Redlich-Kwong equation of state: Difference between revisions

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:<math>b = \frac{9(2^{1/3}-1)}{3}  \frac{RT_c}{p_c}  \approx 0.08664034995 \frac{RT_c}{p_c}</math>
:<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 16:09, 7 November 2011

The Redlich-Kwong equation of state is [1]:

[p+aT1/2v(v+b)](v−b)=RT.

The Redlich-Kwong equation of state has a critical point compressibility factor of [2]:

Zc=pcvcRTc=13

leading to

a=19(21/3−1)R2Tc5/2pc≈0.4274802336R2Tc5/2pc

and

b=(21/3−1)3RTcpc≈0.08664034995RTcpc

where p is the pressure, T is the temperature and R is the molar gas constant. Tc is the critical temperature and Pc 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:

α(T)=(1+(0.48508+1.55171ω−0.15613ω2)(1−TTc))2

where Tc is the critical temperature and ω is the acentric factor for the gas. This leads to an equation of state of the form:

[p+aα(T)v(v+b)](v−b)=RT

or equivalently:

p=RTv−b−aα(T)v(v+b)


References