2012
DOI: 10.1016/j.jbiotec.2011.11.007
|View full text |Cite
|
Sign up to set email alerts
|

Optimization of HEK-293S cell cultures for the production of adenoviral vectors in bioreactors using on-line OUR measurements

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
1
1
1
1

Citation Types

2
23
0

Year Published

2013
2013
2024
2024

Publication Types

Select...
6
2
1

Relationship

0
9

Authors

Journals

citations
Cited by 36 publications
(25 citation statements)
references
References 26 publications
2
23
0
Order By: Relevance
“…As indicated in Table 2, CDE is generally observed for HEK293 cells between 1 and 2 × 10 6 cells/ml [1,61,70], whereas cell densities of 8-10 × 10 6 cells/ml can be achieved in batch cultures [64]. CDE is virus dependent with specific adenovirus production decreasing at densities higher than 2 × 10 6 cell/ml [1,70,71], while for influenza virus, high productivity is maintained up to 4 × 10 6 cells/ml in batch cultures [58,64]. Consequently, most of the transfection/infection steps are operated at cell concentrations below 4 × 10 6 cell/ml.…”
Section: Feeding Strategies and Medium Modification For Viral Productmentioning
confidence: 94%
“…As indicated in Table 2, CDE is generally observed for HEK293 cells between 1 and 2 × 10 6 cells/ml [1,61,70], whereas cell densities of 8-10 × 10 6 cells/ml can be achieved in batch cultures [64]. CDE is virus dependent with specific adenovirus production decreasing at densities higher than 2 × 10 6 cell/ml [1,70,71], while for influenza virus, high productivity is maintained up to 4 × 10 6 cells/ml in batch cultures [58,64]. Consequently, most of the transfection/infection steps are operated at cell concentrations below 4 × 10 6 cell/ml.…”
Section: Feeding Strategies and Medium Modification For Viral Productmentioning
confidence: 94%
“…The medium is removed through the OT, leaving the cell spheroids in culture, until the medium level falls below the bottom of the OT. This method of volume control with continuous feeding is used in many large-scale culture applications used to generate cell products [34], [35]. The system is designed to be simple without the need for specialized sensors and automation systems to control pump speeds.…”
Section: Methodsmentioning
confidence: 99%
“…Several studies (Smith et al 1991;Hiller et al 1993;Zhang et al 1993;Kyung et al 1994) were published in the early 1990s using cellulose ester HF achieving varying densities of hybridoma or HEK293 cells from a few millions cells/mL to a maximum of 10 8 cells/mL by Kyung. Several years later, Cortin et al (2004) and Galvez et al (2012) successfully produced adenovirus in HEK 293 cell system. In 2011, Clincke et al published a comparative study of perfusion in wave bioreactor Fig.…”
Section: Tffmentioning
confidence: 99%
“…This approach requires that the cell specific glucose consumption rate is constant so it should be applied when steady-state culture is established. The oxygen uptake rate (OUR) has also been used to control the perfusion rate, given that the OUR is a good indicator of the physiological state of the cells (Kyung et al 1994;Galvez et al 2012). …”
Section: Perfusion Rate Strategy Based On Main Substrate Measurementmentioning
confidence: 99%