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Caloric Equations of State

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Technical Thermodynamics for Engineers
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Abstract

In the previous chapters the law of energy conservation has been thoroughly discussed. By this, it was possible to evaluate thermodynamic systems energetically. A distinction has been made between closed and open systems. However, next to thermal state values, such as pressure p or temperature T, that can be measured easily, a new category of state values has been introduced: These state values, i.e. specific internal energy u and specific enthalpy h for instance, can not be determined by a sensor and thus need to be calculated.

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Notes

  1. 1.

    Such as \(\left[ u\right] ={1}{\frac{\text {kJ}}{\text {kg}}}\) and \(\left[ h\right] ={1}{\frac{\text {kJ}}{\text {kg}}}\).

  2. 2.

    The indices at the brackets indicate, that this variable is kept constant!

  3. 3.

    At constant specific volume v.

  4. 4.

    At constant pressure p.

  5. 5.

    The thermodynamic proof is given in Sect. 12.3.2.

  6. 6.

    To be honest, it is even difficult to find a physical meaning of the internal energy. Though you probably have accepted its existence by now.

  7. 7.

    Known as integrating factor!

  8. 8.

    Similar to the first law of thermodynamics: The state value internal energy is influenced by process values work and heat!

  9. 9.

    For the Gibbs free enthalpy there is a physical motivation for chemical reactive systems, e.g. fuel cells or Lithium Ion batteries. This will be handled in part III of this book, see Sect. 24.3!

  10. 10.

    With the assumptions, that \(c_{v}=\text {const.}\) and \(c_{p}=\text {const.}\)

  11. 11.

    Indicated by the v-subscript.

  12. 12.

    Indicated by the p-subscript.

  13. 13.

    Very slow is a synonym for no turbulence inside, see also Theorem 7.25.

  14. 14.

    Gravity constant g is not relevant, since the piston is operated horizontally.

  15. 15.

    The change of kinetic energy can be ignored, since the change of state is quasi-static! There is no change of potential energy, since the cylinder is horizontal!

  16. 16.

    According to \(V=\frac{mRT}{p}\).

  17. 17.

    Mind, that \(H=mh\).

  18. 18.

    Fluid motion would need to be initiated, e.g. by a moving piston.

  19. 19.

    Mind, that \(U=mu\).

  20. 20.

    This part is for the advanced readers, who are already familiar with the Ts-diagram, see Sect. 13.4.

  21. 21.

    Assuming, that \(c_{p}=\text {const.}\)!

  22. 22.

    For the calculation a temperature difference is required, so it does not make any difference, if you apply \(\Delta \vartheta \) or \(\Delta T\), see Eq. 12.175!

  23. 23.

    The specific enthalpy remains constant!

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Correspondence to Achim Schmidt .

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Schmidt, A. (2019). Caloric Equations of State. In: Technical Thermodynamics for Engineers. Springer, Cham. https://doi.org/10.1007/978-3-030-20397-9_12

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  • DOI: https://doi.org/10.1007/978-3-030-20397-9_12

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  • Publisher Name: Springer, Cham

  • Print ISBN: 978-3-030-20396-2

  • Online ISBN: 978-3-030-20397-9

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