, shear stress caused by continuous agitation deteriorated spheroids gradually. In this work we immobilized spheroids to prolong liver specific activities. First, hepatocyte spheroids were suspended in collagen solution containing calcium chloride and then dropped into alginate solution. A thin layer of calcium alginate was formed around the droplet and then was removed after the inner collagen was gelled by treatment of sodium citrate buffer. Spheroids embedded in collagen-gel bead maintained liver specific functions such as albumin secretion rate longer than hepatocyte spheroids exposed to shear stress. Therefore, we suggest that this immobilization technique may offer an effective long-term hepatocyte cultivation and facilitate the development of a bioartificial liver support device.

Efficient assembly of rat hepatocyte spheroids for tissue engineering applications

Freshly harvested primary rat hepatocytes cultivated as multicellular aggregates, or spheroids, have been observed to exhibit enhanced liver-specific function and differentiated morphology compared to cells cultured as monolayers. An efficient method of forming spheroids in spinner vessels is described. Within 24 h after inoculation, greater than 80% of inoculated cells formed spheroids. This efficiency was significantly greater than that reported previously for formation in stationary petri dishes. With a high specific oxygen uptake rate of 2.0 x 10(-9) mmol O(2)/cell/h, the oxygen supply is critical and should be monitored for successful formation. Throughout a 6-day culture period, spheroids assembled in spinner cultures maintained a high viability and produced albumin and urea at constant rates. Transmission electron microscopy indicated extensive cell-cell contacts and tight junctions between cells within spheroids. Microvilli-lined bile canaliculus-like channels were observed in the interior of spheroids and appeared to access the exterior through pores at the outer surface. Spheroids from spinner cultures exhibited at least the level of liver-specific activity as well as similar morphology and ultrastructure compared to spheroids formed in stationary petri dishes. Hepatocytes cultured as spheroids are potentially useful three-dimensional cell systems for application in a bioartificial liver device and for studying xenobiotic drug metabolism. (c) 1996 John Wiley & Sons, Inc.

Study of hydrodynamics in microcarrier culture spinner vessels: A particle tracking velocimetry approach

Three-dimensional particle tracking velocimetry (3-D PTV), a modern, quantitative, visualization tool, has been applied to the characterization of the flow field in the impeller region of cell culture reactor vessels. The experimental system used here is a 250-mL microcarrier spinner vessel. The studies were conducted at three different agitation rates, 90, 150, and 210 rpm, corresponding to healthy, mildly damaging, and severely damaging shear intensities, respectively. The flow can be classified into three regions: a predominantly tangential (azimuthal) flow generated by the impeller; a trailing vortex region coming off the impeller tip; and a converging flow region close to the center of the vessel. The latter two are the regions of highest velocity gradients. Energy dissipation rates due to mean velocity gradients were also calculated to characterize the impeller stream. Local specific energy dissipation rates > 10,000 erg/(cm3sec) · have been measured. It is proposed that the critical regions for microcarrier culture damage due to impeller hydrodynamics are the trailing vortex region and the high energy converging flow region. Graphical representation of the mean velocity flow fields and the distribution of energy dissipation rates in the impeller region are also presented here. The merits of using the dissipation function (measure of specific energy dissipation rate) as a possible scale-up parameter are also discussed. © 1996 John Wiley & Sons, Inc.

Scale up cultivation of primary human umbilical vein endothelial cells on microcarriers from spinner vessels to bioreactor fermentation

Five types of dextran-based microcarriers (Dormacell(™), Pfeifer and Langen) with different concentrations of dimeric DEAE anion-exchange groups (nitrogen contents from 1.2 up to 2.9%) were tested as growth substrates for the cultivation of human umbilical vein endothelial cells (HUVECs). All microcarriers were gelatinized before use to improve cell adhesion. The one with the highest DEAE-group density was found to be most suitable for HUVEC propagation reaching final cell densities of 8×10(5) viable cells ml(-1) (95% viability) using microcarrier concentrations of 3 g l(-1). Furthermore, metabolic data of glucose/lactate and amino acid metabolism are presented in this study. The concentrations of 18 amino acids were monitored throughout cultivation. A considerable decrease of glutamine and inverse increase of glutamate was observed. Cultivation with initial glucose concentration of 16.5 mmol l(-1) resulted in high glutamine consumption rates, whereas high glucose-supplemented starting culture medium (30 mmol l(-1)) gave considerably lowered rates, indicating altered glutamine metabolism due to different glucose feeding. The glucose consumption and lactate production rates increased 2.6 fold and 3.5 fold, respectively, due to switch over from low to high glucose supplemented cultures. The rate of glucose metabolism was found not to be directly related to cell growth, because almost identical growth rates and doubling times were obtained. Considering the remaining 16 amino acids measured, serine concentrations considerably declined and glycine as well as alanine concentrations raised strongly. Most amino acid values were found insignificantly altered during 14 days of cultivation. Spinner vessel cultures served as inoculum for up scale propagation of HUVECs in membrane stirred 2 liter bioreactors. About 5×10(9) HUVECs were produced, which were used for the isolation and structural characterization of glycosphingolipids, cell membrane compounds, which are suggested to be involved in e.g. selectin-carbohydrate interaction (cell-cell adhesion), carcinogenesis and atherogenesis.

