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Experimental and Computational Study on Liquid-Liquid Equilibrium in Ternary Systems of gamma-Valerolactone, Toluene, and Hydrocarbons

Identifikátory výsledku

  • Kód výsledku v IS VaVaI

    <a href="https://www.isvavai.cz/riv?ss=detail&h=RIV%2F60461373%3A22340%2F16%3A43900372" target="_blank" >RIV/60461373:22340/16:43900372 - isvavai.cz</a>

  • Výsledek na webu

    <a href="http://pubs.acs.org/doi/abs/10.1021/acs.jced.5b00611" target="_blank" >http://pubs.acs.org/doi/abs/10.1021/acs.jced.5b00611</a>

  • DOI - Digital Object Identifier

    <a href="http://dx.doi.org/10.1021/acs.jced.5b00611" target="_blank" >10.1021/acs.jced.5b00611</a>

Alternativní jazyky

  • Jazyk výsledku

    angličtina

  • Název v původním jazyce

    Experimental and Computational Study on Liquid-Liquid Equilibrium in Ternary Systems of gamma-Valerolactone, Toluene, and Hydrocarbons

  • Popis výsledku v původním jazyce

    ?-Valerolactone is a biomass-derived compound widely applicable in chemical industry, especially as a solvent, additive to fuels or precursor for other chemicals. In contrast with the industrial importance of ?-valerolactone, there is an insufficient number of mixture phase-equilibria in the literature. Therefore the aim of this work was to measure liquid-liquid equilibrium data for ternary systems ?-valerolactone + toluene + hydrocarbon (hydrocarbons were n-heptane, n-decane, n-dodecane, and cyclohexane) by the direct analytical method at 298.15 K and 0.1 MPa. The obtained experimental data were processed and correlated by the nonrandom two-liquid (NRTL) model. The NRTL binary parameters between ?-valerolactone and toluene were evaluated from the measured ternary liquid-liquid equilibrium data while the other binary parameters were obtained by regression of binary liquid-liquid equilibrium data or vapor-liquid equilibrium and excess enthalpy data taken from literature. The predictive performance of the perturbed-chain induced-polar SAFT (PCIP-SAFT) equation of state was also studied for the ternary systems. Based on the pure-components data only, the PCIP-SAFT predictions can be considered as relatively successful because of the ability of PCIP-SAFT to take into account the dipolar interactions.

  • Název v anglickém jazyce

    Experimental and Computational Study on Liquid-Liquid Equilibrium in Ternary Systems of gamma-Valerolactone, Toluene, and Hydrocarbons

  • Popis výsledku anglicky

    ?-Valerolactone is a biomass-derived compound widely applicable in chemical industry, especially as a solvent, additive to fuels or precursor for other chemicals. In contrast with the industrial importance of ?-valerolactone, there is an insufficient number of mixture phase-equilibria in the literature. Therefore the aim of this work was to measure liquid-liquid equilibrium data for ternary systems ?-valerolactone + toluene + hydrocarbon (hydrocarbons were n-heptane, n-decane, n-dodecane, and cyclohexane) by the direct analytical method at 298.15 K and 0.1 MPa. The obtained experimental data were processed and correlated by the nonrandom two-liquid (NRTL) model. The NRTL binary parameters between ?-valerolactone and toluene were evaluated from the measured ternary liquid-liquid equilibrium data while the other binary parameters were obtained by regression of binary liquid-liquid equilibrium data or vapor-liquid equilibrium and excess enthalpy data taken from literature. The predictive performance of the perturbed-chain induced-polar SAFT (PCIP-SAFT) equation of state was also studied for the ternary systems. Based on the pure-components data only, the PCIP-SAFT predictions can be considered as relatively successful because of the ability of PCIP-SAFT to take into account the dipolar interactions.

Klasifikace

  • Druh

    J<sub>x</sub> - Nezařazeno - Článek v odborném periodiku (Jimp, Jsc a Jost)

  • CEP obor

    CF - Fyzikální chemie a teoretická chemie

  • OECD FORD obor

Návaznosti výsledku

  • Projekt

  • Návaznosti

    S - Specificky vyzkum na vysokych skolach

Ostatní

  • Rok uplatnění

    2016

  • Kód důvěrnosti údajů

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

Údaje specifické pro druh výsledku

  • Název periodika

    Journal of Chemical Engineering Data

  • ISSN

    0021-9568

  • e-ISSN

  • Svazek periodika

    61

  • Číslo periodika v rámci svazku

    1

  • Stát vydavatele periodika

    US - Spojené státy americké

  • Počet stran výsledku

    7

  • Strana od-do

    391-397

  • Kód UT WoS článku

    000368564600044

  • EID výsledku v databázi Scopus