1. No | 2. Title | 0. ID | 5. Type | 9. Subtopic | 10. Topic | 11. Reference | 8.Minor Subject | 12. Subject |

1301 | Comparison of performance of single CSTR and PFR for the nth order reaction | 30 | Figure | Flow Reactors, Steady State | Flow Reactors, Steady State |
Levenspiel |
Reactor Equations |
Kinetics |

1306 | Comparison of performance of a series of N equal-size CSTR reactors | 31 | Figure | Flow Reactors, Steady State | Flow Reactors, Steady State |
Levenspiel |
Reactor Equations |
Kinetics |

1307 | Comparison of performance of a series of N equal-size CSTR reactors | 32 | Figure | Flow Reactors, Steady State | Flow Reactors, Steady State |
Levenspiel |
Reactor Equations |
Kinetics |

1308 | Distribution of materials in a batch or plug flow reactor | 33 | Figure | Batch Reactor | Batch Reactor |
Levenspiel |
Integrated Reactor Equations for Irreversible Reaction |
Kinetics |

1309 | Comparison of performance of recycle and plug flow for first-order reaction | 34 | Figure | First-Order | Flow Reactors, Steady State |
Levenspiel |
Reactor Equations |
Kinetics |

1310 | Comparison of performance of recycle with plug flow for elementary reaction | 35 | Figure | Flow Reactors, Steady State | Flow Reactors, Steady State |
Levenspiel |
Reactor Equations |
Kinetics |

1311 | Performance of plug-flow and back-mix reactors [Fig 4-6] | 36 | Figure | Flow Reactors, Steady State | Flow Reactors, Steady State |
Levenspiel |
Reactor Equations |
Kinetics |

2201 | Compressibility Factors of Gases and Vapors | 38 | Figure | Nonideal Systems | Nonideal Systems |
Hougen and Watson |
Behavior of Single-Component Systems |
Mass/Energy Balances and Thermodynamics |

2202 | Generalized Plot of Z(0) values [Fig 3-45] | 39 | Figure | Nonideal Systems | Nonideal Systems |
Perry |
Behavior of Single-Component Systems |
Mass/Energy Balances and Thermodynamics |

2203 | Generalized Plot of Z(1) values [Fig 3-46] | 40 | Figure | Nonideal Systems | Nonideal Systems |
Perry |
Behavior of Single-Component Systems |
Mass/Energy Balances and Thermodynamics |

2213 | Generalized Reduced Viscosities | 51 | Figure | Thermodynamics | Thermodynamics |
Hougen and Watson |
Ideal and Real Gas Laws |
Mass/Energy Balances and Thermodynamics |

2204 | Enthalpy Correction for Gases and Vapors due to Lack of Ideal Behavior | 57 | Figure | Nonideal Systems | Nonideal Systems |
Hougen and Watson |
Thermodynamic Properties |
Mass/Energy Balances and Thermodynamics |

2205 | Correlation of H/RT_{c}^{(0)} [Fig 4-30] | 58 | Figure | Nonideal Systems | Nonideal Systems |
Perry |
Thermodynamic Properties |
Mass/Energy Balances and Thermodynamics |

2206 | Correlation of H/RTc(1) [Fig 4-31] | 59 | Figure | Nonideal Systems | Nonideal Systems |
Perry |
Thermodynamic Properties |
Mass/Energy Balances and Thermodynamics |

2216 | Generalized heat-capacity differences | 60 | Figure | Thermodynamics | Thermodynamics |
Chopey |
Thermodynamic Properties |
Mass/Energy Balances and Thermodynamics |

2218 | Entropy Correction for Gases and Vapors | 62 | Figure | Nonideal Systems | Nonideal Systems |
Hougen and Watson |
Thermodynamic Properties |
Mass/Energy Balances and Thermodynamics |

2207 | Entropy Correction for Gases and Vapors due to Lack of Ideal | 63 | Figure | Nonideal Systems | Nonideal Systems |
Hougen and Watson |
Non-Ideal Systems |
Mass/Energy Balances and Thermodynamics |

