Advertisement

Single-Phase Flow Performance Evaluation Criteria

  • Sujoy Kumar Saha
  • Hrishiraj Ranjan
  • Madhu Sruthi Emani
  • Anand Kumar Bharti
Chapter
Part of the SpringerBriefs in Applied Sciences and Technology book series (BRIEFSAPPLSCIENCES)

Abstract

This chapter is mainly focused on performance evaluation criteria for single-phase flow. The objectives and constraints of fixed geometry criteria, variable geometry criteria and fixed cross-sectional flow area criteria have been discussed here. The thermal resistance, St and f relations, heat exchanger effectiveness, effect of reduced exchanger flow rate and flow over finned tube bank topics have been presented.

Keywords

Shell and tube heat exchanger Effectiveness NTU Single-phase flow Finned tube banks Fixed geometry criteria Variable geometry criteria Fixed cross-sectional flow rate criteria 

References

  1. 1.
    Bergles AE, Bunn RL, Junkhan GH (1974) Extended performance evaluation criteria for enhanced heat transfer surfaces. Lett Heat Mass Transfer 1:113–120CrossRefGoogle Scholar
  2. 2.
    Garcia A, Vicente PG, Viedma A (2005) Experimental study of heat transfer enhancement with wire coil inserts in laminar-transition-turbulent regimes at different Prandtl numbers. Int J Heat Mass Transfer 48(21–22):4640–4651CrossRefGoogle Scholar
  3. 3.
    Vicente PG, Garcı́a A, Viedma A (2002) Heat transfer and pressure drop for low Reynolds turbulent flow in helically dimpled tubes. Int J Heat Mass Transfer 45(3):543–553CrossRefGoogle Scholar
  4. 4.
    Bergles AE (1981) Applications of heat transfer augmentation. In: Kakac S, Bergles AE, Mayinger F (eds) Heat exchangers: thermal hydraulic fundamentals and design. Hemisphere, Washington, DCGoogle Scholar
  5. 5.
    Gholami A, Wahid MA, Mohammed HA (2017) Thermal–hydraulic performance of fin-and-oval tube compact heat exchangers with innovative design of corrugated fin patterns. Int J Heat Mass Transfer 106:573–592CrossRefGoogle Scholar
  6. 6.
    Petkov VM, Zimparov VD, Bergles AE (2014) Performance evaluation of ducts with non-circular shapes: laminar fully developed flow and constant wall temperature. Int J Therm Sci 79:220–228CrossRefGoogle Scholar
  7. 7.
    White WJ, Wilkie L (1970) The effect of rib profile on heat transfer and pressure loss properties of transversely ribbed roughened surfaces. In: Bergles AE, Webb RL (eds) Augmentation of convective heat and mass transfer. ASME, New York, pp 44–54Google Scholar
  8. 8.
    Usui H, Sano Y, Iwashita K, Isozaki A (1986) Enhancement of heat transfer by a combination of internally grooved rough tube and a twisted tape. Int Chem Eng 26(1):97–104Google Scholar
  9. 9.
    Tauscher R, Mayinger F (1998) Heat transfer enhancement in a plate heat exchanger with rib-roughened surfaces. In: Kakaç S (ed) Energy conservation through heat transfer enhancement of heat exchangers. Nato Advanced Study Institute, Cesme, İzmir, Turkey, pp 121–135Google Scholar
  10. 10.
    Song D, Gu W (1990) The optimization analysis calculation for high performance heat exchanger. In: Deng SJ, Veziroğlu TN, Tan YK, Chen LQ (eds) Heat transfer enhancement and energy conservation. Hemisphere, New York, pp 535–542Google Scholar
  11. 11.
    Sekulic DP, Kmecko I (1995) Three-fluid heat exchanger effectiveness-revisited. J Heat Transfer 117:226–229CrossRefGoogle Scholar
  12. 12.
    Sara ON, Pekdemir T, Yapıcı S, Yılmaz M (2001a) Enhancement of heat transfer from a flat surface in a channel flow by attachment of rectangular blocks. Int J Energy Res 25(7):563–576CrossRefGoogle Scholar
  13. 13.
    Sara ON, Pekdemir T, Yapici S, Yilmaz M (2001b) Heat-transfer enhancement in a channel flow with perforated rectangular blocks. Int J Heat Fluid Flow 22:509–518CrossRefGoogle Scholar
  14. 14.
    Raju KSN, Bansal JC (1981) Design of plate heat exchangers, in low Reynolds number forced convection in channels and bundles. In: ASI proceedings, Ankara, Turkey, pp 597–616Google Scholar
  15. 15.
    Picon-Nunez M, Polley GT, Tores-Reyes E, Gallegos-Munoz A (1999) Surface selection and design of plate-fin heat exchangers. Appl Therm Eng 19:917–931CrossRefGoogle Scholar
  16. 16.
    Nunner W (1958) Heat transfer and pressure drop in rough pipes. AERE Lib/Trans, p 786Google Scholar
  17. 17.
    Norris RH (1939) Proceedings of the fifth international congress of applied mechanics, p 585Google Scholar
  18. 18.
    Miyashita H, Fukushima K, Kometani M, Yamaguchi S (1990) Enhanced heat transfer mechanism using turbulence promoters in rectangular duct. In: Deng SJ, Veziroğlu TN, Tan YK, Chen LQ (eds) Heat transfer enhancement and energy conservation. Hemisphere, New York, pp 159–166Google Scholar
  19. 19.
    Manzoor M, Ingham DB, Heggs PJ (1983) The one-dimensional analysis of fin assembly heat transfer. J Heat Transfer 105:646–651CrossRefGoogle Scholar
  20. 20.
    London AL (1964) Compact heat exchangers: Part 2. surface geometry. Mech Eng 86:31–34Google Scholar
  21. 21.
    Le Foll J (1957) Experimental research heat transfer. La Houille Blanche 1:30–45Google Scholar
  22. 22.
    Kumada M (1998) A study on the high performance ceramic heat exchanger for ultra high temperatures. In: Kakaç S (ed) Energy conservation through heat transfer enhancement of heat exchangers. Nato Advanced Study Institute, Cesme, İzmir, Turkey, pp 597–620Google Scholar
  23. 23.
    Kreith F, Black WZ (1980) Basic heat transfer. Harper & Row, New YorkGoogle Scholar
  24. 24.
    Kern DQ, Kraus AD (1972) Extended surface heat transfer. McGraw-Hill, New YorkGoogle Scholar
  25. 25.
    Horvath CD (1977) Three-fluid heat exchangers of two and three surfaces. Period Polytech 1:33–44Google Scholar

Copyright information

© The Author(s), under exclusive license to Springer Nature Switzerland AG 2020

Authors and Affiliations

  • Sujoy Kumar Saha
    • 1
  • Hrishiraj Ranjan
    • 1
  • Madhu Sruthi Emani
    • 1
  • Anand Kumar Bharti
    • 1
  1. 1.Mechanical Engineering DepartmentIndian Institute of Engineering, Science and Technology, ShibpurHowrahIndia

Personalised recommendations