Re-evaluation of experimental data on the second virial coefficient for steam and development of its analytical representation as a function of the internal energy

A re-evaluation of the second virial coefficient of steam is presented in the paper. The work is a part of broader effort to develop a formulation of the properties of dry and metastable steam suitable for CFD computations. The re-evaluation follows up previous work by Harvey and Lemmon [1], however...

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Main Authors: Hrubý J., Duška M.
Format: Article
Language:English
Published: EDP Sciences 2013-04-01
Series:EPJ Web of Conferences
Online Access:http://dx.doi.org/10.1051/epjconf/20134501024
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spelling doaj-6ca69c517cf8499f80b1e133ce125d922021-08-02T06:01:04ZengEDP SciencesEPJ Web of Conferences2100-014X2013-04-01450102410.1051/epjconf/20134501024Re-evaluation of experimental data on the second virial coefficient for steam and development of its analytical representation as a function of the internal energyHrubý J.Duška M.A re-evaluation of the second virial coefficient of steam is presented in the paper. The work is a part of broader effort to develop a formulation of the properties of dry and metastable steam suitable for CFD computations. The re-evaluation follows up previous work by Harvey and Lemmon [1], however with a special care for the lower temperature region close to the triple point and including more experimental data. The second virial coefficient was evaluated from volumetric (pvT) data, calorimetric measurements for saturated vapor, steam expansion experiments (measurements of the Joule–Thomson coefficient and the isothermal throttling coefficient) and measurements of the speed of sound. To accurately evaluate the uncertainty of calorimetric measurements, the uncertainty of the temperature derivative of the saturation pressure was determined based on refitting of the IAPWS saturation pressure formula to the experimental data. In the second step, the evaluated data and their uncertainties were used to develop an analytical formula to compute the second virial coefficient as function of internal energy in a range corresponding to the ideal-gas temperatures from 273.16 K to 1073.15 K. The choice of internal energy and density as independent variables is required for the CFD computations to avoid time-consuming iterations. http://dx.doi.org/10.1051/epjconf/20134501024
collection DOAJ
language English
format Article
sources DOAJ
author Hrubý J.
Duška M.
spellingShingle Hrubý J.
Duška M.
Re-evaluation of experimental data on the second virial coefficient for steam and development of its analytical representation as a function of the internal energy
EPJ Web of Conferences
author_facet Hrubý J.
Duška M.
author_sort Hrubý J.
title Re-evaluation of experimental data on the second virial coefficient for steam and development of its analytical representation as a function of the internal energy
title_short Re-evaluation of experimental data on the second virial coefficient for steam and development of its analytical representation as a function of the internal energy
title_full Re-evaluation of experimental data on the second virial coefficient for steam and development of its analytical representation as a function of the internal energy
title_fullStr Re-evaluation of experimental data on the second virial coefficient for steam and development of its analytical representation as a function of the internal energy
title_full_unstemmed Re-evaluation of experimental data on the second virial coefficient for steam and development of its analytical representation as a function of the internal energy
title_sort re-evaluation of experimental data on the second virial coefficient for steam and development of its analytical representation as a function of the internal energy
publisher EDP Sciences
series EPJ Web of Conferences
issn 2100-014X
publishDate 2013-04-01
description A re-evaluation of the second virial coefficient of steam is presented in the paper. The work is a part of broader effort to develop a formulation of the properties of dry and metastable steam suitable for CFD computations. The re-evaluation follows up previous work by Harvey and Lemmon [1], however with a special care for the lower temperature region close to the triple point and including more experimental data. The second virial coefficient was evaluated from volumetric (pvT) data, calorimetric measurements for saturated vapor, steam expansion experiments (measurements of the Joule–Thomson coefficient and the isothermal throttling coefficient) and measurements of the speed of sound. To accurately evaluate the uncertainty of calorimetric measurements, the uncertainty of the temperature derivative of the saturation pressure was determined based on refitting of the IAPWS saturation pressure formula to the experimental data. In the second step, the evaluated data and their uncertainties were used to develop an analytical formula to compute the second virial coefficient as function of internal energy in a range corresponding to the ideal-gas temperatures from 273.16 K to 1073.15 K. The choice of internal energy and density as independent variables is required for the CFD computations to avoid time-consuming iterations.
url http://dx.doi.org/10.1051/epjconf/20134501024
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