Expression of Multispecific Antibodies.

Bi- and multispecific antibody formats allow the development of new therapeutic strategies to address previously unmet medical needs. However, due to the increased complexity (e.g., the interface design and the presence of multiple binders), such molecules are generally more challenging to express and purify compared to standard monoclonal antibodies (mAbs). We describe here an optimized methodology to express and purify basic bispecific antibodies using the BEAT® interface. This interface allows to generate antibodies with very high levels of heterodimer product (reported titers exceed 10 g/L) and comes with a built-in purification strategy allowing removal of residual levels of undesired product-related impurities (e.g., homodimers and half molecules).

Expression of Bispecific Antibodies Using Cellular Display.

The identification and selection of high-producing cell lines can be a resource- and time-consuming process. The screening effort can be simplified by assessing the potential for high expression (or a desired product quality attribute) of the individual cell directly in a mix of cells. Here, we describe protocols for the use of such a cellular display technology. Using alternate splicing, two mRNA constructs are generated at tunable ratios. The first mRNA codes for the secreted product, the second mRNA attaches a transmembrane domain to the antibody and directs it to the cellular membrane. The design of the basic construct as well as efficient ways to tune the strength of the cellular display is detailed in this chapter. Further, enrichment methods are provided enabling the flow cytometric sorting of a cell population based on the quantity of cellular display or on the product quality (heterodimerization level of a bispecific antibody).

Alternative splicing for tuneable expression of protein subunits at desired ratios.

The controlled expression of two or more proteins at a defined and stable ratio remains a substantial challenge, particularly in the bi- and multispecific antibody field. Achieving an optimal ratio of protein subunits can facilitate the assembly of multimeric proteins with high efficiency and minimize the production of by-products. In this study, we propose a solution based on alternative splicing, enabling the expression of a tunable and predefined ratio of two distinct polypeptide chains from the same pre-mRNA under the control of a single promoter. The pre-mRNA used in this study contains two open reading frames situated on separate exons. The first exon is flanked by two copies of the chicken troponin intron 4 (cTNT-I4) and is susceptible to excision from the pre-mRNA by means of alternative splicing. This specific design enables the modulation of the splice ratio by adjusting the strength of the splice acceptor. To illustrate this approach, we developed constructs expressing varying ratios of GFP and dsRED and extended their application to multimeric proteins such as monoclonal antibodies, achieving industrially relevant expression levels (>1 g/L) in a 14-day fed-batch process. The stability of the splice ratio was confirmed by droplet digital PCR in a stable pool cultivated over a 28-day period, while product quality was assessed via intact mass analysis, demonstrating absence of product-related impurities resulting from undesired splice events. Furthermore, we showcased the versatility of the construct by expressing two subunits of a bispecific antibody of the BEAT® type, which contains three distinct subunits in total.

Development of a 10 g/L process for a difficult-to-express multispecific antibody format using a holistic process development approach.

Ichnos has developed a multi-specific antibody platform based on the BEAT® (Bispecific engagement by antibodies based on the T-cell receptor) interface. The increased complexity of the bi- and multi-specific formats generated with this platform makes these molecules difficult-to-express proteins compared to standard monoclonal antibodies (mAbs). This report describes how expression limitations of a bi-specific bi-paratopic BEAT antibody were improved in a holistic approach. An initial investigation allowed identification of a misbalance in the subunits composing the BEAT antibody as the potential root cause. This misbalance was then addressed by a signal peptide optimization, and the overall expression level was increased by the combination of two vector design elements on a single gene vector. Further improvements were made in the selection of cell populations and an upstream (USP) platform process was applied in combination with a cell culture temperature shift. This allowed titer levels of up to 6 g/L to be reached with these difficult-to-express proteins. Furthermore, a high-density seeding process was developed that allowed titers of around 11 g/L for the BEAT antibody, increasing the initial titer by a factor of 10. The approach was successfully applied to a tri-specific antibody with titer levels reaching 10 g/L. In summary, a platform process for difficult-to-express proteins was developed using molecular biology tools, cell line development, upstream process optimization and process intensification.

Viral inactivation for pH-sensitive antibody formats such as multi-specific antibodies.

