File Type: Figure
1. No2. Title0. ID5. Type9. Subtopic10. Topic11. Reference8.Minor Subject12. Subject
1301Comparison of performance of single CSTR and PFR for the nth order reaction30FigureFlow Reactors, Steady StateFlow Reactors, Steady State RH_p178 Reactor Equations Kinetics
1306Comparison of performance of a series of N equal-size CSTR reactors31FigureFlow Reactors, Steady StateFlow Reactors, Steady State RH_p178 Reactor Equations Kinetics
1307Comparison of performance of a series of N equal-size CSTR reactors32FigureFlow Reactors, Steady StateFlow Reactors, Steady State RH_p178 Reactor Equations Kinetics
1308Distribution of materials in a batch or plug flow reactor33FigureBatch ReactorBatch Reactor RH_p178 Integrated Reactor Equations for Irreversible Reaction Kinetics
1309Comparison of performance of recycle and plug flow for first-order reaction34FigureFirst-OrderFlow Reactors, Steady State RH_p178 Reactor Equations Kinetics
1310Comparison of performance of recycle with plug flow for elementary reaction35FigureFlow Reactors, Steady StateFlow Reactors, Steady State RH_p178 Reactor Equations Kinetics
1311Performance of plug-flow and back-mix reactors [Fig 4-6]36FigureFlow Reactors, Steady StateFlow Reactors, Steady State RH_p178 Reactor Equations Kinetics
2201Compressibility Factors of Gases and Vapors38FigureNonideal SystemsNonideal Systems RH_p97 Behavior of Single-Component Systems Mass/Energy Balances and Thermodynamics
2202Generalized Plot of Z(0) values [Fig 3-45]39FigureNonideal SystemsNonideal Systems RH_p97 Behavior of Single-Component Systems Mass/Energy Balances and Thermodynamics
2203Generalized Plot of Z(1) values [Fig 3-46]40FigureNonideal SystemsNonideal Systems RH_p97 Behavior of Single-Component Systems Mass/Energy Balances and Thermodynamics
2213Generalized Reduced Viscosities51FigureThermodynamicsThermodynamics Hougen and Watson Ideal and Real Gas Laws Mass/Energy Balances and Thermodynamics
2204Enthalpy Correction for Gases and Vapors due to Lack of Ideal Behavior57FigureNonideal SystemsNonideal Systems RH_p97 Thermodynamic Properties Mass/Energy Balances and Thermodynamics
2205Correlation of H/RTc(0) [Fig 4-30]58FigureNonideal SystemsNonideal Systems RH_p97 Thermodynamic Properties Mass/Energy Balances and Thermodynamics
2206Correlation of H/RTc(1) [Fig 4-31]59FigureNonideal SystemsNonideal Systems RH_p97 Thermodynamic Properties Mass/Energy Balances and Thermodynamics
2216Generalized heat-capacity differences60FigureThermodynamicsThermodynamics Chopey Thermodynamic Properties Mass/Energy Balances and Thermodynamics
2218Entropy Correction for Gases and Vapors62FigureNonideal SystemsNonideal Systems RH_p97 Thermodynamic Properties Mass/Energy Balances and Thermodynamics
2207Entropy Correction for Gases and Vapors due to Lack of Ideal63FigureNonideal SystemsNonideal Systems RH_p97 Non-Ideal Systems Mass/Energy Balances and Thermodynamics
2208Molal Heat Capacity Correction for Gases64FigureThermodynamicsThermodynamics Hougen and Watson Thermodynamics Mass/Energy Balances and Thermodynamics
2217Enthalpy Correction for Gases and Vapors65FigureNonideal SystemsNonideal Systems RH_p97 Thermodynamic Properties Mass/Energy Balances and Thermodynamics
2209Generalized Heat-Capacity Differencess, Cp-Cv [Fig 1-5]66FigureThermodynamicsThermodynamics Chopey Ideal and Real Gas Laws Mass/Energy Balances and Thermodynamics
2214Appendix K - Mollier Chart74FigureThermodynamicsThermodynamics Lindeburg Thermodynamics Mass/Energy Balances and Thermodynamics
2219Enthalpy-log pressure diagram for Refrigerant 1179FigureThermodynamicsThermodynamics Perry Thermodynamics Mass/Energy Balances and Thermodynamics
2210Fugacity Coefficents of Gases and Vapors89FigureNonideal SystemsNonideal Mixtures RH_p97 Behavior of Multicomponent Systems Mass/Energy Balances and Thermodynamics
2211Correlation of -ln(φ)0 vs Tr90FigureNonideal SystemsNonideal Systems RH_p97 Non-Ideal Systems Mass/Energy Balances and Thermodynamics
