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1 | (46) |
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1 | (5) |
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2 | (2) |
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1.1.2 Timescales, Lengthscales, and Dimensionless Groups |
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4 | (2) |
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1.2 Thermodynamics of Phase Change |
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6 | (4) |
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1.2.1 Effect of the Carrier Gas Concentration |
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8 | (1) |
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1.2.2 Effect of Curvature and Surface Tension |
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9 | (1) |
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10 | (17) |
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1.3.1 Steady, Stokesian Flow for Spheres |
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11 | (2) |
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1.3.2 Steady Flow at Higher Reynolds Numbers |
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13 | (4) |
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1.3.3 Drag on Irregular Particles |
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17 | (1) |
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18 | (2) |
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1.3.5 Other Effects on the Steady Drag Coefficients |
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20 | (1) |
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20 | (4) |
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1.3.7 Transverse Forces and Lift Effects |
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24 | (3) |
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1.4 Heat and Mass Transfer |
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27 | (20) |
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1.4.1 Steady, Stokesian Heat Transfer for Spheres |
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27 | (2) |
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1.4.2 Inertia Effects, Higher Res |
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29 | (2) |
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31 | (1) |
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32 | (4) |
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36 | (1) |
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1.4.6 Heat Transfer from Irregularly Shaped Particles |
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37 | (1) |
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1.4.7 Rarefaction and Interface Temperature Discontinuity Effects |
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38 | (1) |
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39 | (1) |
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1.4.9 Temperature Measurements |
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40 | (2) |
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42 | (5) |
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2 Numerical Modeling and Simulations |
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47 | (42) |
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2.1 Multiphase and Particulate Modeling |
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47 | (3) |
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2.1.1 Desired Attributes of Models |
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49 | (1) |
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2.2 Classification of Particulate Flows |
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50 | (3) |
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50 | (1) |
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51 | (1) |
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51 | (1) |
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52 | (1) |
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2.3 Modeling of the Carrier Phase: Governing Equations |
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53 | (5) |
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54 | (1) |
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54 | (4) |
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58 | (1) |
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2.4 Modeling of Particulate Systems |
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58 | (19) |
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2.4.1 Eulerian Homogeneous Model |
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59 | (1) |
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2.4.2 Eulerian, Two-Fluid Model |
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60 | (2) |
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2.4.3 Lagrangian, Point-Source Model |
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62 | (2) |
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2.4.4 Lagrangian, Resolved-Particle Model |
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64 | (2) |
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2.4.5 The Probability Distribution Function Model |
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66 | (2) |
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2.4.6 Particle Collisions |
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68 | (6) |
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2.4.7 Droplet Collisions and Coalescence |
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74 | (2) |
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2.4.8 Heat Transfer During Collisions |
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76 | (1) |
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2.5 The Treatment of Particle Boundaries |
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77 | (12) |
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2.5.1 Body-Fitted Coordinates |
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77 | (2) |
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2.5.2 The Front-Tracking Method |
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79 | (1) |
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2.5.3 The Lattice Boltzmann Method |
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80 | (2) |
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2.5.4 The Immersed Boundary Method |
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82 | (3) |
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2.5.5 Application of the IBM to Heat Transfer |
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85 | (1) |
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86 | (3) |
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89 | (32) |
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3.1 Types of FBRs and Air Distributors |
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92 | (1) |
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3.2 Basics of the Operation of FBRs |
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93 | (5) |
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3.2.1 Fluidization Regimes |
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94 | (2) |
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3.2.2 Minimum Fluidization Velocity |
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96 | (2) |
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3.3 Heat Transfer in FBRs |
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98 | (5) |
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3.4 Industrial Types of FBRs: Applications |
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103 | (12) |
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104 | (2) |
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3.4.2 Catalytic Synthesis |
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106 | (2) |
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3.4.3 Thermal Cracking and Coking |
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108 | (1) |
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3.4.4 Fluidized Bed Combustors |
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109 | (2) |
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3.4.5 Other Chemical Applications |
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111 | (2) |
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3.4.6 Nonchemical Applications |
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113 | (2) |
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3.5 Computer Modeling: The MFIX Code |
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115 | (6) |
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3.5.1 The MFIX Numerical Code |
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117 | (2) |
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119 | (2) |
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4 Heat Transfer with Nanofluids |
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121 | (44) |
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121 | (1) |
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4.2 Continuum and Molecular Considerations |
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122 | (2) |
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4.3 Characteristics of Nanofluids |
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124 | (10) |
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4.3.1 Surface-to-Volume Ratio |
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125 | (1) |
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125 | (3) |
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128 | (2) |
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4.3.4 Electrical Double Layer, Zeta Potential, and Electrophoresis |
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130 | (2) |
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4.3.5 Aggregation and Separation of Particles |
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132 | (2) |
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4.4 Thermodynamic Properties |
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134 | (3) |
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137 | (19) |
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4.5.1 Viscosity of Nanofluids |
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138 | (6) |
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4.5.2 Thermal Conductivity |
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144 | (7) |
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4.5.3 Heat Transfer Coefficients |
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151 | (5) |
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156 | (9) |
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158 | (7) |
Index |
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165 | |