Find entropy where the temperature is lower than the saturated temperature

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SUMMARY

The discussion focuses on calculating entropy and enthalpy for a system starting at 100 bar and 260°C, where the saturation temperature is 311°C. The user seeks to determine the dryness fraction (x) to compute availability using the formula availability = (h-h0) - T0(s-s0). The specific equations for entropy (s = sf + xsfg) introduce two unknowns, necessitating a method to compute s and h. The ASME steam tables are recommended for accurate calculations.

PREREQUISITES
  • Understanding of thermodynamic properties, specifically enthalpy and entropy.
  • Familiarity with the concept of dryness fraction in steam systems.
  • Knowledge of the ASME steam tables for steam property calculations.
  • Basic grasp of thermodynamic availability and its significance.
NEXT STEPS
  • Study the ASME steam tables for detailed steam property data.
  • Learn how to calculate the dryness fraction (x) in steam systems.
  • Research the concept of thermodynamic availability and its applications.
  • Explore the use of Keenan & Keyes steam tables as an alternative resource.
USEFUL FOR

Thermodynamic engineers, mechanical engineers, and students studying thermodynamics who need to understand steam properties and calculations related to entropy and enthalpy.

civic_67
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my starting of system is 100 bar and 260 degree C. the saturation temperature for 100 bar is 311 degree C. so in order to find my enthalpy and entropy, i need to find x, dryness fraction. but my equation have 2 unknowns. how do I calculate availability?

availability = (h-h0) -T0(s-s0)

s = sf + xsfg

have 2 unknowns. how do i compute s and h in order to compute availability?
 
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