Characterization of the co-elution of host cell proteins with monoclonal antibodies during protein A purification.

Protein A chromatography is commonly used as the initial step for purifying monoclonal antibody biotherapeutics expressed in mammalian tissue culture cells. The purpose of this step, as well as later chromatography steps, is, in part, to remove host cell proteins (HCPs) and other related impurities. Understanding the retention mechanism for the subset of HCPs retained during this step is of great interest to monoclonal antibody (mAb) process developers because it allows formation of a guided HCP clearance strategy. However, only limited information is available about the specific HCPs that co-purify with mAbs at this step. In this study, a comprehensive comparison of HCP subpopulations that associated with 15 different mAbs during protein A chromatography was conducted by a 2D-LC-HDMS(E) approach. We found that a majority of CHO HCPs binding to and eluting with the mAbs were common among the mAbs studied, with only a small percentage (∼10% on average) of a mAb's total HCP content in the protein A (PrA) eluate specific for a particular antibody. The abundance of these HCPs in cell culture fluids and their ability to interact with mAbs were the two main factors determining their prevalence in protein A eluates. Potential binding segments for HCPs to associate with mAbs were also studied through their co-purification with individual Fc and (Fab')2 antibody fragments. © 2016 American Institute of Chemical Engineers Biotechnol. Prog., 32:708-717, 2016.

Comprehensive tracking of host cell proteins during monoclonal antibody purifications using mass spectrometry.

An advanced two-dimensional liquid chromatography/mass spectrometry platform was used to quantify individual host cell proteins (HCPs) present at various purification steps for several therapeutic monoclonal antibodies (mAbs) produced in Chinese hamster ovary cells. The methodology produced reproducible identifications and quantifications among replicate analyses consistent with a previously documented individual limit of quantification of ~13 ppm. We were able to track individual HCPs from cell culture fluid to protein A eluate pool to subsequent viral inactivation pool and, in some cases, further downstream. Approximately 500 HCPs were confidently identified in cell culture fluid and this number declined progressively through the purification scheme until no HCPs could be confidently identified in polishing step cation-exchange eluate pools. The protein A eluate pool of nine different mAbs contained widely differing numbers, and total levels, of HCPs, yet the bulk of the total HCP content in each case consisted of a small subset of normally intracellular HCPs highly abundant in cell culture fluid. These observations hint that minimizing cell lysis during cell culture/harvest may be useful in minimizing downstream HCP content. Clusterin and actin are abundant in the protein A eluate pools of most mAbs studied. HCP profiling by this methodology can provide useful information to process developers and lead to the refinement of existing purification platforms.

Multipronged approach to managing beta-glucan contaminants in the downstream process: control of raw materials and filtration with charge-modified nylon 6,6 membrane filters.

(1→3)-ß-D-Glucans (beta-glucans) have been found in raw materials used in the manufacture of recombinant therapeutics. Because of their biological activity, beta-glucans are considered process contaminants and consequently their level in the product needs to be controlled. Although beta-glucans introduced into the cell culture process can readily be removed by bind-and-elute chromatography process steps, beta-glucans can also be introduced into the purification process through raw materials containing beta-glucans as well as leachables from filters made from cellulose. This article reports a multipronged approach to managing the beta-glucan contamination in the downstream process. Raw material screening and selection can be used to effectively limit the level of beta-glucan introduced into the downstream process. Placement of a cellulosic filter upstream of the last bind-and-elute column step or effective preuse flushing can also limit the level of contaminant introduced. More importantly, this article reports the active removal of beta-glucan from the downstream process when necessary. It was discovered that the Posidyne(®) filter, a charge-modified nylon 6,6 membrane filter, was able to effectively remove beta-glucans from buffers at relatively low pH and salt concentrations. An approach of using low beta-glucan buffer components combined with filtration of the buffer with a Posidyne membrane has been successfully demonstrated at preparative scale. Additionally, the feasibility of active removal of beta-glucan from in-process product pools by Posidyne membrane filtration has also been demonstrated. Based on the data presented, a mechanism for binding is proposed, as well as a systematic approach for sizing of the Posidyne filter.

Characterization of 64Cu-DOTA-conatumumab: a PET tracer for in vivo imaging of death receptor 5.

UNLABELLED: Conatumumab is a fully human monoclonal antibody that binds to and activates human death receptor 5 (DR5; also known as TRAIL receptor 2). The purpose of this study was to characterize (64)Cu-labeled conatumumab as a PET tracer for imaging DR5 in tumors. METHODS: DOTA-conatumumab was synthesized by incubating conatumumab with 2,2',2″-(10-(2-(2,5-dioxopyrrolidin-1-yloxy)-2-oxoethyl)-1,4,7,10-tetraazacyclododecane-1,4,7-triyl)triacetic acid (DOTA-NHS). The absolute numbers of DOTA molecules per conatumumab molecules were determined by matrix-assisted laser desorption ionization mass spectrometry and electrospray ionization quadrupole time-of-flight mass spectrometry. (64)Cu-DOTA-conatumumab was prepared by incubating (64)CuCl(2) (33-222 MBq) with DOTA-conatumumab at 37°C for 1 h. Binding of conatumumab and DOTA-conatumumab to Fc-coupled human DR5 (huTR2-Fc) was tested in a kinetic analysis assay, and the biologic activity of copper-DOTA-conatumumab was measured using a caspase-3/7 luminescent assay. In vivo evaluation of DOTA-conatumumab and copper-DOTA-conatumumab was done in severe combined immunodeficiency mice bearing Colo205 xenografts: tissue uptake was determined with biodistribution studies, and small-animal PET and autoradiography were used to determine the uptake of (64)Cu-DOTA conatumumab into tumors and other tissues. RESULTS: DOTA-conatumumab was prepared with an average of 5 DOTA molecules per conatumumab molecule. The in vitro median effective concentration required to induce a 50% effect of DOTA-conatumumab and conatumumab from the assay were 389 and 320 pM, respectively. The median effective dose (±SD) of DOTA-conatumumab and conatumumab via the caspase assay was 135 ± 31 and 128 ± 30 pM, respectively. In female CB17 severe combined immunodeficiency mice bearing Colo205 xenografts, DOTA-conatumumab and conatumumab inhibited tumor growth to the same extent. Small-animal PET studies showed tumor uptake at 24 h after injection of the tracer, with a mean standardized uptake value of 3.16 (n = 2). Tumor uptake was decreased by the coadministration of 400 µg of unlabeled conatumumab (mean standardized uptake value, 1.55; n = 2), suggesting saturable uptake. Tissue uptake determined by biodistribution studies was in agreement with the small-animal PET findings. CONCLUSION: These results suggest that (64)Cu-DOTA-conatumumab is a potential PET tracer for imaging DR5 in tumors and may be useful for measuring on-target occupancy by conatumumab.