制备可溶性肿瘤坏死因子受体II－脂联素球部融合蛋白的两种细胞培养工艺比较

利用7.5 L生物反应器篮式贴壁培养和全悬浮批式培养CHO工程细胞株表达可溶性肿瘤坏死因子受体Ⅱ-脂联素球部(sTNFRⅡ-gAD)融合蛋白,比较这两种培养方法的产率,以便优化高效表达sTNFRⅡ-gAD融合蛋白的制备工艺.篮式贴壁培养首先小规模培养CHO工程细胞株,待细胞增殖到一定密度后以3× 105～4× 105 cells/mL密度接种生物反应器贴壁培养3d,调换成不含血清的LK021培养基继续培养4d.而全悬浮无血清批式培养则以3×105～4×105 cells/mL密度的CHO工程细胞株接种于生物反应器,连续培养7d.培养过程实时监测培养条件,维持pH和DO的稳定.分别收集细胞上清,离心去细胞后用Pellicon切相流超滤系统对蛋白进行浓缩,并通过DEAE离子交换柱进行纯化.结果显示,篮式贴壁培养和全悬浮批式培养均成功表达了sTNFRⅡ-gAD融合蛋白,产量分别为8.0 mg/L和7.5 mg/L、纯度分别为95％和98％,从而为sTNFRⅡ-gAD融合蛋白的中试工艺研究提供了一定的基础.     

Design and validation of a pulsatile perfusion bioreactor for 3D high cell density cultures

This study presents the design and validation of a pulsatile flow perfusion bioreactor able to provide a suitable environment for 3D high cell density cultures for tissue engineering applications. Our bioreactor system is mobile, does not require the use of traditional cell culture incubators and is easy to sterilize. It provides real‐time monitoring and stable control of pH, dissolved oxygen concentration, temperature, pressure, pulsation frequency, and flow rate. In this bioreactor system, cells are cultured in a gel within a chamber perfused by a culture medium fed by hollow fibers. Human umbilical vein endothelial cells (HUVEC) suspended in fibrin were found to be living, making connections and proliferating up to five to six times their initial seeding number after a 48‐h culture period. Cells were uniformly dispersed within the 14.40 mm × 17.46 mm × 6.35 mm chamber. Cells suspended in 6.35‐mm thick gels and cultured in a traditional CO₂ incubator were found to be round and dead. In control experiments carried out in a traditional cell culture incubator, the scarcely found living cells were mostly on top of the gels, while cells cultured under perfusion bioreactor conditions were found to be alive and uniformly distributed across the gel. Biotechnol. Bioeng. 2009; 104: 1215–1223. © 2009 Wiley Periodicals, Inc.     

Intracellular pH based controlled cultivation of yeast cells: I. Measurement methodology

A method has been developed to continuously measure the intracellular pH (pH(i)) of cells cultivated in a bioreactor in an on-line fashion over extend time periods. The methods is attractive in its simplicity and involves the use of a fluorescent pH(i) indicator 9-aminoacridine (9A A) which is a week base. An expression has been derived to calculate changes in pH(i) from measured 9AA-fluorescence changes. The indicator 9AA was found t be nontoxic to yeast cells at concentrations used to measure pH(i) (7 muM). The fluorescence of nicotinamide adenine dinucleotide (NADH) molecules did not interfere significantly with the measurement of 9AA-fluorescence. The pH(i) change in yeast cell following the addition of a proton ionophore carbonyl cyanide m-chlorophenyl hydrazone (CCCP) measured by 9AA compared favorably with that measured by the well-established pH(i), indicator (which is however unsuitable for on-line applications in a bioreactor) bis-carboxyethyl carboxy fluorescein (BCECF). The pH(i) of yeast under substrate starved conditions was 6.4 units. The responses of pH(i) of yeast cells to induced metabolic transitions were studied. Under aerobic condition, pH(i) increased by 0.12 unit following a 100-ppm glucose pulse addition and by 0.25 unit following a 300-ppm ethanol pulse addition. Under anaerobic condition, pH(i) increased by 0.1 unit following a 500-ppm glucose pulse addition. Comparison of pH(i) with other indicators of cellular metabolic state suggests that pH(i) is a cellular metabolic state indicator. (c) 1993 John Wiley & Sons, Inc.     

