𝔖 Bobbio Scriptorium
✦   LIBER   ✦

Batch centrifuge scale-up for virus processing

✍ Scribed by Patrick, William C. ;Freeman, Robert R.


Publisher
Wiley (John Wiley & Sons)
Year
1959
Weight
349 KB
Volume
1
Category
Article
ISSN
0368-1467

No coin nor oath required. For personal study only.

✦ Synopsis


Abstract

The mathematical relationship between the throughput of a batch centrifuge and its mechanical characteristics has been applied to the scale‐up of one of the steps in virus processing for possible application to the production of vaccines and similar antigens. Slurries that contained a test virus were purified in a laboratory centrifuge. The Q/Ξ£ relationship, developed by Ambler, was used to predict the operating conditions of a larger centrifuge in order to achieve the same clarification of slurry as that produced in the laboratory centrifuge. A correlation between conditions of centrifugation and amount of virus removed from the feed to the centrifuge shows that there is a well‐defined Q/Ξ£ value at which significant concentrations of the test virus are sedimented.


πŸ“œ SIMILAR VOLUMES


A computer system for process scale-up
✍ E. StΓ€heli; C. Fischer πŸ“‚ Article πŸ“… 1979 πŸ› Elsevier Science 🌐 English βš– 340 KB
The theory of scaling up laboratory data
✍ Ambler, Charles M. πŸ“‚ Article πŸ“… 1959 πŸ› Wiley (John Wiley & Sons) βš– 805 KB

## Abstract The mathematical theory of the sedimentation type of centrifuge is developed in terms of unhindered settling of a single particle that has reached equilibrium velocity. From this is derived the sigma value for several of the different forms of sedimentation type centrifuge which is the

Fed-batch bioreactor process scale-up fr
✍ Jeng-Dar Yang; Canghai Lu; Brad Stasny; Joseph Henley; Woodrow Guinto; Carlos Go πŸ“‚ Article πŸ“… 2007 πŸ› John Wiley and Sons 🌐 English βš– 381 KB πŸ‘ 2 views

## Abstract This case study focuses on the scale‐up of a Sp2/0 mouse myeloma cell line based fed‐batch bioreactor process, from the initial 3‐L bench scale to the 2,500‐L scale. A stepwise scale‐up strategy that involved several intermediate steps in increasing the bioreactor volume was adopted to