| No | Title | Handout | Type | Transcript | Audio | Topic | Reference: | Subject |
| 1301 | Comparison of performance of single CSTR and PFR for the nth | Yes | Figure | Yes | Yes | Comparison of CSTR and PFR | Levenspiel, Fig 8-8 | kinetics |
| 1306 | Comparison of performance of a series of N equal-size CSTR r | Yes | Figure | Yes | Yes | Performance - First Order Reaction | Levenspiel, Fig 8-15 | kinetics |
| 1307 | Comparison of performance of a series of N equal-size CSTR r | Yes | Figure | Yes | Yes | Performance - Second Order Reaction | Levenspiel, Fig 8-16 | kinetics |
| 1308 | Distribution of materials in a batch or plug flow reactor fo | Yes | Figure | Yes | Yes | Performance - Series or Parallel Reactions | Levenspiel, Fig 15 | kinetics |
| 1309 | Comparison of performance of recycle and plug flow for first | Yes | Figure | Yes | Yes | Recycle and Plug Flow - First Order Reaction | Levenspiel, Fig 16 | kinetics |
| 1310 | Comparison of performance of recycle with plug flow for elem | Yes | Figure | Yes | Yes | Recycle and Plug Flow - Second Order Reaction | Levenspiel, Fig 17 | kinetics |
| 1311 | Performance of plug-flow and back-mix reactors [Fig 4-6] | Yes | Figure | Yes | Yes | Performance of Plug Flow and Back-mix Reactors | Levenspiel, Fig 4-6 | kinetics |
| 2201 | Compressibility Factors of Gases and Vapors [Fig 103] | Yes | Figure | Yes | Yes | Vapor Density | Hougen, Fig 103 | thermo |
| 2202 | Generalized Plot of Z(0) values [Fig 3-45] | Yes | Figure | Yes | Yes | Compressibility Factor | Perry, Fig 3-45 | thermo |
| 2203 | Generalized Plot of Z(1) values [Fig 3-46] | Yes | Figure | Yes | Yes | Compressibility Factor | Perry, Fig 3-46 | thermo |
| 2213 | Generalized Reduced Viscosities [Fig 175] | Yes | Figure | Yes | Yes | Generalized Reduced Viscosities | Hougen, Fig 175 | thermo |
| 2204 | Enthalpy Correction for Gases and Vapors due to Lack of Idea | Yes | Figure | Yes | Yes | Enthalpy Correction | Hougen, Fig 106 | thermo |
| 2205 | Correlation of H/RTc(0) [Fig 4-30] | Yes | Figure | Yes | Yes | Enthalpy Correction | Perry, Fig 4-30 | thermo |
| 2206 | Correlation of H/RTc(1) [Fig 4-31] | Yes | Figure | Yes | Yes | Enthalpy Correction | Perry, Fig 4-31 | thermo |
| 2216 | Isothermal pressure correction to the molar heat capacity of | Yes | Figure | Yes | Yes | Correction to the molar heat capacity of gases | Chopey, Fig 1-4 | thermo |
| 2218 | Entropy departure of gases and liquids [Fig 1-11] | Yes | Figure | Yes | Yes | Entropy departure of gases and liquids | Chopey, Fig 1-11 | thermo |
| 2207 | Entropy Correction for Gases and Vapors due to Lack of Ideal | Yes | Figure | Yes | Yes | Entropy Correction | Hougen, Fig 107 | thermo |
| 2208 | Effect of Pressure on Molal Heat Capacity of Gases [Fig 108] | Yes | Figure | Yes | Yes | Effect of Pressure on Molal Heat Capacity of Gases | Hougen, Fig 108 | thermo |
| 2217 | Enthalpy departure from idea-gas state [Fig 1-8] | Yes | Figure | Yes | Yes | Enthalpy departure from idea-gas state | Chopey, Fig 1-8 | thermo |
| 2209 | Generalized Heat-Capacity Differencess, Cp-Cv [Fig 1-5] | Yes | Figure | Yes | Yes | Heat Capacity Differencess | Perry, Fig 1-5 | thermo |
| 2214 | Appendix K - Mollier Chart | Yes | Figure | Yes | Yes | Mollier Chart for Steam | Perry | thermo |
| 2219 | Enthalpy-log pressure diagram for Refrigerant-11 [Fig 3-33] | Yes | Figure | Yes | Yes | Refrigerant Chart | Perry, Fig 3-33 | thermo |