Membrane-aerated microbioreactor for high-throughput bioprocessing

A microbioreactor with a volume of microliters is fabricated out of poly(dimethylsiloxane) (PDMS) and glass. Aeration of microbial cultures is through a gas-permeable PDMS membrane. Sensors are integrated for on-line measurement of optical density (OD), dissolved oxygen (DO), and pH. All three parameter measurements are based on optical methods. Optical density is monitored via transmittance measurements through the well of the microbioreactor while dissolved oxygen and pH are measured using fluorescence lifetime-based sensors incorporated into the body of the microbioreactor. Bacterial fermentations carried out in the microbioreactor under well-defined conditions are compared to results obtained in a 500-mL bench-scale bioreactor. It is shown that the behavior of the bacteria in the microbioreactor is similar to that in the larger bioreactor. This similarity includes growth kinetics, dissolved oxygen profile within the vessel over time, pH profile over time, final number of cells, and cell morphology. Results from off-line analysis of the medium to examine organic acid production and substrate utilization are presented. By changing the gaseous environmental conditions, it is demonstrated that oxygen levels within the microbioreactor can be manipulated. Furthermore, it is demonstrated that the sensitivity and reproducibility of the microbioreactor system are such that statistically significant differences in the time evolution of the OD, DO, and pH can be used to distinguish between different physiological states. Finally, modeling of the transient oxygen transfer within the microbioreactor based on observed and predicted growth kinetics is used to quantitatively characterize oxygen depletion in the system.     

Ex vivo expansion of hematopoietic stem cells derived from umbilical cord blood in rotating wall vessel

Expansion of umbilical cord blood mononuclear cells (UCB MNCs) was carried out in a rotating wall vessel (RWV) bioreactor and tissue culture flasks (T-flasks) in serum-containing medium supplemented with relatively low doses of purified recombinant human cytokines (5.33 ng/ml IL-3, 16 ng/ml SCF, 3.33 ng/ml G-CSF, 2.13 ng/ml GM-CSF, 7.47 ng/ml FL and 7.47 ng/ml TPO) for 8 days. The cell density, pH and osmolality of the culture medium in the two culture systems were measured every 24h. Flow cytometric assay for CD34+ cells was carried out at 0, 144 and 197 h and methylcellulose colony assays were performed at 0, 72, 144 and 197 h. The pH and osmolality of the medium in the two culture systems were maintained in the proper ranges for hematopoietic stem cells (HSCs) and progenitors culture. The RWV bioreactor, combined with a cell-dilution feeding protocol, was efficient to expand UCB MNCs. At the end of 200 h culture, the total cell number was multiplied by 435.5+/-87.6 times, and CD34+ cells 32.7+/-15.6 times, and colony-forming units of granulocyte-macrophage (CFU-GM) 21.7+/-4.9 times. While in T-flasks, however, total cells density changed mildly, CD34+ cells and CFU-GM decreased in number. It is demonstrated that the RWV bioreactor can provide a better environment for UCB MNCs expansion, enhance the contact between HSCs and accessory cells and make the utilization of cytokines more effective than T-flask.     

