Isentropic Specific Enthelpy HELP

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SUMMARY

The discussion centers on calculating the isentropic specific enthalpy (hout,s) for a compressor in a vapor compression cycle (VCC) system. Andreas seeks clarity on the equation for enthalpy change, specifically hout = (hout,s - hin)/ns + hin, where ns represents isentropic efficiency. The key takeaway is that hout,s is determined by the inlet temperature and pressure, requiring reference to thermodynamic tables to find the corresponding outlet enthalpy at the same entropy level. Accurate modeling necessitates understanding that hout,s varies with suction pressure, making constant values inadequate for precise calculations.

PREREQUISITES
  • Understanding of vapor compression cycle (VCC) systems
  • Familiarity with thermodynamic tables for enthalpy and entropy
  • Knowledge of isentropic efficiency calculations
  • Basic principles of thermodynamics, particularly enthalpy changes
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  • Research how to utilize thermodynamic tables for specific enthalpy calculations
  • Learn about the impact of suction pressure on isentropic enthalpy in VCC systems
  • Study the derivation and application of isentropic efficiency in compressor performance
  • Explore advanced modeling techniques for VCC systems to improve accuracy
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Engineers, thermodynamics students, and HVAC professionals involved in designing or optimizing vapor compression cycle systems will benefit from this discussion.

bobboviking
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Hi guys,

I'm struggling with some equations regarding the enthalpy change over a compressor in a vcc system.

I'm currently working on a model for the whole system and I think I've got all equations except the one describing the enthalpy difference betweeen the inlet and outlet of the compressor.
I can't really understand how to handle the isentropic specific enthalpy, hout,s, in the following equation:

hout = (hout,s - hin)/ns + hin

where ns is the isentropic efficiency

I also know that ns = (Tout,s-Tin)/(Tout-Tin) (assuming constant specific heat)

I would prefer the model to be as "general" as possible, meaning that I don't have to perform a bunch of experimental test to determine certain coefficients.

I would greatly appreciate some help with how to calculate/estimate hout,s. I think that the value of hout,s depends on the suction pressure (?) so assuming a constant value (from example a table at some operating condition) isn't good enough for an accurate model? I mean that value of hout,s does change when the system moves from that particular condition, right?

Thanks in advance,
Andreas
 
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To get the isentropic enthalpy out, you start with the inlet conditions of temperature and pressure and determine from the tables the entropy in. You must have already don this since you seem to know hin. Then you look up in your tables the enthalpy at the outlet pressure and at the same entropy as inlet. Simple as that. This is hout,s.
 

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