| Autor: |
Schilling, Bernhard M., Goodrick, Jason C., Wan, Nick C. |
| Zdroj: |
Biotechnology Progress; 2001, Vol. 17 Issue: 4 p629-633, 5p |
| Abstrakt: |
The feasibility of large‐scale production of recombinant human chitinase using a constitutive Pichia pastorisexpression system was demonstrated in a 21‐L continuous stirred tank reactor. A steady‐state recombinant protein concentration of 250 mg/L in the supernatant was sustained for 1 month at a dilution rate of 0.042 h−1(equivalent to one volume exchange per day), enabling a volumetric productivity of 144 mg/L d (240 U/L d). The steady‐state dry cell weight concentration in this high cell density culture reached 110 g/L. Considering safety and economical aspects, all large‐scale cultivations were conducted without molecular oxygen supplementation. Conventional air sparging was used instead. The oxygen demand of the process was determined by off‐gas analysis (OUR = 4.8 g O2L−1h−1with kLa = 846 h−1) and evaluated with regard to further reactor scale‐up. |
| Databáze: |
Supplemental Index |
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