scholarly journals A Modified EPA Method 1623 that Uses Tangential Flow Hollow-fiber Ultrafiltration and Heat Dissociation Steps to Detect Waterborne Cryptosporidium and Giardia spp.

Author(s):  
Eric R. Rhodes ◽  
Leah Fohl Villegas ◽  
Nancy J. Shaw ◽  
Carrie Miller ◽  
Eric N. Villegas
Author(s):  
Marc D. Hein ◽  
Anshika Chawla ◽  
Maurizio Cattaneo ◽  
Sascha Y. Kupke ◽  
Yvonne Genzel ◽  
...  

AbstractRespiratory diseases including influenza A virus (IAV) infections represent a major threat to human health. While the development of a vaccine requires a lot of time, a fast countermeasure could be the use of defective interfering particles (DIPs) for antiviral therapy. IAV DIPs are usually characterized by a large internal deletion in one viral RNA segment. Consequentially, DIPs can only propagate in presence of infectious standard viruses (STVs), compensating the missing gene function. Here, they interfere with and suppress the STV replication and might act “universally” against many IAV subtypes. We recently reported a production system for purely clonal DIPs utilizing genetically modified cells. In the present study, we established an automated perfusion process for production of a DIP, called DI244, using an alternating tangential flow filtration (ATF) system for cell retention. Viable cell concentrations and DIP titers more than 10 times higher than for a previously reported batch cultivation were observed. Furthermore, we investigated a novel tubular cell retention device for its potential for continuous virus harvesting into the permeate. Very comparable performances to typically used hollow fiber membranes were found during the cell growth phase. During the virus replication phase, the tubular membrane, in contrast to the hollow fiber membrane, allowed 100% of the produced virus particles to pass through. To our knowledge, this is the first time a continuous virus harvest was shown for a membrane-based perfusion process. Overall, the process established offers interesting possibilities for advanced process integration strategies for next-generation virus particle and virus vector manufacturing.Key points• An automated perfusion process for production of IAV DIPs was established.• DIP titers of 7.40E + 9 plaque forming units per mL were reached.• A novel tubular cell retention device enabled continuous virus harvesting.


Vaccine ◽  
2015 ◽  
Vol 33 (35) ◽  
pp. 4255-4260 ◽  
Author(s):  
Sophia T. Mundle ◽  
Maryann Giel-Moloney ◽  
Harry Kleanthous ◽  
Konstantin V. Pugachev ◽  
Stephen F. Anderson

1983 ◽  
Vol 15 (5) ◽  
pp. 75-89 ◽  
Author(s):  
David M Dziewulski ◽  
Georges Belfort

The efficacy of tangential flow hollow fiber Ultrafiltration (TFHFU) as a means of concentrating poliovirus 2 (Sabin) from large volumes of tap water was studied. Initially, hydrodynamic studies using 50-1 tap water feed solutions were conducted to evaluate transmembrane flux as a function of axial flow rates (or Reynold's numbers, Re). With increasing Reynold's number, flux-decline rates were reduced. As a result, experimental duration was shortened from 110 min at Re=300 to 30 min at Re=1728. In all cases, radial flow was assisted by a vacuum force applied to the outside of the hollow fibers. Virus recovery capability was evaluated using 20-, 50-, and 100-1 feed samples seeded with poliovirus 2 from 604 to 0.5 pfu/ml. All virus experiments were conducted at Re=1728 and a vacuum force of 3.27 × 104 Pa. The mean duration of the 20-, 50-, and 100-1 experiments was 13, 42, and 79 minutes, respectively. The overall average virus recovery from all experiments was 69.1 ± 24.6%. In operating the tangential-flow hollow fiber ultrafiltration module in its normal recycle-mode with low turbidity waters (<10 NTU), the expected steady flux-decline resulting from membrane fouling was not observed. Instead, the transmembrane permeation flux was maintained at a relatively constant value especially near the end of the experiments when the solute concentration in the feed increased the fastest. Increased feed water temperature resulting from the addition of pumping energy during recycle is responsible for this unexpected advantage. Final temperatures never exceeded a point at which virus inactivation would occur. For high turbidity feed waters (75 to 85 NTU), obtained by the addition of kaolin clay, virus recoveries varied from 30 to 49%, Final turbidities at the termination of a 50-1 run were from 950 to >1000 NTU. In spite of the high turbidity, the mean experiment duration for dehydrating 50 liters of turbid feed water was 39 minutes; approximately the same as for the low-turbidity tap water runs.


2009 ◽  
Vol 38 (2) ◽  
pp. 822-825 ◽  
Author(s):  
Vincent R. Hill ◽  
Amy L. Polaczyk ◽  
Amy M. Kahler ◽  
Theresa L. Cromeans ◽  
Donghyun Hahn ◽  
...  
Keyword(s):  

2021 ◽  
Author(s):  
Marc Dominique Hein ◽  
Anshika Chawla ◽  
Maurizio Cattaneo ◽  
Sascha Young Kupke ◽  
Yvonne Genzel ◽  
...  

Respiratory diseases including influenza A virus (IAV) infections represent a major threat to human health. While the development of a vaccine requires a lot of time, a fast countermeasure could be the use of defective interfering particles (DIPs) for antiviral therapy. IAV DIPs are usually characterized by a large internal deletion in one viral RNA segment. Consequentially, DIPs can only propagate in presence of infectious standard viruses (STVs), compensating the missing gene function. Here, they interfere with and suppress the STV replication and might act "universally" against many IAV subtypes. We recently reported a production system for purely clonal DIPs utilizing genetically modified cells. In the present study, we established an automated perfusion process for production of a DIP, called DI244, using an alternating tangential flow filtration (ATF) system for cell retention. Viable cell concentrations and DIP titers more than 10-times higher than for a previously reported batch cultivation were observed. Further, we investigated a novel tubular cell retention device for its potential for continuous virus harvesting into the permeate. Very comparable performances to typically used hollow fiber membranes were found during the cell growth phase. During the virus replication phase the tubular membrane, in contrast to the hollow fiber membrane, allowed 100% of the produced virus particles to pass through. To our knowledge, this is the first time a continuous virus harvest was shown for a membrane-based perfusion process. Overall, the process established offers interesting possibilities for advanced process integration strategies for next-generation virus particle and virus vector manufacturing.


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