Analysis of the performance of single capillary and multiple capillary (monolith) reactos for the multiphase pd-catalysed hydrogenation of 2-Butyne-1,4-Diol

Keyphrases

• Hydrogenation 100%
• Capillary 100%
• 2-Butyne-1,4-diol 100%
• Capillary Monolith 100%
• Capillary Reactor 100%
• Pd-catalyzed 100%
• Temperature Range 33%
• Alkynes 33%
• Reaction Products 33%
• Product Distribution 33%
• High Selectivity 33%
• Pressure Range 33%
• Reaction Rate 33%
• Single Channel 33%
• Monolith 33%
• Downflow 33%
• 1,4-diols 33%
• Langmuir-Hinshelwood Mechanism 33%
• Hydrodynamic Conditions 33%
• Zero Order 33%
• Reaction Rate Distribution 33%
• 2-Propanol 33%
• 2-Butene 33%
• Surface Concentration 33%
• Monolith Reactor 33%
• 1-butene 33%
• Transport Problem 33%
• Water Solvent 33%
• Taylor Flow 33%

Chemistry

• Hydrogenation 100%
• Diol 100%
• Alkyne 25%
• Product Distribution 25%
• Butene 25%

Chemical Engineering

• Hydrogenation 100%
• Butene 50%
• Propanol 50%
• Monolith Reactor 50%