High-pressure phase equilibrium of the ternary system carbon dioxide + water + acetic acid at temperatures from 313 to 353 K

Journal of Supercritical Fluids

Volumn 32, Issue 1-3, 2004, Pages 15-25

  Bamberger, A ^a,b   Sieder, G ^a,c   Maurer, G ^a  

^a University of Koblenz Landau   (Germany)

^b BAYER AG   (Germany)

^c BASF SE   (Germany)

Author keywords

Acetic acid; Carbon dioxide; Dimerization; Peng Robinson equation of state; Ternary high pressure equilibrium; Water

Indexed keywords

ACETIC ACID; CARBON DIOXIDE; DIMERIZATION; EQUATIONS OF STATE; HIGH PRESSURE EFFECTS; MIXING; PHASE EQUILIBRIA; WATER;

BINARY SUB SYSTEMS; CONTINUOUS FLOW TECHNIQUE; HIGH-PRESSURE PHASE EQUILIBRIUM; PENG-ROBINSON EQUATION;

TERNARY SYSTEMS;

ACETIC ACID; CARBON DIOXIDE; WATER;

ARTICLE; CALCULATION; CHEMICAL ANALYSIS; CHEMICAL INTERACTION; DIMERIZATION; EXPERIMENT; FLOW MEASUREMENT; LIQUID; PARAMETER; PREDICTION; PRESSURE; RELIABILITY; TEMPERATURE; VAPOR;

EID: 14344261354     PISSN: 08968446     EISSN: None     Source Type: Journal    
DOI: 10.1016/j.supflu.2003.12.014     Document Type: Article

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