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Vapor–liquid equilibrium - Wikiwand
![PDF] Vapor–Liquid Equilibrium Data for the Carbon Dioxide (CO2) + 1,1,1,3,3-Pentafluorobutane (R365mfc) System at Temperatures from 283.15 to 337.15 K | Semantic Scholar](https://d3i71xaburhd42.cloudfront.net/41236103d2b9c81bab8dfe341d7be95b4e6fb18d/14-Table3-1.png "PDF] Vapor–Liquid Equilibrium Data for the Carbon Dioxide (CO2) + 1,1,1,3,3-Pentafluorobutane (R365mfc) System at Temperatures from 283.15 to 337.15 K | Semantic Scholar")
PDF] Vapor–Liquid Equilibrium Data for the Carbon Dioxide (CO2) + 1,1,1,3,3-Pentafluorobutane (R365mfc) System at Temperatures from 283.15 to 337.15 K | Semantic Scholar
Density and Phase Behavior of the CO2 + Methylbenzene System in Wide Ranges of Temperatures and Pressures | Industrial & Engineering Chemistry Research
High-Pressure Densities and Excess Molar Volumes for the Binary Mixture of Carbon Dioxide and Hydrogen Sulfide at T = 343–397 K | Journal of Chemical & Engineering Data
Vapor-liquid equilibrium, liquid density and excess enthalpy of the carbon dioxide+acetone mixture: Experimental measurements and correlations - ScienceDirect
New compact Equations for the Compressibility Factor Z and Density of Liquid and Vapor Carbon Dioxide | Chem-Eng-Musings
Vapor-Liquid Equilibrium Ideal Solution - YouTube
![PDF] Vapor–Liquid Equilibrium Data for the Carbon Dioxide (CO2) + 1,1,1,3,3-Pentafluorobutane (R365mfc) System at Temperatures from 283.15 to 337.15 K | Semantic Scholar](https://d3i71xaburhd42.cloudfront.net/41236103d2b9c81bab8dfe341d7be95b4e6fb18d/25-Figure5-1.png "PDF] Vapor–Liquid Equilibrium Data for the Carbon Dioxide (CO2) + 1,1,1,3,3-Pentafluorobutane (R365mfc) System at Temperatures from 283.15 to 337.15 K | Semantic Scholar")
PDF] Vapor–Liquid Equilibrium Data for the Carbon Dioxide (CO2) + 1,1,1,3,3-Pentafluorobutane (R365mfc) System at Temperatures from 283.15 to 337.15 K | Semantic Scholar
Vapor-liquid equilibrium, liquid density and excess enthalpy of the carbon dioxide+acetone mixture: Experimental measurements and correlations - ScienceDirect
VAPOR-LIQUID EQUILIBRIUM DATA FOR CO2+ DIMETHYLFORMAMIDE | Download Table
![PDF] Vapor–Liquid Equilibrium Data for the Carbon Dioxide (CO2) + 1,1,1,3,3-Pentafluorobutane (R365mfc) System at Temperatures from 283.15 to 337.15 K | Semantic Scholar](https://d3i71xaburhd42.cloudfront.net/41236103d2b9c81bab8dfe341d7be95b4e6fb18d/21-Figure1-1.png "PDF] Vapor–Liquid Equilibrium Data for the Carbon Dioxide (CO2) + 1,1,1,3,3-Pentafluorobutane (R365mfc) System at Temperatures from 283.15 to 337.15 K | Semantic Scholar")
PDF] Vapor–Liquid Equilibrium Data for the Carbon Dioxide (CO2) + 1,1,1,3,3-Pentafluorobutane (R365mfc) System at Temperatures from 283.15 to 337.15 K | Semantic Scholar
PDF) PVT properties of 1-propanol in the critical and supercritical regions | Ilmutdin Abdulagatov - Academia.edu
![PDF] Viscosity of CO2-rich mixtures from 243 K to 423 K at pressures up to 155 MPa: New experimental viscosity data and modelling](https://www.researchgate.net/profile/Mahmoud-Nazeri-3/publication/321034612/figure/tbl2/AS:668724877094913@1536447843019/Compositions-of-the-multi-component-mixtures-in-mol-with-the-expanded-uncertainties_Q320.jpg "PDF] Viscosity of CO2-rich mixtures from 243 K to 423 K at pressures up to 155 MPa: New experimental viscosity data and modelling")
PDF] Viscosity of CO2-rich mixtures from 243 K to 423 K at pressures up to 155 MPa: New experimental viscosity data and modelling
Vapor-liquid equilibrium, liquid density and excess enthalpy of the carbon dioxide+acetone mixture: Experimental measurements and correlations - ScienceDirect
New Equation for Calculating Enthalpy of saturated Liquid Carbon Dioxide ( CO2) | Chem-Eng-Musings
Density and Phase Behavior of the CO2 + Methylbenzene System in Wide Ranges of Temperatures and Pressures | Industrial & Engineering Chemistry Research
PDF) Solucionario Smith | luis perez - Academia.edu
Pentane - Density and Specific Weight vs. Temperature and Pressure
Density and Phase Behaviour of (CO2 + Methylbenzene) in Wide Ranges of Temperatures and Pressures
PVT, saturated liquid density and vapor-pressure measurements of main components of the biofuels at high temperatures and high pressures: Methyl palmitate - ScienceDirect
High-Pressure Densities and Excess Molar Volumes for the Binary Mixture of Carbon Dioxide and Hydrogen Sulfide at T = 343–397 K | Journal of Chemical & Engineering Data
Density and Phase Behavior of the CO2 + Methylbenzene System in Wide Ranges of Temperatures and Pressures | Industrial & Engineering Chemistry Research
Density Characteristics of a Multicomponent CO2/N2/CH4 Ternary Mixture at Temperature of 293.15–353.15 K and Pressure of 0.5–18 MPa | Journal of Chemical & Engineering Data
