| Preface |
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iii | |
| Part I. Feedstock Terminology, Availability, and Evaluation |
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Definitions, and Terminology |
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1 | (24) |
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1 | (2) |
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3 | (8) |
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3 | (3) |
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6 | (1) |
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7 | (1) |
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Bituminous Rock and Bituminous Sand |
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8 | (1) |
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9 | (1) |
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10 | (1) |
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10 | (1) |
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11 | (2) |
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13 | (12) |
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13 | (7) |
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20 | (2) |
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22 | (1) |
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22 | (1) |
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22 | (1) |
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23 | (1) |
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23 | (1) |
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24 | (1) |
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Occurrence and Availability |
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25 | (16) |
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25 | (4) |
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29 | (12) |
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31 | (2) |
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33 | (3) |
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36 | (1) |
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Bitumen (Extra Heavy Oil) |
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37 | (2) |
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39 | (2) |
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41 | (32) |
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41 | (1) |
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Ultimate (Elemental) Composition |
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42 | (2) |
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44 | (6) |
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Bulk (Fractional) Composition |
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50 | (15) |
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53 | (5) |
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58 | (5) |
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63 | (2) |
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65 | (8) |
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69 | (4) |
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73 | (29) |
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73 | (2) |
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75 | (7) |
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Elemental (Ultimate) Analysis |
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75 | (1) |
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Density and Specific Gravity |
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76 | (2) |
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78 | (4) |
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82 | (16) |
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83 | (8) |
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Liquefaction and Solidification |
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91 | (1) |
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92 | (2) |
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94 | (1) |
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95 | (1) |
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Pressure-Volume-Temperature Relationships |
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95 | (1) |
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96 | (2) |
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98 | (4) |
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100 | (2) |
| Part II. Engineering Aspects of Refining |
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102 | (12) |
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102 | (1) |
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Stoichiometry of Chemical Reactions |
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102 | (2) |
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Stoichiometrically Independent Reactions |
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104 | (1) |
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Material Balance for a Single Reaction |
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104 | (1) |
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105 | (1) |
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Concentration Changes with a Single Reaction |
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106 | (2) |
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108 | (1) |
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Concentration Changes with Several Reactions |
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109 | (1) |
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110 | (2) |
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Concentration Changes in Continuous Mixtures |
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112 | (2) |
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113 | (1) |
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114 | (18) |
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114 | (1) |
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115 | (1) |
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Thermodynamics and Reaction Kinetics |
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116 | (4) |
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Reaction Rates and Chemical Equilibrium |
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120 | (2) |
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Steady-State Approximation and Catalysis |
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122 | (3) |
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Concentration Change Measurements and Reaction Rates |
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125 | (2) |
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127 | (1) |
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Propagation, Branching, and Autocatalysis |
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128 | (1) |
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Arrhenius Relation and Its Importance |
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129 | (3) |
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131 | (1) |
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Thermochemistry and Chemical Equilibrium |
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132 | (14) |
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132 | (1) |
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Heat of Formation and Heat of Reaction |
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133 | (3) |
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First Law of Thermodynamics |
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136 | (2) |
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Second Law of Thermodynamics: Chemical Equilibrium |
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138 | (8) |
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144 | (2) |
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Kinetic Measurements and Data Analysis |
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146 | (16) |
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146 | (1) |
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Kinetic Models and Calculation of Rate Constants |
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147 | (5) |
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Kinetic Rate Constants in Gas-Solid Reactions |
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152 | (2) |
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Material Balances for Different Types of Reactors |
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154 | (4) |
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154 | (1) |
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Continuous Flow Stirred Tank Reactor |
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155 | (1) |
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Plug Flow Tubular Reactor |
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156 | (1) |
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Axially Dispersed Tubular Reactor |
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157 | (1) |
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158 | (1) |
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159 | (3) |
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161 | (1) |
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162 | (31) |
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162 | (1) |
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Continuous Flow Stirred Tank Reactors |
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163 | (17) |
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Mass Balance for Continuous Flow Stirred Tank Reactors |
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164 | (1) |
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Reactor Volume and Reactor Optimization |
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165 | (4) |
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Independence of Material Balances |
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169 | (1) |
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Energy Balance for Continuous Flow Stirred Tank Reactors |
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169 | (2) |
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Reactor Design and Reactor Stability for Continuous Flow Stirred Tank Reactors |
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171 | (5) |
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Stability Analysis for Continuous Flow Stirred Tank Reactors |
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176 | (4) |
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180 | (4) |
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Mass Balance for Batch Reactors |
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180 | (1) |
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Energy Balance for Batch Reactors |
