An anti-apoptotic HEK293 cell line provides a robust and high titer platform for transient protein expression in bioreactors

ABSTRACT

HEK293 transient expression systems are used to quickly generate proteins for research and pre-clinical studies. With the aim of engineering a high-producing host that grows and transfects robustly in bioreactors, we deleted the pro-apoptotic genes Bax and Bak in an HEK293 cell line. The HEK293 Bax Bak double knock-out (HEK293 DKO) cell line exhibited resistance to apoptosis and shear stress. HEK293 DKO cells sourced from 2 L seed train bioreactors were most productive when a pH setpoint of 7.0, a narrow pH deadband of ±0.03, and a DO setpoint of 30% were used. HEK293 DKO seed train cells cultivated for up to 60 days in a 35 L bioreactor showed similar productivities to cells cultivated in shake flasks. To optimize HEK293 DKO transfection cultures, we first evaluated different pH and agitation parameters in ambr15 microbioreactors before scaling up to 10 L wavebag bioreactors. In ambr15 microbioreactors with a pH setpoint of 7.0, a wide pH deadband of ±0.3, and an agitation of 630 rpm, HEK293 DKO transient cultures yielded antibody titers up to 650 mg/L in 7 days. The optimal ambr15 conditions prompted us to operate the 10 L wavebag transfection without direct pH control to mimic the wide pH deadband ranges. The HEK293 DKO transfection process produces high titers at all scales tested. Combined, our optimized HEK293 DKO 35 L bioreactor seed train and 10 L high titer transient processes support efficient, large-scale recombinant protein production for research studies.     

Identification of a novel miRNA that increases transient protein expression in combination with valproic acid

Transient gene expression in mammalian cells is an efficient process to produce recombinant proteins for various research applications and large molecule therapeutics development. For the first time, we report a screen to identify human microRNAs (miRNAs) that increase titers after polyethylenimine (PEI) mediated transient transfection of a HEK293 cell line. From a library of 875 miRNAs, we identified 2 miRNAs, miR‐26a‐5p and miR‐337‐5p, that increased human IgG1 (huIgG1) yields by 50 and 25%, respectively. The titer increase was achievable by expressing miR‐26a‐5p from oligonucleotides or a plasmid. Furthermore, combining miR‐26a‐5p with valproic acid (VPA) treatment doubled huIgG1 titers. Assessment of miR‐26a‐5p and VPA treatment across a panel of 32 human and murine antibodies demonstrates that the level of yield enhancement was molecule‐dependent, with most exhibiting a range of 50–100% titer increase. These findings exemplify that combining genetic and chemical manipulation can be an effective strategy to enhance transient transfection productivity. © 2017 American Institute of Chemical Engineers Biotechnol. Prog., 33:1139–1145, 2017     

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. This revised version was published online in July 2006 with corrections to the Cover Date.     

High throughput screening identifies novel,cell cycle‐arresting small molecule enhancers of transient protein expression

Transient gene expression in mammalian cells is an efficient process for producing recombinant proteins for various research applications to support large molecule therapeutics development. For the first time, we report a high throughput small molecule (SM) screen to identify novel compounds that increase antibody titers after polyethylenimine (PEI) transient transfection of a HEK293 cell line. After screening 31,413 SMs in a 50 μL scaled‐down process, we validated 164 SMs to improve yields by up to twofold. The titer increase mediated by the SMs varied for different antibodies. SM dose optimizations resulted in almost threefold higher titers. The top 2, structurally distinct SM hits, increased antibody titers more than twofold in a 1 mL production process. Averaged across three antibodies of different expression levels, the compounds enhanced transient productivity by ～80%. Intriguingly, both compounds arrested cells in the G2/M cell cycle phase leading to a decrease in growth and nutrient consumption, while elevating titer, nuclear plasmid DNA (pDNA) copy numbers, and mRNA levels. © 2017 American Institute of Chemical Engineers Biotechnol. Prog., 3:1579–1588, 2017     

Large-scale Transient Transfection of Mammalian Cells: A Newly Emerging Attractive Option for Recombinant Protein Production

Mammalian expression systems have an undisputed long-standing and very successful history for the generation of recombinant proteins, mainly as biopharmaceuticals. However, for use as ‘tool proteins’ in, e.g. assay development and screening, for structure elucidation and as antigens these expression systems were generally regarded as being cumbersome, tedious and expensive. This bias has largely been overcome with the very recent development of large-scale transient transfection (LST) approaches. Especially the HEK.EBNA expression system described here has contributed significantly to this success. The simplicity and speed of this approach compares well with expression trials using the widely applied Baculovirus/insect cell system. In addition, proteins generated in mammalian cells are usually correctly folded, fully processed and functionally active.     

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. This revised version was published online in July 2006 with corrections to the Cover Date.     

