The excess molar enthalpies of [xCO2 + (1 − x){0.5CH3(CH2)4CH3 + 0.5CH3(CH2)10CH3}] at the temperatures (308.15, 323.15, 373.15, and 413.15) K and at the pressures 7.50 MPa and 12.50 MPa, and of {xCO2 + (1 − x)CH3(CH2)7CH3} at 373.15 K and 7.50 MPa and 12.50 MPa-Reference-Cited by-同舟云学术

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The excess molar enthalpies of [xCO2 + (1 − x){0.5CH3(CH2)4CH3 + 0.5CH3(CH2)10CH3}] at the temperatures (308.15, 323.15, 373.15, and 413.15) K and at the pressures 7.50 MPa and 12.50 MPa, and of {xCO2 + (1 − x)CH3(CH2)7CH3} at 373.15 K and 7.50 MPa and 12.50 MPa

Published:1991-10 Issue:10 Volume:23 Page:941-949
ISSN:0021-9614
Container-title:The Journal of Chemical Thermodynamics
language:en
Short-container-title:The Journal of Chemical Thermodynamics

Author:

Cordray D.R.,Gunderson L.D.,Oscarson J.L.,Izatt R.M.

Funder

Basic Energy Sciences

American Chemical Society

U.S. Department of Energy

American Chemical Society Petroleum Research Fund

Publisher

Elsevier BV

Subject

Physical and Theoretical Chemistry,General Materials Science,Atomic and Molecular Physics, and Optics

Reference16 articles.

1. An isothermal flow calorimeter designed for high temperature, high pressure operation

2. The effect of pressure on the excess enthalpies of cyclohexane + n-hexane at 298.15 K

3. The excess enthalpies of 10 (n-butane + alcohol) mixtures at 298.15 K

4. The excess enthalpies of (carbon dioxide + pentane) at 348.15, 373.15, 413.15, 470.15, and 573.15 K from 7.58 to 12.45 MPa

5. Heats of mixing in the critical region

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1. The impressive impact of including enthalpy and heat capacity of mixing data when parameterising equations of state. Application to the development of the E-PPR78 (Enhanced-Predictive-Peng-Robinson-78) model.;Fluid Phase Equilibria;2022-09

2. Enthalpy and Heat Capacity Changes on Mixing: Fundamental Aspects and Prediction by Means of the PPR78 Cubic Equation of State;Energy & Fuels;2013-10-17

3. Excess Enthalpy Data in Binary Systems Containing a Supercritical Fluid and Their Correlation;Journal of Chemical & Engineering Data;1998-07-03

4. Calculation of the thermodynamic properties of model mixtures by Monte Carlo simulation;Fluid Phase Equilibria;1995-03

5. Carbon dioxide CO2 + C9H20 Nonane;Binary Gaseous, Liquid, Near-Critical, and Supercritical Fluid Systems of Nonelectrolytes

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