Sage Journals: Discover world-class research

Abstract

The steady boundary-layer flow of a nanofluid past a permeable moving flat plate in the presence of a coflowing fluid is theoretically investigated. The plate is assumed to move in the same or opposite direction of the free stream. The governing partial differential equations are first transformed into ordinary differential (similarity) equations before they are solved numerically using a finite-difference scheme along with a shooting method. Numerical results are obtained for the skin-friction coefficient, the local Nusselt number, and the local Sherwood number as well as the velocity, temperature, and nanoparticle volume fraction profiles for some values of the governing parameters, namely, the plate velocity parameter, the Prandtl number, the Lewis number, the Brownian motion parameter, the thermophoresis parameter, and the nanoparticle volume fraction parameter. The numerical results indicate that dual solutions exist when the plate and the free stream move in the opposite directions.

1. Introduction

Conventional fluids, such as water, ethylene glycol, and engine oil are widely used as heat transfer fluids in thermal system. However, low heat transfer performance of these conventional fluids limits the performance enhancement and the efficiency of heat exchangers. Therefore, effective thermal conductivity of the nanofluids is expected to enhance the heat transfer performance (Masuda et al. [1]). Choi [2] was the first who introduced the term nanofluid and it refers to the fluids with suspended nanoparticles (Nield and Kuznetsov [3]). Most commonly used nanoparticles are aluminium, copper, iron, and titanium or their oxides.

Experimental studies by Masuda et al. [1], Pak and Cho [4], Eastman et al. [5], Das et al. [6], Xuan and Li [7], and Minsta et al. [8] show that only a small volumetric fraction of nanoparticles (usually less than 5%) is needed to enhance the thermal conductivity of the base liquid by 5–15%. The improved thermal conductivity of nanofluid together with the thermal conductivity of the base liquid and turbulence induced by their motion contributes to a remarkable improvement in the convective heat transfer coefficient. This phenomenon suggests the possibility of using nanofluids in advanced nuclear systems (Buongiorno and Hu [9]) and cylindrical heat pipes (Shukla et al. [10]). The comprehensive references on nanofluids can be found in the recent book by Das et al. [11] and in the review papers by Buongiorno [12], Kakaç and Pramuanjaroenkij [13], Lee et al. [14], Wong and de Leon [15], Yu and Lin [16], Ghadimi et al. [17], Ramesh and Prabhu [18], Sarkar [19], Fan and Wang [20], Saidur et al. [21], Thomas and Panicker Sobhan [22], and Mahian et al. [23].

It is worth mentioning that the nanofluid model proposed by Buongiorno [12] was frequently used by Nield and Kuznetsov [3, 24], Kuznetsov and Nield [25, 26], Khan and Pop [27], Bachok et al. [28], Khan and Aziz [29], and Tham et al. [30] in their papers. Besides the above model, another nanofluid model proposed by Tiwari and Das [31] has also been used by several authors such as Ahmad et al. [32], Rohni et al. [33], Bachok et al. [28, 34, 35], Nazar et al. [36], and Yasin et al. [37]. Different from the previous approach, the present paper considers a problem using a combination of both nanofluid models (see Buongiorno [12] and Tiwari and Das [31]) stated above. Results for the reduced Nusselt and Sherwood numbers are presented in tables and graphs for various values of the involved parameters. Dual (upper and lower branch) solutions of the similarity equations are shown to exist and based on the stability analysis proposed by Weidman et al. [38] it can be shown that the upper branch solution is stable and, therefore, physically realizable in practice, while the lower branch solution is unstable and not physically realizable. It should be mentioned that this new type of shrinking sheet flow is essentially a backward flow as discussed by Goldstein [39]. To the best of our knowledge, the present problem along with the combined nanofluid models has not been considered before; therefore, the reported results are new and original.

