Joule-Thomson Expansion of a van der Waals gas

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SUMMARY

The discussion focuses on the Joule-Thomson expansion of a van der Waals gas, specifically determining the minimal starting temperature for cooling to occur. The enthalpy equation derived is H = (5/2)Nτ + N²(bτ/(V - Nb) - 2a/V), with the conservation of enthalpy applied across the system. The initial temperature τ₁ was calculated as τ₁ = (2Na((V₁ + V₂)/(V₁V₂)))/((5/2) + (Nb/(V₁ - Nb))). However, it was concluded that the correct approach requires setting T₂ equal to T₁ to find the boundary between heating and cooling.

PREREQUISITES
  • Understanding of van der Waals gas equations
  • Knowledge of thermodynamic principles, specifically enthalpy conservation
  • Familiarity with Joule-Thomson expansion concepts
  • Basic calculus for integrating thermodynamic equations
NEXT STEPS
  • Study the derivation of the van der Waals equation of state
  • Learn about the Joule-Thomson coefficient and its implications
  • Investigate the relationship between temperature, pressure, and volume in real gases
  • Explore thermodynamic identities and their applications in phase transitions
USEFUL FOR

This discussion is beneficial for thermodynamics students, chemical engineers, and physicists interested in gas behavior under varying pressure and temperature conditions, particularly in applications involving van der Waals gases.

eep
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Hi,
Consider a pipe with thermally insulated walls. A thermally insulating porous plug in the pipe provides a constriction to the flow of gas. We model this as a sudden jump in pressure. A continuous stream of gas flows from left to right, with the pressure p_1 upstream being larger than the pressure p_2 downstream. The gas is in thermal equilibrium on each of the two sides.

For a van der Waals gas, what is the minimal starting temperature for cooling to occur in a Joule-Thomson expansion?

I was able to derive that the enthalphy for a van Der Waals gas is

<br /> H = \frac{5}{2}N\tau + N^2(\frac{b\tau}{V - Nb} - \frac{2a}{V})<br />

and I know that enthalphy is conserved in the process.

I set the enthalphy on both sides equal to one another, and then set \tau_2 equal to zero since that is the lowest possible temperature. Solving the equation for \tau_1 left me with

<br /> \tau_1 = \frac{2Na(\frac{V_1 + V_2}{V_1V_2})}{\frac{5}{2} + \frac{Nb}{V_1 - Nb}}<br />

I assumed that N would be the same on both sides of the barrier. I don't like this result, however, as it depends on V_1 and V_2. Is this correct or should I be approaching this differently?
 
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eep said:
Hi,
Consider a pipe with thermally insulated walls. A thermally insulating porous plug in the pipe provides a constriction to the flow of gas. We model this as a sudden jump in pressure. A continuous stream of gas flows from left to right, with the pressure p_1 upstream being larger than the pressure p_2 downstream. The gas is in thermal equilibrium on each of the two sides.

For a van der Waals gas, what is the minimal starting temperature for cooling to occur in a Joule-Thomson expansion?

I was able to derive that the enthalphy for a van Der Waals gas is

<br /> H = \frac{5}{2}N\tau + N^2(\frac{b\tau}{V - Nb} - \frac{2a}{V})<br />

and I know that enthalphy is conserved in the process.

I set the enthalphy on both sides equal to one another, and then set \tau_2 equal to zero since that is the lowest possible temperature. Solving the equation for \tau_1 left me with

<br /> \tau_1 = \frac{2Na(\frac{V_1 + V_2}{V_1V_2})}{\frac{5}{2} + \frac{Nb}{V_1 - Nb}}<br />

I assumed that N would be the same on both sides of the barrier. I don't like this result, however, as it depends on V_1 and V_2. Is this correct or should I be approaching this differently?
This was not done correctly. In order to be at the boundary between heating and cooling, we must have ##T_2=T_1##.

For a VDW gas, we find that $$du=C_vdT+a\frac{dv}{v^2}$$The form of this equation implies that Cv is independent of v, and so is equal to the ideal gas Cv. So integrating this equation from the initial to the final state yields $$\Delta u=a\left(\frac{1}{v(T_1,P_1)}-\frac{1}{v(T_1,P_2)}\right)$$So we have $$\Delta h=a\left(\frac{1}{v(T_1,P_1)}-\frac{1}{v(T_1,P_2)}\right)+P_2v(T_1,P_2)-P_1v(T_1,P_1)$$$$=0$$
One needs to solve for the value of T1 that makes good on this equation.
 

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