Ernst-Jürgen Schlaeger

The protein hydrolysate, Primatone RL, is a cost-effective multiple growth promoter of mammalian cell culture in serum-containing and serum-free media and displays anti-apoptosis properties.

The tryptic meat digest Primatone RL is a low-cost medium supplement of a complex nature which serves as a source of amino acids, oligopeptides, iron salts, some lipids and other trace low molecular weight substances. Its addition to mammalian and insect cell culture media significantly improves the cell growth properties of many cell lines. In this work the growth promoting effects of Primatone RL are described in more detail using different mouse hybridomas, a mouse myeloma cell line, and human promyelocytic leukemia HL-60 cells. The positive effects on cell growth induced by Primatone were observed in the presence of serum but were even more pronounced in serum-free culture. In addition the adaptation time from high serum to low (1%) or serum-free growth in the presence of Primatone is also significantly reduced. Primatone RL, when added to HL and DHI medium, improves cell growth under low serum or serum-free conditions by increasing the maximum cell numbers and in particular the viability of the culture. The observed decrease in cell death (apoptosis) induction leads to a significant improvement in antibody (recombinant protein) production by increasing the volumetric yields during long-term batch culture. The so-called anti-apoptotic effects of Primatone RL for mouse hybridomas, which is concentration dependent, is not fully understood.

Transient gene expression in mammalian cells grown in serum-free suspension culture

In order to establish a simple and scaleable transfection system we have used the cationic polymer polyethylenimine (PEI) to study transient transfection in HEK293 and 293(EBNA) cells grown in serum-free suspension culture. The transfection complexes were made directly within the cell culture by consecutively adding plasmid and PEI (direct method). Alternatively, the DNA-PEI transfection complexes were prepared in fresh medium (1/10 culture volume) and then added to the cells (indirect method). The results of this study clearly show that the ratio of PEI nitrogen to DNA phosphate is very important for high expression levels. The precise ratio is dependent on the DNA concentration. For example, using 1 μg/ml DNA by the indirect method, the ratio of optimal PEI:DNA was about 10–13:1. However, the ratio increases to 33:1 for 0.1–0.2 μg/ml DNA. By testing several different molecular weights of the polycationic polymer we could show that the highest transfection efficiency was obtained with the PEI 25 kDa. Using PEI 25 kDa the indirect method is superior to the direct addition because significantly lower DNA concentrations are needed. The expression levels of the soluble human TNF receptor p55 are even higher at low DNA compared to 1 μg/ml plasmid. The EBV-based pREP vectors gave better transient gene expression when used in 293(EBNA) cells compared to HEK293 cells in suspension culture. No differences in expression levels in the two cell lines were observed when the pC1 (CMV)-TNFR was used. In conclusion, PEI is a low-toxic transfection agent which provides high levels of transient gene expression in 293(EBNA) cells grown in serum-free suspension culture. This system allows highly reproducible, cost-effective production of milligram amounts of recombinant proteins in 2–5 l spinner culture scale within 3–5 days. Fermentor scale experiments, however, are less efficient because the PEI-mediated transient tranfection is inhibited by conditioned medium.

Growth study of lactate and ammonia double-resistant clones of HL-60 cells.

The possibility that lactate and ammonia accumulation may have less detrimental effect on cell growth than usually admitted is investigated. We report here the isolation of several HL-60 subclones able to proliferate in the presence of 60 mM sodium lactate and 4 mM ammonium chloride, concentrations usually considered to be toxic for cell proliferation. Growth kinetics and final cell densities of these clones in suspension cultures were similar to the HL-60 cell population in control medium as well as in medium containing ammonia and lactate in which control cells were unable to grow. The metabolic pattern of the double-resistant clones revealed that lactate and ammonia formation was inhibited in the presence of lactate and ammonia in the medium, while alanine production and arginine consumption were enhanced irrespective of the medium.

