Continuous flow cultures of a HeLa cell line as a basis for a steady supply of Rubella virus

A HeLa cell line was propagated in semicontinuous suspension culture, 85 liters final volume, and in continuous flow culture with a volume of 300 ml. or 5 liters in an autoclavable medium to which 8% calf serum had been added. A medium containing 0.1% Methocel and 2% calf serum was also tested. Maximum productivity was obtained at a dilution rate of 0.33 day^?1 with a cell density of about 1.0 × 10⁶ cells/ml. The same cell line was also infected with Rubella virus and the production of virus was followed at the 5-liter cultivation level.     

Suspension culture of drosophila cells employing a gyratory shaker

Summary To develop a method for culturing a large number of small-scale suspension cultures ofDrosophila melanogaster cells simultaneously, basic conditions were studied using a cell line GM₂ and a gyratory shaker. Under gyration at more than 180 rpm, a majority (>80%) of the cells still remained as suspension and grew normally. Lower speed of gyration caused adhesion of the cells to a substratum. Furthermore, size of the culture vessels was found to affect the pattern of cell growth. Five- or 10-ml Erlenmeyer flasks gave satisfactory results, but the growth curves in 30-ml flasks differed from flask to flask and the saturation level was lower. Besides, the growth curves in the latter case were quite different depending on the volume of the medium. A preliminary experiment showed that the type of flask might affect the pattern of a growth curve. Initial cell densities has to be more than 6×10⁴ cells per ml. Lower densities resulted in the longer doubling time or no increase in the cell number. Therefore the following conditions are recommended as a standard for gyration culture ofD. melanogaster cell, GM₂: speed of gyration, 180 rpm; culture vessel, 5- or 10-ml Erlenmeyer flask of a certain type; initial cell density, 1 to 5×10⁵ per ml. Both D20 and modified Schneider’s medium could be utilized as the medium.     

Large-Scale Temperature-Induced Synchrony of Cell Division in Euglena gracilis*

SYNOPSIS. Temperature-induced patterns of synchronous cell division and cell size were obtained with Euglena gracilis. The alga was cultured in a glutamate-sucrose medium in 6-liter quantities. Synchrony was induced by non-lethal shifts of temperature between 14.5 and 28.5 C. Three liters of cells containing 2 × 10⁶ cells/ml were harvested in each 24-hour cycle.     

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.     

Evaluation of the new serum-free medium (MDSS2) for the production of different biologicals: Use of various cell lines

The presence of serum in cell culture raises safety problems for the production of biologicals, thus a new serum-free medium (MDSS2) was developed. The evaluation of this medium for the growth of different cell lines (BHK-21 C13, BSR and Vero) has shown that cells grew in this medium similarly to standard serum-containing medium, independently of the culture system used: in static (as monolayer) as well as in agitated systems (in suspension in spinner and perfusion reactors). BHK-21 and BSR cells grew as aggregate cultures and could proliferate in both static and agitated culture systems. Vero cells stayed attached to a substrate and proliferated equally in static and in agitated microcarrier-culture systems. The cell densities obtained with BHK-21 cells depended only on the culture system used. They ranged from 2–3×10⁶ to 6–12×10⁶ cells per ml for static batch and perfusion reactor cultures respectively. The cell concentration was 3 to 6 times higher than in classical cultures performed in serum-containing medium. The cell densities obtained with Vero cells were indistinguishable from those obtained in serum-containing medium, whatever the cell culture system used. These cell lines have been used for the production of rabies virus. With respect to BHK-21 and BSR, similar production rates of rabies glycoprotein have been found as in the standard roller bottle process. The production of rabies virus and of viral glycoprotein by Vero cells cultivated in serum-free medium was augmented 1.5-fold and 2.5-fold, respectively, when compared to serum-containing medium.A recombinant BHK-21 cell line, producing human IL-2, can also proliferate in MDSS2, after addition of insulin. The specific IL-2 production rate was augmented 3–4 fold in comparison to serum-containing medium.For the cells tested, the MDSS2 serum-free medium is a good growth and production medium. Its use for cultivating other cell lines and/or for the production of other biologicals is discussed.     

