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مدلسازی و کنترل هیبرید مبدل تشدیدی سری
جعفری، محمد حسین Jafari, Mohammad Hossein
Cataloging brief
مدلسازی و کنترل هیبرید مبدل تشدیدی سری
پدیدآور اصلی :
جعفری، محمد حسین Jafari, Mohammad Hossein
ناشر :
صنعتی شریف
سال انتشار :
1394
موضوع ها :
مبدل های قدرت Power Converters مبدل تشدید Resonant Converter سیستم ترکیبی Hybrid System ...
شماره راهنما :
05-48270
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thesis.pdf
Chapter 1 Introduction
(15)
1.1 Porous Medium
(15)
1.2 Porosity
(17)
1.3 Permeability
(17)
1.4 Application of Porous Media
(18)
1.5 Objective
(19)
Chapter 2 Literature Review
(21)
Chapter 3 Mathematical Formulation
(27)
3.1 Momentum Transport Equation
(27)
3.1.1 Darcy Flow Model
(27)
3.1.2 Forchheimer-Darcy Flow Model
(28)
3.1.3 Brinkman-Darcy Flow Model
(29)
3.1.4 Darcy-Brinkman-Forchheimer Flow Model
(29)
3.1.5 Various Darcy-Brinkman-Forchheimer Parameters in Flow Models
(31)
3.2 Energy Equation
(32)
3.3 Nondimensionalization of Equations
(34)
3.3.1 Natural Convection
(34)
3.3.2 Forced Convection
(35)
3.4 Nusselt Number
(41)
Chapter 4 Numerical Solution
(44)
4.1 The Discretization of the General Convection-Diffusion Equation
(45)
4.2 Staggered Grid and the Discretized Porous media Governing Equations
(47)
4.3 SIMPLEC Algorithm
(61)
4.3.1 Velocity Corrections
(61)
4.3.2 Pressure Correction
(64)
4.4 Line-by-Line Method
(67)
Chapter 5 Results and Discussion
(68)
5.1 Validation Test Case 1: Heat Transfer in a 2-D Rectangular Channel
(68)
5.2 Validation Test Case 2: Fluid Flow in a 2-D Rectangular Channel
(70)
5.3 Validation Test Case 3: Fluid flow in a 2-D Rectangular Channel with porous media
(71)
5.4 Geometric Configuration and Boundary Conditions
(72)
5.5 Effect of Reynolds Number (Re) on Developing Velocity Profile
(73)
5.6 Effect of Darcy Number (Da) on Developing Velocity Profile
(74)
5.7 Effect of Non-Dimensional Porous substrate Thickness (S) on Developing Velocity Profile
(75)
5.8 Effect of Porosity (ε) on Developing Velocity Profile
(76)
5.9 Effect of Thermal Conductivity Ratio (TCR) on Heat Transfer
(77)
5.10 Effect of Non-Dimensional Porous Substrate Thickness (S) on Heat Transfer
(79)
5.11 Effect of Darcy Number (Da) on Heat Transfer
(80)
5.12 Effect of Porosity (ε) on Heat Transfer
(82)
5.13 Effect of Reynolds Number (Re) on Heat Transfer
(83)
5.14 Pressure Drop
(85)
5.15 Pressure Drop and Nusselt Number for the Porous Layer at Core of Channel
(87)
Chapter 6 Conclusion and Future Works
(91)
