Redlich-Kwong equation of state: Difference between revisions
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Carl McBride (talk | contribs) (Added critical point compressibility factor) |
Carl McBride (talk | contribs) m (Corrected pre-factor for b) |
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:<math>b = \frac{ | :<math>b = \frac{(2^{1/3}-1)}{3} \frac{RT_c}{p_c} \approx 0.08664034995 \frac{RT_c}{p_c}</math> | ||
where <math>p</math> is the [[pressure]], <math>T</math> is the [[temperature]] and <math>R</math> is the [[molar gas constant]]. <math>T_c</math> is the [[critical points | critical]] temperature and <math>P_c</math> is the pressure at the critical point. | where <math>p</math> is the [[pressure]], <math>T</math> is the [[temperature]] and <math>R</math> is the [[molar gas constant]]. <math>T_c</math> is the [[critical points | critical]] temperature and <math>P_c</math> is the pressure at the critical point. |
Revision as of 17:09, 7 November 2011
The Redlich-Kwong equation of state is [1]:
- .
The Redlich-Kwong equation of state has a critical point compressibility factor of [2]:
leading to
and
where is the pressure, is the temperature and is the molar gas constant. is the critical temperature and is the pressure at the critical point.
Soave Modification
A modification of the the Redlich-Kwong equation of state was presented by Giorgio Soave in order to allow better representation of non-spherical molecules[3]. In order to do this, the square root temperature dependence was replaced with a temperature dependent acentricity factor:
where is the critical temperature and is the acentric factor for the gas. This leads to an equation of state of the form:
or equivalently:
References
- ↑ Otto Redlich and J. N. S. Kwong "On the Thermodynamics of Solutions. V. An Equation of State. Fugacities of Gaseous Solutions", Chemical Reviews 44 pp. 233-244 (1949)
- ↑ Reino. W. Hakala "The value of the critical compressibility factor for the Redlich-Kwong equation of state of gases", Journal of Chemical Education 62 pp. 110-111 (1985)
- ↑ Giorgio Soave "Equilibrium constants from a modified Redlich-Kwong equation of state", Chemical Engineering Science 27 pp. 1197-1203 (1972)