High-density tissue-like cultivation of JAR choriocarcinoma cells for the in vitro production of human xylosyltransferase

Human xylosyltransferase is the chain-initiating enzyme involved in the biosynthesis of glycosaminoglycans. Large amounts of xylosyltransferase are required to study the biochemical properties of the native enzyme. To achieve this goal a scale-up of animal cell culture systems was inevitable due to the small amounts of the enzyme present in tissues, e.g. only 0.5 microg XT can be obtained from a chick embryo. JAR choriocarcinoma cells cultured with 10% fetal calf serum were found to secrete xylosyltransferase with relatively high activities (1.10 mU l(-1)). To reduce contaminating proteins JAR cells were adapted to serum-free conditions. Xylosyltransferase activities up to 0.22 mU l(-1) were determined in the harvested cell culture supernatant. Scaling-up of JAR cell culture in the hybrid hollow fiber bioreactor Tecnomouse resulted in the production of 15.8 mU or 270 microg XT in 0.5 l of XT-enriched cell culture supernatant using 57 l of serum-free cell culture medium. The XT activity per ml harvest solution was 200-280-fold higher in this cell culture supernatant than in cell culture flasks. In addition, the specific XT activity of the bioreactor product was 6 microU mg(-1) of total protein, which is 2-fold higher than that obtained under static culture conditions. This study clearly demonstrates the successful high-density, tissue-like cultivation of JAR choriocarcinoma cells in a hollow fiber bioreactor resulting in an effective production of native human xylosyltransferase.     

Perfusion bioreactors for the production of recombinant proteins in insect cells

Conclusion High density perfusion culture of insect cells for the production of recombinant proteins has proved to be an attractive alternative to batch and fed-batch processes. A comparison of the different production processes is summarized in Table 3. Internal membrane perfusion has a limited scale-up potential but appears to the method of choice in smaller lab-scale production systems. External membrane perfusion results in increased shear stress generated by pumping of cells and passing through microfiltration modules at high velocity. However, using optimized perfusion strategies this shear stress can be minimized such that it is tolerated by the cells. In these cases, perfusion culture has proven to be superior to batch production with respect to product yields and cell specific productivity. Although insect cells could be successfully cultivated by immobilization and perfusion in stationary bed bioreactors, this method has not yet been used in continuous processes. In fluidized bed bioreactors with continuous medium exchange cells showed reduced growth and protein production rates.For the cultivation of insect cells in batch and fedbatch processes numerous efforts have been made to optimize the culture medium in order to allow growth and production at higher cell densities. These improved media could be used in combination with a perfusion process, thus allowing substantially increased cell densities without raising the medium exchange rate. However, sufficient oxygen supply has to be guaranteed during fermentation in order to ensure optimal productivity.     

Immobilization of genetically engineered cells: a new strategy for higher stability.

The r-DNA clones improve the bioprocess and provide better economics, if and when properly developed. In recent times, many approaches were made to improve the stability of recombinants in a reactor which includes both genetic and environmental methods, but many of them were proved to be unsuccessful in the scale-up process. The immobilization technique, exploited recently for the cultivation of recombinants, in many cases gave high cell concentrations, better expression of cloned gene products and also maintained plasmid stability for longer periods in a host under continuous operation in comparison to a free cell system. Many plasmids and hosts were tested for improved stabilities. So far, no explanation was provided for higher stability in the immobilized system. However, it was observed to reduce the competition between the plasmid harboring and plasmid free cells in a matrix. The stability of recombinant strains under immobilization technique is affected by various factors, and these are important parameters for the commercial process. Thus, the immobilization system is promising for the successful cultivation and scale-up of genetically engineered cells.     

Fortification of a protein-free cell culture medium with plant peptones improves cultivation and productivity of an interferon-γ-producing CHO cell line

A strong tendency is currently emerging to remove not only serum but also any product of animal origin from animal cell culture media during production of recombinant proteins. This should facilitate downstream processing and improve biosafety. One way consists in the fortification of protein-free nutritive media with plant protein hydrolysates. To investigate the effects of plant peptones on mammalian cell cultivation and productivity, CHO 320 cells, a clone of CHO K1 cells genetically modified to secrete human interferon-gamma (IFN-gamma), were first adapted to cultivation in suspension in a protein-free medium. Both cell growth and IFN-gamma secretion were found to be equivalent to those reached in serum-containing medium. Eight plant peptones, selected on the basis of their content in free amino acids and oligopeptides, as well as molecular weight distribution of oligopeptides, were tested for their ability to improve culture parameters. These were improved in the presence of three peptones, all having an important fraction of oligopeptides ranging from 1 to 10 kDa and a small proportion of peptides higher than 10 kDa. These peptones do not seem to add significantly to the nutritive potential to basal protein-free nutritive medium. Nevertheless, supplementation of an oligopeptide-enriched wheat peptone improved cell growth by up to 30% and IFN-gamma production by up to 60% in shake-flask experiments. These results suggest that the use of plant peptones with potential growth factor-like or antiapoptotic bioactivities could improve mammalian cell cultivation in protein-free media while increasing the product biosafety.     

