Some aspects of rate-based modelling and simulation of three-phase distillation columns.

Result code in IS VaVaI

<a href="https://www.isvavai.cz/riv?ss=detail&h=RIV%2F60461373%3A22340%2F00%3A00005729" target="_blank" >RIV/60461373:22340/00:00005729 - isvavai.cz</a>

Alternative codes found

RIV/60461373:22340/00:00005737

Result on the web

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DOI - Digital Object Identifier

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Result language

angličtina

Original language name

Some aspects of rate-based modelling and simulation of three-phase distillation columns.

Original language description

The application of the bate-based approach to the dynamic and stationary modelling of three-phase distillation columns is presented. The resulting combined non-equilibrium and equilibrium model is compared to the classical equilibrium model and also to experimental data for ethanol-water-cyclohexane separation in a number of examples.

Czech name

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Czech description

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Type

D - Article in proceedings

CEP classification

CI - Industrial chemistry and chemical engineering

OECD FORD branch

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Project

<a href="/en/project/GA104%2F97%2F0916" target="_blank" >GA104/97/0916: Steady state and dynamic modelling of separation processes using the rate based approach</a><br>

Continuities

Z - Vyzkumny zamer (s odkazem do CEZ)

Publication year

2000

Confidentiality

S - Úplné a pravdivé údaje o projektu nepodléhají ochraně podle zvláštních právních předpisů

Article name in the collection

European Symposium on Computer

ISBN

0-444-50520-2

ISSN

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e-ISSN

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Number of pages

6

Pages from-to

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Publisher name

Elsevier Sciences B.V.

Place of publication

Florence, Italy

Event location

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Event date

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Type of event by nationality

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UT code for WoS article

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