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  • The application of the bate-based approach to the dynamic and stationary modelling of three-phase distillation columns is presented. The main problem can be seen in finding adequate models for the mass and heat transfer over phase interfaces to be utilised in the Maxwell-Stefan equations. While for the vapour - (continuous) liquid interface there are a number of methods and data available, the interface between continuous and dispersed liquid phases has not been studied for the case of distillation processes. A reasonable alternative approach to modelling of a three-phase distillation column can be found where the liquid-liquid interface is treated as equilibrium. The resulting combined non-equilibrium and equilibrium model is compared to the classicalequilibrium model and also to experimental data for ethanol-water-cyclohexane separation in a number of examples.
  • The application of the bate-based approach to the dynamic and stationary modelling of three-phase distillation columns is presented. The main problem can be seen in finding adequate models for the mass and heat transfer over phase interfaces to be utilised in the Maxwell-Stefan equations. While for the vapour - (continuous) liquid interface there are a number of methods and data available, the interface between continuous and dispersed liquid phases has not been studied for the case of distillation processes. A reasonable alternative approach to modelling of a three-phase distillation column can be found where the liquid-liquid interface is treated as equilibrium. The resulting combined non-equilibrium and equilibrium model is compared to the classicalequilibrium model and also to experimental data for ethanol-water-cyclohexane separation in a number of examples. (en)
Title
  • Some aspects of rate-based modelling and simulation of three-phase distillation columns
  • Some aspects of rate-based modelling and simulation of three-phase distillation columns (en)
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  • Some aspects of rate-based modelling and simulation of three-phase distillation columns
  • Some aspects of rate-based modelling and simulation of three-phase distillation columns (en)
skos:notation
  • RIV/60461373:22340/01:00004079!RIV/2004/MSM/223404/N
http://linked.open.../vavai/riv/strany
  • 603;612
http://linked.open...avai/riv/aktivita
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  • Z(MSM 223400007)
http://linked.open...iv/cisloPeriodika
  • 4-6
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  • 696364
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  • RIV/60461373:22340/01:00004079
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  • Rate-based approach; Three-phase distillation; Non-equilibrium tray model; Simulation. (en)
http://linked.open.../riv/klicoveSlovo
http://linked.open...odStatuVydavatele
  • GB - Spojené království Velké Británie a Severního Irska
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  • [AA91AA2AFA8B]
http://linked.open...i/riv/nazevZdroje
  • Computers Chem. Engng.
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http://linked.open...UplatneniVysledku
http://linked.open...v/svazekPeriodika
  • 25
http://linked.open...iv/tvurceVysledku
  • Vaněk, Tomáš
  • Eckert, Egon
http://linked.open...n/vavai/riv/zamer
issn
  • 0098-1354
number of pages
http://localhost/t...ganizacniJednotka
  • 22340
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