(Vapour + liquid) equilibria for (methanol + butyl acetate), (vinyl acetate + butyl acetate), (methanol + isobutyl acetate), and (vinyl acetate + isobutyl acetate)
✍ Scribed by J.M. Resa; C. González; B. Moradillo; J. Lanz
- Publisher
- Elsevier Science
- Year
- 1998
- Tongue
- English
- Weight
- 184 KB
- Volume
- 30
- Category
- Article
- ISSN
- 0021-9614
No coin nor oath required. For personal study only.
✦ Synopsis
Isobaric vapour q liquid equilibria were determined at p s 101.3 kPa for methanol q butyl . Ž . Ž . Ž acetate , methanol q isobutyl acetate , vinyl acetate q butyl acetate , and vinyl acetate q . isobutyl acetate . The thermodynamic consistency of the experimental data was checked by using a modified Dechema test. The activity coefficients were correlated with Margules, van Laar, Wilson, NRTL, and Wilson equations. Among the solvents chosen as potential extractive distillation entrainers, none shows azeotropy. It was found more appropriate to use butyl acetate as solvent for the extractive distillation from an economical perspective.
📜 SIMILAR VOLUMES
Isobaric (vapour + liquid) equilibria were determined at p = 101.3 kPa for {methanol + allyl acetate (3-acetoxy-1-propene)} and {vinyl acetate (1-acetoxyethylene) + allyl acetate}. The thermodynamic consistency of the experimental data was determined with a modified Dechema test. The activity coeffi
The design of high-performance pervaporation membranes for the selective removal of ethanol from ethyl t-butyl ether (ETBE) was performed by using the polymer blending method. Binary blends of cellulose acetate or cellulose triacetate with a specific copolymer, poly(vinyl pyrrolidone-co-vinyl acetat