RISING VELOCITY AND SHAPE OF SINGLE AIR BUBBLES IN HIGHLY VISCOUS LIQUIDS
スポンサーリンク
概要
著者
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KOJIMA EIICHI
Research Laboratory of Resourses Utilization, Tokyo Institute of Technology
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KOJIMA EIICHI
Research Laboratory of Resources Utilization, Tokyo Institute of Technology
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SHIRAI TAKASHI
Research Laboratory of Resources Utilization
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SHIRAI TAKASHI
Research Laboratory of Resourses Utilization, Tokyo Institute of Technology
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AKEHATA TAKASHI
Research Laboratory of Resourses Utilization, Tokyo Institute of Technology
関連論文
- Rotation of a horizontal disk within an aerated particle bed. Behavior of solid particles and torque requirements.:BEHAVIOR OF SOLID PARTICLES AND TORQUE REQUIREMENTS
- Liquid phase velocity in A 5.5M diameter bubble column.
- EXPERIMENTAL STUDY ON THE POWER REQUIREMENTS FOR AGITATING BEDS OF SOLID PARTICLES, AND PROPOSAL OF A NEW MODEL
- DISCHARGE RATE OF SOLID PARTICLES THROUGH ORIFICE WITH COCURRENT STREAM OF GAS
- DEAD ZONE PILED ON THE PLATE IMMERSED IN A FLUIDISED BED
- EXPERIMENTAL STUDY OF THE POWER NUMBERS FOR AGITATING BEDS OF SOLID PARTICLES WITH MULTIPLE BLADES AND UPWARD STREAMS OF GAS LESS THAN Umf
- RISING VELOCITY AND SHAPE OF SINGLE AIR BUBBLES IN HIGHLY VISCOUS LIQUIDS
- Axial dispersion of liquid in concurrent gas-liquid downflow in packed beds.
- Behavior of bubbles in large scale bubble column.
- Increase in the rate of reduction of hematite to iron by prereducing under high concentration of hydrogen.
- Equilibrium bed heights when a fluidized bed and a fixed bed are connected through an opening. Effect of contracting the bed columns at the gas exit.:EFFECT OF CONTRACTING THE BED COLUMNS AT THE GAS EXIT
- Application of a cation exchange membrane to a sodium ion pump.
- IMPULSE RESPONSE OF A MIXING MODEL CONSIDERING THE FLUID EXCHANGE BETWEEN UP- AND DOWN-FLOWS
- CIRCULATION OF SOLID PARTICLES WITHIN THE FLUIDIZED BED WITH A DRAFT TUBE:EQUILIBRIUM BED HEIGHTS WHEN A FLUIDIZED BED AND A FIXED BED ARE CONNECTED THROUGH AN OPENING
- BEHAVIOR OF SINGLE AIR BUBBLES HELD STATIONARY IN DOWNWARD FLOWS
- POWER REQUIREMENTS FOR AGITATING AIR-FLUIDISED BEDS
- Correlation for dynamic holdup in packed beds with cocurrent gas-liquid downflow.
- EFFECT OF LIGHT-SOURCE CHARACTERISTICS ON THE PERFORMANCE OF CIRCULAR ANNULAR PHOTOCHEMICAL REACTOR
- DYNAMIC EFFECTIVE DIFFUSIVSTY WHEN APPLIED TO THE PRESSURE INCREASE DURING REACTION FOR MULTICOMPONENT GASEOUS SYSTEMS WITHIN A POROUS SOLID:REDUCTION OF IRON-OXIDE POWDER BED BY HYDROGEN-INERT GAS MIXTURES AT 900°C