2006
DOI: 10.1063/1.2201308
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Viscosity, SecondpVT-Virial Coefficient, and Diffusion of Pure and Mixed Small Alkanes CH4, C2H6, C3H8,n-C4H10,i-C4H10,n-C5H12,i-C5H12, and C(CH3)4 Calculated by Means of an Isotropic Temperature-Dependent Potential. I. Pure Alkanes

Abstract: Reference tables of second pVT-virial coefficients B(T), viscosity η(T), and self-diffusion ρD(T) are given for all neat alkanes CnH2n+2, n<6, for temperatures T⩽1200 K starting at 100 K for CH4, 150 K for C2H6, and 180 K for C3H8, n-C4H10, i-C4H10, n-C5H12, i-C5H12, and C(CH3)4. Restricting ourselves to low densities the thermophysical properties are calculated by means of an isotropic (n-6) Lennard-Jones temperature dependent potential (LJTDP). In this model the potential well depth εeff(T) and the se… Show more

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Cited by 27 publications
(16 citation statements)
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“…Finally, Fig. 2 also shows a comparison with values recommended as reference data by Zarkova et al 63 These values were calculated via an isotropic three-parameter Lennard-Jones ͑n − 6͒ potential obtained from a multiproperty fit to experimental data for the second pressure and acoustic virial coefficients, as well as for viscosity and selfdiffusion at low density. They agree neither with the calculated values nor with the experimental data and hence cannot be considered as standard viscosity values for methane.…”
Section: Comparison With Experimentsmentioning
confidence: 90%
“…Finally, Fig. 2 also shows a comparison with values recommended as reference data by Zarkova et al 63 These values were calculated via an isotropic three-parameter Lennard-Jones ͑n − 6͒ potential obtained from a multiproperty fit to experimental data for the second pressure and acoustic virial coefficients, as well as for viscosity and selfdiffusion at low density. They agree neither with the calculated values nor with the experimental data and hence cannot be considered as standard viscosity values for methane.…”
Section: Comparison With Experimentsmentioning
confidence: 90%
“…On the contrary, the data of Douslin et al 32 show virtually no differences to the EOS, because they were used to determine the equation. Figure 5 also shows a comparison with values recommended as reference data by Zarkova et al 46 In the case of methane the basis for these values is an isotropic threeparameter Lennard-Jones-͑n −6͒ potential obtained from a multiproperty fit to experimental data for the second pressure and acoustic virial coefficients as well as for viscosity and self-diffusion at low density. Figure 5 also shows a comparison with values recommended as reference data by Zarkova et al 46 In the case of methane the basis for these values is an isotropic threeparameter Lennard-Jones-͑n −6͒ potential obtained from a multiproperty fit to experimental data for the second pressure and acoustic virial coefficients as well as for viscosity and self-diffusion at low density.…”
Section: Adjustment Of the Intermolecular Potential Energy Surfacmentioning
confidence: 94%
“…Model inadequacy can sometimes be seen as a consequence of the use of a unique parameter set in different experimental conditions: a "better" model can indeed be obtained by using different values of the parameters along the control space. This can be achieved by modeling the dependence of the physical parameters on the control variable, [75][76][77] or by splitting the data in series along the control space and using a hierarchical model identical to the one in Section 3.2.2.2 for inference of the hyperparameters describing the model's parameters distribution (model M H2 in Wu et al 9 ). To differentiate both hierarchical schemes, the present one is named HierC.…”
Section: Hierc: Local Parameters In Control Spacementioning
confidence: 99%