Chinese hamster ovary (CHO-K1) cells expressed native insulin-like growth factor-1 (IGF-1) gene towards efficient mammalian cell culture host system

2011 ◽  
Vol 10 (81) ◽  
Author(s):  
Vasila Packeer Mohamed
2001 ◽  
Vol 171 (1) ◽  
pp. 153-162 ◽  
Author(s):  
M Amoui ◽  
BP Craddock ◽  
WT Miller

Insulin receptor (IR) and insulin-like growth factor I receptor (IGF-IR) are closely related receptor tyrosine kinases. Despite their high degree of homology, recent evidence suggests that the two receptors have distinct biological roles. In several recent studies, the cytoplasmic tyrosine kinase domains of the two receptors have been shown to possess different signalling specificities. In this study, we examine the hypothesis that differential phosphorylation of insulin receptor substrate 1 (IRS-1) may contribute to these differences in signalling between the two receptors. Using Chinese hamster ovary (CHO) cells stably expressing human IR or IGF-IR and activated by their respective ligands, we show that there are differences between the two receptors with regard to the complement of SH2-containing proteins recruited to IRS-1. In particular, IGF-IR appears to couple IRS-1 preferentially to Grb2 whereas, in contrast, IR appears to couple IRS-1 preferentially to the p85 subunit of phosphatidyl inositol 3-kinase (PI3-kinase) and to Nck. The two receptors couple IRS-1 equally to the tyrosine phosphatase SHP2. We have also generated phosphospecific antibodies to three important tyrosine phosphorylation sites on IRS-1 (pY608, pY895 and pY1172). We used these antibodies to probe the phosphorylation status of these sites in intact CHO/IR and CHO/IGF-IR cells. In the case of pY608, these results also show evidence for differential phosphorylation of IRS-1 by the two receptors. Taken together, the results presented here support the notion that the cytoplasmic domains of IR and IGF-IR have differences in their intrinsic signalling potentials.


1994 ◽  
Vol 36 (1) ◽  
pp. 75-83
Author(s):  
Hicham Bekkari ◽  
Driss Sekkat ◽  
Jean Straczek ◽  
Ketsia Hess ◽  
Francine Belleville-Nabet ◽  
...  

Processes ◽  
2021 ◽  
Vol 9 (11) ◽  
pp. 2073
Author(s):  
Tobias Wallocha ◽  
Oliver Popp

In mammalian cell culture, especially in pharmaceutical manufacturing and research, biomass and metabolic monitoring are mandatory for various cell culture process steps to develop and, finally, control bioprocesses. As a common measure for biomass, the viable cell density (VCD) or the viable cell volume (VCV) is widely used. This study highlights, for the first time, the advantages of using VCV instead of VCD as a biomass depiction in combination with an oxygen-uptake- rate (OUR)-based soft sensor for real-time biomass estimation and process control in single-use bioreactor (SUBs) continuous processes with Chinese hamster ovary (CHO) cell lines. We investigated a series of 14 technically similar continuous SUB processes, where the same process conditions but different expressing CHO cell lines were used, with respect to biomass growth and oxygen demand to calibrate our model. In addition, we analyzed the key metabolism of the CHO cells in SUB perfusion processes by exometabolomic approaches, highlighting the importance of cell-specific substrate and metabolite consumption and production rate qS analysis to identify distinct metabolic phases. Cell-specific rates for classical mammalian cell culture key substrates and metabolites in CHO perfusion processes showed a good correlation to qOUR, yet, unexpectedly, not for qGluc. Here, we present the soft-sensoring methodology we developed for qPyr to allow for the real-time approximation of cellular metabolism and usage for subsequent, in-depth process monitoring, characterization and optimization.


2000 ◽  
Vol 16 (5) ◽  
pp. 698-702 ◽  
Author(s):  
N.-A.S. Sunstrom ◽  
R.D. Gay ◽  
D.C. Wong ◽  
N.A. Kitchen ◽  
L. DeBoer ◽  
...  

1993 ◽  
Vol 156 (1) ◽  
pp. 145-152 ◽  
Author(s):  
Hisanori Kato ◽  
Teresa N. Faria ◽  
Bethel Stannard ◽  
Rachel Levy-Toledano ◽  
Simeon I. Taylor ◽  
...  

1986 ◽  
Vol 261 (30) ◽  
pp. 14076-14081
Author(s):  
J M Podskalny ◽  
D G Rouiller ◽  
G Grunberger ◽  
R C Baxter ◽  
A McElduff ◽  
...  

2012 ◽  
Vol 59 (1) ◽  
Author(s):  
Mohd Helmi Sani ◽  
Frank Baganz

At present, there are a number of commercial small scale shaken systems available on the market with instrumented controllable microbioreactors such as Micro–24 Microreactor System (Pall Corporation, Port Washington, NY) and M2P Biolector, (M2P Labs GmbH, Aachen, Germany). The Micro–24 system is basically an orbital shaken 24–well plate that operates at working volume 3 – 7 mL with 24 independent reactors (deep wells, shaken and sparged) running simultaneously. Each reactor is designed as single use reactor that has the ability to continuously monitor and control the pH, DO and temperature. The reactor aeration is supplied by sparging air from gas feeds that can be controlled individually. Furthermore, pH can be controlled by gas sparging using either dilute ammonia or carbon dioxide directly into the culture medium through a membrane at the bottom of each reactor. Chen et al., (2009) evaluated the Micro–24 system for the mammalian cell culture process development and found the Micro–24 system is suitable as scaledown tool for cell culture application. The result showed that intra-well reproducibility, cell growth, metabolites profiles and protein titres were scalable with 2 L bioreactors.


1995 ◽  
Vol 13 (4) ◽  
pp. 389-392 ◽  
Author(s):  
Michael Zang ◽  
Helmut Trautmann ◽  
Christine Gandor ◽  
Ferruccio Messi ◽  
Fred Asselbergs ◽  
...  

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