Gas hold-up in three-phase multiimpeller stirred reactor

Kód výsledku v IS VaVaI
<a href="https://www.isvavai.cz/riv?ss=detail&h=RIV%2F60461373%3A22340%2F01%3A00004362" target="_blank" >RIV/60461373:22340/01:00004362 - isvavai.cz</a>
Výsledek na webu
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Jazyk výsledku
angličtina
Název v původním jazyce
Gas hold-up in three-phase multiimpeller stirred reactor
Popis výsledku v původním jazyce
The gas hold-up has been measured in the tank stirred with two pitch blade turbines downward pumping effect. The used gas was air and liquid charge were suspensions of glass beads of mean diameter 0.14 mm and/or polyvinyl particles 0.94 mm. The liquid was either water (coalescing system), 0.5 M solution sodium sulphate and 0.1 M ethanol solution (non-coalescing systems). The higher gas hold-up has been found in non-coalescing systems. The presence of solid particles had ambiguous effect on hold-up. Thedata has been correlated according the equation in which stirred speed and gas flow rates occur.
Název v anglickém jazyce
Gas hold-up in three-phase multiimpeller stirred reactor
Popis výsledku anglicky
The gas hold-up has been measured in the tank stirred with two pitch blade turbines downward pumping effect. The used gas was air and liquid charge were suspensions of glass beads of mean diameter 0.14 mm and/or polyvinyl particles 0.94 mm. The liquid was either water (coalescing system), 0.5 M solution sodium sulphate and 0.1 M ethanol solution (non-coalescing systems). The higher gas hold-up has been found in non-coalescing systems. The presence of solid particles had ambiguous effect on hold-up. Thedata has been correlated according the equation in which stirred speed and gas flow rates occur.

Rok uplatnění
2001
Kód důvěrnosti údajů
S - Úplné a pravdivé údaje o projektu nepodléhají ochraně podle zvláštních právních předpisů

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