VAPOR-LIQUID-EQUILIBRIA OF ETHANOL PLUS OCTANE AT 343.15-K AND 1-PROPANOL PLUS OCTANE AT 358.15-K

被引:16
作者
HIAKI, T [1 ]
TAKAHASHI, K [1 ]
TSUJI, T [1 ]
HONGO, M [1 ]
KOJIMA, K [1 ]
机构
[1] NIHON UNIV,COLL SCI & TECHNOL,DEPT IND CHEM,CHIYODA KU,TOKYO 101,JAPAN
关键词
D O I
10.1021/je00017a059
中图分类号
O414.1 [热力学];
学科分类号
摘要
Isothermal vapor-liquid equilibria were measured for ethanol + octane at 343.15 K and 1-propanol + octane at 358.15 K. The measurements were made in a still with the aid of a computer for control of the temperature and measurement of the total pressure. The results were best correlated with the Wilson equation for the system of ethanol + octane and with the nonrandom two-liquid (NRTL) equations for the 1-propanol + octane system.
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页码:271 / 273
页数:3
相关论文
共 20 条
  • [1] STATISTICAL THERMODYNAMICS OF LIQUID-MIXTURES - NEW EXPRESSION FOR EXCESS GIBBS ENERGY OF PARTLY OR COMPLETELY MISCIBLE SYSTEMS
    ABRAMS, DS
    PRAUSNITZ, JM
    [J]. AICHE JOURNAL, 1975, 21 (01) : 116 - 128
  • [2] BERRO C, 1987, INT DATA SER SEL D A, V1, P73
  • [3] Boublik T., 1984, VAPOUR PRESSURES PUR
  • [4] BOUBLIKOVA L, 1969, J APPL CHEM, V19, P89
  • [5] Bridgeman O.C., 1964, J HEAT MASS TRANSFER, V86, P279, DOI [10.1115/1.3687121, DOI 10.1115/1.3687121, DOI 10.11151/3687121]
  • [6] Fredenslund A., 1977, VAPOR LIQUID EQUILIB, V1st
  • [7] GMEHLING J, 1977, CHEM DATA SERIES 2A
  • [8] GENERALIZED METHOD FOR PREDICTING 2ND VIRIAL-COEFFICIENTS
    HAYDEN, JG
    OCONNELL, JP
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1975, 14 (03): : 209 - 216
  • [9] Herington E. F. G., 1951, J I PETROL, V37, P457
  • [10] VAPOR-LIQUID-EQUILIBRIA OF 2,3-DIMETHYLBUTANE + METHANOL OR ETHANOL AT 101.3 KPA
    HIAKI, T
    YAMATO, K
    KOJIMA, K
    [J]. JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1992, 37 (02) : 203 - 206