2008
DOI: 10.1016/j.jct.2008.06.010
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Estimation of 2nd-order derivative thermodynamic properties using the crossover lattice equation of state

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Cited by 7 publications
(4 citation statements)
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“…Examples of such studies that relate to the general SAFT framework include the work of Llovell et al, 88 Dias et al, 89 Vilaseca et al, 90 and Forte et al 91 Other crossover methods have also been applied to the study of derivative properties, such as the crossover-cubic 92 and the crossoverlattice EoSs. 93 An aim our current work is to demonstrate the impact of the intermolecular potential model that is employed within a SAFT GC treatment on the accuracy that can be achieved in the simultaneous description of the fluid-phase behavior and second-order derivative thermodynamic properties. It is important to note that SAFT approaches based on segmentsegment interactions treated with Mie potentials of variable attractive and repulsive ranges are recognized to provide such a capability.…”
Section: Introductionmentioning
confidence: 99%
“…Examples of such studies that relate to the general SAFT framework include the work of Llovell et al, 88 Dias et al, 89 Vilaseca et al, 90 and Forte et al 91 Other crossover methods have also been applied to the study of derivative properties, such as the crossover-cubic 92 and the crossoverlattice EoSs. 93 An aim our current work is to demonstrate the impact of the intermolecular potential model that is employed within a SAFT GC treatment on the accuracy that can be achieved in the simultaneous description of the fluid-phase behavior and second-order derivative thermodynamic properties. It is important to note that SAFT approaches based on segmentsegment interactions treated with Mie potentials of variable attractive and repulsive ranges are recognized to provide such a capability.…”
Section: Introductionmentioning
confidence: 99%
“…28,29 The second-order derivative properties, such as isothermal compressibility, thermal expansion coefficient, Joule−Thomson coefficient, heat capacity, and speed of sound, are not predicted accurately by the majority of EoS models. 28,29 These properties serve as a basis for the design and modeling of pipeline transportation systems. Especially, knowledge on speed of sound is crucial in characterizing the state and structure of the fluid in pipeline transportation systems.…”
Section: Introductionmentioning
confidence: 99%
“…The thermodynamic and transport properties of impure CO 2 can be computed from thermodynamic models such as Equations of State (EoS) or other empirical correlations available in the literature. The validity of EoS predictions majorly depends on the interaction parameters that are obtained by fitting Vapor–Liquid Equilibrium (VLE) data obtained from experiments and assumptions used to develop EoS. , Most EoS models accurately predict the thermodynamic properties related to first-order derivatives of the thermodynamic potentials (Gibbs energy, Helmholtz energy, enthalpy, and internal energy), i.e., the phase equilibria. , The second-order derivative properties, such as isothermal compressibility, thermal expansion coefficient, Joule–Thomson coefficient, heat capacity, and speed of sound, are not predicted accurately by the majority of EoS models. , These properties serve as a basis for the design and modeling of pipeline transportation systems. Especially, knowledge on speed of sound is crucial in characterizing the state and structure of the fluid in pipeline transportation systems. , Many literature studies predict the thermodynamic and transport properties of impure CO 2 using either a simple or advanced EoS, , but no general agreement has been made to use a particular EoS with specific interaction parameters for CO 2 mixtures with small amount of impurities. , …”
Section: Introductionmentioning
confidence: 99%
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