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Prediction of power consumption and mass transfer in mechanically agitated fermenters, physical interpretation of experimental data.
volumetric mass transfercoefficients (kLa) for non-coalescent batches under high is switched with P it improved the closeness of the correlation for non-coalescent batches-coalescent
CI - Průmyslová chemie a chemické inženýrství
- 2014 •
- D •
- Link
Rok uplatnění
D - Stať ve sborníku
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Volumetric mass transfer coefficient in the gas-liquid contactor agitated by Rushton turbines of various diameters in non-coalescent batch
an appropriate correlation for kLa prediction in non-coalescent batch the extensive) in the non-coalescent type of the batch. The experiments were carried out in a multiple in the non-
Chemical engineering (plants, products)
- 2019 •
- D
Rok uplatnění
D - Stať ve sborníku
Volumetric mass transfer coefficient in the gas-liquid contactor agitated by Rushton turbines of various diameters in non-coalescent batch
an appropriate correlation for kLaprediction in non-coalescent batch the extensive industrialdesign of gas-liquid contactors operating with non-coalescent batch. at the kLadependencies i...
Fluids and plasma physics (including surface physics)
- 2019 •
- O
Rok uplatnění
O - Ostatní výsledky
Power Input Prediction in Agitated Gas-Liquid Contactors with Non-coalescent Batch
for the industrial design of the process with a non-coalescent batch that would be appropriate...
Chemical engineering (plants, products)
- 2019 •
- Jimp •
- Link
Rok uplatnění
Jimp - Článek v periodiku v databázi Web of Science
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Power input prediction in agitated gas-liquid contractors with non-coalescent batch
for the industrial design of the process with a non-coalescent batch thatnwould be appropriate...
Fluids and plasma physics (including surface physics)
- 2019 •
- Jimp •
- Link
Rok uplatnění
Jimp - Článek v periodiku v databázi Web of Science
Výsledek na webu
Lactic acid separation by the liquid membrane at high pH
and transport characteristic (mainly kLa) in the non-coalescent type of the batch correlation for kLa prediction in the non-coalescent batch is presented. Presented). With an intent to create an ...
Chemical engineering (plants, products)
- 2019 •
- D
Rok uplatnění
D - Stať ve sborníku
HEAT TRANSFER BETWEEN GAS AND NON-COALESCENT LIQUID IN A BUBBLE COLUMN
. The aqueous solution of 0.3 M Na2SO4 was used as a non-coalescent batch. The gas-to-liquid heat transfer measurements were performed by a non-steady state method based for the heat transfer between gas and the
Chemical process engineering
- 2019 •
- JSC •
- Link
Rok uplatnění
JSC - Článek v periodiku v databázi SCOPUS
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Power and mass transfer correlations for the design of multi-impeller gas-liquid contactors for non-coalescent electrolyte solutions
-liquid pilot plant vessel of diameter of 0.6 m using a fully non-coalescent (0.5 M Na2SO4) non-viscous batch. Physical relevance of the kLa data measured by the dynamic data at high absorption rates in the non...
CI - Průmyslová chemie a chemické inženýrství
- 2012 •
- Jx •
- Link
Rok uplatnění
Jx - Nezařazeno - Článek v odborném periodiku (Jimp, Jsc a Jost)
Výsledek na webu
The effect of surface active additives on bubble coalescence and gas holdup in viscous aerated batches.
Original scientific paper dealing with The effect of surface active additives on bubble coalescence and gas holdup in viscous aerated batches....
CI - Průmyslová chemie a chemické inženýrství
- 1999 •
- Jx
Rok uplatnění
Jx - Nezařazeno - Článek v odborném periodiku (Jimp, Jsc a Jost)
Gas-Liquid Mass Transfer Rates and Impeller Power Consumptions for Industrial Vessel Design
kLa for non-coalescent batches under high energy dissipation rates. Accurate kLa non-coalescent and coalescent batches. Applying the proposed correlations......
CI - Průmyslová chemie a chemické inženýrství
- 2015 •
- Jx •
- Link
Rok uplatnění
Jx - Nezařazeno - Článek v odborném periodiku (Jimp, Jsc a Jost)
Výsledek na webu
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