Understanding Steam at High Pressures: Enthalpy and Volume Explained

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SUMMARY

This discussion focuses on the behavior of steam at high pressures, specifically analyzing the specific volume and enthalpy at 40 bar and 350°C compared to 20 bar and 350°C. At 40 bar, the specific volume is approximately 66.4 m³/kg with an enthalpy of 3095 kJ/kg, while at 20 bar, the specific volume increases to 138.56 m³/kg and the enthalpy rises to 3138.6 kJ/kg. The conversation highlights the non-ideal behavior of steam, emphasizing that the relationship between pressure, volume, and enthalpy does not follow simple gas laws due to steam's compressibility and phase changes.

PREREQUISITES
  • Understanding of steam tables and thermodynamic properties
  • Knowledge of enthalpy and its calculation (h = U + PV)
  • Familiarity with the concept of compressibility factors
  • Basic principles of phase changes in substances
NEXT STEPS
  • Study the implications of compressibility in real gases versus ideal gases
  • Learn about the phase behavior of steam under varying pressure and temperature conditions
  • Explore the derivation and application of the enthalpy equation in thermodynamics
  • Investigate the effects of temperature on enthalpy in non-ideal gas scenarios
USEFUL FOR

Engineers, thermodynamics students, and professionals working with steam systems or high-pressure applications will benefit from this discussion, particularly those involved in energy production and heat exchange processes.

Dogberry
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Hi,

Can someone please explain this to me:

Looking at the steam tables, if I have steam at 40bar and 350C then the specific volume is ~66.4 m^3/kg and enthalpy is 3095 kJ/kg.

If I halve the pressure to 20bar (still at 350C), thus 'doubling' the specific volume to 138.56 m^3/kg, the enthalpy becomes 3138.6 kJ/kg.

Two questions:

1. The volume is not exactly double, it's more than that, and while understand this is not an ideal gas, my understanding of the compressibility factor led me to believe the volume should be greater than expected at higher pressures. This is the other way round.

2. From my understanding of enthalpy: h = U + PV, because the volume has 'doubled' and the pressure has halved, the enthalpy should have stayed approximately constant. It doesn't. In fact, to achieve the same enthalpy, I would need to drop the temperature to 330C (@20bar). I don't understand why, where is this drop captured in the equation? Surely lower temperature = lower enthalpy?

Any help will be greatly appreciated and thank you for your time!

Ed
 
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Dogberry said:
Hi,

Can someone please explain this to me:

Looking at the steam tables, if I have steam at 40bar and 350C then the specific volume is ~66.4 m^3/kg and enthalpy is 3095 kJ/kg.

If I halve the pressure to 20bar (still at 350C), thus 'doubling' the specific volume to 138.56 m^3/kg, the enthalpy becomes 3138.6 kJ/kg.

Two questions:

1. The volume is not exactly double, it's more than that, and while understand this is not an ideal gas, my understanding of the compressibility factor led me to believe the volume should be greater than expected at higher pressures. This is the other way round.

2. From my understanding of enthalpy: h = U + PV, because the volume has 'doubled' and the pressure has halved, the enthalpy should have stayed approximately constant. It doesn't. In fact, to achieve the same enthalpy, I would need to drop the temperature to 330C (@20bar). I don't understand why, where is this drop captured in the equation? Surely lower temperature = lower enthalpy?

Any help will be greatly appreciated and thank you for your time!
Start with dH = dU + d(PV). So \Delta H = \int dH = \Delta U + <br /> \int VdP + \int PdV

If \int Pdv + \int VdP = 0 there is no change in enthalpy if temperature is constant.
But for steam, this is not the case because it is not an ideal gas. \int Pdv + \int VdP &gt; 0. As you compress saturated steam, some of the steam condenses.

AM
 

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