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Demonstrations 121 - 140 of 180
Idealized Closed Loop for Processes in Three Continuous Stirred-Tank Reactors
Impulse Response of Two and Three Continuous Stirred-Tank Reactors in Series: Exact and Approximate Solutions
Residence Time Distribution of Single Continuous Stirred-Tank Reactors Subject to a Square Pulse Input
Comparison of One- and Two-Dimensional Models of Plate Reactors
Residence Time Distribution for Continuous Stirred-Tank Reactors in Series Using the First Four Moments
Computation of the Volume of a CSTR and a PFR
Maximizing Conversion to an Intermediate Product in a Chain of Three CSTRs in Series
Maximizing Conversion to an Intermediate Product in a Two-Stage CSTR
Series Reactions in a CSTR with Time-Varying Input
Transient Behavior of an Adiabatic CSTR
Multistage Operation with Cold-Shot Cooling
Mass Balance in the Haber Process
Numerical Solution of the Dispersion Equation for a First-Order Reaction
Briggs-Rauscher Mechanism: The Chemical Color Clock
Product Distribution Curves for Laminar, Plug, and Mixed Flows
Dynamics of Counter-Current Cooled CSTRs
Maximizing Selectivity in the Trambouze Reactions
Yield and Selectivity for Series-Reaction Network in a CSTR and a PFR
Control of Thermal Runaway of an Exothermic Reaction by Coupling with an Endothermic Reaction
CSTR and PFR Holding-Time Ratio versus Conversion for Various Reaction Orders
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