Power input in viscous liquid in mechanically agitated fermenters. Measurements and Scale-up.
Identifikátory výsledku
Kód výsledku v IS VaVaI
<a href="https://www.isvavai.cz/riv?ss=detail&h=RIV%2F60461373%3A22340%2F18%3A43916800" target="_blank" >RIV/60461373:22340/18:43916800 - isvavai.cz</a>
Výsledek na webu
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DOI - Digital Object Identifier
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Alternativní jazyky
Jazyk výsledku
angličtina
Název v původním jazyce
Power input in viscous liquid in mechanically agitated fermenters. Measurements and Scale-up.
Popis výsledku v původním jazyce
Transport characteristic such as power input, P, is the key parameter in the design of mechanically agitated gas–liquid contactors. For their successful design, values of the key parameter can be estimated using empirical correlations. The goal of this work is to complete a complex study to investigate the behavior of P in multiple-impeller vessels in non-coalescent viscous batch. The experiments were conducted in multiple-impeller vessels of both laboratory and pilot-plant scale, which enabled the scale-up studies. Several impeller types with different diameters and their combinations on a common shaft were used in the vessel, under various impeller tip speeds and gassing rates. For all impeller combinations, the gassed and ungassed power consumption were measured in viscous batch. The measured transport characteristic was summarized into correlations. Several literature correlations were judged, using these extensive datasets. In addition to this, new correlation shapes were also established. These correlations can be used to predict transport characteristics in industrial-scale vessels under a wide range of operational conditions.
Název v anglickém jazyce
Power input in viscous liquid in mechanically agitated fermenters. Measurements and Scale-up.
Popis výsledku anglicky
Transport characteristic such as power input, P, is the key parameter in the design of mechanically agitated gas–liquid contactors. For their successful design, values of the key parameter can be estimated using empirical correlations. The goal of this work is to complete a complex study to investigate the behavior of P in multiple-impeller vessels in non-coalescent viscous batch. The experiments were conducted in multiple-impeller vessels of both laboratory and pilot-plant scale, which enabled the scale-up studies. Several impeller types with different diameters and their combinations on a common shaft were used in the vessel, under various impeller tip speeds and gassing rates. For all impeller combinations, the gassed and ungassed power consumption were measured in viscous batch. The measured transport characteristic was summarized into correlations. Several literature correlations were judged, using these extensive datasets. In addition to this, new correlation shapes were also established. These correlations can be used to predict transport characteristics in industrial-scale vessels under a wide range of operational conditions.
Klasifikace
Druh
D - Stať ve sborníku
CEP obor
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OECD FORD obor
20401 - Chemical engineering (plants, products)
Návaznosti výsledku
Projekt
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Návaznosti
S - Specificky vyzkum na vysokych skolach
Ostatní
Rok uplatnění
2018
Kód důvěrnosti údajů
S - Úplné a pravdivé údaje o projektu nepodléhají ochraně podle zvláštních právních předpisů
Údaje specifické pro druh výsledku
Název statě ve sborníku
Proceedings of 45th International Conference of Slovak Society of Chemical Engineering
ISBN
978-80-89597-89-5
ISSN
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e-ISSN
neuvedeno
Počet stran výsledku
15
Strana od-do
183-197
Název nakladatele
Slovak Society of Chemical Engineering
Místo vydání
Bratislava
Místo konání akce
Tatranské Matriare
Datum konání akce
21. 5. 2018
Typ akce podle státní příslušnosti
WRD - Celosvětová akce
Kód UT WoS článku
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