Measurement and prediction of the bubble/dew point locus in the near-critical region and of the compressed fluid densities of the methanecarbon dioxide-n-butane ternary system-Reference-Cited by-同舟云学术

Measurement and prediction of the bubble/dew point locus in the near-critical region and of the compressed fluid densities of the methanecarbon dioxide-n-butane ternary system

Published:1995-04 Issue:2 Volume:105 Page:259-271
ISSN:0378-3812
Container-title:Fluid Phase Equilibria
language:en
Short-container-title:Fluid Phase Equilibria

Author:

Pan H.-Q,Yang T,Guo T.-M

Publisher

Elsevier BV

Subject

Physical and Theoretical Chemistry,General Physics and Astronomy,General Chemical Engineering

Reference16 articles.

1. Vapor-liquid equilibria for the binary systems of nitrogen, carbon dioxide, and n-butane at temperatures form 220 to 344 K;Brown;Fluid Phase Equilibria,1989

2. Data compilation tables of properties of pure compounds;Daubert,1985

3. Liquid-vapor equilibria at 250.00 K for systems containing methane, ethane, and carbon dioxide;Davalos;J. Chem. Eng. Data,1976

4. Experimental and modeling studies on the phase behavior of high H2S-content natural gas mixtures;Gu;Fluid Phase Equilibria,1993

5. An accurate equation of state for carbon dioxide;Huang;J. Chem. Eng. Jpn.,1985

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