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Phase diagrams for oil/methanol/ether mixtures
Author(s) -
Boocock David G. B.,
Konar Samir K.,
Sidi Hanif
Publication year - 1996
Publication title -
journal of the american oil chemists' society
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 0.512
H-Index - 117
eISSN - 1558-9331
pISSN - 0003-021X
DOI - 10.1007/bf02525453
Subject(s) - methanol , ether , chemistry , miscibility , organic chemistry , tetrahydrofuran , diethyl ether , soybean oil , food science , solvent , polymer
One‐phase transmethylations of vegetable oils with methanol to form methyl esters occur considerably faster than conventional two‐phase reactions. Addition of simple ethers is an efficient method for producing a single phase. Ternary phase diagrams have been determined at 23°C for oil/methanol/ether mixtures; these are useful when applying the one‐phase method across a wide range of conditions. Soybean, canola, palm, and coconut oils were used in combination with five ethers, namely, tetrahydrofuran (THF), 1,4‐dioxane (DO), diethyl ether (DE), diisopropyl ether (DI), and tert ‐butyl methyl ether (TBM). All five ethers can produce miscibility for all methanol/oil compositions. The ether/methanol volumetric ratios required for miscibility at a methanol/soybean or canola oil volumetric ratio of 0.20 (5.4 molar ratio) at 23°C are: THF, 1.15; DO, 1.60; DE, 1.38 DI, 1.57; and TBM, 1.57. For THF, this results in one‐phase mixtures that contain 65 vol% oil. Soybean and canola oil form identical diagrams. Palm oil requires slightly less ether at the lower methanol concentrations, but coconut oil requires considerably less across the whole concentration range. Acid‐catalyzed reactions, when performed at the boiling point of the most volatile component, require less ether than predicted from the diagrams.