MASS TRANSFER IN THE CONTINUOUS PHASE AROUND A SINGLE DROP

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概要

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• A simple model is proposed for mass transfer in a continuous phase around a single liquid drop. The model is based upon the assumption that the ratio of the average Sherwood number for a drop to that for its equivalent solid sphere is equal to the ratio of the local values at their front stagnation points. The available data for some binary systems are reasonably well correlated with the model, and it is theoretically more consistent than the analogical models proposed by Griffith, and Shirotsuka and Hirata which are based upon the boundary-layer analysis of the flow over a flat interface moving with a constant velocity.

• 公益社団法人 化学工学会の論文

著者

• OGAWA KANEHIRO

  Department of Chemical Engineering, University of Osaka Prefecture

• UEYAMA KORETSUNE

  Department of Chemical Engineering, University of Osaka Prefecture

• HATANAKA JUN-IGHI

  Department of Chemical Engineering, University of Osaka Prefecture

• Ueyama Koretsune

  Department of Chemical Engineering, College of Engineering, University of Osaka Prefecture

関連論文

• Mechanism of copper transport through a diaphragm-type liquid membrane.
• MASS TRANSFER IN A LAMINAR BOUNDARY LAYER WITH MOVING INTERFACE
• MASS TRANSFER IN THE CONTINUOUS PHASE AROUND A SINGLE DROP
• NUMERICAL CALCULATIONS OF MASS TRANSFER THROUGH LAMINAR BOUNDARY LAYER WITH MOVING INTERFACE
• THE PENETRATION THEORY WITH HIGH MASS FLUX AND VARIABLE PROPERTIES
• CORRECTIONS OF THE PAPER "DRAG COEFFICIENTS AND MASS TRANSFER IN THE CONTINUOUS PHASE FOR SINGLE DROPS AT LOW REYNOLDS NUMBERS"
• SIMILARITY CONDITION OF MASS TRANSFER IN LIQUID-LIQUID SYSTEMS

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