Vapor–liquid equilibria for supercritical carbon dioxide+butanol systems at 313.2K

Author:

Hiaki Toshihiko,Miyagi Hideki,Tsuji Tomoya,Hongo Masaru

Publisher

Elsevier BV

Subject

Physical and Theoretical Chemistry,Condensed Matter Physics,General Chemical Engineering

Reference7 articles.

1. Vapor–liquid equilibrium for carbon dioxide: 1-butanol at high pressure;Ishihara;J. Chem. Eng. Data,1996

2. M.B. King, D.A. Alderson, F.H. Fallah, K.M. Kassim, J.R. Sheldon, R.S. Mahmud, Some vapour/liquid and vapor/solid equilibrium measurements of relevance for supercritical extraction operations, and their correlation, in: M.E. Paulaitis, J.M.L. Penninger, R.D. Gray, Jr, P. Davidson (Eds.), Chemical Engineering at Supercritical Fluid Conditions, Ann Arbor, MI, 1983, p. 31.

3. Mutual solubility of 1-butanol and carbon dioxide, ethene, ethane, or propane at a reduced supercritical solvent temperature of 1.03;Jensen;J. Supercrit. Fluids,1994

4. Vapor–liquid equilibria in the carbon dioxide+ethanol and carbon dioxide+1-butanol systems;Jennings;J. Chem. Eng. Data,1991

5. Liquid–liquid–vapor phase equilibrium behavior of certain binary carbon dioxide+n-alkanol mixtures;Lam;Fluid Phase Equilib.,1990

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