Heat-transfer characteristics of flowing and stationary particle-bed-type fusion-reactor blankets Page: 8 of 282
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TABLE OF CONTENTS
LIST OF TABLES
LIST OF FIGURES
CHAPTER I INTRODUCTION
1.1 Reactor Design Studies
1.2 Research Program Objectives
CHAPTER 2 EXPERIMENTAL METHODS IN PACKED BED HEAT TRANSFER
2.1 Overall Heat Transfer Coefficient
2.2 Overall Effective Thermal Conductivity
2.2.1 Constant Superficial Gas Velocity,
2.2.2 Radially Varying ko
2.2.3 Velocity Distributions in Packed Beds
2.2.4 Effect of Velocity Distribution on ko
2.3 Effective Thermal Conductivity and Wall Heat
2.4 Axial Effective Conductivity
CHAPTER 3 TWO PARAMETER PACKED BED MODELS
3.1 Models of the Effective Thermal Conductivity
3.1.1 Models Based Upon the Particle-to-Gas
Heat Transfer Coefficient
3.1.2 Particle-to-Gas Heat Transfer
3.1.3 Simple Models of the Effective Thermal
3.1.4 Static Effective Thermal Conductivity
at Low Pressure
3.1.5 Models of k@ Based Upon
3.2 Models of the Wall Heat Transfer Coefficient
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Nietert, R.E. Heat-transfer characteristics of flowing and stationary particle-bed-type fusion-reactor blankets, report, February 1, 1983; [Livermore,] California. (https://digital.library.unt.edu/ark:/67531/metadc1113214/m1/8/: accessed May 20, 2019), University of North Texas Libraries, Digital Library, https://digital.library.unt.edu; crediting UNT Libraries Government Documents Department.