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Ahmed Bellagi
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Demonstrations 121  140 of 141
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
Residue Curve and Bubble Temperature Distribution for Methyl TertButyl Ether Chemistry at 8 atm
Residue Curve and Bubble Temperature Distribution for a Ternary Mixture
Residue Curve and Temperature Distribution for Ethyl Acetate Chemistry
Economic TradeOffs in the Operation of a Single Reactor
Flash Distillation Cascade for an AcetoneChloroform Mixture
Flash Distillation Cascade for an Ethyl AcetateEthanol Mixture
Flash Distillation Cascade for a BenzeneToluene Mixture
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