2014
DOI: 10.1186/1475-2859-13-32
|View full text |Cite
|
Sign up to set email alerts
|

Exometabolome analysis reveals hypoxia at the up-scaling of a Saccharomyces cerevisiae high-cell density fed-batch biopharmaceutical process

Abstract: BackgroundScale-up to industrial production level of a fermentation process occurs after optimization at small scale, a critical transition for successful technology transfer and commercialization of a product of interest. At the large scale a number of important bioprocess engineering problems arise that should be taken into account to match the values obtained at the small scale and achieve the highest productivity and quality possible. However, the changes of the host strain’s physiological and metabolic be… Show more

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
1
1
1
1

Citation Types

3
48
0

Year Published

2014
2014
2023
2023

Publication Types

Select...
5
1
1

Relationship

1
6

Authors

Journals

citations
Cited by 39 publications
(51 citation statements)
references
References 35 publications
3
48
0
Order By: Relevance
“…Taking into account that in large scale processes energy dissipation rates (ε T ) for high cell density fermentations are normally applied only up to 5 W/kg because of power restrictions (Nienow, ) and ε T correlates with k L a (Van't Riet, ) we already operated at the upper limit of the OTR (Fuchs and Ryu, ). Higher k L a values are only feasible when additional gassing with cost‐intensive pure oxygen is applied (Fu et al, ). Hence, yields should be assessed taking the process conditions into account.…”
Section: Resultsmentioning
confidence: 99%
“…Taking into account that in large scale processes energy dissipation rates (ε T ) for high cell density fermentations are normally applied only up to 5 W/kg because of power restrictions (Nienow, ) and ε T correlates with k L a (Van't Riet, ) we already operated at the upper limit of the OTR (Fuchs and Ryu, ). Higher k L a values are only feasible when additional gassing with cost‐intensive pure oxygen is applied (Fu et al, ). Hence, yields should be assessed taking the process conditions into account.…”
Section: Resultsmentioning
confidence: 99%
“…The S. cerevisiae strain was originally developed from the parental S. cerevisiae strain AH22 (ATCC 38626) and the gene encoding for the product is in a high‐copy number plasmid. The fermentation process to produce a therapeutic recombinant protein, Pr‐1, at the small scale (10 L) was described previously . Briefly, Pr‐1 production is conditionally induced in the host strain by glucose limitation that elicits product secretion into the medium.…”
Section: Methodsmentioning
confidence: 99%
“…Previously, we presented a stepwise approach to optimize a S. cerevisiae fermentation process and quantifying the reliable operating region of the process using the multivariate Bayesian posterior predictive approach . The optimized fermentation process was further successfully scaled‐up to a 10,000 L scale . This optimization and scale‐up program significantly contributed to process and product knowledge understanding.…”
Section: Introductionmentioning
confidence: 99%
“…Following another 48 hours, 40 µL of this first seed-train culture was transferred to a 4-mL shake flask culture, and after another 48 hours this culture was used to inoculate a 400-mL bioreactor. This seed train from 40 µL to 400 mL represents the same number of generations encountered in industrial seed trains starting from 1L and ending at 10,000 L (Fu et al, 2014).…”
Section: Industrial Scale-up Mimicmentioning
confidence: 99%