Pregled bibliografske jedinice broj: 95187
Tubular Bioreactors-Mixing and Scale-up Procedure
Tubular Bioreactors-Mixing and Scale-up Procedure // Biotechnology and Environment / Kniewald, Zlatko (ur.).
Zagreb: Hrvatsko Društvo za Biotehnologiju, 2001. (pozvano predavanje, međunarodna recenzija, sažetak, znanstveni)
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Naslov
Tubular Bioreactors-Mixing and Scale-up Procedure
Autori
Novak, Srđan ; Šantek, Božidar ; Horvat, Predrag ; Marić, Vladimir
Vrsta, podvrsta i kategorija rada
Sažeci sa skupova, sažetak, znanstveni
Izvornik
Biotechnology and Environment
/ Kniewald, Zlatko - Zagreb : Hrvatsko Društvo za Biotehnologiju, 2001
Skup
Biotechnology and Environment
Mjesto i datum
Zagreb, Hrvatska, 19.02.2001. - 22.02.2001
Vrsta sudjelovanja
Pozvano predavanje
Vrsta recenzije
Međunarodna recenzija
Ključne riječi
tubular bioreactors; mixing; mathematical models; scale-up procedure
Sažetak
Tubular bioreactors are characterized by plug flow and are proven to be suitable for continuous processes. Comparison between tank and tubular bioreactors shows that tubular bioreactors are characterized by simplified construction, increased surface/volume ratio and concentration gradients of broth components along the bioreactor. Main disadvantage of tubular bioreactors is a relatively low aeration capacity. Tubular bioreactors are suitable for various processes such as wastewater treatment the production of ethanol, organic acids, biopesticides and cultivation of animal cells and phototrophic organisms Horizontal rotating tubular bioreactor (HRTB) was designed as combination of a "thin layer' bioreactor and "biodisc" reactor. Its interior was divided by O-ring shaped partition walls that served as carriers for active biomass. Mixing investigations in HRTB were carried on for different combinations of process parameters by using temperature step method. The axial dispersion model and modified cascade models ("simple" and "spiral" flow model, respectively) were used to describe the mixing in HRTB. Comparison between these models showed that the "spiral" flow model was the most suitable for mixing characterization in HRTB. In order to incorporate the "spiral" flow model in semifundamental scale-up it was necessary to make relations between the adjustable model parameters and bioreactor process parameters expressed as dimensionless numbers. Mathematica1 equations which relate adjustable model parameters and dimensionless numbers were used for the formation of prediction systems for adjustable model parameters. The analysis based o different criteria selected the most suitable prediction system for mixing description in HRTB. This prediction system could be based as a part of bioreactor scale-up procedure.
Izvorni jezik
Engleski
Znanstvena područja
Biotehnologija, Prehrambena tehnologija