How Is Energy Transferred in a Refrigeration Compressor System?

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Energy transfer in a refrigeration compressor system involves analyzing the refrigerant R134a as it transitions from saturated vapor to superheated vapor. The refrigerant enters at 0.14 MPa and exits at 0.8 MPa and 50 degrees Celsius, with a mass flow rate of 0.04 kg/s. The discussion emphasizes that energy calculations can be performed on a per unit mass basis, eliminating the need for direct mass values. Kinetic energy can be calculated using the formula V²/2, while thermodynamic properties like specific enthalpy are typically expressed in J/kg. Understanding these principles is crucial for determining energy transfer rates into and out of the compressor.
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Hi guys i really need some help on this question.

Refrigerant 134a enters the compressor of a refrigeration system as saturated vapour at 0.14MPa and leaves as superheated vapour at 0.8MPa and 50 degrees celsius as a rate of 0.04kg/s. The suction area of the compressor is 10cm^2 and the discharge area 5cm^2. Determine the rates od energy transfer by mass into and out of the compressor, neglecting potential energy. Note the order of magnitude of the enthalpy and kinetic energy terms.

I can't seem to be able to get the value for the mass. can someone help? thanks
 
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Determine the rates od energy transfer by mass into and out of the compressor
One does not need mass, since the problem seems to be asking for energy on a per unit mass basis.

The kinetic energy per unit mass is simply V2/2. Thermodynamic properties are usually given on a per unit mass basis, e.g. specific enthalpy, h (J/kg), or internal energy, u (J/kg).

Mass flow rate is given - 0.04kg/s - and assuming the continuity equation, as steady-state, mass rate (in) = mass rate (out), otherwise there would be an accumulation (if mass flow in exceeds mass flow out) of the system.
 
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