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Demonstrations 61 - 80 of 390
Extractive Distillation of an Azeotropic Mixture of Isopropyl Alcohol and Water: Effect of Entrainer Feed TemperatureFlash Distillation of a Benzene, Toluene, p-Xylene MixtureMulticomponent Distillation Column with a SidestreamBoundary-Layer Flow Past a Semi-Infinite Wedge: The Falkner-Skan ProblemMethyl Acetate Synthesis Using a Reactive Distillation Unit
Extractive Distillation of an Azeotropic Mixture of Isopropyl Alcohol and Water: Effect of Entrainer Feed Temperature
Flash Distillation of a Benzene, Toluene, p-Xylene Mixture
Multicomponent Distillation Column with a Sidestream
Boundary-Layer Flow Past a Semi-Infinite Wedge: The Falkner-Skan Problem
Methyl Acetate Synthesis Using a Reactive Distillation Unit
Analysis of an Extractive Distillation Column with Three Design VariablesDistillation Column Calculation Incorporating Pressure Drop EffectEntrainer Selection for Homogeneous Azeotropic DistillationSteady-State Distillation of a Quaternary MixtureFinding the Minimum Reflux Ratio Using the Underwood Equations
Analysis of an Extractive Distillation Column with Three Design Variables
Distillation Column Calculation Incorporating Pressure Drop Effect
Entrainer Selection for Homogeneous Azeotropic Distillation
Steady-State Distillation of a Quaternary Mixture
Finding the Minimum Reflux Ratio Using the Underwood Equations
Mapping the Maxima for a Nonisothermal Chemical SystemSeparating Binary Azeotropes Using Pressure Swing DistillationLocal Solution of a Nonlinear ODE Using a Power Series ExpansionMaxima and Minima for the Three-Variable AutocatalatorInversion of the Laplace Transform Using the Gaver-Stehfest Algorithm
Mapping the Maxima for a Nonisothermal Chemical System
Separating Binary Azeotropes Using Pressure Swing Distillation
Local Solution of a Nonlinear ODE Using a Power Series Expansion
Maxima and Minima for the Three-Variable Autocatalator
Inversion of the Laplace Transform Using the Gaver-Stehfest Algorithm
Finding the Global Minimum of a Function Using Simulated AnnealingBreaking the Acetone-Methanol Azeotrope with Different Extraction SolventsVolatility Inversion in Extractive DistillationExtractive Distillation of an Equimolar Acetone-Methanol Mixture Using WaterSteady State of an Extractive Distillation Column
Finding the Global Minimum of a Function Using Simulated Annealing
Breaking the Acetone-Methanol Azeotrope with Different Extraction Solvents
Volatility Inversion in Extractive Distillation
Extractive Distillation of an Equimolar Acetone-Methanol Mixture Using Water
Steady State of an Extractive Distillation Column

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