✦ LIBER ✦

Vapor−Liquid Equilibria for the Binary System Hexane + 1,1-Dimethylpropyl Methyl Ether at 298.15, 308.15, 318.15, and 328.15 K

✍ Scribed by del Río, Armando; Coto, Baudilio; Pando, Concepción; Renuncio, Juan A. R.

Book ID: 126125761
Publisher: American Chemical Society
Year: 2002
Tongue: English
Weight: 72 KB
Volume: 41
Category: Article
ISSN: 0888-5885
DOI: 10.1021/ie0106128

No coin nor oath required. For personal study only.

📜 SIMILAR VOLUMES

Vapor–liquid equilibria for the binary s

Vapor–liquid equilibria for the binary system hexan-1-ol + tert-butyl methyl ether (MTBE) at 298.15, 318.15, and 338.15 K

✍ Julieta Jiménez de Llano; Luisa Segade; Eulogio Jiménez; Armando del Rı́o; Juan 📂 Article 📅 2003 🏛 Elsevier Science 🌐 English ⚖ 81 KB

Vapor–liquid equilibria for the binary s

Vapor–liquid equilibria for the binary system 2,2−dimethylbutane + 1,1−dimethylpropyl methyl ether (TAME) at 298.15, 318.15, and 338.15 K

✍ Armando del Rı́o; Baudilio Coto; Juan A.R Renuncio; Concepción Pando 📂 Article 📅 2004 🏛 Elsevier Science 🌐 English ⚖ 111 KB

Vapor−Liquid Equilibria for the Binary S

Vapor−Liquid Equilibria for the Binary System Difluoromethane (HFC-32) + Propane (HC-290) at Seven Temperatures [(268.15, 278.15, 283.15, 288.15, 298.15, 308.15, and 318.15) K]

✍ Lee, Byung Gwon; Yang, Woong-Jo; Kim, Jae-Duck; Lim, Jong Sung 📂 Article 📅 2003 🏛 American Chemical Society 🌐 English ⚖ 99 KB

Vapor−Liquid Equilibria in Ethanol + (Bu

Vapor−Liquid Equilibria in Ethanol + (Butyl Methyl Ether or Dipropyl Ether) Systems at 308.15, 323.15, and 338.15 K

✍ Hofman, Tadeusz; Sporzyński, Andrzej; Gołdon, Andrzej 📂 Article 📅 2000 🏛 American Chemical Society 🌐 English ⚖ 49 KB

Excess enthalpies of (methyl 1,1-dimethy

Excess enthalpies of (methyl 1,1-dimethylpropyl ether + hexane + decane or dodecane) at the temperature 298.15 K

✍ Andjela Knežević-Stevanović; Zhang-Li Jin; George C. Benson; Benjamin C.-Y. Lu 📂 Article 📅 1995 🏛 Elsevier Science 🌐 English ⚖ 522 KB

Measurements of excess molar enthalpies at the temperature 298.15 K are reported for the ternary mixtures {x1C2H5C )n-2CH3} with n = 10 and 12. Smooth representations of the results are presented and used to construct constant-enthalpy contours on Roozeboom diagrams. Comparisons of the experimental

Liquid extraction equilibria of type 2:

Liquid extraction equilibria of type 2: (tert-amyl methyl ether + 1-octonal + water) atT=(298.15 and 308.15) K

✍ Alberto Arce; Manuel Blanco 📂 Article 📅 1998 🏛 Elsevier Science 🌐 English ⚖ 144 KB

## Ž . Ž Experimental liquid q liquid equilibrium data for tert-amyl methyl ether q 1-octanol q . Ž . water at T s 298.15 and 308.15 K were satisfactorily fitted with UNIQUAC, TK-Wilson, and NRTL equations, and predicted by the UNIFAC group contribution method.