Importance of Sox2 in maintenance of cell proliferation and multipotency of mesenchymal stem cells in low-density culture

Objectives: This study has aimed to repopulate ‘primitive’ cells from late‐passage mesenchymal stem cells (MSCs) of poor multipotentiality and low cell proliferation rate, by simply altering plating density. Materials and methods: Effects of low density culture compared t high density culture on late‐passage bone marrow (BM)‐derived MSCs and pluripotency markers of multipotentiality were investigated. Cell proliferation, gene expression, RNA interference and differentiation potential were assayed. Results and conclusions: We repopulated ‘primitive’ cells by replating late‐passage MSCs at low density (17 cells/cm²) regardless of donor age. Repopulated MSCs from low‐density culture were smaller cells with spindle shaped morphology compared to MSCs from high‐density culture. The latter had enhanced colony‐forming ability, proliferation rate, and adipogenic and chondrogenic potential. Strong expression of osteogenic‐related genes (Cbfa1, Dlx5, alkaline phosphatase and type Ι collagen) in late‐passage MSCs was reduced by replating at low density, whereas expression of three pluripotency markers (Sox2, Nanog and Oct‐4), Osterix and Msx2 reverted to levels of early‐passage MSCs. Knockdown of Sox2 and Msx2 but not Nanog, using RNA interference, showed significant decrease in colony‐forming ability. Specifically, knockdown of Sox2 significantly inhibited multipotentiality and cell proliferation. Our data suggest that plating density should be considered to be a critical factor for enrichment of ‘primitive’ cells from heterogeneous BM and that replicative senescence and multipotentiality of MSCs during in vitro expansion may be predominantly regulated through Sox2.     

Ex vivo expansion of primitive hematopoietic cells for cellular therapies: An overview

Sources of hematopoietic cells for bone marrow transplantation are limited by the supply of compatible donors, the possibility of viral infection, and autologous (patient) marrow that is depleted from prior chemo- or radiotherapy or has cancerous involvement. Anex vivo system to amplify hematopoietic progenitor cells could increase the number of patients eligible for autologous transplant, allow use of cord blood hematopoietic cells to repopulate an adult, reduce the amount of bone marrow and/or mobilized peripheral blood stem and progenitor cells required for transplantation, and reduce the time to white cell and platelet engraftment. The cloning of hematopoietic growth factors and the identification of appropriate conditions has enabled the development of successfulex vivo hematopoietic cell cultures. Purification systems based on the CD34 marker (which is expressed by the most primitive hematopoietic cells) have proven an essential tool for research and clinical applications. Present methods for hematopoietic cultures (HC) on stromal (i.e. accessory cells that support hematopoiesis) layers in flasks lack a well-controlled growth environment. Several bioreactor configurations have been investigated, and a first generation of reactors and cultures has reached the clinical trial stage. Our research suggests that perfusion conditions improve substantially the performance of hematopoietic reactors. We have designed and tested a perfusion bioreactor system which is suitable for the culture of non-adherent cells (without stromal cells) and readily scaleable for clinical therapies. Eliminating the stromal layer eliminates the need for a stromal cell donor, reduces culture time, and simplifies the culture system. In addition, we have compared the expansion characteristics of both mononuclear and CD34⁺ cells, since the latter are frequently assumed to give a superior performance for likely transplantation therapies.Abbreviations BFU0-E burst forming unit-erythroid - BM bone marrow - CB cord blood - CFU-C colony forming unit-culture - CFU-E colony forming unit-erythroid - CFU-F colony forming unit-fibroblast - CFU-GEMM colony forming unit-granulocyte, erythroid, macrophage, megakaryocyte - CFU-GM colony forming unit-granulocyte, macrophage - CFU-Mix colony forming unit-mixed (also known as CFU-GEMM) - CML chronic myeloid leukemia - CSF colony stimulating factor - DMSO dimethyl sulfoxide - ECM extracellular matrix - EPO erythropoietin - FL fetal liver - HC hematopoietic culture - LTBMC long-term bone marrow culture - LTC-IC long-term culture initiating cell - LTHC long-term hematopoietic culture - MNC mononuclear cells - PB peripheral blood     

