Liquid-liquid equilibrium for the system n-heptane+o-xylene+triethylene glycol from 293.1 to 323.1 K

Chemical Engineering and Processing

Volumn 41, Issue 9, 2002, Pages 737-741

  Darwish, Naif A ^a  

^a UNITED ARAB EMIRATES UNIVERSITY   (United Arab Emirates)

Author keywords

Extraction; Liquid extraction; Liquid phase models; n Heptane; o Xylene; Triethylene glycol; UNIFAC

Indexed keywords

DATABASE SYSTEMS; EXTRACTION; GLYCOLS; HEPTANE; INDUSTRIAL APPLICATIONS; TERNARY SYSTEMS; XYLENE;

GROUP INTERACTION PARAMETERS;

PHASE EQUILIBRIA;

LIQUID-LIQUID EQUILIBRIUM; LIQUID-LIQUID EXTRACTION; PETROLEUM INDUSTRY; SOLVENT;

EID: 0036827224     PISSN: 02552701     EISSN: None     Source Type: Journal    
DOI: 10.1016/S0255-2701(01)00195-7     Document Type: Article

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