Modeling and Design of a Multi-Tubular Packed-Bed Reactor for Methanol Steam Reforming over a Cu/ZnO/Al2O3 Catalyst

Engineering

• Reactor 100%
• Packed Bed 100%
• Multi--Tubular 100%
• Models 100%
• Design 100%
• Shell Side 66%
• Simulation Result 33%
• Proton-Exchange Membrane Fuel Cells 33%
• Kinetic Model 33%
• Temperature Profile 33%
• Fuel Cell Stack 33%
• Diameter Tube 33%
• Low Flow Rate 33%
• Geometric Parameter 33%
• Effectiveness Factor 33%
• Heat Transfer Phenomenon 33%
• Langmuir Kinetics 33%
• Catalyst Particle 33%
• Baffle Plate 33%
• Mass Transfer 33%
• High Concentration 33%

Chemical Engineering

• Methanol 100%
• Methanol Steam Reforming 100%
• Temperature 60%
• Hydrogen 20%
• Heat Transfer 20%