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181 | (3) |
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Plug Flow Tubular Reactors |
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184 | (4) |
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Mass Balance for Plug Flow Tubular Reactors |
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184 | (3) |
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Energy Balance for Plug Flow Tubular Reactors |
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187 | (1) |
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Axially Dispersed Tubular Reactors |
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188 | (5) |
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Mass Balance for Axially Dispersed Tubular Reactors |
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188 | (3) |
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Energy Balance for Axially Dispersed Tubular Reactors |
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191 | (1) |
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192 | (1) |
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Mixing in Flow Systems and Reactors |
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193 | (17) |
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193 | (1) |
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Residence Time Distribution |
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193 | (3) |
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196 | (3) |
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Continuous Flow Stirred Tank Reactors with Perfect Mixing |
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196 | (2) |
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Piston Flow Tubular Reactors |
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198 | (1) |
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Mean, Moments, and Distribution Functions |
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199 | (2) |
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Residence Time Distribution Measurement Techniques |
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201 | (1) |
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Residence Time Distribution Models |
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202 | (3) |
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Dispersion Models for Tubular Reactors |
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205 | (2) |
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Dispersion Models for Axial Distribution Tubular Reactors |
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207 | (3) |
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209 | (1) |
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210 | (72) |
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210 | (1) |
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Formulation of Property Balance Equations |
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211 | (2) |
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Momentum Transfer (Fluid Dynamics) |
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213 | (36) |
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General Properties of the Navier-Stokes Equation and Its Solutions |
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214 | (4) |
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Exact Solutions (Laminar Viscous Flow) |
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218 | (4) |
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222 | (12) |
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234 | (15) |
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249 | (18) |
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Energy Balance (Equation of Energy) |
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249 | (2) |
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Integration of the Thermal Energy Equation |
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251 | (1) |
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Steady-State Heat Conduction |
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251 | (6) |
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Unsteady-State Heat Conduction |
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257 | (3) |
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Convective Heat Transfer in Laminar Flow |
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260 | (7) |
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267 | (12) |
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Equation of Changes in Multicomponent Systems |
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269 | (4) |
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Similarity in Mass, Momentum, and Energy Transfer |
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273 | (1) |
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Forced Convective Mass Transfer in Laminar Viscous Flow |
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274 | (3) |
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Forced Convective Mass Transfer in Turbulent Flow |
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277 | (2) |
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Computational Fluid Dynamics |
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279 | (3) |
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280 | (2) |
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Heterogeneous Gas-Solid Reactions and Heterogeneous Catalysis |
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282 | (28) |
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282 | (1) |
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Reaction Regimes in Heterogeneous Gas-Solid Reactions |
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283 | (5) |
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Combustion and Gasification |
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288 | (3) |
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291 | (1) |
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Interaction of Reactants with Heterogeneous Catalysts |
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292 | (2) |
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Mechanism of Heterogeneous Catalysis |
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294 | (5) |
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295 | (1) |
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Selectivity and Catalytic Activity |
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295 | (2) |
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Thermodynamics of Adsorption |
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297 | (1) |
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Reaction Pathways in Heterogenous Catalysis |
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298 | (1) |
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299 | (5) |
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Chemisorption and Reaction Rate in Heterogeneous Catalysts |
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304 | (6) |
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Langmuir-Hinshelwood Model |
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304 | (4) |
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Apparent Activation Energies |
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308 | (1) |
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309 | (1) |
| Part III. Refining |
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Pretreatment and Distillation |
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310 | (34) |
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310 | (2) |
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312 | (7) |
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319 | (17) |
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324 | (7) |
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331 | (5) |
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336 | (8) |
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336 | (1) |
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337 | (1) |
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Stabilization and Light End Removal |
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337 | (3) |
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340 | (1) |
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Azeotropic Distillation and Extractive Distillation |
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340 | (2) |
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342 | (2) |
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344 | (44) |
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344 | (6) |
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350 | (1) |
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351 | (17) |
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368 | (17) |
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369 | (5) |
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Fluid Coking and Flexicoking |
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374 | (11) |
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385 | (3) |
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386 | (2) |
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388 | (51) |
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388 | (6) |
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394 | (2) |
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396 | (4) |
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400 | (6) |
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406 | (12) |
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406 | (5) |
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411 | (1) |
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412 | (1) |
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413 | (1) |
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414 | (1) |
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414 | (1) |
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415 | (1) |
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415 | (1) |
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416 | (1) |
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417 | (1) |
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417 | (1) |
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418 | (21) |
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418 | (2) |
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420 | (1) |
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421 | (1) |
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422 | (1) |
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423 | (1) |
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424 | (13) |
