Effects of natural gas compositions on its Joule-Thomson coefficients and Joule-Thomson inversion curves

被引:14
作者
Farzaneh-Gord, Mahmood [1 ]
Rahbari, Hamid Reza [1 ]
Zangeneh, Jalal [1 ]
机构
[1] Ferdowsi Univ Mashhad, Fac Engn, Mech Engn Dept, Mashhad, Razavi Khorasan, Iran
关键词
Natural gas; Natural gas inversion curve; Joule-Thomson coefficient; Natural gas compositions; GERG-2008 equation of state; EQUATION-OF-STATE; ACCURATE THERMODYNAMIC PROPERTIES; CUBIC EQUATIONS; CARBON-DIOXIDE; HEAT-CAPACITY; PURE FLUIDS; MIXTURES; PRESSURES; PREDICTION; TEMPERATURES;
D O I
10.1016/j.cryogenics.2020.103169
中图分类号
O414.1 [热力学];
学科分类号
摘要
The main goal of this study is to investigate the effect of natural gas composition on the Joule-Thomson coefficient and Joule-Thomson inversion curve. The Joule-Thomson inverse curve is the geometrical location of points where the Joule-Thomson coefficient is zero. The curve is an important parameter for the liquefaction capability of natural gas. The GERG-2008 equation of state is utilized to calculate the Joule-Thomson coefficient as well as the JT inversion curve. To validate the numerical values, the results are compared with measured values and the validation results show the GERG-2008 calculated Joule-Thomson inversion curve with high accuracy. The results show, that natural gases with larger molecular weights have higher pressures at the same temperature. Also, Based on GERG-2008 data, a novel correlation is presented for the calculation of the Joule-Thomson inversion curve. The correlation has an average absolute percent deviation of less than 2.5% in determining the natural gas Joule-Thomson inversion curve. It should be pointed out that for developing the correlation a huge database of 33,000 natural gas mixture is employed.
引用
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页数:13
相关论文
共 42 条
[1]   Joule-Thomson coefficients and Joule-Thomson inversion curves for pure compounds and binary systems predicted with the group contribution equation of state VTPR [J].
Abbas, Rima ;
Ihmels, Christian ;
Enders, Sabine ;
Gmehling, Juergen .
FLUID PHASE EQUILIBRIA, 2011, 306 (02) :181-189
[2]  
[Anonymous], COMPRESSIBILITY SUPE
[3]  
[Anonymous], 2015, ISO 20765-2 Natural gas-calculation of thermodynamic properties-Part 2: single-phase properties (gas, liquid, and dense fluid) for extended ranges of application
[4]  
Bejan A., 2016, IRREVERSIBLE THERMOD, V4th ed.
[5]   Joule-Thomson Inversion Curves and Third Virial Coefficients for Pure Fluids from Molecular-Based Models [J].
Castro-Marcano, F. ;
Olivera-Fuentes, C. G. ;
Colina, C. M. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2008, 47 (22) :8894-8905
[6]   THE ISOTHERMAL JOULE-THOMSON COEFFICIENT OF SOME BINARY GAS MIXTURES [J].
CHARNLEY, A ;
ROWLINSON, JS ;
SUTTON, JR ;
TOWNLEY, JR .
PROCEEDINGS OF THE ROYAL SOCIETY OF LONDON SERIES A-MATHEMATICAL AND PHYSICAL SCIENCES, 1955, 230 (1182) :354-358
[7]  
Chase M., 1998, Technical Report, V4th, P1
[8]  
Doble M., PERRYS CHEM ENG HDB
[9]   Numerical procedures for natural gas accurate thermodynamic properties calculation [J].
Farzaneh-Gord, M. ;
Rahbari, H. R. .
JOURNAL OF ENGINEERING THERMOPHYSICS, 2012, 21 (04) :213-234
[10]  
Farzaneh-Gord M., 2010, INT J CHEM ENG APPL, V1, P20, DOI DOI 10.7763/IJCEA.2010.V1.4