The GERG-2008 Wide-Range Equation of State for Natural Gases and Other Mixtures: An Expansion of GERG-2004

被引:973
作者
Kunz, O. [1 ]
Wagner, W. [1 ]
机构
[1] Ruhr Univ Bochum, Lehrstuhl Thermodynam, D-44780 Bochum, Germany
关键词
VAPOR-LIQUID-EQUILIBRIA; DEW-POINT CURVES; HEAVY NORMAL-PARAFFINS; PROPANE-N-DECANE; HETEROGENEOUS PHASE-EQUILIBRIA; ISOTHERMAL FLASH PROBLEM; HYDROGEN SULFIDE SYSTEM; PLUS CARBON-DIOXIDE; GIBBS FREE-ENERGIES; MOLAR-MASS ALKANES;
D O I
10.1021/je300655b
中图分类号
O414.1 [热力学];
学科分类号
摘要
A new equation of state for the thermodynamic properties of natural gases, similar gases, and other mixtures, the GERG-2008 equation of state, is presented in this work. This equation is an expanded version of the GERG-2004 equation. GERG-2008 is explicit in the Helmholtz free energy as a function of density, temperature, and composition. The equation is based on 21 natural gas components: methane, nitrogen, carbon dioxide, ethane, propane, n-butane, isobutane, n-pentane, isopentane, n-hexane, n-heptane, n-octane, n-nonane, n-decane, hydrogen, oxygen, carbon monoxide, water, hydrogen sulfide, helium, and argon. Over the entire composition range, GERG-2008 covers the gas phase, liquid phase, supercritical region, and vapor-liquid equilibrium states for mixtures of these components. The normal range of validity of GERG-2008 includes temperatures from (90 to 450) K and pressures up to 35 MPa where the most accurate experimental data of the thermal and caloric properties are represented to within their accuracy. The extended validity range reaches From (60 to 700) K and up to 70 MPa. The given numerical information (including all of the sophisticated derivatives) enables the use of GERG-2008 for all of the various technical applications. Examples are processing, transportation through pipeline:: or by shipping, storage and liquefaction of natural gas, and processes to separate gas components. Comparisons with other equations of state, for example, AGA8-DC92 and Peng-Robinson equation (P-R), are also presented. GERG-2008 will be adopted as an ISO Standard (ISO 20765-2/3) for natural gases.
引用
收藏
页码:3032 / 3091
页数:60
相关论文
共 196 条
[1]  
Aavatsmark I, 1995, MATH EINFUHRUNG THER
[2]  
[Anonymous], HYDROCARBON PROCESS
[3]  
[Anonymous], 8 AM GAS ASS TRANSM
[4]  
[Anonymous], 2006, 1221322006 ISO
[5]  
[Anonymous], 2005, 207651 ISO COP OFF
[6]  
[Anonymous], 1959, J. Chem. Eng. Data
[7]   p-ρ-T Behavior of Three Lean Synthetic Natural Gas Mixtures Using a Magnetic Suspension Densimeter and Isochoric Apparatus from (250 to 450) K with Pressures up to 150 MPa: Part II [J].
Atilhan, M. ;
Aparicio, S. ;
Ejaz, S. ;
Cristancho, D. ;
Mantilla, I. ;
Hall, K. R. .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2011, 56 (10) :3766-3774
[8]   PρT Behavior of a Lean Synthetic Natural Gas Mixture Using Magnetic Suspension Densimeters and an Isochoric Apparatus: Part I [J].
Atilhan, M. ;
Aparicio, S. ;
Ejaz, S. ;
Cristancho, D. ;
Hall, K. R. .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2011, 56 (02) :212-221
[9]   DENSITIES, VISCOSITIES, AND REFRACTIVE-INDEXES OF SOME N-ALKANE BINARY-LIQUID SYSTEMS AT 298.15-K [J].
AUCEJO, A ;
BURGUET, MC ;
MUNOZ, R ;
MARQUES, JL .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1995, 40 (01) :141-147
[10]   Viscosity and density of mixtures of methane and n-decane from 298 to 393 K and up to 75 MPa [J].
Audonnet, F ;
Pádua, AAH .
FLUID PHASE EQUILIBRIA, 2004, 216 (02) :235-244