Mini-scale bioprocessing systems for highly parallel animal cell cultures

Animal cells have been used extensively in therapeutic protein production. The growth of animal cells and the expression of therapeutic proteins are highly dependent on the culturing environments. A large number of experimental permutations need to be explored to identify the optimal culturing conditions. Miniaturized bioreactors are well suited for such tasks as they offer high-throughput parallel operation and reduce cost of reagents. They can also be automated and be coupled to downstream analytical units for online measurements of culture products. This review summarizes the current status of miniaturized bioreactors for animal cell cultivation based on the design categories: microtiter plates, flasks, stirred tank reactors, novel designs with active mixing, and microfluidic cell culture devices. We compare cell density and product titer, for batch or fed-batch modes for each system. Monitoring/controlling devices for engineering parameters such as pH, dissolved oxygen, and dissolved carbon dioxide, which could be applied to such systems, are summarized. Finally, mini-scale tools for process performance evaluation for animal cell cultures are discussed: total cell density, cell viability, product titer and quality, substrates, and metabolites profiles.     

Proteome analysis of virus–host cell interaction: rabies virus replication in Vero cells in two different media

The use of Vero cells for rabies vaccine production was recommended from the WHO in 2005. A controlled production process is necessary to reduce the risk of contaminants in the product. One step towards this is to turn away from animal-derived components (e.g. serum, trypsin, bovine serum albumin) and face a production process in animal component-free medium. In this study, a proteomic approach was applied, using 2-D differential gel electrophoresis and mass spectrometry to compare rabies virus propagation in Vero cells under different cultivation conditions in microcarrier culture. Protein alterations were investigated for uninfected and infected Vero cells over a time span from 1 to 8 days post-infection in two different types of media (serum-free versus serum-containing media). For mock-infected cells, proteins involved in stress response, redox status, protease activity or glycolysis, and protein components in the endoplasmic reticulum were found to be differentially expressed comparing both cultivation media at all sampling points. For virus-infected cells, additionally changes in protein expression involved in general cell regulation and in calcium homeostasis were identified under both cultivation conditions. The fact that neither of these additional proteins was identified for cells during mock infection, but similar protein expression changes were found for both systems during virus propagation, indicates for a specific response of the Vero cell proteome on rabies virus infection.     

Modeling and scale-up of the unsterile scleroglucan production process with Sclerotium rolfsii ATCC 15205

An empirical model was applied to describe the growth related formation of scleroglucan in batchwise cultivation of Sclerotium rolfsii. In this case, the level of oxygen supply controls the carbon flux into glucan, biomass, and CO₂ evolution and therefore determines the yield coefficients Y_Glucan/BDM and Y_BDM/O2. It was observed that scleroglucan formation is enhanced under microaerobic conditions. However, as the empirical model and data of actual batch cultivations show, different maxima exist for product end concentration [g/l] and volumetric productivity [g/ld] depending on the total oxygen uptake during cultivation. A sufficient bulk mixing of the highly viscous culture suspension becomes particularly important during large-scale cultivations. In addition, the scleroglucan production process proved to be shear sensitive. A correlation between the attainable molecular weight of the glucan and the stirrer tip velocity in bioreactors of different sizes is presented. For all these reasons, a scale-up of this process is very complex. Large-scale cultivations under microaerobic conditions, aiming for maximum product end concentration, were slowed down by poor bulk mixing leading to a lower carbon flux into glucan formation. On the other hand, a scale-up designed for maximum volumetric productivity using high oxygen supply was successfully conducted up to a reactor volume of 1.500 l. To minimize the loss in product quality (molecular weight of the glucan) due to high stirrer tip velocities, a mixing concept was developed employing reduced agitation combined with maximum aeration to secure a sufficient axial bulk mixing in the reactor.     

