VAPOR-LIQUID-EQUILIBRIA OF BINARY-MIXTURES CONTAINING METHYL TERT-BUTYL ETHER (MTBE) AND/OR SUBSTITUTION HYDROCARBONS AT 298.15 K AND 313.15 K

被引：59

作者：

LOZANO, LM ^{[1
]}

MONTERO, EA ^{[1
]}

MARTIN, MC ^{[1
]}

VILLAMANAN, MA ^{[1
]}

机构：

[1] UNIV VALLADOLID,ETS INGN IND,DEPT INGN ENERGET & FLUIDOMECAN,TERMODINAM LAB,E-47071 VALLADOLID,SPAIN

来源：

FLUID PHASE EQUILIBRIA | 1995年 / 110卷 / 1-2期

关键词：

EXPERIMENTS; DATA; VLE LOW PRESSURE; HYDROCARBONS; MTBE;

D O I：

10.1016/0378-3812(95)02756-5

中图分类号：

O414.1 [热力学];

学科分类号：

摘要：

An up-to-date high accuracy vapor-liquid equilibrium apparatus (Van Ness' type) for binary and ternary mixtures has been newly built and successfully tested. A program on thermodynamic characterization of binary and ternary mixtures of oxygenate additives and/or hydrocarbons substituting the main classes of constituents of a real gasoline is presented. Some of the early results are reported, discussed and compared with literature data. These systems are the binary mixtures cyclohexane + n-heptane, benzene + cyclohexane and methyl tert-buthyl ether (MTBE) + n-hexane, all have been measured at 313.15 K and the first of them at 298.15 K too.

引用

页码：219 / 230

页数：12

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