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Nanoscale Res Lett. 2012; 7(1): 94.
Published online Jan 30, 2012. doi:  10.1186/1556-276X-7-94
PMCID: PMC3305502

Boundary layer flow of nanofluid over an exponentially stretching surface

Abstract

The steady boundary layer flow of nanofluid over an exponential stretching surface is investigated analytically. The transport equations include the effects of Brownian motion parameter and thermophoresis parameter. The highly nonlinear coupled partial differential equations are simplified with the help of suitable similarity transformations. The reduced equations are then solved analytically with the help of homotopy analysis method (HAM). The convergence of HAM solutions are obtained by plotting h-curve. The expressions for velocity, temperature and nanoparticle volume fraction are computed for some values of the parameters namely, suction injection parameter α, Lewis number Le, the Brownian motion parameter Nb and thermophoresis parameter Nt.

Keywords: nanofluid, porous stretching surface, boundary layer flow, series solutions, exponential stretching

1 Introduction

During the last many years, the study of boundary layer flow and heat transfer over a stretching surface has achieved a lot of success because of its large number of applications in industry and technology. Few of these applications are materials manufactured by polymer extrusion, drawing of copper wires, continuous stretching of plastic films, artificial fibers, hot rolling, wire drawing, glass fiber, metal extrusion and metal spinning etc. After the pioneering work by Sakiadis [1], a large amount of literature is available on boundary layer flow of Newtonian and non-Newtonian fluids over linear and nonlinear stretching surfaces [2-10]. However, only a limited attention has been paid to the study of exponential stretching surface. Mention may be made to the works of Magyari and Keller [11], Sanjayanand and Khan [12], Khan and Sanjayanand [13], Bidin and Nazar [14] and Nadeem et al. [15,16].

More recently, the study of convective heat transfer in nanofluids has achieved great success in various industrial processes. A large number of experimental and theoretical studies have been carried out by numerous researchers on thermal conductivity of nanofluids [17-22]. The theory of nanofluids has presented several fundamental properties with the large enhancement in thermal conductivity as compared to the base fluid [23].

In this study, we have discussed the boundary layer flow of nanofluid over an exponentially stretching surface with suction and injection. To the best of our knowledge, the nanofluid over an exponentially stretching surface has not been discussed so far. However, the present paper is only a theoretical idea, which is not checked experimentally. The governing highly nonlinear partial differential equation of motion, energy and nanoparticle volume fraction has been simplified by using suitable similarity transformations and then solved analytically with the help of HAM [24-39]. The convergence of HAM solution has been discussed by plotting h-curve. The effects of pertinent parameters of nanofluid have been discussed through graphs.

2 Formulation of the problem

Consider the steady two-dimensional flow of an incompressible nanofluid over an exponentially stretching surface. We are considering Cartesian coordinate system in such a way that x-axis is taken along the stretching surface in the direction of the motion and y-axis is normal to it. The plate is stretched in the x-direction with a velocity Uw = U0 exp (x/l). defined at y = 0. The flow and heat transfer characteristics under the boundary layer approximations are governed by the following equations

ux+vy=0,
(1)
uux+vuy=ν2uy2,
(2)
uTx+vTy=α2Ty2+ρcpρcfDBCyTy+DTTTy2,
(3)
uCx+vCy=DB2Cy2+DTT2Ty2,
(4)

where (u, v) are the velocity components in (x, y) directions, ρf is the fluid density of base fluid, ν is the kinematic viscosity, T is the temperature, C is the nanoparticle volume fraction, (ρc)p is the effective heat capacity of nanoparticles, (ρc)f is the heat capacity of the fluid, α = k/(ρc)f is the thermal diffusivity of the fluid, DB is the Brownian diffusion coefficient and DT is the thermophoretic diffusion coefficient.

The corresponding boundary conditions for the flow problem are

u=Uwx=U0expx/l,v=-βx,T=Tw,C=Cwaty=0,u=0,T=TC=Casy,
(5)

in which U0 is the reference velocity, β(x) is the suction and injection velocity when β(x) > 0 and β(x) < 0, respectively, Tw and Tare the temperatures of the sheet and the ambient fluid, Cw, Care the nanoparticles volume fraction of the plate and the fluid, respectively.

