Alexandria Engineering Journal (2016) xxx, xxx–xxx
H O S T E D BY
Alexandria University
Alexandria Engineering Journal www.elsevier.com/locate/aej www.sciencedirect.com
ORIGINAL ARTICLE
CVFEM for free convective heat transfer of CuO-water nanofluid in a tilted semi annulus M. Sheikholeslami a,*, D.D. Ganji b a b
Department of Mechanical Engineering, Babol University of Technology, Babol, Iran Department of Mechanical Engineering, Sari Branch, Islamic Azad University, Sari, Iran
Received 26 July 2016; revised 4 October 2016; accepted 6 November 2016
KEYWORDS Half-annulus enclosure; Nanofluid; Natural convection; CVFEM; Inclined enclosure
Abstract Influence of adding CuO nanoparticles in the base fluid on flow and heat transfer in an inclined half-annulus was studied considering constant heat flux as boundary condition of hot wall. Control Volume based Finite Element Method (CVFEM) is applied in order to simulate procedure. Pressure gradient source terms are eliminated by using vorticity stream function formulation. Influences of CuO volume fraction, inclination angle and Rayleigh number on hydrothermal manners are presented. Results indicate that inclination angle makes changes in flow style. The strength of eddies reaches to its minimum value when the upper wall is hot. Temperature gradient enhances with rise of buoyancy forces while it reduces with augment of inclination angle. Ó 2016 Faculty of Engineering, Alexandria University. Production and hosting by Elsevier B.V. This is an open access article under the CC BY-NC-ND license (http://creativecommons.org/licenses/by-nc-nd/4.0/).
1. Introduction Nanotechnology was proposed as new way to improve heat transfer. 3D flow over plate has been examined by Mustafa et al. [1] considering radiation influence. They proved that temperature ratio has significant influence on thermal boundary layer. Magnetohydrodynamic (MHD) flow in a cavity with oscillating wall was examined by Selimefendigil and O¨ztop [2]. They illustrated that inclination angle of 90° has maximum performance. Sheikholeslami and Ganji [3] presented various applications of nanofluid in their review paper. Sheremet et al. [4] simulated the MHD unsteady free convective flow * Corresponding author. E-mail addresses:
[email protected],
[email protected] (M. Sheikholeslami), mirgang@ nit.ac.ir (D.D. Ganji). Peer review under responsibility of Faculty of Engineering, Alexandria University.
in a wavy cavity. They used finite difference method (FDM) to simulate that paper. Influence of asymmetric heating on the heat transfer improvement in a microchannel was examined by Malvandi et al. [5]. Their results illustrated that Lorentz forces enhance the Nusselt number about 42%. Influence of axial magnetic field on nanofluid thermal management has been analyzed by Sheikholeslami and Abelman [6]. Influences of space reliant magnetic field on ferrofluid motion were investigated by Sheikholeslami et al. [7]. They concluded that the higher speed of lid wall causes temperature gradient to enhance. Influence of single magnetic source on Fe3O4-water flow style has been reported by Sheikholeslami and Ganji [8]. They concluded that Kelvin force has various behaviors according to buoyancy forces and Lorentz forces reduce the nanofluid motion. Kandasamy et al. [9] investigated the reaction of nanofluid versus chemical reaction. Sheikholeslami and Rashidi [10] applied single phase model for Fe3O4-water nanofluid. They indicated that Lorentz forces make velocity to reduce. Radia-
http://dx.doi.org/10.1016/j.aej.2016.11.012 1110-0168 Ó 2016 Faculty of Engineering, Alexandria University. Production and hosting by Elsevier B.V. This is an open access article under the CC BY-NC-ND license (http://creativecommons.org/licenses/by-nc-nd/4.0/). Please cite this article in press as: M. Sheikholeslami, D.D. Ganji, CVFEM for free convective heat transfer of CuO-water nanofluid in a tilted semi annulus, Alexandria Eng. J. (2016), http://dx.doi.org/10.1016/j.aej.2016.11.012
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M. Sheikholeslami, D.D. Ganji
Nomenclature Nuloc Nuave Pr q00 X; Y U; V Ra ! g k
local Nusselt number average Nusselt number Prandtl number (=t/a) heat flux dimensionless space coordinates horizontal and vertical velocity components Rayleigh number ð¼ gbq00 ðrout rin Þ4 =ðk amÞÞ gravitational acceleration vector thermal conductivity
Greek symbols b thermal expansion coefficient
l a / q
dynamic viscosity thermal diffusivity volume fraction fluid density
Subscripts nf nanofluid c cold f base fluid s solid particles h hot
Figure 1 (a) Geometry and the boundary conditions with (b) The mesh of half-annulus enclosure considered in this work; (c) A sample triangular element and its corresponding control volume.
