Fig. 1. Schematic diagram of the physical model.
Fig. 2. Streamlines, isotherms contours for different
: (a)
= 0.3; (b)
= 0.5; (c)
= 0.7; (d)
= 0.9.
Fig. 3. (a) Vertical velocity distribution at
X = 0; (b) horizontal velocity distribution at
Y = 1 for different
.
Fig. 4. (a) At the heated wall
Nuave number; (b) local
Nu number for different
.
Fig. 5. Streamlines, isotherms contours for different Ra number: (a) Ra = 103; (b) Ra = 104; (c) Ra = 105; (d) Ra = 106.
Fig. 6. (a) Vertical velocity distribution at
X = 0; (b) horizontal velocity distribution at
Y = 1 for different
.
Fig. 7. (a) At the heated wall Nuave number; (b) local Nu number for different Ra.
Fig. 8. Streamlines, isotherms contours for different γ number: (a) γ = 0°; (b) γ = 40°; (c) γ = 80°; (d) γ = 120°.
Fig. 9. (a) Local temperature distribution along the Y = 0.5; (b) average velocity in the y direction & Nuave number at the heated wall in different γ.
Fig. 10. (a) Local velocity in the y direction; (b) local Nuave number at the heated wall in different γ.
Fig. 11. (a) Variation of
Nuave number as a function of
in different
γ at the heated wall; (b) when
γ = 0°, 40°, variation of local
Nu number at the heated wall in different
.
Fig. 12. (a) Variation of Nuave number as a function of ϕ in different γ at the heated wall; (b) when γ = 0°, 40°, variation of local Nu number at the heated wall in different ϕ.
物性参数 | H2O
| Al2O3 | Glass fiber[23,24] | ρ/kg·m–3 | 997.1 | 397 | 1650 | Cp/J·kg–1·K–1 | 4179 | 765 | 750 | k/W·m–1·K–1 | 0.613 | 25 | 1.2 | β/K–1 | 21 × 10–5 | 1.89 × 10–5 | — | ds/nm
| — | 47 | — |
|
Table 1. Thermophysical properties of water, Al2O3 and glass fibers.
H2O, Al2O3和玻璃纤维的热物理性质
热物性参数 | 计算表达式 | 纳米流体粘度 | $\mu {}_{nf} = \dfrac{{{\mu _f}}}{{{{\left( {1 - \phi } \right)}^{2.5}}}}$![]() ![]() | 纳米流体密度 | ${\rho _{nf}} = \left( {1 - \phi } \right){\rho _f} + \phi {\rho _s}$![]() ![]() | 纳米流体热容 | ${\left( {\rho {C_p}} \right)_{nf}} = \left( {1 - \phi } \right){\left( {\rho {C_p}} \right)_f} + \phi {\left( {\rho {C_p}} \right)_s}$![]() ![]() | 纳米流体热扩散系数 | ${\alpha _{nf}} = \dfrac{{{k_{nf}}}}{{{{\left( {\rho {C_p}} \right)}_{nf}}}}$![]() ![]() | 纳米流体热膨胀系数 | ${\left( {\rho \beta } \right)_{nf}} = \left( {1 - \phi } \right){\left( {\rho \beta } \right)_f} + \phi {\left( {\rho \beta } \right)_s}$![]() ![]() | 纳米流体导热系数 | ${k_{nf}} = \dfrac{{{k_p} + 2{k_f} - 2\left( {{k_f} - {k_p}} \right)\phi }}{{{k_p} + 2{k_f} + 2\left( {{k_f} - {k_p}} \right)\phi }}{k_f}$![]() ![]() | 多孔介质有效
导热系数
| ${k_m} = \left( {1 - \epsilon} \right){k_p} + {\epsilon k_{nf}}$![]() ![]() |
|
Table 2. Calculation formula for thermodynamic properties of nanofluids.
纳米流体的热物性参数计算公式
| 不同网格数下的Nuave数
| 80 × 80 | 100 × 100 | 120 × 120 | 140 × 140 | Nuave数
| 8.528 | 8.670 | 8.744 | 8.785 | 误差/% | 3.39% | 1.70% | 0.83% | 0.36% |
|
Table 3. Comparison of
Nuave number with literature
[33] in different grids number.
Ra数
| 文献[27]
| 本文结果 | 误差/% | 103 | 1.116 | 1.123 | 0.63 | 104 | 2.238 | 2.266 | 1.25 | 105 | 4.509 | 4.556 | 1.04 | 106 | 8.817 | 8.744 | 0.83 |
|
Table 4. Comparison of
Nuave number with previous literature[
33].
NO. | Da数
| Ra数
| 文献[34]
| 本文结果 | 误差/% | 1 | 10–2 | 104 | 1.530 | 1.497 | 2.16 | 2 | 10–2 | 105 | 3.555 | 3.441 | 3.09 | 3 | 10–2 | 5 × 105 | 5.740 | 5.694 | 0.87 |
|
Table 5. Comparison of
Nuave number with previous literature[
34].