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Corrigendum to “Modeling derivative properties and binary mixtures with CO2 using the CPA and the quadrupolar CPA equations of state” [Fluid Phase Equilib. 408 (2016) 151–169]
Fluid Phase Equilibria 421 (2016) 104
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Fluid Phase Equilibria j o u r n a l h o m e p a g e : w w w . e l s e v i e r . c o m / l o c a t e / fl u i d
Corrigendum
Corrigendum to “Modeling derivative properties and binary mixtures with CO2 using the CPA and the quadrupolar CPA equations of state” [Fluid Phase Equilib. 408 (2016) 151e169] Martin G. Bjørner*, Georgios M. Kontogeorgis Center for Energy Resources Engineering (CERE), Department of Chemical and Biochemical Engineering, Technical University of Denmark, Building 229, DK-2800 Kgs. Lyngby, Denmark
The authors regret the printed mistakes in Eq. (15) and Eq. (16) of the above article. The correct form of Eq. (15) is
Ar3;2;Quad RT
¼
nc nc X X Qij6 36 NA HS ni nj 12 I15 3 245 Vðkb TÞ i sij j
(15)
The correct form of Eq. (16) is
Ar3;3;Quad RT
¼
6 nc nc nc X X X Qijk 1 N2A HS n n n i j k 3 3 3 ITQ 6400 V 2 ðkb TÞ3 i s s s ij j ik jk k
(16)
All calculations presented in the above article have been performed with the correct equations. The authors would like to apologise for any inconvenience caused.
DOI of original article: http://dx.doi.org/10.1016/j.fluid.2015.08.011. * Corresponding author. E-mail address: [email protected] (M.G. Bjørner). http://dx.doi.org/10.1016/j.fluid.2016.04.019 0378-3812/© 2016 Elsevier B.V. All rights reserved.
Contents lists available at ScienceDirect
Fluid Phase Equilibria j o u r n a l h o m e p a g e : w w w . e l s e v i e r . c o m / l o c a t e / fl u i d
Corrigendum
Corrigendum to “Modeling derivative properties and binary mixtures with CO2 using the CPA and the quadrupolar CPA equations of state” [Fluid Phase Equilib. 408 (2016) 151e169] Martin G. Bjørner*, Georgios M. Kontogeorgis Center for Energy Resources Engineering (CERE), Department of Chemical and Biochemical Engineering, Technical University of Denmark, Building 229, DK-2800 Kgs. Lyngby, Denmark
The authors regret the printed mistakes in Eq. (15) and Eq. (16) of the above article. The correct form of Eq. (15) is
Ar3;2;Quad RT
¼
nc nc X X Qij6 36 NA HS ni nj 12 I15 3 245 Vðkb TÞ i sij j
(15)
The correct form of Eq. (16) is
Ar3;3;Quad RT
¼
6 nc nc nc X X X Qijk 1 N2A HS n n n i j k 3 3 3 ITQ 6400 V 2 ðkb TÞ3 i s s s ij j ik jk k
(16)
All calculations presented in the above article have been performed with the correct equations. The authors would like to apologise for any inconvenience caused.
DOI of original article: http://dx.doi.org/10.1016/j.fluid.2015.08.011. * Corresponding author. E-mail address: [email protected] (M.G. Bjørner). http://dx.doi.org/10.1016/j.fluid.2016.04.019 0378-3812/© 2016 Elsevier B.V. All rights reserved.