Wolfram Demonstrations Project
Chemical Engineering
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Demonstrations 181 - 200 of 374
Optimal Economic Strategy for the Operation of a Batch Reactor with Dead TimeNumerical Solution of the Dispersion Equation for a First-Order ReactionResidence Time Distribution of Single Continuous Stirred-Tank Reactors Subject to a Square Pulse InputDynamic Behavior of an Addition Polymerization in a Batch ReactorOxidation of Naphthalene in a Tubular Flow Reactor
Optimal Economic Strategy for the Operation of a Batch Reactor with Dead Time
Numerical Solution of the Dispersion Equation for a First-Order Reaction
Residence Time Distribution of Single Continuous Stirred-Tank Reactors Subject to a Square Pulse Input
Dynamic Behavior of an Addition Polymerization in a Batch Reactor
Oxidation of Naphthalene in a Tubular Flow Reactor
Optimal Operation of a Batch Reactor with Dead TimeVapor Liquid Equilibrium Data in Tert-Amyl Methyl Ether (TAME) ProductionChromatographic Reactions of Three ComponentsStripping and Rectifying Cascades for Isopropyl Acetate ChemistryYield and Selectivity for Series-Reaction Network in a CSTR and a PFR
Optimal Operation of a Batch Reactor with Dead Time
Vapor Liquid Equilibrium Data in Tert-Amyl Methyl Ether (TAME) Production
Chromatographic Reactions of Three Components
Stripping and Rectifying Cascades for Isopropyl Acetate Chemistry
Yield and Selectivity for Series-Reaction Network in a CSTR and a PFR
Operation of a Stripping ColumnSelectivity for Adsorption of Ethylene Relative to Ethane in NaX Zeolite at 20 °CProportional-Integral Control of Batch Rectification ProcessOperation of a Rectifying ColumnStripping a Hydrocarbon from Oil Using Live Steam
Operation of a Stripping Column
Selectivity for Adsorption of Ethylene Relative to Ethane in NaX Zeolite at 20 °C
Proportional-Integral Control of Batch Rectification Process
Operation of a Rectifying Column
Stripping a Hydrocarbon from Oil Using Live Steam
Temperature Dependence of Dehydrogenation of Ethyl Benzene to StyreneResidue Curve and Bubble Temperature Distribution for Methyl Tert-Butyl Ether Chemistry at 8 atmFlow in a Rectangular Channel with Double Orthogonal CollocationResidue Curve and Bubble Temperature Distribution for a Ternary MixtureResidue Curve and Temperature Distribution for Ethyl Acetate Chemistry
Temperature Dependence of Dehydrogenation of Ethyl Benzene to Styrene
Residue Curve and Bubble Temperature Distribution for Methyl Tert-Butyl Ether Chemistry at 8 atm
Flow in a Rectangular Channel with Double Orthogonal Collocation
Residue Curve and Bubble Temperature Distribution for a Ternary Mixture
Residue Curve and Temperature Distribution for Ethyl Acetate Chemistry

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