Propagation ofSpodoptera frugiperda cells (Sf9) and production of recombinant proteins with the baculovirus expression system using improved spinner flasks with membrane aeration

Summary It has been shown that the growth of Spodoptera frugiperda cells is significantly reduced or ceased under oxygen limiting culture conditions. This paper describes the use of a new membrane-aerated spinner flask which was compared to conventional surface-aerated spinner flasks with regard to growth of the insect cell line Sf9 and recombinant protein production after infection with baculovirus. Using a commercially available serum-free culture medium Sf9 cells reached highest cell densities (3×10⁶ ml^–1) in the membrane-aerated spinner flask. Production of recombinant protein was also influenced by the oxygen supply. In the membrane-aerated spinner flask and in a surface-aerated spinner flask with reduced filling volume more than 20000 U ml^–1 of a recombinant interleukin-2 variant were accumulated whereas only 100 U ml^–1 were produced in a surface-aerated spinner flask with insufficient oxygen supply. Sufficient oxygenation appears to be essential for proliferation of Sf9 cells as well as recombinant protein production after infection with baculovirus. Membrane oxygenation allows sufficient oxygen supply at high cell density and an at least 2.5 fold higher filling volume per spinner unit.     

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.     

On-line monitoring of oxygen in Tubespin, a novel, small-scale disposable bioreactor

A novel, optical sensor was fixed in a new type of disposable bioreactor, Tubespin, for the on-line (real-time) monitoring of dissolved oxygen concentrations during cell culture. The cell density, viability and volumetric mass transfer coefficient were also determined to further characterize the bioreactors. The k_La value of the Tubespin at standard conditions was 24.3 h⁻¹, while that of a spinner flask was only 2.7 h⁻¹. The maximum cell density in the Tubespin bioreactor reached 6 × 10⁶ cells mL⁻¹, which was two times higher than the cell density in a spinner flask. Furthermore, the dynamic dissolved oxygen level was maintained above 90% air-saturation in the Tubespin, while the value was only 1.9% in a spinner flask. These results demonstrate the competitive advantage of using the Tubespin system over spinner flasks for process optimization and scale-down studies of oxygen transfer and cell growth.     

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.     

杂交瘤细胞培养中摄氧速率(OUR)的在线检测及其与细胞生长及代谢的关系

在批式及灌流培养条件下研究了杂交瘤细胞在无血清培养基中的生长、代谢情况与氧消耗的关系。应用动力学方法在线进行OUR的检测,同时离线取样检测其他参数。结果发现OUR与谷氨酰胺的消耗、抗体的生成及活细胞密度间有明显的相关关系,进一步的分析还发现在对数生长期,OUR与活细胞密度间具有良好的线性关系,qOUR(0.103±0.028)×10^-12mol/cell/h,可以通过它来进行细胞密度的在线检测。并通过以ΔOUR=0时刻作为灌流调整点进行连续灌流培养的初步实验验证了OUR作为培养过程反馈控制参数的可能性。     

Continuous insect cell (Sf-9) culture with aeration through sparging

The continuous growth of Spodoptera frugiperda Sf-9 cells in a 250-ml blown-glass jacketed spinner flask under a direct air sparging environment was investigated. Even at 220 ml working volume (about 90% of total volume), this spinner flask provided good mixing and oxygenation as demonstrated by a higher cell density compared with fermentor cultures. This eliminates a common limitation of the traditional spinner flask, namely much lower cell density at high working volume. Furthermore, this spinner flask has been run with Sf-9 cell culture at five different dilution rates and two different air sparging rates at steady state, demonstrating its utility in research applications where cell size, metabolic activity and environmental conditions can be constantly maintained. In addition to demonstrating the utility of the reactor, three novel points are made in this report. First, cell density in continuous cultures is increased significantly due to a high agitation rate and, especially, air sparging rate, which is seldom used in animal cell or insect cell culture. Second, there is no apparent difference in the specific death rate at two different sparging rates (0.0093 vvm and 0.0125 vvm). Finally, we have maintained Sf-9 cells for more than 4 months in a continuous culture using a serum-free medium without loss of recombinant protein expression in infected cells.     

Effects of oxygen on recombinant protein production by suspension cultures of Spodoptera frugiperda (Sf-9) insect cells.

Spodoptera frugiperda (Sf-9) insect cells have been grown in serum-free medium in 250-ml spinner flasks. The maximum cell density obtained in these cultures was dependent on the aeration rate of the culture. Similar yields of uninfected cells were obtained when cultures were stirred in spinner flasks at 80 rev min-1 and in a 4-1 stirred-tank bioreactor and the dissolved oxygen in the bioreactor was controlled at 20% of air saturation. Cells were infected with a recombinant baculovirus at different multiplicities of infection: the timing and maximum level of expression of the recombinant protein were dependent on the multiplicity of infection, the cell density at infection, and on the aeration rate of the culture. Oxygen-limited growth resulted in undetectable levels of recombinant protein (< 6 ng recombinant protein 10(-7) cells). Compared with the maximum yields observed in spinner flask cultures, higher levels of recombinant protein were produced when cells were grown and infected in the bioreactor. The level of dissolved oxygen in the bioreactor was controlled at 50% of air saturation.     