2212Correlation of -ln(φ)1 vs Tr91FigureNonideal SystemsNonideal Systems RH_p97 Non-Ideal Systems Mass/Energy Balances and Thermodynamics
2215Reaction Equilibrium Constants93FigureThermodynamicsThermodynamics Hougen and Watson Thermodynamics Mass/Energy Balances and Thermodynamics
3202Psychrometric chart - low temperatures [Fig 12-1]111FigureHumidification and DehumidificationHumidification and Dehumidification RH_p338 Miscellaneous Mass Transfer Processes (Continuous, Batch, and Semicontinuous) Mass Transfer
3203Psychrometric chart - medium temperatures [Fig 12-2]112FigureHumidification and DehumidificationHumidification and Dehumidification RH_p338 Miscellaneous Mass Transfer Processes (Continuous, Batch, and Semicontinuous) Mass Transfer
3204Psychrometric Chart (High Temperatures) [Fig 12-3]113FigureHumidification and DehumidificationHumidification and Dehumidification RH_p338 Miscellaneous Mass Transfer Processes (Continuous, Batch, and Semicontinuous) Mass Transfer
3205Enthalpy-Concentration Diagram for Aqueous Sulfuric Acid123FigureMass/Energy BalancesMass/Energy Balances Perry Thermodynamics Mass/Energy Balances and Thermodynamics
3201Graphic Relationship of SI Units with Names126FigureMass/Energy BalancesMass/Energy Balances Perry Thermodynamics Mass/Energy Balances and Thermodynamics
4202Flow Coefficient C for Nozzles.131FigureOrifice, Nozzle, and Venturi MetersOrifice, Nozzle, and Venturi Meters RH_p256 Flow and Pressure Measurement Techniques Fluids
4203Flow Coefficient C for Square-Edge Orifices.132FigureOrifice, Nozzle, and Venturi MetersOrifice, Nozzle, and Venturi Meters RH_p256 Mass and Volumetric Meters Fluids
4204Net Expansion Factor Y for Compressible Flow Through Nozzles133FigureOrifice, Nozzle, and Venturi MetersOrifice, Nozzle, and Venturi Meters RH_p256 Flow and Pressure Measurement Techniques Fluids
4201Kinematic Viscosity of fluids.[Fig A-2]135FigureTransport PropertiesTransport Properties Lindeburg Transport Properties Fluids
4205Critical Pressure Ratio, rc for Compressible Flow through N139FigureCompressible FlowCompressible Flow RH_p216 Flow Behavior Fluids
4209Roughness factors (expressed in feet) for Commercial Pipes.143FigureBernoulli EquationBernoulli Equation Crane Flow Behavior Fluids
4210Friction factor Chart. 144FigureFrictionFriction RH_p199 Flow Behavior Fluids
4211Friction factor Chart, √NRef vs. f.[Fig 5-11]145FigureFrictionFriction RH_p199 Flow Behavior Fluids
4206Enlargement and Contraction Losses157FigureTurbulent FlowTurbulent Flow RH_p201 Flow Behavior Fluids
4207Resistance due to Pipe Entrance and Exit158FigureTurbulent FlowTurbulent Flow RH_p201 Flow Behavior Fluids
4208Equivalent Length of Pipe Fittings and Valves.161FigureTurbulent FlowTurbulent Flow RH_p201 Flow Behavior Fluids
4212Upper Limits of Specific Speeds of Centrifugal Pumps170FigurePumpsPumps RH_p221 Pumps Fluids
4213Upper Limits of Specific Speeds of Single-Suction Mixed-Flow171FigurePumpsPumps RH_p221 Flow Applications Fluids
4214Approximate Relative Impeller Shapes and Efficiency Variatio172FigureFlow ApplicationsFlow Applications Chopey Flow Applications Fluids
4215Typical Pump Suction and Discharge Piping Arrangements (Perr173FigurePumpsPumps RH_p221 Flow Applications Fluids
4216Typical Selection Chart for Centrifugal Pumps174FigurePumpsPumps RH_p221 Flow Applications Fluids
5201Plot of f2(4 α θ /l2) for Various Shapes185FigureHeat-Exchange Equipment DesignHeat-Exchange Equipment Design Kern Heat-Transfer Applications Heat Transfer
5205Gurney-Lurie Chart for Cylinders187FigureHeat-Exchange Equipment DesignHeat-Exchange Equipment Design Kern Heat-Transfer Applications Heat Transfer
5208Condensing Coefficients204FigureCondensationDesign Parameters for Non-Trayed Units Kern Heat-Transfer With Phase Change Heat Transfer
5210LMTD Correction Factors for Heat Exchangers.207FigureHeat Transfer without Phase ChangeHeat Transfer without Phase Change Perry Heat-Transfer Mechanisms Heat Transfer
