Biopharmaceutical Processing 2018
DOI: 10.1016/b978-0-08-100623-8.00024-4
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Upstream Processing Equipment

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Cited by 14 publications
(15 citation statements)
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“…They are usually placed in a heated environment on a rack that slowly revolves (ranging between 5 and 240 revolutions/hour). They are inexpensive and are a common method used for the initial scale-up of adherent cells ( 42 ). The cells attach and cover the inner surface of the bottle; hence the cells are cyclically bathing in culture medium and exposed to gases.…”
Section: Small Scale Technologies–or Compact Technologiesmentioning
confidence: 99%
See 1 more Smart Citation
“…They are usually placed in a heated environment on a rack that slowly revolves (ranging between 5 and 240 revolutions/hour). They are inexpensive and are a common method used for the initial scale-up of adherent cells ( 42 ). The cells attach and cover the inner surface of the bottle; hence the cells are cyclically bathing in culture medium and exposed to gases.…”
Section: Small Scale Technologies–or Compact Technologiesmentioning
confidence: 99%
“…Like static flasks, rotating flasks are also labor intensive. For high cell numbers, a further constraint of a roller bottle process through scaling-out is the limitation in the control of O 2 and CO 2 in both the gas and the liquid phase of culture ( 39 , 42 ).…”
Section: Small Scale Technologies–or Compact Technologiesmentioning
confidence: 99%
“…While in the chemical industry, for example, a ratio of 1:1 is typical, a ratio of 2:1 is preferred for cell culture bioreactors at laboratory and pilot scales. For microbial systems, values of 3:1 dominate since this leads to longer residence times for supplied gases, such as air or oxygen, and better temperature control due to the larger surface to volume ratio (Menkel 1992;Jossen et al 2017;Clapp et al 2018). Nevertheless, as bioreactor size increases, H/D ratios of 5:1 (Chisti 2006) and up to 6:1 (Najafpour 2015) can also be…”
Section: Main Components Of Stirred Bioreactorsmentioning
confidence: 99%
“…However, in contrast to topdriven systems, the sealing elements are exposed to chemical, biological, and abrasive loads (Menkel 1992;Jagani et al 2010), which result in increased periodic maintenance and shorter replacement intervals (EKATO Holding GmbH 2012). Agitators are mostly arranged centrically in both topand bottom-driven systems (Jagani et al 2010;Clapp et al 2018). It should be noted that in order to avoid vortex formation and to ensure proper mixing, drives can also be installed eccentrically or mounted at an angle so that baffles can be avoided (Penicot et al 1998;Assirelli et al 2008;Jagani et al 2010;Clapp et al 2018).…”
Section: Drive Systems and Seals Commonly Used In Biotechnological Prmentioning
confidence: 99%
“…Many well-known manufacturers offer standard stainless steel systems with volumes from 2 to 1000 L, whereby larger systems with several cubic meters are also available according to customer specifications. The smaller scale glass bioreactors are used in research and process development [8]. The single-use systems, depending on their size, are either available as flexible bags or rigid vessels.…”
Section: Introductionmentioning
confidence: 99%