Isobaric Vapor-Liquid Equilibria for Binary Mixtures of 2-Phenylethanol with 1-Phenylethanol, 2-Phenylpropan-2-ol, Ethylbenzene, and Isopropylbenzene at 101.3 kPa

被引:6
|
作者
Das, Sudip [1 ]
Ghosh, Shashwata [2 ]
Nadeem, Mohd [1 ]
Seethamraju, Srinivas [2 ]
Mahajani, Sanjay [1 ]
机构
[1] Indian Inst Technol, Dept Chem Engn, Mumbai 400076, Maharashtra, India
[2] Indian Inst Technol, Dept Energy Sci & Engn, Mumbai 400076, Maharashtra, India
来源
关键词
Maximum likelihood estimation - Testing - Liquids - Ethylbenzene;
D O I
10.1021/acs.jced.0c01040
中图分类号
O414.1 [热力学];
学科分类号
摘要
The isobaric binary vapor-liquid equilibrium (VLE) data for the mixture of 2-phenylethanol (2PEA) with 1-phenylethanol (1PEA), 2-phenylpropan-2ol (2P2P), ethylbenzene (ETB), and isopropylbenzene (IPB) is generated at 101.3 kPa. The Fredenslund test and Redlich-Kister area test methods were used to confirm the consistency of the measured VLE experimental data. Subsequently, the data sets are correlated by the nonrandom two-liquid (NRTL) and universal quasi-chemical (UNIQUAC) thermodynamic models, and the binary interaction parameters for the two models were estimated using the Britt-Luecke algorithm and the maximum likelihood objective function. The estimation was found to be good for both the activity coefficient models.
引用
收藏
页码:1754 / 1762
页数:9
相关论文
共 50 条
  • [31] Isobaric vapor-liquid equilibrium, density and speed of sound of binary mixtures 2,2,4-trimethylpentane+1-butanol or dibutyl ether (DBE) at 101.3 kPa
    Rubio-Perez, Gabriel
    Munoz-Rujas, Natalia
    Srhiyer, Adil
    Montero, Eduardo A.
    Aguilar, Fernando
    FLUID PHASE EQUILIBRIA, 2018, 475 : 10 - 17
  • [32] Isobaric vapor-liquid equilibria for the system 1-pentanol-1-propanol-water at 101.3 kPa
    Loras, S
    Fernández-Torres, MJ
    Gomis-Yagües, V
    Ruíz-Beviá, F
    FLUID PHASE EQUILIBRIA, 2001, 180 (1-2) : 205 - 210
  • [33] Isobaric Vapor-Liquid Equilibria for the Binary and Ternary Systems of Methanol, Epichlorohydrin, and Glycerol Dimethyl Ether at 101.3 kPa
    Ding, Xiaoshu
    Liu, Hao
    Li, Naihua
    Wang, Shufang
    Wang, Guirong
    Zhao, Xinqiang
    Wang, Yanji
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2015, 60 (03): : 541 - 544
  • [34] Isobaric vapor-liquid equilibria of the binary system acetone plus acetone oxime methyl ether at 101.3 kPa
    Wang, Hongxing
    Li, Ling
    Ye, Changshen
    FLUID PHASE EQUILIBRIA, 2013, 342 : 42 - 46
  • [35] Vapor-Liquid Equilibrium at p/kPa=101.3 of the Binary Mixtures of Ethenyl Acetate with Methanol and Butan-1-ol
    Camacho, Javier
    Diez, Eduardo
    Diaz, Ismael
    Ovejero, Gabriel
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2012, 57 (11): : 3198 - 3202
  • [36] Isobaric Vapor-Liquid Equilibrium Data for the Binary System of Water+2-Methylpyridine at 101.3, 60.0, and 20.0 kPa
    Yang, Ying
    Fan, Kaigong
    Bai, Peng
    Guo, Xianghai
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2017, 62 (02): : 684 - 690
  • [37] Isobaric vapor-liquid equilibria for binary and ternary mixtures with cyclohexane, cyclohexene, and morpholine at 100 kPa
    Marrufo, Beatriz
    Sanchotello, Margarita
    Loras, Sonia
    FLUID PHASE EQUILIBRIA, 2010, 296 (02) : 178 - 183
  • [38] Isobaric vapor-liquid equilibrium for binary and ternary systems with toluene, 2-methoxyethanol and dimethyl sulfoxide at 101.3 kPa
    Zhao, Shuo
    Bai, Peng
    Sun, Chang
    FLUID PHASE EQUILIBRIA, 2014, 375 : 37 - 44
  • [39] Isobaric vapor-liquid equilibria for the binary and ternary mixtures of 2-propanol, water, and 1,3-propanediol at P=101.3 kPa: Effect of the 1,3-propanediol addition
    Lin, Yi-Feng
    Tu, Chein-Hsiun
    FLUID PHASE EQUILIBRIA, 2014, 368 : 104 - 111
  • [40] Vapor-liquid equilibria of methanol, ethanol, propan-2-ol, and 2-methylpropan-2-ol with a five-component hydrocarbon mixture at 101.3 kPa
    Tu, CH
    Hsian, HY
    Chou, YT
    Wang, WF
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2001, 46 (05): : 1239 - 1243