Hydrogen production by steam reforming of DME in a large scale CFB reactor. Part I: computational model and predictions

Keyphrases

• Computational Model 100%
• Hydrogen Production 100%
• Steam Reforming 100%
• Computational Prediction 100%
• Circulating Fluidized Bed Reactor 100%
• Dimethyl Ether Steam Reforming 66%
• Dynamic Study 33%
• Temperature Variation 33%
• Temperature Distribution 33%
• Molar Ratio 33%
• Computational Fluid Dynamics 33%
• ZSM-5 33%
• Computational Fluid Dynamics Modeling 33%
• User-defined Function 33%
• Reaction Kinetics 33%
• Reactor Design 33%
• Operating Conditions 33%
• Steam 33%
• Eulerian-Eulerian 33%
• Reaction Zone 33%
• Product Gas 33%
• Bifunctional Catalyst 33%
• Reactor Performance 33%
• Gas Residence Time 33%
• Commercial Software 33%
• Mass Ratio 33%
• CuO-ZnO-Al2O3 33%
• Gas Species 33%
• Bioreactor Hydrodynamics 33%
• Reaction Scheme 33%
• Conversion Yield 33%
• ANSYS Software 33%
• Steam Reforming Reaction 33%
• Dispersed Flow 33%
• Operating Condition Effects 33%
• Species Concentration 33%
• Hydrogen Yield 33%
• Product Gas Composition 33%
• DME Conversion 33%
• ANSYS Fluent 33%

Engineering

• Fluidized Bed Reactor 100%
• Circulating Fluidized Bed 100%
• Hydrogen Production 100%
• Steam Reforming 100%
• Computational Fluid Dynamics 66%
• Product Gas 66%
• Dynamic Models 33%
• Hydrodynamics 33%
• Mols 33%
• Spatial Variation 33%
• Gas Composition 33%
• Reactor Design 33%
• Reaction Zone 33%
• Reaction Scheme 33%
• Molar Ratio 33%
• Commercial Software 33%
• Gas Specie 33%
• Temperature Distribution 33%
• Mass Ratio 33%

Chemical Engineering

• Hydrogen Production 100%
• Circulating Fluidized Bed Reactor 100%
• Temperature Distribution 33%