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 …
equilibrium data were published between 2000 and 2004 is given. Vapor–liquid equilibria …
Global fluid phase equilibria and critical phenomena of selected mixtures using the crossover soft-SAFT equation
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 …
SAFT) equation of state to mixtures, as well as some illustrative applications of the …
Condensed-phase ethanol conversion to higher alcohols
TL Jordison, CT Lira, DJ Miller - Industrial & Engineering …, 2015 - ACS Publications
Higher alcohols (C4+) can be formed from ethanol via condensation pathways collectively
known as Guerbet reactions. Most prior Guerbet reaction studies involve vapor-phase …
known as Guerbet reactions. Most prior Guerbet reaction studies involve vapor-phase …
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 …
to 363 K and up to 25 MPa with an uncertainty lower than±0.05%. The calibration method of …
Liquid–liquid behaviour of ionic liquid–1-butanol–water and high pressure CO 2-induced phase changes
The liquid–liquid equilibrium of the [C4mim][NTf2]–1-butanol system presents upper critical
solution temperature (UCST) behaviour. We report the influence of added water as well as …
solution temperature (UCST) behaviour. We report the influence of added water as well as …
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} …
fractions, for the systems {n-hexane+ methanol, or+ ethanol, or+ propan-1-ol, or+ butan-1-ol} …
Compressed liquid densities of carbon dioxide+ ethanol mixtures at four compositions via a vibrating tube densimeter up to 363 K and 25 MPa
A Zúñiga-Moreno, LA Galicia-Luna - Journal of Chemical & …, 2002 - ACS Publications
PvT properties in a single phase were determined for carbon dioxide+ ethanol mixtures at
four compositions from 313 to 363 K and up to 25 MPa with an uncertainty less than (±0.04 …
four compositions from 313 to 363 K and up to 25 MPa with an uncertainty less than (±0.04 …
CO2-binding organic liquids for high pressure CO2 absorption: Statistical mixture design approach and thermodynamic modeling of CO2 solubility using LJ-Global …
A Hedayati, F Feyzi - Journal of Molecular Liquids, 2021 - Elsevier
CO 2-binding organic liquids (CO 2-BOLs) or switchable ionic liquids (SILs) are switchable
polarity solvents (SPS) that can be used as non-aqueous, energy efficient solvents for CO 2 …
polarity solvents (SPS) that can be used as non-aqueous, energy efficient solvents for CO 2 …
Vapor–liquid equilibria and critical points of the CO2+ 1-hexanol and CO2+ 1-heptanol systems
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 …
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 …
equilibria (VLE) for CO2+ alkanol systems. Equilibrium measurements for the CO2+ 1 …