造血细胞体外悬浮培养和生物反应器开发

为解决造血细胞的静态培养中由浓度梯度引起的培养不稳定、环境不均一、难放大等问题,首先采用转瓶对脐血单个核细胞进行了悬浮培养研究,结果表明,悬浮培养中总细胞、集落和CD34^＋细胞的扩增都高于静态的方瓶培养。在测试了所用材料生物相容性的基础上,开发了可以控制溶氧和pH的生物反应器,并将其应用到造血细胞的批培养中,结果表明反应器的培养环境均一,可实现较高密度的培养,而且总细胞、集落和CD34^＋细胞的扩增都优于静态培养。大规模的反应器培养有利于解决临床应用中细胞数量不足的问题。     

体外培养脐血单个核细胞与CD34+富集细胞

对比MNC和CD34 +富集细胞在SCF +IL 3+IL 6 +FL +Tpo细胞因子组合下的体外扩增特性 ,发现 :CD34 +富集细胞具有很高的扩增潜力 ,在本实验条件下其总细胞持续扩增了 8周 ,扩增倍数达 312 70 9± 86 40 5倍 ;而MNC在培养至第 4周扩增就已呈现下降趋势 ,最大仅扩增了 5 3 3± 6 2倍。对比集落和CD34 +细胞的扩增发现 ,MNC的集落密度和CD34 +细胞含量由第 0天至第 7天有一个上升的过程 ,而CD34 +富集细胞在培养过程中 ,集落密度和CD34 +细胞含量却始终呈下降趋势。在体外培养过程中 ,CD34 +富集细胞的CFU GM和CD34 +细胞最大分别扩增了 185 7± 14 1和 191 7± 188 8倍 ,明显高于MNC的 12 4± 3 2和 5 0 6± 33 2倍 ;而CD34 +富集细胞和MNC的BFU E则只实现了少量扩增 ,分别为 7 2± 5 2和 10 1± 3 4倍。结果显示 ,从CD34 +富集细胞出发扩增造血干 祖细胞 ,可以得到更多的CD34 +细胞和CFU GM集落形成细胞     

Genetic factors influencing murine hematopoietic productivity in culture

In order to study a previously described genetic difference manifested in stem cell kinetics of specific mouse strains, effects of this putative gene, stk, were measured on growth and expansion of stem and progenitor cell populations ex vivo. Bone marrow cells from each of two inbred mouse strains, C57BL/6J and DBA/2J, were placed into separate bioreactor cultures perfused continuously with growth medium containing erythropoietin (Epo), interleukin-3 (IL-3), granulocyte-macrphage colony stimulating factor (GM-CSF), and Kit ligand as well as 5% CO₂. Expansion of cell numbers reached 20-fold for DBA/2J and 10-fold for C57BL/6J marrow within about 1 week of culture. Significant production was also seen of colonyforming unit (CFU)-GM (up nine-fold from input levels) just prior to the cell production peak, and, importantly, moderate expansion of day 12 colony-forming unit-spleen (CFU-S; two- to threefold) occurred as well, although CFU-S production peaked at a relatively short 4 days. CFU-S and CFU-GM levels declined rapidly in culture, either because of unfavorable growth conditions or terminal differentiation. Attempts to remove toxic metabolites by increasing the media perfusion rate resulted in a boost in cell expansion capability by DBA/2J marrow. In bioreactors in which stromal cells were established before marrow inoculation, there was greater expansion of CFU-S (especially by DBA/2J) and CFU-GM, although total cell yield appeared to be unaffected, perhaps because the maximum cell density had already been reached. The relative high potential for CFU-S expansion measured in DBA/2J marrow over that of C57BL/6J will be useful in following genetic contributions to bone marrow production capacity. © 1995 Wiley-Liss, Inc.     

