Scale-up of mouse embryonic stem cell expansion in stirred bioreactors

The aim of this study was to develop a robust, quality controlled and reproducible large-scale culture system using serum-free (SF) medium to obtain vast numbers of embryonic stem (ES) cells as a starting source for potential applications in tissue regeneration, as well as for drug screening studies. Mouse ES (mES) cells were firstly cultured on microcarriers in spinner flasks to investigate the effect of different parameters such as the agitation rate and the feeding regimen. Cells were successfully expanded at agitation rates up to 60 rpm using the SF medium and no significant differences in terms of growth kinetics or metabolic profiles were found between the two feeding regimens evaluated: 50% medium renewal every 24 h or 25% every 12 h. Overall, cells reached maximum concentrations of (4.2 ± 0.4) and (5.6 ± 0.8) ×10(6) cells/mL at Day 8 for cells fed once or twice per day; which corresponds to an increase in total cell number of 85 ± 7 and 108 ± 16, respectively. To have a more precise control over culture conditions and to yield a higher number of cells, the scale-up of the spinner flask culture system was successfully accomplished by using a fully controlled stirred tank bioreactor. In this case, the concentration of mES cells cultured on microcarriers increased 85 ± 15-fold over 11 days. Importantly, mES cells expanded under stirred conditions, in both spinner flask and fully controlled stirred tank bioreactor, using SF medium, retained the expression of pluripotency markers such as Oct-4, Nanog, and SSEA-1 and their differentiation potential into cells of the three embryonic germ layers.     

Dynamic cell culture on porous biopolymer microcarriers in a spinner flask for bone tissue engineering: a feasibility study

Porous microspherical carriers have great promise for cell culture and tissue engineering. Dynamic cultures enable more uniform cell population and effective differentiation than static cultures. Here we applied dynamic spinner flask culture for the loading and multiplication of cells onto porous biopolymer microcarriers. The abilities of the microcarriers to populate cells and to induce osteogenic differentiation were examined and the feasibility of in vivo delivery of the constructs was addressed. Over time, the porous microcarriers enabled cell adhesion and expansion under proper dynamic culture conditions. Osteogenic markers were substantially expressed by the dynamic cell cultures. The cell-cultured microcarriers implanted in the mouse subcutaneous tissue for 4 weeks showed excellent tissue compatibility, with minimal inflammatory signs and significant induction of bone tissues. This first report on dynamic culture of porous biopolymer microcarriers providing an effective tool for bone tissue engineering.     

Mouse embryonic stem cell expansion in a microcarrier-based stirred culture system

Embryonic stem (ES) cells have the ability to differentiate in vitro into a wide variety of cell types with potential applications for tissue regeneration. However, a large number of cells are required, thus strengthening the need to develop large-scale systems using chemically defined media for ES cell production and/or controlled differentiation. In the present studies, a stirred culture system (i.e. spinner flask) was used to scale-up mouse ES (mES) cell expansion in serum-containing (DMEM/FBS) or serum-free medium, both supplemented with leukemia inhibitory factor (LIF), using either Cytodex 3 or Cultispher S microcarriers. After 8 days, maximal cell densities achieved were (1.9+/-0.1), (2.6+/-0.7) and 3.5x10(6)cells/mL for Cytodex 3 in DMEM/FBS, Cultispher S in DMEM/FBS and Cultispher S in serum-free cultures, respectively, with fold increases of 38+/-2, 50+/-15 and 70. Both microcarriers were suitable to sustain mES cell expansion, though the macroporous Cultispher S seemed to be advantageous in providing a more protective environment against shear stress forces, which harmful effects are exacerbated in serum-free conditions. Importantly, mES cells expanded under stirred conditions using serum-free medium retained their pluripotency and the ability to commit to the neural lineage.     

