Boundary-layer flow of a nanofluid past a stretching sheet
Introduction
The flow over a stretching surface is an important problem in many engineering processes with applications in industries such as extrusion, melt-spinning, the hot rolling, wire drawing, glass–fiber production, manufacture of plastic and rubber sheets, cooling of a large metallic plate in a bath, which may be an electrolyte, etc. In industry, polymer sheets and filaments are manufactured by continuous extrusion of the polymer from a die to a windup roller, which is located at a finite distance away. The thin polymer sheet constitutes a continuously moving surface with a non-uniform velocity through an ambient fluid [1]. Experiments show that the velocity of the stretching surface is approximately proportional to the distance from the orifice [2]. Crane [3] studied the steady two-dimensional incompressible boundary layer flow of a Newtonian fluid caused by the stretching of an elastic flat sheet which moves in its own plane with a velocity varying linearly with the distance from a fixed point due to the application of a uniform stress. This problem is particularly interesting since an exact solution of the two-dimensional Navier–Stokes equations has been obtained by Crane [3]. After this pioneering work, the flow field over a stretching surface has drawn considerable attention and a good amount of literature has been generated on this problem [4], [5], [6], [7], [8], [9].
In recent years, some interest has been given to the study of convective transport of nanofluids. Conventional heat transfer fluids, including oil, water, and ethylene glycol mixture are poor heat transfer fluids, since the thermal conductivity of these fluids plays an important role on the heat transfer coefficient between the heat transfer medium and the heat transfer surface. Therefore, numerous methods have been taken to improve the thermal conductivity of these fluids by suspending nano/micro or larger-sized particle materials in liquids [10]. An innovative technique to improve heat transfer is by using nano-scale particles in the base fluid [11]. Nanotechnology has been widely used in industry since materials with sizes of nanometers possess unique physical and chemical properties. Nano-scale particle added fluids are called as nanofluid, which is firstly utilized by Choi [11]. Choi et al. [12] showed that the addition of a small amount (less than 1% by volume) of nanoparticles to conventional heat transfer liquids increased the thermal conductivity of the fluid up to approximately two times. Khanafer et al. [13] seem to be the first who have examined heat transfer performance of nanofluids inside an enclosure taking into account the solid particle dispersion. After these authors, nanotechnology is considered by many to be one of the significant forces that drive the next major industrial revolution of this century. It represents the most relevant technological cutting edge currently being explored. It aims at manipulating the structure of the matter at the molecular level with the goal for innovation in virtually every industry and public endeavor including biological sciences, physical sciences, electronics cooling, transportation, the environment and national security. Some numerical and experimental studies on nanofluids include thermal conductivity [14], convective heat transfer [15], [16], [17], [18], [19]. A comprehensive survey of convective transport in nanofluids was made by Buongiorno [20] and. Kakaç and Pramuanjaroenkij [10]. Very recently, Kuznetsov and Nield [21] have examined the influence of nanoparticles on natural convection boundary-layer flow past a vertical plate, using a model in which Brownian motion and thermophoresis are accounted for. The authors have assumed the simplest possible boundary conditions, namely those in which both the temperature and the nanoparticle fraction are constant along the wall. Further, Nield and Kuznetsov [22] have studied the Cheng–Minkowycz [23] problem of natural convection past a vertical plate, in a porous medium saturated by a nanofluid. The model used for the nanofluid incorporates the effects of Brownian motion and thermophoresis. For the porous medium the Darcy model has been employed.
The objective of the present study is to analyze the development of the steady boundary layer flow, heat transfer and nanoparticle fraction over a stretching surface in a nanofluid. A similarity solution is presented. This solution depends on a Prandtl number Pr, a Lewis number Le, a Brownian motion number Nb and a thermophoresis number Nt. The dependency of the local Nusselt and local Sherwood numbers on these four parameters is numerically investigated. To our best of knowledge, the results of this paper are new and they have not been published before.
Section snippets
Basic equations
We consider the steady two-dimensional boundary layer flow of a nanofluid past a stretching surface with the linear velocity uw(x) = ax, where a is a constant and x is the coordinate measured along the stretching surface, as shown in Fig. 1. The flow takes place at , where y is the coordinate measured normal to the stretching surface. A steady uniform stress leading to equal and opposite forces is applied along the x-axis so that the sheet is stretched keeping the origin fixed. It is assumed
Results and discussion
Eqs. (8), (9), (10) subject to the boundary conditions (11) have been solved numerically for some values of the governing parameters Pr, Pe, Nb and Nt using an implicit finite-difference method. Neglecting the effects of Nb and Nt numbers, the results for the reduced Nusselt number −θ′(0) are compared with those obtained by Wang [24], and Gorla and Sidawi [25] for different values of Pr in Table 1. We notice that the comparison shows good agreement for each value of Pr. Therefore, we are
Conclusions
The problem of laminar fluid flow resulting from the stretching of a flat surface in a nanofluid has been investigated numerically first time. The model used for the nanofluid incorporates the effects of Brownian motion and thermophoresis. A similarity solution is presented which depends on the Prandtl number Pr, Lewis number Le, Brownian motion number Nb and thermophoresis number Nt. The variation of the reduced Nusselt and reduced Sherwood numbers with Nb and Nt for various values of Pr and Le
Acknowledgments
The authors wish to express their very sincerely thanks to the reviewers for their valuable comments and suggestions.
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