5211Gurney-Lurie Chart for Spheres209FigureHeat-Exchange Equipment DesignHeat-Exchange Equipment Design Kern Heat-Transfer Applications Heat Transfer
5212Gurney-Lurie Chart for Semiinfinite Solid210FigureHeat-Exchange Equipment DesignHeat-Exchange Equipment Design Kern Heat-Transfer Applications Heat Transfer
10201Boiling-point rise of aqueous solutions226FigureHeat Transfer in EvaporatorsHeat Transfer in Evaporators Perry Boiling-point rise of aqueous solutions Heat Transfer
10202Evaporator Types227FigureEvaporator Types and ApplicationsEvaporator Types and Applications Perry Evaporators Heat Transfer
6201K-values (K =y/x) in light-hydrocarbon systems, low-temperature range229FigureMaterial and Energy Balances for Trayed and Packed UnitsMaterial and Energy Balances for Trayed and Packed Units RH_p285 Continuous Vapor-Liquid Contactors Mass Transfer
6202K-values (K = y/x) in light-hydrocarbon systems, high-temperature range230FigureMaterial and Energy Balances for Trayed and Packed UnitsMaterial and Energy Balances for Trayed and Packed Units RH_p285 Continuous Vapor-Liquid Contactors Mass Transfer
6208Minimum Reflux at infinite theoretical plates237FigureMaterial and Energy Balances for Trayed and Packed UnitsMaterial and Energy Balances for Trayed and Packed Units RH_p285 Continuous Vapor-Liquid Contactors Mass Transfer
6207Approximate solution for N and L/D in Distillation239FigureMaterial and Energy Balances for Trayed and Packed UnitsMaterial and Energy Balances for Trayed and Packed Units RH_p285 Continuous Vapor-Liquid Contactors Mass Transfer
6203Comparison of rigorous calculations with Gilliland Correleation244FigureMaterial and Energy Balances for Trayed and Packed UnitsMaterial and Energy Balances for Trayed and Packed Units RH_p285 Continuous Vapor-Liquid Contactors Mass Transfer
6204Separation operations related to distillation245FigureMaterial and Energy Balances for Trayed and Packed UnitsMaterial and Energy Balances for Trayed and Packed Units RH_p285 Continuous Vapor-Liquid Contactors Mass Transfer
6205Empirical correlations of overall efficiencies for fractionation and absorption246FigureMaterial and Energy Balances for Trayed and Packed UnitsMaterial and Energy Balances for Trayed and Packed Units RH_p285 Continuous Vapor-Liquid Contactors Mass Transfer
6206Graphical Representation of Fenske-Underwood-Gilliland proce247FigureMaterial and Energy Balances for Trayed and Packed UnitsMaterial and Energy Balances for Trayed and Packed Units RH_p285 Continuous Vapor-Liquid Contactors Mass Transfer
7205Packed Column performance nomograph256FigureMaterial and Energy Balances for Trayed and Packed UnitsMaterial and Energy Balances for Trayed and Packed Units RH_p285 Miscellaneous Mass Transfer Processes (Continuous, Batch, and Semicontinuous) Mass Transfer
7206Packing factors for use with Fig 9-11D (Fig 9-12D)257FigureDesign Parameters for Non-Trayed UnitsDesign Parameters for Non-Trayed Units RH_p285 Continuous Vapor-Liquid Contactors Mass Transfer
7203Generalized flooding and pressure drop correlation for packings259FigureDesign Parameters for Trayed UnitsDesign Parameters for Trayed Units RH_p299 Continuous Vapor-Liquid Contactors Mass Transfer
7204Generalized pressure-drop correlation for packed towers [Fig260FigureMaterial and Energy Balances for Trayed and Packed UnitsMaterial and Energy Balances for Trayed and Packed Units RH_p285 Continuous Vapor-Liquid Contactors Mass Transfer
7201Absorption and Stripping Factors263FigureMaterial and Energy Balances for Trayed and Packed UnitsMaterial and Energy Balances for Trayed and Packed Units RH_p285 Continuous Vapor-Liquid Contactors Mass Transfer
7202Number of overall gas-phase mass-transfer units in a packed absorption tower264FigureMaterial and Energy Balances for Trayed and Packed UnitsMaterial and Energy Balances for Trayed and Packed Units RH_p285 Continuous Vapor-Liquid Contactors Mass Transfer
5206Gurney-Lurie Chart for Slab1586FigureHeat-Exchange Equipment DesignHeat-Exchange Equipment Design Kern Heat-Transfer Applications Heat Transfer