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Development of a novel Peng–Robinson plus association equation of state for industrially important associating compounds

  • Theory and Applications of Soft Computing Methods
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Abstract

Cubic plus association (CPA) equations of state (EoSs) have found great interest in describing thermodynamic properties of associating fluids. In CPA EoSs, the association contribution proposed by Wertheim is added to cubic EoSs such as Soave–Redlich–Kwong (SRK) and Peng–Robinson (PR). In different developments of CPA EoSs, adjusting the pure component properties such as critical temperature and critical pressure in addition to the association parameters is proposed in some works in the literature. In this work, the PR EoS has been extended to water, phenol, and a number of alcohols (methanol up to dodecanol) by addition of the Wertheim association contribution. In contrast to other CPA EoSs, the experimental values of critical properties are used. The energy and co-volume parameters of PR EoS are modified by introducing a correction factor that is correlated as a function of reduced temperature. The results show that this model is capable of reproducing experimental saturated liquid density and vapor pressure data accurately.

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Abbreviations

a 0 :

Parameter in the energy term (a) (bar dm6 mol−2)

A i :

Site A in molecule i

b :

Co-volume parameter (dm3 mol−1)

B i :

Site B in molecule j

c 1 :

Parameter in the energy term (a) (dimensionless)

ΔC pi :

Heat capacity change of the component i at the melting temperature (J mol−1 K−1)

g :

Radial distribution function

ΔH fus i :

Heat of fusion of the component i at the melting temperature (J mol−1)

k ij :

Binary interaction parameter

P :

Pressure (bar)

R :

Gas constant (bar dm3 mol−1 K−1)

T :

Temperature (K)

T m, i :

Melting temperature of the component i (K)

V m :

Molar volume (dm3 mol−1)

x i :

Liquid mole fraction of component i

X :

Monomer fraction

y j :

Vapor mole fraction of component i

Z :

Compressibility factor

β :

Association volume parameter (dimensionless)

Δ :

Association strength (dm3 mol−1)

ε :

Association energy parameter (bar dm3 mol−1)

η :

Reduced density

ρ :

Molar density (mol dm−3)

References

  1. Kontogeorgis GM (1996) An equation of state for associating fluid. Ind Eng Chem Res 35:4310–4318

    Article  Google Scholar 

  2. Soave G (1972) Equilibrium constants from a modified Redlich–Kwong equation of state. Chem Eng Sci 27:1197–1203

    Article  Google Scholar 

  3. Chapman WG., Keith EG, George J, Maciej R (1989) SAFT: equation-of-state solution model for associating fluids. Fluid Phase Equilibria 52:31–38

    Article  Google Scholar 

  4. Huang SH (1990) Equation of state for small, large, polydisperse, and associating molecules. Ind Eng Chem Res 29:2284–2294

    Article  Google Scholar 

  5. Kontogeorgis GM (2006) Ten years with the CPA (Cubic-Plus-Association) equation of state. Part 1. Pure compounds and self-associating systems. Ind Eng Chem Res 45:4855–4868

    Article  Google Scholar 

  6. Kontogeorgis GM (2006) Ten years with the CPA (Cubic-Plus-Association) equation of state. Part 2. Cross-associating and multicomponent systems. Ind Eng Chem Res 45:4869–4878

    Article  Google Scholar 

  7. Wu J, Prausnitz JM (1998) Phase equilibria for systems containing hydrocarbons, water, and salt: an extended Peng–Robinson equation of state. Ind Eng Chem Res 37:1634–1643

    Article  Google Scholar 

  8. Zoghi AT, Feyzi F (2011) Solubility of light reservoir gasses in water by the modified Peng–Robinson plus association equation of state using experimental critical properties of pure water. Pet Sci Eng 78:109–118

    Article  Google Scholar 

  9. Perakis C, Voutsas E, Magoulas K, Tassios D (2006) Thermodynamic modeling of the vapor–liquid equilibrium of the water/ethanol/CO2 system. Fluid Phase Equilib 243(1):142–150

    Article  Google Scholar 

  10. Hajiw M, Chapoy A, Coquelet C (2015) Hydrocarbons–water phase equilibria using the CPA equation of state with a group contribution method. Can J Chem Eng 93(2):432–442

    Article  Google Scholar 

  11. Pfohl O (1999) Phase equilibria in systems containing o-cresol, p-cresol, carbon dioxide and ethanol at 323.15–473.15 K and 10–35 Mpa. Fluid Phase Equilib 157:53–79

    Article  Google Scholar 

  12. Aparicio-Martinez S, Hall KR (2007) Phase equilibria in water containing binary systems from molecular based equations of state. Fluid Phase Equilib 254:112–125

    Article  Google Scholar 

  13. Huttenhuis PJG, Agrawal NJ, Solbraa E, Versteeg GF (2008) The solubility of carbon dioxide in aqueous N-methyl diethanol amine solutions. Fluid Phase Equilib 264:99–112

    Article  Google Scholar 

  14. Smith Bd, Srivastava R et al (1986) Thermodynamic data for pure compounds, Part B. Elsevier, New York, NY

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Correspondence to Leila Eslami.

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Eslami, L., Khadem-Hamedani, B. Development of a novel Peng–Robinson plus association equation of state for industrially important associating compounds. Neural Comput & Applic 31, 2107–2115 (2019). https://doi.org/10.1007/s00521-015-2126-2

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  • DOI: https://doi.org/10.1007/s00521-015-2126-2

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