Modelling of planar and spherical phase interfaces for multicomponent systems using density gradient theory
Identifikátory výsledku
Kód výsledku v IS VaVaI
<a href="https://www.isvavai.cz/riv?ss=detail&h=RIV%2F61388998%3A_____%2F19%3A00496348" target="_blank" >RIV/61388998:_____/19:00496348 - isvavai.cz</a>
Výsledek na webu
<a href="https://www.sciencedirect.com/science/article/pii/S0378381218304369" target="_blank" >https://www.sciencedirect.com/science/article/pii/S0378381218304369</a>
DOI - Digital Object Identifier
<a href="http://dx.doi.org/10.1016/j.fluid.2018.10.014" target="_blank" >10.1016/j.fluid.2018.10.014</a>
Alternativní jazyky
Jazyk výsledku
angličtina
Název v původním jazyce
Modelling of planar and spherical phase interfaces for multicomponent systems using density gradient theory
Popis výsledku v původním jazyce
This study presents mathematical modelling of the properties of vapour-liquid phase interfaces for multi-component mixtures. The developed model can be applied both on a standard case of a planar phase interface and on a spherical interface representing droplets or bubbles. The PCP-SAFT equation of state is utilized for thermodynamic property evaluation. The fundamentals of the presented model lie in the Density Gradient Theory (DGT) used to formulate the governing differential equations. An innovative approach to the problem formulation divides the solution into two parts, an algebraic solution and a differential equations solution, that can be solved individually. The developed solution method can be applied on both interface geometries, for which the density profile is solved as the main quantity describing the interface. In addition to the density profile, the surface tension and adsorptions of mixture components within the interface are computed. Mixtures with CO2 were selected as the demonstrative systems in this work. Modelled mixtures of n-butane + CO2, n-decane + CO2, and SF6 + CO2 were compared with available experimental data for surface tension and also with the predictions of a more general Density Functional Theory (DFT). Based on these comparisons, the model was found to be in a good agreement with experimental data and comparable to the DFT predictions.
Název v anglickém jazyce
Modelling of planar and spherical phase interfaces for multicomponent systems using density gradient theory
Popis výsledku anglicky
This study presents mathematical modelling of the properties of vapour-liquid phase interfaces for multi-component mixtures. The developed model can be applied both on a standard case of a planar phase interface and on a spherical interface representing droplets or bubbles. The PCP-SAFT equation of state is utilized for thermodynamic property evaluation. The fundamentals of the presented model lie in the Density Gradient Theory (DGT) used to formulate the governing differential equations. An innovative approach to the problem formulation divides the solution into two parts, an algebraic solution and a differential equations solution, that can be solved individually. The developed solution method can be applied on both interface geometries, for which the density profile is solved as the main quantity describing the interface. In addition to the density profile, the surface tension and adsorptions of mixture components within the interface are computed. Mixtures with CO2 were selected as the demonstrative systems in this work. Modelled mixtures of n-butane + CO2, n-decane + CO2, and SF6 + CO2 were compared with available experimental data for surface tension and also with the predictions of a more general Density Functional Theory (DFT). Based on these comparisons, the model was found to be in a good agreement with experimental data and comparable to the DFT predictions.
Klasifikace
Druh
J<sub>imp</sub> - Článek v periodiku v databázi Web of Science
CEP obor
—
OECD FORD obor
20303 - Thermodynamics
Návaznosti výsledku
Projekt
Výsledek vznikl pri realizaci vícero projektů. Více informací v záložce Projekty.
Návaznosti
P - Projekt vyzkumu a vyvoje financovany z verejnych zdroju (s odkazem do CEP)
Ostatní
Rok uplatnění
2019
Kód důvěrnosti údajů
S - Úplné a pravdivé údaje o projektu nepodléhají ochraně podle zvláštních právních předpisů
Údaje specifické pro druh výsledku
Název periodika
Fluid Phase Equilibria
ISSN
0378-3812
e-ISSN
—
Svazek periodika
483
Číslo periodika v rámci svazku
March
Stát vydavatele periodika
NL - Nizozemsko
Počet stran výsledku
14
Strana od-do
70-83
Kód UT WoS článku
000456757100005
EID výsledku v databázi Scopus
2-s2.0-85056223160