2208 | Molal Heat Capacity Correction for Gases | 64 | Figure | Thermodynamics | Thermodynamics |
Hougen and Watson |
Thermodynamics |
Mass/Energy Balances and Thermodynamics |

2217 | Enthalpy Correction for Gases and Vapors | 65 | Figure | Nonideal Systems | Nonideal Systems |
Hougen and Watson |
Thermodynamic Properties |
Mass/Energy Balances and Thermodynamics |

2209 | Generalized Heat-Capacity Differencess, Cp-Cv [Fig 1-5] | 66 | Figure | Thermodynamics | Thermodynamics |
Chopey |
Ideal and Real Gas Laws |
Mass/Energy Balances and Thermodynamics |

2214 | Appendix K - Mollier Chart | 74 | Figure | Thermodynamics | Thermodynamics |
Lindeburg |
Thermodynamics |
Mass/Energy Balances and Thermodynamics |

2219 | Enthalpy-log pressure diagram for Refrigerant 11 | 79 | Figure | Thermodynamics | Thermodynamics |
Perry |
Thermodynamics |
Mass/Energy Balances and Thermodynamics |

2210 | Fugacity Coefficents of Gases and Vapors | 89 | Figure | Nonideal Systems | Nonideal Systems |
Hougen and Watson |
Behavior of Multicomponent Systems |
Mass/Energy Balances and Thermodynamics |

2211 | Correlation of -ln(φ)^{0} vs T_{r} | 90 | Figure | Nonideal Systems | Nonideal Systems |
Perry |
Non-Ideal Systems |
Mass/Energy Balances and Thermodynamics |

2212 | Correlation of -ln(φ)^{1} vs T_{r} | 91 | Figure | Nonideal Systems | Nonideal Systems |
Perry |
Non-Ideal Systems |
Mass/Energy Balances and Thermodynamics |

2215 | Reaction Equilibrium Constants | 93 | Figure | Thermodynamics | Thermodynamics |
Hougen and Watson |
Thermodynamics |
Mass/Energy Balances and Thermodynamics |

3202 | Psychrometric chart - low temperatures [Fig 12-1] | 111 | Figure | Humidification and Dehumidification | Humidification and Dehumidification |
Lindeburg |
Humidification and Dehumidification |
Plant Design and Operation |

3203 | Psychrometric chart - medium temperatures [Fig 12-2] | 112 | Figure | Humidification and Dehumidification | Humidification and Dehumidification |
Lindeburg |
Humidification and Dehumidification |
Plant Design and Operation |

3204 | Psychrometric Chart (High Temperatures) [Fig 12-3] | 113 | Figure | Humidification and Dehumidification | Humidification and Dehumidification |
Lindeburg |
Humidification and Dehumidification |
Plant Design and Operation |

3205 | Enthalpy-Concentration Diagram for Aqueous Sulfuric Acid | 123 | Figure | Mass/Energy Balances | Mass/Energy Balances |
Perry |
Thermodynamics |
Mass/Energy Balances and Thermodynamics |

3201 | Graphic Relationship of SI Units with Names | 126 | Figure | Mass/Energy Balances | Mass/Energy Balances |
Perry |
Thermodynamics |
Mass/Energy Balances and Thermodynamics |

4202 | Flow Coefficient C for Nozzles. | 131 | Figure | Orifice, Nozzle, and Venturi Meters | Orifice, Nozzle, and Venturi Meters |
Crane |
Flow and Pressure Measurement Techniques |
Fluids |

4203 | Flow Coefficient C for Square-Edge Orifices. | 132 | Figure | Orifice, Nozzle, and Venturi Meters | Orifice, Nozzle, and Venturi Meters |
Crane |
Mass and Volumetric Meters |
Fluids |

4204 | Net Expansion Factor Y for Compressible Flow Through Nozzles | 133 | Figure | Orifice, Nozzle, and Venturi Meters | Orifice, Nozzle, and Venturi Meters |
Crane |
Flow and Pressure Measurement Techniques |
Fluids |