Application of bioreactors for large-scale micropropagation systems of plants

Summary The application of bioreactor culture techniques for plant micropropagation is regarded as one of the ways to reduce production cost by scaling-up and automation. Recent experiments are restricted to a small number of species that, however, demonstrate the feasibility of this technology. Periodic immersion liquid culture using ebb and flood system and column-type bubble bioreactors equipped with a raft support system to maintain plant tissues at the air and liquid interface were found to be suitable for micropropagation of plants via the organogenic pathway. Balloon-type bubble bioreactors proved to be fit for micropropagation via somatic embryogenesis with less shear stress on cultured cells. Several cultivars of Lilium were successfully propagated using a two-stage culture method in one bioreactor. A large number of small-scale segments were cultured for 4 wk with periodic immersion liquid culture to induce multiple bulblets from each segment, then the bulblet induction medium was changed into bulblet growth medium by employing a submerged liquid bioreactor system. This culture method resulted in a nearly 10-fold increase in bulblet growth compared to conventional culture with solid medium. About 20 000 cuttings of virus-free potato could be obtained from 120 singlenode explants in a 20-liter balloon-type bubble bioreactor after 8 wk of culture. The percentage of ex vitro survival and root induction of the cuttings was more than 95%. Other successful results were obtained from the micropropagation and transplant production of chrysanthemum, sweetpotato, Chinese foxglove. Propagation systems via somatic embryogenesis in Acanthopanax koreanum and thornless Aralia elata were established using a liquid suspension of embryogenic determined cells. More than 500 000 somatic embryos in different stages were harvested from a 10-liter balloon-type bubble bioreactor after a 6-wk culture. Further development of these embryos in solid medium and eventually in the field was successful. The bioreactor system could reduce initial and operational cost for micropropagation, but further development of sophisticated technology might be needed to apply this system to plant micropropagation industries.     

Modified CelliGen-packed bed bioreactors for hybridoma cell cultures

This study describes two packed bed bioreactor configurations which were used to culture a mouse-mouse hybridoma cell line (ATCC HB-57) which produces an IgG₁ monoclonal antibody. The first configuration consists of a packed column which is continuously perfused by recirculating oxygenated media through the column. In the second configuration, the packed bed is contained within a stationary basket which is suspended in the vessel of a CelliGen^™ bioreactor. In this configuration, recirculation of the oxygenated media is provided by the CelliGen Cell Lift impeller. Both configurations are packed with disk carriers made from a non-woven polyester fabric. During the steady-state phase of continuous operation, a cell density of 10⁸ cells per cm³ of bed volume was obtained in both bioreactor configurations. The high levels of productivity (0.5 gram MAb per 1 of packed bed per day) obtained in these systems demonstrates that the culture conditions achieved in these packed bed bioreactors are excellent for the continuous propagation of hybridomas using media which contains low levels (1 %) of serum as well as serum-free media. These packed bed bioreactors allow good control of pH, dissolved oxygen and temperature. The media flows evenly over the cells and produces very low shear forces. These systems are easy to set up and operate for prolonged periods of time. The potential for scale-up using Fibra-cel carriers is enhanced due to the low pressure drop and low mass transfer resistance, which creates high void fraction approaching 90% in the packed bed.     

Suspension culture on microcarriers and as aggregates enables expansion and differentiation of pluripotent stem cells (PSCs)

Background aimsHuman pluripotent stem cells (PSCs) hold a great promise for promoting regenerative medical therapies due to their ability to generate multiple mature cell types and for their high expansion potential. However, cell therapies require large numbers of cells to achieve desired therapeutic effects, and traditional two-dimensional static culture methods cannot meet the required production demand for cellular therapies. One solution to this problem is scaling up expansion of PSCs in bioreactors using culture strategies such as growing cells on microcarriers or as aggregates in suspension culture.MethodsIn this study, we directly compared PSC expansion and quality parameters in microcarrier- and aggregate-cultures grown in single-use vertical-wheel bioreactors.ResultsWe showed comparable expansion of cells on microcarriers and as aggregates by day 6 with a cell density reaching 2.2 × 10⁶ cells/mL and 1.8 × 10⁶ cells/mL and a fold-expansion of 22- and 18-fold, respectively. PSCs cultured on microcarriers and as aggregates were comparable with parallel two-dimensional cultures and with each other in terms of pluripotency marker expression and retention of other pluripotency characteristics as well as differentiation potential into three germ layers, neural precursor cells and cardiomyocytes.ConclusionsOur study did not demonstrate a clear advantage between the two three-dimensional methods for the quality parameters assessed. This analysis adds support to the use of bioreactor systems for large scale expansion of PSCs, demonstrating that the cells retain key characteristics of PSCs and differentiation potential in suspension culture.     

