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http://hdl.handle.net/10603/222730
Title: | Unsteady Convective Heat Transfer in Liquid Saturated and Unsaturated Porous Media with Reference to an Energy Storage System |
Researcher: | Singh, Chanpreet |
Guide(s): | Tathgir, R. G. and Muralidhar, K. |
Keywords: | 1-Equation Model 2-Equation Model Forced Convection Glass-Water Bed Porous Medium Steel-Water Bed |
University: | Thapar Institute of Engineering and Technology |
Completed Date: | 2007 |
Abstract: | Flow and heat transfer in porous media has received much attention due to its importance in various fields of engineering: mechanical, chemical, ground water hydrology, petroleum engineering, soil mechanics and environmental science. The examination of transport in porous media relies on the knowledge gained in studying these phenomena in plain media. The mathematical modeling of convective heat transfer in a porous medium is carried out by volume averaging of governing energy equations for the fluid and the solid phases. The interphase convective heat transfer coefficient hsf couples these two energy equations at the interface. In addition, this model also contains effective thermal conductivity and dispersion tensors and is expected to give reasonably good predictions. This model is called the thermal non-equilibrium model or the 2-equation model. It is advantageous to use this model, as against the thermal equilibrium or 1-equation model, when there is significant heat generation in one of the phases, during sudden heating/cooling of the medium and when the thermal properties of the two phases are distinct. The volume-averaged energy equations based on thermal equilibrium and thermal non-equilibrium between the two phases are developed. The finite difference discretization of the model is carried out by using implicit format for the time derivatives, central difference scheme for second order partial-spatial derivatives and the upwind scheme and QUICK approaches for modeling of convective terms. The resulting algebraic equations are solved by Gauss-Seidel iterations using sufficiently fine grid in space and large number of time-steps. The numerical simulation is first compared with analytical results obtained by neglecting various terms of the mathematical model such as interphase heat transfer and convection. These include 2-D unsteady state conduction, 1-D and 2-D unsteady advection-diffusion in plain flow i.e. no solid phase present in the medium. |
Pagination: | xxxvii, 335p. |
URI: | http://hdl.handle.net/10603/222730 |
Appears in Departments: | Department of Mechanical Engineering |
Files in This Item:
File | Description | Size | Format | |
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file10(chapter 7).pdf | Attached File | 473.01 kB | Adobe PDF | View/Open |
file11(chapter 8).pdf | 463.58 kB | Adobe PDF | View/Open | |
file12(chapter 9).pdf | 447.54 kB | Adobe PDF | View/Open | |
file13(chapter 10).pdf | 566.41 kB | Adobe PDF | View/Open | |
file14(chapter 11).pdf | 328.72 kB | Adobe PDF | View/Open | |
file15(chapter 12).pdf | 71.06 kB | Adobe PDF | View/Open | |
file16(reference).pdf | 80.88 kB | Adobe PDF | View/Open | |
file17(list of publications).pdf | 34.95 kB | Adobe PDF | View/Open | |
file1(title).pdf | 79.4 kB | Adobe PDF | View/Open | |
file2(certificate).pdf | 101.72 kB | Adobe PDF | View/Open | |
file3(preliminary pages).pdf | 213.28 kB | Adobe PDF | View/Open | |
file4(chapter 1).pdf | 75.95 kB | Adobe PDF | View/Open | |
file5(chapter 2).pdf | 186.45 kB | Adobe PDF | View/Open | |
file6(chapter 3).pdf | 190.53 kB | Adobe PDF | View/Open | |
file7(chapter 4).pdf | 511.98 kB | Adobe PDF | View/Open | |
file8(chapter 5).pdf | 545.49 kB | Adobe PDF | View/Open | |
file9(chapter 6).pdf | 582.91 kB | Adobe PDF | View/Open |
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