Liquid mixing time and gas distribution in aerated multiple-impeller stirred tanks
Identifikátory výsledku
Kód výsledku v IS VaVaI
<a href="https://www.isvavai.cz/riv?ss=detail&h=RIV%2F60461373%3A22340%2F22%3A43925331" target="_blank" >RIV/60461373:22340/22:43925331 - isvavai.cz</a>
Výsledek na webu
<a href="https://reader.elsevier.com/reader/sd/pii/S0263876222003021?token=99BCA6301B499E40519147A4ACD1ABB788C5CC0AE4DD4C2F5F401A87F0235CABB3F07B1D908766007C438752A0B808D3&originRegion=eu-west-1&originCreation=20230221075045" target="_blank" >https://reader.elsevier.com/reader/sd/pii/S0263876222003021?token=99BCA6301B499E40519147A4ACD1ABB788C5CC0AE4DD4C2F5F401A87F0235CABB3F07B1D908766007C438752A0B808D3&originRegion=eu-west-1&originCreation=20230221075045</a>
DOI - Digital Object Identifier
<a href="http://dx.doi.org/10.1016/j.cherd.2022.06.021" target="_blank" >10.1016/j.cherd.2022.06.021</a>
Alternativní jazyky
Jazyk výsledku
angličtina
Název v původním jazyce
Liquid mixing time and gas distribution in aerated multiple-impeller stirred tanks
Popis výsledku v původním jazyce
Gas-liquid fluid dynamics and mass transfer are crucial aspects of aerobic fermentation and robust methodologies for their determination in industrial bioreactors are expected to provide significant improvements in many production processes. In this work, a gas-liquid stirred tank of high aspect ratio, that replicates the geometry of typical industrial aerated fermenters, is investigated. In particular, the liquid phase homogenization dynamics and the gas phase spatial distribution are determined. The selected methodology is based on the analysis of the conductivity measurements obtained by Electrical Resistance Tomography. The gas-liquid flow regimes and the mixing time are identified at various gas flow rates and impeller speeds, thus covering different gas-liquid regimes. Data collected with vertical and horizontal arrangements of the electrodes allow to obtain a detailed picture of the equipment working mode and to gain insight into the gas-liquid flow dynamics under optically inaccessible conditions. Quantitative evaluation of the reliability of the collected data is attempted by comparing the results obtained with the vertical and horizontal arrangements in the same locations. © 2022 Institution of Chemical Engineers
Název v anglickém jazyce
Liquid mixing time and gas distribution in aerated multiple-impeller stirred tanks
Popis výsledku anglicky
Gas-liquid fluid dynamics and mass transfer are crucial aspects of aerobic fermentation and robust methodologies for their determination in industrial bioreactors are expected to provide significant improvements in many production processes. In this work, a gas-liquid stirred tank of high aspect ratio, that replicates the geometry of typical industrial aerated fermenters, is investigated. In particular, the liquid phase homogenization dynamics and the gas phase spatial distribution are determined. The selected methodology is based on the analysis of the conductivity measurements obtained by Electrical Resistance Tomography. The gas-liquid flow regimes and the mixing time are identified at various gas flow rates and impeller speeds, thus covering different gas-liquid regimes. Data collected with vertical and horizontal arrangements of the electrodes allow to obtain a detailed picture of the equipment working mode and to gain insight into the gas-liquid flow dynamics under optically inaccessible conditions. Quantitative evaluation of the reliability of the collected data is attempted by comparing the results obtained with the vertical and horizontal arrangements in the same locations. © 2022 Institution of Chemical Engineers
Klasifikace
Druh
J<sub>imp</sub> - Článek v periodiku v databázi Web of Science
CEP obor
—
OECD FORD obor
20401 - Chemical engineering (plants, products)
Návaznosti výsledku
Projekt
—
Návaznosti
S - Specificky vyzkum na vysokych skolach
Ostatní
Rok uplatnění
2022
Kód důvěrnosti údajů
S - Úplné a pravdivé údaje o projektu nepodléhají ochraně podle zvláštních právních předpisů
Údaje specifické pro druh výsledku
Název periodika
Chemical Engineering Research and Design
ISSN
0263-8762
e-ISSN
1744-3563
Svazek periodika
184
Číslo periodika v rámci svazku
August
Stát vydavatele periodika
SG - Singapurská republika
Počet stran výsledku
12
Strana od-do
501-512
Kód UT WoS článku
000841163700006
EID výsledku v databázi Scopus
2-s2.0-85132941254