Vapor-Liquid Phase Equilibrium Data of CO2 in Some Physical Solvents from 285.19 K to 313.26 K

被引:36
|
作者
Gui, Xia [1 ]
Wang, Wei [1 ]
Wang, Chen Wei [1 ]
Zhang, Ling [1 ]
Yun, Zhi [1 ]
Tang, Zhg [2 ]
机构
[1] Nanjing Univ Technol, Coll Chem & Chem Engn, Nanjing 210009, Jiangsu, Peoples R China
[2] Tsinghua Univ, Dept Chem Engn, State Key Lab Chem Engn, Beijing 100084, Peoples R China
来源
基金
中国国家自然科学基金;
关键词
CARBON-DIOXIDE; SOLUBILITY; CAPTURE; PRESSURES; GAS;
D O I
10.1021/je400985u
中图分类号
O414.1 [热力学];
学科分类号
摘要
The solubility of CO2 in polyethylene glycol dimethyl ether (NHD), octamethyl cyclotetrasiloxane (D4), and diethyl succinate (DS) was determined at the temperature variations from 285.19 K to 313.26 K up to 6 MPa by the constant-volume method. Then, Henry's law constant (H) based on mole fraction was obtained by linear fitting of the vapor liquid phase equilibrium data, and some thermodynamic properties of solutions were also calculated from the correlation of H. The values of H in NHD, D4, and DS vary from 2.5 MPa to 8 MPa and increase in the following order: DS < D4 < NHD, which is identical to the order of the solvents ability to dissolve CO2. Additionally, Henry's law constant increase to confirm the solubility of CO2 decrease in the corresponding solvents for the pressure range studied.
引用
收藏
页码:844 / 849
页数:6
相关论文
共 50 条
  • [1] Vapor-liquid equilibrium for mixtures of hexane and squalane at temperatures from 469.8 K to 623.3 K
    Joyce, PC
    Thies, MC
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1997, 42 (02): : 321 - 323
  • [2] Measurement and modelling of the vapor-liquid equilibrium of (CO2 + CO) at temperatures between (218.15 and 302.93) K at pressures up to 15 MPa
    Souza, Lorena F. S.
    Al Ghafri, Saif Z. S.
    Trusler, J. P. Martin
    JOURNAL OF CHEMICAL THERMODYNAMICS, 2018, 126 : 63 - 73
  • [3] Additive and nonadditive models of vapor-liquid equilibrium in CO2 from first principles
    Oakley, Mark T.
    Wheatley, Richard J.
    JOURNAL OF CHEMICAL PHYSICS, 2009, 130 (03):
  • [4] Experimental measurement and modeling of the vapor-liquid equilibrium of β-diketones with CO2
    Lubbers, CM
    Scurto, AM
    Brennecke, JF
    SUPERCRITICAL CARBON DIOXIDE: SEPARATIONS AND PROCESSES, 2003, 860 : 245 - 258
  • [5] Evaluation of alkanolamine chemical absorbents for CO2 from vapor-liquid equilibrium measurements
    Mimura, T
    Yagi, Y
    Takashina, T
    Yoshiyama, R
    Honda, A
    KAGAKU KOGAKU RONBUNSHU, 2005, 31 (04) : 237 - 242
  • [6] Vapor-liquid equilibrium measurements of the binary mixtures CO2 + acetone and CO2 + pentanones
    Hsieh, Chieh-Ming
    Vrabec, Jadran
    JOURNAL OF SUPERCRITICAL FLUIDS, 2015, 100 : 160 - 166
  • [7] New Vapor-Liquid Phase Equilibrium Data of CO2 in Several Heavy n-Alkanes at High Pressures
    He, JinTao
    Xu, XueMan
    Gui, Xia
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2021, 66 (04): : 1600 - 1610
  • [8] Vapor-liquid equilibrium in phenol+2-ethoxyethanol at 563.15 to 383.15 K
    Chylinski, K
    Fras, Z
    Malanowski, SK
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2001, 46 (01): : 29 - 33
  • [9] Vapor-liquid equilibrium in 2-ethoxyethanol + methanol at 313.15 to 333.15 K
    Antosik, Maria
    Fraś, Zbigniew
    Malanowski, Stanislaw K.
    Journal of Chemical and Engineering Data, 44 (03): : 368 - 372
  • [10] Vapor-liquid equilibrium data of the methane plus tetrafluoromethane system at temperatures from (159.61 to 178.93) K
    Zhu, Hongbo
    Gong, Maoqiong
    Zhang, Yu
    Wu, Jianfeng
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2007, 52 (02): : 463 - 467