人皮肤成纤维细胞在不同培养系统中的生长代谢特性

大面积烧伤病人及多种皮肤溃疡病人很难用自体皮肤移植来进行治疗.早期治疗方法采用尸体来源的皮肤移植,但由于来源有限、且有传播疾病的危险,因此应用组织工程技术构建生物活性人工皮肤已成为近十几年来在组织工程和创伤治疗领域的研究热点,目前已有几种人工皮肤成功地走向临床[1].然而,在构建大面积皮肤组织过程中,如何大量制备皮肤种子细胞仍然是一大棘手的难题,成为人体皮肤组织工程迫切需要解决的技术关键.获得大量扩增的皮肤细胞,解决种子细胞的供应问题,是构建人工皮肤的一个关键.     

Evaluation of production parameters with the vaccinia virus expression system using microcarrier attached HeLa cells

Parameters that affect production of the recombinant reporter protein, EGFP, in the T7 promoter based VOTE vaccinia virus-HeLa cell expression system were examined. Length of infection phase, inducer concentration, and timing of its addition relative to infection were evaluated in 6-well plate monolayer cultures. One hour infection with 1.0 mM IPTG added at the time of infection provided a robust process. For larger scale experiments, anchorage-dependent HeLa cells were grown on 5 g/L Cytodex 3 microcarriers. The change to this dynamic culture environment, with cell-covered microcarriers suspended in culture medium in spinner flasks, suggested a re-examination of the multiplicity of infection (MOI) for this culture type that indicated a need for an increase in the number of virus particles per cell to 5.0, higher than that needed for complete infection in monolayer tissue flask culture. Additionally, dissolved oxygen level and temperature during the protein production phase were evaluated for their effect on EGFP expression in microcarrier spinner flask culture. Both increased dissolved oxygen, based on surface area to volume (SA/V) adjustments, and decreased temperature from 37 to 31 degrees C showed increases in EGFP production over the course of the production phase. The level of production achieved with this system reached approximately 17 microg EGFP/10(6) infected cells.     

Japanese encephalitis virus production in Vero cells with serum-free medium using a novel oscillating bioreactor.

A novel oscillating bioreactor, BelloCell, was successfully applied for the cultivation of Vero cells using serum-free medium, and the production of Japanese encephalitis virus. The BelloCell requires no air sparging, pumping, or agitation, and thus provides a low shear environment. Owing to its simple design, BelloCell is extremely easy to handle and operate. Using this BelloCell (500 ml culture), Vero cells reached a maximum number of 2.8 x 10(9) cells and the Japanese encephalitis virus yield reached 6.91 x 10(11) PFU, versus 9.0 x 10(8) cells and 2.98 x 10(11) PFU using a spinner flask (500 ml) with microcarriers. The cell yield and virus production using BelloCell were markedly higher than with microcarrier culture. The neutralizing capacity of the Japanese encephalitis virus produced using BelloCell was equal to that using a microcarrier system. Therefore, these benefits should enable BelloCell to be adopted as a simple system for high population density cell culture and virus production.     

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。     

Bead-to-bead transfer of chinese hamster ovary cells using macroporous microcarriers

Chinese hamster ovary cells (CHO-K1) were cultivated in macroporous gelatin microcarriers (CultiSpher G and CultiSpher S) in spinner flasks and a 5 1 bioreactor. Near-to-confluent cultures were harvested by bead-to-bead transfer where intact microcarriers with cells were transferred from a spinner flask to another spinner flask or to the bioreactor with naked microcarrier beads. Successful bead-to-bead transfer was achieved in various split ratios. The duration of attachment seemed to be important where the direct contact of beads to each other can be achieved by intermittent stirring. Repeated transfers were performed and at least four transfers in spinner flasks were achieved.Two variations of bead-to-bead transfer were performed in the 5 1 bioreactor either by seeding the bioreactor with near-to-confluent beads cultivated in spinner flasks orin situ transfer by adding fresh beads to the bioreactor. As in the spinner case, attachment was achieved by intermittent stirring where donor beads were in close proximity to the acceptor beads. Again successful transfers were obtained as evidenced by the good growth on acceptor beads where cell yields were in the range of 3100–4500 cells/bead.The results suggest that bead-to-bead transfer of CHO-K1 cells can be easily performed and do provide an alternative route to applications where dissolution techniques may not offer an efficient solution.     

