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Recuperators: Through-the-Wall Nonstoring Exchangers

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Abstract

Recuperators are heat exchangers wherein the two fluids transferring heat are kept away from each other by a wall. Their design requires two pieces of information.

$$ \frac{1}{UA}=\frac{1}{h_1{A}_1}+\frac{\Delta x}{k{A}_{\mathrm{mean}}}+\frac{1}{h_2{A}_2} $$

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Notes

  1. 1.

    Note that uppercase letters \( \dot{M} \), C, and T represent the shell-side fluid; lowercase letters \( \dot{m} \), c, and t represent the tube-side fluid; ΔT = T – t represents the temperature driving force; and subscripts 1 and 2 stand for the entering and leaving fluid stream, respectively.

References and Related Readings

  • B.S. Baclic, A simplified formula for cross flow for heat exchanger effectiveness. ASME J. Heat Transf. 100, 746 (1978)

    Article  Google Scholar 

  • R.A. Bowman, A.C. Mueller, W.M. Nagle, Mean temperature difference in design. Trans. ASME 62, 283 (1940)

    Google Scholar 

  • V. Cavesano (ed.), Process Heat Exchange, Sec. 1 (McGraw-Hill, New York, 1979). Presents the collective wisdom and practical art of real live designers of recuperators

    Google Scholar 

  • N.L. Hurd, Mean temperature difference in the field or bayonet tube. Ind. Eng. Chem. 38, 1266 (1946)

    Article  CAS  Google Scholar 

  • M. Jakob, Heat Transfer, Chapter 34 (Wiley, New York, 1957)

    Google Scholar 

  • W.A. Kays, A.L. London, Compact Heat Exchangers, 2nd edn. (McGraw-Hill, New York, 1964)

    Google Scholar 

  • D.Q. Kern, Process Heat Transfer (McGraw-Hill, New York, 1950). An excellent primary reference to recuperators of all types

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  • A.C. Mueller, in Handbook of Heat Transfer, ed. by W.M. Roshenow, J.P. Hartnett, Sec. 18, (McGraw-Hill, New York, 1973)

    Google Scholar 

  • J.H. Perry, Chemical Engineers’ Handbook, 3rd edn. (McGraw-Hill, New York, 1950)

    Google Scholar 

  • TEMA, Standards of Tubular Exchanger Manufacturers Association, 6th edn. (Tubular Exchanger Manufacturers Association, Inc, New York, 1978)

    Google Scholar 

  • J.P. Todd, H.B. Ellis, Applied Heat Transfer (Harper & Row, New York, 1982), p. 430

    Google Scholar 

  • R. Turton, C.D. Ferguson, O. Levenspiel, Performance and design charts for heat exchangers. J. Heat Transf. 106, 893 (1984). Chem. Eng. 93, 81, Aug. 18, 1986

    Article  CAS  Google Scholar 

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Levenspiel, O. (2014). Recuperators: Through-the-Wall Nonstoring Exchangers. In: Engineering Flow and Heat Exchange. Springer, Boston, MA. https://doi.org/10.1007/978-1-4899-7454-9_13

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