Development of a small-scale bioreactor: application to in vivo NMR measurement

A perfused bioreactor allowing in vivo NMR measurement was developed and validated for Eschscholtzia californica cells. The bioreactor was made of a 10-mm NMR tube. NMR measurement of the signal-to-noise ratio was optimized using a sedimented compact bed of cells that were retained in the bioreactor by a supporting filter. Liquid medium flow through the cell bed was characterized from a mass balance on oxygen and a dispersive hydrodynamic model. Cell bed oxygen demand for 4 h perfusion required a minimal medium flow rate of 0.8 mL/min. Residence time distribution assays at 0.8-2.6 mL/min suggest that the cells are subjected to a uniform nutrient environment along the cell bed. Cell integrity was maintained for all culture conditions since the release of intracellular esterases was not significant even after 4 h of perfusion. In vivo NMR was performed for (31)P NMR and the spectrum can be recorded after only 10 min of spectral accumulation (500 scans) with peaks identified as G-6P, F-6P, cytoplasmic Pi, vacuolar Pi, ATP(gamma) and ADP(beta), ATP(alpha) and ADP(alpha), NADP and NDPG, NDPG and ATP(beta). Cell viability was shown to be maintained as (31)P chemical shifts were constant with time for all the identified nuclei, thus suggesting constant intracellular pH.     

Improved laminaribiose phosphorylase production by <Emphasis Type="Italic">Euglena gracilis</Emphasis> in a bioreactor: A comparative study of different cultivation methods

Laminaribiose phosphorylase (EC 2.4.1.31) catalyzes a reversible phosphorolysis reaction in which laminaribiose, a very high value sugar is produced. This enzyme is not being produced commercially therefore, to realize the most effective method for producing laminaribiose phosphorylase and obtaining as much activity units as possible per liter of culture, different cultivation methods of Euglena gracilis were compared. Heterotrophic and mixotrophic cultivations of Euglena gracilis in two different pHs, in flask and bioreactor were performed. The reverse phosphorolysis activity of laminaribiose phosphorylase produced under different cultivation methods was measured. The heterotrophic approach showed to be the more effective cultivation method as 47.6 IU/L was obtained compared to 27 IU/L in the mixotrophic one. The heterotrophic cultivation then was further investigated under two different pH values of the culture media. The culture at pH 6.8 resulted in 7.94 IU/L/day whereas only 4.06 was obtained for the culture at pH 4. Cultivation in a bioreactor resulted in a distinctive amount of 191.5 IU/L and an activity yield of 9.7 IU/g glucose compared to 5.4 in flask cultivation. Heterotrophic cultivation of Euglena gracilis in a bioreactor containing a culture media at pH 6.8 and controlled operation conditions showed enhanced laminaribiose phosphorylase activity production per liter and day of cultivation.     

Cultivation of primary porcine hepatocytes in an OXY-HFB for use as a bioartificial liver device

Bioreactors being developed for bioartificial liver devices vary greatly in their construction. Until now, primary liver cells were cultivated either in sandwich configuration, as spheroids, or in special hollow fiber systems. Primary hepatocytes are demanding on their environment and have a high oxygen consumption. To get good results, optimal cultivation conditions are needed. The idea of the project was to investigate a new concept of an oxygenating hollow fiber bioreactor (OXY-HFB). The OXY-HFB should consist exclusively of oxygenating and internal heat exchange fibers to yield a simple and effective design. Primary liver cells were seeded on the surface of the fibers in the extrafiber space. Oxygen requirements and temperature control were supplied through the fibers. The culture medium was perfused through the extrafiber space and therefore brought into direct hepatocellular contact. The OXY-HFB concept offers different advantages. A high cell density of 2.5 x 10(7) cells/mL can be obtained. This results in a cell number of 2.5 x 10(9) liver cells per bioreactor. Furthermore, the OXY-HFB is easily handled because no incubator is required. To study the efficiency of this bioreactor technique, various parameters were investigated over a cultivation period of three weeks. These included urea synthesis, lactate formation, glucose elimination, albumin synthesis, oxygen level, and pH. Furthermore, the metabolites of diazepam were measured. The biochemical performance of the bioreactor remained stable over the investigated time period. These results demonstrate that porcine liver cells preserve their viability and primary metabolism in the OXY-HFB over the complete period of study.     

