✦ LIBER ✦

Vapor Liquid Equilibrium for Six Binary Systems of C 4 -Hydrocarbons + 2-Propanone

✍ Scribed by Pasanen, Matti; Zaytseva, Anna; Uusi-Kyyny, Petri; Pokki, Juha-Pekka; Pakkanen, Minna; Aittamaa, Juhani

Book ID: 126921337
Publisher: American Chemical Society
Year: 2006
Tongue: English
Weight: 73 KB
Volume: 51
Category: Article
ISSN: 0021-9568
DOI: 10.1021/je050403k

No coin nor oath required. For personal study only.

📜 SIMILAR VOLUMES

Vapor−Liquid Equilibrium in Binary Syste

Vapor−Liquid Equilibrium in Binary Systems Ethanol + C4 and C5 Hydrocarbons

✍ Verrazzi, A.; Kikic, I.; Garbers, P.; Barreau, A.; Le Roux, D. 📂 Article 📅 1999 🏛 American Chemical Society 🌐 English ⚖ 8 KB

Vapor−Liquid Equilibrium in Binary Syste

Vapor−Liquid Equilibrium in Binary Systems Ethanol + C4 and C5 Hydrocarbons

✍ Verrazzi, Andrea; Kikic, Ireneo; Garbers, Petra; Barreau, Alain; Le Roux, Domini 📂 Article 📅 1998 🏛 American Chemical Society 🌐 English ⚖ 52 KB

99/02495 Vapor—liquid equilibrium in bin

99/02495 Vapor—liquid equilibrium in binary systems ethanol + C4 and C5 hydrocarbons

📂 Article 📅 1999 🏛 Elsevier Science ⚖ 193 KB

In Japanese

Vapor-liquid equilibriums at 25.ETA. for

Vapor-liquid equilibriums at 25.ETA. for nine alcohol-hydrocarbon binary systems

✍ Hwang, Shuen-cheng; Robinson, Robert L. 📂 Article 📅 1977 🏛 American Chemical Society 🌐 English ⚖ 580 KB

Vapor-liquid equilibriums of binary syst

Vapor-liquid equilibriums of binary systems containing selected hydrocarbons with perfluorobenzene

✍ Chinikamala, Abid; Houth, George N.; Taylor, Z. Lowell 📂 Article 📅 1973 🏛 American Chemical Society 🌐 English ⚖ 366 KB

Predicting NRTL parameters for binary hy

Predicting NRTL parameters for binary hydrocarbon mixtures for calculating liquid—vapor equilibriums of multicomponent systems

✍ M.J. Huron; J. Vidal; L. Asselineau 📂 Article 📅 1976 🏛 Elsevier Science 🌐 English ⚖ 962 KB

Ah&w&The parameters of the NRTL method are fitted, for binary hydrocarbon systems, on the activity coefficients calculated by the Flory-Hildebrand method with binary coefficients ii, of deviation from the geometric mean assumption for cohesive energy densities (NRTL-FH parameters). For aromatic satu