2. Problem Formulation

Steady boundary-layer flow due to a permeable moving flat plate in the presence of a coflowing water-based nanofluid containing Cu (copper), Al₂O₃ (alumina), and TiO₂ (titania) nanoparticles is considered. It is assumed that the plate moves with the velocity λU, where λ is the moving plate velocity parameter and U is the constant positive velocity of the ambient (inviscid) nanofluid as shown in Figure 1. It is also assumed that the constant surface temperature of the plate is T_w and the constant surface nanoparticle volume fraction is C_w, while the ambient nanofluid has a temperature T_∞ and a nanoparticle concentration C_∞. The boundary layer equations for the steady flow on the moving surface can be written as

\frac{\partial u}{\partial x} + \frac{\partial v}{\partial y} = 0,

(1)

u \frac{\partial u}{\partial x} + v \frac{\partial u}{\partial y} = \frac{μ_{nf}}{ρ_{nf}} \frac{\partial^{2} u}{\partial y^{2}},

(2)

u \frac{\partial T}{\partial x} + v \frac{\partial T}{\partial y} = α_{nf} \frac{\partial^{2} T}{\partial y^{2}} + τ [D_{B} \frac{\partial C}{\partial y} \frac{\partial T}{\partial y} + (\frac{D_{T}}{T_{\infty}}) {(\frac{\partial T}{\partial y})}^{2}],

(3)

u \frac{\partial C}{\partial x} + v \frac{\partial C}{\partial y} = D_{B} \frac{\partial^{2} C}{\partial y^{2}} + (\frac{D_{T}}{T_{\infty}}) \frac{\partial^{2} T}{\partial y^{2}},

(4)

subject to the boundary conditions

\begin{matrix} v = v_{w} (x), u = u_{w} = λ U, T = T_{w}, C = C_{w} \\ at y = 0, \\ u ⟶ U, T ⟶ T_{\infty}, C ⟶ C_{\infty} as y ⟶ \infty, \end{matrix}

(5)

where x and y are the Cartesian coordinates measured along the flat plate and normal to it, respectively, u and v are the velocity component along the x and y axes, respectively, T is the nanofluid temperature, C is the nanoparticle volume fraction, D_B is the Brownian diffusion coefficient, D_T is the thermophoretic diffusion coefficient, $τ = {(ρ C_{p})}_{s} / {(ρ C_{p})}_{f}$ is the heat capacity ratio, where ${(ρ C_{p})}_{f}$ is the heat capacity of the fluid and ${(ρ C_{p})}_{s}$ is the effective heat capacity of the nanoparticle material, and v_w(x) is the mass flux velocity with v_w(x)<0 for suction and v_w(x)>0 for injection. Meanwhile λ is the plate velocity ratio where λ>0 when the plate moves away or downstream from the origin and λ<0 when the plate moves towards the origin. Further, μ_nf, ρ_nf, and α_nf are the effective viscosity of the nanofluid, the effective density of the nanofluid, and the thermal diffusivity of the nanofluid, respectively, which are defined as (Oztop and Abu-Nada [40])

\begin{matrix} μ_{nf} = \frac{μ_{f}}{{(1 - ϕ)}^{2.5}}, α_{nf} = \frac{k_{nf}}{{(ρ C_{p})}_{nf}}, \\ {(ρ C_{p})}_{nf} = (1 - ϕ) {(ρ C_{p})}_{f} + ϕ {(ρ C_{p})}_{s}, \\ ρ_{nf} = (1 - ϕ) ρ_{f} + ϕ ρ_{s}, \\ \frac{k_{nf}}{k_{f}} = \frac{(k_{s} + 2 k_{f}) - 2 ϕ (k_{f} - k_{s})}{(k_{s} + 2 k_{f}) + ϕ (k_{f} - k_{s})} . \end{matrix}

(6)

Here, ϕ is the solid volume fraction of the nanofluid or the nanoparticle volume fraction parameter and k_nf is the effective thermal conductivity of the nanofluid. The thermophysical properties of the fluid and nanoparticles are given in Table 1.

Table 1:

Thermophysical properties of fluid and nanoparticles (Oztop and Abu-Nada [40]).

Physical properties	Fluid phase (water)	Cu	Al₂O₃	TiO₂

C_p (J/kg K)	4179	385	765	686.2
ρ (kg/m³)	997.1	8933	3970	4250
k (W/mK)	0.613	400	40	8.9538
α × 10⁷ (m²/s)	1.47	11163.1	131.7	30.7
β × 10⁻⁵ (1/K)	21	1.67	0.85	0.9

Figure 1:

Physical model and coordinate system.

