Preface |
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xiii | |
Symbols and Acronyms |
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xvii | |
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1 | (11) |
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1.1 Importance of Thermodynamics |
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1 | (4) |
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1.2 Laws of Thermodynamics |
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5 | (2) |
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1.3 Importance of Combustion |
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7 | (5) |
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2 Thermodynamics of a Pure Substance |
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12 | (36) |
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12 | (1) |
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2.2 Important Definitions |
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12 | (6) |
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2.2.1 System, Surroundings and Boundary |
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12 | (1) |
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2.2.2 Work and Heat Interactions |
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13 | (1) |
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2.2.3 Closed (Constant-Mass) System |
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13 | (1) |
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2.2.4 Open (Constant-Volume) System |
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14 | (1) |
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14 | (1) |
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2.2.6 Thermodynamic Equilibrium |
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15 | (1) |
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2.2.7 Properties of a System |
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16 | (1) |
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17 | (1) |
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2.3 Behavior of a Pure Substance |
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18 | (3) |
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18 | (1) |
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18 | (3) |
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2.4 Law of Corresponding States |
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21 | (2) |
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23 | (4) |
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2.5.1 Real and Quasistatic Processes |
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24 | (1) |
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2.5.2 Reversible and Irreversible Processes |
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25 | (2) |
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27 | (1) |
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2.6 First Law of Thermodynamics |
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27 | (8) |
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2.6.1 First Law for a Finite Process - Closed System |
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28 | (2) |
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30 | (1) |
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2.6.3 Specific Heats and Enthalpy |
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31 | (1) |
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2.6.4 Ideal Gas Relations |
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32 | (1) |
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2.6.5 First Law for an Open System |
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32 | (3) |
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2.7 Second Law of Thermodynamics |
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35 | (13) |
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2.7.1 Consequence for a Finite Process - Closed System |
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36 | (2) |
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2.7.2 Isolated System and Universe |
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38 | (2) |
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2.7.3 First Law in Terms of Entropy and Gibbs Function |
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40 | (1) |
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2.7.4 Thermal Equilibrium |
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40 | (2) |
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2.7.5 Equilibrium of a General Closed System |
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42 | (1) |
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2.7.6 Phase-Change Processes |
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43 | (1) |
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2.7.7 Second Law for an Open System |
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44 | (4) |
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3 Thermodynamics of Gaseous Mixtures |
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48 | (22) |
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48 | (1) |
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49 | (2) |
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49 | (1) |
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3.2.2 Mole Fraction and Partial Pressure |
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50 | (1) |
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3.2.3 Molar Concentration |
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51 | (1) |
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3.2.4 Specifying Composition |
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51 | (1) |
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3.3 Energy and Entropy Properties of Mixtures |
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51 | (3) |
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3.4 Properties of Reacting Mixtures |
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54 | (10) |
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3.4.1 Stoichiometric Reaction |
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54 | (2) |
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56 | (1) |
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3.4.3 Equivalence Ratio Φ |
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57 | (1) |
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3.4.4 Effect of Φ on Product Composition |
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57 | (3) |
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3.4.5 Heat of Combustion or Heat of Reaction |
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60 | (2) |
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3.4.6 Enthalpy of Formation |
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62 | (1) |
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3.4.7 Entropy of Formation |
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63 | (1) |
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3.4.8 Adiabatic Flame Temperature |
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63 | (1) |
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3.4.9 Constant-Volume Heat of Reaction |
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64 | (1) |
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3.5 Use of Property Tables |
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64 | (6) |
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70 | (20) |
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4.1 Progress of a Chemical Reaction |
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70 | (1) |
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4.2 Dissociation Reaction |
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71 | (1) |
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4.3 Conditions for Chemical Equilibrium |
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72 | (2) |
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4.3.1 Condition for a Finite Change |
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72 | (1) |
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4.3.2 Consequences for an Infinitesimal Change |
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72 | (2) |
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4.4 Equilibrium Constant Kp |
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74 | (4) |
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74 | (1) |
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75 | (3) |
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4.5 Problems in Chemical Equilibrium |
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78 | (12) |
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78 | (2) |
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80 | (2) |
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4.5.3 Multistep Reactions |
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82 | (4) |
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4.5.4 Constant-Volume Combustion |
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86 | (4) |
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90 | (22) |
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5.1 Importance of Chemical Kinetics |
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90 | (1) |
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5.2 Reformed View of a Reaction |
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91 | (1) |
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5.3 Reaction Rate Formula |
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92 | (9) |
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5.3.1 Types of Elementary Reactions |
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92 | (2) |
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5.3.2 Rate Formula for A + B → C + D |
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94 | (4) |
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5.3.3 Tri- and Unimolecular Reactions |
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98 | (1) |
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5.3.4 Relation between Rate Coefficient and Kp |
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98 | (3) |
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5.4 Construction of Global Reaction Rate |
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101 | (8) |
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5.4.1 Useful Approximations |
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101 | (3) |
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5.4.2 Zeldovich Mechanism of NO Formation |
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104 | (4) |
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5.4.3 Quasi-Global Mechanism |
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108 | (1) |
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5.5 Global Rates for Hydrocarbon Fuels |
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109 | (3) |
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6 Derivation of Transport Equations |
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112 | (22) |
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112 | (1) |
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6.2 Navier-Stokes Equations |
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113 | (2) |
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6.2.1 Mass Conservation Equation |
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113 | (1) |
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6.2.2 Momentum Equations ui (i = 1, 2, 3) |
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113 | (2) |
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6.3 Equations of Mass Transfer |
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115 | (2) |