Synchronization of somatic embryogenesis from carrot cells at high frequency as a basis for the mass production of embryos

Synchronization of somatic embryogenesis at high frequency is a useful system for the mass production of embryos. Many attempts have been carried out, however, it was difficult to obtain the system in which most of the initial embryogenic cells or cell clusters synchronously differentiate to embryos. In carrot suspension cultures, high frequency, synchronous embryogenesis systems (following three systems) have been established.(1) Small spherical single cells from suspension cultures obtained by sieving and density gradient centrifugation in Percoll solutions differentiated to embryogenic cell clusters at high frequency when they were cultured in a medium containing 2,4-dichlorophenoxyacetic acid (0.05 micromolar), zeatin (1 micromolar) and mannitol (0.2 molar). (2) Embryogenic cell clusters from suspension cultures obtained by sieving, density gradient centrifugation in Ficoll solutions, and subsequent centrifugation at a low speed for a short time synchronously differentiated to embryos, especially globular embryos at high frequency, when they were cultured in a medium containing zeatin (0.1 micromolar) but no auxin. (3) Embryogenic cell clusters obtained by above method are cultured at cell densities of 2×10³ cell clusters ml^-1. Globular embryos which were sieved from embryos induced synchronously differentiated to torpedo-shaped embryos at high frequency when they were cultured at densities below 150 globular embryos ml^-1.Using these systems, the whole process of embryogenesis from single cells to whole plants could be synchronously induced at high frequency.Abbreviations ABA abscissic acid - 2,4-d 2,4-dichlorophenoxyacetic acid - GA₃ gibberellin A₃ - IAA indoleacetic acid - NAA naphthylacetic acid     

Enhanced Production of Human Recombinant Proteins from CHO cells Grown to High Densities in Macroporous Microcarriers

Macroporous microcarriers entrap cells in a mesh network allowing growth to high densities and protect them from high shear forces in stirred bioreactor cultures. We report the growth of Chinese hamster ovary (CHO) cells producing either recombinant human beta-interferon (β-IFN) or recombinant human tissue-plasminogen activator (t-PA) in suspension or embedded in macroporous microcarriers (Cytopore 1 or 2). The microcarriers enhanced the volumetric production of both β-IFN and t-PA by up to 2.5 fold compared to equivalent suspension cultures of CHO cells. Under each condition the cell specific productivity (Q _P) was determined as units of product/cell per day based upon immunological assays. Cells grown in Cytopore 1 microcarriers showed an increase in Q _P with increasing cell densities up to a threshold of >1 × 10⁸ cells/ml. At this point the specific productivity was 2.5 fold higher than equivalent cells grown in suspension but cell densities above this threshold did not enhance Q _P any further. A positive linear correlation (r ² = 0.93) was determined between the specific productivity of each recombinant protein and the corresponding cell density for CHO cells grown in Cytopore 2 cultures. With a cell density range of 25 × 10⁶ to 3 × 10⁸ cells/ml within the microcarriers there was a proportional increase in the specific productivity. The highest specific productivity measured from the microcarrier cultures was ×5 that of suspension cultures. The relationship between specific productivity and cell density within the microcarriers leads to higher yields of recombinant proteins in this culture system. This could be attributed to the environment within the microcarrier matrix that may influence the state of cells that could affect protein synthesis or secretion.     

Plant regeneration from indica rice (Oryza sativa L.) protoplasts

Rice (Oryza sativa L.) plants of the indica cultivar IR54 were regenerated from protoplasts. Conditions were developed for isolating and purifying protoplasts from suspension cultures with protoplast yields ranging from 1·10⁶ to 15·10⁶ viable protoplasts/1 g fresh weight. Protoplast viability after purification was generally over 90%. Protoplasts were cultured in a slightly modified Kao medium in a Petri plate by placing them onto a Millipore filter positioned on top of a feeder (nurse) culture containing cells from a suspension culture of the japonica rice, Calrose 76. Plating efficiencies of protoplasts ranged from 0.5 to 3.0%; it was zero in the absence of the nurse culture. Protoplast preparations usually contained no contaminating cells, and when present, the number of cells never exceeded 0.1% of the protoplasts. After three weeks the Millipore filter with callus colonies were transferred off feeder cells and onto a Linsmaier and Skoog-type medium for an additional three weeks. Selected callus colonies that had embryo-like structures were then transferred to regeneration medium containing cytokinins, and regeneration frequencies up to 80% were obtained. Small shoots emerged and were transferred to jars for root development prior to transferring to pots of soil and growing the plants to maturity in growth chambers. Of the cytokinins evaluated, N⁶-benzylaminopurine was the most effective in promoting shoot formation; however, kinetin was also somewhat effective. Regeneration medium could be either an N₆ or Murashige and Skoog basal medium. Of 76 plants grown to maturity, 62 were fertile, and the plant heights averaged about three-fourths the height of seed-grown plants.Two other suspension cultures of IR54, one developed from the protoplast callus of the initial IR54 line, and the other developed from callus produced by mature seeds, have yielded protoplasts capable of regenerating plants when using cells of the Calrose 76 suspension as a nurse culture. In addition, protoplasts obtained from three-week-old primary callus of immature embryos of IR54 were capable of regenerating plants when using the same culture conditions.Abbreviations 2,4-D 2,4-dichlorophenoxyacetic acid - pcy packed cell volume - BAP N⁶-benzylaminopurine - FDA fluorescein diacetate - FW fresh weight - IAA indole-3-acetic acid Media AA Muller and Grafe (1978) - CPW Frearson et al. (1973) - Kao^* Kao (1977) - LS Linsmaier and Skoog (1965) - MS Murashige and Skoog (1962) - N₆ Chu et al. (1975) - PCM Ludwig et al. (1985)     