Please cite this article in press as: M. Sheikholeslami, D.D. Ganji, CVFEM for free convective heat transfer of CuO-water nanofluid in a tilted semi annulus, Alexandria Eng. J. (2016), http://dx.doi.org/10.1016/j.aej.2016.11.012
CVFEM for free convective heat transfer of CuO-water nanofluid Table 1 The coefficient CuO Water nanofluid [36].
values
of
Coefficient values
CuO Water
a1 a2 a3 a4 a5 a6 a7 a8 a9 a10
26.593310846 0.403818333 33.3516805 1.915825591 6.42185846658E02 48.40336955 9.787756683 190.245610009 10.9285386565 0.72009983664
tion and magnetic source terms have been added by Sheikholeslami et al. [11] in governing equations. They revealed that Lorentz forces can decrease the temperature gradient. Awais et al. [12] reported the slip impact on nanofluid flow in existence of magnetic field. Influence of chemical reaction on micropolar fluid over a plate has been presented by Rashad et al. [13]. Homotopy Analysis Method (HAM) was used by Joneidi et al. [14] to investigate the mass transfer over a plate. The influence of atherosclerosis on hemodynamics of stenosis has been forecasted by Nadeem and Ijaz [15]. They showed that the velocity gradient on the wall of titled arteries reduces with augment of Strommers number. Ahmad and Mustafa [16] investigated the rotating nanofluid flow induced by an exponentially stretching. Their results revealed that temperature gradient reduces with augment of angular velocity. Hayat et al. [17] presented the influence of radiation on mass transfer of nanofluid. They showed that temperature gradient reduces with augment of thermal radiation. Hussein et al. [18] investigated the free convection of nanofluid in T-shaped cavity. They proved that temperature gradient reduces with rise of heat source length. Radiation heat transfer over a sensor surface has been studied by Hamzah et al. [19]. They showed 30% enhancement in Nusselt number with use of nanofluid. Several authors reported their results about nanofluid and natural convection decade [20–35]. The goal of this article was to present a simulation of free convective heat transfer in an inclined half annulus using CVFEM. Simulation is carried out for various inclination angles, CuO volume fraction and Rayleigh number. Also a correlation for Nusselt number is presented. 2. Problem definition
Water CuO
Figure 2 (a) Comparison of the temperature on axial midline between the present results and numerical results by Sharif et al. [38]; (b) comparison of average Nusselt number between the present results and numerical results by Khanafer et al. [39] Gr ¼ 104 , / ¼ 0:1 and Pr ¼ 6:2ðCu WaterÞ.
3. Governing equation and simulation
Fig. 1 illustrates the important geometric parameters of current geometry. Also sample mesh is presented. Constant heat flux is applied on inner surface and other conditions are clear in Fig. 1.
Table 2
3
3.1. Governing formulation The flow is laminar and steady and in two dimensional. Boussinesq approximation has been considered for momentum
Thermo physical properties of water and nanoparticles [36]. q (kg/m3)
Cp (j/kg k)
k (W/m k)
b 105 ðK1 Þ
dp (nm)
r ðX mÞ1
997.1 6500
4179 540
0.613 18
21 29
– 1010
0:05 6500
Please cite this article in press as: M. Sheikholeslami, D.D. Ganji, CVFEM for free convective heat transfer of CuO-water nanofluid in a tilted semi annulus, Alexandria Eng. J. (2016), http://dx.doi.org/10.1016/j.aej.2016.11.012
4
M. Sheikholeslami, D.D. Ganji Table 3
Comparison of the average Nusselt number Nuave for different grid resolutions at Ra ¼ 105 , k ¼ 0 and / ¼ 0:04.
