VERO细胞生物反应器放大培养初探

目的:研究用生物反应器放大进行Vero细胞微载体培养,实现生物反应器之间Veto细胞放大培养.方法:5L微载体生物反应器以10g/L微载体浓度培养Vero细胞,96h时经漂洗、消化、接种于30L微载体生物反应器,实现放大后的30L微载体生物反应器细胞怏速增殖,期间对不同时期的微载体细胞进行细胞计数、细胞代谢分析和形态观察.结果:5L生物反应器细胞经过96h灌注培养,平均细胞密度达到7.81×10~6cells/mL.5L微载体细胞放大到30L微载体生物反应器,平均细胞收获率为32.3%;放大到30L生物反应器后经过144h培养,细胞密度达到9.19×10~6cells/mL;放大后的细胞代谢途径依然以葡萄糖氧化代谢乳酸为主.结论:生物反应器由5L到30L进行Veto细胞放大培养是可行的.     

转瓶培养与生物反应器微载体培养乙脑病毒的比较

分别用15L转瓶与15L生物反应器微载体(2.5g/L CytodexⅢ)系统培养Vero细胞并接种乙型脑炎病毒(简称乙脑病毒)。转瓶培养Vero细胞7~8d,细胞数最高能达到8×108;当单层细胞长至3.0~4.5×108时接种乙脑病毒,病毒滴度能达到6.5~6.98 lg PFU/ml,并能够连续收获4~5次;采用微载体系统培养Vero细胞,细胞密度最高能达到170×108;当单层细胞长至60~70×108时接种乙脑病毒,病毒滴度能达到7~7.5 lg PFU/ml,并能够连续收获13~15次。两种方式培养的乙脑病毒收获液分别经灭活、浓缩、柱层析纯化后制备Vero细胞乙脑纯化疫苗,各项检定指标均符合《中国药典》的相关要求。     

微载体培养动物细胞技术的研究进展

微载体是一种新兴的大规模细胞培养技术,是当前贴壁依赖型细胞大规模培养的主要方法。它具有均相培养兼具平板培养和悬浮培养的优势,培养条件(温度、pH值、二氧化碳浓度等)容易控制,并且培养过程系统化、自动化,不易被污染。本文简要介绍了近几年来常用的几种制备微载体的天然聚合材料,比较了固体微载体和液体微载体各自特点,列举了微载体培养技术的几种生物反应器系统。     

小牛皮提取的胶原－微载体用于贴壁细胞大规模培养

由于胶原蛋白具有与含牛血清培养基中纤粘素(Fibronectin)一类物质相结合的特点,因而胶原是一类来源广泛的可用作制备细胞培养介质的优良基质。经过各种形式的细胞培养试验,以变性胶原为材料合成得到的GT一2微载体可成功地用于Vero,CHO、Bowes以及鱼类细胞的贴壁培养。培养规模包括不同容积的静置培养,滚瓶培养以及1．5L和20L进口和国产生物反应器的大规模细胞培养。     

VerO细胞在气升式反应器中的微载体培养

哺乳动物细胞的大规模培养是生产许多医学上重要生物制品的一种主要方法之－⑴。很多有工业价值的动物细胞都是贴壁细胞,必须附着在一定的表面上才能生长,微载体培养是一种有效的体系⑵。用于微载体培养的反应器多为搅拌式反应器,近年来,流化床式反应器越来越引起生化工程学家的重视。有希望用于大规模动物细胞培养的主要是液升和气升式。液升式反应器的优点是培养液可以间接氧饱和,气泡和细胞不直接接触。在气升式流态反应器中,气泡与细胞直接接触,其优点是操作方便,设备筒单。本文报道通过气升流态化反应器实现高密度贴壁细胞培养工艺条件的研究。     

甘草细胞放大培养中搅拌式反应器操作策略优化

为获得甘草细胞在反应器中放大培养的最佳条件,在建立稳定的甘草细胞搅拌式生物反应器放大培养体系的基础上,分别以单因素和正交实验获得的数据为样本,以细胞净增长生物量为考察指标,运用BP神经网络耦合遗传算法对反应器操作策略进行优化。结果表明,接种量6.4%、摇床转速89r/min、通气速率0.1vvm是甘草细胞进行反应器培养的最优条件;与传统的正交实验方法相比,这种基于神经网络耦合遗传算法的优化方法使反应器中细胞生物量的积累提高了6.9%。     