4201 | Kinematic Viscosity of fluids.[Fig A-2] | 135 | Figure | Transport Properties | Transport Properties |
Lindeburg |
Transport Properties |
Fluids |

4205 | Critical Pressure Ratio, r_{c} for Compressible Flow through N | 139 | Figure | Compressible Flow | Compressible Flow |
Crane |
Flow Behavior |
Fluids |

4209 | Roughness factors (expressed in feet) for Commercial Pipes. | 143 | Figure | Bernoulli Equation | Bernoulli Equation |
Crane |
Flow Behavior |
Fluids |

4210 | Friction factor Chart. | 144 | Figure | Friction | Friction |
McCabe and Smith |
Flow Behavior |
Fluids |

4211 | Friction factor Chart, √N_{Re}f vs. f.[Fig 5-11] | 145 | Figure | Friction | Friction |
McCabe and Smith |
Flow Behavior |
Fluids |

4206 | Enlargement and Contraction Losses | 157 | Figure | Turbulent Flow | Turbulent Flow |
Crane |
Flow Behavior |
Fluids |

4207 | Resistance due to Pipe Entrance and Exit | 158 | Figure | Turbulent Flow | Turbulent Flow |
Crane |
Flow Behavior |
Fluids |

4208 | Equivalent Length of Pipe Fittings and Valves. | 161 | Figure | Turbulent Flow | Turbulent Flow |
Chopey |
Flow Behavior |
Fluids |

4212 | Upper Limits of Specific Speeds of Centrifugal Pumps | 170 | Figure | Pumps | Pumps |
Chopey |
Pumps |
Fluids |

4213 | Upper Limits of Specific Speeds of Single-Suction Mixed-Flow | 171 | Figure | Pumps | Pumps |
Chopey |
Flow Applications |
Fluids |

4214 | Approximate Relative Impeller Shapes and Efficiency Variatio | 172 | Figure | Flow Applications | Flow Applications |
Chopey |
Flow Applications |
Fluids |

4215 | Typical Pump Suction and Discharge Piping Arrangements (Perr | 173 | Figure | Pumps | Pumps |
Chopey |
Flow Applications |
Fluids |

4216 | Typical Selection Chart for Centrifugal Pumps | 174 | Figure | Pumps | Pumps |
Chopey |
Flow Applications |
Fluids |

5201 | Plot of f_{2}(4 α θ /l^{2}) for Various Shapes | 185 | Figure | Heat-Exchange Equipment Design | Heat-Exchange Equipment Design |
Kern |
Heat-Transfer Applications |
Heat Transfer |

5205 | Gurney-Lurie Chart for Cylinders | 187 | Figure | Heat-Exchange Equipment Design | Heat-Exchange Equipment Design |
Kern |
Heat-Transfer Applications |
Heat Transfer |

5208 | Condensing Coefficients | 204 | Figure | Design Parameters for Non-Trayed Units | Design Parameters for Non-Trayed Units |
Kern |
Heat-Transfer With Phase Change |
Heat Transfer |

5210 | LMTD Correction Factors for Heat Exchangers. | 207 | Figure | Heat Transfer without Phase Change | Heat Transfer without Phase Change |
Perry |
Heat Exchange Equipment Design |
Heat Transfer |

5211 | Gurney-Lurie Chart for Spheres | 209 | Figure | Heat-Exchange Equipment Design | Heat-Exchange Equipment Design |
Kern |
Heat-Transfer Applications |
Heat Transfer |

5212 | Gurney-Lurie Chart for Semiinfinite Solid | 210 | Figure | Heat-Exchange Equipment Design | Heat-Exchange Equipment Design |
Kern |
Heat-Transfer Applications |
Heat Transfer |

10201 | Boiling-point rise of aqueous solutions | 226 | Figure | Heat Transfer in Evaporators | Heat Transfer in Evaporators |
Perry |
Boiling-point rise of aqueous solutions |
Heat Transfer |

10202 | Evaporator Types | 227 | Figure | Evaporator Types and Applications | Evaporator Types and Applications |
Perry |
Evaporators |
Heat Transfer |