Mesh size in radial direction angular direction 51 163 61 207 71 241 81 261 7:1086 7:0498 6:9871 6:9230
101 321 6:8586
111 351 6:8358
121 381 6:8171
131 411 6:8016
Ra= 103
91 291 6:8868
nf
= 1.3, Ψ max
f
=1.271
Ra= 104
Ψ max
nf
= 6.519, Ψ max f =5.989
Ra= 105
Ψ max
Ψ max
nf
= 17.86, Ψ max f =16
Figure 3 Comparison of the streamlines (left) and isotherms (right) contours between nanofluid (/ ¼ 0:04) (- - -) and pure fluid (/ ¼ 0) (––) for different values of Ra at k ¼ 0 and Pr ¼ 6:2.
equations. Nanofluid is assumed as homogenous fluid. According to these assumptions the governing equations can be presented as follows: @v @u þ ¼0 @y @x
@u @u 1 @P lnf @ 2 u @ 2 u þ ¼ þ v þu @y @x qnf @x qnf @y2 @x2 lnf @ 2 v @ 2 v @v @v @P 1 ðTc TÞgbnf ¼ þ þv þ u @x @y @y qnf qnf @x2 @y2 2 knf @ T @2T @T @T ¼ v þ þ u ðqCp Þnf @x2 @y2 @y @x bnf , ðqCp Þnf and qnf are defined as follows:
ð1Þ ð2Þ ð3Þ ð4Þ
bnf ¼ bf ð1 /Þ þ bs /
ð5Þ
ðqCp Þnf ¼ ðqCp Þf ð1 /Þ þ ðqCp Þs /
ð6Þ
qnf ¼ qf ð1 /Þ þ qs /
ð7Þ
ðkn f Þ and ðln f Þ are obtained according to Koo–Kleinstreuer–Li (KKL) model [20]: sffiffiffiffiffiffiffiffiffi k 3 kpf 1 / jb T 4 0 knf ¼ 1 þ þ 5 10 g ð/; T; dp Þ/qf cp;f kp kp q p dp þ 2 kf 1 / kf g0 ð/; T; dp Þ ¼ a1 þ a2 Lnðdp Þ þ a3 Lnð/Þ þ a4 Lnð/Þ lnðdp Þ 2 þa5 Lnðdp Þ LnðTÞ þ ða6 þ a7 Lnðdp Þ þ a8 Lnð/Þ
ð8Þ
2
þ a9 lnðdp ÞLnð/Þ þ a10 Lnðdp Þ ÞRf ¼ dp =kp;eff dp =kp ; Rf ¼ 4 10
8
km =W 2
Please cite this article in press as: M. Sheikholeslami, D.D. Ganji, CVFEM for free convective heat transfer of CuO-water nanofluid in a tilted semi annulus, Alexandria Eng. J. (2016), http://dx.doi.org/10.1016/j.aej.2016.11.012
CVFEM for free convective heat transfer of CuO-water nanofluid
5
Ra = 10 4
λ = 45˚
Ra = 10 5
(Ψ min )nf = −0.71 (Ψ max )nf = 1.49
(Ψ min )nf = −5.86 (Ψ max )nf = 7.39
(Ψ min )nf = −16.68 (Ψ max )nf = 18.78
λ = 90˚
Ra = 10 3
(Ψ min )nf = 0.00 (Ψ max )nf = 1.587
(Ψ min )nf = 0.00 (Ψ max )nf = 8.27
(Ψ min )nf = 0.00 (Ψ max )nf = 23.11
Figure 4 Isotherms (down) and streamlines (up) contours for different values of Rayleigh number when k ¼ 45 and 90 for CuO-water nanofluid (/ ¼ 0:04).