Two-dimensional versus three-dimensional culture systems: Effects on growth and productivity of BHK cells

The influence of surface growth (two-dimensional microcarriers) and three-dimensional growth (aggregates and macroporous supports) in agitated, suspended batch culture systems upon growth and productivity of BHK was compared. Cultures using three porous microcarriers (CultiSpher G, Cellsnow EX, and Cytocell), one nonporous microcarrier (Cytodex 3) and natural aggregates were performed in stirred tanks using two different agitation rates (60 and 100 RPM). With the exception of Cytocell, cell growth, viability, and productivity were similar when three-dimensional structures (porous microcarriers and aggregates) were used. Nonporous microcarriers only compared well at 60 RPM as growth ceased under overagitation. These results suggest that cultures less susceptible to fluid shear are advantageous for scale-up. (c) 1996 John Wiley & Sons, Inc.     

Defined Essential 8? Medium and Vitronectin Efficiently Support Scalable Xeno-Free Expansion of Human Induced Pluripotent Stem Cells in Stirred Microcarrier Culture Systems

Human induced pluripotent stem (hiPS) cell culture using Essential 8™ xeno-free medium and the defined xeno-free matrix vitronectin was successfully implemented under adherent conditions. This matrix was able to support hiPS cell expansion either in coated plates or on polystyrene-coated microcarriers, while maintaining hiPS cell functionality and pluripotency. Importantly, scale-up of the microcarrier-based system was accomplished using a 50 mL spinner flask, under dynamic conditions. A three-level factorial design experiment was performed to identify optimal conditions in terms of a) initial cell density b) agitation speed, and c) to maximize cell yield in spinner flask cultures. A maximum cell yield of 3.5 is achieved by inoculating 55,000 cells/cm² of microcarrier surface area and using 44 rpm, which generates a cell density of 1.4x10⁶ cells/mL after 10 days of culture. After dynamic culture, hiPS cells maintained their typical morphology upon re-plating, exhibited pluripotency-associated marker expression as well as tri-lineage differentiation capability, which was verified by inducing their spontaneous differentiation through embryoid body formation, and subsequent downstream differentiation to specific lineages such as neural and cardiac fates was successfully accomplished. In conclusion, a scalable, robust and cost-effective xeno-free culture system was successfully developed and implemented for the scale-up production of hiPS cells.     

Low-molecular-weight inhibitors of cell differentiation enable efficient growth of mouse iPS cells under feeder-free conditions

Embryonic stem cells and induced pluripotent stem (iPS) cells are usually maintained on feeder cells derived from mouse embryonic fibroblasts (MEFs). In recent years, the cell culture of iPS cells under serum- and feeder-free conditions is gaining attention in overcoming the biosafety issues for clinical applications. In this study, we report on the use of multiple small-molecular inhibitors (i.e., CHIR99021, PD0325901, and Thiazovivin) to efficiently cultivate mouse iPS cells without feeder cells in a chemically-defined and serum-free condition. In this condition, we showed that mouse iPS cells are expressing the Nanog, Oct3/4, and SSEA-1 pluripotent markers, indicating that the culture condition is optimized to maintain the pluripotent status of iPS cells. Without these small-molecular inhibitors, mouse iPS cells required the adaptation period to start the stable cell proliferation. The application of these inhibitors enabled us the shortcut culture method for the cellular adaptation. This study will be useful to efficiently establish mouse iPS cell lines without MEF-derived feeder cells.     

Production of mouse embryoid bodies with hepatic differentiation potential by stirred tank bioreactor

Embryonic stem (ES) cells can differentiate into functional hepatic lineage cells, which can potentially be used in biomedicine. To obtain hepatic lineage cells from ES cells, embryoid bodies (EBs) must be formed. In this study, we developed an EB formation system using a spinner flask for mass production of EBs. ES cells were inoculated into the spinner flask, where they formed EBs within 4 d. The EBs were then transferred into an attached culture for hepatic differentiation. To verify the hepatic lineage cells, albumin secretion and hepatic-specific gene expression were examined. We found that EBs formed by either the spinner flask or hanging drops exhibited similar albumin secretion potential and hepatic-specific gene expression. We conclude that the spinner flask method can be used to produce mouse EBs that can be used to mass produce hepatic lineage cells for use in biomedicine.     

