Subatmospheric <i>P-T-x-y</i> Measurements and Modeling for the Butan-1-ol/Butan-2-ol + Oct-1-ene Systems in the Range of <i>T</i> = (323.2–363.2) K

The phase behaviors of alkene-oxygenate mixtures are highly nonideal and not well studied in the literature. To expand the available literature for these systems, isothermal vapor–liquid equilibrium (VLE) data were measured for the butan-1-ol/butan-2-ol + oct-1-ene systems using the dynamic circulation method. The measurements were conducted at three temperatures in the subatmospheric range (T = 333.2, 343.2, 363.2) K, and complex azeotropic behavior was observed. The data were fit using the γ-Φ formulation to the NRTL and UNIQUAC activity coefficient models combined with the virial equation of state using parameters from the Hayden-O’Connell correlation. A temperature-dependent activity coefficient model parameter term was used. The NRTL model combination generally resulted in a superior fit of the VLE data when considering deviations in pressure and vapor composition. This is attributed to the model strength and the additional regressed nonrandomness parameter. The VLE data were found to be thermodynamically consistent according to the Area, Point, and Infinite dilution tests.

Authors

Institutions

Publication Details

Journal
Journal of Chemical & Engineering Data
Published
2026-03-11
DOI
https://doi.org/10.1021/acs.jced.5c00785
Primary Topic
Phase Equilibria and Thermodynamics
Type
article
Field-Weighted Citation Impact
0.00
Controls
|||
ALL TIME
JAN
FEB
MAR
APR
MAY
JUN
JUL
AUG
SEP
OCT
article

Subatmospheric P-T-x-y Measurements and Modeling for the Butan-1-ol/Butan-2-ol + Oct-1-ene Systems in the Range of T = (323.2–363.2) K

Kuveneshan Moodley
Journal of Chemical & Engineering Data
Phase Equilibria and Thermodynamics
article

Subatmospheric P-T-x-y Measurements and Modeling for the Butan-1-ol/Butan-2-ol + Oct-1-ene Systems in the Range of T = (323.2–363.2) K

Kuveneshan Moodley
article en

Abstract

The phase behaviors of alkene-oxygenate mixtures are highly nonideal and not well studied in the literature. To expand the available literature for these systems, isothermal vapor–liquid equilibrium (VLE) data were measured for the butan-1-ol/butan-2-ol + oct-1-ene systems using the dynamic circulation method. The measurements were conducted at three temperatures in the subatmospheric range (T = 333.2, 343.2, 363.2) K, and complex azeotropic behavior was observed. The data were fit using the γ-Φ formulation to the NRTL and UNIQUAC activity coefficient models combined with the virial equation of state using parameters from the Hayden-O’Connell correlation. A temperature-dependent activity coefficient model parameter term was used. The NRTL model combination generally resulted in a superior fit of the VLE data when considering deviations in pressure and vapor composition. This is attributed to the model strength and the additional regressed nonrandomness parameter. The VLE data were found to be thermodynamically consistent according to the Area, Point, and Infinite dilution tests.

Journal of Chemical & Engineering Data
University of KwaZulu-Natal (ZA)
Openalex Percentile: Top 26%
Phase Equilibria and Thermodynamics
AI Navigator

Ask Laika to Summarize, Analyze, and Connect papers live on the map.

Summarize Papers & Methodologies

Extract key findings, datasets, and comparative methods across publications.

Benchmark Rankings & Visual Analytics

Rank top research institutions, authors, funders, topics, and journals by Field-Weighted Citation Impact (FWCI) and paper volume with instant charts.

Connect Distant Disciplines

Bridge topological clusters on the map to find hidden collaborative intersections.