MDCK细胞微载体悬浮培养放大工艺研究

MDCK细胞对各种流感病毒具有高度敏感性,广泛应用于流感病毒的分离和疫苗制备.通过探索培养基中促进细胞贴壁的关键组分,并筛选水解物,开发了适合MDCK细胞生长的低血清培养基.发现钙、镁离子是细胞贴壁不可缺少的物质,麦麸水解物可以部分代替培养基中的血清.利用该低血清培养基,经过消化转移将MDCK细胞从5L反应器放大至25 L反应器,微载体上细胞贴附均匀、生长旺盛,25 L反应器中培养48 h细胞密度可达30.5×105 cells/ml.研究结果为工业规模反应器微载体悬浮培养MDCK细胞生产流感病毒奠定了基础.     

长春花培养细胞在摇瓶和生物反应器中生长和生物碱生成的比较

比较了不同体积摇瓶和１６Ｌ（工作体积１０Ｌ）搅拌式生物反应器中长春花（Ｃａｔｈａｒａｎｔｈｕｓｒｏｓｅｕｓ（Ｌ．）Ｇ．Ｄｏｎ）培养细胞生长和生物碱生成情况,发现在摇瓶中小规模放大培养,细胞生长和生物碱生成无显著差异,摇瓶体积不变而培养物体积增加时,细胞干重和生物碱生成均下降。反应器中培养细胞干重与摇瓶中相当,但生物碱含量大大下降。从而提示,培养环境的改变,特别是通气状况和剪切力是培养细胞从摇瓶到反应器放大过程中影响生物碱生成的主要因素。     

Bioreactors to influence stem cell fate: Augmentation of mesenchymal stem cell signaling pathways via dynamic culture systems

Background

Mesenchymal stem cells (MSCs) are a promising cell source for bone and cartilage tissue engineering as they can be easily isolated from the body and differentiated into osteoblasts and chondrocytes. A cell based tissue engineering strategy using MSCs often involves the culture of these cells on three-dimensional scaffolds; however the size of these scaffolds and the cell population they can support can be restricted in traditional static culture. Thus dynamic culture in bioreactor systems provides a promising means to culture and differentiate MSCs in vitro.

Scope of review

This review seeks to characterize key MSC differentiation signaling pathways and provides evidence as to how dynamic culture is augmenting these pathways. Following an overview of dynamic culture systems, discussion will be provided on how these systems can effectively modify and maintain important culture parameters including oxygen content and shear stress. Literature is reviewed for both a highlight of key signaling pathways and evidence for regulation of these signaling pathways via dynamic culture systems.

Major conclusions

The ability to understand how these culture systems are affecting MSC signaling pathways could lead to a shear or oxygen regime to direct stem cell differentiation. In this way the efficacy of in vitro culture and differentiation of MSCs on three-dimensional scaffolds could be greatly increased.

General significance

Bioreactor systems have the ability to control many key differentiation stimuli including mechanical stress and oxygen content. The further integration of cell signaling investigations within dynamic culture systems will lead to a quicker realization of the promise of tissue engineering and regenerative medicine. This article is part of a Special Issue entitled Biochemistry of Stem Cells.     

Getting ready for PAT: Scale up and inline monitoring of protein refolding of Npro fusion proteins

Screening for optimal refolding conditions for recombinant protein overexpressed in Escherichia coli as inclusion bodies is often carried out on micro-scale in non-agitated reactors. Currently, scale up of refolding of N^pro fusion proteins is based on geometric similarity and constant Re number. Refolding/cleavage kinetics is recorded offline by HPLC and via fluorescence intensity. We show that the results for refolding obtained on the micro-scale can be transferred to the laboratory scale stirred tank reactor, with increases in scale up to a factor of 5000, with high agreement of kinetic constants and yield. Progress of refolding kinetics on the laboratory scale is monitored inline by attenuated total reflectance – Fourier transform infrared spectroscopy (ATR-FTIR). Addressing the demands for better process understanding, we demonstrate that ATR-FTIR enables the inline monitoring of refolding processes on the laboratory scale, replacing offline analysis which delivers the results with a time delay. Implementing inline monitoring will allow the integration of process control, thereby resulting in a more efficient and knowledge based production process.     