We are interested in similarity solution of the above boundary value problem; therefore, we introduce the following similarity transformations

u=U0expxlfη,v=-vU02lexpx2lfη+ηfη,η=yU02vlexpx2l,θ=T-TTw-T,g=C-CCw-C.
(6)

Making use of transformations (6), Eq. (1) is identically satisfied and Equations (2)-(4) take the form

fηηη+ffηη-2fη2=0,
(7)
θηη+Prfθη-fηθ+Nbθηgη+Ntθη2=0
(8)
gηη+Lefgη-fηg+NtNbθηη=0,
(9)
f=-vw,fη=1,θ=1,g=1atη=0,fη0,θ0,g0asη,
(10)

where

Nt=DBρcpρcfCw-C,Nb=DTTρcpρcfTw-Tυ,Le=υDB,Pr=υα.

The physical quantities of interest in this problem are the local skin-friction coefficient Cf, Nusselt number Nux and the local Sherwood number Shx, which are defined as

equation image
(11)

where Rex = Uwx/ν is the local Renolds number.

3 Solution by homotopy analysis method

For HAM solutions, the initial guesses and the linear operators Li (i = 1 - 3) are

f0η=1-vw-e-η,θ0η=e-η,g0η=e-η,
(12)
1f=f-f,2θ=θ-θ,3g=g-g.
(13)

The operators satisfy the following properties

1c1e-η+c2eη+c3=0,
(14)
2c4e-η+c5eη=0,
(15)
3c6e-η+c7eη=0,
(16)

in which C1 to C7 are constants. From Equations (7) to (9), we can define the following zeroth-order deformation problems

1-p1f ^η,p-f0η=p1H1Ñ1f ^η,p,
(17)
1-p2θ^η,p-θ0η=p2H2Ñ2θ^η,p,
(18)
1-p3ĝη,p-g0η=p3H3Ñ3ĝη,p,
(19)
f ^0,p=-vw,f ^0,p=1,f ^,p=0,
(20)
θ^0,p=1,θ^,p=0,
(21)
ĝ0,p=1,ĝ,p=0.
(22)

In Equations (17)-(22), ħ1, ħ2, and ħ3 denote the non-zero auxiliary parameters, H1, H2 and H3 are the non-zero auxiliary function (H1 = H2 = H3 = 1) and

Ñ1f ^η,p=3fη3-2fη2+f2fη2,
(23)
Ñ2θ^η,p=2θη2+Prfθη-fηθ+Nbθηgη+Ntθη2,
(24)
Ñ3ĝη,p=2gη2+Lefgη-fηg+NtNbθηη+NtNb2θη2.
(25)

Obviously

f ^η,0=f0η,f ^η,1=fη,
(26)
θ^η,0=θ0η,θ^η,1=θη,
(27)
ĝη,0=g0η,ĝη,1=gη.
(28)

When p varies from 0 to 1, then f ^η,p, θ^η,p, ĝη,p vary from initial guesses f0 (η), θ0 (η) and g0 (η) to the final solutions f (η), θ (η) and g (η), respectively. Considering that the auxiliary parameters ħ1, ħ2 and ħ3 are so properly chosen that the Taylor series of f ^η,p, θ^η,p and ĝη,p expanded with respect to an embedding parameter converge at p = 1, hence Equations (17)-(19) become

f ^η,p=f0η+m=1fmηpm,
(29)
θ^η,p=θ0η+m=1θmηpm,
(30)
ĝη,p=g0η+m=1gmηpm,
(31)
fmη=1m!mf ^η,ppmp=0,
(32)
θmη=1m!mθ^η,ppmp=0,
(33)
gmη=1m!mĝη,ppmp=0.
(34)

The mth-order problems are defined as follow

1fmη-χmfm-1η=1Řm1η,
(35)
2θmη-χmθm-1η=2Řm2η,
(36)
3gmη-χmgm-1η=3Řm3η,
(37)
fm0=fm0=fm=0,
(38)
θm0=θm=0,
(39)
gm0=gm=0,
(40)

where

χm=0,m1,1,m>1.
(41)
Řm1η=fm-1η+k=0m-1fm-1-kfk-2k=0m-1fm-1-kfk,
(42)
Řm2η=θm-1+Prk=0m-1fm-1-kθk-fm-1-kθk+Nbθm-1-kgk+Ntθm-1-kθk,
(43)
Řm3η=gm-1+Lek=0m-1fm-1-kgk-fm-1-kgk+NtNbθm-1.
(44)

Employing MATHEMATICA, Equations (35)-(40) have the following solutions

fη=m=0fmη=limMm=0Mam,00+n=1M+1e-nηm=n-1Mk=0m+1-nam,nkηk,
(45)
θη=m=0θmη=limMn=1M+2e-nηm=n-1M+1k=0m+1-nAm,nkηk,
(46)
gη=m=0gmη=limMn=1M+2e-nηm=n-1M+1k=0m+1-nFm,nkηk,
(47)

in which am,00, am,nk, Am,nk, Fm,nk are the constants and the numerical data of above solutions are shown through graphs in the following section.

