AbstractLee-Kesler (LK) Equation of State (EoS) is the most accurate enthalpy model for gases. The pressures at some condensate gas well heads are higher than 70 MPa. Accurate calculating the compressibility factors of the high pressure gas is essential to the enthalpy calculation of LK EoS. The basic parameters of the LK EoS are the reduced pressure and temperature which should be calculated based on mixing rules. This work researches the API, Plocker and Knapp, Lee and Kesler mixing rules, the combinations composed of Prausnitz and Gunn high pressure mixing rule and the above three rules. Comparisons of 11 experimental and calculated compressibility factors show the API mixing rule is the most accurate one when the pressure is lower than ...
Natural gases containing sour components exhibit different gas compressibility factor (Z) behavior t...
In this study the pressure effect on the inversion temperature of gases was determined. The gases se...
Estimation of thermodynamic properties of gas mixtures using modified Benedict-Webb-Rubin equation b...
AbstractLee-Kesler (LK) Equation of State (EoS) is the most accurate enthalpy model for gases. The p...
The compressibility factor is an essential parameter for natural gas exploitation and processing. Th...
Enhanced oil recovery (EOR), is an essential part of oil and gas production nowadays. Gases used in...
This paper proposed a new empirical K-value equation is developed to calculate dew pressure for gas ...
Gas condensates are hydrocarbons found to be in the gaseous phase while in the reservoir but as prod...
Accurate gas property prediction is a necessary component throughout the oil and gas industry for en...
LecturePg. 121-130Accurate prediction of centrifugal compressor aero/thermodynamic performance is es...
International audienceThis paper presents calculations of Joule-Thomson inversion effects in high-pr...
A study was carried out to address the need to compute Lennard-Jones (LJ) densities as a function of...
An accurate equation of state has been developed for the prediction of volumes of pure hydrocarbons ...
Abstract: Natural gases containing sour components exhibit different gas compressibility factor (Z) ...
Compressibility factors and fugacity coefficients for hydrogen, niftrogen, oxygen, carbon dioxide, a...
Natural gases containing sour components exhibit different gas compressibility factor (Z) behavior t...
In this study the pressure effect on the inversion temperature of gases was determined. The gases se...
Estimation of thermodynamic properties of gas mixtures using modified Benedict-Webb-Rubin equation b...
AbstractLee-Kesler (LK) Equation of State (EoS) is the most accurate enthalpy model for gases. The p...
The compressibility factor is an essential parameter for natural gas exploitation and processing. Th...
Enhanced oil recovery (EOR), is an essential part of oil and gas production nowadays. Gases used in...
This paper proposed a new empirical K-value equation is developed to calculate dew pressure for gas ...
Gas condensates are hydrocarbons found to be in the gaseous phase while in the reservoir but as prod...
Accurate gas property prediction is a necessary component throughout the oil and gas industry for en...
LecturePg. 121-130Accurate prediction of centrifugal compressor aero/thermodynamic performance is es...
International audienceThis paper presents calculations of Joule-Thomson inversion effects in high-pr...
A study was carried out to address the need to compute Lennard-Jones (LJ) densities as a function of...
An accurate equation of state has been developed for the prediction of volumes of pure hydrocarbons ...
Abstract: Natural gases containing sour components exhibit different gas compressibility factor (Z) ...
Compressibility factors and fugacity coefficients for hydrogen, niftrogen, oxygen, carbon dioxide, a...
Natural gases containing sour components exhibit different gas compressibility factor (Z) behavior t...
In this study the pressure effect on the inversion temperature of gases was determined. The gases se...
Estimation of thermodynamic properties of gas mixtures using modified Benedict-Webb-Rubin equation b...