Model for non-suspension gas-solids flow of fine powders in pipes

Engineering

• Energy Engineering 100%
• Finer Powder 100%
• Experimental Observation 66%
• Pressure Profile 66%
• Initial Condition 66%
• Fully Developed Flow 66%
• Dense Layer 66%
• Parametric Study 33%
• Mass Flowrate 33%
• Pneumatic Conveying System 33%
• Moving Bed 33%
• Equations for Mass 33%
• Conservation Equation 33%
• Momentum Transfer 33%
• Relative Significance 33%
• Dilute Gas 33%
• Dense Phase 33%
• Flow Velocity 33%
• Bulk Material 33%

Keyphrases

• Two-layer 100%
• Gas-solid Flow 100%
• Fine Powder 100%
• Momentum Transfer 40%
• Pressure Profile 40%
• Gas-solid Mixture 40%
• Dense Layer 40%
• Fully Developed Flow 40%
• Mass Transfer 20%
• Gas Phase 20%
• Solid Phase 20%
• Energy Transfer 20%
• Pneumatic Conveying 20%
• Moving Bed 20%
• Horizontal pipe 20%
• Conservation Equations 20%
• Solid Mass Flow Rate 20%
• Total Gas 20%
• Dense Phase 20%
• Dense Gas 20%
• Liquid-solid Flow 20%
• Total Solids 20%
• Dilute Gas 20%
• Mean Flow Velocity 20%
• Overall Behaviors 20%
• Bulk Material 20%
• Relative Significance 20%
• Gas Mass Flow Rate 20%