4 Results and discussion

The numerical data of the solutions (45)-(47), which is obtained with the help of Mathematica, have been discussed through graphs. The convergence of the series solutions strongly depends on the values of non-zero auxiliary parameters ħi (i = 1, 2, 3, h1 = h2 = h3), which can adjust and control the convergence of the solutions. Therefore, for the convergence of the solution, the ħ-curves is plotted for velocity field in Figure Figure1.1. We have found the convergence region of velocity for different values of suction injection parameter vw. It is seen that with the increase in suction parameter vw, the convergence region become smaller and smaller. Almost similar kind of convergence regions appear for temperature and nanoparticle volume fraction, which are not shown here. The non-dimensional velocity f′ against η for various values of suction injection parameter is shown in Figure Figure2.2. It is observed that velocity field increases with the increase in vw. Moreover, the suction causes the reduction of the boundary layer. The temperature field θ for different values of Prandtle number Pr, Brownian parameter Nb, Lewis number Le and thermophoresis parameter Nt is shown in Figures Figures3,3, ,4,4, ,55 and and6.6. In Figure Figure3,3, the temperature is plotted for different values of Pr. It is observed that with the increase in Pr, there is a very slight change in temperature; however, for very large Pr, the solutions seem to be unstable, which are not shown here. The variation of Nb on θ is shown in Figure Figure4.4. It is depicted that with the increase in Nb, the temperature profile increases. There is a minimal change in θ with the increase in Le (see Figure Figure5).5). The results remain unchanged for very large values of Le. The effects of Nt on θ are seen in Figure Figure6.6. It is seen that temperature profile increases with the increase in Nt; however, the thermal boundary layer thickness reduces. The nanoparticle volume fraction g for different values of Pr, Nb, Nt and Le is plotted in Figures Figures7,7, ,8,8, ,99 and and10.10. It is observed from Figure Figure77 that with the increase in Nb, g decreases and boundary layer for g also decreases. The effects of Pr on g are minimal. (See Figure Figure8).8). The effects of Le on g are shown in Figure Figure9.9. It is observed that g decreases as well as layer thickness reduces with the increase in Le. However, with the increase in Nt, g increases and layer thickness reduces (See Figure Figure1010).

Figure 1
h-Curve for velocity.
Figure 2
Velocity for different values of suction and injection parameter.
Figure 3
Variation of temperature for different values of Pr when Le = 2, h = -0.1, Nt = Nb = 0.5, vw= 1.
Figure 4
Variation of temperature for different values of Nb when Le = 2, h = -0.1, Nt = 0.5, vw = 1, Pr = 2.
Figure 5
Variation of temperature for different values of Le when h = -0.1, Nt = Nb = 0.5, vw = 1, Pr = 2.
Figure 6
Variation of temperature for different values of Nt when Le = 2, h = -0.1, Nb = 0.5, vw = 1, Pr = 2.
Figure 7
Variation of nanoparticle fraction g for different values of Nb when Le = 2, h = -0.1, Nt = 0.5, vw = 1, Pr = 2.
Figure 8
Variation of nanoparticle fraction g for different values of Pr when Le = 2, h = -0.1, Nt = 0.5, vw = 1, Nb = 0.5.
Figure 9
Variation of nanoparticle fraction g for different values of Le when Pr = 2, h = -0.1, Nt = 0.5, vw = 1, Nb = 0.5.
Figure 10
Variation of nanoparticle fraction g for different values of Nt when Le = 2, h = -0.1, Nt = 0.5, vw = 1, Pr = 2.

Competing interests

This is just the theoretical study, every experimentalist can check it experimentally with our consent.

Authors' contributions

SN done the major part of the article; however, the funding and computational suggestions and proof reading has been done by CL. All authors read and approved the final manuscript.

Acknowledgements

This research was supported by WCU (World Class University) program through the National Research Foundation of Korea (NRF) funded by the Ministry of Education, Science and Technology R31-2008-000-10049-0.

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