Advancements in mammalian cell transient gene expression (TGE) technology for accelerated production of biologics

Transient gene expression (TGE) in animal cell cultures has been used for almost 30 years to produce milligrams and grams of recombinant proteins, virus-like particles and viral vectors, mainly for research purposes. The need to increase the amount of product has led to a scale-up of TGE protocols. Moreover, product quality and process reproducibility are also of major importance, especially when TGE is employed for the preparation of clinical lots. This work gives an overview of the different technologies that are available for TGE and how they can be combined, depending on each application. Then, a critical assessment of the challenges of large-scale transient transfection follows, focusing on suspension cell cultures transfected with polyethylenimine (PEI), which is the most widely used methodology for transfection. Finally, emerging opportunities for transient transfection arising from gene therapy, personalized medicine and vaccine development are reviewed.     

Performance of a membrane-dialysis bioreactor with a radial-flow fixed bed for the cultivation of a hybridoma cell line

A bioreactor system for the continuous cultivation of animal cells with a high potential for scale-up is presented. This reactor system consists of radial-flow fixed-bed units coupled with a dialysis module. The dialysis membrane enables the supply of low-molecular-weight nutrients and removal of toxic metabolites, while high-molecular-weight nutrients and products (e.g. monoclonal antibodies) are retained and accumulated. This concept was investigated on the laboratory scale in a bioreactor with an integrated dialysis membrane. The efficiency of the reactor system and the reproducibility of the cell activity (hybridoma cells) under certain process conditions could be demonstrated in fermentations up to 77 days. Based on model calculations, an optimized fermentation strategy was formulated and experimentally confirmed. Compared to chemostat cultures with suspended cells, a ten-times higher mAb concentration (383 mgl⁻¹) could be obtained. The highest volumetric specific mAb production rate determined was 6.1 mg mAb (1 fixed bed)⁻¹ h⁻¹.     

Disposable bioreactor for cell culture using wave-induced agitation

This work describes a novel bioreactor system for the cultivation of animal, insect, and plant cells using wave agitation induced by a rocking motion. This agitation system provides good nutrient distribution, off-bottom suspension, and excellent oxygen transfer without damaging fluid shear or gas bubbles. Unlike other cell culture systems, such as spinners, hollow-fiber bioreactors, and roller bottles, scale-up is simple, and has been demonstrated up to 100 L of culture volume. The bioreactor is disposable, and therefore requires no cleaning or sterilization. Additions and sampling are possible without the need for a laminar flow cabinet. The unit can be placed in an incubator requiring minimal instrumentation. These features dramatically lower the purchase cost, and operating expenses of this laboratory/pilot scale cell cultivation system. Results are presented for various model systems: 1) recombinant NS0 cells in suspension; 2) adenovirus production using human 293 cells in suspension; 3) Sf9 insect cell/baculovirus system; and 4) human 293 cells on microcarrier. These examples show the general suitability of the system for cells in suspension, anchorage-dependent culture, and virus production in research and GMP applications. This revised version was published online in July 2006 with corrections to the Cover Date.     

From shake flasks to bioreactors: survival of E. coli cells harboring pGST-hPTH through auto-induction by controlling initial content of yeast extract

A high content of yeast extract in complex media can cause auto-induction of phage T7 RNA polymerase and the consequent expression of recombinant protein in Escherichia coli BL21(DE3) during long-term cultivation. Our study demonstrated that the auto-induction of recombinant protein varied in different vectors harboring heterologous genes. Trx, GST, and their fusion proteins such as GST–human parathyroid hormone (hPTH), expressed by pET32a (+), were easily auto-induced by media containing a high content of yeast extract; however, rtPA was not easily auto-induced when using pET22b (+), although both pET systems were under the control of T7lac promoter. Furthermore, the auto-induction of GST–hPTH may start within 1–2 h after inoculation in bioreactors, which is a deficiency in the scale-up from shake flasks to bioreactors. Our results indicated that too much yeast extract in bioreactor cultivations may be responsible for the early auto-induction of target proteins and consequent loss of cell viability and plasmid instability. To achieve a satisfactory yield, host cells with both high cell viability and plasmid stability were necessary for the starter cultures in shake flasks and pre-induction cultures in bioreactors. This could be achieved simply by controlling the initial content of yeast extract and its subsequent supplementation.     

Pilot- and process-scale techniques for cell disruption

Microorganisms are a source of protein with catalytic and/or biological activity, which are of increasing commercial interest for applications in industry or therapy. For the isolation of intracellular products cell disruption is necessary. In principle, chemical, biological, or physical means may be employed to release proteins from cells. These different approaches are reviewed with special emphasis on scale-up and possible industrial operation. Mechanical devices have been improved considerably in recent years and appear most universally suited to cell disintegration. Chemical extraction or enzymatic lysis offers improved selectivity but requires individual procedures for each product. For a final process design, product yield and cost of the unit operation must be considered as well as the possible implications for the subsequent steps in product recovery, especially on solid/liquid separation.     