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6.3.1 Species Conservation |
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115 | (1) |
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6.3.2 Element Conservation |
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116 | (1) |
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117 | (4) |
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117 | (1) |
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6.4.2 Convection and Conduction |
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117 | (1) |
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6.4.3 Volumetric Generation |
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118 | (2) |
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6.4.4 Final Form of Energy Equation |
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120 | (1) |
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6.4.5 Enthalpy and Temperature Forms |
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120 | (1) |
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6.5 Two-Dimensional Boundary Layer Flow Model |
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121 | (4) |
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6.5.1 Governing Equations |
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122 | (1) |
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6.5.2 Boundary and Initial Conditions |
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123 | (2) |
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6.6 One-Dimensional Stefan Flow Model |
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125 | (1) |
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126 | (2) |
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128 | (6) |
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128 | (1) |
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128 | (6) |
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7 Thermochemical Reactors |
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134 | (30) |
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134 | (1) |
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135 | (11) |
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7.2.1 Governing Equations |
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135 | (9) |
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144 | (2) |
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146 | (9) |
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7.3.1 Governing Equations |
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146 | (2) |
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148 | (4) |
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152 | (3) |
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7.4 Constant-Mass Reactor |
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155 | (9) |
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7.4.1 Constant-Volume CMTCR |
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156 | (3) |
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7.4.2 Variable-Volume CMTCR |
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159 | (5) |
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164 | (34) |
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164 | (1) |
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8.2 Laminar Premixed Flames |
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165 | (11) |
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8.2.1 Laminar Flame Speed |
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165 | (1) |
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8.2.2 Approximate Prediction of Sl and δ |
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166 | (3) |
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8.2.3 Refined Prediction of Sl and δ |
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169 | (4) |
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8.2.4 Correlations for Sl and δ |
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173 | (3) |
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8.3 Turbulent Premixed Flames |
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176 | (2) |
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178 | (4) |
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8.5 Externally Aided Ignition |
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182 | (6) |
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8.5.1 Spherical Propagation |
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182 | (2) |
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184 | (4) |
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8.6 Self- or Auto-Ignition |
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188 | (4) |
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8.6.1 Ignition Delay and Fuel Rating |
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188 | (1) |
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8.6.2 Estimation of Ignition Delay |
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189 | (3) |
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192 | (2) |
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194 | (4) |
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198 | (25) |
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198 | (2) |
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9.2 Laminar Diffusion Flames |
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200 | (10) |
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9.2.1 Velocity Prediction |
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200 | (3) |
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9.2.2 Flame Length and Shape Prediction |
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203 | (4) |
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207 | (1) |
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208 | (2) |
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9.3 Turbulent Diffusion Flames |
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210 | (8) |
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9.3.1 Velocity Prediction |
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210 | (2) |
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9.3.2 Flame Length and Shape Prediction |
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212 | (4) |
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9.3.3 Correlations for Lf |
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216 | (1) |
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9.3.4 Correlations for Liftoff and Blowout |
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217 | (1) |
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218 | (2) |
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220 | (3) |
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10 Combustion of Particles and Droplets |
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223 | (38) |
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223 | (3) |
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226 | (2) |
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228 | (11) |
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10.3.1 Inert Mass Transfer without Heat Transfer |
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228 | (6) |
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10.3.2 Inert Mass Transfer with Heat Transfer |
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234 | (5) |
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239 | (7) |
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240 | (1) |
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10.4.2 Interpretation of B |
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240 | (2) |
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10.4.3 Flame Front Radius and Temperature |
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242 | (4) |
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10.5 Solid Particle Combustion |
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246 | (15) |
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10.5.1 Stages of Combustion |
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246 | (3) |
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249 | (12) |
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11 Combustion Applications |
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261 | (34) |
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261 | (1) |
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11.2 Wood-Burning Cookstove |
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261 | (17) |
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11.2.1 CTARA Experimental Stove |
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262 | (1) |
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11.2.2 Modeling Considerations |
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263 | (3) |
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266 | (4) |
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270 | (1) |
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271 | (1) |
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11.2.6 Reference Stove Specifications |
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272 | (2) |
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11.2.7 Effect of Parametric Variations |
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274 | (3) |
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11.2.8 Overall Conclusions |
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277 | (1) |
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11.3 Vertical Shaft Brick Kiln |
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278 | (11) |
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11.3.1 VSBK Construction and Operation |
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280 | (1) |
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11.3.2 Modeling Assumptions |
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281 | (2) |
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283 | (1) |
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284 | (2) |
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11.3.5 Inlet and Exit Conditions |
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286 | (1) |
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11.3.6 Results for the Reference Case |
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286 | (2) |
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11.3.7 Parametric Studies |
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288 | (1) |
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11.3.8 Overall Conclusions |
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289 | (1) |
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11.4 Gas Turbine Combustion Chamber |
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289 | (6) |
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289 | (1) |
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290 | (3) |
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293 | (2) |
Appendix A Thermochemistry Data |
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295 | (17) |
Appendix B Curve-Fit Coefficients for Δhc, Tad, Kp, Cp, h, and s |
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312 | (7) |
Appendix C Properties of Fuels |
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319 | (6) |
Appendix D Thermophysical and Transport Properties of Gases |
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325 | (9) |
Appendix E Atmospheric Data |
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334 | (1) |
Appendix F Binary Diffusion Coefficients at 1 atm and T = 300 K |
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335 | (2) |
Bibliography |
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337 | (6) |
Index |
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