Following Weidman et al. [38], we express the similarity solutions of (1)–(4) in terms of the following variables:

\begin{matrix} ψ = ν_{f} \sqrt{2 R e_{x}} f (η), θ (η) = \frac{T - T_{\infty}}{T_{w} - T_{\infty}}, \\ g (η) = \frac{C - C_{\infty}}{C_{w} - C_{\infty}}, η = \frac{y}{x} \sqrt{\frac{R e_{x}}{2}}, \end{matrix}

(7)

where ψ is the stream function, which is defined as u = ∂ψ/∂y and v = −∂ψ/∂x, which automatically satisfies (1). Thus, we have

u = {U f}^{'} (η), v = - \sqrt{\frac{ν_{f} U}{2 x}} [f (η) - η f^{'} (η)],

(8)

where prime denotes differentiation with respect to η. The velocity v in (8) shows that the suction/injection velocity v_w(x) must have the form

v_{w} (x) = - \sqrt{\frac{ν_{f} U}{2 x}} f (0)

(9)

so that v_w(x) should be $v_{w} (x) = - \sqrt{2 x / ν_{f} U} s$ with s>0 for suction and s<0 for injection.

Substituting (7) into (2)–(4), we obtain the following nonlinear ordinary differential equations:

\frac{1}{{(1 - ϕ)}^{2.5} [(1 - ϕ) + ϕ (ρ_{s} / ρ_{f})]} f^{'''} + f f^{''} = 0,

(10)

\frac{k_{nf} / k_{k}}{(1 - ϕ) + ϕ {(ρ C_{p})}_{s} / {(ρ C_{p})}_{f}} \frac{1}{Pr} θ^{′′} + f θ^{'} + Nb g^{'} θ^{'} + Nt θ^{' 2} = 0,

(11)

g^{''} + Le f g^{'} + \frac{Nt}{Nb} θ^{''} = 0,

(12)

with the boundary conditions (5) taking the form

\begin{matrix} f (0) = s, f^{'} (0) = λ, \\ θ (0) = 1, g (0) = 1, \\ f^{'} (η) ⟶ 1, θ (η) ⟶ 0, g (η) ⟶ 0 as η ⟶ \infty, \end{matrix}

(13)

where Pr is the Prandtl number, Le is the Lewis number for the base fluid, Nb is the modified Brownian motion parameter, and Nt is the modified thermophoresis parameter of the nanofluids, which are defined as

\begin{matrix} Pr = \frac{ν_{f}}{α_{f}}, Le = \frac{ν_{f}}{D_{B}}, \\ Nb = \frac{τ D_{B} (C_{w} - C_{\infty})}{ν_{f}}, Nt = \frac{τ D_{T} (T_{w} - T_{\infty})}{T_{\infty} ν_{f}} . \end{matrix}

(14)

It should be noted that when ϕ = 0 (regular fluid) and Nb=Nt = 0, (10) and (11) involve only two dependent variables, namely, f(η) and θ(η). The boundary-value problem for f(η) reduces to the classical problem studied by Weidman et al. [38] and the boundary-value problem for g(η) then becomes ill-posed and is of no physical significance.

The physical quantities of practical interest are the skin friction coefficient C_f, the local Nusselt number Nu_x, and the local Sherwood number Sh_x, which are defined as

\begin{matrix} C_{f} = \frac{τ_{w}}{ρ_{f} U^{2}}, {Nu}_{x} = \frac{x q_{w}}{k_{f} (T_{w} - T_{\infty})}, \\ {Sh}_{x} = \frac{x q_{m}}{D_{B} (C_{w} - C_{\infty})}, \end{matrix}

(15)

where τ_w is the skin friction or the shear stress along the surface of the plate, q_w is the wall heat flux, and q_m is the wall mass flux, which are given by

\begin{matrix} τ_{w} = μ_{nf} {(\frac{\partial u}{\partial y})}_{y = 0}, q_{w} = - k_{nf} {(\frac{\partial T}{\partial y})}_{y = 0}, \\ q_{m} = - D_{B} {(\frac{\partial C}{\partial y})}_{y = 0}, \end{matrix}

(16)

respectively. Using (7), (15), and (16), we get

\begin{matrix} {(2 R e_{x})}^{1 / 2} C_{f} = \frac{1}{{(1 - ϕ)}^{2.5}} f^{′′} (0), \\ {(\frac{2}{R e_{x}})}^{1 / 2} {Nu}_{x} = - \frac{k_{nf}}{k_{f}} θ^{'} (0), \\ {(\frac{2}{R e_{x}})}^{1 / 2} {Sh}_{x} = - g^{'} (0), \end{matrix}

(17)

where Re_x = Ux/ν_f is the local Reynolds number.

