Prediction of natural gas densities using equations of state of Soave-Redlich-Kwong, Peng-Robinson and AGA8-DC92

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In this work the Soave-Redlich-Kwong(SRK), Peng-Robinson (PR) y AGA8-DC92 (AGA) equations of state have been used to predict the density of different natural gas mixtures. AS a result, SRK and PR are strongly recommended for temperatures within the range 240-350 K. As for the pressure, SRK...

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Detalles Bibliográficos
Autores: Zavaleta Ortiz, Jack, Pilco Nuñez, Alex, Villanueva Guzmán, Sergio
Formato: artículo
Fecha de Publicación:2006
Institución:Universidad Nacional de Ingeniería
Repositorio:Revistas - Universidad Nacional de Ingeniería
Lenguaje:español
OAI Identifier:oai:oai:revistas.uni.edu.pe:article/389
Enlace del recurso:https://revistas.uni.edu.pe/index.php/tecnia/article/view/389
Nivel de acceso:acceso abierto
Materia:gas natural
ecuaciones de estado
factor de compresibilidad
densidad
natural gas
equation of state
compressibility factor
density
Descripción
Sumario:In this work the Soave-Redlich-Kwong(SRK), Peng-Robinson (PR) y AGA8-DC92 (AGA) equations of state have been used to predict the density of different natural gas mixtures. AS a result, SRK and PR are strongly recommended for temperatures within the range 240-350 K. As for the pressure, SRK yielded better results within the range 1-8 MPa, whereas PR was more accurate for pressures ranging from 1 to 15 MPa. The errors obtained were smaller than 3% for all the 613 experimental point taken from the literature, which is convenient due to the fact that AGA is not easy to handle. Nevertheless, AGA displayed the best performance in every calculation and proved to be superior to either SRK or PR in the whole range of conditions used in this investigation. Finally, a computational tool has been developed to calculate density (ρ) and compressibility factor (Z). Such a tool incorporates an experimental database of ρ for different gas natural mixtures.
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