Thermodynamic properties of propane. III. A reference equation of state for temperatures from the melting line to 650 K and pressures up to 1000 MPa
EW Lemmon, MO McLinden… - Journal of Chemical & …, 2009 - ACS Publications
An equation of state is presented for the thermodynamic properties of propane that is valid
for temperatures from the triple point temperature (85.525 K) to 650 K and for pressures up …
for temperatures from the triple point temperature (85.525 K) to 650 K and for pressures up …
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 …
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 …
and prediction of thermodynamic properties of fluids. They not only can be applied to pure …
Experimental measurements and correlation of vapor–liquid equilibrium and critical data for the CO2+ R1234yf and CO2+ R1234ze (E) binary mixtures
Isothermal (Pxy) vapor–liquid equilibrium data for the CO 2+ 2, 3, 3, 3-tetrafluoroprop-1-ene
(R1234yf) binary system are reported at seven temperatures ranging from 283.15 K to …
(R1234yf) binary system are reported at seven temperatures ranging from 283.15 K to …
Vapor–liquid equilibrium and molecular simulation data for carbon dioxide (CO2)+ trans-1, 3, 3, 3-tetrafluoroprop-1-ene (R-1234ze (E)) mixture at temperatures from …
S Wang, R Fauve, C Coquelet, A Valtz… - International Journal of …, 2019 - Elsevier
Abstract Isothermal Vapor–Liquid Equilibrium (VLE) data for the binary mixture of CO 2+ R-
1234ze (E)(trans-1, 3, 3, 3-tetrafluoroprop-1-ene) were measured using a static-analytic …
1234ze (E)(trans-1, 3, 3, 3-tetrafluoroprop-1-ene) were measured using a static-analytic …
The full pressure–temperature phase envelope of a mixture in 1000 microfluidic chambers
Knowing the thermodynamic state of complex mixtures—liquid, gas, supercritical or two‐
phase—is essential to industrial chemical processes. Traditionally, phase diagrams are …
phase—is essential to industrial chemical processes. Traditionally, phase diagrams are …
Fluid-phase-equilibrium prediction of fluorocompound-containing binary systems with the predictive E-PPR78 model
In order to reduce the overall emissions of greenhouse gases and to be in compliance with
the current environmental regulations, a new class of refrigerants has appeared. Such …
the current environmental regulations, a new class of refrigerants has appeared. Such …
On the anomalous composition dependence of viscosity and surface tension in refrigerant blends
Abstract The Polar PC-SAFT equation of state coupled with DGT and excess entropy scaling
was applied to predict the phase, interfacial and transport properties of refrigerant blends …
was applied to predict the phase, interfacial and transport properties of refrigerant blends …
Experimental determination of phase diagram and modeling: Application to refrigerant mixtures
C Coquelet, D Richon - International journal of refrigeration, 2009 - Elsevier
Accurate knowledge of phase diagrams is an essential step for optimized chemical
engineering design and effective solution of engineering-related problem. As an example of …
engineering design and effective solution of engineering-related problem. As an example of …
Vapor–liquid equilibrium data for the carbon dioxide (CO2)+ difluoromethane (R32) system at temperatures from 283.12 to 343.25 K and pressures up to 7.46 MPa
Isothermal vapor–liquid equilibrium (VLE) data have been measured for the binary system
carbon dioxide (CO2)+ difluoromethane (R32) at eight temperatures between 283.12 and …
carbon dioxide (CO2)+ difluoromethane (R32) at eight temperatures between 283.12 and …