Modeling Vapor Liquid Equilibrium of Binary and Ternary Systems of CO<sub>2</sub> + Hydrocarbons at High-Pressure Conditions

In this work, binary and ternary systems composed by hydrocarbons and CO2 in liquid-vapor equilibrium conditions (LV) were thermodynamically modeled using Peng-Robinson (PR) and Patel-Teja (PT) equations of state (EoS) in combination with van der Waals mixing rule with two adjustable parameters (vdW...

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Bibliographic Details
Main Authors: D.C. Silva, R. Guirardello, A.C.D. Freitas
Format: Article
Language:English
Published: AIDIC Servizi S.r.l. 2017-03-01
Series:Chemical Engineering Transactions
Online Access:https://www.cetjournal.it/index.php/cet/article/view/2310