Enhancement of tannase production by Lactobacillus plantarum CIR1: validation in gas-lift bioreactor

The optimization of tannase production by Lactobacillus plantarum CIR1 was carried out following the Taguchi methodology. The orthogonal array employed was L18 (2¹ × 3⁵) considering six important factors (pH and temperature, also phosphate, nitrogen, magnesium, and carbon sources) for tannase biosynthesis. The experimental results obtained from 18 trials were processed using the software Statistical version 7.1 using the character higher the better. Optimal culture conditions were pH, 6; temperature, 40 °C; tannic acid, 15.0 g/L; KH₂PO₄, 1.5 g/L; NH₄Cl, 7.0 g/L; and MgSO₄, 1.5 g/L which were obtained and further validated resulting in an enhance tannase yield of 2.52-fold compared with unoptimized conditions. Tannase production was further carried out in a 1-L gas-lift bioreactor where two nitrogen flows (0.5 and 1.0 vvm) were used to provide anaerobic conditions. Taguchi methodology allowed obtaining the optimal culture conditions for the production of tannase by L. plantarum CIR1. At the gas-lift bioreactor the tannase productivity yields increase 5.17 and 8.08-fold for the flow rates of 0.5 and 1.0 vvm, respectively. Lactobacillus plantarum CIR1 has the capability to produce tannase at laboratory-scale. This is the first report for bacterial tannase production using a gas-lift bioreactor.     

Intracellular pH-based controlled cultivation of yeast cells: II. cultivation methodology

Intracellular pH (pH(i)) was measured on-line in a bioreactor using a fluorescent pH(i) indicator, 9-aminoacridine, and controlled fed-batch cultivations of yeast cells based on pH(i) (FB-pH(i)) were performed. In FB-pH(i) cultivations, automated glucose additions were made to the culture in response to culture pH(i). The average ethanol (an-aerobic product) yield was significantly lower [0.12 g g(-1) glucose in fed-batch pH(i) cultivations with 100 ppm glucose additions (FB-pH(i)-100 cultivation) vs. 0.48 g g(-1) glucose in batch] and cell yield was higher (0.54 g g(-1) glucose in FB-pH(i)-100 cultivation vs. 0.3 g g(-1) glucose in batch) compared to batch cultivation. An expression has been derived to calculate changes in pH(i) from measured fluorescence values when the cell concentration increases during growth. Cultivations based on pH(i), performed with different magnitudes of glucose addition (100, 50, and 10 ppm additions), showed that lower magnitudes of glucose addition resulted in lower ethanol yields while cell yield remained unaffected. The ratio of specific oxygen uptake rate to specific glucose uptake rate (OUR/GUR) increased with decreased in magnitude of glucose additions in FB-pH(i) cultivations, suggesting that the culture aerobic state was higher when the magnitude of glucose addition was lower. The average cell productivity in FB-pH(i) cultivations was 29% higher than in batch cultivation. Cells were also cultivated at high OUR conditions, and the results are compared with other cultivations. (c) 1993 John Wiley & Sons, Inc.     

Non-invasive methods for determination of cellular growth inPodophyllum hexandrum suspension cultures

Culture conductivity and on-line NADH fluorescence were used to measure cellular growth in plant cell suspension cultures ofPodophyllum hexandrum. An inverse correlation between dry cell weight and medium conductivity was observed during shake flask cultivation. A linear relationship between dry cell weight and culture NADH fluorescence was obtained during the exponential phase of batch cultivation in a bioreactor under the pH stat (pH 6) conditions. It was observed that conductivity measurement were suitable for biomass characterisation under highly dynamic uncontrolled shake flask cultivation conditions. However, if the acid/alkali feeding is done for pH control the conductivity measurement could not be applied. On the other hand the NADH fluorescence measurement allowed online-in situ biomass monitoring of rather heterogenous plant cell suspension cultures in bioreactor even under the most desirable pH stat conditions.     

