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rdf:type
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Description
| - Mechanically agitated gas-liquid contactors are frequently used in the chemical, food and biochemical industries such as fermenters and hydrogenation or chlorination reactors. However wide the usage of such vessels is, their design is not based on chemical engineering data but is still rather empirical. It is highly desirable to have a tool for the rational design of agitated gas-liquid contactors based on fundamental chemical engineering parameters transferable to other systems and operating conditions. In the cases of a liquid film-controlled process, the volumetric mass transfer coefficient, kLa, is the key parameter for the design. Experimental kLa data obtained both for laboratory and for pilot-plant fermenter are presented for non-coalescent (sulphate solution) batch, which represents most of the industrial batches. The experimental kLa data obtained for various impeller configurations were treated with the aim to find the tightest correlation shapes to describe the effect i) of the vessel size and ii) of the impeller geometry.
- Mechanically agitated gas-liquid contactors are frequently used in the chemical, food and biochemical industries such as fermenters and hydrogenation or chlorination reactors. However wide the usage of such vessels is, their design is not based on chemical engineering data but is still rather empirical. It is highly desirable to have a tool for the rational design of agitated gas-liquid contactors based on fundamental chemical engineering parameters transferable to other systems and operating conditions. In the cases of a liquid film-controlled process, the volumetric mass transfer coefficient, kLa, is the key parameter for the design. Experimental kLa data obtained both for laboratory and for pilot-plant fermenter are presented for non-coalescent (sulphate solution) batch, which represents most of the industrial batches. The experimental kLa data obtained for various impeller configurations were treated with the aim to find the tightest correlation shapes to describe the effect i) of the vessel size and ii) of the impeller geometry. (en)
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Title
| - TRANSPORT CHARACTERISTICS IN MULTI-IMPELLER FERMENTERS. THE EFFECTS OF VESSEL SIZE AND IMPELLER TYPE
- TRANSPORT CHARACTERISTICS IN MULTI-IMPELLER FERMENTERS. THE EFFECTS OF VESSEL SIZE AND IMPELLER TYPE (en)
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skos:prefLabel
| - TRANSPORT CHARACTERISTICS IN MULTI-IMPELLER FERMENTERS. THE EFFECTS OF VESSEL SIZE AND IMPELLER TYPE
- TRANSPORT CHARACTERISTICS IN MULTI-IMPELLER FERMENTERS. THE EFFECTS OF VESSEL SIZE AND IMPELLER TYPE (en)
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skos:notation
| - RIV/60461373:22340/13:43895946!RIV14-MSM-22340___
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http://linked.open...avai/riv/aktivita
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http://linked.open...avai/riv/aktivity
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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
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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/60461373:22340/13:43895946
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http://linked.open...riv/jazykVysledku
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http://linked.open.../riv/klicovaSlova
| - volumetric mass transfer coefficient; scale-up; multipleimpeller; mixing; mass transfer correlations; gas-liquid mass transfer; fermenter (en)
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http://linked.open.../riv/klicoveSlovo
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http://linked.open...ontrolniKodProRIV
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http://linked.open...v/mistoKonaniAkce
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http://linked.open...i/riv/mistoVydani
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http://linked.open...i/riv/nazevZdroje
| - Proceedings of the 40th International Conference of Slovak Society of Chemical Engineering
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http://linked.open...in/vavai/riv/obor
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http://linked.open...ichTvurcuVysledku
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http://linked.open...cetTvurcuVysledku
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http://linked.open...UplatneniVysledku
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http://linked.open...iv/tvurceVysledku
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http://linked.open...vavai/riv/typAkce
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http://linked.open.../riv/zahajeniAkce
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number of pages
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http://purl.org/ne...btex#hasPublisher
| - Slovak Society of Chemical Engineering
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https://schema.org/isbn
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http://localhost/t...ganizacniJednotka
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