An Equation of State for the Thermodynamic Properties of Dimethyl Ether

被引:62
|
作者
Wu, Jiangtao [1 ]
Zhou, Yong [1 ]
Lemmon, Eric W. [2 ]
机构
[1] Xi An Jiao Tong Univ, State Key Lab Multiphase Flow Power Engn, Xian 710049, Shaanxi, Peoples R China
[2] Natl Inst Stand & Technol, Thermophys Properties Div, Boulder, CO 80305 USA
基金
中国国家自然科学基金; 国家高技术研究发展计划(863计划);
关键词
correlation; dimethyl ether; equation of state; thermodynamic properties; VAPOR-LIQUID-EQUILIBRIUM; 2ND VIRIAL-COEFFICIENTS; HIGH-PRESSURE SOLUBILITY; SULFUR-DIOXIDE; CARBON-DIOXIDE; BINARY-SYSTEMS; N-BUTANE; PHASE-EQUILIBRIA; OXYGEN COMPOUNDS; HEAT-CAPACITY;
D O I
10.1063/1.3582533
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
A thermodynamic property formulation for dimethyl ether has been developed based on a selection of experimental thermodynamic property data. The formulation includes a fundamental equation, a vapor-pressure equation, and saturated-density equations for liquid and vapor states. In determining the coefficients of the equation of state, multi-property fitting methods were used that included single-phase pressure-density-temperature (p rho T), heat capacity, vapor pressure, and saturated density data. Deviations between experimental and calculated data are generally within the experimental accuracy. The equation of state has been developed to conform to the Maxwell criterion for two-phase liquid-vapor equilibrium states, and is valid for temperatures from the triple-point temperature to 550 K, with pressures up to 50 MPa and densities up to 19 mol dm(-3). The uncertainties of the equation of state in density are 0.1% for the liquid phase and 0.3% for the vapor phase. In the extended critical region, the uncertainties in density are 0.5%, except for very near the critical point. The uncertainties in vapor pressure are 0.2% above 230 K, and increase as temperature decreases. The uncertainties in saturated liquid density are 0.05%, except for near the critical point. The uncertainties in heat capacity are 2.0%. Detailed comparisons between the experimental data and calculated values are given. (C) 2011 American Institute of Physics. [doi:10.1063/1.3582533]
引用
收藏
页数:16
相关论文
共 50 条
  • [1] Dimethyl ether in a state of saturation. Calculation of thermodynamic properties
    Kamfer, GM
    Ryzhkin, SV
    CHEMISTRY AND TECHNOLOGY OF FUELS AND OILS, 2005, 41 (01) : 77 - 83
  • [2] Dimethyl ether in a state of saturation. Calculation of thermodynamic properties
    G. M. Kamfer
    S. V. Ryzhkin
    Chemistry and Technology of Fuels and Oils, 2005, 41 : 77 - 83
  • [3] A helmholtz equation of state for dimethyl ether
    State Key Laboratory of Multiphase Flow in Power Engineering, Xi'an Jiaotong University, Xi'an 710049, China
    Kung Cheng Je Wu Li Hsueh Pao, 2009, 12 (1999-2002):
  • [4] The effects of diethyl ether, diethylene glycol dimethyl ether, and dimethyl carbonate addition on the physical and thermodynamic properties of biodiesel
    Osman, Sibel
    Sara, Osman Nuri
    Kavakli, Aycan Altun
    Lungu, Mioara-Jeanina
    JOURNAL OF THERMAL ANALYSIS AND CALORIMETRY, 2024, : 14489 - 14513
  • [5] Thermodynamic Properties and Equation of State for Tungsten
    Kozyrev, Nikolay V.
    Gordeev, Vladimir V.
    CRYSTALS, 2023, 13 (10)
  • [6] An Equation of State for the Thermodynamic Properties of Cyclohexane
    Zhou, Yong
    Liu, Jun
    Penoncello, Steven G.
    Lemmon, Eric W.
    JOURNAL OF PHYSICAL AND CHEMICAL REFERENCE DATA, 2014, 43 (04)
  • [7] THE EQUATION OF STATE AND THERMODYNAMIC PROPERTIES OF PROPYLENE
    KAZAVCHINSKII, YZ
    ZAGORUCHENKO, VA
    ZHURNAL FIZICHESKOI KHIMII, 1959, 33 (03): : 662 - 664
  • [8] EQUATION OF STATE FOR THERMODYNAMIC PROPERTIES OF FLUIDS
    GOODWIN, RD
    JOURNAL OF RESEARCH OF THE NATIONAL BUREAU OF STANDARDS SECTION A-PHYSICS AND CHEMISTRY, 1975, A 79 (01): : 71 - 79
  • [9] Thermodynamic equilibrium calculations of dimethyl ether steam reforming and dimethyl ether hydrolysis
    Semelsberger, TA
    Borup, RL
    JOURNAL OF POWER SOURCES, 2005, 152 (01) : 87 - 96
  • [10] Thermodynamic properties of polyoxyethyleneglycol dimethyl ether + n-alkane mixtures
    Universidad de Vigo, Orense, Spain
    Fluid Phase Equilib, 1-2 (223-234):