Effects of internals and distributors on the distribution and growth of bubbles in the conventional gas–solid fluidized bed

Keyphrases

• Fluidized Bed 100%
• Distributor 100%
• Pore Size 50%
• Small Pore 50%
• Opening Area 50%
• Two-layer 25%
• Superficial Gas Velocity 25%
• Gas Distributor 25%
• Small Bubbles 25%
• Low Pressure Drop 25%
• Pressure Drop 25%
• Local Dynamics 25%
• Solids Holdup 25%
• Bubble Phase 25%
• Optical Fiber Probe 25%
• Four-layer 25%
• Local Solid Holdup 25%
• Bubble Dynamics 25%
• Dense Phase 25%
• Bed Expansion 25%
• Differential Pressure 25%
• Local Bubble 25%
• Perforated Plate 25%
• Early Transition 25%
• Large Pore Size 25%
• Mesh Type 25%
• Turbulent Flow Regime 25%

Engineering

• Internals 100%
• Fluidized Bed 100%
• Pressure Drop 33%
• Open Area 33%
• Gas Distributor 16%
• Superficial Gas Velocity 16%
• Optical Fiber 16%
• Turbulent Flow 16%
• Flow Regime 16%
• Dense Phase 16%
• Bed Expansion 16%
• Differential Pressure 16%
• Perforated Plate 16%
• Bubble Phase 16%