Journal ArticleDOI
Description and evaluation of reciprocating plate bioreactors
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TLDR
The performance of reciprocating plate bioreactors for the production of an exocellular polysaccharide (pullulan) by yeast Aureobasidium pullulans is analyzed and results clearly show that a more efficient substrate utilisation is achieved with reciprocating plates.Abstract:
The environment in which live microorganisms has a major impact on their productivity. One important factor is the mechanical mixing that is used to promote good heat and mass transfer in bioreactors. In this paper, the performance of reciprocating plate bioreactors is first evaluated for their ability to produce high oxygen transfer coefficients. Pure water and a glycerol water (50∶50 wt%) solution are used for this evaluation. Then, the performance of reciprocating plate bioreactors for the production of an exocellular polysaccharide (pullulan) by yeast Aureobasidium pullulans is analyzed in terms of quantity and quality of the polysaccharide. Results clearly show that a more efficient substrate utilisation is achieved with reciprocating plate bioreactors.read more
Citations
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Journal ArticleDOI
Growth of filamentous fungi in submerged culture: problems and possible solutions
TL;DR: The influence of the chemical and physical environment on culture morphology, the process engineering challenges presented by different fungal morphologies, and the relationship between fungal morphology and metabolite production are all discussed.
Journal ArticleDOI
Power consumption and mass transfer in agitated gas‐liquid columns: A comparative study
TL;DR: In this paper, the power consumption, gas holdup and oxygen mass transfer in agitated gas-liquid columns have been studied for an air-water system, and a linear fit of the correlation of power consumption obtained for all mixing devices plotted against the reciprocating frequency or speed of rotation to the third power has been obtained.
Journal ArticleDOI
Pullulan fermentation in a reciprocating plate bioreactor
TL;DR: It appears that the optimum yield would be achieved at an intermediate dissolved oxygen concentration, while the quality of the product, expressed in terms of the viscosity of the fermentation broth, was nevertheless reduced.
Journal ArticleDOI
A review of bioreactor technology used for enzymatic hydrolysis of cellulosic materials
TL;DR: Different bioreactors have been reviewed for cellulase production with the aim to investigate main factors for designing a bioreactor, including efficient mixing, sufficient mass transfer, low shear stress, low foaming problems and low consumption of water and energy.
Journal ArticleDOI
Polysaccharide production: Experimental comparison of the performance of four mixing devices
TL;DR: In this paper, the performance of four different mixing devices for the production of the polysaccharide pullulan with Aureobasidium pullulans (2552) was compared experimentally.
References
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Book
Biochemical engineering fundamentals
James E. Bailey,David F. Ollis +1 more
TL;DR: Biochemical Engineering Fundamentals, 2/e as mentioned in this paper combines contemporary engineering science with relevant biological concepts in a comprehensive introduction to biochemical engineering, which enables students to comprehend the major problems in biochemical engineering and formulate effective solutions.
Journal ArticleDOI
A critical review and experimental verification of the correct use of the dynamic method for the determination of oxygen transfer in aerated agitated vessels to water, electrolyte solutions and viscous liquids
V. Linek,Václav Vacek,P. Beneš +2 more
TL;DR: In this article, the authors compared the performance of different dynamic methods for the volumetric mass transfer coefficient for oxygen kla obtained by various dynamic methods and concluded that only one variant gives correct results over a wide range of power dissipated per unit volume.
Book ChapterDOI
Design of biochemical reactors mass transfer criteria for simple and complex systems
M. Moo-Young,H. W. Blanch +1 more
TL;DR: In this paper, the authors treat biochemicals as heterogeneous catalytic (HC) this paper in which physical mass transfer completely or significantly controls the overall rate of the process being promoted in the reactor.
Journal ArticleDOI
Gas-liquid mass transfer and holdup in vessels stirred with multiple Rushton turbines: water and water-glycerol solutions
TL;DR: In this article, the gas-liquid mass transfer coefficient, holdup, and power consumption were measured in vessels stirred with multiple Rushton turbines, with viscosity up to 70 mPa[center dot]s.
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