2010
DOI: 10.1002/btpr.494
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Achieving high mass‐throughput of therapeutic proteins through parvovirus retentive filters

Abstract: Parvovirus retentive filters that assure removal of viruses and virus-like particles during the production of therapeutic proteins significantly contribute to total manufacturing costs. Operational approaches that can increase throughput and reduce filtration area would result in a significant cost savings. A combination of methods was used to achieve high throughputs of an antibody or therapeutic protein solution through three parvovirus retentive filters. These methods included evaluation of diatomaceous ear… Show more

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Cited by 26 publications
(26 citation statements)
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“…Viral filtration is one of the most expensive steps during the downstream processing of therapeutic proteins (G. R. Bolton, Basha, & LaCasse, 2010). Viral filtration is one of the most expensive steps during the downstream processing of therapeutic proteins (G. R. Bolton, Basha, & LaCasse, 2010).…”
Section: Introductionmentioning
confidence: 99%
“…Viral filtration is one of the most expensive steps during the downstream processing of therapeutic proteins (G. R. Bolton, Basha, & LaCasse, 2010). Viral filtration is one of the most expensive steps during the downstream processing of therapeutic proteins (G. R. Bolton, Basha, & LaCasse, 2010).…”
Section: Introductionmentioning
confidence: 99%
“…Decreased throughput due to membrane fouling during the production processes is another critical issue in virus filtration . Membrane fouling is commonly observed regardless of filter type and two main causes for the related decline in filter performance have been proposed . First, the adsorption of proteins onto a wide variety of membrane surfaces (caused by protein‐surface interaction) reduces the effective size of the membrane pores and causes caking on the membrane surface.…”
Section: Introductionmentioning
confidence: 99%
“…Therefore, when designing any viral filtration into a continuous flow‐through process, product specific factors, such as buffer pH, conductivity, pressure, or flow rates and their effect on viral filter retention must be considered. Potential frameworks for these considerations exist for batch processing (Bolton et al, ; Dishari et al, ; Hongo‐Hirasaki et al, ) that may be utilized in designing continuous viral filtration methods or when performing validation studies. As with batch processing methods, integrating any novel or adapted viral filtration into a continuous flow‐through polishing process will require validation of clearance, but often this can be performed as an isolated unit in batch mode.…”
Section: Viral Filtrationmentioning
confidence: 99%
“…The utilization of novel polishing processes, such as the charcoal based process seen in a case study by Gillespie et al () may increase the pressure and load limitations of viral filters in a CP. Another step utilized in batch processes to mitigate filter fouling and extend their lifetimes, is the use of pre‐filtration devices prior to utilizing viral filters in the purification process (Bolton et al, , ; Brown et al, ; Challener, ) which can be utilized based on evaluated bioburden limits of the filters chosen (Yang et al, ). The potential for these technologies is discussed elsewhere in this review, but these would also require periodic switch out as well.…”
Section: Viral Filtrationmentioning
confidence: 99%