Isobaric (vapour plus liquid) equilibria for N-formylmorpholine with ethylbenzene, n-butylbenzene, iso-propylbenzene and 1,2,4-trimethylbenzene at 101.33 kPa

被引:6
作者
Liu, Tao [1 ]
Wang, Zhengrong [1 ]
Xia, Shuqian [1 ]
Ma, Peisheng [1 ]
机构
[1] Tianjin Univ, Sch Chem Engn & Technol, State Educ Minist, Key Lab Green Chem Technol, Tianjin 300072, Peoples R China
基金
中国国家自然科学基金;
关键词
N-formylmorpholine; (Vapour plus liquid) equilibrium; UNIFAC (Do) model; NRTL model; UNIQUAC model; BINARY-SYSTEMS; TOLUENE; XYLENE;
D O I
10.1016/j.jct.2012.04.016
中图分类号
O414.1 [热力学];
学科分类号
摘要
The isobaric (vapour + liquid) equilibrium (VLE) of N-formylmorpholine with aromatics (ethylbenzene, n-butylbenzene, isopropylbenzene, 1,2,4-trimethylbenzene) at 101.33 kPa was investigated. The experimental VLE data for the four binary systems were tested and verified to be thermodynamically consistent by the Herington analysis method. At the same time, the non-random two-liquid (NRTL) and universal quasi-chemical (UNIQUAC) activity coefficient models were used to correlate the experimental data with temperature-independent parameters. The average absolute deviations of the temperature correlated by NRTL model and UNIQUAC model for all the systems are below 0.62 K and the average absolute deviations for the vapour phase compositions are all below 0.083. In addition, the UNIFAC (Do) group contribution model was used to correlate and estimate the VLE data. The N-formylmorpholine was treated as a group (NFM). The group interaction parameters for CH2-NFM, ACH-NFM and ACCH(2)-NFM were regressed. The UNIFAC (Do) model can correlate the experimental data well. The group interaction parameters were used to estimate VLE data of the (o-xylene + N-formylmorpholine), (m-xylene + N-formylmorpholine) and (p-xylene + N-formylmorpholine) binary systems. The estimated data fit well with the literature data. The average absolute deviations of the temperature for N-formylmorpholine with (o-xylene, m-xylene, p-xylene) are 1.67 K, 1.77 K and 1.35 K, respectively, and the average absolute deviations for the vapour phase compositions of o-xylene, m-xylene and p-xylene are 0.0133, 0.0057 and 0.0059, respectively. (C) 2012 Elsevier Ltd. All rights reserved.
引用
收藏
页码:9 / 15
页数:7
相关论文
共 25 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] [Anonymous], ASP PHYS PROP SYST V
  • [3] INFINITE DILUTION ACTIVITY-COEFFICIENTS PREDICTED BY UNIFAC GROUP CONTRIBUTION
    BASTOS, JC
    SOARES, ME
    MEDINA, AG
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1988, 27 (07) : 1269 - 1277
  • [4] Broughton D., 1967, Seventh World Pet. Congr. Proc, V4, P65
  • [5] Liquid-liquid equilibria of methylcyclohexane-benzene-N-formylmorpholine at several temperatures
    Chen DongChu
    Ye HongQi
    Wu Hao
    [J]. FLUID PHASE EQUILIBRIA, 2007, 255 (02) : 115 - 120
  • [6] Cincotti A, 1999, J CHEM ENG DATA, V44, P480, DOI 10.1021/je980168o
  • [7] Daubert T.E., 2002, PHYS THERMODYNAM S11
  • [8] Daubert TE., 1989, PHYS THERMODYNAMIC P, DOI DOI 10.5860/CHOICE.27-3319
  • [9] Deal C.H., 1959, 5 WORLD PET C P, V3, P283
  • [10] A MODIFIED UNIFAC MODEL .2. PRESENT PARAMETER MATRIX AND RESULTS FOR DIFFERENT THERMODYNAMIC PROPERTIES
    GMEHLING, J
    LI, JD
    SCHILLER, M
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1993, 32 (01) : 178 - 193