lnf ¼
lf ð1 /Þ
þ 2:5
kBrownian lf kf Pr
ð9Þ
All needed coefficients and properties are illustrated in Tables 1 and 2 [36]. Vorticity and stream function should be defined as follows: @u @v @w @w xþ ¼ 0; ¼ v; ¼u @y @x @x @y
ð10Þ
By removing pressure gradient source terms from Eqs. (2) and (3), the final form of equations can be obtained as follows:
@2x @2x @T @x @w @x @w ¼ b þ g nf @x2 @y2 @x @x @y @y @x 2 @ T @2T @T @w @T @w knf ¼ þ qCp nf @y2 @x2 @x @y @y @x
tnf
@2w @2w þ þx¼0 @y2 @x2
ð11Þ ð12Þ ð13Þ
Dimensionless parameters are as follows: H¼
T Tc ðy; xÞ ðw; xL2 Þ ; ðW; XÞ ¼ ; ðY; XÞ ¼ L af ðq00 L=kf Þ
ð14Þ
Please cite this article in press as: M. Sheikholeslami, D.D. Ganji, CVFEM for free convective heat transfer of CuO-water nanofluid in a tilted semi annulus, Alexandria Eng. J. (2016), http://dx.doi.org/10.1016/j.aej.2016.11.012
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M. Sheikholeslami, D.D. Ganji Ra = 10 4
λ = 180˚
λ = 135˚
Ra = 10 3
Ra = 10 5
(Ψ min )nf = −0.31 (Ψ max )nf = 1.66
(Ψ min )nf = −0.75 (Ψ max )nf = 7.99
(Ψ min )nf = −0.79 (Ψ max )nf = 21.32
(Ψ min )nf = −1.17 (Ψ max )nf = 1.17
(Ψ min )nf = −4.62 (Ψ max )nf = 4.62
(Ψ min )nf = −9.92 (Ψ max )nf = 9.92
Figure 5 Isotherms (down) and streamlines (up) contours for different values of Rayleigh number when k ¼ 135 and 180 for CuOwater nanofluid (/ ¼ 0:04).
Using the above formulae the governing equations change to the following:
@H b Raf Prf / s þ ð1 /Þ bf @X 2 q @ X @2X þ Prf ð1 /Þ2:5 / s þ ð1 /Þ þ qf @Y2 @X2 @W @X @W @X ¼ þ ð15Þ @X @Y @Y @X !# 2 ," @ H @ 2 H knf ðqCpÞs ð1 /Þ þ ð1 /Þ þ / þ kf ðqCpÞf @X2 @Y2 ¼ þ
@W @H @W @H @Y @X @X @Y
@2W @2W þ ¼ X @Y2 @X2
ð16Þ ð17Þ
Prandtl and Rayleigh numbers are introduced as follows: Prf ¼ tf =af ; Raf ¼ gbf L4 q00 =ðkf af tf Þ; respectively. Nuloc and Nuave over the hot wall should be calculated as follows: knf 1 ð18Þ Nuloc ¼ kf H Z p 1 Nuave ¼ Nuloc ðfÞdf ð19Þ p 0
3.2. Numerical procedure Linear interpolation is utilized for approximation of variables in the triangular element which is considered as building block (Fig. 1(c)). Gauss-Seidel method is utilized to solve the algebraic equations. More details exist in reference book [37].