Population dynamics of a continuous fermentation of recombinant Saccharomyces cerevisiae using flow cytometry

The plasmid instability of genetically modified microorganisms during prolonged bioreactor operations is one of the major problems to be overcome in the production of recombinant proteins. The use of flow cytometry to monitor a fermentation process with recombinant cells in a CSTR is reported here. This technique has been applied to determine the fraction of plasmid-bearing cells (P+) of a recombinant Saccharomyces cerevisiae strain harboring the EXG1 gene in a continuous stirred tank bioreactor with a working volume of 2 L. The different levels in the expression of the EXG1 gene, which encodes the enzyme exo-beta-glucanase, were used to determine the P+ fraction. Other parameters such as viability, cellular protein, cell size and structure were also monitored using flow cytometry. This technique has two main advantages over the conventional method of determining the P+ fraction (plating in selective and non-selective solid media): (a) it takes a very short period of time to obtain a measurement that provides multiple parametric information; and (b) it is more representative of the bioreactor cell population since it can analyze thousands of cells in the same sample. A continuous operation (432 h) with the recombinant strain in a CSTR was carried out to test the application of this technique. Measurements of cellular exo-beta-glucanase activity and cellular protein content closely correlates to the measured fraction of plasmid-containing cells in the population. Moreover, the standard deviation of the fraction of P+ cells determined using this technique was very low (about 2%). Recombinant protein production also increased the size of the yeast cells, whereas the recombinant cells also had a more complex internal structure than the non-recombinant host strain.     

Examination of chlorophyll fluorescence decay kinetics in sulfur deprived algae Chlamydomonas reinhardtii

Chlorophyll fluorescence decay kinetics was measured in sulfur deprived cells of green alga Chlamydomonas reinhardtii with a home made picosecond fluorescence laser spectrometer. The measurements were carried out on samples either shortly adapted to the dark ('Fo conditions') or treated to reduce Qa ('Fm conditions'). Bi-exponential fitting of decay kinetics was applied to distinguish two components one of them related to energy trapping (fast component) and the other to charge stabilization and recombination in PS 2 reaction centers (slow component). It was found that the slow component yield increased by 2.0 and 1.2 times when measured under 'Fo' and 'Fm conditions', respectively, in sulfur deprived cells as compared to control ones. An additional rapid rise of the slow component yield was observed when incubation was carried out in a sealed bioreactor and cell culture turned to anaerobic conditions. The obtained results strongly indicate the existence of the redox control of PS 2 activity during multiphase adaptation of C. reinhardtii to sulfur deficiency stress. Probable mechanisms responsible for the observed increased recombinant fluorescence yield in starved cells are discussed.     

Physiological heterogeneity of Pseudomonas taetrolens during lactobionic acid production

Physiological heterogeneity constitutes a critical parameter in biotechnological systems since both metabolite yield and productivity are often hampered by the presence of undesired physiological cell subpopulations. In the present study, the physiological status and functionality of Pseudomonas taetrolens cells were monitored by multiparameter flow cytometry during fermentative lactobionic acid production at the shake-flask and bioreactor scale. In shake-flask fermentation, the onset of the lactobionic acid production phase was accompanied by a progressive loss of cellular metabolic activity, membrane polarization, and membrane integrity concomitantly to acidification. In fact, population dynamics has shown the prevalence of damaged and dead subpopulations when submitted to a pH?<?4 from 16?h onwards. Furthermore, fluorescence-activated cell sorting revealed that these sublethally injured cells were nonculturable. In contrast, P. taetrolens cells exhibited a robust physiological status during bioreactor cultivations performed with a pH-shifted strategy at 6.5, remaining predominantly healthy and metabolically active (>96?%) as well as maintaining bioconversion efficiency throughout the course of the fermentation. Additionally, an assessment of the seed culture’s physiological robustness was carried out in order to determine the best seed culture age. Results showed that bioreactor culture performance, growth, and lactobionic acid production efficiency were strongly dependent on the physiological heterogeneity displayed by the seed culture. This study provides the most suitable criteria for optimizing lactobionic acid production efficiency through a novel flow cytometric-based approach based on the physiological status of P. taetrolens. It also constitutes a valuable, broad-ranging methodology for the enhancement of microbial bioprocesses involved in the production of secondary metabolites.     

