Vapor-liquid equilibria and phase densities at saturation of carbon dioxide+1-butanol and carbon dioxide+2-butanol from 313 to 363 K

被引:10
|
作者
Elizalde-Solis, Octavio [2 ]
Galicia-Luna, Luis A. [1 ]
机构
[1] Inst Politecn Nacl, Lab Termodinam, SEPI ESIQIE, UPALM, Mexico City 07738, DF, Mexico
[2] Inst Politecn Nacl, Dept Ingn Quim Petr, ESIQIE, UPALM, Mexico City 07738, DF, Mexico
关键词
Saturated density; Densitometer; Vapor-liquid equilibria; DIOXIDE PLUS 1-BUTANOL; HIGH-PRESSURE; 2-BUTYL ACETATE; CUBIC EQUATIONS; VINYL-ACETATE; N-BUTANOL; SYSTEMS; MIXTURES; 2-BUTANOL; TEMPERATURES;
D O I
10.1016/j.fluid.2010.03.042
中图分类号
O414.1 [热力学];
学科分类号
摘要
Experimental vapor-liquid equilibria for the systems carbon dioxide + 1-butanol and carbon dioxide + 2-butanol were obtained from 313 to 363 K via a static-analytic set-up. A vibrating U-tube densitometer was coupled to this apparatus to perform simultaneous measurements of both saturated densities of the vapor and liquid phases. The suitability of this apparatus was checked by comparing the experimental vapor-liquid equilibrium and saturated density results with the literature data. The experimental vapor-liquid equilibrium data were correlated using the Peng-Robinson equation of state coupled to the Wong-Sandler mixing rules with good agreement: however densities using the same model were not satisfactorily represented. (c) 2010 Elsevier B.V. All rights reserved.
引用
收藏
页码:66 / 71
页数:6
相关论文
共 50 条
  • [1] Vapor-liquid equilibria for supercritical carbon dioxide plus butanol systems at 313.2 K
    Hiaki, T
    Miyagi, H
    Tsuji, T
    Hongo, M
    JOURNAL OF SUPERCRITICAL FLUIDS, 1998, 13 (1-3): : 23 - 27
  • [2] Volumetric properties of carbon dioxide+2-butanol mixtures at 313.15 K
    Kodama, Daisuke
    Kato, Masahiro
    Hashimoto, Satoshi
    Kaneko, Tomoo
    JOURNAL OF SUPERCRITICAL FLUIDS, 2010, 55 (02): : 696 - 700
  • [3] VAPOR-LIQUID-EQUILIBRIA IN THE CARBON-DIOXIDE + ETHANOL AND CARBON-DIOXIDE + 1-BUTANOL SYSTEMS
    JENNINGS, DW
    LEE, RJ
    TEJA, AS
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1991, 36 (03): : 303 - 307
  • [4] Vapor-liquid equilibrium for carbon dioxide plus 1-butanol at high pressure
    Ishihara, K
    Tsukajima, A
    Tanaka, H
    Kato, M
    Sako, T
    Sato, M
    Hakuta, T
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1996, 41 (02): : 324 - 325
  • [5] High-pressure phase equilibria for the carbon dioxide-2-methyl-1-butanol, carbon dioxide-2-methyl-2-butanol, carbon dioxide-2-methyl-1-butanol-water, and carbon dioxide-2-methyl-2-butanol-water systems
    Lee, HS
    Mun, SY
    Lee, H
    FLUID PHASE EQUILIBRIA, 1999, 157 (01) : 81 - 91
  • [6] High-pressure vapor-liquid equilibria in the system carbon dioxide plus 1-butanol at temperatures from (293.15 to 324.15) K
    Secuianu, C
    Feroiu, V
    Geana, D
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2004, 49 (06): : 1635 - 1638
  • [7] Vapor-liquid equilibria of carbon dioxide plus methyl methacrylate at 308, 313, 323, and 333 K
    Zwolak, G
    Lioe, L
    Lucien, FP
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2005, 44 (04) : 1021 - 1026
  • [8] Vapor-liquid equilibria for the binary system of carbon dioxide and 1,3-butadiene at 303, 313 and 333 K
    Wagner, KD
    Zappe, J
    Reeps, A
    Dahmen, N
    Dinjus, E
    FLUID PHASE EQUILIBRIA, 1998, 153 (01) : 135 - 142
  • [9] Compressed liquid densities of 1-butanol and 2-butanol at temperatures from 313 K to 363 K and pressures up to 25 MPa
    Zuniga-Moreno, Abel
    Galicia-Luna, Luis A.
    Camacho-Camacho, Luis E.
    JOURNAL OF CHEMICAL THERMODYNAMICS, 2007, 39 (02): : 254 - 260
  • [10] High-pressure phase equilibria of carbon dioxide plus 1-butanol, and carbon dioxide plus water plus 1-butanol systems
    Chen, HI
    Chang, HY
    Chen, PH
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2002, 47 (04): : 776 - 780