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Rachael L. Baumann and John L. Falconer (University of Colorado Boulder, Department of Chemical and Biological Engineering)
Demonstrations 1 - 10 of 10
Fugacities in an Ideal Binary Mixture
Gas-Phase Chemical Equilibrium at Constant Pressure or Constant Volume
Multiple Steady States in a Continuous Stirred-Tank Reactor with Heat Exchange
Pressure Drop in a Packed Bed Reactor (PBR) Using the Ergun Equation
Batch Reactors at Constant Volume or Constant Pressure
Sensitivity of a Plug Flow Reactor to Model Parameters
Selectivity in a Semibatch Reactor
Effect of Tube Diameter on Plug Flow Reactor
Inhibition of Enzyme Reactions in Continuous Stirred-Tank Reactor and Batch Reactor
Multiple States in an Isothermal Continuous Stirred-Tank Reactor
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