Engineering challenges in high density cell culture systems

High density cell culture systems offer the advantage of production of bio-pharmaceuticals in compact bioreactors with high volumetric production rates; however, these systems are difficult to design and operate. First of all, the cells have to be retained in the bioreactor by physical means during perfusion. The design of the cell retention is the key to performance of high density cell culture systems. Oxygenation and media design are also important for maximizing the cell number. In high density perfusion reactors, variable cell density, and hence the metabolic demand, require constant adjustment of perfusion rates. The use of cell specific perfusion rate (CSPR) control provides a constant environment to the cells resulting in consistent production. On-line measurement of cell density and metabolic activities can be used for the estimation of cell densities and the control of CSPR. Issues related to mass transfer and mixing become more important at high cell densities. Due to the difference in mass transfer coefficients for oxygen and CO₂, a significant accumulation of dissolved CO₂ is experienced with silicone tubing aeration. Also, mixing is observed to decrease at high densities. Base addition, if not properly done, could result in localized cell lysis and poor culture performance. Non-uniform mixing in reactors promotes the heterogeneity of the culture. Cell aggregation results in segregation of the cells within different mixing zones. This paper discusses these issues and makes recommendations for further development of high density cell culture bioreactors.     

The umbilical cord matrix is a better source of mesenchymal stem cells (MSC) than the umbilical cord blood

Many studies have drawn attention to the emerging role of MSC (mesenchymal stem cells) as a promising population supporting new clinical concepts in cellular therapy. However, the sources from which these cells can be isolated are still under discussion. Whereas BM (bone marrow) is presented as the main source of MSC, despite the invasive procedure related to this source, the possibility of isolating sufficient numbers of these cells from UCB (umbilical cord blood) remains controversial. Here, we present the results of experiments aimed at isolating MSC from UCB, BM and UCM (umbilical cord matrix) using different methods of isolation and various culture media that summarize the main procedures and criteria reported in the literature. Whereas isolation of MSC were successful from BM (10:10) and (UCM) (8:8), only one cord blood sample (1:15) gave rise to MSC using various culture media [DMEM (Dulbecco's modified Eagle's medium) +5% platelet lysate, DMEM+10% FBS (fetal bovine serum), DMEM+10% human UCB serum, MSCGM®] and different isolation methods [plastic adherence of total MNC (mononuclear cells), CD3⁺/CD19⁺/CD14⁺/CD38⁺‐depleted MNC and CD133⁺‐ or LNGFR⁺‐enriched MNC]. MSC from UCM and BM were able to differentiate into adipocytes, osteocytes and hepatocytes. The expansion potential was highest for MSC from UCM. The two cell populations had CD90⁺/CD73⁺/CD105⁺ phenotype with the additional expression of SSEA4 and LNGFR for BM MSC. These results clearly exclude UCB from the list of MSC sources for clinical use and propose instead UCM as a rich, non‐invasive and abundant source of MSC.     

动物细胞培养用生物反应器及相关技术

动物细胞大量培养是生产生物制品的重要途径,它用到的关键设备是生物反应器。根据培养细胞、培养载体、培养液混合方式的不同,生物反应器主要有搅拌式、气升式、中空纤维式、回转式等,其中搅拌式规模最大。回转式是NASA于20世纪90年代中期开发的一种新型生物反应器,被誉为空间生物反应器,可用于组织工程研究。与生物反应器配套的技术主要有灌注、微载体、多孔微球、转入抗凋亡基因等,可以有效地提高细胞密度,增加生物制品产量,提高质量。今后生物反应器研制主要朝两个方向发展:一是,以高密度培养动物细胞生产蛋白质药物为目的,二是以三维培养动物细胞(主要是人类细胞)再生组织或器官为目的。     

Evaluation of criteria for bioreactor comparison and operation standardization for mammalian cell culture

Development of bioprocesses with mammalian cell culture deals with different bioreactor types and scales. The bioreactors might be intended for generation of cell inoculum and production, research, process development, validation, or transfer purposes. During these activities, not only the difficulty of up and downscaling might lead to failure of consistency in cell growth, but also the use of different bioreactor geometries and operation conditions. In such cases, criteria for bioreactor design and process transfer should be carefully evaluated in order to select appropriate cultivation parameters. In this work, power input, mixing time, impeller tip speed, and Reynolds number have been compared systematically for the cultivation of the human cell line AGE1.HN within three partner laboratories using five different bioreactor systems. Proper operation ranges for the bioreactors were identified using the maximal cell‐specific growth rate (μ_max) as indicator. Common optimum values for process transfer criteria were found in these geometrically different bioreactors, in which deviations of μ_max between cultivation systems can be importantly reduced. The data obtained in this work are used for process standardization and comparability of results obtained in different bioreactor systems, i.e. to guarantee lab‐to‐lab consistency for systems biology approaches using mammalian cells.     