| 2210 | Fugacity Coefficents of Gases and Vapors [Fig 142] | Yes | Figure | Yes | Yes | Fugacity Coefficents of Gases and Vapors | Hougen, Fig 142 | thermo |
| 2211 | Correlation of -ln(0) vs Tr [Fig 4-32] | Yes | Figure | Yes | Yes | Fugacity Coefficient | Perry, Fig 4-32 | thermo |
| 2212 | Correlation of -ln(1) vs Tr [Fig 4-33] | Yes | Figure | Yes | Yes | Fugacity Coefficient | Perry, Fig 4-33 | thermo |
| 2215 | Reaction Equilibrium Constants [Fig - 156] | Yes | Figure | Yes | Yes | Reaction Equilibrium Constants | Hougen, Fig 156 | thermo |
| 3202 | Psychrometric chart - low temperatures [Fig 12-1] | Yes | Figure | Yes | Yes | Psychrometric chart - low temperatures | Perry, Fig 12-1 | meb |
| 3203 | Psychrometric chart - medium temperatures [Fig 12-2] | Yes | Figure | Yes | Yes | Psychrometric chart - medium temperatures | Perry, Fig 12-2 | meb |
| 3204 | Psychrometric Chart (High Temperatures) [Fig 12-3] | Yes | Figure | Yes | Yes | Psychrometric Chart (High Temperatures) | Perry, Fig 12-3 | meb |
| 3205 | Enthalpy-concentration Diagram for Aqueous Sulfuric Acid at | Yes | Figure | Yes | Yes | Enthalpy-concentration Diagram | Hougen, Fig 3-38 | meb |
| 3201 | Graphic Relationship of SI Units with Names [Fig 1-1] | Yes | Figure | Yes | Yes | Graphic Relationship of SI Units with Names | Perry, Fig 1-1 | meb |
| 4202 | Flow Coefficient C for Nozzles. [Fig A-20] | Yes | Figure | Yes | Yes | Nozzles | Crane, Fig A-20 | fluid_flow |
| 4203 | Flow Coefficient C for square-edged Orifices.[Fig A-20] | Yes | Figure | Yes | Yes | Orifices | Crane, Fig A-20 | fluid_flow |
| 4204 | Net Expansion Factor Y for Compressible Flow Through Nozzles | Yes | Figure | Yes | Yes | Nozzles and Orifices. | Crane, Fig A-20 | fluid_flow |
| 4201 | Kinematic Viscosity of fluids.[Fig A-2] | Yes | Figure | Yes | Yes | Kinematic Viscosity of fluids | Crane, Fig A-2 | fluid_flow |
| 4205 | Critical Pressure Ratio, rc for Compressible Flow through N | Yes | Figure | Yes | Yes | Nozzles and Venturi Tubes | Crane, Fig A-21 | fluid_flow |
| 4209 | Roughness factors (expressed in feet) for Commercial Pipes.[ | Yes | Figure | Yes | Yes | Roughness factors | Crane, Fig A-4 | fluid_flow |
| 4210 | Friction factor Chart. [Fig 5-10] | Yes | Figure | Yes | Yes | Friction factor Chart | McCabe, Fig 5-10 | fluid_flow |
| 4211 | Friction factor Chart, NRe Цf vs. f.[Fig 5-11] | Yes | Figure | Yes | Yes | Friction factor Chart | McCabe, Fig 5-11 | fluid_flow |
| 4206 | Enlargement and Contraction Losses | Yes | Figure | Yes | Yes | Enlargement and Contraction Losses | Crane, Fig A-26 | fluid_flow |
| 4207 | Resistance due to Pipe Entrance and Exit | Yes | Figure | Yes | Yes | Entrance and Exit Losses | Crane, Fig A-26 | fluid_flow |
| 4208 | Equivalent Length of Pipe Fittings and Valves.[Fig 6-5] | Yes | Figure | Yes | Yes | Pipe Fittings and Valves | Perry, Fig 6-5 | fluid_flow |
| 4212 | Upper Limits of Specific Speeds of Single-Stage Single- and | Yes | Figure | Yes | Yes | Specific Speeds of Pumps | Perry, Fig 6-10 | fluid_flow |
| 4213 | Upper Limits of Specific Speeds of Single-Suction Mixed-Flow | Yes | Figure | Yes | Yes | Specific Speeds of Pumps | Perry, Fig 6-11 | fluid_flow |
| 4214 | Approximate Relative Impeller Shapes and Efficiency Variatio | Yes | Figure | Yes | Yes | Specific Speeds | Perry, Fig 6-12 | fluid_flow |
| 4215 | Typical Pump Suction and Discharge Piping Arrangements (Perr | Yes | Figure | Yes | Yes | Pump Piping Arrangements | Perry, Fig 6-13 | fluid_flow |
