Reaction and liquid-liquid distribution equilibria in oleic acid/methanol/methyl oleate/water system at 73°C

Journal of Chemical Engineering of Japan

Volumn 34, Issue 12, 2001, Pages 1479-1485

  Chen, Fuming ^a   Sun, Haifeng ^a   Naka, Yuji ^b   Kawasaki, Junjiro ^b  

^a TSINGHUA UNIVERSITY   (China)

^b TOKYO INSTITUTE OF TECHNOLOGY   (Japan)

Author keywords

Algorithm; Esterification; Extraction coupled reaction; Liquid liquid distribution equilibrium; Methyl oleate

Indexed keywords

ALGORITHMS; CATALYSTS; DEHYDRATION; ESTERIFICATION; ESTERS; EXTRACTION; ION EXCHANGE; METHANOL; PHASE EQUILIBRIA; POSITIVE IONS;

DISTRIBUTION EQUILIBRIA;

OLEIC ACID;

CATALYST; EQUILIBRIUM; LIQUID-LIQUID SEPARATION; WATER RECOVERY; YIELD;

EID: 0035544416     PISSN: 00219592     EISSN: None     Source Type: Journal    
DOI: 10.1252/jcej.34.1479     Document Type: Article

References (8)

1. The use of catalytically active pervaporation membranes in esterification reactions to simultaneously increase product yield, membrane permselectivity and flux
2. Use of ion-exchange membrane in a reactor for esterification of oleic acid and methanol at room temperature
3. The esterification of oleic acid with ethanol accompanied by membrane separation
4. Simultaneous chemical and phase equilibrium calculation
5. Phase equilibrium calculations for chemically reacting systems
6. UNIFAC parameter table for prediction of liquid-liquid equilibria
7. An algorithm for simultaneous chemical and phase equilibrium calculation