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Approximation and analysis of pervaporation of binary mixtures using nonequilibrium thermodynamics approach. / Toikka, A.; Naumkin, P.; Penkova, A.

в: Chemical Engineering Research and Design, Том 104, 2015, стр. 669-680.

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Toikka, A. ; Naumkin, P. ; Penkova, A. / Approximation and analysis of pervaporation of binary mixtures using nonequilibrium thermodynamics approach. в: Chemical Engineering Research and Design. 2015 ; Том 104. стр. 669-680.

BibTeX

@article{17d76f945ff441569fc4146000fba76f,
title = "Approximation and analysis of pervaporation of binary mixtures using nonequilibrium thermodynamics approach",
abstract = "In present work the nonequilibrium thermodynamic advantages for pervaporation process approximation are discussed. The calculation model, which aligns nonequilibrium thermodynamic, pervaporation data and vapor–liquid equilibrium data, is presented. The approximation of vapor–liquid equilibrium data for feed mixtures was performed by Wilson and NRTL equations. Approbation of proposed approach with the use of different membranes was carried out for six binary systems: methanol – water, ethanol – water, propanol-1 – water, propanol-2 – water, butanol-1 – water and acetone – water. The compatibility between the experimental pervaporation data and the results of estimation are discussed.",
keywords = "Pervaporation, Nonequilibrium thermodynamics, Membrane, Selectivity prediction",
author = "A. Toikka and P. Naumkin and A. Penkova",
year = "2015",
doi = "10.1016/j.cherd.2015.10.007",
language = "English",
volume = "104",
pages = "669--680",
journal = "Chemical Engineering Research and Design",
issn = "0263-8762",
publisher = "Institution of Chemical Engineers",

}

RIS

TY - JOUR

T1 - Approximation and analysis of pervaporation of binary mixtures using nonequilibrium thermodynamics approach

AU - Toikka, A.

AU - Naumkin, P.

AU - Penkova, A.

PY - 2015

Y1 - 2015

N2 - In present work the nonequilibrium thermodynamic advantages for pervaporation process approximation are discussed. The calculation model, which aligns nonequilibrium thermodynamic, pervaporation data and vapor–liquid equilibrium data, is presented. The approximation of vapor–liquid equilibrium data for feed mixtures was performed by Wilson and NRTL equations. Approbation of proposed approach with the use of different membranes was carried out for six binary systems: methanol – water, ethanol – water, propanol-1 – water, propanol-2 – water, butanol-1 – water and acetone – water. The compatibility between the experimental pervaporation data and the results of estimation are discussed.

AB - In present work the nonequilibrium thermodynamic advantages for pervaporation process approximation are discussed. The calculation model, which aligns nonequilibrium thermodynamic, pervaporation data and vapor–liquid equilibrium data, is presented. The approximation of vapor–liquid equilibrium data for feed mixtures was performed by Wilson and NRTL equations. Approbation of proposed approach with the use of different membranes was carried out for six binary systems: methanol – water, ethanol – water, propanol-1 – water, propanol-2 – water, butanol-1 – water and acetone – water. The compatibility between the experimental pervaporation data and the results of estimation are discussed.

KW - Pervaporation

KW - Nonequilibrium thermodynamics

KW - Membrane

KW - Selectivity prediction

U2 - 10.1016/j.cherd.2015.10.007

DO - 10.1016/j.cherd.2015.10.007

M3 - Article

VL - 104

SP - 669

EP - 680

JO - Chemical Engineering Research and Design

JF - Chemical Engineering Research and Design

SN - 0263-8762

ER -

ID: 3977969