Effects of calcination and activation conditions on ordered mesoporous carbon supported iron catalysts for production of lower olefins from synthesis gas

Keyphrases

• Activation Conditions 100%
• Active Iron 66%
• Alternative Feedstocks 33%
• Calcination 66%
• Calcination Activation 33%
• Calcination Conditions 100%
• Calcination Temperature 66%
• Carbon Support 100%
• Carbothermal Reduction 33%
• Catalytic Activity 33%
• Catalytic Properties 33%
• Catalytically Active Sites 33%
• CMK-3 33%
• CO 2 33%
• CO Conversion 33%
• Commodity Chemicals 33%
• Fischer-Tropsch Synthesis 33%
• Fluid Catalytic Cracking 33%
• Graphite Layer 33%
• High Catalytic Activity 33%
• High Ratio 33%
• High Temperature 33%
• Hydrocarbons 33%
• Iron Carbide 100%
• Iron Catalyst 33%
• Iron Oxide Nanoparticles 33%
• Iron Oxide Reduction 33%
• Iron-sulfur 33%
• Low Calcination Temperature 33%
• Lower Olefins 100%
• Mesoporous Carbon CMK-3 33%
• Metal Species 33%
• Methane 33%
• Nanostructured Carbon 33%
• Naphtha 33%
• Olefin Selectivity 33%
• Olefins 33%
• Ordered Mesoporous Carbon 100%
• Particle Blocking 33%
• Particle Growth 33%
• Pore Structure 33%
• Sodium-sulfur 33%
• Stable Operation 33%
• Steam Cracking 33%
• Structure-performance Relationship 33%
• Support Material 66%
• Supported Catalysts 33%
• Supported Iron Catalyst 100%
• Synthesis Gas 100%
• Synthetic Approaches 33%
• Time on Stream 33%
• Vacuum Gas Oil 33%
• Weak Interactions 33%
• Well-defined 33%

Chemical Engineering

• Calcination 100%
• Catalytic Cracking 16%
• Iron Nanoparticle 16%
• Iron Oxide 16%
• Olefin 100%