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Thermodynamic Optimization of Helium Liquefaction Cycles

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Advances in Cryogenic Engineering

Part of the book series: Advances in Cryogenic Engineering ((ACRE,volume 35 A))

Abstract

With the advent of superconducting technology, there has been a major emphasis in the design of helium refrigeration/liquefaction systems. In the past, refrigeration systems have been designed and built to provide cryogenic cooling to the superconducting windings. However, because of the large demand for refrigeration at cryogenic temperatures and the increase in energy costs, a renewed interest has developed in designing helium refrigeration/liquefaction systems which are much more energy efficient. Recent examples of superconducting applications have been mentioned in the literature [1].

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Abbreviations

h :

= specific enthalpy

:

= mass flow rate

N2 :

= nitrogen mass flow rate

c :

= compressor mass flow rate

T :

= turbine mass flow rate

L :

= liquid helium flow rate

P :

= pressure

\(\dot Q\) :

= heat transfer rate

\(\dot Q_{\rm{hl}}\) :

= heat leak

R :

= gas constant

S :

= entropy

s :

= specific entropy

T :

= temperature

T 0 :

= ambient temperature

T s :

= temperature at which entropy is generated

υ :

= specific volume

W act :

= actual work

ΔW irr :

= irreversible work

W rev :

= reversible work

ΔṠ irr :

= entropy generation term

Δ T :

= temperature difference

References

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© 1980 Springer Science+Business Media New York

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Hubbell, R.H., Toscano, W.M. (1980). Thermodynamic Optimization of Helium Liquefaction Cycles. In: Timmerhaus, K.D., Snyder, H.A. (eds) Advances in Cryogenic Engineering. Advances in Cryogenic Engineering, vol 35 A. Springer, Boston, MA. https://doi.org/10.1007/978-1-4613-9856-1_65

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  • DOI: https://doi.org/10.1007/978-1-4613-9856-1_65

  • Publisher Name: Springer, Boston, MA

  • Print ISBN: 978-1-4613-9858-5

  • Online ISBN: 978-1-4613-9856-1

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