| 4216 | Typical Selection Chart for Centrifugal Pumps (Perry, Fig 6- | Yes | Figure | Yes | Yes | Selection Chart for Centrifugal Pumps | Perry, Fig 6-16 | fluid_flow |
| 5201 | Plot of f2(4 alpha theta /l2) for Various Shapes. [Fig 18-9] | Yes | Figure | Yes | Yes | Unsteady-state Heat Transfer Chart for Various Shapes. | Kern, Fig 18-9 | heat_t |
| 5205 | Gurney-Lurie Chart for Cylinders. [Fig 18-13] | Yes | Figure | Yes | Yes | Gurney-Lurie Chart for Cylinders. | Kern, Fig 18-13 | heat_t |
| 5208 | Condensing Coefficients. [Fig 12-9] | Yes | Figure | Yes | Yes | Heat Transfer Condensing Coefficients. | Kern, Fig 12-9 | heat_t |
| 5209 | Dukler Plot Showing Average Condensing Film Coefficient.[Fig | Yes | Figure | Yes | Yes | Condensing Film Coefficient. | Chopey, Fig 10-10 | heat_t |
| 5210 | LMTD Correction Factors for Heat Exchangers.[Fig 10-14] | Yes | Figure | Yes | Yes | LMTD Correction Factors for Heat Exchangers. | Perry, Fig 10-14 | heat_t |
| 5211 | Temperature Efficiency for Counterflow Exchangers. [Fig 7-14 | Yes | Figure | Yes | Yes | Temperature Efficiency for Counterflow Exchangers. | Chopey, Fig 7-14 | heat_t |
| 5212 | Temperature Efficiency for Heat Exchangers with One Shell Pa | Yes | Figure | Yes | Yes | Temperature Efficiency for Heat Exchangers | Chopey, Fig 7-15 | heat_t |
| 10201 | Evaporator Types. [Fig 11-21] | Yes | Figure | Yes | Yes | Evaporator Types. | Perry, Fig 11-21 | heat_t |
| 10202 | Boiling-point Rise of Aqueous Solutions.[Fig 11-23] | Yes | Figure | Yes | Yes | Boiling-point Rise of Aqueous Solutions. | Perry, Fig 11-23 | heat_t |
| 6201 | K-values (K = y/x) in light-hydrocarbon systems, low-tempe | Yes | Figure | Yes | Yes | Distillation | Perry, Fig 13-14a | mass_t |
| 6202 | K-values (K = y/x) in light-hydrocarbon systems, high-tempe | Yes | Figure | Yes | Yes | Distillation | Perry, Fig 13-14b | mass_t |
| 6208 | Minimum Reflux at infinite theoretical plates [Fig 8-5a] | Yes | Figure | Yes | Yes | Distillation | Ludwig, Fig 8-5B | mass_t |
| 6207 | Approximate solution for N and L/D in distillation of id | Yes | Figure | Yes | Yes | Distillation | Ludwig, Fig 8-5A | mass_t |
| 6203 | Comparison of rigorous calculations with Gilliland correlati | Yes | Figure | Yes | Yes | Distillation | Perry, Fig 13-41 | mass_t |
| 6204 | Separation operations related to distillation [Fig 13-7] | Yes | Figure | Yes | Yes | Distillation | Perry, Fig 6-8 | mass_t |
| 6205 | Empirical correlations of overall efficiencies for fractiona | Yes | Figure | Yes | Yes | Distillation | Ludwig, Fig 8-11 | mass_t |
| 6206 | Graphical Representation of Fenske-Underwood-Gilliland proce | Yes | Figure | Yes | Yes | Distillation | Chopey, Fig 8-5 | mass_t |
| 7205 | Packed Column performance nomograph [Fig 9-11c] | Yes | Figure | Yes | Yes | Absorption | Ludwig, Fig 9-11C | mass_t |
| 7206 | Packing factors for use with Fig 9-11D (Fig 9-12D) | Yes | Figure | Yes | Yes | Absorption | Ludwig, Fig 9-12D | mass_t |
| 7203 | Generalized flooding and pressure drop correlation for packi | Yes | Figure | Yes | Yes | Absorption | Perry, Fig 18-38 | mass_t |
| 7204 | Generalized pressure-drop correlation for packed towers [Fig | Yes | Figure | Yes | Yes | Absorption | Chopey, Fig 8-18 | mass_t |
| 7201 | Absorption and Stripping Factors [Fig 13-43] | Yes | Figure | Yes | Yes | Absorption | Perry, Fig 13-43 | mass_t |
| 7202 | Number of overall gas-phase mass-transfer units in a packed | Yes | Figure | Yes | Yes | Absorption | Perry, Fig 14-9 | mass_t |