Using Enthelpy to define flow work for a non-ideal gas

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SUMMARY

This discussion focuses on the application of Enthalpy in calculating flow work for non-ideal gases in open systems. The user seeks clarity on the relationship between boundary work, defined as the integral of P dV from V1 to V2, and the Enthalpy equation, Enthalpy = U + PV, where the PV term represents flow work. The confusion arises from the differing results obtained from the integral of P dV and the direct calculation of flow work using P2V2 - P1V1. The user questions the validity of using Enthalpy for flow work calculations due to these discrepancies.

PREREQUISITES
  • Understanding of thermodynamic concepts, specifically boundary work and flow work.
  • Familiarity with the Enthalpy equation and its components (U + PV).
  • Knowledge of calculus, particularly integration techniques for variable relationships.
  • Basic principles of non-ideal gas behavior and equations of state.
NEXT STEPS
  • Study the derivation and implications of the Enthalpy equation in thermodynamics.
  • Learn about the different types of work in thermodynamic systems, including boundary work and flow work.
  • Explore the concept of non-ideal gas behavior and how it affects calculations of work and energy.
  • Investigate the relationship between pressure and volume in various thermodynamic processes, including isothermal and adiabatic processes.
USEFUL FOR

This discussion is beneficial for thermodynamics students, engineers working with fluid systems, and researchers focused on energy transfer in non-ideal gases.

timsea81
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For an open system with mass flowing in and out, where mass exits the system there is work associated with the mass transport. When this work is used to say, push up a piston, this is pretty intuitive, but even when it does not lift a weight since, the force COULD be used to lift a weight, it is thermodynamic work. I'm trying to understand how we quantify that work. Since it is boundary work we say that

Work = the integral of P dV from V1 to V2

And then we have Enthalpy = U + PV, and from what I read the PV term represents the flow work. I don't understand how this is, since the integral of P dV from V1 to V2 is different depending on the relationship between P and V. If you look at work as the area under the P/V curve, you see how you need to more than just the end states to know the integral.

Am I wrong to use Enthalpy to calculate the flow work in this way? Or is there something about it that I don't get, that makes it okay to do so?
 
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For example, if PV^k=C, we write P in terms of V as P=CV^(-k), and the integral of that with respect to V is (-C/k-1)V^(k-1), so from point a to point b the work done is

(-C/k-1)(V2k-1 - V1k-1) but the the change in flow work is just

P2V2 - P1V1I am confused why they are not equal.
 

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