2001
DOI: 10.1016/s0378-3812(01)00488-5
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A modified temperature dependence for the Peng–Robinson equation of state

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Cited by 176 publications
(90 citation statements)
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“…Hence, all the calculations in Treiman (2003) relating to siderite decomposition involving the presence of a CO gas phase product are wrong. Using the most recent version of the thermodynamic dataset used by THERMOCALC v3.26 (and hence for referred to as HP98 12 ), in combination with the PengRobertson-Gasem cubic EOS (Gasem et al, 2001), and assuming Lewis Randall fugacity mixing rules (Lewis and Randall, 1961), the correct siderite stability P-T plot is shown in Fig. 7C.…”
Section: Thermodynamic Carbonate Decomposition -Treiman Modelmentioning
confidence: 99%
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“…Hence, all the calculations in Treiman (2003) relating to siderite decomposition involving the presence of a CO gas phase product are wrong. Using the most recent version of the thermodynamic dataset used by THERMOCALC v3.26 (and hence for referred to as HP98 12 ), in combination with the PengRobertson-Gasem cubic EOS (Gasem et al, 2001), and assuming Lewis Randall fugacity mixing rules (Lewis and Randall, 1961), the correct siderite stability P-T plot is shown in Fig. 7C.…”
Section: Thermodynamic Carbonate Decomposition -Treiman Modelmentioning
confidence: 99%
“…Calculations were made using thermodynamic data from the updated Holland and Powell (1998) database (THERMOCALC Ver. 3.26) and assuming a Peng-Robinson-Gasem EOS (Gasem et al, 2001) for gas phase species. Fig.…”
Section: 223mentioning
confidence: 99%
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“…7): -The first of these is the temperature dependence of the attraction parameter (a(T)). The coefficients in such a relation can be fitted on the vapour pressure of the pure components using expressions as reviewed by Gasem (2001). The best-known equations are those of Soave…”
Section: For Phase Equilibrium Problemsmentioning
confidence: 99%