Pregled bibliografske jedinice broj: 4180
Comparison of dispersion model and structured model for mixing in a horizontal rotating tubular bioreactor
Comparison of dispersion model and structured model for mixing in a horizontal rotating tubular bioreactor // 1st European Symposium on Biochemical Engineering Science / Glennon, B. ; Kieran, P. M. ; Luyben, K. Ch. A. M. (ur.).
Dublin: ESBES Secretariat, Dublin, 1996. str. 185 - 185 (poster, međunarodna recenzija, sažetak, znanstveni)
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Naslov
Comparison of dispersion model and structured model for mixing in a horizontal rotating tubular bioreactor
Autori
Šantek, Božidar ; Horvat, Predrag ; Novak, Srđan ; Moser, Anton ; Marić, Vladimir
Vrsta, podvrsta i kategorija rada
Sažeci sa skupova, sažetak, znanstveni
Izvornik
1st European Symposium on Biochemical Engineering Science
/ Glennon, B. ; Kieran, P. M. ; Luyben, K. Ch. A. M. - Dublin : ESBES Secretariat, Dublin, 1996, 185 - 185
Skup
1st European Symposium on Biochemical Engineering Science
Mjesto i datum
Dublin, Irska, 19.09.1996. - 21.09.1996
Vrsta sudjelovanja
Poster
Vrsta recenzije
Međunarodna recenzija
Ključne riječi
horizontal rotating tubular bioreactor; "spiral" flow model; dispersion model
Sažetak
A horizontal rotating tubular bioreactor (HRTB) was designed as a combination of a "thin-layer bioreactor" and a "biodisc" reactor whose interior was divided by O-ring shaped partition walls (1). Mixing properties of this new type of bioreactor were investigated by using a temperature step method and different mixing models. A dispersion model for mixing with Bodenstein number as a parameter was compared with a structured "spiral flow" model (2) by using following experimental and mathematical procedures :
-experimental results were obtained by measuring the response to temperature step of six
Pt-100 sensors (t_90 response time 0.08 s and resolution 0.002 K) for wide range of
process conditions (eight dilution rates combined with seven rotation speeds).
- the two sets of differential equations for heat balances were established based on two
mathematical models, the axial dispersion model and structured model with "spiral
flow", respectively.
- the above systems were simulated by using Runge-Kutta-Fehlberg integration and
optimised by the "Monte-Carlo" method.
- the comparison of mixing models was based on mathematical criteria (the sum of
temperature differences between measured and simulated results for all six sensors and
whole experimental time range).
The results obtained with above procedure show that structured "spiral flow" model (containing four adjustable parameters) is more capable to describe mixing properties in HRTB than the one parameter axial dispersion model.
1. B. Šantek et al.; Bioprocess Eng.; 14; 195-203; 1996
2. B. Šantek et al.; Bioprocess Eng.; 14; 223-229; 1996
Izvorni jezik
Engleski
Znanstvena područja
Prehrambena tehnologija