Please cite this article in press as: M. Sheikholeslami, D.D. Ganji, CVFEM for free convective heat transfer of CuO-water nanofluid in a tilted semi annulus, Alexandria Eng. J. (2016), http://dx.doi.org/10.1016/j.aej.2016.11.012
CVFEM for free convective heat transfer of CuO-water nanofluid
Ra = 10 3
2.8
2.4
Ra = 10 4
5.6
φ=0 φ = 0.02 φ = 0.04
7
Ra = 10 5
10
φ=0 φ = 0.02 φ = 0.04
φ=0 φ = 0.02 φ = 0.04
4.8
2
Nuloc
Nuloc
Nuloc
λ=0
7.5 4
3.2 5
1.6
1.2
2.4
0
45
90
135
1.6
180
0
45
φ=0 φ = 0.02 φ = 0.04
135
180
135
180
90
135
180
90
135
180
90
135
180
φ=0 φ = 0.02 φ = 0.04
8 7
4
3.2
2.4
6
0
45
90
135
1.6
180
4
0
45
ζ
135
3
180
3.6
5.4
Nuloc
Nuloc
2.8 2.4
1.5
2.7
45
90
ζ
135
180
Nuloc
Nuloc
2.5
1.5
2
0
2.7
45
90
ζ
135
1.5
180
2.4
90
ζ
135
180
45
ζ
φ=0 φ = 0.02 φ = 0.04
5
4
3
0
45
90
ζ
135
2
180
0
7
φ=0 φ = 0.02 φ = 0.04
4
45
ζ
φ=0 φ = 0.02 φ = 0.04
6
3.5
Nuloc
2.1
1.8
3
1.5
3
2
0
45
90
ζ
135
180
1.5
5
4
2.5
1.2
0
6
φ=0 φ = 0.02 φ = 0.04
4.5
φ=0 φ = 0.02 φ = 0.04
45
3
1.8
1.2
0
3.5
2.1
Nuloc
2.4
4
φ=0 φ = 0.02 φ = 0.04
2.4
3
1.2
Nuloc
0
4.2
1.6
Nuloc
0.9
4.8
3.6
2 1.2
90
φ=0 φ = 0.02 φ = 0.04
6
3.2
1.8
45
6.6 φ=0 φ = 0.02 φ = 0.04
4
2.1
0
ζ
4.4 φ=0 φ = 0.02 φ = 0.04
2.4
Nuloc
90
ζ
2.7
λ = 135
90
5
1.2
λ = 180
45
9
Nuloc
2
1.6
Figure 6 number.
0
ζ
φ=0 φ = 0.02 φ = 0.04
4.8
Nuloc
2.4
Nuloc
2.5
180
5.6
2.8
λ = 45
135
ζ
ζ
λ = 90
90
0
45
90
ζ
135
180
2
0
45
ζ
Effects of the nanoparticle volume fraction, Rayleigh number and inclination angle for CuO-water nanofluids on local Nusselt
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M. Sheikholeslami, D.D. Ganji
(b) log ( Ra ) = 5
(a) λ = 180
(c) log ( Ra ) = 5 , φ = 0.04 , λ = 180 Figure 7 Effects of the nanoparticle volume fraction, Rayleigh number and inclination angle for CuO-water nanofluids on average Nusselt number.
4. Mesh independency and verification Various grids have been considered for the case of / ¼ 0:04; Ra ¼ 105 and k ¼ 0 as presented in Table 3. This table indicates that the mesh size 71 211 can be chosen. Fig. 2(a and b) depicts the validation of current FORTRAN code. These figures prove the accuracy of this code in comparison with [38,39]. 5. Results and discussion In this work, the influence of CuO nanoparticle on the hydrothermal behavior in an inclined half-annulus is studied using CVFEM. Simulation is made for different values of Rayleigh number (Ra ¼ 103 ; 104 and 105 ), inclination angle
(k ¼ 0 ; 45 ; 90 , 135 and 180 ) and volume fraction of CuO (/ ¼ 0% and 4%). Fig. 3 depicts the effect of CuO nanoparticles on hydrothermal characteristics. The nanofluid velocity augments due to enhancement in the solid movements. Temperature gradient augments with rise of volume fraction CuO. Figs. 4 and 5 illustrate the impact of inclination angle, Rayleigh number and CuO volume fraction. Conduction mode is dominated in low Rayleigh number. Two rotating vortexes exist in streamlines. As buoyancy forces augment, temperature gradient enhances and thermal plume appears near the vertical center line. The core of vortexes moves upward. At k ¼ 45 , the counterclockwise vortex is stronger than other one due to more space for circulation. At k ¼ 90 , the two main eddies merged into one counterclockwise eddy. The streamlines and isotherms at k ¼ 135 and 180 are depicted in Fig. 5. As seen, the impact
Please cite this article in press as: M. Sheikholeslami, D.D. Ganji, CVFEM for free convective heat transfer of CuO-water nanofluid in a tilted semi annulus, Alexandria Eng. J. (2016), http://dx.doi.org/10.1016/j.aej.2016.11.012
CVFEM for free convective heat transfer of CuO-water nanofluid
9
(a) φ = 0.04
(b) λ = 180
(c) log ( Ra ) = 5 Figure 8
Contour plots of average Nusselt number.
