Development of an unsteady-state model for a biological system in miniaturized bioreactors

被引:7
|
作者
Amoabediny, Ghassem [1 ,2 ]
Ziaie-Shirkolaee, Yaser [1 ,3 ]
Buechs, Jochen [3 ]
机构
[1] Univ Tehran, Sch Engn, Fac Chem Engn, Dept Biotechnol, Tehran, Iran
[2] Univ Tehran, Res Ctr New Technol Life Sci Engn, Tehran, Iran
[3] Rhein Westfal TH Aachen, D-52074 Aachen, Germany
关键词
biological system; bioreactor; gas transfer coefficient of sterile closure; shake flask; unsteady-state modelling; MASS-TRANSFER RESISTANCE; SHAKE-FLASKS; OXYGEN-TRANSFER; SURFACE AERATION; CULTURES; VENTILATION; CAPACITY; DEVICE; RATES;
D O I
10.1042/BA20090141
中图分类号
Q5 [生物化学]; Q7 [分子生物学];
学科分类号
071010 ; 081704 ;
摘要
In the present study, the special shake flasks, so-called ventilation flasks, are equipped with oxygen sensors and then an unsteady-state gas transfer model for shake flasks was developed and experimentally investigated for a wide range of gas transfer resistances (k(plug)). For the validation of our unsteady-state model to simulate the gas transfer in a biological system in the ventilation flasks, a strain of Corenobacterium glutamicum DM1730 was used as a model organism. For further easy processing, the resulting total mass-transfer resistance (k(plug)) is described as a function of the mass flow through the sterile plug (OTR(plug)) by an empirical equation. This equation is introduced into a simulation model that calculates the gas partial pressures in the headspace of the flask. Additionally, the gas transfer rates through the sterile closure and gas/liquid interface inside the flask are provided. This unsteady-state model would be a very useful method for scaling up from a shake flask to a fermentor; comparing the results of the gas concentration in the gas phase, there is good agreement between the introduced unsteady-state model and experimental results for the biological system.
引用
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页码:163 / 170
页数:8
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