Propagation of a mouse myeloma cell line J558L producing human CD4 immunoglobulin G1

Transfected mouse myeloma cells are of increasing interest for the production of a wide variety of solubilised recombinant fusion proteins. A stably transfected J558L mouse myeloma subclone (J558L-CD4) secreting human CD4-immunoglobulin type G1 receptor (CD4-H gamma 1) was employed as a model system for cell suspension culture and expression of chimaeric molecules. Cells were grown up to 3-5 x 10(6) cells/ml in serum-free and protein-reduced DHI medium consisting of a mixture of DMEM, HamF12 and IMDM media supplemented with transferrin, insulin, Primatone RL and Pluronic F68. Primatone RL was the essential growth-promoting factor in protein-free medium. The soluble CD4-H gamma 1 receptor, the production of which was not growth-associated, accumulated in the medium to concentrations of 40 micrograms/ml with a specific formation rate of 0.18 micrograms/10(6) cells/h in conventional cultures. The cell density was further increased by growing the cells in dialysis tubing or by using a perfusion system with cell retention. Because of the continuous exchange of nutrients and metabolic end-products average concentrations of 35 x 10(6) cells/ml were achieved. CD4-H gamma 1 accumulated in the dialysis tubing up to 1.3 mg/ml. After an initial rapid growth period, a ten-fold reduction in specific nutrient consumption rates and metabolic end-product formation was observed. Chimaeric proteins purified by protein G chromatography from conventional and perfusion cultures were indistinguishable when compared by SDS-PAGE, limited proteolysis and isoelectric focusing analysis (isoelectric point: 8.5-8.6).

Non-GMP plasmid production for transient transfection in bioreactors

We describe a generic plasmid purification process for producing DNA for larger-scale transient transfection. Data on plasmid quality with regard to residual protein, endotoxin content and presence of different plasmid forms is given. The effects of contaminants and plasmid forms on expression levels of TNFRp55 and SEAP are discussed. Transient transfection of serum-free suspension grown mammalian cells represents a suitable approach to provide research quantities of proteins (50–100 mg) within1–2 weeks.

Stable expression in Chinese hamster ovary cells of a homogeneous recombinant active fragment of human platelet glycoprotein Ibα

A fragment (residues His1-Val289) of the α chain of human platelet glycoprotein Ib containing the von Willebrand factor and thrombin binding sites has been expressed in Chinese hamster ovary cells. The secreted soluble recombinant protein had an apparent molecular mass of 42 kD and reacted with a conformation-dependent monoclonal antibody that only binds to native GP Ib, thus demonstrating its proper folding. The rather broad band obtained after immobilization of the recombinant fragment on nitrocellulose could be resolved into a very sharp band of molecular weight of about 35 kD by growing the cells in the presence of tunicamycin, and inhibitor of N-linked glycosylation. The recombinant GP Ibα fragments (with or without glycosylation) were purified by immunoaffinity chromatography. Both truncated forms bound vWF in the presence of botrocetin with comparable affinity as a proteolytic 42 kD fragment of purified human platelet GP Ib-IX. They were also retained on thrombin-Sepharose. We then selected a cell clone (B1) that produced over at least three months about 1.5 μg of recombinant protein per million cells per day. Using this clone a large-scale production finally yielded milligram amounts of the functionally active recombinant human GP Ibα fragment.

Expression, purification and crystallization of fully active, glycosylated human interleukin-5

Recombinant human interleukin‐5 (hIL‐5) has been expressed at high levels and produced in large quantities in baculovirus infected Sf9 insect cells. The glycosylated protein was purified using immuno‐affinity chromatography and gel filtration. Purified hIL‐5 has been crystallized using standard vapour diffusion techniques with PEG as a coprecipitant. The crystals belong to the C2 space group and diffract to 2 Å.

Safety aspects related to recombinant protein expression from Semliki Forest virus vectors

Semliki Forest virus vectors (SFV) have been developed for efficient transgene expression to result in high receptor yields(50–200 pmol receptor/mg protein) in a variety of mammalian host cells. Transfer of the SFV technology to mammalian cells growing in suspension cultures has made it feasible to produce hundreds of milligrams of receptor proteins in a short time. Large-scale production, however, raises the questions of the safety of handling virally infected cells for down-stream processing. Analysis of cell culture medium and SFV-infected cells revealed that some infectious particles were still present. Replacement of virus-containing medium at 2 h post-infection efficiently removed the majority of infectious replication-deficient SFV particles. Washes with PBS further reduced the number of infectious particles significantly both in the medium and associated with cells to levels that allowed safe handling of SFV-infected cells outside the cell culture facility for biochemical, pharmacological, or electrophysiological assays or down-stream processes in connection to receptor purification. Furthermore, engineering of novel temperature-sensitive mutant SFV vectors resulted in temperature-controlled transgene expression, which completely eliminates the risk of contaminating laboratory personnel.