Design and performance of a trickle-bed bioreactor with immobilized hybridoma cells

A trickle-bed system employing inert matrices of vermiculite or polyurethane foam packed in the downcomer section of a split-flow air-lift reactor has been developed for hybridoma culture to enhance antibody productivity. This quiescent condition favoured occlusion and allowed the cells to achieve densities twelve fold greater (12.8×10⁶ cells/ml reactor for polyurethane foam) than in free cell suspension. The reactor was operated in a cyclic batch mode whereby defined volumes of medium were periodically withdrawn and replaced with equal volumes of fresh medium. The pH of the medium was used as the indicator of the feeding schedule. Glucose, lactate and ammonia concentrations reached a stationary value after 5 days. With vermiculite packing, a monoclonal antibody (MAb) concentration of 2.4 mg/l was achieved after 12 days. The MAb concentration declined then increased to a value of 1.8 mg/l. In the polyurethane foam average monoclonal antibody (MAb) concentrations reached a stationary value of 1.1 mg/l in the first 20 days and increased to a new stationary state value of 2.1 mg/l for the remainder of the production. MAb productivity in the trickle-bed reactor was 0.3 mg/l·d (polyurethane foam) and 0.18 mg/l.d (vermiculite) in comparison to 0.12 mg/l·d for free cell suspension. This trickle-bed system seems to be an attractive way of increasing MAb productivity in culture.     

Carbon Dioxide as an Essential Requirement for Cultured Sycamore Cells

Carbon dioxide (optimum concentration c. 1.0%) is essential to the initiation of the growth in suspension culture or on agar plates of cultured sycamore cells. By effective flushing of the cultures with CO₂-free air it is possible to demonstrate this requirement with initial cell densities up to 50 × 10³ cells ml^?1. This growth-promoting activity of carbon dioxide is not related to any effect it may have on the pH of the culture medium. The cells fix applied carbon dioxide into organic and amino acids but attempts to replace the carbon dioxide requirement by non-toxic levels of organic or amino acids have not been successful.     

Reduction of medium consumption in perfusion mammalian cell cultures using a perfusion rate equivalent concentrated nutrient feed

Media preparation for perfusion cell culture processes contributes significantly to operational costs and the footprint of continuous operations for therapeutic protein manufacturing. In this study, definitions are given for the use of a perfusion equivalent nutrient feed stream which, when used in combination with basal perfusion medium, supplements the culture with targeted compounds and increases the medium depth. Definitions to compare medium and feed depth are given in this article. Using a concentrated nutrient feed, a 1.8-fold medium consumption (MC) decrease and a 1.67-fold increase in volumetric productivity (PR) were achieved compared to the initial condition. Later, this strategy was used to push cell densities above 100 × 10⁶ cells/ml while using a perfusion rate below 2 RV/day. In this example, MC was also decreased 1.8-fold compared to the initial condition, but due to the higher cell density, PR was increased 3.1-fold and to an average PR value of 1.36 g L⁻¹ day⁻¹ during a short stable phase, and versus 0.46 g L⁻¹ day⁻¹ in the initial condition. Overall, the performance improvements were aligned with the given definitions. This multiple feeding strategy can be applied to gain some flexibility during process development and also in a manufacturing set-up to enable better control on nutrient addition.     

新型旋转壁式生物反应器内三维组织工程骨的构建

利用微载体悬浮培养法将成骨细胞在旋转壁式生物反应器内进行大规模扩增,并检测细胞的组织形态和生物功能.然后以此作为种子细胞,分别以2×10⁶个/ml和1×10⁶个/ml两种密度接种到支架材料上,于旋转壁式生物反应器(RWV)内进行三维组织工程骨的构建.并将所构建的骨组织分别进行倒置显微镜(inverted microscope)、扫描电镜(SEM)、碱性磷酸酶(ALP)、矿化结构和AO/EB双重荧光染色等生物学性能检测,以及对培养过程的营养物质代谢情况进行监控和分析.结果表明,在RWV中培养的骨组织生长良好,分泌大量胶原纤维,并有矿化基质和新骨样组织形成. 由上述结果可断定,通过RWV内部流体对流所产生的应力刺激,可提高成骨细胞碱性磷酸酶的活性表达,并加速矿化结节的形成,从而完成成骨细胞的快速增殖与分化以及工程化组织的三维构建.     