应用动力学方法在线检测Vero细胞培养过程中的摄氧率

流加和灌注培养已被广泛应用于动物细胞培养 ,以获得高活性、高密度的细胞和高的产物得率。在这些培养过程中 ,一般通过离线检测关键参数 (如细胞密度、营养和代谢产物的浓度 )来人为调整灌注速率和补料策略 ,但是 ,当细胞密度较高时 ,由于细胞代谢旺盛使得培养的微环境变化很快 ,这就需要更加频繁快速地调整操作条件 ,从而导致因频繁取样和离线分析所带来的污染危险及大量人力、物力的浪费。这在大规模细胞培养过程中是不可取的。因此 ,要建立大规模、高效动物细胞培养过程 ,有必要研究和探索在线检测技术 ,以实时掌握细胞培养过程所处的状…     

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.     

利用一种新型反应器——BelloCell培养动物细胞

利用Bello Cell这种新型的生物反应器,来培养COS7细胞和昆虫Sf9细胞。COS7细胞和昆虫sf9细胞分别用T75培养瓶及spinnerflask培养之后,经细胞计数接入Bello Cell之中,同时检测并分析培养基中葡萄糖、谷氨酰胺、乳酸和氨浓度变化情况。COS7细胞初始接种量为4．208×10^7cells,最终在培养156h后细胞数量达到了4．68×10^8cells,是初始细胞量的11倍。sf9细胞初始接种细胞量为1×10^8cells,在培养192h时,细胞总量达到了最高为4．01×10^9cells,是最初细胞量的40倍。培养基的代谢物进行有规律的变化。Bello Cell适合COS7细胞和昆虫Sf9细胞高密度大规模培养,为动物细胞高效大规模表达药物蛋白,奠定重要的基础。     

Online monitoring of oxygen in spinner flasks

We show the application of a novel optical on-line sensor fixed in spinner flasks for the online monitoring of dissolved O₂ concentrations during mammalian cell growth. Using this sensor that requires only minute changes to the flask to be made, we could determine the volumetric O₂ transfer coefficient as well as O₂ consumption rates. Under normal growth conditions the cells did not undergo O₂ limitation. Also, the transfer of O₂ from the atmosphere to the spinner flasks is influenced by the use of screw caps. The on-line measurement was further applied to determine the O₂ uptake rates which can then be used to monitor the metabolic state of the cells and also for online process monitoring.     

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。     

以摇瓶所得摄氧率为基准进行发酵放大

通过设计特殊摇瓶,用亚硫酸盐法测出摇瓶口纱布层氧通透率的基础上,在实际发酵情况下通过测定瓶内气、液相氧的变化得出其发酵过程中的摄氧率(OUR)及氧传递系数(K_La)。以特制摇瓶取得的菌体CUR为基准进行发酵过程和发酵罐的放大。通过质谱仪在线检测及采样分析,研究了3种不同供气流量及搅拌转速下的放大结果。摇瓶与发酵罐在菌体OUR、菌体产量方面吻合很好,而在整个放大过程中,发现摇瓶与发酵罐内的氧传递系数(K_La)、溶解氧(C_L)差异较大。     

On-line characterization of a hybridoma cell culture process

The on-line determination of the physiological state of a cell culture process requires reliable on-line measurements of various parameters and calculations of specific rates from these measurements. The cell concentration of a hybridoma culture was estimated on-line by measuring optical density (OD) with a laser turbidity probe. The oxygen uptake rate (OUR) was determined by monitoring dynamically dissolved oxygen concentration profiles and closing oxygen balances in the culture. The base addition for neutralizing lactate produced by cells was also monitored on-line via a balance. Using OD and OUR measurements, the specific growth and specific oxygen consumption rates were determined on-line. By combining predetermined stoichiometric relationships among oxygen and glucose consumption and lactate production, the specific glucose consumption and lactate production rates were also calculated on-line. Using these on-line measurements and calculations, the hybridoma culture process was characterized on-line by identifying the physiological states. They will also facilitate the implementation of nutrient feeding strategies for fed-batch and perfusion cultures. (c) 1994 John Wiley & Sons, Inc.     

A stable, sensitive, and inexpensive amplifier for oxygen electrode studies

A stable, compact, and inexpensive amplifier is described that permits using the Clark oxygen electrode to measure the oxygen consumption of even slowly respiring mammalian cells at the lowest cell densities at which exponential growth will take place. A modification of the usual spinner flask used in mammalian cell culture greatly reduces the noise picked up by the electrode circuit and makes possible measurements at the highest sensitivity range.     

