Vapor-liquid equilibrium measurements for the ternary systems of CO 2 + n-hexane + n-decane and CO2 + n-octane + n-decane

Carmen Sánchez-García; Karla E. Vázquez-Hernández; Luis A. Galicia-Luna; Octavio Elizalde-Solis

doi:10.1021/ie201516g

Vapor-liquid equilibrium measurements for the ternary systems of CO ₂ + n-hexane + n-decane and CO₂ + n-octane + n-decane

Carmen Sánchez-García, Karla E. Vázquez-Hernández, Luis A. Galicia-Luna, Octavio Elizalde-Solis

Producción científica: Contribución a una revista › Artículo › revisión exhaustiva

8 Citas (Scopus)

Resumen

The experimental vapor-liquid equilibrium (VLE) data for two ternary systems containing CO₂ + n-alkane + n-decane were measured using an online static-analytic apparatus with a movable ROLSI sampler. The studied CO₂ + n-hexane + n-decane and CO₂ + n-octane + n-decane systems were measured at temperatures of (312.89, 342.50, and 376.20) K and (313.59, 344.28, and 373.49) K, respectively. The Peng-Robinson equation of state was used to predict the VLE data of the ternary systems from the temperature-independent interaction parameters of the binary systems.

Idioma original	Inglés
Páginas (desde-hasta)	12254-12258
Número de páginas	5
Publicación	Industrial and Engineering Chemistry Research
Volumen	50
N.º	21
DOI	https://doi.org/10.1021/ie201516g
Estado	Publicada - 2 nov. 2011
Publicado de forma externa	Sí

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title = "Vapor-liquid equilibrium measurements for the ternary systems of CO 2 + n-hexane + n-decane and CO2 + n-octane + n-decane",

abstract = "The experimental vapor-liquid equilibrium (VLE) data for two ternary systems containing CO2 + n-alkane + n-decane were measured using an online static-analytic apparatus with a movable ROLSI sampler. The studied CO2 + n-hexane + n-decane and CO2 + n-octane + n-decane systems were measured at temperatures of (312.89, 342.50, and 376.20) K and (313.59, 344.28, and 373.49) K, respectively. The Peng-Robinson equation of state was used to predict the VLE data of the ternary systems from the temperature-independent interaction parameters of the binary systems.",

author = "Carmen S{\'a}nchez-Garc{\'i}a and V{\'a}zquez-Hern{\'a}ndez, {Karla E.} and Galicia-Luna, {Luis A.} and Octavio Elizalde-Solis",

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doi = "10.1021/ie201516g",

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Vapor-liquid equilibrium measurements for the ternary systems of CO ₂ + n-hexane + n-decane and CO₂ + n-octane + n-decane. / Sánchez-García, Carmen; Vázquez-Hernández, Karla E.; Galicia-Luna, Luis A. et al.
En: Industrial and Engineering Chemistry Research, Vol. 50, N.º 21, 02.11.2011, p. 12254-12258.

Producción científica: Contribución a una revista › Artículo › revisión exhaustiva

TY - JOUR

T1 - Vapor-liquid equilibrium measurements for the ternary systems of CO 2 + n-hexane + n-decane and CO2 + n-octane + n-decane

AU - Sánchez-García, Carmen

AU - Vázquez-Hernández, Karla E.

AU - Galicia-Luna, Luis A.

AU - Elizalde-Solis, Octavio

PY - 2011/11/2

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AB - The experimental vapor-liquid equilibrium (VLE) data for two ternary systems containing CO2 + n-alkane + n-decane were measured using an online static-analytic apparatus with a movable ROLSI sampler. The studied CO2 + n-hexane + n-decane and CO2 + n-octane + n-decane systems were measured at temperatures of (312.89, 342.50, and 376.20) K and (313.59, 344.28, and 373.49) K, respectively. The Peng-Robinson equation of state was used to predict the VLE data of the ternary systems from the temperature-independent interaction parameters of the binary systems.

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