3. Results and Discussion

The nonlinear transformed (similarity) boundary layer equations (10), (11), and (12) subject to the boundary conditions (13) have been solved numerically using two different methods, namely, the Keller-box method and the Runge-Kutta-Fehlberg (RKF) method with shooting technique. The Keller-box method is a very efficient and flexible implicit finite-difference scheme with second order truncation error (Cebeci and Bradshaw [41, 42]). Meanwhile the well-known and more simple shooting method is an iterative algorithm technique implemented in MAPLE program which attempts to identify the appropriate initial conditions for a related initial value problem (IVP) that provides the solution to the original boundary value problem (BVP) (Meade et al. [43]). In this method, the dual (first and second) solutions were obtained by setting different initial guesses for the missing values of f″(0), θ′(0), and g′(0), where all profiles satisfy the far field boundary conditions (13) asymptotically. The results obtained by both methods show a favorable agreement. Thus, this gives confidence to the accuracy of the numerical results presented in this paper. The effects of the solid volume fraction of nanofluid ϕ and the Prandtl number Pr are analyzed for three different nanofluids, namely, Cu-water, Al₂O₃-water, and TiO₂-water, as the working fluids. Following Oztop and Abu-Nada [40], the value of the Prandtl number Pr is taken as 6.2 (water) and the range of nanoparticle volume fraction is considered as 0 ≤ ϕ ≤ 0.2, in which ϕ = 0 corresponds to the regular base fluid. The variation of the reduced skin friction coefficient f″(0) with λ is shown in Figure 2(a) when f₀ = 0, Nb = 0.5, and Nt = 0.5 As seen from the figure, the values of f″(0) are positive when λ<1, while they are negative when λ>1. Physically, a positive sign for f″(0) implies that the fluid exerts a drag force on the plate and a negative sign implies the opposite. The value f″(0) = 0.4696 when λ = 0 (Blasius problem [44] as given in Figure 2(a) is in excellent agreement with that reported by White [45]). Figure 2(a) shows the existence of dual (upper and lower branches) solutions when λ<0, that is, when the plate and the free stream move in the opposite directions. Dual solutions of (10)–(12) subject to the boundary conditions (13) exist in the range λ_c ≤ λ<0, where λ_c is the critical value of λ<0 for the existence of the dual solutions. For λ ≤ λ_c<0 the solution of the above mentioned equations based upon the boundary layer approximations is not possible and the full Navier-Stokes equations, energy, and nanoparticle volume fraction equations need to be solved. The present computation gives λ_c = −0.3541 and it is in agreement with that reported by Weidman et al. [38].

Figure 2:

(a) Variation of reduced skin friction coefficient f″(0) with λ for different values of ϕ, (b) variation of reduced heat transfer $- θ^{'} (0)$ with λ for different values of ϕ, (c) variation of reduced mass transfer $- g^{'} (0)$ with λ for different values of ϕ, (d) velocity profiles f′(η) for different values of ϕ, (e) temperature profiles θ(η) for different values of ϕ, and (f) nanoparticle volume fraction profiles g(η) for different values of ϕ.

The variation of the reduced local Nusselt number $- θ^{'} (0)$ (heat transfer rate) and reduced Sherwood number (mass flux rate) with λ for various values of the nanoparticle volume fraction ϕ are presented in Figures 2(b) and 2(c) when f₀ = 0, Le = 2, Nb = 0.5, and Nt = 0.5 in a Cu-water based nanofluid. It is seen that heat transfer rate is consistently higher for higher value of nanoparticle volume fraction parameter, while for λ>0, the mass flux rate is higher for lower value of ϕ. The plots of streamwise velocity profile, temperature profile, and nanofluids volume fraction profile when λ = −0.25, f(0)=0, and Nb=Nt = 0.5 in a Cu-water based nanofluid are shown in Figures 2(d)–2(f), respectively. These profiles show that there exist two different profiles which satisfy the far field boundary conditions (13) asymptotically, thus supporting the dual solutions presented in Figures 2(a)–2(c) for the case of λ<0.

Figures 3(a)–3(c) illustrate the variations of the reduced skin friction coefficient f″(0), reduced Nusselt number $- θ^{'} (0)$ , and reduced Sherwood number -g′(0) with λ, respectively, for various values of f₀, when ϕ = 0.2, Le = 2, and Nb=Nt = 0.5 in a Cu-water based nanofluid. From these figures, it is seen that the skin friction coefficient, heat transfer rate, and mass flux rate are consistently higher as f₀ increases. It is worth mentioning that dual solutions are found only for the suction case (f₀>0) and impermeable case (f₀ = 0) but not for the injection case (f₀<0). On the other hand, we notice that the critical value of the moving parameter $| λ_{c} |$ increases as f₀ increases, as illustrated in Table 2.