Animal component‐free Agrobacterium tumefaciens cultivation media for better GMP‐compliance increases biomass yield and pharmaceutical protein expression in Nicotiana benthamiana

Transient expression systems allow the rapid production of recombinant proteins in plants. Such systems can be scaled up to several hundred kilograms of biomass, making them suitable for the production of pharmaceutical proteins required at short notice, such as emergency vaccines. However, large‐scale transient expression requires the production of recombinant Agrobacterium tumefaciens strains with the capacity for efficient gene transfer to plant cells. The complex media often used for the cultivation of this species typically include animal‐derived ingredients that can contain human pathogens, thus conflicting with the requirements of good manufacturing practice (GMP). We replaced all the animal‐derived components in yeast extract broth (YEB) cultivation medium with soybean peptone, and then used a design‐of‐experiments approach to optimize the medium composition, increasing the biomass yield while maintaining high levels of transient expression in subsequent infiltration experiments. The resulting plant peptone Agrobacterium medium (PAM) achieved a two‐fold increase in OD₆₀₀ compared to YEB medium during a 4‐L batch fermentation lasting 18 h. Furthermore, the yields of the monoclonal antibody 2G12 and the fluorescent protein DsRed were maintained when the cells were cultivated in PAM rather than YEB. We have thus demonstrated a simple, efficient and scalable method for medium optimization that reduces process time and costs. The final optimized medium for the cultivation of A. tumefaciens completely lacks animal‐derived components, thus facilitating the GMP‐compliant large‐scale transient expression of recombinant proteins in plants.     

Understanding the effect of high gas entrance velocity on Chinese hamster ovary (CHO) cell culture performance and its implications on bioreactor scale-up and sparger design

There are three main potential sources for cell shear damage existing in stirred tank bioreactors. One is the potential high energy dissipation in the immediate impeller zones; another from small gas bubble burst; and third is from high gas entrance velocity (GEV) emitting from the sparger. While the first two have been thoroughly addressed for the scale-up of Chinese hamster ovary (CHO) cell culture knowing that a wide tolerable agitation range with non-damaging energy dissipation exists and the use of shear protectants like Pluronic F68 guard against cell damage caused by bubble burst, GEV remains a potential scale-up problem across scales for the drilled hole or open pipe sparger designs. GEV as high as 170 m/s due to high gas flow rates and relatively small sparger hole diameters was observed to be significantly detrimental to cell culture performance in a 12,000 L bioreactor when compared to a satellite 2 L bioreactor run with GEV of <1 m/s. Small scale study of GEV as high as 265 m/s confirmed this. Based on the results of this study, a critical GEV of >60 m/s for CHO cells is proposed, whereas previously 30 m/s has been reported for NS0 cells by Zhu, Cuenca, Zhou, and Varma (2008. Biotechnol. Bioeng., 101, 751–760). Implementation of new large scale spargers with larger diameter and more holes lowered GEV and helped improve the cell culture performance, closing the scale-up gap. Design of such new spargers was even more critical when hole plugging was discovered during large scale cultivation hence exacerbating the GEV impact. Furthermore, development of a scale down model based on mimicry of the large scale GEV profile as a function of time was proven to be beneficial for reproducing large scale results.     

Biologicals produced from animal cells in culture--an overview

A wide spectrum of biologicals are produced from animal cells in culture. Among these biologicals are viral vaccines (human and veterinary), monoclonal antibodies, immunoregulators, enzymes, hormones, polypeptide growth factors, viral bioinsecticides, tumor antigens, cell mass as a product and reconstitution of living skin. For research and development (R&D) and production of these products requires knowledge and experience in one or more of the following advanced technologies: 1) Development of novel as well as modification of conventional cultivation equipment; 2) Adaptation of cultivation techniques to the production of the desired product; 3) Hybridization technologies; 4) Genetic engineering techniques suitable for animal cells; 5) Development of a wide range of microcarriers and fixed-bed culturing systems; 6) Microencapsulation techniques; 7) Development of suitable media for cell cultivation; 8) Adaptation of suitable protein concentration and purification techniques.     

