| Attributes | Values |
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| rdf:type
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| Description
| - Mixing intensity of the liquid phase,power consumption and volumetric mass transfer coef cients are presented for various single-,double- and triple-impeller con gurations.The measurements were carried out in a at-bottomed vessel of inner diameter 0.29 m.Twenty-eight combinations of various impeller types inducing radial,axial and combined liquid ow were used,viz.a Rushton Turbine (RT),a six Pitched Blade (PB),Techmix 335 (TX)impellers pumping downwards (D)and upwards (U),Lightnin A315 (LTN)and a Narcissus (NS)impeller. Water,0.5 M Na 2 SO 4 solution and solution of commercial thickener (Sokrat 44)were used as a liquid phase,representing coalescent,non- coalescent and viscous batches,respectively.Mixing intensity of the liquid phase was characterized by both exchange ows and homogenization times.The dimensionless mixing time,Nt m ,does not depend on Reynolds number but on the direction of liquid ow induced by the impeller. The axial impellers (TXU,TXD,and LTN)provide more effective homogenizati
- Mixing intensity of the liquid phase,power consumption and volumetric mass transfer coef cients are presented for various single-,double- and triple-impeller con gurations.The measurements were carried out in a at-bottomed vessel of inner diameter 0.29 m.Twenty-eight combinations of various impeller types inducing radial,axial and combined liquid ow were used,viz.a Rushton Turbine (RT),a six Pitched Blade (PB),Techmix 335 (TX)impellers pumping downwards (D)and upwards (U),Lightnin A315 (LTN)and a Narcissus (NS)impeller. Water,0.5 M Na 2 SO 4 solution and solution of commercial thickener (Sokrat 44)were used as a liquid phase,representing coalescent,non- coalescent and viscous batches,respectively.Mixing intensity of the liquid phase was characterized by both exchange ows and homogenization times.The dimensionless mixing time,Nt m ,does not depend on Reynolds number but on the direction of liquid ow induced by the impeller. The axial impellers (TXU,TXD,and LTN)provide more effective homogenizati (en)
- Mixing intensity of the liquid phase,power consumption and volumetric mass transfer coef cients are presented for various single-,double- and triple-impeller con gurations.The measurements were carried out in a at-bottomed vessel of inner diameter 0.29 m.Twenty-eight combinations of various impeller types inducing radial,axial and combined liquid ow were used,viz.a Rushton Turbine (RT),a six Pitched Blade (PB),Techmix 335 (TX)impellers pumping downwards (D)and upwards (U),Lightnin A315 (LTN)and a Narcissus (NS)impeller. Water,0.5 M Na 2 SO 4 solution and solution of commercial thickener (Sokrat 44)were used as a liquid phase,representing coalescent,non- coalescent and viscous batches,respectively.Mixing intensity of the liquid phase was characterized by both exchange ows and homogenization times.The dimensionless mixing time,Nt m ,does not depend on Reynolds number but on the direction of liquid ow induced by the impeller. The axial impellers (TXU,TXD,and LTN)provide more effective homogenizati (cs)
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| Title
| - Mass transfer correlations for multiple-impeller gas -liquid contactors.
- Korelace koeficientu přestupu hmoty v nádobě s více míchadly (cs)
- Mass transfer correlations for multiple-impeller gas -liquid contactors. (en)
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| skos:prefLabel
| - Mass transfer correlations for multiple-impeller gas -liquid contactors.
- Korelace koeficientu přestupu hmoty v nádobě s více míchadly (cs)
- Mass transfer correlations for multiple-impeller gas -liquid contactors. (en)
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| skos:notation
| - RIV/60461373:22340/07:00018471!RIV08-MSM-22340___
|
| http://linked.open.../vavai/riv/strany
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| http://linked.open...avai/riv/aktivita
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| http://linked.open...avai/riv/aktivity
| - P(GA104/06/0736), Z(MSM6046137306)
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| http://linked.open...iv/cisloPeriodika
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| http://linked.open...vai/riv/dodaniDat
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| http://linked.open...aciTvurceVysledku
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| http://linked.open.../riv/druhVysledku
| |
| http://linked.open...iv/duvernostUdaju
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| http://linked.open...titaPredkladatele
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| http://linked.open...dnocenehoVysledku
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| http://linked.open...ai/riv/idVysledku
| - RIV/60461373:22340/07:00018471
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| http://linked.open...riv/jazykVysledku
| |
| http://linked.open.../riv/klicovaSlova
| - Mass transfer; Multiple-impeller vessel; Mass transfer coef cient; Gas -liquid axial dispersion (en)
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| http://linked.open.../riv/klicoveSlovo
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| http://linked.open...odStatuVydavatele
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| http://linked.open...ontrolniKodProRIV
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| http://linked.open...i/riv/nazevZdroje
| - Chemical Engineering Science
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| http://linked.open...in/vavai/riv/obor
| |
| http://linked.open...ichTvurcuVysledku
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| http://linked.open...cetTvurcuVysledku
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| http://linked.open...vavai/riv/projekt
| |
| http://linked.open...UplatneniVysledku
| |
| http://linked.open...v/svazekPeriodika
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| http://linked.open...iv/tvurceVysledku
| - Linek, Václav
- Moucha, Tomáš
- Fujasová, Mária
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| http://linked.open...n/vavai/riv/zamer
| |
| issn
| |
| number of pages
| |
| http://localhost/t...ganizacniJednotka
| |
| is http://linked.open...avai/riv/vysledek
of | |
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