Microcarrier cultivation of bovine aortic endothelial cells in spinner vessels and a membrane stirred bioreactor

Primary bovine aortic endothelial cells were cultivated in serum supplemented medium without any additional growth factors. The anchorage dependent cells were propagated on Dormacell(®) microcarriers with covalently bound dimeric DEAE-groups at the surface of the dextrane beads. Cultivations were performed in 200 ml spinner cultures containing 1 g l(-1) to 3 g l(-1) of microcarriers. Out of five types of Dormacell(®) microcarriers with different ion exchange capacities ranging from 0.30 up to 0.65 meq g(-1), corresponding to nitrogen contents from 1.2% to 2.9%, respectively, optimal attachment and growth of endothelial cells were obtained with beads of highest nitrogen content (2.9%). Cells were seeded withca. 5 viable cells per microcarrier being sufficient to achieve fully confluent microcarriers after 4 to 5 days. Glucose concentrations decreased from 21 mM to uppermost half of the original concentrations. 4 mM glutamine was rapidly consumed and virtually exhausted after the cells reached confluency. Lactate concentrations raised to a maximum of 7 mM in spinner cultures, but was found to be reutilized in the stationary phase after glutamine limitation occurred. Serine was found to be the second most prominent amino acid being almost exhausted at confluency whereas alanine was produced in noteworthy amounts. Considerable decrease was determined for threonine, lysine and arginine; low consumption rates were observed for leucine, phenylalanine and methionine. All other amino acids did not alter significantly throughout cultivation. These data support that bovine aortic endothelial cells are capable to utilize glucose and glutamine as well as lactic acid (after glutamine exhaustion) as energy and/or carbon source. Finally, batch cultures in a 2 liter membrane stirred bioreactor with bubble-free aeration were performed to produce large quantities of endothelial cells using microcarrier concentrations of 3 g l(-1).

Characterization of agitation environments in 250 ml spinner vessel, 3 L, and 20 L reactor vessels used for animal cell microcarrier culture

Three dimensional particle tracking velocimetry (3-D PTV) was used to characterize the flow fields in the impeller region of three microcarrier reactor vessels. Three typical cell culture bioreactors were chosen: 250 ml small-scale spinner vessels, 3 L bench-scale reactor, and 20 L medium-scale reactor. Conditions studied correspond to the actual operating conditions in industrial setting and were determined based on the current scale-up paradigm: the Kolmogorov eddy length criterion. In this paper we present characterization of hydrodynamics on the basis of flow structures produced because of agitation. Flow structures were determined from 3-D mean velocity results obtained using 3-D PTV. Although the impellers used in 3 L and 20 L reactors were almost identical, the flow structures produced in the two reactors differed considerably. Results indicate that near geometric scale up does not necessarily amount to scale-up of flow patterns and indicates that intensity as well as distribution of energy may vary considerably during such a scale-up.

Selection of host cell lines for scale-up growth conditions of a recombinant baculovirus vector expressing the measles virus nucleocapsid protein

Various insect cell lines were grown as suspension cultures in spinner vessels and infected with a recombinant baculovirus vector expressing the measles virus nucleoprotein. The highest yields of recombinant protein production were achieved using Trichoplusia ni (BTI-Tn 5B1-4) cells growing as natural aggregates in suspension and cell line Mb as a single cell suspension culture.

Effects of paddle impeller geometry on power input and mass transfer in small‐scale animal cell culture vessels

Process scaleup for stirred-tank animal cell cultures such as suspension and microcarrier cultures often begins at the bench scale in small spinner vessels. In order to initiate process development under the proper conditions, it is essential to know the physical conditions under which the cells are grown. In this article, power inputs and surface oxygen transfer rates to culture medium in 500-mL Corning spinner vessels were determined as a function of the impeller geometry, impeller height, and agitation speed. The results obtained indicate that power dissipation dependency differs from literature correlations and may compromise scale up at constant power input from these vessels. These results are of general utility to researchers using small-scale vessels.

Interactions between misonidazole and hyperthermia in EMT6 spheroids.

The effect of hypoxic misonidazole (MISO) pretreatment on the subsequent heat sensitivity of EMT6 multicellular tumour spheroids has been investigated. Spheroids were grown in static culture and treated when either 200-300 micrometers or 650-800 micrometers in diameter. Pretreatment was carried out in glass spinner vessels containing 100 ml medium with or without 5mM MISO under conditions of hypoxia. Three-hour hypoxic pretreatment with 5mM MISO significantly enhanced the subsequent response of 200 micrometers spheroids to heat at 43 degrees C. Oxic incubation at 37 degrees C between pretreatment and heating caused progressively loss of heat sensitization with time, recovery being almost complete after 6 h. Recovery was inhibited by incubation at 0 degree C during the interval. Preheating 200 micrometers spheroids at 43 degrees C for 2 h increased their subsequent sensitivity to hypoxic MISO at 37 degrees C. These results are discussed in relation to known mechanisms of MISO metabolism.

Oxidation-reduction potential and concomitant growth patterns of cultures of Earle's "L" cells in centrifuge bottle spinners.

AbstractPrevious studies of oxidation‐reduction potential (ORP) variation in monolayer (Roux bottle) cultures pointed out the need for data on pH and ORP patterns in simple spinner cultures. This information was desirable for optimizing conditions of growth in small 1‐L and New Brunswick fermentors. Results of experiments in 250‐ml centrifuge spinner vessels are presented showing that incubation of media prior to inoculation induces desirable qualities reflected in better growth. The importance of initial ORP values of the medium is discussed. The relationship of ORP levels to yield and longevity of cell growth is also considered. The ORP level of the medium at inoculation is shown to be effected by previous incubation.