p–ρ–TBehavior 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

2011 ◽  
Vol 56 (10) ◽  
pp. 3766-3774 ◽  
Author(s):  
M. Atilhan ◽  
S. Aparicio ◽  
S. Ejaz ◽  
D. Cristancho ◽  
I. Mantilla ◽  
...  
Keyword(s):  
Natural Gas ◽  
Gas Mixtures ◽  
Magnetic Suspension ◽  
Synthetic Natural Gas

Measurement of H–LW–V and Dissociation Enthalpy of Carbon Dioxide Rich Synthetic Natural Gas Mixtures

2014 ◽  
Vol 59 (11) ◽  
pp. 3502-3509 ◽  
Author(s):  
Khalik M. Sabil ◽  
Qazi Nasir ◽  
Bezhad Partoon ◽  
Akbar A. Seman
Keyword(s):  
Carbon Dioxide ◽  
Natural Gas ◽  
Gas Mixtures ◽  
Synthetic Natural Gas ◽  
Dissociation Enthalpy

PρTBehavior of a Lean Synthetic Natural Gas Mixture Using Magnetic Suspension Densimeters and an Isochoric Apparatus: Part I

2011 ◽  
Vol 56 (2) ◽  
pp. 212-221 ◽  
Author(s):  
M. Atilhan ◽  
S. Aparicio ◽  
S. Ejaz ◽  
D. Cristancho ◽  
K. R. Hall
Keyword(s):  
Natural Gas ◽  
Magnetic Suspension ◽  
Gas Mixture ◽  
Synthetic Natural Gas ◽  
Apparatus Part

Isothermal PρT measurements on Qatar’s North Field type synthetic natural gas mixtures using a vibrating-tube densimeter

2012 ◽  
Vol 53 ◽  
pp. 1-8 ◽  
Author(s):  
Mert Atilhan ◽  
Santiago Aparicio ◽  
Ferdi Karadas ◽  
Kenneth R. Hall ◽  
Rafael Alcalde
Keyword(s):  
Natural Gas ◽  
Gas Mixtures ◽  
Synthetic Natural Gas ◽  
Field Type ◽  
Vibrating Tube Densimeter

Measurement of the Hydrocarbon Dew Point of Real and Synthetic Natural Gas Mixtures by Direct and Indirect Methods

2009 ◽  
Vol 23 (3) ◽  
pp. 1640-1650 ◽  
Author(s):  
Andrew S. Brown ◽  
Martin J. T. Milton ◽  
Gergely M. Vargha ◽  
Richard Mounce ◽  
Chris J. Cowper ◽  
...  
Keyword(s):  
Natural Gas ◽  
Gas Mixtures ◽  
Dew Point ◽  
Indirect Methods ◽  
Synthetic Natural Gas ◽  
Direct And Indirect Methods

Viscosity Measurements and Data Correlation for Two Synthetic Natural Gas Mixtures

2010 ◽  
Vol 55 (7) ◽  
pp. 2498-2504 ◽  
Author(s):  
Mert Atilhan ◽  
Santiago Aparicio ◽  
Rafael Alcalde ◽  
Gustavo A. Iglesias-Silva ◽  
Mahmoud El-Halwagi ◽  
...  
Keyword(s):  
Natural Gas ◽  
Gas Mixtures ◽  
Data Correlation ◽  
Synthetic Natural Gas ◽  
Viscosity Measurements

Measurement and Prediction of Hydrocarbon Dew Points of Synthetic Natural Gas Mixtures

2018 ◽  
Vol 63 (11) ◽  
pp. 4226-4233
Author(s):  
Liang Mu ◽  
Qingyan Cui
Keyword(s):  
Natural Gas ◽  
Gas Mixtures ◽  
Synthetic Natural Gas

scholarly journals Comparative Study of Equations of State for the Dew Curves Calculation in High Pressure Natural Gas Mixtures. [Estudio Comparativo de Ecuaciones de Estado para el Cálculo de Curvas de Rocío en Mezclas de Gas Natural a Alta Presión]

2018 ◽  
Vol 11 (1) ◽  
pp. 152-164
Author(s):  
Natalia Prieto Jiménez ◽  
Germán González Silva
Keyword(s):  
Experimental Data ◽  
Natural Gas ◽  
High Pressures ◽  
Equations Of State ◽  
Absolute Error ◽  
Gas Mixtures ◽  
Synthetic Natural Gas ◽  
Gas Processing ◽  
Processing Plants ◽  
Correct Estimation

he success during the operation of natural gas processing plants depends on the correct estimation of thermodynamic properties of the system. This paper calculates the equilibrium curves of real and synthetic natural gas mixtures means of three Equations of State (EOS). These equilibrium curves were constructed and compared with experimental data found in the literature covered. The results showed that, above 4 MPa the Peng-Robinson equation presented a considerable deviation with respect to the experimental data, reaching an absolute error of 4.36%; therefore, the GERG2008 equation is recommended for systems that operate at high pressures when the components present in the mixture apply.Keywords:Gas Mixtures, Dew curves, Equations of State; Peng-Robinson, Soave-Redlich-Kwong, GERG2008.ResumenEl éxito durante la operación de plantas de tratamiento de gas natural depende de la correcta estimación de las propiedades termodinámicas del sistema. Este artículo calcula las curvas de equilibrio de mezclas de gas natural reales y sintéticas por medio de tres ecuaciones de estado (EOS). Estas curvas de equilibrio fueron construidas y comparadas con datos experimentales presentes en la literatura. Los resultados mostraron que, por encima de 4 MPa la ecuación de Peng-Robinson presentó una desviación considerable con respecto a los datos experimentales, alcanzando un error absoluto de 4,36%; por lo cual se recomienda la ecuación de GERG2008 para sistemas que operen a altas presiones cuando los componentes presentes en la mezcla apliquen.Palabras clave:  Mezclas de gas, Curvas de rocío, Ecuaciones de estado, Peng-Robinson, Soave-Redlich-Kwong, GERG2008.ResumoO sucesso na operação de usinas de tratamento de gás natural depende da correta estimação das propriedades termodinâmicas do sistema. Este artigo calcula as curvas de equilíbrio de misturas de gás natural reais e sintéticas por meio de três equações de estado (EOS). As curvas de equilíbrio foram construídas e comparadas com dados experimentais presentes na literatura. Os resultados mostraram que, acima de 4 Mpa a equação de Peng-Robinson apresentou um desvio considerável em relação aos dados experimentais, atingindo um erro absoluto de 4,36%; por tanto, é recomendável a equação de GERG2008 para sistemas que operam em alta pressão quando os componentes presentes no sistema apliquem.Palavras-chave:Misturas de gás, Curvas de orvalho, Equações de estado, Peng-Robinson, Soave-Redlich-Kwong, GERG2008. 

Measurement and modeling of hydrocarbon dew points for five synthetic natural gas mixtures

2006 ◽  
Vol 239 (2) ◽  
pp. 138-145 ◽  
Author(s):  
Ø. Mørch ◽  
Kh. Nasrifar ◽  
O. Bolland ◽  
E. Solbraa ◽  
A.O. Fredheim ◽  
...  
Keyword(s):  
Natural Gas ◽  
Gas Mixtures ◽  
Synthetic Natural Gas

Application of Continuous Thermodynamics to Natural-Gas Mixtures

1990 ◽  
Vol 45 (5) ◽  
pp. 633-643 ◽  
Author(s):  
J. M. Prausnitz ◽  
R. L. Cotterman
Keyword(s):  
Natural Gas ◽  
Gas Mixtures
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