An accurate empirical correlation for predicting natural gas compressibility factors

被引:28
作者
Sanjari, Ehsan [1 ]
Lay, Ebrahim Nemati [1 ]
机构
[1] Univ Kashan, Fac Engn, Dept Chem Engn, Kashan, Iran
来源
JOURNAL OF NATURAL GAS CHEMISTRY | 2012年 / 21卷 / 02期
关键词
natural gas; compressibility factor; correlation; empirical model; equation of state; 3RD VIRIAL-COEFFICIENTS; METHANE PLUS NITROGEN; VOLUMETRIC PROPERTIES; CARBON-DIOXIDE; 99.93; MPA; VISCOSITY MEASUREMENTS; HYDROCARBON SYSTEMS; TEMPERATURES; 323.15; SINKER DENSIMETER; PHASE-EQUILIBRIA;
D O I
10.1016/S1003-9953(11)60352-6
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
The compressibility factor of natural gas is an important parameter in many gas and petroleum engineering calculations. This study presents a new empirical model for quick calculation of natural gas compressibility factors. The model was derived from 5844 experimental data of compressibility factors for a range of pseudo reduced pressures from 0.01 to 15 and pseudo reduced temperatures from 1 to 3. The accuracy of the new empirical correlation has been compared with commonly used existing methods. The comparison indicates the superiority of the new empirical model over the other methods used to calculate compressibility factor of natural gas with average absolute relative deviation percent (AARD%) of 0.6535.
引用
收藏
页码:184 / 188
页数:5
相关论文
共 33 条
[1]  
Ababio BD, 2001, J CHEM THERMODYN, V33, P413
[2]   REFRACTIVE-INDEX AND DENSITY ISOTHERMS FOR METHANE FROM 273-K TO 373-K AND AT PRESSURES UP TO 34-MPA [J].
ACHTERMANN, HJ ;
HONG, JG ;
WAGNER, W ;
PRUSS, A .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1992, 37 (04) :414-418
[3]  
Ahmed TH., 1989, HYDROCARBON PHASE BE, P79
[4]   Viscosity of natural-gas mixtures: Measurements and prediction [J].
Assael, MJ ;
Dalaouti, NK ;
Vesovic, V .
INTERNATIONAL JOURNAL OF THERMOPHYSICS, 2001, 22 (01) :61-71
[5]   An efficient correlation for calculating compressibility factor of natural gases [J].
Azizi, Navid ;
Behbahani, R. ;
Isazadeh, M. A. .
JOURNAL OF NATURAL GAS CHEMISTRY, 2010, 19 (06) :642-645
[6]   Isothermal p V T measurements on gas hydrocarbon mixtures using a vibrating-tube apparatus [J].
Capla, L ;
Buryan, P ;
Jedelsky, J ;
Rottner, M ;
Linek, J .
JOURNAL OF CHEMICAL THERMODYNAMICS, 2002, 34 (05) :657-667
[7]   Measurement of the (pressure, density, temperature) relation of two (methane plus nitrogen) gas mixtures at temperatures between 240 and 400 K and pressures up to 20 MPa using an accurate single-sinker densimeter [J].
Chamorro, C. R. ;
Segovia, J. J. ;
Martin, M. C. ;
Villamanan, M. A. ;
Estela-Uribe, J. F. ;
Trusler, J. P. M. .
JOURNAL OF CHEMICAL THERMODYNAMICS, 2006, 38 (07) :916-922
[8]   VISCOSITY OF METHANE, HYDROGEN, AND 4 MIXTURES OF METHANE AND HYDROGEN FROM -100DEGREESC TO 0DEGREESC AT HIGH-PRESSURES [J].
CHUANG, SY ;
CHAPPELEAR, PS ;
KOBAYASHI, R .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1976, 21 (04) :403-411
[9]  
Douslin D.R., 1964, J CHEM ENG DATA, V9, P358
[10]   CALCULATION OF Z FACTORS FOR NATURAL GASES USING EQUATIONS OF STATE [J].
DRANCHUK, PM ;
ABOUKASSEM, JH .
JOURNAL OF CANADIAN PETROLEUM TECHNOLOGY, 1975, 14 (03) :34-36