6201 | K-values (K =y/x) in light-hydrocarbon systems, low-temperature range | 229 | Figure | Material and Energy Balances for Trayed and Packed Units | Material and Energy Balances for Trayed and Packed Units |
Perry |
Continuous Vapor-Liquid Contactors |
Mass Transfer |

6202 | K-values (K = y/x) in light-hydrocarbon systems, high-temperature range | 230 | Figure | Material and Energy Balances for Trayed and Packed Units | Material and Energy Balances for Trayed and Packed Units |
Perry |
Continuous Vapor-Liquid Contactors |
Mass Transfer |

6208 | Minimum Reflux at infinite theoretical plates | 237 | Figure | Material and Energy Balances for Trayed and Packed Units | Material and Energy Balances for Trayed and Packed Units |
Ludwig |
Continuous Vapor-Liquid Contactors |
Mass Transfer |

6207 | Approximate solution for N and L/D in Distillation | 239 | Figure | Material and Energy Balances for Trayed and Packed Units | Material and Energy Balances for Trayed and Packed Units |
Ludwig |
Continuous Vapor-Liquid Contactors |
Mass Transfer |

6203 | Comparison of rigorous calculations with Gilliland Correleation | 244 | Figure | Material and Energy Balances for Trayed and Packed Units | Material and Energy Balances for Trayed and Packed Units |
Perry |
Continuous Vapor-Liquid Contactors |
Mass Transfer |

6204 | Separation operations related to distillation | 245 | Figure | Material and Energy Balances for Trayed and Packed Units | Material and Energy Balances for Trayed and Packed Units |
Perry |
Continuous Vapor-Liquid Contactors |
Mass Transfer |

6205 | Empirical correlations of overall efficiencies for fractionation and absorption | 246 | Figure | Material and Energy Balances for Trayed and Packed Units | Material and Energy Balances for Trayed and Packed Units |
Ludwig |
Continuous Vapor-Liquid Contactors |
Mass Transfer |

6206 | Graphical Representation of Fenske-Underwood-Gilliland proce | 247 | Figure | Material and Energy Balances for Trayed and Packed Units | Material and Energy Balances for Trayed and Packed Units |
Chopey |
Continuous Vapor-Liquid Contactors |
Mass Transfer |

7205 | Packed Column performance nomograph | 256 | Figure | Material and Energy Balances for Trayed and Packed Units | Material and Energy Balances for Trayed and Packed Units |
Hougen and Watson |
Miscellaneous Mass Transfer Processes |
Mass Transfer |

7206 | Packing factors for use with Fig 9-11D (Fig 9-12D) | 257 | Figure | Design Parameters for Non-Trayed Units | Design Parameters for Non-Trayed Units |
PE |
Continuous Vapor-Liquid Contactors |
Mass Transfer |

7203 | Generalized flooding and pressure drop correlation for packings | 259 | Figure | Design Parameters for Trayed Units | Design Parameters for Trayed Units |
Perry |
Continuous Vapor-Liquid Contactors |
Mass Transfer |

7204 | Generalized pressure-drop correlation for packed towers [Fig | 260 | Figure | Material and Energy Balances for Trayed and Packed Units | Material and Energy Balances for Trayed and Packed Units |
Chopey |
Continuous Vapor-Liquid Contactors |
Mass Transfer |

7201 | Absorption and Stripping Factors | 263 | Figure | Material and Energy Balances for Trayed and Packed Units | Material and Energy Balances for Trayed and Packed Units |
Perry |
Continuous Vapor-Liquid Contactors |
Mass Transfer |

7202 | Number of overall gas-phase mass-transfer units in a packed absorption tower | 264 | Figure | Material and Energy Balances for Trayed and Packed Units | Material and Energy Balances for Trayed and Packed Units |
Perry |
Continuous Vapor-Liquid Contactors |
Mass Transfer |

5206 | Gurney-Lurie Chart for Slab | 1586 | Figure | Heat-Exchange Equipment Design | Heat-Exchange Equipment Design |
Kern |
Heat-Transfer Applications |
Heat Transfer |