How tds=du+pdv valid for open flow system?

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Discussion Overview

The discussion revolves around the validity of the equation tds = du + pdv in the context of open flow systems, particularly addressing the inclusion of various forms of work and energy, such as kinetic and potential energy, in thermodynamic equations.

Discussion Character

  • Technical explanation
  • Conceptual clarification
  • Debate/contested

Main Points Raised

  • One participant questions why the equation tds = du + pdv is used instead of including other forms of work (e.g., shaft work) in the equation, suggesting that the work done by the system should account for more than just boundary work.
  • Another participant asserts that internal energy (u), specific volume (v), and entropy (s) are state properties that do not depend on the process used to reach thermodynamic equilibrium, emphasizing their independence from kinetic and potential energy.
  • A participant reiterates the concern about kinetic and potential energy in open flow systems, proposing that the equation should be tds = dE + pdv, where E represents total energy, including kinetic and potential components.
  • A further elaboration is made on the nature of state properties, indicating that they are unique functions of temperature and pressure and remain unaffected by the frame of reference or motion of the material.

Areas of Agreement / Disagreement

Participants express differing views on the applicability of the equation tds = du + pdv, with some advocating for the inclusion of additional forms of work and energy, while others maintain that the equation is valid as it stands for thermodynamic equilibrium states.

Contextual Notes

The discussion highlights the limitations of the equation in open flow systems, particularly regarding the assumptions made about energy forms and the specific conditions under which the equation applies.

hemant singh
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I have been having this doubt for long. As by the first law dq=du+dw (neglecting KE and PE change). And we know that the work done by the system can be utilized in things (eg. boundary work, shaft work, shear work, paddle wheel work..etc).
For open flow system replacing dq=tds, we get,
tds=du+ dw (process should be reversible)
if we replace dw= pdv+(shaft work..etc), then we get,
tds=du+pdv+(shaft work..etc)

Why isn't the above equation valid, instead we use tds=du+pdv. Why are we considering only boundary work not other works?
 
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You are aware that u, v, and s are functions of state, independent of any process or kind of equipment arrangement used the bring the material comprising the system to that thermodynamic equilibrium state, correct?

Chet
 
I know that u v s are state properties. But in open flow system KE PE both are present if that is taken into consideration then tds=dE+pdv?
where E is total macroscopic and microscopic energy? Why do we use tds= du+ pdv ?
 
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hemant singh said:
I know that u v s are state properties. But in open flow system KE PE both are present if that is taken into consideration then tds=dE+pdv?
where E is total macroscopic and microscopic energy? Why do we use tds= du+ pdv ?
As you said, u,v,and s are state properties. That means that they each are unique functions of T and P only. So they are actually physical properties of the material being processed, and do not depend on the nature of any process. Also, it doesn't matter whether the material is traveling at 10 km/hr or 0 km/hr, or whether the material is on top of mount Everest or at the bottom of Death Valley. This does not affect its u, v, and s. For example, regarding kinetic energy, to an observer traveling with the same velocity as the material, the material is standing still. Since the properties of a material cannot depend on the frame of reference of the observer, u, v, and s are independent of its Kinetic energy.

Imagine two closely neighboring thermodynamic equilibrium states of a material at temperatures and pressures (T,P) and (T+dT ,P+dP). The equation Tds=du+Pdv describes the unique relationship between ds, du, and dv between these two thermodynamic equilibrium states for the material. So the equation only applies to differentially separated thermodynamic equilibrium states.

Hope this helps. Something else that might help is the following link to my recent Physics Forums Insights article: https://www.physicsforums.com/insights/understanding-entropy-2nd-law-thermodynamics/

Chet
 
Thanks a lot sir.. doubt cleared.
 

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