Monoclonal antibodies (mAbs) are highly efficacious therapeutics; however, due to their large, dynamic nature, structural perturbations and regional modifications are often difficult to study. Moreover, the homodimeric, symmetrical nature of mAbs makes it difficult to elucidate which heavy chain (HC)-light chain (LC) pairs are responsible for any structural changes, stability concerns, and/or site-specific modifications. Isotopic labeling is an attractive means for selectively incorporating atoms with known mass differences to enable identification/monitoring using techniques such as mass spectrometry (MS) and nuclear magnetic resonance (NMR). However, the isotopic incorporation of atoms into proteins is typically incomplete. Here we present a strategy for incorporating 13C-labeling of half antibodies using an Escherichia coli fermentation system. Unlike previous attempts to generate isotopically labeled mAbs, we provide an industry-relevant, high cell density process that yielded >99% 13C-incorporation using 13C-glucose and 13C-celtone. The isotopic incorporation was performed on a half antibody designed with knob-into-hole technology to enable assembly with its native (naturally abundant) counterpart to generate a hybrid bispecific (BsAb) molecule. This work is intended to provide a framework for producing full-length antibodies, of which half are isotopically labeled, in order to study the individual HC-LC pairs.

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

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.

Background: Protein secretion to the periplasm of Escherichia coli offers an attractive route for producing heterologous proteins including antibodies. In this approach, a signal peptide is fused to the N-terminus of the heterologous protein. The signal peptide mediates translocation of the heterologous protein from the cytoplasm to the periplasm and is cleaved during the translocation process. It was previously shown that optimization of the translation initiation region (TIR) which overlaps with the nucleotide sequence of the signal sequence improves the production of heterologous proteins. Despite the progress, there is still room to improve yields using secretion as a means to produce protein complexes such as full-length monoclonal antibodies (mAbs).Results: In this study we identified the inefficient secretion of heavy chain as the limitation for full-length mAb accumulation in the periplasm. To improve heavy chain secretion we investigated the effects of various signal peptides at controlled TIR strengths. The signal peptide of disulfide oxidoreductase (DsbA) mediated more efficient secretion of heavy chain than the other signal peptides tested. Mutagenesis studies demonstrated that at controlled translational levels, hydrophobicity of the hydrophobic core (H-region) of the signal peptide is a critical factor for heavy chain secretion and full-length mAb accumulation in the periplasm. Increasing the hydrophobicity of a signal peptide enhanced heavy chain secretion and periplasmic levels of assembled full-length mAbs, while decreasing the hydrophobicity had the opposite effect.Conclusions: This study demonstrates that under similar translational strengths, the hydrophobicity of the signal peptide plays an important role in heavy chain secretion. Increasing the hydrophobicity of the H-region and controlling TIR strengths can serve as an approach to improve heavy chain secretion and full-length mAb production in E. coli.

High throughput protein production from transient transfection of mammalian cells is used in multiple facets of research and development studies. Commonly used formats for these high number expressions are 12‐, 24‐ and 96‐well plates at various volumes. However there are no published examples of a 96‐deep well plate microscale (1,000 μL) suspension process for mammalian transient expression. For this reason, we aimed to determine the optimal operating conditions for a high producing, microscale HEK293 transient system. We evaluated the hydrodynamic flow and measured the oxygen transfer rate (OTR) and transient protein expression for 96‐deep well plates of different well geometries filled at 600–1,000 μL working volumes and agitated at various speeds and orbital diameters. Ultimately, a round well‐round bottom (RR) 96‐deep well plate with a working volume of 1,000 µL agitated at 1,000 RPM and a 3 mm orbital diameter yielded the highest and most consistent total transient protein production. As plate cultures are subject to evaporation, water loss from different plate seals was measured to identify an optimal plate sealing method. Finally, to enable higher capacity protein production, both expression and purification processes were automated. Functionality of this end‐to‐end automation workflow was demonstrated with the generation of high levels of human IgG1 antibodies (≥360 µg/mL) with reproducible productivity, product quality and ≥78% purification recovery. Biotechnol. Bioeng. 2015;112: 1832–1842. © 2015 Wiley Periodicals, Inc.

Transient gene expression in mammalian cells allows for rapid production of recombinant proteins for research and preclinical studies. Here, we describe the development of a polyethylenimine (PEI) transient transfection system using an anti-apoptotic host cell line. The host cell line, referred to as the Double Knockout (DKO), was generated by deleting two pro-apoptotic factors, Bax and Bak, in a CHO-K1 cell line using zinc finger nuclease mediated gene disruption. Optimized DNA and PEI volumes for DKO transfections were 50% and 30% lower than CHO-K1, respectively. During transfection DKO cells produced relatively high levels of lactate, but this was mitigated by a temperature shift to 31°C which further enhanced productivity. DKO cells expressed ∼3- to 4-fold higher antibody titers than CHO-K1 cells. As evidence of their anti-apoptotic properties post-transfection, DKO cells maintained higher viability and had reduced levels of active caspase-3 compared to CHO-K1 cells. Nuclear plasmid DNA copy numbers and message levels were significantly elevated in DKO cells. Although DNA uptake levels, as early as 40 min post-transfection, were higher in DKO cells this was not due to differences in cell surface heparan sulfate (HS) or initial endocytosis mechanism as both cell types utilized caveolae- and clathrin-mediated endocytosis to internalize DNA:PEI complexes. These results suggest that the increased transfection efficiency and titers from DKO cells are attributed to their resistance to transfection-induced apoptosis and not differences in endocytosis mechanism.