培养方式对真皮组织体外构建的影响

采用静态培养和转瓶培养方式分别构建真皮组织,考察培养方式和搅拌转速对细胞在三维支架材料中增殖、代谢、分布的影响。结果表明,由转瓶培养方式构建的细胞-材料复合物,其最终细胞密度和细胞比生长速率均明显高于静态培养（14.2~27.6×106 cells/cm3 vs 10.1×106 cells/cm3和0.145~0.262 d-1 vs 0.111 d-1）,而转速达80 r/min的转瓶尤其突出;静态培养的细胞-材料复合物内部细胞稀少,且分布不均匀,转瓶培养的细胞-材料复合物在材料表面和内部细胞密度都有所提高,分布情况也得到改善,且80 r/min转瓶培养的组织其细胞密度和分布均优于10 r/min和40 r/min转瓶培养。转瓶培养在其转速达到一定强度时能明显提高细胞在支架中的增殖速率,缩短培养时间,并有效改善细胞在支架内的分布,是一种理想的培养方式。     

Production of Mouse Embryoid Bodies with Hepatic Differentiation Potential by Stirred Tank Bioreactor

Embryonic stem (ES) cells can differentiate into functional hepatic lineage cells, which can potentially be used in biomedicine. To obtain hepatic lineage cells from ES cells, embryoid bodies (EBs) must be formed. In this study, we developed an EB formation system using a spinner flask for mass production of EBs. ES cells were inoculated into the spinner flask, where they formed EBs within 4 d. The EBs were then transferred into an attached culture for hepatic differentiation. To verify the hepatic lineage cells, albumin secretion and hepatic-specific gene expression were examined. We found that EBs formed by either the spinner flask or hanging drops exhibited similar albumin secretion potential and hepatic-specific gene expression. We conclude that the spinner flask method can be used to produce mouse EBs that can be used to mass produce hepatic lineage cells for use in biomedicine.     

在静态和动态培养条件下杂交瘤细胞的生长和代谢

通过对WuT3杂交瘤细胞在静态和动态培养条件下的比较,发现细胞生长和代谢有很大不同。在静态培养条件下,细胞培养周期较长,细胞密度较高;但在动态培养条件下,细胞代谢更加旺盛,葡萄糖、氨基酸等营养物质的消耗加快,乳酸、氨、丙氨酸等代谢产物的比生成速率较大。     

Increased rate of chondrocyte aggregation in a wavy-walled bioreactor

A novel wavy-walled bioreactor designed to enhance mixing at controlled shear stress levels was used to culture chondrocytes in suspension. Chondrocyte aggregation in suspensions mixed at 30, 50, and 80 rpm was characterized in the wavy-walled bioreactor and compared with that in conventional smooth-walled and baffled-walled spinner flask bioreactors. Aggregation was characterized in terms of the percentage of cells that aggregated over time, and aggregate size changes over time. The kinetics of chondrocyte aggregation observed in the bioreactors was composed of two phases: early aggregation between 0 and 2 h of culture, and late aggregation between 3 and 24 h of culture. At 50 rpm, the kinetics of early aggregation in the wavy-walled bioreactor was approximately 25% and 65% faster, respectively, than those in the smooth-walled and baffled-walled spinner flask bioreactors. During the late aggregation phase, the kinetics of aggregation in the wavy-walled bioreactor were approximately 45% and 65% faster, respectively, than in the smooth-walled and baffled-walled spinner flasks. The observed improved kinetics of chondrocyte aggregation was obtained at no cost to the cell survival rate. Results of computerized image analysis suggest that chondrocyte aggregation occurred initially by the formation of new aggregates via cell-cell interactions and later by the joining of small aggregates into larger cell clumps. Aggregates appeared to grow for only a couple of hours in culture before reaching a steady size, possibly determined by limitations imposed by the hydrodynamic environment. These results suggest that the novel geometry of the wavy-walled bioreactor generates a hydrodynamic environment distinct from those traditionally used to culture engineered cartilage. Such differences may be useful in studies aimed at distinguishing the effects of the hydrodynamic environment on tissue-engineered cartilage. Characterizing the wavy-walled bioreactor's hydrodynamic environment and its effects on cartilage cell/tissue culture can help establish direct relationships between hydrodynamic forces and engineered tissue properties.     