Overcoming challenges in WAVE Bioreactors without feedback controls for pH and dissolved oxygen

The biopharmaceutical industry is increasing its use of the WAVE Bioreactor for culturing cells. Although this disposable bioreactor can be equipped to provide real-time pH and dissolved oxygen (DO) monitoring and control, our goal was to develop a process for culturing CHO cells in this system without relying on pH and DO feedback controls. After identifying challenges in culturing cells without controlling for pH and DO in the WAVE Bioreactor, we characterized O(2) and CO(2) transfer in the system. From these cell-free studies, we identified rock rate and rock angle as key parameters affecting O(2) transfer. We also identified the concentration of CO(2) in the incoming gas and the rate of gas flow into the headspace as key parameters affecting CO(2) transfer--and therefore pH--in the disposable culture chamber. Using a full-factorial design to evaluate the rock rate, rock angle, and gas flow rate defined for this WAVE Bioreactor process, we found comparable cell growth and pH profiles in the ranges tested for these three parameters in two CHO cell lines. This process supported cell growth, and maintained pH and DO within our desired range--pH 6.8-7.2 and DO exceeding 20% of air saturation--for six CHO cell lines, and it also demonstrated comparable cell growth and viability with the stirred-tank bioreactor process with online pH and DO control. By eliminating the use of pH and DO probes, this process provides a simple and more cost-effective method for culturing cells in the WAVE Bioreactor.     

A microfluidic bioreactor with integrated transepithelial electrical resistance (TEER) measurement electrodes for evaluation of renal epithelial cells

We have developed a bilayer microfluidic system with integrated transepithelial electrical resistance (TEER) measurement electrodes to evaluate kidney epithelial cells under physiologically relevant fluid flow conditions. The bioreactor consists of apical and basolateral fluidic chambers connected via a transparent microporous membrane. The top chamber contains microfluidic channels to perfuse the apical surface of the cells. The bottom chamber acts as a reservoir for transport across the cell layer and provides support for the membrane. TEER electrodes were integrated into the device to monitor cell growth and evaluate cell–cell tight junction integrity. Immunofluorescence staining was performed within the microchannels for ZO‐1 tight junction protein and acetylated α‐tubulin (primary cilia) using human renal epithelial cells (HREC) and MDCK cells. HREC were stained for cytoskeletal F‐actin and exhibited disassembly of cytosolic F‐actin stress fibers when exposed to shear stress. TEER was monitored over time under normal culture conditions and after disruption of the tight junctions using low Ca²⁺ medium. The transport rate of a fluorescently labeled tracer molecule (FITC‐inulin) was measured before and after Ca²⁺ switch and a decrease in TEER corresponded with a large increase in paracellular inulin transport. This bioreactor design provides an instrumented platform with physiologically meaningful flow conditions to study various epithelial cell transport processes. Biotechnol. Bioeng. 2010;107:707–716. © 2010 Wiley Periodicals, Inc.     

Characterization of oxygen transfer in a membrane-aerated hollow-fibre bioreactor using modified microcoaxial needle electrodes

In this work the volumetric O₂ transfer coefficient (OTC) through a membrane of a miniaturized hollow-fibre bioreactor was measured by the use of modified O₂ microaxial needle electrodes. Before measurment, available electrodes were modified by inserting and gluering them in thin galss capillaries to avoid damage. No differences in the behaviour of the electrodes occurred in comparison to the non-modified electrodes. These modified electrodes allowed O₂ partial pressure measurement in the 0.8-mm-high extracapillary space (ECS) of the bioreactor with high sensitivity and reliability. O₂ measurements were carried out the two ports of the ECS at different insertion depths. The results of the measurements showed a homogenous O₂ supply during variation of the radial co-coordinate of the electrode. In addition to these results, an increase in the local supply in the direction of medium flow was observed . The calculated mean OTC (47–63 h^–1) gave extremely improved O₂ transfer due to membrane aeration compared to conventional hallow-fibre systems and other bioreactors used in animal-cell culture technology. The improved OTC and the small ECS volume (4.3 ml) makes this culture system suitable for the cultivation of primary cells with tissue-like densities.     