of Rayleigh number on the size of eddies for k ¼ 135 is opposite to that of k ¼ 45 . By increasing buoyancy forces, the size of secondary eddy decreases and finally at Ra ¼ 105 a small vortex appears on the top of the secondary eddy, which turns in clockwise directions. This behavior of thermal boundary layer may be due to the stronger flow circulation at higher Rayleigh numbers at these points. The isotherms and streamlines for k ¼ 180 , are almost symmetric to the vertical centerline. However, enhancing the buoyancy forces has no significant influence on the location of two main eddies’ core. In fact, when the hot circular wall locates above the cold one, the impact of convection on the velocity and temperature is less pronounced. Similar to the inclination angle of 135 , the temperature gradient becomes thinner near the inner wall except to the two inner corners. Influences of important parameters on Nuloc and Nuave are depicted in Figs. 6–8. The correlation for this parameter is as follows:
Figure 9 Effects of k and Ra on the heat transfer enhancement due to addition of nanoparticles when Pr ¼ 6:2.
Please cite this article in press as: M. Sheikholeslami, D.D. Ganji, CVFEM for free convective heat transfer of CuO-water nanofluid in a tilted semi annulus, Alexandria Eng. J. (2016), http://dx.doi.org/10.1016/j.aej.2016.11.012
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M. Sheikholeslami, D.D. Ganji
Nuave ¼ 2:12 1:2 logðRaÞ þ 0:01k 11:81/ 4:88 k logðRaÞ þ 7:94 / logðRaÞ 0:027k/ þ 0:38 log ðRaÞ2 þ 2:19k2 þ 0:07/2
[7]
ð20Þ
Response surface methodology (RSM) is utilized to find this correlation. This method presented polynomial formulation according to input data. As volume fraction of CuO augments, Nuloc augments. Nusselt number augments with rise of Ra. Nuloc profiles are symmetric to f ¼ 90 when k ¼ 0 and 180 . At k ¼ 0 and 45 minimum amount of Nuloc is located at f ¼ 90 and 55 respectively. Also Fig. 8 shows that for k ¼ 135 and 180 maximum amount of Nuloc is located at f ¼ 100 and 90 respectively. Nusselt number decreases with enhancement of inclination angle. Fig. 9 shows the influence of k and Ra on the heat transfer enhancement. This parameter can be calculated as follows: E¼
Nuð/ ¼ 0:04Þ NuðbasefluidÞ 100 NuðbasefluidÞ
ð21Þ
According to this figure, heat transfer enhances with augment of inclination angle. Higher Rayleigh number leads to lower values of E. In low Rayleigh number and k ¼ 180 , the dominant mechanism is conduction and in this way adding nanoparticles has significant impact on thermal conductivity. 6. Conclusions Nanofluid free convective heat transfer in an inclined halfannulus is studied using CVFEM. Flow style and temperature distribution are presented for different inclination angles, CuO volume fraction and Rayleigh number. Results indicate that temperature gradient enhances with rise of CuO volume fraction and buoyancy forces but it reduces with augment of inclination angle. As inclination angle increases, the maximum value of stream function reduces. Moreover, the impact of CuO volume fraction on temperature gradient is more significant at lower Rayleigh number. The streamlines and isotherms clearly indicate that the inclination angle of enclosure can be utilized as a control parameter.
[8]
[9]
[10]
[11]
[12]
[13]
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[15]
[16]
[17]
[18]
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