Recently developed multi-specific antibody formats enable new therapeutic concepts. Conveniently, formats with an Fc domain allow purification in well-established mAb platform processes. However, due to the structural complexity of the formats, the assembled molecules may be sensitive to extreme pH commonly used for viral inactivation. An alternative to low pH incubation for virus inactivation is the use of a mixture of tri-n-butyl phosphate (TnBP, solvent) and Polysorbate 80 (PS80, detergent). While TnBP is toxic, this combination has a long history of use in the manufacturing of human plasma-derived products that are sensitive to low or high pH incubation. Data are provided demonstrating that the solvent/detergent (S/D) treatment using TnBP and PS80 can be successfully used for pH-sensitive, multi-specific antibody formats in the clarified cell culture fluid (CCCF). A different placement of the S/D within the purification process, namely during the capture by Protein A (PA), has been evaluated. This alternative placement allows effective viral inactivation by S/D while preserving the viral reduction and viral inactivation achieved through the PA step itself, enabling the cumulation of these effects. Furthermore, the process alternative simplifies the liquid handling by reducing the added volumes of the required S/D liquids, thus reducing the amount of toxic TnBP to a minimum. Data are shown demonstrating a complete removal of TnBP and PS80 in the process.

Blinding Approaches for Large Clinical Trials Involving Sub-Cutaneous Administration of Biologicals - A CMC Perspective.

A well-controlled clinical trial is one of the critical steps to evaluate the efficacy and safety of novel medicaments. The use of a placebo is employed in several types of clinical trials in order to set a baseline against which the efficacy of the investigational drug is evaluated. An ideal placebo should match the final formulation as close as possible such that the patient/health care providers are unable to identify any difference. This is difficult for high concentration biologic intended for subcutaneous administration, mainly because of their color and viscosity. Currently, the challenge is overcome by using opaque labels or by unblinded pharmacists, both solutions are expensive. The present study provides an efficient alternative where a protein excipient (recombinant albumin) is used to prepare a placebo for biologicals. We have demonstrated that the use of recombinant albumin can match the color of the active when used in the right quantity. The evaluated solution is highly flexible and has the potential to match the color of different biopharmaceuticals at different concentrations/formulations.

Stability of Biologics and the Quest for Polysorbate Alternatives.

Most biopharmaceutical formulations use polysorbates: surfactants that are highly efficient but difficult to manage in terms of compositional variability, quality, and stability. Alternatives, such as poloxamers, albumin, and cyclodextrin, are becoming popular and are being explored for their potential to protect biopharmaceuticals against physical and mechanical stresses.

A new large-scale manufacturing platform for complex biopharmaceuticals.

Complex biopharmaceuticals, such as recombinant blood coagulation factors, are addressing critical medical needs and represent a growing multibillion-dollar market. For commercial manufacturing of such, sometimes inherently unstable, molecules it is important to minimize product residence time in non-ideal milieu in order to obtain acceptable yields and consistently high product quality. Continuous perfusion cell culture allows minimization of residence time in the bioreactor, but also brings unique challenges in product recovery, which requires innovative solutions. In order to maximize yield, process efficiency, facility and equipment utilization, we have developed, scaled-up and successfully implemented a new integrated manufacturing platform in commercial scale. This platform consists of a (semi-)continuous cell separation process based on a disposable flow path and integrated with the upstream perfusion operation, followed by membrane chromatography on large-scale adsorber capsules in rapid cycling mode. Implementation of the platform at commercial scale for a new product candidate led to a yield improvement of 40% compared to the conventional process technology, while product quality has been shown to be more consistently high. Over 1,000,000 L of cell culture harvest have been processed with 100% success rate to date, demonstrating the robustness of the new platform process in GMP manufacturing. While membrane chromatography is well established for polishing in flow-through mode, this is its first commercial-scale application for bind/elute chromatography in the biopharmaceutical industry and demonstrates its potential in particular for manufacturing of potent, low-dose biopharmaceuticals.

Continuous separation of multicomponent protein mixtures by annular displacement chromatography.

Displacement chromatography is a predominantly nonlinear mode of chromatography, which has certain advantages over the elution mode for preparative bioseparations. Whereas continuous production (and separation) processes have their theoretical benefits in this context, protein displacement chromatography has up to now only been performed in the batch mode. In this contribution, we demonstrate that the principle of continuous annular chromatography can be adapted to displacement chromatography. Separations of up to three standard proteins (two whey proteins, soybean trypsin inhibitor) were developed and optimized using a small (4 x 250 mm) batch column. These separations were subsequently transferred directly to the continuous system (500-mL column). Separations of similar quality in terms of final product purity and recovery yield were obtained using the continuous system.