Patel-Teja cubic equation of state–A review of modifications and applications till 2022

PNP Ghoderao, M Narayan, VH Dalvi, HS Byun - Fluid Phase Equilibria, 2023 - Elsevier
Abstract The Patel-Teja equation of state (PT EOS) is extensively researched, modified, and
applied three-parameter cubic equation of state for the prediction of volumetric and …

High-pressure fluid-phase equilibria: Experimental methods and systems investigated (2000–2004)

R Dohrn, S Peper, JMS Fonseca - Fluid Phase Equilibria, 2010 - Elsevier
As a part of a series of reviews, a compilation of systems for which high-pressure phase-
equilibrium data were published between 2000 and 2004 is given. Vapor–liquid equilibria …

Benchmark database containing binary-system-high-quality-certified data for cross-comparing thermodynamic models and assessing their accuracy

JN Jaubert, Y Le Guennec… - Industrial & …, 2020 - ACS Publications
In the last two centuries, equations of state (EoSs) have become a key tool for the correlation
and prediction of thermodynamic properties of fluids. They not only can be applied to pure …

Global fluid phase equilibria and critical phenomena of selected mixtures using the crossover soft-SAFT equation

F Llovell, LF Vega - The Journal of Physical Chemistry B, 2006 - ACS Publications
We present here the extension of the crossover soft-statistical associating fluid theory (soft-
SAFT) equation of state to mixtures, as well as some illustrative applications of the …

Evaluation of the CO2 behavior in binary mixtures with alkanes, alcohols, acids and esters using the Cubic-Plus-Association Equation of State

MB Oliveira, AJ Queimada, GM Kontogeorgis… - The Journal of …, 2011 - Elsevier
Knowledge regarding the high pressure phase behavior of CO2 mixtures is of primary
importance for designing, operating and optimizing many industrial processes, such as …

Densities of 1-Propanol and 2-Propanol via a Vibrating Tube Densimeter from 313 to 363 K and up to 25 MPa

A Zúñiga-Moreno, LA Galicia-Luna - Journal of Chemical & …, 2002 - ACS Publications
PvT properties were determined in the liquid phase for 1-propanol and 2-propanol from 313
to 363 K and up to 25 MPa with an uncertainty lower than±0.05%. The calibration method of …

Experimental determination of the critical loci for {n-C6H14 or CO2+ alkan-1-ol} mixtures. Evaluation of their critical and subcritical behavior using PC-SAFT EoS

L Gil, ST Blanco, C Rivas, E Laga, J Fernández… - The Journal of …, 2012 - Elsevier
Vapor–liquid critical locus (x, Tc, Pc) has been determined, in the whole range of mole
fractions, for the systems {n-hexane+ methanol, or+ ethanol, or+ propan-1-ol, or+ butan-1-ol} …

Vapor–liquid equilibria and critical points of the CO2+ 1-hexanol and CO2+ 1-heptanol systems

O Elizalde-Solis, LA Galicia-Luna, SI Sandler… - Fluid phase …, 2003 - Elsevier
Vapor–liquid equilibria (VLE), vapor–liquid–liquid equilibria (VLLE) and critical point (CP)
data for the carbon dioxide+ 1-hexanol (at 324.56, 353.93, 397.78, 403.39, 431.82 and …

High-pressure vapor–liquid equilibria for CO2+ alkanol systems and densities of n-dodecane and n-tridecane

O Elizalde-Solis, LA Galicia-Luna… - Fluid Phase …, 2007 - Elsevier
An apparatus based on the static-analytic method was used to measure the vapor–liquid
equilibria (VLE) for CO2+ alkanol systems. Equilibrium measurements for the CO2+ 1 …

Effect of Lewis acid-base complexes between CO2 and alkanols on phase behavior at high pressure

BH Park, HY Shin, BS Lee - Journal of CO2 Utilization, 2021 - Elsevier
Due to the electropositivity of the carbon atom in CO 2 which results from its lower electron
density compared to that of the oxygen atom, CO 2 molecules can act either as proton …