Novel bioreactors for the culture and expansion of aggregative neural stem cells

Neural stem cells have been cultured as three-dimensional aggregates in a number of different types of bioreactors. The design and configuration of the bioreactor are shown to be crucial factors for the successful propagation of the cells. A novel bioreactor with liquid re-circulation and a working volume of 200 ml has been designed, tested and shown to be able to produce a higher cell vitality compared to those produced in multi-well plates, shake flasks and stirred flasks. The novel reactor was able to produce a total density of cells of 3.5 x 10(6) cells/ml consisting of a larger number of smaller and proliferative aggregates, compared to only 1.8 x 10(6) cells/ml produced in a multi-well plate. Shake flasks and stirred flasks commonly used for facilitating mass transfer in the culture of micro-organisms are shown to be unsuitable for the propagation of neural stem cells.     

Scale up production of isoflavonoids in cell suspension cultures of Pueraria tuberosa grown in shake flasks and bioreactor

Cell cultures of Pueraria tuberosa were grown in vessels of different sizes and 2L stirred tank bioreactor containing modified MS medium with morphactin (0.1 mg l^?1) and 2iP (5.0 mg l^?1) and 20% inoculum. Stable growth and total isoflavonoid yield of 76.6 mg l^?1 were recorded in the cultures during scale up. This was in concordance with the persistent yield of the individual isoflavonoids regardless of the vessel size.     

Bridging the gap between traditional cell cultures and bioreactors applied in regenerative medicine: practical experiences with the MINUSHEET perfusion culture system

To meet specific requirements of developing tissues urgently needed in tissue engineering, biomaterial research and drug toxicity testing, a versatile perfusion culture system was developed. First an individual biomaterial is selected and then mounted in a MINUSHEET^® tissue carrier. After sterilization the assembly is transferred by fine forceps to a 24 well culture plate for seeding cells or mounting tissue on it. To support spatial (3D) development a carrier can be placed in various types of perfusion culture containers. In the basic version a constant flow of culture medium provides contained tissue with always fresh nutrition and respiratory gas. For example, epithelia can be transferred to a gradient container, where they are exposed to different fluids at the luminal and basal side. To observe development of tissue under the microscope, in a different type of container a transparent lid and base are integrated. Finally, stem/progenitor cells are incubated in a container filled by an artificial interstitium to support spatial development. In the past years the described system was applied in numerous own and external investigations. To present an actual overview of resulting experimental data, the present paper was written.     

The potential of hydrodynamic damage to animal cells of industrial relevance: current understanding

Suspension animal cell culture is now routinely scaled up to bioreactors on the order of 10,000 L, and greater, to meet commercial demand. However, the concern of the ‘shear sensitivity’ of animal cells still remains, not only within the bioreactor, but also in the downstream processing. As the productivities continue to increase, titer of ~10 g/L are now reported with cell densities greater than 2 × 10⁷ cells/mL. Such high, and potentially higher cell densities will inevitably translate to increased demand in mass transfer and mixing. In addition, achieving productivity gains in both the upstream stage and downstream processes can subject the cells to aggressive environments such as those involving hydrodynamic stresses. The perception of ‘shear sensitivity’ has historically put an arbitrary upper limit on agitation and aeration in bioreactor operation; however, as cell densities and productivities continue to increase, mass transfer requirements can exceed those imposed by these arbitrary low limits. Therefore, a better understanding of how animal cells, used to produce therapeutic products, respond to hydrodynamic forces in both qualitative and quantitative ways will allow an experimentally based, higher, “upper limit” to be created to guide the design and operation of future commercial, large scale bioreactors. With respect to downstream hydrodynamic conditions, situations have already been achieved in which practical limits with respect to hydrodynamic forces have been experienced. This review mainly focuses on publications from both the academy and industry regarding the effect of hydrodynamic forces on industrially relevant animal cells, and not on the actual scale-up of bioreactors. A summary of implications and remaining challenges will also be presented.     

