Thiele hard sphere equation of state: Difference between revisions
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where: | where: | ||
:<math>Z_{hs}</math> is the compressibility factor of the hard sphere fluid; | :<math>Z_{hs}</math> is the [[compressibility factor]] of the hard sphere fluid; | ||
:<math>p_{hs}</math> is the pressure of the fluid; | :<math>p_{hs}</math> is the [[pressure]] of the fluid; | ||
:<math>V_m</math> is the molar volume of the fluid; | :<math>V_m</math> is the molar volume of the fluid; | ||
:<math>T</math> is the absolute temperature of the fluid; | :<math>T</math> is the absolute [[temperature]] of the fluid; | ||
:<math>R</math> is the gas constant; and | :<math>R</math> is the [[molar gas constant]]; and | ||
:<math>\eta</math> is the [[packing fraction]] of the fluid. | :<math>\eta</math> is the [[packing fraction]] of the fluid. | ||
Revision as of 23:18, 12 June 2024
The Thiele hard sphere equation of state is an equation of state for modeling a hard sphere fluid developed by Thiele in 1963 [1]. The equation provides a better approximation of the repulsive forces between molecules than the Van der Waals repulsive term. The equation is given below:
,
where:
- is the compressibility factor of the hard sphere fluid;
- is the pressure of the fluid;
- is the molar volume of the fluid;
- is the absolute temperature of the fluid;
- is the molar gas constant; and
- is the packing fraction of the fluid.
In terms of accuracy, the Thiele equation is superseded by the Carnahan-Starling equation of state