Abstract
A mathematical model is proposed for predicting the air-side pressure drop and heat-transfer rate of straight fin-tube heat exchangers of a household refrigerator under nofrosting conditions. The six-sigma method is employed to optimize the preliminary critical-to-quality (CTQ). The proposed model is consistent with the experimental data with an error of less than 15 %. The numerical results agree well with the experimental data. It can be applied to evaluate the thermal-hydraulic performance of a fin-tube heat exchanger with varying fin pitch along the airflow direction.
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Abbreviations
- A b/w_F :
-
Surface area of outer tube in j-section without fin thickness
- A c :
-
Cross-section area
- A f :
-
Surface fin area in j-section
- A o :
-
Surface area of outer tube in j-section
- A Tube :
-
Cross-section tube area
- A 0 :
-
Full cross-section area
- C:
-
Nozzle discharge coefficient
- C j :
-
Friction coefficient of j section
- d H :
-
Hydraulic diameter
- d i :
-
Inner diameter of tube
- do :
-
Outer diameter of tube
- D :
-
Diameter
- ε eq :
-
Average roughness height
- f B,1 :
-
Function of bypass body 1
- f B,2 :
-
Function of bypass body 2
- f H :
-
Function of main body
- \({{\bar h}_c}\) :
-
Mean heat-transfer coefficient of coolant
- \({{\bar h}_o}\) :
-
Mean heat-transfer coefficient of air
- L :
-
Length
- l j :
-
Length of j-section
- Nu :
-
Nusselt number
- Π:
-
Perimeter
- ΔPN :
-
Pressure drop of nozzle
- ΔPB,1 :
-
Pressure drop of bypass body 1
- ΔPb,2 :
-
Pressure drop of bypass body 2
- ΔPh :
-
Pressure drop of main body
- ΔPp :
-
Prediction of pressure drop
- ΔPe :
-
Experiment of pressure drop
- ΔPj :
-
Pressure drop of j-section
- ΔPfj :
-
Frictional pressure drop of j-section
- ΔPtj :
-
Tube bank pressure drop of j-section
- ρair :
-
Density of air
- Pr :
-
Prandtl number
- q c :
-
Heat flux density of coolant
- q a :
-
Heat flux density of air
- Q p :
-
Prediction of heat-transfer rate
- Q e :
-
Experiment of heat-transfer rate
- R e :
-
Reynolds number
- Re dH :
-
Reynolds number of hydraulic diameter
- Re n :
-
Reynolds number of narrow cross-section
- S l :
-
Longitudinal pitch
- S t :
-
Transverse pitch
- t a :
-
Temperature of air
- t F :
-
Temperature of fin
- t o :
-
Temperature of outer tube surface
- \({{\bar t}_o}\) :
-
Mean temperature of outer tube surface
- \({{\bar t}_c}\) :
-
Mean temperature of coolant
- u j :
-
Number of tubes in the airflow direction in j-section
- V dh :
-
Velocity of hydraulic diameter
- V narrow :
-
Velocity of narrow cross-section
- VB,1 :
-
Air volume flow rate of bypass body 1
- V B,2 :
-
Air volume flow rate of bypass body 2
- \({\dot V_H}\) :
-
Air volume flow rate of main body
- V a :
-
Total air volume flow rate
- Y:
-
Expansion factor
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Acknowledgments
This work was supported by a 2-Year Research Grant of Pusan National University.
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Bong-Jun Choi is an engineer of LG Electronics in Changwon, Korea. He received his bachelor’s and master’s degrees in mechanical engineering from Chung-Ang University in 1997 and 1999, respectively. His research interest is focused on heat exchangers and refrigeration systems.
Ji Hwan Jeong is a Professor of the School of Mechanical Engineering at Pusan National University in Busan, Korea. He received his bachelor’s degree in nuclear engineering from Seoul National University in 1988 and his master’s degree and Ph.D. in nuclear engineering from KAIST in 1990 and 1995, respectively. His research interests include heat transfer augmentation, heat exchangers, heat pumps, and nuclear thermal hydraulics.
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Choi, BJ., Jeong, J.H. Modeling of air-side heat transfer and pressure drop of straight fin-tube no-frost evaporators for a household refrigerator. J Mech Sci Technol 34, 4773–4784 (2020). https://doi.org/10.1007/s12206-020-1034-2
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DOI: https://doi.org/10.1007/s12206-020-1034-2