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。     

Oscillating perfusion of cell suspensions through three-dimensional scaffolds enhances cell seeding efficiency and uniformity

We developed a bioreactor for automated cell seeding of three-dimensional scaffolds by continuous perfusion of a cell suspension through the scaffold pores in oscillating directions. Using quantitative biochemical and image analysis techniques, we then evaluated the efficiency and uniformity of perfusion seeding of Polyactive foams as compared to conventional static and spinner flask methods. Finally, we assessed the efficacy of the perfusion seeding technique for different scaffolds and cell types. Perfusion seeding of chondrocytes into Polyactive foams resulted in "viable cell seeding efficiencies," defined as the percentages of initially loaded cells that were seeded and remained viable, that were significantly higher (75 +/- 6%) than those by static (57% +/- 5%) and spinner flask seeding (55% +/- 8%). In addition, as compared to static and spinner flask methods, cells seeded by perfusion were respectively 2.6-fold and 3.8-fold more uniformly distributed and formed more homogeneously sized cell clusters. Chondrocytes seeded by perfusion into Hyaff-11 nonwoven meshes were 26% and 63%, respectively, more uniformly distributed than following static and spinner flask seeding. Bone marrow stromal cells seeded by perfusion into ChronOS porous ceramics were homogeneously distributed throughout the scaffold volume, while following the static method, cells were found only near the top surface of the ceramic. In summary, we demonstrated that our cell seeding perfusion bioreactor generated constructs with remarkably uniform cell distributions at high efficiencies, and was effective for a variety of scaffolds and different mesenchymal cell types.     

Oxygen uptake rate measurements to monitor the activity of terpene transforming fungi

The application of a simple system for measuring the oxygen uptake rate (OUR) to determine the activity of pellet-forming fungi is described. A non-invasive easy-to-use respirometric system was used to measure the OUR as an activity parameter. The model sensor system was optimized in shake flask experiments with Pleurotus sapidus (DSMZ 8266) and Chaetomium globosum (DSMZ 1962). The toxicity of (+)-limonene and (+)-valencene to submerged fungal cultures and the influence of solvents on C. globosum were investigated. Finally, the new respirometric method was used for the determination of oxygen uptake rates in small scale bioreactors to control the activity of terpene transforming fungi.     

Bioprocess development for the production of a recombinant MUC1 fusion protein expressed by CHO-K1 cells in protein-free medium

The mucin MUC1 is a candidate for use in specific immunotherapy against breast cancer, but this requires the large-scale production of a MUC1 antigen. In this study, a bioprocess for the expression of a recombinant MUC1 fusion protein with a cancer associated glycosylation in CHO-K1 cells has been developed. Cells permanently expressing parts of the extracellular portion of MUC1 fused to IgG Fc were directly transferred from adherent growth in serum-containing medium to suspension culture in the protein-free ProCHO4-CDM culture medium. Using the Cellferm-pro system, optimal culture parameter as pH and pO(2) were determined in parallel spinner flask batch cultures. A pH of 6.8-7.0 and a pO(2) of 40% of air saturation was found to give best cell growth and productivity of secreted recombinant protein. Specific productivity strongly depended the pO(2) and correlated with the online monitored oxygen uptake rate (OUR) of the cells, which indicates a positive influence of the rate of oxidative phosphorylation on productivity. The optimised conditions were applied to continuous perfusion culture which gave very high cell densities and space time yields of the recombinant MUC1 fusion protein, allowing production at gram scale. The product degradation was much lower in supernatants from continuous perfusion culture compared to batch mode. Antibodies reacting with cancer associated MUC1 glycoforms strongly bound to the fusion protein, indicating that the desired glycoforms were obtained and suggesting that the recombinant MUC1 protein could be tested for use in immunotherapy.     

Bubble bed reactor: A reactor design to minimize the damage of bubble aeration on animal cells

A new bubble aeration system was designed to minimize cell killing and cellular damage due to sparging. The residence time of the bubbles in the developed bubble bed reactor was prolonged dramatically by floating them in a countercurrent produced by an impeller. The performance of the new reactor bubble aeration system, implemented in a laboratory reactor, was tested in dynamic aeration experiments with an without cells. An efficiency up to 95% in oxygen transfer could be achieved, which enables a much lower gas flow rate compared with conventional bubble aeration reactors. The low gas flow rate is important to keep cell damage by bubbles as low as possible. A laser light sheet technique used to find the optimal flow pattern in the reactor. The specific power dissipation of the impeller is a good measure to predict cell damage in a turbulent flow. Typical values for the power dissipation measured in the bubble bed reactor were in the range of 0.002 to 0.013 W/kg, which is far below the critical limit for animal cells. The growth of a hybridoma cell line was studied in cell cultivation experiments. A protein-free medium without supplements such as serum or Pluronic F68 was used to exclude any effect of cell-protecting factors, No difference in the specific growth rate and the yield of the antibodies was observed in cell grown in the bubble free surface aeration in the spinner flask. In contrast to the spinner flask, however, the bubble bed reactor design could be scaled up. (c) 1994 John Wiley & Sons, Inc.