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1.
J Pharm Sci ; 110(12): 3811-3818, 2021 12.
Article in English | MEDLINE | ID: mdl-34461112

ABSTRACT

Identification and accurate quantitation of host cell proteins (HCPs) in biotherapeutic drugs has become increasingly important due to the negative impact of certain HCPs on the safety, stability, and other product quality of biotherapeutics. Recently, several lipase HCPs have been identified to potentially cause the enzymatic degradation of polysorbate, a widely used excipient in the formulation of biotherapeutics, which can severely impact the stability and product quality of drug products. In this study, we identified three lipase HCPs that were frequently detected in Chinese hamster ovary (CHO) cell cultures using shotgun proteomics, including phospholipase B-like 2 (PLBL2), lipoprotein lipase (LPL), and lysosomal acid lipase (LIPA). A targeted quantitation method for these three lipase HCPs was developed utilizing liquid chromatography coupled with tandem mass spectrometry (LC-MS/MS) with high-resolution multiple-reaction-monitoring (MRMhr) quantitation. The method demonstrated good sensitivity with low limit of quantitation (LLOQ) around 1 ng/mL, and linear dynamic range of three orders of magnitude for the three lipase HCPs. It has been applied for the characterization of process intermediates from various in-house monoclonal antibody (mAb) production. In addition, the method has also been used to evaluate the robustness of clearance for one of the lipase HCPs, PLBL2, under different column purification process conditions.


Subject(s)
Lipase , Tandem Mass Spectrometry , Animals , Antibodies, Monoclonal/metabolism , CHO Cells , Chromatography, Liquid/methods , Cricetinae , Cricetulus , Tandem Mass Spectrometry/methods
2.
Biotechnol Bioeng ; 118(9): 3359-3366, 2021 09.
Article in English | MEDLINE | ID: mdl-33638385

ABSTRACT

Recent interest in continuous manufacturing of biologics has driven the development and evaluation of multicolumn chromatography systems to drive down resin costs by increasing productivity and maximizing resin utilization, especially for the expensive protein A capture step. Single-pass tangential flow filtration can be used to reduce the volume of perfusion harvest, enabling a further increase in the productivity of the capture step by up to fivefold. However, there are expected to be practical limits for the productivity of the capture step, which must be determined based on the manufacturing batch size, duration, and frequency, especially as it relates to efficient utilization of the column lifetime. For short fed-batch manufacturing campaigns, intensified capture processes may result in up to 82% lower resin consumption, while avoiding the long-term storage of used resin. For perfusion processes and longer fed-batch campaigns, it may be more efficient to operate at a lower productivity that enables the column lifetime to be routinely achieved and achieves the desired resin and buffer savings without introducing unnecessary process risk or complexity. An intensified batch capture process, "super-batch," will be compared as an alternative to multicolumn chromatography processes to achieve high productivity and resin utilization with a potentially simpler process.


Subject(s)
Antibodies, Monoclonal/isolation & purification , Bioreactors , Staphylococcal Protein A/chemistry , Animals , Antibodies, Monoclonal/biosynthesis , Antibodies, Monoclonal/chemistry , CHO Cells , Cricetulus , Efficiency
3.
Biotechnol Prog ; 34(2): 405-411, 2018 03.
Article in English | MEDLINE | ID: mdl-29314774

ABSTRACT

Decoupling upstream and downstream operations in biopharmaceutical production could enable more flexible manufacturing operations and could allow companies to leverage strategic or financial benefits that would be otherwise unattainable. A decoupling process was developed and scaled up utilizing single-pass tangential flow filtration for volume reduction, followed by bulk freezing in single-use bags prior to purification. Single-pass tangential flow filtration can be used to continuously concentrate harvested cell culture fluid, reducing the volume by 15-25× with a step yield of >96%. These concentration factors were reproduced with a second product, indicating that the process could be amenable to platform processes. Experimental data indicate that the product tested was stable for at least one year at -40 or -70°C. The concentration of the harvested cell culture fluid-either with or without a subsequent period of frozen storage-had no impact on the product quality attributes that were tested. © 2018 American Institute of Chemical Engineers Biotechnol. Prog., 34:405-411, 2018.


Subject(s)
Antibodies, Monoclonal/metabolism , Cell Culture Techniques/methods , Filtration/methods , Protein Engineering/methods , Animals , CHO Cells , Cricetulus , Hydrogen-Ion Concentration , Protein Engineering/instrumentation , Temperature
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