ISOTHERMAL VAPOR-LIQUID-EQUILIBRIA AND EXCESS VOLUMES IN THE METHANOL-ALIPHATIC ETHER SYSTEMS

被引：27
作者：
FARKOVA, J
LINEK, J
WICHTERLE, I
机构：
[1] Institute of Chemical Process Fundamentals, Academy of Sciences of the Czech Republic
来源：
FLUID PHASE EQUILIBRIA | 1995年 / 109卷 / 01期
关键词：
EXPERIMENTS; DATA; VLE LOW PRESSURE; EXCESS VOLUME; METHANOL; ALIPHATIC ETHER;
D O I：
10.1016/0378-3812(95)02710-V
中图分类号：
O414.1 [热力学];
学科分类号：
摘要：
Vapour-liquid equilibria were measured isothermally in the binary systems containing methanol with butyl methyl ether, tert-butyl methyl ether, ethyl propyl ether, diisopropyl ether and butyl ethyl ether. The data were correlated using the Redlich-Kister, Wilson, and NRTL equations within the accuracy of experimental errors. The excess free volumes of liquid mixtures were determined and correlated at 25 degrees C.
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页码：53 / 65
页数：13
相关论文
共 17 条
  • [1] Aim K., 1980, J CHEM ENG DATA, V25, P100
  • [2] SATURATED VAPOUR PRESSURES OF SOME ETHERS
    CIDLINSKY, J
    POLAK, J
    [J]. COLLECTION OF CZECHOSLOVAK CHEMICAL COMMUNICATIONS, 1969, 34 (04) : 1317 - +
  • [3] Tertiary alkyl ethers preparation and properties
    Evans, TW
    Edlund, KR
    [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1936, 28 : 1186 - 1188
  • [4] FARKOVA J, 1995, IN PRESS INT ELECTRO
  • [5] HALA E, 1982, ROVNOVAHA KAPALINA P
  • [6] GENERALIZED METHOD FOR PREDICTING 2ND VIRIAL-COEFFICIENTS
    HAYDEN, JG
    OCONNELL, JP
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1975, 14 (03): : 209 - 216
  • [7] Hougen O. A., 1947, CHEM PROCESS PRINCIP, V3
  • [8] LINEK J, 1995, ELDATA INT ELECT J P, V1, P43
  • [9] ) Mullins S. R., 1989, AICHE S SER, V85, P94
  • [10] VAPOR LIQUID EQUILIBRIUM IN THE ACETONE WATER-SYSTEM AT 101.325 KPA
    POLEDNOVA, J
    WICHTERLE, I
    [J]. FLUID PHASE EQUILIBRIA, 1984, 17 (01) : 115 - 121
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