High density culture of hybridoma cells in a dual hollow fiber bioreactor

Summary Hybridoma cells were cultured for two months in the dual hollow fiber bioreactor (DHFBR) which had been successfully used for high cell density cultures of various microbial cells. In batch suspension culture the concentration of monoclonal antibody (Mab) against human Chorionic Gonadotropin (hCG) and the cell density of Alps 25-3 hybridoma cells were obtained in 30 μg/mL and 2.35×10⁶ cells/mL, respectively. The continuous culture with DHFBR produced Mab of 100–130 μg/mL for 30 days and the estimated cell density in the extracapillary space of DHFBR was 1.87×10⁸ cells/mL based on the antibody production rate. The productivity of Mab was 205 mg/day per litre of the total reactor volume while that of the batch suspension culture was only 10 mg/L day.     

High cell density perfusion cultures of anchorage-dependent Vero cells in a depth filter perfusion system

A depth filter perfusion system (DFPS) with polypropylene fibers had been demonstrated to support high density cultures of anchorage-independent hybridoma cells. The DFPS provides advantages of high surface-to-volume ratio of 450–600 cm²/cm³, low cost set-up, easy operation and scale-up. To test the feasibility of using DFPS for high density cultures of anchorage-dependent cells, Vero cells were cultivated in the DFPS. Gelatin coating on polypropylene fibers in the DFPS was necessary to promote cell attachment and growth. Dissolved oxygen (DO) concentrations could be controlled by sparging air into the reservoir vessel through a filter sparger. When DO concentration was controlled above 40% of air saturation in the DFPS with 40 m pore size, the maximum cell concentration as estimated on specific lactate production rate, was 3.81×10⁷ cells/ml of the total reactor volume. This viable cell concentration is approximately 18 times higher than that obtained in a T-flask batch culture. Taken together, the results obtained here showed the potential of DFPS for high-density cultures of anchorage-dependent cells.     

Establishment of embryogenic callus and high protoplast yielding suspension cultures of sugarcane (Saccharum spp. hybrids)

For 18 sugarcane cultivars, four distinct callus types developed on leaf explant tissue cultured on modified MS medium, but only Type 3 (embryogenic) and Type 4 (organogenic) were capable of plant regeneration. Cell suspension cultures were initiated from embryogenic callus incubated in a liquid medium. In stage one the callus adapted to the liquid medium. In stage two a heterogeneous cell suspension culture formed in 14 cultivars after five to eight weeks of culture. In stage three a homogeneous cell suspension culture was developed in six cultivars after 10 to 14 weeks by selective subculturing to increase the proportion of actively dividing cells from the heterogeneous cell suspension culture. Plants were regenerated from cell aggregates in heterogeneous cell suspension cultures for up to 148 days of culture but plants could not be regenerated from homogeneous cell suspension cultures. High yields of protoplasts were obtained from homogeneous cell suspension cultures (3.4 to 5.2 × 10⁶ protoplasts per gram fresh weight of cells [gfwt^-1]) compared to heterogeneous cell suspension cultures (0.1 × 10⁶ protoplasts gfwt^-1). Higher yields of protoplasts were obtained from homogeneous cell suspension cultures for cultivars Q63 and Q96 after regenerating callus from the cell suspension cultures, then recycling this callus to liquid medium (S-cell suspension cultures). This process increased protoplast yield to 9.4 × 10⁶ protoplasts gfwt^-1. Protoplasts isolated from S-cell suspension cultures were regenerated to callus and recycled to produce SP-cell suspension cultures yielding 6.4 to 13.2 × 10⁶ protoplasts gfwt^-1. This recycling of callus to produce S-cell suspension cultures allowed protoplasts to be isolated for the first time from cell lines of cultivars Q110 and Q138.     

