2011•Journal of Wuhan Institute of TechnologyRequires access

Optimization design of stirrer in bioreactor

Dong Hou-sheng

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Abstract

The forms of agitator blades were outlined.The flow field in the fermentation tank was simulated by using computational fluid dynamics software.There was a fermenter,diameter D=3 800 mm,liquid height H=8 600 mm,Speed n=110 r/min.A315 turbine agitator was used as up impeller Rushton turbine agitator was used as down impeller.The simulated data shows that the six-leaves turbine stirrer effect is more excellent than Rushton turbine agitator,and much more conducive to the exchange of substances.

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What this paper is about

The forms of agitator blades were outlined.The flow field in the fermentation tank was simulated by using computational fluid dynamics software.There was a fermenter,diameter D=3 800 mm,liquid height H=8 600 mm,Speed n=110 r/min.A315 turbine agitator was used as up impeller Rushton turbine agitator was used as down impeller.The simulated data shows that the six-leaves turbine stirrer effect is more excellent than Rushton turbine agitator,and much more conducive to the exchange of substances.

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Available abstract

The forms of agitator blades were outlined.The flow field in the fermentation tank was simulated by using computational fluid dynamics software.There was a fermenter,diameter D=3 800 mm,liquid height H=8 600 mm,Speed n=110 r/min.A315 turbine agitator was used as up impeller Rushton turbine agitator was used as down impeller.The simulated data shows that the six-leaves turbine stirrer effect is more excellent than Rushton turbine agitator,and much more conducive to the exchange of substances.

Key concepts: Agitator, Impeller, Rushton turbine, Turbine, Industrial fermentation, Computational fluid dynamics, Mechanical engineering, Engineering

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