Wolfram Demonstrations Project
Chemical Engineering
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Demonstrations 141 - 160 of 374
Transient Behavior of an Adiabatic CSTRConversion versus Reactor Volume for CSTR and PFTRVariation of Temperature and Concentration versus Residence Time for Adiabatic ReactorsK-value of Several Hydrocarbons versus Temperature and PressurePerformance of CSTR and Plug Flow Reactors versus Temperature
Transient Behavior of an Adiabatic CSTR
Conversion versus Reactor Volume for CSTR and PFTR
Variation of Temperature and Concentration versus Residence Time for Adiabatic Reactors
K-value of Several Hydrocarbons versus Temperature and Pressure
Performance of CSTR and Plug Flow Reactors versus Temperature
Reaction Paths of Wei-Prater Complex Reaction NetworksLever Rule Applied to the Benzene-Toluene Vapor Pressure DiagramEnriching Oxygen in Air by Cross-Flow Membrane PermeationButler-Volmer Equation for Electrochemical ReactionComputing Gas Permeation Using the Complete Mixing Model
Reaction Paths of Wei-Prater Complex Reaction Networks
Lever Rule Applied to the Benzene-Toluene Vapor Pressure Diagram
Enriching Oxygen in Air by Cross-Flow Membrane Permeation
Butler-Volmer Equation for Electrochemical Reaction
Computing Gas Permeation Using the Complete Mixing Model
Computation of Tie Lines for Ternary MixturesSteady-States of a Nonlinear Chemical System Using the Arc Length Continuation MethodDoehlert Design for Wet PelletizationHeat Exchanger EffectivenessEthylene Glycol Synthesis with a Reactive Distillation Unit
Computation of Tie Lines for Ternary Mixtures
Steady-States of a Nonlinear Chemical System Using the Arc Length Continuation Method
Doehlert Design for Wet Pelletization
Heat Exchanger Effectiveness
Ethylene Glycol Synthesis with a Reactive Distillation Unit
Dynamic Behavior of Isothermal Flash VesselMethyl Tert-Butyl Ether (MTBE) Decomposition with a Reactive Distillation UnitMethyl Tert-Butyl Ether (MTBE) Synthesis with a Reactive Distillation UnitTransient Behavior of N CSTRs in Series with Chemical ReactionOptimal Temperature Policy for First-Order Reversible Reactions
Dynamic Behavior of Isothermal Flash Vessel
Methyl Tert-Butyl Ether (MTBE) Decomposition with a Reactive Distillation Unit
Methyl Tert-Butyl Ether (MTBE) Synthesis with a Reactive Distillation Unit
Transient Behavior of N CSTRs in Series with Chemical Reaction
Optimal Temperature Policy for First-Order Reversible Reactions

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