Understanding Cubic Equations of State (Pressure-Volume Relationship)

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SUMMARY

This discussion focuses on the pressure-volume relationship described by cubic equations of state, specifically using the equation P = (RT/(V-b)) - (a/((V+εb)(V+σb))). The user, Ben, initially miscalculated the derivative of pressure with respect to volume while keeping temperature constant, which led to confusion regarding the existence of extrema on isotherm lines. After correcting his differentiation, he acknowledged that the terms in the equation can indeed lead to local minima and maxima, particularly for isotherm T3 at temperatures below the critical temperature.

PREREQUISITES
  • Understanding of chemical thermodynamics principles
  • Familiarity with cubic equations of state
  • Knowledge of differentiation in calculus
  • Ability to interpret thermodynamic diagrams and isotherms
NEXT STEPS
  • Study the implications of critical temperature on phase behavior
  • Learn about the van der Waals equation and its applications
  • Explore graphical methods for analyzing isotherm lines
  • Investigate the role of constants a, b, ε, and σ in cubic equations of state
USEFUL FOR

Chemical engineers, thermodynamics students, and professionals involved in fluid property evaluation and phase behavior analysis will benefit from this discussion.

ben_ob1
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I am trying to teach myself some chemical thermodynamics, in particular some methods for fluid property evaluation. I am reading an excellent book which has helped a lot ("Introduction to Chemical Engineering Thermodynamics", Smith-Van Ness-Abbott, Ed. 7, ISBN: 007-124708-4).

One thing that the book described, which I am now having some problems with, is the pressure-volume relationship of the cubic equations of state. Figure 3.11 in this book (page 92) shows a nice graph of this relationship with 3 isotherm lines. I have tried to make my own version of this figure (hopefully it is attached ok):

attachment.php?attachmentid=37873&stc=1&d=1312914978.jpg


The diagram shows that at temperatures less than the critical temperature (e.g. the T3 line) and for low pressures there are 3 vapour solutions (intersections with a horizontal pressure line).

Here is the equation:
P=\frac{RT}{V-b}-\frac{a}{\left(V+\epsilon b\right)\left(V+\sigma b\right)}

Where P is pressure, T is temperature and V is molar volume; a is a function of temperature (but is always positive) and b, \epsilon and \sigma are positive constants; R is the universal gas constant.

Differentiating this with respect to Volume while keeping T constant (an isotherm line) gives:
\left(\frac{dP}{dV}\right)_{T}=-\frac{RT}{\left(b-V\right)^{2}}-\frac{a\left(\epsilon b + \sigma b + 2V\right)}{\left(V+\epsilon b\right)^{2}\left(V+\sigma b\right)^{2}}

Did I do this right? If this differential is correct then I don't see how there can be any extrema (maxima or minima) for any isotherm lines. The 2 terms in the equation would have to cancel each other out in order for the differential to equal zero. As far as I can see both terms will always have the same sign (for positive values of V) meaning they can never cancel out. Is my logic wrong? How does the isotherm T3 get its local minimum and local maximum?

Hope you can help explain this for me.
Ben.
 

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ben_ob1 said:
Differentiating this with respect to Volume while keeping T constant (an isotherm line) gives:
\left(\frac{dP}{dV}\right)_{T}=-\frac{RT}{\left(b-V\right)^{2}}-\frac{a\left(\epsilon b + \sigma b + 2V\right)}{\left(V+\epsilon b\right)^{2}\left(V+\sigma b\right)^{2}}

Oops found the mistake.

\left(\frac{dP}{dV}\right)_{T}=-\frac{RT}{\left(b-V\right)^{2}}+\frac{a\left(\epsilon b + \sigma b + 2V\right)}{\left(V+\epsilon b\right)^{2}\left(V+\sigma b\right)^{2}}
 

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