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Cooldown Temperatures and Cooldown Time during Mist Flow

  • J. W. H. Chi
Part of the Advances in Cryogenic Engineering book series (ACRE, volume 10)

Abstract

In recent years, cryogenic fluids have found wide applications as coolants as well as propellants in rocket propulsion. During transient operation of such systems, the transfer lines or flow passages must be cooled down to the liquid boiling point before the maximum flow rate is attained. In order to design coolant channels and transfer lines, the duration of the cooldown period must be known. Consequently, a number of cooldown studies have been carried out. Burke et al. [1] studied the cooldown of a 175-ft, 2-in.-OD stainless steel line by liquid nitrogen, and Bronson et al. [2] studied the cooldown of a 50-ft, 13/8-in.-ID test section by liquid hydrogen. The former investigator used a gross effect to calculate cooldown time. In this method, an average exit exhaust temperature was used. Bronson et al. [2] assumed a constant wall-to-coolant temperature difference along the entire length of the line. Although these techniques may provide sufficient accuracy when the gross effect over an extremely long transfer line is considered, it is doubtful that they can be applied over a short tube. In addition, these methods do not permit the estimation of instantaneous wall and bulk fluid temperatures.

Keywords

Test Section Mass Flow Rate Wall Temperature Fluid Temperature Boiling Heat Transfer 
These keywords were added by machine and not by the authors. This process is experimental and the keywords may be updated as the learning algorithm improves.

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References

  1. 1.
    J. C. Burke et al., in Advances in Cryogenic Engineering, Vol. 4, Plenum Press, New York (1960), p. 378.Google Scholar
  2. 2.
    J. C. Bronson et al., in Advances in Cryogenic Engineering, Vol. 4, Plenum Press, New York (1960), p. 198.Google Scholar
  3. 3.
    J. W. H. Chi and A. M. Vetere, in Advances in Cryogenic Engineering, Vol. 9, Plenum Press, New York (1964), p. 243.Google Scholar
  4. 4.
    J. W. H. Chi, “Forced Convection Boiling Heat Transfer to Hydrogen,” WANL-TNR-154 (February 21, 1964).Google Scholar
  5. 5.
    H. S. Mickeley, T. K. Sherwood, and C. E. Reed, Applied Mathematics for Chemical Engineers, 2nd ed., McGraw-Hill, New York (1957), p. 304.Google Scholar
  6. 6.
    O. A. Hougen and K. M. Watson, Chemical Process Principles, Part III, J. Wiley & Sons, New York (1947), p. 1084.Google Scholar

Copyright information

© Plenum Press, New York 1965

Authors and Affiliations

  • J. W. H. Chi
    • 1
  1. 1.Westinghouse Electric CorporationPittsburghUSA

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