Abstract

In the present study, the onset of thermal convection in a liquid layer overlying a porous layer where the whole system is being laterally heated is investigated. The non-linear two-dimensional Navier Stokes equations, the energy equation, the mass balance equation and the continuity equation are solved for the liquid layer. Instead of the Navier Stokes equations, the Brinkman model is used for the porous layer. The partial differential equations are solved numerically using the finite element technique. A two-dimensional geometrical model with lateral heating is considered. Two different cases are analyzed in this thesis. In the first case, the gravity driven buoyancy convection and the Marangoni convection are studied. For the Marangoni convection, the microgravity condition is considered and the surface tension is assumed to vary linearly with temperature. Different aspect ratios, as well as thickness ratios, are studies in detail for both the buoyancy and the Marangoni convection. Results revealed that for both the buoyancy and the Marangoni cases, flow penetrates into the porous layer, only when the thickness ratio is more than 0.90. In the case of thermo-solutal convection in the presence of Soret effect, it has been found that the isopropanol component goes either towards the hot or the cold walls depending on the fluid mixtures which has been used in the system.

Highlights

  • Introduction and Literature Review1.1 IntroductionA vertically stacked system of porous and fluid layers.1 with heat and mass transfer taking place through the interface.1 is related to many natural phenomena and various industrial applications

  • From this figure we can see that for the thickness ratio d = 0.50 the flow is limited to the liquid layer only

  • For the buoyancy convection case, it has been found that the switching of the flow from fluid layer don1inated to porous layer dominated convection depends upon the thickness ratio, aspect ratio, Prandtl number and Rayleigh number of the liquid

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Summary

G Non-dimensional overall thermal conductivity

Velocity component in the x direction u Non-di1nensional velocity cmnponent in the X direction = _!!__ Uo Characteristic velocity =-Jg. f3r· 11T. L. Velocity con1ponent in the y direction v Non-di1nensional velocity co1nponent in the Y direction = ~ Uo. So1uta1Ray1e1.gh number 1c.0r porous 1ayer= .g.:.::f:3::c..../.1..C:~-.-d---2-=.=K--. Therma1Ray1et.gh number 1c.0r porous 1ayer= g .f3r .11T.d2. Sr f3c Solutal expansion fJr Thennal volume expansion y

Introduction
Onset of gravity driven and Marangoni convection
Onset of Thermo-solutal Convection with Soret Effect
Model Description
Research objective
Liquid Layer Governing Equations
Momentum Balance Equation
Porous Layer Governing Equations
Non-Dimensional Analysis
Energy Balance Equation
Model Boundary Conditions
Numerical Solution technique
Finite Element Analysis
Mesh Sensitivity Analysis
Convection in the presence of Buoyancy
Various effects on Buoyancy Convection
Convection in the presence of Marangoni
Various effects on Marangoni Convection
Summary
Thermo-solutal Convection
Buoyancy Convection Condition
Thermodiffusion
Thermodiffusion with negative S T
Thermodiffusion with PositiveSr
Separation ratio
Thermo-Solutal Convection for Combined Fluid
Marangoni Convection Condition
Thermodiffusion Effect for Combined Fluid
Conclusion and Future Work
X-direction Momentum Balance equation
Continuity equation
Liquid Layer
For the case when different compositions present in the liquid and in the porous layer
Findings
Thermo-solutal convection
Full Text
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