Multiphase Bioreactor Design
DOI: 10.4324/9780203303047_chapter_fourteen
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Bioreactor Design for Plant Cell Suspension Cultures

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Cited by 14 publications
(25 citation statements)
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“…Another point to consider is that under gassing conditions, the impeller power input is reduced, and hence the cumulative energy dissipation is expected to decrease according to equation (3). While shear damage resulting from the hydrodynamic forces associated with bubble rupture is believed to be insignificant in plant cell cultures [18,43], there is no evidence indicating shear damage is reduced with increasing bubble aeration rates at a fixed stirrer speed. The suitability of E c as a common basis to quantify the agitationbased shear forces under different bubble aeration rates apparently warrants further investigations.…”
Section: Shear Sensitivitymentioning
confidence: 91%
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“…Another point to consider is that under gassing conditions, the impeller power input is reduced, and hence the cumulative energy dissipation is expected to decrease according to equation (3). While shear damage resulting from the hydrodynamic forces associated with bubble rupture is believed to be insignificant in plant cell cultures [18,43], there is no evidence indicating shear damage is reduced with increasing bubble aeration rates at a fixed stirrer speed. The suitability of E c as a common basis to quantify the agitationbased shear forces under different bubble aeration rates apparently warrants further investigations.…”
Section: Shear Sensitivitymentioning
confidence: 91%
“…Separating and dispersing the cells from the aggregates by mechanical means in a bioreactor (e.g. by increasing bioreactor agitation) is usually not very effective and may lead to cell damage, or even larger aggregates [18]. Addition of pectinase and cellulase, higher cytokinin concentration, or lower calcium concentration in the media may help to reduce the aggregate size [28].…”
Section: Cell Morphology Degree Of Aggregation and Culture Rheologymentioning
confidence: 99%
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