PARTICLE-STAGNANT FLUID HEAT TRANSFER COEFFICIENTS IN PACKED BEDS

スポンサーリンク

概要

• 論文の詳細を見る

• The Nusselt number for heat transfer between particle and stagnant fluid in packed beds is theoretically computed and found to be Nu=2.0. This may be regarded as the lower limiting Nusselt number for beds where each particle is in good contact with flowing fluid.

• 公益社団法人 化学工学会の論文

著者

• Wakao Noriaki

  Department Of Chemical Engineering Faculty Of Engineering Yokohama National University

• TAKANO YOSHINOBU

  Department of Chemical Engineering, Yokohama National University

• PEI D.

  Department of Chemical Engineering, Yokohama National University

関連論文

• Production of Activated Carbon from Bagasse (Waste) of Sugarcane Grown in Brazil
• Average Pore Radius and Effective Diffusivity in Porous Catalysts
• Radiant Heat Transfer in Adiabatic Tubular Reactor Containing Gray Gas
• Delignification of Acacia mollissima willd in steam explosion. Effect of adding ethylene glycol on oil produced.
• Oil extraction from Australian condor oil shale with water - Effects of adding toluene, CO and NaOH.
• Liquid pumps driven by temperature difference between two waters or temperature variations in the environment.
• Heat input-response in cooling tower. Zeroth moments of temperature variations.
• PARTICLE-STAGNANT FLUID HEAT TRANSFER COEFFICIENTS IN PACKED BEDS
• Determination of liquid-side and gas-side volumetric mass transfer coefficients in a bubble column.
• Molecular diffusion coefficients of vitamin K3 in mixtures of CO2 and n-hexane at temperature of 313.2K and total pressure of 16.0 MPa.

スポンサーリンク