Development of structured catalyst and reactor technologies for biomass conversion: Continuous production of sugar alcohols

Chemistry

• Catalyst 100%
• Foam 76%
• Mass Transfer 70%
• Liquid 47%
• Adsorption 35%
• Hydrogenation 23%
• Structure 23%
• Solid 23%
• Sugar Alcohol 17%
• Mixture 17%
• Chemical Kinetics Characteristics 17%
• Reactor 17%
• Flow 17%
• Surface Area 11%
• Hydrogen 11%
• L-Arabinose 11%
• Gas 11%
• Chemical Reactor 11%
• Nanoparticle 5%
• Physisorption 5%
• Reaction Parameter 5%
• Diffusion 5%
• Nitrogen 5%
• Porosity 5%
• Scanning Electron Microscopy 5%
• Pharmacokinetics 5%
• Reaction Activation Energy 5%
• Pressure Drop 5%
• Mass Balance 5%
• D-Glucose 5%
• Galactose 5%
• Arabinose 5%
• D-Galactose 5%
• Carbon Monoxide 5%
• Chemical Industry 5%
• Velocity 5%
• Turbulence 5%
• Polymerization Reaction 5%
• Procedure 5%
• Reaction Temperature 5%
• Analytical Method 5%
• Engineering Process 5%
• Chemical Reaction Product 5%
• Reaction Selectivity 5%
• Inert 5%
• Time 5%
• Fiber 5%
• Precipitation (Chemical) 5%
• Energy 5%
• Pressure 5%
• Inductively Coupled Plasma Method 5%
• Intravenous 5%
• Rate Equation 5%
• Tracer 5%
• Error 5%
• Residence Time 5%
• Flow Kinetics 5%
• Chemisorption 5%

Chemical Engineering

• Carbon 23%
• Sugar 23%
• Aluminum 23%
• Ruthenium 17%
• Trickle Bed Reactor 11%
• Reactor Technology 11%
• Multiphase Reactor 11%
• Heat Transfer 11%
• Hydrogen 11%
• Biomass Conversion 11%
• Physisorption 5%
• Nitrogen 5%
• Diffusion 5%
• Precipitation (Chemical) 5%
• Temperature 5%
• Deposition 5%
• Screening 5%
• Carbon Monoxide 5%
• Chemisorption 5%