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Housam Binous and Ahmed Bellagi
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Demonstrations 61  80 of 83
Conversion of Ethylbenzene to Styrene in the Presence of Steam
Residence Time Distribution for Continuous StirredTank Reactors in Series Using the First Four Moments
Two Isothermal Continuous StirredTank Reactors with a Recycle Stream
Step and Impulse Response of a SecondOrder System
Slurry Reactor with Declining Catalyst Activity
Optimal Economic Strategy for the Operation of a Batch Reactor with Dead Time
Numerical Solution of the Dispersion Equation for a FirstOrder Reaction
Residence Time Distribution of Single Continuous StirredTank 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 Time
Stripping and Rectifying Cascades for Isopropyl Acetate Chemistry
Yield and Selectivity for SeriesReaction Network in a CSTR and a PFR
Operation of a Stripping Column
Selectivity for Adsorption of Ethylene Relative to Ethane in NaX Zeolite at 20 °C
ProportionalIntegral Control of Batch Rectification Process
Operation of a Rectifying Column
Temperature Dependence of Dehydrogenation of Ethyl Benzene to Styrene
Economic TradeOffs in the Operation of a Single Reactor
Flash Distillation Cascade for an AcetoneChloroform Mixture
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