Table 2:

Variation of λ_c with suction/injection parameter f₀.

f0	λ_c

−0.5	−0.0649883
0	−0.354107
0.5	−0.815891

Figure 3:

(a) Variation of reduced skin friction coefficient $f^{''} (0)$ with λ for various values of f0, (b) variation of reduced Nusselt number -θ′(0) with λ for various values of f0, (c) variation of reduced Sherwood number -g′(0) with λ for various values of f0, (d) velocity profiles f′(η) for different values of f₀, (e) temperature profiles θ(η) for different values of f₀, and (f) nanoparticle volume fraction profiles g(η) for different values of f0.

Meanwhile the effect of the suction/injection parameter f₀ on the streamwise velocity profiles, temperature profiles, and nanoparticle volume fraction profiles is shown in Figures 3(d)–3(f), respectively, when λ = 0.5 and f₀ = 0.5 (suction case).

Figures 4(a)–4(c) show the variations of the reduced skin friction coefficient, reduced Nusselt number, and reduced Sherwood number with λ, respectively, for different types of nanofluid when ϕ = 0.2, f₀ = 0, Le = 2, and Nb=Nt = 0.5. The value of reduced skin friction coefficient is significantly higher for Cu-water based nanofluid, while its value for TiO₂-water based nanofluid is just slightly higher compared to Al₂O₃-water based nanofluid. It can be seen that Cu-water based nanofluid has the highest heat transfer rate when λ ≤ 1, while Al₂O₃-based nanofluid has the highest heat transfer rate when λ>1. Meanwhile TiO₃-water based nanofluid has the lowest heat transfer rate among the three for the whole observed domain of λ. It is worth mentioning that the critical value of suction/injection parameter λ_c is unique (λ_c = −0.3541) no matter what type of nanofluid is being used and it is again in agreement with that reported by Weidman et al. [38]. The effect of the different nanofluids used on the streamwise velocity profile, temperature profile, and nanoparticle volume fraction profile is shown in Figure 4(d) when λ = 0.

Figure 4:

(a) Variation of reduced skin friction coefficient f″(0) with λ for different types of nanofluid, (b) variation of reduced Nusselt number with λ for different types of nanofluids, (c) variation of reduced Sherwood number with λ for different types of nanofluids, and (d) velocity, temperature, and nanoparticle volume fraction profiles for different nanoparticles.

Figures 5(a) and 5(b) show the effect of Lewis number Le on temperature profile and nanoparticle volume fraction profile, respectively, when Nb=Nt = λ = 0.5, ϕ = 0.2, and f₀ = 0. It can be seen that the effect is more significant on nanoparticle volume fraction profile where increasing the Lewis number resulted in a decrease in the nanoparticle volume fraction boundary layer thickness, which agrees with Bachok et al. [28].

Figure 5:

(a) Temperature profiles θ(η) for various values of Le and (b) nanoparticle volume fraction profiles g(η) for various values of Le.

Figures 6(a) and 6(b) demonstrate the effect of Brownian motion parameter Nb on the temperature profile and nanoparticle volume fraction profile when Le = 2, Nt = 0.5, λ = 0.5, ϕ = 0.2, and f₀ = 0. As seen from the figures, increasing Nb thickens the thermal boundary layer but the reverse effect is seen on nanoparticle volume fraction boundary layer thickness. Similarly, increasing the thermophoresis parameter Nt thickens the thermal boundary layer but there are inconsistent patterns for the nanoparticle volume fraction profile, as shown in Figures 7(a) and 7(b).

Figure 6:

(a) Temperature profiles θ(η) for various values of Nb and (b) nanoparticle volume fraction profiles g(η) for various values of Nb.

Figure 7:

(a) Temperature profiles θ(η) for various values of Nt when Le = 2, Nb = 0.5, λ = 0.25, ϕ = 0.2, and f₀ = 0 and (b) nanoparticle volume fraction profiles ϕ(η) for various values of Nt when Le = 2, Nb = 0.5, λ = 0.25, ϕ = 0.2, and f₀ = 0.