Perfusion flow bioreactor for 3D in situ imaging: investigating cell/biomaterials interactions

The capability to image real time cell/material interactions in a three-dimensional (3D) culture environment will aid in the advancement of tissue engineering. This paper describes a perfusion flow bioreactor designed to hold tissue engineering scaffolds and allow for in situ imaging using an upright microscope. The bioreactor can hold a scaffold of desirable thickness for implantation (>2 mm). Coupling 3D culture and perfusion flow leads to the creation of a more biomimetic environment. We examined the ability of the bioreactor to maintain cell viability outside of an incubator environment (temperature and pH stability), investigated the flow features of the system (flow induced shear stress), and determined the image quality in order to perform time-lapsed imaging of two-dimensional (2D) and 3D cell culture. In situ imaging was performed on 2D and 3D, culture samples and cell viability was measured under perfusion flow (2.5 mL/min, 0.016 Pa). The visualization of cell response to their environment, in real time, will help to further elucidate the influences of biomaterial surface features, scaffold architectures, and the influence of flow induced shear on cell response and growth of new tissue.     

Effects of oxygen and culture system on in vitro propagation and redifferentiation of osteoarthritic human articular chondrocytes

Regenerative medicine-based approaches for the repair of damaged cartilage rely on the ability to propagate cells while promoting their chondrogenic potential. Thus, conditions for cell expansion should be optimized through careful environmental control. Appropriate oxygen tension and cell expansion substrates and controllable bioreactor systems are probably critical for expansion and subsequent tissue formation during chondrogenic differentiation. We therefore evaluated the effects of oxygen and microcarrier culture on the expansion and subsequent differentiation of human osteoarthritic chondrocytes. Freshly isolated chondrocytes were expanded on tissue culture plastic or CultiSpher-G microcarriers under hypoxic or normoxic conditions (5% or 20% oxygen partial pressure, respectively) followed by cell phenotype analysis with flow cytometry. Cells were redifferentiated in micromass pellet cultures over 4 weeks, under either hypoxia or normoxia. Chondrocytes cultured on tissue culture plastic proliferated faster, expressed higher levels of cell surface markers CD44 and CD105 and demonstrated stronger staining for proteoglycans and collagen type II in pellet cultures compared with microcarrier-cultivated cells. Pellet wet weight, glycosaminoglycan content and expression of chondrogenic genes were significantly increased in cells differentiated under hypoxia. Hypoxia-inducible factor-3α mRNA was up-regulated in these cultures in response to low oxygen tension. These data confirm the beneficial influence of reduced oxygen on ex vivo chondrogenesis. However, hypoxia during cell expansion and microcarrier bioreactor culture does not enhance intrinsic chondrogenic potential. Further improvements in cell culture conditions are therefore required before chondrocytes from osteoarthritic and aged patients can become a useful cell source for cartilage regeneration.     

Photoautotrophic high-density cultivation of vegetative cells of Haematococcus pluvialis in airlift bioreactor

This work aimed to investigate the effects of the bioreactor configurations and their design variables on the cultivation of vegetative cells Haematococcus pluvialis to achieve sustainable high cell density. The addition of vitamin B to F1 growth medium could appreciably enhance the final cell density. Employing this medium, the cultivation in the airlift bioreactor was demonstrated to outperform the bubble column at the same operating conditions. Aeration was crucial for a proper growth of the alga in the airlift bioreactor, but it must be maintained at low level to minimize shear stress. The most appropriate aeration velocity (superficial velocity) was at the lower limit of the pump, i.e. 0.4 cm s(-1) and a smaller riser was shown to have positive influence on the cell growth. A 1% CO(2) supplement to the air supply considerably enhanced the growth rate of H. pluvialis and the most suitable light intensity for the growth was at 20 micromol photon m(-2) s(-1). The semi-continuous culture was successfully implemented with the optimal airlift bioreactor design and under optimal conditions the harvest could be performed every four days with the specific growth rate of 0.31 d(-1).