过表达Grx1抑制HEK293T细胞中H2O2诱导的p38MAPK信号通路

谷氧还蛋白1（glutaredoxin1,Grx1）是细胞内一种重要的巯基 二硫键氧化还原酶,在细胞内氧化还原状态的调控及抵抗氧化应激损伤过程中发挥重要作用.为进一步探讨Grx1的抗氧化机制,本实验将重组质粒pcDNA3.1(+)-hGrx1瞬时转染HEK293T细胞,经RT-PCR和Western印迹验证,细胞转染后实现了Grx1的过表达;以不同浓度H₂O₂为损伤因素,建立细胞氧化应激模型,检测过表达Grx1后细胞存活率,丙二醛（MDA）含量,超氧化物歧化酶（SOD）活力和乳酸脱氢酶（LDH）漏出率的变化,观察过表达Grx1后细胞的抗氧化能力;用终浓度100 μmol/LH₂O₂作用于细胞,利用Western 印迹检测120 min内HEK293T细胞中p38MAPK磷酸化水平.实验结果表明,HEK293T细胞过表达Grx1后,缓解了细胞的氧化应激损伤;转染空载体组细胞p38MAPK磷酸化水平在H₂O₂刺激后5 min开始升高,15 min达到最高值,并可维持至120 min左右;而过表达Grx1组细胞p38MAPK磷酸化水平在H₂O₂刺激后各时间段没有明显改变,提示Grx1通过抑制H₂O₂诱导的p38MAPK信号通路激活发挥其抗氧化作用.     

100-liter transient transfection

This is the first report of two successful 100 l scale transienttransfections in a standard stirred bioreactor. More than half a gram of a monoclonal antibody (IgG) were produced in less than 10 days using a technology called large-scale transient gene expression(LS-TGE). Suspension adapted HEK 293 EBNA SF cells were transfectedwithin a 150 l (nominal) bioreactor by a modified calcium phosphateco-precipitation method with more than 75 mg of plasmid DNA per run.A mixture of three different plasmids, one encoding for the heavychain of a human recombinant immunoglobulin, the other for the corresponding light chain and a third one for the green fluorescent protein (GFP, 2–4% of DNA in transfection cocktail)were co-transfected. The GFP vector was chosen to monitor transfection efficiency. Expression of GFP could be registered asearly as 20 h after DNA addition, using fluorescence microscopy. We demonstrate that transient transfection can be done at the100 l scale, thus providing a new tool to produce hundreds of milligrams or even gram amounts of recombinant protein. Akey advantage of LS-TGE resides in its speed. In the presentedcases, the entire production process for the synthesis of halfa gram of a recombinant antibody, including DNA preparationand necessary expansion of cells prior to transfection, wasexecuted in less than a month. Having an established transfection/expression process allows to run productioncampaigns for any given protein, within one facility, with onesingle host cell line and therefore only one single seed train. Without any need to create and maintain stable cell lines, expression of new r-proteins is not only faster and more economical but also more flexible.     

Recombinant soluble human Fcgamma receptor I with picomolar affinity for immunoglobulin G

The ectodomain of human FcgammaRI (rsCD64) was expressed in HEK 293T cells and purified by immobilized-metal affinity chromatography. Binding activity to human IgG was verified by ELISA and the isotype-specificity determined by a surface plasmon resonance inhibition assay was found to be the same as for native CD64. The active concentration of the rsCD64 preparation was derived using a solution competition assay and was used for the subsequent kinetic analysis. Binding curves were well described by a simple monovalent interaction model confirming the known stoichiometry of the interaction. Mass-transport limitation was prevented by using sufficiently low surface capacities. For binding to the recombinant mouse/human chimeric antibody cPIPP (IgG1/kappa) a high association rate of k(ass)=1.7 x 10(6) (M s)(-1) and a low dissociation rate of k(diss)=1.8 x 10(-4) s(-1) were observed. The derived dissociation equilibrium constant of K(D)=110 pM was significantly lower than that reported for binding to native FcgammaRI.     

Continuous production and recovery of recombinant Ca2+ binding receptor from HEK 293 cells using perfusion through a packed bed bioreactor

The extracellular domain of human parathyroid Ca²⁺ receptor was needed in order to study itsstructure and clinical application. The Ca²⁺receptor is a unique member of the G protein-coupledreceptor super-family, expressed in parathyroid andkidney cells where it has been shown to play acritical role in extracellular calcium homeostasis.The desired protein was produced by immobilizing thetransformed HEK 293 cells in a packed-bedconfiguration using a 1.6 l (working volume)bioreactor equipped with a vertical mixing impellerassembly and an internal basket. The process includeda propagation phase followed by a production phase. Inthe propagation phase, lasting approximately 160 h, the bed was perfused with a serum-containingmedium, allowing the cells to grow at a constantgrowth rate to approximately 3 × 10¹⁰. At this point the production phase was begun, replacing themedium with serum-free medium and continuing theperfusion process for additional 350 h. Duringthis phase, the medium was pumped through the packedbed at a rate of 4–6 l per day, keeping theresidual glucose concentration around 1 g l^-1 andcollecting and processing approximately 80 l ofspent medium. This continuous perfusion method of thepacked-bed bioreactor was compared to a repeated batchmethod in which existing medium was replenished whenthe glucose concentration was down to 1 g l^-1. Using this method, serum-free medium was replaced withserum containing medium a few times when a decline inthe glucose consumption was observed. Though mediumconsumption and protein yield are similar in bothmethods (roughly 10 mg l^-1), there aredifferences related to the ease of operation andprocessing of the produced protein. The continuousperfusion operation was found to be preferable and waschosen as the production strategy.