The effect of Prandtl number Pr on the temperature profile and the nanoparticle volume fraction profile is depicted in Figures 8(a) and 8(b), respectively. The temperature at every location in the thermal boundary layer decreases as Pr increases. On the other hand, significant effects of Prandtl number on the nanoparticle volume fraction profile occur in the middle of the boundary layer, specifically when 0.8 ≤ η ≤ 1.6 as shown in Figure 8(b). As Pr increases, the nanoparticle boundary layer thickness increases until η = 1.6, beyond which it decreases to satisfy the far field boundary condition asymptotically, thus supporting the numerical result obtained.

Figure 8:

(a) Temperature profiles θ(η) for various values of Pr when Le = 2, Nb = 0.5, Nt = 0.5, λ = 0.25, ϕ = 0.2, and f₀ = 0 and (b) nanoparticle volume fraction profiles g(η) for various values of Pr when Le = 2, Nb = 0.5, Nt = 0.5, λ = 0.25, ϕ = 0.2, and f₀ = 0.

4. Conclusions

In the present paper, we have studied theoretically the problem of the steady boundary-layer flow of a nanofluid past a permeable moving surface. The governing partial differential equations are transformed into ordinary differential equations, a more convenient form for numerical computation, using a similarity transformation. These equations are solved numerically using the Keller-box method and the shooting method. Numerical results for the skin-friction coefficient, the local Nusselt number, and the local Sherwood number as well as for the velocity, temperature, and the nanoparticle volume fraction profiles are illustrated in some graphs for various parameter conditions. It is found that the reduced skin-friction coefficient and the reduced Nusselt number increase as the nanoparticle volume fraction parameter increases while the opposite effect is seen on the reduced Sherwood number. Besides the reduced skin-friction coefficient, the reduced Nusselt number and the reduced Sherwood number increase due to suction while they decrease due to injection. The surface heat transfer rate in Cu-water nanofluid and Al₂O₃-water nanofluid is consistently higher compared to the rate in TiO₃-water nanofluid. The results also indicate that dual solutions exist when the plate and the free stream flow move in the opposite directions.

Footnotes

Nomenclatures

Conflict of Interests

The authors declare that there is no conflict of interests regarding the publication of this paper.

Acknowledgments

This work is supported by a research university Grant (AP-2013-009) from the Universiti Kebangsaan Malaysia and an FRGS research Grant (Project Code: FRGS/1/2012/SG04/UKM/03/3) from the Ministry of Higher Education, Malaysia. The authors would also like to express their very sincere thanks to the competent reviewers for the very good comments and suggestions.

References

Masuda

Ebata

Teramea

, and Hishinuma

, “Altering the thermal conductivity and viscosity of liquid by dispersing ultra-fine particles,” Netsu Bussei, vol. 4, no. 4, pp. 227–233, 1993.

Choi

S. U. S.

, “Enhancing thermal conductivity of fluids with nanoparticle,” in Developments and Applications of Non-Newtonian Flows, Siginer

D. A.

and Wang

H. P.

, Eds., vol. 231, pp. 99–105, ASME, New York, NY, USA, 1995.

Nield

D. A.

and Kuznetsov

A. V.

, “The Cheng-Minkowycz problem for natural convective boundary-layer flow in a porous medium saturated by a nanofluid,” International Journal of Heat and Mass Transfer, vol. 52, no. 25–26, pp. 5792–5795, 2009.

Pak

B. C.

and Cho

Y. I.

, “Hydrodynamic and heat transfer study of dispersed fluids with submicron metallic oxide particles,” Experimental Heat Transfer, vol. 11, no. 2, pp. 151–170, 1998.

Eastman

J. A.

Choi

S. U. S.

, and Thompson

L. J.

, “Anomalously increased effective thermal conductivities of ethylene glycol-based nanofluids containing copper nanoparticles,” Applied Physics Letters, vol. 78, no. 6, pp. 718–720, 2001.

Das

S. K.

Putra

Thiesen

, and Roetzel

, “Temperature dependence of thermal conductivity enhancement for nanofluids,” Journal of Heat Transfer, vol. 125, no. 4, pp. 567–574, 2003.

Xuan

and Li

, “Investigation on convective heat transfer and flow features of nanofluids,” Journal of Heat Transfer, vol. 125, no. 1, pp. 151–155, 2003.

Mintsa

H. A.

Roy

Nguyen

C. T.

, and Doucet

, “New temperature dependent thermal conductivity data for water-based nanofluids,” International Journal of Thermal Sciences, vol. 48, no. 2, pp. 363–371, 2009.

Buongiorno

and Hu

L.-W.

