Abstract
This experimental study investigates the effects of vortex-generator (VG) and Cu/water nanofluid flow on performance of plate-fin heat exchangers. The Cu/water nanofluids are produced by using a one-step method, namely electro-exploded wire technique, with four nanoparticles weight fractions (i.e. 0.1, 0.2, 0.3, and 0.4 %). Required properties of nanofluids are systematically measured, and empirical correlations are developed. A highly precise test loop is fabricated to obtain accurate results of the heat transfer and pressure drop characteristics. Experiments are conducted for nanofluids flow inside the plain and VG channels. Based on the experimental results, utilizing the VG channel instead of the plain channel enhances the heat transfer rate, remarkably. Also, the results show that the VG channel is more effective than the nanofluid on the performance of plate-fin heat exchangers. It is observed that the combination of the two heat transfer enhancement techniques has a noticeably high thermal–hydraulic performance, about 1.67. Finally, correlations are developed to predict Nusselt number and friction factor of nanofluids flow inside the VG channel.
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Abbreviations
- A c :
-
Minimum free flow area (m2)
- A ch.f :
-
Total surface area in contact with working fluid (m2)
- C p :
-
Specific heat (J kg−1 K−1)
- D h :
-
Hydraulic diameter (m)
- F h :
-
Channel height (m)
- F p :
-
Channel pitch (m)
- G :
-
Mass velocity (kg m−2 s−1)
- h :
-
Effective heat transfer coefficient (W m−2 K−1)
- L :
-
Channel length (m)
- M :
-
Number of the independent variables
- m :
-
Mass flow rate (kg s−1)
- Q conv :
-
Convective heat transfer rate (W)
- T :
-
Temperature (K)
- t :
-
Channel thickness (m)
- \( \dot{V} \) :
-
Volumetric flow rate (m3 s−1)
- V h :
-
Vortex height (m)
- V l :
-
Longitudinal vortex spacing (m)
- V t :
-
Transverse vortex spacing (m)
- ∆P :
-
Pressure drop (Pa)
- R :
-
Dependent variable
- R 2 :
-
Coefficient of determination
- ∆T :
-
Temperature difference (K)
- X :
-
Independent variables
- α :
-
Angle of attack (°)
- ρ :
-
Density (kg m−3)
- μ :
-
Dynamic viscosity (Pa s)
- κ :
-
Thermal conductivity (W m−1 K−1)
- φ :
-
Nanoparticle weight fraction
- j :
-
Colburn factor = Nu/RePr 1/3
- JF :
-
Thermal–hydraulic performance factor = (j VGC /j PC )/(f VGC /f PC )1/3
- f :
-
Fanning friction factor = ρD h ∆P/2LG 2
- Nu :
-
Nusselt number = hD h /κ
- Pr :
-
Prandtl number = μC p /κ
- Re :
-
Reynolds number = GD h /μ
- St :
-
Stanton number = h/GC p
- BF :
-
Base fluid
- NF :
-
Nanofluid
- PC :
-
Plain channel
- DW:
-
Deionized-water
- EEW:
-
Electro-exploded wire
- PEC:
-
Performance evaluation criteria
- PFHE:
-
Plate-fin heat exchangers
- PI:
-
Process intensification
- TEM:
-
Transmission electron microscope
- THW:
-
Transient hot-wire
- VG:
-
Vortex-generator
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Acknowledgments
The author would like to express their thanks to University of Semnan and Materials and Energy Research Center for their financial supports through the set-up fabrication and research implementation.
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Khoshvaght-Aliabadi, M. Thermal performance of plate-fin heat exchanger using passive techniques: vortex-generator and nanofluid. Heat Mass Transfer 52, 819–828 (2016). https://doi.org/10.1007/s00231-015-1603-6
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DOI: https://doi.org/10.1007/s00231-015-1603-6