Comparison of five methods for concentrating progenitor cells in human marrow transplantation

Enrichment of bone marrow (BM) aspirates is an important prerequisite prior to in vitro treatment or cryopreservation. In this regard, we have analyzed the results obtained on 190 BM processed by the following 5 techniques: HES sedimentation with centrifugation; COBE 2991 blood cell processor; Ficoll/hypaque (F/H) gradient centrifugation; Continuous flow cell separator (CS 3000 Fenwal); Semicontinuous blood cell separator (Dideco T 90). Each procedure was evaluated by measuring the recovery of nucleated marrow cells (NC), mononuclear cells (MNC), committed progenitor cells (CFU-GM), the reduction of BM volume and the removal of red blood cells (RBC) and polymorphonuclear cells (PMN). The results of this comparative study show that F/H gradient on a COBE 2991 cell washer provides the most efficient system for purifying a MNC fraction (89% recovery) from unwanted cells (RBC less than 2% and PMN less than 2%) in a very small volume (98% reduction) with a good recovery of CFU-GM (80%).     

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.     

Periodic harvesting of embryonic stem cells from a hollow‐fiber membrane based four‐compartment bioreactor

Different types of stem cells have been investigated for applications in drug screening and toxicity testing. In order to provide sufficient numbers of cells for such in vitro applications a scale‐up of stem cell culture is necessary. Bioreactors for dynamic three‐dimensional (3D) culture of growing cells offer the option for culturing large amounts of stem cells at high densities in a closed system. We describe a method for periodic harvesting of pluripotent stem cells (PSC) during expansion in a perfused 3D hollow‐fiber membrane bioreactor, using mouse embryonic stem cells (mESC) as a model cell line. A number of 100 × 10⁶ mESC were seeded in bioreactors in the presence of mouse embryonic fibroblasts (MEF) as feeder cells. Over a cultivation interval of nine days cells were harvested by trypsin perfusion and mechanical agitation every second to third culture day. A mean of 380 × 10⁶ mESC could be removed with every harvest. Subsequent to harvesting, cells continued growing in the bioreactor, as determined by increasing glucose consumption and lactate production. Immunocytochemical staining and mRNA expression analysis of markers for pluripotency and the three germ layers showed a similar expression of most markers in the harvested cells and in mESC control cultures. In conclusion, successful expansion and harvesting of viable mESC from bioreactor cultures with preservation of sterility was shown. The present study is the first one showing the feasibility of periodic harvesting of adherent cells from a continuously perfused four‐compartment bioreactor including further cultivation of remaining cells. © 2015 American Institute of Chemical Engineers Biotechnol. Prog., 32:141–151, 2016     

Aujeszky’s disease virus production in disposable bioreactor

A novel, disposable-bag bioreactor system that uses wave action for mixing and transferring oxygen was evaluated for BHK 21 C13 cell line growth and Aujeszky’s disease virus (ADV) production. Growth kinetics of BHK 21 C13 cells in the wave bioreactor during 3-day period were determined. At the end of the 3-day culture period and cell density of 1.82 × 10⁶ cells ml^-1, the reactor was inoculated with 9 ml of gE^- Bartha K-61 strain ADV suspension (10^5.9 TCID₅₀) with multiplicity of infection (MOI) of 0.01. After a 144 h incubation period, 400 ml of ADV harvest was obtained with titre of 10^7.0 TCID₅₀ ml⁻¹, which corresponds to 40,000 doses of vaccine against AD. In conclusion, the results obtained with the wave bioreactor using BHK 21 C13 cells showed that this system can be considered as suitable for ADV or BHK 21 C13 cell biomass production.     

Large‐scale culture of a megakaryocytic progenitor cell line with a single‐use bioreactor system

