Phase equilibrium studying for the supercritical fluid extraction process using carbon dioxide solvent with 1.35 mole ratio of octane to ethanol mixture

Chemical Engineering Journal

Volumn 140, Issue 1-3, 2008, Pages 173-182

  Kassim, K M ^a   Davarnejad, R ^a   Zainal, A ^a  

^a SCHOOL OF CHEMICAL ENGINEERING   (Malaysia)

Author keywords

CO2 solvent; Ethanol octane; Immiscibility; Regular solution theory; Supercritical extraction

Indexed keywords

CARBON DIOXIDE; ETHANOL; SOLUBILITY; SOLVENTS; SUPERCRITICAL FLUID EXTRACTION;

ETHANOL-OCTANE; REGULAR SOLUTION THEORY; SUPERCRITICAL EXTRACTION;

PHASE EQUILIBRIA;

CARBON DIOXIDE; ETHANOL; PHASE EQUILIBRIA; SOLUBILITY; SOLVENTS; SUPERCRITICAL FLUID EXTRACTION;

INSECTIVORA;

EID: 44049085215     PISSN: 13858947     EISSN: None     Source Type: Journal    
DOI: 10.1016/j.cej.2007.09.040     Document Type: Article

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