Effect of streptomycin on the active force of bioengineered heart muscle in response to controlled stretch

In this study, we describe a bioreactor system to deliver controlled stretch protocols to bioengineered heart muscle (BEHMs) and test the system when streptomycin (an aminoglycoside antibiotic, which blocks stretch-activated channels) is either added to or excluded from the culture medium. Streptomycin is a very commonly used component of cell culture antibiotic-antimycotic media additives, so its effects on muscle development and functional response to mechanical signals in vitro is worthy of investigation. Our hypothesis is that BEHMs will not adapt to the applied mechanical stretch protocol when streptomycin is present in the culture medium, but will do so when streptomycin is excluded. Bioengineered heart muscles were formed by culturing primary neonatal cardiac myocytes in a fibrin gel using a method previously developed in our laboratory. A custom bioreactor system was designed using SolidWorks and structural components manufactured using fusion deposition modeling. We utilized a stretch protocol of 1 Hz, 10% strain for 7 d. BEHMs were stretched in the presence and absence of streptomycin. As controls, BEHMs were maintained in a cell culture incubator with and without streptomycin. The contractile properties of all BEHMs were evaluated to determine the active force. We were able to demonstrate compatibility of the bioreactor system with BEHMs and were able to stretch 58 constructs with zero incidence of failure. When the BEHMs were stretched in the absence of streptomycin, the active force increased from a mean value of 51.7 +/- 5.6 (N = 10) to 102.4 +/- 16.3 muN (N = 10), with p < 0.05. However, BEHMs that were stretched in the presence of streptomycin did not show any significant increase in active force generation. The average active force of BEHMs increased from a mean value of 57.6 +/- 10.2 (N = 10) to 91.4 +/- 19.8 muN (N = 10) when stretched in the presence of streptomycin. In this study, we demonstrate compatibility of the a bioreactor system with BEHMs, stability of the BEHMs in response to stretch protocols, and significant functional improvement in response to controlled stretch only when streptomycin is excluded from the culture medium, supporting our hypothesis.     

Scale up of a viscous fungal fermentation: application of scale-up criteria with regime analysis and operating boundary conditions

The scale up of the novel, pharmaceutically important pneumocandin (B(0)), from the filamentous fungus Glarea lozoyensis was successfully completed from pilot scale (0.07, 0.8, and 19 m(3)) to production scale (57 m(3)). This was accomplished, despite dissimilar reactor geometry, employing a combination of scale-up criteria, process sensitivity studies, and regime analysis using characteristic time constants for both oxygen mass transfer and bulk mixing. Dissolved oxygen tension, separated from the influence of agitation by gas blending at the 0.07 m(3)-scale, had a marked influence on the concentrations of pneumocandin analogs with different levels of hydroxylation, and these concentrations were used as an indicator of bulk mixing upon scale up. The profound impact of dissolved oxygen tension (DOT) (low and high levels) on analog formation dictated the use of constant DOT, at 80% air saturation, as a scale-up criterion. As a result k(L)a, Oxygen uptake rate (OUR) and hence the OTR were held constant, which were effectively conserved across the scales, while the use of other criterion such as P(g)/V(L), or mixing time were less effective. Production scale (57 m(3)) mixing times were found to be faster than those at 19 m(3) due to a difference in liquid height/tank diameter ratio (H(L)/D(T)). Regime analysis at 19 and 57 m(3) for bulk mixing (t(c)) and oxygen transfer (1/k(L)a) showed that oxygen transfer was the rate-limiting step for this highly shear thinning fermentation, providing additional support for the choice of scale-up criterion.     

Scale architecture of the palmar and plantar epidermis of Polychrus acutirostris Spix, 1825 (Iguania, Polychrotidae) and its relationship to arboreal locomotion

In tetrapod squamates, the diversity of micro-ornamentations of the epidermis of the contact areas of hands and feet is generally associated with constraints and modalities related to locomotion. Polychrus acutirostris is a medium-sized lizard that occurs in open heterogeneous habitats in South America, such as the cerrados, caatingas, and fallow lands. It progresses slowly on branches of various diameters in its arboreal environment. It can also move more rapidly on the ground. The hands and feet are prehensile and may be considered an adaptation for grasping and climbing. Epidermal surfaces from the palmar and plantar areas of the hands and feet of P. acutirostris were prepared for SEM examination, and studied at various magnifications. They show three major levels of complexity: (1) scale types, organized in gradients of size and imbrication, (2) scalar ornamentations, organized by increasing complexity and polarity, and (3) presence of Oberhäutchen showing typically iguanian honeycomb micro-ornamentations. The shape and surface structure of the scales with their pattern of micro-ornamental peaks, which improve grip, and the grasping hands and feet indicate that P. acutirostris is morpho-functionally specialized for arboreality.