Abstract
Hydrodynamic and heat transfer characteristics of long-term stable nanofluids are very crucial for their industrial applications. Also utilization of coils is beneficial for industries as it provides a high rate of heat transfer and is compact in size too. So, the main focus of this study is to investigate the hydrodynamic and heat transfer characteristics of long-term stable f-CNT nanofluids when flowing inside a coil-based heat exchanger. f-CNT nanofluids were prepared by utilizing modified two-step method. To analyze the effect of different parameters on hydrodynamic and convective heat transfer characteristics, f-CNT concentration, \( {\varvec{D}}_{{\mathbf{c}}}\), and Re were varied from 0 to 0.048 vol%, 95 to 175 mm, and 2300 to 9500, respectively. According to results, f-CNT concentration, \( {\varvec{D}}_{{\mathbf{c}}}\), and Re substantially influenced the hydrodynamic and heat transfer characteristics of f-CNT nanofluids. It was found that improvement in h (152%) was much higher than the enhancement in friction factor (49%) when f-CNT nanofluid at 0.048 vol% was flowing through the coil of 95 mm diameter. Based on the heat transfer and hydrodynamic data, performance index was evaluated. The maximum performance index was calculated ⁓ 2.5, suggesting that the utilization of helical coils and f-CNT nanofluids is an excellent choice in industrial applications. Based on the experimental data, empirical correlations have been proposed to calculate the friction factor and Nusselt number for f-CNT nanofluids when flowing inside coils of different diameters and at different f-CNT concentrations. The proposed correlations explain the present experimental data within ± 15% and ± 20%, for friction factor and Nu, respectively.
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Abbreviations
- A, A i :
-
Inside heat transfer area, m2
- A o :
-
Outside heat transfer area, m2
- CNT:
-
Carbon nanotubes
- \(C_{{p,\;{\text{f - CNT}}\;{\text{nanofluid}}}}\) :
-
Specific heat of f-CNT nanofluid, J/g.°C
- \(C_{{p,\;{\text{Water}}}}\) :
-
Specific heat of water, J/g.°C
- \(C_{{p,\;{\text{f - CNT}}}}\) :
-
Specific heat of f-CNT, J/g.°C
- C :
-
Constant
- \(D_{{\text{c}}}\) :
-
Diameter of helical coil, mm
- \(d_{{\text{t}}}\) :
-
Inside diameter of the tube, mm
- \(d_{{\text{t}}} /D_{{\text{c}}}\) :
-
Curvature ratio, dimensionless
- \(d_{{\text{o}}}\) :
-
Outside diameter of the tube, mm
- f-CNT:
-
–COOH functionalized carbon nanotubes
- \(f_{{\text{s}}}\), \(f_{{\text{c}}}\) :
-
Friction factor of straight tube and helical coil, dimensionless
- \(f_{{{\text{c }}\left( {{\text{cal}}} \right)}}\) :
-
Calculated friction factor of helical coil, dimensionless
- \(f_{{{\text{c}} \left( {{\text{exp}}} \right)}}\) :
-
Experimental friction factor of helical coil, dimensionless
- h :
-
Convective heat transfer coefficient of water or CNT nanofluids, W/m2.K
- \(h_{{\text{i}}}\) :
-
Tube side convective heat transfer coefficient, W/m2.K
- \(h_{{\text{o}}}\) :
-
Bath or shell side convective heat transfer coefficient, W/m2.K
- hr:
-
Hour
- ID:
-
Inside diameter of CNT, nm
- k w :
-
Thermal conductivity of copper tube, W/mK
- K :
-
Thermal conductivity of water or CNT nanofluids, W/mK
- \(k_{{{\text{CNT}}\;{\text{nanofluid}}}}\) :
-
Thermal conductivity, W/m.K
- \(k_{{\text{f}}}\) :
-
Thermal conductivity of fluid (water), W/m.K
- \(L_{{\text{c}}}\) :
-
Length of the helical coil, m
- L :
-
Length of CNT, µm
- \(\dot{m}_{{\text{c}}}\) :
-
Mass flow rate of coolant, kg/s
- n :
-
Exponent
- N :
-
Number of turns in helical coil
- Nu :
-
Nusselt number
- Pr :
-
Prandtl number
- P :
-
Helical coil pitch, m
- ΔP :
-
Pressure drop, N/m2 or Pa
- \({\text{d}}P/L_{{\text{c}}}\) :
-
Pressure drop per unit length, Pa/m
- \(\dot{Q}_{{\text{c}}}\) :
-
Heat flow of coolant, W
- Re :
-
Reynolds number
- \( {Re}_{{\text{c}}}\) :
-
Critical Reynolds number, dimensionless
- \(\Delta T_{{{\text{lmtd}}}}\) :
-
Logarithmic mean temperature difference, °C
- \(T_{{{\text{bath}}}}\) :
-
Hot water bath temperature, °C
- \(T_{{{\text{out}}}}\) :
-
Outlet temperature, °C
- \(T_{{{\text{in}}}}\) :
-
Inlet temperature, °C
- \(T_{{\text{b, in}}}\) :
-
Bulk fluid temperature at inlet, °C
- \(T_{{\text{b, in}}}\) :
-
Bulk fluid temperature at outlet, °C
- \(U_{i}\) :
-
Overall heat transfer coefficient, W/m2.K
- \(\dot{V}\) :
-
Volumetric flow rate, m3/sec
- \(v,v_{i}\) :
-
Velocity of water or CNT nanofluids, m/s
- \(\rho_{{{\text{water}}}}\) :
-
Density of water
- \(\rho_{{\text{f - CNT}}}\) :
-
Density of f-CNT
- \(\rho_{{{\text{f - CNT}}\;{\text{nanofluid}}}}\) :
-
Density of f-CNT nanofluid
- \(\varphi\) :
-
Volumetric fraction, vol%
- µ :
-
Viscosity of water or CNT nanofluids, kg/m.s
- \(\mu_{{\text{f}}}\) :
-
Viscosity of base fluid (water), kg/m.s
- \(\mu_{{{\text{nf}}}}\) :
-
Viscosity of nanofluid, kg/m.s
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This study is financially supported by GGSIP University, New Delhi, India, under FRGS.
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Sharma, B., Sharma, S.K. & Gupta, S.M. Experimental Studies of f-CNT Nanofluids in a Helical Coil Heat Exchanger. Arab J Sci Eng 47, 5821–5840 (2022). https://doi.org/10.1007/s13369-021-05573-z
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DOI: https://doi.org/10.1007/s13369-021-05573-z