, “Nanofluid coolants for advanced nuclear power plants 2005,” in Proceedings of the International Congress on Advances in Nuclear Power Plants (ICAPP '05), paper no. 5705, pp. 3581–3585, Seoul, Republic of Korea, May 2005.

10.

Shukla

K. N.

Solomon

A. B.

Pillai

B. C.

, and Ibrahim

, “Thermal performance of cylindrical heat pipe using nanofluids,” Journal of Thermophysics and Heat Transfer, vol. 24, no. 4, pp. 796–802, 2010.

11.

Das

S. K.

Choi

S. U. S.

, and Pradet

, Nanofluids: Science and Technology, John Wiley & Sons, Hoboken, NJ, USA, 2007.

12.

Buongiorno

, “Convective transport in nanofluids,” Journal of Heat Transfer, vol. 128, no. 3, pp. 240–250, 2006.

13.

Kakaç

and Pramuanjaroenkij

, “Review of convective heat transfer enhancement with nanofluids,” International Journal of Heat and Mass Transfer, vol. 52, no. 13–14, pp. 3187–3196, 2009.

14.

Lee

J. H.

Choi

S. H.

Jang

C. J.

, and Choi

S. U. S.

, “A review of thermal conductivity data, mechanics and models for nanofluids,” International Journal of Micro-Nano Scale Transport, vol. 1, no. 4, pp. 269–322, 2010.

15.

Wong

K. V.

and de Leon

, “Applications of nanofluids: current and future,” Advances in Mechanical Engineering, vol. 2010, Article ID 519659, 11 pages, 2010.

16.

and Lin

, “Nanoparticle-laden flows via moment method: a review,” International Journal of Multiphase Flow, vol. 36, no. 2, pp. 144–151, 2010.

17.

Ghadimi

Saidur

, and Metselaar

H. S. C.

, “A review of nanofluid stability properties and characterization in stationary conditions,” International Journal of Heat and Mass Transfer, vol. 54, no. 17–18, pp. 4051–4068, 2011.

18.

Ramesh

and Prabhu

N. K.

, “Review of thermo-physical properties, wetting and heat transfer characteristics of nanofluids and their applicability in industrial quench heat treatment,” Nanoscale Research Letters, vol. 6, article 334, 2011.

19.

Sarkar

, “A critical review on convective heat transfer correlations of nanofluids,” Renewable and Sustainable Energy Reviews, vol. 15, no. 6, pp. 3271–3277, 2011.

20.

Fan

and Wang

, “Review of heat conduction in nanofluids,” Journal of Heat Transfer, vol. 133, no. 4, Article ID 040801, 14 pages, 2011.

21.

Saidur

Kazi

S. N.

Hossain

M. S.

Rahman

M. M.

, and Mohammed

H. A.

, “A review on the performance of nanoparticles suspended with refrigerants and lubricating oils in refrigeration systems,” Renewable and Sustainable Energy Reviews, vol. 15, no. 1, pp. 310–323, 2011.

22.

Thomas

and Panicker Sobhan

C. B.

, “A review of experimental investigations on thermal phenomena in nanofluids,” Nanoscale Research Letters, vol. 6, article 377, 2011.

23.

Mahian

Kianifar

Kalogirou

S. A.

Pop

, and Wongwises

, “A review of the applications of nanofluids in solar energy,” International Journal of Heat and Mass Transfer, vol. 57, no. 2, pp. 582–594, 2013.

24.

Nield

D. A.

and Kuznetsov

A. V.

, “The Cheng-Minkowycz problem for the double-diffusive natural convective boundary layer flow in a porous medium saturated by a nanofluid,” International Journal of Heat and Mass Transfer, vol. 54, no. 1–3, pp. 374–378, 2011.

25.

Kuznetsov

A. V.

and Nield

D. A.

, “Natural convective boundary-layer flow of a nanofluid past a vertical plate,” International Journal of Thermal Sciences, vol. 49, no. 2, pp. 243–247, 2010.

26.

Kuznetsov

A. V.

and Nield

D. A.

, “Double-diffusive natural convective boundary-layer flow of a nanofluid past a vertical plate,” International Journal of Thermal Sciences, vol. 50, no. 5, pp. 712–717, 2011.

27.

Khan

W. A.

and Pop

, “Boundary-layer flow of a nanofluid past a stretching sheet,” International Journal of Heat and Mass Transfer, vol. 53, no. 11–12, pp. 2477–2483, 2010.