High density and scale-up cultivation of recombinant CHO cell line and hybridomas with porous microcarrier Cytopore

Using porous microcarrier Cytopore and a low-serum medium supplement BIGBEF-3, we have successfully cultivated recombinant CHO cell line CL-11G producing prourokinase and hybridomas producing anti-prourokinase monoclonal antibody in Celligen 1.5 or 5 L bioreactor. The cell density obtained ranged from 1 to 2 × 107 cells mL-1. The yields of prourokinase and monoclonal antibody increased with increasing cell density. As the cells could spontaneously release from and reattach to porous microcarriers, it was very easy to scale-up the cultivation. Thus the bead to bead cell transfer method has been used to scale up the cultivation of CL-11G cells to a 20 L reactor-scale for the pilot production of prourokinase, and also to scale-up the culture of hybridomas for the production of monoclonal antibody for the purification of prourokinase. This revised version was published online in July 2006 with corrections to the Cover Date.     

Biotechnological aspects of the production of the anticancer drug podophyllotoxin

The natural lignan podophyllotoxin, a dimerized product of two phenylpropanoid moieties which occurs in a few plant species, is a pharmacologically important compound for its anticancer activities. It is used as a precursor for the chemical synthesis of the anticancer drugs etoposide, teniposide and etopophose. The availability of this lignan is becoming increasingly limited because of the scarce occurrence of its natural sources and also because synthetic approaches for its production are still commercially unacceptable. Biotechnological production using cell culture may be considered as an alternative source. Selection of the best performing cell line, its maintenance and stabilization are necessary prerequisites for its production in bioreactors and subsequent scale-up of the cultivation process to the industrial level. Scale-up of growth and product yield depends on a multitude of factors, such as growth medium, physicochemical conditions, seed inoculum, type of reactor and processing conditions. The composition of the growth medium, elicitors and precursors, etc. can markedly influence the production. Optimum levels of parameters that facilitate high growth and product response in cell suspensions of Podophyllum hexandrum have already been determined by statistical design. P. hexandrum cells have successfully been cultivated in a 3-l stirred-tank bioreactor under low shear conditions in batch and fed-batch modes of operation. The batch kinetic data were used to identify the mathematical model which was then used to develop nutrient-feeding strategies for fed-batch cultivation to prolong the productive log phase of cultivation. An improvement in the production of podophyllotoxin to 48.8 mg l^–1 in a cell culture of P. hexandrum was achieved, with a corresponding volumetric productivity of 0.80 mg l^–1 day^–1, when the reactor was operated in continuous cell-retention mode. Efforts are being made to further enhance its production levels by the development of hairy root culture or by varying the channeling of precursors towards the desired biosynthetic pathway by molecular approaches.     

Use of Plant Viruses for Production of Plant-Derived Vaccines

Plants produce appropriately folded, post-translationally processed proteins that, as antigens, elicit efficacious immune responses in preclinical animal models and antigen-specific responses in humans. Plant-produced vaccine candidates have been produced using transgenic technologies and the utilization of plant viruses for the transient protein expression. The later approach has numerous advantages in recombinant protein production, including rapid protein expression and higher yields of antigenic proteins. In some cases, plant viruses are “decorated” with human or animal antigens from pathogens to form chimeric virus particles (CVPs). Immunization of animals with CVPs induces specific and often efficacious immune responses. While there are no plant-produced vaccines commercially available, the diversity and effectiveness of the products presently in development coupled with production advantages, including, reduced cost of production, the rapid scale-up capabilities, and the safety of the final product, should encourage continued investment and progress through clinical testing.     

Influence of low temperature on productivity, proteome and protein phosphorylation of CHO cells.

Proliferation of mammalian cells can be controlled by low cultivation temperature. However, depending on cell type and expression system, varying effects of a temperature shift on heterologous protein production have been reported. Here, we characterize growth behavior and productivity of the Chinese hamster ovary (CHO) cell line XM111-10 engineered to synthesize the model-product-secreted alkaline phosphatase (SEAP). Shift of cultivation temperature from 37 degrees C to 30 degrees C caused a growth arrest mainly in the G1 phase of the cell cycle concomitant with an up to 1.7-fold increase of specific productivity. A low temperature cultivation provided 3.4 times higher overall product yield compared to a standard cultivation at 37 degrees C. The cellular and molecular mechanisms underlying the effects of low temperature on growth and productivity of mammalian cells are poorly understood. Separation of total protein extracts by two-dimensional gel electrophoresis showed altered expression levels of CHO-K1 proteins after decrease in cultivation temperature to 30 degrees C. These changes in the proteome suggest that mammalian cells respond actively to low temperature by synthesizing specific cold-inducible proteins. In addition, we provide the first evidence that the cold response of mammalian cells includes changes in postranslational protein modifications. Two CHO proteins were found to be phosphorylated at tyrosine residues following downshift of cultivation temperature to 30 degrees C. Elucidating cellular events during cold exposure is necessary for further optimization of host-cell lines and expression systems and can provide new strategies for metabolic engineering.