Modelo para determinar la densidad y el factor de expansión de mezclas multicomponentes de hidrocarburos en fase líquida

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The purpose of the research was: to develop the model that allows determining the density and expansion factor of multicomponent mixtures of hydrocarbons in the liquid phase, for which the Peng-Robinson, Lee-Kesler and Raoult equations were combined. Three mixtures were used, which are indicated wit...

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Detalles Bibliográficos
Autores: Barrera Vela, Richar Nixon, Chu Carmona, Dengxiao André
Formato: tesis de maestría
Fecha de Publicación:2025
Institución:Universidad Nacional De La Amazonía Peruana
Repositorio:UNAPIquitos-Institucional
Lenguaje:español
OAI Identifier:oai:repositorio.unapiquitos.edu.pe:20.500.12737/12437
Enlace del recurso:https://hdl.handle.net/20.500.12737/12437
Nivel de acceso:acceso abierto
Materia:Densidad
Factor de emisión
Fase líquida
https://purl.org/pe-repo/ocde/ford#2.07.01
Descripción
Sumario:The purpose of the research was: to develop the model that allows determining the density and expansion factor of multicomponent mixtures of hydrocarbons in the liquid phase, for which the Peng-Robinson, Lee-Kesler and Raoult equations were combined. Three mixtures were used, which are indicated with their respective molar composition: Camisea natural gas (GNC) (88.54 % methane, 10.32 % ethane, 0.02 % propane, 0.54 % nitrogen and 0.58 % carbon dioxide); liquefied natural gas (GNL) (85 % methane, 10 % ethane and 5 % propane), and liquefied petroleum gas (GLP) (60 % propane and 40 % n butane). The results when applying said model indicate that GNC has a density and expansion factor of 457.856 kg/m3 and 621.458, with the temperature being 111.15 K and the pressure being 1.14357 atm. In the same way, the density and expansion factor for GNL were: 471.496 kg/m3 and 601.763, being at 111.15 K and 1.00206 atm. Finally, when applying the model for LPG, the density and expansion factor resulted: 539.304 kg/m3 and 260.996, being at 280.15 K and 5.00105 atm.These results were compared with those obtained using the Aspen HYSYS V14.0 simulator and with other sources, from which it was verified that the developed model determines with great accuracy the density and expansion factor of multicomponent mixtures of hydrocarbons in the liquid phase. In conclusion, the general objective was met and the general hypothesis was tested.
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