28.

Bachok

Ishak

Nazar

, and Pop

, “Flow and heat transfer at a general three-dimensional stagnation point in a nanofluid,” Physica B: Condensed Matter, vol. 405, no. 24, pp. 4914–4918, 2010.

29.

Khan

W. A.

and Aziz

, “Natural convection flow of a nanofluid over a vertical plate with uniform surface heat flux,” International Journal of Thermal Sciences, vol. 50, no. 7, pp. 1207–1214, 2011.

30.

Tham

Nazar

, and Pop

, “Mixed convection boundary layer flow past a horizontal circular cylinder embedded in a porous medium saturated by a nanofluid: Brinkman model,” Journal of Porous Media, vol. 16, no. 5, pp. 445–457, 2013.

31.

Tiwari

R. K.

and Das

M. K.

, “Heat transfer augmentation in a two-sided lid-driven differentially heated square cavity utilizing nanofluids,” International Journal of Heat and Mass Transfer, vol. 50, no. 9–10, pp. 2002–2018, 2007.

32.

Ahmad

Rohni

A. M.

, and Pop

, “Blasius and Sakiadis problems in nanofluids,” Acta Mechanica, vol. 218, no. 3–4, pp. 195–204, 2011.

33.

Rohni

A. M.

Ahmad

, and Pop

, “Boundary layer flow over a moving surface in a nanofluid beneath a uniform free stream,” International Journal of Numerical Methods for Heat and Fluid Flow, vol. 21, no. 7, pp. 828–846, 2011.

34.

Bachok

Ishak

, and Pop

, “Flow and heat transfer over a rotating porous disk in a nanofluid,” Physica B: Condensed Matter, vol. 406, no. 9, pp. 1767–1772, 2011.

35.

Bachok

Ishak

, and Pop

, “Flow and heat transfer characteristics on a moving plate in a nanofluid,” International Journal of Heat and Mass Transfer, vol. 55, no. 4, pp. 642–648, 2012.

36.

Nazar

Tham

Pop

, and Ingham

D. B.

, “Mixed convection boundary layer flow from a horizontal circular cylinder embedded in a porous medium filled with a nanofluid,” Transport in Porous Media, vol. 86, no. 2, pp. 517–536, 2011.

37.

Yasin

M. H. M.

Arifin

N. M.

Nazar

Ismail

, and Pop

, “Mixed convection boundary layer flow embedded in a thermally stratified porous medium saturated by a nanofluid,” Advances in Mechanical Engineering, vol. 2013, Article ID 121943, 8 pages, 2013.

38.

Weidman

P. D.

Kubitschek

D. G.

, and Davis

A. M. J.

, “The effect of transpiration on self-similar boundary layer flow over moving surfaces,” International Journal of Engineering Science, vol. 44, no. 11–12, pp. 730–737, 2006.

39.

Goldstein

, “On backward boundary layer and flow in converging passages,” Journal of Fluid Mechanics, vol. 21, no. 1, pp. 33–45, 1965.

40.

Oztop

H. F.

and Abu-Nada

, “Numerical study of natural convection in partially heated rectangular enclosures filled with nanofluids,” International Journal of Heat and Fluid Flow, vol. 29, no. 5, pp. 1326–1336, 2008.

41.

Cebeci

and Bradshaw

, Momentum Transfer in Boundary Layers, Hemisphere, New York, NY, USA, 1977.

42.

Cebeci

and Bradshaw

, Physical and Computational Aspects of Convective Heat Transfer, Springer, New York, NY, USA, 1988.

43.

Meade

D. B.

Haran

B. S.

, and White

R. E.

, “The shooting technique for the solution of two-point boundary value problems,” Maple Technologies, vol. 3, pp. 85–93, 1996.

44.

Blasius

, “Grenzschichten in flüsssigkeiten mit kleiner reibung,” Zeitschrift für Angewandte Mathematik und Physik, vol. 56, pp. 1–37, 1908.

45.

White

F. M.

, Viscous Fluid Flowed, McGraw-Hill, New York, NY, USA, 3rd edition, 2006.

Boundary-Layer Flow and Heat Transfer of Nanofluids over a Permeable Moving Surface in the Presence of a Coflowing Fluid

Abstract

1. Introduction

2. Problem Formulation

3. Results and Discussion

4. Conclusions

Footnotes

Nomenclatures

Conflict of Interests

Acknowledgments

References