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Performance of J–T refrigerators operating with mixtures and coiled wire-finned heat exchangers

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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)

:

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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Correspondence to S. S. Harish Kruthiventi.

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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

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