On line estimation of oxygen uptake rate for insect cells growing in a modified spinner flask

The simple design of traditional spinner flasks makes the on-line estimation of cellular metabolism impossible. An on-line estimation system has been developed and used for the monitoring of oxygen uptake rate (OUR) for insect cells growing in a modified spinner flask. Neglect of oxygen desorption from culture media is a common source of error in OUR measurements for Sf21 cells. Therefore, an algorithm was developed to compensate for the affect of such desorption process on the determination of OUR. A modified spinner flask was successfully used as a low-volume bioreactor for insect cell cultivation and the OUR measurement developed here is both convenient and reliable.     

Vero细胞微载体培养的化学成分明确无血清培养基的设计

目的：设计适用于Vero细胞微载体培养的化学成分明确无血清培养基。方法：以商品化的DMEM／F12合成培养基为基础培养基,应用Plackett—Burman实验设计和响应面分析法设计支持Vero细胞微载体培养的化学成分明确无血清培养基。结果：以细胞密度为评价指标,在单因素实验的基础上采用Plackett-Burman实验设计考察10种培养基添加成分对Vero细胞生长的影响,确定了3种对Vero细胞生长起明显促进作用的培养基添加成分,为胰岛素、血清素和腐胺。继而利用响应面法分析了这3种添加成分的最佳水平范围,设计了一种支持Vero细胞贴附培养的无血清培养基（VERO—SFM—A）。在Bellco搅拌式培养瓶中采用VERO-SFM．A和Cytodex1微载体培养Vero细胞,细胞密度由接种时的4×10^5cells／ml增加到培养6d后的22．3×10^cells／ml,细胞活力保持在96％以上。结论：VERO—SFM—A能够有效地支持Vero细胞在微载体表面固定化生长并达到较高的细胞密度,具有实际应用于Vero细胞微载体规模化培养的应用潜力。     

Comparisons of microcarrier cell culture processes in one hundred mini-liter spinner flask and fifteen-liter bioreactor cultures

Microcarrier cell culture process can be used to culture anchorange-dependent cells in large bioreactor vessels. The process performance in large bioreactors is usually less prominent than that in spinner flask vessels and bench scale reactors. In this study we investigated the microcarrier cell culture processes in 100?ml spinner flask and 15-liter bioreactor cultures, including the kinetics for cell attachment, cell growth and the production of Japanese encephaltilis vaccine strain (Beijing-1) virus. Under a fixed concentration of microcarrier and cell density used in inoculations, the attachment kinetics of Vero cells on Cytodex 1 microcarrier in a 15-liter bioreactor vessel was 2 folds slower than with 100?ml spinner flask culture. Virus replication in 15-liter bioreactor culture also revealed an approximately one day lag-time compared to 100?ml spinner flask culture. Findings presented herein provide valuable information for designing and operating microcarrier cell culture processes in large bioreactor vessels.     

Evaluation of different culture techniques of osteoblasts on 3D scaffolds

Bones adjust their structure to withstand the mechanical demands they experience. It is suggested that flow-derived shear stress may be the most significant and primary mediator of mechanical stimulation. In this study, we designed and fabricated a fluid flow cell culture system that can load shear stress onto cells cultured on 3D scaffolds. We evaluated the effect of different culture techniques, namely, (1) continuous perfusion fluid flow, (2) intermittent perfusion fluid flow, and (3) static condition, on the proliferation of osteoblasts seeded on partially deproteinized bones. The flow rate was set at 1 ml/min for all the cells cultured using flow perfusion and the experiment was conducted for 12 days. Scanning electron microscopy analysis indicated an increase in cell proliferation for scaffolds subjected to fluid shear stress. In addition, the long axes of these cells lengthened along the flowing fluid direction. Continuous perfusion significantly enhanced cell proliferation compared to either intermittent perfusion or static condition. All the results demonstrated that fluid shear stress is able to enhance the proliferation of cells and change the form of cells.