By enabling the simultaneous engagement of two distinct targets, bispecific antibodies broaden the potential utility of antibody-based therapies. However, bispecific-antibody design and production remain challenging, owing to the need to incorporate two distinct heavy and light chain pairs while maintaining natural nonimmunogenic antibody architecture. Here we present a bispecific-antibody production strategy that relies on co-culture of two bacterial strains, each expressing a half-antibody. Using this approach, we produce 28 unique bispecific antibodies. A bispecific antibody against the receptor tyrosine kinases MET and EGFR binds both targets monovalently, inhibits their signaling, and suppresses MET and EGFR-driven cell and tumor growth. Our strategy allows rapid generation of bispecific antibodies from any two existing antibodies and yields milligram to gram quantities of bispecific antibodies sufficient for a wide range of discovery and preclinical applications.

Human bispecific antibodies have great potential for the treatment of human diseases. Although human IgG1 bispecific antibodies have been generated, few attempts have been reported in the scientific literature that extend bispecific antibodies to other human antibody isotypes. In this paper, we report our work expanding the knobs-into-holes bispecific antibody technology to the human IgG4 isotype. We apply this approach to generate a bispecific antibody that targets IL-4 and IL-13, two cytokines that play roles in type 2 inflammation. We show that IgG4 bispecific antibodies can be generated in large quantities with equivalent efficiency and quality and have comparable pharmacokinetic properties and lung partitioning, compared with the IgG1 isotype. This work broadens the range of published therapeutic bispecific antibodies with natural surface architecture and provides additional options for the generation of bispecific antibodies with differing effector functions through the use of different antibody isotypes.

Significance Therapeutic antibodies have revolutionized the treatment of human disease. Despite these advances, antibody bivalency limits their utility against some targets. Here, we describe the development of a one-armed (monovalent) antibody, onartuzumab, targeting the receptor tyrosine kinase MET. While initial screening of bivalent antibodies produced agonists of MET, engineering them into monovalent antibodies produced antagonists instead. We explain the structural basis of the mechanism of action with the crystal structure of onartuzumab antigen-binding fragment in complex with MET and HGF-β. These discoveries have led to an additional antibody-based therapeutic option and shed light on the underpinnings of HGF/MET signaling.

The number of monoclonal antibodies approved for use as therapeutic agents by regulatory agencies has increased in the past several years. Monoclonal antibodies are predicted to become an increasingly larger part of biopharmaceutical products, and perhaps dominate the market share by the end of the decade (Walsh 2006). Mammalian expression systems, such as Chinese Hamster Ovary cells (CHO), are currently the preferred system for producing full-length monoclonal antibodies. Fungal systems could become more of a contender for the production of antibodies if titers can be increased (Andersen and Reilly 2004). However, with fungal production systems, there may be concerns about potential non-native mammalian N-linked or O-linked glycosylation that could result in immunogenic responses in humans. Technology developed in recent years (Hamilton et al. 2003) could help to alleviate this concern.

Removal of the core alpha1,6 fucose from the glycans in the Fc region of IgG1 antibodies has been demonstrated to improve antibody-dependent cellular cytotoxicity (ADCC) activity. In order to produce afucosylated antibodies using transient transfection, a FUT8 knockout (FUT8KO) cell line was generated in a CHO host cell line using the zinc finger nuclease technology. Transient transfection of DNA into mammalian cells using the cationic polymer, polyethylenimine (PEI), is commonly used for rapid generation of recombinant proteins. FUT8KO cells evaluated in PEI transfections yielded lower titers than parental CHO WT cells. FACS and HPLC analyses revealed that the FUT8KO cells had lower cell surface heparan sulfate (HS) levels than CHO WT. Removal of cell surface HS resulted in reduced uptake of PEI-transfected DNA (PEI:DNA) and lower transfection titers suggesting that PEI:DNA relies on HS for binding and cellular entry. The absence of cell surface HS did not severely impact transfections performed with cationic liposomes. We undertook two approaches to improve transient production of afucosylated antibodies. First, we evaluated transfection of FUT8KO cells with cationic liposomes, which were observed to be less dependent on HS levels for uptake. Transfection of FUT8KO cells using the cationic liposome, DMRIE-C, produced similar titers to CHO WT in both shake flask and large-scale 10 L bioreactors. The second approach was to engineer a cell line overexpressing exostosin-1 (EXT1), an enzyme responsible for HS chain elongation, to increase HS content. EXT1-FUT8KO and CHO WT cells produced comparable levels of antibody from PEI transfections.

Vascular endothelial growth factor (VEGF(165)) is a potent mitogen that induces angiogenesis and vascular permeability in vivo and has demonstrated potential in therapeutic applications for accelerating wound healing. An industrial production method that provides high yield as well as high purity, quality, and potency is needed. The process described in this report involves a bacterial expression system capable of producing approximately 9g of rhVEGF per liter of broth and a downstream purification process consisting of protein refolding and three chromatography steps prior to formulation of the drug substance. A high cell density (HCD) fed-batch fermentation process was used to produce rhVEGF in periplasmic inclusion bodies. The inclusion bodies are harvested from the cell lysate and subjected to a single-step protein solubilization and refolding operation to extract the rhVEGF for purification. Overall recovery yields observed during development, including refolding and chromatography, were 30+/-6%. Host cell impurities are consistently cleared below target levels at both laboratory and large-scale demonstrating process robustness. The structure of the refolded and purified rhVEGF was confirmed by mass spectrometry, N-terminal sequencing, and tryptic peptide mapping while product variants were analyzed by multiple HPLC assays. Biological activity was verified by the proliferation of human umbilical vein derived endothelial cells.