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Chemical Engineering
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Demonstrations 101  120 of 420
Maximizing Conversion to an Intermediate Product in a Chain of Three CSTRs in Series
Control of Thermal Runaway of an Exothermic Reaction by Coupling with an Endothermic Reaction
Entrainer Selection for Homogeneous Azeotropic Distillation
SteadyState Distillation of a Quaternary Mixture
Finding the Minimum Reflux Ratio Using the Underwood Equations
Separating Binary Azeotropes Using Pressure Swing Distillation
Maximizing Conversion to an Intermediate Product in a TwoStage CSTR
Breaking the AcetoneMethanol Azeotrope with Different Extraction Solvents
Volatility Inversion in Extractive Distillation
Extractive Distillation of an Equimolar AcetoneMethanol Mixture Using Water
Steady State of an Extractive Distillation Column
Simple Arrhenius Model for Activation Energy and Catalysis
Rigorous SteadyState Simulation of a Multicomponent Distillation Column
Separating a Ternary Mixture of Water, 2Propanol, and Acetone at Atmospheric Pressure
SteadyState Distillation of a MethanolWater Mixture
PonchonSavarit Diagram for MethanolWater Mixture
PonchonSavarit Diagram for an EthanolWater Binary Mixture
Zeolite A
Zeolite Unit Cell Based on Cuboctahedron
Gas Absorption Computed Using the Successive OverRelaxation (SOR) Method
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