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437 | (2) |
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439 | (46) |
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439 | (10) |
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449 | (7) |
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451 | (1) |
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Downflow Fixed-Bed Reactor |
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451 | (2) |
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Upflow Expanded-Bed Reactor |
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453 | (1) |
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Demetallization Reactor (Guard Bed Reactor) |
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454 | (1) |
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455 | (1) |
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Distillate Hydrodesulfurization |
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456 | (10) |
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456 | (5) |
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461 | (5) |
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Residuum Hydrodesulfurization |
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466 | (19) |
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466 | (7) |
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473 | (11) |
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484 | (1) |
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485 | (53) |
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485 | (11) |
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Processes and Process Design |
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496 | (30) |
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499 | (2) |
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501 | (1) |
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H-G Hydrocracking Process |
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502 | (1) |
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503 | (1) |
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IFP Hydrocracking Process |
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504 | (2) |
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506 | (2) |
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508 | (3) |
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511 | (1) |
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511 | (2) |
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Mild Hydrocracking Process |
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513 | (3) |
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516 | (1) |
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517 | (2) |
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519 | (1) |
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Residue Hydroconversion Process |
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520 | (1) |
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520 | (3) |
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Veba Combi-Cracking Process |
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523 | (3) |
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526 | (12) |
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536 | (2) |
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The Next Generation Process |
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538 | (52) |
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538 | (4) |
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Thermal (Carbon Rejection) Processes |
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542 | (11) |
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Asphalt Coking Technology Process |
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542 | (2) |
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Cherry-P (Comprehensive Heavy Ends Reforming Refinery) Process |
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544 | (1) |
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Deep Thermal Conversion Process |
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544 | (1) |
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545 | (2) |
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547 | (2) |
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Fluid Thermal Cracking Process |
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549 | (1) |
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High Conversion Soaker Cracking Process |
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550 | (2) |
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552 | (1) |
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Catalytic Cracking (Carbon Rejection) Processes |
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553 | (13) |
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Asphalt Residua Treating Process |
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554 | (2) |
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Heavy Oil Treating Process |
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556 | (2) |
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558 | (1) |
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Reduced Crude Oil Conversion Process |
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558 | (1) |
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Residual Fluid Catalytic Cracking Process |
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558 | (6) |
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564 | (1) |
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S&W Fluid Catalytic Cracking Process |
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565 | (1) |
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Hydrogen Addition Processes |
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566 | (6) |
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Asphaltenic Bottoms Cracking Process |
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566 | (4) |
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Hydrovisbreaking (HYCAR) Process |
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570 | (1) |
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571 | (1) |
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572 | (18) |
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572 | (7) |
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Deep Solvent Deasphalting Process |
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579 | (2) |
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581 | (3) |
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584 | (1) |
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Residuum Oil Supercritical Extraction Process |
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585 | (2) |
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587 | (1) |
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587 | (3) |
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590 | (49) |
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590 | (3) |
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Desulfurization and Heteroatom Removal |
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593 | (5) |
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595 | (1) |
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596 | (2) |
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598 | (25) |
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598 | (4) |
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602 | (19) |
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621 | (1) |
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622 | (1) |
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623 | (5) |
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624 | (1) |
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624 | (4) |
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628 | (1) |
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628 | (6) |
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629 | (1) |
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629 | (4) |
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633 | (1) |
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634 | (5) |
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634 | (1) |
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635 | (1) |
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636 | (1) |
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637 | (2) |
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639 | (24) |
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639 | (6) |
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645 | (5) |
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645 | (2) |
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647 | (3) |
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650 | (7) |
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Heavy Residue Gasification and Combined Cycle Power Generation |
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650 | (1) |
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Hybrid Gasification Process |
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650 | (1) |
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651 | (1) |
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651 | (1) |
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Shell Gasification (Partial Oxidation) Process |
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651 | (1) |
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652 | (1) |
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653 | (1) |
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653 | (2) |
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Texaco Gasification (Partial Oxidation) Process |
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655 | (2) |
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657 | (2) |
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657 | (1) |
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Shift Conversion Catalysts |
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658 | (1) |
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659 | (1) |
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659 | (4) |
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660 | (1) |
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Pressure Swing Adsorption Units |
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660 | (1) |
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661 | (1) |
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662 | (1) |
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662 | (1) |
| Glossary |
|
663 | (30) |
| Conversion Factors and SI Units |
|
693 | (2) |
| Index |
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695 | |