The increasing application of regenerative medicine has generated a growing demand for stem cells and their derivatives. Single‐use bioreactors offer an attractive platform for stem cell expansion owing to their scalability for large‐scale production and feasibility of meeting clinical‐grade standards. The current work evaluated the capacity of a single‐use bioreactor system (1 L working volume) for expanding Meg01 cells, a megakaryocytic (MK) progenitor cell line. Oxygen supply was provided by surface aeration to minimize foaming and orbital shaking was used to promote oxygen transfer. Oxygen transfer rates (k_La) of shaking speeds 50, 100, and 125 rpm were estimated to be 0.39, 1.12, and 10.45 h^?1, respectively. Shaking speed was a critical factor for optimizing cell growth. At 50 rpm, Meg01 cells exhibited restricted growth due to insufficient mixing. A negative effect occurred when the shaking speed was increased to 125 rpm, likely caused by high hydrodynamic shear stress. The bioreactor culture achieved the highest growth profile when shaken at 100 rpm, achieving a total expansion rate up to 5.7‐fold with a total cell number of 1.2 ± 0.2 × 10⁹ cells L^?1. In addition, cells expanded using the bioreactor system could maintain their potency to differentiate following the MK lineage, as analyzed from specific surface protein and morphological similarity with the cells grown in the conventional culturing system. Our study reports the impact of operational variables such as shaking speed for growth profile and MK differentiation potential of a progenitor cell line in a single‐use bioreactor. © 2017 American Institute of Chemical Engineers Biotechnol. Prog., 34:362–369, 2018     

Compact Cell Settlers for Perfusion Cultures of Microbial (and Mammalian) Cells

As microbial secretory expression systems have become well developed for microbial yeast cells, such as Saccharomyces cerevisiae and Pichia pastoris, it is advantageous to develop high cell density continuous perfusion cultures of microbial yeast cells to retain the live and productive yeast cells inside the perfusion bioreactor while removing the dead cells and cell debris along with the secreted product protein in the harvest stream. While the previously demonstrated inclined or lamellar settlers can be used for such perfusion bioreactors for microbial cells, the size and footprint requirements of such inefficiently scaled up devices can be quite large in comparison to the bioreactor size. Faced with this constraint, we have now developed novel, patent‐pending compact cell settlers that can be used more efficiently with microbial perfusion bioreactors to achieve high cell densities and bioreactor productivities. Reproducible results from numerous month‐long perfusion culture experiments using these devices attached to the 5 L perfusion bioreactor demonstrate very high cell densities due to substantial sedimentation of the larger live yeast cells which are returned to the bioreactor, while the harvest stream from the top of these cell settlers is a significantly clarified liquid, containing less than 30% and more typically less than 10% of the bioreactor cell concentration. Size of cells in the harvest is smaller than that of the cells in the bioreactor. Accumulated protein collected from the harvest and rate of protein accumulation is significantly (> 6x) higher than the protein produced in repeated fed‐batch cultures over the same culture duration. © 2017 American Institute of Chemical Engineers Biotechnol. Prog., 33:913–922, 2017     

A cell-detaching reactor for inoculation of anchorage-dependent CHD and Vero cells between stepwise-expanded bioreactors

A cell-detaching reactor was developed to collect cells growing on microcarriers for inoculation between stepwise-expanded bioreactors. It consisted of a trypsinization zone and a separation zone, which were separated by a 200-mesh stainless steel screen. The screen allowed the cells only to pass through to the next bioreactor, after the cells have been trypsinized and detached from microcarriers. The operating feasibility of the cell-detaching reactor was tested with anchorage-dependent recombinant Chinese hamster ovary (rCHO) and African green monkey kidney (Vero) cells. rCHO and Vero cells were first cultured in a small microcarrier bioreactor, and then inoculated via the cell-detaching reactor into either a packed-bed bioreactor (for rCHO cells) or a larger microcarrier bioreactor (for Vero cells). For rCHO cells, the cell density reached 1.3 × 10⁷ cells/ml in the perfusion culture, and Vero cells reached 1.3 × 10⁶ cells/ml in the batch culture.     

CO2 accumulation in bioreactor suspension cultures of Cyclamen persicum Mill. and its effect on cell growth and regeneration of somatic embryos

CO₂ accumulation in different culture systems containing embryogenic cell suspension cultures of cyclamen (Cyclamen persicum Mill.) was analyzed. In bioreactors equipped with a bubble-free or a bubble aeration system, CO₂ mole fractions in the gas phase of more than 10% were determined whereas in Erlenmeyer flasks, CO₂ mole fractions were below 2%. CO₂ accumulation in bioreactors was severely growth inhibiting in comparison to the flasks. By removing CO₂ in the aeration gas of a bubble-free aerated bioreactor, cell growth comparable to that in flasks was achieved. The regeneration ability of cell suspensions after being cultured in bioreactors with CO₂ accumulation was better than those after culture in bioreactors without CO₂ accumulation or in flasks. Received: 16 June 1998 / Revision received: 13 August 1998 / Accepted: 1 December 1998