Abstract
Joule–Thomson refrigerators operating with mixtures require heat exchangers with an effectiveness of over 96% for the system to function. The hot (high pressure) stream enters the heat exchanger in a superheated condition and leaves in a subcooled state. The cold (low pressure) stream, on the other hand, enters the heat exchanger in a two-phase state and leaves in a superheated state. The streams undergo a temperature change of over 200 K in the heat exchanger. The above requirements mandate the use of innovative heat transfer surfaces in the heat exchanger. Coiled wire-finned heat exchangers have been employed successfully in this work. In this paper, we present the performance of the J–T refrigerator with two different wire-finned heat exchangers (wire-fin pitches of 8 mm and 12.7 mm) measured in our test stand. About 20 K lower temperature could be obtained when the wire-fin pitch was changed from 12.7 to 8 mm. The exergy efficiency of the refrigerator also improved.
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Abbreviations
- d :
-
Diameter (mm)
- D :
-
Coil diameter (mm)
- h :
-
Enthalpy (kJ kg−1)
- H p :
-
High pressure (bar)
- HX:
-
Heat exchanger
- L :
-
Length (mm)
- L p :
-
Low pressure (bar)
- ṅ :
-
Mass flow rate of the refrigerant (kg s−1)
- p :
-
Pitch of the wire (mm)
- s :
-
Specific entropy (KJ K−1)
- t :
-
Time (min)
- T :
-
Temperature of the refrigerant (K)
- Q :
-
Applied heat load (W)
- Evap:
-
Evaporator
- In:
-
Inside
- O:
-
Ambient
- Out:
-
Outside
- Ref:
-
Actual
- S:
-
Shell
- Tube:
-
Tube
- we:
-
Warm end
- * :
-
Equivalent
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Kruthiventi, S.S.H., Venkatarathnam, G. Performance of J–T refrigerators operating with mixtures and coiled wire-finned heat exchangers. J Therm Anal Calorim 141, 2169–2175 (2020). https://doi.org/10.1007/s10973-020-09338-y
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DOI: https://doi.org/10.1007/s10973-020-09338-y