Mass transfer coefficient of tubular ultrafiltration membranes under high‐flux conditions |
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Authors: | Kazuki Akamatsu Keita Ishizaki Shotaro Yoshinaga Shin‐ichi Nakao |
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Affiliation: | Dept. of Environmental Chemistry and Chemical Engineering, School of Advanced Engineering, Kogakuin University, 2665‐1 Nakano‐machi, Hachioji‐shi, Tokyo 192‐0015, Japan |
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Abstract: | The effect of suction flow on the mass transfer coefficient of tubular ultrafiltration membranes, in particular that under a high‐flux condition, was studied. We pointed out that is proportional to under turbulent conditions, and that the proportional constant, b, exceeds 0.023 when the effect of suction flow is not negligible. We conducted the velocity variation method using ultrafiltration membranes with MWCOs of 20k and 100k and dextrans having molecular weights of 40,000 and 70,000 at the conditions, where exceeded . We demonstrated that the effect of suction flow includes not only flux but also the diffusion coefficient of solute, and that the ratio of the flux to the diffusion coefficient, expressed as , is an important index. Finally, we concluded that , when is smaller than , giving the Deissler equation itself, and that , when exceeds . © 2017 American Institute of Chemical Engineers AIChE J, 64: 1778–1782, 2018 |
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Keywords: | mass transfer coefficient wall Peclet number suction flux diffusion coefficient |
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