Phase equilibria for separation of high boiling point organics from ionic liquids by supercritical CO2 or C3H8

Chemical Engineering Journal

Volumn 147, Issue 1, 2009, Pages 63-70

  Liu, Jie ^a   Sun, Xuewen ^a   Fu, Dongbao ^a   Zhao, Suoqi ^a  

^a CHINA UNIVERSITY OF PETROLEUM   (China)

Author keywords

Carbon dioxide; Dibenzothiophene (DBT); Extraction; Ionic liquid (IL); Naphthalene; Propane; Solubility; Supercritical (SC)

Indexed keywords

BATCH DATA PROCESSING; BOILING LIQUIDS; BOILING POINT; CARBON DIOXIDE; CARBON MONOXIDE; DISSOLUTION; EFFLUENT TREATMENT; ELECTRIC LOAD MANAGEMENT; EXTRACTION; INDUSTRIAL WASTE TREATMENT; IONIZATION OF LIQUIDS; IONS; LIQUIDS; NAPHTHALENE; OXIDES; PHASE EQUILIBRIA; PHASE SEPARATION; PROPANE; SOLUBILITY; SOLVENT EXTRACTION; SOLVENTS; SUPERCRITICAL FLUID EXTRACTION; SUPERCRITICAL FLUIDS; TERNARY ALLOYS; TERNARY SYSTEMS;

1 BUTYL 3 METHYLIMIDAZOLIUM HEXAFLUOROPHOSPHATE; 1 BUTYL 3 METHYLIMIDAZOLIUM TRIFLUOROMETHANESULFONATE; ASSOCIATION MODELS; BATCH PROCESSING; DIBENZOTHIOPHENE (DBT); FEED RATIOS; IONIC LIQUID (IL); LIQUID+LIQUID EQUILIBRIA (LLE); LONG TIME; ORGANICS; REACTION MEDIUM; ROOM-TEMPERATURE (RT); SUPERCRITICAL (SC); TERNARY PHASE; VOLUME EXPANSIVITY;

IONIC LIQUIDS;

EID: 58749092639     PISSN: 13858947     EISSN: None     Source Type: Journal    
DOI: 10.1016/j.cej.2008.11.017     Document Type: Article

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