Brinkman convection induced by purely internal heating in a rotating porous medium layer saturated by a nanofluid
Graphical abstract
Introduction
In recent years, nanofluid flow in porous medium has increased into a substantial area of research due to their numerous applications in different fields such as chemical industry, solar collectors, microbial fuel cells, materials processing, biological propulsion, nuclear waste disposals, and geothermal energy systems, where nanofluid injection results in greater thermal efficiency [1], [2], [3], [4], [5]. The term “nanofluid” was first coined by Choi [6] to show engineered colloids which are composed of nanoparticles dispersed in a base fluid. Materials commonly utilized for nanoparticles include metals such as copper and gold, and oxides such as alumina, silica and copper oxide. Popular base fluids consist of water, oil and organic fluids. Relative to the base fluid, it has been detected consistently by many researchers that the nanofluids have abnormal thermal conductivity, viscosity and single-phase convective heat transfer coefficient. These fluids are considered to offer vital advantages over conventional heat transfer fluids [7], [8], [9], [10].
In review of its importance, many authors have studied the flow of nanofluid in a porous medium between two parallel plates. Nield and Kuznetsov [11] were the first to study the onset of convection in the horizontal porous layer saturated by a nanofluid with Darcy model on the basis of the transport equations developed by Buongiorno [12]. Later, Yadav et al. [13], [14], [15], [16], [17], [18], [19], Nield and Kuznetsov [20], [21], [22], Kuznetsov and Nield [23], [24], [25], Umavathi et al. [26], Shivakumara et al. [27], Hosseini et al. [28] and Hatami et al. [29] extended this problem with varying assumptions. The effect of magnetic field on the nanofluid flow and heat transfer characteristic was studied by Yadav et al. [30], [31], [32], [33], Jalilpour et al. [34], Sheikholeslami et al. [35], Ghasemi et al. [36] and Hatami et al. [37]. The common finding of those studies was that the fluid experienced a Lorentz force. This force, in turn, affects the buoyant flow field and the heat transfer rate.
It is known that there are large numbers of practical situation in which convection is driven by its own source of heat. This gives a different way in which a convective flow can be set up through the internal heat generation within the porous medium layer. Such a situation can happen through nuclear reaction, radioactive decay or a rather weak exothermic reaction which can take place within the porous material. Therefore, the role of internal heat generation becomes very important in several applications including chemical engineering, nuclear heat cores, nuclear energy, nuclear waste disposals, oil extractions and crystal growth. But, there are only few studies available in which the convection induced by purely internal heating has been investigated. Gasser and Kazimi [38] were the first to study the convection in a porous medium which is induced by both internal heat generation and heating from below. They introduced two Rayleigh number; one corresponding to internal heating, other to the external temperature gradient. The Brinkman model for natural convection in a porous layer with nonuniform thermal gradient was analyzed by Vasseur and Robillard [39]. They obtained a stability problem similar to that of Gasser and Kazimi [38] except that the disturbance temperatures satisfy Neumann rather than Dirichlet boundary conditions. Later, Nouri-Borujerdi et al. [40] analysed the influence of Darcy number on the onset of convection in a porous layer induced by purely internal heating for rigid–rigid boundaries. They obtained a smooth monotonic variation in the critical internal Rayleigh number accurately. Recently, Ghasemi et al. [41] studied thermal analysis of convective fin with temperature-dependent thermal conductivity and heat generation. They used a simple and highly accurate semi-analytical method called the Differential Transformation Method (DTM) for solving the nonlinear temperature distribution equation.
The study related to internal heat source in porous medium saturated by nanofluid was first presented by Yadav et al. [42]. They completed their analysis in terms of a standard external Rayleigh–Darcy number and used the same boundary conditions on the nanofluid fraction as those used by Nield and Kuznetsov [11]. These boundary conditions were of limited practical validity. Very recently, Nield and Kuznetsov [43] considered the case of purely internal heating for Darcy porous medium and re-examine the boundary conditions for volumetric fraction of nanoparticles that the nanofluid particle fraction was allowed to adapt to the temperature profile induced by the internal heating. They obtained that the presence of the nanofluid particles leads to increased instability of the system.
In all of the above studies, the convection via purely internal heating in rotating porous medium saturated by a nanofluid was not studied. However, it is well known the convection via purely internal heating in rotating porous medium saturated by a nanofluid is of great interest in the microwave heating of liquids. Microwave heating finds application in the chemical engineering, particle deposition rate in nuclear reactors, electronic chips, semiconductor and wafers food industry such as in pasteurization, sterilization etc. Therefore, in this paper, we analyze the stability criteria of a horizontal nanofluid layer undergoing rotation, irradiated by purely internal heating, such as that produced by microwave heating or chemical reaction, instead of bottom heating for two sets of thermal boundary conditions.
Section snippets
Problem formulation
The physical configuration is as shown in Fig. 1. We consider convection due to uniform internal heating of strength Q0⁎ in a system consisting of a horizontal layer of an incompressible nanofluid-saturated Brinkman porous medium of thickness L. The porous layer is rotating uniformly about vertical axis at a constant angular velocity Ω* = (0, 0, Ω*). A Cartesian coordinate system (x, y, z) is chosen such that the origin is at the bottom of the porous layer and the gravity is acting in the negative
Method of solution
Eqs. (40), (41), (42), (43) together with the boundary conditions (44) constitute a linear eigenvalue problem of the system. The resulting eigenvalue problem is solved numerically by the higher order Galerkin method to get more accurate results. Accordingly, the variables are written in a series of base functions as:
where, As, Bs, Cs and Ds are unknown coefficients, s = 1, 2, 3, … N and the base functions Ws, Θs, Φs and Ζs are assumed in the following
Results and discussion
The onset of convection induced by purely internal heating is investigated in a horizontal layer of rotating Brinkman porous medium saturated by a nanofluid. The boundaries are considered to be rigid–rigid and the normal flux of volume fraction of nanoparticles is assumed to be zero on the boundaries. As the thermal nature of boundary surface, two cases are considered namely; Case (i) – both boundaries isothermal – and Case (ii) – lower insulated and upper isothermal. For problem considered
Conclusions
The criterion for the onset of convection induced by purely internal heating in a rotating porous layer saturated by a nanofluid was examined numerically for rigid–rigid boundary surfaces with two sets of thermal boundary conditions. Results show that the convection, when it occurs for Case (i) – both boundaries isothermal, is concentrated in the upper portion of the layer, while for Case (ii) – lower insulated and upper isothermal boundaries, it is concentrated in the whole layer. The effects
Acknowledgment
This work was supported by the Yonsei University Research Fund of 2014–15. and the Korea Institute of Energy Technology Evaluation and Planning (KETEP, No. 20144030200560) grant funded by the Korea government Ministry of Trade, Industry and Energy.
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