High pressure vapour-liquid equilibria of the binary and some of the ternary and multicomponent mixtures of the carbon dioxide + acetic anhydride + α-methylbenzyl alcohol + acetic acid + α-methylbenzyl acetate system. Experimental and modelling results

Fluid Phase Equilibria

Volumn 244, Issue 2, 2006, Pages 179-187

  Calvo, Lourdes ^a   de Loos, Theo W ^b  

^a UNIVERSIDAD COMPLUTENSE DE MADRID   (Spain)

^b DELFT UNIVERSITY OF TECHNOLOGY   (Netherlands)

Author keywords

Methylbenzyl acetate; Methylbenzyl alcohol; 1 Phenylethanol; Acetic acid; Acetic anhydride; Bubble point pressures; High pressure carbon dioxide; Modelling; Multicomponent mixtures; Peng Robinson equation of state; Styrallyl acetate; Vapour liquid equilibrium; Wong Sandier mixing rules

Indexed keywords

ACETIC ACID; BINARY MIXTURES; BUBBLES (IN FLUIDS); CARBON DIOXIDE; EQUATIONS OF STATE; PRESSURE EFFECTS;

Α-METHYLBENZYL ACETATE; Α-METHYLBENZYL ALCOHOL; 1-PHENYLETHANOL; ACETIC ANHYDRIDE; BUBBLE-POINT PRESSURES; HIGH PRESSURE CARBON DIOXIDE; MODELING; PENG-ROBINSON EQUATION OF STATE; STYRALLYL ACETATE; WONG-SANDIER MIXING RULES;

PHASE EQUILIBRIA;

ACETIC ACID; BINARY MIXTURES; BUBBLES (IN FLUIDS); CARBON DIOXIDE; EQUATIONS OF STATE; PHASE EQUILIBRIA; PRESSURE EFFECTS;

EID: 33745469524     PISSN: 03783812     EISSN: None     Source Type: Journal    
DOI: 10.1016/j.fluid.2006.04.011     Document Type: Article

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