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1.
Biotechnol Bioeng ; 120(10): 2977-2988, 2023 10.
Artigo em Inglês | MEDLINE | ID: mdl-37288613

RESUMO

There are few reports of the adoption of continuous processes in bioproduction, particularly the implementation of end-to-end continuous or integrated processes, due to difficulties such as feed adjustment and incorporating virus filtration. Here, we propose an end-to-end integrated continuous process for a monoclonal antibody (mAb) with three integrated process segments: upstream production processes with pool-less direct connection, pooled low pH virus inactivation with pH control and a total flow-through integrated polishing process in which two columns were directly connected with a virus filter. The pooled virus inactivation step defines the batch, and high impurities reduction and mAb recovery were achieved for batches conducted in succession. Viral clearance tests also confirmed robust virus reduction for the flow-through two-column chromatography and the virus filtration steps. Additionally, viral clearance tests with two different hollow fiber virus filters operated at flux ranging from 1.5 to 40 LMH (liters per effective surface area of filter in square meters per hour) confirmed robust virus reduction over these ranges. Complete clearance with virus logarithmic reduction value ≥4 was achieved even with a process pause at the lowest flux. The end-to-end integrated continuous process proposed in this study is amenable to production processes, and the investigated virus filters have excellent applicability to continuous processes conducted at constant flux.


Assuntos
Anticorpos Monoclonais , Vírus , Anticorpos Monoclonais/química , Filtração/métodos , Cromatografia , Inativação de Vírus
2.
Biotechnol Bioeng ; 118(9): 3569-3580, 2021 09.
Artigo em Inglês | MEDLINE | ID: mdl-34032276

RESUMO

We evaluated filtration behavior and virus removal capability for a monoclonal antibodies (mAb) and plasma IgG under constant flow rate directly following flow-through column chromatography in an integrated process. mAb solution with quantified host cell protein (HCP) content processed in flow-through mode on in-series mixed-mode AEX and modified CEX columns connected to the Planova BioEX filter (pool-less) achieved HCP logarithmic reduction value (LRV) of 2.3 and 93.9% protein recovery, demonstrating comparable or higher HCP LRV with high protein recovery compared to previous reports. For 5-15 mg/ml plasma IgG run to 100 L/m2 , similar filtration behavior was achieved for flux of 10-100 LMH, and lower flux runs remained well below the maximum operating pressure, suggesting that higher throughput in continuous processing is achievable. Comparison of fit of plasma IgG and mAb filtration behavior to four blocking models showed little differences but slightly better fit to the cake filtration model. Viral clearance of the filtration step tested by in-line spiking X-MuLV or MVM into purified plasma IgG following the chromatography step showed robust removal at low flux. Integrating the Planova BioEX filter into continuous processes with column chromatography can achieve efficient downstream processing with reduced footprint and process time.


Assuntos
Anticorpos Monoclonais/química , Imunoglobulinas Intravenosas/química , Vírus da Leucemia Murina/química , Cromatografia , Filtração
3.
J Chromatogr A ; 1218(17): 2381-8, 2011 Apr 29.
Artigo em Inglês | MEDLINE | ID: mdl-21051042

RESUMO

It is widely recognized that membrane adsorbers are powerful tools for the purification of biopharmaceutical protein products and for this reason a novel hollow-fiber AEX type membrane adsorber has been developed. The membrane is characterized by grafted chains including DEA ligands affixed to the pore surfaces of the membrane. In order to estimate the membrane performance, (1) dynamic binding capacities for pure BSA and DNA over a range of solution conductivity and pH, (2) virus reduction by flow-through process, and (3) HCP and DNA removal from cell culture, are evaluated and compared with several other anion-exchange membranes. The novel hollow-fiber membrane is tolerant of high salt concentration when adsorbing BSA and DNA. When challenged with a solution containing IgG the membrane has high impurity removal further indicating this hollow-fiber based membrane adsorber is an effective tool for purification of biopharmaceutical protein products including IgG.


Assuntos
Cromatografia por Troca Iônica/instrumentação , Cromatografia por Troca Iônica/métodos , Compostos de Epóxi/química , Metacrilatos/química , Adsorção , Animais , Ânions/química , Ânions/metabolismo , Células CHO , Bovinos , Cricetinae , Cricetulus , DNA/isolamento & purificação , Contaminação de Medicamentos , Eletroforese em Gel de Poliacrilamida , Compostos de Epóxi/metabolismo , Humanos , Concentração de Íons de Hidrogênio , Imunoglobulina G/isolamento & purificação , Metacrilatos/metabolismo , Microscopia Eletrônica de Varredura , Porosidade , Ligação Proteica , Soroalbumina Bovina/isolamento & purificação , Cloreto de Sódio/química , Vírus/isolamento & purificação
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