High density continuous production of murine pluripotent cells in an acoustic perfused bioreactor at different oxygen concentrations

Strategies for the production of pluripotent stem cells (PSCs) rely on serially dissociated adherent or aggregate‐based culture, consequently limiting robust scale‐up of cell production, on‐line control and optimization of culture conditions. We recently developed a method that enables continuous (non‐serially dissociated) suspension culture‐mediated reprogramming to pluripotency. Herein, we use this method to demonstrate the scalable production of PSCs and early derivatives using acoustic filter technology to enable continuous oxygen‐controlled perfusion culture. Cell densities of greater than 1 × 10⁷ cells/mL were achieved after 7 days of expansion at a specific growth rate (µ) of 0.61 ± 0.1 day^?1 with a perfusion rate (D) of 5.0 day^?1. A twofold increase in maximum cell density (to greater than 2.5 × 10⁷ cells/mL) was achieved when the medium dissolved oxygen was reduced (5% DO). Cell densities and viabilities >80% were maintained for extended production periods during which maintenance of pluripotency was confirmed by stable expression of pluripotency factors (SSEA‐1 and Nanog), as well as the capacity to differentiate into all three germ layers. This work establishes a versatile biotechnological platform for the production of pluripotent cells and derivatives in an integrated, scalable and intensified stirred suspension culture. Biotechnol. Bioeng. 2013; 110: 648–655. © 2012 Wiley Periodicals, Inc.     

Polystyrene substratum for bulk culture of anchorage dependent cells

Twisted ribbons made of polystyrene were used as a packing material for the cultivation of anchorage dependent cells. Normal human fibroblast cells grown on this support in a laboratory scale reactor reached densities of about 5–7×10⁵ cells/ml. The cells adhered strongly to the carrier and no cell detachment was observed upon transfer to serum free medium. The properties of this packing material and its potential use are discussed.     

紫茉莉悬浮细胞培养体系的建立

为建立紫茉莉(Mirabilis jalapa L.)悬浮细胞培养体系,以紫茉莉无菌苗叶片诱导的愈伤组织为材料,筛选紫茉莉悬浮细胞的适宜培养体系。结果表明,紫茉莉愈伤组织在MS+2,4-D 1 mg L-1+KT 0.5 mg L-1的液体培养基中悬浮继代培养3~4次,能得到稳定的悬浮细胞系。培养基的pH值为5.5~5.9,蔗糖浓度为30 g L-1更适合悬浮细胞的生长。紫茉莉悬浮细胞的生长曲线大致呈S型。最佳继代培养时间是10 d,培养液的体积为40 mL时,接种量为7.5 mL,可以较好地保持悬浮细胞系。1 L培养液中可提取分泌蛋白(0.42±0.15) g。这些有助于对悬浮细胞提取分泌蛋白的研究。     

Reassessing culture media and critical metabolites that affect adenovirus production

Adenovirus production is currently operated at low cell density because infection at high cell densities still results in reduced cell‐specific productivity. To better understand nutrient limitation and inhibitory metabolites causing the reduction of specific yields at high cell densities, adenovirus production in HEK 293 cultures using NSFM 13 and CD 293 media were evaluated. For cultures using NSFM 13 medium, the cell‐specific productivity decreased from 3,400 to 150 vp/cell (or 96% reduction) when the cell density at infection was increased from 1 to 3 × 10⁶ cells/mL. In comparison, only 50% of reduction in the cell‐specific productivity was observed under the same conditions for cultures using CD 293 medium. The effect of medium osmolality was found critical on viral production. Media were adjusted to an optimal osmolality of 290 mOsm/kg to facilitate comparison. Amino acids were not critical limiting factors. Potential limiting nutrients including vitamins, energy metabolites, bases and nucleotides, or inhibitory metabolites (lactate and ammonia) were supplemented to infected cultures to further investigate their effect on the adenovirus production. Accumulation of lactate and ammonia in a culture infected at 3 × 10⁶ cells/mL contributed to about 20% reduction of the adenovirus production yield, whereas nutrient limitation appeared primarily responsible for the decline in the viral production when NSFM 13 medium was used. Overall, the results indicate that multiple factors contribute to limiting the specific production yield at cell densities beyond 1 × 10⁶ cells/mL and underline the need to further investigate and develop media for better adenoviral vector productions. © 2009 American Institute of Chemical Engineers Biotechnol. Prog., 2010     

Cell aggregate suspension culture for large-scale production of biomolecules

Summary A method is described for the rapid reversible conversion of a number of continuous cell lines from anchorage-dependent growth to growth as aggregates of cells in suspension culture. Employing this technique, an inoculum of three 75-cm² flasks of BALB/c SV3T3 cells was grown to 60 liters of aggregate suspension in 14 days. This yielded 120 ml of packed cells or 9.1×10¹⁰ cells. Similar results were obtained for other cell lines. Biomolecules such as migration-inhibition factor (MIF) and plasminogen activator were produced from these cultures.