Startseite Technik Advances in triple tube heat exchangers regarding heat transfer characteristics of single and two-phase flows in comparison to double tube heat exchangers part 1
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Advances in triple tube heat exchangers regarding heat transfer characteristics of single and two-phase flows in comparison to double tube heat exchangers part 1

  • Dogan Akgul ORCID logo , Hatice Mercan ORCID logo , Ozgen Acikgoz ORCID logo und Ahmet Selim Dalkilic ORCID logo EMAIL logo
Veröffentlicht/Copyright: 30. Oktober 2023
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Abstract

Triple concentric-tube heat exchangers are used widely in refrigeration, drying, energy storage, chemical systems, and the food industry. To handle excessive temperature differences, the heat transfer area, as an option, the heat exchanger’s length, is necessary to be increased. Triple tubes have a significant advantage in this regard in comparison to double ones. The target of this review is to discuss the most recent publications, including the single-phase flows in these heat exchangers, focusing on the heat transfer and hydrodynamic characteristics, and to classify them with various contemporary aspects. The operating conditions, enhanced surfaces, and sizes, as well as the geometrical parameters, are categorized as being part of experimental, numerical, and analytical research. The studies indicate that the heat transfer characteristics of triple concentric-tube heat exchangers are better than those of double tube heat exchangers. In single-phase studies, the convective and overall heat transfer coefficients, Nusselt number, heat transfer rate, and effectiveness are greater in triple heat exchangers than in double heat exchangers, and the heat exchanger length required to achieve the same heat transfer performance is shorter in triple heat exchangers than in double heat exchangers. Heat transfer surface area increases by adding a concentric third tube. Advanced surfaces enhance heat transfer compared to smooth surfaces and flow turbulence in comparison to smooth surfaces. Heat transfer from triple-one enhanced surfaces is not well-analyzed. Design and use of triple ones as a double one’s alternative should advance shortly.


Corresponding author: Ahmet Selim Dalkilic, Department of Mechanical Engineering, Faculty of Mechanical Engineering, Yildiz Technical University (YTU), Istanbul 34349, Türkiye, E-mail:

Acknowledgment

The authors would like to acknowledge that this paper is submitted in partial fulfilment of the requirements for PhD degree at Yildiz Technical University.

  1. Research ethics: Not applicable.

  2. Author contributions: The authors have accepted responsibility for the entire content of this manuscript and approved its submission.

  3. Competing interests: The authors state no conflict of interest.

  4. Research funding: This work was supported by a grant of the Yildiz Technical University Scientific Research Project Coordination Unit, YTU-BAPK, Project no: FCD-2021-4267.

  5. Data availability: Not applicable.

Nomenclature

f

friction factor

h

heat transfer coefficient, W/m2°C

Nu

Nusselt number

Re

Reynolds number

Q ˙

heat transfer rate, W

U

overall heat transfer coefficient, W/m2°C

Greek letters

ΔP

pressure drop

ε

effectiveness

Acronyms

CFD

computational fluid dynamics

DTHEX

double tube heat exchanger

HEX

heat exchanger

HT

heat transfer

LMTD

logarithmic mean temperature difference

TTHEX

triple tube heat exchanger

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Received: 2023-03-31
Published Online: 2023-10-30
Published in Print: 2023-12-15

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