Experimental Vapor–Liquid Equilibrium (<i>p</i>, <i>T</i>, <i>x</i>) Data for Binary Systems of Propane (1) in <i>n</i>-Decane, <i>n</i>-Undecane, <i>n</i>-Dodecane, and <i>n</i>-Tridecane (2)-Reference-Cited by-同舟云学术

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Experimental Vapor–Liquid Equilibrium (p, T, x) Data for Binary Systems of Propane (1) in n-Decane, n-Undecane, n-Dodecane, and n-Tridecane (2)

Published:2023-11-08 Issue:12 Volume:68 Page:3328-3337
ISSN:0021-9568
Container-title:Journal of Chemical & Engineering Data
language:en
Short-container-title:J. Chem. Eng. Data

Author:

Goni Mustapha U.¹²,Burgass Rod¹,Chapoy Antonin¹³^ORCID,Ahmadi Pezhman¹^ORCID

Affiliation:

1. Hydrates, Flow Assurance & Phase Equilibria Group, Institute of Petroleum Engineering, Heriot-Watt University, Edinburgh EH14 4AS, Scotland, U.K.

2. Department of Petroleum Engineering, Abubakar Tafawa Balewa University, Bauchi PMB 0248, Nigeria

3. MINES ParisTech, CTP-Centre Thermodynamique des Procédés, 35, Rue Saint Honoré, Fontainebleau 77305, France

Funder

Petroleum Technology Development Fund

Publisher

American Chemical Society (ACS)

Subject

General Chemical Engineering,General Chemistry

Link

https://pubs.acs.org/doi/pdf/10.1021/acs.jced.3c00486

Reference19 articles.

1. VLE predictions with the Peng–Robinson equation of state and temperature dependent kij calculated through a group contribution method

2. Bubble-Point Measurements of n-Propane + n-Decane Binary Mixtures with Comparisons of Binary Mixture Interaction Parameters for Linear Alkanes

3. Phase Equilibria in Hydrocarbon Systems. Volumetric and Phase Behavior of the Propane-n-Decane System.

4. Comparison of High-Pressure Vapor−Liquid Equilibria of Mixtures of CO2 or Propane with Nonane and C9 Alkylbenzenes

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1. Experimental (ρ,P,T) data of H2 + CH4 mixtures at temperatures from 278 to 398 K and pressures up to 56 MPa;International Journal of Hydrogen Energy;2024-05

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